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Flue gas and multilayer network liquid film contact desulfurization, denitrification, dust removal and heat exchange method

A thermal method and flue gas technology, applied in the field of boilers, can solve the problem of inability to contact the droplet core, and achieve the effect of increasing the cross-sectional area

Inactive Publication Date: 2019-04-16
陈雅华
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0003] In view of the deficiencies in the above problems, the present invention provides a method for contacting desulfurization, denitrification, dust removal, and heat exchange between flue gas and multi-layer network liquid membrane, so as to maximize the expansion of desulfurization, denitrification, dust removal, heat exchange fluid and The surface area in contact with the flue gas solves the problem that the flue gas cannot contact the droplet nucleus in contact with the surface of the droplet

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  • Flue gas and multilayer network liquid film contact desulfurization, denitrification, dust removal and heat exchange method

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[0039] In order to make the object, technical solution and advantages of the present invention clearer, the present invention will be further described in detail below in conjunction with the accompanying drawings and examples, but the given examples are not intended to limit the present invention.

[0040] like figure 1 As shown, the technical solution of the embodiment of the present invention is: install desulfurization, denitrification, dust removal, heat exchange towers at the outlet of boiler flue gas, in the tower body, be provided with venturi section flue, and set in venturi section flue Spray desulfurization, denitrification, dust removal, and heat transfer atomized spray device to the flue gas to realize the first desulfurization, denitrification, dust removal, and heat exchange in the contact between the flue gas and the atomized spray liquid; the dust in the flue gas After contacting with the droplets, the gravity increases, and then it is directly sprayed to the ...

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Abstract

The invention provides a flue gas and multilayer network liquid film contact desulfurization, denitrification, dust removal and heat exchange method, and relates to the technical field of boilers, wherein the method comprises a venturi scrubber method of flue gas, a bubble reactor method, a spraying tower method, a multilayer network liquid membrane contact method, and a multilayer network defogging method. According to the present invention, with the method, the contact surface areas between the flue gas and the desulfurization liquid, between the flue gas and the denitrification liquid, between the flue gas and the dust removal liquid and between the flue gas and the heat exchange liquid can be maximized, and the problem that the flue gas contacts the surface of the mist droplet and cannot contact the core of the mist droplet can be solved.

Description

technical field [0001] The invention relates to the technical field of boilers, in particular to a method for desulfurization, denitrification, dust removal and heat exchange by contacting flue gas with a multi-layer mesh liquid film. Background technique [0002] At present, energy and the environment are two major problems facing human beings. The fact that coal is the main resource is in line with the fact that my country's resource endowment cannot be changed. Other energy sources are only auxiliary energy sources and cannot become the main force. Due to the smog caused by excessive sulfur, nitrate, dust and other pollutants in coal-fired flue gas emissions, coal-to-gas conversion is being promoted in various provinces and cities in various ways, including administrative means, resulting in excess coal production capacity, or in various ways. These methods include administrative measures to reduce coal energy. my country is a big country with more coal and less gas. The c...

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/79B01D53/78B01D53/75B01D53/60B01D53/96B01D47/12
CPCB01D47/12B01D53/343B01D53/60B01D53/75B01D53/78B01D53/79B01D53/96B01D2247/107B01D2258/0283Y02A50/20Y02A50/2351
Inventor 陈雅华阎海智陈明
Owner 陈雅华