Looking for breakthrough ideas for innovation challenges? Try Patsnap Eureka!

The production method of thionyl chloride

A technology of thionyl chloride and its production method, which is applied in the direction of thionyl chloride, sulfur and halogen compounds, can solve the problems of increasing the production load of the rectification tower, reducing the safety performance of the device, and not being able to condense the tail gas, so as to reduce energy consumption, Ease of operation and load reduction effect

Active Publication Date: 2019-03-15
SHANDONG KAISHENG NEW MATERIALS
View PDF5 Cites 0 Cited by
  • 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

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • The production method of thionyl chloride

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0020] (1) The synthesis gas produced by the reaction of sulfur and chlorine in the synthesizer enters the reactor together with sulfur dioxide gas, and the crude thionyl chloride generated by the reaction in the reactor directly passes through the absorption tower in gaseous form and then enters the decomposer and the absorption tower The liquid phase enters the receiving tank;

[0021] (2) The gas phase crude product thionyl chloride from the decomposer enters the rectification tower, the liquid phase in the receiving tank is recycled to the synthesis kettle, the heavy components generated at the bottom of the rectification tower are recycled back to the synthesis kettle, and the gas phase at the top of the rectification tower is recycled After condensing, it enters the reflux tank. Part of the liquid phase in the reflux tank is pumped to the rectification tower for reflux by the first machine pump. The remaining liquid phase in the reflux tank is extracted and reused in the syn...

Embodiment 2

[0024] (1) The synthesis gas produced by the reaction of sulfur and chlorine in the synthesizer enters the reactor together with sulfur dioxide gas, and the crude thionyl chloride generated by the reaction in the reactor directly passes through the absorption tower in gaseous form and then enters the decomposer and the absorption tower The liquid phase enters the receiving tank;

[0025] (2) The gas phase crude product thionyl chloride from the decomposer enters the rectification tower, the liquid phase in the receiving tank is recycled to the synthesis kettle, the heavy components generated at the bottom of the rectification tower are recycled back to the synthesis kettle, and the gas phase at the top of the rectification tower is recycled After condensing, it enters the reflux tank. Part of the liquid phase in the reflux tank is pumped to the rectification tower for reflux by the first machine pump. The remaining liquid phase in the reflux tank is extracted and reused in the syn...

Embodiment 3

[0028] (1) The synthesis gas produced by the reaction of sulfur and chlorine in the synthesizer enters the reactor together with sulfur dioxide gas, and the crude thionyl chloride generated by the reaction in the reactor directly passes through the absorption tower in gaseous form and then enters the decomposer and the absorption tower The liquid phase enters the receiving tank;

[0029] (2) The gas phase crude product thionyl chloride from the decomposer enters the rectification tower, the liquid phase in the receiving tank is recycled to the synthesis kettle, the heavy components generated at the bottom of the rectification tower are recycled back to the synthesis kettle, and the gas phase at the top of the rectification tower is recycled After condensing, it enters the reflux tank. Part of the liquid phase in the reflux tank is pumped to the rectification tower for reflux through the first machine pump. The remaining liquid phase in the reflux tank is extracted and reused in th...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention belongs to the technical field of chemical production, and particularly relates to a production method for thionyl chloride. The production method comprises the following step: introducing synthesis gas generated by reaction, in a reaction kettle, of sulfur and chlorine gas, and sulfur dioxide gas into a reactor, and enabling a crude product thionyl chloride generated by the reactor to directly enter a splitter in the form of gas after passing through an absorption tower; introducing gas-phase crude product thionyl chloride from the splitter to enter a rectifying column, condensing gas-phase on the top of the rectifying tower, and introducing the condensed gas-phase into a reflux tank; introducing the gas phase in the reflux tank to enter a vacuum-pumping tank through an ejector and alloying a synthesis kettle in a circulating mode, and recovering a qualified product from the middle part of the rectifying column. According to the production method, a light component in the crude product thionyl chloride is converted into a heavy component through the adsorption tower, and pressure drop before and after conversion is relatively small, operation is easy, automation is easily realized and conversion is more complete by adopting the tower, so that the load of the rectifying system is greatly reduced.

Description

Technical field [0001] The invention belongs to the technical field of chemical production, and specifically relates to a production method of thionyl chloride. Background technique [0002] ZL95110380.6 announced a manufacturing method of thionyl chloride. The method is to cool the crude product of thionyl chloride produced by catalytic synthesis into a distillation kettle with sulfur powder beforehand. Distillation to obtain liquid thionyl chloride product. [0003] According to the literature, in the preparation process of thionyl chloride, the crude product of thionyl chloride synthesized in the reactor is condensed and then subjected to batch distillation or two-stage distillation column / three-stage distillation column distillation. [0004] During the preparation of thionyl chloride, the crude product of thionyl chloride in the gas phase from the reactor is condensed and sulfurized, and then the liquid phase is rectified, and the gas phase is recycled to the reaction system; a...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Patents(China)
IPC IPC(8): C01B17/45
CPCC01B17/4584
Inventor 李云龙谢圣斌王荣海张善民孙丰春毕义霞张清新刘嵩张良王鑫海
Owner SHANDONG KAISHENG NEW MATERIALS
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Patsnap Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Patsnap Eureka Blog
Learn More
PatSnap group products