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An Electrochemical Fluorination External Circulation Electrolysis System

An electrolysis system and external circulation technology, which is applied in the field of electrolysis system and electrochemical fluorination external circulation electrolysis system, can solve the problems of low efficiency, explosion of cathode gas and anode gas, non-circulation of electrolyte, etc., and achieve miniaturization and energy efficiency Ratio improvement, the effect of improving recovery efficiency

Active Publication Date: 2022-08-05
PERIC SPECIAL GASES CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The fluorinating agent in electrolytic production usually uses hydrogen fluoride, and the electrolyte and hydrogen fluoride are mixed in a certain proportion to form the electrolyte. The current fluorination electrolysis system uses the Simmons fluorination electrolysis system. The electrolyte does not circulate and is stored in square or round containers. The electrode is inserted into the electrolyte, and the heat generated by the electrode reaction is taken out of the system through the refrigerant installed in the coil pipe inside the electrolytic cell, resulting in a large volume and low efficiency of the fluorinated electrolytic cell. The upper part of the tank is a gas phase space, which is easy to cause the cathode gas and anode gas to mix and explode

Method used

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  • An Electrochemical Fluorination External Circulation Electrolysis System

Examples

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Comparison scheme
Effect test

Embodiment 1

[0025] Example 1: The system implements forced circulation

[0026]The control cabinet 14 is started, and the electrolyte and hydrogen fluoride enter the anode gas-liquid separator 3 through the control valve in a certain proportion, and continue to feed until the electrolyte level reaches the remote magnetic flap level gauge in the anode gas-liquid separator 3. At one point, stop feeding, start the circulating pump 11 after the electrolysis system is purged with nitrogen, and start the rectifier cabinet 12 to send electricity. The anode gas and the cathode gas respectively enter the anode cooler 2 and the cathode cooler 6 with the electrolyte, and enter the anode gas-liquid separator 3 and the cathode gas-liquid separator 7 respectively after preliminary heat exchange. The gas phase in the anode gas and cathode gas is then raised into the anode condenser 5 and the cathode condenser 8. After fully recovering the liquid components carried, it flows out of the electrolysis throu...

Embodiment 2

[0027] Example 2: System implements natural circulation

[0028] The control cabinet 14 is started, and the electrolyte and hydrogen fluoride enter the anode gas-liquid separator 3 through the control valve in a certain proportion, and continue to feed the electrolyte liquid level to the remote magnetic flap liquid level meter in the anode gas-liquid separator 3 for three points In one place, the feeding is stopped, and after the electrolysis system is purged with nitrogen, the rectifier cabinet 12 starts to send electricity, and under the action of the DC power supply, the cathode and anode reactions occur in the electrolytic cell 1 . The anode gas and the cathode gas respectively enter the anode cooler 2 and the cathode cooler 6 with the electrolyte, and enter the anode gas-liquid separator 3 and the cathode gas-liquid separator 7 respectively after preliminary heat exchange. The gas phase in the anode gas and cathode gas is then raised into the anode condenser 5 and the cat...

Embodiment 3

[0030] If the cathode gas is directly discharged into the waste gas treatment tower without being recovered, the cathode cooler 6, the cathode gas-liquid separator 7 and the cathode condenser 8 can be removed in the whole electrolysis system. The control cabinet 14 is started, and the electrolyte and hydrogen fluoride enter the anode gas-liquid separator 3 through the control valve in a certain proportion, and continue to feed the electrolyte liquid level to the remote magnetic flap liquid level meter in the anode gas-liquid separator 3 for three points At one point, stop feeding, start the circulating pump 11 after the electrolysis system is purged with nitrogen, and start the rectifier cabinet 12 to send electricity. The anode gas entrains the electrolyte into the anode cooler 2, and enters the anode gas-liquid separator 3 after preliminary heat exchange. The gas phase in the anode gas then rises into the anode condenser 5, and after fully recovering the liquid components ca...

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Abstract

The invention provides an electrochemical fluorination external circulation electrolysis system, comprising an electrolytic cell, an anode cooler, an anode gas-liquid separator, a total cooler, an anode condenser, a cathode cooler, a cathode gas-liquid separator and a cathode condenser The anolyte outlet of the electrolytic cell is connected to the liquid inlet of the anode cooler by means of pipes, and the liquid outlet of the anode cooler is connected to the liquid inlet of the upper part of the anode gas-liquid separator by means of pipes; the bottom of the anode gas-liquid separator The liquid outlet of the total cooler is connected with the liquid inlet at the top of the total cooler by means of pipes, and the liquid outlet at the bottom of the total cooler is connected with the liquid inlet of the electrolytic cell by means of pipes. The invention facilitates the miniaturization of the electrolytic cell, can eliminate the risk of inter-connection of refrigerants and electrolytes and the mixed explosion of yin and yang gases, significantly improves the energy efficiency ratio of the electrolytic cell, is safe and reliable, the heat management is completed by the cooler, and the electrolysis temperature can be accurately controlled. Liquid separation can fully obtain high-purity product gas.

Description

technical field [0001] The invention belongs to the field of electrochemical fluorination, relates to an electrolysis system, in particular to an electrochemical fluorination external circulation electrolysis system. Background technique [0002] Compound fluorination can be accomplished by synthetic chemical reaction or electrolysis. Chemical synthesis fluorination has low conversion rate, severe reaction, difficult process control, high safety risk, and many purification steps. Electrochemical fluorination is the use of electrode reactions to introduce fluorine atoms into organic or An effective route for inorganic substances, with high conversion rate and mild reaction. At present, fluorination reactions such as nitrogen trifluoride and perfluorosulfonyl fluoride are all completed by electrochemical fluorination processes. [0003] The electrochemical fluorination system was invented by American chemist Simons in 1941. In 1946, 3M Company of the United States began to ap...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C25B9/17C25B3/28C25B9/67C25B15/021C25B15/027C25B3/11C25B1/245C25B15/08
CPCC25B9/00C25B15/08C25B15/02
Inventor 吝子东郝春辉冀延治李柄缘李林曹红梅杨雷雷袁瑞玲李虹璘
Owner PERIC SPECIAL GASES CO LTD
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