JPS58133846A - Treatment of waste gas - Google Patents

Treatment of waste gas

Info

Publication number
JPS58133846A
JPS58133846A JP57015891A JP1589182A JPS58133846A JP S58133846 A JPS58133846 A JP S58133846A JP 57015891 A JP57015891 A JP 57015891A JP 1589182 A JP1589182 A JP 1589182A JP S58133846 A JPS58133846 A JP S58133846A
Authority
JP
Japan
Prior art keywords
dust
waste gas
electrodes
precipitator
efficiency
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP57015891A
Other languages
Japanese (ja)
Inventor
Tatsuya Yoshioka
達也 吉岡
Shigeyuki Noso
能祖 茂幸
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Electric Power Development Co Ltd
Sumitomo Heavy Industries Ltd
Original Assignee
Electric Power Development Co Ltd
Sumitomo Heavy Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Electric Power Development Co Ltd, Sumitomo Heavy Industries Ltd filed Critical Electric Power Development Co Ltd
Priority to JP57015891A priority Critical patent/JPS58133846A/en
Publication of JPS58133846A publication Critical patent/JPS58133846A/en
Pending legal-status Critical Current

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  • Electrostatic Separation (AREA)

Abstract

PURPOSE:To improve dust collecting efficiency as well as to prevent white smoking from a chimney and to improve a diffusion effect in the stage of treating waste gas with a wet type desulfurizer through an electrical dust precipitator by conducting the waste gas from the desulfurizer into the hollow dust precipitating electrodes in the dust precipitator. CONSTITUTION:For example, the waste gas of a coal boiler is cooled with an air heater 1 and is introduced into an electrical dust precipitator 2 consist of hollow dust precipitating electrodes 3 of pipe or square shape. However, in this state, the dust of high resistant sticks on the electrodes 3, and causes back corona phenomena, by which dust precipitating efficiency is decreased. Thereupon, the waste gas passes through the precipitator 2 and since the waste gas flowing out from a wet type desulfurizer 4 is low in temp., the waste gas is conducted to the electrodes 3 to cool the electrodes 3, whereby the temp. of the high resistance dust stuck thereon is reduced and the electric resistance value is decreased. Thus, back corona phenomena are prevented and dust precipitating efficiency is improved. On the other hand, the waste gas past the electrodes 3 is heated, whereby the white smoking of the gas released from a chimney 5 is prevented and a diffusion efficiency is improved.

Description

【発明の詳細な説明】 本発明は、例えば石炭ボイラ排ガスを、電気惨m装置お
よびそれに後置した湿式脱硫装置等の排カス処理機器に
よって処理する方法に関する 従来、石炭ボイラ等の排ガスを処理する場合、Fイ1 
畳ボイラエコノマイザ→エアヒータ→電′911執率俳
賀−漫式脱鑓、肺買−◆煙突と排ガスは、通過する。こ
の際、エアヒータから流出し、電気集塵装置へ流入でる
排ガス温度は150でから150でであり、また湿式脱
硫装置から流出するガスは45〜60℃となる。このた
め、煙突から排出される排ガスは白煙ヶ生じ、また、拡
散効果も悪く、電気集塵装置へ流入−rる排ガス温度も
この状態では高いσ)で、電気抵抗値が大きく、パック
コロナ現象が発生し、集塵率の低下を招(・ていた。十
こで、これケ防止する手段として、電気集塵装置の集塵
極ケ中空状σ)パイプまたは角板として内部に水等の熱
媒体VJAt。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for treating exhaust gas from a coal boiler, for example, by using an electric waste treatment device and exhaust gas treatment equipment such as a wet desulfurization device installed after it. In case, F i1
Tatami boiler economizer → air heater → electric '911 shutsu haiga - comic style descaling, lung purchase - ◆The chimney and exhaust gas pass through. At this time, the temperature of the exhaust gas flowing out from the air heater and flowing into the electrostatic precipitator is between 150 and 150 degrees Celsius, and the temperature of the gas flowing out from the wet desulfurization device is 45 to 60°C. For this reason, the exhaust gas discharged from the chimney produces white smoke, has a poor diffusion effect, and the temperature of the exhaust gas flowing into the electrostatic precipitator is high (σ) in this state, the electrical resistance is large, and the pack corona is high. This phenomenon occurred, leading to a decrease in the dust collection rate.As a means to prevent this, the dust collection electrode of the electrostatic precipitator was installed as a hollow pipe or square plate with water etc. The heating medium VJAt.

て集塵極の温度ケ下げ、集塵ダストの電気抵抗を下げて
集塵率W向上させる方法が一般的に知られている。
A method is generally known in which the dust collection rate W is improved by lowering the temperature of the dust collecting electrode and lowering the electrical resistance of the collected dust.

本発明は、電気集塵装置の中空状集率極内忙浸式脱硫装
置から流出−Cる排ガス!導入してi集塵極ケ冷却し集
塵極板付着ダストの電気抵抗値ヶ下げ、パックコロナ現
象を防止L、隼奉率ケ向上せ[2めろと同時に、洋式脱
硫装置の排ガスV昇温1−て、白煙化を防止し、拡散効
−Pv高めbことV目的とする、 1!J、f、本発明の一実施例〉図面Y参照して説明(
石と、図中1はエアヒータで、排ガスの熱量v炉焼空気
の加熱用として使うための熱交換器である。2は電気集
塵装置で排ガス中の粉塵Y除塵して清浄化−1″るため
のものである。このW気隼@俳賃2の集塵極はパイプま
たは□角型の中空状であり、この中ケ後述てる湿式脱硫
装置4かr)σ)排ガスが通過できる構造である。4は
7臀式騨硫装!で、ここで排ガス中の硫黄分が除去J!
L11石。5は煙突で、湿式脱硫装置から流出した排ガ
スはここから大気中に放出拡散される。
The present invention is directed to exhaust gas flowing out from an active immersion type desulfurization device in a hollow collector pole of an electrostatic precipitator! It cools the dust collecting electrode, lowers the electrical resistance value of the dust adhering to the dust collecting electrode, prevents the pack corona phenomenon, and improves the service efficiency. The purpose is to prevent white smoke from forming and increase the diffusion effect - Pv. J, f, One embodiment of the present invention〉Described with reference to drawing Y (
1 in the figure is an air heater, which is a heat exchanger used to heat the furnace air. 2 is an electrostatic precipitator that removes dust from the exhaust gas and purifies it. The dust collection electrode of this W 2 is a hollow pipe or □ rectangular shape. This wet desulfurization device (4), which will be described later, has a structure that allows exhaust gas to pass through.4 is a 7-butt type desulfurization device, which removes the sulfur content in the exhaust gas.
L11 stones. Reference numeral 5 denotes a chimney from which the exhaust gas flowing out from the wet desulfurization equipment is released and diffused into the atmosphere.

四F・のI11成におい゛r1石炭ボイラ排ガスは工’
7):J1v出て130℃から150″Cの温度Cw気
隼廟装置2へ入る。そこで、このままでは、幇気集秦装
置2の集塵極3に高抵抗のダストがイ1* L 、パラ
クコ晶す現象を生起して集塵率が借上−fろつそこで電
気集塵装置2v通過し、湿f:、幹硫装置4v渡、出1
−る排ガスがその温度が45℃から6orと低いσ)で
、こσ)排ガスシ中空状の集塵極3へ導いて、集塵1j
 5 V、冷却し集塵極5に付着すb高抵抗ダストの温
度ケ低下せしめ、電気抵抗値を低くしてバックコロナ現
象な防止し、隼隋率ケ向上せしめす、、一方、湿式脱硫
装置4から集塵極3ヶ通過−する排ガスは加熱されて9
0でから110℃になり、煙道6と煙突5v経て大気中
へ排出される。これにより煙突5Jり大気中へ放出され
る排ガス0白煙防止とともに拡散効果!高める。
In the I11 construction of the 4th floor, the exhaust gas of the r1 coal boiler was
7): J1v exits and enters the Qw air device 2 at a temperature of 130°C to 150″C.If this continues, high-resistance dust will accumulate on the dust collecting electrode 3 of the air collecting device 2. This causes a phenomenon of crystallization, and the dust collection rate increases. Then, the electrostatic precipitator 2V passes through, and the humidity f:, the main sulfur unit 4V passes, and the dust collection rate increases.
- The temperature of the exhaust gas is as low as 6or from 45℃, and the exhaust gas is guided to the hollow dust collection electrode 3 and collected at
5 V, the temperature of the high-resistance dust that adheres to the dust collection electrode 5 is lowered, the electric resistance value is lowered, the back corona phenomenon is prevented, and the evaporation rate is increased.Meanwhile, the wet desulfurization equipment The exhaust gas passing through 4 and 3 dust collecting electrodes is heated and passes through 9
The temperature increases from 0 to 110°C and is discharged into the atmosphere through the flue 6 and chimney 5V. This prevents zero white smoke from being released into the atmosphere from the chimney 5J and has a diffusion effect! enhance

以上、本発明によると、湿式脱硫装置から流出てろ排ガ
スを、咳雷気集塵装置σ)中空状集塵極内へ通過せ1め
、該電気集塵装置内部Y通過イる排ガスによって昇Sす
るとともに、骸集塵極舎冷却するようにしたから、電気
業11. * wの集塵極表面付着ダストの温度が低下
し、付着ダクトの電気抵抗が下り、集塵率が向丘Tるば
かりでなく、湿式脱硫装置出口ガスの温度り上げ、煙突
から大気中へ放出される白煙ケ防+1.1−1大気拡散
効4Iv高めると(・う効果v*−rb−
As described above, according to the present invention, the filtered exhaust gas flowing out from the wet desulfurization device is passed into the hollow dust collecting electrode of the electrostatic precipitator σ), and the exhaust gas passing through the inside of the electrostatic precipitator raises S. At the same time, the electric industry 11. * The temperature of the dust adhering to the surface of the dust collection electrode decreases, the electrical resistance of the adhesion duct decreases, and the dust collection rate not only increases, but also increases the temperature of the wet desulfurization equipment outlet gas and releases it into the atmosphere from the chimney. White smoke prevention +1.1-1 Atmospheric diffusion effect 4Iv is increased (・U effect v*-rb-

【図面の簡単な説明】[Brief explanation of the drawing]

目上は本発明の具体的な実施例を示すフローである。 1、・・・・・・エアヒータ、2・・・・・・電気集塵
装置、3・・・・・・集塵極、4・・・・・・脱硫装量
、5・・・・・・煙突。
The above is a flow showing a specific embodiment of the present invention. 1... Air heater, 2... Electrostatic precipitator, 3... Dust collection electrode, 4... Desulfurization amount, 5... ·chimney.

Claims (1)

【特許請求の範囲】[Claims] 排ガスを電気集塵装置・\流入せしめ除塵り、た後、湿
式脱硫装置を通過せしめ、硫黄分を除去する方法におい
て、#湿式脱硫装置から流出する#Pナスを、峡電気隼
塵装貴の中空状集塵極内・・導λせ1.2めて、峡雫、
気集lIi装置内部を通過する排ガスによって昇温する
とともに1誼集秦極を冷却簀しめることを特徴とする排
ガス処理方法
In this method, the exhaust gas is passed through an electrostatic precipitator to remove dust, and then passed through a wet desulfurization device to remove the sulfur content. Inside the hollow dust collecting pole...Introducing λ1.2, the canyon drops,
An exhaust gas treatment method characterized by raising the temperature of the exhaust gas passing through the inside of the air collector IIi device and cooling a single collector pole.
JP57015891A 1982-02-03 1982-02-03 Treatment of waste gas Pending JPS58133846A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57015891A JPS58133846A (en) 1982-02-03 1982-02-03 Treatment of waste gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57015891A JPS58133846A (en) 1982-02-03 1982-02-03 Treatment of waste gas

Publications (1)

Publication Number Publication Date
JPS58133846A true JPS58133846A (en) 1983-08-09

Family

ID=11901406

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57015891A Pending JPS58133846A (en) 1982-02-03 1982-02-03 Treatment of waste gas

Country Status (1)

Country Link
JP (1) JPS58133846A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006038461A1 (en) * 2004-10-01 2006-04-13 Isuzu Motors Limited Gas treatment device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006038461A1 (en) * 2004-10-01 2006-04-13 Isuzu Motors Limited Gas treatment device
JP2006102575A (en) * 2004-10-01 2006-04-20 Isuzu Motors Ltd Gas treatment device
JP4529013B2 (en) * 2004-10-01 2010-08-25 いすゞ自動車株式会社 Gas processing equipment

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