JPS601044B2 - Dust collection method using bug filter - Google Patents

Dust collection method using bug filter

Info

Publication number
JPS601044B2
JPS601044B2 JP15269481A JP15269481A JPS601044B2 JP S601044 B2 JPS601044 B2 JP S601044B2 JP 15269481 A JP15269481 A JP 15269481A JP 15269481 A JP15269481 A JP 15269481A JP S601044 B2 JPS601044 B2 JP S601044B2
Authority
JP
Japan
Prior art keywords
dust
dust collection
air volume
suction
exhaust blower
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.)
Expired
Application number
JP15269481A
Other languages
Japanese (ja)
Other versions
JPS5855023A (en
Inventor
紘一郎 伊藤
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.)
SHINWA BOEKI KK
Original Assignee
SHINWA BOEKI KK
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 SHINWA BOEKI KK filed Critical SHINWA BOEKI KK
Priority to JP15269481A priority Critical patent/JPS601044B2/en
Publication of JPS5855023A publication Critical patent/JPS5855023A/en
Publication of JPS601044B2 publication Critical patent/JPS601044B2/en
Expired legal-status Critical Current

Links

Description

【発明の詳細な説明】 この発明は、コークス炉や電気炉・高炉銭床、製鋼工場
等の如く各作業内容により発塵量が大小変化する発塵源
からのダストガスをバグフィルターに吸引導通して集塵
処理する集塵方法に関する。
[Detailed Description of the Invention] This invention is designed to suck and conduct dust gas from a dust generation source such as a coke oven, an electric furnace, a blast furnace bank, a steel factory, etc., where the amount of dust generated varies depending on the content of the work, to a bag filter. The present invention relates to a dust collection method in which dust collection is performed using a dust collection method.

従来、この種のバグフィルターを用いた集塵方法では、
発塵源からのダストガスを、その発塵量に応じ吸引風量
制御機構により排気ブロヮの吸引風量を制御しながら、
バグフィルタ−の複数に分割された集塵セクションに吸
引導通して、その袋塵セクション内の多数のバグで炉過
捕集すると共に、そのバグに捕集したダストは、タイマ
ーにより各集塵セクション毎にダンバー開閉切換え機構
を動作させて払い落として専用の吸引プロワの吸引で逆
洗気流を起こし、これにてバグを収縮膨張させて払い落
とし除去するようにしている。
Conventionally, in the dust collection method using this type of bag filter,
The dust gas from the dust source is controlled by the suction air volume control mechanism according to the amount of dust generated, while controlling the suction air volume of the exhaust blower.
The suction is conducted to the dust collection section divided into multiple parts of the bag filter, and the dust collected in the bag is collected by a large number of bugs in the bag filter. Each time, a damper opening/closing switching mechanism is operated to shake the bugs off, and a special suction blower generates a backwash airflow, which causes the bugs to contract and expand, and is then brushed off and removed.

つまり、発塵量に応じ吸引風量を制御して、排気プロワ
の電力消費の無駄を少なくして省エネルギーを図ってい
ると共に、バグの払い蕗としをタイマーにより各集塵セ
クション毎に行って、その払い落としをしていない他の
集塵セクションでダストガスの炉過捕集を行うことによ
り、発塵源からのダストガスを止めずに長期間連続して
集塵処理できるようにしている。また、上述したタイマ
ー制御により動作するダンバー開閉切換え機構を吸引風
量制御機構に電気的にインターロックし、発塵源のダス
トガス発生量の増大に伴い最大吸引風量を得るべく制御
している時は、タイマーによるダスト払い落とし時期が
来てもダスト払い落とし機構を動作させずにおいて、発
塵源からのダストガスを全集塵セクションに導通して集
塵処理し、発塵源のダストガス発生量の減少あるいは停
止に伴い吸引風量制御機構が風量制御している状態時の
みダスト払い落とし機構を動作させるようにして、過大
な容量を備えていなくても炉過風速の上昇則ち、炉過集
塵効率の低下を招くことなく運転可能として、装置全体
の小型化・設備費及び運転経費の軽減を図るようにして
いる。
In other words, the suction air volume is controlled according to the amount of dust generated, reducing wasted power consumption of the exhaust blower and saving energy.In addition, bugs are removed from each dust collection section using a timer. By performing over-collection of dust gas in the other dust collection sections that are not being brushed off, it is possible to continuously collect dust for a long period of time without stopping the dust gas from the dust source. In addition, when the damper opening/closing switching mechanism operated by the above-mentioned timer control is electrically interlocked with the suction air volume control mechanism and controlled to obtain the maximum suction air volume as the amount of dust gas generated from the dust generation source increases, Even when the time for dust removal by the timer comes, the dust removal mechanism is not operated, and the dust gas from the dust source is conducted to all the dust collection sections to collect the dust, thereby reducing or stopping the amount of dust gas generated by the dust source. Accordingly, by operating the dust removal mechanism only when the suction air volume control mechanism is controlling the air volume, even if the furnace does not have an excessive capacity, the furnace overflow speed increases and the furnace dust collection efficiency decreases. The system is designed to be able to operate without causing problems, thereby reducing the size of the entire device and reducing equipment costs and operating costs.

ところで上述した従来方法では、ダストガスを各集塵セ
クションに吸引導通して排気する排気ブロヮと、バグの
楠集ダスト払い落としのための逆洗気流を起こす吸引ブ
ロワとを別々に備えて運転している。
By the way, in the above-mentioned conventional method, an exhaust blower that suctions and conducts dust gas to each dust collection section and exhausts it, and a suction blower that generates a backwash airflow to blow off the dust collected from bugs are separately provided and operated. There is.

従って、高価なプロワを2台必要としており不経済であ
ったと共に、その両ブロワを各々運転制御しなければな
らず面倒であった。そこで、最近ではダスト払い落とし
のための逆洗気流発生専用の吸引ブロワを用いずに、発
塵源からのダストガスをバグフィルターの集塵セクショ
ンに吸引導適するメインの排気ブロワだけを備え、その
排気ブロワの吸引作用でダストガスの集塵と各集塵セク
ション毎のダスト払い落とし作用との両方を行う方法が
考えられて来た。このメインの排気ブロワだけを備えて
ダストガスの集塵処理並びにダスト払い蕗としを行うよ
うにしたバグフィルター装置の概略的構成を第1図によ
り述べると、そのバグフィルタ−1は複数に分割された
集塵セクション2・・・と、この各集塵セクション2内
に多数個づつ吊持されたバグ3・・・と、各集塵セクシ
ョン2の下部に各々配された払い落としダスト除去ホッ
パー4・・・と、各ホッパー4から突設された吸引口5
・・・並びにそれら各吸引口5に接続されたダストガス
導通ダクト6と、上記各集塵セクション2の上端部に設
けられた開閉ダンパー7a付き排気口7・・・並びに開
閉ダンパー8a付き逆洗気流導入口8と、上記各排気口
7に接続された排気ダクト9及びその排気ダクト9端末
に配する一合の排気ブロワ10と、上記各逆洗気流導入
口8に接続された外気取入ダクト11とから構成されて
いる。そして排気ブロワ10の吸引作用で発塵源(図示
せず)からのダストガスをダストガス導入ダクト6を介
して各吸引口5・・・より各ホッパー4内に吸引導通し
、そこから各集塵セクション2・・・内のバグ3に通し
て炉過楠集し、該バグ3外側に抜けた清浄空気は上部排
気口7から排気ダクト9を介し排気ブロワ10より大気
中へ放出する。
Therefore, two expensive blowers were required, which was uneconomical, and the operation of both blowers had to be controlled individually, which was troublesome. Therefore, recently, instead of using a suction blower dedicated to generating backwash airflow for dust removal, only a main exhaust blower is installed to suck and guide the dust gas from the dust source to the dust collection section of the bag filter. A method has been considered in which the suction action of a blower performs both the collection of dust gas and the action of removing dust from each dust collection section. The schematic configuration of a bag filter device that is equipped with only this main exhaust blower and performs dust collection processing and dust removal is described with reference to Fig. 1.The bag filter 1 is divided into a plurality of parts. A dust collection section 2..., a large number of bugs 3 suspended in each dust collection section 2, and a dust removal hopper 4 disposed at the bottom of each dust collection section 2. ...and a suction port 5 protruding from each hopper 4
. . . and a dust gas communication duct 6 connected to each suction port 5, an exhaust port 7 with an opening/closing damper 7a provided at the upper end of each dust collection section 2, and a backwash airflow with an opening/closing damper 8a. An exhaust duct 9 connected to the inlet 8 and each of the exhaust ports 7, a set of exhaust blowers 10 disposed at the terminals of the exhaust duct 9, and an outside air intake duct connected to each of the backwash airflow inlets 8. It consists of 11. Then, by the suction action of the exhaust blower 10, dust gas from a dust source (not shown) is sucked and conducted into each hopper 4 through each suction port 5 through a dust gas introduction duct 6, and from there to each dust collection section. The clean air passing through the bag 3 inside the bag 3 is collected, and the clean air that escapes to the outside of the bag 3 is discharged from the upper exhaust port 7 through the exhaust duct 9 to the atmosphere from the exhaust blower 10.

また、その集塵運転中には各集塵セクション2・・・毎
に夕ィマーによりダンパー開閉切換え機構(図示せず)
を動作させて開閉ダンパー7a,8aを交互に繰返し開
閉せしめ、これにて開閉ダンパー7aを閉じて8aを開
くことにより、当該集塵セクション2内に他の集塵セク
ション2・・・からダストガス導通ダクト6、吸引口5
を介して排気プロワ10の吸引作用を働かせることで、
当該集塵セクション2内にその上部から外気を逆洗気流
として吸引導適すると云った具合にして、その外気の逆
洗気流と通常のダストガス流とを交互に当該集塵セクシ
ョン2内に発生させて、バグ3・・・の収縮・膨張を繰
返して該バグ3・・・に補集されているダストを払い落
として下部ホッパー4内に沈降除去するのである。しか
しながら、上述したメインの排気ブロワ10の吸引作の
みでダストガスの集塵並びにダスト払い落とし作用を行
う方法では、従来同様に電力消費の無駄を少なくすべく
「発塵源からのダストガス発塵量に応じ吸引風量制御機
構(図示せず)により排気ブロヮ10の吸引風量を制御
すると、発塵源の休止時や発塵量が少ない時は排気ブロ
ワ10の吸引風量が最小となるので、その状態の時とタ
イマーによる払い落とし時期が一致した場合は、当該集
塵セクション2の開閉ダンパー7a,8aが開閉切換わ
っても、吸引圧が低いことから当該集塵セクション2内
に所要の逆洗気流が発生せず、従ってダスト払い落とし
を有効に行なえずに、即ちバグ3・・・の再生がなされ
ないままに払い落とし時期が経過してダストガスが導入
されるようになってしまい、このためにバグの圧損抵抗
が異常に上昇して集塵に大きな支障をきたす問題があつ
た。
Also, during the dust collection operation, a damper opening/closing mechanism (not shown) is installed in each dust collection section 2 using a damper.
is operated to repeatedly open and close the opening/closing dampers 7a and 8a, thereby closing the opening/closing damper 7a and opening the opening/closing damper 8a, thereby conducting dust gas from other dust collecting sections 2 into the dust collecting section 2 concerned. Duct 6, suction port 5
By applying the suction action of the exhaust blower 10 through the
Outside air is sucked into the dust collection section 2 from above as a backwash airflow, and a backwash airflow of the outside air and a normal dust gas flow are alternately generated inside the dust collection section 2. By repeating the contraction and expansion of the bags 3, the dust collected on the bags 3 is brushed off and settled in the lower hopper 4 for removal. However, in the above-mentioned method of collecting dust gas and removing dust only by the suction operation of the main exhaust blower 10, in order to reduce wasteful power consumption, as in the past, the amount of dust gas generated from the dust source is If the suction air volume of the exhaust blower 10 is controlled by a suction air volume control mechanism (not shown), the suction air volume of the exhaust blower 10 will be at its minimum when the dust source is at rest or when the amount of dust generated is small. If the time and the timing of dusting off by the timer match, even if the opening/closing dampers 7a and 8a of the dust collection section 2 are switched open and closed, the suction pressure is low, so the required backwash airflow is not generated in the dust collection section 2. Therefore, the dust gas cannot be removed effectively, and the dust gas is introduced after the dust removal period has elapsed without the bug 3... being regenerated. There was a problem in which the pressure drop resistance of the filter increased abnormally, causing a major problem in dust collection.

この発明は上記事情に鑑みなされたもので、発塵源から
のダストガスをその発塵量に応じ吸引風量制御機構によ
り制御される排気ブ。
The present invention has been made in view of the above circumstances, and provides an exhaust blower in which dust gas from a dust source is controlled by a suction air volume control mechanism according to the amount of dust generated.

ワにて各集塵セクションに吸引導通して炉過捕集すると
共に、タイマーにより各集塵セクション毎にダンパー開
閉切換え機構を動作させて上記排気ブロワの吸引により
逆洗気流を起こしてダストの払い落としを行う方法にお
いて、上記ダンバ−開閉切換え機構を吸引風量制御機構
に電気的にインターロックして、発塵源の発塵量の増大
に伴う最大吸引風量制御時と、発塵量の減少に伴う低吸
引風量制御時には、上記タイマーによるダスト払い落と
し時期が来てもダンバー開閉切換え機構を動作させずに
、そのまま各集塵セクションにダストガスの導通を続け
て中間吸引風量制御状態となるまでダスト払い落とし時
期を遅らせることを特徴とし、これにて最大吸引風量時
における炉過風速の上昇則ち、炉過集塵効率の低下を防
止すると共に、低吸引風量制御時の逆洗気流発生圧不足
によるダスト払い落とし不能と言った不祥事態を回避し
て、常に効果的に集塵運転し続けて行けるようにした方
法を提供することにある。以下この発明の方法の一実施
例を説明する。
At the same time, suction is conducted to each dust collection section by a blower to collect the dust in the furnace, and a timer is used to operate a damper opening/closing mechanism for each dust collection section to generate a backwash airflow by suction from the exhaust blower to remove dust. In the method for removing dust, the damper opening/closing switching mechanism is electrically interlocked with the suction air volume control mechanism to control the maximum suction air volume when the amount of dust generated by the dust source increases, and when the amount of dust generated is reduced. During the low suction air volume control, the dust gas is continued to be conducted to each dust collecting section without operating the damper opening/closing switching mechanism even when the time for dust removal by the timer comes, and the dust is removed until the intermediate suction air volume control state is reached. It is characterized by delaying the dropping time, and this prevents an increase in the furnace overflow speed at maximum suction airflow, which in turn prevents the furnace overflow dust collection efficiency from decreasing, and also prevents the generation of backwash airflow from insufficient pressure during low suction airflow control. The object of the present invention is to provide a method that avoids scandals such as inability to remove dust and allows continuous and effective dust collection operation at all times. An embodiment of the method of the present invention will be described below.

なお、ここでは上記第1図に示したバグフィルター1を
用いて発塵源であるコークス炉(図示せず)から発生す
るダストガスを集塵処理する方法を例示する。先ず上記
コークス炉においては、通常第2図に示す如くその炉作
業過程で各種変化する発塵源に応じた吸引風量でもつて
集塵を行う。即ち、コークスケーキ押出しlこ際して炉
蓋取りを行った状態時に窯口よりダストガスが発生する
。この時は排気ブロワ10を中間吸引風量に制御して窯
口集塵を行う。この窯口集塵途中で行われるコークスケ
ーキ押出し作業時はガイド車附近に多量のダストガスが
発生することから、排気ブロワ10を最大吸引風量に制
御してガイド車集塵を行う。又コークスケーキ押出完了
後の装炭作業は装炭口よりダストガスが発生するので、
排気ブロワ10を中間吸引風量に制御して装炭車集塵を
行う。更にガイド車等の各炉作業機器が次の炉へ移動す
る時や休止している時はほとんどダストガスが発生しな
いので、排気ブロワ10を最4・吸引風量に制御して休
止状態となす。なお上記吸引風量の制御を行う吸引風量
制御機構は上記ガイド車等の炉作業機器の動作に応動し
て自動的に例えば流体継手・サィリスタモータ・セルビ
ュースモータ・海式クラッチ等の手段で排気ブロワ10
の回転数をコントロールしたり、或いは排気ブロワ1川
こ組込んだべーンを開閉コントロールしたりして制御す
る。しかして、コークス炉より発生するダストガスを、
その各種炉作業のダストガス発生量に応じた吸引風量で
バグフィルター1の各集塵セクション2・・・に吸引導
通して炉過捕集して行くと共に、その運転中に予め設定
したタイマーによりダンパー開閉切換え機構を動作させ
て各集塵セクション2…毎に次々とダスト払い落としを
行う。
Here, a method of collecting dust gas generated from a coke oven (not shown) which is a source of dust generation using the bag filter 1 shown in FIG. 1 will be exemplified. First, in the above-mentioned coke oven, dust is normally collected using a suction air volume that corresponds to the various dust sources that change during the operation of the oven, as shown in FIG. That is, when the furnace lid is removed during coke cake extrusion, dust gas is generated from the furnace mouth. At this time, the exhaust blower 10 is controlled to an intermediate suction air volume to collect dust at the kiln mouth. Since a large amount of dust gas is generated near the guide car during coke cake extrusion work performed during this furnace mouth dust collection, the guide car dust is collected by controlling the exhaust blower 10 to the maximum suction air volume. In addition, dust gas is generated from the coal charging port during the coal charging operation after coke cake extrusion is completed.
The exhaust blower 10 is controlled to an intermediate suction air volume to collect dust from the coal loading car. Furthermore, since almost no dust gas is generated when each furnace working equipment such as a guide car is moved to the next furnace or is at rest, the exhaust blower 10 is controlled to the maximum suction air volume of 4.0 and the furnace is at rest. The suction air volume control mechanism that controls the suction air volume automatically controls the exhaust blower by means of a fluid coupling, a thyristor motor, a Serbus motor, a marine clutch, etc. in response to the operation of the furnace working equipment such as the guide car. 10
It is controlled by controlling the rotation speed of the exhaust blower, or by controlling the opening and closing of the vanes built into the exhaust blower. Therefore, the dust gas generated from the coke oven,
The suction air volume corresponding to the amount of dust gas generated during the various furnace operations is conducted to each dust collection section 2 of the bag filter 1 to over-collect the furnace. The opening/closing switching mechanism is operated to remove dust from each dust collecting section 2 one after another.

この際ダンパー開閉切換え機構は吸引風量制御機構に電
気的にインターロックして、タイマーによるダスト払い
落とし時期が第3図に示す如く装炭車集塵時等の排気ブ
ロワ10が中間吸引風量に制御されている状態時と一致
した場合のみ、ダンパー開閉切換え機構を動作させて当
該集塵セクション2の開閉ダンパ−7a,8aを相互に
開閉せしめ、これにて外気による逆洗気流とダストガス
流を交互に繰返し発生させてバグ3・・・のダストを払
い落として該バグ3・・・の再生を行い、それ以外のガ
イド車集塵時の最大吸引風量状態の制御時と休止時及び
最小吸引風量状態の制御時に上記タイマーによるダスト
払い落とし時期が来た場合には、ダンパー開閉切換え機
構を動作させずにそのまま遅延して通常の集塵運転を続
け、そして排気ブロワ10が上述した中間吸引風量に制
御される状態となった時点でダンパー開閉切換え機構を
動作させて上記同様にダスト払い落としを行う。なお、
上記実施例ではコークス炉の集塵方法を述べたが、これ
のみに限定されることなく、その他電気炉等の各種発塵
源からのダストガス集塵にも適用可である。
At this time, the damper opening/closing switching mechanism is electrically interlocked with the suction air volume control mechanism, and the dust blowing timing by the timer is controlled to an intermediate suction air volume by the exhaust blower 10 during dust collection of the coal loading car, etc., as shown in FIG. Only when the state is the same as the state in which The bug 3... is generated repeatedly and the dust from it is brushed off to regenerate the bug 3..., and the maximum suction air volume state during other guide car dust collection is controlled, when it is stopped, and the minimum suction air volume state. When the time for dust removal by the above-mentioned timer comes during the control, the damper opening/closing switching mechanism is not operated and normal dust collection operation is continued without operating, and the exhaust blower 10 is controlled to the above-mentioned intermediate suction air volume. When this state is reached, the damper opening/closing switching mechanism is operated to remove dust in the same manner as above. In addition,
Although the above embodiment describes a method for collecting dust from a coke oven, the present invention is not limited to this, and can also be applied to collecting dust gas from various dust sources such as electric furnaces.

この発明の方法は以上詳述した如くなしたから、発塵源
の発塵量に応じ吸引風量が制御されるメインの排気ブロ
ワのみの吸引によりダストガスを導通して炉過橘集する
と共に、逆洗気流を起こしてバグの橘集ダストの払い落
としを行うのであるが、そのダスト払い落とし時期をタ
イマーで設定すると共に吸引風量制御機構に電気的にイ
ンターロックして最大吸引風量時と所定以下の低吸引風
量時には該ダスト払い落とし動作を行わないようにした
ので、最大吸引風量時における炉過風速の上昇良Pち、
炉過集塵効率の低下を防止できる上に、低吸引風量時の
逆洗気流発生圧不足によるダスト払い落とし不能と言っ
た不祥事態の回避を図ることができて、常に効果的な集
塵運転を続けて行くことができることとなる。
Since the method of this invention is performed as described in detail above, the dust gas is passed through the furnace by suction only by the main exhaust blower whose suction air volume is controlled according to the amount of dust generated by the dust source, and the dust gas is collected through the furnace. The system uses a timer to set the timing of dust removal, and also electrically interlocks the suction air volume control mechanism to set the time when the suction air volume is at maximum and when it is below a certain level. Since the dust removal operation is not performed when the suction air volume is low, the increase in the furnace overflow speed at the maximum suction air volume is reduced.
In addition to preventing excessive dust collection efficiency from decreasing in the furnace, it is also possible to avoid problems such as inability to remove dust due to insufficient backwash air flow generation pressure at low suction air volumes, resulting in always effective dust collection operation. This means that you can continue to do so.

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

第1図はこの発明の方法に用いたバグフィルター装置の
概略的構成図、第2図はこの発明の方法の一実施例を示
す発塵源であるコークス炉の各炉作業過程における各集
塵時の吸引風量状態をタイムフローチャート的に示す説
明図、第3図は同実施例におけるバグ内圧をタイムフロ
ーチャート的に示す説明図である。 1・・・バグフィルター、2・・・集塵セクション、3
…バグ、10…排気ブロワ、7a,8a…開閉ダン/f
−o第1図 第2図 第3図
Fig. 1 is a schematic diagram of a bag filter device used in the method of the present invention, and Fig. 2 is a diagram showing an embodiment of the method of the present invention. FIG. 3 is an explanatory diagram illustrating the suction air volume state in a time flow chart at the time of the operation, and FIG. 3 is an explanatory diagram illustrating the bag internal pressure in the same embodiment in a time flow chart. 1... Bag filter, 2... Dust collection section, 3
...bug, 10...exhaust blower, 7a, 8a...opening/closing dan/f
-oFigure 1Figure 2Figure 3

Claims (1)

【特許請求の範囲】[Claims] 1 発塵源からのダストガスを、その発塵量に応じ吸引
風量制御機構によりバグフイルターの複数に分割された
各集塵セクシヨン内に吸引導通し、その集塵セクシヨン
内の多数のバグで濾過捕集すると共に、これにて清浄化
された空気は上記排気ブロワを介して外部に排出し、バ
グに捕集したダストはタイマーにより各集塵セクシヨン
毎にダンバー開閉切換え機構を動作させて上記排気ブロ
ワの吸引で逆洗気流を起こして払い落として除去し、一
方上記吸引風量制御機構にダンバー開閉切換え機構を電
気的にインターロツクし、発塵源の発塵量の増大に伴い
排気ブロワを最大吸引風量に制御している時と、発塵量
が減少して排気ブロワをこの吸引による逆洗気流発生圧
以下の低吸引風量に制御している時には、上記タイマー
によるダスト払い落とし時期が来てもダンパー開閉切換
え機構を動作させずに、そのまま各集塵セクシヨンにダ
ストガスの導通を続けて中間吸引風量に制御されるまで
ダスト払い落とし時期を遅らせることを特徴とするバグ
フイルターを用いた集塵方法。
1 Dust gas from a dust generation source is sucked and conducted into each dust collection section divided into multiple parts of the bag filter by a suction air volume control mechanism according to the amount of dust generated, and is filtered and captured by a large number of dust collection sections in the dust collection section. At the same time, the purified air is discharged to the outside via the exhaust blower, and the dust collected in the bugs is removed by the exhaust blower by operating the damper opening/closing mechanism for each dust collection section using a timer. At the same time, the suction airflow control mechanism is electrically interlocked with the damper opening/closing switching mechanism, and the exhaust blower is turned to maximum suction as the amount of dust from the dust source increases. When the air volume is controlled to a low level, or when the amount of dust generated decreases and the exhaust blower is controlled to a low suction air volume that is less than the backwash air flow generation pressure due to this suction, even when the time for dust removal by the above timer comes. This dust collection method using a bag filter is characterized in that dust gas is continued to be conducted to each dust collection section without operating a damper opening/closing switching mechanism, and the timing of dust removal is delayed until the dust collection air volume is controlled to an intermediate suction air volume.
JP15269481A 1981-09-26 1981-09-26 Dust collection method using bug filter Expired JPS601044B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15269481A JPS601044B2 (en) 1981-09-26 1981-09-26 Dust collection method using bug filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15269481A JPS601044B2 (en) 1981-09-26 1981-09-26 Dust collection method using bug filter

Publications (2)

Publication Number Publication Date
JPS5855023A JPS5855023A (en) 1983-04-01
JPS601044B2 true JPS601044B2 (en) 1985-01-11

Family

ID=15546091

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15269481A Expired JPS601044B2 (en) 1981-09-26 1981-09-26 Dust collection method using bug filter

Country Status (1)

Country Link
JP (1) JPS601044B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6262621A (en) * 1985-09-13 1987-03-19 Sankusu Kk Photoelectric switch

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2709726B2 (en) * 1988-09-30 1998-02-04 エービービー株式会社 How to detect damage on cloth in bag filter
EP0887195B1 (en) 1996-03-04 2003-01-29 Copyer Co., Ltd. Image forming device
JP4654530B2 (en) * 2001-04-16 2011-03-23 五洲薬品株式会社 Simple foot bath device
JP2011242055A (en) * 2010-05-18 2011-12-01 Daido Steel Co Ltd Operation method of dust collector for arc furnace

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6262621A (en) * 1985-09-13 1987-03-19 Sankusu Kk Photoelectric switch

Also Published As

Publication number Publication date
JPS5855023A (en) 1983-04-01

Similar Documents

Publication Publication Date Title
JP3835810B2 (en) Capture of emissions when charging coke oven
CN101469938A (en) Flue gas purification and residual heat utilization method and apparatus for silicon-aluminum alloy electric furnace
JPS601044B2 (en) Dust collection method using bug filter
JP2518576B2 (en) Control method of bag filter device
CN203518640U (en) Smoke collection and prevention and dust removal device for AOD smelting furnace and medium frequency smelting furnace
CN1830520A (en) Cylindrical self-suction glass fiber bag type dust separator
CN208145638U (en) A kind of atmosphere backblown cloth-bag dust collector and roller drying device
CN207576043U (en) Calcination, fluidization stove dust-extraction unit
CN207146423U (en) A kind of preposition device for reducing dust of boiler back end ductwork
CN211302375U (en) Pulse bag type dust collector
CN101590351B (en) Static hop-pocket mixed dust removal device and control method thereof
CN211601596U (en) High-temperature dust removal system of brown corundum high-temperature smelting furnace
CN2626585Y (en) Glass fiber bag-type dust collector
CN206897044U (en) AB sack cleaners
CN205461469U (en) Strain locellus blowback bag collector in inertia
RU2256489C1 (en) Method of controlling bag filter
CN217119622U (en) Bag-type dust collector atmosphere blowback system
JP4673512B2 (en) Bag filter type dust collection stabilization method
CN217297730U (en) Dry quenching system and dust remover thereof
CN211025509U (en) Ash removal device for cloth bag of dust collector
CN109603356A (en) Empty blowback bag-type dust collector and its dedusting control method are pressed in the passive heating of one kind
CN109173470A (en) Deashing device and modularization deduster
CN216320596U (en) Smoke dust discharging device with back-blowing mechanism
CN215962794U (en) Aluminum ingot furnace waste gas dust collector
CN217139939U (en) Coke oven coal-charging dust removal flue gas desulfurization system