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Method for synergistically realizing efficient removal of PM2.5/SO3 in high-moisture flue gas and zero water consumption in wet desulphurization

A wet desulfurization and high-moisture technology, applied in the field of dust removal, can solve the problems of high operating cost and complex equipment, and achieve the effects of suppressing evaporation, simple process, and deep utilization

Inactive Publication Date: 2017-05-17
SOUTHEAST UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, the reduction of water consumption in the flue gas wet desulfurization system is mainly based on the treatment and reuse of discharged wastewater. There are problems such as complex equipment and high operating costs. How to reduce the gaseous water taken away by the desulfurized clean flue gas has not yet attracted attention.

Method used

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  • Method for synergistically realizing efficient removal of PM2.5/SO3 in high-moisture flue gas and zero water consumption in wet desulphurization

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Effect test

Embodiment 1

[0033] Such asfigure 1 As shown, a synergy of the present invention realizes PM in high-moisture flue gas 2.5 / SO 3 The method of high-efficiency desulfurization and wet desulfurization with zero water consumption mainly consists of low-temperature heat exchanger 1, electrostatic precipitator 2, low-low temperature heat exchanger 3, desulfurization tower 4, desulfurization liquid spray layer 5, and mist eliminator 6. The low-temperature heat exchanger 1 is set at the inlet flue of the electrostatic precipitator 2, and the low-low temperature heat exchanger 3 is set between the flue gas outlet of the electrostatic precipitator 2 and the flue gas inlet of the desulfurization tower 4; the cooling water of the low-temperature heat exchanger 1 comes from The cooling water in the low and low temperature heat exchanger 3 is discharged. The desulfurization tower 4 can adopt tower types such as spray tower, swirl plate tower, packed tower, turbulent ball tower, etc. The tower is provi...

Embodiment 2

[0036] The flue gas is produced by a fully automatic coal-fired boiler with a flue gas volume of 350Nm 3 / h, supplemented by an aerosol generator, SO 3 Add appropriate amount of coal-fired fly ash, SO 3 , water vapor, so that the dust concentration in the coal-fired flue gas is 3240mg / m 3 , in which the concentration of fine particles is 162mg / m 3 , SO 3 The concentration is 39mg / m 3 , the water vapor volume fraction is 14.35%. A low-temperature heat exchanger, an electric dust collector, a booster fan, a low-low temperature heat exchanger, and a limestone-gypsum flue gas desulfurization tower are arranged in sequence along the flue gas flow direction. The electrostatic precipitator has a three-electric field structure, the cathode is a conventional acupuncture electrode, and the distance between the plates is 0.30m. The heat exchange tube of the low temperature heat exchanger is made of finned tube and ND corrosion-resistant steel. The heat exchange tubes of the low an...

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Abstract

The invention provides a method for synergistically realizing efficient removal of PM2.5 / SO3 in high-moisture flue gas and zero water consumption in wet desulphurization. The method comprises the following steps: making the high-moisture flue gas pass through a low-temperature heat exchanger before entering an electric precipitator, so that the smoke temperature drops below an acid dew point, gaseous SO3 in the flue gas is condensed and adsorbed onto the surface of fine particulate matters, the PM2.5 removal of the electric precipitator is enhanced, and synergistic removal of SO3 is realized; after the flue gas leaves the electric precipitator, further cooling through a low-low-temperature heat exchanger to obtain high-relative-humidity flue gas, then reaching oversaturation in a desulfurization tower within a low-temperature desulfurization fluid contact process, and nucleating and condensing the oversaturated water vapor on the acid mist surface of the PM2.5 and the SO3, so that the particle size increases, and the removal of the acid mist of the PM2.5 and the SO3 in the desulfurization process is facilitated. At the same time, an oversaturated water vapor environment is established in the tower, so that a part of moisture is condensed from the flue gas to the desulfurization fluid, and zero water consumption in the wet desulphurization is realized synergistically. The method has the characteristics of high efficiency, energy saving, low investment and treatment cost, and the like.

Description

[0001] 1. Technical field [0002] The present invention designs a synergistic realization of PM in high-moisture flue gas 2.5 / SO 3 The invention relates to a method for efficient removal and wet desulfurization with zero water consumption, which belongs to the technical field of dust removal. [0003] 2. Background technology [0004] PM 2.5 It is one of the important factors leading to major environmental problems such as reduced atmospheric visibility, acid rain and haze weather. Controlling PM 2.5 Emissions are a key issue that urgently needs to be addressed. At present, more than 80% of the large and medium-sized coal-fired power plants in my country adopt the dust removal and desulfurization technology of electrostatic precipitator + wet flue gas desulfurization system. In recent years, people have done a lot of research and improvement on the electrostatic precipitator from the aspects of pole distance, pole matching method, dust cleaning method, air flow distributi...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D50/00B01D53/50B01D53/78
CPCB01D50/00B01D53/002B01D53/343B01D53/346B01D53/504B01D2258/0283B01D2259/124B01D2259/65
Inventor 杨林军吴昊潘丹萍张瑞
Owner SOUTHEAST UNIV
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