JPS6283019A - Dust collector - Google Patents

Dust collector

Info

Publication number
JPS6283019A
JPS6283019A JP60225461A JP22546185A JPS6283019A JP S6283019 A JPS6283019 A JP S6283019A JP 60225461 A JP60225461 A JP 60225461A JP 22546185 A JP22546185 A JP 22546185A JP S6283019 A JPS6283019 A JP S6283019A
Authority
JP
Japan
Prior art keywords
dust
particles
air
case
dust collector
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
JP60225461A
Other languages
Japanese (ja)
Other versions
JPH0757299B2 (en
Inventor
Isao Miyahara
宮原 勇郎
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP22546185A priority Critical patent/JPH0757299B2/en
Publication of JPS6283019A publication Critical patent/JPS6283019A/en
Publication of JPH0757299B2 publication Critical patent/JPH0757299B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Electrostatic Separation (AREA)

Abstract

PURPOSE:To effectively remove fine particles of as small as less than 0.1mum, by sequentially arranging a first dust-collecting means, an ionizing means, a dust particle enlarging means, and a second dust-collecting means in a case. CONSTITUTION:Dust particles larger than 0.1mum in the air introduced through an air inlet port 1a are collected by a first dust-collecting means 3 comprising a filter, electrostatic precipitator, or the like. Dust particles passing through it are ionized by an ionizing means 4, and introduced into a dust enlarging means 5. In the dust enlarging means 5 steam is overcooled and oversaturated since the steam is sprayed from nozzles 513, and cooled water is sprayed from nozzles 523. When dust particles are introduced into the enlarging means 5 in such a condition, water molecules adhere to the dust particles to form fine water drops. The fine water drops are collected and removed by a second dust-collecting means 7 comprising an eliminator 6 and a wet-type electrostatic precipitator.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、空気中の塵、金属イオン等を除去する集塵装
置に関する。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a dust collector that removes dust, metal ions, etc. from the air.

(従来技術) 電子工業、機械工業、化学工業等の分野においては、室
内の空気中の塵や金属イオン等の微粒子を除去する集塵
装置が使用されている。
(Prior Art) In fields such as the electronic industry, mechanical industry, and chemical industry, dust collectors are used to remove fine particles such as dust and metal ions from indoor air.

この集塵装置としては、従来、フィルタ(通常は粒径0
.17zmの微粒子の捕捉率99.9995%のいわゆ
るHEPAフィルタ)を用い、空気が前記フィルタを通
過することにより、空気中の塵や金属イオン等をフィル
タ上に捕捉するものが一般に用いられている。
Conventionally, this dust collector uses a filter (usually a particle size of 0
.. A so-called HEPA filter (17zm, which has a particle capture rate of 99.9995%) is generally used to trap dust, metal ions, etc. in the air by allowing air to pass through the filter.

(発明が解決しようとする問題点) しかしながら、近年は空気中の微粒子のうち、粒径0.
lpm以下のものも除去することができる集塵装置が要
求されており、前記フィルタによる集塵装置では1粒径
0 、 l #Lm以下の微粒子を捕捉することは困難
であった。
(Problems to be Solved by the Invention) However, in recent years, among the fine particles in the air, particle sizes of 0.
There is a demand for a dust collector capable of removing particles of lpm or less, and it has been difficult to capture fine particles with a particle diameter of 0.1 #Lm or less with the dust collector using the filter described above.

(発明の目的) 本発明の目的は、0.1gm以下の微粒子でも有効に捕
捉することができる集塵装置を提供することにある。
(Object of the Invention) An object of the present invention is to provide a dust collector that can effectively capture even fine particles of 0.1 gm or less.

(問題点を解決するための手段) 本発明によれば、空気入口および出口を備えたケースと
、該ケース内に配設された第1の集塵手段と、該第1の
集塵手段の後段に配設され空気中の塵粒子をイオン化す
るイオン化手段と、該イオン化手段の後段に配設された
塵粒子増大手段と、該塵粒子増大手段の後段に配設され
た第2の集塵手段を有する集塵装置が提供される。
(Means for Solving the Problems) According to the present invention, there is provided a case including an air inlet and an air outlet, a first dust collecting means disposed in the case, and a first dust collecting means arranged in the case. Ionization means arranged at a later stage to ionize dust particles in the air, dust particle increasing means arranged at a later stage of the ionizing means, and second dust collecting means arranged at a rear stage of the dust particle increasing means. A dust collector is provided having means.

(作用) ケースの空気入口から導入された空気は、第1の集塵手
段によって粒径の大きな塵粒子が捕捉される。該第1の
集塵手段を通過した微小な塵粒子は、イオン化手段によ
ってイオン化され、塵粒子増大手段を通過する際に、そ
の回りに水分子が結合して微小水滴を生成する。この塵
粒子を凝結核とした微小水滴を第2の集塵手段によって
捕捉することにより1粒径の小さい塵粒子を有効に除去
することができる。
(Function) In the air introduced from the air inlet of the case, large-sized dust particles are captured by the first dust collecting means. The minute dust particles that have passed through the first dust collecting means are ionized by the ionization means, and when passing through the dust particle increasing means, water molecules are bonded around them to form minute water droplets. By capturing microscopic water droplets with the dust particles as condensation nuclei by the second dust collection means, dust particles as small as one particle size can be effectively removed.

(実施例) 以下、本発明を図示の実施例に基づいて具体的に説明す
る。
(Examples) Hereinafter, the present invention will be specifically described based on illustrated examples.

第1図は本発明による集塵装置の一実施例を示す概略構
成図である。同図において、1は集塵装置のケースで、
空気人口1aおよび空気出口1bを備えている。2は該
空気入口11部に配設された送風機で、室内空気をケー
スl内に導入する。
FIG. 1 is a schematic diagram showing an embodiment of a dust collector according to the present invention. In the figure, 1 is the case of the dust collector;
It has an air port 1a and an air outlet 1b. Reference numeral 2 denotes a blower disposed at the air inlet 11, which introduces indoor air into the case l.

3は該送風機2の後段に配設された第1の集塵手段で、
フィルタによる集塵機或は電気集!1機等によって構成
される。4は該第1の集塵手段3の後段に配設され、第
1の集塵手段3を通過した空気中に含まれる微小な塵粒
子をイオン化するイオン化手段で、以下第2図に基づい
て詳述する。同区において、4aは例えばタングステン
の線で構成された電極であり、電源4Cより例えば9K
Vの高電圧が印加され、アース極46との間で不平等電
界を発生せしめる。この放電極4aとアース極4bとの
間を空気が通過するとき(矢印B方向)に、(−)又は
中性の塵粒子自体は(+)に帯電することになる。なお
、すでに(+)に帯電している塵粒子は、その帯電の量
を増す。
3 is a first dust collecting means arranged after the blower 2;
Dust collector or electric collector with filter! Consists of 1 aircraft, etc. Reference numeral 4 denotes an ionization means that is disposed after the first dust collection means 3 and ionizes minute dust particles contained in the air that has passed through the first dust collection means 3. Explain in detail. In the same area, 4a is an electrode made of, for example, a tungsten wire, and is powered by a power source of 9K, for example, from a power source 4C.
A high voltage of V is applied to generate an unequal electric field with the ground pole 46. When air passes between the discharge electrode 4a and the earth electrode 4b (in the direction of arrow B), the dust particles themselves are charged (-) or neutral (+). Note that dust particles that are already (+) charged increase the amount of charge.

なお、該イオン化手段4の放電極4aには(−)の高電
圧を印加してもよいことは言うまでもなく、この場合は
空気中の塵粒子は(−)に帯電される。
It goes without saying that a negative (-) high voltage may be applied to the discharge electrode 4a of the ionization means 4, and in this case, the dust particles in the air are charged (-).

このイオン化手段4の前段に加熱手段を配設し、導入空
気を加熱するようにすれば、イオン化手段4による空気
中の微粒子のイオン化が効果的に行われる。
By disposing a heating means upstream of the ionization means 4 to heat the introduced air, the ionization means 4 can effectively ionize the particles in the air.

5は前記イオン化手段4の後段に配設された塵粒子増大
手段で、ケース1内に水蒸気を供給する水蒸気供給手段
51と、ケース1内を冷却する冷却手段として冷却水を
散布する冷却水散布手段52とからなっている。前記水
蒸気供給手段51は、水の水蒸気を発生させる水蒸気発
生装置511と、該水蒸気発生装置511によって発生
した水蒸気をケースl内に導くパイプ512と、該バイ
ブ512の先端に装着されたスプレーノズル513とか
らなっている。なお、前記水ノに気発生装J511とし
ては1種々のものが考えられ、例えば、水槽中に電気ヒ
ータを配設した装置、超音波振動により水蒸気を発生さ
せる装置、赤外線水蒸気発生装置等がある。前記冷却水
散布手段は水を例えば3°C程度に冷却する冷凍機52
1と、該冷凍機521によって冷却された水をケース1
内に導くパイプ522と、該バイブ522の先端に装着
されたスプレーノズル523とからなっている。なお、
冷却手段として該冷却水散布手段52に代えて冷凍装置
による冷却コイルをケース1内に配設してもよい。
Reference numeral 5 denotes a dust particle increasing means disposed after the ionization means 4, including a water vapor supply means 51 for supplying water vapor into the case 1, and a cooling water spraying means for spraying cooling water as a cooling means for cooling the inside of the case 1. It consists of means 52. The steam supply means 51 includes a steam generator 511 that generates water steam, a pipe 512 that guides the steam generated by the steam generator 511 into the case l, and a spray nozzle 513 attached to the tip of the vibrator 512. It consists of Note that various types of water vapor generation device J511 can be considered, such as a device in which an electric heater is installed in a water tank, a device that generates water vapor by ultrasonic vibration, an infrared steam generation device, etc. . The cooling water distribution means includes a refrigerator 52 that cools water to, for example, about 3°C.
1 and the water cooled by the refrigerator 521 in case 1.
It consists of a pipe 522 that leads inside, and a spray nozzle 523 attached to the tip of the vibrator 522. In addition,
As a cooling means, instead of the cooling water distribution means 52, a cooling coil using a refrigeration device may be disposed inside the case 1.

6は前記塵粒子増大手段5の後段に配設された水切用の
エリミネータで、金属メツシュフィルタ等で構成されて
いる。
Reference numeral 6 denotes an eliminator for draining water disposed downstream of the dust particle increasing means 5, and is composed of a metal mesh filter or the like.

7は該エリミネータ6の後段に配設された第2の集塵手
段で、例えば、湿式平行電極をもつ湿式電気集塵機によ
って構成されている。
Reference numeral 7 denotes a second dust collecting means disposed after the eliminator 6, and is constituted by, for example, a wet electrostatic precipitator having wet parallel electrodes.

なお、図中8はケースlの空気出口ibに必要に応じて
接続される空調装置である。
Note that 8 in the figure is an air conditioner connected to the air outlet ib of the case 1 as necessary.

本実施例による集塵装置は、以−ヒのように構成されて
おり、以下、その作用について説明する。
The dust collector according to this embodiment is constructed as follows, and its operation will be explained below.

送風機2が作動すると、室内の空気はケースlの空気入
口1aから導入され、第1の集塵手段3によって、空気
中に含まれている例えば0.14m以上の大きな粒径の
塵粒子が捕捉される。該第1の集塵手段3を通過した微
小な塵粒子は、イオン化手段4によってイオン化され、
塵粒子増大手段5内に導入される。該塵粒子増大手段5
はケース1内に水蒸気発生手段511によって発生せし
められた水蒸気がパイプ512を通ってスプレーノズル
512から噴霧されるとともに、冷凍機521によって
冷却された木がパイプ522を通ってスプレーノズル5
23から噴霧されるため、水蒸気が過冷却、過飽和の状
態となっている。このようにして、水蒸気が過冷却、過
飽和の状態となっている塵粒子増大手段5内にイオン化
された空気中の塵粒子が導入されると、空気中の微粒子
の回りには水分子が付着して、微粒子を凝結核とした微
小水滴となる。即ち、水蒸気(H20)の分子は水素D
;〔了−2個と酸素原子1個により構成されているが、
第3図に示すように分極している。
When the blower 2 operates, indoor air is introduced from the air inlet 1a of the case l, and the first dust collecting means 3 captures dust particles with a large particle size of, for example, 0.14 m or more contained in the air. be done. The minute dust particles that have passed through the first dust collection means 3 are ionized by the ionization means 4,
The dust particles are introduced into the dust particle increasing means 5. The dust particle increasing means 5
The steam generated by the steam generating means 511 in the case 1 passes through the pipe 512 and is sprayed from the spray nozzle 512, and the wood cooled by the refrigerator 521 passes through the pipe 522 and is sprayed from the spray nozzle 5.
Since the water vapor is sprayed from 23, the water vapor is in a supercooled and supersaturated state. In this way, when ionized dust particles in the air are introduced into the dust particle increasing means 5 where the water vapor is supercooled and supersaturated, water molecules adhere to the particles in the air. As a result, the particles become microscopic water droplets with condensation nuclei. That is, the molecules of water vapor (H20) are hydrogen D
; [Although it is composed of 2 atoms and 1 oxygen atom,
It is polarized as shown in Figure 3.

H20分子はこの両極間の距離が他の分子に比べて非常
に大きく、液体にあってはH2020分子第4図に示す
ように水素結合力で強く引き合う。
The distance between the two poles of the H20 molecule is much larger than that of other molecules, and in a liquid, the H2020 molecule is strongly attracted to each other by hydrogen bonding force, as shown in Figure 4.

塵粒子増大手段5内のH20分子は、第5図(a)、(
b)、(c)に示すように、空気中の(12電又は分極
している微粒子Aに対して強力なり−ロン力で結びつく
、第5図(a)は十に帯准した微粒子Aの回りにH20
分子が結合し、全体としてひとまわり大きな+の微粒子
となる状態を示す、第5図(b)は−に帯電した微粒子
Aの回りにH20分子が結合し、全体としてひとまわり
大きな−の微粒子となる状態を示す。また、第5図(C
)は十と−に分極した微粒子AのまわりにH20分子が
結合し、全体としてひとまわり大きな分極微粒子となる
状態を示す、このように空気中の微粒はO,1sec以
下の時間で水蒸気(H20分子)に囲まれて微小水滴に
成長する。この微小水滴は過冷却、過飽和状態の空気中
にあるため、再蒸発することなく、微粒子を凝結核とし
て成長し、その表面積が増大するため、益々H20分子
の結合力を促進し、更に大きな微小水滴に成長する。そ
して、この微小水滴はスプレーノズル523から噴霧さ
れた冷水の水滴と衝突して捕捉されるか、又は冷水滴と
の温度差による熱吸引力で吸引捕捉されるか、微小水滴
と冷水滴のクーロン力による結合が生じ更に大きな水滴
となる。
The H20 molecules in the dust particle increasing means 5 are as shown in FIG.
As shown in b) and (c), Fig. 5 (a) shows the polarized particles A in the air. Around H20
Figure 5(b) shows a state in which the molecules combine to form a slightly larger positive particle as a whole, with H20 molecules bonding around a negatively charged particle A, resulting in a slightly larger negative particle as a whole. Indicates the state of being. In addition, Fig. 5 (C
) shows a state in which H20 molecules bond around fine particles A polarized to 10 and -, forming a polarized fine particle that is one size larger as a whole.In this way, fine particles in the air absorb water vapor (H20 molecules) and grow into microscopic water droplets. Since these minute water droplets exist in supercooled and supersaturated air, they do not re-evaporate and grow as fine particles as condensation nuclei, increasing their surface area, which further promotes the binding force of H20 molecules, resulting in even larger minute droplets. Grows into a droplet. Then, these minute water droplets collide with the cold water droplets sprayed from the spray nozzle 523 and are captured, or they are attracted and captured by the heat suction force due to the temperature difference between the minute water droplets and the cold water droplets, or the coulomb of the minute water droplets and the cold water droplets is captured. Bonding occurs due to force and becomes an even larger water droplet.

このようにして、空気中の水蒸気は微粒子を凝結核とし
て、微小水滴に生成せしめられ、その粒径が微粒子の1
0倍以上になることが確認されている。従って、例えば
、0.01gm程度の塵粒子であっても0.1#Lm以
上の微小水滴にすることができ、これは十分に従来の集
塵方式で分離できる粒径である。
In this way, the water vapor in the air uses fine particles as condensation nuclei to form minute water droplets, and the particle size is 1/1 of that of the fine particles.
It has been confirmed that the increase is more than 0 times. Therefore, for example, even dust particles of about 0.01 gm can be turned into minute water droplets of 0.1 #Lm or more, which is a particle size that can be sufficiently separated by conventional dust collection methods.

以上のようにして、塵粒子を凝結核として生成された微
小水滴は、エリミネータ6で分離され、該エリミネータ
6で分離されなかった微小水滴は湿式電気集塵機によっ
て構成される第2の集塵手段7で、クーロン力により捕
捉される。
As described above, the minute water droplets generated as dust particles as condensation nuclei are separated by the eliminator 6, and the minute water droplets that are not separated by the eliminator 6 are collected by the second dust collection means 7 constituted by a wet electrostatic precipitator. , and is captured by Coulomb force.

実験によれば、湿式f行゛市極集塵機は、イオン化した
0 、 OIILmの塵粒子を99.999%の効率で
捕捉できるので、本発明の集塵装置に湿式1・行電極束
1!Il1機を用いた場合には、0.001#i。
According to experiments, the wet type f-row city electrode dust collector can capture ionized 0 and OIILm dust particles with an efficiency of 99.999%, so the wet type f-row electrode bundle 1! When using Il1 machine, 0.001#i.

m以1;の塵粒子の捕捉が可能となる。It becomes possible to capture dust particles of m or more.

このようにして、空気中に含まれている塵等の微粒子が
除去された空気は、ケースlの空気出口lbがら空調装
置8に導入され、ここで温度調整されて室内に吐出され
る。
The air from which fine particles such as dust contained in the air have been removed in this manner is introduced into the air conditioner 8 through the air outlet lb of the case 1, where the temperature is adjusted and the air is discharged into the room.

なお、前記実施例によれば、第2の集塵手段として湿式
゛電気集塵機を用いているので、電気集塵機では負荷と
なる塵粒子の電気抵抗値が雰囲気等により変化するため
に集塵能力が低下することによる+Ir飛散の問題も解
消でき、集塵率を安定化することができる。また、前記
実施例によれば、塵粒子増大手段5は水蒸気の過冷却、
過飽和状態を構成し、塵粒子を凝結核とした微小水滴を
生成せしめ、この微小水滴を第2の集塵手段によって捕
捉するようにしたので、クリーンルーム等で問題となる
空間電荷の原因であるイオンの放出がなく、また、空間
電荷を水草気で減少させることができる。
In addition, according to the above embodiment, since a wet electrostatic precipitator is used as the second dust collection means, the dust collection ability of the electrostatic precipitator is limited because the electrical resistance value of dust particles serving as a load changes depending on the atmosphere, etc. The problem of +Ir scattering due to the decrease can also be solved, and the dust collection rate can be stabilized. Further, according to the embodiment, the dust particle increasing means 5 supercools water vapor,
By creating a supersaturated state and generating minute water droplets with dust particles as condensation nuclei, these minute water droplets are captured by the second dust collection means, so that ions, which are the cause of space charges that are a problem in clean rooms, etc. In addition, the space charge can be reduced in aquatic plants.

以−ヒ、本発明を図示の実施例に基づいて説明したが、
本発明は゛実施例に示されたもののみに限定されるもの
ではなく、本発明の主旨の範囲で種々の変形は可能であ
り、これらを本発明の範囲から除外するものではない。
Hereinafter, the present invention has been explained based on the illustrated embodiments, but
The present invention is not limited to only those shown in the examples, but various modifications are possible within the scope of the spirit of the present invention, and these are not excluded from the scope of the present invention.

(発明の効果) 以ト、詳細に説明したように、本発明は空気入口および
出口を備えたケースと、該ケース内に配設された第1の
集塵手段と、該第1の集塵手段の後段に配設され空気中
の塵粒子をイオン化するイオン化手段と、該イオン化手
段の後段に配設された塵粒子増大手段と、該塵粒子増大
手段の後段に配設された第2の集塵手段とによって構成
したので、第1の集塵手段によって粒径の大きな塵粒子
を捕捉し、該第1の集塵手段を通過した微小な塵粒子は
イオン化手段によってイオン化された後、塵粒子増大手
段によってその粒径が増大され、第2の集塵手段によっ
て捕捉されるため、従来の集塵装置では捕捉が困難であ
った0、01gm以下の塵粒子をも確実に捕捉すること
ができる。
(Effects of the Invention) As described in detail below, the present invention includes a case provided with an air inlet and an air outlet, a first dust collection means disposed in the case, and a first dust collection means. an ionizing means arranged after the means to ionize dust particles in the air; a dust particle increasing means arranged after the ionizing means; and a second dust particle increasing means arranged after the dust particle increasing means. Since the first dust collecting means captures dust particles with a large particle size, the fine dust particles that have passed through the first dust collecting means are ionized by the ionization means, and then the dust particles are collected. Since the particle size is increased by the particle enlarging means and captured by the second dust collecting means, it is possible to reliably capture dust particles of 0.01 gm or less, which were difficult to capture with conventional dust collecting devices. can.

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

第1図は本発明による集塵装置の一実施例を示す概略構
成図、第2図は本発明装置に用いるイオン化り段の一実
施例を示す説明図、第3図は水分子の形状を示す説明図
、第4図は水分子間の引力の状y島を示す説明図、第5
図(a)、(b)。 (c)は微粒子と水分子との結合状態を示す説明図であ
る。 ■・・・ケース、2・・・送風機、3・・・第1の集塵
手段、4・・・イオン化手段、5・・・塵粒子増大手段
、51・・・水法気供給手段、52・・・冷却水散布手
段、7・・・第2の集塵手段。
Fig. 1 is a schematic diagram showing an embodiment of the dust collector according to the present invention, Fig. 2 is an explanatory diagram showing an embodiment of the ionization stage used in the apparatus of the present invention, and Fig. 3 shows the shape of water molecules. Figure 4 is an explanatory diagram showing the state of attraction between water molecules, y-island, Figure 5
Figures (a), (b). (c) is an explanatory diagram showing the bonding state between fine particles and water molecules. ■...Case, 2...Blower, 3...First dust collection means, 4...Ionization means, 5...Dust particle increasing means, 51...Water method air supply means, 52 ...Cooling water spraying means, 7...Second dust collection means.

Claims (4)

【特許請求の範囲】[Claims] (1)空気入口および出口を備えたケースと、該ケース
内に配設された第1の集塵手段と、該第1の集塵手段の
後段に配設され空気中の塵粒子をイオン化するイオン化
手段と、該イオン化手段の後段に配設された塵粒子増大
手段と、該塵粒子増大手段の後段に配設された第2の集
塵手段とを有する集塵装置。
(1) A case equipped with an air inlet and an outlet, a first dust collection means disposed within the case, and a case disposed downstream of the first dust collection means to ionize dust particles in the air. A dust collector comprising ionization means, dust particle increasing means disposed downstream of the ionization means, and second dust collecting means disposed subsequent to the dust particle increasing means.
(2)前記塵粒子増大手段は水蒸気供給手段と冷却手段
とからなる特許請求の範囲第(1)項記載の集塵装置。
(2) The dust collector according to claim (1), wherein the dust particle increasing means comprises a water vapor supply means and a cooling means.
(3)前記冷却手段は冷却水散布手段からなる特許請求
の範囲第(2)項記載の集塵装置。
(3) The dust collector according to claim (2), wherein the cooling means comprises a cooling water spraying means.
(4)前記第2の集塵手段は湿式電気集塵機からなる特
許請求の範囲第(1)項記載の集塵装置。
(4) The dust collector according to claim (1), wherein the second dust collector comprises a wet electrostatic precipitator.
JP22546185A 1985-10-09 1985-10-09 Dust collector Expired - Lifetime JPH0757299B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22546185A JPH0757299B2 (en) 1985-10-09 1985-10-09 Dust collector

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22546185A JPH0757299B2 (en) 1985-10-09 1985-10-09 Dust collector

Publications (2)

Publication Number Publication Date
JPS6283019A true JPS6283019A (en) 1987-04-16
JPH0757299B2 JPH0757299B2 (en) 1995-06-21

Family

ID=16829696

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22546185A Expired - Lifetime JPH0757299B2 (en) 1985-10-09 1985-10-09 Dust collector

Country Status (1)

Country Link
JP (1) JPH0757299B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0735325A (en) * 1993-07-26 1995-02-07 Kobe Steel Ltd Gas cooling chamber and waste treatment apparatus having the same
KR100340334B1 (en) * 2000-06-20 2002-06-12 윤종용 System For Purifying Gas
JP2014509249A (en) * 2011-01-12 2014-04-17 アーヴィ・テクノロジーズ・リミテッド Apparatus and method for purifying air from undesirable components and removing such components
CN106694225A (en) * 2016-12-30 2017-05-24 安徽工业大学 Device for removing fine particulate matter of sintering flue gas by pulse corona charge

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53140675A (en) * 1977-05-14 1978-12-07 Hitachi Ltd Filter type dust collecting device
JPS5630455A (en) * 1979-08-20 1981-03-27 Firestone Tire & Rubber Co Thermoplastic elastomer composition and its manufacture

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53140675A (en) * 1977-05-14 1978-12-07 Hitachi Ltd Filter type dust collecting device
JPS5630455A (en) * 1979-08-20 1981-03-27 Firestone Tire & Rubber Co Thermoplastic elastomer composition and its manufacture

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0735325A (en) * 1993-07-26 1995-02-07 Kobe Steel Ltd Gas cooling chamber and waste treatment apparatus having the same
KR100340334B1 (en) * 2000-06-20 2002-06-12 윤종용 System For Purifying Gas
JP2014509249A (en) * 2011-01-12 2014-04-17 アーヴィ・テクノロジーズ・リミテッド Apparatus and method for purifying air from undesirable components and removing such components
CN106694225A (en) * 2016-12-30 2017-05-24 安徽工业大学 Device for removing fine particulate matter of sintering flue gas by pulse corona charge

Also Published As

Publication number Publication date
JPH0757299B2 (en) 1995-06-21

Similar Documents

Publication Publication Date Title
US6926758B2 (en) Electrostatic filter
US2357354A (en) Electrified liquid spray dust precipitator
KR100859840B1 (en) Air cleaning device
US4162144A (en) Method and apparatus for treating electrically charged airborne particles
JPH0398614A (en) Method and apparatus for purification of air, flue gas or the like
JP4897142B2 (en) Method and apparatus for separating substances in the form of particles and / or droplets from a gas stream
KR20150065501A (en) Air cleaner for air conditioner
JPS6283019A (en) Dust collector
CN110124404B (en) Negative ion bag type smoke dust purifier without ash cleaning
US20040226445A1 (en) Air purifier
JP4507405B2 (en) Kitchen exhaust system
US5711788A (en) Dust neutralizing and floculating system
JPS6138644A (en) Dust collector
TW201000211A (en) Wet electrostatic precipitator with condensation-growth chamber
JPH02218412A (en) Production of clean gas
JPH0439367B2 (en)
JP2019503840A (en) System, apparatus, and method for improving turbine operation using electrostatic precipitator
JPH0773684B2 (en) Dehumidifier
JPH039765B2 (en)
JP3108867B2 (en) Electric field-free air cleaning method and apparatus
JPS6138643A (en) Dust collector
KR100812716B1 (en) Gas eliminator for semiconductor facility
JP2009045594A (en) Kitchen ventilator
JP2004337652A (en) Wet electrostatic precipitator
JP3046633U (en) Wet electric precipitator