JPS60114320A - Dust collector in asphalt plant or the like - Google Patents

Dust collector in asphalt plant or the like

Info

Publication number
JPS60114320A
JPS60114320A JP58221787A JP22178783A JPS60114320A JP S60114320 A JPS60114320 A JP S60114320A JP 58221787 A JP58221787 A JP 58221787A JP 22178783 A JP22178783 A JP 22178783A JP S60114320 A JPS60114320 A JP S60114320A
Authority
JP
Japan
Prior art keywords
dust collector
duct
exhaust gas
dust
waste gas
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
JP58221787A
Other languages
Japanese (ja)
Other versions
JPH0123166B2 (en
Inventor
Sadao Seki
関 貞夫
Suzuo Kayano
茅野 鈴雄
Yoichi Shidara
設楽 洋一
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.)
Niigata Engineering Co Ltd
Original Assignee
Niigata 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 Niigata Engineering Co Ltd filed Critical Niigata Engineering Co Ltd
Priority to JP58221787A priority Critical patent/JPS60114320A/en
Publication of JPS60114320A publication Critical patent/JPS60114320A/en
Publication of JPH0123166B2 publication Critical patent/JPH0123166B2/ja
Granted legal-status Critical Current

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  • Filtering Of Dispersed Particles In Gases (AREA)

Abstract

PURPOSE:To obtain the titled collector with high dust collection efficiency, a simple structure, and a small loss of heat energy which is easy to manufacture by uniting the first and the second dust collector to a body, allowing a duct to pass through the second dust collector and to communicate with the first dust collector. CONSTITUTION:The waste gas discharged from an aggregate dryer 11 is introduced into a duct 17 in a dust collector 10 from a waste gas inlet 17a through a connecting duct, passed through the duct 17, and sent into the first dust collector 14. The waste gas is spiraled along the outer circumference of an inner cylinder 20, and sent into a filtration chamber X of the second dust collector 15 through the inside of the inner cylinder 20. The fine particle components of the dust contained in the waste gas are collected by a filter cloth 16, and the waste gas is purified. Then the purified gas is sent into a gas purifying chamber Y through a venturi sheet 21. The waste gas is discharged to the outside from a stack 13 through a purified gas outlet 22 by an exhaust fan 12.

Description

【発明の詳細な説明】 本発明は、主としてアスファルトプラントから発生する
排気ガス中のダスト(粉塵)を分離捕集する集塵装置に
関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a dust collector that separates and collects dust in exhaust gas mainly generated from an asphalt plant.

従来、アスファルトプラントの骨材乾燥炉から発生する
排ガスを処理する装置は、第1図〜第3図に示すように
骨材乾燥炉AとサイクロンCとがダクトBを介して、か
つサイクロンCとバッグフィルタEとがダク)Dを介し
てそれぞれ連結されていると共に、バッグフィルタEに
排風機Fと煙突Gとが連設されて成り、骨材乾燥炉A内
の排ガスはダクトBによってサイクロンC内に導かれ、
サイクロンC内で排ガス中の粗粒子成分が捕集されて、
サイクロンCの下部から回収されると共に、サイクロン
C内を通った排ガスはダクトDによってバッグフィルタ
E内に送られて、バッグフィルタE内で排ガス中の微粒
子成分が捕集されて、バッグフィルタEの下部に設けら
れたスクリュコンベア1及びロータリバルブ2を介して
回収され、かつバッグフィルタE内で浄化された排ガス
は排風機Fを介して煙突Gから排出されるようになって
いる◎ しかしながら、上記のように構成された装置にあっては
、骨材乾燥炉AとサイクロンCとの間のダクトB及びサ
イクロンCとバッグフィルタEとの間のダク)Dは外部
に露出しているため、これらのダク)B、Dから外部に
逃げる放散熱が、例えば1頗プラントにおいて約10X
10’ 1cal/hと大きく、エネルギー損失が極め
て大きいという問題があり、排ガスの保有熱エネルギー
が何ら回収されずに非常に無駄になっていると共に、ダ
クトB、nによって排ガスがあまり冷却されると、バッ
グフィルタE内で排ガス中に含まれる水蒸気が凝結して
、バッグフィルタE内の濾布3を目詰まりさせて、バッ
グフィルタEの集塵効率を低下させるおそれがある。壕
だ、サイクロンC及びバッグフィルタEとダク)B、D
との接合部は、ダクトBのフランジ部4とサイクロンC
のガス入口部のフランジ部5とが、かつサイクロンCの
排ガス出口部の7ランク部6とダクトDの一端のフラン
ジ部7とが、さらにダクトDの他端の7ランク部8とバ
ッグフィルタEのガス入口部のフランジ部9とが、それ
ぞれボルト等によって連結されるように構成されている
ため、各部の加工及び組立作業に手間がかかり、設備費
が多大になるという問題がある。
Conventionally, in a device for treating exhaust gas generated from an aggregate drying furnace of an asphalt plant, an aggregate drying furnace A and a cyclone C are connected via a duct B, and a cyclone C and a The bag filter E is connected to the bag filter E through a duct D, and the bag filter E is connected to an exhaust fan F and a chimney G. Guided within;
Coarse particle components in the exhaust gas are collected in cyclone C,
The exhaust gas that is collected from the lower part of the cyclone C and passed through the cyclone C is sent to the bag filter E through the duct D, where the particulate components in the exhaust gas are collected and the exhaust gas is collected by the bag filter E. The exhaust gas collected via the screw conveyor 1 and rotary valve 2 provided at the bottom and purified in the bag filter E is discharged from the chimney G via the exhaust fan F.◎ However, the above In a device configured as shown in the figure, the duct B between the aggregate drying oven A and the cyclone C and the duct D between the cyclone C and the bag filter E are exposed to the outside. The radiated heat escaping from B and D to the outside is approximately 10X in one plant, for example.
10' 1cal/h, and there is a problem that the energy loss is extremely large, and the thermal energy retained in the exhaust gas is not recovered at all and is wasted, and if the exhaust gas is not cooled too much by the ducts B and n. There is a possibility that the water vapor contained in the exhaust gas condenses in the bag filter E, clogging the filter cloth 3 in the bag filter E, and reducing the dust collection efficiency of the bag filter E. It's a trench, cyclone C and bag filter E and duct) B, D
The joint between the flange part 4 of the duct B and the cyclone C
The flange part 5 at the gas inlet of the cyclone C, the 7-rank part 6 at the exhaust gas outlet of the cyclone C, the flange part 7 at one end of the duct D, and the 7-rank part 8 at the other end of the duct D and the bag filter E. Since the flange portions 9 of the gas inlet portions of the gas inlet portion are connected to each other by bolts or the like, there is a problem in that processing and assembling each portion takes time and effort, and equipment costs increase.

本発明は、排ガス中の粗粒子を捕集する第1集塵機と上
記排ガス中の微粒子を捕集する第2集塵機とを一体的に
設け、かつ排ガス発生源からのダクトを上記第2集塵機
内を貫通して上記第1集塵機に連設することにより、上
記従来の問題を解消したもので、構造が簡単で、製作が
容易な上に、排ガスが保有する熱エネルギーを損失する
ことが少なく、集塵効率の極めて高いアスファルトプラ
ント等における集塵装置を提供することを目的とする。
The present invention provides a first dust collector for collecting coarse particles in the exhaust gas and a second dust collector for collecting fine particles in the exhaust gas, and a duct from the exhaust gas generation source is connected to the inside of the second dust collector. By penetrating the dust collector and connecting it to the first dust collector, the above conventional problems are solved.The structure is simple and easy to manufacture, and there is less loss of heat energy held by the exhaust gas, making it easier to collect. The purpose of this invention is to provide a dust collector for asphalt plants etc. that has extremely high dust efficiency.

以下、図面を参照して本発明を具体的に説明する。Hereinafter, the present invention will be specifically explained with reference to the drawings.

第4叉ないし第7図は本発明の一実施例を示すもので、
図中符号1(1:本考案に係る集塵装置であり、この集
塵装置10はアスファルトプラントの骨材乾燥炉11内
の排気ガスからダスト(粉塵)を捕集して、浄化した排
気ガスを排風機12を介して煙突13から外部に排出す
るように構成されている。
FIGS. 4 to 7 show an embodiment of the present invention,
Reference numeral 1 in the figure (1: indicates a dust collector according to the present invention, and this dust collector 10 collects dust from exhaust gas in an aggregate drying furnace 11 of an asphalt plant, and purifies the exhaust gas. is configured to be discharged to the outside from a chimney 13 via an exhaust fan 12.

上記集塵袋ft1oは、排気ガス中の粗粒子を遠心力あ
るいは慣性力を利用して捕集する第1集塵機14と排気
ガス中の微粒子を濾過することにより捕集する第2集塵
機15とが集塵機本体Bに一体的に連結されていると共
に、第1集塵機14が、第2集塵機15の複数の濾布1
6を配設した濾過室Xの一方の側面上部(第5図におい
て右側面上部)から濾過室Xの他方の側面下部(第5図
において左側面下部)にかけて、濾過室X内部を貫通し
て設けられているダクト17に連結されて構成されてい
る。また、第1集塵機14ば、上記第2集塵機15の濾
過室Xと第1集塵機14とを仕切る仕切壁18の下面に
固設された外筒19と、仕切壁18の中央部に穿設され
た孔に上端を嵌入させた内筒20とから構成されており
、第1集塵機14の下部の一対のダスト回収部14bu
その上端が、前記集塵機本体Bの一側下部にフランジ結
合されており、その下端には捕集したダストを回収する
捕集口14aが設けられている。さらに、第2集塵機1
5の濾過室Xの上部に、ベンチュリシート21を介して
浄化ガス室Yが設けられており、浄化ガス室Yの一方の
側壁(第5図において右側壁)に浄化ガス出口22が形
成されている。
The dust collection bag ft1o has a first dust collector 14 that collects coarse particles in exhaust gas using centrifugal force or inertial force, and a second dust collector 15 that collects fine particles in exhaust gas by filtering them. The first dust collector 14 is integrally connected to the dust collector main body B, and the first dust collector 14 is connected to the plurality of filter cloths 1 of the second dust collector 15.
6 is arranged, from the upper part of one side of the filtration chamber X (upper right side in Figure 5) to the lower part of the other side of the filtration chamber It is configured to be connected to a duct 17 provided. The first dust collector 14 also includes an outer cylinder 19 fixed to the lower surface of the partition wall 18 that partitions the filtration chamber X of the second dust collector 15 and the first dust collector 14, and an outer cylinder 19 that is bored in the center of the partition wall 18. and an inner cylinder 20 whose upper end is fitted into a hole, and a pair of dust collection parts 14bu at the lower part of the first dust collector 14.
Its upper end is flanged to the lower part of one side of the dust collector main body B, and its lower end is provided with a collection port 14a for collecting the collected dust. Furthermore, the second dust collector 1
A purified gas chamber Y is provided above the filtration chamber There is.

そして、第2集塵機15の下部のダスト捕集部15aは
、その上端が前記集塵機本体Bの下端にフランジ結合さ
れており、その下端には、捕集したダストを移送するス
クリュコンベア23と、このスクリュコンベア23に連
結されたロータリバルブ24とが設けられている。
The upper end of the lower dust collecting section 15a of the second dust collector 15 is flange-bonded to the lower end of the dust collector main body B, and the lower end includes a screw conveyor 23 for transferring the collected dust, and a screw conveyor 23 for transferring the collected dust. A rotary valve 24 connected to the screw conveyor 23 is provided.

上記ダクト17の排気ガス人口17a側は、接続ダクト
(図示せず)を介して、排気ガスの発生源であるアスフ
ァルトプラントの骨材乾燥炉11に接続され、また、該
排気ガス人口17a側に、バイパスダクト25が、ダク
ト17がら分岐して浄化ガス室Yに連通しており、この
バイパスダクト25の浄化ガス室Y側に開口したガス出
口25&には、開閉蓋26が設けられている。この開閉
蓋26は、その取手26aにロッド27aの先端が取付
けられ、かつシリンダ本体27bが取付部材28を介し
て第2集塵機15の上面に取付けられタシリンタ装置2
7により、上下に移動されて上記ガス出口25aを開閉
するようになっている。
The exhaust gas population 17a side of the duct 17 is connected to the aggregate drying furnace 11 of the asphalt plant, which is the source of exhaust gas, through a connecting duct (not shown), and the exhaust gas population 17a side is A bypass duct 25 branches off from the duct 17 and communicates with the purification gas chamber Y, and a gas outlet 25& of the bypass duct 25 that opens toward the purification gas chamber Y side is provided with an opening/closing lid 26. This opening/closing lid 26 has a handle 26a attached to the tip of a rod 27a, and a cylinder body 27b attached to the upper surface of the second dust collector 15 via a mounting member 28.
7, it is moved up and down to open and close the gas outlet 25a.

次に、上記のように構成された集塵装置の作用について
説明する。
Next, the operation of the dust collector configured as described above will be explained.

まず、アスファルトプラントの骨材乾燥炉11が通常運
転をしている状態においては、シリンダ装置27により
、開閉蓋26は閉じられており、骨材乾燥炉11から排
出された排気ガスは、接続ダクト(図示せず)を経て集
塵装置10のダクト17の排気ガス入口17aから導き
入れられ、ダクト17内を通って第1集塵機14に送ら
れる。
First, when the aggregate drying furnace 11 of the asphalt plant is in normal operation, the opening/closing lid 26 is closed by the cylinder device 27, and the exhaust gas discharged from the aggregate drying furnace 11 is passed through the connecting duct. (not shown), is introduced from the exhaust gas inlet 17a of the duct 17 of the dust collector 10, passes through the inside of the duct 17, and is sent to the first dust collector 14.

ダクト17内を排気ガスが通過する際、排気ガスの保有
する熱は、ダクト17を介して第2集塵機15の濾過室
X内に伝わり、濾過室X内を暖める。
When the exhaust gas passes through the duct 17, the heat held by the exhaust gas is transmitted to the filtration chamber X of the second dust collector 15 through the duct 17, thereby warming the inside of the filtration chamber X.

そして、ダクト17内を通って第1集塵機14内に送ら
れた排ガスは、内筒20の外周に沿って旋回した後、内
筒20の内部を通って第2集塵機15の濾過室Xに送ら
れる。この時、排気ガスの中に含まれるダストのうち粗
粒子成分は、第1集塵機14の下部の捕集口14aから
回収され骨材の一部として再利用される。さらに、第2
集塵機15の濾過室X内に送られた排気ガスは、濾布1
6によって排気ガス中に含まれるダストのうち微粒子成
分を捕集されて浄化され、ベンチュリシート21を通っ
て浄化ガス室Yに送られる。この時、捕集された微粒子
成分は、第2集塵機15の下部にたまり、スクリュコン
ベア23によって一端に移送されて、ロータリバルブ2
4を介して回収され石粉の一部として再利用される。浄
化ガス室Yに送られた排気ガスは、浄化ガス出口22を
通って、排風機12により、煙突13から外部に排出さ
れる。
Then, the exhaust gas sent into the first dust collector 14 through the inside of the duct 17 turns around along the outer periphery of the inner cylinder 20 and is then sent to the filtration chamber X of the second dust collector 15 through the inside of the inner cylinder 20. It will be done. At this time, coarse particle components of the dust contained in the exhaust gas are collected from the collection port 14a at the bottom of the first dust collector 14 and reused as part of the aggregate. Furthermore, the second
The exhaust gas sent into the filtration chamber X of the dust collector 15 is filtered through the filter cloth 1
6, particulate components of the dust contained in the exhaust gas are collected and purified, and sent to the purified gas chamber Y through the venturi sheet 21. At this time, the collected particulate components accumulate at the bottom of the second dust collector 15, are transferred to one end by the screw conveyor 23, and are transferred to the rotary valve 2.
4 and reused as part of stone powder. The exhaust gas sent to the purified gas chamber Y passes through the purified gas outlet 22 and is discharged to the outside from the chimney 13 by the exhaust fan 12.

寸た、アスファルトプラントの骨材乾燥炉11内を加熱
するバーナ装置調整時あるいは不具合時に発生する未燃
ミスト(液状成分)は、従来のノックアウトボックス等
のプレダスタでは、はとんど捕集されず9.プレダスタ
の後段に配置されているバッグフィルタの濾布を損傷し
て集塵効率を低下させていたが、本考案にかかる集塵装
置においては、ダクト17あるいは遠心力、慣性力利用
の第1集塵機14に未燃ミストが吸着されるため、第2
集塵機15の濾布16に未燃ミストが吸着することはな
く、集塵効率を低下させることはない。
In addition, unburned mist (liquid component) generated when adjusting or malfunctioning the burner device that heats the inside of the aggregate drying furnace 11 of an asphalt plant is rarely collected by pre-dusters such as conventional knockout boxes. 9. The filter cloth of the bag filter placed after the pre-duster was damaged and the dust collection efficiency was reduced, but in the dust collector according to the present invention, the first dust collector using the duct 17 or centrifugal force or inertial force Since unburned mist is adsorbed by the second
Unburnt mist will not be adsorbed to the filter cloth 16 of the dust collector 15, and the dust collection efficiency will not be reduced.

さらに、バーナ調整時に、未燃ミストによッテ第2集塵
機15の濾布16が焼損するおそれがある場合には、一
時的にシリンダ装置27を作動させて、開閉蓋26を開
き、ダクト17と浄化ガス室Yを連通させ、排気ガスが
直接浄化ガス出口22から排出されるようにする。
Furthermore, when adjusting the burner, if there is a risk that the filter cloth 16 of the second dust collector 15 may be burnt due to unburned mist, the cylinder device 27 is temporarily activated, the opening/closing lid 26 is opened, and the duct 17 is opened. and the purified gas chamber Y, so that the exhaust gas is directly discharged from the purified gas outlet 22.

なお、本発明に係る集塵装置10はアスファルトプラン
トの骨材乾燥炉11から発生する排気ガスの浄化に使用
されるだけでなく、ドラムミキサやアスファルト再生プ
ラント等に使用してもよく、また、一般に排気ガスから
ダスト(粉塵)を捕集する必要がある場合に用いること
ができる。
Incidentally, the dust collector 10 according to the present invention is not only used for purifying exhaust gas generated from the aggregate drying furnace 11 of an asphalt plant, but also can be used for a drum mixer, an asphalt regeneration plant, etc. It can be used when it is necessary to collect dust from exhaust gas.

以上、説明したように、本発明は、排ガス中に含まれる
粗粒子を捕集する第1集塵機と、上記排ガス中の微粒子
を捕集する第2集塵機とを一体的に設け、かつダクトを
上記第2集塵機内を貫通して上記第1集塵機に連設した
ものであるから、従来装置に比べて設置するダクトを少
なくすることができ、部品数の削減をはかれ、構造が簡
単で製作が容易な一部に、外部に熱を放散することが少
なく、ガスの持つ熱エネルギーを損失することが少ない
。また、ダクトが第2集塵機内を通るので、第2集塵機
が暖められ、集塵機内で温度低下による水蒸気の凝結が
起らず、集塵機が目詰まりすることがない。従って、集
塵効率を高く維持することができる等優れた効果を有す
る。
As explained above, the present invention provides a first dust collector that collects coarse particles contained in exhaust gas, and a second dust collector that collects fine particles contained in the exhaust gas, and a duct that Since it penetrates through the second dust collector and is connected to the first dust collector, it is possible to reduce the number of ducts to be installed compared to conventional equipment, reduce the number of parts, and have a simple structure and easy manufacturing. One of the advantages is that less heat is dissipated to the outside, and the thermal energy of the gas is less likely to be lost. Furthermore, since the duct passes through the second dust collector, the second dust collector is warmed, and water vapor does not condense within the dust collector due to a drop in temperature, so that the dust collector does not become clogged. Therefore, it has excellent effects such as being able to maintain high dust collection efficiency.

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

第1図ないし第3図は従来の集塵装置を示すもので、第
1図は排ガス処理の系統図、第2図は正面図、第3図は
側面図、第4図ないし第7図は本発明の一実施例を示す
もので、第4図は系統図、第5図は正面図、第6図は側
面図、第7図は第5図の■−■線に沿う断面図である。 14・・・・・第1集塵機、15・・・・・第2集塵機
、17・・・・・ダクト。 出願人 株式会社 新潟鉄工所 代理人 弁理士 志 習 正 、J”’@。
Figures 1 to 3 show conventional dust collectors. Figure 1 is a system diagram for exhaust gas treatment, Figure 2 is a front view, Figure 3 is a side view, and Figures 4 to 7 are Fig. 4 is a system diagram, Fig. 5 is a front view, Fig. 6 is a side view, and Fig. 7 is a sectional view taken along the line ■-■ in Fig. 5, showing one embodiment of the present invention. . 14...First dust collector, 15...Second dust collector, 17...Duct. Applicant: Niigata Iron Works Co., Ltd. Representative: Patent Attorney: Tadashi Shi Xi, J”'@.

Claims (1)

【特許請求の範囲】[Claims] 塵機とが上記第1集塵機の排ガス出口を上記第2集塵機
の排ガス入口に直結して一体的に設けられ、上記排ガス
を上記第1集塵機内に導くダクトが上記第2集塵機内を
貫通して上記第1集塵機に連設されて成ることを特徴と
するアスファルトプラント等における集塵装置。
A dust collector is integrally provided with the exhaust gas outlet of the first dust collector directly connected to the exhaust gas inlet of the second dust collector, and a duct for guiding the exhaust gas into the first dust collector passes through the inside of the second dust collector. A dust collector in an asphalt plant, etc., characterized in that it is connected to the first dust collector.
JP58221787A 1983-11-25 1983-11-25 Dust collector in asphalt plant or the like Granted JPS60114320A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58221787A JPS60114320A (en) 1983-11-25 1983-11-25 Dust collector in asphalt plant or the like

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58221787A JPS60114320A (en) 1983-11-25 1983-11-25 Dust collector in asphalt plant or the like

Publications (2)

Publication Number Publication Date
JPS60114320A true JPS60114320A (en) 1985-06-20
JPH0123166B2 JPH0123166B2 (en) 1989-05-01

Family

ID=16772192

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58221787A Granted JPS60114320A (en) 1983-11-25 1983-11-25 Dust collector in asphalt plant or the like

Country Status (1)

Country Link
JP (1) JPS60114320A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0588622U (en) * 1992-04-27 1993-12-03 兼松エンジニアリング株式会社 Dry powder suction pumping tank
JP2008030010A (en) * 2006-07-27 2008-02-14 Shinroku Nishiyama Deodorizing method employing bag filter type dust collector and deodorizing device for bag filter type dust collector
WO2008056405A1 (en) * 2006-11-06 2008-05-15 Mitsubishi Heavy Industries, Ltd. Dust collector
CN102872672A (en) * 2012-10-18 2013-01-16 无锡锡通工程机械有限公司 Environment-friendly dust removing device of asphalt mixture equipment
US20130217535A1 (en) * 2010-08-31 2013-08-22 Ishibashi Manufacturing, Co., Ltd. Planetary gear train with thrust collar used as thrust bearing of planetary gear and wind turbine generator incorporating the same
CN110575716A (en) * 2019-10-11 2019-12-17 江苏润广环保科技有限公司 Environment-friendly dust collection and filtration device

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS439185Y1 (en) * 1967-07-06 1968-04-22
JPS5610315A (en) * 1979-07-06 1981-02-02 Nichidoku Jukogyo Kk Dust collector

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS439185Y1 (en) * 1967-07-06 1968-04-22
JPS5610315A (en) * 1979-07-06 1981-02-02 Nichidoku Jukogyo Kk Dust collector

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0588622U (en) * 1992-04-27 1993-12-03 兼松エンジニアリング株式会社 Dry powder suction pumping tank
JP2008030010A (en) * 2006-07-27 2008-02-14 Shinroku Nishiyama Deodorizing method employing bag filter type dust collector and deodorizing device for bag filter type dust collector
WO2008056405A1 (en) * 2006-11-06 2008-05-15 Mitsubishi Heavy Industries, Ltd. Dust collector
US8551204B2 (en) 2006-11-06 2013-10-08 Mitsubishi Heavy Industries, Ltd. Dust collector
US20130217535A1 (en) * 2010-08-31 2013-08-22 Ishibashi Manufacturing, Co., Ltd. Planetary gear train with thrust collar used as thrust bearing of planetary gear and wind turbine generator incorporating the same
US8932177B2 (en) * 2010-08-31 2015-01-13 Mitsubishi Heavy Industries, Ltd. Planetary gear train with thrust collar used as thrust bearing of planetary gear and wind turbine generator incorporating the same
CN102872672A (en) * 2012-10-18 2013-01-16 无锡锡通工程机械有限公司 Environment-friendly dust removing device of asphalt mixture equipment
CN110575716A (en) * 2019-10-11 2019-12-17 江苏润广环保科技有限公司 Environment-friendly dust collection and filtration device

Also Published As

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