JPH01262916A - Dust collecting apparatus - Google Patents

Dust collecting apparatus

Info

Publication number
JPH01262916A
JPH01262916A JP63088809A JP8880988A JPH01262916A JP H01262916 A JPH01262916 A JP H01262916A JP 63088809 A JP63088809 A JP 63088809A JP 8880988 A JP8880988 A JP 8880988A JP H01262916 A JPH01262916 A JP H01262916A
Authority
JP
Japan
Prior art keywords
air
dust collector
dust
air supply
supply mechanism
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
JP63088809A
Other languages
Japanese (ja)
Other versions
JPH0753218B2 (en
Inventor
Ryoichi Hashimoto
良一 橋本
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.)
Nihon Spindle Manufacturing Co Ltd
Original Assignee
Nihon Spindle Manufacturing 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 Nihon Spindle Manufacturing Co Ltd filed Critical Nihon Spindle Manufacturing Co Ltd
Priority to JP63088809A priority Critical patent/JPH0753218B2/en
Publication of JPH01262916A publication Critical patent/JPH01262916A/en
Publication of JPH0753218B2 publication Critical patent/JPH0753218B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Filtering Of Dispersed Particles In Gases (AREA)

Abstract

PURPOSE:To prevent the adhering of dusts to filter cloth due to their moisture absorption and deliquescence, by supplying hot air from a superheated air supply mechanism to a filter chamber of a dust collecting body together with a dust- containing air to increase the internal temperature of the filter chamber so as to maintain the humidity therein at a value not exceeding a predetermined humidity. CONSTITUTION:There are provided a dust collecting body 2 and a superheated air supply mechanism 3 for supplying hot air to said dust collecting body 2. The hot air is supplied from the superheated air supply mechanism 3 to a filter chamber 6 of the dust collecting body 2 together with a dust-containing air to increase the internal temperature of the filter chamber 6 so as to maintain the humidity therein at a value not exceeding a predetermined humidity, thereby eliminating the possibility of the dusts being coagulated by the moisture absorption and preventing the plugging of filter cloth resulting from the coagulation, leading to an easy separation of the dusts from the filter cloth.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は粉塵特に吸湿潮解性を有する粉塵を含む空気を
濾過する集塵装置に間する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a dust collector for filtering air containing dust, particularly dust having hygroscopic and deliquescent properties.

〔従来の技術〕[Conventional technology]

一般に化学肥料、セメント等吸湿性を有する粉体、もし
くは塩類等を含む化学物質で吸湿し潮解性を有する物質
の運搬あるいは櫛分は作業等において発生する粉塵は環
境を汚損するおそれがあり、このため粉塵含有空気は集
塵装置により濾過する手段が採られている。
In general, when transporting or combing hygroscopic powders such as chemical fertilizers and cement, or chemicals that absorb moisture and have deliquescent properties such as salts, the dust generated during work may contaminate the environment. Therefore, a method is adopted to filter the dust-containing air using a dust collector.

〔発明が解決しようとするrR題〕[rR problem that the invention attempts to solve]

しかしこれら粉塵は吸湿してフィルタ面に固着し、目詰
まりを生じ、通常の撮動もしくは圧力空気の逆噴射によ
る払い落しに対しても固着して剥離困難となる場合があ
る。このため目詰まりによる濾過面積の減少分を見込ん
だ大きい目の集塵機が用いられるが、それだけ設備費が
嵩むと共にやはり濾布の寿命が短く、交換に手数を、要
する等の問題がある。
However, these dust particles absorb moisture and stick to the filter surface, causing clogging, and even when removed by normal photographing or back jetting of pressurized air, they may stick and become difficult to remove. For this reason, a dust collector with large mesh size is used to account for the reduction in filtration area due to clogging, but this increases equipment costs and also has problems such as the filter cloth having a short life and requiring a lot of effort to replace.

本発明はかかる点に鑑み、集塵装置内の粉塵含有空気を
導入する濾過室内の温度を上昇し、相対湿度の低下を計
り、上記粉塵の吸湿、潮解による濾布への固着を防止す
ることを目的とする。
In view of this, the present invention aims to increase the temperature in the filtration chamber into which dust-containing air is introduced into the dust collector, reduce the relative humidity, and prevent the dust from adhering to the filter cloth due to moisture absorption and deliquescence. With the goal.

〔課題を解決するための手段〕[Means to solve the problem]

上記目的を達するために本発明の集塵装置は集塵機本体
と該集塵機本体に加熱空気を供給する過熱空気供給機構
とを備え、該過熱空気供給機構からの加熱空気を粉塵含
有空気と共に集塵機本体の濾過室に供給し濾過室内温度
を上昇し所定湿度以下に保持することにある。
In order to achieve the above object, the dust collector of the present invention includes a dust collector main body and a superheated air supply mechanism that supplies heated air to the dust collector main body, and the heated air from the superheated air supply mechanism is supplied to the dust collector main body together with dust-containing air. The purpose is to supply it to the filtration chamber, raise the temperature in the filtration chamber, and maintain it below a predetermined humidity level.

また上記過熱空気供給機構は集塵機本体から排出される
浄化空気の一部を加熱し、集塵機本体濾過室内に循環供
給することが好ましい。
Further, it is preferable that the superheated air supply mechanism heats a part of the purified air discharged from the dust collector main body and circulates it into the dust collector main body filtration chamber.

更にまた過熱空気供給機構に対する空気供給管は集塵機
本体に連なる浄化空気吸引ブロワの排出側に接続され、
該ブロワの作動により加熱空気を濾過室に循環供給する
ことが好ましい。
Furthermore, the air supply pipe for the superheated air supply mechanism is connected to the discharge side of the purified air suction blower connected to the dust collector main body,
Preferably, heated air is circulated and supplied to the filtration chamber by operating the blower.

〔作 用〕[For production]

加熱空気を処理空気と共に濾過室に供給することにより
濾過室内の温度は上昇して相対湿度は低下し、粉塵は吸
湿することがなく粉M状態で維持される。
By supplying heated air to the filtration chamber together with the processing air, the temperature inside the filtration chamber increases and the relative humidity decreases, and the dust is maintained in the powder M state without absorbing moisture.

また集、W機本体からの排気は外気温度より高温であり
、これを循環使用するときは加熱エネルギーの減少を計
ることができる。
In addition, the exhaust gas from the main body of the W machine has a higher temperature than the outside air temperature, and when this is recycled, heating energy can be reduced.

更に集塵機本体に連なる吸気ブロワの排気側と過熱空気
供給機構と連結することにより、該ブロワの吸引圧力に
より加熱空気は濾過室に供給される。
Furthermore, by connecting the exhaust side of the intake blower connected to the dust collector main body with the superheated air supply mechanism, heated air is supplied to the filtration chamber by the suction pressure of the blower.

【実施例〕【Example〕

図は本発明の実施例を示す。集塵装置lは集塵機本体2
と過熱空気供給機構3とを備える。
The figure shows an embodiment of the invention. The dust collector l is the dust collector body 2
and a superheated air supply mechanism 3.

S塵機本体2は内室を垂直の隔壁4により区分して一方
を粉塵含有空気導入ダクト5に連結される濾過室6とし
、他方を浄化空気室7とする。
The S dust machine main body 2 has an inner chamber divided by a vertical partition wall 4, with one side serving as a filtration chamber 6 connected to a dust-containing air introduction duct 5, and the other side serving as a purified air chamber 7.

上記ダクト5は濾過室6の上方に間口し、いわゆるトッ
プインレット方式とし、111通室下室下は下方に至る
に従い順次紋ったホッパ8を形成し、ホッパ下部にはロ
ータリバルブ9を取り付け、ホッパ内に集積したダスト
を気密を保持しつつ繰出すようになっている0図中5a
は導入ダクト50開口部である。
The duct 5 has an opening above the filtration chamber 6, and is of a so-called top inlet type, and the lower chamber of the 111-channel chamber forms a hopper 8 that is shaped sequentially as it goes downwards, and a rotary valve 9 is attached to the lower part of the hopper. The dust accumulated in the hopper is discharged while maintaining airtightness. 5a in Figure 0
is the opening of the introduction duct 50.

上記濾過室6には多数のバッグフィルタlOを所定間隔
を存して並列配置し、間口部を隔壁4に取り付け、浄化
空気室7にはバッグフィルタ100開口部に連結する漏
斗状ベンチュリー11を取り付け、かつベンチュリー1
1に対向して高圧空気を噴射する噴射管12を対設し、
バッグフィルタ10に粉塵が付着し、所定の濾過抵抗に
達したとき噴射管12より高圧空気をバッグフィルタl
O内にパルス的に吹き込み、膨張収縮及び通気流により
付着粉塵を剥離する。
In the filtration chamber 6, a large number of bag filters 1O are arranged in parallel at predetermined intervals, and the frontage portion is attached to the partition wall 4, and in the purified air chamber 7, a funnel-shaped venturi 11 connected to the opening of the bag filter 100 is attached. , and venturi 1
An injection pipe 12 that injects high-pressure air is installed opposite to 1,
When dust adheres to the bag filter 10 and reaches a predetermined filtration resistance, high-pressure air is pumped through the injection pipe 12 to the bag filter l.
Blow into O in a pulsed manner to peel off attached dust by expansion/contraction and ventilation flow.

13は吸気ブロワであり、浄化空気室7とは排気管14
を介して接続される。15は排気管14に取り付けられ
る開閉弁、16はサイレンサである。
13 is an intake blower, and the purified air chamber 7 is an exhaust pipe 14.
connected via. 15 is an on-off valve attached to the exhaust pipe 14, and 16 is a silencer.

過熱空気供給機構3は、空気加熱室20と、該空気加熱
室内に収納される加熱ヒータ21゜22を備える。但し
ヒータ21は大容量加熱ヒータ、22は小容量加熱ヒー
タであり、加熱室排出側は送出し管23を介して上記導
入ダクト5に接続されろ。
The superheated air supply mechanism 3 includes an air heating chamber 20 and heaters 21 and 22 housed within the air heating chamber. However, the heater 21 is a large-capacity heater, and the heater 22 is a small-capacity heater, and the heating chamber discharge side is connected to the introduction duct 5 via a delivery pipe 23.

加熱室20の空気受入れ側は2分して一方は開閉弁24
及びフィルタ25を介して空気供給管26により上記吸
引ブロワ!3の排出側に接続される。また他方は開閉弁
27、吸引ブロワ28及びフィルタ29を介して補助空
気供給管30により排気管14に接続される。
The air receiving side of the heating chamber 20 is divided into two parts, and one side has an on-off valve 24.
And the above-mentioned suction blower by the air supply pipe 26 via the filter 25! Connected to the discharge side of 3. The other end is connected to the exhaust pipe 14 by an auxiliary air supply pipe 30 via an on-off valve 27, a suction blower 28, and a filter 29.

図中40.41はそれぞれ濾過室6、導入ダクト5に設
けた温度測定器、42は制御機構であり、また50.5
1は粉体処理機52.53に対するフードあり、粉体処
理機52は例えばコンベア搬送機、53は榊機構を例示
する。
In the figure, 40.41 is a temperature measuring device installed in the filtration chamber 6 and the introduction duct 5, 42 is a control mechanism, and 50.5
1 has a hood for the powder processing machine 52, 53, the powder processing machine 52 is, for example, a conveyor conveyance machine, and 53 is a Sakaki mechanism.

上記構成において、各粉体処理機52.53より発生す
る粉塵は吸気ブロワ13の吸引作用により導入ダクト5
を介して濾過室6内に吸引さ−れる。同時に吸引ブロワ
13の吸引作用は加熱室20側にも及ぼし、吸気ブロワ
13から排気の一部は空気供給管26を介して加熱室2
0内に吸い込まれ、加熱された熱気流は送り出し管23
及び導入ダクト5を介して濾過室6内に導入され、該室
内温度を上昇する。
In the above configuration, the dust generated from each powder processing machine 52, 53 is removed from the introduction duct 5 by the suction action of the intake blower 13.
is sucked into the filtration chamber 6 through the filtration chamber 6. At the same time, the suction action of the suction blower 13 is also exerted on the heating chamber 20 side, and a part of the exhaust air from the suction blower 13 is passed through the air supply pipe 26 to the heating chamber 20 side.
The heated hot air flow is drawn into the delivery pipe 23.
and is introduced into the filtration chamber 6 via the introduction duct 5, raising the room temperature.

粉塵の性質にもよるが、一般に吸湿性粉体は湿度50〜
60%以上で吸湿して固体化するおそれがある。従って
常温(20℃)で吸引された含塵空気に加熱空気を混合
し、例えば40℃以上とするときは吸引時の湿度が60
〜70%の場合、相対湿度を50%以下とすることがで
きる。従ってバッグフィルタ10に付着する粉塵は固体
化することがなく、圧力空気の逆噴射により容易に剥離
することができる。
Although it depends on the nature of the dust, hygroscopic powder generally has a humidity of 50~
If it exceeds 60%, it may absorb moisture and solidify. Therefore, when heating air is mixed with dust-containing air sucked at room temperature (20℃) to raise the temperature to 40℃ or higher, the humidity at the time of suction is 60℃.
~70%, the relative humidity can be 50% or less. Therefore, the dust adhering to the bag filter 10 does not solidify and can be easily peeled off by back injection of pressurized air.

濾過室6及び導入ダクト5の温度は制御機構42に印加
され、制taan構42はこれに基づいて大容量ヒータ
21、小容量ヒータ22を選択作動し濾過室温度を所定
温度即ち設定湿度以下に1^持する。
The temperature of the filtration chamber 6 and the introduction duct 5 is applied to the control mechanism 42, and the control mechanism 42 selectively operates the large-capacity heater 21 and the small-capacity heater 22 based on this to lower the filtration chamber temperature to a predetermined temperature, that is, the set humidity. 1^Hold.

なお夜間等、粉体処理機の停止には吸気ブロワも停止す
るが、気!!機本体2内には粉塵が残留しており、その
まま放置するときは温度低下により湿度が上昇し吸湿固
化するおそれがある。
Note that the intake blower also stops when the powder processing machine stops, such as at night, but be careful! ! Dust remains inside the machine body 2, and if left as is, there is a risk that the temperature will drop and the humidity will rise, leading to moisture absorption and solidification.

この場合には排気管14及び導入ダクト5及び空気供給
管26の開閉弁15.17.24を閉じ、補助空気供給
管30の開閉器27を開き、吸引きブロワ28を作動し
温風を循環し集塵機本体2内を所定温度に維持する。こ
の場合の循環風量は少量で足り、吸引ブロワ28は小形
とすることができる。
In this case, close the exhaust pipe 14, the inlet duct 5, and the on-off valves 15, 17, and 24 of the air supply pipe 26, open the switch 27 of the auxiliary air supply pipe 30, and operate the suction blower 28 to circulate hot air. The inside of the dust collector body 2 is maintained at a predetermined temperature. In this case, a small amount of circulating air is sufficient, and the suction blower 28 can be made small.

上記実施例は集塵機本体2からの排気の一部を取り入れ
、加熱して濾過室6内に供給する例を示したが、この方
式によるときは排気温度は外気温度より高温であり、加
熱室2oにおける加熱電力の節減を計ることができる。
The above embodiment shows an example in which a part of the exhaust gas from the dust collector main body 2 is taken in, heated and supplied into the filtration chamber 6, but when using this method, the exhaust temperature is higher than the outside air temperature, and the heating chamber 2 is heated. It is possible to save heating power.

なお、外気のン忌湿度あるいは粉塵の種類によっては、
加熱室20から供給する加熱空気は比較的低温で済む場
合がある。この場合には排気を利用せず外気を取り入れ
るようにしてもよく、鎖線で示す外気取入管6oの開閉
弁61を開放し、空気供給管26の該取入管60の接続
部と吸気ブロワ13出口側間に設けた開閉弁62を閉し
ろ。この場合においても吸気ブロワ13の吸引力により
加熱室20において加熱した空気を吸引し濾過室6内に
供給することができる。
Depending on the humidity of the outside air or the type of dust,
The heated air supplied from the heating chamber 20 may be kept at a relatively low temperature. In this case, outside air may be taken in without using exhaust air, by opening the on-off valve 61 of the outside air intake pipe 6o shown by the chain line, and connecting the intake pipe 60 of the air supply pipe 26 and the intake blower 13 outlet. Close the on-off valve 62 provided between the sides. Even in this case, the air heated in the heating chamber 20 can be sucked in by the suction force of the intake blower 13 and supplied into the filtration chamber 6 .

同様に補助空気供給管30にも外気取入管63を設け、
該取入管に設けた開閉弁64を開放し、補助空電取入管
30に設けた開閉弁65を 4閉し、吸引ブロワ28に
より外気を吸引するようにしてもよい。
Similarly, an outside air intake pipe 63 is provided in the auxiliary air supply pipe 30,
The on-off valve 64 provided on the intake pipe may be opened, the on-off valve 65 provided on the auxiliary static electricity intake pipe 30 may be closed, and the suction blower 28 may suck in outside air.

〔発明の効果〕〔Effect of the invention〕

本発明によるときは次の効果を有する。 The present invention has the following effects.

粉塵含有空気と共に加熱空気を濾過室内に供給し濾過室
温度を上昇するようにしたから、相対湿度は低下し、粉
体は吸湿による凝固を生ずるおそれがなく、凝固による
濾布の目詰まりを防止することができ、濾布に付着する
粉体の剥離が容易である。
Since heated air is supplied into the filtration chamber along with dust-containing air to raise the filtration chamber temperature, the relative humidity decreases, there is no risk of the powder coagulating due to moisture absorption, and filter cloth clogging due to coagulation is prevented. This makes it easy to remove powder adhering to the filter cloth.

また濾過室に供給する加熱空気は集塵機本体か−ら排出
される高温空気を利用するときは、加熱電力の節減を計
ることができる。
Furthermore, when the heated air supplied to the filter chamber is the high-temperature air discharged from the dust collector body, it is possible to save heating power.

更にまた集塵機本体に連設する吸気ブロワの排出側から
空気を取り入れ、加熱して濾過室に供給するときは、高
温排気利用による過熱電力の節減と共に過熱空気の循環
に上記吸気ブロワを兼用させることができ、構造簡単と
共に動力費の節減を計ることができる。
Furthermore, when air is taken in from the discharge side of an intake blower connected to the dust collector body, heated, and supplied to the filtration chamber, the intake blower can also be used to circulate the superheated air while saving heating power by using high-temperature exhaust air. The structure is simple and power costs can be reduced.

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

図は本発明の実施例に間駅 第1図は全体の概略説明図
、第2図は第1図におけるI−1線に沿う断面図である
。 1は集塵装置、2は集塵機本体、3は過熱空気供給機構
、6は濾過室、 13は吸引ブロワである。
The drawings show an embodiment of the present invention. FIG. 1 is a schematic explanatory view of the entire structure, and FIG. 2 is a sectional view taken along line I-1 in FIG. 1. 1 is a dust collector, 2 is a dust collector main body, 3 is a superheated air supply mechanism, 6 is a filtration chamber, and 13 is a suction blower.

Claims (3)

【特許請求の範囲】[Claims] (1)集塵機本体と該集塵機本体に加熱空気を供給する
過熱空気供給機構とを備え、該過熱空気供給機構からの
加熱空気を粉塵含有空気と共に集塵機本体の濾過室に供
給し濾過室内温度を上昇し所定湿度以下に保持すること
を特徴とする集塵装置。
(1) Equipped with a dust collector body and a superheated air supply mechanism that supplies heated air to the dust collector body, and supplies the heated air from the superheated air supply mechanism together with dust-containing air to the filtration chamber of the dust collector body to increase the temperature in the filtration chamber. A dust collector characterized in that the humidity is maintained at a predetermined humidity or lower.
(2)過熱空気供給機構は集塵機本体から排出される浄
化空気の一部を加熱し、集塵機本体濾過室内に循環供給
することを特徴とする請求項1記載の集塵装置。
(2) The dust collector according to claim 1, wherein the superheated air supply mechanism heats a part of the purified air discharged from the dust collector main body and circulates and supplies the purified air into the dust collector main body filtration chamber.
(3)過熱空気供給機構に対する空気供給管は集塵機本
体に連なる浄化空気吸引ブロワの排出側に接続され、該
ブロワの作動により加熱空気を濾過室に循環供給するこ
とを特徴とする請求項1記載の集塵装置。
(3) The air supply pipe for the superheated air supply mechanism is connected to the discharge side of a purified air suction blower connected to the dust collector main body, and the heated air is circulated and supplied to the filtration chamber by the operation of the blower. dust collector.
JP63088809A 1988-04-11 1988-04-11 Dust collector Expired - Lifetime JPH0753218B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63088809A JPH0753218B2 (en) 1988-04-11 1988-04-11 Dust collector

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63088809A JPH0753218B2 (en) 1988-04-11 1988-04-11 Dust collector

Publications (2)

Publication Number Publication Date
JPH01262916A true JPH01262916A (en) 1989-10-19
JPH0753218B2 JPH0753218B2 (en) 1995-06-07

Family

ID=13953217

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63088809A Expired - Lifetime JPH0753218B2 (en) 1988-04-11 1988-04-11 Dust collector

Country Status (1)

Country Link
JP (1) JPH0753218B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0361915U (en) * 1989-10-20 1991-06-18

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54147583A (en) * 1978-05-10 1979-11-17 Toray Eng Co Ltd Inflammable powdery dust collecting method
JPS5687420A (en) * 1979-12-18 1981-07-16 Mitsubishi Heavy Ind Ltd Method and apparatus for carrying out dry treatment of waste gas

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54147583A (en) * 1978-05-10 1979-11-17 Toray Eng Co Ltd Inflammable powdery dust collecting method
JPS5687420A (en) * 1979-12-18 1981-07-16 Mitsubishi Heavy Ind Ltd Method and apparatus for carrying out dry treatment of waste gas

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0361915U (en) * 1989-10-20 1991-06-18

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