Biomimetic material - poly(N-vinylimidazole)-zinc complex for … · 2011-12-07 · Biomimetic...

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Biomimetic material - poly(N-vinylimidazole)-zinc complex for CO 2 separation Kai Yao, a, b, c Zhi Wang,* a, b, c Jixiao Wang, a, b, c and Shichang Wang a, b, c Experimental Details 1. Preparation of Poly(N-vinylimidazole) Low molecular weight Poly(N-vinylimidazole): 10.0g N-vinylimidazole monomer (0.11 mol) and 0.2g azobisisobutyronitrile (0.0012mol) were dissolved in 46 ml toluene. Then the polymerization of PVI was carried out in a flask equipped with a stirrer at 70±2 o C for 4 h under nitrogen atmosphere. After polymerization, the deposit was filtered by Buchner funnel, and washed three times with acetone. At last, the product was dried in a vacuum oven at 60±2 o C for 48 h. The average molecular weight is about 3.0×10 4 , determined by viscosimeter. High molecular weight Poly (N-vinylimidazole): 10.0g N-vinylimidazole monomer (0.11mol) and 0.034g azobisisobutyronitrile (0.207 mmol) were dissolved in 30 ml benzene. Then the polymerization of PVI was carried out in a flask equipped with a stirrer at 70±2 o C for 7 h under nitrogen atmosphere. After polymerization, the deposit was filtered by Buchner funnel, and washed three times with acetone. At last, the product was dried in a vacuum oven at 60 o C for 48 h. The average molecular weight is about 2.8×10 6 , determined by viscosimeter. 2. Preparation of PVI-Zn(II) complex Various amount 1.0wt% zinc acetate aqueous solution and deionized water was dropped to 5.0wt% PVI aqueous solution slowly under stirring. Then the mixed Electronic Supplementary Material (ESI) for Chemical Communications This journal is © The Royal Society of Chemistry 2012

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Biomimetic material - poly(N-vinylimidazole)-zinc complex for CO2 separation

Kai Yao,a, b, c Zhi Wang,*a, b, c Jixiao Wang, a, b, c and Shichang Wang a, b, c

Experimental Details

1. Preparation of Poly(N-vinylimidazole)

Low molecular weight Poly(N-vinylimidazole): 10.0g N-vinylimidazole monomer

(0.11 mol) and 0.2g azobisisobutyronitrile (0.0012mol) were dissolved in 46 ml toluene.

Then the polymerization of PVI was carried out in a flask equipped with a stirrer at

70±2 oC for 4 h under nitrogen atmosphere. After polymerization, the deposit was

filtered by Buchner funnel, and washed three times with acetone. At last, the product

was dried in a vacuum oven at 60±2 oC for 48 h. The average molecular weight is about

3.0×104, determined by viscosimeter.

High molecular weight Poly (N-vinylimidazole): 10.0g N-vinylimidazole monomer

(0.11mol) and 0.034g azobisisobutyronitrile (0.207 mmol) were dissolved in 30 ml

benzene. Then the polymerization of PVI was carried out in a flask equipped with a

stirrer at 70±2 oC for 7 h under nitrogen atmosphere. After polymerization, the deposit

was filtered by Buchner funnel, and washed three times with acetone. At last, the

product was dried in a vacuum oven at 60 oC for 48 h. The average molecular weight is

about 2.8×106, determined by viscosimeter.

2. Preparation of PVI-Zn(II) complex

Various amount 1.0wt% zinc acetate aqueous solution and deionized water was

dropped to 5.0wt% PVI aqueous solution slowly under stirring. Then the mixed

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solution was stirred for half an hour in ambience for complexing. The details are

showed in table 1. (I: mole ratio of PVI/Zn(II)=20; II: mole ratio of PVI/Zn(II)=10; III:

mole ratio of PVI/Zn(II)=5)

Table 1 Details of preparation of PVI-Zn(II)complex materials

I II III

5.0wt% PVI 1.6g 1.6g 1.6g

1.0wt% zinc acetate 0.92g 1.85g 3.70g

Deionized water 2.81g 1.89g 0g

3. Permeation measurements

Separation measurements were performed with the coated membrane with the

CO2/N2 (15/85 by volume) gas mixture at 25 oC. The membrane was mounted in a

circular stainless steel cell (effective membrane area = 19.26cm2). CO2/N2 mixed gas

was fed through a humidifier, and the gas saturated with water vapor was admitted to

the permeation cell. H2 saturated with water vapor was used as sweep gas. The outlet

sweep gas composition was analyzed by a gas chromatograph equipped with a thermal

conductivity detector. Pi is the partial pressure difference of component i between the

upstream and downstream side of the membrane. Ni is the flux of component i. The

permeance Ri and selectivity α are given by Ri=Ni/Pi, α(CO2/N2)=RCO2/RN2. Gas

permeance unit(GPU) used in this study is 10-6 cm3(STP)cm−2s−1cmHg−1.

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Fig. S1. Schematic representation of gas permeation apparatus: (1) feed gas; (2) and

(4) humidifier; (3) sweep gas; (5) (9) (10) and (13) valve; (6) pressure gauge; (7)

permeation cell; (8) oven; (11) gas chromatograph; (12) soap-film flow meter.

Characterization

The characterization of the PVI-Zn(II) complex materials was accomplished by

attenuated total reflectance infrared (ATR-FTIR) spectroscopy (FTS-6000, Bio-Rad of

America), 13C-NMR (VARIAN INOVA 500MHz), scanning electron microscopies and

UV-Vis absorption spectroscopy.

The cross-section morphologies and surface of the membranes were observed with

scanning electron microscopies (SEM, Philips XL30 for surface observation and JEOL

JSM-6700F for cross-section inspection). Membrane samples were prepared for

cross-section observation by peeling away the polyester backing fabric, gently to ensure

polysulfone and active layers remained together. Wet fabric free membrane samples

were broken in the liquid nitrogen before being sputtered with gold. The active layer of

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common membranes prepared by low molecular weight PVI-Zn(II) with 150μm

coating thickness is about 700nm, and the active layer of ultra-thin membranes

prepared by high molecular weight PVI-Zn(II) with 50μm coating thickness is about

120nm.

The pure PVI and PVI-Zn(II) complex were characterized by using 13C-NMR

(VARIAN INOVA 500MHz).

CH2 CH

N

N

1

2

3

45

The spectrum of PVI contains characteristic signals from C1(136.3-137.1ppm),

C2(128.6-129.4ppm), C3(116.8-117.2ppm), C4(50.9-53.7ppm), C5(39.8-40.5ppm).

In the spectrum of PVI-Zn(II), there are four new characteristic signals which are

around 180ppm, 141ppm, 121ppm and 22ppm respectively. The peaks around 180ppm

and 22ppm are contributed to C atoms of acetate. The peaks around 141ppm and

121ppm are due to the changing of chemical shift of C1 and C2 of imidazole rings

which coordinate with Zn(II).

Because the No.3 N has lone pair electrons and Zn(II) has unoccupied orbital,

when zinc ions are added into PVI, the No.3 N atoms of imidazole rings will coordinate

with Zn(II). The lone pair electron of N atoms is attracted by Zn(II), leading the

electron density of N atoms reducing. Meanwhile, the electron cloud of C atoms next to

No.3 N is also influenced and moved to N atom. Thus, the shielding effect of C1 and

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C2 become weak and their chemical shift increases, leading new peaks formed.

The NMR proves that the the Zn(II) ions bind imidazole rings around themselves

through coordination bond between Zn(II) and No.3 N atoms.

Fig. S2. SEM image of PVI-Zn(II) membrane surface

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A

B

Fig. S3. SEM image of PVI-Zn(II) membrane cross-section: (A) common membrane,

150μm coating thickness (B) ultra-membrane, 50μm coating thickness

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A

B

Fig. S4. 13C-NMR spectrums of PVI and PVI-Zn(II) (A: PVI, B: PVI-Zn(II))

C1(136.3-137.1ppm), C2(128.6-129.4ppm),

C3(116.8-117.2ppm), C4(50.9-53.7ppm),

C5(39.8-40.5ppm)

CH2 CH

N

N

1

2

3

45

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200 300 400

1

2

Ab

s

ZnAc2 PVI/Zn(II)=20 PVI/Zn(II)=10 PVI/Zn(II)=5 PVI/Zn(II)=2 PVI/Zn(II)=1

Fig. S5. The UV absorption spectroscopy of PVI-Zn(II) complex solution

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0.2 0.4 0.6 0.8 1.0 1.2 1.4 1.6 1.80

5

10

15

Pressure(MPa)

RN

2(GP

U)

PVI-Zn(II) complex I PVI-Zn(II) complex II PVI-Zn(II) complex III PVI

Fig. S6. The N2 permeance of membranes prepared by complex materials and pure PVI

(complex I: PVI/Zn(II)=20; complex II: PVI/Zn(II)=10; complex III: PVI/Zn(II)=5)

0.2 0.4 0.6 0.8 1.0 1.2 1.4 1.6 1.80

5

10

15

20

25

30

pH=7 pH=5 pH=3

Pressure(MPa)

RN

2(GP

U)

Fig. S7. The N2 permeance of the ultra-thin membranes (PVI/Zn=10, 50μm, different

pH of coating solution)

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20 30 40 50 60 70 80 90 100 110700

750

800

850

900

950

1000

RC

O2

(GP

U)

Temperature(oC)

Fig. S8. Effects of temperature on the CO2 permeance of membrane (PVI/Zn=10, 50μm,

0.11MPa feed pressure)

20 30 40 50 60 70 80 90 100 11050

55

60

65

70

75

80

85

90

95

100

a(C

O2/

N2)

Temperature(oC)

Fig. S9. Effects of temperature on the CO2/N2 selectivity of membrane (PVI/Zn=10,

50μm, 0.11MPa feed pressure)

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0.0 0.5 1.0 1.5 2.0 2.5 3.0 3.5 4.0 4.5 5.0 5.5 6.0650

700

750

800

850

900

950 25oC100oC

RC

O2(G

PU

)

Time(h)

25oC

A

0.0 0.5 1.0 1.5 2.0 2.5 3.0 3.5 4.0 4.5 5.0 5.5 6.0

50

55

60

65

70

75

80

85

90

95

250C1000C

a(C

O2/N

2)

Time(h)

250C

B

Fig. S10. The test of thermal stability of membrane (PVI/Zn=10, 50μm, 0.11MPa feed

pressure; A: CO2 permeance, B: CO2/N2 selectivity)

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0 10 20 30 40 50 60 70 80600

700

800

900

1000

1100

1200

0

10

20

30

40

50

60

70

80

90

100

RC

O2

(GP

U)

Time(h)

a(C

O2

/N2)

Fig. S11. Separation performance stability of PVI/Zn(II) membrane (PVI/Zn=10, 50μm,

0.2MPa feed pressure)

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