JPS5912729A - Dust removing apparatus - Google Patents
Dust removing apparatusInfo
- Publication number
- JPS5912729A JPS5912729A JP12093982A JP12093982A JPS5912729A JP S5912729 A JPS5912729 A JP S5912729A JP 12093982 A JP12093982 A JP 12093982A JP 12093982 A JP12093982 A JP 12093982A JP S5912729 A JPS5912729 A JP S5912729A
- Authority
- JP
- Japan
- Prior art keywords
- cylinder
- granular material
- exhaust gas
- combustion exhaust
- screw plate
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Landscapes
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
Description
【発明の詳細な説明】
〔発明の技術分野〕
本発明は、ボイラー、焼却炉等の燃焼装置から発生する
燃焼排ガス中に含ま幻る塵を除去する除塵装置に関する
ものである。DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to a dust removal device for removing dust contained in combustion exhaust gas generated from a combustion device such as a boiler or an incinerator.
気体中に含まれる塵を除去するものとしては種種の装置
があるが、電気集塵機は高価であり、そして、バグフィ
ルタ−は含塵気体の温度が高い場合にはフィルターが高
価になり、しかも耐久性に問題があり、また、スクラバ
ーは水処理設備を必要とするので経済的でなく、また、
慣性、重力及び遠心力等を利用する集塵装置は能力に限
界があり、いずれの@置も、ボイラー、焼却炉等から発
生する燃焼排ガスを処理するには問題がふった。There are various types of devices that remove dust contained in gas, but electrostatic precipitators are expensive, and bag filters are expensive and durable when the temperature of the dust-containing gas is high. In addition, scrubbers are not economical because they require water treatment equipment, and
Dust collectors that use inertia, gravity, centrifugal force, etc. have limited capacity, and all of them have problems in treating combustion exhaust gas generated from boilers, incinerators, etc.
本発明は、上述したような点に@みなされたもので、高
温の燃焼排ガスの処理ができ、しかも能力も高い除塵装
置を安価に提供することを目的とし、さらに、除塵作業
中にフィルターの交換を行なうようにして除塵作業を連
続的に行なえるようrjるものであ4)。The present invention has been made in view of the above-mentioned points, and aims to provide a dust removal device that can treat high temperature combustion exhaust gas and has high performance at a low cost. It is designed so that dust removal work can be carried out continuously by replacing it4).
本発明の除塵装置は、燃焼排ガスの流入口及び流出口を
有する本体内に通気性を有する第1の筒体を回動可能K
Nジけ、この】・1の筒体の外局にスクリュー板を螺旋
状に取付け、このスクリュー板を通気性を有する牙2の
筒体で囲繞し、この牙2の筒体と上記矛1の筒体の間の
一端部に耐熱性粒状物を供給するとともに上記才1の筒
体を介して」1記スクリュー板を回動して上記粒状物を
上記各筒体の間の他端部匠移動して排出し、上記流入口
からσ)燃焼11iガスを上記各筒体を介して上記移動
中の粒状物を通過させて除塵するとともに上記流出口か
ら流出させろようにしたことを特徴とするもので、フィ
ルター素材は、単に耐熱性を有する粒状物であればよく
、したがって砂などを用いることができるので、極めて
安価となり、使い捨てができるとともに再使用する場合
にも洗浄等が容易にでき、そして、装膚自体の構造も単
純で、複雑な機構及び複雑な制御を必要とぜず、使用条
件等も特に制限されることがなく、極めて安価で耐久性
も高く、その上、フィルター累利スなわち耐熱性粒状物
の交換も、牙1の筒体を回動することにより除塵作業中
でも徐々に入れ替えられるので、除塵作業が中断される
ことがない。The dust removal device of the present invention has a rotatable first cylindrical body having air permeability in the main body having an inlet and an outlet for combustion exhaust gas.
A screw plate is spirally attached to the outer part of the cylindrical body 1, this screw plate is surrounded by the cylindrical body of the fang 2 which has air permeability, and the cylindrical body of the fang 2 and the cylindrical body of the above spear 1 are connected. The heat-resistant granules are supplied to one end between the cylindrical bodies, and the granules are supplied to the other end between the cylindrical bodies by rotating the screw plate 1 through the cylindrical body 1. It is characterized in that the σ) combustion gas is passed through the moving particulate matter through the cylinders to remove dust from the inflow port, and is caused to flow out from the outflow port. The filter material only needs to be a heat-resistant granular material, so sand or the like can be used, making it extremely inexpensive, disposable, and easy to clean for reuse. The structure of the skin itself is simple, does not require complicated mechanisms or complicated controls, has no particular restrictions on usage conditions, is extremely inexpensive, has high durability, and has a filter stack. Another advantage is that the heat-resistant granules can be replaced gradually even during dust removal work by rotating the cylinder of fang 1, so that dust removal work is not interrupted.
次に、本発明の除塵装置をツ1面に示す=実施例に基づ
(・て具体的に説明する。Next, the dust removal device of the present invention will be specifically explained based on the embodiment shown on the first page.
牙1図は、本発明の除塵装置をゴミなどの焼却設備VC
C買置た例を示すもので、fi+は操車台、(2)は塵
介壕、(3)はクレーン、(4)はシュート、(5)は
焼却炉、(6)は燃焼排ガス冷却塔、(7)は燃焼差滓
冷却水槽、(8)は除塵装置、(9)は排風機、a〔は
煙突であり、トラックによって運ばれたゴミなどの被焼
却物は、操車台(1)から塵介壕(2)に投入され、つ
いで、クレーン(3)のグラブバケットによってレユー
ト(4)を介して焼却炉(5) K投入されて焼却され
るよう罠なっており、燃焼残滓は冷却水槽(7)に集め
られ、そして、燃焼排ガスは排風機(9)によって冷却
塔(6)及び除塵(+ R(8)を介1〜て煙突aユか
ら大気中に放出さり、るようになっている。Figure 1 shows the dust removal device of the present invention in a garbage incineration facility VC.
This shows an example of C-purchase, where fi+ is a steering platform, (2) is a dust shelter, (3) is a crane, (4) is a chute, (5) is an incinerator, and (6) is a combustion exhaust gas cooling tower. , (7) is the combustion slag cooling water tank, (8) is the dust removal device, (9) is the exhaust fan, a [ is the chimney, and the garbage and other incinerated materials carried by the truck are transported to the steering platform (1). The trap is such that the dust is thrown into the trench (2) and then thrown into the incinerator (5) via the reute (4) by the grab bucket of the crane (3) and incinerated, and the combustion residue is cooled. The flue gas is collected in a water tank (7), and is discharged into the atmosphere from the chimney a through the cooling tower (6) and dust remover (8) by an exhaust fan (9). It has become.
渭・2図ないし矛4図は、上記除塵装F、 (8)を示
すもので、(11)は本体で、この本体01)は、その
内部が仕切板0261 a4)によって4NK区分され
、上方から粒状物供給室05)、上部除塵s、o61、
下部除塵室面及び粒状物排出率αυが形成され、−F記
上部除塵室Oeの後部(矛2図にお(・て上部)VCは
】11図に示した排風機(9)に接続さハる燃貌排ガス
の流出口0!1が形成されているとともに、上記下部除
塵室r+′7)の前部には才1図に示した冷却塔(6)
K接続される・燃焼排ガスの流入口(イ)が形成され
ている、そして、上記各仕切板02)fl:’(104
1に上記供給室(15)及び上記排出室0υに通ずる複
数たとえば7本の通気性を有する矛2の筒体Cυが固定
されているととも(で、この矛2の各筒体(21)内に
は、それぞれ、上記本体(If)上音[(に設けられた
軸支11S!構f22に支持された軸C(を介して吊下
げられた通気性を有する牙1の筒(′*(241が配設
され、この]・1の各筒体(24)の外周にはスクリュ
ー板(29が螺旋状に取付けられている。Figures 2 to 4 show the dust remover F, (8), (11) is the main body, and the inside of this main body 01) is divided into 4NK sections by partition plates 0261 a4), and the upper From particulate matter supply chamber 05), upper dust removal s, o61,
The surface of the lower dust removal chamber and the particulate matter discharge rate αυ are formed, and the rear part of the upper dust removal chamber Oe (in Figure 2 (upper part) VC is connected to the exhaust fan (9) shown in Figure 11). A cooling tower (6) shown in Figure 1 is formed in the front part of the lower dust removal chamber r+'7).
K is connected to the combustion exhaust gas inlet (a), and each of the above partition plates 02)fl:'(104
A plurality of, for example, seven cylinders Cυ of the spear 2 having air permeability are fixed to the supply chamber (15) and the discharge chamber 0υ (each cylinder (21) of the spear 2). Inside, there are tubes ('* (241) is arranged, and a screw plate (29) is spirally attached to the outer periphery of each cylinder (24) of this].1.
なお、上記各筒体(21) C>4)は、1−5図に示
すように、多数の丸棒(至)(27)を平行状にかつ円
環を成すように配置したもので、各丸棒f261 (2
7+間の小許の間隙によって通気性を維持するようにし
たもので、内側の牙10筒体(24)の丸棒(財)は外
側の牙20筒体C+1の九棒内より小径のものを使用し
ている。In addition, each of the above-mentioned cylinders (21) C>4) is made up of a large number of round rods (27) arranged in parallel to form a ring, as shown in Figures 1-5. Each round bar f261 (2
The air permeability is maintained by a small gap between 7+, and the round rod (goods) of the inner fang 10 cylinder (24) has a smaller diameter than the inside of the nine rod of the outer fang 20 cylinder C+1. are using.
そして、上記牙1の各筒体(24+の軸(21の上端部
にそハぞれ1対のスプロケットホイール(281が取付
けられて(・るとともに、隣接した各軸ののスプロケッ
トホイール128)間にそチ1.ぞれ然端チェン(2L
11が順次倦回され、さらに、−fllll殉(j・2
図におり・て左側端)のスプロケットホイール(□’!
8) K近接して照射J用のスプロケットホイール(笥
がS:ケげられ、このスブDケットホ、(−JL c’
1lT) [’E −9cal+が減速機(33を介し
。A pair of sprocket wheels (281) are attached to the upper end of each cylindrical body (24+ shafts (21) of the fangs 1, and sprocket wheels 128 of each adjacent shaft). Nisochi 1.Zorendandanchen (2L
11 is repeated sequentially, and -fllll martyrdom (j・2
The sprocket wheel (□'!
8) Close to K, sprocket wheel for irradiation J
1lT) ['E -9cal+ is the reducer (via 33.
て連結されて(・2)とともに、スプロケットホイール
C())と上%”、(1111m+、jのスプロケット
ホイール(ハ)に駆躬1用の無娼チェンc33)が巻回
さす1、これによって、モータC1)を躯rIiIJ¥
ると矛1の各筒体C(イ)が回期して同方向に回動する
ようになっている。With (・2), the sprocket wheel C ()) and upper %'', (1111m+, j sprocket wheel (c) is wound with the chain c33 for driving 1), thereby 1. , motor C1)
Then, each cylinder C (a) of the spear 1 rotates in the same direction.
また、上記本体01)の上方後部に粒状物搬入¥f05
1が配設され、この搬入管3つの一端上部に粒状物取入
口OθがR′ンげ「〕f1てし・ろとともに、この搬入
管6勺の下部と一ヒ記本体(11)の供給滓0勺の−F
部との間に複数のレユート0″Oが上記各軸支機構(2
21を挾むように位置して接続され、この各シュート(
37)の内部にヲマエヤシリンダC118)によって開
閉するダンノ< (3!17′+’ Rけられ、さら(
で、上町:搬入管c3つの内部に、スフ1ニー板(4(
声を螺旋状に取付けた軸(41)が軸支され、この軸1
411は、搬入宥豆の他端部外側にお(・て、モータ(
42に1対のスプロケットホイール(41(44)及て
メ無婦チェン149を介して連結され、これによって、
モータ(42を駆動すると軸(41)が回動するように
なって(・る。In addition, particulate matter is brought into the upper rear part of the main body 01) ¥f05
1 is arranged, and a granular material intake Oθ is provided at the upper end of one end of the three inlet pipes. -F of 0 slags
A plurality of reutes 0''O are connected to each of the above-mentioned shaft support mechanisms (2
21 and are connected so that each chute (
37) is opened and closed by the air cylinder C118).
So, Kamimachi: Inside the three carry-in pipes c, there are 1 knee plate (4)
A shaft (41) on which the voice is spirally mounted is supported, and this shaft 1
411 is the motor (
A pair of sprocket wheels (41 (44) and a chain 149 are connected to 42, and thereby,
When the motor (42) is driven, the shaft (41) rotates.
また、上記排出室θ印の内底部に、スクリュー板I!5
11を螺旋状に取付けた軸色2が軸支され、この軸6z
は、排出室0槌の一端部に突設された粒状物搬出管63
)の外側において、モータ6イ)に1対のスプロケット
ホイールei51 何及び無姻チェン6ηを介して連結
され、これによって、モータ(54)を駆動すると軸6
邊カー回動するようになっている。In addition, a screw plate I! is attached to the inner bottom of the discharge chamber marked θ! 5
11 is spirally attached to the shaft color 2, and this shaft 6z
is a particulate discharge pipe 63 protruding from one end of the discharge chamber 0 mallet.
) is connected to the motor (54) via a pair of sprocket wheels (ei51) and an uncoupled chain (6η), thereby driving the motor (54).
The side car is designed to rotate.
なお、上記搬出管I5争の下部には粒状物取出口6&が
形成されており、そして、上記本体01)内の下段の仕
切板0(イ)の下部には十Fスクリュー板(ハ)の下端
部を囲繞する牙3の筒体の!J)が取付けられている。A granular material outlet 6& is formed at the bottom of the above-mentioned discharge pipe I5, and a 10F screw plate (c) is formed at the bottom of the lower partition plate 0 (a) in the main body 01). Of the cylindrical body with fangs 3 surrounding the lower end! J) is installed.
次に、この除r!l!!装置(8)の作用を説明する。Next, this removal! l! ! The operation of the device (8) will be explained.
砂などの耐熱性粒状物(60)を取入口amから搬入管
6怜内に投入し、モータi42 Kよって幅It411
を米4図矢印(4)力面に回動して、粒状物(6■をス
クリュー板(4σを介して他側方(剰・2図および牙3
図にオ・ヤいて右方)K送るとともに、エヤシリンダQ
A<よってダンパr3!1を開いて、粒状物60)を各
シュートc’+7)を介して供給室0■内に送り込む。Heat-resistant granules (60) such as sand are introduced into the carry-in pipe 6 from the inlet am, and the motor i42K has a width It411.
Rotate the granules (6) to the force side shown by the arrow (4) in Fig. 4, and pass the granules (6
As shown in the figure, send air cylinder Q to the right).
A<Therefore, the damper r3!1 is opened and the granules 60) are fed into the supply chamber 0■ via each chute c'+7).
この際、各シュート(’+7のダンパ鰻けその下方に粒
状物軸が所定号充填された場合、エヤシリンダ0陽によ
って閉じられるように構成しておλ、供給室aQ内に粒
状物11301が均一に送り込まれるようにしておき、
そして、各シュートC37)のダンパOIがすべ。At this time, when a predetermined number of granular material shafts are filled under each chute ('+7 damper eel), it is configured so that it is closed by the air cylinder 0, λ, and the granular material 11301 is uniformly distributed in the supply chamber aQ. so that it is sent to
And the damper OI of each chute C37) is smooth.
て閉じた場合にはモータ(421を停止して軸(4’l
Jの回1〕を停止するように構成しておく。If the motor (421) is closed, the motor (421) is stopped and the shaft (4'l) is closed.
The configuration is such that the first time of J] is stopped.
そして、モータSυによって第1の各筒体Q4を矛2図
矢印CB)方向に回動して、供給室(1つ内の粒状物6
0をスクリュー板(ハ)を介して牙1の各筒体(24+
と牙2の各筒体(2I)の間の上端部から下端部に密集
状態でゆっくりと移動しそ排出室(IIに排出するとと
もに、モータ54i Kよって軸■を十4図矢印(0方
向に回動して、排出室08)の粒状物鵜をスクリュー板
61)を介して一側方(牙2図及びA−3図にお(・て
左方)に送り、搬出管槌の取出口部から排出する。Then, each first cylindrical body Q4 is rotated by the motor Sυ in the direction of the arrow CB in Fig.
0 to each cylinder body (24+) of fang 1 through the screw plate (c).
The shiso moves slowly in a dense manner from the upper end to the lower end between the cylinders (2I) of the fang 2 and discharges it into the discharge chamber (II), and the motor 54iK moves the shaft ■ in the direction of the arrow in Fig. 14 (0 direction). The granules in the discharge chamber 08) are sent to one side (Fig. 2 and Fig. A-3 (to the left)) through the screw plate 61), and are sent to the outlet of the ejection pipe mallet. discharge from the department.
そうして、この状態において、牙1図に示した冷却塔(
6)からの燃焼排ガスは、排風機(9)の吸引作用によ
って、流入口(21から下部除塵室07)K入り、つυ
・で、1・2の各筒体(21)の外(11+1下部から
粒状物の1間を通過して牙1の各筒体I2(イ)の内側
下部に入り、ついで、矛1の各筒体(24)の内側上部
から粒状物101間を通過して牙2の各筒体(21)の
外側上部すなわち上部除塵室(16)に出て、流出口(
【1を介して排風機(9)に導かれるようになっており
、粒状物(io)間を2回通過する際に塵が除去される
ように1tって(・る。Then, in this state, the cooling tower (
The combustion exhaust gas from 6) enters the inlet (from 21 to the lower dust removal chamber 07) K by the suction action of the exhaust fan (9), and is
・Then, from the outside (11+1 lower part) of each cylinder body (21) of 1 and 2, it passes between the particulate matter 1 and enters the inside lower part of each cylinder body I2 (a) of fang 1, and then each of the spear 1 It passes between the granules 101 from the inner upper part of the cylinder (24), exits to the outer upper part of each cylinder (21) of the fang 2, that is, the upper dust removal chamber (16), and exits from the outlet (
[1] to the exhaust fan (9), and the dust is removed when passing between the granules (io) twice.
こσ)とき、粒状物り;0)は、′At1の各筒体(?
4)の回動により、ゆっくりと下方に移?#Ijるので
、常時交換されることになり、その間にお(・ても燃焼
排ガスの除塵を続けることができる。な畑、1・1の各
筒体0イ)の回動は、必ずしも、連続である必要はなく
、断続的に行なうこともできる。When σ), the granular material; 0) is equal to each cylinder (?) of 'At1.
Due to the rotation in 4), it slowly moves downward? #Ij, so it will be replaced constantly, and in the meantime, the rotation of each cylindrical body in 1 and 1) will not necessarily be the same. It does not have to be continuous and can be done intermittently.
そして、この除塵装置(8)は、フィルター素材として
砂などの耐熱性粒状物のωを使用できるので、フィルク
ー素材が極めて安価とf(す、しかも、使用法人の粒状
物鈷0は単にその表面に塵が付着1.て(・るlごけ′
f′、Cので、洗浄等カー容易にでき、再使用も容易と
なり、そ1−て、装置自体の構造も単純で、複雑な機構
及び複雑な制御が不要で、使用条件等も特に制限される
こともなく、極めて安価で耐久性も高し・。This dust removal device (8) can use heat-resistant granular materials such as sand as the filter material, so the filter material is extremely inexpensive. Dust adheres to 1.
f', C, it is easy to clean and reuse, and the structure of the device itself is simple, requiring no complicated mechanism or complicated control, and there are no particular restrictions on usage conditions. It is extremely inexpensive and highly durable.
なオd、粒状物佑0)は耐熱性を有するものであ11ば
、砂に限らず他の素材たとえば、珪砂等を使用すること
ができ、そして、粒状物伯(2)の大きさケ変えること
(τより種々の態様の塵に対応でき、たとえば、粒状物
側を小さく細か(・ものVCすれば、液体状の塵の除去
に有効であり、粒状物(6■を大きく荒いものにすれば
、固体状の塵の除去に有効であり、大小の粒状物−を混
合使用することもできる。If the granular material (0) is heat resistant, other materials such as silica sand can be used instead of sand, and the size of the granular material (2) is not limited to sand. It is possible to deal with various types of dust by changing (τ), for example, if you change the particulate matter side to small and fine (・), it is effective for removing liquid dust, and if you change the particulate matter (6) to large and rough one, This is effective in removing solid dust, and a mixture of large and small particles can also be used.
そして、この除塵装置(8)は、上述したように、構造
が単純なことなどから、大型化や処理能力を向上させる
ことが極めて簡単で、各筒体(21) (24)を増や
したり大型化するだけでよく、しかも、粒状物FAは各
筒体f2+1241間に充填されるので、燃焼排ガスの
通過面精が増大されており、−処理能力の点で全く不安
がない。As described above, this dust removal device (8) has a simple structure, so it is extremely easy to increase the size and improve the processing capacity, and it is very easy to increase the size and processing capacity by increasing the number of cylinders (21) and (24). In addition, since the particulate matter FA is filled between the cylinders f2+1241, the passage area of the combustion exhaust gas is increased, and there is no concern in terms of throughput.
上述したように、来光FIJJによれば、高温の燃焼排
ガスの処理ができ、しかも、処理峠力も極めて高く、か
つ、装置自体の構造も単純で、耐久性もすぐれた除塵装
置な安価に提供でき、その上、フィルター素材すなわち
粒状物の交換も連続的にまたは断続的にいつでもでき、
燃焼排ガスの処理が連続的にでき、さらに、フィルター
素材も単なる耐熱性粒状物であるので安価で再利用も容
易Cてで磯る。As mentioned above, Raikou FIJJ provides an inexpensive dust removal device that can process high-temperature combustion exhaust gas, has extremely high processing power, has a simple structure, and has excellent durability. Moreover, the filter material or particulates can be replaced continuously or intermittently at any time.
Combustion exhaust gas can be treated continuously, and since the filter material is simply heat-resistant granules, it is inexpensive and easy to reuse.
図は本発明の一実施例を示すもので、矛1図は焼却設備
の説明図、矛2図は除11!装置の平面図、矛3図はそ
の一部を断面にした正面図、矛4図はその側面視断面図
、渭・5図はその要部の断面図である。
(8)・・除塵装置、01)・・本体、α1・・流出口
、■・・流入口、(2υ−・牙2の筒体、Q(イ)・・
層・1の筒体、(至)−・スクリュー板、伯υ・・粒状
物。The figures show one embodiment of the present invention, and Figure 1 is an explanatory diagram of the incineration equipment, and Figure 2 is an explanatory diagram of the incineration equipment. A plan view of the device, Figure 3 is a partially sectional front view, Figure 4 is a side sectional view, and Figure 5 is a sectional view of the main part. (8)...Dust removal device, 01)...Main body, α1...Outlet, ■...Inlet, (2υ-・Fang 2 cylinder, Q(a)...
Layer 1 cylindrical body, (to)--screw plate, and granular material.
Claims (1)
通気性を有する矛1の筒体を回動可能に股げ、この矛1
の筒体の外周にスクリュー板を螺旋状に取付け、このス
クリュー板を通気性を有する1’ 20筒体で囲繞し、
この矛2の筒体と上記牙1の筒体の開の一端部に耐熱性
粒状物を供給するとともに上記矛1の筒体を介して上記
スクリュー板を回動して上記粒状物を上記各筒体の間の
他端部に移動して排出し、上記流入口からの燃焼排ガス
を上記各筒体を介して上記移動中の粒状物を通過させて
除塵するとともに上記流出口から流出させるように1−
たことを特徴とする除塵装置。(1) A cylindrical body of a spear 1 having air permeability is rotatably straddled in the main body having an inlet and an outlet for combustion exhaust gas, and this spear 1
A screw plate is spirally attached to the outer periphery of the cylindrical body, and this screw plate is surrounded by a 1'20 cylinder having air permeability.
Heat-resistant granules are supplied to one open end of the cylindrical body of the spear 2 and the cylindrical body of the fang 1, and the screw plate is rotated through the cylindrical body of the spear 1 to transfer the granular substances to each of the above. The combustion exhaust gas is moved to the other end between the cylindrical bodies and discharged, and the combustion exhaust gas from the inlet is passed through the moving particulate matter through each of the cylindrical bodies to remove dust, and is caused to flow out from the outlet. ni1-
A dust removal device characterized by:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12093982A JPS5912729A (en) | 1982-07-12 | 1982-07-12 | Dust removing apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12093982A JPS5912729A (en) | 1982-07-12 | 1982-07-12 | Dust removing apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5912729A true JPS5912729A (en) | 1984-01-23 |
Family
ID=14798703
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP12093982A Pending JPS5912729A (en) | 1982-07-12 | 1982-07-12 | Dust removing apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5912729A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4652289A (en) * | 1984-11-26 | 1987-03-24 | Hydro-Quebec | Purification of effluent gases |
JPS62256922A (en) * | 1986-04-30 | 1987-11-09 | Mitsubishi Heavy Ind Ltd | Method for preventing thermal deformation of strip supporting roll |
CN1058755C (en) * | 1995-03-23 | 2000-11-22 | 新日本制铁株式会社 | Continuous annealing furnace |
CN107655202A (en) * | 2017-10-25 | 2018-02-02 | 陈琪雯 | A kind of energy saving and environment friendly stabilization boiler |
-
1982
- 1982-07-12 JP JP12093982A patent/JPS5912729A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4652289A (en) * | 1984-11-26 | 1987-03-24 | Hydro-Quebec | Purification of effluent gases |
JPS62256922A (en) * | 1986-04-30 | 1987-11-09 | Mitsubishi Heavy Ind Ltd | Method for preventing thermal deformation of strip supporting roll |
JPH0619120B2 (en) * | 1986-04-30 | 1994-03-16 | 三菱重工業株式会社 | Method for preventing thermal deformation of strip support roll |
CN1058755C (en) * | 1995-03-23 | 2000-11-22 | 新日本制铁株式会社 | Continuous annealing furnace |
CN107655202A (en) * | 2017-10-25 | 2018-02-02 | 陈琪雯 | A kind of energy saving and environment friendly stabilization boiler |
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