JPS63268982A - Breathing mechanism for pump - Google Patents
Breathing mechanism for pumpInfo
- Publication number
- JPS63268982A JPS63268982A JP62102362A JP10236287A JPS63268982A JP S63268982 A JPS63268982 A JP S63268982A JP 62102362 A JP62102362 A JP 62102362A JP 10236287 A JP10236287 A JP 10236287A JP S63268982 A JPS63268982 A JP S63268982A
- Authority
- JP
- Japan
- Prior art keywords
- pump
- porous filter
- liquid
- gas
- discharge
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Landscapes
- Details Of Reciprocating Pumps (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明はポンプのポンプ室等内のガスをポンプ外部に好
適に排気させることができるポンプのガス抜き機構に関
する。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a pump gas venting mechanism that can suitably exhaust gas in a pump chamber or the like of a pump to the outside of the pump.
(従来の技術)
周知の如く、往復動ポンプに於いて次亜塩素酸ソーダの
如きガスを発生し易い液体や予め微量のガスを混入して
なる液体を液送させる場合には、ガスがポンプ室又は吐
出路内に存在すれば適切なポンプ圧縮が行えず、定量吐
出が行えない事態が生じる。また、この様な事態は上記
の如き特別な液体を取扱わない場合であってもポンプ吸
入路側から大気中のエア等が吸引されることによっても
発生する恐れがある。(Prior Art) As is well known, when using a reciprocating pump to pump a liquid that easily generates gas, such as sodium hypochlorite, or a liquid that has been mixed with a small amount of gas, the gas If it is present in the chamber or discharge path, appropriate pump compression cannot be performed, resulting in a situation in which fixed-quantity discharge cannot be performed. Furthermore, even when the above-mentioned special liquid is not handled, such a situation may occur due to atmospheric air being sucked in from the pump suction path side.
従って、従来に於いては上記の様な難点を解決せんとし
て例えば特開昭61−31680号公報に所載のものが
開発されるに至っている。Therefore, in order to solve the above-mentioned difficulties, a device disclosed in, for example, Japanese Patent Application Laid-open No. 31680/1983 has been developed.
すなわち、この従来のものは第3図に示す如く、往復動
ポンプのポンプ室1aに連通ずる吐出路5eに別途連通
路18aを分岐せしめて、該連通路18aにポンプ揚液
よりも比重の小さい材質からなるボール21を用いた逆
止弁22を装着させたものである。That is, as shown in FIG. 3, in this conventional system, a separate communication passage 18a is branched off from the discharge passage 5e communicating with the pump chamber 1a of the reciprocating pump, and the liquid having a specific gravity smaller than that of the liquid pumped by the pump is added to the communication passage 18a. A check valve 22 using a ball 21 made of a material is installed.
よって、この手段によれば、前記逆止弁22のボー、ル
21は常時はポンプ揚液との比重差による浮力によって
逆止弁22を閉状態にすると共に、ポンプ室−Ia内等
のガスが該逆止弁22の位置に到達した際にはボール2
1がその自重により下降して逆止弁22が開状態となり
、その結果ガス排気が行えるのである。Therefore, according to this means, the ball 21 of the check valve 22 normally closes the check valve 22 by the buoyancy caused by the difference in specific gravity with the liquid pumped by the pump, and also prevents the gas in the pump chamber-Ia, etc. When the ball 2 reaches the position of the check valve 22, the ball 2
1 is lowered by its own weight, the check valve 22 is opened, and as a result, gas can be exhausted.
(発明が解決しようとする問題点)
しかしながら、前記従来の逆止弁22によりガス排気を
行わせる手段に於いては、この種逆止弁22のボール2
1を高精度な球面に加工することが困難で、該ボール2
1と逆止弁22の弁座との両者間に間隙が発生すること
が実際王道けられないばかりか1、ボール21はポンプ
揚液との比重差による小さな浮力によって弁座に当接す
るだけのものであるため−に、その圧接力は非常に弱く
、逆止弁22を完全閉塞するに至らないという難点を有
していた。(Problems to be Solved by the Invention) However, in the conventional means for exhausting gas by the check valve 22, the ball 2 of this type of check valve 22
It is difficult to process ball 1 into a highly accurate spherical surface, and the ball 2
1 and the valve seat of the check valve 22 is actually unavoidable, and the ball 21 only comes into contact with the valve seat due to the small buoyant force due to the difference in specific gravity between the ball 21 and the liquid pumped by the pump. Because of this, the pressure contact force is very weak and has the disadvantage that it does not completely close the check valve 22.
しかも、ポンプ揚液が次亜塩素酸ソーダ等の場合には該
揚液が大気と接触する逆止弁22の位置で結晶化を生じ
るために、この結晶粒の存在によって逆止弁22の完全
閉塞が一層困難となっており、この様な難点は同図の如
く逆止弁22を二個連設しても到底解決できるものでは
なかった。Moreover, when the liquid pumped by the pump is sodium hypochlorite or the like, crystallization occurs at the position of the check valve 22 where the pumped liquid comes into contact with the atmosphere. This makes it even more difficult to close the valve, and this difficulty cannot be solved even by installing two check valves 22 in series as shown in the figure.
従って、前記従来の手段に於いては、逆止弁22の位置
からのポンプ揚液の洩れ、圧力損失は避けられないこと
となって、ポンプ吐出流量の減少並びに吐出圧の低下を
招来して定量ポンプ液送が行えず、又そのポンプ効率も
低下するという致命的な問題点を有していたのである。Therefore, in the conventional means, leakage of the pumped liquid from the position of the check valve 22 and pressure loss are unavoidable, resulting in a decrease in the pump discharge flow rate and a decrease in the discharge pressure. This had the fatal problem of not being able to deliver a metered amount of liquid with a pump, and also reducing the efficiency of the pump.
本発明は上記の如き従来の問題点に鑑みて発明されたも
ので、その目的とするところは、ポンプ揚液の液洩れ等
の不都合を何ら生じさせることな・くポンプ室及び吐出
路内のガス抜きを適切に行わせ、もってポンプの適正な
運転を可能ならしめる点にある。The present invention was invented in view of the above-mentioned conventional problems, and its purpose is to prevent the pump chamber and discharge path from causing any inconveniences such as leakage of pumped liquid. The purpose of this invention is to allow proper degassing and thereby enable proper operation of the pump.
(問題点を解決するための手段)
本発明は従来の逆止弁の如きバルブ機構を用いるのでは
なく、ポンプ室等で発生されたガスのみをポンプ外部に
透過させてポンプ揚液の透過を阻止する機能を具備する
部材を用いることにより、上記従来の問題点を解決せん
として構成されたものである。(Means for Solving the Problems) The present invention does not use a valve mechanism such as a conventional check valve, but rather allows only the gas generated in the pump chamber etc. to permeate to the outside of the pump, thereby reducing the permeation of pumped liquid. This structure is designed to solve the above-mentioned conventional problems by using a member having a blocking function.
すなわち、本発明の構成の要旨は、ポンプのポンプ室1
又は吐出路5に連通して設けられたガス抜き用達連部1
8に、前記ポンプ室1又は吐出路5内に発生されたガス
をポンプ外部に排気させるべく通気性を有し且つ液体透
過を阻止する多孔性フィルター13を設けた点にある。That is, the gist of the configuration of the present invention is that the pump chamber 1 of the pump
Or a degassing passage 1 provided in communication with the discharge passage 5
8, a porous filter 13 is provided which has air permeability and prevents liquid permeation in order to exhaust the gas generated in the pump chamber 1 or the discharge passage 5 to the outside of the pump.
(作用)
従って、上記構成を特徴とするガス抜き機構に於いては
、ポンプ室l又は吐出路5内に発生されたガスがガス抜
き用達連部18に到達すると、該ガスは通気性を具備す
る多孔性フィルター13を透過してポンプ外部に排気さ
れることとなる。而して、前記多孔性フィルター13は
液体の透過を阻止するものであるために、ポンプ揚液は
何ら外部に漏れず、よってポンプ吐出流量の減少や吐出
圧の低下を来すことなく、不当なガスのみが外部に排出
されることとなるのである。(Function) Therefore, in the gas venting mechanism characterized by the above configuration, when the gas generated in the pump chamber l or the discharge passage 5 reaches the gas venting passage 18, the gas loses its permeability. It passes through the porous filter 13 provided and is exhausted to the outside of the pump. Since the porous filter 13 prevents the permeation of liquid, the liquid pumped by the pump does not leak to the outside, and therefore, the pump discharge flow rate does not decrease or the discharge pressure decreases unduly. This means that only the gas that is present is exhausted to the outside.
(実施例)
以下、本発明の実施例について図面を参照して説明する
。(Example) Hereinafter, an example of the present invention will be described with reference to the drawings.
、第1図に於いて、1は往復駆動自在のダイアフラム2
を内装着してなるポンプ室で、その下方側には逆止弁3
を備えた流入路4が連設されている。, In Fig. 1, 1 is a diaphragm 2 that can be driven reciprocally.
is installed inside the pump chamber, and a check valve 3 is installed on the lower side of the pump chamber.
An inflow channel 4 with a 100 mA is provided in series.
5はポンプ室1の上部側に連設された吐出路を示し、該
吐出路5はポンプヘッド6に連結された連結体7、接続
バイブ8、及びソケット9の各内部に渡って一連に延設
されて配管用吐出口12に到り、その途中には二連の逆
止弁to、 tiが夫々設けられている。Reference numeral 5 denotes a discharge passage connected to the upper side of the pump chamber 1, and the discharge passage 5 extends continuously inside each of the connecting body 7 connected to the pump head 6, the connecting vibe 8, and the socket 9. The pipes reach the piping outlet 12, and two check valves to and ti are provided in the middle.
18は前記吐出路5の逆止弁10よりも上方側の鉛直部
5aの上部に該吐出路5の水平部5bの高さレベルより
も上方に突出すべく形成されたガス抜き用達連部を示す
。13は前記ガス抜き用達連部18の上部側に設けられ
た四弗化エチレン樹脂単体からなる多孔性フィルターを
示し、該多孔性フィルター13はその全面にO01〜1
0μm程度の微細な孔を多数有する多孔質のもので、空
気、ガスを透過させる機能即ち通気性は具備するが、水
等の液体に対しては↑R水性を示してその透過を阻止す
るものである。14.14は前記多孔性フィルター13
の上下面を挟装してなる挟持板を示し、該挟持板14.
14には数龍径の貫通孔15・・・が多数穿設されてい
る。Reference numeral 18 denotes a degassing connecting part formed at the upper part of the vertical part 5a of the discharge passage 5 above the check valve 10 so as to protrude above the height level of the horizontal part 5b of the discharge passage 5. shows. Reference numeral 13 indicates a porous filter made of tetrafluoroethylene resin, which is provided on the upper side of the gas venting connection part 18, and the porous filter 13 is coated with O01 to O1 on its entire surface.
It is a porous material with many fine pores of about 0 μm, and has the function of allowing air and gas to pass through, that is, has breathability, but exhibits ↑R aqueous properties when it comes to liquids such as water, and prevents their permeation. It is. 14.14 is the porous filter 13
This shows a clamping plate formed by sandwiching the upper and lower surfaces of the clamping plate 14.
14 is provided with a large number of through holes 15 of several diameters.
16は前記挟持板14.14及び多孔性フィルター13
の位置決め固定を図るべく連結体7の上部に螺着された
シリンダを示し、該シリンダ16の孔部19内には水1
7が貯留されている。16 is the holding plate 14.14 and the porous filter 13;
A cylinder is screwed onto the upper part of the connecting body 7 to position and fix the cylinder 16.
7 are stored.
本実施例は以上の構成からなるために、例えば次亜塩素
酸ソーダ等のガス発生を行う液体を、ダイヤフラム2の
往復動によって流入路4側から吐出路5側にポンプ送液
させる際には、ポンプ室1及び吐出路5の各部で発生し
たガス気泡は逆止弁10を通過上昇した後に鉛直部5a
の頂部のガス抜き用連通部18に到達する。而して、該
ガス抜き用連通部18の上面側には通気性を具備する多
孔性フィルター13が存在するために、前記ガスはこの
多孔性フィルター13を透過してシリンダ16内の水1
7中を通過し、その上方の大気中に排気されることとな
る。特にこの様なガスの排気作用は吐出路5内が高圧と
なるポンプの吐出工程時に促進され、またポンプ吐出圧
が高い程ガス抜き作用が良好となる。Since this embodiment has the above configuration, when a liquid that generates gas, such as sodium hypochlorite, is pumped from the inflow path 4 side to the discharge path 5 side by the reciprocating motion of the diaphragm 2, , the gas bubbles generated in each part of the pump chamber 1 and the discharge passage 5 pass through the check valve 10 and rise, and then rise to the vertical part 5a.
It reaches the gas vent communication part 18 at the top of the. Since a porous filter 13 having air permeability is present on the upper surface side of the gas vent communication section 18, the gas passes through this porous filter 13 and enters the water 1 in the cylinder 16.
7 and is exhausted into the atmosphere above. Particularly, such a gas evacuation effect is promoted during the pump discharge process when the pressure inside the discharge passage 5 is high, and the higher the pump discharge pressure, the better the gas evacuation effect becomes.
しかるに、前記多孔性フィルター13は通気性は有する
ものの通水性は有しないために、ポンプ揚液が該多孔性
フィルター13を介して外部に漏洩する様なことがない
と共に、管体16に貯留された水17が吐出路5内に浸
入する様な恐れもない。また、ポンプ吸入工程時に於い
ては、逆止弁10が閉状態となるために鉛直部5a側に
は負圧を生じないのであるが、何らかの支障が生じて該
鉛直部5a側に負圧が生じても、多孔性フィルター13
の上方には水17が貯留されているために、大気中のエ
アが前記負圧によって多孔性フィルター13を透過して
吐出路5内に混入される様なことが好適に回避できる。However, since the porous filter 13 has air permeability but not water permeability, the pumped liquid does not leak to the outside through the porous filter 13 and is stored in the pipe body 16. There is no fear that the water 17 will enter the discharge passage 5. Further, during the pump suction process, the check valve 10 is closed, so no negative pressure is generated on the vertical portion 5a side, but some kind of hindrance occurs and negative pressure is generated on the vertical portion 5a side. Even if the porous filter 13
Since the water 17 is stored above the discharge passage 5, it is possible to prevent atmospheric air from passing through the porous filter 13 and being mixed into the discharge passage 5 due to the negative pressure.
尚、当然ながらこの場合に於いても水17が吐出路5内
に浸入することはない。更に、前記多孔性フィルター1
3の上方部に水17が貯留されることにより、揚液と大
気との直接的な接触を回避できて該揚液の結晶化をも阻
止できることとなる。Of course, even in this case, the water 17 will not enter into the discharge passage 5. Furthermore, the porous filter 1
By storing the water 17 above the pump 3, direct contact between the pumped liquid and the atmosphere can be avoided, and crystallization of the pumped liquid can also be prevented.
更に、前記多孔性フィルター13は四弗化エチレン樹脂
製なるために、次亜塩素酸ソーダの如き化学薬液に対し
て優れた耐蝕性を示し、しかも咳多孔性フィルター13
はその上下面が貫通孔15・・・を有する挟持板14.
14にて挟装されてなるために、ポンプ吐出圧が高圧の
場合であってもこの吐出圧による撓みが小さく抑制され
て、耐圧強度面でも優れたものとなり、その使用寿命は
非常に長いものとなる。Furthermore, since the porous filter 13 is made of tetrafluoroethylene resin, it exhibits excellent corrosion resistance against chemical solutions such as sodium hypochlorite.
is a clamping plate 14. having through holes 15 on its upper and lower surfaces.
14, even when the pump discharge pressure is high, the deflection due to this discharge pressure is suppressed to a small level, and it has excellent pressure resistance and has a very long service life. becomes.
尚、上記実施例に於いては、0.1〜10μm程度の微
細孔を多数有する四弗化エチレン樹脂製の多孔性フィル
ター13を用いてなるが、本考案に係る多孔性フィルタ
ー13の具体的な構成は決してこれに限定されず、その
具体的な材質、孔径等は問うものではない。要は通気性
を具備する一方で液体の透過を阻止するフィルター機能
を具備すればよいのである。但し、本考案に係る多孔性
フィルター13はポンプ送液される特定の種類の液体の
透過を阻止できれば充分であって、必ずしも全ての種類
の液体の透過を阻止する機能を具備する必要はない。け
だし、例えばアセトン等の液体は透過させるが次亜塩素
酸ソーダの透過は阻止する多孔性フィルター13であれ
ば、該次亜塩素酸ソーダのポンプ送液が適切に行えるか
らである。In the above embodiment, a porous filter 13 made of tetrafluoroethylene resin having a large number of micropores of about 0.1 to 10 μm is used, but the specifics of the porous filter 13 according to the present invention are The structure is by no means limited to this, and the specific material, hole diameter, etc. are not in question. In short, it is sufficient to have a filter function that prevents permeation of liquid while providing breathability. However, it is sufficient that the porous filter 13 according to the present invention can block the permeation of a specific type of liquid pumped, and it is not necessarily necessary to have the function of blocking the permeation of all types of liquid. This is because if the porous filter 13 allows liquids such as acetone to pass therethrough but blocks sodium hypochlorite from passing through, the sodium hypochlorite can be pumped appropriately.
また、上記実施例に於いては、多孔性フィルター13の
上方部に水17を貯留させて大気エアがポンプ吐出路5
内へ不用意に浸入することや次亜塩素酸ソーダ等のポン
プ揚液の結晶化の抑制を図ってなるが、本発明は必ずし
も上記実施例の如く多孔性フィルター13の外面側に水
17を貯留させる必要はない。例えば上記第1図の実施
例に於いて、ポンプ吸入工程時に逆止弁10が略完全な
状態に閉塞して多孔性フィルター13の内側に負圧が作
用しない状態であれば、水17が存在しなくとも大気中
のエアが吐出路5内に浸入する様なことはなく、充分実
用に供することができるのである。尚、上記実施例に於
いて多孔性フィルター13の外面側の水17に代えて該
多孔性フィルター13を透過しない他の種類の液体を貯
留させた場合でも前記と同様な作用が得られることは説
明を要しないであろう。Further, in the above embodiment, the water 17 is stored in the upper part of the porous filter 13, and atmospheric air flows into the pump discharge path 5.
Although the present invention is intended to prevent water 17 from inadvertently entering the interior of the porous filter 13 and from crystallizing pumped liquid such as sodium hypochlorite, the present invention does not necessarily require water 17 to be placed on the outer surface of the porous filter 13 as in the above embodiment. There is no need to store it. For example, in the embodiment shown in FIG. 1, if the check valve 10 is almost completely closed during the pump suction process and no negative pressure is applied inside the porous filter 13, water 17 is present. Even if this is not done, atmospheric air will not enter into the discharge passage 5, and it can be put to practical use. In addition, in the above embodiment, even if another type of liquid that does not pass through the porous filter 13 is stored instead of the water 17 on the outer surface of the porous filter 13, the same effect as described above can be obtained. No explanation needed.
更に、上記実施例に於いては、吐出路5側の第1の逆止
弁10よりも後段側にガス抜き用連通部18及び多孔性
フィルター13を設けてなるが、本発明はこれらの具体
的な形成、取付位置並びに取付態様も決して上記の如く
限定されるものではない。Furthermore, in the above embodiment, the degassing communication portion 18 and the porous filter 13 are provided on the downstream side of the first check valve 10 on the discharge path 5 side, but the present invention does not require these specific features. The formation, mounting position, and mounting manner are by no means limited to the above.
すなわち、例えば第2図の如くポンプ吐出路5側の第1
の逆止弁10の前段側に別途分岐状のガス抜き用連通部
18を形成せしめて、該ガス抜き用連通部18の側方に
多孔性フィルター13を設ける様にしても何ら構わない
ばかりか、当該実施例の如く吐出路5にはガス抜き用連
通部18を連設せずに、ポンプ室1の上部位置等に直接
ガス抜き用連通部18を連設しても何ら構わない。That is, for example, as shown in FIG.
There is nothing wrong with forming a separate branch-shaped gas vent communication section 18 on the upstream side of the check valve 10 and providing the porous filter 13 on the side of the gas vent communication section 18. However, instead of providing the communication part 18 for degassing in the discharge passage 5 as in the embodiment, the communication part 18 for degassing may be directly provided in the upper part of the pump chamber 1 or the like.
尚、上記第2図に示す実施例に於いては、ポンプ吸入工
程時に多孔性フィルター13の内側位置に負圧が生じて
ポンプ外部の大気中のエアが多孔性フィルター13を透
過して吐出路5内に浸入する恐れを有するが、これを解
消する策としては例えば同図の如く、多孔性フィルター
13の前段に吐出路5側から多孔性フィルター13側へ
の流体流通を可能ならしめてこれとは逆方向の流体流通
は阻止する機能を具備するダックビルバルブ20の如き
手段を設ければよい。この様な構成とすれば、ポンプ外
部の大気中のエアが該ダックビルバルブ20を通過して
吐出路5内に浸入される様なことが好適に阻止できるこ
ととなる。また、該ダックビルバルブ20に付加して又
は該ダックビルバルブ20に代わるものとして、多孔性
フィルター13の外方側に装着せしめたシリンダ16内
に水17等の液体を貯留させることによってもポンプ外
部のエアがポンプ内部に浸入することを阻止できること
は勿論である(尚、第2図で第1図と同符号のものは第
1図と同一部品を示す)。In the embodiment shown in FIG. 2 above, negative pressure is generated inside the porous filter 13 during the pump suction process, and air in the atmosphere outside the pump passes through the porous filter 13 and flows into the discharge path. However, as a measure to eliminate this problem, for example, as shown in the same figure, fluid can flow from the discharge path 5 side to the porous filter 13 side at the stage before the porous filter 13, and this can be avoided. A means such as a duckbill valve 20 having a function of preventing fluid flow in the opposite direction may be provided. With such a configuration, it is possible to suitably prevent air in the atmosphere outside the pump from passing through the duckbill valve 20 and entering the discharge passage 5. Additionally, in addition to or in place of the duckbill valve 20, it is also possible to store a liquid such as water 17 in a cylinder 16 attached to the outside of the porous filter 13, so that the outside of the pump can be removed. Of course, it is possible to prevent air from entering the inside of the pump (note that the same reference numerals in FIG. 2 as in FIG. 1 indicate the same parts as in FIG. 1).
この様に、本発明はガス抜き用連通部18並びに多孔性
フィルター13の具体的な取付位置や形成状態等は任意
に設計変更自在であり、要はポンプ室1又は吐出路5の
何れかの位置に連通して設けられておればよいのである
。尚、多孔性フィルター13を二枚の挟持Fj、14.
14で挟装させる様なことは本発明の必須要件ではない
。As described above, in the present invention, the specific mounting position and formation state of the degassing communication section 18 and the porous filter 13 can be changed as desired; It suffices if it is provided in communication with the position. Note that the porous filter 13 is held between two sheets Fj, 14.
14 is not an essential requirement of the present invention.
更に、本発明はポンプの具体的な種類も決して上記実施
例の如くダイアフラムポンプに限定されず、その他のピ
ストンポンプ、プランジャポンプ等にも当然適用できる
もので、その具体的な種類や構造等は問わない他、ポン
プの使用態様等も問うものではない。Furthermore, the specific type of pump of the present invention is by no means limited to the diaphragm pump as in the above embodiment, but can of course be applied to other piston pumps, plunger pumps, etc., and the specific type and structure thereof are subject to change. In addition, it does not ask how the pump is used.
その他、本発明は各部の具体的な構成は全て本発明の意
図する範囲内で設計変更自在である。In addition, the design of the specific configuration of each part of the present invention can be changed within the intended scope of the present invention.
(発明の効果)
畝上の様に、本発明はポンプ室又は吐出路に連通させて
設けたガス抜き用連通部に、通気性を有して液体の透過
を阻止する機能を具備する多孔性フィルターを設けて、
ポンプ室等内で発生されたガスを多孔性フィルターを介
してポンプ外部に排気可能に構成してなるために、従来
のバルブ機構によってガス抜きを行っていた手段の如く
バルブの完全閉塞の困難化に起因して該バルブ位置から
ポンプ揚液の液洩れが発生する様な恐れが一切無く、ポ
ンプ揚液が該多孔性フィルターを透過して外部に液洩れ
する様なことが完全に阻止できることとなり、その結果
ポンプ運転に支障を生じるガスの適切な排除とこれに伴
う液洩れが解消できて、次亜塩素酸ソーダの如きガス発
生を行う液体等を取扱う場合でもそのポンプ吐出流量並
びに吐出圧の適正な維持が図れて、ポンプ効率が良好な
定量吐出が行えるという格別な効果を得るに至った。(Effects of the Invention) Like the ridges, the present invention provides a gas vent communication section provided in communication with the pump chamber or the discharge path, which has a porous structure that has air permeability and has the function of blocking liquid permeation. Set up a filter,
Since the gas generated in the pump chamber etc. can be exhausted to the outside of the pump through a porous filter, it is difficult to completely close the valve, unlike the conventional method of venting gas using a valve mechanism. There is no risk of liquid pumped by the pump leaking from the valve position due to this, and it is completely possible to prevent pumped liquid from passing through the porous filter and leaking to the outside. As a result, it is possible to properly remove gases that interfere with pump operation and eliminate liquid leakage, and to reduce the pump discharge flow rate and discharge pressure even when handling liquids that generate gas such as sodium hypochlorite. Proper maintenance has been achieved, and a special effect has been achieved in that it is possible to perform quantitative discharge with good pump efficiency.
しかも、本発明はガス抜き用連通部に多孔性フィルター
を設けるだけでよいために、従来の構造が複雑で且つ各
部を高精度に加工せねばならなかったバルブ機構を用い
る手段に比して、その製作が格段部品で、製作コストの
大幅な低減化が図れる。という大なる実益をも有する。Moreover, since the present invention only requires providing a porous filter in the gas venting communication section, compared to the conventional means using a valve mechanism, which has a complicated structure and requires high-precision processing of each part, The parts are manufactured by a large number of parts, and the manufacturing cost can be significantly reduced. It also has great practical benefits.
第1図は本発明に係るガス抜き機構の一実施例を示す要
部断面図。 ・
第2図は他の実施例を示す要部断面図。
第3図は従来例を示す要部断面図。
l・・・ポンプ室 5・・・吐出路13・・
・多孔性フィルター 18・・・ガス抜き用連通部出
願人 日本フィーダー工業株式会社
代理人 弁理士 藤 本 昇
第2図
第3図FIG. 1 is a sectional view of a main part showing an embodiment of a gas venting mechanism according to the present invention. - Fig. 2 is a cross-sectional view of main parts showing another embodiment. FIG. 3 is a sectional view of main parts showing a conventional example. l...Pump chamber 5...Discharge path 13...
・Porous filter 18...Communication part for gas venting Applicant: Nippon Feeder Industries Co., Ltd. Agent Patent attorney Noboru Fujimoto Figure 2 Figure 3
Claims (1)
れたガス抜き用連通部18に、前記ポンプ室1又は吐出
路5内に発生されたガスをポンプ外部に排気させるべく
通気性を有し且つ液体透過を阻止する多孔性フィルター
13が設けられてなることを特徴とするポンプのガス抜
き機構。 2 前記多孔性フィルター13がその外部側に水17を
貯留可能とすべく孔部19を有するシリンダ16の前面
側に設けられてなる特許請求の範囲第1項記載のポンプ
のガス抜き機構。[Scope of Claims] 1 Gas generated in the pump chamber 1 or discharge passage 5 is exhausted to the outside of the pump through a gas venting communication portion 18 provided in communication with the pump chamber 1 or discharge passage 5 of the pump. A gas venting mechanism for a pump, characterized in that it is provided with a porous filter 13 that has air permeability and prevents liquid permeation. 2. The pump gas venting mechanism according to claim 1, wherein the porous filter 13 is provided on the front side of a cylinder 16 having holes 19 so as to be able to store water 17 on the outside thereof.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62102362A JP2649042B2 (en) | 1987-04-24 | 1987-04-24 | Pump venting mechanism |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62102362A JP2649042B2 (en) | 1987-04-24 | 1987-04-24 | Pump venting mechanism |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63268982A true JPS63268982A (en) | 1988-11-07 |
| JP2649042B2 JP2649042B2 (en) | 1997-09-03 |
Family
ID=14325347
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62102362A Expired - Fee Related JP2649042B2 (en) | 1987-04-24 | 1987-04-24 | Pump venting mechanism |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2649042B2 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0166479U (en) * | 1987-10-23 | 1989-04-27 | ||
| JPH0452570U (en) * | 1990-09-07 | 1992-05-06 | ||
| US6475974B1 (en) | 2000-09-01 | 2002-11-05 | Dow Corning Corporation | Mechanical microemulsions of blended silicones |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6383473U (en) * | 1986-11-20 | 1988-06-01 |
-
1987
- 1987-04-24 JP JP62102362A patent/JP2649042B2/en not_active Expired - Fee Related
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6383473U (en) * | 1986-11-20 | 1988-06-01 |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0166479U (en) * | 1987-10-23 | 1989-04-27 | ||
| JPH0452570U (en) * | 1990-09-07 | 1992-05-06 | ||
| US6475974B1 (en) | 2000-09-01 | 2002-11-05 | Dow Corning Corporation | Mechanical microemulsions of blended silicones |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2649042B2 (en) | 1997-09-03 |
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