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Title: Catalytic Removal of Oxygen Impurities from Pressurized Oxy-Combustion Flue Gas for the Production of High-Purity Carbon Dioxide

Journal Article · · Energy and Fuels
 [1]; ORCiD logo [2];  [3];  [4];  [5]; ORCiD logo [4]; ORCiD logo [4]
  1. Univ. of Illinois at Urbana-Champaign, IL (United States); University of Illinois at Urbana-Champaign
  2. Univ. of Illinois at Urbana-Champaign, IL (United States); China Univ. of Petroleum, Qingdao (China)
  3. Univ. of Illinois at Urbana-Champaign, IL (United States); Intel Corporation, Chandler, AZ (United States)
  4. Univ. of Illinois at Urbana-Champaign, IL (United States)
  5. Univ. of Illinois at Urbana-Champaign, IL (United States); Virginia Commonwealth Univ., Richmond, VA (United States)

Flue gas purification is important for pressurized oxy-combustion systems to produce pure carbon dioxide (CO2) streams ready for storage or utilization. A catalytic approach to removing oxygen (O2) impurities from pressurized oxy-combustion flue gas via reduction with methane (CH4) was investigated in this work. Two types of catalysts were studied: palladium (Pd)-based catalysts supported on titania (TiO2) prepared by incipient wetness impregnation and cobalt–manganese (CoMn) composite catalysts prepared by coprecipitation. The performance of the catalysts was evaluated in a high-pressure–high-temperature, fixed-bed reactor at a pressure of 15 bar and a gas hourly space velocity of 30 000 h–1 (standard conditions), with a simulated feeding gas composed of 3 vol % O2, 1.5 vol % CH4, and CO2 as the balance gas. Among the Pd catalysts, 5% Pd/TiO2 achieved the maximum 86% O2 removal at ≥350 °C. The CoMn oxide catalysts displayed comparable or better activities for O2 reduction compared with the Pd catalysts. Among them, the Co40Mn1 catalyst exhibited the best performance, able to reduce 99.9% of O2 impurities at ~370 °C with negligible carbon monoxide (CO) formation (<10 ppmv). Both trivalent and divalent Co and Mn were detected on the catalyst surface, and the superior activity of Co40Mn1 might be associated with the resultant disordered structure. Furthermore, the activity of the catalyst was not affected by the presence of a trace amount of nitric oxide (NO) gas contaminant. Results of this study provide the basis for scale-up studies in both the synthesis and performance of non-noble metal catalysts.

Research Organization:
Univ. of Illinois at Urbana-Champaign, IL (United States)
Sponsoring Organization:
USDOE
Grant/Contract Number:
FE0029161
OSTI ID:
1875660
Journal Information:
Energy and Fuels, Journal Name: Energy and Fuels Journal Issue: 5 Vol. 36; ISSN 0887-0624
Publisher:
American Chemical Society (ACS)Copyright Statement
Country of Publication:
United States
Language:
English

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