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Extraction method for a segment of butadiene with NMP method

A technology for butadiene and C4 fractions, which is applied in the field of one-stage extraction of butadiene, can solve the problems of high refrigerant grade requirements and large heat load, and achieve the effects of improving operational safety, improving adaptability and simplifying the process.

Active Publication Date: 2008-05-07
CHINA PETROLEUM & CHEM CORP +1
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  • Abstract
  • Description
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Problems solved by technology

[0008] In order to solve the problems of large heat load at the top of the extractive distillation tower in the one-stage extraction process of NMP butadiene, the need for a circulating gas compressor and high requirements for refrigerant grade, the present invention proposes to introduce a A new method for one-stage extraction of butadiene with the removal of the tower and the cycle gas compressor

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  • Extraction method for a segment of butadiene with NMP method
  • Extraction method for a segment of butadiene with NMP method

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Embodiment Construction

[0035] Refer below figure 1 The method of the present invention is further explained, but the present invention is not limited thereto.

[0036] One stage extraction method of NMP method butadiene of the present invention, comprises the following steps:

[0037] (1) Selective hydrogenation: the flow rate is 7830Kg / h liquid phase mixed C4 fraction (main composition: n-butane 4.0%, isobutane 1.1%, 1-butene 11.0%, isobutene 24.8%, 1,3- 48.1% of butadiene, 0.8% of ethyl acetylene, 0.4% of vinyl acetylene) and hydrogen are mixed in a ratio of 4.0 in the molar ratio of hydrogen to acetylene, with 3h -1 The volume hourly space velocity is fed into the reactor 7 from the top, and the catalyst loaded is the catalyst disclosed in the patent CN00107257.9, and the reaction temperature is 40°C and the pressure is 1.2MPa. The reaction is carried out, and the content of the mixed C4 fraction is 1.2% of alkynes were removed to 15 ppm.

[0038] (2) Removal of green oil: the reaction product...

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Abstract

The invention discloses a NMP butadiene sectional extraction method with a forward hydrogenation technology. The invention solves the problems existed in the prior NMP butadiene sectional extraction method that the tower top of a leaching and rectifying tower has large load, needs a circulated pressure compressor and has high requirement on the grade of refrigerant. The invention provides a butadiene section extraction method of leading a slight tower and canceling the circulated pressure compressor in the sectional extraction technology, and the invention comprises the steps of hydrogenation,releasing the slight components, leaching and rectifying, adsorption stripping, refining and so on. The invention is characterized in that the forward hydrogenation technology is adopted so that theacetylene hydrocarbon is released before leaching and rectifying, thereby increasing the operational safety, and the slight components are released in advance before leaching and refining so that thematerial positioned on the tower top of the adsorption stripping tower can be condensed to liquid phase, thereby being able to be transported to a refining tower through a pump; the invention cancelsthe compressor, thereby saving the device investment, decreasing the energy consumption, simplifying the operation, and being high in safety. Besides, with strong adaptive capacity on raw material, the operation of the device is not influenced by the regeneration period of catalyst.

Description

technical field [0001] The present invention relates to a kind of butadiene extraction method, more specifically, the present invention relates to a kind of one-stage extraction of butadiene using NMP (N-methylpyrrolidone, N-methylpyrrolidone) as solvent using pre-hydrogenation technology ene method. Background technique [0002] Butadiene is an important petrochemical basic organic raw material and synthetic rubber monomer, and is one of the most important components in the C4 fraction. At present, butadiene in the world is mainly extracted from the mixed C4 fraction produced by the ethylene cracking unit. This type of method is low in cost and has economic advantages. [0003] The traditional butadiene extraction process uses a two-stage extractive distillation process, but as the depth of ethylene cracking increases, the content of alkynes in the by-product C4 fraction of ethylene cracking gradually increases. The increase in alkyne content and the increase in the purit...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C11/167C07C7/163C07C7/04
CPCY02P20/584
Inventor 李东风程建民刘智信戴伟乐毅徐立英郭彦来彭晖廖丽华侯经纬王婧
Owner CHINA PETROLEUM & CHEM CORP
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