JP3499943B2 - Dust removal device - Google Patents

Dust removal device

Info

Publication number
JP3499943B2
JP3499943B2 JP32682594A JP32682594A JP3499943B2 JP 3499943 B2 JP3499943 B2 JP 3499943B2 JP 32682594 A JP32682594 A JP 32682594A JP 32682594 A JP32682594 A JP 32682594A JP 3499943 B2 JP3499943 B2 JP 3499943B2
Authority
JP
Japan
Prior art keywords
filter
tube
filter cylinder
dust
tube sheet
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 - Fee Related
Application number
JP32682594A
Other languages
Japanese (ja)
Other versions
JPH08173736A (en
Inventor
重泰 石神
雄一郎 北川
寛 秋山
久隆 浦方
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP32682594A priority Critical patent/JP3499943B2/en
Publication of JPH08173736A publication Critical patent/JPH08173736A/en
Application granted granted Critical
Publication of JP3499943B2 publication Critical patent/JP3499943B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Filtering Of Dispersed Particles In Gases (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は除塵装置、特に石炭等の
化石燃料を使用する燃焼設備・ガス化設備から排出され
る高温含塵ガス用除塵装置に関する。本発明は、しかし
これに限らず製鉄・セメント・化学プラント等の排ガス
の除塵装置にも適用可能である。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a dust remover, and more particularly to a dust remover for high temperature dust-containing gas discharged from a combustion facility / gasification facility using fossil fuel such as coal. However, the present invention is not limited to this, but can be applied to exhaust gas dust removers such as those for iron making, cement, and chemical plants.

【0002】[0002]

【従来の技術】図8,図9に従来の除塵装置の一例を断
面図でしめす。この従来の除塵装置は、複数の多孔質濾
筒1を含塵ガスの流れ方向に沿って配列したものであ
る。即ち、各多孔質濾筒1は、ほぼ鉛直に配置された缶
体33内に塵含ガスの流れ方向に沿って配列されてい
る。そしてこの缶体33の上部の含塵ガス入口30から
缶体33内に流入した含塵ガスは、各多孔質濾筒1内に
流入し、その濾壁を内側から外側へと通過する過程で除
塵され、清浄ガスとなって清浄ガス出口31から流出す
る。一方ガスから除去された粉塵は、缶体33の下部の
粉塵ホッパ34へ導かれ、排出される。なお、各多孔質
濾筒1の上下端はそれぞれ管板(仕切り板)5,21,
37によって支持されている。図8(A)は1本の濾
筒、即ち単位濾筒1を複数本、ほぼ鉛直に缶体33内に
配置し、濾筒上端部及び濾筒下端部を上部管板5及び下
部管板21により粉塵シール36されて支持される除塵
装置の1例を示したものである。単位濾筒1はセラミッ
クファイバーローブなどを使用し粉塵シール36でシー
ルされ、濾筒1と管体33との熱膨張差による相対変位
を半径方向、軸方向共に許容しているが濾筒を逆洗によ
り再生する方法を使用するとき、上部管板5を下部管板
21に逆洗時の差圧による変形を生じて濾筒に曲げモー
メントによる応力が作用し、強度の弱いセラミックフィ
ルタでは実用規模の長尺化が困難となる。
2. Description of the Related Art FIGS. 8 and 9 are sectional views showing an example of a conventional dust remover. In this conventional dust remover, a plurality of porous filter cylinders 1 are arranged along the flow direction of dust-containing gas. That is, the respective porous filter cylinders 1 are arranged along the flow direction of the dust-containing gas in the can body 33 arranged substantially vertically. The dust-containing gas flowing into the can body 33 from the dust-containing gas inlet 30 at the top of the can body 33 flows into each porous filter cylinder 1 and passes through the filter wall from the inside to the outside. The dust is removed, and the gas becomes clean gas and flows out from the clean gas outlet 31. On the other hand, the dust removed from the gas is guided to the dust hopper 34 below the can body 33 and discharged. It should be noted that the upper and lower ends of each porous filter cylinder 1 have tube plates (partition plates) 5, 21,
It is supported by 37. FIG. 8 (A) shows one filter cylinder, that is, a plurality of unit filter cylinders 1 arranged substantially vertically in the can body 33, and the filter cylinder upper end and the filter cylinder lower end are the upper tube sheet 5 and the lower tube sheet. 1 shows an example of a dust removing device supported by a dust seal 36 by 21. The unit filter cylinder 1 is sealed by a dust seal 36 using a ceramic fiber lobe or the like, and allows relative displacement due to the difference in thermal expansion between the filter cylinder 1 and the tubular body 33 in both the radial direction and the axial direction, but the filter cylinder is reversed. When the method of regenerating by washing is used, the upper tube sheet 5 is deformed in the lower tube sheet 21 due to the differential pressure during backwashing, and the bending moment exerts a stress on the filter tube. It becomes difficult to make the length longer.

【0003】図8(B)は従来の除値装置の他の1例を
示す。濾筒1の分割部分(連結部)39に支持管板37
を設けて支持すると共に、粉塵シール36が必要箇所に
設けられている。この従来例においても、前記曲げモー
メントによる応力が作用し、実用規模の長尺化は困難で
ある。
FIG. 8B shows another example of a conventional dividing device. The support tube plate 37 is attached to the divided portion (connecting portion) 39 of the filter cylinder 1.
Is provided and supported, and a dust seal 36 is provided at a required position. Also in this conventional example, the stress due to the bending moment acts, and it is difficult to increase the length on a practical scale.

【0004】図9は多孔質固体から単位濾筒を連結して
1本の濾筒をなし、同濾筒群を少なくとも連結部をダス
トタイトにシールすると共に、同連結部を管板によって
支持する集塵装置の1例を示したものである。(B)は
図9における濾筒連結部R部分の拡大断面図、(C)は
図9における下端の水冷管板40と濾筒1との接続部の
拡大断面図、(D)は図9における上端の水冷管板40
と濾筒1との接続部の拡大断面図を示す。図9には、1
枚の水冷管板40の挿通孔に上下2本の濾筒を構成する
セラミック管1,1の端部をそれぞれ挿通して接続した
構造が示されている。この接続構造では、下のセラミッ
ク管に上のセラミック管を載せており、かつ各セラミッ
ク管と挿通孔との管にファイバーローブなどからなる紐
状のシールを巻回し充填してシールしている。しかしな
がら前記の接続構造のいては、上のセラミック管を下の
セラミック管で支持しているので、多段構造になると、
下のセラミック管に過大な荷重がかかり、破損しやすく
なる。また上下にセラミック管の端面が接触しているの
で、この端面も破損しやすい。更に多段構造となると、
熱膨張差による伸びが累積され、上にいくほど膨張量が
多くなり、継ぎ目位置が管板の厚み内におさまらなくな
ることがある。また前記の接続構造を用いた集塵装置に
おける逆洗時には、例えば管板の下側かつセラミック管
の外側の空間にパルス的に加圧された逆洗気流を流し、
一方、管板の上側かつセラミック管の外側の空間には通
常圧のままの除塵された気体が流れていることがある。
このとき、逆洗気流は、その全量がセラミック管壁を通
って管内に流れるべきであるが、シール部のシール性が
不足しているので、シール部を通過して逆洗気流が上の
通常圧の空間に流れてしまい、逆洗が充分に行われない
ことが多い。
In FIG. 9, unit filter cylinders are connected from a porous solid to form one filter cylinder, and at least the connection part of the filter cylinder group is sealed dust-tight, and the connection part is supported by a tube plate. 1 shows an example of a dust collector. 9B is an enlarged cross-sectional view of the filter tube connecting portion R portion in FIG. 9, FIG. 9C is an enlarged cross-sectional view of the connection portion between the water cooling tube plate 40 at the lower end and the filter tube 1 in FIG. 9, and FIG. Top water cooling tube plate 40
The expanded sectional view of the connection part of the filter barrel 1 and FIG. In FIG. 9, 1
The structure is shown in which the ends of the ceramic tubes 1, 1 constituting the upper and lower two filter tubes are inserted and connected to the insertion holes of the water cooling tube plate 40. In this connection structure, the upper ceramic tube is placed on the lower ceramic tube, and a string-shaped seal made of a fiber lobe or the like is wound around and filled in the tube between each ceramic tube and the insertion hole for sealing. However, in the above-mentioned connection structure, since the upper ceramic tube is supported by the lower ceramic tube, when it becomes a multi-stage structure,
The lower ceramic tube is subject to excessive load and is easily damaged. Further, since the upper and lower end faces of the ceramic tube are in contact with each other, this end face is also easily damaged. When it becomes a multi-stage structure,
Elongation due to the difference in thermal expansion is accumulated, the amount of expansion increases as it goes up, and the seam position may not fit within the thickness of the tube sheet. Further, at the time of backwashing in the dust collector using the connection structure, for example, a pulsed backwash airflow is made to flow in the space below the tube plate and outside the ceramic tube,
On the other hand, in the space above the tube plate and outside the ceramic tube, dust-removed gas at normal pressure may flow.
At this time, the total amount of the backwash airflow should flow through the ceramic tube wall into the tube, but since the sealability of the seal part is insufficient, the backwash airflow passes through the seal part and is usually above. It often flows into the space of pressure and backwashing is not performed sufficiently.

【0005】[0005]

【発明が解決しようとする課題】前記従来の除塵装置
を、粉塵発生量の多い石炭等の化石燃料を使用する燃焼
設備から排出される高温含塵ガスの除塵に用いる場合に
は、大容量の含塵ガスを除塵するため、ガスが通過する
面積を確保するように複数の多孔質濾筒を含塵ガスの流
れ方向にほぼ鉛直に長尺化して配置する必要があった。
この多孔質濾筒は、焼成前は一般的に強度が非常に小さ
く、長尺物はハンドリング及び焼成の過程で変形しやす
いために、1本の長さがせいぜい1〜2m程度にしか製
作できない。またこの短い多孔質セラミック管同士を接
合する技術も存在するが、長尺化すればするほど自励及
び他からの振動等で破壊する問題があった。即ち、従来
の除塵装置では濾筒の連結部をダストタイトにシールす
ると共に管板によって支持して長尺化を図り、缶体と濾
筒との熱伸び差の吸収、地震、自励及び他からの強制振
動等の対策を行っているが、逆洗時の差圧による上部管
板、下部管板の変形、また高温下の熱変形により濾筒に
作用する曲げモーメントの低減を図るため、上下の濾筒
端部を、管板の挿通孔の範囲内で接続し、濾筒と挿通孔
の間にシール材を充填してシールおよび支持するので、
熱伸び差等で接続部が挿通孔から外れると成立たない構
造であるなど、種々の技術課題があった。本発明は以上
の問題点を解決して大きな荷重の作用や熱膨張差が累積
されても破損や除塵能力が低下することのない長尺化さ
れた除塵装置を提供する。
When the above conventional dust remover is used to remove high-temperature dust-containing gas discharged from a combustion facility that uses fossil fuel such as coal, which produces a large amount of dust, it has a large capacity. In order to remove dust-containing gas, it was necessary to arrange a plurality of porous filter cylinders so as to be vertically long in the flow direction of dust-containing gas so as to secure an area through which the gas passes.
This porous filter cylinder generally has a very low strength before firing, and a long product is easily deformed in the process of handling and firing, so that one length can be manufactured at most about 1 to 2 m. . There is also a technique for joining these short porous ceramic tubes to each other, but there is a problem that the longer they are, the more they are destroyed by self-excitation and vibration from others. That is, in the conventional dust removing device, the connecting portion of the filter cylinder is dust tightly sealed and supported by the tube plate to increase the length, thereby absorbing the difference in thermal expansion between the can body and the filter cylinder, earthquake, self-excitation and other factors. However, in order to reduce the bending moment that acts on the filter tube due to the deformation of the upper tube plate and the lower tube plate due to the differential pressure during backwashing, and the thermal deformation at high temperature, Since the upper and lower ends of the filter cylinder are connected within the range of the insertion hole of the tube plate and the sealing material is filled between the filter cylinder and the insertion hole to seal and support,
There are various technical problems such as a structure that cannot be established when the connecting portion is disengaged from the insertion hole due to a difference in thermal expansion or the like. The present invention solves the above problems and provides an elongated dust removing device which does not suffer damage or lower dust removing capability even when a large load is applied or a thermal expansion difference is accumulated.

【0006】[0006]

【課題を解決するための手段】このため本発明は、通気
性を有する多孔質セラミックスからなる濾筒の内側に含
塵ガスを供給し、濾筒の外側から清浄ガスを取り出す除
塵装置において、単位濾筒を接合して長尺の濾筒とな
し、同濾筒の中間に一箇所屈折可能な緩い凹凸構造の連
結部を有し、これらの濾筒を下部管板に回転変位可能
に、上部管板に対し上下に摺動可能に設けた円環体に回
転変位可能に支持し、上部濾筒または下部濾筒のいずれ
か一端の濾筒中間部を上下に摺動可能に支持して濾筒を
直立に自立させるとともに、前記上部濾筒または前記下
部濾筒のいずれか一端の前記濾筒中間部を支持する金物
が容器に取付けられた管板に固定され、濾筒が前記管板
に挿通する所の周囲に上下室の均圧連通を行う間隔を設
け、上下室の差圧による前記管板の変形を抑止し、濾筒
の支持点での振れをなくしてなるもので、これを課題解
決のための手段とするものである。また本発明は、前記
下部管板と濾筒の下端は緩い凹凸構造とし、パッキンを
介してダストタイトにシールして回転変位可能に支持
し、上部管板に対し上下に摺動シール可能に設けた円環
体と濾筒の上端は緩い凹凸構造とし、パッキンを介して
ダストタイトにシールして回転変位可能に支持するもの
であり、更に前記下部濾筒と上部濾筒の連結部が、屈折
可能な緩い凹凸構造のパッキンを介した連結構造とし、
下部管板、上部管板の変形に対し個別に回転変位シール
可能に構成されてなるもので、これらを課題解決のため
の手段とするものである。
For this reason, the present invention provides a dust removing apparatus in which a dust-containing gas is supplied to the inside of a filter cylinder made of porous ceramic having air permeability and clean gas is taken out from the outside of the filter cylinder. The filter tubes are joined together to form a long filter tube, and there is a connecting part with a loose concavo-convex structure that can be bent in one place in the middle of the filter tube. It is rotatably supported by an annular body that is slidable up and down relative to the tube plate, and the middle part of the filter barrel at either end of the upper filter barrel or the lower filter barrel is slidably supported up and down. While making the tube stand upright, the upper filter tube or the lower tube
Which supports the middle part of the filter cylinder at one end of the filter cylinder
Is fixed to the tube plate attached to the container, and the filter tube is attached to the tube plate.
A space for equalizing the upper and lower chambers is provided around the place where the
The deformation of the tube sheet due to the pressure difference between the upper and lower chambers is suppressed,
It eliminates the swing at the support point of, and makes this a means for solving the problem. According to the present invention, the lower tube sheet and the lower end of the filter tube have a loose concavo-convex structure, which is sealed by dust tight through a packing so as to be rotatably displaceable, and slidably sealed vertically with respect to the upper tube sheet. The ring-shaped body and the upper end of the filter cylinder have a loose concavo-convex structure, which is sealed by dust tight through a packing to support rotatably displacement. With a connecting structure via a packing with a loose uneven structure that is possible,
Lower tube plate, in which respect the deformation of the upper tube sheet composed is configured to be rotationally displaced individually sealed, it is an unit for the these problems solved.

【0007】[0007]

【作用】上部濾筒又は下部濾筒の何れか一方のみを支持
し、管板の挿通孔を外れた位置で、上下濾筒の緩い凹凸
構造部にパッキンを取付け、シール性を保ちつつ屈折可
能に連結し、濾筒の管板挿通部周囲には間隔が設けてあ
る本発明の濾筒連結・支持構造によって、下部濾筒に大
きな荷重が作用しても、緩い凹凸構造部にクッション性
のあるパッキンを取付けて連結しているので、破損する
心配は無く、熱膨張差が累積されても、管板の挿通孔と
は無関係にシール及び支持されているので、シール低
下、支持の問題を生じず、濾筒と管板の挿通孔の間に間
隔を設け、上下方向一括逆洗するので、逆洗性能低下の
心配は無く、また連結部をシール性を保ちつつ屈折可能
な構造としているため、逆洗時に上部管板・下部管板の
変形が生じても濾筒に曲げモーメントによる応力が作用
することは無く、強度の弱いセラミックフィルタで実用
規模の長尺を達成できる。
[Function] Only one of the upper filter cylinder and the lower filter cylinder is supported, and the packing is attached to the loose concavo-convex structure part of the upper and lower filter cylinders at the position out of the insertion hole of the tube plate, and it is possible to bend while maintaining the sealing property. The filter tube connecting / supporting structure of the present invention in which a space is provided around the tube plate insertion portion of the filter tube allows the loose concavo-convex structure portion to have a cushioning property even when a large load is applied to the lower filter tube. Since a certain packing is attached and connected, there is no risk of breakage, and even if the thermal expansion difference is accumulated, it is sealed and supported regardless of the insertion hole of the tube sheet, so there is no problem of seal deterioration and support. Since it does not occur, a gap is provided between the filter cylinder and the insertion hole of the tube plate, and back-and-forth vertical back washing is not performed, so there is no concern about back wash performance deterioration, and the connecting portion has a structure that can be bent while maintaining sealing performance. Therefore, even if the upper and lower tube sheets are deformed during backwashing, the filter tube It is not the stress caused by the bending moment acts, the utility-scale long at weak ceramic filter strength can be achieved.

【0008】[0008]

【実施例】以下本発明の実施例を図面について詳細に説
明する。図1〜図7において、同一の部分には同一の符
号を付して重複する説明は省略する。図1は本発明の第
1実施例に係る濾筒連結・支持構造を示す。図3は連結
部構造の断面図、図5は上部管板部における濾筒の取付
部断面図、図6は下部管板部における濾筒の取付部断面
図を示す。第1実施例では図7に示す除塵装置の缶体3
3内に複数の通気性を有する多孔質濾筒1がほぼ鉛直に
配置され、その内側に含塵ガスを供給し、多孔質濾筒の
外側から清浄ガスを取出すように構成されている。図1
に示すように、ほぼ鉛直に配置された単位濾筒は各濾筒
接合部17にて加熱圧接されて1本の濾筒を形成し上部
濾筒2と下部濾筒3が濾筒連結部4にて連結され、ほぼ
鉛直な長尺の濾筒を構成し、上部管板5と下部管板21
との間に設置され支持される。
Embodiments of the present invention will now be described in detail with reference to the drawings. 1 to 7, the same parts are designated by the same reference numerals, and overlapping description will be omitted. FIG. 1 shows a filter barrel connecting / supporting structure according to a first embodiment of the present invention. 3 is a cross-sectional view of the connecting portion structure, FIG. 5 is a cross-sectional view of the filter tube mounting portion in the upper tube sheet portion, and FIG. 6 is a cross-sectional view of the filter tube mounting portion in the lower tube sheet portion. In the first embodiment, the can body 3 of the dust removing device shown in FIG.
A plurality of air-permeable porous filter cylinders 1 are arranged substantially vertically in the chamber 3, and dust-containing gas is supplied to the inside thereof to take out clean gas from the outside of the porous filter cylinder. Figure 1
As shown in FIG. 2, the unit filter cylinders arranged substantially vertically are heated and pressure-bonded at each filter cylinder joint portion 17 to form one filter cylinder, and the upper filter cylinder 2 and the lower filter cylinder 3 are connected to each other by the filter cylinder connecting portion 4. Connected to each other to form a vertically long filter cylinder, and the upper tube sheet 5 and the lower tube sheet 21 are connected to each other.
Installed between and supported by.

【0009】図5において、上部管板5は濾筒の挿通孔
16を有し挿通孔16には円環状で上側外周部はフラン
ジを形成している金属環9が挿入されて上部管板5に固
定される。また挿通孔16内には、上部濾筒2の上端部
にセラミックス繊維等を編合わせたシールパッキン
(b)10を介して円環体7の下端取付座8との間で緩
い凹凸構造とし、円環体7の自重により回転変位シール
可能とされている。この円環体7の外周部と円環状の金
属環9との間にセラミックス繊維等を編合わせたロープ
状のシールパッキン(a)6を介し、前記円環体7が上
下に摺動可能に、かつ粉塵をシールした状態で金属環9
介して上部管板5に支持されている。更にシールパッキ
ン(a)6の上には、円環体7の外周部と金属環の内周
部の間に押え板11が載せられ、シールパッキン(a)
6が脱落するのを防止している。
In FIG. 5, the upper tube sheet 5 has an insertion hole 16 for a filter cylinder, and a metal ring 9 having an annular shape and a flange on the upper outer peripheral portion is inserted into the insertion hole 16 to insert the upper tube sheet 5 into the upper tube sheet 5. Fixed to. Further, in the insertion hole 16, a loose concavo-convex structure is formed between the upper end of the upper filter cylinder 2 and the lower end mounting seat 8 of the annular body 7 via a seal packing (b) 10 in which ceramic fibers or the like are woven, It is possible to seal the rotational displacement by the weight of the annular body 7. The ring-shaped body 7 is slidable up and down through a rope-shaped seal packing (a) 6 in which ceramic fibers or the like are woven between the outer peripheral portion of the ring-shaped body 7 and the ring-shaped metal ring 9. , And the metal ring 9 with dust sealed
It is supported by the upper tube sheet 5 via. Further, a pressing plate 11 is placed on the seal packing (a) 6 between the outer peripheral portion of the annular body 7 and the inner peripheral portion of the metal ring.
6 is prevented from falling off.

【0010】図6において、下部管板21は円環状の濾
筒受け金物20を有し、濾筒受け金物20の上端取付座
8と下部濾筒3の下端との間で緩い凹凸構造とし、シー
ルパッキン(b)10を介して円環体7、上部濾筒2、
下部濾筒3の自重により、回転変位シール可能に支持し
ている。図3は上部濾筒2と下部濾筒3の濾筒連結・支
持構造を示し、連結部は下部濾筒3の上端部に取付座8
を形成し、その上部に上部濾筒2の下端部をシールパッ
キン(b)10を介して載せ、個別に屈折可能な緩い凹
凸構造とし、円環体7、上部濾筒2の自重により回転変
位シール可能としている。また前記回転変位を上下濾筒
で個別に可能とするため、上部濾筒の濾筒中間部を管板
12に固定された支持金物(a)13により上下に摺動
可能に支持して、上下濾筒を直立に自立させる。また管
板12に設ける挿通孔16には、下部濾筒3の間隔18
を形成し、管板12の上下空間で逆洗時に均圧連通を促
進すると共に、逆洗時差圧により管板12の変位が生じ
ない様にしている。
In FIG. 6, the lower tube sheet 21 has an annular filter barrel receiving member 20, and has a loose concavo-convex structure between the upper end mounting seat 8 of the filter barrel receiving member 20 and the lower end of the lower filter barrel 3. The ring body 7, the upper filter cylinder 2, and the seal packing (b) 10
The lower filter cylinder 3 is supported by its own weight so that it can be rotationally displaced and sealed. FIG. 3 shows a filter barrel connecting / supporting structure of the upper filter barrel 2 and the lower filter barrel 3, and the connecting portion is a mounting seat 8 at the upper end of the lower filter barrel 3.
Is formed, and the lower end of the upper filter cylinder 2 is placed on the upper part thereof through the seal packing (b) 10 to form a loose concavo-convex structure capable of being individually refracted. The circular ring body 7 and the upper filter cylinder 2 are rotationally displaced by their own weight. It is possible to seal. Further, in order to enable the rotational displacement individually by the upper and lower filter cylinders, the intermediate portion of the filter cylinder of the upper filter cylinder is slidably supported in the vertical direction by the support metal (a) 13 fixed to the tube plate 12, Make the filter tube stand upright. Further, the insertion hole 16 provided in the tube sheet 12 has a space 18 between the lower filter cylinders 3.
Is formed to promote equalization communication in the upper and lower spaces of the tube sheet 12 during backwashing, and prevent displacement of the tubesheet 12 due to the differential pressure during backwashing.

【0011】図2は本発明の第2実施例に係る濾筒連結
・支持構造を示す。図4は連結部構造の断面図を示す。
第2実施例では、図4に示すように、上部濾筒2と下部
濾筒3の濾筒連結.支持構造の連結部は図3と同一の構
造とし、円環体7、上部濾筒2の自重により回転変位シ
ール可能に構成されている。更に、前記回転変位を上下
濾筒で個別に可能とするため、下部濾筒3の濾筒中間部
を管板12に固定された支持金物(b)14により上下
に摺動可能に支持し、上下濾筒を直立に自立させる。
FIG. 2 shows a filter barrel connecting / supporting structure according to a second embodiment of the present invention. FIG. 4 shows a sectional view of the connecting portion structure.
In the second embodiment, as shown in FIG. 4, the filter barrel connection of the upper filter barrel 2 and the lower filter barrel 3. The connecting portion of the support structure has the same structure as that of FIG. 3, and is configured to be sealed by rotational displacement by the weight of the annular body 7 and the upper filter cylinder 2. Further, in order to enable the rotational displacement individually by the upper and lower filter barrels, the intermediate portion of the filter barrel of the lower filter barrel 3 is supported slidably up and down by the support metal member (b) 14 fixed to the tube plate 12. Make the upper and lower filter tubes stand upright.

【0012】[0012]

【発明の効果】以上詳細に説明した如く本発明によれ
ば、上部濾筒と下部濾筒の連結・支持構造により、下部
濾筒に大きな荷重が作用しても、緩い凹凸構造部にクッ
ション性があるパッキンを取付けて連結しているので、
破損する心配は無く、熱膨張差が累積されても、管板の
挿通孔とは無関係にシール及び支持されているので、シ
ールの低下、支持の問題は生じず、濾筒と管板の挿通孔
の間に間隔を設け、上下方向一括逆洗するので、逆洗性
能低下の心配は無く、また連結部をシール性を保ちつつ
屈折可能な構造としているため、逆洗時に上部管板・下
部管板の変形が生じても濾筒に曲げモーメントによる応
力が作用することは無く、強度の弱いセラミックフィル
タで実用規模の長尺化を達成できる。
As described in detail above, according to the present invention, due to the connecting / supporting structure of the upper filter cylinder and the lower filter cylinder, even if a large load is applied to the lower filter cylinder, the cushioning property of the loose concavo-convex structure is obtained. Since there is a packing that has a connection,
There is no risk of breakage, and even if the difference in thermal expansion is accumulated, the seal and support are independent of the insertion hole of the tube sheet, so there is no problem of deterioration of the seal or support, and the insertion of the filter tube and tube sheet. Since there is a space between the holes, and there is no need to worry about backwashing performance deterioration because it is backwashed in the vertical direction at the same time, and because the connection part has a structure that can be bent while maintaining sealing performance, the upper tube sheet and lower part Even if the tube plate is deformed, the stress due to the bending moment does not act on the filter cylinder, and the ceramic filter having low strength can be made long on a practical scale.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の第1実施例に係る濾筒連結・支持構造
図である。
FIG. 1 is a structural view of a filter barrel connection / support structure according to a first embodiment of the present invention.

【図2】本発明の第2実施例に係る濾筒連結・支持構造
図である。
FIG. 2 is a filter barrel connection / support structure diagram according to a second embodiment of the present invention.

【図3】第1実施例の連結部構造の断面図である。FIG. 3 is a sectional view of a connecting portion structure of the first embodiment.

【図4】第2実施例の連結部構造の断面図である。FIG. 4 is a sectional view of a connecting portion structure according to a second embodiment.

【図5】同実施例の上部管板部における濾筒の取付部断
面図である。
FIG. 5 is a sectional view of an attachment portion of a filter cylinder in the upper tube sheet portion of the embodiment.

【図6】同実施例の下部管板部における濾筒の取付部断
面図である。
FIG. 6 is a sectional view of an attachment portion of a filter tube in the lower tube sheet portion of the embodiment.

【図7】同実施例の除塵装置全体を示す説明図である。FIG. 7 is an explanatory view showing the entire dust removing device of the same embodiment.

【図8】従来の除塵装置の一例を示す断面図である。FIG. 8 is a sectional view showing an example of a conventional dust remover.

【図9】従来の除塵装置の他の例を示す断面図である。FIG. 9 is a cross-sectional view showing another example of a conventional dust removing device.

【符号の説明】[Explanation of symbols]

1 濾筒 2 上部濾筒 3 下部濾筒 4 濾筒連結部 5 上部管板 6 シールパッキン(a) 7 円環体 8 取付け座 9 金属環 10 シールパッキン(b) 11 押え板 12 管板 13 支持金物(a) 14 振れ止め 15 支持リング 16 挿通孔 17 濾筒接合部 18 間隔(クリアランス) 19 支持金物(b) 20 濾筒受け金物 21 下部管板 30 含塵ガス入口 31 清浄ガス出口 32 灰抜出し部 33 缶体 34 ホッパ 35 内筒 1 filter tube 2 Upper filter cylinder 3 Lower filter tube 4 Filter tube connection part 5 Upper tube sheet 6 Seal packing (a) 7 torus 8 mounting seat 9 metal rings 10 Seal packing (b) 11 Presser plate 12 tube sheet 13 Support hardware (a) 14 steady rest 15 Support ring 16 insertion holes 17 Filter tube joint 18 intervals (clearance) 19 Support hardware (b) 20 Filter barrel hardware 21 Lower tube sheet 30 Dust-containing gas inlet 31 Clean gas outlet 32 Ash extraction section 33 cans 34 hopper 35 inner cylinder

───────────────────────────────────────────────────── フロントページの続き (72)発明者 秋山 寛 長崎市飽の浦町1番1号 三菱重工業株 式会社 長崎造船所内 (72)発明者 浦方 久隆 長崎市飽の浦町1番1号 三菱重工業株 式会社 長崎造船所内 (56)参考文献 特開 平6−285320(JP,A) 実開 平4−57218(JP,U)   ─────────────────────────────────────────────────── ─── Continued front page    (72) Inventor Hiroshi Akiyama               1-1 Nagasaki City Atunoura-cho Mitsubishi Heavy Industries Ltd.               Inside the Nagasaki Shipyard (72) Inventor Hisataka Urakata               1-1 Nagasaki City Atunoura-cho Mitsubishi Heavy Industries Ltd.               Inside the Nagasaki Shipyard                (56) References JP-A-6-285320 (JP, A)                 Actual Kaihei 4-57218 (JP, U)

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】通気性を有する多孔質セラミックスからな
る濾筒の内側に含塵ガスを供給し、濾筒の外側から清浄
ガスを取り出す除塵装置において、単位濾筒を接合して
長尺の濾筒となし、同濾筒の中間に一箇所屈折可能な緩
い凹凸構造の連結部を有し、これらの濾筒を下部管板に
回転変位可能に、上部管板に対し上下に摺動可能に設け
た円環体に回転変位可能に支持し、上部濾筒または下部
濾筒のいずれか一端の濾筒中間部を上下に摺動可能に支
持して濾筒を直立に自立させるとともに、 前記上部濾筒または前記下部濾筒のいずれか一端の前記
濾筒中間部を支持する金物が容器に取付けられた管板に
固定され、濾筒が前記管板に挿通する所の周囲に上下室
の均圧連通を行う間隔を設け、上下室の差圧による前記
管板の変形を抑止し、濾筒の支持点での振れをなくした
ことを特徴とする除塵装置。
1. A dust removing device, wherein a dust-containing gas is supplied to the inside of a filter cylinder made of porous ceramics having air permeability, and clean gas is taken out from the outside of the filter cylinder. Without a cylinder, it has a loose concavo-convex connecting part that can be bent at one place in the middle of the filter cylinder, and these filter cylinders can be rotationally displaced on the lower tube sheet and can slide up and down with respect to the upper tube sheet. rotating displaceably supported in an annular body provided, causes self-standing the濾筒the upright濾筒intermediate portion of one end of the upper濾筒or lower濾筒slidably supporting and vertically, the upper Either the filter tube or the lower filter tube at one end
The metal supporting the middle part of the filter cylinder is attached to the tube plate attached to the container.
The upper and lower chambers are fixed around the place where the filter tube is inserted into the tube plate.
There is an interval for equalizing and communicating with each other.
Prevents deformation of the tube sheet and eliminates runout at the support point of the filter tube
A dust removing device characterized in that
【請求項2】請求項1において、下部管板と濾筒の下端
は緩い凹凸構造とし、パッキンを介してダストタイトに
シールして回転変位可能に支持し、上部管板に対し上下
に摺動シール可能に設けた円環体と濾筒の上端は緩い凹
凸構造とし、パッキンを介してダストタイトにシールし
て回転変位可能に支持することを特徴とする除塵装置。
2. The lower tube sheet and the lower end of the filter tube according to claim 1, wherein the lower tube sheet and the lower end of the filter tube have a loose concavo-convex structure. A dust remover characterized in that a sealable annular body and the upper end of a filter cylinder have a loose concavo-convex structure, and are sealed to dust tight through a packing so that they can be rotationally displaced.
【請求項3】請求項1において下部濾筒と上部濾筒の連
結部が、屈折可能な緩い凹凸構造のパッキンを介した連
結構造とし、下部管板、上部管板の変形に対し個別に回
転変位シール可能に構成されたことを特徴とする除塵装
置。
3. The connecting part between the lower filter cylinder and the upper filter cylinder according to claim 1, wherein the connecting structure is via a packing having a concave and convex structure which can be bent, and is rotated independently with respect to deformation of the lower tube plate and the upper tube plate. A dust remover characterized by being capable of displacement sealing.
JP32682594A 1994-12-28 1994-12-28 Dust removal device Expired - Fee Related JP3499943B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP32682594A JP3499943B2 (en) 1994-12-28 1994-12-28 Dust removal device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP32682594A JP3499943B2 (en) 1994-12-28 1994-12-28 Dust removal device

Publications (2)

Publication Number Publication Date
JPH08173736A JPH08173736A (en) 1996-07-09
JP3499943B2 true JP3499943B2 (en) 2004-02-23

Family

ID=18192139

Family Applications (1)

Application Number Title Priority Date Filing Date
JP32682594A Expired - Fee Related JP3499943B2 (en) 1994-12-28 1994-12-28 Dust removal device

Country Status (1)

Country Link
JP (1) JP3499943B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010184198A (en) * 2009-02-12 2010-08-26 Inax Corp Bonded ceramic filter and water cleaning cartridge

Also Published As

Publication number Publication date
JPH08173736A (en) 1996-07-09

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