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Wet desulfurization tower with ridge type trays

A wet desulfurization and desulfurization tower technology, applied in separation methods, chemical instruments and methods, use of liquid separation agents, etc., can solve the problems of low desulfurization efficiency of desulfurization towers, enhance desulfurization and dust washing effects, and increase gas-liquid contact area. , the effect of increasing the gas-liquid contact area

Pending Publication Date: 2018-11-30
CHINA HUADIAN SCI & TECH INST
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] In order to solve the problem of low desulfurization efficiency of existing desulfurization towers, the present invention provides a wet desulfurization tower equipped with roof-type trays. Arrangement, the slurry falling on the orifice plate flows down the surface of the plate, and forms a liquid film due to the flow inertia when flowing through the opening of the tray, and forms a non-countercurrent cross flow with the upward flue gas, and the liquid film is broken into smaller liquid particles. Drops can greatly increase the gas-liquid contact area

Method used

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  • Wet desulfurization tower with ridge type trays
  • Wet desulfurization tower with ridge type trays
  • Wet desulfurization tower with ridge type trays

Examples

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example 1

[0050] In the wet desulfurization tower of a 600,000-kilowatt unit, the inner diameter of the desulfurization tower body 3 is 16m, and there are 4 spray layers 6 in total, and the height difference between two adjacent spray layers 6 is 2m. A layer of ridge tray 2 is set at 2m below the bottom spraying layer 6. There are 16 longitudinal units 11 in the ridge tray 2. The width W of the orifice plate 12 and the spacing X between the orifice plates are 1.414m. The angle α with the horizontal plane (the plane where the XY axes are located) is 45°. The opening 14 of the orifice plate 12 is elliptical, the minor axis a is 70 mm, the major axis b is 99 mm, and the horizontal projection is a circle with a diameter of 70 mm. The openings 14 are arranged in staggered rows, the transverse spacing c of the openings 14 is 140 mm, and the longitudinal spacing (that is, the spacing between rows) d of the openings 14 is 140 mm. Correspondingly, the opening ratio of the orifice plate 12 is 28...

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Abstract

The invention discloses a wet desulfurization tower with ridge type trays. The wet desulfurization tower comprises a desulfurization tower body (3) and ridge type trays (2) arranged in the desulfurization tower body (3); each ridge type tray (2) is of a waved plate type structure; each ridge type tray (2) comprises a plurality of longitudinal row units (11) which are arranged along the X-axis direction; each longitudinal row unit (11) is of a strip shape; each longitudinal row unit (11) comprises a plurality of hole plates (12) which are connected in sequence; every two adjacent longitudinal row units (11) form a longitudinal row unit pair (16) with a ridge structure; and a gap exists between every two adjacent longitudinal row unit pairs (16). The wet desulfurization tower with the ridgetype trays comprises the ridge type trays, slurry falling on the pore plates flows down along the surface of a flat plate, and a non-countercurrent cross flow is formed by the slurry and ascending flue gas. A liquid film is broken into small liquid drops, and the gas-liquid contact area can be greatly increased, so that the desulfurization and dust-washing effects of the slurry can be remarkably enhanced.

Description

technical field [0001] The invention relates to the field of environmental protection and energy-saving and emission-reduction equipment for coal-fired power plants, in particular to a wet desulfurization tower equipped with roof-mounted trays. Background technique [0002] Large and medium-sized coal-fired power plants in my country generally use limestone-gypsum wet desulfurization system for desulfurization. The spray slurry and incoming flue gas flow in reverse in the desulfurization absorption tower. 2 Absorbed by slurry droplets to achieve flue gas SO 2 Emissions up to standard. my country's air pollutant SO for coal-fired power plants 2 The emission standard of the desulfurization system is very strict. In order to ensure the desulfurization effect, power plants generally adopt the measures of increasing the liquid-gas ratio of a single tower or adding a second desulfurization tower. Therefore, it is necessary to develop high-efficiency, low-energy desulfurization ...

Claims

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Application Information

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IPC IPC(8): B01D53/78B01D53/50B01D47/14B01D47/06
CPCB01D47/06B01D47/14B01D53/504B01D53/78B01D2251/604B01D2251/404
Inventor 柳冠青李宗慧段翠佳曹文广石战胜马治安邹重恩董方
Owner CHINA HUADIAN SCI & TECH INST
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