Hydrogen separation process
Abstract
A method for separating a hydrogen-rich product stream from a feed stream comprising hydrogen and at least one carbon-containing gas, comprising feeding the feed stream, at an inlet pressure greater than atmospheric pressure and a temperature greater than 200.degree. C., to a hydrogen separation membrane system comprising a membrane that is selectively permeable to hydrogen, and producing a hydrogen-rich permeate product stream on the permeate side of the membrane and a carbon dioxide-rich product raffinate stream on the raffinate side of the membrane. A method for separating a hydrogen-rich product stream from a feed stream comprising hydrogen and at least one carbon-containing gas, comprising feeding the feed stream, at an inlet pressure greater than atmospheric pressure and a temperature greater than 200.degree. C., to an integrated water gas shift/hydrogen separation membrane system wherein the hydrogen separation membrane system comprises a membrane that is selectively permeable to hydrogen, and producing a hydrogen-rich permeate product stream on the permeate side of the membrane and a carbon dioxide-rich product raffinate stream on the raffinate side of the membrane. A method for pretreating a membrane, comprising: heating the membrane to a desired operating temperature and desired feed pressure in a flow of inert gasmore »
- Inventors:
-
- Longmont, CO
- Foster City, CA
- (Lafayette, CO)
- Issue Date:
- Research Org.:
- Eltron Research & Development, Inc. (Boulder, CO)
- Sponsoring Org.:
- USDOE
- OSTI Identifier:
- 1019538
- Patent Number(s):
- 7947116
- Application Number:
- 11/671,344
- Assignee:
- Eltron Research & Development, Inc. (Boulder, CO)
- Patent Classifications (CPCs):
-
B - PERFORMING OPERATIONS B01 - PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL B01D - SEPARATION
C - CHEMISTRY C01 - INORGANIC CHEMISTRY C01B - NON-METALLIC ELEMENTS
- DOE Contract Number:
- FC26-00NT40762; FC26-05NT42469; FG02-04ER83934; FG02-04ER83935; FG02-05ER84199
- Resource Type:
- Patent
- Country of Publication:
- United States
- Language:
- English
- Subject:
- 08 HYDROGEN
Citation Formats
Mundschau, Michael, Xie, Xiaobing, Evenson, IV, Carl, Grimmer, Paul, and Wright, Harold. Hydrogen separation process. United States: N. p., 2011.
Web.
Mundschau, Michael, Xie, Xiaobing, Evenson, IV, Carl, Grimmer, Paul, & Wright, Harold. Hydrogen separation process. United States.
Mundschau, Michael, Xie, Xiaobing, Evenson, IV, Carl, Grimmer, Paul, and Wright, Harold. Tue .
"Hydrogen separation process". United States. https://www.osti.gov/servlets/purl/1019538.
@article{osti_1019538,
title = {Hydrogen separation process},
author = {Mundschau, Michael and Xie, Xiaobing and Evenson, IV, Carl and Grimmer, Paul and Wright, Harold},
abstractNote = {A method for separating a hydrogen-rich product stream from a feed stream comprising hydrogen and at least one carbon-containing gas, comprising feeding the feed stream, at an inlet pressure greater than atmospheric pressure and a temperature greater than 200.degree. C., to a hydrogen separation membrane system comprising a membrane that is selectively permeable to hydrogen, and producing a hydrogen-rich permeate product stream on the permeate side of the membrane and a carbon dioxide-rich product raffinate stream on the raffinate side of the membrane. A method for separating a hydrogen-rich product stream from a feed stream comprising hydrogen and at least one carbon-containing gas, comprising feeding the feed stream, at an inlet pressure greater than atmospheric pressure and a temperature greater than 200.degree. C., to an integrated water gas shift/hydrogen separation membrane system wherein the hydrogen separation membrane system comprises a membrane that is selectively permeable to hydrogen, and producing a hydrogen-rich permeate product stream on the permeate side of the membrane and a carbon dioxide-rich product raffinate stream on the raffinate side of the membrane. A method for pretreating a membrane, comprising: heating the membrane to a desired operating temperature and desired feed pressure in a flow of inert gas for a sufficient time to cause the membrane to mechanically deform; decreasing the feed pressure to approximately ambient pressure; and optionally, flowing an oxidizing agent across the membrane before, during, or after deformation of the membrane. A method of supporting a hydrogen separation membrane system comprising selecting a hydrogen separation membrane system comprising one or more catalyst outer layers deposited on a hydrogen transport membrane layer and sealing the hydrogen separation membrane system to a porous support.},
doi = {},
journal = {},
number = ,
volume = ,
place = {United States},
year = {2011},
month = {5}
}
Works referenced in this record:
Hydrogen separation by dense cermet membranes
journal, January 2006
- Balachandran, U.; Lee, T.; Chen, L.
- Fuel, Vol. 85, Issue 2
Dense inorganic membranes for production of hydrogen from methane and coal with carbon dioxide sequestration
journal, October 2006
- Mundschau, M. V.; Xie, X.; Evenson, C. R.
- Catalysis Today, Vol. 118, Issue 1-2, p. 12-23