CIESC Journal ›› 2019, Vol. 70 ›› Issue (6): 2316-2324.DOI: 10.11949/0438-1157.20181499
• Material science and engineering, nanotechnology • Previous Articles Next Articles
Qingnan SONG(),Yuting ZHANG,Chun ZHANG,Zhiliang ZHU,Xuehong GU()
Received:
2018-12-21
Revised:
2019-03-20
Online:
2019-06-05
Published:
2019-06-05
Contact:
Xuehong GU
通讯作者:
顾学红
作者简介:
<named-content content-type="corresp-name">宋庆南</named-content>(1994—),男,硕士研究生,<email>565458761@qq.com</email>
基金资助:
CLC Number:
Qingnan SONG, Yuting ZHANG, Chun ZHANG, Zhiliang ZHU, Xuehong GU. Diethylamine template-directed synthesis of hollow fiber supported SAPO-34 membranes[J]. CIESC Journal, 2019, 70(6): 2316-2324.
宋庆南, 张玉亭, 张春, 朱志良, 顾学红. 二乙胺导向合成中空纤维负载型SAPO-34分子筛膜[J]. 化工学报, 2019, 70(6): 2316-2324.
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Sample | x(DEA) | O/%(mol) | Al/%(mol) | Si/%(mol) | P/%(mol) |
---|---|---|---|---|---|
M1 | 0 | 68.83 | 13.95 | 1.29 | 15.93 |
M2 | 0.5 | 73.30 | 13.01 | 1.60 | 12.09 |
M3 | 1.0 | 70.52 | 14.01 | 2.58 | 12.89 |
M4 | 1.5 | 73.02 | 12.39 | 3.39 | 11.20 |
M5 | 2.0 | 76.57 | 11.68 | 3.73 | 8.02 |
M6 | 2.5 | 62.98 | 35.46 | 1.17 | 0.39 |
Table 1 Surface element composition results of membranes synthesized under different DEA contents in precursor
Sample | x(DEA) | O/%(mol) | Al/%(mol) | Si/%(mol) | P/%(mol) |
---|---|---|---|---|---|
M1 | 0 | 68.83 | 13.95 | 1.29 | 15.93 |
M2 | 0.5 | 73.30 | 13.01 | 1.60 | 12.09 |
M3 | 1.0 | 70.52 | 14.01 | 2.58 | 12.89 |
M4 | 1.5 | 73.02 | 12.39 | 3.39 | 11.20 |
M5 | 2.0 | 76.57 | 11.68 | 3.73 | 8.02 |
M6 | 2.5 | 62.98 | 35.46 | 1.17 | 0.39 |
Crystallization time/h | CO2 permeance×106/(mol·m?2·s?1·Pa?1) | CO2/CH4 selectivity |
---|---|---|
24 | leaking | ≈1 |
30 | 0.96 | 30 |
36 | 1.11 | 80 |
42 | 0.87 | 83 |
Table 2 Effect of crystallization time on CO2/CH4 separation performance of SAPO-34 membranes
Crystallization time/h | CO2 permeance×106/(mol·m?2·s?1·Pa?1) | CO2/CH4 selectivity |
---|---|---|
24 | leaking | ≈1 |
30 | 0.96 | 30 |
36 | 1.11 | 80 |
42 | 0.87 | 83 |
项目 | 课题组前期工作 | 本文工作 |
---|---|---|
制膜液组成 | 1.0Al2O3∶1.0P2O5∶0.45SiO2∶1.2TEAOH∶1.6DPA∶100H2O | 1.0Al2O3∶0.9P2O5∶0.6SiO2∶2.0DEA∶100H2O |
CO2渗透性×106/(mol·m?2·s?1·Pa?1) | 1.18 | 1.11 |
CO2/CH4分离选择性 | 160 | 80 |
铝源 | 异丙醇铝(Sigma) | 拟薄水铝石(工业级) |
磷酸 | 磷酸(Sigma) | 磷酸(国产) |
硅源 | 硅溶胶(Sigma) | 硅溶胶(Sigma) |
模板剂 | 四乙基氢氧化铵/二丙胺(Sigma) | 二乙胺(国产) |
水 | 蒸馏水 | 蒸馏水 |
试剂成本/(CNY·m?2) | ~2700 | ~50 |
Table 3 Comparison in separation performance and materials cost between SAPO-34 membranes in this work and our previous work
项目 | 课题组前期工作 | 本文工作 |
---|---|---|
制膜液组成 | 1.0Al2O3∶1.0P2O5∶0.45SiO2∶1.2TEAOH∶1.6DPA∶100H2O | 1.0Al2O3∶0.9P2O5∶0.6SiO2∶2.0DEA∶100H2O |
CO2渗透性×106/(mol·m?2·s?1·Pa?1) | 1.18 | 1.11 |
CO2/CH4分离选择性 | 160 | 80 |
铝源 | 异丙醇铝(Sigma) | 拟薄水铝石(工业级) |
磷酸 | 磷酸(Sigma) | 磷酸(国产) |
硅源 | 硅溶胶(Sigma) | 硅溶胶(Sigma) |
模板剂 | 四乙基氢氧化铵/二丙胺(Sigma) | 二乙胺(国产) |
水 | 蒸馏水 | 蒸馏水 |
试剂成本/(CNY·m?2) | ~2700 | ~50 |
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