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Production device and production method of p-xylene

A technology for p-xylene and production equipment, applied in chemical instruments and methods, purification/separation of hydrocarbons, hydrocarbons, etc., can solve problems such as environmental pollution, reduce back-mixing, reduce equipment investment and floor space, The effect of reducing the operating load

Pending Publication Date: 2021-10-01
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 in the prior art, the object of the present invention is to provide a production device and production method of p-xylene. The present invention adjusts the trend of the logistics in the process by arranging a clapboard type reactive distillation column, and further optimizes the conversion process. The thermal network reduces the operating load of the xylene tower, saves the fuel gas consumption of the xylene reboiler, solves the problems of waste clay replacement and environmental pollution, and simultaneously performs the isomerization reaction and product separation to realize energy Coupling utilization, reducing the fuel gas consumption of the isomerization reaction heating furnace, greatly reducing energy consumption, and improving economic and social benefits

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

[0057] The production device of p-xylene, including xylene fractionation unit, adsorption separation unit and isomerization reaction unit;

[0058] Described xylene fractionation unit such as figure 1 Shown, including xylene tower 101, heat exchanger I 102 and xylene reboiler 103, also includes the C 8 Aromatic hydrocarbon mixture raw material 104 is fed to the feed line 107 of the xylene tower 101; the tower top discharge is sent to the pipeline 108 of the heat exchanger I102; The pipeline 109 of the toluene tower; another part of the tower top discharge 105 after heat exchange by the heat exchanger I102 is sent to the pipeline 110 of the adsorption separation feed; a part of the tower bottom material 111 is sent to the feed of the tower bottom reboiler 103 Pipeline 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 material 106 is discharged from the pip...

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Abstract

The invention discloses a production device and a production method of p-xylene. The production 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 heat exchanger II, a heat exchanger III, a finished product tower, a finished product tower reboiler I and a finished product tower reboiler II; and the isomerization reaction unit comprises an isomerization reaction rectifying tower, a hydrogenation reactor, an isomerization reaction heating furnace, a heat exchanger IV, a heat exchanger V and a compressor. The invention also provides a production method of p-xylene. The fuel gas consumption of the xylene reboiling furnace is reduced, isomerization reaction and product separation are carried out at the same time, and coupling utilization of energy is achieved; and the device and the method reduce the consumption of fuel gas in an isomerization reaction heating furnace, improve the efficiency of removing olefin, carbonyl and other unsaturated hydrocarbons from isomerization products, solve the problems of frequent replacement of spent bleaching clay and environmental pollution, optimize a heat exchange network, greatly reduces energy consumption, and improve economic and social benefits.

Description

technical field [0001] The invention relates to a production device and a production method of p-xylene. Background technique [0002] C 8 Aromatics include o-xylene, p-xylene, m-xylene and ethylbenzene four isomers, among which p-xylene has the largest market, so the industry usually prefers to increase the specific C 8 The production of para-xylene from aromatics feedstock sources even maximizes it. Due to their similar chemical structure and physical properties and the same molecular weight, p-xylene-depleted C is generally depleted by isomerization 8 Aromatics are converted to equilibrium concentrations of C 8 Aromatic mixture, and then obtain high-purity p-xylene products through technical means such as rectification and adsorption separation, depleted p-xylene C 8 Aromatics are re-isomerized in the system cycle. In industry, crystallization method and adsorption separation method are generally used, among which adsorption separation method is widely used. The raw...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C5/27C07C7/00C07C7/163C07C15/08
CPCC07C5/2732C07C5/277C07C7/005C07C7/163C07C15/08Y02P20/10
Inventor 胡珺薄德臣高明张英
Owner CHINA PETROLEUM & CHEM CORP
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