Energy-saving dust removing and intelligent regulation synergetic white smoke removing system and energy-saving dust removing and intelligent regulation synergetic white smoke removing method

A technology for coal-fired power plants and temperature adjustment systems, which is applied in chemical instruments and methods, separation methods, and the use of liquid separation agents, etc. It can solve the problem of large temperature influence on the effect of white mist removal, high operation and maintenance costs, and the effect of white smoke removal. Poor and other problems, to achieve the effect of reducing water loss, reducing energy consumption, and good energy saving effect

Active Publication Date: 2017-11-07
ZHEJIANG UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The energy consumption of direct steam heating method is large, resulting in the loss of water, and at the same time, the smoke and SO x No corresponding deep removal
The saturated wet flue gas condensation method controls the phase change degree of the process through an external condensation source, and cooperates with a high-efficiency demister to effectively promote the condensation of fine particles and remove condensation. The method can reduce emissions, reduce water consumption, and consume less energy, but the corresponding The effect of white mist removal is greatly affected by the external environment temperature. When the ambient temperature is low, the effect of white mist removal is not good. To deeply solve the white fog, it is necessary to further heat the saturated wet flue gas
[0006] Chinese patent CN102980171A discloses a coal-fired boiler flue gas waste heat deep recovery utilization and flue gas condensation desulfurization and dust removal...

Method used

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  • Energy-saving dust removing and intelligent regulation synergetic white smoke removing system and energy-saving dust removing and intelligent regulation synergetic white smoke removing method
  • Energy-saving dust removing and intelligent regulation synergetic white smoke removing system and energy-saving dust removing and intelligent regulation synergetic white smoke removing method

Examples

Experimental program
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Effect test

Embodiment 1

[0035] refer to figure 1 , figure 2 , a coal-fired power plant energy-saving, dust removal and synergistic intelligent regulation and control whitening system, the whitening system includes a desulfurization tower 1, a flue gas phase change coalescer 4, a wet electrostatic multi-extractor 7, and a flue gas heating and whitening device 8 And an intelligent temperature adjustment system 31, the desulfurization tower 1 communicates with the flue gas phase-change coalescer 4 through the outlet flue 2 of the desulfurization tower, and the flue gas phase-change coalescer 4 passes through the outlet flue of the flue gas phase-change coalescer 6 communicates with the wet electrostatic multi-extractor 7, and the wet electrostatic multi-extractor 7 communicates with the flue gas heating and whitening device 8, and the flue gas heating and whitening device 8 communicates with the chimney 21, and the intelligent adjustment The temperature system 31 is connected with the external air mon...

Embodiment 2

[0042] refer to figure 1 , figure 2 , a coal-fired power plant energy-saving dust removal synergistic intelligent regulation and control whitening method, using the whitening system described in embodiment 1, comprising the following steps:

[0043] (1) The saturated wet flue gas processed by the desulfurization tower 1 enters the flue gas phase change condenser 4 through the outlet flue 2 of the desulfurization tower;

[0044] (2) The saturated wet flue gas passes through the flue gas phase change condenser 4, and the industrial water of the power plant is used as a cold source to reduce the temperature of the flue gas by 1 to 3°C. Due to the temperature drop, the saturated wet flue gas forms The condensate film absorbs and adsorbs part of SOx and fine particles in the flue gas, and the condensate enters the drain tank 9 through the condensate collection pipe 16; at the same time, the fine particles and droplets condense and grow near the condensation heat exchange tube 28,...

Embodiment 3

[0050] refer to figure 1 , figure 2 , for a boiler with a capacity of 220t / h, the theoretical flue gas volume at the outlet of desulfurization tower 1 is 300,000Nm 3 / h, the temperature of the saturated wet flue gas is 53°C, the saturated wet flue gas treated by the desulfurization tower 1 enters the flue gas phase change condenser 4 through the outlet flue 2 of the desulfurization tower; the saturated wet flue gas passes through the flue gas phase The variable condenser 4 uses the industrial water of the power plant as a cold source to reduce the temperature of the flue gas by 2°C. Due to the temperature drop of the saturated wet flue gas, the condensate film formed on the surface of the condensation heat exchange tube 28 absorbs and adsorbs part of SOx and Fine particles and condensate enter the drainage tank 9 through the condensate collection pipe 16; meanwhile, the fine particles and droplets condense and grow near the condensation heat exchange tube 28, and the wet ele...

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Abstract

The present invention relates to an energy-saving dust removing and intelligent regulation synergetic white smoke removing system and an energy-saving dust removing and intelligent regulation synergetic white smoke removing method. The energy-saving dust removing and intelligent regulation synergetic white smoke removing system comprises a desulfurization tower, a flue gas phase-change condensation device, a wet electrostatic multi-precipitator, a flue gas heating white smoke removing device and an intelligent temperature regulation system, wherein the desulfurization tower, the flue gas phase-change condensation device, the wet electrostatic multi-precipitator, the flue gas heating white smoke removing device and the intelligent temperature regulation system are sequentially communicated, the flue gas phase-change condensation device and the wet electrostatic multi-precipitator are respectively communicated to a water discharging box, the water discharging box is communicated to the desulfurization tower and a circulation water box, and the circulation water box is communicated to a wet electrostatic multi-precipitator spraying water pipe and a demister rinsing water pipe through a self-washing filter. According to the present invention, the system has advantages of high stability, low investment, low operation cost, and simpleness; the smoke discharging temperature is intelligently regulated, such that the flue gas discharging with characteristics of high reliability, low cost and no significant visible white smoke is achieved; the water in the system can be repeatedly utilized so as to reduce the waste of the water resource, and the boiler low-grade steam is used as the heat source so as to reduce the energy consumption by more than 10%; and with the system and the method, the advantages of low energy consumption and no white smoke emission are provided while the particulate matter removing efficiency is comprehensively improved by more than 20%, and the gas-stage SOx synergistic removal efficiency is improved by more than 10%.

Description

technical field [0001] The invention belongs to the technical field of coal-fired flue gas pollutant control, and specifically relates to a coal-fired power plant energy-saving, dust-removal and efficiency-enhancing collaborative intelligent regulation and whitening removal system and method. Background technique [0002] With the promulgation of the "Notice on Printing and Distributing the Action Plan for Upgrading and Transformation of Coal Power Energy Conservation and Emission Reduction (2014-2020)" (Fagai Energy [2014] No. The emission concentration of air pollutants from coal has basically reached the emission limit of gas turbines (that is, under the condition of a reference oxygen content of 6%, the emission concentrations of soot, sulfur dioxide, and nitrogen oxides are not higher than 10, 35, and 50 mg / m3, respectively). The main technical route to achieve the ultra-low emission requirements of soot and sulfur dioxide is the integrated wet desulfurization and dust ...

Claims

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Application Information

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IPC IPC(8): B01D53/00B01D53/26B01D53/14B01D47/05
CPCB01D47/05B01D53/002B01D53/14B01D53/26B01D2257/302Y02E20/30
Inventor 高翔郑成航张涌新周灿翁卫国竺新波王毅吴卫红岑可法
Owner ZHEJIANG UNIV
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