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Method for simultaneous desulfurization and denitrification of dry flue gas

A technology for desulfurization and denitrification and flue gas, applied in separation methods, chemical instruments and methods, gas treatment, etc., can solve problems such as high operating costs, increased resistance of desulfurization and denitrification equipment, and difficulty in removing NO

Active Publication Date: 2021-05-18
KUNMING UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In fact, two steps are used for wet desulfurization and denitrification. Not only the process is long, but also the wet equipment occupies a large area and the operation steps are cumbersome. In addition, O 3 The generator has high operating cost, O 3 Disadvantages such as low utilization rate and secondary pollution (nitrate wastewater)
The Chinese utility model patents with the announcement numbers CN2712446Y and CN2746971Y respectively proposed a "flue gas desulfurization and denitrification device" and "desulfurization and denitrification integrated flue gas purification tower", but the desulfurization and denitrification equipment are all large packing devices, and Directly using ammonia solution to absorb nitrogen oxides in flue gas not only greatly increases the resistance of the entire desulfurization and denitrification equipment, but also cannot effectively remove nitrogen oxides in flue gas
The reason is NO x NO accounts for more than 90% in the medium, and NO is insoluble in water, so it is difficult to remove NO by simple washing method

Method used

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  • Method for simultaneous desulfurization and denitrification of dry flue gas

Examples

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Effect test

Embodiment 1

[0046] Embodiment 1: as figure 1 As shown, the method of simultaneous desulfurization and denitrification of flue gas in this dry process is as follows:

[0047] A coke oven in an iron and steel enterprise, the exhaust gas contains nitrogen oxides, sulfur dioxide, and dust, of which the average concentration of NO is 320mg / Nm³, NO 2 The average concentration is about 30mg / Nm³, NO x The concentration can reach 1000mg / Nm instantaneously 3 ;SO 2 The average concentration of about 110mg / Nm 3 ;The dust content of flue gas is about 1000mg / Nm 3 ; The flue gas temperature is 220°C.

[0048] (1) Flue gas pretreatment: the flue gas 1 is collected by the flue gas header 3 lined with Teflon, and the Teflon coating can work for a long time in a high temperature environment of 250 ° C; Soot content about 5mg / Nm 3 , the removal rate of dust with a particle size ≥ 25 μm is 99.9%;

[0049] (2) ClO 2 Preparation of gas: ClO 2 Generating device 5 adopts a packing type circulating spray...

Embodiment 2

[0058] Embodiment 2: as figure 2 As shown, the method of simultaneous desulfurization and denitrification of flue gas in this dry process is as follows:

[0059] The sintering flue gas of an iron and steel enterprise contains nitrogen oxides, sulfur dioxide, HCl, and dust in the flue gas. The average concentration of NO is 300mg / Nm³, and the NO 2 The average concentration is about 20mg / Nm³; SO 2 The average concentration of about 300mg / Nm 3 ; HCl concentration about 50mg / Nm 3 ;The dust content of flue gas is about 4000mg / Nm 3 , the flue gas temperature is 180 ℃;

[0060] (1) Flue gas pretreatment: the flue gas 1 is collected by the flue gas header 3 lined with Teflon, and the Teflon coating can work for a long time in a high temperature environment of 250°C; the dust is firstly removed by the bag filter 2, and the dust is removed After the dust content is about 10mg / Nm 3, the removal rate of dust with a particle size ≥ 25 μm is 99.0%;

[0061] (2) ClO 2 Preparation of...

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Abstract

The invention discloses a method for simultaneous desulfurization and denitrification of dry flue gas. The method comprises the following steps: collecting flue gas to be treated by adopting a header, introducing ClO2 gas into a pipeline containing the flue gas to be treated or introducing the ClO2 gas and the flue gas to be treated into a mixing tank through the pipeline, and oxidizing NO and SO2 into NO2 and SO3 by ClO2 in a flue or the mixing tank; conveying a powdery deacidification agent into the flue containing treated flue gas, thermally activating the deacidification agent through the high temperature of the flue gas, enabling the deacidification agent to make full contact with the flue gas for a chemical reaction so as to absorb and purify SOx and NOx in the flue gas; feeding the treated flue gas into a dust remover, removing dust generated in the reaction, then discharging the flue gas, and completing desulfurization and denitrification of the flue gas; the method is simple in technological process, low in energy consumption, low in one-time investment, low in safety risk and free of ammonia leakage risk, heating equipment is not needed in the technological process, and the risks of fire disasters, explosions and the like are low; the method is suitable for market and industrial popularization and application.

Description

technical field [0001] The invention belongs to the technical field of waste gas treatment, and in particular relates to a method for simultaneous desulfurization and denitrification of dry flue gas. Background technique [0002] With the continuous development and progress of the economy and society, the environmental pollution caused by the energy consumption structure is becoming more and more serious. Among them, the greenhouse effect, acid rain, and atmospheric smoke and dust pollution have caused serious harm to people's production and life. In China, SO released from coal combustion 2 Accounting for 85% of total emissions, NO x Accounting for 60% of the total emissions, the acid rain caused by the two accounts for 82% of the total acid rain. According to relevant studies, the economic loss caused by acid rain pollution in my country is about 500 billion yuan per year. [0003] Common flue gas desulfurization technologies include wet method (lime / limestone method, d...

Claims

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Application Information

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IPC IPC(8): B01D53/60B01D53/75B01D53/76B01D53/83B01D53/54B01D53/78
CPCB01D53/60B01D53/75B01D53/76B01D53/83B01D53/54B01D53/78B01D2251/108B01D2251/304B01D2251/604B01D2257/408B01D2258/0283Y02A50/20
Inventor 王学谦李翔王郎郎
Owner KUNMING UNIV OF SCI & TECH
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