development of wettable cathode for aluminum …€¦ · developing new materials, as alternative...
TRANSCRIPT
HAMED HEIDARI
DEVELOPMENT OF WETTABLE CATHODE FOR
ALUMINUM SMELTING
Thèse présentée
à la Faculté des études supérieures et postdoctorales de l’Université Laval
dans le cadre du programme de doctorat en génie des matériaux et de la métallurgie
pour l’obtention du grade de Philosophiae doctor (Ph.D.)
DÉPARTEMENT DE GÉNIE DES MINES, DE LA MÉTALLURGIE ET DES MATÉRIAUX
FACULTÉ DES SCIENCES ET DE GÉNIE UNIVERSITÉ LAVAL
QUÉBEC
2012
© Hamed Heidari, 2012
Résumé
Le procédé de l’électrolyse Hall-Héroult demeure la méthode principale pour la production
mondiale de l’aluminium primaire depuis son invention en 1887. L'utilisation de cathodes
mouillables au lieu de cathodes de carbone usuelles a été proposée afin de réduire de plus
de 10% de la consommation d'énergie électrique du procédé, ce qui constitue plus de 35%
de coûts de la production de l'aluminium. Cependant, à cause des conditions sévères qui
prévalent dans le bain d'électrolyse, la fabrication d'une bonne cathode mouillable a été un
défi au cours des 60 dernières années et aucune cathode mouillable commerciale n’est
encore disponible sur le marché mondial. Dans ce projet, une nouvelle céramique poreuse a
été développée par frittage sans pression de TiB2 avec additif de Ti-Fe pré-allié. Ce
matériau possède les propriétés requises pour servir de cathode mouillable.
Dans cette étude doctorale, le frittage en phase liquide sans pression a été choisi comme
méthode de consolidation permettant la fabrication de grandes pièces à un coût relativement
bas. Des essais ont été réalisés afin de comprendre l'effet de différentes conditions de
traitement y compris la composition d'additif, la température de frittage, le temps de
broyage, et la pré-alliage des additifs sur les propriétés physiques, mécaniques et
métallurgiques ainsi que le comportement de mouillage et la stabilité des spécimens dans
l'aluminium liquide.
Après l'ajustement des paramètres de procédé, le matériau sélectionné a été fabriqué par le
mélange de TiB2 en poudre avec 10% en poids d'additif 7Ti-3Fe pré-allié dans le broyeur à
billes à haute énergie pendant 30 min, suivi par un pressage à 150 MPa et un frittage sous
atmosphère de Ar/H2 à 1650°C pendant 1 h.
Une microstructure sans fissures avec une distribution uniforme de pores, une densité
maximale relative de 91%, une résistance à la flexion de 300 MPa et une résistivité
électrique de 54 μΩ.cm ont donc été obtenues. Une goutte d’aluminium a très bien mouillé
la surface de l'échantillon et une solidification isotherme s'est produite lors de sa
pénétration due à l'interaction avec les additifs métalliques et la formation des phases TiAl3
et Fe4Al13.
ii
Malgré la dissolution des additifs métalliques, le matériau développé a montré une
excellente stabilité après exposition dans l'aluminium fondu à 960°C pour une durée
maximale de 5 jours tout en maintenant sa forme, et aucun signe d’expansion ou de
gonflement n’ont été observés. Les analyses microstructurales ont révélé la formation de
ponts de TiB2 entre les particules, en présence de phase liquide de Ti-Fe au cours du
frittage, et donc la formation d’un squelette TiB2 qui est la cause de la stabilité du matériau
développé dans l'aluminium liquide. Par conséquent, ce matériau est proposé en tant qu’un
candidat fiable pour l'application en tant que cathodes mouillables dans la production
d'aluminium.
iii
Abstract
Hall-Héroult electrolysis process has been the major method for world production of
primary aluminum since its invention in 1887. The use of wettable cathodes instead of
usual carbon cathodes has been proposed to reduce more than 10% of the electrical energy
consumption of the process which constitutes more than 35% of the aluminum production
costs. However, due to the severe conditions of the electrolysis bath, the fabrication of a
proper wettable cathode has been a challenge during the last 60 years and no commercial
wettable cathode is available in the world market yet. In this project, a novel porous
ceramic by pressureless sintering of TiB2 with pre-alloyed Ti-Fe additives was developed.
This material showed to meet the required properties to be used as wettable cathode. In this
doctoral study, the pressureless sintering in the presence of liquid phase was selected as the
consolidation method allowing the fabrication of large parts at relatively lower
temperatures and costs. Experimental efforts were made in order to understand the effect of
different processing conditions including additive composition, sintering temperature,
milling time and pre-alloying of additives on the physical, mechanical and metallurgical
properties as well as wetting behavior and stability in liquid aluminum of specimens. Based
on the results of the adjustment of processing parameters, the selected material was
fabricated by mixing of TiB2 powder and 10 wt% pre-alloyed 7Ti-3Fe additive in high
energy ball mill for 30 min, compacting under the pressure of 150 MPa to prepare the green
parts, and sintering under Ar/H2 atmosphere at 1650C for 1 h. Uniform crack-free
microstructure with even distribution of pores as well as maximum relative density of 91%,
bending strength of 300 MPa and electrical resistivity of 54 µΩ.cm were accordingly
obtained. Aluminum drop wetted the surface of the specimen very well and isothermal
solidification occurred during its penetration due to the interaction with the metallic
additives and the formation of TiAl3 and Fe4Al13 phases. Despite of the dissolution of
metallic additives, this material showed excellent stability after being exposed to molten
aluminum at 960C for up to 5 days by maintaining its shape and no sign of expansion or
swelling was observed. Microstructural investigation revealed the precipitation of inter-
iv
particle bridges of TiB2 nature in the presence of Ti-Fe liquid phase during sintering
forming a TiB2 skeleton, which is the cause of the stability of the developed material in
liquid aluminum. This material is proposed as a reliable candidate for application as
wettable cathodes in aluminum smelting.
Preface
This doctoral thesis is presented to the department of mining, materials and metallurgical
engineering of Laval university and reports the works carried out as part of the project:
Development of wettable cathode for aluminum smelting. The project was supported by a
Collaborative Research and Development (CRD) grant from The Natural Science and
Engineering Research Council of Canada (NSERC) and Hydro Québec as a part of “Energy
Efficient Programs”.
Hall-Héroult electrolysis process has been the major method for producing primary
aluminum in the world since its invention in 1887. A lot of improvements and
modifications have been made to this process in order to reduce the energy consumption
from more than 50 kWh/kg Al in year 1900 to less than 15 kWh/kg Al in 2010. Despite the
considerable increase of the energy efficiency of the process, it is still the major consumer
of electrical energy in Canada as the third largest producer of primary aluminum in the
world. Developing new materials, as alternative for common carbon cathodes, which are
wettable by liquid aluminum has been proposed as a solution for further increase of the
energy efficiency of this process.
TiB2 is one of the few materials, with good electrical conductivity, which could withstand
the severe conditions of electrolysis cell for long durations. However, the fabrication of
large TiB2 cathode parts is encountered by several scientific and technical issues, which
made the development of wettable TiB2-based cathodes a 60-years challenge for aluminum
industry.
This thesis reports firstly the review of the previous works reported on this subject,
followed by materials selection and proposed methodology. Efforts made during this
doctoral study include the design, development and evaluation of a new candidate material
for wettable cathode. Numerous preliminary experiments were performed at the beginning
of the study to choose the best combination of materials and process parameters for this
challenging application.
vi
In this context, we propose, for the first time, the use of a pre-alloyed Ti-Fe additive for
pressureless sintering of TiB2-based ceramics at the presence of liquid phase. Fabrication of
ceramic materials which meet the property requirements of wettable cathode with the use of
commercial grade TiB2 powder, short milling time of 30 min, compacting pressure of 150
MPa and pressureless sintering at temperature of 1650°C make the developed method a
potential choice for fabrication of large cathode parts at relatively low price in industrial
scales.
This doctoral project was carried out under the direction of Professor Houshang Alamdari
and co-direction of Professor Dominique Dubé from Laval University and collaboration of
Dr. Robert Schulz from Hydro Québec research institute (IREQ). This thesis has been
prepared as an article insertion thesis and includes four peer-reviewed articles (submitted
and/or published), which report the results obtained from collaborative works of the authors
in Laval University and Hydro-Québec during the different stages of the project.
My contribution to these articles was the identification of the objective of each article,
preparation of the plan of experiments, design and assembly of the experimental set-ups
and performing the experiments including: consolidation of specimens, metallographic
preparations, microstructural studies, mechanical and electrical evaluations, and chemical
stability investigations. I performed the density and electrical resistivity measurements as
well as wettability evaluations with the help of Dr. Robert Schulz and Mr. Sylvio Savoie at
IREQ. I subsequently prepared the first draft of the articles, which were revised by the co-
authors before submission.
The first article titled: Pressureless sintering of TiB2–based composites using Ti and Fe
additives for development of wettable cathodes, co-authored by Prof. Houshang Alamdari,
Prof. Dominique Dubé and Dr. Robert Schulz, was presented at TMS 2011 international
conference and was published in the journal: Light Metals 2011, P. 1111-1116 1. In this
article the effect of composition and processing parameters on the microstructure and
physical properties of consolidated TiB2 parts was studied.
vii
The second article titled: Investigating the potential of TiB2-based composites with Ti and
Fe additives as wettable cathode, co-authored by Prof. Houshang Alamdari, Prof.
Dominique Dubé and Dr. Robert Schulz, was presented in Thermec 2011 international
conference and was published in both the journal: Materials Science Forum, 2012, Vol.
706-709, P. 655-660 2; and the journal: Advanced Materials Research, 2012, Vol. 409, P.
195-200 3. In this paper the microstructure, physical properties and wettability of TiB2-
based specimens with different milling time were compared. The interaction of specimens
with liquid Al when exposed to molten Al up to 24 h was investigated as well.
The third article titled: Interaction of molten aluminum with porous TiB2-based ceramics
containing Ti-Fe additives, co-authored by Prof. Houshang Alamdari, Prof. Dominique
Dubé and Dr. Robert Schulz, was published in: Journal of the European Ceramic Society,
2012, Vol. 32, Issue 4, P. 937-945 4. In this paper the interaction of TiB2 ceramics
consolidated using Ti-Fe additive with aluminum drop was investigated. First the
interaction of surface oxide layer with liquid Al was studied. Then the mechanism of
penetration of Al inside the specimen and its interaction with the metallic phases in the
inter-particle spaces were discussed.
The fourth article titled: Pressureless sintering of TiB2-based ceramics with Ti-Fe additive:
sintering mechanism and stability in liquid aluminum, co-authored by Prof. Houshang
Alamdari, Prof. Dominique Dubé and Dr. Robert Schulz, was published in: Advanced
Engineering Materials journal, 2012, Vol. 14, P. 802–880 5. In this paper the effect of
different sintering additives including Fe, Ti and Ti-Fe on the stability of consolidated parts
in molten aluminum was investigated. A complete discussion was presented to explain how
Ti-Fe additive could promote the formation of TiB2 phase as the inter-particle bridges
during the sintering process which is responsible for the stability of this material in molten
aluminum at prolonged exposure time.
viii
Acknowledgments
I would like to express my appreciation to my thesis director Prof. Houshang Alamdari, and
my co-director, Prof. Dominique Dubé, for having confidence in me to conduct this project,
for their great availability for meetings and discussions and for their valuable comments
and suggestions. Their encouragement, guidance, knowledge and advices were very helpful
and appreciated all through my studies. I am also thankful to my co-director in Hydro
Québec Research Institute, Dr. Robert Schulz, for his insight, support, and his valuable
comments and discussions throughout this project. Moreover, I grateful to him for
providing me with the experimental setups, materials and equipment in IREQ laboratories,
which greatly helped me evaluate the developed materials and progress my project. This
dissertation would not have happened without you all.
Special thanks goes to Sylvio Savoie for his proficiency and expertise in the fabrication of
the experimental set-ups I used for my experiments and for his technical assistance to help
me realize the analyses.
I would like to acknowledge Prof. Carl Blais and his team: Philippe Lapointe, Nicolas
Giguère, Bernard Tougas for their kind help and for generously allowing me to use their
laboratory and equipment.
Thanks to all of the staff of Mining, Metallurgical and Materials Engineering Department
of Laval University for their help and support. I am grateful to Maude Larouche, Marc
Choquette André Fernand and Jean Frenette for their help with microstructural analyses,
Daniel Marcotte and Marie-Josée Bouchard for their availability and technical assistance.
Thanks also to my friends and colleagues Mohammad Ghasdi, Kamran Azari, Francois
Chevarin, Milad Mardan, and all my friends at the department for making a lively and
joyful environment and for the greats moments we had together.
ix
I would like to thank my parents for their support, patience, and sacrifice in all and every
stage of my life, and my brother Majid who has made me feel having my family beside me
here in Québec.
Last, but not least, I am very deeply grateful to my lovely wife, Maryam, for her love,
dedication, understanding, patience, support and encouragement. My special thanks for her
guidance, technical discussions and for kindly revising my manuscripts during my doctoral
study.
To my loved ones
Table of contents
Résumé .......................................................................................................................................... i
Abstract ....................................................................................................................................... iii
Preface.......................................................................................................................................... v
Acknowledgments .................................................................................................................... viii
Table of contents ........................................................................................................................ xi
List of tables ............................................................................................................................ xvii
List of figures ......................................................................................................................... xviii
Chapter 1: Introduction ............................................................................................................... 1
1.1 General context .............................................................................................................. 2
1.2 Project motivations ........................................................................................................ 5
1.3 Structure of thesis .......................................................................................................... 6
Chapter 2: Literature review ....................................................................................................... 9
2.1 Aluminum..................................................................................................................... 10
2.1.1 Aluminum production industry ........................................................................... 10
2.1.2 Hall-Héroult process ............................................................................................ 10
2.2 Issues with carbon cathode in Hall-Héroult cell ........................................................ 18
2.2.1 Non-wettable for liquid aluminum ...................................................................... 18
2.2.2 Penetration of electrolyte and liquid aluminum ................................................. 18
2.3 Wettable drained cathode ............................................................................................ 20
xii
2.3.1 General property requirements for an ideal cathode material ........................... 20
2.3.2 Choice of material ................................................................................................ 21
2.4 Titanium diboride ........................................................................................................ 24
2.4.1 Phase diagram, crystal structure and properties of TiB2 .................................... 24
2.4.2 Synthesis of TiB2 .................................................................................................. 26
2.5 TiB2-based cathode technologies ................................................................................ 27
2.6 TiB2-based cathodes .................................................................................................... 30
2.6.1 Use of metallic sinter additives ........................................................................... 31
2.6.2 Use of ceramic sinter additives............................................................................ 34
Chapter 3: Thesis outline .......................................................................................................... 37
3.1 Objectives ..................................................................................................................... 38
3.2 Choices of sintering additives ..................................................................................... 39
3.3 Originality of the project ............................................................................................. 41
Chapter 4: Materials and methods............................................................................................ 43
4.1 Introduction .................................................................................................................. 44
4.2 Experimental procedures ............................................................................................. 44
4.2.1 Starting powders ................................................................................................... 44
4.2.2 Powder processing................................................................................................ 45
4.2.3 Forming method ................................................................................................... 45
xiii
4.2.4 Consolidation and sintering ................................................................................. 45
4.3 Characterisation methods ............................................................................................ 47
4.3.1 Bulk density and apparent porosity measurements ............................................ 47
4.3.2 Mechanical properties evaluation ........................................................................ 48
4.3.3 Measurement of electrical resistivity .................................................................. 49
4.3.4 Wettability in liquid aluminum ........................................................................... 50
4.3.5 Chemical stability and durability to liquid aluminum ....................................... 50
4.3.6 Scratch test ............................................................................................................ 51
4.3.7 Microstructural characterisation .......................................................................... 51
4.3.8 Compositional and phase analysis....................................................................... 52
Chapter 5: Pressureless sintering of TiB2–based composites using Ti and Fe additives for
development of wettable cathodes ........................................................................................... 53
5.1 Résumé ......................................................................................................................... 54
5.2 Abstract ........................................................................................................................ 54
5.3 Introduction .................................................................................................................. 56
5.4 Materials and methods................................................................................................. 58
5.5 Results and discussion ................................................................................................. 60
5.5.1 Effect of additive composition ............................................................................ 60
5.5.2 Effect of sintering temperature ............................................................................ 61
xiv
5.5.3 Effect of pre-alloying additives ........................................................................... 62
5.5.4 Effect of milling time ........................................................................................... 62
5.5.5 Wettability and stability in liquid aluminum ...................................................... 70
5.6 Conclusions .................................................................................................................. 71
5.7 Acknowledgement ....................................................................................................... 71
Chapter 6: Investigating the potential of TiB2–based composites with Ti and Fe additives as
wettable cathode ........................................................................................................................ 72
6.1 Résumé ......................................................................................................................... 73
6.2 Abstract ........................................................................................................................ 73
6.3 Introduction .................................................................................................................. 74
6.4 Materials and methods................................................................................................. 75
6.5 Results and discussion ................................................................................................. 77
6.6 Conclusions .................................................................................................................. 83
Chapter 7: Interaction of molten aluminum with porous TiB2–based ceramics containing
Ti-Fe additives ........................................................................................................................... 84
7.1 Résumé ......................................................................................................................... 85
7.2 Abstract ........................................................................................................................ 85
7.3 Introduction .................................................................................................................. 86
7.4 Materials and methods................................................................................................. 87
7.5 Results and discussion ................................................................................................. 88
xv
7.5.1 Sessile drop tests .................................................................................................. 88
7.5.2 Early Stage of Interaction .................................................................................... 90
7.5.3 Later Stage of Interaction..................................................................................... 93
7.5.4 Reaction Mechanism ............................................................................................ 99
7.6 Conclusion.................................................................................................................. 102
7.7 Acknowledgements ................................................................................................... 103
Chapter 8: Pressureless sintering of TiB2-based ceramics with Ti-Fe additives: sintering
mechanism and stability in liquid aluminum......................................................................... 104
8.1 Résumé ....................................................................................................................... 105
8.2 Abstract ...................................................................................................................... 105
8.3 Introduction ................................................................................................................ 106
8.4 Materials and methods............................................................................................... 107
8.5 Results and discussion ............................................................................................... 110
8.5.1 Influence of additives on physical and metallurgical properties ..................... 110
8.5.2 Interaction with a liquid aluminum drop .......................................................... 113
8.5.3 Stability in liquid aluminum .............................................................................. 118
8.5.4 Scratch test .......................................................................................................... 119
8.5.5 TEM analysis ...................................................................................................... 120
8.6 Conclusions ................................................................................................................ 122
xvi
8.7 Acknowledgements ................................................................................................... 123
Chapter 9: General discussion and conclusions .................................................................... 124
Chapter 10: Perspectives of the project ................................................................................. 130
References: .............................................................................................................................. 133
Appendix 1: Ceramic fabrication ........................................................................................... 140
List of tables
Table 2–1- Electrical resistivity of some ceramics (in Ω cm) 27
............................................ 22
Table 2–2- Physical properties of some RHMs 22
................................................................... 23
Table 4–1- Starting powders specification .............................................................................. 44
Table 5–1- Experimental conditions used for consolidation of specimens ........................... 59
Table 5–2- Relative density of specimens with separate (T7F3M10) and pre-alloyed
(T7F3PM10) additives...................................................................................................... 62
Table 8–1- The starting composition of sintered specimens, their relative density and 3-
point bending strength. ................................................................................................... 110
List of figures
Figure 2–1- Schematic of a typical Hall-Héroult cell for electrolytic smelting of aluminum
13 ......................................................................................................................................... 11
Figure 2–2- Voltage distribution in a Hall- Héroult cell 10
..................................................... 16
Figure 2–3- Binary Ti-B phase diagram 32
.............................................................................. 25
Figure 2–4- The structure of TiB2 in a projection along the hexagonal axis (right) and a
perspective view (left) 34
.................................................................................................. 25
Figure 2–5- Transmission electron micrograph of the specimen with 0.5 wt% Cr and 0.5
wt% Fe and energy dispersive spectra of X-ray microanalysis at a triple junction 51
. . 32
Figure 3–1- Binary phase diagram of Fe-Ti 64
. ....................................................................... 40
Figure 4–1- Diagram of sintering cycle ................................................................................... 46
Figure 4–2- Schematic of three-point loading for measuring the flexural strength of
ceramics 68
. ........................................................................................................................ 48
Figure 4–3- Schematic of setup used for sessile drop test and wettability investigation ..... 50
Figure 5–1- Comparison of the relative density as a function of sintering temperature and
composition of sintering additives (T8F2M10: TiB2+8%Ti+2%Fe; T7F3M10:
TiB2+7%Ti+3%Fe). .......................................................................................................... 60
Figure 5–2- Backscattered SEM micrograph of T8F2M10 (TiB2+8%Ti+2%Fe) specimen,
sintered at 1400°C for 1 h (The arrows show segregated phases containing the
additives). .......................................................................................................................... 61
Figure 5–3- Influence of milling time on relative density of green and sintered specimens
(TiB2+7%Ti+3%Fe) using pre-alloyed additive and sintered at 1650°C for 1h........... 63
xix
Figure 5–4- Influence of milling time on bending strength of specimens
(TiB2+7%Ti+3%Fe) prepared using pre-alloyed additive and sintered at 1650°C for
1h. ...................................................................................................................................... 64
Figure 5–5- Effect of milling time on the particle size distribution for powder mixtures
containing the 70%Ti and 30%Fe pre-alloyed additive. ................................................ 65
Figure 5–6- SEM micrograph of a large agglomerate formed after 240 min milling in
T7F3PM240 powder (TiB2+7%Ti+3%Fe). .................................................................... 66
Figure 5–7- XRD analysis of powders containing pre-alloyed additives after 10 and 240
min milling. (Cu Kα). ....................................................................................................... 67
Figure 5–8- Backscattered SEM micrograph of T7F3PM10 specimen (TiB2+7%Ti+3%Fe)
milled for 10 min and sintered 1 h at 1650°C. ................................................................ 68
Figure 5–9- Backscattered SEM micrograph of T7F3PM30 specimen (TiB2+7%Ti+3%Fe)
milled for 30 min and sintered 1h at 1650°C. ................................................................. 69
Figure 5–10- Backscattered SEM micrograph of T7F3PM120 specimen
(TiB2+7%Ti+3%Fe) milled for 120 min and sintered 1 h at 1650°C............................ 69
Figure 5–11- Behavior of liquid Al drop over T7F3PM30 specimen (TiB2+7%Ti+3%Fe)
during the wettability test at different time. (The time from beginning of test are
reported in minutes) .......................................................................................................... 70
Figure 6–1- Cumulative particle size distribution diagram of pure TiB2, pre-alloyed 7Ti3Fe,
and mixtures after different milling times (M10 e.g. means mixed powder milled for
10 min)............................................................................................................................... 77
Figure 6–2- Micrograph of specimens milled for a) 10 min, b) 30 min, c) 240 min and
sintered at 1650°C for 1h. (Phases in the microstructure are A: TiB2 ; B: TiFe ; C: α-Ti
; D: TiFe2) .......................................................................................................................... 78
xx
Figure 6–3- Photo taken from liquid Al drop on the surface of M30 specimen. .................. 79
Figure 6–4- Wetting angle of liquid Al on M30 and M240 specimens as a function of
elapsed time ....................................................................................................................... 80
Figure 6–5- Micrograph of M30 specimens exposed to liquid Al at 960°C: for 1h: a) BSE
micrograph of contact area, b) Mapping of Al element, c) Mapping of Fe element; and
for 24h: d) BSE micrograph of contact area, e) Mapping of Al element, f) Mapping of
Fe element ......................................................................................................................... 81
Figure 6–6- Micrograph of M240 specimens exposed to liquid Al at 960°C: for 1h: a) BSE
micrograph of Al penetration zone, b) Mapping of Al element, c) Mapping of Fe
element; and for 24h: d) BSE micrograph of Al penetration zone, e) Mapping of Al
element, f) Mapping of Fe element.................................................................................. 82
Figure 7–1- Photos from the contact between a liquid Al drop and a polished specimen’s
surface during a sessile drop test ..................................................................................... 89
Figure 7–2- Average contact angle versus time during sessile drop tests for the as sintered
and polished specimens. ................................................................................................... 90
Figure 7–3- BSE micrograph from the cross section of a specimen with partial penetration
of Al (S3-PP) ..................................................................................................................... 91
Figure 7–4- Partially penetrated test (S3-PP) a, b) BSE micrograph and EDX analysis of
TiAl3 particles formed inside Al drop, c,d) BSE micrograph and EPMA maps of Fe
element within Al drop ..................................................................................................... 92
Figure 7–5- Elemental distribution of aluminum and oxygen at the drop-specimen interface
after the partially penetrated test (S3-PP)........................................................................ 93
Figure 7–6- SEM micrograph of the cross section of a S1-P specimen after the sessile drop
test ...................................................................................................................................... 94
xxi
Figure 7–7- Elemental line scans carried out through the thickness of the specimen after a
sessile drop test at 960°C. (Depth=0 is corresponds to the aluminum-specimen
interface at the beginning of the test) .............................................................................. 95
Figure 7–8- Mapping of aluminum and titanium showing the transition between zone 1 and
zone 2 ................................................................................................................................. 96
Figure 7–9- Mapping of iron and titanium revealing the transition between zone 2 and zone
3.......................................................................................................................................... 96
Figure 7–10- Mapping of aluminum and titanium between zone 3 and zone 4 .................... 97
Figure 7–11- BSE micrographs of zone 2 and zone 3. Arrows show the presence of TiAl3
(P1) and Fe-Al compound (P2) ........................................................................................ 98
Figure 7–12- TiAl3 precipitate in zone 2, a) Transmission electron micrograph, b) SAED
pattern from the [010] zone axis of TiAl3 ....................................................................... 98
Figure 7–13- Fe4Al13 phase precipitated in zone 3, a) Transmission electron micrograph, b)
SAED pattern from the [010] zone axis of Fe4Al13 ........................................................ 99
Figure 7–14- Isothermal section of the Al-Fe-Ti phase diagram at 1000°C 88
................... 101
Figure 7–15- SEM micrograph of cross section of specimen subjected to two subsequent
sessile drop tests .............................................................................................................. 102
Figure 8–1- BSE micrographs from the microstructure of as-sintered specimens: a) 10T, b)
7T3F, c) 10F. Arrows in (a) indicate the presence of metallic titanium between TiB2
particles............................................................................................................................ 112
Figure 8–2- BSE micrograph of the cross section of specimens after reaction with
aluminum drop: a) 10T, b) 7T3F, c) 10F. Numbers on images refer to the different
zones formed as a result of aluminum infiltration. ....................................................... 114
xxii
Figure 8–3- BSE micrograph and EDX spectrum of phase A formed in the Al infiltrated
area (zone 2 in Figure 8–2-a) of 10Ti specimen, A: TiAl3 phase, B: Ti rich phase. .. 115
Figure 8–4- a) BSE micrograph from the expanded portion of 10F specimen (zone 1 in
Figure 8–2-c) after reaction with the liquid aluminum drop (A: TiB2, B: Al, C: Fe4Al13
phase, the black areas correspond to mounting resin), b) EDX spectrum of phase C.
.......................................................................................................................................... 117
Figure 8–5- SEM micrograph of the 7T3F specimen after immersion into molten Al for 5
days at 960C revealing the solid TiB2 skeleton. The metallic phases were dissolved in
a NaOH solution. ............................................................................................................ 119
Figure 8–6- Comparing the scratch resistance (Fx) between specimens (AS: as sintered, 5
days: 7T3F after 5 days of Al exposure, Ceradyne: Hot pressed TiB2 provided from
Ceradyne Inc.; The reported Fx is associated with 7T3F specimen after 5 days of Al
exposure.) ........................................................................................................................ 120
Figure 8–7- TEM micrographs from boundary between two TiB2 grains forming a TiB2
bridge: a) selected area for FIB, b-c) Interface of G1 and G2 grains, d) SAED of G1, e)
SAED of G2, f) Inter-particle bridge ............................................................................. 121
Chapter 1:
Introduction
2
1.1 General context
The primary aluminum production in Canada, has been increased from 1.6 Mt at 1990 to
3.0 Mt in 2009 6 which makes it the third largest aluminum producer in the world
7. Almost
90% of primary aluminum (about 2.6 Mt) of Canada is produced in the province of Québec
8. The electrolysis process used to produce aluminum requires large quantities of electric
power and consequently, the aluminum industry is the largest industrial consumer of energy
in this province. Even though Quebec has no bauxite, this province is one of the main
aluminum producers due to its competitive cost of electric power and its proximity to the
United States. Over 95% of the electrical energy used for electrolysis of aluminum in
Quebec is clean and renewable hydroelectric energy 8.
In 2009, Canada’s aluminum industry consumed about 164,700 terajoules (TJ) of electrical
energy. With an electricity consumption of less than 15 kWh/kg Al, the Canadian
production is ranked as one of the most efficient in the world 6. Although the quantity of
energy required to produce primary aluminum has been reduced by 15% in Canada from
1990 to 2009, still more than 35% of its production cost is devoted to electric consumption.
Aluminum industry takes great care in reducing energy consumption, which is so essential
to its survival. Several technological and scientific research and development programs
have been defined to improve the energy efficiency of electrolytic potlines like: wettable
cathode and drained cell, inert anode, cell and anode insulation modification, etc. It has
been proposed that using a wettable cathode instead of the common carbon cathodes could
reduce the electrical energy consumption by more than 10% 9.
The aluminum reduction process consists of electrolytic reduction of alumina dissolved in
molten cryolite salt (Na3AlF6) at 960C. The theoretical minimum electrical energy
requirement for conventional aluminum electrolysis is approximately 6 kWh/kg Al 10
.
Compared to the theoretical value, modern plants are operating at roughly 40% energy
efficiency. The energy consumed in an electrolysis cell is a function of the current
efficiency and operating voltage. The modern Hall-Héroult cells operate at 95% current
3
efficiency. The applied voltage to the electrolysis cell is consumed by different voltage
components of cell circuit. The theoretical minimum voltage required for the reduction
reaction is the cell reaction voltage which is a function of temperature and at 960C is 1.2
V DC 10
.The overall cell voltage is however about 4.6 V DC for new cells which is the sum
of required potential for cell reaction, overvoltage, bath, cathode, anode, connectors and the
voltage drops due to different resistances such as polarization. A considerable amount of
this voltage drop is due to the bath resistance, which accounts for more than 38% of the
total voltage drop and is directly related to the anode-cathode-distance, so called ACD.
The conventional electrolysis cells use cathodes made from carbonaceous materials which
are commercially available in three main types: amorphous based, semi-graphitic and
graphitized. None of these types of cathodes is wetted by liquid aluminum resulting in a
bad electrical contact and inhomogeneous current distribution at carbon cathode/aluminum
interface 10
. In addition, the non-wetted cathode surface increases the risk of cryolite
penetration at the interface which might cause cathode degradation and extra voltage drop
10. The aluminum pad on the top of carbon cathode should therefore be thick enough to
make a better contact and to avoid the risk of cryolite penetration within the interface. The
thickness of the metal pad is typically kept between 20 and 25 cm.
The liquid aluminum pad is a cathodically charged surface for the reduction reaction and
acts as real cathode in the process. Since there is a high current flow through the cell,
typically around 0.9 A/cm2, the resulting electromagnetic fields induce Lorentz forces
causing turbulent motion of the liquid pad. This turbulence deforms the aluminum-cryolite
interface. The joint gap between carbon cathode blocks can produce additional turbulences
in the moving pad. The combinations of these movements form waves in the metal pad
surface, which can approach the anode and result in electrical short-circuit. These short-
circuits are the cause of major loss of power and productivity and affect the stability of the
cell 10
. The turbulences also produce erosion of the carbon lining and decrease the cell life.
To avoid contact between the liquid aluminum pad and the anode, the ACD must be kept
4
large enough which in turn increases the power consumption of the cell. The typical ACD
in conventional cells is about 4.5 cm 11
.
The concept of using “wettable drained cathode cell” is an approach to overcome the
difficulties associated with thick metal pad. In this approach, the bulk of the liquid metal is
drained continuously from the cell while the cathode surface remains wet by a thin metal
layer resulting in a good electrical contact and acts as a penetration barrier between cathode
and cryolite. By using this concept, it would be possible to operate the cell with a thinner
metal pad, which will considerably reduce the risks associated with short-circuits or
inhomogeneous current distributions. Consequently, the reduction of ACD leads to a
significant improvement of energy efficiency and huge energy gain in this industry.
The major requirement for drained cathode cell is to replace conventional carbon cathodes
with new type of materials, which could be properly wetted by liquid aluminum. It should
be noted that beside the wettability for molten aluminum, the candidate materials should
also possess some other properties close or superior to those of usual carbon cathodes.
These properties include: high electrical conductivity, satisfactory mechanical properties,
low solubility and reaction with molten aluminum, good thermal shock resistance,
capability of being fabricated economically into desired shapes, and acceptable resistance
to penetration and corrosion by molten cryolite and specially sodium ions which will be
discussed in details in chapter 2.
Since almost all refractory metals are attacked by molten aluminum or molten cryolite at
the cell operating temperature, the candidate material should be selected among ceramics.
Most of ceramics, however, are either dielectric or have low electrical conductivity.
Borides, carbides and nitrides of the transition metals in the fourth to sixth groups of the
periodic table have interesting properties including good electrical conductivity, which
make them potential candidate materials for replacement of carbon cathodes. These
materials are known as “refractory hard metals (RHM)”.
5
The material that has attracted most attention in terms of chemical inertness with respect to
molten aluminum and of electrical properties is titanium diboride. Several research works
have been performed on the production and characterization of TiB2-based cathodes.
However, the manufacturing process of TiB2-based cathodes is still facing challenges such
as: high fabrication cost related to high processing temperatures, size limitations related to
the special manufacturing processes e.g. hot isostatic pressing (HIP), and low chemical
stability due to the reaction of grain boundaries with molten aluminum.
Many attempts have been made and fully dense TiB2 parts are successfully obtained at
relatively low processing temperatures using metallic sintering aids. Although the
consolidated parts are suitable for some applications such as cutting tools, they are not
proper choices for wettable cathodes as the grain boundaries are attacked by liquid
aluminum resulting in the disintegration of TiB2 grains and degradation in electrolysis cell.
As a result, none of these works led to the commercial implementation of these ceramics as
wettable cathode in aluminum electrolysis 12
.
1.2 Project motivations
The development of a suitable and low cost wettable cathode for aluminum industry, which
could fulfill all the requirements mentioned previously, is therefore a real challenge and
seems insurmountable. However, the potential gain in energy savings of at least 35 TWh, in
Canada alone, is worth the effort and justifies any additional investment.
With the aim of developing wettable cathodes and taking advantage of huge potential of
energy savings in this field, the objectives of this project were defined. The general
objective of the project was to develop TiB2-based ceramic materials, which meet the
property requirements of wettable cathode. The specific objectives were to consolidate the
TiB2-ceramic parts using new sintering aids offering the possibility to consolidate them at
relatively low temperatures while being able to withstand severe smelting environments. To
meet these goals, a series of practical sintering aids were proposed and the effect of their
composition and the processing parameters on the characteristics of consolidated
6
specimens, including physical, mechanical and metallurgical properties as well as their
behaviour and stability in liquid aluminum were investigated.
The technical objective of the project was, on the other hand, to consider the technological
and economical aspects in order to provide applicable, robust and optimized fabricating
process, which has the ability to produce large cathode block parts in reasonable production
costs. The guideline to achieve these goals was to consolidate the specimens via pressure-
less sintering while keeping the sintering temperature as low as possible.
1.3 Structure of thesis
This thesis is presented in eight chapters. The first chapter is the general introduction of the
thesis and presents the idea and problem identification and objectives of the project. The
structure of the thesis is presented at the end of this chapter as well.
The literature review on the basic knowledge and previous efforts on this subject is
presented in chapter 2. This chapter contains a brief review about the primary aluminum
production and Hall-Héroult process for better understanding the issues with common
carbon cathodes, the idea of wettable drained cathode as a solution for decreasing energy
consumption of primary aluminum production. A detailed review on the properties,
material selection and fabrication process of wettable cathodes then follows.
Chapter 3 emphasises the thesis outlines and the originality of the project.
Chapter 4 is assigned to the general materials and methods used in the experimental parts of
the project describing starting materials, processing and consolidation process and materials
characterization and evaluation methods.
This thesis has been prepared as an article insertion thesis. The results obtained during the
doctoral study are published in the form of four scientific conference and journal articles
with review committee. These articles show the evolution of the project toward the
objectives to develop a reliable material as a wettable cathode. These articles are presented
7
in chapters 5-8, which report the experimental approach as well as results of this thesis. In
all articles I have acted as the principle researcher and the first author.
The first article is reported in chapter 5. In this article the effect of composition and
processing parameters such as preparation of sintering additives, milling conditions and
sintering temperature on the final microstructure and physical properties of TiB2-based
parts consolidated pressureless sintering method was studied. It was shown that pre-
alloying of additives and milling time had significant effect on the final properties of
specimens.
In the second article, chapter 6, the effect of milling time on the particle size distribution of
the starting powder mixture as well as the properties of sintered specimens and especially
their behaviour in molten aluminum was investigated. In this work, the microstructure,
physical properties and wettability of specimens with different milling time were
compared. The interaction with liquid Al when exposed in molten Al up to 24 h was also
studied. It was concluded that the specimen milled for 30 min had the most promising
properties for further investigations.
Chapter 7 is dedicated to the third article. The main purpose of this article was to study the
interaction of TiB2-based specimen with molten aluminum drop. In this paper, first the
interaction of the surface oxide layer with liquid aluminum was studied. Then the
mechanism of the penetration of aluminum drop inside the specimen and its interaction
with the metallic phases in the inter-particle spaces was discussed. It was found that despite
the penetration of aluminum, there were no signs of swelling and expansion of the
specimen.
The fourth article is presented in chapter 8 of this thesis. In this paper, the effect of different
sintering additives including Fe, Ti and Ti-Fe on the stability of consolidated parts in
molten aluminum was investigated. It was shown that only the specimen with Ti-Fe
additive had good stability in liquid aluminum after prolonged immersion time. TEM
analysis of the exposed specimen revealed that the formation of TiB2 phase in the inter-
8
particle bridges is responsible for the stability of specimens in molten aluminum. A
complete discussion was made to explain the way Ti-Fe additive promotes the formation of
TiB2 phase as inter-particle bridges during the sintering process. The results reported in this
article confirm that the developed material could be a reliable candidate, considering the
scientific, technical and economic aspects, to be used as wettable cathode.
In chapter 9, concluding remarks of the project are presented. Some perspectives for further
progress of this work are suggested in chapter 10.
Chapter 2:
Literature review
10
2.1 Aluminum
Aluminum is an essential material for modern manufacturing. It is a lightweight, structural,
and excellent atmospheric corrosion resistant metal with high electrical and thermal
conductivities, and easy to recycle 10
.
2.1.1 Aluminum production industry
Aluminum is the most abundant metal in the Earth's crust, and the third most abundant
element therein, behind oxygen and silicon. However, it does not exist in nature in metallic
form due to its high reactivity. It is typically found as one of the several aluminum oxides
or silicates mixed with other minerals 10
. The most common aluminum ore from which
aluminum is produced is bauxite. It consists largely of the minerals such as gibbsite
Al(OH)3, boehmite γ-AlO(OH) and diaspore α-AlO(OH) 13
. Aluminum production is the
largest consumer of energy on a per-weight basis and is the largest electric energy
consumer of all industries 10
. Most new (primary) aluminum is produced by a sequence of
two processes: a) Bayer process, which extracts aluminum oxide (Al2O3) powder by
refining bauxite and b) Hall-Héroult process during which the aluminum oxide is reduced
by electrolysis 13
.
2.1.2 Hall-Héroult process
The Hall-Héroult process (developed in 1886) is an electrolytic process, which has
undergone modifications and improvements over a century. A modern Hall-Héroult
reduction cell (pot) (Figure 2–1) is a rectangular steel shell of 9 to 12 m long, 3 to 4 m wide
and 1 to 1.5 m deep 10
. It has an inner lining of carbon surrounded by refractory thermal
insulation, which keeps it isolated thermally, and electrically from the steel shell. The
capacity of the commercial cells ranges from 450 to 4,000 kg of aluminum per day
requiring electrical current of 60,000 A to more than 500,000 A, respectively 10
.
11
Figure 2–1- Schematic of a typical Hall-Héroult cell for electrolytic smelting of
aluminum 13
A typical electrolytic cell consists of prebaked anodes (positive electrode) and a cathode
(negative electrode) both made of carbon, and an electrolyte. Cryolite (Na3AlF6), which has
limited solubility of aluminum oxide, was found to be the best molten salt as an electrolyte.
Usually, the cell operates with 1–6.0% aluminum oxide in the electrolyte 14
. Additions of
fluorides of Ca, Al, Li, and Mg reduce the melting temperature of pure cryolite from
1012C to 950–980C and increase the current efficiency 13, 14
. Once the refined alumina is
dissolved in the electrolyte, its ions are free to move around. The reduction reaction is
continuous and alumina must be supplied to the bath at a controlled rate to maintain
constant conditions. This is accomplished with automatic feeders that break the frozen
surface crust and deposit alumina into the molten bath where it is dissolved and distributed
by convection currents. Alumina is also used to cover the carbon anodes and the frozen
bath surface and it serves as thermal insulator and a protective cover to reduce air burning
of the anode 10
.
Direct current enters the cells through the anodes, passes through the electrolyte carried
primarily by sodium ions, passes through the molten aluminum and exits the cell through
the cathode and steel current collector bars. The positively charged aluminum ions migrate
12
to the electrically negative cathode and pick up electrons to yield aluminum metal. The
reaction at the cathode is:
Cathodic Reaction: Al3+
(in electrolyte) + 3 e− → Al (l) ( 2-1)
Molten aluminum layer with 3-25 cm thick is accumulated at the bottom of the cell and is
siphoned at intervals into an external crucible. The purity of produced aluminum is about
99.5–99.8% and the major impurities are silicon and iron. It is then transferred to other
units of plant for further alloying preparations prior to casting into ingots or forming into
other shapes 13, 14
.
The oxygen ions migrate to the anodes, react with carbon and evacuated from the system in
the form of carbon dioxide.
Anodic reaction: O2−
(in electrolyte) + C (s) → CO (g) + 2 e− ( 2-2)
The gas molecules accumulate into large bubbles that are collected and move across the
anode surface to escape around the edge of anode. The buoyancy of gas creates movement
which contributes to the motion of the bath and a molten metal layer 10
.
Overall reaction: Al2O3 (in electrolyte) + 3C (s) → 2Al (l) + 3CO (g) ( 2-3)
Approximately 0.45 kg of carbon anode is consumed for each kilogram of aluminum
produced. The carbon anodes provide a large part of the energy required for aluminum
reduction (about 45% of energy requirement of reaction) 10
. Two types of anodes are in use:
pre-baked carbon blocks and self-baked anodes (known as Soderberg type) 13
. The
consumable carbon anodes are periodically replaced about every four weeks in modern
plants 10
. The pot cover, which is part of the gas collection system, is removed, the used
anode is pulled out from the frozen surface crust, and the new anode is inserted. This has to
be accomplished without significant pot crust breakage or alumina falling into the bath.
Anode changing results in thermal, current, and magnetic disturbance in cell operation 10
.
13
Since the carbon anodes are consumed in the reduction cell and must therefore be replaced
regularly they are mounted on the busbars so that the distance between the anode and the
metal pad can be adjusted and kept constant during the whole process.
The carbonaceous cell linings are composed of the cathode at the bottom and the sidewalls.
The carbon cathode carries the current from molten aluminum layer to the steel collector
bars 13
. The major constituents of carbon cathode blocks are Anthracite and to some extent
graphite, and metallurgical coke 14
. Some cathode blocks contain a higher content of
graphitic carbon in attempt to reduce the resistance. However, less resistive graphite is also
less wear resistant and this compromises the life of the cathode 10
. The commonly used
types of cathodes are: amorphous carbon, semi-graphite and fully graphitized 13
. The
cathode blocks are bonded in the cell by a pitch-carbon paste rammed between the joint 13
.
Since cathode replacement requires the complete dismantling of a cell, the cathode life
generally determines the cell life which maybe last for up to 10 years 14
.
Molten cryolite has low viscosity and interfacial tension that allows it to easily penetrate
any porosity in the carbon lining 14
. The carbon lining could absorb fused electrolyte up to
its own weight 14
. To protect the lining, the thermal insulation is adjusted to provide
sufficient heat loss to freeze a protective coating of the electrolyte, known as “ledge,” on
the inner walls. The cell is never tapped completely dry of molten aluminum in order to
prevent the direct contact between electrolyte and cathode. The carbon cathode must
remain bare for good electrical contact with the aluminum pad and for this reason it is
essential that no alumina or frozen ledge form under the metal pad 10
. Unlike the anodes,
the cathodes are not oxidized because they are protected by the liquid aluminum inside the
cells. Nevertheless, cathodes do corrode and erode, mainly due to electrochemical
processes and metal movement 15
. One of the main causes suggested for the cathode failure
is the accumulated expansion and damage caused by sodium penetration. The sodium
attack causes the swelling and cracking of carbon lining 15
. Cell failure occurs either when
the bath penetrates through the cathode material or the sidewall carbon. In either case, the
cell can no longer contain the electrolyte or the molten metal and must be shut down and
14
rebuilt. Normally the electrical resistance of the cathode increases with time and the lining
is rebuilt after 1200 to 3000 days operation 16
.
There are three main factors that can compromise cell life 12
. The first factor is starting up
and shutting down the cell multiple times. When starting up a cell, significant stresses
occur in the cathode lining because of the significant changes in temperature, from room
temperature to more than 400°C. These stresses can cause cracking that lead to cathode
failure. Cells are rarely completely shut down, in part because of this danger.
The second compromising factor is sludge accumulation under the metal pad. Sludge is a
mixture of undissolved bath and alumina that sinks to the bottom of the cell. Sludge forms
when the bath temperature is not sufficiently above the liquidus temperature or when the
alumina is fed too rapidly. The sludge promotes the erosion of the cathode, which can lead
to cathode failure. Thus, it is important to feed the cell at an appropriate rate and to
maintain the cell within an acceptable temperature range.
The third factor that can shorten the cell life is the melting of the sidewall ledge, exposing
the sidewall carbon to the corrosive molten electrolyte. If this protective layer melts, the
electrolyte will begin to dissolve the sidewall carbon, leading to sidewall failure. Thus, it is
imperative to operate the cell within the proper temperature range to maintain the sidewall
freeze.
Several plant designs have been proposed over the years to minimize electrical energy loss.
Modern plants convert alternating current with a silicon rectifier into 600–900 V DC 13
.
Each electrolytic cell operates at 4.6 V DC, so roughly 150 to 180 cells are connected
electrically in series of long rows called “potlines.” They are placed as close as possible to
each other while maintaining sufficient room for anode changing, alumina feeding, and
reasonably low electromagnetic interference. Current density is calculated by dividing the
amperage supplied to an anode by its geometric face area. It is generally expressed in
amperes per square centimetre (A/cm2) and is considered as an indicator for the
productivity of a cell. Most potlines operate in the range of 0.8 to 1.0 A/cm2 10
. Depending
15
on the length of the potline, the total current flow can be between 50 and 360 kA 13
. Thus,
the electrodes must be good electrical conductors capable of carrying high currents. The
quantity of aluminum produced per cell increases with increasing current density. On the
other hand when the current density increases, its efficiency decreases, resulting in higher
energy consumption per unit of metal produced. Lower current densities are more energy
efficient, but increase capital and labour costs per unit of output 10, 13
.
The energy consumed in an electrolytic reaction is a function of the voltage used and the
current efficiency of the operating cell. The approximate voltage components of a
conventional cell are shown in Figure 2–2. The electric current flows through the cell and
the cell voltage components can be described as a set of resistors in series. The total
resistance of a series circuit is equal to the sum of the resistances of the individual
components in the circuit. The current is the same everywhere in the series circuit.
According to the Ohm's law, potential difference (V) is equal to current (A) × resistance
(Ω). So the sum of the potential drops equals to the sum of the voltage on each component.
E total = E cell reaction + E overvoltage + E bath + E cathode + E anode + E connectors ( 2-4)
The cell reaction voltage is a function of temperature, which is 1.2 V DC at 960oC.
16
Figure 2–2- Voltage distribution in a Hall- Héroult cell 10
The electrical energy consumed in a primary aluminum cell (excluding energy generation
and transmission losses) varies from less than 13 kWh/kg Al, for the modern plants, up to
more than 20 kWh/kg (for older Söderberg facilities) 10
. The theoretical minimum energy
requirement for carbon anode aluminum electrolysis is approximately 6 kWh/kg Al 10
. Heat
dissipated during aluminum smelting is about 8 kWh/kg of Al. The electrodes are
obviously key components in aluminum smelting and play a major role in efficiency as
well as pollutant emissions. Since 10% of the total cell voltage drop is in the carbon
cathode blocks, it is important that they have good electrical conductivity 10
.
The anode-cathode distance (ACD) is the distance between top surface of the aluminum
pad and the lower face of the anode. The space between anode and metal pad is occupied
by electrolyte bath. Decreasing the ACD reduces the cell voltage and the energy
consumption of the bath. The operating ACD should kept short to lowering the bath
17
resistance while at the same time large enough to let the rich alumina electrolyte to reach
the charged surfaces, let the reactant gas bubbles to escape and prohibit the contact of
disturbed liquid metal pad with anode surface 16
.
A part of heat that is required to keep the cell at operating temperature is supplied by the
electrical resistivity of bath as current passes through it. The amount of heat developed
depends on ACD and changing the ACD is one method of controlling the operation
temperature. The ACD is typically in the range of 4 to 5 cm 10
.
The liquid aluminum pad that forms at the bottom of the cell is the cathodically-charged
surface for the reduction reaction. When the large amperage passes through the cell, it
creates a huge electromagnetic field. The electromagnetic forces cause local liquid
aluminum stirring. Cells are designed to minimize this melt stirring. Nowadays melt
velocities of about 5 cm/s are observed, that is three times less than what was common
about fifty years ago 10
. Movement of the aluminum pad is also caused in smaller extent by
the interfacial drag of the bath fluid. Joint discontinuity of cathode carbon blocks also
creates additional disturbance flow in metal pad. The combination of all these forces
produces waves at the surface of the pad. These waves can reach the anode surface and
result in electrical short circuit at the cell. The current that flows during this shorting
produces no aluminum and results in major loss of energy and productivity. The motion of
the aluminum pad also makes erosion on carbon lining and reduces the cell life. The ACD
is constantly changing as a result of waving metal pad. Designing systems to minimize
metal pad movement is a key factor to reduce the ACD and accordingly increasing in cell
efficiency 10
. A better concept is to drain the bulk of the liquid metal to a sump and the
cathode is left wetted only by a thin layer of metal. Essentially the “drained cathode cell” is
a concept to approach to get rid of the difficulties associated with keeping the metal pad
stable.
18
2.2 Issues with carbon cathode in Hall-Héroult cell
2.2.1 Non-wettable for liquid aluminum
The carbon cathodes are not wettable by molten aluminum pad. Therefore, there is always a
gap between the metal pad and the carbon lining 10
. This gap creates an electrical junction
causes a small voltage drop and if the gap becomes thinner, the junction voltage decreases.
Therefore, the higher thickness of metal pad keeps at the bottom of the cell which applies a
greater weight of liquid metal on the cathode surface and lowers the junction voltage drop
10. As a result the metal pad must have a minimum thickness in order for the cell to operate
smoothly 12
. In the other hand, the electromagnetic forces create movement and standing
waves in the aluminum pad and to prevent the shorting between anode and the molten
metal, the ACD must be kept at a safe range of 4 to 5 cm. For traversing the ACD by the
current, the voltage drop in the range of 1.3 to 2.0 V is occurring, compared to the
theoretical voltage of 1.2 V required for the electrochemical reduction of alumina (using
carbon anodes) 10
.
Replacing the carbon cathode with new materials to be wetted by liquid aluminum is
proposed as a solution to reduce the energy loss in the cell. It decreases the junction voltage
drop and would allow decreasing the thickness of metal pad. A thinner pad would be more
hydrodynamically stable and would not be affected by electromagnetic forces. Therefore,
there will be no waves, swirls and electrical shorting. The ACD could considerably be
reduced resulting lower cell voltage. This, combined with a lower cathode voltage drop will
keeping down the energy consumption and will improve the power efficiency 10, 13
.
2.2.2 Penetration of electrolyte and liquid aluminum
The NaF/AlF3 ratio, which is called cryolite ratio (CR), is 3 in pure cryolite. Aluminum
fluoride is usually added to the electrolyte in excess of the Na3AlF6 composition. Although
lowering the cryolite ratio can increase the current efficiency and metal production, it
increases the volatility of the electrolyte 14
. It also adversely affects the electrical
19
conductivity of the bath and the solubility of alumina. The characteristic CR value used in
the aluminum industry lies between 2 and 3 14
.
During cell start-up and operation, electrolytically produced sodium enters the carbon
matrix porosity. Sodium is the by-product of the electrolysis process from the primary
deposition of aluminum melts. It is absorbed by the carbon cathode according to the
following reaction 17
.
Al (l) + 3NaF (in electrolyte) = 3Na (in C) + AlF3 (in electrolyte) ( 2-5)
Since metallic sodium is present in the carbon cathode, the reaction proceeds to the right as
long as the carbon matrix is not saturated with sodium and the sodium activity rises to unity
17. After penetration of sodium, the lining wetting conditions by the electrolyte changes,
thereby allowing the electrolyte to penetrate the carbon cathode. The penetration of both
sodium and electrolyte into the carbon materials causes various cathode defects, e.g.
swelling and crack propagation, cathode heaving and disruption 18
.
Another complication of carbon cathode in cell is the reaction between aluminum and
carbon and formation of aluminum carbide at the surface of carbon cathode:
4 Al (1) + 3 C (s) = A14C3 (s) ( 2-6)
According to Worrell 19
, the Gibbs energy for the reaction is -147 kJ/mole at 970°C, so that
this reaction is thermodynamically favoured at the temperatures of electrolytic aluminum
production. The reaction proceeds and a solid layer of Al4C3 is formed, whereupon the
diffusion-controlled reaction virtually stops. According to solubility data of A14C3 in the
electrolyte and liquid aluminum, solid Al4C3 might be dissolved and be reoxidized by the
anode gas:
Al4C3 (s) + 9CO2 (g) = 2Al2O3 (S) + 12CO (g) ( 2-7)
This reaction leads to under-saturation and dissolution of carbide films formed. Hence, a
steady consumption of carbon cathode may result 20
. In case of an uncontrollable
20
consumption of carbon cathode, the molten aluminum may reach the steel bars resulting in
excessive iron content in the product. In more serious cases, it may tap-out the cell.
It is because of the abovementioned problems related to the carbon cathodes that the
aluminum industry is seeking alternative materials for cathode. A cathode that is wetted by
aluminum would allow a dramatic reduction of ACD, which would decrease losses from
electrical resistance. A consequent increase in electrical efficiency would be a major
breakthrough.
2.3 Wettable drained cathode
Researches in the field of wettable drained cathode cells started in the 1950’s under the
leadership of Charles E. Ransley 21
who obtained patents with the British Aluminum Co. At
that time, he started experimental works on various carbides and borides of transition
metals and cell designs. Since then, lots of research efforts have been undertaken having
been focused on two main areas: a) the development of practical wettable cathode material
b) the design of a reduction cell to utilise such a material. Extensive review about inert
cathodes for aluminum electrolysis was published by Billehaug and Oye in 1980 22
. After
that, only the scarce information on trials on an industrial scale was available in the open
literature and most of the information was taken from the patent literatures 12
. Zhang et al.
15 have reviewed the development of wettable cathodes up to the beginning of 1990s. For
replacing common carbon cathodes, the new material must meet some properties to be
selected as a proper wettable cathode.
2.3.1 General property requirements for an ideal cathode material
It was thought that the non-carbon cathode is capable of providing a longer service life and
a significant power saving by narrowing the electrode gap and decreasing the cathode
voltage 23
. Based on the working conditions of the cathode in Hall-Héroult cell and the
existing problems with carbon materials, following properties are desirable for an ideal
cathode material 12, 15, 22, 24
:
21
1. High electrical conductivity (electrical resistivity < 500 μΩcm)
2. Low solubility and reaction with molten aluminum at 960°C
3. Wettability to molten aluminum
4. Good resistance to penetration and to corrosion by sodium and molten electrolyte
5. Adequate mechanical strength and resistance to cracking due to thermal or chemical
forces
6. Capability of being fabricated economically into desired shapes
7. Reliable electrical contact with current collectors
8. Resistance to abrasion/erosion from the metal and electrolyte
9. Good resistance to oxidation and to corrosion by any reactive gases to which it may
be exposed, particularly at elevated temperature at the exterior of the cell.
It is clear that no conventional carbon and carbon composite can comply with all these
requirements to be an ideal cathode. It is also obvious that few materials, if any, could meet
these requirements. The selected material should have these property requirements equal or
better than carbon cathodes.
2.3.2 Choice of material
High electrical conductivity and low solubility and reaction with molten aluminum at
operating conditions are two essential properties required for a material to be selected as a
wettable cathode. Metals generally have a high electrical conductivity because of their
metallic bond and the “sea of electrons” and some of them have high melting point to be
operated at cell temperature (about 960°C) but none of them could be a candidate to use as
wettable cathode due to the lack of durability in molten aluminum. Most of metallic
elements readily dissolve in liquid aluminum at cell temperatures 25
.
Ceramics are a unique class of materials that are distinguished from common metals and
plastics by their a) high hardness, stiffness and good wear properties; b) ability to withstand
high temperatures; c) chemical durability; and d) electrical properties 26
. They could be
electrical insulators, semiconductors, or ionic conductors. Most of ceramics are
22
predominantly electrical insulators. Some ceramics, like SiC, B4C and TiN, are semi-
conductor and can be used as heating elements or electrodes. Only a few groups of them
have good electrical conductivity in room temperature. The electrical resistivity values of
several ceramics are listed in Table 2–1 27
.
Table 2–1- Electrical resistivity of some ceramics (in Ω cm) 27
Material Electrical resistivity
(Ωcm-1
) at 25oC
Material Electrical resistivity
(Ωcm-1
) at 25oC
TiB2 10-5
MoSi2 2×10-5
ZrB2 10-5
Graphite 10-3
TiC 7×10-5
Si3N4 107-10
12
WC 2×10-5
ZrO2 109-10
11
B4C 0.1-100 Al2TiO5 >1011
SiC 0.1-10 Diamond 1012
TiN 0.5 Al2O3 1014
AlN 1013
-1015
BeO 1014
BN 1011
-1013
MgO 1014
According to the values in Table 2–1, the ceramics with high electrical conductivity are:
TiC, WC, TiB2, ZrB2 and MoSi2. They all belong to a group of ceramics so called
Refractory Hard Metals (RHM).
The RHM are in general defined as borides, carbides, silicides and nitrides of the transition
metals in the fourth to sixth group in the periodic system 28
. Reviews of research works on
wettable cathodes 12, 15, 22
show that most of efforts have been also focused on the use of
RHM, either as a single compound or a mixture of compounds. Some physical properties of
selected RHMs are listed in Table 2–2.
23
Table 2–2- Physical properties of some RHMs 22
Compound* Melting
temperature oC
Density
g/cm3
Electrical
resistivity
25°C
μΩcm
Electrical
resistivity
1000°C
μΩcm
Thermal
conductivity
Wm-1K-1
Thermal
expansion
Coeff.
K-1 108
Elastic
modulus
25°C
GPa
TiB2 2850 – 2980 4.52 9 – 15 60 24 – 59 4.6 253 – 550
ZrB2 3000 – 3040 6.09 – 6.17 7 – 16.6 74 24 5.9 343 – 491
MoB2 2100 – 2140 7.8 – 8.1 20 – 40
B4C 2450 2.52 0.2× 104–7× 10
4 High 29 4.5 448
TiC 3067 – 3250 4.92 – 4.95 51 – 250 119 17 – 21 5.5 – 7. 74 269 - 462
WC 2600 – 2870 15.7 – 15.8 17 – 22 106 – 118 29 – 121 4.5 669 – 710
Si3N4 1870 – 1885 2.37 – 3.19 1019
High 2.5
AlN 2400 decomp. 3.25 High High 30 5.6 345
BN 3000 decomp. 2.25 – 2.27 1.7 × 1018
High 15 7.5
TiN 2950 5.39 – 5.44 21.7 – 53.9 130 17 9.35
Graphite** 3500 subl. 570 – 1170 7.8 6.4 – 13.7 * Commercial polycrystalline grade
** Not RHM, but included for comparison
Titanium diboride (TiB2) has been always the most interesting RHM for the efforts on
development of wettable cathodes fot both economic and material property reasons 12, 15, 22
.
It is well established that TiB2 and ZrB2 have excellent wettability with molten aluminum
29. Ta and Nb borides also have interesting properties but compared to TiB2 they are too
expensive to be use for this application at commercial scale 22
. ZrB2 appeared to be at least
the technical equivalent of TiB2 but was rejected by industry because it is more expensive
30. Other RHMs, such as nitrides (AIN, BN and Si3N4), carbides (TiC, ZrC) are either poor
electrical conductors or have greater solubility in liquid aluminum. The presence of weak
reactions of TiC, ZrC and especially TiC 31
with molten aluminum has been detected 29
.
Many carbides and specially TiC have high melting points and are cheaper to produce but
they are very sensitive to structural defects such as vacancies both on the metal and non-
metal sites 15
.
The oxidation rates of the transition metal borides are low at lower temperature where a
protective layer of B2O3 glass appears on the surface. At temperatures above 1100°C or in
presence of water vapour the oxidation rate increases rapidly 22
.
24
2.4 Titanium diboride
2.4.1 Phase diagram, crystal structure and properties of TiB2
The Ti–B binary equilibrium phase diagram is presented in Figure 2–3 32
. As can be
observed, three intermetallic phases including orthorhombic TiB, orthorhombic Ti3B4 and
hexagonal TiB2 has been confirmed to exist. While Ti3B4 has been shown to be in a line
compound, both TiB and TiB2 exhibit a small composition variation. TiB and Ti3B4
decompose peritectically at 2180°C and 2200°C, respectively, TiB2 melts congruently at
3225°C (Figure 2–3). TiB2 exists over a stoichiometry range of 65.5 – 67.0 at.% B at
ambient temperature 32-34
.
TiB2 crystallizes with a hexagonal close packed structure (HCP) with P6/mmm space group
(a = b = 0.3028 nm, c = 0.3228 nm; α = β = 90, γ = 120) 28
. These dimensional parameters
lead to a density of 4.52 g/cm3, which is identical to the pycnometrically determined values
28. The hexagonal unit cell of TiB2 single crystal is shown in Figure 2–4
34. It is a simple
hexagonal lattice in which HCP Ti layers alternate with graphite-like B layers. By choosing
appropriate primitive lattice vectors, the atoms are positioned at Ti(0,0,0), B(1/3,2/3,1/2)
and B(2/3,1/3,1/2) in the unit cell 35
. Each boron atom has three boron neighbours in a
trigonal planar arrangement, forming a strong covalently bonded hexagonal network
structure. The high hardness of TiB2 and its chemical resistance are attributed to its inherent
crystal structure and atomic bonding 32-34, 36
.
However the relatively strong covalent bonding of the constituents results in low self-
diffusion rates, it gives also a high melting point and stable chemical composition 33
. A
higher mass fraction of TiB2 in composites yields a higher value of elastic modulus E.
When the mass fraction of TiB2 in composites exceeds 90 %, the value of the elastic
modulus appears to converge to 565 GPa at 23oC as the density increases towards 4.5 g/cm
3
33.
25
Figure 2–3- Binary Ti-B phase diagram 32
Figure 2–4- The structure of TiB2 in a projection along the hexagonal axis (right) and a
perspective view (left) 34
26
2.4.2 Synthesis of TiB2
Borides are generally produced by reaction of metals with boron or suitable boron
compounds 37
. The following processes are of practical interest 32, 37
:
1. Synthesis by fusion of metal (or metal hydrides) and boron
2. Synthesis by reactive sintering of metal (or metal hydrides) and boron at
temperatures below the melting point
3. Reducing the mixtures of metal oxide with B2O3, e.g., by aluminum, magnesium,
silicon, or carbon
4. Reaction of metal, metal oxide, or metal hydrides with boron carbide, with or
without the addition of B2O3
5. Electrolysis of fused-salt baths containing metal oxide and boron oxide
6. Deposition of boride layers from vapour phase, e.g. hydrogen reduction of boride
halides in the presence of metal or its halides
Among various synthesis methods, electrochemical synthesis and solid-state reactions have
been developed to produce finer TiB2 powder in large quantity. Borothermic reaction is an
example of solid-state reaction, which can be illustrated by the following reaction:
2TiO2 + B4C + 3C –> 2TiB2 + 4CO ( 2-8)
Typical oxygen and carbon content in as-synthesized TiB2 is less than 0.5 to 0.6 wt%
respectively. Synthesised TiB2 powder is observed to have finer sizes with particle size
distribution with a D50 value around 1.1 mm 32
. It is worthwhile mentioning here that it is
now possible to produce large quantity (kilogram scale) phase pure TiB2 powders on both
laboratory and commercial scale using borothermic reduction process.
A potential way to produce submicron-sized TiB2 powder is mechanical alloying of a
mixture of elemental Ti and B powders. The elemental powders were found to react to form
stable TiB2. It was noted that the size of the transition metal and the heat of formation of
borides greatly affected the mechanical alloying time, while producing finer size TiB2 32
.
27
Self-Propagating High-Temperature Synthesis (SHS) is an advanced technology for the
synthesis of a wide variety of inorganic compounds, either as powders or near net-shape
products. In this method, synthesis progresses by exploiting the heat-energy released by the
exothermic reaction of raw materials via a self-sustaining combustion wave, which
propagates, from one end of the specimen to the other. Ultrafine (nanometric) TiB2 powder
could also be produced through a SHS process involving addition of varying amounts of
NaCl. As the amount of NaCl (diluents) increases, the particle size of TiB2 was found to
decrease, reaching 26 nm in case of 20 wt% NaCl addition. The ignition temperature for the
stoichiometric mixture of TiO2, H3BO3 and Mg was found to be as low as 685°C 32
.
2.5 TiB2-based cathode technologies
As mentioned, titanium diboride and composites containing a major fraction of TiB2 have
appeared to be the best candidate for wettable cathodes. The use of pure TiB2 as a wettable
cathode has suffered from several problems 12, 15, 22, 30
:
Low sinterability because of its low diffusion coefficient
Expensive fabrication costs
Brittle nature and poor thermal shock resistance
Being subjected to inter-granular corrosion by molten aluminum
Difficulty of retrofit into the existing cells
Due to the production difficulties and high fabrication costs the amount of RHM used has
considered to be kept at minimum in some efforts. Some researchers tried to cover the
surface of carbonaceous cathodes with coatings, tiles or pieces sticking out from the surface
12. Acceptable cost, ease of application and strong and stable adhesion to the substrate are
required to make these cathodes interesting to the industry.
Raynolds Company tested hot-pressed and sintered TiB2 bars in a pilot scale cell on 1962
30. They claimed to have produced flawless TiB2 parts with good quality and high density.
However, even these parts had the major problem of crack propagation, associated with
28
inter-granular corrosion. Impurities in TiB2 powder such as carbon and oxygen precipitate
at grain boundaries resulting in subsequent inter-granular penetration of sodium and
aluminum which initiated slow-developing cracks. According to McMinn 30
, the task to
keep the tiles or plates in place on the substrate proved to be really difficult and efforts to
solve this problem were never entirely successful and breakage of TiB2 parts frequently
occurred during the operating in the electrolysis cell.
Raynolds also developed TiB2-AlN-Al cermets, as well as graded cermets with the metal
phase enriched away from the pure TiB2 surface 30
. Although these composites improved
the abovementioned problem caused by impurities in TiB2, they increased the electrical
resistivity of the components and did not completely eliminate the slow crack and crack
propagation problem.
In 1980-1990s, more emphasis was put upon technical solutions that apply TiB2-carbon
coatings or fabricated TiB2-graphite (TiB2-G) composites 12
. Provided that a high enough
TiB2 content is present in the mixture, it was expected that such materials have acceptable
electrical conductivity, partly inert towards electrolyte and molten aluminum and proper
wetting by the aluminum. However, these materials have problems majorly due to the
formation of aluminum carbide in service, leads to degradation and failure of the cathode
parts 12
.
TiB2-carbon coatings with high porosity and permeability have a problem following metal
and salt penetration, as aluminum carbide build-up at the coating-carbon interface causing
the degradation of electrical contact 12
.
In 1984, Martin Marietta Aluminum has reported 38
the application of a 1 cm layer of TiB2-
carbon paste on carbon cathode substrates. It was followed by curing and carbonization to
temperatures of 600-1000°C. The author reported that throughout the test period muck did
not adhere to the coated cathode surface and was more easily dispersed. During normal
operation of the test cells the current efficiency increased approximately 2%. The
29
technology then was acquired by Comalco and the development work of this coating has
been continued in Australia 30
.
TiB2-G composites developed by Great Lakes and Reynolds have been tested in pilot cells
since 1985 12
. They selected these composite materials over hot-pressed TiB2 parts to
reduce materials and processing costs and to increase thermal shock resistance. Exposure of
TiB2-G components in liquid aluminum indicated a gradual dissolution/erosion caused by
penetration of molten aluminum into the bulk porosity of the fabricated shapes but was
limited to the thin outer skin. Aluminum penetration only progressed deeper into the body
when loose material was removed from the outer edges 12
.
Pilot reduction cell tests were also conducted with the TiB2-G composite (90 wt% TiB2-10
wt% graphite) fabricated into mushroom-shaped cathode elements 30
. The elements were
stood out, wetted and drained above the metal pool. However, they had the same problem
as for the TiB2-G composite parts.
It is possible to apply a relatively thin layer of TiB2 coating with the thickness of about 1
mm on the carbon cathode substrate by various techniques including electro-deposition 39
,
plasma spraying 40
, glazing with a powder layer, or chemical vapour deposition. Most
coating techniques, however, are generally not suitable for utilization on an industrial scale.
In addition, it is essential that the coating prevent sodium and carbon interaction and
sodium related buckling damages, while a thin coating is susceptible to crack and
delaminates from the carbon during cell operation 41
.
Some efforts have been focused on the development of relatively inexpensive wettable
cathode coatings which contain large amount (20 to 50 wt%) of a carbonaceous pitch or
resin binder 42-44
. However such coatings also deform and swell because of the absorption
of sodium 41
.
The degradation of TiB2 materials with the TiC secondary phase is caused by the
penetration of Al and its reactions with TiC. The reaction forms Al4C3 phase with increased
molar volume, which builds up internal stresses and possibly induces crack formation and
30
by the way increases the rate of degradation. Such effect has been reported for the reaction
4Al + 3TiC = Al4C3 + 3Ti 45
.
In an effort to avoid the presence of carbon phase in the composition, which results in
formation of aluminum carbide, a TiB2-based non-carbonaceous coating for cathode blocks
has been developed and tested on number of cells. This coating contains a small amount
(less than 10 wt%) of a non-carbonaceous inorganic binder which is mostly colloidal
alumina 41
. The coating can be applied by painting one to several layers on the cathode
surface of the lined cell. An aluminum sheet is placed on the top of the coating before
preheating and allowing it to melt, prior to adding the cryolite and starting the cell
operations. Although the wettability and beneficial physical properties of the coating have
been claimed, there is still the sodium-trapping and the formation of sodium aluminate
during the initial stages of cell operation. Sodium penetrates the pores and partially reacts
with the alumina contained in the coating. However, the absorption is considerably less
than what the pitch in the carbon cathode can absorb 41
.
Having investigated several components and methods, which have been proposed as
wettable cathodes, it was concluded that the proposed material should mainly consist of
TiB2 (TiB2-based). In addition, the components used as sintering aids should promote the
formation of electrically conductive phases with low reactivity and solubility in molten
aluminum at grain boundaries.
2.6 TiB2-based cathodes
Sintering of TiB2 as a polycrystalline bulk material for industrial applications is a challenge
due to its high melting point (~3000°C) and low diffusion coefficient. For this reason, very
high temperatures are required for the activation of the transport mechanisms in TiB2-based
materials. Along with the lower porosity obtained from increasing the sintering
temperatures, an exaggerated grain growth also takes place, degrading the mechanical
properties. The presence of titanium oxides, on the surface of particles enhances the
material transfer at temperatures above 1700°C resulting in a dramatic grain growth.
31
Controlling grain growth is important since microcracking is known to occur above a
critical grain size 45
. Therefore, the consolidation of TiB2-based materials using commercial
powders is limited to temperatures below 1700°C 46
. A very fine powder, sintering aids or
hot pressing are necessary in order to obtain high density and at the same time control grain
growth during sintering.
Different techniques have been used for sintering pure titanium diboride such as hot-
pressing 47-49
, hot isostatic pressing 50
, pressureless sintering 47, 51, 52
, reactive electric
discharge sintering 53
and spark plasma sintering 54
.
Most studies used hot pressing to achieve a significant improvement in densification 47, 55,
56. Some others used pressureless sintering, but the sintering temperature was higher than
1800°C 47, 51, 52
. Hot pressing is an effective densification process and has been a major
fabrication route for dense TiB2 bodies. However, it is relatively expensive and not proper
for the production of large and complex shapes 47
. The cost of fabrication, size limitations,
machining difficulties and some mechanical problems have made hot-pressed TiB2 solution
less attractive in recent years 12
.
Pressureless sintering is a less expensive route for fabricating of near net-shaped large
parts, but high-temperature sintering of 2000°C causes exaggerated grain growth that
results in a decrease of the mechanical properties and thermal shock resistance. Therefore
the use of low-melting-point sintering additives was proposed which allows the
pressureless sintering of TiB2-based materials at relatively lower temperatures through
liquid-phase sintering.
2.6.1 Use of metallic sinter additives
The rather low self-diffusion coefficient of TiB2 caused it’s low sinterability 52
. Therefore,
various sintering additives have been used to facilitate its sintering and increase the
densification. Metals such as Fe, Ni, Co, Cr, Mn have appropriate melting points, above
operating temperature of cell and well below the melting point of TiB2, and possess very
good wetting properties on TiB2 to promote liquid phase sintering 52
. They enhance the
32
densification of TiB2 liquid phase sintering by the presence of eutectic reactions at
relatively low temperature 57, 58
. It has been suggested that this eutectic reactions are based
on the reaction of metallic additive (Ni, Co, Cr, etc.) with TiB2 forming various metal
borides with low melting temperature e.g. Fe3B 58
. These borides also exhibit good wetting
behaviour. Sintering experiments using metallic additives have demonstrated that the very
dense TiB2 parts with very high hardness can be achieved by liquid phase sintering 32
.
Kang and Kim 51
investigated the effect of Cr and Fe on densification and mechanical
properties of TiB2 ceramics fabricated by pressureless sintering. They used 0.5 wt% Cr and
0.5 wt% Fe and sintered the specimens at 1800 and 1900°C for 2 h and the densities of
97.6% and 98.8% of theoretical density were achieved respectively. Figure 2–5 shows the
triple junction of grains and its related energy dispersive spectra (EDS). The authors
suggests liquid phase sintering mechanism. They were suggested that Ti dissolves into the
Cr–Fe solution at the sintering temperature and a Ti-rich liquid phase was formed which
may have a good wettability with TiB2. They believed that this Ti-rich liquid phase
enhanced mass transfer and this accelerated densification. The microstructure of the
specimen sintered at lower temperature showed equiaxed grains with uniform size
distribution but sintering at 1900°C led to an excessive grain growth.
Figure 2–5- Transmission electron micrograph of the specimen with 0.5 wt% Cr and 0.5
wt% Fe and energy dispersive spectra of X-ray microanalysis at a triple junction 51
.
33
However, the fracture toughness of TiB2 containing metallic additives and sintered at
1800°C is as low as that of monolithic TiB2, since the binder phases obtained after sintering
are mainly composed of brittle phases 57
.
Liquid phase sintering with metallic additives enhances mass transport but simultaneously
exaggerated grain growth of TiB2 crystals at much lower processing temperatures than that
of binder-less TiB2 due to dissolution precipitation phenomena 59
. This exaggerated grain
growth results in spontaneous microcracking of TiB2 during cooling, since high residual
stresses are developed among larger TiB2 grains due to their highly anisotropic thermal
properties 32, 57
.
Addition of grain growth inhibitor such as metal borides (TaB2 and W5B2) and carbides
(WC or TiC) has shown to avoid exaggerated grain growth. However, these additives do
not significantly improve mechanical properties due to the dominant effect of the binder
phase. Einarsrud et al 52
studied the effect of adding relatively small amounts (1-5%) of Ni,
NiB and Fe as sintering aids to promote liquid sintering of TiB2. They also added carbon to
some samples to reduce the amount of oxygen impurities from the starting powder. The
samples were sintered both under vacuum and argon atmosphere at the sintering
temperature varied between 1300 and 1700°C. High densities (>94% theoretical density)
were obtained for samples sintered at temperatures higher than 1500°C. Sintering under
vacuum resulted in the higher weight loss and lower density of specimens. A significant
grain growth was observed in the specimens containing Ni, NiB and Fe during sintering at
1700°C. The exaggerated grain growth 52
was observed to be related to the oxygen content
of the samples and to temperature. They proposed a mechanism that is dependent on
surface diffusion through an oxide layer and they consider that the surface diffusion is
enhanced by a titanium oxide rich surface layer 52
. The addition of carbon strongly reduced
the oxygen content and thereby, inhibited grain growth, but it increased the porosity as well
47.
34
2.6.2 Use of ceramic sinter additives
Apart from to the metallic additives, various non-metallic additives were also used to
enhance the sinterability and mechanical properties of TiB2 parts. Although the addition of
metallic additives improves the sinterability of TiB2, they generally degrade some
properties of the ceramics e.g. the fracture toughness. Therefore, non-metallic additives are
used for reasons such as to improve sinterability without grain growth or to retain good
oxidation resistance at high-temperatures 32, 48, 55, 60
.
It has been reported that some non-metallic additives could also promote the liquid phase
sintering of TiB2 and significantly enhance the density and reduce the grain size by the
secondary phase formation. It would be considered that the quantity of additives has
important effect on final density and grain size which must be investigated in each
particular case 32, 55, 60
.
Non-metallic additives are typically added in higher amount to densify TiB2, while a much
smaller amount of metallic additives is used to obtain dense TiB2 32
. A combination of high
Vickers hardness (20–27 GPa) and moderate indentation toughness (4–7 MPa.m1/2
) is
obtainable with the use of a large variety of non-metallic sinter additive (added in an
appropriate amount). A modest flexural strength of 500 MPa or higher is also measured,
depending on the density of sintered TiB2 32, 48, 55, 59, 60
.
Recently, Murthy et al. 55
reported that MoSi2 enhances the densification of TiB2 via liquid
phase sintering (LPS) and the formation of TiSi2 when hot-pressed at 1700°C for 1 h in
vacuum. The addition of MoSi2 does not degrade the mechanical properties and also exhibit
better wear resistance against bearing steel when compared with monolithic TiB2. They
detected the presence of a SiO2-rich layer on the surface. In their next work 56
, the addition
of TiSi2 as a sintering aid was explored. The hot-pressing experiments were conducted at
temperatures between 1400 and 1650°C on the samples containing 0–10 wt% TiSi2 for 1 h.
The sample with 5 wt% TiSi2 and hot-pressed at 1650°C showed the optimal results of high
hardness of 25 GPa, an elastic modulus of 518 GPa, an indentation toughness of ~ 6
35
MPa.m1/2
, a four-point flexural strength of more than 400 MPa, and an electrical resistivity
of 10 μΩ.cm.
Similarly, Torizuka et al. 60
observed the formation of grain boundary liquid phase
(amorphous SiO2), when SiC was used as an additive. They achieved densities greater than
95% of theoretical density by adding 2.5-5.0 wt% SiC and sintering temperature of 1700°C.
They also reached 99% of theoretical density by hot isostatic pressing (HIP) of TiB2- 5
wt% SiC at 1700°C. Optimising the amount of binder and sintering temperature is critical
for obtaining higher densification and improved mechanical properties through finer grain
size. They suggested that the improved sinterability of TiB2 resulted from the SiO2 liquid
phase that was formed during sintering when the raw TiB2 powder had 1.5 wt% of oxygen.
The effect of SiC and ZrO2 on sinterability and mechanical properties of titanium diboride
was investigated by Torizuka et al. 61
. The combined addition of ZrO2 and SiC were found
to be effective in improving the sinterability and mechanical properties of TiB2. The
density of TiB2 and TiB2–20ZrO2 (wt%) after sintering at 1700°C was 70% of theoretical
density. The addition of ZrO2 alone had therefore, little effect in improving the sinterability
of TiB2. However, the addition of SiC was found to be effective in improving the sintered
density. For example, the density of TiB2–19.5ZrO2–2.5SiC (wt%) was 97% of theoretical
density. It was reported that TiO2, existing on the surface of TiB2 powder, reacted with SiC
and formed TiC and SiO2.
Park et al. 48
investigated the effect of hot pressing temperature (1500–1800°C) on the
densification behaviour of TiB2–2.5Si3N4 (wt%). A considerable increase in density at
1500–1600°C is attributed to the formation of silica (SiO2) during hot pressing. Unlike the
density, the average grain size increased steadily as the sintering temperature is increased.
This result is in contrast to the case of transition metal additions, where extensive grain
growth occurs during densification. In the TiB2–Si3N4 composite system, the presence of
reaction products such as TiN and BN has been observed. The fracture toughness decreased
steadily as the Si3N4 addition was increased 48
.
36
When a small amount of AlN (5 wt%) was added to TiB2, the rutile phase (TiO2), present
on the TiB2 powder surface was eliminated by a reaction with AlN to form TiN and Al2O3.
The elimination of TiO2 markedly improved the sinterability and consequently the
mechanical properties of TiB2. It should be pointed out that large AlN addition (>10 wt%)
decreased the sinterability and mechanical properties, apparently owing to the
remaining/unreacted AlN 62, 63
.
As it was stated in this part, there are some ceramic materials, which have the potential to
be used as proper additives for sintering of TiB2. The use of ceramic sinter additives could
be considered as an alternative of the metallic additives for certain application of TiB2-
based materials.
Chapter 3:
Thesis outline
38
3.1 Objectives
The objectives of this project were defined with the aim of developing wettable cathodes
with regard to the huge potential of energy savings in this field. A review of the basic
knowledge of primary aluminum production and earlier efforts on the development and
application of suitable wettable cathodes for aluminum electrolysis was presented in the
previous chapter. After reviewing the conditions of electrolysis bath and the issues with
common carbon cathodes, particularly the energy loss caused by non-wettability for liquid
aluminum, the importance of the development of wettable cathodes as a solution becomes
more clear. TiB2 has been always the most trusted materials in the researches to develop
wettable cathodes because it fulfills the property requirements of this application. However,
fabrication of suitable TiB2-based cathode parts encounters some difficulties and despite a
lot of efforts on the development of TiB2-based wettable cathode since 1950’s, no proper
commercial product is available yet. Reviewing the previous works provides a lot of useful
ideas and insights for further investigation on this subject.
The objective of this project was to develop TiB2-based ceramic materials meeting the
property requirements of a suitable wettable cathode. In other words, the developed
materials must have the physical, chemical, mechanical and metallurgical properties equal
to or superior to the current carbon cathodes. They should also possess good wettability for
molten aluminum (<90) and the electrical resistivity lower than 500 cm and most
importantly, the grain boundaries of such materials must have physical and chemical
stability in molten aluminum at 960C to keep the integrity of the part in electrolysis cell
during the cathode life cycle.
In addition to the material characteristics, the process proposed for the fabrication of the
developed wettable cathodes is of great importance. Although methods such as HP, HIP
and SPS are already used for the production of TiB2-based materials, they are not suitable,
either technically or economically, for the fabrication of large cathode parts in industrial
scale. In this project, pressureless sintering was selected as it has the capacity to produce
large-scale near net shape parts with lower investment and operating costs. The important
39
concern with sintering of TiB2-based parts is that sintering at temperatures higher than
1700°C results in exaggerated grain growth and hence low mechanical properties and
thermal shock resistance due to the hexagonal crystalline structure of TiB2. Therefore, the
addition of metallic sintering aids was suggested in order to provide liquid phase and to
promote sintering at lower temperatures. In addition, metallic additives do not have
negative effect on the electrical conductivity. These additives should promote the formation
of phases in grain boundaries with low reactivity and solubility in molten aluminum
without deteriorating the wetting properties of TiB2. The composition of sintering additives
as well as processing parameters has a great influence on the final properties of the sintered
parts. Therefore, the investigation of the effect of additives composition and processing
parameters on the characteristics of consolidated specimens as well as their behaviour and
stability in liquid aluminum was also part of the project objectives.
3.2 Choices of sintering additives
As mentioned in previous sections, TiB2-based ceramic is the most trusted material for
application as wettable cathode in aluminum electrolysis. However, monolithic TiB2
ceramic has low sinterability. It has also poor resistance to thermal shock due to its thermal
expansion anisotropy. Addition of sintering aids could enhance the sinterability and the
thermal shock resistance of TiB2 32
. Metallic additives such as Fe, Co or Ni improve the
densification of TiB2 via liquid phase sintering by the presence of eutectic reactions at
relatively low temperatures 51, 52
. However, the residual binder phases after sintering are
mainly comprised of phases which could be attacked by molten aluminum and cryolite and
consequently decrease the resistance and stability of the specimens in the bath conditions.
Studies have shown that the grain boundary chemistry is more important than the density
and the strength of TiB2 material used as cathode during Al electrolysis 45
.
In the preliminary experiments, we have introduced boron filament in molten aluminum
and we found that above the certain Ti concentration, the filament will have chemical
stability and will not dissolve in molten aluminum. TEM investigation revealed the
formation of TiB2 layer on the surface of boron filament, which protects the filament from
40
dissolution in molten Al. In fact, when the concentration of Ti in liquid aluminum is more
than 200 ppm of Ti, segregation of TiB2 on the surface of boron is energetically favourable.
Based on this result, we proposed that the controlled addition of Ti to the powder mixtures
as sintering aid might promote the segregation of TiB2 phase at the grain boundaries, which
is durable in liquid aluminum. In addition, the binary phase diagram of Fe-Ti, Figure 3–1,
shows that the Fe-Ti system forms a liquid phase over a wide range of compositions at
temperatures higher than 1450°C. They specially have a eutectic point at around 30 wt% Fe
with a melting point of 1085°C. Fe has been suggested as a proper sintering additive for
liquid phase sintering of TiB2 51
. As conclusion, the mixture of Ti and Fe was selected as
sintering additive to enhance the sinterability by forming the liquid phase during
pressureless sintering of TiB2-based wettable cathode parts.
Figure 3–1- Binary phase diagram of Fe-Ti 64
.
41
3.3 Originality of the project
Several works have been previously reported on development of TiB2-based ceramics as
wettable cathode for aluminum electrolysis industry 12, 15, 22
. However, none of these
materials has been widely used to replace common carbon cathodes in industrial scale. The
majority of works on the fabrication of dense TiB2 cathodes have focused on costly and
complicated fabrication methods. The main disadvantage of the proposed fabrication
methods is their inability to form the designed final shape of cathode lining due to their
technical limitations. Another limitation of the previous researches is the addition of
components to TiB2 which react with the bath compounds mainly molten aluminum and
cryolite 30, 45
. The products of such reactions can destroy the TiB2 grain junctions by
penetration and swelling which lead to separation of TiB2 particles and thereby cathode
abrasion 41
. Some efforts have been focused on using carbonic additives to fabricate TiB2-
based composites or coatings, but the problem of sodium penetration and swelling still
exists 41
. Use of colloidal alumina bonding for coating of TiB2 was also investigated.
Although the wettability and beneficial physical properties of the coating have been
claimed, there is still the sodium-trapping and the formation of sodium aluminate during
the initial stages of cell operation 41
.
In this project, for fabrication of TiB2-based cathode, inexpensive pressureless sintering
method has been used which permits the production of large-scale cathode parts with the
designed final shape at relatively lower costs. The use of Ti as a major metallic additive has
been also investigated. The effect of the excess amount of titanium on sintering of TiB2-
based cathodes had not been previously studied. The processing parameters including
starting powder particle size, sintering additives composition and content, milling
conditions, compacting conditions, sintering cycle, temperature and atmosphere were
investigated and modified to achieve dense parts with required properties. Besides
performing general physical, mechanical and metallurgical characterizations of the
developed materials, other properties for wettable cathode application such as interactions
and wettability by liquid aluminum, stability in molten aluminum and the nature of grain
42
boundaries and inter-particle bridges were studied as well. The majority of literatures found
on the fabrication of consolidated TiB2-based materials do not contain most of these
characterizations, which are essential for cathode application.
Another important achievement of this project was the obtaining of uniformly distributed
pores within the microstructure of the developed TiB2-based material, which could
potentially help prevent crack propagation and failure of the parts during service due to the
probable thermal shock and molar volume changes, caused by the interaction of
components with liquid aluminum. This aspect is proposed to considered in the target
microstructure of TiB2 ceramics for wettable cathode application in future investigations
and in further modifications of the fabrication process parameters.
Chapter 4:
Materials and methods
44
4.1 Introduction
In this project, starting powders were prepared by mixing of TiB2 powder with sintering
additives using high-energy ball mill. Compaction performed in uniaxial die to form the
green parts. They were then sintered under the flow Ar/5%H2 reducing atmosphere for 1 h
at temperatures between 1400 and 1650C. The physical and mechanical properties of
specimens were measured and the microstructures were studied. Their wettability for
molten aluminum was evaluated and their stability in molten aluminum at 960°C was
investigated. The general information about the experimental procedure as well as
characterization methods is explained in this chapter. Further details are provided at the
materials and methods section of each article.
4.2 Experimental procedures
4.2.1 Starting powders
The control of the powder quality has a great influence on the production of green body and
the final sintered microstructure. The powder characteristics of greatest interest are the size,
size distribution, morphology, degree of agglomeration, chemical composition, and purity
65. The specifications of starting TiB2 and additive powders used during the project are
shown in Table 4–1. These materials were purchased from Atlantic Equipment Engineers
Inc. in powder form.
Table 4–1- Starting powders specification
Substances Particle size Purity
TiB2 2-10 micron > 99.7%
Ti < 20 micron > 99.7%
Fe 1-9 micron > 99.9%
45
4.2.2 Powder processing
From the results of preliminary experiments the total amount of 10 wt% of metallic
additives was selected to be added to TiB2 powder for preparing the powder mixture. The
additives were constituted of Ti and Fe powders, either separately or in pre-alloyed form.
Different mixtures of additives were investigated to determine the proper composition for
desired application.
To achieve homogeneous compositional distribution, the powder blends were mixed in
high-energy ball mill (SPEX 8000, Spex Industries, Inc.) using hardened steel vial and balls
with a ball-to-powder weight ratio of 4:1. The particle size distribution was determined
using Laser Scattering Particle Size Distribution Analyser (LA-900, HORIBA).
Pre-alloying of Ti and Fe powders was performed, first by mixing titanium and iron in a
70:30 Ti:Fe weight ratio and then by pressing the powder mixture at 400 MPa using an
uniaxial steel die. The compacted specimens were then sintered at 1150°C for 1 hour. The
resulting pellets were subsequently crushed and milled using high-energy ball milling for 1
h to obtain the pre-alloyed additive in powder form.
4.2.3 Forming method
Uniaxial dies were used to compact the powder mixtures into green parts. The compressing
pressure of 150 MPa was selected from the results obtained during preliminary
experiments. Three cylindrical dies with 13 mm, 16 mm and 25 mm diameters and one
rectangular die with the dimensions of 35 mm × 15 mm were used.
The RHM powders do not exhibit plastic flow even at high pressure; therefore, special care
should be taken during compaction process in order to achieve relatively uniform compact
density in the specimen and to prevent residual internal stresses.
4.2.4 Consolidation and sintering
Sintering of specimens was performed in the temperatures ranging between 1400 and
1650C. Green parts were placed on a high alumina plate (Al2O3 > 99.5%, Anderman
46
Ceramics Co.) and were inserted in a high temperature tube furnace (INP15-20, Norax
Canada inc.). The flow Ar-5%H2 reducing atmosphere was used during sintering process.
The heating rate was about 6C /min and the specimens were maintained at sintering
temperature for 1 h. The specimens were then furnace cooled. Figure 4–1 shows an
example of sintering profile used in the experiments.
Figure 4–1- Diagram of sintering cycle
47
4.3 Characterisation methods
The physical and mechanical properties of specimens including as density, electrical
conductivity and flexural strength were determined in order to study the effect of
fabrication parameters on their properties with regard to their application as wettable
cathode for aluminum electrolysis. The wettability behaviour of specimens for liquid
aluminum was also investigated. Chemical stability of selected specimens in molten
aluminum at 960°C was then studied. Morphology and microstructure of specimens were
characterized using optical microscope (OM), scanning electron microscope (SEM) and
transmission electron microscope (TEM). Compositional and phase analysis of samples
were performed using X-ray diffraction and energy dispersive spectroscopy.
4.3.1 Bulk density and apparent porosity measurements
The bulk density of compacts was determined using the Archimedes method with
isopropanol as the immersing medium, which is applicable to almost all refractory shapes,
only if they have sufficient structural integrity to permit handling. In this method the
specimen was weighed in dry state (WD), then it was immersed in iso-propanol while its
weight was recorded in real time by a computer. The specimen was kept inside the liquid
since there were no more significant changes in the measured weight, which was assumed
as apparent immersed weight (WI). The density of the specimen (DS) was calculated using
these weights and the density of iso-propanol alcohol at experiment’s temperature (DL):
( ) ( 4-1)
Theoretical density was estimated using the rule-of-mixtures calculations that assumed the
nominal compositions of the powder specimens as specified, neglecting the limited
products of the interface reactions. The theoretical density of pure dense TiB2 fired bodies
was considered as 4.52 g/cm3
66. The theoretical density of Fe, Ti, and Al were also
considered as 7.87, 4.50, 2.70 g/cm3 respectively
67. Relative densities were calculated by
dividing the measured bulk density by the calculated theoretical density. Based on
48
replicated measurements on identical specimens, the uncertainty on relative density was
estimated to be less than ±1%. Hence, no error bar was included in the figures.
4.3.2 Mechanical properties evaluation
The evaluation of mechanical properties of the brittle ceramics is usually performed using
transverse bending test, in which a rod specimen (with either circular or rectangular cross
section) is bent under a three-point or four-point loading technique until fracture. In this
technique the bottom surface of specimen is placed under a tension stress, since the upper
surface is in the state of compressive stress. Considering that the compressive strength of
ceramics is higher than their tensile strength in the order of ten, the samples are always
fractured starting from their bottom surface; the flexure test is a reasonable substitute for
tensile strength. Since during bending the specimen is subjected to both compressive and
tensile stresses, the magnitude of its flexural strength is greater than its tensile fracture
strength 68
.
Figure 4–2- Schematic of three-point loading for measuring the flexural strength of
ceramics 68
.
The flexural strength of TiB2-based specimens in this project was measured using three-
point bending method with a 25.4 mm span at a deflection rate of 0.5mm/min following
49
ASTM C1161-02 standard method 69
. This test method covers the determination of flexural
strength of advanced ceramic materials at ambient temperature.
For three-point test, flexural strength (MPa) of rectangular specimens, S, was calculated
based on following equation:
( 4-2)
where:
P = breaking force (N),
L = outer (support) span (mm),
b = specimen width (mm),
d = specimen thickness (mm) 68, 69
.
4.3.3 Measurement of electrical resistivity
For the measurement of electrical resistivity at ambient temperature, a specimen was placed
between two copper plates, and pressure was applied (10 MPa) to obtain a good electrical
connectivity. The current density of about 1 A/cm2 was applied which is similar to the
current density of cathodes at cell condition. The resistance was measured and the electrical
resistivity (ρ) of the specimen was calculated using the following equation:
( 4-3)
where R is the electrical resistance, A is the contact surface area and l is the specimen’s
thickness.
22
3
bd
PLS
50
4.3.4 Wettability in liquid aluminum
The wettability of specimens by molten aluminum was investigated using sessile drop
technique. The surface of the Al pellet was polished prior to the test in order to reduce
surface oxides. The surface of specimens was also polished before the tests to remove
surface contamination, especially oxides. Polishing was carried out using a diamond
abrasive (6 µm) followed by cleaning with isopropanol in an ultrasonic bath. An aluminum
piece (90 mg) was placed on the surface of the specimen that was then heated up rapidly to
960°C under vacuum (10-3
Pa) and kept at this temperature. A light was fixed at one end of
the tube and the image of the Al drop over the specimen was recorded at the other end
during the experiment. The schematic of the setup used for this experiment is shown in
Figure 4–3. A software was used to evaluate the contact angle between the specimen
surface and the aluminum drop from the recorded images. The reported contact angle is the
average of left and right side angles. The time t=0 was set when the specimens’ temperature
reached 700°C approximately and a spherical liquid Al drop formed over the surface of the
sample. After the experiment, the furnace was cooled down at a rate of about 15°C/min
below the melting point of pure aluminum.
Figure 4–3- Schematic of setup used for sessile drop test and wettability investigation
4.3.5 Chemical stability and durability to liquid aluminum
Chemical stability and durability of specimens in liquid aluminum were also evaluated. The
specimen was glued to the tip of an alumina rod, using ceramic glue (Aremco Ceramabond
51
571), and it was then inserted into liquid aluminum under protecting argon flow at 960°C.
The surface of the specimen was covered by pure aluminum foil to protect the surface from
the oxidation during the insertion process. The specimen was removed after the test, cross
sectioned, polished and analyzed by SEM, EDS, EPMA, and TEM in order to examine the
microstructure and to evaluate their interaction with liquid aluminum.
4.3.6 Scratch test
The scratch test was conducted at room temperature by using a micro-tribometer test
system (UMT-2; CETR). The specimen surface was polished down to 6 µm diamond
abrasive paper prior to the test. The specimen was fixed to the lower holder, which was
automatically driven along a single horizontal axis while a conical diamond indenter
mounted in an upper holder sliding over the surface of the specimen and applying a vertical
force. The cone angle of the diamond indenter was 75o and its diameter tip was 400 µm.
The vertical component of the force (Fz) was increased gradually from 2 to 50 N over the
10 mm sliding distance. The horizontal component of the force (Fx), applied to the
specimen through the diamond indenter, was measured in a real time with a dynamometer
and reported as the test result.
4.3.7 Microstructural characterisation
Microstructure characterisation of the processed TiB2 specimens included optical
microscopy, scanning electron microscopy, and transmission electron microscopy. For OM
and SEM analysis, specimens were cut by automatic cutting machine (Struers) using a
Diamond Wafering Blade (Buehler) to obtain their cross section. Then, they were mounted
in epoxy resin and hardener (Struers) under vacuum. The cross sections were grounded and
polished to 0.1 µm surface finish using successively finer Diamond Grinding Discs
(Buehler) and diamond pastes. The final polishing was performed using a 0.05 µm alumina
suspension.
For the exposed specimens to aluminum, the infiltrated aluminum was removed by soaking
in a 0.3 N sodium hydroxide solution for 48 h at room temperature. Once the infiltrated
52
aluminum was removed, a porous structure, mainly composed of a TiB2 solid skeleton, was
obtained and characterized using SEM.
The SEM secondary electron images were used to observe the morphology and the back-
scattered electron imaging provided a distinctive image of different phases based on their
compositional differences.
TEM sample preparation was performed using focus ion beam (FIB; Hitachi FB2000A)
milling. TEM (Jeol JEM-2100F) observation enabled us to study the location and
composition of inter-particle bridges and grain boundaries as well as the nature of phases in
the microstructure.
4.3.8 Compositional and phase analysis
Phase analysis of the bulk of each sample was identified by X-ray diffraction (XRD;
Siemens D5000) using Cu Kα radiation at a scanning rate of 1.min-1
in the 2θ range of 25-
80. The detection limit of XRD apparatus was about 5 wt%. Energy dispersive
spectroscopy (EDS; PGT Avalon) was also used to identify the elemental composition of
the phases.
For precise element analysis of secondary phases, electron microprobe analysis (EMPA;
SX-100 CAMECA microprobe) was used. EMPA uses a high-energy focused beam of
electrons for detecting and measuring characteristic X-rays. Its electron beam current is
roughly 1000 times greater than that in a SEM. These higher beam currents produce more
X-rays from the sample and improve both the detection limits and accuracy of the resulting
analysis. Analysis locations are selected using a light optical microscope, which allows
accurate positioning to about 1 micron.
Chapter 5:
Pressureless sintering of TiB2–based composites using Ti
and Fe additives for development of wettable cathodes
Hamed Heidari1; Houshang Alamdari
1; Dominique Dubé
1; Robert Schulz
2
1 Department of Mining, Metallurgical and Materials Engineering, Université Laval, Québec (QC), Canada G1V 0A6
2 Hydro-Quebec Research Institute, 1800 Boul. Lionel Boulet, Varennes, QC, Canada J3X 1S1
This article was presented in TMS 2011 international conference and was published in the
journal: Light Metals 2011, P. 1111-1116.
54
5.1 Résumé
La diborure de titane est le matériau le plus prometteur pour la fabrication des cathodes
mouillables destinés à la production de l’aluminium. Il est considéré comme une alternative
au carbone afin de réduire la distance cathode-anode, ce qui entraine une meilleure
efficacité énergétique dans les cellules d'électrolyse. Dans ce travail, des spécimens à base
de TiB2 ont été consolidés en utilisant des additifs métalliques suivis par un frittage en
phase liquide sans pression. Différentes proportions de fer et de titane (≤ 10% en poids) ont
été étudiés pour la fabrication des additifs. Le frittage a été réalisé entre 1400-1650°C sous
atmosphère contrôlée. Les effets de la composition, de la température de frittage, du temps
de broyage ainsi que le pré-alliage des additifs sur la densification, la microstructure et les
propriétés mécaniques ont été étudiés. Il a été constaté que le pré-alliage et le temps de
broyage avaient une influence significative sur la densification, l'uniformité de la
microstructure et la résistance à la flexion. L’utilisation des additifs pré-alliées, broyés
pendant 30 min et frittés à 1650°C/1 h a permis d’obtenir une microstructure uniforme, et
sans fissures avec une distribution uniforme des pores ainsi qu’une densité relative
maximale de 91%. Une résistance à la flexion de 300 MPa a aussi été obtenue.
5.2 Abstract
Titanium diboride is the most promising candidate material for development of wettable
cathodes for aluminum smelting. It is considered as an alternative for carbon cathodes in
order to reduce the anode cathode distance resulting in higher energy efficiency in
electrolysis cells. In this work, TiB2-based ceramic specimens were consolidated using
metallic additives followed by pressureless sintering. Different proportions of iron and
titanium (≤ 10 wt%) were used as low melting point sintering additives. Sintering was
conducted at 1400–1650°C under controlled atmosphere. The effects of composition,
sintering temperature, milling time and pre-alloying of the additives on densification,
microstructure, and mechanical properties were investigated. It was found that pre-alloying
and milling time have significant influence on densification, microstructure uniformity and
bending strength. Uniform crack-free microstructure with even distribution of pores as well
55
as maximum relative density of 91% and bending strength of 300 MPa were obtained using
pre-alloyed additives, milling time of 30 min and sintering for 1 h at 1650°C.
56
5.3 Introduction
Liquid aluminum reacts with almost all materials with only a few having good stability 25
.
Most of the stable materials are very expensive metals or non-conductive ceramics, which
are major obstacles for their application as cathode material. Nevertheless there are some
electrically conductive ceramics such as graphite and TiB2. Graphite has been used for
more than a century in aluminum electrolysis cells 14
. However, liquid aluminum does not
wet graphite. Thus a relatively thick liquid metal pad is kept on top of the graphite cathode
to avoid the diffusion of electrolytes through the cathode blocks and to insure good
electrical current distribution within the cell. The magnetic fields present in smelting cells
apply significant Lorentz forces on the metal pad resulting in wave creation. In order to
avoid the short circuits between the metal pad and anode, the anode-cathode distance is
kept large (typically 4.5 cm) unnecessarily increasing the bath resistance 12, 13
.
TiB2 has very high melting point (about 3000°C), low density, excellent strength, high
hardness, and very good thermal and electrical conductivities 33, 70, 71
. It is chemically stable
in and well wetted by liquid aluminum 12, 13, 15
. It has been therefore the most promising in
the attempts to find an alternative material for carbon cathodes since the search began in the
1950’s 22
. Despite its extraordinary properties, strong covalent bonding and low diffusion
coefficient make sintering of TiB2-based ceramics quite difficult 33
.
Fully dense TiB2 is probably not necessary for cathode application. It has been shown that
using dense TiB2 cathodes results in early failure by cracking 30
. Liquid aluminum reacts
with impurities at grain boundaries and, after a period of time, results in the formation of
new phases, internal stress build up and crack formation 45
.
A number of techniques have been used to consolidate TiB2 49, 53, 60, 72
. Pressureless
sintering is a low cost technique to produce large and near net-shape components. However
to consolidate pure TiB2 with this technique, very high sintering temperatures are required
resulting in exaggerated grain growth and reduced mechanical properties. It has been
reported that at temperatures above 1700°C, the presence of titanium oxide at the surface of
57
particles increases both pore and grain size by increasing the surface diffusivity 46, 47
. In
industrial conditions, it is difficult to remove this oxide layer. Thus, it is preferred to sinter
TiB2-based ceramics below 1700°C. At these relatively low temperatures the use of
sintering additives are almost unavoidable to provide a liquid phase promoting
consolidation of TiB2-based composite. Under these conditions, the sintering of TiB2-based
composite requires an appreciable amount of liquid phase, wettability of TiB2 by the liquid
phase, and small solubility of the solid phase in the liquid 73
.
In this study, titanium and iron were used as additives to reduce the sintering temperature.
Titanium was chosen as the principal metallic additive. Upon infiltration of aluminum into
the porous cathode, it could react with the titanium additive to produce TiAl3 with a
melting point higher than that of aluminum. TiAl3 also shows a very good wettability with
respect to molten aluminum. Although TiAl3 is soluble in liquid Aluminum, it has been
shown to be stable when formed at the surface of TiB2 74, 75
. Iron, in turn, was chosen to
somewhat reduce the melting point of additives. Ti and Fe have a eutectic at 1078°C and
71.1 mol% Ti 76
. These metals wet the surface of TiB2 77
while TiB2 has a small solubility
in liquid Ti-Fe 78
.
The TiB2-Fe system is characterized also by a eutectic at 1340°C and 6.3 mol% TiB2 79
.
The reaction between TiB2 and Fe may accelerate densification and lead to the formation of
Fe2B. This phase could cause deterioration in the mechanical properties as well as the
resistance to liquid aluminum. The presence of titanium in the liquid mixture could prevent
the formation of Fe2B 80
. Fe can also react with liquid aluminum to form FeAl3 having a
melting at about 1160°C 81
.
In this work, the effects of different compositions, processing conditions, and sintering
temperature on density, microstructure and mechanical properties were investigated. A total
amount of 10 wt% Ti and Fe was selected as metallic additives to provide about 10 vol% of
liquid phase during sintering.
58
5.4 Materials and methods
Commercial TiB2, Ti and Fe powders (Atlantic Equipment Engineers Inc., Bergenfield, NJ)
were used as starting materials. The particle size of TiB2 powder was between 2 and 10 µm
with a mean size of 6 µm. Its purity was >99.7 % and the impurities were C, N, O and Al.
For Ti powder the particle size was <20 µm and for Fe powder, the particle size was
between 1 and 9 µm.
The TiB2 powder was mixed with selected proportions of Ti and Fe powders and then
milled in a high energy ball mill (SPEX 8000, Spex Industries, Inc., Edison, NJ) using
hardened steel vial and balls with a ball-to-powder weight ratio of 4:1. Ti and Fe powders
were added to TiB2 either separately or after being pre-alloyed.
Pre-alloying of Ti and Fe powders was performed, first by mixing titanium and iron in a
70:30 Ti:Fe weight ratio and then by pressing the powder mixture at 400 MPa using an
uniaxial steel die. The compacted specimens were then sintered at 1150°C for 1 hour. The
resulting pellets were subsequently crushed and milled using high-energy ball milling for 1
h to obtain the pre-alloyed additive in powder form. XRD analysis showed the presence of
α-Ti and the FeTi intermetallic compound in this powder.
The TiB2-Ti-Fe powder mixtures were pressed at 150 MPa in a uniaxial die to form pellets
of 16 mm in diameter and bars of 38 × 13 mm. The specimens were then heated in a tube
furnace (INP15-20, Norax Canada inc., QC) at a rate of 6°C/min from room temperature to
the specified sintering temperature. Sintering of pellets was performed under an Ar/5%H2
protective atmosphere for 1 hour. The various experimental conditions of this study are
given in Table 5–1.
59
Table 5–1- Experimental conditions used for consolidation of specimens
No. Code* Additives wt%** Sintering
Temperature (°C) Pre-alloying
Milling time
(min) Ti Fe
1 T8F2M10 8 2 1400-1600-1650 - 10 2 T7F3M10 7 3 1400-1600-1650 - 10
3 T8F2M30 8 2 1650 - 30 4 T7F3PM10 7 3 1600-1650 yes 10 5 T7F3PM30 7 3 1650 yes 30 6 T7F3PM60 7 3 1650 yes 60 7 T7F3PM120 7 3 1650 yes 120 8 T7F3PM240 7 3 1650 yes 240
*T: Titanium, F: Iron, P: Pre-alloying, M: milling time
**Unless noted, all compositions in this article are in weight percent
The green density of specimens was evaluated by measuring their weight and geometrical
dimensions. The bulk density of sintered specimens was determined using the Archimedes
method with isopropanol as the immersing medium. Theoretical density was estimated
using the rule-of-mixtures calculations that assumed the nominal compositions of the
powder specimens as specified. Relative densities were calculated by dividing the measured
bulk density by the calculated theoretical density. Based on replicated measurements on
identical specimens, the uncertainty on relative density was estimated to be less than ±1%.
Hence, no error bar was included in the figures.
The bending strength of the sintered specimens was measured using the three-point bending
test with a 26 mm span at a loading rate of 0.5 mm/min according to the ASTM C1161
standard 69
. The dimensions of the test specimens used for bending strength measurements
were 38 mm × 13 mm × 4 mm.
For microstructural investigations, the specimens were cut with a diamond saw and
polished to 0.1 µm surface finish using successively finer diamond abrasives. The
microstructure of specimens was investigated using a scanning electron microscope and the
chemical microanalysis was performed by energy dispersive X-ray spectroscopy (EDX;
PGT Avalon, Princeton, NJ). The crystalline structure was determined by X-ray diffraction
method (XRD; Siemens D5000) with a Cu Kα radiation at a scanning rate of 1° min−1
.
60
Wettability of sintered specimens was studied by placing a 90 mg aluminum piece at the
surface of sintered specimen surface and heating under high vacuum (1.2E-5
mbar) to
960°C. The wetting angle was monitored using an instant imaging system. From these
images, contact angles can be measured as a function of time.
5.5 Results and discussion
5.5.1 Effect of additive composition
The relative density was measured for specimens with two different compositions after
sintering at 1400, 1600 and 1650°C. As shown in Figure 5–1, at all sintering temperatures,
specimens containing 7 wt% Ti and 3 wt% Fe (T7F3M10) had higher density than that of
specimens containing 8% Ti and 2% Fe (T8F2M10). According to the Fe-Ti phase diagram
82 the additive with a mass ratio of 7Ti:3Fe is closer to eutectic. A lower melting point leads
to earlier formation of liquid phase during sintering, therefore promoting better
densification.
Figure 5–1- Comparison of the relative density as a function of sintering temperature
and composition of sintering additives (T8F2M10: TiB2+8%Ti+2%Fe; T7F3M10:
TiB2+7%Ti+3%Fe).
61
5.5.2 Effect of sintering temperature
As shown in Figure 5–1, for both compositions (T7F3M10 and T8F2M10), there is not
much densification after sintering at 1400°C. However, sintering at 1600 and 1650°C
resulted in an appreciable densification to approximately 70%. Between 1600 and 1650°C,
there is no further densification. An SEM backscattered (BS) micrograph of the T8F2M10
specimen, sintered at 1400°C, is presented in Figure 5–2. It shows that the additives formed
segregated phases. A temperature of 1400°C, well below the melting point of Fe and Ti, is
not high enough to provide the liquid phase required to promote densification. Moreover,
these additives were not locally mixed in the proper ratio and were not in intimate contact
with each other.
When Fe and Ti particles are in intimate contact, solid-state diffusion occurs at the interface
resulting in the formation of a thin liquid layer in between. Increasing the sintering
temperature to 1600°C resulted in the formation of significant amount of liquid and
consequently in higher densification of specimens.
Figure 5–2- Backscattered SEM micrograph of T8F2M10 (TiB2+8%Ti+2%Fe)
specimen, sintered at 1400°C for 1 h (The arrows show segregated phases containing the
additives).
62
5.5.3 Effect of pre-alloying additives
Besides the uniform distribution of additives, it is important to have Ti and Fe particles in
contact with each other to promote the formation of the liquid phase. Hence, the addition of
pre-alloyed additives, instead of adding Ti and Fe separately, was considered to achieve
this goal. The pre-alloyed additives were prepared by mixing, pressing, and sintering Ti and
Fe powders with a mass ratio of 7:3.
Table 5–2 compares the relative densities of specimens with pre-alloyed additives
(T7F3PM10) with those obtained by adding the additives separately (T7F3M10) after
sintering at two different temperatures. Under the same processing and sintering conditions,
pre-alloying of the additives resulted in better densification. The difference is significant at
1650°C.
Table 5–2- Relative density of specimens with separate (T7F3M10) and pre-alloyed
(T7F3PM10) additives
Specimen Relative density (%)
Green Density Sinter. 1600°C Sinter. 1650°C
T7F3M10 59 72 72
T7F3PM10 62 74 80
5.5.4 Effect of milling time
Milling was performed in order to achieve a uniform distribution of additives. However,
milling time should be as short as possible to reduce costs and to prevent oxidation of
powders. To investigate the effect of milling time on the densification process, powder
mixtures were milled for different times prior to sintering. Preliminary results showed that
by increasing the milling time from 10 to 30 min, density after sintering increased. These
preliminary experiments suggest that the milling time has an important influence on
densification. The effect of milling time was further investigated in a systematic way for
specimens containing 90 wt% TiB2, 7 wt% Ti, and 3 wt% Fe using five different milling
63
times (10, 30, 60, 120 and 240 minutes) followed by compaction and sintering at 1650°C.
(Specimens 4-8, Table 5–1).
The densities of specimens (green and after sintering) were plotted as a function of milling
time in Figure 5–3. No significant influence of milling time on green density was observed.
However specimens milled for 30 min showed a maximum density of 91% after sintering.
Further milling resulted in a slight decrease in density. Figure 5–4 shows that the three-
point bending strength of sintered specimens follows a similar trend: a maximum bending
strength of 300 MPa was achieved for specimens milled 30 min.
Figure 5–3- Influence of milling time on relative density of green and sintered specimens
(TiB2+7%Ti+3%Fe) using pre-alloyed additive and sintered at 1650°C for 1h.
64
Figure 5–4- Influence of milling time on bending strength of specimens
(TiB2+7%Ti+3%Fe) prepared using pre-alloyed additive and sintered at 1650°C for 1h.
In order to understand the influence of milling time on sintering, the particle size
distribution was determined and XRD analyses were performed on milled powders while
the microstructure of sintered specimens was investigated by SEM.
The effect of milling time on the particle size distribution of powders is shown in Figure 5–
5. After 10 min of milling, the powder mixture is mainly composed of particles with a
mean size of 6 micrometers similar to that of the starting TiB2 powder. However, a wider
particle size distribution was observed. This distribution widening as well as the appearance
of a shoulder at around 2 micrometers is most likely due to the TiB2 particle fracturing and
refining during milling. In addition, EDX analysis of the very large particles showed that
the peak at 200 micrometers is related to the Ti and Fe pre-alloyed particles. Milling of
mixed powders for 10 min reduced the particle size of additive powders, but some large
additive particles remained. Milling for 30 min, however resulted in a quite different
particle size distribution. The distribution is much wider and shifted toward the small
diameters. The quantity of particles smaller than 0.7 micrometer increased, and the peak
related to the metallic additive particles disappeared. This suggests that milling for 30
65
minutes results in a good refining and dispersion of metallic additives within the powder
mixture and provides partial refining of TiB2 particles (particles smaller than 0.7
micrometer).
Figure 5–5- Effect of milling time on the particle size distribution for powder mixtures
containing the 70%Ti and 30%Fe pre-alloyed additive.
By increasing the milling time to 60 min, a second peak appeared in the particle size
distribution at around 100 micrometers. Since the powder samples are deagglomerated
using an ultrasonic bath prior to analysis, the presence of this second peak suggests the
formation of strong agglomerates in the powder. By further increasing the milling time, the
quantity of these strong agglomerates increases but no significant increase is observed in
the quantity of small particles. EDX analysis of large agglomerates showed that they were
rich in Ti and Fe. They are usually formed by plastic deformation and cold welding of
smaller particles and are very difficult to deagglomerate even in an ultrasonic bath.
66
The typical shape of the large agglomerates observed after 240 min of milling is shown in
Figure 5–6. These large particles are basically composed of TiB2 particles welded together
by metallic additives.
Figure 5–6- SEM micrograph of a large agglomerate formed after 240 min milling in
T7F3PM240 powder (TiB2+7%Ti+3%Fe).
The XRD patterns of the TiB2 powders milled for 10 and 240 min are shown in Figure 5–7.
The peaks were slightly broadened after 240 min of milling while the intensities decreased
owing to the overall decrease of the crystal size of TiB2. At the resolution of these x-ray
scans, the minor phases corresponding to the pre-alloyed additives were not detected.
67
Figure 5–7- XRD analysis of powders containing pre-alloyed additives after 10 and 240
min milling. (Cu Kα).
SEM micrographs of polished sections of specimens containing pre-alloyed additives and
sintered at 1650°C are shown in Figure 5–8 to Figure 5–10. In Figure 5–8, the
microstructure of the specimen milled for 10 min revealed a highly porous structure. The
high level of porosity explains the low density (84%) and reduced bending strength of this
specimen (197 MPa). By increasing the milling time to 30 min (Figure 5–9), a more
uniform and denser microstructure was achieved after sintering. A significant increase of
density (91%, Figure 5–3) and bending strength (300 MPa, Figure 5–4) was observed for
this specimen compared with the previous one.
As shown in Figure 5–5, after 30 min of milling, there was a refinement of the particle size
and a broader distribution was observed leading to higher densification. During liquid
phase sintering, densification is mostly caused by rearrangement of particles upon
formation of the liquid phase 83
. Further densification is achieved by the solution-
precipitation process: small particles promote this stage due to their higher surface energy
and therefore higher solubility in the liquid phase 83
. A broader particle size distribution
increases the overall contact area between particles and eases the particle rearrangement in
68
the early stage of sintering. Moreover, the presence of small particles can help the solution-
precipitation stage. As a result, higher densification and bending strength could be achieved
after 30 min of milling.
By further increasing milling time, densification and bending strength decrease. As
revealed by the microstructure of T7F3PM120 specimens ball milled for 120 min (Figure
5–10), cracks were formed after sintering. These cracks explain the dramatic decrease of
bending strength (Figure 5–4). Crack formation was attributed to the presence of hard
agglomerates in the powder mixture. As shown in Figure 5–6, these large agglomerates are
formed by the cold welding of TiB2 particles with additive particles. In the early stage of
milling, the TiB2 particles are partially refined and stick to the additives. Upon further
milling, the TiB2 particles become embedded in additives and form large and dense
agglomerates. Upon sintering, these large agglomerates shrink initiating cracks around
them in the compact. This phenomenon has also been reported previously 73, 83
. These
cracks limit the densification of the sintered specimens and reduce their strength.
Figure 5–8- Backscattered SEM micrograph of T7F3PM10 specimen
(TiB2+7%Ti+3%Fe) milled for 10 min and sintered 1 h at 1650°C.
69
Figure 5–9- Backscattered SEM micrograph of T7F3PM30 specimen
(TiB2+7%Ti+3%Fe) milled for 30 min and sintered 1h at 1650°C.
Figure 5–10- Backscattered SEM micrograph of T7F3PM120 specimen
(TiB2+7%Ti+3%Fe) milled for 120 min and sintered 1 h at 1650°C.
70
5.5.5 Wettability and stability in liquid aluminum
Since specimens milled 30 min with pre-alloyed additives (T7F3PM30) show the best
density, strength and uniform microstructure, their wettability by liquid aluminum was
investigated. Figure 5–11 shows images of the aluminum drop on the surface of T7F3PM30
specimen at 960°C during the wettability test. From these images, the contact angles were
measured as a function of time. The first image taken as the temperature reached 960°C
(t=0) shows that the liquid Al drop was almost spherical. The contact angle between liquid
aluminum and the specimen at this moment was 169°. After a while, the contact angle
started to decrease. After 60 min the contact angle was 96° and only 14° after 175 min.
After 185 min, liquid aluminum was completely spread over the surface, which indicates
that wetting occurs quite rapidly on this specimen and it has good wettability for liquid
aluminum.
Figure 5–11- Behavior of liquid Al drop over T7F3PM30 specimen (TiB2+7%Ti+3%Fe)
during the wettability test at different time. (The time from beginning of test are
reported in minutes)
The stability and reactivity of T7F3PM30 specimen in liquid aluminum have also been
investigated. The specimen keeps its integrity after being exposed to liquid aluminum
during 24h. Detailed results of these experiments will be published in an upcoming report.
71
5.6 Conclusions
TiB2-based composites with 10% of Ti and Fe additives were consolidated using
pressureless sintering. Specimens with 7%Ti+3%Fe additives showed better densification
due to the formation of liquid phase during sintering. Best results were obtained for a
sintering temperature of 1650°C. Pre-alloying of Fe and Ti before addition to TiB2 powder
significantly improved the densification. The milling time has also a marked influence on
densification and on the properties of the sintered TiB2 specimens. A maximum relative
bulk density of 91% and maximum bending strength of 300 MPa were achieved with
specimens milled for 30 min and sintered at 1650°C for 1h. The micrographs of specimens
milled for 30 min reveal a uniform crack free microstructure with an even distribution of
pores while those milled for longer times show the presence of numerous cracks in the
specimens. The sintered specimens showed some resistance in liquid aluminum although
more tests are needed. The resistance of specimens against aluminum infiltration and
erosion are under investigation.
5.7 Acknowledgement
The authors wish to acknowledge the kind collaboration of the technicians of the Dept.
Mining, Metallurgical and Materials Engineering of Laval University and of Sylvio Savoie
from Hydro-Quebec. The financial support of this project was provided by Hydro Quebec
and the Natural Sciences and Engineering Research Council of Canada (NSERC). The
research project was also partially financed by the “Fonds Québécois de la Recherche sur la
Nature et les Technologies (FQRNT)” via the Aluminum Research Centre – REGAL.
Chapter 6:
Investigating the potential of TiB2–based composites with
Ti and Fe additives as wettable cathode
Hamed Heidari1; Houshang Alamdari
1; Dominique Dubé
1; Robert Schulz
2
1 Department of Mining, Metallurgical and Materials Engineering, Université Laval, Québec (QC), Canada G1V 0A6
2 Hydro-Quebec Research Institute, 1800 Boul. Lionel Boulet, Varennes, QC, Canada J3X 1S1
This article was presented in Thermec 2011 international conference and was published in
both the journal of the: Materials Science Forum, 2012, Vol. 706-709, P. 655-660; and the
journal of the: Advanced Materials Research, 2012, Vol. 409, P. 195-200.
73
6.1 Résumé
Dans ce travail, les matériaux céramiques poreux à base de TiB2 ont été frittés en phase
liquide à l'aide de Ti et Fe comme additifs métalliques afin d'effectuer le frittage aux
températures inférieures de 1700°C. Il a été montré que les paramètres de procédé, y
compris la durée du broyage avaient un effet considérable sur les propriétés finales des
spécimens frittés et leur comportement dans l'aluminium fondu. Les études de
microstructures ont été réalisées en utilisant le microscope optique, le MEB et la
microsonde électronique. Il a été trouvé que les spécimens avec une microstructure
uniforme et sans fissure pourraient être produits en utilisant des poudres pré-mélangées et
broyées pour une durée aussi courte que 30 min, avant le pressage et le frittage. Le test
mouillage avec la goutte a été effectué sur les échantillons broyés pendant 30 et 240
minutes. Leur interaction avec l'aluminium fondu a également été étudiée. Il a été trouvé
que le temps de broyage de 30 min permet à une meilleure conductivité électrique, ainsi
qu’une bonne mouillabilité et une bonne stabilité dans l'aluminium liquide.
6.2 Abstract
In this work, porous TiB2 ceramics were consolidated by pressureless sintering method
using metallic Ti and Fe as additives in order to perform sintering at temperatures lower
than 1700°C. It was shown that processing parameters including milling time of the starting
mixture had a considerable effect on final properties of sintered specimens and their
behaviour in molten aluminum. Microstructural studies were carried out using optical
microscope, SEM and EPMA. It was found that specimens with uniform and crack-free
microstructure could be produced using the pre-mixed powders milled for as low as 30 min
prior to compaction and sintering. Sessile drop test was performed on the specimens milled
for 30 and 240 minutes. Their interaction with molten aluminum was also studied. It was
found that 30 min milling time resulted in better electrical conductivity, wettability and
stability in liquid aluminum.
74
6.3 Introduction
TiB2-based ceramics have been studied since 1950’s as alternatives for carbon cathodes 21
.
Despite their widespread use for more than a century in aluminum smelting industry,
carbon cathodes are not ideal materials from the energy efficiency point of view 10
. The
issue with carbon cathodes is that they are not wettable by molten aluminum which results
in an increase in energy consumption for the production of primary aluminum. As they are
not wetted by aluminum, the gap between the cathode surface and aluminum pad increases
the electrical resistivity. In order to have a better contact, it is necessary to increase the
thickness of the pad. Moreover, a relatively large anode-cathode distance (ACD) must be
maintained to avoid electrical shortcut due to turbulence generated by Lorentz forces. The
gap and the superior ACD increase the resistivity and energy loss in the cell 10, 16
.
Improving the energy efficiency in energy-intensive industries such as aluminum
production has become critical due to the rising cost of energy. Wettable cathodes represent
therefore an interesting solution for saving energy 12
.
Numerous researches have been focused on the fabrication of wettable cathodes, and a wide
range of processing methods and materials including TiB2-based materials have been
proposed 15, 22
. However, none of the proposed solutions has yet been used in commercial
scale either because they are not economically feasible or because it is technically too
difficult to fabricate large cathodes. From the technical point of view, using highly dense
TiB2 components is not a viable solution because molten aluminum reacts with grain
boundaries after extended immersion time causing internal stresses at grain boundaries of
TiB2 due to volume expansion of reaction products. These stresses eventually result in
rapid crack propagation and failure of immersed components 30, 45, 84
. Considering these
issues, an economical process must be developed to fabricate large near net shape and
porous TiB2-based cathodes.
The pressureless sintering of TiB2-based composites for wettable cathode application was
previously investigated 1. The effect of composition, sintering temperature, pre-alloying of
additives and milling time on density, bending strength and microstructure were studied 1.
75
It was found that better density and bending strength could be achieved using pre-alloyed
Ti-Fe additive of near eutectic composition (70:30 Ti:Fe wt. ratio) and sintering
temperature of 1650°C. It also has been shown that the milling time of powder mixtures
had an important effect on the final properties of the specimens. Increasing the milling time
from 10 to 30 min increased the relative density from 84 to 91% and the bending strength
from 197 to 300 MPa. Further increase of milling time reduced these properties and a
milling time of 240 minutes resulted in relative density of 87% and bending strength of 192
MPa. In addition, shorter milling time reduces the production cost as well as the risk of
oxidation of starting powders which are important from industrial and technical points of
view.
In this work, the effect of milling time on microstructure, electrical conductivity, and
behavior in molten aluminum were studied considering their application as wettable
cathodes. Wettability of TiB2-based composites and its stability in molten aluminum were
investigated.
6.4 Materials and methods
Titanium (Ti >99.8%) and iron (Fe >99.9%) powders (Atlantic Equip. Eng. Inc) were
mixed in 70:30 Ti:Fe wt. ratio, compacted and then sintered at 1150°C for 1 h. The
resulting pellets were subsequently crushed and milled for 1 h using high energy ball
milling in order to obtain the pre-alloyed 7Ti3Fe additive in powder form (particle size
distribution in Fig.1). Commercial TiB2 powder (99.7 % pure, Atlantic Equip. Eng. Inc)
with particle size ranging between 2 and 10 µm was mixed with 10% of the pre-alloyed
7Ti3Fe powder and then milled using high energy ball mill (SPEX 8000) in stainless still
vial and balls (balls/powder ratio: 4/1). The milling was performed for 10, 30, 60, 120 and
240 min to study the effect of milling time on properties of TiB2-based composites. Particle
size distribution of the milled powders was measured using laser scattering particle size
analyzer (LA-900, HORIBA).
76
The milled mixtures were compacted in a uniaxial die under 150 MPa pressure and then
sintered in a tube furnace for 1 h at 1650°C under Ar-5%H2 atmosphere (heating and
cooling ramp: 6°C/min). Specimens were cross sectioned with a diamond saw and polished
down to 0.1 µm surface finish with successively finer diamond abrasives.
Microstructural studies and chemical analysis were carried out using optical microscope,
scanning electron microscope equipped with energy dispersive X-ray spectroscopy (EDX;
PGT Avalon) and electron probe microanalysis (SX-100 CAMECA microprobe).
For measurement of electrical resistivity at ambient temperature, specimen was placed
between two copper plates, and pressure was applied (10 MPa) to obtain a good electrical
connectivity. The resistance was measured and the electrical resistivity (ρ) of the specimen
was calculated using the following equation:
( 6-1)
where R is the electrical resistance, A is the contact surface area and l is the specimen’s
thickness.
The wettability of specimens by molten aluminum was investigated using sessile drop
technique. An aluminum piece (90 mg) was placed on the surface of specimen that was
then heated at 960°C under vacuum (1.2x10-8
bar). The wetting angle was monitored using
an instant imaging system. The contact angle was measured from these images as a
function of time. Starting time (t=0) was considered once a spherical liquid aluminum drop
was formed over the surface.
The chemical stability of specimens in liquid Al was also evaluated. The specimen was
glued (Aremco Ceramabond 571) to the tip of an alumina rod and was then inserted into
liquid aluminum under protecting argon flow at 960°C. The exposure durations were 1h
and 24 h. The specimen was removed after the test, cross sectioned using a diamond saw,
77
polished according to abovementioned method and analyzed by EPMA in order to examine
the microstructure and evaluate their interaction with liquid aluminum.
6.5 Results and discussion
Cumulative particle size distributions of the starting mixtures milled for different period of
time are shown in Figure 6–1. As shown in this diagram, pre-alloyed additive contains
large particles (>30 µm), but most of them were eliminated after 10 min of milling.
Increasing the milling time to 30 min completely eliminated these large particles while the
volume fraction of particles smaller than 4 µm increased. By further increasing the milling
time, large particles reappeared and the volume of the fine particles decreased due to the
formation of large agglomerates.
Figure 6–1- Cumulative particle size distribution diagram of pure TiB2, pre-alloyed
7Ti3Fe, and mixtures after different milling times (M10 e.g. means mixed powder
milled for 10 min)
78
Microstructures of the sintered specimens with different milling time of starting powders
are shown in Figure 6–2. After only 10 min of milling (Figure 6–2-a), large and unevenly
dispersed particles of additives remain visible in the microstructure. The liquid phase did
not infiltrate between TiB2 particles to enhance densification. As a result of these
phenomena, a highly porous microstructure with non-uniform distribution of additives was
formed.
The specimen milled for 30 min (Figure 6–2-b) had lower porosity and uniform
microstructure with even distribution of additives. Their particle size distribution resulted
in a better compaction and therefore sinterability of the powder. The microstructure of the
specimen milled for 240 min (Figure 6–2-c) showed a higher level of porosity compared to
M30, large cracks and segregated additives due to the presence of large agglomerates in the
powder.
The M30 and M240 specimens were then selected for further investigations. The
microstructure of M30 was quite uniform whereas that of M240 was cracked and more
porous. The nature of phases in microstructure of composites as determined by EDX
analysis is given in Figure 6–2 as follows: A: TiB2, B: TiFe, C: αTi, D: TiFe2.
Figure 6–2- Micrograph of specimens milled for a) 10 min, b) 30 min, c) 240 min and
sintered at 1650°C for 1h. (Phases in the microstructure are A: TiB2 ; B: TiFe ; C: α-Ti ;
D: TiFe2)
The electrical conductivity of specimens is an important parameter considering their
application as wettable cathodes. The measured electrical resistivity of M30 and M240
specimens were approximately 54 and 243 µΩ.cm, respectively. The electrical conductivity
79
of M30 was much higher than that of M240 which could be attributed to its lower porosity,
absence of crack as well as more uniform distribution of additives. Although the electrical
resistances of these two specimens were much different, they were well below that of
graphite which is about 1000 µΩ.cm 27
showing that this TiB2-based composite is more
conductive than the usual carbon cathodes.
Figure 6–3- Photo taken from liquid Al drop on the surface of M30 specimen.
The sessile drop technique was used to investigate the wettability of the specimens by
liquid aluminum. Figure 6–3 shows a typical image of a liquid aluminum drop formed over
the surface of M30 specimen during measurement. The wetting angle, θ, was measured
using these images. The wetting angle of M30 and M240 as a function of elapsed time is
shown in Figure 6–4. It shows that the wetting angle of both specimens decrease with time.
However, the curve for M30 presents continuous and smooth changes of wetting angles
with time, whereas for M240, the changes of wetting angle versus elapsed time exhibit a
step-like curve. The wetting behaviour of these specimens can be explained by differences
in their microstructure. For M30 specimen, during the sintering process, liquid phase was
formed upon melting of 7Ti3Fe additives. That liquid entered inside small pores and
applied capillary forces over pore walls resulting in particle rearrangement and
densification. However, for M240 specimen, strong agglomerates composed of intimate
mixture of TiB2 and Ti-Fe particle were formed. Inside these agglomerates, densification
occurred early during sintering leaving large cracks around the agglomerates. During the
sessile drop test of M240 specimen, the sudden reduction of the wetting angle corresponds
80
to a quick penetration of liquid aluminum into these cracks. Generally, the penetration of
liquid aluminum in cracks and pores is a sign of good wettability of the composite.
Figure 6–4- Wetting angle of liquid Al on M30 and M240 specimens as a function of
elapsed time
Another important parameter for wettable cathode materials is their stability during
immersion in molten aluminum. Figure 6–5 shows the EPMA micrographs of M30
specimen after being exposed to molten aluminum for 1 and 24 h. After 1 h, aluminum
wetted the surface as shown in Figure 6–5-a but started to penetrate inside the specimen
only in some areas. This is in accordance with the wetting curve of M30 specimen (Figure
6–4) which shows that complete wetting occurred after about 1 h. As it could be observed
from Figure 6–5-b and c, aluminum started to penetrate inside the specimen and Fe was
dissolved in aluminum and washed out from that area.
For M240 specimen, after 1 h of immersion, aluminum penetrated inside the specimen.
Figure 6–6-a and b shows the penetrated zone. EPMA investigation (Figure 6–6-c) revealed
that liquid aluminum dissolved iron and pushed it further inside the specimen. The
81
concentration of iron in front of the aluminum-penetrated interface is much higher than the
original concentration of iron in the specimen.
The microstructural investigation of cross sections of specimens after 24 h of aluminum
exposure revealed that liquid aluminum penetrated completely inside both specimens
(Figure 6–5-e and Figure 6–6-e). It is interesting to note that specimens maintained their
shape after aluminum penetration and no cracking or failure occurred. It confirms that TiB2
particles sintered together very well and their junctions are resistant to liquid aluminum.
Therefore, this porous TiB2 composite meets an important requirement for wettable cathode
which is resistance to aluminum penetration without cracking.
Figure 6–5- Micrograph of M30 specimens exposed to liquid Al at 960°C: for 1h: a)
BSE micrograph of contact area, b) Mapping of Al element, c) Mapping of Fe element;
and for 24h: d) BSE micrograph of contact area, e) Mapping of Al element, f) Mapping
of Fe element
82
Figure 6–6- Micrograph of M240 specimens exposed to liquid Al at 960°C: for 1h: a)
BSE micrograph of Al penetration zone, b) Mapping of Al element, c) Mapping of Fe
element; and for 24h: d) BSE micrograph of Al penetration zone, e) Mapping of Al
element, f) Mapping of Fe element
The mapping of elemental aluminum in Figure 6–5-e and Figure 6–6-e reveals that less
aluminum penetrated in M30 specimen than in M240 specimen. The lower aluminum
penetration in M30 is a result of the absence of crack in its microstructure. Figure 6–5-f and
Figure 6–6-f show that most of the iron was washed out after complete penetration of
aluminum and only a little trace of iron remained. These results suggest that 30 min of
milling had an important effect on the refinement of particle size and thereby a better
sinterability of TiB2 which led to higher electrical conductivity, enhanced wettability and
stability in liquid aluminum.
The detailed investigation on wettability and aluminum interaction of M30 specimen as
well as its stability in liquid aluminum for prolonged time is ongoing and the results will be
reported later.
83
6.6 Conclusions
TiB2-based porous composites were consolidated from starting powders milled for different
time. The particle size distribution and the microstructure of sintered parts were
significantly influenced by milling time. It was found that 30 min of milling eliminated
large particles and produced a higher volume of fine particles which resulted in a uniform
microstructure after sintering. The electrical conductivity of this specimen was higher than
that of graphite having the highest conductivity among the carbon cathodes. Liquid
aluminum completely wetted the produced TiB2 composites but M30 had a better
wettability due to its uniform and crack-free microstructure. The M30 was stable in liquid
aluminum after 1 h of exposure. Aluminum penetrated completely into M30 and M240
specimens after 24 h, however, the specimens maintained their forms and no sign of crack
propagation and failure was observed. M30 specimen showed better stability in liquid
aluminum due to the absence of cracks in its microstructure and hence lower liquid
aluminum penetration.
Chapter 7:
Interaction of molten aluminum with porous TiB2–based
ceramics containing Ti-Fe additives
Hamed Heidari1; Houshang Alamdari
1; Dominique Dubé
1; Robert Schulz
2
1 Department of Mining, Metallurgical and Materials Engineering, Université Laval, Québec (QC), Canada G1V 0A6
2 Hydro-Quebec Research Institute, 1800 Boul. Lionel Boulet, Varennes, QC, Canada J3X 1S1
This article was published in the: Journal of the European Ceramic Society, 2012, Vol. 32,
Issue 4, P. 937-945.
85
7.1 Résumé
Dans cette étude, la mouillabilité et les interactions des composites poreux à base de TiB2
avec l'aluminium liquide ont été examinées. Les composites de TiB2 ont été frittés en phase
liquide avec des additifs Ti et Fe. Ces composites possèdent une bonne mouillabilité par
l'aluminium liquide. Lors de l'infiltration par l’aluminium liquide, des additifs de Fe et de
Ti sont dissous. Des composés intermétalliques contenant le Ti, Fe et Al sont formés à la
profondeur de pénétration. Puisque ces phases ont des points de fusion supérieure à la
température du bain liquide (960°C), la solidification isotherme a lieu au cours de la
pénétration de l'aluminium fondu. L’aluminium liquide n’attaqué pas le "squelette solide"
des spécimens de TiB2 et aucun signe de gonflement ou de fissuration n’a été détecté.
7.2 Abstract
In this study, the wettability and interaction of porous TiB2-based composites with liquid
aluminum has been investigated. TiB2 composites were consolidated with Ti and Fe
additives using pressureless sintering. The composites show good wettability with respect
to molten aluminum. During liquid infiltration, Ti and Fe additives are dissolved.
Intermetallic compounds containing Ti, Fe and Al are formed within the penetration depth.
Since these phases have melting points higher than the experiment’s temperature (960°C),
isothermal solidification takes place during the penetration of molten aluminum. Liquid
aluminum does not seem to attack the solid skeleton of the TiB2 specimens and no signs of
swelling or cracking were detected.
86
7.3 Introduction
Molten aluminum reacts with almost all materials except with some ceramics such as
borides which exhibit very good stability in liquid Al 25
. Due to its intrinsic stability, high
electrical conductivity and good wettability with respect to liquid aluminum, TiB2 has been
extensively investigated as an alternative for graphite cathodes in aluminum smelters. It has
been mentioned that by replacing graphite cathodes by TiB2 electrodes, more than 10% of
the energy required to produce aluminum could be saved 12, 13, 22
.
However, the fabrication of large and dense TiB2 parts is quite complicated 32, 71
due to the
poor sinterability of the material. Consolidation of pure TiB2 requires very high
temperatures. At temperatures higher than 1700°C however, exaggerated grain growth
occurs leading to materials with poor mechanical and thermal shock resistances 46, 47
. In
TiB2 ceramics consolidated with current methods, liquid Al is able to penetrate the grain
boundaries and this leads to cracking of components due to the low toughness of materials
22, 30, 85. Micro-cracks can result from the anisotropic thermal expansion of TiB2 or from the
formation of phases with higher molar volumes 45
when liquid Al reacts with grain
boundary impurities.
The addition of sintering aids is a way to lower the consolidation temperature and hence
prevent the exaggerated grain growth. The use of iron, chromium and nickel as sintering
aids for TiB2 has been reported 51, 52, 84
. In a previous work, 7wt % Ti and 3wt % Fe were
added to TiB2 particles to promote liquid phase sintering during consolidation 1, 2
. Sintering
of specimens at 1650°C for 1h resulted in a relative density of 91% and a bending strength
of 300 MPa. No attempt was made to achieve higher densities because it was expected that
the presence of uniformly distributed small porosities could help to prevent the propagation
of micro-cracks when samples are in contact with molten aluminum. However, porosities
ease melt penetration since liquid Al wets TiB2 quite well 86, 87
.
In this work, the reaction of porous TiB2 composites containing 7 wt% Ti and 3 wt% Fe
additives with molten aluminum was investigated. Microstructural characterizations were
87
performed in order to understand the reaction mechanisms between the composites and
liquid aluminum.
7.4 Materials and methods
The TiB2 composites were prepared by mixing commercially pure TiB2 powder (2-10 µm)
with 10 wt% of pre-alloyed additives in powder form (7 wt% Ti and 3 wt% Fe). The
additives (a mixture of Ti and FeTi phases) were then milled with TiB2 for 30 min using a
high-energy ball mill. The powder was compacted with a uniaxial pressure and sintered for
1 h at 1650°C under an Ar-5%H2 atmosphere 1.
Sessile drop tests were used to investigate the wettability of the specimens with liquid
aluminum. An Al pellet (0.09 g) was used for the experiments. The surface of the Al pellet
was polished prior to the test in order to reduce surface oxides. The pellet was placed on
top of the specimen in a resistance tube furnace under high vacuum (10-3
Pa). The furnace
was heated up rapidly to 960oC (corresponding to the operating temperature of aluminum
electrolysis cells) and kept at this temperature. A light was fixed at one end of the tube and
the image of the Al drop over the specimen was recorded at the other end during the
experiment. A software was used to evaluate the contact angle between the specimen
surface and the aluminum drop from the recorded images. The reported contact angle is the
average of left and right side angles. The time t=0 was set when the specimens’ temperature
reached 700°C approximately and a spherical liquid Al drop formed over the surface of the
sample. After the experiment, the furnace was cooled down at a rate of about 15°C/min
below the melting point of pure aluminum.
The surface of some TiB2 samples was polished before the tests in order to remove surface
contamination, especially oxides. Polishing was carried out using a diamond abrasive (6
µm) followed by cleaning with isopropanol in an ultrasonic bath. Therefore, experiments
were performed on polished surfaces (identified as S1-P, P: Polished) as well as on as-
sintered surfaces (identified as S2-AS, AS: As Sintered).
88
For one specimen, the sessile test was performed using a bigger Al pellet (0.18 g). In this
case, the early stage of the liquid infiltration process was investigated by interrupting the
experiment after t=100 min. The sample was identified as S3-PP (PP: Partially Penetrated).
In a last experiment, a polished specimen was subjected to a complete sessile drop test then,
another aluminum piece was placed on the same surface and a second sessile drop
experiment was conducted (S4-2D, 2D: 2nd
Drop).
Reactions between liquid aluminum and ceramics were investigated by examining the
cross-sections of the specimens. The samples were mounted in epoxy resin, cut using a
diamond saw and polished down to 0.1 µm. The final polishing was performed using a 0.05
µm alumina suspension. The microstructure of specimens was investigated using a
scanning electron microscope (SEM) equipped with an energy dispersive X-ray detector
(EDX). Electron probe microanalysis (EPMA) was performed for elemental mapping of
aluminum, titanium, iron and oxygen. Focused ion beam (FIB) was used to prepare samples
for transmission electron microscopy (TEM) characterization. Phase identification was
carried out based on selected area electron diffraction (SAED) pattern analysis.
7.5 Results and discussion
7.5.1 Sessile drop tests
Figure 7–1 shows images of a molten aluminum drop on the surface of a polished specimen
(S1-P) during a sessile drop test after different time intervals. The measured average
contact angles (average between the right and left contact angle) are shown below each
figure. During the experiment, the Al drop spreads over the surface and penetrates inside
the specimen. After 9 min, the specimen temperature was about 870°C and there was no
visible wetting. After 22 minutes, the temperature reached 940°C, wetting occurred and the
contact angle was about 85 degrees. The measured contact angles after 30 and 50 min were
29 and 6 degrees, respectively.
89
Figure 7–1- Photos from the contact between a liquid Al drop and a polished specimen’s
surface during a sessile drop test
Figure 7–2 shows the average contact angle as a function of the elapsed time for the
polished (S1-P) and the as-sintered specimen (S2-AS). Two steps can be distinguished in
the case of the S2-AS sample. During the first step (incubation period), the contact angle
decreases very slowly probably because of surface oxides and reaches 120° after about 140
min. In a second step, the drop starts spreading over the surface rapidly and penetrates the
specimen. The contact angle decreases at a much higher rate and reaches 5° after 180 min.
90
Figure 7–2- Average contact angle versus time during sessile drop tests for the as
sintered and polished specimens.
For the S2-AS specimen, the shape of the curve in the second step is similar to that of the
polished specimen for the same range of wetting angles. This suggests that the polishing
eliminates surface oxides and impurities and reduces significantly the incubation period.
7.5.2 Early Stage of Interaction
To study step one and the early stage of the interaction between liquid aluminum and the
as-sintered specimen, an experiment was carried out in which the test was interrupted after
100 min (specimen S3-PP). Figure 7–3 shows the backscattered electron (BSE) micrograph
from the cross section of the specimen-aluminum interface revealing the penetration of Al
inside the specimen.
91
Figure 7–3- BSE micrograph from the cross section of a specimen with partial
penetration of Al (S3-PP)
To investigate if counter-diffusion of elements from the TiB2 specimen towards liquid Al is
taken place, the cross section of the aluminum drop on top of the substrate was analyzed.
Figure 7–4-a shows small white particles found inside the Al matrix. Semi-quantitative
EDX analysis revealed that the composition of these particles corresponds to TiAl3 phase.
Particles of TiAl3 are usually found in aluminum either as a needle-like structure or in the
form of chunky equiaxed particles 29
. These results suggest that the Ti additives in TiB2
dissolve and diffuse in the Al droplet during the test and precipitate as small TiAl3 particles
during solidification 88-91
.
Chemical mapping was performed in selected areas within the Al matrix. A Fe map is
shown in Figure 7–4-b. Contrary to Ti, which was mostly found in the form of Ti-Al
particles, iron precipitated at grain boundaries during solidification.
These results indicate that the metallic Ti and Fe additives are dissolved in the liquid Al
during the sessile drop tests and precipitate in the form of Ti and Fe aluminum phases upon
solidification.
92
Figure 7–4- Partially penetrated test (S3-PP) a, b) BSE micrograph and EDX analysis of
TiAl3 particles formed inside Al drop, c,d) BSE micrograph and EPMA maps of Fe
element within Al drop
The interface region between the Al droplet and the S3-PP specimen’s surface was also
analyzed using EPMA. Figure 7–5-a) and b) show the elemental distribution of aluminum
and oxygen respectively in this region. The mapping of oxygen indicates a 20 µm thick
oxide-rich layer near the interface. Comparison of this map with that of Al reveals that
oxygen is present in the form of aluminum oxide. In the as-prepared specimen, oxygen is
most likely picked-up by the Ti additives during the sintering process. During the sessile
drop test, liquid Al reduces the Ti oxides to form aluminum oxide. A similar observation
was also reported by Pettersen 84
when hot pressed TiB2 specimens containing Ti additives
were put in contact with liquid aluminum. Ti reacts with the oxygen present on the surface
of TiB2 particles and with the oxygen from the atmosphere to form trigonal Ti2O3
93
predominantly. He also mentioned that the reduction of this titanium oxide with liquid
aluminum is thermodynamically feasible at temperatures around 1000°C. According to our
results, titanium oxide is present on the free surface of the particles and in the porosities.
The reaction of titanium oxide with liquid aluminum may result in some reaction products
with higher molar volume. However, the presence of about 9% of porosity in the specimen
provides enough space for these volume changes and thereby prevents the detachment of
TiB2 grains and specimen swelling.
The delay observed before the wetting takes place in the S2-AS case (Figure 7–2) can
therefore be explained by the presence of a thin oxide layer on the surface of sintered TiB2.
However, this surface oxide did not prevent full wetting of specimen ultimately.
Figure 7–5- Elemental distribution of aluminum and oxygen at the drop-specimen
interface after the partially penetrated test (S3-PP)
7.5.3 Later Stage of Interaction
By examining the cross section of specimens after complete sessile drop test, it was found
that the Al penetration resulted in the formation of four different zones. These zones are
identified as zones 1 to 4 in Figure 7–6. The zone 1 showed a high level of porosity with
almost no sign of metallic additives. In zone 2 and zone 3, the pores contain Ti and Fe
aluminum phases in addition of Al. These zones will be discussed in more details later in
94
this work. Zone 4 remained intact. It represents the microstructure of the specimen before
the sessile drop test.
Figure 7–6- SEM micrograph of the cross section of a S1-P specimen after the sessile
drop test
Figure 7–7 shows elemental line scans of Ti, Fe and Al through the cross section of the S1-
P specimen. The approximate boundaries between the different zones are indicated by
dotted-lines. The concentration of aluminum in zone 1 and 2 varies from point to point
depending on pore location and density. Its average concentration in zone 2 is considerably
higher than that in zone 1. It seems that the Al concentration decreases in zone 3 and falls
to zero in zone 4. There is a very low concentration of Fe in zone 1. Fe was detected at
some points in zone 2 and its concentration increases and reaches a maximum in zone 3
before falling to the bulk Fe additive concentration of 3 wt% in zone 4. The Ti distribution
in Figure 7–7 shows only small variations since the signal comes from both TiB2 particles
and the Ti metallic additives.
95
Figure 7–7- Elemental line scans carried out through the thickness of the specimen after
a sessile drop test at 960°C. (Depth=0 is corresponds to the aluminum-specimen
interface at the beginning of the test)
Figure 7–8 shows elemental maps of Ti and Al near the interface between zone 1 and 2.
The maps seem to indicate that the Ti concentration in the pores where Al is present is
lower in zone 1 (darker blue) than in zone 2 suggesting that the Ti additives have been
washed out from zone 1 during the liquid infiltration. The simultaneous presence of Ti and
Al in the pores of zone 2 suggests the presence of Ti-Al phases in this zone.
96
Figure 7–8- Mapping of aluminum and titanium showing the transition between zone 1
and zone 2
Figure 7–9 shows the mapping of Fe and Ti near the interface of zones 2 and 3. The
concentration of Fe in zone 3 is much higher than in zone 2 in agreement with Figure 7–7.
The Ti concentration in pores is lower (darker blue) in zone 3 than in zone 2 and in these
pores, Fe is present instead of Ti. The simultaneous presence of Fe and Al in the pores of
zone 3 suggests the presence of Fe-Al phases in zone 3.
Figure 7–9- Mapping of iron and titanium revealing the transition between zone 2 and
zone 3
97
Finally, Figure 7–10 shows elemental maps near the transition between zones 3 and 4. The
Al concentration decreases down to zero from zone 3 to zone 4 in agreement with the line
scan of Figure 7–7. The Ti content between the TiB2 grains or in the pores seems to
increase as we move from zone 3 to zone 4 in agreement with what as been said previously
regarding zone 3.
Figure 7–10- Mapping of aluminum and titanium between zone 3 and zone 4
Figure 7–11-a) and b) show SEM images of the specimen in zone 2 and 3 respectively. In
zone 2, the phase identified as P1 contains Ti and Al. Studies on the Ti-Al system have
shown that at temperatures between 700 to 1000°C, TiAl3 is formed prior to any other
titanium aluminide phases. It was also reported that this intermetallic compound can
dissolve 1.2 at.% Fe at 1000°C 81
. To verify the exact nature of this phase, TEM analysis
was performed. A TEM micrograph of such a phase is shown in Figure 7–12-a). EDX
analysis and the SAED pattern (Figure 7–12-b) taken from the [010] zone axis of P1
confirm that this phase is TiAl3. This titanium aluminide phase precipitates from Ti
saturated liquid Al in the pores between the TiB2 particles when the liquid phase enters
zone 2.
98
Figure 7–11- BSE micrographs of zone 2 and zone 3. Arrows show the presence of TiAl3
(P1) and Fe-Al compound (P2)
Figure 7–12- TiAl3 precipitate in zone 2, a) Transmission electron micrograph, b) SAED
pattern from the [010] zone axis of TiAl3
The phase identified as P2 in zone 3 (see Figure 7–11-b) contains Al and Fe with traces of
Ti. The phase P1 is also detected in zone 3. Studies have shown that Fe4Al13 and Fe2Al5
phases are more likely to precipitate in the Al rich side of the phase diagram 92
. Although
the growth rate of Fe2Al5 is higher, the formation of Fe4Al13 is dominant in Al-rich
interfaces. Therefore, it is highly probable that the P2 phase is Fe4Al13. The Ti solid
99
solubility limit in that phase is 6.5 at%. Ti can partially replace Fe in certain
crystallographic sites 93, 94
.
TEM analysis was also performed on P2 observed in zone 3 to confirm the nature of the
Fe4Al13 phase (see Figure 7–13-a) and b)). The SAED pattern shown in Figure 7–13 b) is
characteristic of the Fe4Al13 structure.
Figure 7–13- Fe4Al13 phase precipitated in zone 3, a) Transmission electron micrograph,
b) SAED pattern from the [010] zone axis of Fe4Al13
7.5.4 Reaction Mechanism
Based on these results, the reaction mechanism between the liquid Al drop and the
specimen could be described as follows. When liquid aluminum forms over the polished
surface of the specimen, it interacts with surface oxides and three other major
microstructural features: TiB2 particles, pores, and the metallic additives. After the
reduction of surface oxides by liquid aluminum and wetting of the TiB2 particles, the
metallic additives are dissolved and the liquid enters the pores. At the beginning of the test,
the liquid is pure aluminum. As it enters the porous structure, the concentration of Ti and
Fe in the liquid gradually increases. The liquid has a solubility limit for Fe and Ti above
which new phases will precipitate. Based on the binary phase diagrams of Al-Fe and Al-Ti,
100
the solubility limit of Fe and Ti in liquid aluminum at 960°C is about 17 and 2 wt%,
respectively. Figure 7–14 shows the ternary phase diagram of Al-Ti-Fe. In this work, the Ti
to Fe weight ratio was 7/3 and therefore, the concentration of Ti in the liquid should
increase more rapidly than that of Fe.
Since the Fe and Ti content in the liquid is below the solubility limit in zone 1, the additives
in this zone are simply dissolved while the aluminum is penetrating into the specimen.
Once the concentration of Ti reaches the solubility limit near 2 wt%, TiAl3 phase starts to
precipitate forming zone 2. In this zone, the concentration of Fe is still below its solubility
limit (17 wt%), thus Al continues to dissolve the additives and penetrates inside the
specimen until the solubility limit of Fe is reached. This marks the beginning of zone 3
where the Fe4Al13 phase is formed. At this point, the TiAl3 phase continues to precipitate
and this explains the presence of both P1 and P2 phases in zone 3. By the precipitation of
Fe4Al13 and TiAl3, the liquid aluminum is gradually consumed. In the final stage of the
reaction, the liquid aluminum acts as a “transient liquid phase” 95
which means that after
the diffusion of iron and titanium in the remaining liquid, its transforms gradually to solid
phases via isothermal solidification processes.
101
Figure 7–14- Isothermal section of the Al-Fe-Ti phase diagram at 1000°C 88
The formation of zone 3 where the liquid isothermally solidifies by the formation of
aluminide phases raises the question on whether this zone could act as a barrier against
further aluminum penetration. This hypothesis was put to test by performing an additional
sessile drop test on the specimen formerly subjected to this test. The cross section
micrograph of S4-2D specimen is shown in Figure 7–15. Comparing the cross section of
S4-2D with that of the S1-P specimen, we see that the penetration of the second aluminum
drop lead to an increase of the width of zone 1, zone 2, and zone 3.
102
Figure 7–15- SEM micrograph of cross section of specimen subjected to two subsequent
sessile drop tests
This observation suggests that the second drop follows the same reaction mechanism as the
first one resulting in the dissolution of solid phases and precipitation of new phases until
the solubility limits of Fe and Ti are reached. Zone 3 cannot act as a barrier to the
penetration of liquid aluminum.
However, it is important to note that the TiB2 specimens remained intact despite the
penetration of liquid aluminum and the dissolution of the metallic additives. This could be
attributed to the stability of the grain boundaries (bridges) between the TiB2 particles. The
boundaries formed between the TiB2 particles during sintering with Ti-Fe additives are
quite stable in liquid Al. The specimens did not show any swelling or crack in the
microstructure. The expansion of the structure of TiB2 sintered using transitional methods
has already been reported in the literature 96
. Further investigations concerning the stability
of these TiB2 composites in liquid Al will be presented in an upcoming publication.
7.6 Conclusion
The interaction of TiB2-base porous ceramics with liquid Al was investigated. The
reactions were occurring faster on polished surfaces because of the removal of the surface
103
oxide layer. The penetration of the liquid Al drop resulted in the formation of three distinct
zones. Only Al was found in the first zone, TiAl3 was found in the second zone and both
TiAl3 and Fe4Al13 phases were found in the third zone. When penetration of liquid Al into
the material occurs, the metallic additives are dissolved and their concentration increases
gradually. Once the Ti saturation limit is achieved, the TiAl3 phase starts to precipitate
inside the pores (Zone 2). The residual liquid continues to penetrate and dissolve the
additives until the saturation point of Fe is reached leading to the precipitation of Fe4Al13
(Zone 3). Dissolution and precipitation will continue up to the complete depletion of the
liquid phase (Isothermal solidification). Liquid aluminum did not seem to alter the solid
TiB2 skeleton of the specimen and no sign of swelling or cracking was detected.
7.7 Acknowledgements
The authors wish to acknowledge the kind contribution of the technicians of the Dept. of
Mining, Metallurgical and Materials Engineering of Laval University, of Sylvio Savoie
from Hydro-Quebec and of Jean-Philippe Masse from École Polytechnique de Montréal for
TEM analysis. The financial support of this project was provided by Hydro Quebec and the
Natural Sciences and Engineering Research Council of Canada (NSERC). The research
project was also partially financed by the “Fonds Québécois de la Recherche sur la Nature
et les Technologies (FQRNT)” via the Aluminum Research Centre – REGAL.
Chapter 8:
Pressureless sintering of TiB2-based ceramics with Ti-Fe
additives: sintering mechanism and stability in liquid aluminum
Hamed Heidari1; Houshang Alamdari
1; Dominique Dubé
1; Robert Schulz
2
1 Department of Mining, Metallurgical and Materials Engineering, Université Laval, Québec (QC), Canada G1V 0A6
2 Hydro-Quebec Research Institute, 1800 Boul. Lionel Boulet, Varennes, QC, Canada J3X 1S1
This article was published in: Advanced Engineering Materials journal, 2012, Vol. 14, P.
802–880.
105
8.1 Résumé
Le développement d'un procédé approprié pour la fabrication de cathodes mouillables à
base de TiB2 pour l’électrolyse de l'aluminium demeure un défi depuis plus d'un demi
siècle. Dans ce travail, les céramiques à base de TiB2 ont été consolidées via le frittage sans
pression à l'aide des additifs de Ti, Fe et Ti-Fe. La microstructure, les propriétés physiques
et mécaniques ainsi que l'interaction et la stabilité du matériau dans aluminium liquide ont
été examinés. Il a été montré que les spécimens frittés avec l’additive Ti-Fe ont une
excellente stabilité dans l'aluminium liquide car le squelette solide de TiB2 a conservé son
intégrité et la résistance après 5 jours d’exposition dans l'aluminium liquide à 960°C.
L’analyse par le MET a révélé que la formation de ponts entre les particules de TiB2 pur est
la cause de cette bonne résistance dans l'aluminium fondu. Un mécanisme de frittage a été
proposé pour la consolidation de TiB2 avec l’additif de Ti-Fe. Le matériau céramique à
base de TiB2, fritté avec un alliage de Ti-Fe est donc suggéré comme un matériau
potentiellement fiable pour l'application en tant que la cathode mouillable pour électrolyse
de l'aluminium.
8.2 Abstract
The development of a proper processing method for the fabrication TiB2-based wettable
cathodes for aluminum electrolysis has been challenging for more than half a century. In
this work, TiB2-based ceramics were consolidated via pressureless sintering using Ti, Fe
and Ti-Fe additives. The microstructure, physical and mechanical properties as well as the
interaction and the stability of the material in liquid aluminum were investigated. It was
shown that specimens sintered with a Ti-Fe additive have excellent stability in liquid
aluminum as the solid TiB2 skeleton maintained its integrity and strength after 5 days of
exposure in liquid aluminum at 960C. TEM analysis revealed that the formation of inter-
particle bridges of pure TiB2 is the reason for the good resistance of the material in molten
aluminum. A sintering mechanism was proposed for the consolidation of TiB2 with a Ti-Fe
additive. TiB2-based ceramic sintered with a Ti-Fe alloy is suggested as a potentially
reliable material for application as wettable cathode for aluminum electrolysis.
106
8.3 Introduction
The idea of using a wettable cathode in Hall-Héroult aluminum electrolysis cells aiming at
reducing the energy consumption of primary aluminum production was first proposed in
1950’s 21
. Lots of efforts have been made thereafter to fabricate an operational wettable
cathode at reasonable cost while TiB2 has been always the most promising candidate for
this application 12, 22
. In addition to its excellent stability, pure TiB2 has a good wettability
for molten aluminum 29, 97
. Despite these advantages along with high electrical and thermal
conductivity, the use of TiB2-based wettable cathode for aluminum smelting has not yet
been established. This is mainly due to challenges related to the fabrication process and
difficulties of meeting the required properties of the consolidated parts. Considering the
technical and economical aspects, pressureless sintering could be an attractive fabrication
method to make large near-net-shape cathode parts at reasonable cost. However, TiB2 has a
very high melting point (3000C) and a low inter-diffusion coefficient which make
sintering using pressureless method quite difficult 32
.
Pressureless sintering of pure TiB2 is typically performed at temperatures higher than
2000C. However, above 1800C the oxide layer at the surface of TiB2 particles promotes
the growth of some TiB2 grains in preferential directions resulting in exaggerated grain
growth, lowering the mechanical properties and especially the thermal shock resistance of
the consolidated part 47
.
To address this problem, researches have been conducted toward using transition metals as
sintering additives 46, 52, 57, 72, 98-100
. These additives promote the densification of TiB2 parts
at much lower temperatures via liquid phase sintering and reduce the risk of abnormal grain
growth 101
. Although TiB2-based specimens consolidated using these additives are suitable
for wear resistant and structural applications 102
, they require sufficient chemical stability to
be used as cathode in liquid aluminum. Aluminum could penetrate and react with different
phases at the grain boundaries resulting in swelling and degradation of TiB2 parts 84
.
107
In previous works 1, 3, 4
, a near eutectic Ti-Fe sintering additive has been used with the aim
of preventing the formation of undesirable phases at grain boundaries and promoting liquid
phase sintering. The influence of processing parameters was studied because they were
found to have a great impact on the final properties after consolidation. Upon exposure of
sintered specimens to molten aluminum, no sign of expansion, swelling or cracking was
observed. These characteristics were found particularly interesting for wettable cathode
applications. In this work, specimens were further characterized before and after exposure
to molten aluminum. The effect of additives on final microstructure, physical and
mechanical properties as well as stability of specimens in molten aluminum for prolonged
exposure time have been investigated. Other specimens were consolidated using Fe only or
Ti only as additives and their mechanical properties and stability in liquid aluminum were
compared to those obtained for the specimens consolidated with Ti-Fe. The inter-particle
bridges in the specimen with the Ti-Fe additive were studied using transmission electron
microscopy (TEM) to understand the reasons of its good chemical stability with respect to
molten aluminum.
8.4 Materials and methods
Commercial TiB2 powder (99.7 % pure), titanium (Ti >99.8% pure metal basis) and iron
(Fe >99.9% pure metal basis) were used as starting materials (Atlantic Equip. Eng. Inc.).
The particle size of TiB2 powder was ranging between 2 and 10 µm with a mean size of 6
µm. For Ti powder, the particle size was <20 µm and for Fe powder, the particle size was
between 1 and 9 µm. Specimens were consolidated with three different sintering additives:
Ti, Fe, and pre-alloyed Ti-Fe. To prepare the pre-alloyed Ti-Fe additive, Ti and Fe powders
were mixed in a 70-30 weight ratio respectively, compacted in the form of rectangular bars
and sintered at 1150˚C for 1 h. The resulting pellets were subsequently crushed and milled
for 1 h using high-energy ball milling (more details have been provided elsewhere 1).
The powder mixtures were then prepared by milling TiB2 powder with 10 wt.% of additives
in a high-energy ball mill (SPEX 8000) for 30 min using hardened steel vial and balls with
a ball to powder weight ratio of 4:1. The milled mixtures were then compacted in a uniaxial
108
die under 150 MPa pressure and sintered in a tube furnace at 1650˚C under a reducing Ar -
5%H2 atmosphere for 1 h.
The bulk density of the sintered specimens was determined with Archimedes method using
isopropanol as the immersion medium. Theoretical density was calculated using the rule-
of-mixtures assuming the nominal compositions of the starting powder mixtures. Relative
densities were calculated by dividing the measured bulk density by the calculated
theoretical density.
The three-point bending test was performed at room temperature following the ASTM
C1161 standard with a 25.4 mm span and a displacement rate of about 0.01 mm/s 69
. The
dimensions of the specimens used for bending strength measurements were 38 mm × 13
mm × 4 mm and the reported results are the average of measurements on at least five
representative specimens.
The interactions between the sintered specimens and molten aluminum were first studied
using the sessile drop test. A pure aluminum pellet (0.1 g) was placed on top of the
specimen in an electrical tube furnace under a high vacuum (10-3
Pa). The furnace was
rapidly heated up to 960oC (corresponding to the operation temperature of aluminum
electrolysis cells) and maintained at this temperature for 1 h. Prior to the drop test, the
surface of specimens was polished using 6 µm diamond abrasive followed by cleaning with
isopropanol in an ultrasonic bath. After the tests, the microstructures of specimens were
then examined. The dynamic wetting behavior of TiB2-based specimens by molten
aluminum has already been reported 3, 4
.
To evaluate the chemical stability of the specimens in liquid Al, they were covered with an
aluminum foil and then inserted into molten aluminum at 960˚C under a protective flow of
argon. Three different immersion times were used: 1h, 24 h and 5 days. Specimens were
removed after the tests and their microstructure were examined.
For some immersed specimens, the infiltrated aluminum was removed by soaking them in a
0.3 N sodium hydroxide solution for 48 h at room temperature. Once the infiltrated
109
aluminum was removed, a porous structure, mainly composed of a TiB2 solid skeleton, was
obtained and characterized using SEM.
Microstructural studies and chemical analysis were carried out using optical microscope
and scanning electron microscope (SEM) equipped with energy dispersive X-ray
spectroscopy (EDX; PGT Avalon). Electron probe microanalysis (EPMA; SX-100
CAMECA microprobe) equipped with the wavelength dispersive X-ray spectroscopy
(WDS) spectrometers was utilized to perform detailed multi-element compositional
mappings. Specimens were cross sectioned with a diamond saw, vacuum-mounted in epoxy
resin and polished down to 0.1 µm surface finish with successively finer diamond
abrasives. The final polishing was performed using a 0.05 µm alumina suspension. Focused
ion beam (FIB; Hitachi FB2000A) was used to cut out 100 nm thick samples for
examination in transmission electron microscope (TEM; Jeol JEM-2100F). Phase
identification was carried out based on selected area electron diffraction (SAED) pattern
analysis.
A scratch test was used to compare the bonding strength of particles at the surface of
specimens before and after immersion in molten aluminum. The scratch test was conducted
at room temperature by using a micro-tribometer test system (UMT-2; CETR). The
specimen surface was polished down to 6 µm diamond abrasive paper prior to the test. The
specimen was fixed to the lower holder which was automatically driven along a single
horizontal axis while a conical diamond indenter mounted in a upper holder was sliding
over the surface of the specimen applying a vertical force. The cone angle of the diamond
indenter was 75o and its diameter tip was 400 µm. The vertical component of the force (Fz)
was increased gradually from 2 to 50 N over the 10 mm sliding distance. The horizontal
component of the force (Fx), applied to the specimen through the diamond indenter, was
measured in a real time with a dynamometer. A hot-pressed TiB2 specimen obtained from a
commercial supplier (Ceradyne Inc., Costa Mesa, CA, USA) was used to compare the
results of scratch tests. Its reported relative density and flexural strength were 98% and 265
MPa, respectively.
110
8.5 Results and discussion
8.5.1 Influence of additives on physical and metallurgical properties
Specimens with three different sintering additives were consolidated: Ti, Fe, and a pre-
alloyed Ti-Fe powder. The starting compositions of specimens as well as their as-sintered
properties are reported in Table 8–1.
Table 8–1- The starting composition of sintered specimens, their relative density and 3-
point bending strength.
Specimen Composition (wt%)* Relative
density**
(%)
Bending
strength
(MPa) TiB2 Ti Fe
10T 90 10 0 77 -- 10F 90 0 10 90 520 41
7T3F 1 90 7 3 91 300 32 * Unless otherwise indicated, percentages in this text are wt% ** The uncertainty on relative density was estimated to be less than 1%.
The back-scattered electron (BSE) micrographs from the polished cross-section of
specimens are shown in Figure 8–1. Figure 8–1-a) shows the microstructure of the 10T
specimen. Some discontinuities and the lack of integrity can be observed in the
microstructure of this specimen. Arrows indicate the presence of partially fused Ti-rich
phase between TiB2 particles. The relative density of this specimen, as reported in Table 8–
1, is about 77%. Its bending strength was low with widely dispersed measurements.
Usually, in pressureless sintering of ceramics, densification is achieved by formation of a
liquid phase at the early stage of sintering. This liquid phase enters inter-particle spacings
and applies a capillary force to the walls resulting in re-arrangement and densification 83,
103. Since the sintering temperature of 1650C used in this study was slightly below the
melting point of titanium (1660C), no liquid phase is expected to promote the re-
arrangement of particles. However, even a trace concentration of iron contamination
coming from the milling process can drastically reduce the melting point of the Ti resulting
in its partial fusion as shown by the arrows in Figure 8–1-a). The low relative density and
bending strength of the sample with Ti additive is due to the low sintering temperature and
111
its microstructure represents almost the original size and form of the starting TiB2 powder.
The shape of particles is angular and a lot of fine particles are present.
Figure 8–1-b) shows the microstructure of the 7T3F specimen in which a relatively dense
structure of TiB2 grains with a fine distribution of additives and pores is observed. This
specimen was sintered using a pre-alloyed Ti-Fe additive with a near eutectic composition
of 70%Ti-30%Fe (7T3F). In the Ti-Fe system, an eutectic reaction occurs at 1078C and
67%Ti 76
. Consequently, a liquid phase should form at sintering temperature enabling the
re-arrangement of particles and densification of specimen. Compared to 10Ti, the
discontinuities and gaps are not present in the microstructure of this specimen and most
small pores between grains disappeared. Aside from the small rounded pores, some larger
ones with longitudinal form were distributed uniformly in the microstructure. The size of
TiB2 grains in 7T3F specimen is slightly larger than that of 10Ti, but the grains are still
angular and the inter-particle distances are smaller. The relative density and bending
strength of this specimen are 91% and 300 MPa, respectively. The major phases found in
the microstructure after sintering the 7T3F specimen were TiB2, α-Ti, TiFe and TiFe2 3.
As shown in Table 8–1, specimens sintered with the Fe additive had a relative density of
90% and a bending strength of 520 MPa. Their typical microstructure (Figure 8–1-c)
reveals a uniform distribution of iron (the white components) suggesting that Fe is a
suitable sintering additive for pressureless sintering of TiB2. The very fine TiB2 particles
and sharp edges of grains were eliminated by dissolving in liquid phase and precipitation
on larger grains and surface with greater curvatures. In consequence the angular grains
transformed into larger and rounded shapes and left some large round-shape pores in the
microstructure. According to Shurin et al. 104
, in the pseudobinary Fe-TiB2 system, a
eutectic reaction is expected to occur at 1340C and 6.3 mol% TiB2. Jüngling et al. 80
found
that this eutectic provides a liquid phase suitable for sintering of TiB2. Einarsrud et al. 52
reported that abnormal grain growth could occur by sintering of TiB2+1.5%Fe specimen at
1700C which strongly reduces the mechanical properties. No abnormal grain growth was
observed in our specimens.
112
Figure 8–1- BSE micrographs from the microstructure of as-sintered specimens: a) 10T,
b) 7T3F, c) 10F. Arrows in (a) indicate the presence of metallic titanium between TiB2
particles.
113
In conclusion, the microstructure and physical properties of both 7T3F and 10F specimens
showed a similar degree of densification and relatively uniform microstructures. However,
the bending strength of the 10F specimens was 520 MPa, which is considerably higher than
that of 7T3F (300 MPa).
8.5.2 Interaction with a liquid aluminum drop
The interaction of specimens with a liquid aluminum drop was studied as a first step to
characterize their stability in liquid aluminum. Figure 8–2 shows the BSE micrograph of
10Ti, 7ti3fe and 10Fe specimens after interaction with a sessile aluminum drop. The 10T
specimen had about 23% porosity after sintering. During the experiment, aluminum
infiltrated the specimen immediately upon melting due to the high level of porosity and the
good wettability of TiB2 surfaces by liquid aluminum (Figure 8–2-a). Despite the rapid
infiltration of molten aluminum, it dissolved some of the titanium additive on its way inside
the specimen (zone 1). According to Al-Ti binary phase diagram 89
at 960°C, when the
titanium content of molten aluminum reaches about 2%, TiAl3 phase starts to precipitate
resulting in the complete depletion of aluminum and solidification of liquid phase (zone 2).
Quantitative EDX analysis of the phases in the Al-infiltrated area of 10Ti specimen also
confirmed the formation of TiAl3 phase (Phase A in Figure 8–3). The aluminum drop did
not infiltrate zone 3.
114
Figure 8–2- BSE micrograph of the cross section of specimens after reaction with
aluminum drop: a) 10T, b) 7T3F, c) 10F. Numbers on images refer to the different
zones formed as a result of aluminum infiltration.
115
Figure 8–3- BSE micrograph and EDX spectrum of phase A formed in the Al infiltrated
area (zone 2 in Figure 8–2-a) of 10Ti specimen, A: TiAl3 phase, B: Ti rich phase.
As shown in Figure 8–2-b 4, complete penetration of aluminum inside the 7T3F specimen
and its reaction with the Ti-Fe additive resulted in the formation of three new distinct zones
in the microstructure of specimens. Titanium and iron additives were dissolved as
aluminum infiltrated the specimen (zone 1) 91
and since the quantity of liquid aluminum is
limited in this experiment (0.1 g), Ti and Fe reached their solubility limits and Ti-Al-Fe
phases segregated (zone 2 and 3). The mechanism of the penetration of liquid Al and the
precipitation of Al-Ti-Fe phases was discussed in a previous work 4. Most of the Ti-Fe
additive was washed out from zone 1 (Figure 8–2-b). EDX analysis detected a Ti-Al phase
in zone 2, and it was confirmed later by SAED pattern that TiAl3 starts to precipitate in
zone 2 as Ti reached its solubility limit. By reaching the solubility limit of Fe, Fe4Al13
precipitated in zone 3 until the complete depletion of the liquid phase. The rest of specimen
(zone 4) was not infiltrated by liquid aluminum. In spite of the penetration of Al inside the
116
specimens and its reaction with the metallic additives, there was no sign of deformation or
swelling of the specimen due to the penetration of aluminum.
As shown in Figure 8–2-c, the 10F specimen was not resistant to liquid aluminum.
Aluminum penetrated and reacted with the phases at grain boundaries which resulted in the
separation of TiB2 particles and the expansion near the contact area (zone 1). Figure 8–4
shows the typical microstructure in the expanded volume of the 10F specimen. The TiB2
particles were separated after less than 1 h of exposure, showing a weak stability of grain
boundaries in liquid aluminum. EDX analysis showed the presence of metallic Al and Fe-
Al phases between TiB2 particles in the expanded volume. A similar behavior had been
reported for the TiB2 specimens consolidated using Ni as sintering additive. Finch and
Tennery 105
reported the disintegration of hot-pressed TiB2-10%Ni after being exposed to
liquid aluminum for 3 h. Weirauch et al. 96
also observed the expansion of the surface of
TiB2-Ni specimen due to the reaction of grain boundaries with aluminum drop during
wetting tests.
117
Figure 8–4- a) BSE micrograph from the expanded portion of 10F specimen (zone 1 in
Figure 8–2-c) after reaction with the liquid aluminum drop (A: TiB2, B: Al, C: Fe4Al13
phase, the black areas correspond to mounting resin), b) EDX spectrum of phase C.
In previous studies about the sintering of TiB2 with Fe additive 51, 106
, the presence of
elemental Ti was found at the triple junctions. In these studies, the only source of Ti in the
specimens was TiB2 grains; therefore, the presence of Ti at triple points confirms the
dissolution of TiB2 phase in liquid iron during a dissolution-precipitation stage. However,
as reported by Jüngling et al. 80
, during the precipitation process, Fe2B phase precipitates at
the grain boundaries and some Ti remains in the liquid phase. Iron borides are not stable in
liquid aluminum 107
and when the 10F specimen comes in contact with the aluminum drop,
118
the grain boundaries react with aluminum resulting in the separation of TiB2 particles and
swelling of the specimen.
8.5.3 Stability in liquid aluminum
To investigate the stability of the specimens in liquid aluminum, they were immersed in
liquid aluminum for 24 h. The 10F and 10T specimens were totally disintegrated in liquid
aluminum, as expected from the results of their interaction with the aluminum drop in the
previous experiment. The 7T3F specimens, however, maintained their integrity and keep
the same shape before and after immersion in liquid aluminum. SEM and EDX analysis
revealed that aluminum penetrated inside the specimen and dissolved most of the metallic
Ti-Fe additive. As reported in an earlier work 3, elemental mapping of the exposed
microstructure did not reveal any Fe within the specimen. Ti was not detected between
TiB2 grains, either. The solid skeleton of TiB2 particles appeared to be stable and grains
remained bonded together.
The stability of the 7T3F specimen in liquid aluminum was also studied during 5 days (120
h) immersion test. SEM investigation of the microstructure of this specimen showed that,
the solid skeleton of TiB2 grains maintained its structural integrity. To reveal the structure
of the TiB2 solid skeleton after prolonged Al exposure, the infiltrated aluminum was
dissolved in a NaOH solution. Figure 8–5 shows the solid TiB2 skeleton of this specimen
after removing the infiltrated aluminum. The TiB2 grains are connected to each other
through inter-particle bridges that are stable in liquid Al.
119
Figure 8–5- SEM micrograph of the 7T3F specimen after immersion into molten Al for
5 days at 960C revealing the solid TiB2 skeleton. The metallic phases were dissolved in
a NaOH solution.
8.5.4 Scratch test
A scratch test was performed in order to investigate the bonding strength between TiB2
particles in the 7T3F specimen immersed in molten aluminum for 5 days. The scratch test
results are shown in a diagram in Figure 8–6. An increasing vertical force was applied from
2 to 50 N over 10 mm length of sliding distance. The measured horizontal force (Fx)
reported here is the force applied to remove the particles from the surface and is ascribed as
scratch resistance. It is observed that the as-sintered 7T3F specimen shows higher
scratching resistance compared to the specimen exposed to liquid aluminum. The higher
scratch resistance of as-sintered specimen is attributed to the presence of FeTi phase which
acts as binder for the TiB2 matrix. The influence of the FeTi binder on the scratch
resistance can be evidenced by comparing with the scratch resistance of a hot-pressed TiB2
specimen provided by Ceradyne Inc.
As shown in Figure 5, despite the greater porosity of the specimen exposed to molten
aluminum, the strength of inter-particle bridges is slightly higher than that of the hot-
pressed specimen. These results suggest that the present sintered TiB2 ceramic possesses
acceptable mechanical strength even after exposure to liquid Al and the inter-particle
bridges have good stability in liquid aluminum.
120
Figure 8–6- Comparing the scratch resistance (Fx) between specimens (AS: as sintered,
5 days: 7T3F after 5 days of Al exposure, Ceradyne: Hot pressed TiB2 provided from
Ceradyne Inc.; The reported Fx is associated with 7T3F specimen after 5 days of Al
exposure.)
8.5.5 TEM analysis
The nature of inter-particle bridges and grain boundaries of the exposed 7T3F specimen to
liquid aluminum were studied using TEM. TiB2 exhibits hexagonal symmetry with
P6/mmm space group (a = b = 0.3028 nm, c = 0.3228 nm; α = β = 90°, γ = 120°) 28
. The
atoms are positioned at Ti(0,0,0), B(1/3,2/3,1/2) and B(2/3,1/3,1/2) in the unit cell 35
. Each
boron atom has three boron neighbors in a trigonal planar arrangement, forming a strong
covalently bonded hexagonal network structure 33
. Figure 8–7-a to c show the area selected
for TEM analysis and the interface between two contiguous grains identified as G1 and G2.
Figure 8–7-d shows the SAED pattern of G1 grain from zone axis and Figure 8–7-e
121
shows the SAED pattern of G2 grain from zone axis. It confirms that G1 and G2 are
distinct grains. EDX analysis detected the presence of aluminum in the unattached
interfaces of TiB2 grains. However, no sign of aluminum or other impurities was observed
in bridges developed at the interface of grains and only Ti and B were detected by EDX
analysis in these areas. The inter-particle bridge between G1 and G2 grains shown in Figure
8–7-f reveals that pure TiB2 crystallizes during sintering and binds the two TiB2 particles.
Since TiB2 has a good chemical stability in liquid aluminum, the stability of the specimen
is therefore attributed to the nature of the inter-particle bridges developed during sintering.
Figure 8–7- TEM micrographs from boundary between two TiB2 grains forming a TiB2
bridge: a) selected area for FIB, b-c) Interface of G1 and G2 grains, d) SAED of G1, e)
SAED of G2, f) Inter-particle bridge
Although both 7Ti3Fe and 10Fe specimens were consolidated through the liquid phase
sintering mechanism, unlike 7Ti3Fe, 10Fe specimen did not have chemical stability in
contact with liquid aluminum. During sintering of 10Fe, TiB2 dissolves partially in liquid
122
iron; however, as reported by Jüngling et al. 80
, Fe2B phase precipitates at the grain
boundaries instead of TiB2. The lack of stability of Fe2B in liquid aluminum is responsible
for the rapid degradation of 10Fe specimen in molten aluminum 80, 108
. According to
published thermodynamic data on the Fe-Ti-B system, a quasi-binary section can be found
along the TiB2-(Fe, 2 at% Ti) line characterized by a simple eutectic at about 1320C 78, 104,
108, 109. It has been proposed that below 2 at% Ti, Fe2B coexists with TiB2
100, 110. Therefore,
in order to avoid the precipitation of this undesirable boride, higher amounts of Ti must be
added to the starting composition.
During the sintering of 7T3F specimen, the excess amount of Ti in the liquid phase
promotes the precipitation of the TiB2 phase instead of Fe2B. The formation and growth of
new TiB2 crystalline planes result in the bonding of TiB2 particles and the consolidation of
specimens. Figure 8–7-f clearly shows that the inter-particle bridges between G1 and G2
TiB2 grains formed from the growth of new TiB2 crystalline planes during sintering. As
SAED pattern revealed, the growth of TiB2 mostly occurred epitaxially on (0001) basal
planes of G1 grain. Since TiB2 has hexagonal crystalline structure, the (0001) planes are
closely packed atomic layers and the growth on this orientation is energetically favorable
49. Therefore the presence of Ti not only prevents the formation of secondary boride phases
but also promotes the precipitation of TiB2 as inter-particle bridges.
The presence of oxygen on the surface of TiB2 particles increases the surface diffusivity
and promotes the abnormal grain growth. However, it has been suggested that the use of
strong reducing additives could reduce the adverse effect of oxygen 47, 111
. The excess
content of Ti in the liquid phase and the presence of hydrogen in the sintering atmosphere
used in this study likely removed the oxygen from the surface of TiB2 grains and thereby
prevented the exaggerated grain growth during sintering.
8.6 Conclusions
Pressureless sintering of TiB2 was performed using Ti, Fe and pre-alloyed Ti-Fe additives.
Fe or the pre-alloyed Ti-Fe promotes the sinterability of TiB2 by producing liquid phase
123
sintering. These specimens showed similar degree of densification and a uniform
microstructure after sintering at 1650C for 1h. Although the use of Fe resulted in higher
mechanical properties, the consolidated specimens did not resist to liquid aluminum and
their interactions with molten aluminum caused the disaggregation of TiB2 particles and the
swelling of the specimens. The lack of stability of these specimens is attributed to the
formation of Fe2B in the bonding regions which do not have stability in liquid aluminum.
In contrast, the specimens sintered with pre-alloyed Ti-Fe showed excellent stability in
liquid aluminum. The solid skeleton of TiB2 grains maintained its integrity after 5 days of
exposure in aluminum. Scratch tests confirmed that the strong bonds between grains are
comparable to those of a hot-pressed TiB2 reference specimen. TEM analyses revealed that
the TiB2 grains are bonded to each other with pure TiB2 phase. The excess concentration of
Ti promotes the precipitation of the TiB2 phase in the inter-particle bridges and this leads to
the stability of the specimens in liquid aluminum.
8.7 Acknowledgements
The authors wish to acknowledge the kind contribution and technical support of André
Ferland from Laval University, Sylvio Savoie from Hydro-Québec and of Jean-Philippe
Masse from École Polytechnique de Montréal for TEM analysis.
Chapter 9:
General discussion and conclusions
125
This thesis reports the works carried out as part of the project: Development of wettable
cathode for aluminum smelting. Developing new materials which are wettable by liquid
aluminum has been proposed as alternative for common carbon cathodes to increase the
energy efficiency of Hall Héroult process for production of primary aluminum. TiB2 has
been the most promising material in the efforts made for developing wettable cathodes due
to its excellent wettability for molten metals and electrical conductivity along with good
chemical stability to withstand the severe conditions of electrolysis bath for long durations.
However, the fabrication of large TiB2 cathode parts is encountered by several scientific
and technical issues, which made the development of wettable TiB2-based cathodes a
challenge for aluminum industry since 1950’s.
The objective of the project was to develop TiB2-based ceramic materials, which their
mechanical strength, electrical conductivity, and stability in molten aluminum are close or
superior to those of usual carbon cathodes, and also have good wettability by molten
aluminum. In addition to these properties, it is important to be able to fabricate large
cathode parts of the developed materials economically into desired shapes.
We proposed pressureless sintering method as a less expensive route for consolidation of
large near net-shaped parts. TiB2 has poor sinterability due to its high melting point
(3000°C) and low inter-diffusion coefficient and its consolidation requires very high
sintering temperatures (~2000°C), especially in the absence of applied pressure. However
sintering of TiB2 at temperatures higher than 1700°C results in exaggerated grain growth
which drastically decreases the mechanical properties and thermal shock resistance. To
avoid this issue, the use of low-melting-point sintering additives was proposed to provide
liquid phase at relatively lower temperatures and promotes the pressureless liquid-phase
sintering of TiB2-based materials. Titanium and Iron binary system forms a liquid phase
over a wide range of compositions at temperatures higher than 1450°C. Therefore the
mixtures of Ti and Fe were chosen as sintering additives.
TiB2-based composites with 10% of different proportions of Ti and Fe additives were
sintered at temperatures between 1400 and 1650°C. Specimens with 7%Ti+3%Fe additives
126
(7Ti3Fe), due to the formation of liquid phase at lower temperatures during sintering,
showed better densification compared to those with 8%Ti+2%Fe. Ti-Fe system have a
eutectic point at around 30 wt% Fe with a melting point of 1085°C. Besides the uniform
distribution of additives in powder mixture, it is important to have Ti and Fe particles in
contact with each other to promote the formation of the liquid phase during sintering. For
this purpose, instead of adding Ti and Fe separately, they were added in pre-alloyed form,
which significantly improved the densification. Maximum density was obtained for the
specimen with pre-alloyed additives sintered at 1650°C. Other investigated parameter in
this work was the effect of the milling time, which was found to have a marked influence
on the densification and properties of sintered TiB2 specimens. Powder mixtures were
milled for various milling periods from 10 to 240 min. A maximum relative bulk density of
91% and maximum bending strength of 300 MPa were achieved with specimens milled for
30 min (M30) and sintered at 1650°C for 1h. By increasing the milling time from 10 min to
30 min, a significant increase of density and bending strength was observed and a more
uniform and denser microstructure was achieved after sintering. While the specimen milled
for 30 min had a uniform crack free microstructure with an even distribution of pores, the
presence of numerous cracks was observed in the microstructures of specimens milled for
longer periods. Particles size distribution analyses revealed that the milling of the starting
powder mixture for 30 min results in grinding of large additive particles and produces a
higher volume of fine particles; thereby a uniform microstructure is obtained after sintering.
However, further increase of the milling time leads to the formation of some large strong
agglomerates through the cold welding of TiB2 particles with additive particles. Upon
sintering, these large agglomerates shrink initiating cracks around them in the compact,
which limits the densification and reduces the mechanical strength.
The measured electrical resistivity of specimens milled for 30 and 240 min were
approximately 54 and 243 µΩ.cm, respectively. The higher electrical conductivity of
specimen milled for 30 min was attributed to its lower porosity, absence of crack as well as
more uniform distribution of additives. The electrical resistances of developed TiB2-based
127
ceramics were well below that of graphite (~500 µΩ.cm) which has the highest
conductivity among the carbon cathodes.
The wettability behaviour of specimens for molten aluminum was studied as well. During
the sessile drop test, liquid aluminum completely wetted the surface of the specimens. The
diagram of wetting angle as a function of elapsed time for specimen milled for 30 min was
a continuous and smooth curve due to its uniform and crack-free microstructure.
Another important parameter for wettable cathode materials is their stability during
immersion in molten aluminum. The specimens milled for 30 and 240 min were immersed
in molten aluminum of 960°C for up to 24 h. The microstructural analyses of exposed
specimens revealed that aluminum penetrated completely all inside the specimens and
dissolved the metallic phases. However, the specimens maintained their forms and no sign
of crack propagation and failure was observed. Specimen milled for 30 min showed better
stability in liquid aluminum due to the absence of cracks in the microstructure and hence
the lower liquid aluminum penetration.
The interaction of the developed TiB2-base porous ceramic with molten aluminum drop
was also investigated. Results showed that the removal of the surface oxide layer by
polishing the surface of as-sintered specimen before the sessile drop test led to a faster
wetting by molten aluminum. The microstructural analyses and elemental mapping of the
cross section of the as-sintered specimen after the test revealed that molten aluminum
reacted with the thin titanium oxide layer formed on the surface and reduced it which made
a delay before wetting the surface.
Molten aluminum drop penetrated inside the specimen after wetting and its interaction with
the metallic phases resulted in the formation of three distinct zones in the cross section. In
the first zone (close to the surface), almost all metallic phases were washed out from the
spaces between TiB2 grains and only traces of Al was detected on the surface of TiB2
grains. TiAl3 phase was detected in the second zone and both TiAl3 and Fe4Al13 phases
were identified in the third zone. The penetration and interaction mechanism of aluminum
128
drop was proposed as follows: the metallic additives were dissolved in liquid Al during its
penetration into the material, and their concentration increased in aluminum gradually.
Once the Ti saturation limit was achieved, TiAl3 phase started to precipitate inside the
pores (Zone 2). The residual liquid (saturated on Ti) continued to penetrate and dissolve the
additives until the saturation point of Fe was reached leading to the precipitation of Fe4Al13
(Zone 3). Dissolution and precipitation were continued up to the complete depletion of the
liquid phase (Isothermal solidification). Liquid aluminum did not seem to alter the solid
TiB2 skeleton of the specimen and no sign of swelling or cracking was detected.
Pressureless sintering of TiB2 was also performed using Ti, Fe and pre-alloyed Ti-Fe
additives. Specimens with Fe and pre-alloyed Ti-Fe additives showed similar degree of
densification and a uniform microstructure after sintering at 1650C for 1h. These additives
promoted the sinterability of TiB2 by producing liquid phase at sintering temperature.
Although the use of Fe resulted in higher mechanical properties, the consolidated specimen
did not resist to liquid aluminum and its interaction with molten aluminum caused the
disaggregation of TiB2 particles and the swelling of the specimen. The lack of stability of
this specimen is attributed to the formation of Fe2B in the bonding regions, which do not
have stability in liquid aluminum. In contrast, the specimens sintered with pre-alloyed Ti-
Fe showed excellent stability in liquid aluminum. The solid skeleton of TiB2 grains
maintained its integrity even after 5 days of exposure in aluminum. Scratch tests confirmed
that the strong bonds between grains are comparable to those of a hot-pressed TiB2
reference specimen. TEM analyses revealed that the TiB2 grains are bonded to each other
with pure TiB2 phase which is the reason for the stability of the specimens in liquid
aluminum. The excess amount of Ti in the liquid phase promotes the precipitation of the
TiB2 phase, instead of Fe2B, in the inter-particle bridges. The formation and growth of new
TiB2 crystalline planes result in the bonding of TiB2 particles and the consolidation of the
specimen. In addition, The excess content of Ti in the liquid phase and the presence of
hydrogen in the sintering atmosphere used in this study likely removed the oxygen from the
surface of TiB2 grains and thereby prevented the exaggerated grain growth during sintering.
The results of this investigation provided us with more insight about the sintering
129
mechanism of TiB2 with Ti-Fe additive and the advantage of using this additive system
over the previously studied materials in terms of stability in liquid aluminum.
It is therefore concluded that the material developed by pressureless sintering of TiB2 using
a Ti-Fe additive meets the required properties and chemical stability in liquid aluminum
and is proposed as a reliable material for application as wettable cathodes in aluminum
smelting.
Chapter 10:
Perspectives of the project
131
The developed TiB2-based ceramic showed to be a promising candidate for wettable
cathode application. The use of Ti-Fe additive promotes pressureless sintering at relatively
lower temperature and most importantly, forms the inter-particle bridges with TiB2 nature
which make the solid skeleton of TiB2 with good stability in molten aluminum. Further
investigations would be suggested more evaluation of developed material or for fine-tuning
of the processing parameters:
The evaluation of the chemical stability of the developed material in molten cryolite
and its resistance for sodium penetration is proposed as an important property
requirement of wettable cathode.
Studying the stability of the developed material to liquid aluminum in dynamic
condition (exposed to the flow of molten aluminum on the surface and applying the
electrical current similar to the electrolysis bath conditions) and comparing the
corrosion rate with static condition. Preliminary results showed that the rate of
aluminum penetration in the dynamic condition is lower than the static condition.
Impregnate the pores or apply a coating on the developed TiB2 with a proper
material to protect it from oxidation and infiltration of the bath electrolyte during
the start-up period in the electrolysis cell; during the start-up cycle, electrolyte will
be in direct contact with the surface of the cathode. By increasing the cell
temperature and melting of cryolite and before the formation of aluminum pad, the
molten electrolyte might penetrate inside the pores and result in subsequent issues.
Investigation of the other compositions and processing parameters e.g. sintering
time, the percentage of additives, sintering cycle for consolidation of large parts,
possibility of using vibro-compactor to achieve more uniform densification during
the compaction of large parts.
132
Although the proposed material in this project is developed for wettable cathode
application, its potential for using in other applications such as armours, wear resistant parts
could also be investigated.
133
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Appendix 1: Ceramic fabrication
A 1.01 Introduction
Generally, ceramic fabrication involves creating fine particle size powders, forming
powders into compact and sintering to produce a cohesive body with the desired
microstructure and properties for a given application. Specific surface area of powders is
relatively high; therefore ceramic processing involves understanding and controlling the
physical chemistry of surface and interfaces. The finer the particles are, the higher the
specific surface area of powder and hence the surface energy of the system is. Surface
energy, which is also called surface tension, γ, is obviously very important in ceramic
powder processing and sintering, as it causes liquids to form spherical drops, and allow
solids to preferentially adsorb atoms to lower the free energy of the system. It also creates
pressure differences and chemical potential differences across curved surfaces that cause
matter to move.
The Laplace equation, which defines the pressure difference, ΔP, across a curved surface of
radius, r,
ΔP = γ (1/r1 + 1/r2) ( 1-1)
has been characterized as the fundamental equation of capillary 1. In ceramic processing,
the pressure associated with surface tension and capillary forces contribute to particle
clustering (i.e. agglomeration) and rearrangement, to the migration of liquids through pores
during mixing, shape forming, and drying, and to pores shrinkage during sintering.
The equilibrium vapour pressure, P, over a curved surface is defined by the Kelvin equation
ln P/P0 = 2γΩ/rkT ( 1-2)
where P0 is the equilibrium vapour pressure over a planar surface, Ω is the molecular
volume of condensed phase, k is Boltzmann’s constant, and T is the absolute temperature.
Because the chemical potential difference, Δμ, between a curved and flat surface is related
to the vapour pressure over those respective surfaces,
141
Δμ = kT ln P/P0 ( 1-3)
chemical potential is also related to surface curvature:
Δμ = μ – μ0 = 2γΩ/r ( 1-4)
The chemical potential of a curved surface is extremely critical in ceramic processing. It
determines reactivity, the solubility of a solid in a liquid, the rate of liquid evaporation from
solid surfaces, and material transport during sintering 1.
A 1.02 Powder processing
Advanced ceramics are typically made from refined raw materials or chemically
synthesized ceramic powders. The chemical and physical properties and characteristics of a
powder are modified within beneficiation processes. Advanced ceramics are sensitive to the
chemical and physical defects present in the starting raw materials, or those that are
introduced during manufacturing. Particles size reduction using mechanical energy may be
the most common process. Grinding or milling creates new surfaces by breaking down
aggregates and by fracturing particles 1.
Consolidating powder generally involves a forming pressure to produce the desired size or
shape ceramic component. Forming additives or processing aids are commonly added to a
ceramic powder to enhance processing. Organic additives adhere onto the surfaces of
ceramic particles to modify surface energy and particle-particle interactions. Two common
additives used in ceramic processing are binders and lubricants 1. The main purpose of a
binder, which also called coagulant or flocculent, is to provide strength to the powder
compact after shape forming. It may be necessary for subsequent handling or green
machining. Lubricant is added to lower interfacial frictional forces between individual
particles or between particles and forming die surfaces to improve compaction and ejection.
Coating with a film of low-viscosity lubricant can lubricate die surfaces.
Powder pressing is the most common method of forming ceramic components. The
powders can be compacted by applying mechanical pressure, which is most simply done
142
under uniaxial compression in steel dies (or with those with WC-Co lining). It is called die
pressing or cold pressing to distinguish it from hot pressing. Cold pressing, is an
economical, yet versatile technique for fabricating small, relatively simple-shape powder
compacts 1. Such pressing can be done with no or limited use of lubricant or binder. Dies
have a vertical cylindrical through hole whose shape and dimensions are based on desired
piece shape considering sintering shrinkage and machining (if applicable). In die cavity, the
pressure is applied onto the powder by opposing rams. The limit for cavity clearance is less
than 25 μm for fine micron-sized powders up to four time for coarser particles 2. An
important issue is the relative motion of the top versus the bottom ram. The uniformity of
the packing in the consolidated material is very important. In general, any non-uniformity
in the green body is exaggerated in the sintering process, leading to the development of
crack like voids or large pores between relatively dense regions 3.
Basically the die pressing consists of three stages: 1) die filling 2) powder compaction and
3) part ejection. Figure 1 shows the schematic of uniaxial die which is used for compaction
of powders. Friction between the powder and the die wall must be controlled, e.g. by using
lubricants, during forming to minimize pressing pressure gradients that can create defects in
the form of density gradients or cracking in a pressed powder compact 1. It may need
binders to enhance strength of green body that is required for part ejection from the die and
subsequent handling before sintering 2.
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Figure 1- The schematic of uniaxial pressing of powders
A 1.03 Thermal processing
Generally, the last step in ceramic component manufacturing is thermal processing. It is the
stage where the weakly bounded particulate body produced during shape forming is heat
treated to produce a cohesive body with the desired properties for its end-use application.
Thermal consolidation, which is more commonly referred to as ‘firing’, typically involves
two steps, burnout and sintering. Generally both are accomplished in a single firing process
with burnout preceding sintering.
The burnout stage involves eliminating the organic processing aids and any residual
organic impurities or water prior to sintering. Most organic binders used in ceramic
forming can be burned out by heating to 500°C 1.
A 1.04 Sintering
Sintering involves the densification and microstructure development that transform the
loosely bond particles in a powder compact into a dense, cohesive body. The final
properties of a ceramic are largely dependent on the degree of densification achieved
144
during sintering, and on the microstructure produced; consequently, sintering is one of the
most critical steps in ceramic processing. Sintering is usually accomplished by heating a
powder compact to approximately two-thirds of its melting temperature for a given time 1.
Sintering can also occur by subjecting a powder compact to externally applied pressure, or
heat and pressure simultaneously (e.g. hot pressing and hot isostatic pressing). A ceramic
densifies during sintering as the porosity between the solid particles is reduced in size with
time. Concurrently, the cohesiveness of the body increases as the inter-particle contact (e.g.
grain boundary) area increases during sintering.
A 1.05 Driving force for sintering
Ceramic powder compacts are sintered as a result of the thermodynamic driving force to
minimize the Gibb’s free energy, G, of a system. This includes minimizing the volume,
interfacial, and surface energy in the system. In a powder compact, excess free energy is
present primarily in the form of surface or interfacial energy (i.e. liquid-vapour or solid-
vapour interfaces) associated with porosity 1. Under influence of elevated temperature
and/or pressure during sintering, atoms migrate to thermodynamically more stable positions
within a powder compact. Material transport is driven by the chemical potential difference
that exists between surfaces of dissimilar curvature within the system. Physically, in a
particulate system, atoms or ions move from higher energy convex particle surfaces to
lower energy concave particle surfaces to decrease the curvature and chemical potential
gradients in the system.
Material transport can occur by solid-state, liquid-phase, and vapour-phase mechanisms.
For polycrystalline ceramics, material transport commonly occurs as ions diffuse through
the volume, along grain boundaries and on particle surfaces. Additionally, ions can
vaporize from, and consequently condense onto, particle surfaces (evaporation-
condensation) 1. A powder compact will densify when material transport occurs in a
manner that allows particle centres to approach during sintering. Material transport by
volume and grain boundary diffusion can results in densification. Material transport that
145
changes the geometry of the system without densification is termed coarsening. Grain
growth is perhaps the most common form of coarsening during sintering. Coarsening can
occur when material is transported by volume diffusion, surface diffusion, or evaporation-
condensation.
Figure 2 shows the classic two-particle sintering model illustrating material transport and
neck growth at the particle contacts resulting in coarsening and densification during
sintering. Surface diffusion (a), evaporation-condensation (b), and volume diffusion (c)
contribute to coarsening, while volume diffusion (d), grain boundary diffusion (e), solution-
precipitation (f), and dislocation motion (g) contribute to densification.
Figure 2- The classic sintering model illustrating material transport and neck growth at
particle contacts resulting in coarsening (left) and densification (right) during sintering
1.
146
A 1.06 Densification and microstructure development
In a microstructure point of view, material transport during sintering shows itself as inter-
particle pore shrinkage, grain boundary formation, a decrease in the total volume of the
system (i.e. densification), and an increase in the average size of the particles that make up
the compact (i.e. grain growth) 1. Inter-particle contacts flatten, the curvature within the
system decreases, and the surface area and free energy of the system decrease during
sintering.
The ideal sintering process can be divided into three basic stages. Initially, material is
transported from convex particle surfaces to the pore-grain boundary intersection to form
necks between adjacent particles. As this occurs, grain boundaries grow to create a three-
dimensional array of approximately cylindrical, interconnected pore-channels at triple grain
junctions throughout the compact. These pore-channels shrink in diameter during
intermediate-stage sintering. Ultimately, the channels punch off to form approximately
spherical, closed pores at four grain junctions within the ceramic matrix. The radial
shrinkage of closed pores and the growth of larger grains at the expense of smaller ones
constitute final-stage sintering.
Factors like surface energy anisotropy and packing heterogeneities in real systems can
contribute to heterogeneous densification and microstructure development. To overcome
this problem, minor concentration of selected chemicals, which called sintering aids or
dopants, are commonly added prior to the sintering. These chemical impurities
preferentially segregate to high-energy crystallographic planes to decrease the crystalline
anisotropy in the system to provide improved control over microstructure development
during sintering (e.g. MgO-doped Al2O3) 1. Impurity segregation to high-energy grain
boundaries will also produce lower-energy interfaces that reduce the overall driving force
for material transport during sintering.
147
A 1.07 Solid-state sintering
Ceramics can be densified by solid-state, liquid-phase, and viscous sintering. Solid-state
sintering refers to the process whereby densification occurs by solid-state, diffusion-
controlled material transport. Densification occurs as higher-energy, solid-vapour (i.e. pore)
interfaces are replaced by lower energy, solid-solid (i.e. grain boundary) interfaces 1. The
change in free energy associated with the elimination of porosity, which drives
densification, can be approximated by:
dG = γssdAss - γsvdAsv ( 1-5)
Grain growth can further reduce the free energy of the system by reducing the amount of
high-energy, solid-solid interfacial area. The change in free energy associated with the
elimination of particle-particle interfaces, which drives grain growth, can be approximated
by:
dG = - γssdAss ( 1-6)
Because densification occurs via shrinkage of thermodynamically unstable pores,
densification and microstructure development can be assessed on the basis of the dihedral
angle, θ, formed as a result of the surface energy balance between the two solid-vapour and
one solid-solid interfaces at the pore-grain boundary intersection.
( 1-7)
where γss and γsv are the solid-solid and solid-vapour interfacial energies, respectively
(Figure 3) 1.
sv
ss
2cos2 1
148
Figure 3- Interfacial energies and dihedral angle, θ, 1
In the presence of a vapour phase, θ is larger than 120° because γsv is usually higher than
γss. In general, γsv is 2–3 times higher than γss and θ is around 150°. If the dihedral angle is
constant and the junction edges are randomly distributed in three dimensions, the measured
angle with the maximum frequency is the true dihedral angle 4.
The larger the dihedral angle, the larger the inter-granular pores that can be eliminated
during sintering and the greater the surface tension driving force for pore shrinkage.
Thermodynamics and/or kinetics limit the shrinkage of pores trapped within grains (i.e.
inter-granular porosity) and pores above critical size 1.
A 1.08 Liquid phase sintering
To promote faster densification at lower temperatures, relatively small concentrations of
chemical additives, called sintering aids, are commonly used to create a liquid-phase
sintering. The formation of liquid phase during sintering considerably increases the
diffusion rate of the components. It facilitates the displacement of solid particles with
respect to each other, which results in rapid filling of pores and capillaries and usually
increases the sintering rate. In liquid-phase sintering (LPS) the theoretical density of the
149
material may be attained in a short time 5. Kingery et al.
6 proposed that for having the
rapid densification, it is essential to have:
An appreciable solubility of the solid in the liquid,
An appreciable amount of liquid phase, and
Wetting of the solid by the liquid.
During sintering in the presence of liquid phase, a number of phenomena occur
simultaneously and it is significantly more complex process than the solid state process. In
LPS, there are more phases, interfaces, and material transport mechanisms to consider.
In general, densification will occur as long as it is energetically favourable to replace
liquid-vapour (lv), solid-solid (ss), and solid-vapour (sv) interfaces with solid-liquid (sl)
interfaces during sintering 1:
dG = γsldAsl – (γlvdAlv + γssdAss + γsvdAsv) ( 1-8)
where γsl and γlv are the solid-liquid and liquid-vapour interfacial energies, respectively.
With considering weak chemical reaction between the constituents; the surface tension
from the liquid phase is a significant factor in determining the sintering rate. In liquid phase
sintering, densification and microstructure development can be assessed on the basis of the
liquid contact or wetting angle, ϕ, formed as a result of the interfacial energy balance at the
solid-liquid-vapour intersection as defined by Young equation 1:
( 1-9)
A low contact angle favours liquid wetting of particle surfaces and densification during
LPS. Theoretically, ϕ must be less than 60° to achieve 100% of the theoretical density 1.
lv
slsv
1cos
150
Figure 4- Illustration of the wetting angle, ϕ 1
The liquid wets the solid particles and applies capillary force on the solid particles to
eliminate porosity and reduce interfacial area. It can be considered that the material is under
uniform hydrostatic pressure. Diffusion rates in liquid are relatively high and results in
faster bonding and densification compared to equivalent solid state sintering 5.
If the liquid do not wet the solid particles, it will not penetrate between each of the solid
particles and they will be joined only in contact points. In this case, sintering must occur
with the transfer of materials within the solid phase, in order for particle centers to move
closer and shrinkage take place in the specimen. Although, material transfer may take place
by solution-precipitation process in which the material is transferred through the liquid, it is
not essentially different from the single-phase process in which the materials are vaporized
and condense at the junction between particles 7.
Considering the solubility factors, four possible combinations of interactions and sintering
behaviours encountered in liquid-phase sintering are 5:
Low liquid solubility in the solid combined with a high solid solubility in the liquid
which result in LPS. It is applied to wide variety of systems that results in
densification, including: W-Ni-Fe, WC-Co, Si3N4-Y2O3, Al2O3-SiO2, TiC-Ni, and
Fe-Cu.
The opposite solubility situation, high liquid solubility in the solid combined with a
low solid solubility in the liquid, which gives swelling and a transient liquid. The
Fe-Al system has such behaviour.
151
The combination of low liquid and solid solubilities, requires high temperature to
induce significant liquid phase sintering and corresponds to a system such as W-Cu.
In this case, similar to the solid-state process, the materials transfer in an initially
porous compact under the force of surface energy and form pore-free structure. For
such a system solid state sintering of the skeletal structure can be more significant
than liquid-phase sintering.
Finally, the situation of high solubility proves to be the least predictable. This
combination exhibits both swelling and densification and is sensitive to many
processing variables such as sintering temperature, particle size and green density.
A conceptual summarization of the key solubility factors encountered in liquid-phase
sintering is shown in Figure 5 5.
Solid solubility in liquid
Low High
Liq
uid
so
lub
ilit
y in
soli
d
Lo
w Limited densification,
Rearrangement
Extensive densification,
LPS
Hig
h Swelling,
Transient liquid
Mixed effect,
Swelling & densification
Figure 5- Conceptual summarization of four possible interactions and sintering
behaviours considering the solubility factor 5.
When the surface energies are dominant, liquid-phase sintering densification occurs in
stages as sketched in Figure 6. Initially, mixed powders are heated to a temperature where
liquid forms. Based on phenomenological observations, Kingery 7, 8
considered that after
the formation of liquid three stages can appropriately be distinguished:
Rearrangement,
Solution-precipitation, and
Final-stage sintering or coalescence.
152
Figure 6- Schematic diagram of the classic liquid-phase sintering stages 5
Figure 7- Density dependence on the liquid content 5
Figure 7 summarize these stages by plotting the density versus the volume of liquid phase 5.
With good wetting the liquid infiltrates to the contacting sections of the solid particles,
153
which sharply reduces friction and wedging. The solid particles are rearranged, due to the
exertion of capillary force by the liquid; the voids and bridges between them disappear, and
thus the volume of the sintered material decreases 9. If there is a high liquid level, full
density can be achieved via rearrangement upon liquid formation. On the other hand, at low
liquid contents the solid skeleton inhibits densification, requiring the participation of
solution-precipitation events, where mass transport through the liquid controls
densification. Residual final porosity is eliminated by solid-state sintering of the rigid solid
skeleton 5.
With liquid formation, grains shrink as solid dissolves into the liquid and the solid grains
pack to a higher density, releasing liquid to fill pores between grains. For wetting liquids,
the surface energy of solid-liquid is lower than that of solid-vapour and densification results
in reducing system energy 5. During rearrangement the compacts exhibit viscous response
to the capillary action. The elimination of porosity increases the compact viscosity. As a
consequence, the densification rate decreases continuously. Full density is possible by
rearrangement if enough liquid is formed 5, 9
.
Another important condition for occurrence of the rearrangement is the penetration of
liquid between the grains. The extent to which the liquid enters the joints between particles
depends on the dihedral angle formed by the liquid phase at the boundary with two grains
of the solid phase 4. The dihedral angle is determined only by the interfacial energies and is
independent of the pressures in the phases. This means that the dihedral angle is constant,
irrespective of the pressure of liquid phase 4.
Whether viscous flow occurs or not at the beginning of liquid phase sintering depends
strongly on two parameters: the dihedral angle between the solid grains and the volume
fraction of liquid. When this dihedral angle is greater than 0° and a solid skeleton forms
during heating to the liquid phase sintering temperature, no viscous flow of particles and no
particle rearrangement are expected 4. Viscous flow and particle rearrangement may occur
only when the dihedral angle is 0°. If the liquid volume fraction is high, viscous flow can
occur. However, for a low liquid volume fraction, local rearrangement of particles must be
154
predominant 4. While a slight shrinkage can be achieved, larger pores are formed by
particle rearrangement, as in the case of solid state sintering. This result suggests that
particle rearrangement may not be beneficial for overall densification because the final
densification is governed by the elimination of the larger pores in the compact 4.
The second stage termed solution-precipitation. Although the various other events are
concurrent with rearrangement, the kinetics of rearrangement are initially so fast that the
other events are overshadowed 10
. As densification by rearrangement slows, solubility and
diffusivity effects dominate. Therefore, this stage followed by solution-precipitation. At
least a limited solubility of the solid in the liquid phase is necessary for this stage to take
place; otherwise this stage of densification is completely absent. Densification occurs more
slowly than in the rearrangement stage, because the transport of material must proceed by
means of dissolution and diffusion in the melt. Small grains with strongly convex
curvatures go into solution and the substance is precipitated on large particles
accompanying by grain growth and grain shape accommodation. The driving force for
material transport, results from the increased compressive stresses and hence from the
enhanced chemical potential and higher solubility in the contact zones 10
. The solubility of
grains in surrounding liquid varies inversely with their size; small ones, owning the smaller
radius of curvature, have higher energy and solubility compared to the large ones with
larger radius of curvature. The difference in solubility establishes a concentration gradient
in the liquid. Material is transported from the small grains to the large grains by diffusion
through the liquid. The net result is a progressive growth of the larger grains at the expense
of the smaller grains, giving fewer grains with a lager average size. Solution-precipitation
not only contributes to grain coarsening but also to densification via grain shape
accommodation, allowing a customized fitting together the growing grains to better fill
space. The amount of liquid determines the diffusion distance and the necessary degree of
grain shape accommodation 5, 9
. According to Cannon and Lenel 11
, the solution-
precipitation process cannot occur with less than 5 vol.% of liquid phase.
155
The final stage of liquid-phase sintering is coalescence and it is controlled by densification
of the solid structure. In the case of incomplete wetting or insufficient liquid phase, the
solid grains remain partly in contact without the interposition of the melt 10
. In their
sintering model, Cannon and Lenel 11
suggested that, after considerable densification by a
solution-precipitation process and the formation of grain boundaries, the contribution of
solution-precipitation became negligible and that final densification occurred by a sintering
process similar to solid state sintering. This type of sintering, however, is not believed to be
operative in liquid phase sintering because the densification kinetics of liquid phase
sintering are much faster than the estimated kinetics of solid state sintering 9.
Microstructural coarsening continues and the residual pores enlarge if they contain trapped
gas, giving contact swelling. In general, properties of most liquid-phase sintered materials
are degraded by prolong final-stage sintering. Hence, short sintering times are preferred in
practice 5. Figure 8 shows a hypothetical densification curve for these three stages of liquid-
phase sintering 9. The time scale in this diagram is logarithmic and it gives a sense of the
densification event.
Figure 8- Densification time scale for the three stages of liquid phase sintering 9
156
A 1.09 References
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Institute of Physics Pub., Bristol; Philadelphia, 2001.
[2] R.W. Rice, Forming and pressurless sintering of powder-drived bodies, in: Ceramic
fabrication technology Marcel Dekker, Inc., New york, NY, 2003.
[3] M.N. Rahaman, Ceramic Fabrication Processes, in: 2nd (Ed.) Ceramic Processing and
Sintering, Routledge, USA 2003
[4] S.-J. L.Kang, Densification models and theories, in: Sintering: Densification, Grain
Growth, and Microstructure, Elsevier Butterworth-Heinemann, 2005, pp. 227-247.
[5] R.M. German, Liquid-phase sintering, in: Sintering theory and practice, John Wiley &
Sons Ltd., New York, 1996, pp. 225-313.
[6] W.D. Kingery, H.K. Bowen, D.R. Uhlmann, Introduction to ceramics, 2 ed., Wiley,
New York, 1976.
[7] W.D. Kingery, Densification during sintering in the presence of a liquid phase. I.
theory, Journal of Applied Physics, 30 (1959) 301-306.
[8] W.D. Kingery, M.D. Narasimhan, Densification during sintering in the presence of a
liquid phase. II. experimental, J Appl Phys, 30 (1959) 307-310.
[9] V.N. Eremenko, Y.V. Niadich, I.A. Lavrinenko, General principles of sintering in the
presence of a liquid metallic phase, in: Liquid phase sintering, Plenum Publishing
Corporation, 1970, pp. 1-15.
[10] F. Thummler, W. Thomma, The sintering process, Met. Rev., 12 (1967) 69-108.
[11] H.S. Cannon, F.V. Lenel, Some observations on the mechanism of liquid phase
sintering, in: Pulvermetallurgie, Plansee seminar de re metallica, Springer-Verlag, Vienna,
1953, pp. 106-110.