preparation of a novel chelating fiber with amino and its adsorption for hg 2+ reporter : yang...
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Preparation of a novel chelating fiber with amino and its adsorption for Hg2+
Reporter : Yang Ying
Tutor: Professor Chen Shuixia
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v The effective treatment of heavy metals ions in the environment has been one of the major issues owing to economic and environmental factors.
v Adsorption is one of the methods commonly used to remove heavy metal ions from various aqueous solutions with relatively low metal ion concentrations.
v Chelating fibers are effective adsorbents and have several advantages : easy to prepare, highly selective, high absorption capacity, and good removal for heavy metals ions
Ⅰ.Significance of this study
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v Graft polymerization of glycidyl methacrylate (GMA) onto PP
� increase surface-to-surface interactions
� the epoxy group of GMA have a unique reaction capability
� ring opening with various compounds possessing hydroxyl, amine, or activated methylene groups
� introduce amine groups which are well-established chelating groups.
Ⅰ. Significance of this study
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II. Objective
v To prepare a novel chelating fiber with amino group.
v Properties of the fiber:
1) high thermal stability and mechanical properties
2) high adsorption capacity for Hg2+
3) thorough removal of trace Hg2+
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Ⅲ. Research programmes
γ-ray
GMA DETAn
mC O
OHC CH2
ONH
HNH2N
n
mC O
OHC CH2
OH
n
PP-g-GMAACHF
Scheme l. Synthesis of chelating fiber with amino groups (ACHF )
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Ⅳ. results and discussion
v 1 Preparation of ACHF v 2 IR spectra v 3 SEM photographsv 4 Mechanical propertiesv 5 Thermal stability v 6 Adsorption capacity
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Effects of reaction conditions on grafting rate of PP-g-GMA
v 1.1The reaction medium v 1.2The reaction temperaturev 1.3The reaction time v 1.4The concentration of monomer
1 Preparation of ACHF
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10 20 30 40 50
0
20
40
60
80
100
Acetone
Methanol
THF
Gra
ftin
g r
ate
/%
Concentration of Monomer /%
Fig.1Effect of reaction medium on grafting rate
1.1The reaction medium
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Fig.2 Effect of reaction temperature on grafting rate
50 60 70 80 90 100 110
0
20
40
60
80
100
120
Gra
ftin
g r
ate
/%
Reaction temperature/0C
1.2The reaction temperature
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1 2 3 4 5
0
20
40
60
80
100
120
Gra
ftin
g r
ate
/%
Time/h
Fig.3 Effect of reaction time on grafting rate
1.3The reaction time
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10 20 30 40 50 600
50
100
150
200
250
Gra
ftin
g r
ate
/%
the concentration of Monomer /%
Fig.4 Effect of the concentration of monomer on grafting rate
1.4The concentration of monomer
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The optimal grafting conditions:
v solvent tetrahydrofuranv reaction time 3hv reaction temperature 100oCv monomer concentration 50 wt%
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2 IR spectra
Fig.5 FT-IR spectra of original PP, PP-g-GMA and ACHF
1000 1500 2000 2500 3000 3500
ACHF
PP-g-GMA
PP
Wavenumber/cm-1
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1000 1500 2000 2500 3000 3500
ACHF
ACHF-Hg2+
Wavenumber/cm-1
Fig.6 FT-IR spectra of ACHF and ACHF chelated Hg2+
2 IR spectra
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3 SEM photographs
Fig.6 SEM photographs of original PP and ACHF
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4 Mechanical properties
Tab.1 Mechanical properties of PP and ACHF fibers
Fiber Elongation/mm Tensile strength/cN
PP 2.3 11.5
ACHF 2.8 16.9
Growth/% 47 22
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5 Thermal stability
100 200 300 400 500 600
0
20
40
60
80
100
ACHF PP-g-GMA PP
Mas
s/%
Temperature/0C
Fig.7 TGA results of PP, PP-g-GMA and ACHF
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6 Adsorption capacity
v 6.1Effect of pH on adsorption for Hg2+
v 6.2Effect of initial concentration on adsorption v 6.3Effect of coexistence ion Cu2+ on adsorptionv 6.4Dynamic adsorption
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1 2 3 4 5 6 7
20
40
60
80
100
120
140
C=100mg.L-1;time=24h;T=29.90C
Ads
orpt
ion
capa
city
/mg.
g-1
pH value
Fig.8 Effect of pH on the adsorption capacity of Hg2+
6.1 Effect of pH
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0 200 400 600 800 10000
100
200
300
400
500
600
700
800
900
pH=4;time=20h,T=29.90C
Ads
orpt
ion
capa
city
/mg.
g-1
C0/mg.L-1
Fig.9 Adsorption capacity of ACHF for high concentration of Hg2+ in water
6.2Effect of initial concentration
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0 200 400 600 800 10000
2
4
6
8
10
12
14
16
0.0
0.2
0.4
0.6
0.8
1.0
Max allowable conc.
of Hg2+ for drinking water
C
e/u
g.L
-1
C0/ug.L-1
ad
sorp
tion
ca
pa
city
/mg
.g-1
Fig.10 Removal of trace Hg2+ in water
6.2Effect of initial concentration
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Conc. of Cu2+/mg.L-1 0 100 200 400 600 800 1000
initial conc. of Hg2+/ mg.L-1 100 100 100 100 100 100 100
residual conc. of Hg2+ / mg.L-1 0 0 0 0 0 0 0.08
Tab.2 Hg2+ adsorption amount on ACHF with Cu2+ coexist in solution
6.3Effect of coexistence ion Cu2+
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Fig.11 Effect of adsorption time on the adsorption capacity of Hg2+
6.4Dynamic adsorption
0 100 200 300 400 500 600
0
20
40
60
80
100
C0=123mg.L-1
A
dsor
ptio
n ca
paci
ty/m
g.g-1
Adsorption time/min
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Fig.12 Effect of adsorption time on the adsorption capacity of Hg2+
6.4Dynamic adsorption
0 100 200 300 400 500 600
0.0
0.2
0.4
0.6
0.8
C0=500ug.L-1
A
dsor
ptio
n ca
paci
ty/m
g.g-1
Adsorption time/min
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Ⅴ. Conclusions
v A chelating fiber with amino (ACHF) has been prepared by pre-irradiation grafting and consequently aminating.
v The results show that ACHF has better elasticity and flexibility, and good stability for common use.
v Its adsorption capacity for Hg2+ is up to 785.28mg/g .
v The fiber can get rid of trace mercury in water to meet the max allowable concentration of Hg2+ for drinking water.
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Acknowlegements:
v Professor Chen is acknowledged for both the support of this work and his sincere instruction.
v Dr. Ma, Dr. Zhang and other colleagues
v Financial supports from Key project of Sci-Tech of Guangdong Province, and Innovation Research Fund of the School of Chemistry and Chemical Engineering
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