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Diaphragm electrolysis method for preparing carbon monoxide and pypocholoride in micro-gap electrolytic tank

A technology of hypochlorite and carbon monoxide, applied in the direction of electrolysis components, electrolysis process, etc., can solve the problems of low cathode reaction current density, accelerated hydrogen evolution reaction speed, no economic feasibility, etc., and achieves easy start and stop and low production cost. , The effect of the equipment occupying a large area

Pending Publication Date: 2022-05-27
KUNMING UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

This method has a history of more than 100 years of research, and it has not yet been applied industrially. The main problems are: first, carbon dioxide is a non-polar molecule, and its solubility in aqueous solution is very small, only 0.033mol / L in the standard state. The current density of the reaction is too low; second, when electrolyzing carbon dioxide to produce carbon monoxide in an aqueous solution, in order to improve the conductivity of the electrolyte, it is necessary to add an inorganic supporting electrolyte to the electrolyte, thus inevitably bringing some inorganic impurities into the electrolysis In the liquid, some of the impurities are electrodeposited on the surface of the cathode to form surface active sites with low hydrogen evolution overpotential, which leads to the acceleration of the hydrogen evolution reaction, and also reduces the electrocatalytic activity of the electrode material for the carbon dioxide electroreduction reaction; When electrolyzing carbon dioxide in aqueous solution to produce carbon monoxide, due to the specific electrode / electrolyte interface environment, a small amount of carbon dioxide undergoes deep reduction to form amorphous carbon, which adheres to the surface of the cathode, resulting in electrode poisoning [Y.Hori. Electrochimica Acta 50 (2005) 5354- 5369], the current efficiency of generating carbon monoxide is rapidly reduced to zero; the 4th, the reaction of carbon monoxide produced by electrolysis of carbon dioxide, its cathode reaction product is carbon monoxide, and the anode reaction product is oxygen, because carbon monoxide can be made by coal gas method, oxygen can be made by air separation method Therefore, the production cost of the latter two methods is very low, resulting in the high production cost of electrolyzing carbon dioxide to produce carbon monoxide, which is not economically feasible.

Method used

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  • Diaphragm electrolysis method for preparing carbon monoxide and pypocholoride in micro-gap electrolytic tank

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Embodiment 1

[0041] The diaphragm electrolysis method for preparing carbon monoxide and hypochlorite in a micro-gap electrolytic cell, the specific operation steps are as follows:

[0042] Step 1: The electrolytic cell is divided into a cathode compartment, an intermediate compartment and an anode compartment by a bipolar membrane and a perfluorosulfonic acid type cation exchange membrane. A porous Au electrode is placed in the cathode compartment as a cathode, and a porous iridium oxide coating is placed in the anode compartment. A layered titanium electrode was used as the anode, and water was added to the intermediate chamber. The anion permeation layer of the bipolar membrane is an imidazole polyether ether ketone anion permeation layer with a thickness of 200 microns, and the cation permeation layer is a perfluorosulfonic acid type cation permeation layer with a thickness of 150 microns. The interfacial region of the layer introduces titanium oxide / nickel oxide nanoparticles as a wate...

Embodiment 2

[0047] The diaphragm electrolysis method for preparing carbon monoxide and hypochlorite in a micro-gap electrolytic cell, the specific operation steps are as follows:

[0048] Step 1: The electrolytic cell is divided into a cathode compartment, an intermediate compartment and an anode compartment by a bipolar membrane and a sulfonated polyethylene cation exchange membrane. A porous Ag electrode is placed in the cathode compartment as a cathode, and a porous IrO is placed in the anode compartment. 2 ·Ta 2 O 5 The coated titanium electrode acts as the anode, and water is added to the intermediate chamber. The anion permeation layer of the bipolar membrane is a sub-permeation layer of a diamine-containing styrene / vinylbenzyl chloride copolymer anion permeation layer with a thickness of 180 microns, and the cation permeation layer is a sulfonated polyethylene cation permeation layer with a thickness of 180 microns. 250 microns, and polyvinyl acid / polyvinyl pyridinium complex was...

Embodiment 3

[0053] The diaphragm electrolysis method for preparing carbon monoxide and hypochlorite in a micro-gap electrolytic cell, the specific operation steps are as follows:

[0054] Step 1. The electrolytic cell is divided into a cathode compartment, an intermediate compartment and an anode compartment by a bipolar membrane and a sulfonated polystyrene cation exchange membrane. A porous Zn electrode is placed in the cathode compartment as a cathode, and a porous glassy carbon electrode is placed in the anode compartment. As an anode, water is added to the intermediate chamber. The anion permeation layer of the bipolar membrane is a quaternized polyvinyl chloride anion permeation layer with a thickness of 210 microns, and the cation permeation layer is a sulfonated polyvinylidene fluoride cation permeation layer with a thickness of 150 microns. The interfacial region of the permeable layer introduced sulfonated polyetheretherketone as a water dissociation catalyst.

[0055] Step 2, ...

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Abstract

The invention relates to a diaphragm electrolysis method for preparing carbon monoxide and pypocholoride in a micro-gap electrolytic tank, which comprises the following steps: fully reducing the inter-electrode distance of the electrolytic tank by adopting a snakelike gas-liquid circulation channel and a porous electrode; the electrolytic tank is divided into a cathode chamber, a middle chamber and an anode chamber by a bipolar membrane and a cation exchange membrane to form a three-compartment electrolytic tank; the cathode chamber is an organic composite electrolyte in which a large amount of carbon dioxide gas flows, the electrolyte in the middle chamber is a metal chloride aqueous solution, and the electrolyte in the anode chamber is also a metal chloride aqueous solution. In the electrolytic reaction process, carbon monoxide is generated on the cathode chamber, chlorine is generated on the anode, and hydroxide is continuously generated in the middle chamber; chlorine is separated through the gas-liquid separation tank and then guided into the middle chamber, the chlorine reacts with metal hydroxide generated in the middle chamber to generate pypocholoride, and the pypocholoride belongs to a main component of the 84 disinfectant. The method has the advantages of short process flow, simple operation method, low production cost, small occupied area of equipment, easiness in starting and stopping and the like.

Description

Background technique [0001] Carbon monoxide is the main component of chemical synthesis gas and an important raw material for the synthesis of a series of basic organic chemical products and intermediates; hypochlorite is an important disinfectant and bleaching agent, mainly used in bleaching, industrial wastewater treatment, papermaking, Textiles, pharmaceuticals, fine chemicals, sanitation and disinfection and many other fields. At present, the industry mainly uses coal and natural gas to synthesize carbon monoxide. This method uses natural resources coal, natural gas, etc. as raw materials to synthesize carbon monoxide through processes such as gasification and carbonylation, and then separate and purify carbon monoxide according to the purity requirements of production. , to obtain various contents of carbon monoxide; hypochlorite is mainly synthesized by calcium hydroxide and chlorine as raw materials in industry: 2Ca(OH) 2 +2Cl 2 =Ca(ClO) 2 +CaCl 2 +2H 2 O, the req...

Claims

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Application Information

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IPC IPC(8): C25B1/23C25B1/26C25B1/50
CPCC25B1/23C25B1/26C25B1/50Y02E60/36
Inventor 刘建雄张金忠施锦沈风霞宋文康华雅鑫吴帅
Owner KUNMING UNIV OF SCI & TECH
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