%A"Taffe, P" %D1979 %I; %2 %J[] %K01 COAL, LIGNITE, AND PEAT, 10 SYNTHETIC FUELS, COAL GASIFICATION PLANTS, DESIGN, METHANOL, SYNTHESIS, MOBIL M-GASOLINE PROCESS, ALKYLATION, COAL, COAL GASIFICATION, COMMERCIALIZATION, COST, FEASIBILITY STUDIES, FRACTIONATION, GASOLINE, HYDROFLUORIC ACID, USA, ALCOHOLS, CARBONACEOUS MATERIALS, CHEMICAL REACTIONS, ENERGY SOURCES, FOSSIL FUELS, FUELS, GASIFICATION, HYDROGEN COMPOUNDS, HYDROXY COMPOUNDS, INDUSTRIAL PLANTS, INORGANIC ACIDS, NORTH AMERICA, ORGANIC COMPOUNDS, PETROLEUM PRODUCTS, SEPARATION PROCESSES, THERMOCHEMICAL PROCESSES, 010405* - Coal, Lignite, & Peat- Hydrogenation & Liquefaction, 010404 - Coal, Lignite, & Peat- Gasification, 090221 - Alcohol Fuels- Chemical Synthesis- (1976-1989) %PMedium: X; Size: Pages: 14-15 %TAmbitious coal to gasoline plan %XA design study carried out by Badger Energy concludes that the first US commercial gasoline from coal facility could be completed in eight years. The cost of gasoline would be 1.09 US dollars/gal. in 1990 with coal at 25 US dollars/ton. The process involves oxygen-blown coal gasification, conversion to methanol by the Mobil process, gas fractionation and HF alkylation. %0Journal Article %N;Journal ID: CODEN: CHAGA %1 %CUnited Kingdom %Rhttps://doi.org/ Journal ID: CODEN: CHAGA CLA %GEnglish