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Production device and production method of p-xylene

A technology for para-xylene and production equipment, which is applied in the production of bulk chemicals, chemical instruments and methods, and purification/separation of hydrocarbons. Cracking, saving consumption, reducing the effect of aromatic saturation

Active Publication Date: 2021-07-16
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] Aiming at the deficiencies of the prior art, the present invention provides a p-xylene production device and production method, which reduces equipment investment and floor space, reduces the operating load of the xylene tower, and saves xylene reboiler and isomerization Reacting the amount of fuel gas in the heating furnace, improving the removal efficiency of unsaturated hydrocarbons such as olefins and carbonyls in the isomerization reaction products, solving the problems of waste clay replacement and environmental pollution, and optimizing the heat exchange network at the same time, greatly reducing energy consumption and improving economic efficiency benefit and social benefit

Method used

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  • Production device and production method of p-xylene
  • Production device and production method of p-xylene
  • Production device and production method of p-xylene

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Embodiment 1

[0055] The production device of p-xylene, including xylene fractionation unit, adsorption separation unit and isomerization reaction unit;

[0056] Described xylene fractionation unit such as figure 1 shown, including: will contain C 8 Aromatic hydrocarbon mixture raw material 104 is fed to the feed line 107 of the xylene tower; the tower top discharge is sent to the pipeline 108 of the heat exchanger I102; a part of the tower top discharge after heat exchange by the heat exchanger I102 is recycled back to xylene The pipeline 109 of the tower; another part of the tower top discharge 105 after the heat exchange of the heat exchanger I102 is sent to the pipeline 110 of the heat exchanger IV306; a part of the bottom material 111 is sent to the feed pipeline of the reboiler 103 at the bottom of the tower 112; The pipeline 113 that is used to circulate the tower bottom material heated by the tower bottom reboiler 103 back to the xylene tower; Another part of the tower bottom mater...

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PUM

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Abstract

The invention discloses a production device and a production method of p-xylene. The device comprises a xylene fractionation unit, an adsorption separation unit and an isomerization reaction unit, the adsorption separation unit comprises an adsorption separation tower, an extract tower, a raffinate tower, a finished product tower, a finished product tower reboiler I, a finished product tower reboiler II, a heat exchanger II and a heat exchanger III; the isomerization reaction unit comprises an isomerization reactor, a hydrogenation reactor, an isomerization product fractionating tower, an isomerization reaction heating furnace, a heat exchanger IV, a heat exchanger V and a compressor. The invention also provides a p-xylene production process. The invention reduces equipment investment and floor area, reduces the operation load of a xylene tower, saves the fuel gas consumption of a xylene reboiling furnace and an isomerization reaction heating furnace, improves the efficiency of removing olefin, carbonyl and other unsaturated hydrocarbons from the isomerization product, solves the problems of frequent replacement of spent bleaching clay and environmental pollution, optimizes the heat exchange network, the energy consumption is greatly reduced, and the economic benefit and the social benefit are improved.

Description

technical field [0001] The invention relates to a production device and a production method of p-xylene. Background technique [0002] In industry, the adsorption separation method is generally used to obtain high-purity p-xylene products, and the raw material C 8 Aromatics include four isomers of o-xylene, p-xylene, m-xylene and ethylbenzene. Using the difference in selectivity of the adsorbent for the four isomers, the p-xylene-rich component and the depleted component are separated. Paraxylene component. The rich p-xylene is used as the feed of the extract liquid tower, and the components can be obtained through a series of rectification processes to obtain p-xylene products, and the lean p-xylene is used as the feed of the raffinate, and the components are converted into equilibrium concentration of C by isomerization reaction. 8 Aromatics mixture returns to the xylene tower for fractional distillation. In this process, the heat of the reboiler of the finished product...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C7/04C07C7/12C07C7/163C07C5/27C07C15/08
CPCC07C7/005C07C7/04C07C7/12C07C7/163C07C5/27C07C15/08Y02P20/52Y02P20/10
Inventor 胡珺薄德臣高明张英
Owner CHINA PETROLEUM & CHEM CORP
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