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Studies in Surface Science and Catalysis | 2007

Natural gas purification with a DDR zeolite membrane; permeation modelling with maxwell-stefan equations

Johan van den Bergh; W. Zhu; Johan C. Groen; Freek Kapteijn; Jacob A. Moulijn; Kenji Yajima; Kunio Nakayama; Toshihiro Tomita; Shuichi Yoshida

Abstract The permeation of CO 2 , N 2 and CH 4 and their mixtures through a DDR membrane has been investigated over a wide range of temperatures and pressures. The synthesized DDR membrane exhibits a very high selectivity for CO 2 and a moderate selectivity for N 2 over CH 4 with good permeances. At a total pressure of 101 kPa and temperature of 225 K, the selectivity for CO 2 was found to be over 3000 and 40 for N 2 in a 50/50 feed mixture with CH 4 , both decrease with temperature. The N 2 /CH 4 selectivity remains constant with pressure, while that for CO 2 /CH 4 decreases. An engineering model, based on the generalized Maxwell-Stefan equations, has been used to interpret the transport phenomena in the membrane. The diffusivity of these permanent gases is strongly dependent on the loading in the membrane, severely complicating modelling work. A model developed by Reed and Ehrlich [ 1 ] could describe this phenomenon well for both the unary as the binary permeances. The feasibility of DDR membranes as applied to CO 2 and N 2 removal from natural gas is anticipated.


Research on Chemical Intermediates | 2008

Separation of CO2 and CH4 by a DDR membrane

Johan van den Bergh; W. Zhu; Freek Kapteijn; Jacob A. Moulijn; Kenji Yajima; Kunio Nakayama; Toshihiro Tomita; Shuichi Yoshida

The permeation of CO2 and CH4 and their binary mixtures through a DDR membrane has been investigated over a wide range of temperatures and pressures. The synthesized DDR membrane exhibits a high permeance and maintains a very high selectivity for CO2. At a total pressure of 101 kPa, the highest selectivity for CO2 in a 50∶50 feed mixture was found to be over 4000 at 225 K. This is ascribed to the higher adsorption affinity, as well as to the higher mobility for the smaller CO2 molecules in the zeolite, preventing the bypassing of the CH4 through the membrane. An engineering model, based on the generalized Maxwell-Stefan equations, has been used to interpret the transport phenomena in the membrane. The feasibility of DDR membranes as applied to CO2 removal from natural gas or biogas is anticipated.


Microporous and Mesoporous Materials | 2004

Gas separation characteristics of DDR type zeolite membrane

Toshihiro Tomita; Kunio Nakayama; Hitoshi Sakai


Microporous and Mesoporous Materials | 2007

Characterization and selectivity for methane and carbon dioxide adsorption on the all-silica DD3R zeolite

Shuji Himeno; Toshihiro Tomita; Kenji Suzuki; Shuichi Yoshida


Industrial & Engineering Chemistry Research | 2007

Synthesis and Permeation Properties of a DDR-Type Zeolite Membrane for Separation of CO2/CH4 Gaseous Mixtures

Shuji Himeno; Toshihiro Tomita; Kenji Suzuki; Kunio Nakayama; Kenji Yajima; Shuichi Yoshida


Journal of Membrane Science | 2008

Dehydration performance of a hydrophobic DD3R zeolite membrane

Jelan Kuhn; Kenji Yajima; Toshihiro Tomita; Joachim Gross; Freek Kapteijn


Archive | 2005

Method for preparing ddr type zeolite membrane, ddr type zeolite membrane, and composite ddr type zeolite membrane, and method for preparation thereof

Kunio Nakayama; Kenji Suzuki; Manabu Yoshida; Kenji Yajima; Toshihiro Tomita


Archive | 2002

Method for preparing DDR type zeolite film, DDR type zeolite film, and composite DDR type zeolite film, and method for preparation thereof

Kunio Nakayama; Kenji Suzuki; Manabu Yoshida; Kenji Yajima; Toshihiro Tomita


Archive | 2008

Method of dehydration, dehydrating apparatus, and membrane reactor

Kenji Yajima; Kunio Nakayama; Makiko Niino; Toshihiro Tomita


Archive | 2002

METHOD FOR MANUFACTURING DDR TYPE ZEOLITE

Nobuhiko Mori; Kunio Nakayama; Toshihiro Tomita; Kenji Yajima; 中山 邦雄; 富田 俊弘; 森 伸彦; 谷島 健二

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Shuichi Yoshida

Nagaoka University of Technology

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Akira Takahashi

National Institute of Advanced Industrial Science and Technology

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Shuji Himeno

Nagaoka University of Technology

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Freek Kapteijn

Delft University of Technology

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