4.8 Article

Catalytic and adsorption studies for the hydrogenation of CO2 to methane

期刊

APPLIED CATALYSIS B-ENVIRONMENTAL
卷 152, 期 -, 页码 184-191

出版社

ELSEVIER SCIENCE BV
DOI: 10.1016/j.apcatb.2014.01.016

关键词

Ru/Al2O3 particles and monolith; CO2 methanation; Thermal and cyclic stability; TGA/DSC adsorption studies; Carbon neutrality

资金

  1. BASF

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CO2 methanation has been evaluated as a means of storing intermittent renewable energy in the form of synthetic natural gas. A range of process parameters suitable for the target application (4720h(-1) to 84,000h(-1) and from 160 degrees C to 320 degrees C) have been investigated at 1 bar and H-2/CO2 =4 over a 10% Ru/gamma-Al2O3 catalyst. Thermodynamic equilibrium was reached at Tk approximate to, 280 degrees C at a GHSV of 4720 h(-1). Cyclic and thermal stability tests specific to a renewable energy storage application have also been conducted. The catalyst showed no sign of deactivation after 8 start-up/shut-down cycles (from 217 degrees C to RT) and for total time on stream of 72 h, respectively. In addition, TGA-DSC was employed to investigate adsorption of reactants and suggest implications on the mechanism of reaction. Cyclic TGA-DSC studies at 265 degrees C in CO2 and H-2, being introduced consecutively, suggest a high degree of short term stability of the Ru catalyst, although it was found that CO2 chemisorption and hydrogenation activity was lowered by a magnitude of 40% after the first cycle. Stable performance was achieved for the following 19 cycles. The CO2 uptake after the first cycle was mostly restored when using a H-2-pre-treatment at 320 degrees C between each cycle, which indicated that the previous drop in performance was not linked to an irreversible form of deactivation (sintering, permanent poisoning, etc.). CO chemisorption on powder Ru/gamma-Al2O3 was used to identify metal sintering as a mechanism of deactivation at temperatures higher than 320 degrees C. A 10% Ru/gamma-Al2O3//monolith has been investigated as a model for the design of a catalytic heat exchanger. Excellent selectivity to methane and CO2 conversions under low space-velocity conditions were achieved at low hydrogenation temperatures (T= 240 degrees C). The use of monoliths demonstrates the possibility for new reactor designs using wash-coated heat exchangers to manage the exotherm and prevent deactivation due to high temperatures.(c) 2014 Elsevier B.V. All rights reserved.

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