JPS61178013A - Dust collector - Google Patents

Dust collector

Info

Publication number
JPS61178013A
JPS61178013A JP1959985A JP1959985A JPS61178013A JP S61178013 A JPS61178013 A JP S61178013A JP 1959985 A JP1959985 A JP 1959985A JP 1959985 A JP1959985 A JP 1959985A JP S61178013 A JPS61178013 A JP S61178013A
Authority
JP
Japan
Prior art keywords
air
section
air stream
particles
bubble
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
JP1959985A
Other languages
Japanese (ja)
Inventor
Masuzo Hamamura
浜村 益三
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 JP1959985A priority Critical patent/JPS61178013A/en
Publication of JPS61178013A publication Critical patent/JPS61178013A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To especially collect a large amount of micron-order particles with a particle size of a 0.1mum or less continuously with high efficiency, by allowing a particle-containing air stream guided to a dust collector to successively pass through an air bubble collecting section filled with high pressure air bubbles and a bubble washing section by a pressurized liquid shower. CONSTITUTION:A particle-containing air stream (b) is introduced into an air bubble collecting section A from an air stream suction port 7 to be allowed to pass through a flow channel filled with high pressure air bubbles W. Herein, particles (a) are separated and removed from the air stream (b) with high efficiency by the efficient adsorbing action of the high pressure air bubbles W. The air stream (b) flowed out from the outlet 4 of said section A is further guided to a bubble washing section B and washed with the washing solution injected from pressure showers S so as to block the channel of the air stream (b). Bubbles are burst in this section B and adsorbed particles are separated and removed from the air stream (b) along with the residual particles in the air streams (b) while the air stream (b) is further continuously washed by plural stages of succeeding showers S and exhausted to the open air from an exhaust port 8.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、主として金属微粒子を連続的に。[Detailed description of the invention] (Industrial application field) The present invention mainly uses fine metal particles continuously.

且つ大容量に捕集できる集塵装置に関するもので、更に
詳しくは、粒子径10μ以下のもの、そして特に0.1
μ以下のミクロ粒子の捕集に有効な集塵装置に関する。
It also relates to a dust collector that can collect a large amount of dust, and more specifically, it collects particles with a particle size of 10 μm or less, and especially 0.1 μm or less.
This invention relates to a dust collector that is effective in collecting microparticles smaller than μ.

(従来の技術) 従来より粒子径10μ以上のものは、重力集塵、慣性集
塵、遠心力集塵、洗浄集帳、ろ過集塵、電気集塵等公知
の各種の装置で容易に捕集できるところであるが、10
μ以下のものの捕集に有効な手段としてはスクラツバー
と総称される洗浄集塵、ろ過集塵(バッグ・フィルター
)。
(Prior art) Particles with a diameter of 10 μm or more have been easily collected using various known devices such as gravity dust collection, inertial dust collection, centrifugal dust collection, cleaning collection, filtration dust collection, and electrostatic dust collection. Although it is possible, 10
Effective means for collecting particles smaller than μ are cleaning dust collection, collectively called scrubbers, and filtration dust collection (bags and filters).

そして0.1μ以下のものの捕集には電気集塵(コット
ン/I/)が夫々有効とされている。
Electrostatic precipitators (cotton/I/) are said to be effective for collecting particles of 0.1 μm or less.

(発明が解決しようとする問題点) シカし乍ら、スフラッパーおよびバッグ・フィルターは
設計および操業の良否が捕集効率を大きく左右し、特に
1μ以下は捕集困難となり。
(Problems to be Solved by the Invention) However, the design and operation quality of the flapper and bag filter greatly affect the collection efficiency, and it is particularly difficult to collect particles of 1μ or less.

とくに注意してつくられた装置によらなければならず、
個々の手段について考察してみても、バッグ・フィμタ
ーやス°クラッパ−では特に0.1μ以下のミクロ粒子
の捕集は不可能であシ、又コツ8戸〆は0.1μ以下の
ミクロ粒子の捕集が可能で性能が最も優秀とされるが、
コスト高である上に取扱いが面倒であり、加えてミクロ
粒子が大量に供給される場合には全く有効たシ得ない。
must be performed by equipment that has been constructed with particular care;
Even if we consider the individual methods, it is impossible to collect microparticles of 0.1μ or less with bag filters or scrapers, and the trick 8 is to collect microparticles of 0.1μ or less. It is capable of collecting microparticles and is said to have the best performance.
In addition to being expensive, it is difficult to handle, and in addition, it is not effective at all when microparticles are supplied in large quantities.

 更に取扱われる微粒子によっては、たとえばカーボン
、木材、石炭、あるいはアルミニウム、マグネシウム等
は粒塵爆発の危険性をともない、慎重な操作が要求され
る。
Further, depending on the fine particles to be handled, for example, carbon, wood, coal, aluminum, magnesium, etc., there is a risk of particle dust explosion, and careful handling is required.

本発明は、以上の従来各手段を比較検討し、且つ長年の
研究実験の結果、5μ以上の粗大粒子ははソ完全に捕集
できる上KO01μ以下のミクロ粒子の捕集は、他に類
を見ない高率で連続的に、且つ大量に行える集塵装置を
提供しようとするものである。
The present invention has been developed by comparing and examining each of the conventional means described above, and as a result of many years of research and experimentation, it is possible to completely collect coarse particles of 5μ or more, and to collect microparticles of KO01μ or less, which is unparalleled. The purpose of the present invention is to provide a dust collection device that can perform dust collection continuously at a high rate and in large quantities.

(問題点を解決するための手段) 本発明集塵装置は上記の技術的課題を達成するためK、
浮揚沈澱による手段を採用した。
(Means for solving the problems) In order to achieve the above technical problems, the dust collector of the present invention has K,
A method of flotation and sedimentation was adopted.

即ち更に具体的に述べると、第1図に示すように、集塵
装置に導いた、各種粒子(イ)を含有する、気流(ロ)
を高圧気泡(資)が充満する気泡捕集区画囚にしである
To be more specific, as shown in Figure 1, the airflow (b) containing various particles (b) led to the dust collector.
A bubble collection compartment is filled with high-pressure bubbles.

気泡捕集区画(4)は気流吸入口(7)と出口(4)と
を備えた気密空間に形成すると共に、起泡剤を混入した
水中に、高圧空気を連続的に噴射して高続される気流導
入口(5)と、排気口(8)を備え、これら導入口から
排気口に至る気流通路中に、該気流通路を遮断する如く
に洗浄液をシャワー状に噴射するシャワー装置を適宜散
設けてある。
The air bubble collection section (4) is formed into an airtight space equipped with an air flow inlet (7) and an outlet (4), and high-pressure air is continuously injected into the water mixed with a foaming agent. An appropriate shower device is provided which includes an airflow inlet (5) and an exhaust port (8), and sprays a cleaning liquid in the form of a shower into the airflow path from the inlet to the exhaust port so as to block the airflow path. It is scattered.

以上の構成において気泡捕集区画には気流流れ方向に複
数段に衝突板を設け、慣性集塵を併用することも可能で
あり、泡洗浄区画においてはシャワーとフィμターとを
交互に配してフイt・〃ターによる捕集を併用すること
も可能である。
In the above configuration, collision plates are provided in multiple stages in the air flow direction in the bubble collection section, and it is also possible to use inertial dust collection, and in the bubble cleaning section, showers and filters are arranged alternately. It is also possible to use a combination of collection with a filter.

又気泡捕集区画と泡洗浄区画は二つの密閉槽を一体に接
続したシ、一つの密閉槽を隔壁によって二つの空間に区
画したシする等適宜の手段で形成され、又両区画を連通
させるには槽外のダクトや隔壁を貫通するパイプあるい
は孔等の手段によって行われる。
The bubble collecting section and the foam cleaning section may be formed by any appropriate means, such as connecting two sealed tanks together, or partitioning one sealed tank into two spaces with a partition wall, or by communicating the two compartments. This is carried out by means such as a duct outside the tank or a pipe or hole penetrating the partition wall.

気泡捕集区画に供給される起泡剤は気流の含有粒子によ
って公知の種々のものを採用するが、石ケン液が取扱い
上、コスト等の面で好都合であり、又洗浄液はシャワー
装置から噴射されたものを再度繰返して用いる循環方式
の他、区画外へ排出し常に新しい洗浄液を噴射する手段
も採用でき、洗浄液も必要に応じて水のみであっても良
い。
Various known foaming agents may be used as the foaming agent supplied to the air bubble collection section depending on the particles contained in the air stream, but soap liquid is convenient in terms of handling and cost, and cleaning liquid is sprayed from a shower device. In addition to a circulation system in which the washed cleaning fluid is repeatedly used, a method of discharging the cleaning fluid outside the compartment and always injecting new cleaning fluid can also be adopted, and the cleaning fluid may also be water only if necessary.

高圧気泡を得るにはコンプレッサー等を用いて空気を圧
縮し、これを気泡剤混入液中に配した気泡発生パイプか
ら噴射させるようKしである。
In order to obtain high-pressure bubbles, air is compressed using a compressor or the like, and the air is injected from a bubble generating pipe placed in a liquid containing a foaming agent.

プレッシャーシャワーはギヤポンプ等の加圧ポンプによ
って洗浄液を加圧して散・水パイプから噴射させるよう
にしである。
A pressure shower uses a pressure pump such as a gear pump to pressurize cleaning liquid and spray it from a sprinkler/water pipe.

(作用) 次に本発明集塵装置の作用を説明すると、気泡捕集区画
囚に至る粒子含有気流−)は高圧の気泡(ト)が充満す
る流路を通過する際に、その含有粒子(イ)は粗大、ミ
クロを問わずこの高圧気泡陶の効率の良い吸着作用によ
って高能率で気流から分離・除却される。 そしてこの
気泡捕集区画囚を通過した気流−)は更に泡洗浄区画(
B)へと導かれる。 この時、一部の泡も共に導入され
るが、この一部の泡ともどもに気流はプレッシャーシャ
ワー(S)による洗浄作用を受けて、泡は破泡され吸着
粒子は気流内残留粒子ともども気流から分離・除去され
、更に気流は置換複数段のシャワーによる洗浄作用にさ
らされて後大気中に排出される。 このように気流ρ)
は気泡捕集区呼囚の高圧気泡(ト)並びに泡洗浄区画(
8)でのプレッシャーシャワー(S)に間断なく連続し
てさらされることで、大量の粗大、ミクロ粒子Kが\わ
らずこれが連続的に送り込まれても間断なく発生する高
圧気泡で高能率に吸着し、又!&\倣シャワーで間断な
く洗浄して、従来の各種装置では側底達成することがで
きない高能率の捕集が可能となった。
(Function) Next, the function of the dust collector of the present invention will be explained. When the particle-containing airflow leading to the air bubble collection section passes through a flow path filled with high-pressure air bubbles (g), the particles contained therein ( A), regardless of whether it is coarse or microscopic, is separated and removed from the airflow with high efficiency by the efficient adsorption action of this high-pressure cellular ceramic. The airflow that has passed through this bubble collection section is then further transferred to the bubble cleaning section (
It leads to B). At this time, some bubbles are also introduced, but the airflow together with these bubbles is subjected to the cleaning action of the pressure shower (S), the bubbles are broken, and the adsorbed particles are removed from the airflow together with the particles remaining in the airflow. After being separated and removed, the air stream is further exposed to the cleaning action of a multiple-stage displacement shower and then discharged into the atmosphere. In this way the airflow ρ)
The high-pressure bubbles in the air bubble collection area (g) and the foam cleaning area (
By being continuously exposed to the pressure shower (S) in step 8), a large amount of coarse and micro particles K are adsorbed with high efficiency by the high-pressure bubbles that are generated without interruption even if they are continuously fed. Oh, again! &\Continuous cleaning with a copying shower makes it possible to collect highly efficiently, which cannot be achieved with conventional various devices.

(実施例) 次に本発明集塵装置の実施例を図面に基いて説明する。(Example) Next, an embodiment of the dust collector of the present invention will be described based on the drawings.

(1)は9C密発泡区画囚を形成する気密槽、(2)は
その上方に一体的に結合された泡洗浄区画(8)を形成
する気密槽で、両槽は隔壁(3)により隔絶されている
が、夫々−側壁(1m)、(2m)の上部近くに設けた
左右一対の連通孔(4) 、 (4) 、 (5) 、
 (5)を互いにダクト(6) 、 (6)で接続する
ととくより連通連結される。 (7)は気密発泡槽(1
)の連通孔(4) 、 (4)を設けた側壁(1a)と
は反対側の対向側壁(1b)に形成しである粒子含有気
@呻)吸入口、(8)は泡洗浄槽(2)の連通孔(5)
 、 (5)を設けた側壁(2a)とは反対側の°対向
側壁近くの土壁(2b)に設けた排気口である。 従っ
て気密発泡区画国側の連通孔(4)。
(1) is an airtight tank that forms a 9C dense foam compartment, (2) is an airtight tank that forms a foam cleaning compartment (8) that is integrally connected above it, and both tanks are separated by a partition wall (3). However, there are a pair of left and right communication holes (4), (4), (5), provided near the top of the side walls (1m) and (2m), respectively.
When (5) are connected to each other by ducts (6) and (6), they are particularly communicatively connected. (7) is an airtight foaming tank (1
) is a communication hole (4) formed in the opposite side wall (1b) opposite to the side wall (1a) provided with (4), and is a particle-containing air inlet (8) is a foam cleaning tank ( 2) Communication hole (5)
, (5) is an exhaust port provided in the earthen wall (2b) near the opposite side wall (2a) on the opposite side. Therefore, the communication hole (4) on the country side of the airtight foam compartment.

(4)が該区画囚からの気流出口となり、又泡洗浄区画
+8)側の連通孔(5) 、 (5)が発泡区画(Al
から排出されてこの泡洗浄区画(θ)に吸入される気流
の導入口となる。 前記吸入口(7)には一端を作業現
場のブロアーの排風側に接続された送塵ダクト(9)が
接続されていると共に、排気口(8)にはダクト、αQ
を介して、槽上壁(2b)に据置した、排気装置αηと
してのVロツコファンが接続されている。
(4) is the air outlet from the compartment, and the communication hole (5) on the foam cleaning compartment +8) side is the foam compartment (Al
This serves as an inlet for the airflow discharged from the foam washing section (θ) and sucked into this foam washing section (θ). The suction port (7) is connected to a dust duct (9) whose one end is connected to the exhaust side of a blower at the work site, and the exhaust port (8) is connected to a duct, αQ.
A V-rotsuko fan, which serves as an exhaust device αη and is installed on the upper wall of the tank (2b), is connected through the tank.

吸入口並びに排気口は共に槽左右幅方向の中央部分く設
けられている。
Both the suction port and the exhaust port are located in the center of the tank in the left and right width direction.

そして9IC*発泡11(1)内O1壁(ld)ハ吸入
n(7)側から連通孔(4) ? (4)側に向かうに
従って順次下方へと傾斜した傾斜底壁に形成されている
と共に、連通孔(4) 、 (4)のある−側壁(1鳳
)近くで凹没されて粒子溜(2)が形成され、この粒子
溜り(財)には堆積粒子を槽外へ排出するためのパルプ
を備えた一排水管(2)が接続されている。
And the communication hole (4) from the 9IC* foaming 11 (1) inner O1 wall (ld) and suction n (7) side? (4) It is formed on the sloped bottom wall that slopes downward one after another toward the side, and is recessed near the side wall (1) where the communicating holes (4) and (4) are located. ) is formed, and a drainage pipe (2) equipped with pulp for discharging the accumulated particles out of the tank is connected to this particle reservoir.

気泡発生装置は以下の通り構成される。 即ち、傾斜底
壁(1d)の上方には、傾斜方向に沿っては所定間隔置
きで、槽左右方向全長にはy等しい寸法の気泡発生パイ
プα→・・(図例にては4本)が設けられ、一端は夫々
槽外に突出させて空気供給主管(至)に接続されている
。 この気泡発生パイプα◆・・は管壁に無数の空気噴
出孔を備えている。 空気供給主管(至)には圧力計(
至)とパルプ(15a)とが夫々設けられていて、該主
管端末の供給口(1sb)に図外コンプレッサーからの
圧縮空気供給パイプ(ロ)が接続され、パルプ(15m
)の操作により常時0.8ゆ憎〜0.5−の加圧空気が
主管(至)に供給されるようにしである。
The bubble generator is constructed as follows. That is, above the inclined bottom wall (1d), there are bubble generating pipes α→... (4 pipes in the example) at predetermined intervals along the inclination direction and having dimensions equal to y for the total length in the left and right direction of the tank. are provided, one end of which projects outside the tank and is connected to the main air supply pipe. This bubble generating pipe α◆... is equipped with numerous air ejection holes on the pipe wall. The main air supply pipe (to) has a pressure gauge (
A compressed air supply pipe (b) from a compressor (not shown) is connected to the supply port (1sb) of the main pipe terminal, and a pulp (15 m
) so that pressurized air of 0.8 to 0.5 is always supplied to the main pipe.

発泡槽(1)には水と石ケシ液との混合液が所定量注入
されるものでW、Lは水位面である。 又該発泡槽(1
)には吸入口(7)側から連通孔(4) 、 (4)側
に向かって所定間隔置きに隔壁(3)から衝突板(ト)
・・を垂設しである。 これら衝突板(至)・・は下方
遊端側はど連通孔(4) 、 (4)側に偏位した傾斜
姿勢に形成されていると共に下端縁が吸入口(7)の下
端レベルと同等もしくはより下位にあるように上r寸法
が設定されているが、水位面W、Lよシは上方にあるよ
うに設定されていて、図例にては短、長一対が二組設け
られている。 この衝突板(ト)・・は主として粗大粒
子に対する慣性集塵機能を果たす。 又この衝突板(至
)・・群は丁度気泡発生パイプαQ・・の設置領域に対
向して設けるようにしである。 (IIは給水パルプで
ある。
A predetermined amount of a mixed solution of water and limestone liquid is injected into the foaming tank (1), and W and L are water levels. Also, the foaming tank (1
), from the suction port (7) side to the communication hole (4), and from the bulkhead (3) to the collision plate (T) at predetermined intervals toward the (4) side.
...is installed vertically. These collision plates (towards) are formed in an inclined position with the lower free end side facing the communication hole (4), and the lower end edge is at the same level as the lower end of the suction port (7). Or, the upper r dimension is set to be lower, but the water level W and L are set to be higher, and in the example shown, two pairs of short and long lengths are provided. There is. This collision plate (g) mainly performs an inertial dust collection function for coarse particles. Moreover, this group of collision plates (to) is arranged to be exactly opposite to the installation area of the bubble generating pipe αQ. (II is water pulp.

次に泡洗浄j4(2)には連通孔(5) 、 (5)か
ら排気口(8)に至る気流経路の中間部分に、これを遮
断する状態で複数(図例では三つ)のフィルタ員・・が
気流流れ方向に所定間隔を置いて土壁(2b)から垂設
されている。 又この泡洗浄槽(2)の底壁(2d)も
連通孔(5) 、 (5)側から排出口(8)側に向っ
て順次下位となる傾斜底壁に形成されていると共に、所
定量の水と可性ソーダとを注入するもので、(W、L)
は水位面である。
Next, the foam cleaning j4 (2) has a communication hole (5), and a plurality of filters (three in the example shown) are installed in the middle of the airflow path from the communication hole (5) to the exhaust port (8) in a state that blocks this. members are vertically installed from the earthen wall (2b) at predetermined intervals in the air flow direction. The bottom wall (2d) of this foam cleaning tank (2) is also formed into a sloped bottom wall that becomes lower in order from the communication hole (5) and (5) side toward the discharge port (8) side, It injects a fixed amount of water and possible soda, (W, L)
is the water level.

シャワー装置は以下の通り構成される。 即ち、多数も
しくは無数の散水孔を有する散水バイブe2−11・・
を槽上方で槽左右方向のはソ全長にわたって設ける。 
ツーイルター併用の場合は図示するように各フィルター
の間の上方あるいは各散水パイプ(21)・・は上壁(
2b)上に配した給水主管固く夫々接続し、該主管(ロ
)には土壁上に据置した加圧給水ポンプ日(図例ではギ
アポンプを示す)を接続しである。
The shower equipment is constructed as follows. In other words, the watering vibrator e2-11 has many or countless watering holes.
Provided above the tank and along the entire length of the tank in the left and right direction.
When using a two-filter together, the upper part between each filter or each water pipe (21) is connected to the upper wall (21) as shown in the figure.
2b) The main water supply pipes arranged above are firmly connected to each other, and a pressurized water supply pump (a gear pump is shown in the example shown) installed on the earthen wall is connected to the main pipes (b).

散水パイプe211・・の散水孔はパイプ下局面にパイ
プ軸芯を中心にして左右一対づつ設けられるもので、散
水角は約45°に設定されている。
The water sprinkling holes of the water sprinkling pipe e211... are provided in pairs on the left and right sides around the pipe axis on the lower surface of the pipe, and the water sprinkling angle is set to about 45°.

又(2〜は取水パイプで下端を傾斜底壁(2d)の最下
位部近くに位置させると共に上端は前記給水ポンプ(至
)の取水口に接続して洗浄液(T)を循環させるように
しである。
In addition, (2~ is a water intake pipe whose lower end is located near the lowest part of the inclined bottom wall (2d), and whose upper end is connected to the water intake of the water supply pump (to) to circulate the cleaning liquid (T). be.

図中(24は給水パルプ(社)、(26つは夫々両槽(
1)。
In the figure (24 is Water Supply Pulp Co., Ltd., (26 is both tanks)
1).

(2)に設けた水位計、鰭は泡洗浄槽(2)からのオー
バーフロー水を下方の気密発泡槽(1)へ排出するバイ
パスパイプ、(ハ) (28/)は夫々ハツチ、翰は排
気装置(ロ)の駆動用モータ、−は給水ポンプ瞥の駆動
用モータ、Gυはパルプを備えた排水管、曽はマンホー
μである。 前記フィルタ(1)・・は上下寸法を夫々
異ならしめても良く、すべて同一寸法とし水位面とは!
同等レベルにその下端縁がある上下寸法に設定するのも
良い。
The water level gauge installed in (2), the fin is a bypass pipe that discharges the overflow water from the foam cleaning tank (2) to the airtight foaming tank (1) below, (c) (28/) is the hatch, and the fin is the exhaust. The drive motor for the device (b), - is the drive motor for the water supply pump, Gυ is the drain pipe equipped with pulp, and Z is the manhole μ. The filter (1)... may have different upper and lower dimensions, but all have the same dimensions and the water level is!
It is also good to set the upper and lower dimensions so that the lower edges are at the same level.

次に上記実施例構造の作用を説明する。Next, the operation of the structure of the above embodiment will be explained.

まず両槽(1) 、 (2)に夫々給水パルプ(1呻、
(財)を開いて適宜注水し、その後気密発泡槽(1)に
は石ケン液を、泡洗浄槽(2)には可性ソーダを所定量
注入する。 次にパルプ(15a)を開放して圧縮空気
を空気供給主管(ト)に供給すると共に該バ〃ブ(15
a)によって常時0.8 kVd −0,5#/dの適
宜圧となるように圧力駒部し、この加圧空気を各気泡発
生パイプα→・・に送シ込み噴出孔から混合液中に噴出
させて気泡を発生させ気密発泡槽(2)内に高圧石ケン
泡(転)を充満させる。 又、同時に給水ポンプ(至)
を作動させて吐出圧31の加圧水を給水主管固を介して
各散水パイプシυ・・に送り込み、散水孔より噴射させ
てプレッシャ=、VヤワーtS)・・を形成する。
First, water pulp (1 liter, 1 ounce,
(Incorporated) and pour in water appropriately, then pour a predetermined amount of soap solution into the airtight foaming tank (1) and a predetermined amount of soluble soda into the foam cleaning tank (2). Next, the pulp (15a) is opened to supply compressed air to the main air supply pipe (G), and the valve (15a) is supplied with compressed air.
A) is applied to the pressure piece so that the appropriate pressure is always 0.8 kVd -0.5#/d, and this pressurized air is sent to each bubble generation pipe α→... from the nozzle hole into the mixed liquid. The foam is ejected to generate air bubbles and the airtight foaming tank (2) is filled with high-pressure soap foam. Also, at the same time, the water supply pump (to)
is operated to send pressurized water with a discharge pressure of 31 to each water sprinkling pipe υ... through the main water supply pipe, and injecting it from the water sprinkling holes to form pressure =, V, water tS)....

次に気密発泡$ti (1)内の石ケン泡量が充分(8
梼以上の発泡密度)であることをハツチ−〇ガラス°窓
(28@)で確認した後、現場のプロワ−並びに排気装
置iを作動させ、送塵ダクト(9)よシ粒子含有気流(
ロ)を気密発泡槽(1)内に送り込む。
Next, the amount of soap foam in the airtight foam $ti (1) is sufficient (8
After confirming through the hatch glass window (28@) that the foaming density is higher than the foaming density, the on-site blower and exhaust system are activated, and the dust-containing airflow (
B) is sent into the airtight foaming tank (1).

吸入された気流p)は衝突板(至)に衝突して下方へ向
きを変更されるが粒子、特に粗大粒子は衝突によって自
身の飛しようエネルギーがなくなシ、自重により衝突板
(至)に沿って下方へと落下し気流よシ分離される。 
又この最初の衝突板によって分離されなかったものも後
続の衝突板によシ同様の作用を受は効率良く分離される
とと−なるが、核種(1)内は高圧石ケン泡が充満して
おり、殊に衝突板(至)・・存在領域では水面との間に
形成される気流通路が大きく狭ばめられて過密なまでに
石ケン泡(資)が存在しているために、粗大粒子といわ
ず微粒子、殊に気化金属のの高い率を示し、気化金属の
ミクロ粒子も他に類をみない回収率が期待できる。
The inhaled airflow p) collides with the collision plate (top) and is redirected downward, but particles, especially coarse particles, lose their own energy to fly due to the collision, and due to their own weight they collide with the collision plate (top). It falls downward along the line and is separated by the air current.
In addition, those that were not separated by the first collision plate will be efficiently separated by the same effect by the subsequent collision plates, but the nuclide (1) will be filled with high-pressure soap bubbles. Especially in the area where the collision plate exists, the airflow passage formed between it and the water surface is greatly narrowed and is overcrowded with soap bubbles. It shows a high rate of not only coarse particles but also fine particles, especially vaporized metals, and an unparalleled recovery rate of vaporized metal microparticles can be expected.

尚上記の回収率は、金属溶射現場における粒子含有気体
を対象としたもので、溶射時にアークまたはフレームに
より溶融された金属は噴射気流により0.1μ〜150
μまでの粒子に粉砕されると同時に0.1μ以下のイオ
ンガス化した大量のミクロ粒子が発生し、これらのすべ
てを含有している。
The above recovery rate is for the particle-containing gas at the metal spraying site, and the metal melted by the arc or flame during thermal spraying is 0.1 μ to 150 μm due to the jet air flow.
At the same time as it is crushed into particles up to μ in size, a large amount of ion gasified microparticles of 0.1 μ or less are generated, and it contains all of these microparticles.

気密発泡槽(1)で粒子を分離された気流はダク) (
6) 、 (6)から泡洗浄槽(2)内に吸引されで多
段のフィルター作用とプレッシャーシャワー(S)・・
の洗浄作用とを受けると共に、この吸引気流に乗って該
泡洗浄槽(2)に運ばれて来る一部の泡も共にフィルタ
ー作用と洗浄作用を受けて破泡し、吸着粒子は気流内の
残留粒子ともども9C況から分離されて落下しあるいは
捕集される。 そして粒子が除去されて清浄となった気
流は排出口(8)からダクトαOそして排気装置αηよ
り大気中に排気されるのである。
The airflow from which particles are separated in the airtight foaming tank (1) is
6) The foam is sucked from (6) into the cleaning tank (2) and has a multi-stage filter action and pressure shower (S)...
At the same time, some of the bubbles carried by this suction airflow to the foam washing tank (2) are also subjected to the filtering action and washing action to break the bubbles, and the adsorbed particles are absorbed by the airflow. The remaining particles are separated from the 9C situation and fall or are collected. Then, the airflow, which has been purified by removing particles, is exhausted into the atmosphere from the exhaust port (8) through the duct αO and the exhaust device αη.

尚、気密発泡槽(1)と泡洗浄槽<2)とは上記実施例
構造では上下に並設されるものであったが、必ずしも上
下でおる必要はなく、左右方向に並設したり、タテ−列
状に並設したりすることも可能である。 又左右方向に
並設する場合は通気抵抗等を考慮すると、両槽の連通用
ダク) (6) 。
In addition, although the airtight foaming tank (1) and the foam cleaning tank <2) were installed vertically in parallel in the structure of the above embodiment, they do not necessarily have to be installed vertically. It is also possible to arrange them in a vertical row. Also, if they are installed side by side in the left and right direction, considering ventilation resistance, etc., a duct for communication between both tanks) (6).

(6′)はや−大径の一本とし槽中の中央部に設けるよ
うにするのが好ましい。 この連通用ダク)(6) 、
 (6’)は槽外に配しであるが、隔壁(3)を貫通し
て泡洗浄槽(2)内にパイプを立上げるようにして構成
されても良い。
(6') It is preferable to use one large-diameter tube and place it in the center of the tank. This communication duct) (6),
(6') is disposed outside the tank, but it may be configured such that a pipe penetrates the partition wall (3) and stands up inside the foam cleaning tank (2).

又気泡発生パイプαりは、図示のパイプに限らず、連続
気泡を有する素材で形成される袋体あるいは箱体であっ
ても良1<、且つ袋体1箱体は薄巾偏平でマット状に形
成されたもの等でも良い。
In addition, the bubble generating pipe α is not limited to the illustrated pipe, but may be a bag or a box made of a material having open cells. It may also be formed in the form of

(発明の効果) 本発明集塵装置は、高圧気泡による連続的な吸着による
捕集作用とそれに引続くプレッシャーシャワーの連続的
な洗浄作用とを組合せるととにより、粗大粒子はいう′
までもなく、0.1μ以下のミクロ粒子さえもきわめて
高能率でしかも連続して捕集できるもので、従来のスク
ヲパーー?バッグフィルターに較べて設計並びに操作が
著しく簡単で、特に注意してつくられた装置くよらなけ
ればならないといった技術上の制約を完全に解決できる
hK、廉価に提供できる。
(Effects of the Invention) The dust collector of the present invention combines the continuous adsorption action of high-pressure bubbles with the continuous cleaning action of a pressure shower, thereby removing coarse particles.
Needless to say, it is capable of collecting even microparticles of 0.1μ or less with extremely high efficiency and continuously, unlike conventional scoopers. Compared to bag filters, the design and operation are significantly simpler, and the hK can be provided at a lower cost, completely overcoming technical constraints such as having to rely on carefully constructed equipment.

更に捕集作用は高湿潤雰囲気内で行われるものであるか
ら粉塵爆発の危険性もなく安全に、しかも手軽に取扱え
る。
Furthermore, since the collecting action is carried out in a highly humid atmosphere, there is no risk of dust explosion, and it can be handled safely and easily.

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

第1図は本発明集塵装置の原ニー図、第2図以下第4図
は具体的な実施の構iを”示し、第2図は断面図、第8
図は外面図、第4図は第3図中のY矢印外面図である。 符号説明 (1)−・・・・・気密発泡槽、(2)・・・・・・泡
洗浄槽、(3)・・・・・・隔壁、(4)・・・・・・
出口、(5)・・・・・・導入口、(6)・・・・・・
ダク) 、(7)・−・・・吸入口、(8)・・・・・
・排気口、(9)・・・・・・送塵ダクト、(ロ)・・
・・・・排気装置、α◆・・・・・・気泡発生パイプ、
(16・・・・・・空気供給主管、QB+・・・・・・
衝突板、翰・・・・・・フィルタ、休υ・・・・・・散
水パイプ、翰・・・・・・給水主管、(至)・・・・・
・給水ポンプ、囚・旧・・気泡捕集区画、(B)・・・
・・・泡洗浄区画、(W)・・・・・・気泡、(S)・
・・・・・プレッシャージャワ、(イ)・・・・・・気
流、(ロ)・・・・・・粒子。 出願人        浜  村  益  三代理人 
 弁理士   水  口  孝  −第1 図 凛2図 事3日 第4図
Fig. 1 is an original knee diagram of the dust collector of the present invention, Fig. 2 and Fig. 4 show a concrete implementation configuration, Fig. 2 is a sectional view, and
The figure is an external view, and FIG. 4 is an external view shown by the arrow Y in FIG. 3. Explanation of symbols (1)... Airtight foaming tank, (2)... Foam cleaning tank, (3)... Bulkhead, (4)...
Exit, (5)...Inlet, (6)...
duct), (7)... Intake port, (8)...
・Exhaust port, (9)... Dust duct, (b)...
・・・Exhaust device, α◆・・・Bubble generation pipe,
(16... Main air supply pipe, QB+...
Collision plate, kiln...Filter, hiatus...Water pipe, kiln...Main water supply pipe, (to)...
・Water supply pump, former prisoner, bubble collection section, (B)...
... Foam cleaning section, (W) ... Air bubbles, (S)
...pressure jaws, (a) ...airflow, (b) ...particles. Applicant Masumi Hamamura Agent
Patent Attorney Takashi Mizuguchi - Figure 1 Rin 2 Figure 3 Day 4

Claims (3)

【特許請求の範囲】[Claims] (1)気流吸入口(7)と出口(4)とを備えた気密空
間で形成される気泡捕集区画(A)と前記出口(4)と
接続される気流導入口(5)と排気口(8)を備えた気
密空間で形成される泡洗浄区画(B)とを並設し、気泡
捕集区画には該区画内に注入された起泡剤混入液中に加
圧空気を連続的に噴射して高圧気泡を発生する気泡発生
装置を設け、泡洗浄区画には気流導入口(5)から排気
口(8)に至る気流流路を気流流れ方向に沿つて遮断す
る洗浄液高圧シヤワーを形成するシヤワー装置を設けて
あることを特徴とする集塵装置。
(1) A bubble collection section (A) formed in an airtight space including an airflow inlet (7) and an outlet (4), an airflow inlet (5) and an exhaust port connected to the outlet (4); (8) is installed in parallel with the foam cleaning section (B) formed in an airtight space, and pressurized air is continuously supplied to the foaming agent mixed liquid injected into the bubble collecting section A bubble generator is installed to generate high-pressure bubbles by injecting air into the air, and a cleaning liquid high-pressure shower is installed in the foam cleaning section to block the airflow path from the airflow inlet (5) to the exhaust port (8) along the airflow direction. A dust collector characterized in that it is provided with a shower device for forming dust.
(2)泡洗浄区画(B)内には、気流流路を気流流れ方
向に沿つて複数段に遮断するフイルター(20)・・を
設けてある特許請求の範囲第(1)項記載の集塵装置。
(2) The foam washing section (B) is provided with a filter (20) for blocking the airflow channel in multiple stages along the airflow direction. dust equipment.
(3)気泡捕集区画(A)内には吸入口(7)側から出
口(4)側に向つて所定間置きに衝突板(18)・・を
設けてある特許請求の範囲第(1)項記載の集塵装置。
(3) In the bubble collecting section (A), collision plates (18) are provided at predetermined intervals from the inlet (7) side to the outlet (4) side. ) The dust collector described in section 2.
JP1959985A 1985-02-04 1985-02-04 Dust collector Pending JPS61178013A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1959985A JPS61178013A (en) 1985-02-04 1985-02-04 Dust collector

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1959985A JPS61178013A (en) 1985-02-04 1985-02-04 Dust collector

Publications (1)

Publication Number Publication Date
JPS61178013A true JPS61178013A (en) 1986-08-09

Family

ID=12003685

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1959985A Pending JPS61178013A (en) 1985-02-04 1985-02-04 Dust collector

Country Status (1)

Country Link
JP (1) JPS61178013A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0359017U (en) * 1989-10-06 1991-06-10
JPH0453418U (en) * 1990-09-06 1992-05-07
JPH0567315U (en) * 1992-02-13 1993-09-07 株式会社共和製作所 Element cleaner dust collecting and discharging device
JP2003511217A (en) * 1999-10-07 2003-03-25 ペレテックス インコーポレイテッド Method and apparatus for filtering an air stream containing aqueous foam
US7958652B2 (en) * 2005-01-07 2011-06-14 Bissell Homecare Inc. Extraction cleaning with plenum and air outlets facilitating air flow drying
JP5731692B1 (en) * 2014-06-13 2015-06-10 有限会社ケーエスイー Air cleaning device

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4860070A (en) * 1971-11-30 1973-08-23

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4860070A (en) * 1971-11-30 1973-08-23

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0359017U (en) * 1989-10-06 1991-06-10
JPH0453418U (en) * 1990-09-06 1992-05-07
JPH0567315U (en) * 1992-02-13 1993-09-07 株式会社共和製作所 Element cleaner dust collecting and discharging device
JP2003511217A (en) * 1999-10-07 2003-03-25 ペレテックス インコーポレイテッド Method and apparatus for filtering an air stream containing aqueous foam
US7958652B2 (en) * 2005-01-07 2011-06-14 Bissell Homecare Inc. Extraction cleaning with plenum and air outlets facilitating air flow drying
JP5731692B1 (en) * 2014-06-13 2015-06-10 有限会社ケーエスイー Air cleaning device
JP2016002496A (en) * 2014-06-13 2016-01-12 有限会社ケーエスイー Air washing apparatus

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