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Limestone-gypsum wet-process flue gas desulfurization additive

A technology of wet flue gas desulfurization and limestone, which is applied in separation methods, chemical instruments and methods, and separation of dispersed particles, can solve the problems of poor adaptability to coal sulfur content, substandard efficiency, high energy consumption and operating costs, etc. To achieve the effects of enhancing the desulfurization effect, increasing the reactivity, and shortening the contact time

Inactive Publication Date: 2015-09-30
NORTH CHINA ELECTRIC POWER UNIV (BAODING)
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the current operation of limestone-gypsum wet flue gas desulfurization devices in thermal power plants in my country generally has high energy consumption and operating costs, poor adaptability to coal sulfur content, serious blockage and fouling of subsequent equipment in the absorption tower, and equipment wear and tear. serious problems; one of the important reasons is that many power plants have been burning coal with sulfur content exceeding the design for a long time, resulting in the failure of the desulfurization system to operate normally
In order to meet the increasingly stringent environmental emission standards, many power plants are forced to increase the capacity of desulfurization devices, paying a very high economic price; what's more, the efficiency of desulfurization devices after capacity expansion and improvement is still not up to standard

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0017] In this example, wood chip pyrolysis and gasification tar washing liquid (water washing liquid obtained by pyrolysis gasification and tar washing with wood chips as raw material) is used as the wet desulfurization additive. The water content of the tar washing liquid is 98.5%, and the content is relatively Higher organic matter (based on water-soluble organic matter as 100%) mainly includes: phenol (34.2%), 4-methylphenol (21.2%), 2,6-dimethoxyphenol (13.1%), benzene (11.5%) %), toluene (3.2%), 2,4-dimethoxyphenol (0.6%), 2-methylphenol (0.5%), 2-methoxyphenol (0.3%), 2-methoxy- 4-ethylphenol (0.3%), 2-methoxy-4-allylphenol (0.3%); other water-soluble organic substances include ethylbenzene, styrene, p-xylene, m-xylene, Furfural, furfuryl alcohol, naphthalene, pyridine, phenanthrene, anthracene, quinoline, isoquinoline, nitrogen anthracene, 4-propyl biphenyl, etc., are very small.

[0018] Flue gas SO at the inlet of the desulfurization system 2 Concentration 2300mg / N...

Embodiment 2

[0020] In this example, straw pyrolysis gasification tar washing liquid (water washing liquid obtained by pyrolysis gasification and tar washing with straw as raw material) is used as the wet desulfurization additive. The water content of the tar washing liquid is 99.0%, and the content is relatively Higher organic matter (based on water-soluble organic matter as 100%) mainly includes: 30.5% (phenol), 16.2% (1,2-dimethoxyphenol), 15.9% (benzene), 14.8% (2,3, 6-trimethylphenol), 4.1% (toluene), 1.2% (4-methylphenol), 0.4% (2,6-dimethoxyphenol), 0.4% (2-methylphenol), 0.4% (2-methoxyphenol), 0.3% (2-methoxy-4-methylphenol), 0.3% (2,4-dimethoxyphenol), 0.2% (2-methoxy-4-propane phenol); other water-soluble organic compounds include ethylbenzene, styrene, p-xylene, m-xylene, furfural, furfuryl alcohol, naphthalene, pyridine, phenanthrene, anthracene, quinoline, isoquinoline, 3-methyl -1,2-cyclopentanedione, 4-propyl-biphenyl, etc., all in very small amounts.

[0021] Flue gas SO...

Embodiment 3

[0023] The limestone-gypsum wet-process flue gas desulfurization composite additive in this embodiment includes: 95% sawdust pyrolysis gasification tar washing liquid (wood chip pyrolysis gasification tar washing liquid in Example 1), 1% glutaric acid, 1% lemon Acid, 0.5% Sodium Humate, 0.5% Magnesium Sulfate, 0.5% Formamide, 1.5% Ferric Chloride.

[0024] Flue gas SO at the inlet of the desulfurization system 2 Concentration 2500mg / Nm 3 ; The liquid-gas ratio is 9.9, and the Ca / S ratio is 1.06. The concentration of the additive is 12.6g / L, and the desulfurization efficiency is more than 95% in 24 hours, which is 10% higher than that without the additive.

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Abstract

The invention belongs to the technical field of wet-process flue gas desulfurization and particularly relates to a limestone-gypsum wet-process flue gas desulfurization additive. The additive is composed of biomass pyrolyzed and gasified tar washing liquid or is a composite additive which is obtained by combining and mixing the tar washing liquid with any one or more of organic acids, organic acid salts, inorganic metal salts, an active agent and an oxidant in a traditional wet-process desulfurization additive. According to the additive provided by the invention, the solid-liquid mass transferring resistance in desulfurization slurry can be effectively reduced and the pH value of the slurry is stabilized, so that the desulfurization efficiency is improved; and furthermore, the composite additive containing the oxidant can accelerate the catalytic oxidation of a wet-process desulfurization product (calcium sulfite), so that the reaction speed of limestone in the slurry is accelerated and the quality of the wet-process desulfurization byproduct, namely gypsum, is improved.

Description

technical field [0001] The invention belongs to the technical field of limestone-gypsum wet flue gas desulfurization, in particular to a limestone-gypsum wet flue gas desulfurization additive. Background technique [0002] my country's energy consumption is still dominated by coal, and it is one of the countries that emit the most SO2 from coal combustion in the world. Therefore, how to control the emission of SO2 from coal combustion is one of the important tasks in my country at present. Limestone-gypsum wet flue gas desulfurization process is currently widely used in my country's coal-fired power plants and has many advantages. However, the current operation of limestone-gypsum wet flue gas desulfurization devices in thermal power plants in my country generally has high energy consumption and operating costs, poor adaptability to coal sulfur content, serious blockage and fouling of subsequent equipment in the absorption tower, and equipment wear and tear. One of the impor...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/80B01D53/50
Inventor 董长青陆强田伟强孙帅杨勇平
Owner NORTH CHINA ELECTRIC POWER UNIV (BAODING)
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