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Title: Catalyzed gasification of coals and coal chars. [20 refs. ; 500 to 1000 psig; 650 to 850/sup 0/C; KHCO/sub 3/; NaHCO/sub 3/; ZnCl/sub 2/; CH/sub 3/COOAg; UO/sub 2/(NO/sub 3/)/sub 2/; CoCl/sub 2/; Pb(NO/sub 3/)/sub 2/; NiCO/sub 3/; ZnO; WS/sub 2/; CoCO/sub 3/; Al/sub 2/O/sub 3/--SiO/sub 2/]

Conference · · Am. Chem. Soc., Div. Fuel Chem., Prepr.; (United States)
OSTI ID:7264822

Gasification of high volatile bituminous coals and coal chars with hydrogen and steam was studied at 500 and 1000 psig and 650 to 850/sup 0/C in a thermobalance. The following classes of catalysts were used singly and in combination: acidic cracking catalysts, methanation catalysts, hydrogenation catalysts and potassium salts. Simple mathematical modelling indicates that for catalyzed and noncatalyzed systems the geometric similarity of the coal particles change as they are gasified, and hence the mass transfer rates change also. The catalysts had relatively little influence on the initial devolatilization, but had a strong influence on the pre-exponential factor and activation energy of the gasification of the residual char. Annealing of the coal samples in the presence of the catalyst before reaction increased the ultimate reaction rate. It is not known whether this is caused by diffusion of the catalyst into the mass, or whether the specific surface area of the sample was affected. Potassium salts, acting by themselves, were the most effective. In all cases, at least 5 wt. percent of catalyst was required, indicating that physical as well as purely chemical catalytic processes may be operative.

Research Organization:
Case Western Reserve Univ., Cleveland
OSTI ID:
7264822
Journal Information:
Am. Chem. Soc., Div. Fuel Chem., Prepr.; (United States), Vol. 20:3; Conference: 170. American Chemical Society national meeting, Chicago, IL, USA, 24 Aug 1975; Other Information: See CONF-750806--P1
Country of Publication:
United States
Language:
English