One-step cooling condensation and separation process for preparing dimethyl ether from synthetic raw material gas
A technology of dimethyl ether and synthesis gas, applied in ether separation/purification, ether preparation, organic chemistry, etc., can solve the problem of high operating cost, and achieve the effect of reducing energy consumption, improving utilization rate and simplifying process
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Embodiment 1
[0020] according to figure 1 The flow device test shown, H 2 +CO>50%(H 2 / CO volume ratio is 1-8) the rest is CO 2 , N 2 , Ar, CH 4 , O 2 The raw material gas is compressed by compressor 1 to 3.0-7.0 MPa and mixed with the cycle gas from cycle gas compressor 2, then enters heat exchanger 3 to exchange heat with the synthesis gas from the reactor, and then enters synthesis reactor 4. In the catalyst synthesis reactor, under the conditions of pressure 3.0-7.0MPa and temperature 180-320℃, hydrogen and carbon monoxide react to form dimethyl ether. The hot synthesis gas from the reactor first exchanges heat with the raw material gas and then enters the cooler 6 is cooled to 40°C, and methanol antifreeze is added in front of the condenser 8 to prevent freezing during condensation. Methyl ether is condensed out from the gas phase, and the condensed liquid (while part of the CO 2 and a small amount of N 2 , Ar, CH 4 , O 2 (such as the gas is also dissolved in the condensate)...
Embodiment 2
[0024] The industrialization demonstration device of a certain chemical fertilizer factory adopts the same process as in Example 1, and the synthetic raw material gas and synthetic reaction conditions are the same as in Example 1. An antifreeze is added before the dimethyl ether condenser 8, and the antifreeze is sodium chloride brine with a weight concentration of 20%. The amount added is 0.02 times the volume of the synthesis gas. When the outlet temperature of the condenser drops to -20°C, most of the dimethyl ether is condensed out from the gas phase and separated.
[0025] In the pre-distillation tower, under the operating conditions of pressure 1.0-2.0MPa, tower bottom temperature 60-160°C, tower top condensation temperature -30-10°C, the solubility of gas in dimethyl ether solution can be well adjusted separated.
[0026] In the main rectifying tower, under the operating conditions of pressure 0.3-1.0MPa, tower bottom temperature 60-200°C, tower top condenser temperatu...
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