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 1767.    ---------------.  [KING, J. G.]  Synthesis of Methane.  Gas World, vol. 122, 1945, pp. 196-200, 209; Gas Times, vol. 42, Supp., 1945, pp. 1-4; Chem. Abs., vol. 39, 1945, p. 2189.

       Review of research and a discussion of the reactions involved in synthesizing CH4 from water gas and the application of these reactions to the production of city gas.  With a high H2:CO ratio and when the main reaction at a low temperature and atmospheric pressure is CO+3H2=CH4+H2O, (1), the water-gas-shift reaction must be satisfied:  CO+H2O=CO2+H2  (4).

        If the H2:CO ratio is reduced, reaction (4) becomes more effective and more CO2 appears in the final gas.  When the ratio reaches unity, the reaction is:  2CO+2H2=CH4+CO2  (2).

        The effect of increase of temperature is to favor the water-gas reaction (4) at a high ratio and the CH4 reaction (1) at a low ratio.  A constant CO2:CH4 ratio independent of the H2:CO ratio is suggested at a temperature of about 750° C.  The effect of pressure up to 25 atm. is nil at 300° but reduces the effect of increasing temperature.  AT 300° and 1 atm., the percentage of CH4 obtainable in the dry CO2-free gas rises from 83 to 98% as the H2:CO ratio falls from 3:1.  With increase of temperature the % of CH4 falls until it is less than 10% at 700°; a gas containing 50% CH4 is obtained at 500° when the pressure is 1 atm. and at 700° when the pressure is 25 atm.  In operating a technical process, assuming the use of a catalyst active enough to bring reactions (1) and (4) to completion at a high space velocity, the most favorable conditions for obtaining a gas of high CH4 content would be low temperature and atmospheric pressure whatever the H2:CO ratio.  At a higher temperature, however, the CH4 content would be maintained and catalyst activity preserved only by increasing the working pressure.  Care must be taken to prevent deterioration of the catalyst by surface overheating and bringing on reaction:

2CO=CO2+C                                                (5)

The deposition of C can be suppressed by using a high H2:CO ratio, which favors reaction (1).  To obtain a ratio of 3:1, it may be necessary to treat part of the water gas with steam

    H2+CO+H2O=CO2+2H2                                                      (6)

and to remove the CO2 by washing under pressure, thus increasing the H2 content of the original gas to the desired figure.  Ni catalysts have been developed that can be operated at a high space velocity and that have an initial activity many times greater than is necessary to carry the main reactions to equilibrium.  The reactions have been subjected to close study, and the knowledge collected is being applied to the control of the reaction on a larger scale looking towards the development of a pilot plant to operate under the proved conditions.