JPH0634713U - Foreign matter removal device in dust-containing fluid pipeline - Google Patents

Foreign matter removal device in dust-containing fluid pipeline

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Publication number
JPH0634713U
JPH0634713U JP4564691U JP4564691U JPH0634713U JP H0634713 U JPH0634713 U JP H0634713U JP 4564691 U JP4564691 U JP 4564691U JP 4564691 U JP4564691 U JP 4564691U JP H0634713 U JPH0634713 U JP H0634713U
Authority
JP
Japan
Prior art keywords
foreign matter
filter element
pipeline
cleaning
dust
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.)
Withdrawn
Application number
JP4564691U
Other languages
Japanese (ja)
Inventor
進 田淵
与志幸 土居
学 石原
伸 中村
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 JP4564691U priority Critical patent/JPH0634713U/en
Publication of JPH0634713U publication Critical patent/JPH0634713U/en
Withdrawn legal-status Critical Current

Links

Abstract

(57)【要約】 【目的】 短時間に大量の異物が流入してもその円滑な
除去を可能とする含塵流体管路中の異物除去装置を提供
する。 【構成】 フイルターエレメント2a,2bの前端位置
にあって上記管路の断面の上半部,下半部の流れをそれ
ぞれ開閉するフラップ弁3a,3bと、上記先細まり濾
過流域8の後端寄りで上記管路に分岐された排出弁6
a,6bとを有する管路中の異物除去装置において、上
記上半部,下半部内で上記フイルターエレメント2a,
2bのほぼ全長にわたって縦設され上記両半部をそれぞ
れほぼ等断面積に仕切る単数又は複数の縦方向仕切板7
a,7bと、上記各縦方向仕切板7a,7bにより互い
に仕切られた先細まりの各分流濾過流域9の後部にそれ
ぞれ配設された異物排出弁6a1,6a2,6b1,6
b2とを具えたこと。
(57) [Abstract] [Purpose] To provide a foreign matter removing device in a dust-containing fluid pipe that enables smooth removal of a large amount of foreign matter in a short time. [Structure] Flap valves 3a, 3b at the front end positions of the filter elements 2a, 2b for opening and closing the flow in the upper and lower halves of the cross section of the pipeline, respectively, and the rear end of the tapered filtration flow region 8 Discharge valve 6 branched into the above pipe
In the foreign matter removing device in the pipeline having a and 6b, the filter element 2a in the upper half and the lower half is
A single or a plurality of vertical partition plates 7 which are vertically provided over substantially the entire length of 2b and partition the above-mentioned two halves into substantially equal cross-sectional areas.
a, 7b and foreign matter discharge valves 6a1, 6a2, 6b1, 6 respectively disposed at the rear of the respective taper diversion filtration regions 9 partitioned by the vertical partition plates 7a, 7b.
It is equipped with b2.

Description

【考案の詳細な説明】[Detailed description of the device]

【0001】[0001]

【産業上の利用分野】[Industrial applications]

本考案は含塵流体管路中の異物除去装置に関する。 The present invention relates to a foreign matter removing device in a dust-containing fluid line.

【0002】[0002]

【従来の技術】[Prior art]

例えば、臨海発電所においては、復水器冷却水として大量の海水を利用するこ とが必要であるが、海水中には、塵埃,貝等(以下異物という)が含有されてい るので、これらがそのまま復水器へ流入するときは種々の不具合を生ずる故、取 水路にてこれら異物を除去しなければならない。 この種の用途に使用される流路中の異物除去装置として本出願人はさきに下記 するような手段を実願昭61−33852号として提案した。 同提案は、図6縦断面図に示すように、ケーシング1の断面の中央部から下流 側へ一方は上り勾配で他方は下り勾配でそれぞれ斜設されたフイルターエレメン ト2a,2bを設け、ネットよりなるフイルターエレメント2a,2bのそれぞ れの上流寄りにはケーシング外部より駆動される回転軸を有する洗浄フラップ3 a,3bを設けると共に、ケーシングを貫通してフイルターエレメントの下流寄 りの部分に開口する排出口4a,4bとこれに付設された排出管片5a,5b及 び排出弁6a,6bを連設している。 このような構造において、海水は矢印に示すように左方から右方へ流れ、その 際、下流側に先細形状となるフイルターエレメント外側の濾過流域8a,8bの 海水の流れはフイルター自身の持つ流体通過抵抗により下流側にゆくほど異物密 度は大となり、流入異物はフイルターエレメント内部の下流寄りに集合蓄積し、 ここに異物が蓄積すると、異物除去装置の流体抵抗が増加して腹水器への冷却水 供給能力が低下することから、異物蓄積量がある程度に達するとフイルターエレ メントの洗浄を行うのである。 洗浄作業は、図7縦断面図及び図8正面図に示すように、一方のフイルターエ レメント2aの内部に設けられている洗浄フラップ3aを流れに対して平行する 状態(開位置)から流れを妨げる状態(閉位置)に変化することによって、その 下流側でフイルターエレメントの濾過流域8aを攪乱する流れが形成され、この 攪乱流によってフイルターに捕捉された異物が剥離し、濾過流域8aの中を浮遊 する作用が生ずる。濾過流域8a中を浮遊する異物は、異物排出弁6aを開くこ とによって排出口付近に生ずる吸引流れに追従して排出管片5aから外部に排出 される。そしてフイルターエレメント2aに捕捉されていた異物がすっかり外部 へ排出されると、洗浄フラップ3aを閉から開に戻す。このような洗浄フラップ 及び排出弁の開閉を図9線図に示すように、他方のフイルターエレメント2bに ついても行うことにより洗浄を行い洗浄の全工程が終了することになる。 For example, in coastal power plants, it is necessary to use a large amount of seawater as condenser cooling water, but since seawater contains dust, shellfish, etc. When it flows into the condenser as it is, various problems occur, so these foreign substances must be removed in the intake channel. The applicant previously proposed the following means as Japanese Patent Application No. 61-33852 as an apparatus for removing foreign matter in a channel used for this type of application. According to the same proposal, as shown in the vertical sectional view of FIG. 6, from the central portion of the cross section of the casing 1 to the downstream side, one is provided with an ascending slope and the other is provided with a downwardly sloped filter element 2a, 2b. The cleaning flaps 3a and 3b each having a rotary shaft driven from the outside of the casing are provided on the upstream side of each of the filter elements 2a and 2b, and penetrate the casing to the downstream side of the filter element. The discharge ports 4a and 4b which are opened, the discharge pipe pieces 5a and 5b and the discharge valves 6a and 6b attached thereto are connected in series. In such a structure, seawater flows from the left to the right as shown by the arrow, and the flow of seawater in the filtration basins 8a and 8b outside the filter element, which is tapered toward the downstream side, is the fluid that the filter itself has. Due to the passage resistance, the foreign matter density increases toward the downstream side, and the inflowing foreign matter collects and accumulates near the downstream inside the filter element.When foreign matter accumulates here, the fluid resistance of the foreign matter removing device increases and Since the cooling water supply capacity decreases, the filter element is cleaned when the amount of foreign matter accumulated reaches a certain level. As shown in the longitudinal sectional view of FIG. 7 and the front view of FIG. 8, the cleaning operation is performed from a state (open position) in which the cleaning flap 3a provided inside one of the filter elements 2a is parallel to the flow. By changing to the disturbing state (closed position), a flow that disturbs the filtration basin 8a of the filter element is formed on the downstream side, and the turbulent flow causes foreign matter trapped in the filter to separate, causing a flow inside the filtration basin 8a. Floating action occurs. Foreign matter floating in the filtration flow region 8a is discharged to the outside from the discharge pipe piece 5a by following the suction flow generated near the discharge port by opening the foreign matter discharge valve 6a. When the foreign matter captured by the filter element 2a is completely discharged to the outside, the cleaning flap 3a is returned from closed to open. As shown in the diagram in FIG. 9, opening and closing of the cleaning flap and the discharge valve as described above is performed for the other filter element 2b as well, whereby the cleaning is completed and all the cleaning steps are completed.

【0003】[0003]

【考案が解決しようとする課題】[Problems to be solved by the device]

しかしながら、この種の異物除去装置においては、比較的長時間にわたって捕 捉された異物は除去できるのであるが、短時間の内に大量の異物が流入するとな ると、下記のような問題がある。 すなわち、大量の異物が比較的短時間に流入する場合、一方のフイルターエレ メント2aの濾過流域8aに設けられている洗浄フラップ3aが流れを妨げる故 、装置に流入する水は他方のフイルターエレメント2b側だけを流れることにな って絞り効果を生ずることになる。装置に流入する水量は、ポンプ特性により洗 浄フラップ3aの全開状態とその全閉状態とでほぼ同一になり、大差はないので フイルターエレメント2bを通過する水の流速は2倍近くに増加するから、大量 の異物が一気にフイルターに捕捉された状態で洗浄を開始し、洗浄フラップ3a を閉にした場合、フイルターエレメント2b側に捕捉されている異物による流体 抵抗は、通過する水の流速の増加と相俟って一層増加することになり、フイルタ ーを洗浄するために行った動作が、却って復水器への冷却水供給能力を一層低下 させる惧れがあるのである。 この問題を解消するためには、例えば図10に示すようにフイルターエレメン トの表面積(水の透過面積)を増加して、流体抵抗増加への影響を小さくするか 、あるいは図11に示すように装置を2系統に分割して1系統あたりの水流断面 積を1/2とし、1系統ずつ順次洗浄を行うことにより絞り効果を緩和する等の 手段が一応考えられる。 しかしながら、前者では、同図(A) に示すように、フイルターエレメントを長 くすると、装置面間を長くする必要があり、設置スペースの面から不利となると 共に洗浄フラップの閉動作によって生ずる洗浄に有効な流れがフイルターの下流 寄りで弱くなるため、性能低下につながる可能性があり、また同図(B) に示すよ うに、フイルターエレメントの平滑面を凹凸化すると、フイルターの構造が複雑 になり、製作上不利であると共に凹部に捕捉された異物が剥れにくくなり、性能 低下につながる可能性がある。また、後者では2台の装置の設置は、設置スペー スの面から不利となる。 However, this type of foreign matter removing device can remove foreign matter that has been captured for a relatively long time, but if a large amount of foreign matter flows in within a short time, the following problems occur. . That is, when a large amount of foreign matter flows in for a relatively short time, the cleaning flap 3a provided in the filtration flow area 8a of one of the filter elements 2a blocks the flow, so that the water flowing into the apparatus has the other filter element 2b. It will flow only on the side, which will cause a throttling effect. The amount of water flowing into the device is almost the same between the fully opened state and the fully closed state of the cleaning flap 3a due to the pump characteristics, and since there is no great difference, the flow velocity of the water passing through the filter element 2b is nearly doubled. When cleaning is started with a large amount of foreign matter caught in the filter all at once and the cleaning flap 3a is closed, the fluid resistance due to the foreign matter trapped on the filter element 2b side increases with the flow velocity of the passing water. Together with this, the number of actions taken to clean the filter may rather reduce the cooling water supply capacity to the condenser. In order to solve this problem, for example, as shown in FIG. 10, the surface area (water permeation area) of the filter element is increased to reduce the influence on the increase in fluid resistance, or as shown in FIG. It is conceivable that the device is divided into two systems and the water flow cross-sectional area per system is halved to reduce the throttling effect by cleaning each system one by one. However, in the former case, if the filter element is lengthened, it is necessary to increase the distance between the surfaces of the device, as shown in FIG. The effective flow becomes weaker near the downstream of the filter, which may lead to performance degradation.As shown in Fig. 2B, if the smooth surface of the filter element is made uneven, the filter structure becomes complicated. However, it is not easy to manufacture, and the foreign matter trapped in the recesses is less likely to come off, which may lead to deterioration in performance. In the latter case, the installation of two devices is disadvantageous in terms of installation space.

【0004】 本考案はこのような事情に鑑みて提案されたもので、短時間に大量の異物が流 入してもその円滑な除去を可能とする含塵流体管路中の異物除去装置を提供する ことを目的とする。The present invention has been proposed in view of the above circumstances, and provides a foreign matter removing device in a dust-containing fluid line that enables smooth removal of a large amount of foreign matter even if it is introduced in a short time. The purpose is to provide.

【0005】[0005]

【課題を解決するための手段】[Means for Solving the Problems]

そのために本考案は、含塵流体を流す大径管路の断面中心上に前端が位置し上 り勾配,下り勾配でそれぞれ下流へ延び後端が上記管路内面の上下部に固着され 対向する上記内面との間に先細まり濾過域を形成する上下1対のフイルターエレ メントと、上記フイルターエレメントの前端位置にあって上記管路の断面の上半 部,下半部の流れをそれぞれ開閉するフラップ弁と、上記先細まり濾過流域の後 端寄りで上記管路に分岐された排出弁とを有する管路中の異物除去装置において 、上記上半部下半部内で上記フイルターエレメントのほぼ全長にわたって縦設さ れ上記両半部をそれぞれほぼ等断面積に仕切る単数又は複数の縦方向仕切板と、 上記各縦方向仕切板により互いに仕切られた分流先細まり濾過流域の後部にそれ ぞれ配設された異物排出弁とを具えたことを特徴とする。 Therefore, in the present invention, the front end is located on the center of the cross section of the large-diameter pipe through which the dust-containing fluid flows, and the downstream end extends downward with an upward slope and the downward slope, and the rear end is fixed to the upper and lower parts of the inner surface of the pipe to face each other. A pair of upper and lower filter elements forming a tapered filtration area between the inner surface and the inner surface, and opening and closing the flow in the upper half and lower half of the cross section of the pipeline at the front end position of the filter element. In a foreign matter removing device in a pipeline having a flap valve and a discharge valve branched to the pipeline near the rear end of the tapered filtration basin, in the upper half and the lower half of the foreign matter removing device, the filter element is vertically extended over substantially the entire length of the filter element. One or a plurality of vertical partition plates that divide the two halves into approximately equal cross-sectional areas, and a split-tapered filtration basin partitioned by the vertical partition plates. Was Characterized in that comprises the object exhaust valve.

【0006】[0006]

【作用】[Action]

このような構成によれば、1対のフイルターエレメントにより管路中に形成さ れた上下1対の濾過流域は、単数又は複数の縦方向仕切板により、さらに相互に 仕切られて複数の分流濾過流域、すなわち一般的には2n個の分流濾過流域とな る。 そこで、洗浄に際して、図3〜図4に示すように、その洗浄フラップ3a1を 閉めることは、閉鎖される管路断面積は全体の1/2nとなるに過ぎないので絞 り効果による流速つまり流体抵抗の増加を極力小さくする。 これは流速(流体抵抗)の増加を極力小さくすることができる。なぜならば、 これは装置に流入する水量はポンプ特性により洗浄前と洗浄中とで大差はないの で、洗浄中に開状態の洗浄フラップの部分の断面のフイルターエレメント2a2 ,…,2an及び2b1,2b2,…2b2を透過する水の流速が、従来の技術 を適用した場合には2倍近くに増加するのに対し、本考案を適用した場合には2 n/2n−1倍(例えばn=3の場合1.2倍)以内の増加に抑えられることに よる。 従って、短時間の内に大量の異物が一気にフイルターに捕捉された状態で洗浄 を行った場合でも、流速(流体抵抗)の増加による復水器への冷却水供給能力低 下は最小限に抑えられるのである。 According to such a configuration, the pair of upper and lower filtration basins formed in the pipe by the pair of filter elements are further partitioned from each other by the vertical partition plate or plates to form a plurality of split flow filters. There will be a catchment basin, typically 2n shunt filtration basins. Therefore, in cleaning, as shown in FIGS. 3 to 4, when the cleaning flap 3a1 is closed, the cross-sectional area of the closed pipeline becomes only 1 / 2n of the whole, so the flow velocity due to the throttling effect, that is, the fluid. Minimize the increase in resistance. This can minimize the increase in flow velocity (fluid resistance). This is because the amount of water flowing into the device is not so different before and during washing due to the pump characteristics, so that the filter elements 2a2, ..., 2an and 2b1, of the cross section of the washing flap in the opened state during washing. The flow velocity of water passing through 2b2, ..., 2b2 increases nearly twice when the conventional technique is applied, whereas it is 2 n / 2n-1 times (for example, n = In case of 3, the increase is 1.2 times or less). Therefore, even when cleaning is performed with a large amount of foreign matter caught in the filter at once in a short time, the decrease in cooling water supply capacity to the condenser due to the increase in flow velocity (fluid resistance) is minimized. Be done.

【0007】[0007]

【実施例】【Example】

本考案の一実施例を図面について説明すると、図1はその縦断面図、図2は図 1の仕切板の変形例を示す同じく縦断面図、図3は図2の正面図、図4は図3の 変形例を示す同じく正面図、図5は図1の洗浄フラップ及び排出弁の開閉要領を 示す線図である。 まず、図1〜図4において、図6と同一の符号はそれぞれ同図と同一の部材を 示し,本考案が同図の構造と大きく異なるところは、各フイルターエレメントを ハッチングで示す縦方向仕切板により左右に複数の濾過流域に仕切ったことにあ る。 すなわち、7はケーシング1を洗浄フラップ3a及びフイルターエレメント2 aと、洗浄フラップ3b及びフイルターエレメント2bとによって囲む先細まり 濾過流域8a,8bの部分をほぼ等断面積で左右に仕切る直角三角形状の縦方向 仕切板であり、洗浄フラップは全部で図3に示すように3a1,3a2,3b1 ,3b2の4枚にて構成すると共に、異物排出管及び排出弁もそれぞれ各洗浄フ ラップに対応して全部で4個ずつ配設される。 ここで、仕切板7aは図1に示すように、フイルターエレメント2aとほぼ同 一の大きさ直角三角形状のものであってもよいし、また図2にハッチングで示す ように、洗浄フラップの若干上流からフイルターエレメントの若干下流にわたる 比較的長い長方形の仕切板7bとしてもよい。 An embodiment of the present invention will be described with reference to the drawings. FIG. 1 is a longitudinal sectional view thereof, FIG. 2 is a longitudinal sectional view showing a modification of the partition plate of FIG. 1, FIG. 3 is a front view of FIG. 2, and FIG. 3 is a front view showing a modified example of FIG. 3, and FIG. 5 is a diagram showing an opening / closing procedure of the cleaning flap and the discharge valve of FIG. First, in FIGS. 1 to 4, the same reference numerals as those in FIG. 6 denote the same members as in FIG. 6, respectively. The major difference of the present invention from the structure in FIG. 6 is that each filter element is indicated by a vertical partition plate. It means that it is divided into multiple filtration basins on the left and right. That is, reference numeral 7 is a right-angled triangular vertical section that divides the casing 1 into the left and right portions of the tapered filtration basins 8a and 8b which are surrounded by the cleaning flap 3a and the filter element 2a and the cleaning flap 3b and the filter element 2b. This is a partition plate, and the cleaning flap is composed of 4 sheets 3a1, 3a2, 3b1, 3b2 as shown in FIG. 3, and the foreign matter discharge pipe and the discharge valve are all corresponding to the respective cleaning flaps. Are arranged in fours. Here, as shown in FIG. 1, the partition plate 7a may be a right-angled triangular shape having substantially the same size as the filter element 2a, or as shown by hatching in FIG. A relatively long rectangular partition plate 7b extending from upstream to slightly downstream of the filter element may be used.

【0008】 このような実施例構造においてはフイルターエレメントの濾過流域は2枚の仕 切板により全部で4本の分流濾過流域になっているが、図4に示すように、仕切 板の数を増すことで、フイルターエレメント濾過流域は、一般的には、2a1, 2a2,…,2an及び2b1,2b2,…,2bnに仕切板られ、それぞれに 洗浄フラップ3a1,3a2,…,3an及び3b1,3b2,…,3bnと異 物排出口4a1,4a2,…,4an及び4b1,4b2,…,4bnとが設け られる。 そこで、洗浄に際しては、まず、洗浄フラップ3a1が閉作動して、フイルタ ーエレメント2a1部分の洗浄が行われ、このとき洗浄フラップによって閉鎖さ れる断面積は、全体の1/2nとなるので、従来の技術を適用した場合の1/2 に対して、絞り効果による流速(流体抵抗)増加を極力小さくすることができる 。なぜならば、装置に流入する水量はポンプ特性により洗浄前と洗浄中とで大差 はないので、洗浄中に開状態の洗浄フラップの部分(閉鎖されていない)部分の 断面のフイルターエレメント2a2,…,2an及び2b1,2b2,…,2b 2を透過する水の流速が、従来の技術を適用した場合には2倍近くに増加するこ とに対して、本考案を適用した場合には2n/2n−1倍(例えばn=3の場合 1.2倍)以内の増加に抑えられるからである。 従って、短時間の内に大量の異物が一気にフイルターに捕捉された状態で洗浄 を行った場合でも、流速(流体抵抗)の増加による復水器への冷却水供給能力低 下は最小限に抑えられのである。In such an embodiment structure, the filtering basin of the filter element is a total of four shunt filtering basins due to the two partition plates, but as shown in FIG. By increasing, the filter element filtration basin is generally divided into 2a1, 2a2, ..., 2an and 2b1, 2b2, ..., 2bn, and cleaning flaps 3a1, 3a2, ..., 3an and 3b1, 3b2, respectively. , 3bn and foreign matter discharge ports 4a1, 4a2, ..., 4an and 4b1, 4b2, ..., 4bn are provided. Therefore, at the time of cleaning, first, the cleaning flap 3a1 is closed to clean the filter element 2a1 portion. At this time, the cross-sectional area closed by the cleaning flap is 1 / 2n of the whole, so It is possible to minimize the increase in the flow velocity (fluid resistance) due to the throttling effect, as compared with 1/2 when the technology is applied. Because the amount of water flowing into the device is not so different before and during washing due to the characteristics of the pump, the filter elements 2a2, ..., Of the cross section of the washing flap portion (not closed) portion in the opened state during washing. The flow velocity of water passing through 2an and 2b1, 2b2, ..., 2b 2 is nearly doubled when the conventional technique is applied, while it is 2n / 2n when the present invention is applied. This is because the increase can be suppressed within −1 times (for example, 1.2 times when n = 3). Therefore, even when cleaning is performed with a large amount of foreign matter caught in the filter at once in a short time, the decrease in cooling water supply capacity to the condenser due to the increase in flow velocity (fluid resistance) is minimized. It is.

【0009】 なお、フイルター仕切板を設けずに洗浄フラップだけを複数に分割することも 一応は考えられるが、この場合には閉作動した洗浄フラップの下流側で生ずるフ イルターエレメントの濾過流域を攪乱する流れが、その周辺の下流側にまっすぐ 向う流れの影響で弱められる傾向にある。そのため、下流側にまっすぐ向う流れ の影響が及ぶことのないよう仕切板を設けておくことは非常に重要である。 更に、フイルターエレメント一方の濾過流域の洗浄が完了すると、次に他方の 濾過流域の洗浄が開始されるが、本考案では、図5に示すように、洗浄フラップ 3a1が閉から開へ作動するのと同時に、洗浄フラップ3a2が開から閉へ作動 するようにする。 これは洗浄フラップ3a1が閉から開への作動を完了するのを待って、それ以 外の洗浄フラップ3a2を開から閉へ作動する洗浄機能を採用した場合、洗浄フ ラップの数が多くなった分全体の洗浄工程(時間)が長くなることに対して、1 つの洗浄フラップを閉から開へ動作した場合、洗浄フラップの閉鎖による流体抵 抗が開度変化とともに減少することに着目し、それ以外の洗浄フラップを開から 閉作動して前記流体抵抗減少分だけ増加を許容することにより、洗浄時間を短縮 することができることによる。 同図によれば図9に示した従来の技術による異物除去装置の場合と比較して、 洗浄フラップの数が多くなっても洗浄時間はそれ程長くならないことが判る。 仕切板は洗浄フラップの下流側で生ずるフイルターエレメントの濾過流域の攪 乱流が、その周辺の下流側にまっすぐ向う流れの影響で弱められるのを防止する ことを達成できる大きさ、つまり大きい方が望ましいが、目安としてフイルター エレメント以上の大きさとすることがよい。Although it is conceivable that only the cleaning flap is divided into a plurality of parts without providing the filter partition plate, in this case, the filtering flow area of the filter element generated on the downstream side of the closed cleaning flap is set. The disturbing flow tends to be weakened by the effect of the flow going straight downstream to its perimeter. Therefore, it is very important to install a partition plate so that the flow is not affected by a straight flow on the downstream side. Further, when the cleaning of one filtering basin of the filter element is completed, the cleaning of the other filtering basin is started next. In the present invention, as shown in FIG. 5, the cleaning flap 3a1 operates from closed to open. At the same time, the cleaning flap 3a2 is operated from open to closed. This is because the number of cleaning flaps increases when the cleaning function that waits for the cleaning flap 3a1 to complete the operation from closed to open and then operates the other cleaning flaps 3a2 from open to closed is used. It is noted that the fluid resistance due to the closing of the cleaning flap decreases with the change of the opening when one cleaning flap is operated from the closed to the open, whereas the cleaning process (time) of the whole minute becomes long. This is because the cleaning time can be shortened by operating the cleaning flaps other than those described above from opening to closing to allow an increase in the fluid resistance decrease amount. According to the figure, it can be seen that the cleaning time does not become so long even if the number of cleaning flaps increases, as compared with the case of the conventional foreign matter removing device shown in FIG. The partition plate should be large enough to prevent the disturbance of the filter element's filtration basin downstream of the wash flaps from being weakened by the effect of a flow straight down to its perimeter, i.e. larger. Although it is desirable, the size should be larger than the filter element as a guide.

【0010】[0010]

【本考案の効果】[Effect of the present invention]

このような構造によれば、洗浄フラップ閉鎖時のフイルターエレメントを透過 する水の流速の増加を小さくすることができ、従って短時間の内に大量の異物が フイルターに捕捉された状態で洗浄を行った場合でも、流体抵抗の増加による復 水器への冷却水供給能力低下も最小限に抑えられる。 要するに本考案によれば、含塵流体を流す大径管路の断面中心上に前端が位置 し上り勾配,下り勾配でそれぞれ下流へ延び後端が上記管路内面の上下部に固着 され対向する上記内面との間に先細まり濾過域を形成する上下1対のフイルター エレメントと、上記フイルターエレメントの前端位置にあって上記管路の断面の 上半部,下半部の流れをそれぞれ開閉するフラップ弁と、上記先細まり濾過流域 の後端寄りで上記管路に分岐された排出弁とを有する管路中の異物除去装置にお いて、上記上半部下半部内で上記フイルターエレメントのほぼ全長にわたって縦 設され上記両半部をそれぞれほぼ等断面積に仕切る単数又は複数の縦方向仕切板 と、上記各縦方向仕切板により互いに仕切られた分流先細まり濾過流域の後部に それぞれ配設された異物排出弁とを具えたことにより、短時間に大量の異物が流 入してもその円滑な除去を可能とする含塵流体管路中の異物除去装置を得るから 、本考案は産業上極めて有益なものである。 With such a structure, it is possible to reduce the increase in the flow velocity of the water that permeates the filter element when the cleaning flap is closed, so that the cleaning is performed while a large amount of foreign matter is captured by the filter within a short time. In this case, the decrease in cooling water supply capacity to the condenser due to the increase in fluid resistance can be minimized. In short, according to the present invention, the front end is located on the center of the cross section of the large-diameter pipe through which the dust-containing fluid flows, and the upstream end and the downward slope extend downstream respectively, and the rear end is fixed and opposed to the upper and lower parts of the inner surface of the pipe. A pair of upper and lower filter elements forming a tapered filtration zone between the inner surface and the inner surface, and flaps at the front end positions of the filter elements for opening and closing the flow of the upper half part and the lower half part of the cross section of the pipeline, respectively. In a foreign matter removing device in a pipeline having a valve and a discharge valve branched into the pipeline near the rear end of the tapered filtration basin, in the upper half and the lower half of the filter, the filter element extends over substantially the entire length of the filter element. One or a plurality of vertical partition plates that are vertically installed and partition each of the above-mentioned two halves into substantially equal cross-sectional areas, and are installed respectively at the rear of the divergent taper filtration basins that are partitioned by the vertical partition plates. Since a foreign matter discharge valve is provided, a foreign matter removing device in a dust-containing fluid pipeline that enables smooth removal of a large amount of foreign matter in a short time can be obtained. It is extremely useful.

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

【図1】本考案の一実施例を示す縦断面図である。FIG. 1 is a vertical sectional view showing an embodiment of the present invention.

【図2】図1の仕切板の変形例を示す同じく縦断面図で
ある。
FIG. 2 is a vertical sectional view showing a modified example of the partition plate of FIG.

【図3】図2の正面図である。FIG. 3 is a front view of FIG.

【図4】図3の変形例を示す同じく正面図である。FIG. 4 is a front view of the modification of FIG.

【図5】図1の洗浄フラップ及び排出弁の開閉要領を示
す線図である。
5 is a diagram showing how to open and close the cleaning flap and the discharge valve of FIG. 1. FIG.

【図6】公知の発電所復水器冷却水の異物除去装置を示
す縦断面図である。
FIG. 6 is a vertical cross-sectional view showing a known foreign matter removing device for cooling water of a power plant condenser.

【図7】図6の洗浄中の状態を示す同じく、縦断面図で
ある。
FIG. 7 is a vertical sectional view showing the state of FIG. 6 during cleaning.

【図8】図7の正面図である。8 is a front view of FIG. 7. FIG.

【図9】図7の洗浄フラップ及び排出弁の開閉要領を示
す説明図である。
FIG. 9 is an explanatory diagram showing an opening / closing procedure of the cleaning flap and the discharge valve of FIG. 7.

【図10】図6の変形例を示す縦断面図である。10 is a vertical cross-sectional view showing a modified example of FIG.

【図11】図10の変形例を示す側面図及び平面図であ
る。
11A and 11B are a side view and a plan view showing a modified example of FIG.

【符号の説明】[Explanation of symbols]

1 本体ケーシング 2,2a,2b フイルターエレメント 3,3a,3b,…,3an,3bn 洗浄フラップ 4,4a,4b,…,4an,4bn 異物排出口 5,5a,5b,…,5an,5bn 異物排出管片 6,6a,6b,…,6an,6bn 異物排出弁 7,7a,7b 仕切板 8 濾過流域 9 分流濾過流域 1 Main body casing 2,2a, 2b Filter element 3,3a, 3b, ..., 3an, 3bn Cleaning flap 4,4a, 4b, ..., 4an, 4bn Foreign matter discharge port 5,5a, 5b, ..., 5an, 5bn Foreign matter discharge Pipe piece 6,6a, 6b, ..., 6an, 6bn Foreign matter discharge valve 7,7a, 7b Partition plate 8 Filtration basin 9 Separation and filtration basin

───────────────────────────────────────────────────── フロントページの続き (72)考案者 中村 伸 兵庫県高砂市荒井町新浜二丁目1番1号 三菱重工業株式会社高砂製作所内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Shin Nakamura 2-1-1, Niihama, Arai-cho, Takasago, Hyogo Prefecture Mitsubishi Heavy Industries, Ltd. Takasago Plant

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】 含塵流体を流す大径管路の断面中心上に
前端が位置し上り勾配,下り勾配でそれぞれ下流へ延び
後端が上記管路内面の上下部に固着され対向する上記内
面との間に先細まり濾過域を形成する上下1対のフイル
ターエレメントと、上記フイルターエレメントの前端位
置にあって上記管路の断面の上半部,下半部の流れをそ
れぞれ開閉するフラップ弁と、上記先細まり濾過流域の
後端寄りで上記管路に分岐された排出弁とを有する管路
中の異物除去装置において、上記上半部下半部内で上記
フイルターエレメントのほぼ全長にわたって縦設され上
記両半部をそれぞれほぼ等断面積に仕切る単数又は複数
の縦方向仕切板と、上記各縦方向仕切板により互いに仕
切られた分流先細まり濾過流域の後部にそれぞれ配設さ
れた異物排出弁とを具えたことを特徴とする含塵流体管
路中の異物除去装置。
1. An inner surface of a large-diameter pipe through which a dust-containing fluid flows, the front end of which is located on the center of the cross section and extends downstream at an upslope and a downslope, respectively, and the rear end is fixed to the upper and lower portions of the inner surface of the pipe and faces each other. And a pair of upper and lower filter elements that form a tapered filtration area between them and a flap valve that is located at the front end position of the filter element and that opens and closes the flow of the upper half portion and the lower half portion of the cross section of the pipeline, respectively. In the foreign matter removing device in the pipeline having a discharge valve branched into the pipeline near the rear end of the tapered filtration region, in the upper half lower half, the filter element is installed vertically over substantially the entire length of the filter element. A single or a plurality of vertical partition plates for partitioning both halves into approximately equal cross-sectional areas, and a foreign matter discharge valve respectively disposed at the rear of the split taper filtration basin partitioned by the vertical partition plates. A device for removing foreign matter in a dust-containing fluid pipe characterized by comprising:
JP4564691U 1991-05-21 1991-05-21 Foreign matter removal device in dust-containing fluid pipeline Withdrawn JPH0634713U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4564691U JPH0634713U (en) 1991-05-21 1991-05-21 Foreign matter removal device in dust-containing fluid pipeline

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4564691U JPH0634713U (en) 1991-05-21 1991-05-21 Foreign matter removal device in dust-containing fluid pipeline

Publications (1)

Publication Number Publication Date
JPH0634713U true JPH0634713U (en) 1994-05-10

Family

ID=12725141

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4564691U Withdrawn JPH0634713U (en) 1991-05-21 1991-05-21 Foreign matter removal device in dust-containing fluid pipeline

Country Status (1)

Country Link
JP (1) JPH0634713U (en)

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