Cellulose acetate butyrate gas separation membranes
First Claim
1. A process for using a gas separation membrane to separate a feed gas stream having at least two components into a permeate fraction which passes through the membrane and is relatively rich in at least one of the feed gas components and residual fraction which does not pass through the membrane and is relatively depleted in at least one of the feed gas components wherein the gas separation membrane comprises a cellulose acetate butyrate polymer having the formula:
- ##STR2## in which;
R each independently is OH, OOCCH3, and OOCCH2 CH2 CH3 such that the weight percent of the OOCCH2 CH2 CH3 groups in the polymer is about 10 to 45, the weight percent of OOCCH3 groups in the polymer is about 2 to about 35, and the weight percent of OH groups in the polymer is about 0.8 to about 2; and
n is selected so that the number average molecular weight of the polymer is at least about 20,000; and
provided that the membrane has a carbon dioxide permeability of at least about 5 SCFH per ft2 per 100 psi and a carbon dioxide to methane separation factor of at least about 21.
0 Assignments
0 Petitions
Accused Products
Abstract
High performance cellulose acetate butyrate gas separation membranes are prepared from a casting solution containing from about 10 to 30 percent polymer, 35 to 70 percent solvent, and 15 to 30 percent pore-forming agents. A film casting solution is cast onto a substantially flat support surface and a dense layer is formed on the exposed film surface. The film is gelled, washed, and dried to produce a particularly useful gas separation membrane. The cellulose acetate polymers used in this preparation have molecular weights of at least about 20,000, and have about 10 to about 45% butyryl groups, about 2 to about 35% acetyl groups, and about 0.8 to about 2 percent hydroxyl groups, by weight. The membranes may be used for separating a feed gas into a permeate fraction and a residual fraction, and are particularly useful for separating gases in the purge gas stream of ammonia plants to recover a permeate which is relatively rich in hydrogen. Cellulose acetate butyrate membranes may be used to improve the separation of ammonia plant purge gases which contain ammonia as well as hydrogen and nitrogen, especially when there is no pretreatment of the purge gas to remove ammonia gas.
30 Citations
10 Claims
-
1. A process for using a gas separation membrane to separate a feed gas stream having at least two components into a permeate fraction which passes through the membrane and is relatively rich in at least one of the feed gas components and residual fraction which does not pass through the membrane and is relatively depleted in at least one of the feed gas components wherein the gas separation membrane comprises a cellulose acetate butyrate polymer having the formula:
- ##STR2## in which;
R each independently is OH, OOCCH3, and OOCCH2 CH2 CH3 such that the weight percent of the OOCCH2 CH2 CH3 groups in the polymer is about 10 to 45, the weight percent of OOCCH3 groups in the polymer is about 2 to about 35, and the weight percent of OH groups in the polymer is about 0.8 to about 2; andn is selected so that the number average molecular weight of the polymer is at least about 20,000; and provided that the membrane has a carbon dioxide permeability of at least about 5 SCFH per ft2 per 100 psi and a carbon dioxide to methane separation factor of at least about 21. - View Dependent Claims (2, 3, 4, 5, 6)
- ##STR2## in which;
-
7. An asymmetric gas separation membrane comprising a cellulose acetate butyrate polymer having the formula:
- ##STR3## in which;
R each independently is OH, OOCCH3, and OOCCH2 CH2 CH3 such that the weight percent of the OOCCH2 CH2 CH3 group in the polymer is about 10 to 45, the weight percent of OOCCH3 groups in the polymer is about 2 to about 35, and the weight percent of OH groups in the polymer is about 0.8 to about 2; andn is selected so that the number average molecular weight of the polymer is at least about 20,000; and provided that the membrane has a carbon dioxide permeability of at least about 5 SCFH per ft2 per 100 psi and a carbon dioxide to methane separation factor of at least about 21. - View Dependent Claims (8, 9, 10)
- ##STR3## in which;
Specification