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Method for tail gas purification and material recovery in pivaloyl chloride production process

A technology of pivaloyl chloride and production process, applied in the field of exhaust gas purification, can solve the problems of insufficient absorption effect to achieve deep purification, incomplete recovery of organic matter, etc., and achieve the effects of avoiding violent chemical reactions, reducing organic matter content, and high material recovery rate.

Active Publication Date: 2020-04-17
NANTONG TIANSHI CHEM +1
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Problems solved by technology

[0008] Condensation is used only to recover organic materials entrained by hydrogen chloride gas. The recovery of organic matter is not complete, and there are still a large amount of non-condensable organic matter that enters the falling film absorption tower with hydrogen chloride gas.
Absorbent spraying to absorb organic matter in exhaust gas is also a common exhaust gas purification method, but the absorption effect of this method cannot reach the level of deep purification

Method used

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  • Method for tail gas purification and material recovery in pivaloyl chloride production process
  • Method for tail gas purification and material recovery in pivaloyl chloride production process
  • Method for tail gas purification and material recovery in pivaloyl chloride production process

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Embodiment Construction

[0025] Further describe the present invention below in conjunction with embodiment, the scope of the present invention is not limited to these examples.

[0026] A method for purifying tail gas and recovering materials in the production process of pivaloyl chloride, characterized in that it comprises the following steps: hydrogen chloride gas generated in the production process of pivaloyl chloride, entrained materials and air form the tail gas; firstly condense and recover through a condensing system For the organic materials in the tail gas, the condensing system is divided into two stages of circulating water submerged cooling and frozen brine cryogenic cooling. The condensed gas enters the absorption tower, and the benzylidene dichloride, one of the raw materials used in the production of pivaloyl chloride, is used as an absorbent for multi-stage absorption to further purify the gas; the gas after condensation recovery and absorption of benzylidene dichloride , the content...

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Abstract

The invention discloses a method for tail gas purification and material recovery in a pivaloyl chloride production process. The method comprises the following steps: recovering a part of materials entrained in tail gas in a condensation mode, feeding the tail gas into a specially-made absorption tower, and further absorbing organic matters in the tail gas by using low-volatility benzal dichlorideas an absorbent; introducing hydrogen chloride gas obtained through condensation and adsorption treatment into a falling film absorption tower to prepare hydrochloric acid; standing the prepared hydrochloric acid in a standing tank for layering, and recoverying an upper organic phase; wherein the condensed and recovered material and a benzal dichloride absorption liquid are directly reused in a pivaloyl chloride synthesis kettle, and the organic phase separated from hydrochloric acid is dried and dewatered by using a molecular sieve and then reused in the pivaloyl chloride synthesis kettle. The method has the advantages of high tail gas purification efficiency, thorough material recovery, deep purification of the hydrogen chloride gas, improvement of the quality of the byproduct hydrochloric acid, and reduction of the material consumption.

Description

technical field [0001] The invention belongs to the field of tail gas purification and relates to a method for tail gas purification and material recovery in the production process of pivaloyl chloride. Background technique [0002] A large amount of hydrogen chloride gas (see chemical reaction equation 1) is produced in the process of producing pivaloyl chloride with pivalic acid and benzylidene dichloride as raw materials. According to calculation, every 1t of pivaloyl chloride produced will produce 186.7m 3 of hydrogen chloride gas. During the production process of pivaloyl chloride, the reaction temperature is maintained above 120°C. Under the dual effects of high-temperature heating of the synthesis kettle and micro-negative pressure removal of tail gas in the vacuum circulation system, hydrogen chloride gas entrains a large amount of organic materials and forms pivaloyl chloride production together with a small amount of air. process exhaust. According to the test, t...

Claims

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Application Information

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IPC IPC(8): B01D53/00B01D53/14C01B7/07C07C51/60C07C53/42
CPCB01D53/002B01D53/1487B01D53/1456C01B7/0706C07C51/60B01D2252/205C07C53/42
Inventor 陈俊明朱建军王金建周新基张锦山康登海沈鑫鑫杨建军
Owner NANTONG TIANSHI CHEM
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