JPS5949856A - Feed water controlling method of wet-type dust collector - Google Patents

Feed water controlling method of wet-type dust collector

Info

Publication number
JPS5949856A
JPS5949856A JP57159344A JP15934482A JPS5949856A JP S5949856 A JPS5949856 A JP S5949856A JP 57159344 A JP57159344 A JP 57159344A JP 15934482 A JP15934482 A JP 15934482A JP S5949856 A JPS5949856 A JP S5949856A
Authority
JP
Japan
Prior art keywords
water
circulating
wet
dust collector
dust
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.)
Granted
Application number
JP57159344A
Other languages
Japanese (ja)
Other versions
JPH0123183B2 (en
Inventor
Hidehiko Otani
尾谷 英彦
Noriaki Maekawa
前川 式明
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP57159344A priority Critical patent/JPS5949856A/en
Publication of JPS5949856A publication Critical patent/JPS5949856A/en
Publication of JPH0123183B2 publication Critical patent/JPH0123183B2/ja
Granted legal-status Critical Current

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Abstract

PURPOSE:To control effectively the water feeding of a wet-type dust collector conforming to a restriction for soot and dust, by discharging circulating suspended matters together with a drain, and feeding water, corresponding in quantity to the discharging water quantity to a water circulating line, and controlling the feeding quantity of a pH adjusting agent. CONSTITUTION:After catching dust and mist of sulfuric acid at the front and rear chambers 12 and 13 of a wet-type dust collector 11, a dust collecting waste water is returned to a circulating water tank 14 and is circulated to the collector 11 after being filtered by a auto-strainer 16. A drain, containing solid matters separated by the strainer 16, is discharged out of the system. Further, an alkaline pH adjusting liquid is injected to a circulating water tank 14 through a pH controlling device 18 to neutralize the circulating water into a prescribed pH. On the other hand, a fresh water is replenished to the tank 14 as the descreased portion of circulating water caused by the drain discharge. Further, the fresh water is intermittently fed as a washing water to the rear chamber 13 of the dust collector 11 by an intermittently acting pump 20.

Description

【発明の詳細な説明】 本発明は/!111式集塵機における供水を制御する方
tノ:に関する。
[Detailed Description of the Invention] The present invention is /! This article relates to a method for controlling water supply in a Type 111 dust collector.

湿式Its塵機の供水方法としては、従来第1図(Al
または(13)に示す方法が採用されている。第1図(
A) O)方法においては、湿式す」1ノから、い排水
ダンク2に排出された喘塵排水を水処理設備へ送り、水
処理設備からの処理水を洗浄水として集四機1へ循環さ
せるものである。また第1図(鳩の方法では、排水タン
グ2に貯留された集塵排水の一部をブロー水として水処
理膜(+ii+に送り、このブロー水量と同)dの補給
水を循環タンク3に補給して集塵機1へ供給するもので
ある。
Conventionally, the water supply method for a wet-type Its dust machine was as shown in Figure 1 (Al
Alternatively, the method shown in (13) is adopted. Figure 1 (
A) In the O) method, the dust wastewater discharged from the wet drain dunk 2 is sent to the water treatment equipment, and the treated water from the water treatment equipment is circulated to the collector 1 as washing water. It is something that makes you In addition, as shown in Fig. 1 (in the pigeon method, part of the dust collection drainage stored in the drainage tongue 2 is sent to the water treatment membrane (+ii+, and the amount of this blown water is the same as blow water), and the make-up water d is sent to the circulation tank 3. It is used to replenish and supply the dust collector 1.

ところが、最近のボイラープラントにおける煤塵排出規
制の強化により、これまでは排煙脱硫装置からの処理ガ
スはアフターバーニングされた後に煙突から排出されて
いたのに対して。
However, due to the recent tightening of soot and dust emission regulations for boiler plants, whereas previously the treated gas from the flue gas desulfurization equipment was afterburned before being discharged from the chimney.

4虎突からの煤塵濃度を低下させるために排煙脱硫装置
からキャリオーバする゛硫酸ミストおよび残留するボイ
ラーダストを除去するための湿式集塵機が必要となり、
これに伴って従来にない経済的な水処理システムの確立
が要求されるに至った。
4. In order to reduce the concentration of soot and dust from the flue gas stack, a wet dust collector is required to remove the sulfuric acid mist and residual boiler dust carried over from the flue gas desulfurization equipment.
This has led to a demand for the establishment of unprecedented economical water treatment systems.

ところで、ボイラープラントの−9を1(とじてu1煙
脱硫装置^1の後に設置される4(【j式用塵1幾は、
排煙脱硫装置の出口ガス中に残留する硫酸ミストおよび
ボイラーダストを捕イ1トすることを「i的としている
。このため湿式史塵機の1ilB 7(Iy’3<とし
て供給される循];■水は、充分なダス)・拙Iトカ1
七カル有するようにその中に含まれる浮遊固形分の濃1
ツを所値り、下に制mljして用いなければならないと
同時、に、極用の腐食作1[1を有する硫酸ミストを捕
+1′ニーjることがら、集p9機内部の構成材料の+
tJ1食をFJj l卜するためにそのpiJ値を調整
して供給する必要がある。他方、湿式集pμ@がボイラ
ープラントの末端装置として設置されるという条件から
、l!ia式里塵格集塵l(+水による水ミストのキャ
リオーバを極力少なくしてアフターバーニングの効率低
下を防止すると共に、キャリオーバ[、た水ミスト中の
浮遊固形分イ農度を少fc くするように循環水の供水
を:li’l allするこンが必要とされる。
By the way, the -9 of the boiler plant is 1 (1) and the 4 ([J-type dust 1] installed after the u1 smoke desulfurization equipment^1 is
The aim is to capture the sulfuric acid mist and boiler dust remaining in the outlet gas of the flue gas desulfurization equipment.For this purpose, the wet dusting machine's 1ilB7 (circulation supplied as Iy'3) is ;■Water is enough)・I Toka 1
The concentration of suspended solids contained in it is 1 to have 7 Cal.
At the same time, at the same time, it is necessary to collect sulfuric acid mist having a corrosive effect on the material inside the machine. + of
In order to increase FJj from tJ1 meal, it is necessary to adjust and supply the piJ value. On the other hand, from the condition that the wet collector pμ@ is installed as an end unit of a boiler plant, l! IA type dust collector (+) Minimizes carryover of water mist due to water to prevent deterioration of afterburning efficiency, and also reduces carryover [and suspended solid content in water mist] Therefore, it is necessary to supply circulating water.

木イと明はL記IIN情(=喋みてなされたもので、ボ
イラープラントを強化された煤塵排出規制に通合させる
Lで湿式集塵機の徂水に要求される上記“2′、件を満
足し、同時に経済性をも考慮1.た湿式集μ)2杉、兎
0)供水側/1i41 ’)j法を11を供するもので
ある。
Kii and Akira are talking about Lki IIN information (= it was made after talking, and it satisfies the above ``2'' required for the water of wet dust collectors in L to make boiler plants comply with strengthened soot and dust emission regulations. However, at the same time, considering the economical efficiency, 1. Wet collection μ) 2 Cedar, Rabbit 0) Water supply side/1i41')j method 11 is provided.

即ち、不発明は湿式1集塵1幾か1ら1串さ」1.るj
ljl排塵を再び洗、浄水と1〜でl!i+!式ニド四
機に供給するようにした循環水ラインの循上5.lj水
中に含まれている浮遊固形物をドレニンとして系外に4
.It l+せしめ、そのドレーン[44に応じた〜)
1水を循jγ3水ラインに補給すると共に、上記循曙7
j(のp I−(の検出値に応じて循環水ラインに供給
するp)1調整うW品の供給Mを制御するようにしたこ
とを特徴とする湿式集塵機の供水制Wll+方法である
That is, the non-inventive method is 1 wet type 1 dust collection 1 some 1 to 1 skewer.''1. Ruj
ljl Wash the exhaust dust again and add purified water from 1 to 1! i+! Circulation of the circulating water line that supplies the four types of Nido machines 5. lj Suspended solids contained in the water are removed from the system as drenin 4
.. It l+seshime, its drain [according to 44~]
1 water to the circulating jγ3 water line, and the above circulating water line 7.
This is a water supply system Wll+ method for a wet type dust collector, characterized in that the supply M of the W product is controlled by adjusting p supplied to the circulating water line according to the detected value of p I-(of p I-(p) of j(p)1.

以下、7)IB 2図を参照して不発明の−¥li+4
例を説明する。
Below, 7) IB Referring to Figure 2, the uninvented -¥li+4
Explain an example.

第2図は不発明による供水制御方法を採用1した湿式集
塵機システムのフローチャートである。
FIG. 2 is a flowchart of a wet dust collector system employing the water supply control method according to the invention.

同図において、11は/!ii!式畢塵機であl)、そ
の内部には1111室12および後室13が設けらり、
ている。そして、排煙脱硫装置を出た排ガスは図中矢印
で示すように集塵JXAtz内を前室12、後室13の
順序で通過する。14は循環水タンクである。該循環水
り・ンク14に貯留されているa 4F水しま循環水ポ
ンプ15によりオートストレーナ16を経て湿式集塵機
11の前室12および後室13に連続的にスプレーさ薦
るようになっている。前室12および後室13はスプレ
ーされた洗浄水は排ガス中に含ま゛れるボイラーダスト
および硫酸ミストを捕集し、集塵排水として夫々別の経
゛路で循環水タンク14に帰遠する。従って、循環水タ
ンク14から前記オートストレーナ16に向う循環水は
高い浮遊固形物濃度を有しているが、オートストレーナ
I6によってこの固形物を沢過され、充分なダスト捕集
能力を有する1112浄水として湿式集り’、”4機1
1へ循環されるようになっている。メ′−トスト1/−
ナI6で分離された固形物の混入した′ドレインはオー
トストレーナ160)ドレイン配?―″から系外に1非
出される。このドレイン流Mはドレイン配管に設けられ
た流量自動制御装置17によって一定の流i11に制御
される。また、循環水のp I−1値を所定の値に調整
するために、捕集された硫酸ミストをrim lt+す
るNaOH液あるいはCa(01−’L 液’G)7 
ルカ’J □に’l:pH%I、!I !J47rtが
Flit tE4 fl占環水タンク14に注入され2
)。このp I」+i14.i整液の流Mは循環水タン
ク14に帰1ζ]1する史塵uh水のpH値にノ、(づ
いて、p J−1制?:lTl装置18により循環水が
所定のpH値に中和されろように制〈111される。こ
の場合、酸+7.t:ffJ:が品も強くなる前室12
からの集塵排水pI(値をに記p II八へ、1.1整
0)基準情報とすること−によ【]、確実ζ二循1.R
液0)p41低下をμJ5止するようになっている。他
方、オートストレーナ−6からのドレイン排水(二よっ
て循環水の:5)が減少するかへ、その減少分は新たに
新水(工性用水)が前記循1眉;水タング14に補給さ
れるようになっている。即ち、(l+’i環水クンクタ
ンには水位調節装闘19が設けられており、循環水タン
ク14の水位が低下すると所定の水位が同復するまでV
「水を補給する。また新水(工業用水)はタイマーで間
欠的に1101作するように′/、Cつでいるポンプ2
0により、湿式イ1シ塵I@11内における媒塵負葡の
低い後室13へ間欠的(5〜10分/2分間2に洗浄水
として供給されるようになっている。
In the figure, 11 is /! ii! It is a type dusting machine (1), and there are 1111 chambers 12 and a rear chamber 13 inside.
ing. Then, the exhaust gas exiting the flue gas desulfurization device passes through the dust collector JXAtz in the order of the front chamber 12 and the rear chamber 13 as shown by arrows in the figure. 14 is a circulating water tank. A 4F water circulating water pump 15 stored in the circulating water tank 14 continuously sprays the water into the front chamber 12 and rear chamber 13 of the wet dust collector 11 via an auto strainer 16. . The sprayed cleaning water in the front chamber 12 and the rear chamber 13 collects boiler dust and sulfuric acid mist contained in the exhaust gas, and returns to the circulating water tank 14 through separate routes as dust collection wastewater. Therefore, although the circulating water flowing from the circulating water tank 14 to the auto-strainer 16 has a high concentration of suspended solids, the auto-strainer I6 filters out the solids, and the 1112 purified water has sufficient dust collection ability. As a wet gathering', '4 machines 1
1. Me'-tost 1/-
160) Is the drain contaminated with the solids separated by I6 an auto-strainer? This drain flow M is controlled to a constant flow i11 by an automatic flow rate control device 17 provided in the drain piping. To adjust the value, add NaOH solution or Ca(01-'L solution'G)7 to rim lt+ the collected sulfuric acid mist.
Luca'J □ni'l: pH%I,! I! J47rt is injected into Flit tE4 fl Senkan water tank 14 and 2
). This p I''+i14. i The liquid regulating flow M returns to the circulating water tank 14 and the pH value of the water is adjusted to the pH value of the water. It is controlled so that it is neutralized. In this case, the acid +7.t:ffJ: becomes stronger as well.
Dust collection and drainage pI (values should be recorded in p II 8, 1.1 and 0) shall be used as reference information. R
Solution 0) It is designed to stop p41 decrease by μJ5. On the other hand, as the drain water from the auto-strainer 6 (2, therefore, circulating water: 5) decreases, new water (water for industrial use) is replenished into the water tongue 14 to compensate for the decrease. It has become so. That is, (l+'i Kansui Kunkutan is provided with a water level adjustment device 19, and when the water level of the circulating water tank 14 decreases, V is adjusted until the predetermined water level is restored.
``Replenish water.Also, use a timer to intermittently produce fresh water (industrial water).
0, the cleaning water is supplied intermittently (every 5 to 10 minutes/2 minutes) to the rear chamber 13 where the dust load in the wet type I1 is low.

一]二記第2図の湿式集塵機システムにおける供水制ル
111方法によれは、洗浄水として集塵機(二供給され
る循口′d水中の浮遊固形物濃度なYすY定値り、下に
制御できると同時に、p l−I値を所定範囲内に維持
することができる。また、^1(式集塵機1〕の後室複
酸において間欠的に新ポ(中性でしかも〆゛l遊固形分
濃度が低い工業用水)によってz1L浄する方法が採用
されることにより、キャリオーバによる水ミストが低減
されることになる。更ニ、4+i!式’D 塵システ、
ムk・単独のコンパクトな設備とすることができる。
1] 2) According to the method of water supply control in the wet dust collector system shown in Fig. 2, the cleaning water is supplied to the dust collector (2) The circulating port where the suspended solids concentration in the water is controlled below a fixed value. At the same time, the p l-I value can be maintained within a predetermined range.In addition, new po (neutral and By adopting a method of purifying z1L with industrial water (with a low concentration of water), water mist due to carryover will be reduced.
・Can be made into a stand-alone compact facility.

以上詳述したように、本発明によれば煤塵規制が強化さ
れたボイラープラントに適合した効果的な湿式す5塵]
幾の供水制御方法を提供できるものである。
As described in detail above, according to the present invention, an effective wet-type soot that is suitable for boiler plants where soot and dust regulations have been strengthened]
This method can provide several water supply control methods.

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

i1’、 1図(Nおよび(句は夫々湿式寮塵様の従来
の供水方法を示す説明図、似2図は本発明の一実施例に
なる供水制御方法を採用した湿式集塵システムを示すフ
ローチャートで、1)る。 11・・・l!11〕式集共機 I2・・・的室、  13・後室 14・・・循環水タンク、15 ポンプ16・・・オー
トストレーナ 17・・・流け、制御装置 18・・・pH制御装置 19・・・水位調整装置 2θ・・・ポンプ
i1', Figure 1 (N and (phrase) are explanatory diagrams showing the conventional water supply method for wet dust collection, respectively, and Figure 2 shows a wet dust collection system that adopts the water supply control method that is an embodiment of the present invention. In the flowchart, 1). 11...l!11] Formula collection common machine I2...target chamber, 13. Rear chamber 14...circulating water tank, 15 pump 16...auto strainer 17... Flow, control device 18...pH control device 19...water level adjustment device 2θ...pump

Claims (1)

【特許請求の範囲】[Claims] 湿式集塵機から排出される集塵排水を再び洗浄水として
湿式集塵機に供給するようにした循扉水ラインの循環水
中に含まれている浮遊固形物をドレーンとして系外に排
出せしめ、そのドレーン惜に応じた新ポを循環水ライン
に補給すると共に、上記循環水のpnの検出値に応じて
循環水ラインに供給するpHRIM整薬品の供給計を制
御するようにしたことを特徴とする湿式集塵機の供水制
御方法。
The dust collection wastewater discharged from the wet dust collector is supplied to the wet dust collector again as washing water.The suspended solids contained in the circulating water of the circulating door water line are discharged outside the system as a drain. The wet type dust collector is characterized in that the circulating water line is replenished with a new pn according to the detected value of the circulating water, and a supply meter of pHRIM chemicals to be supplied to the circulating water line is controlled according to the detected value of the pn of the circulating water. Water supply control method.
JP57159344A 1982-09-13 1982-09-13 Feed water controlling method of wet-type dust collector Granted JPS5949856A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57159344A JPS5949856A (en) 1982-09-13 1982-09-13 Feed water controlling method of wet-type dust collector

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57159344A JPS5949856A (en) 1982-09-13 1982-09-13 Feed water controlling method of wet-type dust collector

Publications (2)

Publication Number Publication Date
JPS5949856A true JPS5949856A (en) 1984-03-22
JPH0123183B2 JPH0123183B2 (en) 1989-05-01

Family

ID=15691785

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57159344A Granted JPS5949856A (en) 1982-09-13 1982-09-13 Feed water controlling method of wet-type dust collector

Country Status (1)

Country Link
JP (1) JPS5949856A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62180765A (en) * 1986-01-31 1987-08-08 Mitsubishi Heavy Ind Ltd Cleaning method for wet type electrostatic precipitator
JP2009539579A (en) * 2006-06-07 2009-11-19 アルストム テクノロジー リミテッド Wet electrostatic precipitator
JP2010158604A (en) * 2009-01-06 2010-07-22 Mitsubishi Heavy Industries Mechatronics Systems Ltd Method of cleaning electrostatic precipitator and apparatus therefor
CN105855061A (en) * 2016-04-07 2016-08-17 浙江南源环境工程技术有限公司 Interval spraying control technology for water saving of wet electrical dust precipitator
CN106733186A (en) * 2017-01-06 2017-05-31 浙江浙能嘉华发电有限公司 A kind of wet electric back segment spray program and optimization water-saving method

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56121648A (en) * 1980-02-29 1981-09-24 Ishikawajima Harima Heavy Ind Co Ltd Controlling method of water for dust collecting in electrical dust precipitator

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56121648A (en) * 1980-02-29 1981-09-24 Ishikawajima Harima Heavy Ind Co Ltd Controlling method of water for dust collecting in electrical dust precipitator

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62180765A (en) * 1986-01-31 1987-08-08 Mitsubishi Heavy Ind Ltd Cleaning method for wet type electrostatic precipitator
JP2009539579A (en) * 2006-06-07 2009-11-19 アルストム テクノロジー リミテッド Wet electrostatic precipitator
JP2010158604A (en) * 2009-01-06 2010-07-22 Mitsubishi Heavy Industries Mechatronics Systems Ltd Method of cleaning electrostatic precipitator and apparatus therefor
CN105855061A (en) * 2016-04-07 2016-08-17 浙江南源环境工程技术有限公司 Interval spraying control technology for water saving of wet electrical dust precipitator
CN106733186A (en) * 2017-01-06 2017-05-31 浙江浙能嘉华发电有限公司 A kind of wet electric back segment spray program and optimization water-saving method

Also Published As

Publication number Publication date
JPH0123183B2 (en) 1989-05-01

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