JPS6144527B2 - - Google Patents
Info
- Publication number
- JPS6144527B2 JPS6144527B2 JP58006680A JP668083A JPS6144527B2 JP S6144527 B2 JPS6144527 B2 JP S6144527B2 JP 58006680 A JP58006680 A JP 58006680A JP 668083 A JP668083 A JP 668083A JP S6144527 B2 JPS6144527 B2 JP S6144527B2
- Authority
- JP
- Japan
- Prior art keywords
- mesh
- fluid
- plate
- pressure
- hole
- 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
Links
- 239000012530 fluid Substances 0.000 claims description 64
- 230000005484 gravity Effects 0.000 claims description 40
- 239000002184 metal Substances 0.000 claims description 35
- 229910052751 metal Inorganic materials 0.000 claims description 35
- 230000002441 reversible effect Effects 0.000 claims description 21
- 230000003014 reinforcing effect Effects 0.000 claims description 10
- 238000004519 manufacturing process Methods 0.000 claims 1
- 239000002893 slag Substances 0.000 description 23
- 238000011001 backwashing Methods 0.000 description 16
- 230000000694 effects Effects 0.000 description 9
- 238000000034 method Methods 0.000 description 7
- 238000001914 filtration Methods 0.000 description 6
- 238000011084 recovery Methods 0.000 description 6
- 239000007787 solid Substances 0.000 description 6
- 239000002699 waste material Substances 0.000 description 5
- 239000000463 material Substances 0.000 description 4
- 239000004033 plastic Substances 0.000 description 4
- 229920003023 plastic Polymers 0.000 description 4
- 239000004576 sand Substances 0.000 description 4
- 150000002739 metals Chemical class 0.000 description 3
- 230000002787 reinforcement Effects 0.000 description 3
- 230000001680 brushing effect Effects 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 238000007747 plating Methods 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 238000007740 vapor deposition Methods 0.000 description 2
- 238000013022 venting Methods 0.000 description 2
- 229910002114 biscuit porcelain Inorganic materials 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 239000010727 cylinder oil Substances 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 230000002427 irreversible effect Effects 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Filtration Of Liquid (AREA)
Description
【発明の詳細な説明】
本発明は耐圧網目過板を用いる逆重力過装
置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a reverse gravity passing device using a pressure-resistant mesh passing plate.
流体の過は一般に重力を過圧とする自然
過によつて行なわれるのが常であり、また重力に
その他の圧力が附加される場合でも被過流体を
重力の方向に沿つて過するのが一般である。し
かしながら、かような重力方向過においては、
滓は被過流体から孔の上面に分離され、重
力により下方向に圧せられて孔の上部に堆積圧
着し、被過流体の孔への流下流入を阻むので
目詰りが極めて早期に到来する。この目詰りを回
復するには過を中断して特別の目詰り回復策を
講ぜねばならないから、連続過は不能となり、
過能率は著しく害される。 The overpressure of fluid is generally carried out by natural overpressure with gravity, and even when other pressures are added to gravity, it is best to pass the overflowed fluid along the direction of gravity. General. However, in such a direction of gravity,
The slag is separated from the passing fluid on the top surface of the hole, is pressed downward by gravity, and is deposited on the top of the hole, blocking the flowing of the passing fluid into the hole, resulting in clogging very early. . To recover from this clogging, it is necessary to interrupt the flow and take special clogging recovery measures, making continuous flow impossible.
Overefficiency is severely impaired.
しかしながら、実質的に水平に配設された金属
製網目を孔とし、被過流体を重力の方向とは
逆に下方から上方に向けて通過させて過するも
のとすると事情は一変する。滓は過により被
過流体から網目孔の下面において分離され
る。この分離された滓は、過圧による上方向
への圧力を受けることは勿論であるが、それと同
時に重力によるこれに抗する下方向への圧力をも
受ける。 However, the situation changes completely when the holes are made of metal meshes arranged substantially horizontally, and the permeable fluid is passed through from the bottom to the top, opposite to the direction of gravity. The slag is separated from the permeate fluid at the lower surface of the mesh holes by means of a sieve. The separated slag is of course subjected to upward pressure due to overpressure, but at the same time is also subject to downward pressure due to gravity to counteract this pressure.
従つて、重力方向過の場合に滓をその下方
の孔に圧着せしめる働きをした重力は、ここで
は滓を孔から引離し、その下方に湛えられた
被過流体中に沈降拡散せしめる働きをする。こ
の働きは過が停止され上向きの過圧がなくな
つた場合特に顕著となる。以上のような次第で、
金属製網目を孔とする逆重力過の場合には、
重力が目詰りの進行を緩和する働きをするため目
詰りの到来は延期され、後述の簡易効果的な逆洗
が可能なことと相俟つて相当長期に亘る連続過
が可能となり、過能率を著しく向上せしめ得
る。 Therefore, the force of gravity that would have pressed the slag against the hole below it in the case of a gravitational force, now acts to pull the slag away from the hole and cause it to settle and diffuse into the permeable fluid stored below. . This effect becomes especially noticeable when the overpressure is stopped and the upward overpressure disappears. According to the above,
In the case of reverse gravity flow using metal mesh as holes,
Since gravity acts to slow down the progress of clogging, the onset of clogging is postponed, and combined with the possibility of simple and effective backwashing, which will be described later, it is possible to run the system continuously for quite a long time, reducing overefficiency. It can be significantly improved.
網目逆重力過の以上のような長所は、逆重力
過なる過法に負うものであることは勿論であ
るが、同時に孔としての優れた特徴を持つ金属
製網目孔の使用に負ること多大なものがある。
以下金属製網目孔の、孔としての優れた特徴
およびこの特徴が逆重力過に如何に寄与するか
につき詳述する。 Of course, the above-mentioned advantages of the mesh reverse gravity flow are due to the reverse gravity flow method, but at the same time, a great deal is owed to the use of metal mesh holes, which have excellent characteristics as holes. There is something.
The excellent features of the metal mesh holes as holes and how these features contribute to the reverse gravity will be explained in detail below.
金属製網目とは、その網を織成している縦横2
本ずつ計4本の線材によつて劃され、線材の開き
を一辺の長さとし、線材の径を奥行きの深さとす
る四辺形筒状の空間である。この網目空間の断面
は第1A図〜第1C図に示す網目孔模型のA,
B,C,Dによつて囲まれた区域(爾後最狭断面
部と呼称する)で最小面積(爾後最狭断面積と呼
称する)となり、これを境にしてその前後は急速
に末広がり状に広がる。 Metal mesh refers to the length and width of the mesh.
It is a quadrilateral cylindrical space that is separated by a total of four wire rods, with the width of the wire rods being the length of one side and the diameter of the wire rods being the depth. The cross section of this mesh space is A of the mesh hole model shown in Figures 1A to 1C.
The area surrounded by B, C, and D (hereinafter referred to as the narrowest cross-sectional area) has the minimum area (hereinafter referred to as the narrowest cross-sectional area), and from this point on, the area before and after it rapidly widens to the end. spread.
過のため被過流体がこの網目空間に圧入さ
れると、流体中に混在している最狭断面積より大
型の固形物は何れも最狭断面部で流入を阻止さ
れ、その前面空間に分離残置され所謂滓とす
る。最狭断面部を通過し得た小型固形物は、爾後
網目空間の断面積が広がるのみで最狭断面積より
狭くなることがないから、空間内の何処にも停滞
滞留することなくすべて網目空間の外に溢出す
る。従つて最狭断面部以降の網目空間中には停滞
滞留する固形物は皆無である。以上のような構造
上の特徴から、孔としての金属製網目孔は以
下のような優れた長所を発揮する。 When the overflowing fluid is forced into this mesh space, any solids larger than the narrowest cross-sectional area mixed in the fluid are blocked from flowing in at the narrowest cross-sectional area and are separated into the space in front of it. It is left behind and becomes so-called slag. Small solid objects that are able to pass through the narrowest cross-section only expand the cross-sectional area of the mesh space, but do not become narrower than the narrowest cross-sectional area. overflow outside. Therefore, there is no solid matter that stagnates and accumulates in the mesh space after the narrowest cross section. Due to the above-mentioned structural features, metal mesh holes as holes exhibit the following excellent advantages.
(1) 所要過圧が低くて済む。(1) Required overpressure is low.
過のため被過流体が孔を通過する際の
圧力損失、従つてまた所要過圧は他の条件が
同一である限り孔の奥行きの長さに比例し、
孔の断面積に反比例する。金属製網目孔の
奥行きの長さは、砂過における砂層中の
孔、素焼・焼結金属・スポンジプラスチツク等
製の床中の諸孔のような、その径の数百倍
という奥行きの著しく長い孔に比べると比較
にならぬ短かさで、たかだか目の開きの1倍前
後に過ぎず、所要過圧も亦比較にならぬ低圧
力で済む。従つて、素焼・焼結金属・スポンジ
プラスチツクス等の高精度過用孔におい
て、長い孔と微小孔径という所要過圧高化
要因の二つが重なり、所要過圧が甚しい高圧
となる場合でも、金属網目孔においては奥行
きが短いという低所要過圧要因が有利に働
き、同一過精度であるにも拘らず左までの高
過圧を要しない。 The pressure drop due to the passage of the turbid fluid through the hole, and therefore the required overpressure, is proportional to the length of the hole depth, other things being equal.
It is inversely proportional to the cross-sectional area of the pore. The depth of metal mesh holes is extremely long, several hundred times the diameter, such as holes in sand layers in sand filters, holes in floors made of unglazed, sintered metal, sponge plastic, etc. Compared to a hole, it is incomparably shorter, only about one time the opening of the eye, and the required overpressure is also incomparably low. Therefore, in high-precision over-use holes in bisque sintered metals, sintered metals, sponge plastics, etc., the two factors that increase the required overpressure, namely the long hole and the small hole diameter, overlap, and even if the required overpressure becomes extremely high, Metal mesh holes are advantageous because of their short depth, which is a low required overpressure factor, and high overpressure to the left is not required even though the overaccuracy is the same.
前述の通り、逆重力過においては、上向き
の過圧に抗して下向きの重力が目詰りの進行
を緩和する。従つて、過圧が小なるほど重力
の目詰り緩和作用はより効果的となる。この意
味で、所要過圧を比較的低位に押さえ得る金
層製網目孔は逆重力過用孔として極めて
適切なものであり、特に大なる過圧を必要と
する高精度過の場合の逆重力過においては
不可欠な孔ということができる。 As mentioned above, in the case of reverse gravity, the downward force of gravity counteracts the upward force of overpressure and slows down the progress of clogging. Therefore, the smaller the overpressure, the more effective the clogging alleviation effect of gravity becomes. In this sense, the mesh hole made of gold layer, which can keep the required overpressure to a relatively low level, is extremely suitable as a hole for reverse gravity overpressure, especially for high precision overpressure that requires a large overpressure. It can be said that it is an essential hole in the process.
(2) 目詰りの回復が容易である。(2) Recovery from clogging is easy.
砂過における砂層中の孔、素焼・焼結金
属・スポンジプラスチツクス製床中の諸孔
のように、その径に比べて奥行きの極めて長い
孔においては、目詰りはその長い孔中の随
所に発生する。奥行きの深部に発生した目詰り
が床の表面や裏面からの洗浄やブラシ掛けな
どで回復できる道理がない。また逆洗も長い
孔を通過する間に勢いを殺がれ実効は乏しい。
要するにこれ等の孔においては簡易有効な目
詰り回復策は存在しない。これに反し金属製網
目孔においては目詰りはすべて最狭断面部前
面にのみ発生し、滓はすべて最狭断面部前面
の空間に集中する。最狭断面図前面の洗浄・ブ
ブラシ掛けによりその除去は簡単であり、逆洗
も孔の入口部分に止つている滓を、奥行き
の極めて短い孔を通過するのみでなお勢い充
分な流体によつて、その外方に押戻すというこ
とにほかならず、極めて効果的であり得る。 In holes that are extremely deep compared to their diameter, such as holes in the sand layer of a sand filter, or holes in unglazed, sintered metal, or sponge plastic beds, clogging occurs throughout the long hole. Occur. There is no way that clogging that occurs deep within the floor can be recovered by cleaning or brushing from the surface or back of the floor. Also, backwashing loses its momentum while passing through long holes, making it less effective.
In short, there is no simple and effective method to recover from clogging in these holes. On the other hand, in metal mesh holes, all clogging occurs only in the front of the narrowest cross-section, and all slag concentrates in the space in front of the narrowest cross-section. It is easy to remove by cleaning and brushing the front side of the narrowest cross-sectional view, and backwashing also removes slag stuck at the entrance of the hole by passing through the extremely short hole with a powerful fluid. , which is nothing more than pushing it back outwards, and can be extremely effective.
以上のような次第で、金属製網目孔を実質
的に水平に配設した逆重力過においては、
滓はすべて網目孔下面の被過流体中に分離
され、且つ重力方向過の場合と違つてその下
方には滓を支えるものは皆無であるから、重
力は直ちにこれに働き、被過流体中に沈降拡
散させ、目詰りを逐次回復せしめる結果とな
る。前述の網目逆重力過における重力の目詰
り緩和作用の実体はこれであり、金属製網目
孔なればこその効果である。また逆洗も、上述
のような状態にある滓を、網目孔上部に貯
留された過済み流体を短い孔を通して勢い
充分に垂直に落下させ、孔の外に押戻すもの
であり、目詰りを極めて簡易効果的に回復する
ことができる。尚その場合、過済み流体の一
部を過器の外部に貯留し、これをポンプ等に
より加圧し逆洗用として併せ流下させると、よ
り短時間での且つより完全な逆洗効果が収めら
れ、これを自動化することにより自動逆洗連続
過も可能となる。網目孔にのみ期待可能な
効果的逆洗である。 According to the above, in a reverse gravity flow in which the metal mesh holes are arranged substantially horizontally,
All of the slag is separated into the flowing fluid at the bottom of the mesh hole, and unlike in the case of gravitational flow, there is nothing below to support the slag, so gravity acts on it immediately and causes the slag to flow into the flowing fluid. This results in sedimentation and diffusion, which gradually recovers from clogging. This is the actual effect of the clogging alleviation effect of gravity in the above-mentioned mesh reverse gravity flow, and this effect can only be achieved by using metal mesh holes. In addition, backwashing is a method in which the waste fluid stored in the upper part of the mesh holes is dropped vertically with sufficient force through short holes to push the slag in the above-mentioned state back out of the holes, thereby eliminating clogging. It is possible to recover extremely easily and effectively. In that case, if a part of the waste fluid is stored outside the filter, pressurized by a pump, etc., and flowed down together for backwashing, a more complete backwashing effect can be achieved in a shorter time. By automating this process, automatic backwashing and continuous filtration becomes possible. This is an effective backwash that can only be expected from mesh holes.
(3) 鍍金・蒸着等により所望の過精度が得られ
る。(3) Desired overaccuracy can be obtained by plating, vapor deposition, etc.
金属製網目は金属線材を以て織成したもので
あるから、鍍金・蒸着による線材の肉付けによ
つて目の開きを随意狭め、一桁のミクロン数程
度にまで過精度を向上することができる。し
かもこの調製された新網は、その織成線材の線
径が旧網より大となつたのみで、依然として金
属製網であることには変りがないから、前記金
属製網の孔としての長所は充分に保たれてい
る。高精度の場合の逆重力過は、この高精度
にしてなお過の圧力損失が僅少であり、目詰
りの回復も容易であるという、この被鍍金(蒸
着)精密網目孔によつてのみ始めて可能であ
る。素焼・焼結金属・スポンジプラスチツクス
等製の奥行きの長い高精度孔によつては、逆
重力過の充分な効果の発揮は到底望まれ得な
い。 Since the metal mesh is woven from metal wire, the mesh opening can be arbitrarily narrowed by thickening the wire by plating or vapor deposition, and the overaccuracy can be improved to about a single-digit micron number. Moreover, the newly prepared net is still a metal net, only the wire diameter of the woven wire rod is larger than that of the old net, so it has the advantages of the metal net as a hole. is well maintained. High-precision reverse gravity overflow is possible only with this plated (vapor-deposited) precision mesh hole, which has minimal pressure loss and easy recovery from clogging even with high precision. It is. With long, high-precision holes made of unglazed, sintered metal, sponge plastic, etc., the full effect of reverse gravity cannot be expected.
つぎに耐圧網目過板について述べる。 Next, we will discuss the pressure-resistant mesh plate.
上述のように金属製網目孔は、孔としての
優れた特徴を持ち、逆重力過の充分な効果の発
揮もこの金属製網目孔を俟つて始めて可能とな
るものであるが、しかしただ単に金属製網目単独
のものをそのまま孔として使用したのでは過
圧に耐える床としての剛性に乏しく、その織成
線材も繊細脆弱で、高精度の場合の、あるいは目
詰りが進行した場合の高過圧に耐え得ず、破断
され復元不能の変形を受けるおそれがある。従つ
て逆重力過用孔としての金属製網目には、こ
れに備える充分な耐圧補強が施されねばならぬ
が、その補強は金属製網目孔の長所である過
の圧力損失僅少、目詰りの回復容易という特徴を
損なうことなく、また網目孔単独の場合に比べ
てその過能率をいささかも低下せしめることの
ないものでなければならぬ。 As mentioned above, metal mesh holes have excellent characteristics as holes, and it is only through these metal mesh holes that the full effect of reverse gravity can be achieved. If a single mesh made of mesh is used as a hole, it will not have enough rigidity to withstand overpressure, and the woven wire material will also be delicate and brittle, making it difficult to handle high overpressure in cases of high precision or when clogging progresses. There is a risk that the product will not be able to withstand such high temperatures and will be damaged and irreversibly deformed. Therefore, the metal mesh used as the counter-gravity overflow hole must be sufficiently reinforced with pressure resistance, but this reinforcement has the advantages of metal mesh holes, such as minimal pressure loss and no clogging. It must be such that it does not impair its feature of easy recovery and does not reduce its overefficiency in any way compared to the case of using mesh holes alone.
耐圧網目過板はこの要請にこたえる逆重力
過用の耐圧金属製網目孔であり、その構造は第
2A図〜第2C図に示す通りであり、以下同図に
つき耐圧網目過板の構造を説明する。 The pressure-resistant mesh overplate is a pressure-resistant metal mesh hole for reverse gravity that meets this requirement, and its structure is as shown in Figures 2A to 2C.The structure of the pressure-resistant mesh overboard will be explained below with reference to the figures. do.
耐圧網目過板の被過流体流入側最前部に
は、所望の過精度に適合する目の開きの金属製
網の板である網板1が配設される。耐圧網目
過板の最後部には、加えられ得る過圧、過器
内圧に耐え得る剛性を有し且つ被過流体流過に
際しての圧力損失を極微に止め得る、充分に大き
な孔径の多数の被過流体流過用貫通孔4が全面
に分布して設けられている剛性板3が配設され
る。網板1と剛性板3との間には、網板1の
金属製網よりも線径および目の開きの大きな金属
製網であつて、
a 前記貫通孔4上に位置して、過圧・過器
内圧に耐え得る耐圧強度を有すること、
b 前記網を支持して過圧・過器内圧に耐
えさせ得る耐圧補強能を有すること、
c 孔を通過した過済み流体の全量を、目詰
りせしめることなく且つ極微の圧力損失を以て
前記貫通孔まで流過せしめ得る、充分な広さの
断面の過済み流体流過用通路を、前記剛性板
面との間に形成することができる線径の太さを
もつこと、
以上a〜cの条件を満足させ得る金属製網の板
である補強網板2が配設され、これ等3枚の周辺
部は隙間なく熔接着されて、被過流体が網板
の網目、補強網板の網目、補強網板と剛性板面と
の間の過済み流体流過用通路、貫通孔の順に流
過し得るように構成される。 A mesh plate 1, which is a metal mesh plate with a mesh size suitable for a desired overaccuracy, is disposed at the forefront of the pressure-resistant mesh plate on the fluid inflow side. At the rearmost part of the pressure-resistant mesh overplate, there are a large number of holes with sufficiently large diameters that are rigid enough to withstand the overpressure and internal pressure that can be applied, and that can minimize pressure loss when the overflowing fluid flows. A rigid plate 3 is provided with through holes 4 for excessive fluid flow distributed over the entire surface. Between the mesh plate 1 and the rigid plate 3, there is provided a metal mesh having a larger wire diameter and opening than the metal mesh of the mesh plate 1;・Having a pressure-resistance strength capable of withstanding the internal pressure of the over-container; b) Having a pressure-resistance reinforcing ability capable of supporting the net and withstanding the over-pressure and internal pressure of the over-container; c) The total amount of the overflow fluid that has passed through the holes is A wire diameter capable of forming, between the rigid plate surface and a passage for passing the passed fluid, the cross section of which is sufficiently wide to allow the fluid to flow to the through hole without clogging and with minimal pressure loss. A reinforcing mesh board 2, which is a metal mesh board that satisfies conditions a to c above, is provided, and the peripheral portions of these three sheets are welded together without any gaps to reduce the overload. The structure is such that the fluid can flow through the mesh of the mesh plate, the mesh of the reinforcing mesh plate, the passed fluid passage between the reinforcing mesh plate and the rigid plate surface, and the through holes in this order.
耐圧網目過板は以上の構造をとることによ
り、下記のとをり逆重力過用網目孔に要請さ
れている条件のすべてを満足させることができ
る。 By adopting the above-described structure, the pressure-resistant mesh pass plate can satisfy all of the conditions required for the following curved reverse gravity pass mesh holes.
(1) 所要の耐圧強度は使用金属材料の強度に則し
た強度計算に基くことによつて充分に保つこと
ができる。(1) The required pressure resistance can be maintained sufficiently by calculating the strength based on the strength of the metal material used.
(2) 被過流体の流過通路中、補強網板の網目以
降の断面積は網板の網目の面積に比べて比較
にならぬ広さであるから、孔を通過し得た固
形物で補強網板の網目以降の通路に停滞滞留す
るものは存在しない。従つて滓はすべて網
板の最狭断面部前面空間に分離され、目詰りの
発生場所、回復方法とも、網板単独の過の
場合と些かも異るところがない。(2) Because the cross-sectional area after the mesh of the reinforcing mesh plate is incomparably wider than the area of the mesh of the mesh plate in the flow path of the passing fluid, solid matter that could have passed through the holes is There is nothing that stagnates and accumulates in the passages behind the mesh of the reinforcing mesh plate. Therefore, all the slag is separated into the space in front of the narrowest cross section of the screen plate, and the location where clogging occurs and the method of recovery are not the slightest different from the case where the screen plate alone is used.
(3) 上記2と同様の理由から、被過流体が補強
網板の網目以降の流過通路を流過するに際して
の圧力損失は本来の過の圧力損失に比べて比
較にならぬ小ささであるから、耐圧網目過板
による過の場合の所要過圧は網板単独の
過の場合の所要過圧と殆んど変わらない。(3) For the same reason as 2 above, the pressure loss when the overflowing fluid flows through the flow passage after the mesh of the reinforcing mesh plate is incomparably small compared to the original excessive pressure loss. Therefore, the required overpressure when using the pressure-resistant mesh overplate is almost the same as the required overpressure when using the mesh plate alone.
(4) 補強網板と剛性板面との間に形成される空隙
は貫通孔上に位置していない網板の網目に対
しても貫通孔への充分な通路を与えるから、
網板の全網目が孔として機能し得、網板単
独の過の場合に比べて左したる過能率の低
下を来たさない。(4) The gap formed between the reinforcing mesh plate and the rigid plate surface provides a sufficient passage to the through-hole even for the mesh of the mesh plate that is not located above the through-hole.
The entire mesh of the mesh plate can function as holes, and there is no significant decrease in efficiency compared to the case where the mesh plate is alone.
つぎに網目逆重力過における過対象につい
て述べる。 Next, we will discuss the overobject in the mesh reverse gravity overflow.
上掲の記述から明らかなように、網目逆重力
過において目詰りの進行を緩和し簡易且効果的な
逆洗を可能にするものは専ら重力の作用である。
従つて重力によるかような効果が望まれ得ないペ
ースト状のもの、糊状のもの、その他ナフテン系
120シリンダ油のような高粘度の流体は逆重力
過の対象としては不向きである。すなわち網目逆
重力過の過対象となり得る流体は、水その他
これに類する低粘度の流体乃至そのものの品質を
損なわぬ範囲の加温で同様の粘度になり得る流体
に限られる。 As is clear from the above description, it is exclusively the action of gravity that slows down the progress of clogging and enables simple and effective backwashing in mesh backflow.
Therefore, paste-like materials, glue-like materials, and other naphthenic materials for which such effects due to gravity cannot be expected
High viscosity fluids such as 120 cylinder oil are not suitable for reverse gravity. In other words, fluids that can be subjected to mesh reverse gravity flow are limited to water and other similar low-viscosity fluids, or fluids that can be made to have a similar viscosity by heating within a range that does not impair the quality of the fluid itself.
つぎに本発明による網目逆重力過装置の応用
例について説明する。 Next, an application example of the mesh reverse gravity passing device according to the present invention will be explained.
第3図は金属製網目孔として、耐圧網目過
板を使用した網目逆重力過器の断面図である。
11は耐圧網目過板で、13は“0”リング装
着用溝、14は剛性板、14aはその貫通孔、1
5は補強網板、16は網板である。12は過
板押え用筒であり、20は過器本体で、21は
過器蓋とのネジ締め用雄ネジ部、22は“0”
リング装着用溝、23は被過流体取入れ孔、2
4は過済み流体取出し孔、25は逆洗用滓排
出孔、26は“0”リング係合部材である。17
は過器蓋で、18は空気抜きピーユツク取付ネ
ジ部、19は過器本体とのネジ締め用雌ネジ部
である。 FIG. 3 is a sectional view of a mesh reverse gravity filter using a pressure-resistant mesh filter plate as the metal mesh holes.
11 is a pressure-resistant mesh plate, 13 is a groove for attaching the "0" ring, 14 is a rigid plate, 14a is a through hole thereof, 1
5 is a reinforcing mesh board, and 16 is a mesh board. 12 is a cylinder for holding down the overplate, 20 is the overloader body, 21 is a male threaded part for tightening the screw with the overloader lid, 22 is "0"
Ring mounting groove, 23 is fluid intake hole, 2
4 is a drained fluid removal hole, 25 is a backwashing slag discharge hole, and 26 is a "0" ring engagement member. 17
1 is an air vent lid, 18 is an air vent pipe mounting screw portion, and 19 is a female screw portion for tightening the screw to the air vent body.
過の開始に当り耐圧網目過板11を過器
本体20に取付けるには、過板の“0”リング
装着用溝13に“0”リングを装着のうえ、網
板16側を下向きにして水平に過器本体20の
中に挿入、その上に押え用筒12を置き、蓋17
を被せてネジ締めする。このネジ締めによつて、
過板11は押え用筒12を介して過器本体の
“0”リング係合部材26内に押し込まれ押し潰
されて、気密に本体内部をその上部の過済み流
体貯留部とその下部の被過流体滞留部に分離す
る。なお蓋17のネジ締めによつて、予め溝22
中に装着されている“0”リングは蓋17の内側
部によつて押し潰され、過器内部の流体を器外
に対して完全に密封する。 To attach the pressure-resistant mesh overboard 11 to the overboard main body 20 at the start of overheating, attach the "0" ring to the "0" ring attachment groove 13 on the overboard, and then turn the overboard horizontally with the mesh board 16 side facing downward. Insert it into the filter main body 20, place the presser cylinder 12 on top of it, and close the lid 17.
cover and tighten the screws. By tightening this screw,
The over plate 11 is pushed and crushed into the "0" ring engaging member 26 of the over device main body through the holding cylinder 12, and airtightly connects the inside of the main body to the evaporated fluid storage section in the upper part and the covering part in the lower part. Separates into excess fluid retention section. Note that by tightening the screws on the lid 17, the groove 22
The "0" ring installed therein is crushed by the inner side of the lid 17, completely sealing the fluid inside the container from the outside of the container.
過の開始に当つては、まず逆洗用滓排出孔
25および過済み流体取出し孔24を閉じ、蓋
上部に取付けられている空気抜きピーコツクを開
き、次いで被過流体取入れ孔23を開いて被
過流体を器内に圧入する。圧入された被過流体
の流過可能な通路は耐圧網目過板の孔のみで
他は一切閉ざされているから、被過流体はすべ
て重力に抗して上方に向け孔を通過し、過済
み流体貯留部を上昇、ピーコツクから部分の空気
を排出する。空気の排出がおわるとピーコツクを
閉じ、過済み流体取出し孔24を開き、過を
開始する。 To start filtration, first close the backwashing slag discharge hole 25 and the filtrated fluid take-out hole 24, open the air venting peak mounted on the top of the lid, and then open the filtrated fluid intake hole 23 to remove the filtrated fluid. Pressure fluid into the container. The only passage through which the pressurized fluid can flow is the hole in the pressure-resistant mesh plate, and everything else is closed, so all fluid flows upwards against gravity and passes through the hole. Raise the fluid reservoir and expel the partial air from the peak stock. When the air has finished being discharged, the peak stock is closed, the filtrated fluid extraction hole 24 is opened, and filtration is started.
過は被過流体が網板16を通過する過程
で行なわれる。孔の最狭断面積より大型で最狭
断面部を通過し得ない大型固形物は、最狭断面部
より下方の被過流体中に滓として分離残置さ
れ、孔を通過し得たものは過済み流体として
取出し孔24から器外に取出される。 The filtration is performed during the process in which the filtrated fluid passes through the screen plate 16. Large solids that are larger than the narrowest cross-sectional area of the hole and cannot pass through the narrowest cross-section are separated and left in the passing fluid below the narrowest cross-section, and those that can pass through the hole are left as slag. The waste fluid is taken out of the vessel from the take-out hole 24.
過によつて被過流体中に分離残置された
滓に下向きの重力が働き目詰りの進行を緩和する
ことは前述の通りであるが、これは重力方向過
の場合に比べて目詰りの到来を延期できるという
に止まり、やがては同様目詰り的状況を呈するに
至る。この目詰り的状況の回復に著効を示すもの
が本器独得の簡易な逆洗である。 As mentioned above, the downward gravity acts on the slag separated and left in the fluid being passed through due to the gravitational force, which slows down the progress of clogging. It is only possible to postpone this, and eventually a similar situation will arise. A simple backwash unique to this device is highly effective in recovering from this clogging situation.
逆洗に当つては、先ず被過流体取入れ孔23
および過済み流体取出し孔24を閉じ過を停
止する。過が停止されることにより滓は上向
きの過圧から開放されて専ら下向きの重力の作
用下に置かれ、被過流体中への沈降拡散が活発
化する。少時の後空気抜きピーコツクを開き次い
で逆洗用滓排出孔25を手早く一杯に開く。
滓混りの被過流体が排出孔25から器外に奔出
する。同時に過板上部に貯留されている過済
み流体が勢いよく垂直に孔の中に流下して来
る。耐圧網目過板の流体流過用通路断面積は充
分に広く且孔の奥行きは極めて短く、被過流
体の流下の勢いを殺ぐものでないことは前述の通
りである。 For backwashing, first the fluid intake hole 23
Then, the overflow is stopped by closing the overflow fluid extraction hole 24. By stopping the filtration, the slag is freed from the upward overpressure and placed exclusively under the influence of downward gravity, and its sedimentation and diffusion into the filtrated fluid becomes active. After a short time, open the air venting stock and then quickly open the backwashing slag discharge hole 25 fully.
The waste fluid mixed with slag flows out of the vessel from the discharge hole 25. At the same time, the filtrated fluid stored in the upper part of the filtration plate flows down vertically into the hole. As described above, the pressure-resistant mesh plate has a sufficiently wide cross-sectional area for passages through which the fluid flows, and the depth of the holes is extremely short, so that the flow force of the flowing fluid is not reduced.
かくて孔の最狭断面部下方の被過流体中に
在つた滓は奔出する被過流体によつて下方に
吸引され、他方急流下する過済み流体によつて
押し落され、孔空間を離脱して被過流体中に
沈下、過済み流体ともども排出孔25から器外
に排出される。すなわち逆流は極めて簡単な操作
で極めて効果的に行なわれる。 In this way, the slag present in the overflowing fluid below the narrowest section of the hole is sucked downward by the overflowing overflowing fluid, and on the other hand, it is pushed down by the overflowing fluid flowing down rapidly, leaving the hole space. It separates and sinks into the evaporated fluid, and is discharged from the discharge hole 25 together with the evaporated fluid. In other words, backflow can be performed extremely effectively with extremely simple operations.
滓固形物の一部には、孔の最狭断面部に強
く、喰い込んで逆洗による取除きが不能なものが
ある。これ等は多数回の逆洗の間に少しずつ蓄積
され、遂には逆洗によつては回復不能の目詰りを
生じるに至る。この場合には耐圧網目過板を器
外に取り出しての目詰り回復が必要である。但し
耐圧網目過板における目詰りは、素焼・焼結金
属等の奥行きの長い孔の目詰りと異り、目詰り
の場所は孔の最狭断面部のみに限定されるか
ら、その回復は比較的容易である。 Some of the slag solids are strongly embedded in the narrowest section of the hole and cannot be removed by backwashing. These substances accumulate little by little during multiple backwashings, and eventually lead to irreversible clogging during backwashing. In this case, it is necessary to remove the pressure-resistant mesh plate outside the vessel to recover from the clogging. However, unlike clogging in long holes in unglazed or sintered metals, clogging in pressure-resistant mesh plates is limited to the narrowest cross-section of the hole, so recovery is difficult. It is easy to understand.
第1A図は網目孔模型の平面図、第1B図は
第1A図のX−X′線断面側面図、第1C図は第
1A図のY−Y′線断面側面図、第2A図は耐圧
網目過板の部分断面平面図、第2B図は第2A
図の断面側面図、第2C図は第2B図のC部拡大
図、第3図は本発明による耐圧網目過板を用い
る逆重力過装置の応用例の断面図である。
1……網板、2……補強網板、3……剛性
板、4……貫通孔、11……耐圧網目過板、1
2……過板押え用筒、13……“O”リング装
着用溝、14……剛性板、14a……貫通孔、1
5……補強網板、16……網板、20……過
器本体、23……被過流体取入れ孔、24……
過済み流体取出し孔、25……逆洗用滓排出
孔。
Fig. 1A is a plan view of the mesh hole model, Fig. 1B is a cross-sectional side view taken along the line X-X' in Fig. 1A, Fig. 1C is a cross-sectional side view taken along the line Y-Y' in Fig. 1A, and Fig. 2A is a pressure-resistant Partial cross-sectional plan view of the mesh plate, Figure 2B is Figure 2A
FIG. 2C is an enlarged view of section C in FIG. 2B, and FIG. 3 is a cross-sectional view of an application example of a reverse gravity passing device using a pressure-resistant mesh passing plate according to the present invention. 1...Mesh plate, 2...Reinforcement mesh plate, 3...Rigid plate, 4...Through hole, 11...Pressure resistant mesh plate, 1
2... Cylinder for overplate holding down, 13... Groove for attaching "O" ring, 14... Rigid plate, 14a... Through hole, 1
5... Reinforcement net plate, 16... Net plate, 20... Passage unit body, 23... Fluid intake hole, 24...
Waste fluid take-out hole, 25... backwashing slag discharge hole.
Claims (1)
金属製網からなる網板を被過流体流入側最前
部に配設し、加えられる過圧、過器内圧に耐
え得る剛性を有し被過流体流過に際しての圧力
損失を極微に止めるのに十分な大きさの孔径を有
する多数の貫通孔が設けられた剛性板を最後部に
配設し、前記網板の金属製網より線径、目の開
きの大きな金属製網であつて、 a 前記貫通孔上にあつて過圧、過器内圧に
耐え得る強度を有すること、 b 前記網板を支持して過圧、過器内圧に
耐えさせ得る耐圧補強能を有すること、 c 前記網板を通過した過済み流体を目詰り
せしめることなく且つ極微の圧力損失を以て前
記貫通孔まで流過せしめるのに十分な広さの断
面の通路を前記剛性板面との間に形成し得る線
径を有すること、 以上a〜cの条件を満足させ得る金属製網から
なる補強網板を前記網板および剛性板の間に配
設した耐圧網目過板を水平に且つ網板を下に
して装着し、被過流体を重力の方向とは逆に下
方から上方に向けて通過させて過するようにな
つていることを特徴とする耐圧網目過板を用い
る逆重力過装置。[Claims] 1. A mesh plate made of a metal mesh having mesh openings that matches the desired overaccuracy is disposed at the forefront of the inflow side of the fluid to be subjected to overflow, and is capable of withstanding applied overpressure and overpressure internal pressure. A rigid plate having a large number of through-holes having a sufficient size to minimize pressure loss when the fluid flows through is disposed at the rearmost part, and the metal of the mesh plate is It is a metal mesh having a larger wire diameter and opening than a manufacturing mesh, and (a) is placed above the through-hole and has the strength to withstand overpressure and internal pressure of the overpressure vessel, and (b) supports the above-mentioned mesh plate to prevent overpressure. , have a pressure-reinforcing ability capable of withstanding the internal pressure of the overcapacitor, and c. have a sufficient width to allow the overflowed fluid that has passed through the mesh plate to flow to the through-hole without clogging and with minimal pressure loss. A reinforcing mesh plate made of a metal mesh that satisfies conditions a to c above is arranged between the mesh plate and the rigid plate. The pressure-resistant mesh plate is installed horizontally with the mesh plate facing down, and the overflowing fluid is passed through from the bottom to the top, opposite to the direction of gravity. Reverse gravity passing device using pressure-resistant mesh passing plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58006680A JPS59132912A (en) | 1983-01-20 | 1983-01-20 | Inverse gravity filter apparatus using pressure resistant reticulated filter plate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58006680A JPS59132912A (en) | 1983-01-20 | 1983-01-20 | Inverse gravity filter apparatus using pressure resistant reticulated filter plate |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59132912A JPS59132912A (en) | 1984-07-31 |
| JPS6144527B2 true JPS6144527B2 (en) | 1986-10-03 |
Family
ID=11645075
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58006680A Granted JPS59132912A (en) | 1983-01-20 | 1983-01-20 | Inverse gravity filter apparatus using pressure resistant reticulated filter plate |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59132912A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS648638U (en) * | 1987-07-03 | 1989-01-18 | ||
| JPH0241123U (en) * | 1988-09-14 | 1990-03-22 |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61195312U (en) * | 1985-05-24 | 1986-12-05 | ||
| JP2011173054A (en) * | 2010-02-24 | 2011-09-08 | Toray Ind Inc | Filter and coating apparatus equipped with the same |
-
1983
- 1983-01-20 JP JP58006680A patent/JPS59132912A/en active Granted
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS648638U (en) * | 1987-07-03 | 1989-01-18 | ||
| JPH0241123U (en) * | 1988-09-14 | 1990-03-22 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59132912A (en) | 1984-07-31 |
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