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Flue gas purification device and method combining photo-catalytic oxidization and double cyclic absorption

A photocatalytic oxidation and flue gas purification technology, applied in the field of flue gas purification, can solve the problems of less control, high energy consumption, waste of resources, etc.

Active Publication Date: 2016-05-04
NORTH CHINA ELECTRIC POWER UNIV (BAODING)
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

From the perspective of ammonia utilization, SCR denitrification is only an expedient measure: ammonia is an important basic raw material in industrial production, and the ammonia synthesis reaction (N 2 +3H 2 =2NH 3 ) is an extremely important chemical reaction with high energy consumption, and in the utilization of ammonia, tens of thousands of tons of ammonia are used for SCR denitrification every year, and the final NH 3 and converted to N 2 , which is equivalent to the secondary consumption of energy, and it is also a huge waste of resources
[0005] In recent years, the ultra-low emission technology represented by the optimized double-cycle desulfurization system has been applied in some power plants. 2 However, the system has less control over other pollutants in coal-fired flue gas

Method used

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  • Flue gas purification device and method combining photo-catalytic oxidization and double cyclic absorption
  • Flue gas purification device and method combining photo-catalytic oxidization and double cyclic absorption
  • Flue gas purification device and method combining photo-catalytic oxidization and double cyclic absorption

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0080] The first-stage absorption liquid: the mass concentration of potassium humate is 15wt%, and the pH is 12.

[0081] The second-stage absorption liquid: the mass concentration of KOH is 3wt%, and the pH is 10.

[0082] Liquid composite oxidant: H 2 o 2 and K 2 S 2 o 8 The mass concentration ratio is 30:10, and the pH is 4.5.

[0083] The reaction conditions of the flue gas purification system with photocatalytic oxidation combined with double-cycle absorption are shown in Table 2.

[0084] Table 2

[0085]

[0086]

[0087] The flue gas is purified according to the above conditions, and it is detected that the desulfurization efficiency reaches 99%, the denitrification efficiency reaches 86%, the mercury removal efficiency reaches 91%, and the decarbonization efficiency is 46%.

Embodiment 2

[0089] The first-stage absorption liquid: the mass concentration of potassium humate is 20wt%, and the pH is 13.

[0090] The second-stage absorption liquid: the mass concentration of KOH is 1wt%, and the pH is 9.

[0091] Liquid composite oxidant: H 2 o 2 and K 2 S 2 o 8 The mass concentration ratio is 30:5, and the pH is 5.

[0092] The reaction conditions of the flue gas purification system with photocatalytic oxidation combined with double-cycle absorption are shown in Table 3.

[0093] table 3

[0094]

[0095]

[0096] The flue gas is purified according to the above conditions, and it is detected that the desulfurization efficiency reaches 98%, the denitrification efficiency reaches 85%, the mercury removal efficiency reaches 90%, and the decarbonization efficiency is 45%.

Embodiment 3

[0098] The first-stage absorption liquid: the mass concentration of potassium humate is 18wt%, and the pH is 12.5.

[0099] The second-stage absorption liquid: the mass concentration of KOH is 2wt%, and the pH is 9.

[0100] Liquid composite oxidant: H 2 o 2 and K 2 S 2 o 8 The mass concentration ratio is 20:10, and the pH is 6.

[0101] The reaction conditions of the flue gas purification system with photocatalytic oxidation combined with double-cycle absorption are shown in Table 4.

[0102] Table 4

[0103]

[0104]

[0105] The flue gas is purified according to the above conditions, and it is detected that the desulfurization efficiency reaches 98%, the denitrification efficiency reaches 88%, the mercury removal efficiency reaches 92%, and the decarbonization efficiency is 46%.

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Abstract

The invention relates to a flue gas purification device and method combining photo-catalytic oxidization and double cyclic absorption. A first flue gas heat exchanger is arranged in a flue between an air pre-heater and an electrostatic dust remover and is used for conveying a compound oxidizing agent; after the compound oxidizing agent absorbs heat of flue gas to be atomized, the atomized compound oxidizing agent is catalyzed and activated in a photoassisted catalysis and activation reactor, various free radicals are generated and make contact with desulfurized and decarburized flue gas, in-situ oxidization reaction of various pollutants is performed, NO is converted into high-valence-state NOx, HgO is oxidized into Hg2+, NOx and Hg2+ enter a second-stage spraying tower along with the flue gas, supernatant of waste liquid of a first-stage spraying tower is mixed with second-stage absorbing liquid to form composite absorbing liquid, the composite absorbing liquid absorbs and removes NOx and Hg2+, and SO2 and CO2 are further removed; humic acid crystals are obtained through solid-phase drying and crystallizing of the two stages of spraying towers, reaction products including potassium sulphate, potassium carbonate, potassium nitrate, potassium nitrite and other agricultural common-use fertilizer are separated out through flue gas heating and drying of liquid phase, and resource utilization is facilitated.

Description

technical field [0001] The invention belongs to the technical field of flue gas purification, and in particular relates to a flue gas purification device and method with photocatalytic oxidation combined with double-cycle absorption. Background technique [0002] In recent years, due to the substantial increase in the number of power station boilers, industrial boilers and civil boilers, the emission of coal-fired flue gas pollutants has shown explosive growth, resulting in frequent occurrence of smog in my country, seriously endangering people's health and the ecological environment. Coal combustion flue gas pollutants mainly include particulate matter, SO 2 , NOx and trace heavy metals (Hg, As, etc.), and there are also a large number of greenhouse gases such as CO 2 and VOCs. [0003] Compared with industrial boilers and civil boilers, power plant boilers have adopted effective control measures for most of the above-mentioned pollutants. Among them, the mainstream desul...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/75B01D53/78B01D53/90B01D53/62B01D53/64B01D53/60
CPCB01D53/60B01D53/62B01D53/64B01D53/75B01D53/78B01D53/90B01D2251/106B01D2251/108B01D2251/60B01D2251/604B01D2251/80B01D2258/0283B01D2259/804Y02A50/20
Inventor 赵毅郝润龙白艳英
Owner NORTH CHINA ELECTRIC POWER UNIV (BAODING)
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