JPH01262915A - Method for precoating filter cloth and dust collecting apparatus - Google Patents
Method for precoating filter cloth and dust collecting apparatusInfo
- Publication number
- JPH01262915A JPH01262915A JP63088810A JP8881088A JPH01262915A JP H01262915 A JPH01262915 A JP H01262915A JP 63088810 A JP63088810 A JP 63088810A JP 8881088 A JP8881088 A JP 8881088A JP H01262915 A JPH01262915 A JP H01262915A
- Authority
- JP
- Japan
- Prior art keywords
- dust
- filter cloth
- precoating
- chamber
- main body
- 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
Links
- 239000000428 dust Substances 0.000 title claims abstract description 117
- 239000004744 fabric Substances 0.000 title claims abstract description 34
- 238000000034 method Methods 0.000 title claims abstract description 11
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 22
- 238000001914 filtration Methods 0.000 claims description 29
- 238000000746 purification Methods 0.000 claims description 6
- 238000004140 cleaning Methods 0.000 claims description 4
- 238000005422 blasting Methods 0.000 abstract 1
- 239000011248 coating agent Substances 0.000 description 13
- 239000003517 fume Substances 0.000 description 11
- 238000002347 injection Methods 0.000 description 10
- 239000007924 injection Substances 0.000 description 10
- 239000000126 substance Substances 0.000 description 7
- 238000000576 coating method Methods 0.000 description 5
- 238000011001 backwashing Methods 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/02—Particle separators, e.g. dust precipitators, having hollow filters made of flexible material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2273/00—Operation of filters specially adapted for separating dispersed particles from gases or vapours
- B01D2273/12—Influencing the filter cake during filtration using filter aids
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
Description
〔産業上の利用分野〕
本発明はダスト、特に燃焼や熱化学反応(各1炉および
溶断、溶接)により発生する固着物質を含むヒユームを
濾過する濾材のプリコート方法及び集!!装置に間する
。
〔従来の技術〕
上記ヒユーム(煙霧)は環境汚染を防止するため、一般
に濾布により濾過する手段が採られている。しかしヒユ
ームには固着物質を含み、早期に濾布の目詰まりを生ず
る欠点がある(第3図におけるA線図)。これは通常の
圧力空気による逆噴射あるいは振動付与等には剥離が困
難で、そのため通常濾布にプリコート剤を付着させ、剥
離を容易にする手段が採られている。
〔発明が解決しようとする!!題〕
上記プリコート剤は一般に市販のものを請人して使用す
る手段が採られている。しかしこのプリコート剤は濾布
の逆噴射等の清掃の都度供給する必要があり、使用量が
大きく、経費が嵩むと共に、連部、貯蔵に手数を要する
等の問題がある。またダストの種類によっては他の用途
に使用できる場合があるが、プリコート剤が異物として
混入するため使用に適しない等の問題もある。
本発明は種々実験の結果、回収したダストをプリコート
剤として使用できることを着目し、この回収ダストを利
用することにより上記欠点を解消することを目的とする
。[Industrial Field of Application] The present invention relates to a method and collection of precoating filter media for filtering dust, particularly fumes containing fixed substances generated by combustion and thermochemical reactions (one furnace, one for each furnace, one for melting, one for melting, and one for welding). ! between the devices. [Prior Art] In order to prevent the above-mentioned fumes from contaminating the environment, a method of filtering them using a filter cloth is generally adopted. However, hume has the disadvantage that it contains fixed substances and causes early clogging of the filter cloth (diagram A in FIG. 3). It is difficult to remove this by normal pressure air injection or vibration application, and therefore a pre-coat agent is usually attached to the filter cloth to facilitate removal. [Invention tries to solve it! ! [Problem] As the precoat agent, a method is generally adopted in which a commercially available one is purchased and used. However, this precoat agent must be supplied each time the filter cloth is cleaned by back spraying, etc., and there are problems such as the amount used is large, the cost is increased, and it requires time and effort for continuous parts and storage. Further, depending on the type of dust, it may be possible to use it for other purposes, but there are also problems such as the pre-coat agent being mixed in as a foreign substance, making it unsuitable for use. As a result of various experiments, the present invention has focused on the fact that the collected dust can be used as a precoat agent, and aims to solve the above-mentioned drawbacks by utilizing the collected dust.
上記目的を達成するために、本発明の濾布のプリコート
方法においては、供給されるダスト含有空気を濾布によ
り濾過し、付着ダストを圧力空気による逆噴射または振
動付与等の剥離手段により剥離し、剥離したダストを回
収し、回収したダストの一部をプリコート剤として濾布
に供給付着させることにある。
また、上記方法を実施する集塵装置は、ダスト含有空気
を濾過する濾布と、該濾布に付着するダストを剥離する
剥離手段とを備えた集lII機本体と、該本体から繰出
されるダストの一部を受け入れ収納する中間取出部とを
備え、該中間取出部は返還ダクトを介して集塵機本体の
ダスト含有空気取入れ側に接続され、剥離手段による濾
布の清掃と、返還ダクトを介して貯留ダストの供給によ
るプリコートとを関連して行なうものである。
なお上記集塵機本体はダスト含有空気を導入する濾過室
と、該濾過室側方に形成した浄化空気貯留用浄化室とに
区分され、濾布はバッグフィルタとして濾過室に設け、
かつ浄化室側に間口し、貯留したダストの返還ダクトは
濾過室上部に間口し、貯留したダストをプリコート剤と
して濾布の上方から供給することが好ましい。
また集塵機本体は複数の単位集塵室に区分され、それぞ
れはバッグフィルタを収納する濾過室と浄化空気貯留用
浄化室並びにバッグフィルタの付着ダスト剥離手段を備
え、かつ共通の剥離ダスト移送コンベアに接続され、該
コンベアには移送ダストの一部を受け入れる中間取出部
を備え、中間取出部は上記各単位集塵室の濾過室に切換
弁を介して接続され、各単位集塵室を順次剥離手段によ
る濾布の清掃と中間取出部に貯留したダストの供給によ
るプリコートとを行なうようにしてもよい。
〔作 用〕
濾布から剥離したダストの一部を集積し、これを濾過室
に還元し濾布に付着させることによりプリコート剤とし
ての作用を行なわせることができる。
この場合、濾過室の上方から上記ダストを供給するとき
は、ダストは濾布の全面に均一かつ早期に付着させるこ
とができる。
また集塵機本体を複数の単位集塵室に区分し、各単位集
塵室毎に順次濾布の清掃と共に、共通の中間取出部から
貯留ダストの供給によるプリコートを行なうことにより
、集塵作用への影響の軽減を計ることができる。
〔実施例〕
第1図乃至第3図は第1実施例を示す。集塵装置fは集
塵機本体2と、該本体から排出されるダストを移送する
移送コンベア3を備える。
集塵機本体2は内室を垂直の隔u4により区分して一方
をヒユーム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。上記ダクト5は濾過
室6の上方に開口し、いわゆるトップインレット方式と
し、濾過室下部には下方に至るに従い順次紋ったダスト
集積用ホッパ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、集積したダストを気密に保持しつつ繰
出すようになっている。
上記濾過室6には多数のバッグフィルタ10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10の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】
lに対向して高圧空気を噴射する噴射管12を対設する
。
即ち本実施例はバッグフィルタ10に付着するダストを
剥離する剥離手段Pとしてベンチュリー11、噴射管1
2による逆噴射方式を示したが、これは例えば振動付与
式としてもよい。
上記移送コンベア3は例えばスクリューコンヘアより構
成し、このコンベア適所には送り出されるダストの一部
を取り出す中間取出部20を、また終端にはダスト残部
を排出する排出部25を設け、それぞれロータリバルブ
21.26を取り付ける。
上記中間取出部20から取り出されるダストはバッグフ
ィルタlOに対するプリコート剤として使用するもので
、プリコート剤供給装萱のホッパ22を連結し、ホッパ
に集積したダストは返還ダクト23を介して前記導入ダ
クト5に供給される。24.27はそれぞれ返還ダクト
23、導入ダクト5に設けられる開閉弁である。
図中、30は電気炉その他燃焼炉等のヒユーム発生器、
31はこのヒユーム発生器に対設するフートであり導入
ダクト5に接続される。また40a、40bは濾過室6
と浄化空気室7との差圧(バッグフィルタの濾過抵抗)
を検出する差圧検出器であり、40aは設定した高差圧
を、また40bは低差圧を検知し信号を発するようにし
たものである。また13は排気ダクト、14は吸引ブロ
ワを示す。
次にバッグフィルタ10に対するプリコート要領を説明
する。第3図はバッグフィルタ10の経時的圧力変化の
一例を示すもので、縦軸は圧力損失を、また横軸は時間
を示す0図に於てA線は通常のヒユーム含有空気をブリ
フィルタを施さずに供給したときの圧力変化を示すもの
である。ヒユーム中には固着物質を含み、従って目詰ま
りが甚だしく、図に示す如くバッグフィルタによる圧力
損失は急速に上昇する。なおこの場合、噴射管12から
圧力空気を吹き込んでも充分な付着ダストの除去は困難
である。
このバッグフィルタ10に対するプリコートに際しては
、導入ダクト5の開閉弁27を閉じ、返還ダクト23の
開閉弁24を廚き、吸引ブロワ14の吸引作用によりプ
リコート剤供給装置のホッパ22内のダストを吸引し、
濾過室6内に導入し、バッグフィルタ10に付着させ、
プリコートを行なう。このときの圧力変化を同図Bに示
す。圧力損失が所定圧(低圧)に達したとき差圧検知器
40bが作動し、上記開閉弁24を閉じ導入ダクト5の
開閉弁27を開きヒユーム含有空気を導入し、通常の濾
過作用を行なう、この時の圧力変化を同図Cに示す、こ
の場合、ヒユーム中に含まれる固着物質はプリコート剤
に吸着されるが濾布によるいわゆる表面濾過とことなり
プリコート剤による体積濾過であり、圧損上昇率は小さ
く、A線に比し緩傾斜である。
圧力損失が所定圧(高圧)に達したとき差圧検知器40
aが作動し、噴射管12より圧力空気をバッグフィルタ
10内に吹き込み、逆噴射により付着ダストを剥離しホ
ッパ8内に落下集積する。このダストはロータリバルブ
9の回動により気密を保持しつつ排出され、移送コンベ
ア3により搬出される。
逆噴射による洗浄終了後は返還ダクト23の開閉弁24
を解放し、吸引ブロワ14によりブリコート剤供給装置
のホッパ22内のダストを吸引し前記要領にてプリコー
トを行なう。この場合導入ダクト5の開閉弁27も間放
し、ヒユーム含有空気と共にプリコート用ダストを吸引
し、混合した空気を吸引するようにしてもよい。
次に第4図乃至第6図は第2実施例を示す。
本実施例の集塵装置50も前例と同様に集塵機本体51
とダスト移送コンベア52を備える。
集塵機本体51は内室を仕切り壁52により仕切り、複
数例えば4個の単位集塵機55a〜55dとする。各単
位集塵機毎何れも同一構造であり、かつ前例の集塵機本
体2とも同一構造であり、同一部品については同一符号
(部品によってはサフィックスa、 b、 c、
dを付す)を付して説明を省略する。またダスト移送
コンベア52は各単位集塵機に共通であり、適所に中間
取出g56を、また終端部には排出部60を設け、それ
ぞれロータリバルブ57.61を取り付け、中間取出部
56にはダスト集積用ホッパ58を備える。62はダス
ト返還ダクトであり、開閉弁24a〜24dを備えた分
岐返還ダク)63a〜63dに接続され、それぞれの分
岐返還ダクトは導入ダクト5に連なる分岐導入ダクト6
4a〜64dに接続され、各分岐導入ダクトは前例と同
様に濾過室6a〜6dの上方に間口している。
上記構成において、逆洗及びプリコートは順次各単位集
塵機毎に行なうようにしたもので、先ず第1の単位集塵
機55aに対し前記要領にてバッグフィルタ10aに対
し逆洗と、プリコート剤供給装置のホッパ58内のダス
トの付着(プリコート)とを行ない、以下順次各単位集
塵機55b〜55dに対し同様の逆洗とプリコート操作
を行なう。
本実施例によるときはヒユーム発生器30カ)ら発生す
るヒユームを経続して効果的に吸引することができる。
〔発明の効果〕
本発明によるときは、次の効果を有する。
濾布に付着したダストを剥離し、これをプリコート剤と
して使用するようにしたから、従来のプリコート剤の購
入、貯蔵及び搬入の手数を省略し、安価にプリコートを
行なうことができる。
また蒐集したダストを他に流用する場合に、従来はプリ
コート剤が異物となって混入し問題があったが、本発明
によるときは蒐集したダストの一部をプリコート剤とし
て使用するため異物の混入がなく流用が可能である。
またプリコートに際し、上記ダストを濾過室上方から供
給することにより濾布への付着が容易かつ均一にしかも
短時間に行なうことができる。
さらに回収ダストをプリコート剤として使用し、従来の
如き別個のプリコート剤を使用しないから、ダストの発
生量の減少を計ることかでき る。
また集塵機本体を複数の単位集塵機に区分し、各単位集
塵機毎に濾布の清掃を行なうと共に、共通のダスト移送
コンベアからダストの一部を取り出し、これをプリコー
ト剤として上記単位集塵機に供給しプリコートを行なう
ことにより、該単位集塵機のダスト吸引の停止中でもダ
ストの連続吸引が可能であり、かつプリコート剤として
のダストの取り出し構造の簡素化を計ることができる。In order to achieve the above object, in the filter cloth precoating method of the present invention, the supplied dust-containing air is filtered through the filter cloth, and the adhering dust is peeled off by a peeling means such as back injection with pressurized air or vibration application. The purpose is to collect the peeled dust and supply a part of the collected dust as a pre-coat agent to the filter cloth. Further, the dust collector for carrying out the above method includes a main body of a collector equipped with a filter cloth for filtering dust-containing air and a peeling means for peeling off dust adhering to the filter cloth, and The intermediate take-out part is connected to the dust-containing air intake side of the dust collector main body through a return duct, and the intermediate take-out part receives and stores a part of the dust. This is performed in conjunction with precoating by supplying stored dust. The dust collector main body is divided into a filtration chamber for introducing dust-containing air and a purification chamber for storing purified air formed on the side of the filtration chamber, and a filter cloth is provided in the filtration chamber as a bag filter.
In addition, it is preferable that the duct for returning the accumulated dust opens to the purification chamber side, opens to the upper part of the filtration chamber, and supplies the accumulated dust from above the filter cloth as a pre-coat agent. The main body of the dust collector is divided into multiple unit dust collection chambers, each of which is equipped with a filtration chamber for housing a bag filter, a purification chamber for storing purified air, and a means for peeling off the dust adhering to the bag filter, and is connected to a common conveyor for conveying the peeled dust. The conveyor is equipped with an intermediate take-out part that receives a portion of the transferred dust, and the intermediate take-out part is connected to the filtration chamber of each of the unit dust collection chambers via a switching valve, and each unit dust collection chamber is sequentially removed by a stripping means. It is also possible to perform cleaning of the filter cloth by using the filter cloth and pre-coating by supplying the dust stored in the intermediate take-out part. [Function] A part of the dust peeled off from the filter cloth is accumulated, returned to the filter chamber, and adhered to the filter cloth, so that it can act as a precoating agent. In this case, when the dust is supplied from above the filtration chamber, the dust can be uniformly and quickly adhered to the entire surface of the filter cloth. In addition, the dust collector body is divided into multiple unit dust collection chambers, and the filter cloth of each unit dust collection chamber is cleaned sequentially and pre-coated by supplying stored dust from a common intermediate extraction part, thereby improving the dust collection function. The impact can be reduced. [Embodiment] FIGS. 1 to 3 show a first embodiment. The dust collector f includes a dust collector main body 2 and a transfer conveyor 3 for transporting dust discharged from the main body. The dust collector main body 2 has an inner chamber divided by a vertical space U4, and one side is a filtration chamber 6 connected to a fume-containing air introduction duct 5.
and the other is designated as a purified air chamber 7. The duct 5 opens above the filtration chamber 6, and is of a so-called top inlet type, and a hopper 8 for collecting dust is formed in the lower part of the filtration chamber, and the hopper 8 is shaped sequentially toward the bottom, and a rotary valve 9 is attached to the lower part of the hopper. It is designed to keep the accumulated dust airtight while discharging it. A large number of bag filters 10 are arranged in parallel at predetermined intervals in the filtration chamber 6, and the frontage portions are attached to the partition wall 4, and the purified air chamber 7 is provided with a funnel-shaped venturi 11 connected to the opening of the bag filter 10. Installation and Venturi]
An injection pipe 12 for injecting high-pressure air is installed opposite to the injection pipe 1. That is, in this embodiment, the venturi 11 and the injection pipe 1 are used as the peeling means P for peeling off the dust adhering to the bag filter 10.
Although the reverse injection method according to No. 2 has been shown, this may also be, for example, a vibration imparting method. The transfer conveyor 3 is composed of, for example, a screw conveyor, and an intermediate take-out part 20 is provided at a suitable location on the conveyor to take out a part of the dust being sent out, and a discharge part 25 is provided at the end to discharge the remaining dust, each of which has a rotary valve. 21. Attach 26. The dust taken out from the intermediate take-out section 20 is used as a pre-coating agent for the bag filter IO, and the hopper 22 of the pre-coating agent supply device is connected, and the dust accumulated in the hopper is passed through the return duct 23 to the introduction duct 5. is supplied to 24 and 27 are on-off valves provided in the return duct 23 and the introduction duct 5, respectively. In the figure, 30 is a fume generator such as an electric furnace or other combustion furnace;
Reference numeral 31 is a foot provided opposite to this fume generator and connected to the introduction duct 5. In addition, 40a and 40b are the filtration chambers 6
Differential pressure between and purified air chamber 7 (filtration resistance of bag filter)
40a is a differential pressure detector that detects a set high differential pressure, and 40b is a differential pressure detector that detects a set low differential pressure and issues a signal. Further, 13 indicates an exhaust duct, and 14 indicates a suction blower. Next, the procedure for precoating the bag filter 10 will be explained. Figure 3 shows an example of pressure change over time in the bag filter 10, where the vertical axis shows pressure loss and the horizontal axis shows time. This shows the pressure change when the gas is supplied without any treatment. The fume contains fixed substances, so clogging is severe, and the pressure loss through the bag filter rapidly increases as shown in the figure. In this case, even if pressurized air is blown from the injection pipe 12, it is difficult to sufficiently remove the attached dust. When precoating the bag filter 10, the on-off valve 27 of the introduction duct 5 is closed, the on-off valve 24 of the return duct 23 is opened, and the dust in the hopper 22 of the pre-coating agent supply device is sucked by the suction action of the suction blower 14. ,
introduced into the filtration chamber 6 and attached to the bag filter 10,
Perform precoat. The pressure change at this time is shown in Figure B. When the pressure loss reaches a predetermined pressure (low pressure), the differential pressure detector 40b is activated, the on-off valve 24 is closed, and the on-off valve 27 of the introduction duct 5 is opened to introduce fume-containing air and perform a normal filtration action. The pressure change at this time is shown in Figure C. In this case, the fixed substances contained in the fume are adsorbed by the precoat agent, but this is volumetric filtration by the precoat agent, which is different from so-called surface filtration by the filter cloth, and the rate of increase in pressure drop is is small and has a gentle slope compared to line A. When the pressure loss reaches a predetermined pressure (high pressure), the differential pressure detector 40
a is activated, pressurized air is blown into the bag filter 10 from the injection pipe 12, and the adhering dust is peeled off by reverse injection and falls and accumulates in the hopper 8. This dust is discharged while maintaining airtightness by rotating the rotary valve 9, and is carried out by the transfer conveyor 3. After the cleaning by reverse injection is completed, the on-off valve 24 of the return duct 23
is released, the dust in the hopper 22 of the bricoating agent supply device is sucked by the suction blower 14, and precoating is performed in the same manner as described above. In this case, the on-off valve 27 of the introduction duct 5 may also be left open so that the pre-coating dust and the fume-containing air are sucked and the mixed air is sucked. Next, FIGS. 4 to 6 show a second embodiment. The dust collector 50 of this embodiment also has a dust collector body 51 similar to the previous example.
and a dust transfer conveyor 52. The dust collector main body 51 has an inner chamber partitioned by a partition wall 52 into a plurality of unit dust collectors, for example, four unit dust collectors 55a to 55d. Each unit dust collector has the same structure, and it also has the same structure as the dust collector main body 2 in the previous example, and the same parts are given the same symbols (some parts have suffixes a, b, c, etc.)
d) and the explanation will be omitted. Further, the dust transfer conveyor 52 is common to each unit dust collector, and an intermediate take-out g56 is provided at a suitable location, and a discharge part 60 is provided at the terminal end, and rotary valves 57 and 61 are attached to each, and the intermediate take-out part 56 is used for collecting dust. A hopper 58 is provided. 62 is a dust return duct, which is connected to branch return ducts 63a to 63d equipped with on-off valves 24a to 24d, and each branch return duct is connected to a branch introduction duct 6 connected to the introduction duct 5.
4a to 64d, and each branch introduction duct opens above the filtration chambers 6a to 6d as in the previous example. In the above configuration, backwashing and precoating are sequentially performed for each unit dust collector. First, the bag filter 10a is backwashed in the same manner as described above for the first unit dust collector 55a, and the hopper of the precoat agent supplying device is After that, the same backwashing and precoating operations are sequentially performed for each unit dust collector 55b to 55d. According to this embodiment, the fume generated from the fume generator 30 can be continuously and effectively sucked. [Effects of the Invention] The present invention has the following effects. Since the dust adhering to the filter cloth is peeled off and used as a pre-coat agent, the conventional trouble of purchasing, storing and transporting the pre-coat agent can be omitted, and pre-coating can be performed at low cost. In addition, when the collected dust is used for other purposes, there was a problem in the past because the pre-coating agent became a foreign substance and got mixed in, but with the present invention, since a part of the collected dust is used as a pre-coating agent, there is no chance of foreign substances getting mixed in. It is possible to use it as there is no such thing. Further, during pre-coating, by supplying the dust from above the filtration chamber, it is possible to easily and uniformly adhere the dust to the filter cloth in a short time. Furthermore, since the recovered dust is used as a pre-coating agent and a separate pre-coating agent as in the conventional method is not used, the amount of dust generated can be reduced. In addition, the dust collector body is divided into multiple unit dust collectors, and the filter cloth of each unit dust collector is cleaned, and a part of the dust is taken out from a common dust transfer conveyor, and this is supplied as a pre-coating agent to the above-mentioned unit dust collectors for pre-coating. By doing so, it is possible to continuously suck dust even when the dust suction of the unit dust collector is stopped, and it is possible to simplify the structure for taking out the dust as a precoating agent.
第1図乃至第3図は第1実施例に関し、第1図は全体の
縦断説明図、第2図は第1図におけるI−1線に沿う断
面図、第3図は濾布の濾過抵抗(圧力損失)の比較グラ
フ、第4図乃至第6図は第2実施例に間し、第4図は全
体の縦断説明図、第5図は第4図における■−■線に沿
う断面図、第6図は第5図における■−■線に沿う断面
図である。
l、50は集塵装置、2,51は集塵機本体、3はダス
ト移送コンベア、6.6a〜6dはyga室、7.7a
〜7dは浄化空気室、10.10a〜10dはバッグフ
ィルタ、20.56は中間取出部、23はダスト返還ダ
クト、27.27a〜27dは開閉弁、55a〜55d
は単位集塵機、Pは剥離手段である。Figures 1 to 3 relate to the first embodiment; Figure 1 is an overall vertical sectional view, Figure 2 is a sectional view taken along line I-1 in Figure 1, and Figure 3 is the filtration resistance of the filter cloth. (Pressure loss) comparison graphs, Figures 4 to 6 are for the second embodiment, Figure 4 is an overall longitudinal sectional view, and Figure 5 is a cross-sectional view along the line ■-■ in Figure 4. , FIG. 6 is a sectional view taken along the line ■-■ in FIG. 1 and 50 are dust collectors, 2 and 51 are dust collector bodies, 3 is a dust transfer conveyor, 6.6a to 6d are yga chambers, 7.7a
-7d are purified air chambers, 10.10a-10d are bag filters, 20.56 are intermediate take-off parts, 23 are dust return ducts, 27.27a-27d are on-off valves, 55a-55d
is a unit dust collector, and P is a stripping means.
Claims (4)
付着ダストを圧力空気による逆噴射または振動付与等の
剥離手段により剥離し、剥離したダストを回収し、回収
したダストの一部をプリコート剤として濾布に供給付着
させることを特徴とする濾布のプリコート方法。(1) Filter the supplied dust-containing air with a filter cloth,
A filter cloth characterized in that adhering dust is peeled off by a peeling means such as reverse jetting with pressurized air or applying vibration, the peeled off dust is collected, and a part of the collected dust is supplied as a pre-coat agent to the filter cloth for adhesion. Precoating method.
するダストを剥離する剥離手段とを備えた集塵機本体と
、該本体から繰出されるダストの一部を受け入れ収納す
る中間取出部とを備え、該中間取出部は返還ダクトを介
して集塵機本体のダスト含有空気取入れ側に接続され、
剥離手段による濾布の清掃と、返還ダクトを介して貯留
ダストの供給によるプリコートとを関連して行なうこと
を特徴とする集塵装置。(2) A dust collector main body equipped with a filter cloth that filters dust-containing air and a peeling means that peels off the dust adhering to the filter cloth, and an intermediate take-out section that receives and stores a part of the dust discharged from the main body. The intermediate take-out part is connected to the dust-containing air intake side of the dust collector main body via the return duct,
A dust collector characterized in that cleaning of a filter cloth by a peeling means and precoating by supplying stored dust through a return duct are performed in conjunction.
、該濾過室側方に形成した浄化空気貯留用浄化室とに区
分され、濾布はバッグフィルタとして濾過室に設け、か
つ浄化室側に開口し、貯留したダストの返還ダクトは濾
過室上部に開口している請求項2記載の集塵装置。(3) The main body of the dust collector is divided into a filtration chamber for introducing dust-containing air and a purification chamber for storing purified air formed on the side of the filtration chamber, and a filter cloth is provided in the filtration chamber as a bag filter and on the side of the purification chamber. 3. The dust collecting device according to claim 2, wherein the return duct for returning the stored dust is opened at the upper part of the filtration chamber.
ぞれはバッグフィルタを収納する濾過室と浄化空気貯留
用浄化室並びにバッグフィルタの付着ダスト剥離手段を
備え、かつ共通の剥離ダスト移送コンベアに接続され、
該コンベアには移送ダストの一部を受け入れる中間取出
部を備え、中間取出部は上記各単位集塵室の濾過室に切
換弁を介して接続され、各単位集塵室を順次剥離手段に
よる濾布の清掃と中間取出部に貯留したダストの供給に
よるプリコートとを行なうことを特徴とする集塵装置。(4) The main body of the dust collector is divided into a plurality of unit dust collection chambers, each of which is equipped with a filtration chamber for storing a bag filter, a purification chamber for storing purified air, and means for peeling off dust attached to the bag filter, and a common peeling dust transfer conveyor. connected to
The conveyor is equipped with an intermediate take-out part that receives a portion of the transferred dust, and the intermediate take-out part is connected to the filtration chamber of each of the unit dust collection chambers via a switching valve, and each unit dust collection chamber is sequentially filtered by the stripping means. A dust collector characterized by cleaning a cloth and precoating it by supplying dust stored in an intermediate take-out section.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63088810A JPH0753216B2 (en) | 1988-04-11 | 1988-04-11 | Dust collector |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63088810A JPH0753216B2 (en) | 1988-04-11 | 1988-04-11 | Dust collector |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01262915A true JPH01262915A (en) | 1989-10-19 |
JPH0753216B2 JPH0753216B2 (en) | 1995-06-07 |
Family
ID=13953248
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63088810A Expired - Lifetime JPH0753216B2 (en) | 1988-04-11 | 1988-04-11 | Dust collector |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0753216B2 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0556211U (en) * | 1991-12-26 | 1993-07-27 | 株式会社プランテック | Pre-coated bag filter device |
JPH06126114A (en) * | 1991-12-26 | 1994-05-10 | Plantec:Kk | Chemical feeding apparatus in precoat-type bag filter apparatus |
JPH06154534A (en) * | 1992-09-22 | 1994-06-03 | Kazuo Mizutani | Cleaning controlling method for bag-type reactive dust collecting apparatus |
JPH06198111A (en) * | 1992-12-28 | 1994-07-19 | Plantec:Kk | Operation control method for precoat type bag filter device |
CN104353300A (en) * | 2014-09-18 | 2015-02-18 | 任治民 | Adjacent-boiler dust pre-coating device for bag-type dust remover of boiler |
Citations (7)
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JPS4937945A (en) * | 1972-08-14 | 1974-04-09 | ||
JPS5216832A (en) * | 1975-07-30 | 1977-02-08 | Hitachi Zosen Corp | Scaffolding device for work at steel tower suporting chimney |
JPS5435713A (en) * | 1977-08-26 | 1979-03-16 | Nec Corp | Magnetic card reader |
JPS5478572A (en) * | 1977-12-03 | 1979-06-22 | Nippon Air Filter | Precoating type bag filter device |
JPS568077A (en) * | 1979-07-03 | 1981-01-27 | Ogasaka Ski Seisakusho | Ski for training |
JPS6112735A (en) * | 1984-06-27 | 1986-01-21 | Japan Styrene Paper Co Ltd | Prefoamed polyolefin resin particle |
JPS62227418A (en) * | 1986-03-29 | 1987-10-06 | Nippon Steel Corp | Dust collecting method for molten iron pretreatment plant |
-
1988
- 1988-04-11 JP JP63088810A patent/JPH0753216B2/en not_active Expired - Lifetime
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4937945A (en) * | 1972-08-14 | 1974-04-09 | ||
JPS5216832A (en) * | 1975-07-30 | 1977-02-08 | Hitachi Zosen Corp | Scaffolding device for work at steel tower suporting chimney |
JPS5435713A (en) * | 1977-08-26 | 1979-03-16 | Nec Corp | Magnetic card reader |
JPS5478572A (en) * | 1977-12-03 | 1979-06-22 | Nippon Air Filter | Precoating type bag filter device |
JPS568077A (en) * | 1979-07-03 | 1981-01-27 | Ogasaka Ski Seisakusho | Ski for training |
JPS6112735A (en) * | 1984-06-27 | 1986-01-21 | Japan Styrene Paper Co Ltd | Prefoamed polyolefin resin particle |
JPS62227418A (en) * | 1986-03-29 | 1987-10-06 | Nippon Steel Corp | Dust collecting method for molten iron pretreatment plant |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0556211U (en) * | 1991-12-26 | 1993-07-27 | 株式会社プランテック | Pre-coated bag filter device |
JPH06126114A (en) * | 1991-12-26 | 1994-05-10 | Plantec:Kk | Chemical feeding apparatus in precoat-type bag filter apparatus |
JPH06154534A (en) * | 1992-09-22 | 1994-06-03 | Kazuo Mizutani | Cleaning controlling method for bag-type reactive dust collecting apparatus |
JPH06198111A (en) * | 1992-12-28 | 1994-07-19 | Plantec:Kk | Operation control method for precoat type bag filter device |
CN104353300A (en) * | 2014-09-18 | 2015-02-18 | 任治民 | Adjacent-boiler dust pre-coating device for bag-type dust remover of boiler |
Also Published As
Publication number | Publication date |
---|---|
JPH0753216B2 (en) | 1995-06-07 |
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