4.6 Article

Synthesis of ZSM-5 and SAPO-34 membranes in a high temperature-pressure recirculating-flow system

Journal

CHEMICAL ENGINEERING RESEARCH & DESIGN
Volume 117, Issue -, Pages 746-755

Publisher

INST CHEMICAL ENGINEERS
DOI: 10.1016/j.cherd.2016.11.035

Keywords

Zeolite membrane; MFI; SAPO-34; Gas separation; Recirculating flow system; High temperature

Funding

  1. Scientific and Technological Research Council of Turkey (TUBITAK) [110M402]
  2. TUBITAK [BIDEB-2218]

Ask authors/readers for more resources

MFI and SAPO-34 type zeolite membranes were prepared on tubular alumina supports in a recirculating flow system at elevated temperatures and reported for the first time in the literature. During membrane synthesis, the synthesis mixture flowed between the reservoir and the membrane module, which includes the membrane support. The highest synthesis temperatures were 180 degrees C and 220 degrees C, and the corresponding system pressures were approximately 20 and 30 bar for MFI and SAPO-34, respectively. The best performing MFI membrane had a CH4 single gas permeance of 2.8 x 10(-7) mol/m(2) s Pa and CH4/n-C4H10 ideal selectivity of 24 at 25 degrees C. The n-C4H10/CH4 separation selectivity was 43.6 with n-C4H10 permeance of 8 x 10(-7) mol/m(2) s Pa at 25 degrees C. The ideal selectivities of CO2/CH4 of SAPO-34 membranes synthesized at 220 and 200 degrees C in an autoclave without flow were 227 and >1000, respectively. However, the membranes synthesized by flow-induced crystallization exhibit CO2/CH4 ideal selectivities of less than 10. (C) 2016 Published by Elsevier B.V. on behalf of Institution of Chemical Engineers.

Authors

I am an author on this paper
Click your name to claim this paper and add it to your profile.

Reviews

Primary Rating

4.6
Not enough ratings

Secondary Ratings

Novelty
-
Significance
-
Scientific rigor
-
Rate this paper

Recommended

No Data Available
No Data Available