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Return to Abstracts of Literature 1750-1999

Literature Abstracts

 1926.    ---------------.  [KODAMA, S., TARAMA, K., TAKAZAWA, T., FUJITA, K., TEJIMA, T., ITO, S., ANDYOKOMAKU, Y.]  Synthesis of Gaseous Hydrocarbons From Carbon Monoxide and Hydrogen.  XV.  Summary of the Studies on the Synthesis Under Pressure.  Jour. Soc. Chem. Ind. (Japan), vol. 48, 1945, pp. 3-8; Chem. Abs., vol. 43, 1949, p. 2399.

        With Fe catalysts pressure increases the life of catalyst, and increases the total rate of reaction; the yield of gasol approaches 30 l. per m.3  Increase in the gasol yield is not attainable by greater elevation of temperature.  The optimum temperature is 270°-320°.  The effect of pressure is comparatively complex.  Raising the pressure increases the tendency to form higher hydrocarbons as well as lower hydrocarbons, especially CH4 and C2H6, because of an increase in the reactivity of H2.  This fact is interpreted to be a peculiarity in the mechanism of the synthesis under pressure.  Therefore, gasol synthesis in which a high degree of unsaturation is desired should be carried out with a catalyst containing white clay as the carrier or by adding K2CO3 to a catalyst containing acid clay or active clay to promote the adsorption of CO.  By raising the temperature it is impossible to increase the yield of gasol without also raising the yield of CH4, as is the case at ordinary pressure.

                    KODAMA, S., TARAMA, K., OSHIMA, T., AND FUJITA, K.  Gasoline Synthesis From Carbon Monoxide and Hydrogen at Atmospheric Pressure.  LVI.  Analysis of the Synthetic Oil by Precision Distillation.  See abs. 1892.

                    KODAMA, S., MATSUMURA, S., TARAMA, K., ANDO, T., AND YOSHIMORI, K.  Physicochemical Research on Gasoline Synthesis.  VII.  Velocity of Adsorption of Hydrogen by Iron.  See abs. 2200.

                    KODAMA, S., MATSUMURA, S., TARAMA, K., ANDO, T., AND YOSHIMORI, K.  Physicochemical Research on Gasoline Synthesis.  VIII.  Velocity of Adsorption of Hydrogen by Iron on Infusorial Earth.  See abs. 2201.

                    KODAMA, S., MATSUMURA, S., TARAMA, K., ANDO, T., AND YOSHIMORI, K.  Physicochemical Research on Gasoline Synthesis.  IX.  Velocity of Adsorption of Hydrogen by a Composite Iron Catalyst.  See abs. 2202.

                    KODAMA, S., MATSUMURA, S., TARAMA, K., ANDO, T., AND YOSHIMORI, K.  Physicochemical Research on Gasoline Synthesis.  X.  Adsorption of Carbon Monoxide on Cobalt, Cobalt-Kieselguhr and Cobalt-Kieselguhr-Thoria Catalysts.  See abs. 2203.

                    KODAMA, S., MATSUMURA, S., TARAMA, K., ANDO, T., AND YOSHIMORI, K.  Physicochemical Research on Gasoline Synthesis.  XII.  Adsorption of Carbon Monoxide on Iron, Iron-Kieselguhr, Iron-Kieselgush-Copper-Manganese Catalysts.  See abs. 2204.

                    KODAMA, S., TAHARA, H., TAKIGUCHI, K., TOSHIMA, S., AND IHARA, K.  Gasoline Synthesis From Carbon Monoxide and Hydrogen at Moderately High Pressure. VI.  Promoter Action of Various Oxides.  See abs. 1910.

                    KODAMA, S., TARAMA, K., MISHIMA, A., FUJITA, K., AND YASUDA, M.  Synthesis of Gaseous Hydrocarbons From Carbon Monoxide and Hydrogen.  III.  Influence of Copper, Manganese, Potassium Carbonate and Boric Acid on Iron Catalysts.  IV.  Influence of the Temperature of the Synthesis on Various Promoters in the Catalyst.  See abs. 1916.

                    KODAMA, S., TARAMA, K., MISHIMA, A., FUJITA, K., AND YASUDA, M.  Synthesis of Gaseous Hydrocarbons From Carbon Monoxide and Hydrogen.  V.  Influence of Potassium Carbonate on Iron Catalyst.  VI.  Influence of Boric Acid on the Iron Catalysts.  See abs. 1917.

        KODAMA, S., MATSUMURA, S., YOSHIMORI, K., NISHIBAYASHI, Y., KADOTA, N., AND IWAMURA, E.  Physicochemical Studies on Gasoline Synthesis.  XIII.  XV.  Influence of Potassium Carbonate and Boric Acid on the Activated Adsorption of Hydrogen and Carbon Monoxide on Iron Catalysts.  See abs. 2205.