Method for producing dimethyl ether by carrying out gas-phase dehydration on methanol
A technology of dimethyl ether and dimethyl ether distillation column, which is applied in the field of methanol gas phase dehydration to produce dimethyl ether, can solve the problems of easy overheating, increased methanol energy consumption, large volume, etc., and achieves easy operation and control, and reduces equipment The effect of simple investment and process
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[0037] Such as figure 1 As shown, the flow rate of methanol as raw material is 206672kg / h, among which the flow rate of methanol buffered above the methanol buffer tank is 9613kg / h, the top pressure of the methanol buffer tank is 0.16MPa, and the temperature is 47.1°C; Flare or fuel gas piping network. One part of the methanol liquid from the methanol buffer tank is used as the top feed of the methanol rectification tower, and the other part is sent to the reactor after multi-stage heat exchange and gasification. The gasification tank uses medium-pressure steam to gasify the methanol liquid through the methanol gasifier. The pressure of the methanol gasification tank is 1.33MPa and the temperature is 148.2°C; the feed flow rate of one section is 153015kg / h, and the heat exchange with the outlet gas of the reactor reaches 260 It enters the reactor at about ℃, and the flow rate of the interstage cold shock gas is 95790kg / h. The synthesized reaction product is sent to the dimet...
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