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Frontiers of Chemical Science and Engineering

ISSN 2095-0179

ISSN 2095-0187(Online)

CN 11-5981/TQ

邮发代号 80-969

2019 Impact Factor: 3.552

Frontiers of Chemical Science and Engineering  2019, Vol. 13 Issue (4): 772-783   https://doi.org/10.1007/s11705-019-1827-y
  本期目录
Preparation and characterization of novel carbon molecular sieve membrane/PSSF composite by pyrolysis method for toluene adsorption
Ying Yan1,2, Peng Huang1, Huiping Zhang1()
1. School of Chemistry and Chemical Engineering, Guangdong Provincial Key Laboratory of Green Chemical Product Technology, South China University of Technology, Guangzhou 510640, China
2. School of Chemical Engineering and Analytical Science, The University of Manchester, Manchester, M13 9PL, UK
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Abstract

Carbon molecular sieve membrane (CMSM)/paper-like stainless steel fibers (PSSF) has been manufactured by pyrolyzing poly (furfuryl alcohol) (PFA) coated on the metal fibers. PFA was synthesized using oxalic acid dihydrate as a catalyst and coated on microfibers by dip coating method. For the purpose of investigating the effects of final carbonization temperature, the composites were carbonized between 400°C and 800°C under flowing nitrogen. The morphology and microstructure were examined by X-ray diffraction, Fourier transforms infrared spectroscopy, scanning electron microscopy, thermogravimetric analysis, N2 adsorption and desorption, Raman spectra and X-ray photoelectron spectra. The consequences of characterization showed that the CMSM containing mesopores of 3.9 nm were manufactured. The specific surface area of the CMSM/PSSF fabricated in different pyrolysis temperature varies from 26.5 to 169.1 m2∙g1 and pore volume varies from 0.06 to 0.23 cm3∙g1. When pyrolysis temperature exceeds 600°C, the specific surface, pore diameter and pore volume decreased as carbonization temperature increased. Besides, the degree of graphitization in carbon matrix increased with rising pyrolysis temperature. Toluene adsorption experiments on different structured fixed bed that was padded by CMSM/PSSF and granular activated carbon (GAC) were conducted. For the sake of comparison, adsorption test was also performed on fixed bed packed with GAC. The experimental results indicated that the rate constant k′ was dramatically increased as the proportion of CMCM/PSSF composites increased on the basis of Yoon-Nelson model, which suggested that structured fixed bed padded with CMSM/PSSF composite offered higher adsorption rate and mass transfer efficiency.

Key wordscarbon molecular sieve membrane    stainless steel fibers    pyrolysis    structured fixed bed    toluene
收稿日期: 2018-09-28      出版日期: 2019-12-04
Corresponding Author(s): Huiping Zhang   
 引用本文:   
. [J]. Frontiers of Chemical Science and Engineering, 2019, 13(4): 772-783.
Ying Yan, Peng Huang, Huiping Zhang. Preparation and characterization of novel carbon molecular sieve membrane/PSSF composite by pyrolysis method for toluene adsorption. Front. Chem. Sci. Eng., 2019, 13(4): 772-783.
 链接本文:  
https://academic.hep.com.cn/fcse/CN/10.1007/s11705-019-1827-y
https://academic.hep.com.cn/fcse/CN/Y2019/V13/I4/772
Fig.1  
Fig.2  
Fig.3  
Fig.4  
Fig.5  
Fig.6  
Sample names BET specific surface /(m2?g1) Pore diameter /nm Pore volume /(cm3?g1)
(p/p0 = 0.99)
Micropore
surface /(m2?g1)
Micropore volume /(cm3?g1)
CM-1 26.5 5.2 0.06
CM-2 135.5 4.9 0.12 100.9 0.05
CM-3 169.1 6.0 0.23 90.8 0.04
CM-4 119.3 4.9 0.13 65.9 0.03
CM-5 118.6 4.2 0.11 64.3 0.03
PSSF 0.8
GAC 1025.5 5.1 0.69 646.3 0.26
Tab.1  
Item CM-1 CM-2 CM-3 CM-4 CM-5
D peak position /cm1 1383 1368 1351 1353 1357
D peak intensity 1546068.3 1982294.6 2320128.5 802482.3 609443.1
G peak position /cm1 1591 1588 1590 1599 1599
G peak intensity 523892.9 707511.7 972305.4 391003.7 355998.4
IG/ID 0.3389 0.3569 0.4191 0.4872 0.5841
La = 4.35 (IG/ID) /nm 1.474 1.553 1.823 2.120 2.541
Tab.2  
Fig.7  
Fig.8  
Fig.9  
Bed structure C0 /(mg?L1) Flow rate /(mL?min1) τ/min κ′ /min?1 R2
3 cm GAC 1.5 100 349.8 0.0282 0.9965
2.5 cm GAC+ 0.5 cm CMSM/PSSF 1.5 100 293.7 0.0328 0.9929
2.0 cm GAC+ 1.0 cm CMSM/PSSF 1.5 100 267.0 0.0386 0.9932
1.5 cm GAC+ 1.5 cm CMSM/PSSF 1.5 100 235.8 0.0432 0.9930
Tab.3  
Bed structure C0 /(mg?L1) Flow rate /(mL?min1) LUB /cm ?Za)
3 cm GAC 1.5 100 0.89 30
2.5 cm GAC+ 0.5 cm CMSM/PSSF 1.5 100 0.59 20
2.0 cm GAC+ 1.0 cm CMSM/PSSF 1.5 100 0.54 18
1.5 cm GAC+ 1.5 cm CMSM/PSSF 1.5 100 0.51 17
Tab.4  
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