JPH0952011A - Dust collector - Google Patents
Dust collectorInfo
- Publication number
- JPH0952011A JPH0952011A JP20872495A JP20872495A JPH0952011A JP H0952011 A JPH0952011 A JP H0952011A JP 20872495 A JP20872495 A JP 20872495A JP 20872495 A JP20872495 A JP 20872495A JP H0952011 A JPH0952011 A JP H0952011A
- Authority
- JP
- Japan
- Prior art keywords
- dust
- filter body
- filter
- porous solid
- 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
Links
- 239000000428 dust Substances 0.000 title claims abstract description 94
- 239000007787 solid Substances 0.000 claims abstract description 28
- 230000035699 permeability Effects 0.000 claims abstract description 3
- 238000001514 detection method Methods 0.000 claims description 7
- 239000007789 gas Substances 0.000 description 60
- 230000006866 deterioration Effects 0.000 description 8
- 238000002485 combustion reaction Methods 0.000 description 6
- 238000007789 sealing Methods 0.000 description 4
- 238000011001 backwashing Methods 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000010248 power generation Methods 0.000 description 2
- 230000003014 reinforcing effect Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000000567 combustion gas Substances 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は加圧流動床ボイラや
ガス化炉等で発生する高温、高圧ガスに対して使用され
る集じん装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a dust collecting apparatus used for high temperature and high pressure gas generated in a pressurized fluidized bed boiler, a gasification furnace or the like.
【0002】[0002]
【従来の技術】加圧流動床ボイラで発生した高温、高圧
の燃焼排ガスをガスタービンへ送気し、ガスタービンを
駆動する複合発電プラントは高効率発電が得られるが、
ガスタービンの摩耗防止上から、ダスト類を除去した清
浄な排ガスをガスタービンに送ることが不可欠である。
そのため、通常は燃焼排ガスのダスト(燃焼灰、ばいじ
ん)等を予め除じんする集じん装置が設置されている。2. Description of the Related Art A combined cycle power plant that drives a gas turbine by supplying high temperature and high pressure combustion exhaust gas generated in a pressurized fluidized bed boiler to a gas turbine can obtain high efficiency power generation.
In order to prevent wear of the gas turbine, it is essential to send clean exhaust gas from which dusts have been removed to the gas turbine.
Therefore, usually, a dust collector is installed to remove dust (combustion ash, dust) and the like of combustion exhaust gas in advance.
【0003】この種の複合発電プラントにおいては、図
3に示すように加圧流動床ボイラ31で発生した燃焼排
ガス32はダクト33をへて遠心力を利用したサイクロ
ン集じん装置34に導びかれ、その集じん装置34にお
いて、燃焼排ガス中の大半のダストは集じんされ除去さ
れる。In this type of combined cycle power plant, as shown in FIG. 3, combustion exhaust gas 32 generated in a pressurized fluidized bed boiler 31 is guided through a duct 33 to a cyclone dust collector 34 utilizing centrifugal force. In the dust collector 34, most dust in the combustion exhaust gas is collected and removed.
【0004】しかしながら、ガスタービン36側として
は、さらに清浄ガスであることが要求され、通気性を有
する多孔質固体からなる例えば、セラミックフィルタと
呼ばれる耐高温、耐圧の精密集じん装置35を通過させ
て清浄ガスとした後、ガスタービン36へ送気される。However, the gas turbine 36 side is required to be a clean gas, and is made to pass through a high-temperature and pressure-resistant precision dust collector 35 called a ceramic filter, which is made of a porous solid having air permeability. After being made into clean gas, it is sent to the gas turbine 36.
【0005】サイクロン集じん装置34及び精密集じん
装置35で集じんされたダストは、ダスト回収器34a
及び35aにて一旦回収された後、系外へ排出される。
また、ガスタービン36を駆動した後、燃焼排ガス37
は図示されていない各種熱交換器等にて熱回収され大気
へ放出される。The dust collected by the cyclone dust collector 34 and the precision dust collector 35 is collected by the dust collector 34a.
And 35a, and then discharged outside the system.
Further, after driving the gas turbine 36, the combustion exhaust gas 37
Is recovered by various heat exchangers (not shown) and released to the atmosphere.
【0006】図2は従来の精密集じん装置の一例を示し
たもので、以下これを説明する。内面に耐火、断熱材を
施した容器21内には通気性の多孔質固体からなる濾過
体22の群が収納されシール用管板23aと補強用管板
23bによって容器21内に固定されている。FIG. 2 shows an example of a conventional precision dust collecting apparatus, which will be described below. A group of filter bodies 22 made of a gas permeable porous solid is housed in a container 21 having a fireproof and heat insulating material on its inner surface, and is fixed in the container 21 by a sealing tube sheet 23a and a reinforcing tube sheet 23b. .
【0007】含じん燃焼ガス32はガス入口孔24を経
て、濾過体22内に入り、濾過体22をその内面から外
面へ通過する際、ガス中のダスト25は濾過体22内面
に付着、脱落し、このダスト25は容器21下部に集め
られた後、系外へ排出される。一方、濾過体22を内面
から外面へ通過し清浄された排ガスは、容器21の側壁
に開口する複数個の出口ダクト26及びガス出口として
の集合排出ダクト27をへてガスタービンへ送気され
る。The dust-containing combustion gas 32 enters the filter body 22 through the gas inlet hole 24, and when passing through the filter body 22 from its inner surface to its outer surface, dust 25 in the gas adheres to and drops off on the inner surface of the filter body 22. Then, the dust 25 is collected in the lower part of the container 21 and then discharged to the outside of the system. On the other hand, the exhaust gas that has passed through the filter body 22 from the inner surface to the outer surface and is cleaned is sent to the gas turbine through a plurality of outlet ducts 26 that open to the side wall of the container 21 and a collective discharge duct 27 that serves as a gas outlet. .
【0008】出口ダクト26内には逆洗気流を導入する
逆洗ノズル11が設置され、圧縮機12から送られる逆
洗気流を共通管12a及び弁12bをへて前記逆洗ノズ
ル11から容器21内へ一定時間(逆洗周期時間)毎に
一定時間(逆洗時間)一定量の気流を吹き込み、濾過体
22内面に付着したダストを濾過体22内へ離脱させた
後、前記した集じん作用を繰り返えす。A backwash nozzle 11 for introducing a backwash airflow is installed in the outlet duct 26, and the backwash airflow sent from the compressor 12 is passed from the backwash nozzle 11 to the container 21 through the common pipe 12a and the valve 12b. After a certain amount of airflow is blown into the inside of the filter body 22 at a constant time (backwash cycle time) to remove the dust adhering to the inner surface of the filter body 22 into the filter body 22, the dust collecting action described above is performed. Repeat.
【0009】[0009]
【発明が解決しようとする課題】集じん装置の容器21
内に収容された濾過体22の群はシール用管板23a部
及び濾過体22の内外壁部にてダストを含んだ排ガスと
清浄ガスとが分離、隔離されている。経年劣化あるいは
不測のトラブルにてシール個所の劣化、あるいは濾過体
22即ちセラミックフィルタ本体の部分的割れ又は破損
が起って集じん性能が劣化することが予測されるが、こ
れらの現象のいずれかが発生すると清浄ガス中にダスト
を含んだ排ガスが混入し、換言すると、ダストを含んだ
清浄ガスが直接ガスタービンへ送気されガスタービンの
摩耗が起こり、全体プラントが運転停止となる。The container 21 of the dust collecting apparatus.
In the group of the filter bodies 22 housed inside, the exhaust gas containing dust and the clean gas are separated and separated at the sealing tube sheet 23a and the inner and outer wall portions of the filter body 22. It is predicted that deterioration of the sealing portion due to deterioration over time or unexpected trouble, or partial cracking or damage of the filter body 22, that is, the ceramic filter body, will deteriorate the dust collection performance. When this occurs, the exhaust gas containing dust is mixed in the clean gas, in other words, the clean gas containing dust is directly sent to the gas turbine, causing wear of the gas turbine, and shutting down the entire plant.
【0010】本発明は通気性の多孔質固体からなる濾過
体を用いた従来の集じん装置にみられるこのような問題
点を解消するもので、それら濾過体の部分的な割れや破
損が起ってもダストが清浄ガスに混入するのを防ぐと共
に、ダストの洩れ発生個所や程度を検出可能とした集じ
ん装置を提供することを課題としている。The present invention solves such a problem found in the conventional dust collecting apparatus using a filter body made of an air-permeable porous solid, and the filter body is partially cracked or damaged. Even if the dust is prevented from being mixed into the clean gas, it is an object to provide a dust collecting apparatus capable of detecting the location and degree of dust leakage.
【0011】[0011]
【課題を解決するための手段】本発明は通気性の多孔質
固体からなる濾過体を含じんガス入口及び清浄ガス出口
を有する容器内に収容し、含じんガス入口から含じんガ
スを濾過体の内側へ供給し、前記濾過体の外側から清浄
ガスを取り出し、清浄ガス出口へ導びくようにした集じ
ん装置において前記課題を解決するため次の手段を講じ
ている。According to the present invention, a filter body made of a gas permeable porous solid is contained in a container having a dust-containing gas inlet and a clean gas outlet, and the dust-containing gas is filtered from the dust-containing gas inlet. In order to solve the above problems, the following means are taken in the dust collecting apparatus in which the clean gas is supplied to the inside of the filter body, the clean gas is taken out from the outside of the filter body, and is guided to the clean gas outlet.
【0012】(1)集じん装置出口の清浄ガス出口部、
例えば清浄ガス出口ダクトに多孔質固体からなる濾過体
を各出口毎あるいは集合部に設置し、この濾過体の前後
の圧力差を検出する圧力検出装置及び流速検知装置を具
備していること。(1) Clean gas outlet at the dust collector outlet,
For example, a filter made of a porous solid is installed in each clean gas outlet duct at each outlet or at a collecting portion, and a pressure detecting device and a flow velocity detecting device for detecting a pressure difference before and after the filter are provided.
【0013】(2)前記容器に収容されている多孔質固
体からなる濾過体群の一部を、ダストが通過できる、よ
り通気性があり、圧力損失の小さな濾過体とし、その濾
過体の開口両端は例えば従来のダストを通過しない多孔
質固体で塞ぎ、さらにその内部に静電容量方式等のレベ
ル検出装置を具備していること。(2) A part of the filter body made of a porous solid contained in the container is used as a filter body which is more permeable to dust and has a smaller pressure loss, and the opening of the filter body. Both ends should be covered with, for example, a conventional porous solid that does not allow dust to pass therethrough, and a level detection device such as an electrostatic capacitance method should be provided inside thereof.
【0014】なお、前記の多孔質濾過体群の一部は単
体、複数個いづれであってもさしつかえなく、また容器
内での位置は限定されるものではないが、通常は当該多
孔質からなる濾過体群の一部の周りに複数個の従来濾過
体群をグループ分けして必要個数配置したものとする。
さらに、当該濾過体は従来の濾過体部の空間部に別途配
置してさしつかえない。It should be noted that a part of the above-mentioned porous filter body may be a single substance or a plurality thereof, and its position in the container is not limited, but it is usually made of the porous substance. It is assumed that a plurality of conventional filter body groups are divided into groups around a part of the filter body group and a required number of them are arranged.
Further, the filter body may be separately arranged in the space portion of the conventional filter body portion.
【0015】(1)本発明による集じん装置は前記
(1)に記載したように清浄ガス出口部等に多孔質固体
からなる濾過体が配置されているのでガスタービンへ送
気される清浄ガス中に、前記の不測現象が発生したこと
によって、ダストが含まれていると、この多孔質固体か
らなる濾過体の入口面にダストが付着し、ガスタービン
へは清浄ガスが従来同様送気される。(1) In the dust collecting apparatus according to the present invention, as described in (1) above, since the filter body made of porous solid is arranged at the clean gas outlet or the like, clean gas to be fed to the gas turbine. When dust is contained due to the occurrence of the above-mentioned unexpected phenomenon, dust adheres to the inlet surface of the filter body made of this porous solid, and clean gas is sent to the gas turbine as in the conventional case. It
【0016】一方、前記多孔質固体からなる濾過体の入
口面へのダスト付着量に比例してその濾過体の前後の圧
損が増加するが、多孔質固体からなる濾過体を通過する
ガス流速と圧力損失には以下の式が成立する。On the other hand, the pressure loss before and after the filter made of the porous solid increases in proportion to the amount of dust adhering to the inlet surface of the filter made of the porous solid. The following equation holds for the pressure loss.
【0017】[0017]
【数1】 [Equation 1]
【0018】従って本発明による集じん装置では前記多
孔質固体からなる濾過体の前後の圧損及び流速の検知装
置が具備されているので経時変化にともなう清浄ガス中
の含じんダスト量の増加分が推定でき、集じん装置の集
じん性能の劣化状況からプラント全体の緊急停止又は運
転停止への予測を行うことができる。Therefore, since the dust collector according to the present invention is equipped with the pressure loss and flow velocity detectors before and after the filter made of the porous solid, the increase in the amount of dust-containing dust in the clean gas due to the change with time can be considered. It can be estimated, and it is possible to predict an emergency stop or an operation stop of the entire plant from the deterioration status of the dust collecting performance of the dust collecting apparatus.
【0019】(2)また前記(2)項に記載したように
濾過体群の一部に内部にレベル検出装置を有した濾過体
が配置されており、前記不測の現象が集じん装置にて発
生すると、逆洗時の容器内圧時にダストを含んだガスが
その濾過体群の一部に流入し、ダストが内部に堆積す
る。このダストの堆積量をレベル検出装置で検出するこ
とによって上記集じん性能の劣化状況及び不測現象発生
場所を特定しうる。(2) Further, as described in the above item (2), a filter body having a level detecting device therein is arranged in a part of the filter body group, and the unexpected phenomenon occurs in the dust collecting device. When the gas is generated, the gas containing dust flows into a part of the filter body group at the time of the internal pressure of the container at the time of backwashing, and the dust is accumulated inside. By detecting the amount of dust accumulated by the level detection device, the situation of deterioration of the dust collection performance and the location of the unexpected phenomenon can be specified.
【0020】(3)従って以上の(1),(2)項から
得られる集じん装置の脱じん性能の劣化程度、状況の情
報を得ることができるので、その後の運転操作可能の判
断を容易にし、あるいは不測現象個所が特定されるので
集じん装置の修理、メンテナンスを容易とすることがで
きる。(3) Therefore, since it is possible to obtain information on the degree of deterioration of the dust removal performance of the dust collector and the situation obtained from the above items (1) and (2), it is easy to determine whether the subsequent operation is possible. Alternatively, since the location of the unexpected phenomenon is specified, the dust collecting apparatus can be easily repaired and maintained.
【0021】[0021]
【発明の実施の形態】以下本発明による集じん装置を図
1に示した実施の一形態に基づいて具体的に説明する。
なお図1において図2,図3に示した従来の装置と同様
な部分については説明を簡単にするため、同一符号をつ
けてある。BEST MODE FOR CARRYING OUT THE INVENTION A dust collecting apparatus according to the present invention will be specifically described below based on the embodiment shown in FIG.
In FIG. 1, the same parts as those of the conventional device shown in FIGS. 2 and 3 are denoted by the same reference numerals for simplification of description.
【0022】本実施形態による集じん装置は図1に示す
構造を有している。すなわち図1に示す出口ダクト26
後方部及び集合排出ダクト27に多孔質固体からなる濾
過体11a及び11bが装着され、例えば濾過体11b
前後の圧力差を測定する差圧検出装置13及び流速を測
定する流速検出装置14が具備されている。The dust collecting apparatus according to this embodiment has the structure shown in FIG. That is, the outlet duct 26 shown in FIG.
Filter bodies 11a and 11b made of a porous solid are attached to the rear part and the collecting and discharging duct 27, for example, the filter body 11b.
A differential pressure detection device 13 for measuring the pressure difference between the front and rear and a flow velocity detection device 14 for measuring the flow velocity are provided.
【0023】さらに容器21内に収容されている多孔質
固体からなる濾過体群22の一部に代り、より通気性が
あり、圧力損失の小さな濾過体15を配置しその両端開
口部は従来の通気性を有する多孔質固体15a,15b
で塞ぎその内部には静電容量方式等のレベル検出装置1
6が具備されている。なお、多孔質固体15a,15b
は脱着可能とすることが望まれるが固定式でもさしつか
えない。Further, instead of a part of the filter body group 22 made of a porous solid housed in the container 21, a filter body 15 which is more breathable and has a small pressure loss is arranged, and the openings at both ends thereof are the same as those in the conventional case. Breathable porous solids 15a, 15b
Closed with a level detector 1 such as a capacitance type
6 are provided. The porous solids 15a, 15b
Is desired to be removable, but a fixed type is also acceptable.
【0024】本実施形態による集じん装置は前記したよ
うに清浄ガス出口部の集合排出ダクト27に多孔質固体
からなる濾過体11bが配置されているので、ガスター
ビンへ送気される清浄ガス中に不測現象が発生したこと
によってダストが含まれても、この多孔質固体からなる
濾過体11bの入口面にダストが付着し、ガスタービン
へは清浄ガスが従来同様送気される。In the dust collecting apparatus according to the present embodiment, since the filter body 11b made of porous solid is arranged in the collecting and discharging duct 27 at the clean gas outlet, as described above, the clean gas to be fed to the gas turbine is Even if dust is included due to the occurrence of an unexpected phenomenon, dust adheres to the inlet surface of the filter 11b made of this porous solid, and clean gas is sent to the gas turbine as in the conventional case.
【0025】また、本実施形態による集じん装置では前
記多孔質固体からなる濾過体11bの前後の圧損を検出
する差圧検出装置13及び流速検知装置14が具備され
ているので経時劣化にともなう清浄ガス中の含じんダス
ト量の増加分が推定でき、集じん装置の集じん性能の劣
化状況からプラント全体の緊急停止又は運転停止への予
測を行うことができる。Further, since the dust collecting apparatus according to the present embodiment is provided with the differential pressure detecting device 13 and the flow velocity detecting device 14 for detecting the pressure loss before and after the filter body 11b made of the porous solid, the dust collecting device cleans with time. The increase in the amount of dust-containing dust in the gas can be estimated, and it is possible to predict an emergency stop or operation stop of the entire plant from the deterioration status of the dust collecting performance of the dust collector.
【0026】更に、本集じん装置では、濾過体22群の
一部に内部にレベル検出装置16を有した濾過体15が
配置されており、濾過体22の破損などの事態が発生す
ると、逆洗時の容器内圧時にダストを含んだガスがその
濾過体群の一部15に流入し、ダストが内部に堆積す
る。このダストの堆積量をレベル検出装置16で検出す
ることによって上記集じん性能の劣化状況及び不測現象
発生場所を知りうる。Further, in the present dust collecting apparatus, the filter body 15 having the level detecting device 16 inside is disposed in a part of the filter body 22 group, and when a situation such as damage of the filter body 22 occurs, it is reversed. The gas containing dust flows into the part 15 of the filter body group at the time of the pressure inside the container during washing, and the dust accumulates inside. By detecting the accumulated amount of dust with the level detection device 16, the deterioration state of the dust collection performance and the place where an unexpected phenomenon occurs can be known.
【0027】このように、本実施形態の集じん装置によ
れば脱じん性能の劣化程度、状況を知ることができるの
で、その後の運転操作可能の判断を容易にし、かつ、集
じん装置の修理、メンテナンスを容易とすることができ
る。As described above, according to the dust collecting apparatus of the present embodiment, it is possible to know the degree of deterioration of the dust removal performance and the situation thereof. Therefore, it is easy to determine whether or not the driving operation is possible thereafter, and the dust collecting apparatus is repaired. The maintenance can be facilitated.
【0028】[0028]
【発明の効果】以上説明したように本発明による集じん
装置においては、清浄ガス出口部に濾過体を配置し、そ
の前後の圧力差圧及び流速を検知することによって集じ
ん装置の集じん性能が劣化する不測の現象発生が検知で
きる。また、そのような現象が発生してもその濾過体の
設置によってガスタービンへは従来同様、清浄ガスを送
気できるので、ガスタービンを停止することなくダスト
の含じん量の経時的増加の情報を得ながら運転可否の判
断を実施することができる。As described above, in the dust collecting apparatus according to the present invention, the dust collecting performance of the dust collecting apparatus is obtained by disposing the filter at the clean gas outlet and detecting the pressure differential pressure and the flow velocity before and after the filter. It is possible to detect the occurrence of an unexpected phenomenon that deteriorates. In addition, even if such a phenomenon occurs, clean gas can be sent to the gas turbine by installing the filter body as in the past, so information on the increase in dust content over time without stopping the gas turbine can be obtained. It is possible to make a judgment as to whether or not the vehicle can be operated.
【0029】また、本発明による集じん装置では、多孔
質固体からなる濾過体群の一部に、より通気性があり圧
力損失の小さな濾過体を配置し、その濾過体の開口両端
を多孔質固体で塞ぎ、さらに、その内部にレベル検出装
置を有しているので、前記不測の現象が発生した際には
逆洗時の容器内の圧力上昇によって含じんダストがこの
濾過体内に堆積する。Further, in the dust collecting apparatus according to the present invention, a filter body which is more permeable and has a smaller pressure loss is arranged in a part of the filter body made of a porous solid, and both ends of the opening of the filter body are made porous. Since it is blocked with a solid and further has a level detecting device inside thereof, when the above-mentioned unexpected phenomenon occurs, dust-containing dust is accumulated in this filter body due to a pressure increase in the container during backwashing.
【0030】濾過体内に堆積したそのダストをレベル検
出装置でその量を検出できるので、不測の現象の発生個
所の特定及びそのトラブルの大小を判断できる情報が得
られ、運転停止可否の判断及び集じん装置の修理、メン
テナンスを容易にする効果が得られる。Since the amount of the dust accumulated in the filter body can be detected by the level detecting device, information can be obtained to identify the location of the unexpected phenomenon and to determine the magnitude of the trouble, and determine whether the operation can be stopped or not. This has the effect of facilitating the repair and maintenance of the dust collector.
【図1】本発明の実施の一形態に係る集じん装置の断面
図で(a)は縦断面図、(b)は横断面図。FIG. 1 is a cross-sectional view of a dust collector according to an embodiment of the present invention, (a) is a vertical cross-sectional view, and (b) is a horizontal cross-sectional view.
【図2】従来例に係る集じん装置の断面図。FIG. 2 is a sectional view of a dust collecting apparatus according to a conventional example.
【図3】従来の集じん装置を具えた複合発電システムの
系統図。FIG. 3 is a system diagram of a combined power generation system including a conventional dust collector.
11 逆洗ノズル 11a 濾過体 11b 濾過体 12 圧縮機 12a 共通管 12b 弁 13 差圧検出装置 14 流速検出装置 15 濾過体 15a 多孔質固体 15b 多孔質固体 16 レベル検出装置 21 容器 22 濾過体 23a シール用管板 23b 補強用管板 24 ガス入口孔 26 出口ダクト 27 集合排出ダクト 11 Backwash Nozzle 11a Filter 11b Filter 12 Compressor 12a Common Pipe 12b Valve 13 Differential Pressure Detector 14 Flow Rate Detector 15 Filter 15a Porous Solid 15b Porous Solid 16 Level Detector 21 Container 22 Filter 23a For Sealing Tube sheet 23b Reinforcing tube sheet 24 Gas inlet hole 26 Outlet duct 27 Collective discharge duct
Claims (1)
を含じんガス入口及び清浄ガス出口を有する容器に収容
して前記含じんガス入口から含じんガスを前記濾過体の
内側へ供給し、同濾過体の外側から清浄ガスを取り出し
て前記清浄ガス出口へ導くように構成した集じん装置に
おいて、前記清浄ガス出口部に濾過体と、その間の圧力
差を検出する圧力検出装置と、流速検出装置とを配置す
ると共に、前記濾過体の群の一部をより通気性があって
圧力損失の小さな濾過体とし、その濾過体の開口両端を
多孔質固体で塞ぎ、更にその内部にレベル検出装置を具
備したことを特徴とする集じん装置。1. A group of filter bodies made of an air-permeable porous solid is housed in a container having a dust-containing gas inlet and a clean gas outlet, and the dust-containing gas is supplied from the dust-containing gas inlet to the inside of the filter body. Then, in the dust collector configured to take out the clean gas from the outside of the filter body and guide it to the clean gas outlet, the filter body at the clean gas outlet portion, and a pressure detection device for detecting a pressure difference therebetween. A flow velocity detecting device is arranged, and a part of the group of the filter bodies is made a filter body having a higher air permeability and a smaller pressure loss, and both ends of the openings of the filter body are closed with a porous solid, and a level is further provided inside the filter body. A dust collecting apparatus comprising a detection device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20872495A JP3327743B2 (en) | 1995-08-16 | 1995-08-16 | Dust collection device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20872495A JP3327743B2 (en) | 1995-08-16 | 1995-08-16 | Dust collection device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0952011A true JPH0952011A (en) | 1997-02-25 |
| JP3327743B2 JP3327743B2 (en) | 2002-09-24 |
Family
ID=16561040
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP20872495A Expired - Fee Related JP3327743B2 (en) | 1995-08-16 | 1995-08-16 | Dust collection device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3327743B2 (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20020031437A (en) * | 2000-10-20 | 2002-05-02 | 홍민선 | Automatic closing device for filter in the dust collector using ceramic filters |
| CN105092300A (en) * | 2015-06-03 | 2015-11-25 | 解海龙 | Method for automatic collection of ash sample at ash discharge port of coal-fired boiler dry type dust remover |
| CN112619214A (en) * | 2020-12-11 | 2021-04-09 | 安徽盛世开元装备科技有限公司 | Method for solving underflow discharge of deep cone thickener |
| CN115569468A (en) * | 2022-09-22 | 2023-01-06 | 浙江海宏气体股份有限公司 | Air separation plant feed gas purification equipment and its purification method |
-
1995
- 1995-08-16 JP JP20872495A patent/JP3327743B2/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20020031437A (en) * | 2000-10-20 | 2002-05-02 | 홍민선 | Automatic closing device for filter in the dust collector using ceramic filters |
| CN105092300A (en) * | 2015-06-03 | 2015-11-25 | 解海龙 | Method for automatic collection of ash sample at ash discharge port of coal-fired boiler dry type dust remover |
| CN112619214A (en) * | 2020-12-11 | 2021-04-09 | 安徽盛世开元装备科技有限公司 | Method for solving underflow discharge of deep cone thickener |
| CN115569468A (en) * | 2022-09-22 | 2023-01-06 | 浙江海宏气体股份有限公司 | Air separation plant feed gas purification equipment and its purification method |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3327743B2 (en) | 2002-09-24 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN208852556U (en) | A kind of purification separation system for blast furnace gas thermal energy recycling | |
| US5348568A (en) | Filtering method of flue gas of a boiler and a filter apparatus for hot gas | |
| JP6537190B2 (en) | Filter chamber for gas turbine and maintenance method thereof | |
| KR102021551B1 (en) | Bag filter pulse control system | |
| US4654059A (en) | Multistage rotary dust collector | |
| Caplan | Source control by centrifugal force and gravity | |
| US9084956B2 (en) | Dust collector with monitor air filter | |
| US4113449A (en) | Baghouse cleaning method | |
| US4416673A (en) | Dust collector for furnace charging installation | |
| CN101340964B (en) | Fabric filter with fluidized dust bed and method of maintenance thereof | |
| JPH0952011A (en) | Dust collector | |
| WO2019062545A1 (en) | Outside-filtering bag-type dust remover | |
| US4248612A (en) | Apparatus for cleaning and recovering power from blast furnace exhaust gas | |
| JP5379069B2 (en) | Black smoke removal device | |
| CN204767895U (en) | High temperature dirty gas dust pelletizing system | |
| CN201150826Y (en) | Automatic reverse-blow bag powder purification apparatus | |
| CN218107192U (en) | Bag type dust collector | |
| FI86667C (en) | KRAFTANLAEGGNING MED RENARE AV CENTRIFUGALTYP FOER FOERBRAENNINGSGASER. | |
| CN220759589U (en) | Self-cleaning cyclone separation device | |
| CN213555893U (en) | Self-checking bag type dust removing equipment | |
| KR200292949Y1 (en) | off- line system for filtering and removing dust and injurious gas | |
| JP2016022463A (en) | Plant exhaust gas cleaning device and cleaning method | |
| CN112569713A (en) | Industrial furnace cloth bag dust remover capable of detecting and replacing damaged cloth bag on line | |
| CN222556868U (en) | Dry quenching system | |
| RU2324524C2 (en) | Sectional sleeve filter for purifying of gas |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20020604 |
|
| LAPS | Cancellation because of no payment of annual fees |