Supercharge Your Innovation With Domain-Expert AI Agents!

Method for producing acid through desulfuration, decyanation and concentration of coke oven gas

A coke oven gas, desulfurization and decyanation technology, which is applied to chemical instruments and methods, sulfur compounds, combustible gas purification, etc., can solve the problems of large investment, poor operation stability, and insufficient utilization of waste heat steam, etc., and achieve high desulfurization efficiency Effect

Inactive Publication Date: 2019-06-07
NINGBO KEXIN CHEM ENG TECH
View PDF4 Cites 2 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, these methods still have deficiencies. For example, high-pressure wet oxidation is used for the treatment of waste liquid in Tahis method. After high-temperature and high-pressure wet oxidation, the waste heat steam is not fully utilized, resulting in high power consumption, and the manufacture of the reaction tower is difficult, so it is difficult to popularize; AS method desulfurization and desulfurization Cyanide efficiency is not very high, desulfurization and decyanation, deamination, ammonia steaming and sulfur recovery must be connected together, local problems will affect the entire desulfurization and decyanation production, and the economic benefits are not good
[0009] 3. Large investment, poor operation stability and high energy consumption

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] A method for coke oven gas desulfurization, decyanation, concentration and acid production, comprising the steps of:

[0038](1). Send the coke oven gas that needs to be processed to the lower part of the desulfurization device (the desulfurization device is a desulfurization device in the prior art, which will not be repeated here), and contact with the poor absorption liquid sprayed from the top of the desulfurization device to absorb the gas The absorption temperature of hydrogen sulfide and hydrogen cyanide is 20-38°C (the absorption temperature can be controlled between 20-38°C, it is not necessary and unlikely to control a very precise temperature value), absorbing the lean liquid and The liquid-to-gas ratio of coke oven gas is 1:1.1, where liquid is measured by weight t (ton) and gas is measured by volume m 3 Calculated, the supplemented concentrated ammonia water enters the desulfurization device from the bottom of the desulfurization device, and the weight conc...

Embodiment 2

[0059] A method for coke oven gas desulfurization, decyanation, concentration and acid production, comprising the steps of:

[0060] (1). Send the coke oven gas that needs to be processed to the lower part of the desulfurization device (the desulfurization device is a desulfurization device in the prior art, which will not be repeated here), and contact with the poor absorption liquid sprayed from the top of the desulfurization device to absorb the gas The absorption temperature of hydrogen sulfide and hydrogen cyanide is 20-38°C (the absorption temperature can be controlled between 20-38°C, it is not necessary and unlikely to control a very precise temperature value), absorbing the lean liquid and The liquid-to-gas ratio of coke oven gas is 1:1, where liquid is measured by weight t (ton) and gas is measured by volume m 3 Calculated, the supplemented concentrated ammonia water enters the desulfurization device from the bottom of the desulfurization device, and the weight conce...

Embodiment 3

[0081] A method for coke oven gas desulfurization, decyanation, concentration and acid production, comprising the steps of:

[0082] (1). Send the coke oven gas that needs to be processed to the lower part of the desulfurization device (the desulfurization device is a desulfurization device in the prior art, which will not be repeated here), and contact with the poor absorption liquid sprayed from the top of the desulfurization device to absorb the gas The absorption temperature of hydrogen sulfide and hydrogen cyanide is 20-38°C (the absorption temperature can be controlled between 20-38°C, it is not necessary and unlikely to control a very precise temperature value), absorbing the lean liquid and The liquid-to-gas ratio of coke oven gas is 1:1.18, where liquid is measured by weight t (ton) and gas is measured by volume m 3 Calculated, the supplemented concentrated ammonia water enters the desulfurization device from the bottom of the desulfurization device, and the weight co...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

A method for producing acid through desulfuration, decyanation and concentration of coke oven gas. The method for producing the acid through desulfuration, decyanation and concentration of the coke oven gas comprises the following steps of (1) sending the coke oven gas which needs to be treated into the lower portion of a desulfuration device, and making the coke oven gas in contact with absorption barren liquor which is sprayed from the top of the desulfuration device; (2) adding an organic compound catalyst into absorption rich liquor which runs out of the desulfuration device, cooling a mixture after pressing the mixture, and then sending the mixture and compressed air into the bottom of an oxidation device; (3) sending the absorption barren liquor which runs out of the upper portion ofthe oxidation device to a subsequent acid production working procedure after concentrating the absorption barren liquor in a concentration device; and (4) sending concentrate into an acid productiondevice, and producing the concentrated sulfuric acid through an incineration acid production technology. According to the method for producing the acid through desulfuration, decyanation and concentration of the coke oven gas, the self-developed organic compound catalyst is used as a wet oxidation catalyst, generated desulfuration waste liquid does not contain sulfur, after evaporation concentration or membrane concentration is adopted, the traditional incineration acid production technology is used for producing the concentrated sulfuric acid, and regenerated tail gas and concentrated exhaustgas are all purified and recovered, so that the defects of the prior art are overcome, and the requirements of relative industries are met.

Description

technical field [0001] The invention belongs to the technical field of coke oven gas purification, and specifically relates to a process method for desulfurization, decyanation, concentration and acid production of coke oven gas. Background technique [0002] In the 1950s and 1960s, my country had the arsenic-alkali method, the ammonia water catalytic method, and the domestic Nanhua Institute, Sichuan Chemical Plant and Wusong Gas Plant jointly developed the improved ADA method in the early 1960s. However, these methods always have one or another disadvantage. For example, the arsenic-alkali method has been eliminated because the arsenic-containing lye is too toxic and harmful to humans. Ammonia catalysis method, the main catalyst is hydroquinone, which has poor activity, and the sulfur is too fine, which is easy to block the tower, so this method is not ideal. Later, other catalysts were added, such as the PDS developed by Northeast Normal University, and then gradually de...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
IPC IPC(8): C10K1/00C10K1/12C01B17/79C01B17/775B01J31/04
Inventor 范文松范文伟朱志雄
Owner NINGBO KEXIN CHEM ENG TECH
Features
  • R&D
  • Intellectual Property
  • Life Sciences
  • Materials
  • Tech Scout
Why Patsnap Eureka
  • Unparalleled Data Quality
  • Higher Quality Content
  • 60% Fewer Hallucinations
Social media
Patsnap Eureka Blog
Learn More