Process for refining C-4 hydrocarbon fluid

A C4 hydrocarbon and logistics technology, which is applied in the refining process of C4 hydrocarbon logistics, can solve the problems of scrapping sulfuric acid, yellowing of alkylated oil, increasing acid consumption, etc.

Active Publication Date: 2015-12-16
CHINA CHENGDA ENG
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  • Abstract
  • Description
  • Claims
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Problems solved by technology

Each ton of sulfide can cause 16-60t of sulfuric acid to be scrapped
In addition to increasing acid consumption, sulfides in raw materials can also cause the color of alkylated oil to turn yellow, have an odor, and even produce foam, which seriously affects the quality of alkylated products.

Method used

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  • Process for refining C-4 hydrocarbon fluid

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Embodiment Construction

[0064] Below in conjunction with accompanying drawing, the present invention is described in detail.

[0065] In order to make the object, technical solution and advantages of the present invention clearer, the present invention will be further described in detail below in conjunction with the accompanying drawings and embodiments. It should be understood that the specific embodiments described here are only used to explain the present invention, not to limit the present invention.

[0066] Such as figure 1 Shown, a kind of refinement equipment of C4 hydrocarbon flow, comprises demethanol tower 1, one-stage hydrogenation reactor 2, two-stage hydrogenation reactor 3, depropanizer 4, deethanizer 5 and adsorption tower 6, all The top of the demethanolizer 1 is connected to the bottom of the one-stage hydrogenation reactor 2 through a high-efficiency coalescer 7, and the top of the one-stage hydrogenation reactor 2 is connected to the bottom of the second-stage hydrogenation reac...

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Abstract

The invention discloses a process for refining C-4 hydrocarbon fluid. Preparation equipment includes a methanol removing tower, a first hydrogenation reactor, a second hydrogenation reactor, a depropanizing column, a dethanizing column and an adsorption tower, wherein the top of the methanol removing tower is connected with the bottom of the first hydrogenation reactor through a high-efficiency coalescer; the top of the first hydrogenation reactor is connected with the bottom of the second hydrogenation reactor through a pipeline; the top of the second hydrogenation reactor is connected with the depropanizing column through another pipeline; the top of the depropanizing column is connected with the dethanizing column through another pipeline; and the bottom of the dethanizing column is connected with the adsorption tower through another pipeline. The process mainly aims to a purification process of an alkylation raw material, and comprises the following steps: by taking mixed C-4 hydrocarbon as a raw material, extracting with water to remove methanol so as to reduce the content of methanol in C-4 hydrocarbon to be lower than 50ppm, selectively adding hydrogen and isomerizing so as to reduce the content of butadiene in C-4 hydrocarbon to be lower than 50ppm, converting more than 70% of 1-butene into 2-butene, and finally rectifying to remove dimethyl ether and C-3, thereby obtaining refined C-4 as the alkylation raw material, and a byproduct refined C-3 as a propane dehydrogenation propylene raw material.

Description

technical field [0001] The invention belongs to the technical field of chemical industry, and in particular relates to a refining process of a C4 hydrocarbon stream. Background technique [0002] C4 hydrocarbons are important petrochemical raw materials. They are the general term for C4 alkanes, monoolefins and dienes. In petrochemical enterprises, catalytic cracking, ethylene cracking, aromatics reforming and coal chemical coal-to-olefins will produce a considerable amount of by-products. Mixed carbon tetrahydrocarbons. For the comprehensive utilization of C4Hs, with the rapid development of my country's petrochemical and coal chemical industries in recent years, the problem of effective utilization of C4Hs resources has become more and more prominent. Especially when the use of MTBE (methyl tert-butyl ether) may be completely banned in the future, it is necessary to process C4 hydrocarbons to produce alkylated oil, and to develop and apply C4 hydrocarbons using new techno...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C9/12C07C11/08C07C7/00C07C7/10C07C7/163C07C7/148C07C7/04C07C7/13
Inventor 陈胜张晓辉周齐领
Owner CHINA CHENGDA ENG
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