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JPS6245355A - Apparatus for removing dust - Google Patents

Apparatus for removing dust

Info

Publication number
JPS6245355A
JPS6245355A JP60185138A JP18513885A JPS6245355A JP S6245355 A JPS6245355 A JP S6245355A JP 60185138 A JP60185138 A JP 60185138A JP 18513885 A JP18513885 A JP 18513885A JP S6245355 A JPS6245355 A JP S6245355A
Authority
JP
Japan
Prior art keywords
mist
dust
electrode
collecting electrode
dust collecting
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
JP60185138A
Other languages
Japanese (ja)
Inventor
Masashi Kitamura
正史 北村
Tomonori Takeda
武田 智則
Akira Shibuya
渋谷 章
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.)
IHI Corp
Original Assignee
Ishikawajima Harima Heavy Industries Co 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 Ishikawajima Harima Heavy Industries Co Ltd filed Critical Ishikawajima Harima Heavy Industries Co Ltd
Priority to JP60185138A priority Critical patent/JPS6245355A/en
Publication of JPS6245355A publication Critical patent/JPS6245355A/en
Pending legal-status Critical Current

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  • Electrostatic Separation (AREA)

Abstract

PURPOSE:To enhance dust removal efficient by forming dust particles into mist, by providing a condenser forming mist by using dust as a nucleus and an electric precipitator for ionizing the mist and moving the ionized mist to a dust collecting electrode to remove the same in a communicated state. CONSTITUTION:When an OFF-gas supply system 3 and a condenser 4 are operated, the liquefiable components such as steam, NOX or the like in the OFF-gas are condensed under cooling and liquefied to be formed into mist having dust as a nucleus and this mist is sent into the space between a linear electrode 7 and a dust collecting electrode 8. Therefore, the mist is ionized by the corona discharge phenomenon of a discharge electrode to be moved to the surface of the dust collecting electrode 8. The each mist on the dust collecting electrode 8 becomes large and subsequently flowed down under its own wt. to perform the taking-in of the mist in an ionized atmosphere. The taken-in mist is collected in a lower casing 10 and subsequently discharged from a drain line 16, as shown by the arrow.

Description

【発明の詳細な説明】 「産業上の利用分り!f」 本発明は、ダスト除去装置に係り、特に、原子燃料サイ
クルプラントで発生するオフガス等のエアロゾル中に含
まれている液化成分を冷却凝縮してミスト化する機能を
有するダスト除去装置に関するものである。
Detailed Description of the Invention "Industrial Applicability!f" The present invention relates to a dust removal device, and in particular, a device for cooling and condensing liquefied components contained in aerosols such as off-gas generated in nuclear fuel cycle plants. The present invention relates to a dust removal device having a function of converting dust into mist.

[゛従来の技術とその問題点」 ダスト除去装置に適用される電気集塵は、その他の集塵
方法と比較して集塵性能が優れてお・)、粒子径の小さ
な乙のまで捕集可能であるとされている。このため、例
えば原子燃料サイクルプラントで発生ずる放射性物質を
各種処理計ることによ−、て発生したオフカス中9)放
射性i・γ子を、捕捉1−て除去する場合に何効なムの
とされている。
[Conventional technology and its problems] Electrostatic precipitators applied to dust removal equipment have superior dust collection performance compared to other dust collection methods, and can collect even small particles. It is said to be possible. For this reason, for example, what is the effectiveness of capturing and removing radioactive i and gamma particles in the off-scrap by various treatments of radioactive materials generated in nuclear fuel cycle plants? has been done.

しかしながら、従来のタスト除去装置て:す、=ゴロナ
放′屯を生じさ口゛るための電界強度が、逆ポnft現
象や再飛散現象を防止する等の理由によ1)、例えば3
 K V / ctn程度に抑制されており、エア2J
ゾル(煙霧質)の粒子径が10μm以−LO′)6つ)
てめるとりJ率良く捕集できるが、1μm程度の0ので
あると、集塵率が例えば99%(除染係数換J9の場合
、102 )程度となって、これ以上に高めることは技
術的に困難となる。さらに、粒子径か小さく、サブミク
ロン中位(1,0μm以下)になると著しく集塵効率か
低下ずろ。したが1・て、IYJ記放耐放射性粒子去す
る」二うな場合であると、除去できない放射性粒子の存
在により、従業員の改射、腺彼曝腺量か大きくなる等の
問題点を生しる。
However, in the conventional dust removal device, the electric field strength for generating gorona radiation is limited for reasons such as preventing reverse polarization phenomenon and re-scattering phenomenon1), for example, 3
It is suppressed to about K V / ctn, and air 2J
The particle size of the sol (mist) is 10 μm or more (LO') 6)
It is possible to collect dust with a good J rate, but if it is about 1 μm, the dust collection rate will be about 99% (102 in case of decontamination coefficient J9), and it is difficult to increase it beyond this level. It becomes difficult. Furthermore, if the particle size is small, in the submicron range (1.0 μm or less), the dust collection efficiency will drop significantly. However, in such a case, the presence of radioactive particles that cannot be removed may cause problems such as an increase in the amount of radiation exposed to the employee's glands, etc. Sign.

: 本発明の[−]的とその達成手段J本発明は、こD
ような従来技術の問題点を有効に解決することを目的と
しているものである。
: [-]Object of the present invention and means for achieving it
The purpose of this invention is to effectively solve the problems of the prior art.

こ(′、らの1」的を達成するために、本発明のタスト
除去装置では、直流電圧を印加して放′、Ti電極の間
(−コcr−+1戊屯を生にさせてイオン化雰囲気とし
ておくととらに・、」フガス中に水分等の液化成分か1
1J:れでいろことを刊用して、この液化成分を凝;3
11さ1」てミスト化状態にしてから、41j記イオン
化雰囲気中に送り込み、ミストをイオン化して、11、
塵1u極に多動きり、また、集塵電極に沿って流1・さ
Uて除去する上へにした乙のである。さらに、このオフ
カス中にN OXが含まれていると、ミス[・に吸収さ
れミストのイオン化が促進される。
In order to achieve this goal, in the dust removal device of the present invention, a DC voltage is applied to discharge the Ti electrodes (-COCR-+1) to generate ionization. If you leave it in an atmosphere, there will be liquefied components such as moisture in the fugas.
1J: Condensate this liquefied component by publishing Redeiroko; 3
11) to make it into a mist state, and then send it into the ionizing atmosphere described in 41j to ionize the mist, 11,
The dust moves a lot to the electrode, and the dust is removed by flowing along the dust collection electrode. Furthermore, if NOx is contained in this off-scum, it will be absorbed by the mist and the ionization of the mist will be promoted.

[一実施例 −1 以[・、本発明のゲスト除去装置の一実施例を第1図に
基ついで説明・する。
[One Embodiment-1] Hereinafter, one embodiment of the guest removal device of the present invention will be described based on FIG. 1.

第1図において、符号lは電気集塵器、符号2:」高1
Ti圧供給系、符吐3はオフカス供給系、符号・1;よ
、疑11ii ’A:’i、1′jぢ5:よ流!1(1
摸用拾水系、剪うじ6:よ必要に応して設(jらイ′4
ろ水I!\気供拾系でめろ、そして、1)1j記電気土
塵fjg lは、高市F1−()(給糸2に接続されて
いる徨状極7と、該徨状極7・)回りを囲んでいろ円筒
状をなオ集空?u !+’li 3とか、、:、 47
η成され、その間の空間か、I−1′!(!ケーシング
9と下部ケーソンろ・10とによ−・てシ(気から区画
さ、シt、十j1ニケーノンク9の内jゴ)には、O[
1,把流水膜用拾+l<系5の貯水タンク11からポン
プ!2にJ、−)て吸い」、げた水をためるノニめのリ
ンク状1111〜l 3か、14〜1更電極8と」一部
ケーン/り9との間に形成さi7でいろ。そして、該リ
ンク状溝13からあふれf二水は、集塵電極8の円部状
内面にiF>−・で流れ落ちて、流水膜を形成する乙の
であり、その水イtは流咀計141によって検出され、
ノ41整さ杓ろようになっている。
In Figure 1, the symbol l is an electrostatic precipitator, and the symbol 2 is a high 1
Ti pressure supply system, sign discharge 3 is off scum supply system, code 1; yo, doubt 11ii 'A: 'i, 1'jji 5: yo flow! 1 (1
Water pickup system for sampling, pruning 6: Installed as necessary.
Romizu I! \Mero with the air supply system, and 1) 1j electric dust fjg l is Takaichi F1-() (the stray pole 7 connected to the yarn feeder 2 and the stray pole 7) Is there a cylindrical shape surrounding it? u! +'li 3 etc...:, 47
η is formed, and the space between I-1′! (!The casing 9 and the lower caisson slot 10 are separated from each other by the casing 9 and the lower caisson 9).
1, Pump from the water storage tank 11 of system 5 for the flow water film + l < system 5! A link-like link 1111 to 1111 to 13 or 14 to 1 is formed between the electrode 8 and a part of the cane/liquid 9 to collect water. Then, the overflowing water from the link-shaped groove 13 flows down onto the circular inner surface of the dust collection electrode 8 at iF>-, forming a running water film, and the water flows down to the flow meter 141. detected by
ノ41 It's like a ladle.

また、前記オフカス併給系3に(す続さ、1−5ている
凝縮器・1のトレノライン15は、l1Fi記下部ケー
ソンク10の排水ラインI6に接続5れている。
Further, the drain line 15 of the condenser 1 connected to the off-gas cofeeding system 3 (1-5) is connected to the drain line I6 of the lower caisson 10.

さらに、上1鄭ケーノンク9には、排気系17か接続ご
; 、j4.、該排気系17と前記オフカス供給系3ど
H:)間に、散↑17子計測器18か接続されて、微粒
(′))捕捉状態をV;;:視しく1トるようになって
いる。
Furthermore, the exhaust system 17 is connected to the upper part 1, j4. A scattering measuring device 18 is connected between the exhaust system 17 and the off-gas supply system 3H:), so that the state of capturing fine particles (')) can be clearly detected at V;;:. ing.

ri J’;、1iii記腺状極7は、コロナ枚重を(
足進させる)−:、:g)に例えば細いffl棒状断面
を打])−るとと乙に、間隔をF3シビご巽、u針が設
(]゛られる等のhX′j造となっている。
ri J';, 1iii.
For example, insert a thin ffl bar-shaped cross-section in (to move the foot forward) -:, :g). ing.

この上;) i;購逍を(+’ 4’るゲスト除去装置
であると、1i1気集j1)i器1に接続されている高
電圧供給系2か連転状態とナー)でいるときに、オフカ
ス供給系:うど凝:宿器・1とを作動さU−ると、オフ
カスの中にt長大している凝縮可能な成分、つまり水蒸
気、\OX″S−の液化成分か、冷却凝縮によって液化
してタストを核としたミストとなり、送風機15によっ
てF部ケーノノグIOから、線状極7と集塵電極8との
間に送り込まれろ。このため、ミストが、放電主峰のコ
ロナ放電現象によってイオン化され、集塵TL極8の表
面に移動されろ。そして、集塵電極8上の各ミストが水
滴状から大きくなり、次いて自重により流れ落らるもの
である。このとき、ミストはし)イつゆろイオノ物質で
あるlこめに、イオン化雰囲気に才、けるミストの取り
込みか1式発に行なイつれ、取り込まれたミストは下部
ケーシング10に集められた後、排水ライン16から第
1図矢印で示すように排出処理される乙のである。
On top of this ;) i; When the high voltage supply system 2 connected to the i device 1 is in continuous operation and the guest removal device is (+'4') When the off-cass supply system: udo condensation: storage unit 1 is activated, the condensable component that is long in the off-cass, that is, water vapor, the liquefied component of \OX''S-, is cooled and condensed. The mist is liquefied and becomes a mist with Tast as the core, and is sent from the F section Kenonog IO to between the linear pole 7 and the dust collection electrode 8 by the blower 15. Therefore, the mist is caused by the corona discharge phenomenon of the main discharge peak. The mist is ionized and moved to the surface of the dust collection TL electrode 8.Then, each mist on the dust collection electrode 8 becomes larger from a water droplet shape, and then flows down due to its own weight. ) When the mist that is absorbed into the ionized atmosphere is absorbed into the ionized atmosphere, the captured mist is collected in the lower casing 10 and then drained from the drainage line 16 to the drain line 16. As shown by the arrow in Figure 1, the waste is discharged and processed.

しノこか−・て、捕集されたミストは自重によって絶え
ず流されて、イオン化雰囲気から排除されろfこめ、ミ
スト及びその核となっているゲス1、かj1% ’I)
昇電極8に堆積」′ろ現象が発生しにくくなる5、なお
、流水膜用給水系5か作動している場合は、集塵電極8
の内面に流水膜か形成されて、イオン化し、こミストを
下方へ流して集塵電極8の表面へのミスト堆積を防止す
ることになる。
The collected mist is constantly swept away by its own weight and removed from the ionized atmosphere.
5. If the water supply system 5 for the flowing water film is in operation, the dust collection electrode 8
A running water film is formed on the inner surface of the dust collection electrode 8, which ionizes and causes the mist to flow downward, thereby preventing the mist from accumulating on the surface of the dust collecting electrode 8.

また、凝縮器4によるミスト化について補足説明すると
、オフカスの中の液体成分か少ないような場合は、水、
に気供給系6を作動さU−て、オフガスと水蒸気とを混
合した状態て凝縮器4に送1−)、ミストの発生を安定
させる。この場合にオフカス(jミストの搬送流体とな
る。なお、オフカスとミストとを混合状態で電気集塵器
1の中へ送り込んてやろと、イオン雰囲気中てミストの
イオン化が(足進さイ1、集塵電極8及び流水膜\の移
動性が向1−すると七乙に、逸電離現象や再飛散現象の
発生原因が消滅するしのである。
In addition, to provide a supplementary explanation about the mist formation by the condenser 4, if there are few liquid components in the off-scrap, water,
Then, the air supply system 6 is activated, and the mixed off-gas and water vapor are sent to the condenser 4 (1-) to stabilize the generation of mist. In this case, it becomes the carrier fluid for the off-scrap (J mist).In addition, if the off-scrap and the mist are sent into the electrostatic precipitator 1 in a mixed state, the ionization of the mist in the ion atmosphere (step speed 1 When the mobility of the dust collection electrode 8 and the flowing water film is in the 1-direction, the cause of the de-ionization phenomenon and the re-scattering phenomenon disappears.

さらに、これら装置の性能の低下等は、微粒子計測器1
8を作動さU−てオフガス供給系3と排気系I7とのカ
ス分析を実施喝るごとにより、任は時に点検il−ろこ
とが可能である。
Furthermore, the performance of these devices may deteriorate due to the particle counter 1.
Each time the off-gas supply system 3 and the exhaust system I7 are operated by operating the off-gas supply system 3 and the exhaust system I7, inspection can be carried out from time to time.

j′′実験例」 1u気集[m4の集塵電極の内径が30cmであるもの
について、その内部にミスト等を送り込み、第2図に示
すように、ミスト等の#i i’kを変数としたときの
除染計数を求めた。
j′′Experimental Example” For a 1u air collection [m4 dust collection electrode with an inner diameter of 30 cm, mist, etc. is sent into it, and as shown in Figure 2, #i i'k of the mist, etc. is set as a variable. The decontamination count was calculated when

fこたし、印加電圧は751<V及び45KV(平均電
界強度換算で5KV/cm及び3KV/(m)、カス線
速度は1.Om/秒、流水膜を形成している’k 、’
Jaは0.5m”7時である。なお、集塵電極の表面状
態を一定とするために、流水膜を形成した状態としたも
のを採用した。また、流水膜を形成しノこ状態にあって
は、電界強度を高めてら放電現象校びイ」ン化t1)−
了の(ρ動性か安定」ろことを知見しl二。このため、
第2図の電V?、強度5 K\’ / cmは、従゛千
′、技91.1と比・咬してかムり高めである。
In this case, the applied voltage was 751<V and 45KV (5KV/cm and 3KV/(m) in terms of average electric field strength, the scrap line velocity was 1.Om/sec, and a flowing water film was formed.
Ja is 0.5 m" 7 o'clock. In order to keep the surface condition of the dust collecting electrode constant, a running water film was formed. In addition, a running water film was formed on the dust collecting electrode. If the electric field strength is increased, the discharge phenomenon can be canceled out.
I found out that the final result is (ρ-dynamic or stable).For this reason,
Electric V in Figure 2? The strength of 5 K\'/cm is considerably higher than that of 91.1.

ごのよう?J、第2図の結果から、次のごとが明らかで
ある。特に、ザブミク〔l)中位の微粒子にk[して除
J:性能か高く、0.1以Fの微粒子に、rjいてはダ
ス+−r+s独のときと比較して、2桁あるいはそれ以
上の除去効果かある。電界強度か5 K V 、、・′
cm以」−の場合、除+:係数10”と−う好結果かH
l、Hられる。
How are you? J. From the results shown in Figure 2, the following is clear. In particular, for medium fine particles, divided by k[J: high performance, for fine particles of 0.1 F or less, rj is two orders of magnitude or more compared to das + - r + s. There is a removal effect above. The electric field strength is 5 KV,...'
If the value is less than cm, the division +: coefficient 10” is a good result.
l, H is done.

「発明の効果」 以り説明したように、本発明のタスト除去装置によれば
、次のような優れたり戸Uを奏・1゛ることかできる。
"Effects of the Invention" As explained above, according to the dust removal device of the present invention, the following excellent effects can be achieved.

■オフガス中に水分等の液化1戊分か7えまれでいるこ
とをl’ll用して、この液化成分を、欠陥させてダス
トを核としてミスト化し、1亥ミストをtli気集Jl
イ;;に送り込む乙のて◇うろj二め、微粒1−をミス
ト化して小粒径のらのを少なく士ろことかでき、’l’
7.g除去効率を向トさ1」−ろごとができろ、■ミス
ト化することにより、ミストのイオン化を促進さ且゛ろ
ことがてき、集塵電極への移動性を高めろことかできる
■Using the presence of liquefied moisture, etc. in the off-gas, this liquefied component is defected and turned into a mist with dust as the nucleus, and the 1000 mist is collected.
Second, fine particles 1- can be made into a mist to reduce the amount of small particles.
7. (1) Improving the removal efficiency; (2) By turning the mist into a mist, the ionization of the mist can be promoted, and the mobility to the dust collecting electrode can be increased.

■、二!−ら■伎び■によりザブミクロン単位の微粒子
に対Σ1−ろ除去効率を飛躍的に高めることがてき′(
3) 2(5H4μ市極−にのミストは、次第に成長し
て自重によ:つ流士するのて、集塵電極の表面を更新し
て微is< 1 、、’)堆積現象の発生を抑制するこ
とができる。
■、Two! The removal efficiency of the Σ1-filter for fine particles in the micron scale can be dramatically increased by
3) The mist of 2 (5H4μ city pole) gradually grows due to its own weight, renews the surface of the dust collection electrode and prevents the occurrence of a deposition phenomenon. Can be suppressed.

、’S riJ記により、一定したコロナ枚重をイイ(
7持するととしに、処理カス流速を高め、高能率化を達
成オろことができるととしに、電気集塵器内のスパーク
の発生を防止し、安定した運転をすることができる。
, according to 'SriJ, a constant coronal sheet weight is required (
In addition to increasing the flow rate of treated waste and achieving high efficiency, it is also possible to prevent sparks from occurring within the electrostatic precipitator and to ensure stable operation.

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

第1図は本発明のゲスト除去装置の一実施例を示す正断
面図、第2図はダスト状態またはミスト状態と除染係数
との関係曲線図である。 l ・・電気集塵器、2・・・・・高電圧(1!、給糸
、3 ・オフカス供給系、・1  凝縮器、5  流水
膜用給水系、6  水蒸気(」(給糸、7  線状的:
、8  集塵1u極、94一部ケーシング、1o・下j
1]<ケーシング、II  貯ノ1(タンク、12・・
ポンプ、I3  ・リンク状i14、l 1i ・・・
流jIt計、15  トレノライン、16  リ1水ラ
イ〉、17 ・ 排気系、I8  ・微粒子計測2;:
。 出願人  石川島播磨市]、業株式会ト1、第1図 第2図 粒子径(ALm)
FIG. 1 is a front sectional view showing an embodiment of the guest removal device of the present invention, and FIG. 2 is a relationship curve diagram between a dust state or a mist state and a decontamination coefficient. l...Electric precipitator, 2...High voltage (1!, Yarn feeding, 3 Off-scum supply system, 1 Condenser, 5 Water supply system for running water membrane, 6 Water vapor (Yam feeding, 7 Linear:
, 8 dust collection 1u pole, 94 part casing, 1o/lower j
1]<Casing, II Storage 1 (tank, 12...
Pump, I3 ・Linked i14, l 1i...
Flow jIt meter, 15 Trueno line, 16 Li1 water line>, 17 ・Exhaust system, I8 ・Particle measurement 2;:
. Applicant Ishikawajima Harima City], Industry Co., Ltd. 1, Figure 1 Figure 2 Particle size (ALm)

Claims (1)

【特許請求の範囲】[Claims] オフガス中に含まれている液化成分を冷却凝縮してダス
トを核としてミスト化する凝縮器と、直流電圧を印加す
ることにより放電電極の間にコロナ放電を生じさせてイ
オン化雰囲気にするとともに前記凝縮器で発生させたミ
ストをイオン化して集塵電極に移動させて除去する電気
集塵器とを連設したことを特徴とするダスト除去装置。
A condenser that cools and condenses the liquefied components contained in the off-gas to form a mist with dust as the nucleus, and a discharge electrode that generates a corona discharge by applying a DC voltage to create an ionized atmosphere and condense the condensate. A dust removal device characterized in that it is connected to an electric precipitator that ionizes the mist generated by the device and moves it to a dust collection electrode for removal.
JP60185138A 1985-08-23 1985-08-23 Apparatus for removing dust Pending JPS6245355A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60185138A JPS6245355A (en) 1985-08-23 1985-08-23 Apparatus for removing dust

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60185138A JPS6245355A (en) 1985-08-23 1985-08-23 Apparatus for removing dust

Publications (1)

Publication Number Publication Date
JPS6245355A true JPS6245355A (en) 1987-02-27

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP60185138A Pending JPS6245355A (en) 1985-08-23 1985-08-23 Apparatus for removing dust

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JP (1) JPS6245355A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009502457A (en) * 2005-07-28 2009-01-29 コミッサリア ア レネルジ アトミック (セーウーアー) Particle extraction apparatus in air by semi-wet electrostatic collection and method of using the apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009502457A (en) * 2005-07-28 2009-01-29 コミッサリア ア レネルジ アトミック (セーウーアー) Particle extraction apparatus in air by semi-wet electrostatic collection and method of using the apparatus

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