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Wet desulfurization system and wet desulfurization method

A wet desulfurization and desulfurization tower technology, applied in the field of desulfurization, can solve the problems of limited flue gas temperature rise, difficult zero discharge of desulfurization wastewater, and the ability to eliminate white smoke needs to be improved, so as to increase the degree of unsaturation and achieve ultra-clean The effect of emissions

Active Publication Date: 2021-11-19
SINOPEC ENG GRP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] The flue gas produced by combustion of boilers, incinerators, and catalytic cracking units needs to be desulfurized before it can be discharged into the air. Desulfurization generally adopts wet desulfurization. After desulfurization, the temperature of the flue gas decreases, and the water vapor in the flue gas is in a supersaturated state. When the flue gas is discharged into the air, it will produce a large number of small water droplets to form white smoke when it is cold, which not only wastes a lot of heat energy and water resources, but also causes strong visual pollution; and, the small liquid droplets condensed by water vapor and the flue gas The residual aerosols and fine particles in the air can easily form smog, which seriously affects the visibility of the surrounding environment and the physical and mental health of residents.
[0003] In order to solve the above problems, condensation, reheating, mixing and mutual combination are generally used to solve the white smoke problem of desulfurization flue gas; but the above-mentioned technology needs to consider the problem of low-temperature cold source and high-temperature heat source, and the temperature rise of the flue gas is limited. The ability to eliminate white smoke needs to be improved; at the same time, the desulfurization wastewater generated by wet flue gas desulfurization is generally treated through neutralization, sedimentation, oxidation, clarification and other steps in conventional processes, but it is difficult to achieve zero discharge of desulfurization wastewater after treatment

Method used

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Examples

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Embodiment 1

[0040] like figure 1 and figure 2 As shown, the embodiment of the present application provides a wet desulfurization system, including: a waste liquid evaporator 1, a desulfurization tower 2, a settling tank 4 and a negative pressure evaporator 3;

[0041] The interior of the desulfurization tower 2 includes an outlet section C, a washing and demisting section B, and a cooling and absorbing section A from top to bottom, and a demister assembly is arranged inside the washing and demisting section B, wherein the demist assembly includes a mist catcher 21 And the mist eliminator 22, the upper space of the cooling absorption section A is provided with a first injection part 24;

[0042] The flue gas inlet of the waste liquid evaporator 1 is used to feed the flue gas to be treated, and the flue gas outlet of the waste liquid evaporator 1 is connected with the cooling absorption section A of the desulfurization tower 2; Part 11; the higher temperature flue gas enters the waste li...

Embodiment 2

[0064] like image 3 and Figure 4 As shown, the embodiment of the present application provides a wet desulfurization system, in addition to the structural features in Embodiment 1, it also includes a second heat exchanger 25, and the washing and demisting section B is provided with a liquid collection port 23, and the liquid collection Port 23 communicates with the first medium inlet of the second heat exchanger 25, and the first medium outlet of the second heat exchanger 25 communicates with the demister 22; The second medium outlet of the second heat exchanger 25 communicates with the inlet of the first heat exchanger 31 .

[0065] The second heat exchanger 25 adopts a heat exchange type with a wide flow channel, and can be a wide flow channel heat exchanger such as a tube type, a plate type, a heat pipe type, and a shell-and-tube type. The material of the heat exchanger can be selected from 314L, 2205 stainless steel, fluoroplastic, Corrosion-resistant materials such as ...

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Abstract

The application provides a wet desulfurization system and a wet desulfurization method, which relate to the technical field of desulfurization, wherein the wet desulfurization system includes a waste liquid evaporator, a desulfurization tower, a negative pressure evaporator and a settling tank; The higher temperature flue gas is used to treat desulfurization wastewater, and the temperature of the circulating slurry is reduced by means of negative pressure evaporation and cooling. At the same time, the unsaturation of the purified flue gas is greatly increased by means of air mixing, thereby achieving the deep elimination of white smoke and zero discharge of desulfurization wastewater. The purpose, and use the principle of condensation phase change to further reduce the content of fine particles in the flue gas, to achieve ultra-clean emission of flue gas.

Description

technical field [0001] The present application relates to the technical field of desulfurization, in particular to a wet desulfurization system and a wet desulfurization method. Background technique [0002] The flue gas produced by combustion of boilers, incinerators, and catalytic cracking units needs to be desulfurized before it can be discharged into the air. Desulfurization generally adopts wet desulfurization. After desulfurization, the temperature of the flue gas decreases, and the water vapor in the flue gas is in a supersaturated state. When the flue gas is discharged into the air, it will produce a large number of small water droplets to form white smoke when it is cold, which not only wastes a lot of heat energy and water resources, but also causes strong visual pollution; and, the small liquid droplets condensed by water vapor and the flue gas The residual aerosols and fine particles in the air can easily form smog, seriously affecting the visibility of the surro...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D53/80B01D53/48B01D47/06C02F1/04
CPCB01D47/06B01D53/48B01D53/80B01D2258/0283C02F1/04
Inventor 李玖重孙志钦李国智高晓红高跃成郜建松周天宇张婧帆
Owner SINOPEC ENG GRP CO LTD
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