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Production process for preparing dimethyl ether by methanol reaction fractional distillation stepwise reaction

A technology of reactive distillation and production process, applied in the field of coal chemical industry, can solve problems such as difficulty in removing moisture, difficulty in large-scale production, and reduced requirements for equipment anticorrosion.

Inactive Publication Date: 2009-07-15
SHANDONG UNIV OF SCI & TECH
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Problems solved by technology

[0009] Patent application CN1111231A discloses a process for synthesizing dimethyl ether by catalytic distillation. Sulfuric acid is used as a dehydration catalyst, and dimethyl ether is prepared by catalytic distillation with a rectification column in a kettle type, so that the reaction product does not contain methyl sulfate toxic substances and acidic substances. The process is simple, and the anti-corrosion requirements of the equipment are reduced, but there is also the fact that the raw material methanol is directly added from the middle and lower part of the rectification column, and the water generated by the reaction returns to the reaction kettle while the heavy phase is removed. There are also defects that are difficult to mass-produce

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  • Production process for preparing dimethyl ether by methanol reaction fractional distillation stepwise reaction

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Embodiment Construction

[0018] The present invention is described in detail below in conjunction with accompanying drawing: Raw methanol is pressurized to 0.6~1.0MPa by feed pump after heat exchanger 1,2,3 and sewage heat exchanger 4 are heated, and part methanol passes through liquid phase raw material inlet 8 Enter the dimethyl ether reactive distillation column 9, and most of the methanol enters the rectification section of the methanol vaporization recovery column 5 for vaporization; the vaporized methanol is heated to 130°C by the heater 6 and enters the dimethyl ether reactive distillation column reactor 9 The inlet of the gas phase reacts rapidly with the liquid phase catalyst at 130-200 °C and 0.05-1.0 MPa; the reaction products dimethyl ether, water vapor and unreacted methanol go up through the washing section 10 and contact with refluxing methanol to wash and remove the heavy phase, and then Enter the rectification section 19 for rectification dehydration and methanol; water is extracted fr...

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Abstract

The invention provides a production process for preparing dimethyl ether through stepwise reaction by a methanol reactive distillation method, comprising the following steps: the material methanol is pressurized to 0.6-1.0MPa by a charge pump, after being heated by a heat exchanger and a sewage heat exchanger, part of the methanol is sent to a dimethyl ether reactive rectification tower by a liquid-phase raw material inlet, and most part is sent to a rectification section of a methanol vaporization and recovery tower for vaporization; the vaporized methanol is heated to 130 DEG C by a heater and sent to a gas-phase inlet of a dimethyl ether reactive rectification tower reactor and quickly react with a liquid-phase catalyst at 130-200 DEG C and at the pressure of 0.05-1.0 MPa; the products dimethyl ether, water vapor and the unreacted methanol go upwards to pass through a washing section to contact with backflow methanol for washing and removing heavy phase, and then are sent to the rectification section for rectifying and removing water and the methanol; the water is pumped from a water outlet of the dimethyl ether reactive rectification tower, part of the water exchanges heat by the heat exchanger and then flows back, the other part thereof is sent to a stripping section of the methanol vaporization and recovery tower for circularly removing the methanol by a reboiler, and sewage is discharged from the bottom of the methanol vaporization and recovery tower, sent to a sewage workshop for treatment after exchanging heat; the dimethyl ether with the water and the methanol removed is cooled to normal temperature, is kept at the pressure or pressurized to over 0.6MPa by a compressor, and is sent to the dimethyl ether rectification tower; and the rectified dimethyl ether runs through the heat exchanger, a water cooler and a dimethyl ether reflux accumulator to obtain the high-purity dimethyl ether product.

Description

1. Technical field [0001] The invention provides a production process for preparing dimethyl ether by a step-by-step reaction of a methanol reactive distillation method, which belongs to the field of coal chemical industry. 2. Background technology [0002] At present, the production process of DME mainly includes one-step method and two-step method. [0003] The one-step method is to combine the three-step reactions of water gas shift reaction, methanol synthesis reaction and methanol dehydration reaction into one step under the action of the dual-functional composite catalyst of methanol synthesis and methanol dehydration, and realize the production of dimethyl ether in the same reactor. Preparation Process. At present, the technology of one-step method is still immature, and large-scale industrialization is facing many problems. [0004] The two-step method is to produce methanol first, and then dehydrate methanol. The two-step method has two processes, one is methanol...

Claims

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Application Information

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IPC IPC(8): C07C43/04C07C41/09
CPCY02P20/10
Inventor 田原宇乔英云盖希坤
Owner SHANDONG UNIV OF SCI & TECH
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