Production method of non-convertible combined methanol and dimethyl ether from coke oven gas

A production method and technology of dimethyl ether, applied in the field of coking enterprises, can solve the problems of high cost, large investment, and difficulty in popularization and application of products.

Active Publication Date: 2006-12-13
河南广硕化工科技有限公司
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Problems solved by technology

[0003] In view of the above situation, the object of the present invention is to provide a new non-conversion co-production method of methanol dimethyl ether in coke oven gas which directly uses the effective components of coke oven gas itself to synthesize methanol and use its reaction heat to prepare dimethyl ether without conversion. The production method can well solve the problems of high energy consumption, high cost, low conversion rate and difficulty in widespread application of the product in the production of dimethyl ether. The purpose of the present invention is achieved in this way, using the coke oven gas To directly pressurize and catalyze the synthesis of methanol or re-catalyze dehydration to produce dimethyl ether, that is, after detarring and fine desulfurization, the coke oven gas is pressurized into a synthesis tower, and after methanol is synthesized under the action of a copper-based catalyst, it is injected into dimethyl ether Synthetic tower, under the same pressure and a certain temperature, use modified alumina to catalyze the rea

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  • Production method of non-convertible combined methanol and dimethyl ether from coke oven gas
  • Production method of non-convertible combined methanol and dimethyl ether from coke oven gas

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Embodiment Construction

[0006] The specific embodiment of the present invention will be described in detail below in conjunction with the production process flow chart.

[0007] Depend on figure 1 As shown, the production method of the present invention is that coke oven gas (i.e. feed gas) enters Roots blower 2 through feed gas cabinet 1, and the gas after the Roots blower passes through coarse desulfurization tower 3 and fine desulfurization tower 4 to remove sulfur and ammonia Harmful components and gas are compressed by compressor 5 and sent to methanol synthesis tower 6 at 3.0-5.0Mpa, where copper-based catalyst (C u ) under the action, the temperature is 220°C-300°C, the pressure is 3.0-5.0Mpa, in the methanol synthesis tower 6, the coke oven gas part H 2 and CO and CO 2 The reaction generates methanol, and the hot mixed gas after generating methanol is input into the dimethyl ether synthesis tower 7 at a temperature of 200-280° C., and the modified alumina catalyst (Al 2 o 3 ) under the ac...

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Abstract

The invention relates the producing method of coking gas non-convertible cogeneration methanol dimethyl ether, solving the problems of high dissipating energy, high cost and low conversion ratio. The method comprises the following steps: making coking gas decoking and desulfurizing, pressurizing them and putting them into converter, synthesizing methanol with copper as accelerating agent, transferring heat, cooling, separating, getting methanol, dimethyl ether and water, putting them into rectifying tower, getting methanol and dimethyl. The method is advanced and simple, and the product can replace diesel fuel, liquefied petroleum gas and Freon. The product is new pattern pollution-free energy and basis chemical engineering material.

Description

1. Technical field [0001] The invention relates to a production method of non-conversion and co-production of methanol dimethyl ether by directly using waste coke oven gas produced by coking to produce methanol and dimethyl ether, and is especially suitable for coking enterprises. 2. Background technology [0002] At present, the use of coke oven gas to produce methanol and dimethyl ether mostly adopts catalytic conversion and non-catalytic conversion methods, that is, the coke oven gas is first converted, and then methanol is synthesized, methanol is dehydrated to produce crude dimethyl ether, and the product is separated after rectification , this method requires a particularly huge investment in production, and also needs to consume a large amount of steam, with high energy consumption, high cost, and low ether conversion rate, and its products are difficult to effectively popularize and apply. 3. Contents of the invention [0003] In view of the above situation, the ob...

Claims

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Application Information

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IPC IPC(8): C07C43/04C07C31/04C07C41/09
Inventor 杨奇申
Owner 河南广硕化工科技有限公司
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