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Electrochemical fluorination external circulation flexible electrolysis system

An electrolysis system and external circulation technology, applied in the field of electrochemical fluorination external circulation flexible electrolysis system, to achieve the effect of solving system risks and reducing corrosion risks

Active Publication Date: 2021-02-19
PERIC SPECIAL GASES CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The purpose of the present invention is to solve the shortcomings in the prior art, and propose a flexible electrolytic system for electrochemical fluorination external circulation, which highly integrates the electrolytic cell and uses the successfully developed bipolar series-parallel combined pressure Filter type electrolytic cell, the heat generated by the electrode reaction is completed by the cooler outside the electrolytic cell, the gas production of the electrolytic cell is adjusted by closing the anode single switch, the electrolytic group I adopts the structure of positive in the middle and negative at both ends to reduce the total voltage of electrolysis Half, to reduce the risk of electrolyte channel corrosion, use several electrolysis groups I in parallel to ensure the output of the electrolysis system, if a certain electrolysis chamber is blocked and the electrolysis voltage is higher than 8V, you only need to open the single switch in the electrolysis group I, The other electrolytic group I can continue to work without interference, which solves the system risk caused by the blockage of a small chamber

Method used

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  • Electrochemical fluorination external circulation flexible electrolysis system

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0040] Example 1: The system implements forced circulation

[0041] The DCS cabinet 1 is started, and the electrolyte and hydrogen fluoride enter the gas-liquid separator 11 through the control valve at a certain ratio, and continue to feed the electrolyte until the liquid level of the electrolyte reaches one-third of the remote liquid level gauge in the anode gas-liquid separator 11. Stop feeding, start the circulation pump M01 after nitrogen purging of the electrolysis system, and start the DC power supply 2 to transmit power.

[0042] The anode gas and cathode gas engulf the electrolyte in the gas-liquid separator 11 respectively.

[0043] The gas phase rises into the gas condenser 12, and after fully recovering the carried liquid components, it flows out of the electrolysis system through a control valve, etc.; the liquid phase enters the cooler I under the action of gravity and enters under the drive of the circulation pump after heat exchange is completed. The electroly...

Embodiment 2

[0044] Example 2: The system implements natural circulation

[0045] The DCS cabinet 1 is started, and the electrolyte and hydrogen fluoride enter the gas-liquid separator 11 through the control valve at a certain ratio, and continue to feed the electrolyte until the liquid level of the electrolyte reaches one-third of the remote liquid level gauge in the anode gas-liquid separator 11. Stop feeding, start the circulation pump M01 after nitrogen purging of the electrolysis system, and start the DC power supply 2 to transmit power.

[0046] The anode gas and cathode gas engulf the electrolyte in the gas-liquid separator 11 respectively.

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Abstract

The invention discloses an electrochemical fluorination external circulation flexible electrolysis system which comprises a cathode copper bar, an anode copper bar, a cathode cable, an anode cable, anelectrolytic cell, a circulating pump, a cooler I, a gas-liquid separator, a gas condenser and a cooler II. A cell body of the electrolytic cell is internally provided with a left-end electrode cathode plate, a right-end electrode cathode plate and a plurality of electrolysis groups I. The electrolytic cell is formed by connecting n electrolysis groups I in parallel, each electrolysis group I isformed by connecting two electrolysis groups II in parallel, and each electrolysis group II is formed by connecting 2-20 electrolysis cabs in series. According to the invention, the electrolytic cellis highly integrated, the successfully developed bipolar series-parallel combined filter pressing type electrolytic cell is used, and heat generated by electrode reaction is completed through the cooler outside the electrolytic cell, so that the corrosion risk of an electrolyte channel is reduced, and the system risk caused by blockage of a certain cab is solved.

Description

technical field [0001] The invention relates to the technical field of organic electrochemical fluorination, in particular to an external circulation flexible electrolytic system for electrochemical fluorination. Background technique [0002] The electrochemical fluorination system of organic matter is divided into two types: internal circulation of electrolyte and external circulation. The internal circulation system of electrolyte is usually improved and optimized on the basis of Simmons fluorination electrolysis system, but the electrolyte is not circulated, and the heat generated by the electrode reaction passes through the inside of the electrolytic cell. The refrigerant in the heat exchange tube is taken out of the system, resulting in the problem of large volume and low efficiency of the fluorination electrolytic cell, which is difficult to fundamentally solve. [0003] The external circulation system of the electrolyte draws lessons from the electrolytic production o...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C25B3/28C25B9/75C25B15/02
CPCC25B15/02Y02P10/20
Inventor 吝子东冀延治李柄缘耿谦王斌朱姜涛曹红梅袁瑞玲
Owner PERIC SPECIAL GASES CO LTD
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