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Organosilicone high-boiling-component removing and low-boiling-component removing tower pressure-variable thermal coupling distillation method and equipment

A technology for stripping towers and organic silicon, applied in the fields of silicon organic compounds, organic chemistry, chemical instruments and methods, etc., can solve the problems of high energy consumption and large consumption, and achieve energy saving, energy consumption reduction, and energy consumption reduction. Effect

Inactive Publication Date: 2016-06-22
天津市华瑞奕博化工科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] In order to solve the problems existing in the prior art, the present invention provides an organosilicon de-elevation and de-degradation tower pressure-swing thermal coupling rectification method and rectification equipment, which overcomes the problems of circulating water and steam in the de-elevation tower and de-degradation tower in the prior art The problem of high consumption and high energy consumption

Method used

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  • Organosilicone high-boiling-component removing and low-boiling-component removing tower pressure-variable thermal coupling distillation method and equipment
  • Organosilicone high-boiling-component removing and low-boiling-component removing tower pressure-variable thermal coupling distillation method and equipment
  • Organosilicone high-boiling-component removing and low-boiling-component removing tower pressure-variable thermal coupling distillation method and equipment

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Embodiment 1

[0022] Such as figure 1 As shown, the methyl chlorosilane crude monomer separation and removal process, the total feed rate of the crude monomer is 17000Kg / hr, which is recorded in mass fraction: the content of Me2 is 78%, the content of Me1 is 7.18%, and the content of Me3 The content is 7.3%, and the remaining high boiling substances and low boiling substances are 7.52%. The raw material enters the de-elevation tower 1 (high pressure), and the heavy components are extracted from the tower kettle, including part of dimethyldichlorosilane (Me2) and high boilers with a higher boiling point than dimethyldichlorosilane (Me2); Dimethyldichlorosilane (Me2) and lower light components than Dimethyldichlorosilane (Me2). The gaseous phase material at the top of the de-elevation tower 1 (high pressure) enters the reboiler 4 of the de-elevation tower 2 (low pressure) as a heat source. After coming out of the de-lowering tower reboiler, it enters the de-higher tower 1 (high pressure) to...

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Abstract

The invention discloses a rectification method and equipment for pressure-variable thermal coupling of organosilicon de-elevation and de-elevation towers. The equipment includes de-elevation towers and de-elevation towers. The heavy components are extracted from the kettle; the light components are extracted from the top of the tower; the gaseous phase material at the top of the de-elevation tower enters the reboiler of the de-elevation tower tower as a heat source; The gaseous phase material at the top of the de-elevation tower also enters the reflux tank at the top of the de-elevation tower after being condensed by the tower top condenser of the de-elevation tower. Part of the condensed liquid phase of the components returns to the top of the de-higher tower as reflux, and the other part enters the de-lowering tower as feed; the mixture extracted from the bottom of the de-lowering tower enters the subsequent refining tower for refining. The present invention adopts pressure swing thermal coupling technology and equipment, uses the gaseous phase material at the top of the de-higher tower as the heat source of the reboiler of the de-higher tower, rationally utilizes the steam energy of the gas phase at the top of the high-removal tower, and reduces energy consumption , and save energy, while reducing the amount of circulating water.

Description

technical field [0001] The invention relates to a rectification device and a rectification method, in particular to a rectification device and a rectification method for a pressure-swinging heat coupling rectification device and a rectification method of a high-removal tower and a low-removal tower in a methylchlorosilane separation device in the organic silicon industry. Background technique [0002] At a higher reaction temperature, the halogenated hydrocarbon and silicon powder are acted on in one step through a catalyst to generate a crude methylchlorosilane monomer, which mainly contains trimethylmonochlorosilane (Me3), monomethyltrichlorosilane (Me1) and Dimethyldichlorosilane (Me2), high boilers with a higher boiling point than dimethyldichlorosilane (Me2) and low boilers with a lower boiling point than trimethylmonochlorosilane (Me3). [0003] The separation of the crude methyl chlorosilane monomer will go through the treatment of de-elevation and de-lowering, that i...

Claims

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Application Information

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IPC IPC(8): C07F7/12C07F7/16C07F7/20
CPCC07F7/12C07F7/16C07F7/20
Inventor 曹平
Owner 天津市华瑞奕博化工科技有限公司
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