2805. REMBASHEVSKIĬ, A. G. [Enriching of Binary Gas Mixtures.] Trudy Leningrad. Khim. Teknol. Inst., No. 6, 1938, pp. 288-312; Khim. Referat. Zhur., vol. 1, No. 8-9, 1938, pp. 3-4; Chem. Abs., vol. 33, 1939, p. 9593. Artificially prepared mixtures of CO and H2 were passed through a layer of the catalyst [Ni obtained from Ni(NO3)2] at 200°, 240°, 280°, and 320°. For CO:H2=1:3, the reaction CO+3H2=CH4+H2O reaches its maximum at 280° (92.8% CH4, 8% H2). the 1:1 and 1:2 mixtures yield less CH4, and C is deposited from the side reaction 2CO=CO2+C. No advantages were obtained from the substitution of Co for Ni. The maximum CH4 formation took place at a higher temperature. The use of Fe-Zn, and of a specially prepared Fe catalyst gave unsatisfactory results. To obtain the CO:H2=1:3 binary gas mixture, half of the gas, free from H2S and from CO2, was passed at 450°-500° through a converter, Fe oxide with the oxides of Cr, Mg and other metals as catalysts. The CO is oxidized by water vapor according to CO+H2O=CO2+H2+10,000 kcal. After removing the CO2, both gases are mixed, dried, and passed over the catalyst. Experiment with binary peat gases gave a product with a 4,500 kcal. heat capacity, and an 80.43% yield. Analogous results were obtained from the 1:1 mixtures, but the 1:3 mixture reaction was faster, and it took place at a lower temperature. The best catalyst was Ni-Al2O3 (stable to contact contamination). Prepared water gas was passed through the catalyst at 250°-280° with an increasing velocity until the heat capacity of the final product was below 4,000 kcal./m.3. The reaction yield increased with the velocity and decreased with the increase of the heat capacity of the final product. A temperature increase, in the 250°-280° region, for the same heat capacity of the final product caused a decrease of the yield and an increase of the velocity. It was calculated that a 100,000 m.3/hr. enriching of the gases to 3,000, 3,600, 4,500, and 5,800 kcal./m.3 is commercially profitable only if the products are used close to the production plant. REMEIKA, J. P. See abs. 1136. |