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Method for selecting model of electrostatic dust collector for deeply cooling flue gas

An electrostatic precipitator and electrostatic precipitator technology, applied in electrostatic separation and other directions, can solve the problems of inability to accurately select an electrostatic precipitator, waste, and small design, and achieve the effect of avoiding excessive dust discharge at the outlet

Active Publication Date: 2018-11-27
浙江菲达环保科技股份有限公司
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Problems solved by technology

[0009] The purpose of the present invention is to provide a type selection method of electrostatic precipitator for deep flue gas cooling, which can effectively solve the problem that the existing method cannot accurately select a suitable electrostatic precipitator, resulting in a design that is too small to meet the emission standards or a design that is too large to cause waste.

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  • Method for selecting model of electrostatic dust collector for deeply cooling flue gas
  • Method for selecting model of electrostatic dust collector for deeply cooling flue gas
  • Method for selecting model of electrostatic dust collector for deeply cooling flue gas

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Embodiment Construction

[0060] The embodiments of the present invention are described in detail below, and are intended to be used to explain the present invention, but should not be construed as a limitation of the present invention.

[0061] The following is a new unit of 2*1000MW in a power plant. According to the requirements of local environmental protection policies and the overall setting of the pollutant removal system after the power plant, the smoke and dust at the chimney outlet must be controlled at 5mg / Nm 3 and below, the smoke and dust at the outlet of the electrostatic precipitator shall be controlled at 15mg / Nm 3 and below (guaranteed if a power supply partition stops working). The main design coal and ash components of this project are shown in the table, and the flue gas parameters and performance requirements at the inlet of the electrostatic precipitator for deep cooling of flue gas are shown in the table below.

[0062]

[0063]

[0064] Main coal and ash composition table...

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Abstract

The invention discloses a method for selecting a model of an electrostatic dust collector for deeply cooling flue gas. The method comprises the following steps: calculating an ash sulfur ratio, takingan apparent migration velocity of a coal, calculating an effect-raising influence factor, calculating the effect-raising influence factor of the apparent migration velocity and calculating the effect-raising influence factor of the apparent migration velocity of a rotary electrode pair, according to a present coal model and design parameter requirements; calculating a dust-collecting area acquired by the electrostatic dust collector according to a calculation mode for the dust collecting efficiency of the electrostatic dust collector; selecting a suitable electrostatic dust collector model. The invention has the advantages that main influence factors and rule of the dust collecting efficiency of the electrostatic dust collector for deeply cooling flue gas are excavated; a specific calculation formula is provided for accurately calculating the dust collecting efficiency and specific model of the electrostatic dust collector for deeply cooling flue gas; the dust emission at an outlet exceeding standard caused by smaller model selection design and the waste problems of materials, sites, running power consumption and the like, caused by oversize model selection design can be avoided.

Description

technical field [0001] The invention relates to a type selection method of an electrostatic precipitator for deep cooling of flue gas. Background technique [0002] At present, with the full implementation of the "ultra-low emission" policy and standards for coal-fired power plants, the electric precipitator (also known as low-temperature electric precipitator) with deep cooling of flue gas has become the mainstream dust removal equipment for coal-fired power plants, but its dust removal Efficiency is affected by complex factors such as coal, ash composition, and flue gas conditions, and the factors are interrelated and interact. [0003] At the same time, there are Deutsch formula and Matts formula to calculate the dust removal efficiency of conventional electrostatic precipitators, both of which calculate the efficiency of electrostatic precipitator through the driving speed of coal types, but the specific calculation method of driving speed is not given. Some manufacture...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B03C3/34
CPCB03C3/34Y02E20/30
Inventor 赵海宝何毓忠郭滢胡露钧梁江马湖刚
Owner 浙江菲达环保科技股份有限公司
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