Zobrazeno 1 - 10
of 27
pro vyhledávání: '"Abolghasem Shamsi"'
Publikováno v:
Fuel. 89:1280-1286
The water gas shift reaction was evaluated in the presence of novel carbon dioxide (CO 2 ) capture sorbents, both alone and with catalyst, at moderate reaction conditions (i.e., 300–600 °C and 1–11.2 atm). Experimental results showed significant
Autor:
Abolghasem Shamsi
Publikováno v:
Catalysis Today. 139:268-273
Partial oxidation of methane into syngas was conducted over fresh and sulfided catalysts at a temperature range of 450–750 °C. The temperature dependence of conversion, H2/CO ratio, and the CO2 concentration were measured for both fresh and sulfid
Autor:
Abolghasem Shamsi, Erik J. Albenze
Publikováno v:
Surface Science. 600:3202-3216
This work presents results on the dissociation of H 2 S over Ni–Mo catalysts suggesting that the presence of surface Mo-atom(s) has a significant impact on both the energetics of the process and the reaction mechanism. The presence of one Mo atom p
Autor:
Abolghasem Shamsi
Publikováno v:
Catalysis Letters. 109:189-193
Partial oxidation and dry reforming of methane to synthesis gas over Ca/Ni/K(Na) catalysts have been studied. Effects of temperature, pressure, and oxygen/methane ratios on catalytic activity, selectivity, and carbon formation have been determined. A
Publikováno v:
Applied Catalysis A: General. 293:145-152
Temperature-programmed oxidation (TPO), Raman spectrometry, and X-ray photoelectron spectroscopy (XPS) are used to characterize coke species deposited on a 0.61 wt% Pt/alumina catalyst for three reactions, carried out separately: partial oxidation (P
Autor:
Abolghasem Shamsi, James J. Spivey
Publikováno v:
Industrial & Engineering Chemistry Research. 44:7298-7305
The catalytic partial oxidation of methane on Ni−MgO solid solutions supported on metal foams has been studied at temperatures from 600 to 800 °C, 1 atm, 3000−19 000 mL/g−h, CH4/O2 = 2/1. The catalysts were prepared in two ways: (a) oxidized f
Publikováno v:
Fuel Processing Technology. 86:275-292
Low-temperature oxidation of buckskin subbituminous coal and derived chars produced in ENCOAL process was studied in a small-scale reactor at several experimental conditions. The consumption of oxygen and the generation of carbon monoxide occurred co
Autor:
Abolghasem Shamsi
Publikováno v:
Applied Catalysis A: General. 277:23-30
Reactions of 13 CH 4 and 12 CH 4 in the presence of either CO 2 or CO over reduced and oxidized Ni–MgO catalyst were studied to obtain mechanistic information on carbon deposition at low and high pressure. As the reaction time increased the amount
Publikováno v:
Catalysis Today. 84:17-25
In production of synthesis gas (syngas) from natural gas, carbon deposition is the major cause of catalyst deactivation, specifically on Ni-based catalysts. Because the rate of carbon formation is greater than the rate of carbon gasification, carbon
Autor:
Fabio B. Noronha, C. Taylor, Abolghasem Shamsi, Susan M. Stagg-Williams, E.C. Fendley, Daniel E. Resasco
Publikováno v:
Catalysis Letters. 90:13-21
CO2 reforming of methane was performed on Pt/ZrO2 and Pt/Ce-ZrO2 catalysts at 1073 K under different reactions conditions: (i) atmospheric pressure and CH4:CO2 ratio of 1:1 and 2:1; (ii) in the presence of water and CH4:CO2 ratio of 2:1; (iii) under