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
View PDF5 Cites 2 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 p

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
  • Production process of sulfoxide chloride

Examples

Experimental program
Comparison scheme
Effect test

Example Embodiment

[0019] Example 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 is directly decolorized in the gaseous form through the sulfur tank and then enters the decomposer, the sulfur tank The bottom liquid phase is recycled to the synthesis kettle;

[0021] (2) The crude gas phase thionyl chloride from the decomposer enters the rectification tower, and the heavy components produced at the bottom of the rectification tower are recycled back to the synthesis kettle. The gas phase at the top of the rectification tower enters the reflux tank after condensation, and part of the liquid in the reflux tank The phase is pumped by the first machine to the rectification tower to reflux, and the remaining liquid phase in the reflux tank is recovered and reused in the synthesis kettle; the volume ratio of part of the liquid pha

Example Embodiment

[0023] Example 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 is directly decolorized in the gaseous form through the sulfur tank and then enters the decomposer, the sulfur tank The bottom liquid phase is recycled to the synthesis kettle;

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

Example Embodiment

[0027] Example 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 is directly decolorized in the gaseous form through the sulfur tank and then enters the decomposer, the sulfur tank The bottom liquid phase is recycled to the synthesis kettle;

[0029] (2) The crude gas phase thionyl chloride from the decomposer enters the rectification tower, and the heavy components produced at the bottom of the rectification tower are recycled back to the synthesis kettle. The gas phase at the top of the rectification tower enters the reflux tank after condensation, and part of the liquid in the reflux tank The phase is pumped by the first machine to the rectification tower to reflux, and the remaining liquid phase in the reflux tank is extracted and reused in the synthesis kettle; the volume ratio of part of the liquid pha

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 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

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

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
Owner SHANDONG KAISHENG NEW MATERIALS
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products