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Exhaust gas treatment system and method

A waste gas treatment device and waste gas technology, which are applied in gas treatment, combustion methods, separation methods, etc., can solve the problems of insufficient performance, increased water consumption, energy loss and large space occupation.

Inactive Publication Date: 2015-07-08
MITSUBISHI HITACHIPOWER SYST LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] However, although the desulfurization device of the wet system has excellent desulfurization performance, it has a problem of increasing water consumption.
[0009] With regard to desulfurization devices of a dry type other than a wet type, it has been proposed, for example, to remove SO using activated coke 2 method, but there are problems of insufficient performance or energy loss and large utility

Method used

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  • Exhaust gas treatment system and method
  • Exhaust gas treatment system and method
  • Exhaust gas treatment system and method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] figure 1 It is a schematic diagram of the waste gas processing apparatus concerning Example 1. Such as figure 1 As shown, the exhaust gas treatment device 10A involved in this embodiment has: a denitrification device 14, which is arranged on the flue 13 that discharges the exhaust gas 12 from the boiler 11, and removes nitrogen oxides in the exhaust gas 12; 2 / SO 3 The reforming catalyst part 15 is provided in the flue on the downstream side of the denitrification device 14, and has SO in the denitrated exhaust gas 12A. 2 (sulfur dioxide) into SO 3 (sulfur trioxide) conversion catalyst; heat exchanger 16 is arranged on SO 2 / SO 3 The flue 13 on the downstream side of the conversion catalyst part 15, and exchanges heat between the exhaust gas 12B and the air 20 so that the temperature of the exhaust gas 12B passing through the catalyst becomes below the acid dew point; and the dust collector 17, in the heat exchanger 16, makes The soot 31 adheres to the surrounding...

Embodiment 2

[0050] Next, an exhaust gas treatment device according to Example 2 of the present invention will be described. In addition, the same code|symbol is attached|subjected to the same component as Example 1, and repeated description is abbreviate|omitted.

[0051] figure 2 is a schematic diagram of an exhaust gas treatment system according to Example 2 of the present invention.

[0052] Such as figure 2 As shown, the exhaust gas treatment system 10B of this embodiment is in SO 2 / SO 3 A powder supply mechanism 42 for introducing powdered limestone 41 is provided in the flue 13 between the reforming catalyst unit 15 and the heat exchanger 16 .

[0053] When coal is used as the fuel F of the boiler 11, the amount of coal dust in the exhaust gas 12 is very large, so there is no problem. However, when using, for example, heavy oil or coal with less ash content as the fuel F, depending on the type of the heavy oil, sometimes The amount of soot in the exhaust gas 12 is relatively...

Embodiment 3

[0059] Next, an exhaust gas treatment device according to Embodiment 3 of the present invention will be described. In addition, the same code|symbol is attached|subjected to the same component as Example 1, and repeated description is abbreviate|omitted.

[0060] image 3 is a schematic diagram of an exhaust gas treatment system according to Example 3 of the present invention.

[0061] Such as image 3 As shown, in the exhaust gas treatment system 10C of this embodiment, the denitrification device 14 and the SO 2 / SO 3 An air preheater 19 is also interposed between the reforming catalyst units 15 .

[0062] In this air preheater 19, the high temperature exhaust gas 12A 1 The preheated air 20A is introduced into the boiler 11 after exchanging heat with the air 20 .

[0063] In this embodiment, the high-temperature exhaust gas 12A is passed through the air preheater 19 1 Become 150°C low-temperature exhaust gas 12A 2 , thus being imported into SO 2 / SO 3 The exhaust ga...

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Abstract

This exhaust gas treatment system has: a denitrification device (14) that is provided in a flue (13) through which an exhaust gas (12) from a boiler (11) is discharged and that removes nitrogen oxides from the exhaust gas (12); an SO2·SO3 conversion catalyst unit (15) that is provided in the flue (13) on the wake side of the denitrification device (14) and that has a conversion catalyst which converts SO2 (sulfur dioxide) in the denitrified exhaust gas (12A) into SO3 (sulfur trioxide); a heat exchanger (16) that is provided in the flue (13) on the wake side of the SO2·SO3 conversion catalyst unit (15) and that conducts heat exchange between the exhaust gas (12B), which has passed through the catalyst, and air (20) to lower the temperature of the exhaust gas (12B) to a sulfuric acid dew point or lower and that makes dust and soot adhere to the surfaces of sulfuric acid droplets contained in the exhaust gas, the temperature of which has been lowered to a sulfuric acid dew point or lower in the heat exchanger (16); and a dust collector (17) that collets not only the dust- and soot-covered sulfuric acid but also dust and soot contained in the exhaust gas (12C). In the exhaust gas treatment system, the desulfurization of an exhaust gas is attained by: catalytically converting SO2 contained in an exhaust gas into SO3; subjecting the SO3-containing exhaust gas to heat exchange with air in a heat exchanger to lower the temperature of the exhaust gas to a sulfuric acid dew point or lower; making dust and soot adhere to the surfaces of sulfuric acid droplets contained in the exhaust gas; and collecting the dust- and soot-covered sulfuric acid together with dust and soot by a dust collector.

Description

technical field [0001] The invention relates to a waste gas treatment device and method. Background technique [0002] In thermal power plants and the like, nitrogen oxides (NOx), sulfur oxides (SOx), coal dust, and the like generated with the combustion of fossil fuels are contained in exhaust smoke (exhaust gas). These NOx, SOx, coal dust, etc. cause air pollution, so in thermal power plants with coal-fired boilers, etc., install exhaust gas treatment equipment with denitrification equipment for removing NOx and exhaust gas desulfurization equipment for removing SOx . [0003] Here, the wet limestone-gypsum method is dominant in the flue gas desulfurization device, in which the limestone slurry is sprayed from the nozzle to make it contact with the waste gas gas-liquid with high reliability, and is often used as a A spray method of spraying limestone slurry in a tower is adopted (Patent Document 1). [0004] Previous technical literature [0005] patent documents [0...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/86B01D53/34B01D53/50
CPCB01D2251/606F23J2215/20B01D2251/404B01D2257/404F23J2219/70B01D53/8609B01D2258/0283F23J15/06Y02A50/20Y02E20/30
Inventor 牛久哲长安立人香川晴治
Owner MITSUBISHI HITACHIPOWER SYST LTD