JPH09201510A - Method for wet dust collection and apparatus therefor - Google Patents

Method for wet dust collection and apparatus therefor

Info

Publication number
JPH09201510A
JPH09201510A JP3303196A JP3303196A JPH09201510A JP H09201510 A JPH09201510 A JP H09201510A JP 3303196 A JP3303196 A JP 3303196A JP 3303196 A JP3303196 A JP 3303196A JP H09201510 A JPH09201510 A JP H09201510A
Authority
JP
Japan
Prior art keywords
dust
air
water
filter
mixed solution
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
JP3303196A
Other languages
Japanese (ja)
Inventor
Satoru Satake
覺 佐竹
Tsunehiko Igarashi
恒彦 五十嵐
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.)
IGARASHI SEISAKUSHO KK
Satake Engineering Co Ltd
Original Assignee
IGARASHI SEISAKUSHO KK
Satake Engineering 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 IGARASHI SEISAKUSHO KK, Satake Engineering Co Ltd filed Critical IGARASHI SEISAKUSHO KK
Priority to JP3303196A priority Critical patent/JPH09201510A/en
Publication of JPH09201510A publication Critical patent/JPH09201510A/en
Pending legal-status Critical Current

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  • Separation Of Particles Using Liquids (AREA)

Abstract

PROBLEM TO BE SOLVED: To control the humidity increase in purified air discharged from an air outlet by mixing ethylene glycol into water to be mixed and brought into contact with dust. SOLUTION: Air containing dust is supplied to a dust removing channel 11 and mixed and brought into contact with the mixed solution of fog-shaped water and ethylene glycol while ascending in the channel 11. In this process, relatively heavy dust drops into a liquid tank 2 with the mixed solution. When the dust and the mixed solution pass through a dust removing filter 21 between partition plates 9, 10, most of the dust is removed and most of the mixed solution is adsorbed by the filter 21. By passing through the filter 21 of fine meshes between the partition plate 10 and a side plate 4b, air which passed through the filter 21 and was nearly purified is discharged outside an apparatus as purified air. The dust which dropped into the tank 2 precipitates by its own weight, is transferred by a discharge conveyer 16, and is received by a dust collecting box 18.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、粉塵を含んだ空気に液
体を噴霧した後除塵する湿式集塵方法及び装置に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a wet dust collecting method and apparatus for removing dust after spraying a liquid on air containing dust.

【0002】[0002]

【従来の技術】金属を加工するための装置、特に、切断
装置及び研削装置等には、これら装置から発生する粉塵
を回収するための集塵装置が付設されており、集塵装置
からの排風を作業室の外へ排出する場合には、集塵装置
を作業室の床面等に固設する必要があるとともに、排風
ダクトを作業室の外まで延ばして設ける必要があり、使
い勝手が悪く、また、コストもかかるため、通常は、排
風を作業室内へ排出する集塵装置が用いられている。以
下、図2を参照して集塵装置について説明する。
2. Description of the Related Art A device for processing metal, particularly a cutting device and a grinding device, is provided with a dust collecting device for collecting dust generated from these devices. When exhausting the wind out of the work room, the dust collector must be fixedly installed on the floor of the work room, etc., and the exhaust duct must be extended to the outside of the work room. Since it is bad and costly, a dust collector that discharges the exhaust air into the working chamber is usually used. Hereinafter, the dust collector will be described with reference to FIG.

【0003】符号50は、いわゆる乾式の集塵装置であ
って、複数の通風口55を有する隔壁51を境に、その
下方を集塵室52に、上部を清浄空気室53に形成され
ている。集塵室52には、金属加工装置(図示せず)に
連通する吸塵ダクト54と、フィルター56と、フィル
ター56から落下した粉塵を回収するための回収箱57
とが設けられており、清浄空気室53には、フィルター
56を通った空気を排出する排風口58と、吸引ファン
59と、吸引ファン59を駆動するためのモータ60と
が設けられている。そして、吸引ファンを駆動すること
により、金属加工装置からの粉塵を含んだ空気は、吸塵
ダクト54を介して集塵室52内へ吸引され、フィルタ
ー56によって粉塵が除去された後、通風口55、清浄
空気室53及び排風ダクト58を通って浄化空気として
装置外へ排出されるという作用を生じるものである。
Reference numeral 50 denotes a so-called dry dust collector, which is formed with a partition wall 51 having a plurality of ventilation ports 55 as a boundary, a lower part thereof being a dust collecting chamber 52, and an upper part being a clean air chamber 53. . In the dust collection chamber 52, a dust suction duct 54 that communicates with a metal processing device (not shown), a filter 56, and a collection box 57 for collecting dust that has fallen from the filter 56.
The clean air chamber 53 is provided with an exhaust port 58 for discharging the air that has passed through the filter 56, a suction fan 59, and a motor 60 for driving the suction fan 59. Then, by driving the suction fan, the air containing dust from the metal working device is sucked into the dust collecting chamber 52 through the dust suction duct 54, and after the dust is removed by the filter 56, the ventilation port 55 is provided. The purified air is discharged to the outside of the apparatus through the clean air chamber 53 and the exhaust duct 58 as purified air.

【0004】ところが、金属の切断装置から発生する粉
塵中には、切断作業に伴い生じる火花(非常に高温の金
属粉)が含まれているため、上記集塵装置の集塵室に火
花が吸引された場合、フィルターの破損又は集塵室内で
火災が発生するという危険性があり、また、金属アルミ
等の微粉を集塵した後に、鉄の切断により発生した粉塵
を集塵した場合には、粉塵爆発を起こす危険性があると
いう問題点があった。
However, since the dust generated from the metal cutting device contains sparks (very high temperature metal powder) generated by the cutting work, the sparks are sucked into the dust collecting chamber of the dust collecting device. If there is a risk that the filter will be damaged or a fire will occur in the dust collection chamber, and if the dust generated by cutting the iron is collected after collecting the fine powder such as metal aluminum, There was a problem that there was a risk of causing a dust explosion.

【0005】一方、上記問題点を解決できる装置とし
て、粉塵に水を噴霧した後、除塵する、いわゆる湿式集
塵装置があるが、作業室内に湿式集塵装置からの清浄空
気を排出した場合には、装置内での水の蒸発により装置
内湿度が上昇しているため、排風口から排出される清浄
空気は高湿度の空気となり、作業室内の湿度を上昇させ
作業室内の環境を不快なものとするとともに、周囲の機
器等に悪影響を及ぼすという問題点があり、この問題点
を解決するためには、湿式集塵装置に調湿装置等を付設
しなければならなかった。
On the other hand, as a device capable of solving the above-mentioned problems, there is a so-called wet dust collecting device which removes dust after spraying water on the dust. Since the humidity inside the equipment is rising due to the evaporation of water inside the equipment, the clean air discharged from the exhaust port becomes high humidity air, which raises the humidity inside the work room and makes the environment inside the work room unpleasant. In addition, there is a problem that it adversely affects peripheral devices and the like, and in order to solve this problem, it was necessary to attach a humidity control device or the like to the wet dust collector.

【0006】[0006]

【発明が解決しようとする課題】本発明は上記問題点に
かんがみ、湿式集塵装置内の湿度上昇を抑えることによ
り、調湿装置等を付設することなく、排風口から排出さ
れる清浄空気の湿度上昇を抑制することができる湿式集
塵方法及び装置を提供することを技術的課題とする。
SUMMARY OF THE INVENTION In view of the above problems, the present invention suppresses an increase in humidity in a wet dust collector so that clean air exhausted from an exhaust port can be provided without attaching a humidity controller or the like. A technical object is to provide a wet dust collecting method and apparatus capable of suppressing an increase in humidity.

【0007】[0007]

【課題を解決するための手段】本発明は上記課題を解決
するため、粉塵と混合接触させる水にエチレングリコー
ルを混合する。
In order to solve the above-mentioned problems, the present invention mixes ethylene glycol with water to be mixed and contacted with dust.

【0008】また、粉塵を含む空気に水を噴霧して、粉
塵と水とを混合接触させる噴霧ノズルから、前記水にエ
チレングリコールを混合した混合溶液を噴霧する、とい
う技術的手段を講じた。
[0008] Further, technical means has been taken in which water is sprayed on air containing dust, and a mixed solution of ethylene glycol is sprayed on the water from a spray nozzle for mixing and contacting the dust and water.

【0009】[0009]

【作用及び効果】エチレングリコールは水に比べ沸点及
び粘度が高いため、エチレングリコールと水との混合溶
液は水に比べ沸点及び粘度が高い溶液となり、沸点が高
いことから混合溶液の蒸発性は低下する。また、粘度が
高いことから、水を噴霧した場合に比べ液滴の粒径が大
きくなり、空気中に滞留する時間が短くなるとともに、
単位容量当たりの表面積が小さくなるために蒸発速度が
低下する。このように、エチレングリコールと水との混
合溶液は水と比べ、蒸発性及び蒸発速度が低下するた
め、粉塵を含む空気に混合溶液を噴霧して、粉塵と混合
溶液を混合接触させた場合でも、前記空気の湿度上昇を
抑えることができ、したがって、調質装置等を付設する
ことなく排風口から排出される清浄空気の湿度上昇を抑
制することができる。
[Action and effect] Since ethylene glycol has a higher boiling point and viscosity than water, the mixed solution of ethylene glycol and water has a higher boiling point and viscosity than water, and the higher boiling point lowers the evaporation of the mixed solution. To do. Moreover, since the viscosity is high, the particle size of the droplets is larger than when water is sprayed, and the time to stay in the air is shortened,
Since the surface area per unit volume is small, the evaporation rate is low. As described above, since the mixed solution of ethylene glycol and water has a lower evaporation rate and evaporation rate than water, even when the mixed solution is sprayed on air containing dust and mixed contact is made with the dust. The increase in humidity of the air can be suppressed, and therefore, the increase in humidity of the clean air discharged from the exhaust port can be suppressed without attaching a heat treatment device or the like.

【0010】[0010]

【実施例】本発明の実施例を図面を参照しながら説明す
る。図1は本発明の湿式集塵装置の側断面図である。符
号1は湿式集塵装置であり、下部を噴霧用の液体を溜め
る液槽2に形成し、液槽2上方を集塵室3に形成する。
前記噴霧用の液体は、水と、通常、液冷式内燃機関用冷
却水の凍結防止及び冷却機構の防食に用いられる、エチ
レングリコールを主成分とするいわゆる不凍液との混合
溶液である。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described with reference to the drawings. FIG. 1 is a side sectional view of the wet dust collector of the present invention. Reference numeral 1 denotes a wet dust collector, the lower part of which is formed as a liquid tank 2 for storing a liquid for spraying, and the upper part of the liquid tank 2 is formed as a dust collecting chamber 3.
The spraying liquid is a mixed solution of water and a so-called antifreeze solution containing ethylene glycol as a main component, which is generally used for freeze prevention of cooling water for a liquid-cooled internal combustion engine and corrosion protection of a cooling mechanism.

【0011】集塵室3の一側板4a下部には吸風口5を
開口するとともに、吸風口5には、粉塵発生源、例えば
金属切断装置(図示せず)等と連通する吸塵ダクト6を
接続し、集塵室3の他側板4b側の天板7には排風口8
を開口し、排風口8には吸引ファン19の吸込口20を
接続する。集塵室3の側板4a側には、前記液体の液面
下から天板7近傍に至る仕切板9を設けるとともに、側
板4b側には、天板7から液槽2近傍に至る仕切板10
を設けることにより、集塵室3を粉塵を含む空気を流通
させるための除塵流路11に形成する。仕切板9と仕切
板10との間の除塵流路11には除塵用フィルター21
を配設し、仕切板10と側板4bとの間の除塵流路11
には、前記除塵フィルター21の目よりも目の細かい除
塵用フィルター22を配設する。そして、吸風口5から
除塵フィルター21までの間の除塵流路11に複数の噴
霧ノズル12を配設する。
An air suction port 5 is opened at the lower part of one side plate 4a of the dust collection chamber 3, and a dust suction duct 6 communicating with a dust generation source such as a metal cutting device (not shown) is connected to the air suction port 5. However, the exhaust port 8 is provided on the top plate 7 on the other side plate 4b side of the dust collection chamber 3.
And the suction port 20 of the suction fan 19 is connected to the exhaust port 8. A partition plate 9 extending from below the liquid surface of the liquid to the vicinity of the top plate 7 is provided on the side plate 4a side of the dust collecting chamber 3, and a partition plate 10 extending from the top plate 7 to the vicinity of the liquid tank 2 is provided on the side plate 4b side.
By providing the above, the dust collection chamber 3 is formed in the dust removal channel 11 for circulating the air containing dust. A dust removal filter 21 is provided in the dust removal passage 11 between the partition plates 9 and 10.
And a dust removal channel 11 between the partition plate 10 and the side plate 4b.
Is provided with a dust removing filter 22 having a finer mesh than the dust removing filter 21. Then, a plurality of spray nozzles 12 are arranged in the dust removal flow path 11 between the air suction port 5 and the dust removal filter 21.

【0012】液槽2内には吸液管13を挿通し、この吸
液管13はポンプ14を介して噴霧ノズル12の給液管
15に連絡する。液槽2の底部には、沈殿した粉塵を装
置外へ搬送する排出コンベア16を横設し、排出コンベ
ア16の落下樋17の下方に粉塵収容箱18を設置す
る。
A liquid suction pipe 13 is inserted into the liquid tank 2, and the liquid suction pipe 13 communicates with a liquid supply pipe 15 of the spray nozzle 12 via a pump 14. At the bottom of the liquid tank 2, a discharge conveyor 16 that conveys the precipitated dust to the outside of the apparatus is installed horizontally, and a dust storage box 18 is installed below the drop gutter 17 of the discharge conveyor 16.

【0013】次に上記構成における作用について説明す
る。
Next, the operation of the above configuration will be described.

【0014】ポンプ14を起動すると、液槽2の混合溶
液は吸液管13から給液管15を介して噴霧ノズル12
へ供給され、吸風口5から除塵フィルター21までの除
塵流路11に噴霧される。
When the pump 14 is started, the mixed solution in the liquid tank 2 is sprayed from the liquid suction pipe 13 through the liquid supply pipe 15 to the spray nozzle 12
Is supplied to the dust removal passage 11 from the air suction port 5 to the dust removal filter 21 and is sprayed.

【0015】吸引ファン19の駆動により、粉塵発生源
からの粉塵を含む空気は、吸塵ダクト6を経て吸風口5
から側板4aと仕切板9との間の除塵流路11に供給さ
れ、この除塵流路11を上昇しながら空気中の粉塵は霧
状の前記混合溶液と混合接触される。このとき、比較的
重たい粉塵は混合溶液と共に液槽2に落下する。そし
て、粉塵及び混合溶液が仕切板9と仕切板10との間の
除塵フィルター21を通過するとき、粉塵はほぼ除去さ
れるとともに、混合溶液も除塵フィルター21にほぼ吸
着される。そして、除塵フィルター21を通過後のほぼ
清浄化された空気は、仕切板10と側板4bとの間の目
の細かい除塵フィルター22を通過することにより、一
部の微小な粉塵及び混合溶液が除去され、清浄空気とし
て排風口8及び吸引ファン19の吸込口20を経て装置
外へ排出される。除塵フィルター21、22に吸着され
た混合溶液は雫となり、一部の粉塵を含んで除塵フィル
ター21、22から液槽2へ落下する。
By driving the suction fan 19, the air containing dust from the dust generating source passes through the dust suction duct 6 and the suction port 5
Is supplied to the dust removal passage 11 between the side plate 4a and the partition plate 9, and the dust in the air is mixed and brought into contact with the atomized mixed solution while rising in the dust removal passage 11. At this time, the relatively heavy dust falls into the liquid tank 2 together with the mixed solution. When the dust and the mixed solution pass through the dust removing filter 21 between the partition plate 9 and the partition plate 10, the dust is almost removed and the mixed solution is almost adsorbed by the dust removing filter 21. Then, the substantially purified air that has passed through the dust removal filter 21 passes through the fine dust removal filter 22 between the partition plate 10 and the side plate 4b, so that some fine dust and mixed solution are removed. Then, the clean air is discharged to the outside of the apparatus through the exhaust port 8 and the suction port 20 of the suction fan 19. The mixed solution adsorbed on the dust removing filters 21 and 22 becomes a drop, and a part of dust is included and drops from the dust removing filters 21 and 22 into the liquid tank 2.

【0016】液槽2へ落下した粉塵は自重により沈降
し、沈降した粉塵は排出コンベア16により搬送され、
落下樋17から放出されて粉塵収容箱18に収容され
る。また、混合溶液は、ポンプ14により噴霧ノズル1
2に供給されて循環再利用される。
The dust that has fallen into the liquid tank 2 is settled by its own weight, and the settled dust is conveyed by the discharge conveyor 16,
It is discharged from the drop gutter 17 and stored in the dust storage box 18. In addition, the mixed solution is supplied by the pump 14 to the spray nozzle 1
It is supplied to No. 2 and recycled.

【0017】なお、本実施例の湿式集塵装置の吸風口及
び排風口に湿度計を取り付け、噴霧用の液体として水と
市販の不凍液との混合溶液を用いた場合と、水を用いた
場合との湿度上昇の測定を行った結果、水を用いた場合
には、吸風と排風との湿度差が約10%あるのに対し、
混合溶液を用いた場合には湿度差は2〜3%であった。
Incidentally, hygrometers were attached to the air intake port and the air exhaust port of the wet dust collector of this embodiment, and a mixed solution of water and a commercially available antifreeze was used as the liquid for spraying, and the case of using water. As a result of measuring the increase in humidity with water, when water is used, the difference in humidity between the intake air and the exhaust air is about 10%.
When the mixed solution was used, the humidity difference was 2-3%.

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

【図1】本発明の湿式集塵装置の側断面図である。FIG. 1 is a side sectional view of a wet dust collector of the present invention.

【図2】従来の乾式集塵装置の側断面図である。FIG. 2 is a side sectional view of a conventional dry dust collector.

【符号の説明】[Explanation of symbols]

1 湿式集塵装置 2 液槽 3 集塵室 4 側板 5 吸風口 6 吸塵ダクト 7 天板 8 排風口 9 仕切板 10 仕切板 11 除塵流路 12 噴霧ノズル 13 吸液管 14 ポンプ 15 給液管 16 排出コンベア 17 落下樋 18 粉塵収容箱 19 吸引ファン 20 吸込口 21 除塵フィルター 22 除塵フィルター 1 Wet Dust Collection Device 2 Liquid Tank 3 Dust Collection Chamber 4 Side Plate 5 Air Suction Port 6 Dust Collection Duct 7 Top Plate 8 Exhaust Vent 9 Partition Plate 10 Partition Plate 11 Dust Removal Flow Path 12 Spray Nozzle 13 Liquid Suction Pipe 14 Pump 15 Liquid Supply Pipe 16 Discharge conveyor 17 Drop trough 18 Dust storage box 19 Suction fan 20 Suction port 21 Dust removal filter 22 Dust removal filter

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 粉塵を含む空気に水を噴霧して、粉塵と
水とを混合接触させた後、前記空気中から粉塵を除去す
る湿式集塵方法において、前記水にエチレングリコール
を混合したことを特徴とする湿式集塵方法。
1. A wet dust collecting method in which water is sprayed on air containing dust to bring the dust and water into mixed contact, and then the dust is removed from the air, wherein ethylene glycol is mixed with the water. Wet dust collecting method characterized by the following.
【請求項2】 粉塵を含む空気を取り入れる吸風口と、
前記空気に水を噴霧して、前記粉塵と水とを混合接触さ
せる噴霧ノズルと、水噴霧後の前記空気から粉塵を除去
する粉塵フィルターと、該除塵フィルターにより清浄化
された空気を排出する排風口とからなる湿式集塵装置に
おいて、前記噴霧ノズルには、前記水にエチレングリコ
ールを混合した混合溶液を供給することを特徴とする湿
式集塵装置。
2. An air intake for taking in air containing dust,
A spray nozzle that sprays water into the air to mix and contact the dust and water, a dust filter that removes dust from the air after water spraying, and an exhaust that discharges the air cleaned by the dust filter. A wet dust collecting apparatus comprising a wind nozzle, wherein the spray nozzle is supplied with a mixed solution of the water and ethylene glycol.
JP3303196A 1996-01-25 1996-01-25 Method for wet dust collection and apparatus therefor Pending JPH09201510A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3303196A JPH09201510A (en) 1996-01-25 1996-01-25 Method for wet dust collection and apparatus therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3303196A JPH09201510A (en) 1996-01-25 1996-01-25 Method for wet dust collection and apparatus therefor

Publications (1)

Publication Number Publication Date
JPH09201510A true JPH09201510A (en) 1997-08-05

Family

ID=12375433

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3303196A Pending JPH09201510A (en) 1996-01-25 1996-01-25 Method for wet dust collection and apparatus therefor

Country Status (1)

Country Link
JP (1) JPH09201510A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20130040373A1 (en) * 2008-06-04 2013-02-14 Greg Weatherman Composition and method for dust suppression wetting agent
KR101457421B1 (en) * 2013-03-18 2014-11-03 주식회사 한성더스트킹 Wet type dust collector system for collecting and exhausting dust
JP2015003296A (en) * 2013-06-20 2015-01-08 アマノ株式会社 Dust collector
CN105194955A (en) * 2015-09-16 2015-12-30 武汉工程大学 High-pressure fine water mist dust removal equipment
US20160089625A1 (en) * 2008-06-04 2016-03-31 Cashmir Composition and method of dust suppression wetting agents

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20130040373A1 (en) * 2008-06-04 2013-02-14 Greg Weatherman Composition and method for dust suppression wetting agent
US9149754B2 (en) * 2008-06-04 2015-10-06 Cashmir Composition and method for dust suppression wetting agent
US20160089625A1 (en) * 2008-06-04 2016-03-31 Cashmir Composition and method of dust suppression wetting agents
US9694309B2 (en) * 2008-06-04 2017-07-04 Cashmir Composition and method of dust suppression wetting agents
KR101457421B1 (en) * 2013-03-18 2014-11-03 주식회사 한성더스트킹 Wet type dust collector system for collecting and exhausting dust
JP2015003296A (en) * 2013-06-20 2015-01-08 アマノ株式会社 Dust collector
CN105194955A (en) * 2015-09-16 2015-12-30 武汉工程大学 High-pressure fine water mist dust removal equipment

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