database of polymeric materials for hydrogen gas seals and … · critical pressure of blister...
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Database of Polymeric Materials for Hydrogen Gas Seals and
Dispensing Hoses
11 September 2018
Department of Mechanical Engineering, Faculty of Engineering, Kyushu University The Research Center for Hydrogen Industrial Use and Storage, Kyushu University
Shin Nishimura
Acknowledgement This research has been supported by the New Energy and Industrial Technology
Development Organization (NEDO) “Hydrogen utilization technology development (2013–2017)".
Chem ca sh ft (d n ppm)
if
Hydrogen Polymers in HYDROGENIUS
Rubbers materials and polymeric materials are "KEY MATERIALS" for hydrogen gas seal in equipment for hydrogen energy system.
Critical Pressure of Blister Fracture, PF, MPa
Hyd
roge
n Co
nten
t at 1
0 MPa
(ppm
)
No Blister
EPDM–CB25phr
EPDM–CB50phr
NBR–CB50phr
EPDM–SC60phr NBR–SC60phr
Blister
NBR–CB25部
EPDM–WC95 Unfilled EPDM Unfilled NBR
0 2 4 6 8 10 0
200
400
600
800
1000
1200
1400
8 7 6 5 4 3 2 1 0 i l i i
Unexpo
35H 23H
14H 1H
CrudeNBR
g) b)
f)
a)
e)
g)
d) h)
c) c)
c)
55H
Chemical Shift(ppm)
Two types of dissolved hydrogen CB filled EPDM
10MPa, 30℃,24hours●: Experimental Value −:Calculated Value
Elapsed Time(sec)
Hyd
roge
n Co
nten
t(mas
s.pp
m)
Development of Material Prototype Evaluation Product Evaluation Chemical Analyses Properties in Hydrogen Damage/Lifetime Analyses
Material Design Model Composites Fracture Modeling Design
Guideline
Model Composites
Hydrogen Content
Solid State NMR
O-rings
Hoses
Product
100℃
80℃ 30℃
Hyd
roge
n Pr
essu
re(M
Pa)
100
10 10 1 100 1000 10000
Cycle Number of Failure
Pressure Cycle Test of O-ring
Product Testing: Collaboration with Hydrogen Testing & Research Center EPDM(Hs70):H2! 35MPa! 100℃! 15hrs.
EPDM(Hs70):H2! 70MPa! 100℃! 3hrs.
Overflow Fracture
Buckling Fracture
EPDM(Hs70):H2! 35MPa! 100℃! 15hrs. 1 mm
Blister Fracture
0.5mm
Magn y
10 mm
1 mm 1 mm 10 mm
Fracture Mechanics
Defect Origin
Matrix Origin
Time
Time
Grow of Blister
Grow of Blister
Molecular Chain Blister Crosslink
Defect
H d1 AOR
AG=H × LL d1:O-ring Diameter,H: Gland hight,L: Gland width Cross section area: AOR:O-ring ,Gland
O-ring squeeze ratio=1ーH/d1・・・ 10〜20% Filling ratio=AOR/AG・・・ 60〜80%
Establishment of Research Group
It is important to understand the relationship between structure of elastomeric compounds and their properties under high-pressure hydrogen.
We need diverse ideas from industries for the model compounds and hydrogen properties for measurement.
In 2012, we have established “The Research Group of Elastomers for Hydrogen Equipment” in The Society of Rubber Science and Technology, Japan.
In the research group, more than 40 members are active from the viewpoints of materials and elastomeric compounds design, hydrogen equipment design.
Polymeric Materials for Hydrogen Equipment
~90MPa pressure difference→ 70MPa Dispenser
Hydrogen Station ←Charging by
Hydrogen Accumulator
Compressor Fuel Cell VehicleGenerator
Rubbers and polymeric materials are used for gas seals and liners in the hydrogen equipment.
Piping System/Valves Breakaway Device
Plug/Receptacle Flexible Hose
Fracture of O-ring by Hydrogen
10mm
90MPa,100° C ×20 cycles
10mm
after 100MPa, 30°C ×25 cycles
Cross section
Fracture
Blister Fracture
Seal Break
Before test
5.5mm
140mm
NBR EPDM
Key Parameters for Fracture Modes of O-ring
EPDM(Hs70):H2×35MPa×100℃×15hrs.
EPDM(Hs70):H2×70MPa×100℃×3hrs.
Overflow Fracture
Buckling Fracture
EPDM(Hs70):H2×35MPa×100℃×15hrs. 1 mm
Blister Fracture
0.5mm
Magnify
10 mm
1 mm 1 mm 10 mm
Material Strength and Hydrogen Solubility of Rubber Materials
Key Parameter:H2 content
Volume Increment of Rubber Materials originated from Swelling by Hydrogen
Gland Design in consideration for Volume Increment of the Rubber Materials
Key Parameter:Volume change
7 Design of Model Rubber Compounds
ITEMS NBR NF
NBR CB50
NBR CB25
NBR SC60
NBR SC30
EPDM NF
EPDM CB50
EPDM CB25
EPDM SC60
EPDM SC30
NBR(Nipol 1042) 100 100 100 100 100 - - - - -EPDM(Esprene
505) - - - - - 100 100 100 100 100
Stearic Acid 1 1 1 1 1 1 1 1 1 1 Zinc Oxide 5 5 5 5 5 5 5 5 5 5
Sulfur 1.5 1.5 1.5 1.5 1.5 1.5 1.5 1.5 1.5 1.5 MBTS 1.5 1.5 1.5 1.5 1.5 1.5 1.5 1.5 1.5 1.5 TMTD 0.7 0.7 0.7 0.7 0.7 0.5 0.5 0.5 0.5 0.5 ZnEDC 0.7 0.7 0.7 0.7 0.7 - - - - -
Carbonblack(N330) - 50 25 - - - 50 25 - -Silica(Nipsil VN3) - - - 60 30 - - - 60 30
Acrylonitoril Butadiene Rubber (NBR)
Ethylene Propylene Rubber (EPDM)
2,2’-Benzothiazyl Bis(dimethylthiocarbamoyl) Zinc Diethylthio-Disulfide (MBTS) Disulfide (TMTD) carbamate (ZnEDC)
Measurement of Hydrogen Content
Thermal Desorption Analysis (TDA)
Gas sampling (5-minute-interval)
Heater
GC (molecular sieve)
H2 gas
Carrier gas (Argon)
TCD
Tube furnace Hydrogen Vessel (30°C/~90MPa/24h)
H2
Hydrogen Exposure
Hydrogen content measurement (TDA)
Hydrogen Content Estimation
・After exposure to hydrogen gas, hydrogen content was measured by TDA.・A large volume of hydrogen release is considered before the measurement tests. ⇒Eq. (1) was fitted to remaining hydrogen content by using the least square method regarding equilibrium hydrogen content and diffusivity as unknown parameters, and the equilibrium hydrogen content was estimated by extrapolation.
Remaining
hyd
roge
n co
nten
t, C
H,R
(wt. ppm
) 200
150
100
50
0 0 5000 10000
Time after decompression , t (s)
Hydrogen release profile of hydrogen–exposed specimen of NBR-NF.
2 =13 mm =2 mm
□ Experimental data (NBR-NF)
Hydrogen exposure condition 10 MPa, 30 oC, 24 h.
Eq. 1
CH0
}]/exp[
{
})12(
]/)12(exp[ {32 )(
1 2
22
0 2
222
H0 2R,H
n n
n
n
tD
n Dt nCtC
function Bessel order -zero the of root The : (m) specimen of Thickness :
(m) specimen of Radius : /s) (m tcoefficienDiffusion :
(wt.ppm) content hydrogen mEquilibriu:
(wt.ppm) at content hydrogen Remained :)(
n
2 H0
RH,
D
C ttC
(5 )
Solution of unsteady diffusion equation at hydrogen release
・・・ Eq. 1
(5) A. Demarez, A. G. Hock, F. A. Meunier, Acta Metallurgica, 2, 214 (1954).
10 Volume Measurement System KEYENCE 2D Silhouette Scanner TM-3000
The equipment is in the thermostat chamber.the temperature of the chamber is controlled at30°C, same as TDA measurement. The volume of 8 samples can be measured atsame time in every 5 minutes, same as TDA measurement.
230mm2 231mm2
229mm2
-----mm2
-----mm2
-----mm2
-----mm2
The surface area of the sample (13mmφ×2mmt) can be measured . The volume of the sample can be estimated by cube square root of the surface area. The results are consistent with Archmedean method.
11 Exposure Pressure Dependency of Hydrogen Content250 3000
▲ NBR-NF ● NBR-CB50 ○ NBR-CB25 ■ NBR-SC60 □ NBR-SC30
0 20 40 60 80 100 0 20 40 60 80 100
▲ NBR-NF ● NBR-CB50 ○ NBR-CB25 ■ NBR-SC60 □ NBR-SC30
Hyd
roge
n Con
tent
(wt pp
m)
2500
2000
1500
1000
200
Volum
e Cha
nge (%
)
150
100
50 500
0 0
Hydrogen Exposure Pressure Hydrogen Exposure Pressure (MPa) (MPa)
Hydrogen contents of model composites after hydrogen exposure are proportional to the hydrogen exposure pressure. Hydrogen contents of carbon black filled NBR are larger than those of unfilled and silica filled rubbers. Volume change of model composites after hydrogen exposure are proportional to the hydrogen exposure pressure. Filled rubbers shows smaller volume change.
12 Relationship between H2 content and volume
Volume Ch
ange V/V
0
2.2
2
1.8
1.6
1.4
1.2
1
Sulfur vulcanized NBR :unfilled :filled with silica 30phr :filled with carbon black :filled with carbon black
25phr 50phr
0 500 1000 1500 2000 2500
Carbon Black controls volume change of the compound Hydrogen Content (wt.ppm)
phr: weight parts per hundred weight parts of rubber
Model NBR Compound
Grade Acrylonitrile Content
Density (g/cm3)
Low Nitrile 18% 0.94
Mid Nitrile 29% 0.97
Mid-High Nitrile 33.5% 0.98
High Nitrile 40.5% 1.00
Very High Nitrile 50% 1.02
Compound:Sulfur vulcanization system Sulfur:1.5 phr, MBTS:1.5 phr, TMTD:0.7 phr, ZnEDC:0.7 phr Stearic acid: 1 phr, Zinc Oxide:5 phr
14 Hyd
roge
n co
nten
t (w
t.pp
m)
Unfilled NBR:Polymer Polarity
Hydrogen Content/NBR Volume Change/NBR 2500 2.2
AN50%
AN40.5%
AN33.5%
AN29%
AN18%
Max
imum
volum
e ratio
(V/
V 0 )
High Polarity
Low Polarity
High Polarity
Low Polarity 2.0 2000
1.8 1500
1.6
1000 1.4
500 1.2
0 1.0 0 20 40 60 80 100 0 20 40 60 80 100
Exposed pressure (MPa) Exposed pressure (MPa)
High polar NBR polymer suppress hydrogen penetration and volume inflation.
15 Unfilled NBR:Polymer Polarity
1.0
1.2
1.4
1.6
1.8
2.0
2.2
Max
imum
volum
e ratio
(V/
Vo)
AN50% AN40.5% AN33.5% AN29% AN18%
0 1000 2000 3000 Hydrogen content (wt.ppm)
Volume inflation per hydrogen content is constant for all NBR.
DBP Absorption (cm3/100g)
115 114 101 115 68 44
10μm 5μm
CB filled NBR:CB surface area
SAF ISAF HAF FEF SRF MT (N110) (N220) (N330) (N550) (N774) (N990)
Average Particle Size 19 22 28 43 66 280 (nm)
Nitrogen Surface Area 142 119 79 42 27 7-12 (m2/g)
HAF (N330)
CB filled NBR:CB surface area Hydrogen Content/NBR Volume Change/NBR 3500 2
○:unfilled unfilled 1.9 ◆:SAF50phr 3000
◆:ISAF50phr 1.8
2500
Volume Ch
ange
(V/
V0) ◆:HAF50phr
1.7 ◆:FEF50phr ◆:SRF50phr 1.6 ◆:MT50phr
1.5
1.4
1.3
CB filled 2000 unfilled
1500
1000 MT filled 1.2
500 CB filled 1.1
0 1 0 10 20 30 40 50 60 70 80 90 100 0 10 20 30 40 50 60 70 80 90 100
Hydrogen Exposure Pressure(MPa) Hydrogen Exposure Pressure(MPa)
Hyd
roge
n Co
nten
t (w
t.pp
m)
Carbonblack filled NBR’s showed high hydrogen content and low volume inflation.
Volume Ch
ange
(V/
V0) 1.7
1.8
1.9
2
unfilled
CB filled NBR:CB surface area
Large surface area suppresses volume inflation by penetrated hydrogen.
NBR
1.4
1.5
1.6 MT50phr SRF50phr
SAF50phr ISAF50phr HAF50phr FEF50phr
1.3
1.2
1.1
1 0 500 1000 1500 2000 2500
Hydrogen Content (wt.ppm) 3000 3500
Issues on polymeric materials for tank and hose 19
Carbon fiber Reinforced Plastic (CFRP) High-pressure
Hydrogen Polymeric Liner
Permeation of H2 through polymeric materials
Deformation during pressurized-decompression cycles
Type IV tank
Hoses
Inner:Polyamide Reinforce:PBO Outer:Polyester
Flexibility and durability
nipple
Leak through interface between polymeric materials and metallic materials
20 Hydrogen Content of Polymeric Materials Oth
ers
Alip
hat
ic PA
PE
Fluor
ine
VOH
>7000
■:30MPa ■:50MPa ■:90MPa
Polyethylene
Category Type Molding χWAXS χDSC ρ
LDPE Low density NOVATEC LD ZE41K Heat Press 44.4 42 0.917
LLDPE Linear low density NOVATEC LL UR951 Heat Press 43.8 36 0.916
UHMWPE Ultra High Mw SKF ECOWARE 1000 Heat Press 62.1 49 0.924
MDPE Middle density JPE PE80 Heat Press 73.4 62 0.934
HDPE High density NOVATEC HD HB111R Heat Press 76.1 59 0.942
NOVATEC HD HB111R Heat Press 76.4 64 0.943
NOVATEC HD HB111R Blow 75.1 56 0.941
NOVATEC HD HB212R Heat Press 78.6 64 0.946
JPE PE100 Heat Press 80.0 65 0.947
Hi-ZEX 7000F Injection 78.7 67 0.947
WAXS(%):Degree of Crystallinity determined by Wide Angle X-ray Scattering
DSC(%):Degree of Crystallinity determined by Differential Scanning Calorimetry
(g/cm3):Density determined by Archimedean method
PEの水素特性評価 Hyd
roge
n co
nten
t (w
t・pp
m) (x10-10)
3500 20
18 3000
4 500
Diffus
ion co
effic
ient
(m
2 /s)
2
0 0 MDPE/HDPE
16
14
12
2500
2000 10
8
6
1500
1000
0 20 40 60 80 100 0 20 40 60 80 100 Exposed pressure (MPa) Exposed pressure (MPa)
23 Summary
• Polymeric materials can be fractured by blisters and volume increment, which are originated from penetrated hydrogen.
• Volume change ratio is proportional to its hydrogen content. Carbon black can reduce the volume change of the compounds nevertheless their hydrogen contents are high.
• According to the results of model materials, O-rings for hydrogen equipment, such as breakaway device, are developed
• Liner materials of high-pressure hydrogen hoses and type IV tanks are required that low permeability of hydrogen, high durability for pressure cycles, good controllability of interface with metal materials.
• Database of elastomers for hydrogen equipment is now under discussion in the research group of the Society of Rubber Science and Technology, Japan.
24
Thank you very much for your kind attention.