Cooling capacity cyclic utilization process for producing thionyl chloride

A thionyl chloride, cooling technology, applied in cooling fluid circulation devices, applications, thionyl chloride and other directions, can solve problems such as insufficient heat exchange, increased compressor load, and inability to condense exhaust gas, avoiding a large amount of evaporation, Reduce the operating load and ensure the effect of good operation

Inactive Publication Date: 2018-04-20
SHANDONG KAISHENG NEW MATERIALS
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] (1) The cold liquid enters the reaction system after being heated and vaporized by high-temperature steam, which causes waste of cooling capacity during the energy transfer process;
[0005] (2) During the operation of the refrigerator, it is necessary to compress the cold liquid for heat exchange. Due to the high temperature in high temperature seasons, the limited heat exchange capacity of the cooling water tower results in insufficient heat exchange, which increases the load on the compressor, resulting in energy loss and equipment damage;
[0006] (3) The cooling effect of circulating water deteriorates, and the high temperature of the refrigerant in the high temperature season makes the condensation effect deteriorate, causing a large amount of tail gas to be unable to condense and fully enter the tail gas system. The entry of a large amount of tail gas increases the pressure of alkali absorption, and more alkali needs to be invested Neutralization is likely to cause environmental protection incidents; at the same time, the increase in exhaust gas absorption pressure reduces the production capacity of the device and limits the production capacity of the device

Method used

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  • Cooling capacity cyclic utilization process for producing thionyl chloride

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] Main parameter settings:

[0026] The liquid level of the cold liquid storage tank 1 is 100mm, and the pressure of the cold liquid storage tank 1 is 0.3Mpa;

[0027] The outlet temperature of heat exchanger 3 is 0°C, and the outlet pressure is ≤0.4Mpa;

[0028] The temperature of vaporizer 4 is 90°C, and the pressure is ≤0.4Mpa.

[0029] The refrigeration cycle utilization process of producing thionyl chloride of the present invention, the steps are as follows:

[0030] The cold liquid after being cryogenically cooled by the cold liquid storage tank 1 enters the heat exchanger 3, and the circulating pump pumps the water in the circulating pool 5 into the heat exchanger 3, and the cold liquid and the circulating water exchange heat in the heat exchanger 3, The cold liquid after heat exchange is vaporized by the vaporizer 4 and then enters the production system, and the circulating water after heat exchange enters the refrigerator 2 to reduce the return temperature of t...

Embodiment 2

[0032] Main parameter settings:

[0033] The liquid level of the cold liquid storage tank 1 is 700mm, and the pressure of the cold liquid storage tank 1 is 0.2Mpa;

[0034] The outlet temperature of heat exchanger 3 is 10°C, and the outlet pressure is ≤0.4Mpa;

[0035] The temperature of vaporizer 4 is 97°C, and the pressure is ≤0.4Mpa.

[0036] The refrigeration cycle utilization process of producing thionyl chloride of the present invention, the steps are as follows:

[0037] The cold liquid after being cryogenically cooled by the cold liquid storage tank 1 enters the heat exchanger 3, and the circulating pump pumps the water in the circulating pool 5 into the heat exchanger 3, and the cold liquid and the circulating water exchange heat in the heat exchanger 3, The cold liquid after heat exchange is vaporized by the vaporizer 4 and then enters the production system, and the circulating water after heat exchange enters the refrigerator 2 to reduce the return temperature of ...

Embodiment 3

[0039] Main parameter settings:

[0040] The liquid level of the cold liquid storage tank 1 is 1000mm, and the pressure of the cold liquid storage tank 1 is 0.2Mpa;

[0041] The outlet temperature of heat exchanger 3 is 20°C, and the outlet pressure is ≤0.4Mpa;

[0042] The vaporizer 4 has a temperature of 100°C and a pressure of ≤0.4Mpa.

[0043] The refrigeration cycle utilization process of producing thionyl chloride of the present invention, the steps are as follows:

[0044] The cold liquid after being cryogenically cooled by the cold liquid storage tank 1 enters the heat exchanger 3, and the circulating pump pumps the water in the circulating pool 5 into the heat exchanger 3, and the cold liquid and the circulating water exchange heat in the heat exchanger 3, The cold liquid after heat exchange is vaporized by the vaporizer 4 and then enters the production system, and the circulating water after heat exchange enters the refrigerator 2 to reduce the return temperature o...

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Abstract

The invention relates to a cooling capacity cyclic utilization process for producing thionyl chloride and belongs to the field of chemical technology production. A cold liquid which is deeply cooled by a cold liquid storage tank enters a heat exchanger. A circulating pump pumps out water in a circulation water pool, and the pumped water enters the heat exchanger. The cold liquid and circulating water perform heat exchange in the heat exchanger. The cold liquid subjected to heat exchange is vaporized by a vaporizer and then enters a production system. Circulating water subjected to heat exchange enters a refrigerator, so that the water return temperature of circulating water is reduced. According to the process, cooling capacity carried by the cold liquid in the production process of thionyl chloride is fully utilized, so that the energy consumption is reduced, and meanwhile, vaporization of lots of circulating water is avoided. The operating load of the refrigerator in high-temperatureseason is reduced, and favorable equipment operation is guaranteed.

Description

technical field [0001] The invention relates to a refrigeration cycle utilization process for producing thionyl chloride, which belongs to the field of chemical technology production. Background technique [0002] The industrial production methods of thionyl chloride mainly include chlorosulfonic acid method, phosphorus oxychloride co-production method, and sulfur dioxide gas phase method. At present, sulfur dioxide gas phase method is mainly used in China. The process route is to react chlorine gas, sulfur dioxide and sulfur dichloride in the presence of activated carbon to generate thionyl chloride. The process is simple, requires less investment and has high product purity. [0003] In order to ensure sufficient reaction in this process, the feeding amount will be higher than the theoretical value, so that the crude thionyl chloride contains excessive chlorine, sulfur dioxide and sulfur dichloride, so the crude product is purified by the sulfur compounding process, most o...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J19/00B01J4/00F25D3/00F25D17/02C01B17/45
CPCB01J19/0013B01J4/001B01J4/008B01J2219/00074C01B17/4584F25D3/005F25D17/02
Inventor 肖广明张良刘嵩王廷谢圣斌王荣海孙丰春李志忠赵婷武张廷君焦忠民
Owner SHANDONG KAISHENG NEW MATERIALS
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