Carbon Dioxide → Methyl formate

참여 물질

반응 단계

Synthesis gas having an inlet composition of 66.6% H2, 33.3% CO and 0.1% CO2 was fed to a 300 cc. stainless steel autoclave charged with 3 gms. copper-chromite (containing 31.1% copper and 29% chromium), 1.36 gms. of cesium chromate and 150 cc. methanol, reduced in situ using a stream of pure H2 flowing at 25 cc/min. for 16 hours at 170° C. Both catalysts were added separately in the powder form. The reactor was pressurized to 910 psig. and the temperature was adjusted to 150° C. Synthesis gas at a flow rate of 105 cc/min. (measured under standard conditions) was made to react under isothermal conditions. After an initial transient period, the process reached a steady state with respect to the amount of synthesis gas converted. A methanol production rate based on H2 consumption of 11.44 gmoles/h/kg catalyst was obtained with 50% synthesis gas conversion and 95% selectivity towards methanol. An exit gas composition of 63.55% H2, 33.75% CO, 0.45% CO2, 1.1% methanol, 1.0% methyl formate, 0.125% H2O and 0.004% dimethyl ether was obtained. A liquid composition of 95 6% methanol, 4% methyl formate, 0 3% water and traces of dimethyl ether and dissolved gases was obtained.

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