Catalytic and adsorption studies for the hydrogenation of CO2 to methane

被引:171
作者
Janke, C. [1 ]
Duyar, M. S. [1 ]
Hoskins, M. [1 ]
Farrauto, R. [1 ]
机构
[1] Columbia Univ, Earth & Environm Engn Dept, New York, NY 10027 USA
关键词
Ru/Al2O3 particles and monolith; CO2; methanation; Thermal and cyclic stability; TGA/DSC adsorption studies; Carbon neutrality; CARBON-DIOXIDE METHANATION; SELECTIVE METHANATION; NICKEL-CATALYSTS; METAL CATALYSTS; LOW-TEMPERATURE; SOLAR-ENERGY; RUTHENIUM; PERFORMANCE; PALLADIUM; MECHANISM;
D O I
10.1016/j.apcatb.2014.01.016
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
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.
引用
收藏
页码:184 / 191
页数:8
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