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A method and device for synchronously removing sulfur and nitric acid to prepare sulfuric acid and nitric acid

A technology for removing sulfur and sulfuric acid, applied in chemical instruments and methods, nitric acid, separation methods, etc., can solve problems such as low resource utilization, large land occupation, and difficult separation of reaction products

Active Publication Date: 2021-04-09
KUNMING UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This process has high desulfurization and denitrification efficiency and simple structure, but it occupies a large area, the reaction products are difficult to separate, and the resource utilization rate is low.

Method used

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  • A method and device for synchronously removing sulfur and nitric acid to prepare sulfuric acid and nitric acid

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] Embodiment 1: at room temperature, utilize anion-exchange membrane, monovalent anion-exchange membrane and cation-exchange membrane to divide reaction chamber into cathode chamber, sulfuric acid chamber, nitric acid chamber, anode chamber, add DC voltage outside reaction chamber, will contain sulfur dioxide The gas with nitrogen oxides is passed into the cathode chamber, and the gas is oxidized and absorbed by the electro-Fenton reaction of the cathode chamber solution, and then discharged into the anode chamber for secondary absorption by the anode chamber solution, and the tail gas is directly discharged after further treatment (emitted after absorbing nitrogen); the anion NO produced by the reaction in the cathode chamber - , SO 4 2- Enter the sulfuric acid chamber through the anion exchange membrane, where NO - Then enter the nitric acid chamber through the monovalent anion exchange membrane to generate nitric acid, and the SO remaining in the sulfuric acid chambe...

Embodiment 2

[0042] Embodiment 2: at room temperature, utilize anion-exchange membrane, monovalent anion-exchange membrane and cation-exchange membrane to divide reaction chamber into cathode chamber, sulfuric acid chamber, nitric acid chamber, anode chamber, add DC voltage outside reaction chamber, will contain sulfur dioxide The gas with nitrogen oxides is passed into the cathode chamber, and the gas is oxidized and absorbed by the electro-Fenton reaction of the cathode chamber solution, and then discharged into the anode chamber for secondary absorption by the anode chamber solution, and the tail gas is directly discharged after further treatment ; The anion NO produced by the reaction in the cathode compartment - , SO 4 2- Enter the sulfuric acid chamber through the anion exchange membrane, where NO - Then enter the nitric acid chamber through the monovalent anion exchange membrane to generate nitric acid, and the SO remaining in the sulfuric acid chamber 4 2- produces sulfuric aci...

Embodiment 3

[0046] Embodiment 3: at room temperature, utilize anion exchange membrane, monovalent anion exchange membrane and cation exchange membrane to divide reaction chamber into cathode chamber, sulfuric acid chamber, nitric acid chamber, anode chamber, add DC voltage outside reaction chamber, will contain sulfur dioxide The gas with nitrogen oxides is passed into the cathode chamber, and the gas is oxidized and absorbed by the electro-Fenton reaction of the cathode chamber solution, and then discharged into the anode chamber for secondary absorption by the anode chamber solution, and the tail gas is directly discharged after further treatment ; The anion NO produced by the reaction in the cathode compartment - , SO 4 2- Enter the sulfuric acid chamber through the anion exchange membrane, where NO - Then enter the nitric acid chamber through the monovalent anion exchange membrane to generate nitric acid, and the SO remaining in the sulfuric acid chamber 4 2- produces sulfuric aci...

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Abstract

The invention discloses a method and device for synchronously removing sulfur and nitric acid to prepare sulfuric acid and nitric acid. DC voltage, the mixed gas containing sulfur dioxide and nitrogen oxides is passed into the cathode chamber, most of the gas is absorbed by the solution in the cathode chamber and oxidized under the electro-Fenton reaction of the solution, and the remaining part of the gas is discharged into the anode chamber to use the anode chamber solution for secondary absorption, and the final tail gas can be discharged directly; the anion NO produced by the reaction in the cathode chamber ‑ , SO 4 2‑ Enter the sulfuric acid chamber through the anion exchange membrane, where NO ‑ Then enter the nitric acid chamber through the monovalent anion exchange membrane to generate nitric acid, and the SO remaining in the sulfuric acid chamber 4 2‑ Generate sulfuric acid to achieve effective separation and enrichment of sulfuric acid and nitric acid; this method effectively purifies SO 2 and NO x The mixed gas realizes the utilization of energy resources and meets the development requirements of the green economy.

Description

technical field [0001] The invention relates to a method and a device for synchronously removing sulfur and nitric acid to prepare sulfuric acid and nitric acid, belonging to the technical field of separation and purification of toxic polluted gases and environmental protection engineering. Background technique [0002] With the increasing environmental pollution, the country has included air pollution control as a key prevention and control target, especially the discharge of sulfur oxides and nitrogen oxides is the top priority of air pollution control. If two sets of equipment are used to remove sulfur and nitrate, it will not only occupy a large area, but also require a large investment and troublesome management. The research and development of simultaneous removal of sulfur and nitrate has become the focus of flue gas pollution control in various countries. At the same time, sulfur dioxide and nitrogen oxides in the gas phase are also good resources. If they are conver...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D53/32B01D53/60C01B21/40C01B17/74
CPCB01D53/326B01D53/60C01B17/74C01B21/40Y02A50/20
Inventor 瞿广飞解若松马曦宁平李志顺成
Owner KUNMING UNIV OF SCI & TECH