Catalyst-free ceramic-carbonate dual-phase membrane reactors for high-temperature water gas shift: A simulation study

Jerry Y.S. Lin, Lie Meng, Oscar Ovalle-Encinia

Research output: Contribution to journalArticlepeer-review

Abstract

Water gas shift (WGS) reaction enhanced by a membrane reactor technology has emerged as a high-efficiency alternative to conventional fixed-bed reactors in integrated gasification combined cycle (IGCC) plants for the electrical power generation with carbon dioxide capture. Herein, the WGS performance of a catalyst-free membrane reactor made of a CO2- permeable ceramic-carbonate dual-phase (CCDP) membrane for converting coal gasification syngas to H2 with CO2capture is studied using a one-dimensional and nonisothermal mathematical model coupled with a CO2permeation equation. The catalyst-free CCDP membrane reactor offers significantly enhanced WGS performance at high reaction pressures than a fixed-bed reactor. At 30 atm and 900°C, WGS conducted in the single-stage, catalyst-free CCDP membrane reactor features a CO conversion >95%, a pure (100%) CO2flow at the permeate side with ultrahigh CO2capture ratio (>98%), and a retentate stream consisting of 100% recovered H2 at a H2 purity >90%. Due to a strong shift in thermodynamic equilibrium and the unique membrane characteristics, the CCDP membrane reactor achieves a superior performance in WGS, which will trigger innovation in catalytic membrane reactors and increase the competitiveness of a membrane reactor technology-based IGCC process with CO2capture.

Original languageEnglish (US)
Pages (from-to)3581-3588
Number of pages8
JournalIndustrial and Engineering Chemistry Research
Volume60
Issue number9
DOIs
StatePublished - Mar 10 2021

ASJC Scopus subject areas

  • Chemistry(all)
  • Chemical Engineering(all)
  • Industrial and Manufacturing Engineering

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