Carbon composite membranes from Matrimid (R) and Kapton (R) polyimides forgas separation

Citation
Ab. Fuertes et al., Carbon composite membranes from Matrimid (R) and Kapton (R) polyimides forgas separation, MICROP M M, 33(1-3), 1999, pp. 115-125
Citations number
33
Categorie Soggetti
Apllied Physucs/Condensed Matter/Materiales Science
Journal title
MICROPOROUS AND MESOPOROUS MATERIALS
ISSN journal
13871811 → ACNP
Volume
33
Issue
1-3
Year of publication
1999
Pages
115 - 125
Database
ISI
SICI code
1387-1811(199912)33:1-3<115:CCMFM(>2.0.ZU;2-6
Abstract
The preparation and characteristics of supported carbon membranes from comm ercial polyimides are reported here. Carbon molecular sieve membranes (CMSM ) with asymmetric and symmetric structures have been obtained in only one c asting step by the phase inversion technique. The precursors were polyimide -type polymers available commercially: Allotherm(R) 610-16 (BASF) and Matri mid(R) 5218 (Ciba Specialty Chemicals). The preparation method involved coa ting of the macroporous carbon supports with a polymeric solution and subse quent gellation of the polymeric film by immersion in a coagulant bath. The carbon membranes were obtained by heat treatment (450-700 degrees C) of th e resulting devices under vacuum. The permeability and selectivity data ind icate that the resulting carbon membranes possess molecular sieve propertie s and that they are suitable for the separation of permanent gases of indus trial interest (O-2/N-2, CO2/CH4, CO2/N-2, etc.). Kapton(R) carbon membrane s are more permeable than those derived from Matrimid(R). The permeability and permselectivity measured at 25 degrees C for Kapton(R)-derived CMSM wer e: permeability (CO2) = 92 Barrer, permselectivity (CO2/CH4) = 16, permsele ctivity (CO2/N-2 = 9; permeability (O-2)=45 Barrer, permselectivity (O-2/N- 2)=4. By contrast, the materials obtained from Matrimid(R) are, in general, less permeable but more selective: permeability (CO2)=12 Barrer, permselec tivity (CO2/CH4)=33, permselectivity (CO2/N-2)=15; permeability (O-2)=5 Bar rer, permselectivity (O-2/N-2)=6. (C) 1999 Elsevier Science B.V. All rights reserved.