CARBON MEMBRANES FOR GAS SEPARATION - DEVELOPMENTAL STUDIES
被引:21
作者:
DAMLE, AS
论文数: 0引用数: 0
h-index: 0
机构:RES TRIANGLE INST,RES TRIANGLE PK,NC 27709
DAMLE, AS
GANGWAL, SK
论文数: 0引用数: 0
h-index: 0
机构:RES TRIANGLE INST,RES TRIANGLE PK,NC 27709
GANGWAL, SK
VENKATARAMAN, VK
论文数: 0引用数: 0
h-index: 0
机构:RES TRIANGLE INST,RES TRIANGLE PK,NC 27709
VENKATARAMAN, VK
机构:
[1] RES TRIANGLE INST,RES TRIANGLE PK,NC 27709
[2] US DOE,MORGANTOWN ENERGY TECHNOL CTR,MORGANTOWN,WV 26507
来源:
GAS SEPARATION & PURIFICATION
|
1994年
/
8卷
/
03期
关键词:
CARBON COMPOSITE MEMBRANES;
GAS SEPARATION;
KNUDSEN DIFFUSION;
MEMBRANE MODIFICATIONS;
D O I:
10.1016/0950-4214(94)80024-3
中图分类号:
TQ [化学工业];
学科分类号:
0817 ;
摘要:
Carbon membranes with 0.2 and 1.0 mum pore sizes are commercially available for liquid microfiltration applications. These membranes may be modified for gas separation applications by providing a gas separation layer with pores in the 1 to 10 nm range. With such pores, gases are separated by Knudsen diffusion with an individual gas species permeation rate inversely proportional to the ratio of the square root of the molecular weight of the permeating species. This paper describes some of the techniques used for depositing a suitable layer starting with various organic polymeric precursors. The in situ polymerization technique was found to be the most promising, and pure component tests with membrane samples prepared with this technique indicated Knudsen diffusion behaviour. The gas separation factors obtained by mixed-gas permeation tests were found to depend strongly on gas temperature and pressure indicating significant viscous flow at high-pressure conditions.