Production process of sulfoxide chloride

A technology of thionyl chloride and production process, applied in the field of production technology of thionyl chloride, can solve the problems of increasing the production load of a rectifying tower, reducing the safety performance of the device, and being unable to condense tail gas, thereby reducing energy consumption and ensuring conversion. Efficiency and load reduction effect

Active Publication Date: 2017-05-17
SHANDONG KAISHENG NEW MATERIALS
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] During the preparation of thionyl chloride, the crude sulfur oxychloride in the gas phase from the reactor is condensed and sulfur mixed, and then the liquid phase is rectified, while the gas phase is recycled back to the reaction system; at the same time, the tail gas generated in the rectification process is condensed and then recycled to the reaction system. Reaction system, but it cannot condense all the tail gas, resulting in a certain material loss. The tail gas that has not been cooled needs to be emptied after water absorption and alkali absorption treatment. The process is relatively complicated and causes material loss; at the same time, too many condensers are used. The safety performance of the device is greatly reduced; the crude thionyl chloride is condensed and then gasified to cause a certain amount of steam consumption, and corresponding power equipment needs to be equipped with high energy consumption; if the gaseous crude thionyl chloride from the reactor directly enters The rectification tower increases the production load of the rectification tower; the finished product of thionyl chloride contains 0.3%-0.5% sulfuryl chloride

Method used

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  • Production process of sulfoxide chloride

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Effect test

Embodiment 1

[0020] (1) The synthesis gas produced by the reaction of sulfur and chlorine in the synthesis kettle enters the reactor together with sulfur dioxide gas, and the crude thionyl chloride generated by the reaction in the reactor directly enters the decomposer after being decolorized in the sulfur tank in gaseous form, and the sulfur tank The bottom liquid phase circulation is applied to the synthesis kettle;

[0021] (2) The crude sulfur oxychloride in the gas phase from the decomposer enters the rectification tower, and the heavy components produced at the bottom of the rectification tower are recycled to the synthesis kettle, and the gas phase at the top of the rectification tower enters the reflux tank after condensation, and part of the liquid The phase is pumped by the first machine to the reflux of the rectifying tower, and the remaining liquid phase in the reflux tank is taken out and put back into the synthesis kettle; the volume ratio of part of the liquid phase to the re...

Embodiment 2

[0024] (1) The synthesis gas produced by the reaction of sulfur and chlorine in the synthesis kettle enters the reactor together with sulfur dioxide gas, and the crude thionyl chloride generated by the reaction in the reactor directly enters the decomposer after being decolorized in the sulfur tank in gaseous form, and the sulfur tank The bottom liquid phase circulation is applied to the synthesis kettle;

[0025] (2) The crude sulfur oxychloride in the gas phase from the decomposer enters the rectification tower, and the heavy components produced at the bottom of the rectification tower are recycled to the synthesis kettle, and the gas phase at the top of the rectification tower enters the reflux tank after condensation, and part of the liquid The phase is pumped by the first machine to the reflux of the rectification tower, and the remaining liquid phase in the reflux tank is taken out and put back into the synthesis kettle; the volume ratio of part of the liquid phase to the...

Embodiment 3

[0028] (1) The synthesis gas produced by the reaction of sulfur and chlorine in the synthesis kettle enters the reactor together with sulfur dioxide gas, and the crude thionyl chloride generated by the reaction in the reactor directly enters the decomposer after being decolorized in the sulfur tank in gaseous form, and the sulfur tank The bottom liquid phase circulation is applied to the synthesis kettle;

[0029] (2) The crude sulfur oxychloride in the gas phase from the decomposer enters the rectification tower, and the heavy components produced at the bottom of the rectification tower are recycled to the synthesis kettle, and the gas phase at the top of the rectification tower enters the reflux tank after condensation, and part of the liquid The phase is pumped by the first machine to the reflux of the rectifying tower, and the remaining liquid phase in the reflux tank is taken out and put back into the synthesis kettle; the volume ratio of part of the liquid phase to the re...

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Abstract

The invention belongs to the technical field of chemical production, and in particular relates to a production process of sulfoxide chloride. The production process comprises the following steps: enabling synthetic gas generated by reaction of sulfur and chlorine gas in a synthesis kettle, and sulfur dioxide gas to enter a reactor together; directly de-coloring a crude product sulfoxide chloride, generated by reaction in the reactor, through a sulfur tank in a gas-state form, and then conveying the crude product into a decomposer; enabling a gas-phase crude product sulfoxide chloride from the decomposer to enter a rectifying tower; after condensing a gas phase at the top of the rectifying tower, enabling the gas phase to enter a refluxing tank; after enabling the gas phase in the refluxing tank to enter an evacuation tank through an injector, recycling the gas phase back into the synthesis kettle, and taking out a qualified product from the middle part of the rectifying tower. The production of the sulfoxide chloride is fully sealed circulating production, and no wastewater, waste gas and waste dreg are discharged; the yield of the product basically reaches 100 percent.

Description

technical field [0001] The invention belongs to the technical field of chemical production, and in particular relates to a production process of thionyl chloride. Background technique [0002] ZL95110380.6 discloses a manufacturing method of thionyl chloride, the method is to put the crude thionyl chloride obtained by cooling the thionyl chloride prepared by catalytic synthesis into the distillation still with sulfur powder added in advance, Distillation to obtain liquid thionyl chloride product. [0003] According to literature, in the preparation process of thionyl chloride, the crude thionyl chloride synthesized by the reactor is condensed and then subjected to batch rectification or rectification of two-stage rectification tower / three-stage rectification tower. [0004] During the preparation of thionyl chloride, the crude sulfur oxychloride in the gas phase from the reactor is condensed and sulfur mixed, and then the liquid phase is rectified, while the gas phase is re...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B17/45
CPCC01B17/4584
Inventor 谢圣斌薛居强张善民毕义霞孙丰春王荣海张良刘嵩王鑫海张泰铭
Owner SHANDONG KAISHENG NEW MATERIALS
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