JPH0435202B2 - - Google Patents

Info

Publication number
JPH0435202B2
JPH0435202B2 JP59157796A JP15779684A JPH0435202B2 JP H0435202 B2 JPH0435202 B2 JP H0435202B2 JP 59157796 A JP59157796 A JP 59157796A JP 15779684 A JP15779684 A JP 15779684A JP H0435202 B2 JPH0435202 B2 JP H0435202B2
Authority
JP
Japan
Prior art keywords
liquid
valve
stock solution
intake chamber
pressurizing
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 - Lifetime
Application number
JP59157796A
Other languages
Japanese (ja)
Other versions
JPS6135815A (en
Inventor
Aizaburo Yagishita
Hideo Saito
Yasunori Iryama
Noboru Mori
Yoichi Kurahashi
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.)
Sanshin Seisakusho KK
Original Assignee
Sanshin Seisakusho KK
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 Sanshin Seisakusho KK filed Critical Sanshin Seisakusho KK
Priority to JP15779684A priority Critical patent/JPS6135815A/en
Publication of JPS6135815A publication Critical patent/JPS6135815A/en
Publication of JPH0435202B2 publication Critical patent/JPH0435202B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明は上部集液式加圧過機に於ける機体内
液の脱液方法及び同装置に関するものである。上
部集液式加圧過機に於いて過原液を変更する
場合、機体内には液と原液が夫々充填状態に在
りながら過運転を停止せざるを得ず、在来は機
体底部のドレンバルブを開放して原液のみを回収
しようとしても原液貯留槽内に液が逆流しなが
ら滓を剥離してしまう為きれいな原液回収は不
可能であつた。メツキ液の如く高価な原液にあつ
ては斯様に液分を廃棄することが経済上許され
ないばかりでなく、材表面に付着せる滓は概
ねプリコート層を介在していることから特に材
内外の差圧を大にしてしまうと容易に原液貯留室
内で剥離脱落してしまうことになり、原液変更の
都度材のプリコート処理をせねばならないこと
になり極めて時間的、稼動経済上悩みの種であつ
た。そこで本発明は原液貯留室に於いて材内外
の差圧を発生させない様に工夫して滓の剥離脱
落現象を防止しながら機内の原液の回収並びに
液の回収をも行い得る様にした発明である。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method and apparatus for removing fluid within a machine in an upper liquid collection type pressurizing machine. When changing the excess liquid in an upper liquid collection type pressurizing machine, over-operation must be stopped while the liquid and stock liquid are both filled inside the machine, and conventionally, the drain valve at the bottom of the machine is used. Even if an attempt was made to recover only the stock solution by opening the tank, the liquid would flow back into the stock solution storage tank and peel off the slag, making it impossible to recover a clean stock solution. In the case of expensive stock solutions such as plating solution, it is not only economically impractical to dispose of the liquid in this way, but also because the slag that adheres to the surface of the material is mostly interposed in the pre-coat layer, so it is especially important to dispose of the liquid inside and outside the material. If the differential pressure is increased, it will easily peel off and fall in the stock solution storage chamber, and the material will have to be pre-coated every time the stock solution is changed, which is extremely time consuming and causes problems in terms of operational economy. Ta. Therefore, the present invention is an invention that makes it possible to recover the stock solution inside the machine as well as the liquid while preventing the flaking and falling phenomenon of the slag by preventing the generation of differential pressure between the inside and outside of the material in the stock solution storage chamber. be.

本発明は運転停止状態に於いて、原液供給バル
ブを閉じ、原液貯留槽に加圧ガスを供給して原液
を材下端位まで強制過せしめて液として
液排出バルブから回収後、少量の原液残液のみド
レンバルブから抜取る原液の脱液方法及び同装置
と、更に上記装置に於いて液回収バルブに通ず
る材内空下端まで回収管を臨ませた液回収チ
ユーブを液摂取室に付加設置せしめることによ
り上記の加圧ガスによる強制過後の材及び
液摂取室に残る液を別途押上げ回収せしめるこ
とを特徴とするものである。
In the present invention, when the operation is stopped, the stock solution supply valve is closed, pressurized gas is supplied to the stock solution storage tank, the stock solution is forced to pass through to the bottom end of the material, and after being recovered as a liquid from the liquid discharge valve, a small amount of stock solution remains. A method and device for removing undiluted liquid from a drain valve, and furthermore, in the above device, a liquid recovery tube with a recovery tube facing the lower end of the interior of the material leading to the liquid recovery valve is additionally installed in the liquid intake chamber. As a result, the material and the liquid remaining in the liquid intake chamber after being forced to pass by the pressurized gas are separately pushed up and collected.

本発明の第1実施例を添附図面の第1〜3図に
従つて説明するに、1は上部集液式加圧過機本
体であつて、中間仕切板2の下方は最下部にドレ
ンバルブB及び原液供給バルブAを設けた過原
液貯留槽3であつて、同上方は液排出バルブE
を設けた液摂取室4にして、単数又は複数本の
材5を仕切板2より上方の液摂取室4から
過原液貯留槽3内へ垂設支持せしめている。Cは
上記過原液貯留槽3に設けた加圧ガスバルブで
ある。エアバルブDは、加圧ガスバルブCと同じ
く原液貯留槽3に設けるものとし、液摂取室4
には、液排出バルブEの他、大気開放又は加圧
バルブFをも設けるものとする。上記材5は外
周面のどの部分からでも液摂取可能に第6図に
示す如く全面有孔形成された管体等有孔芯材6の
表面に布7を被装形成して構成する他、セラミ
ツクス、ステンレス鋼等多孔質材を利用する。
A first embodiment of the present invention will be described with reference to FIGS. 1 to 3 of the attached drawings. Reference numeral 1 denotes an upper liquid collection type pressurizing machine body, and a drain valve is installed at the bottom of the intermediate partition plate 2. The excess stock solution storage tank 3 is equipped with a stock solution supply valve A and a stock solution supply valve A, and the liquid discharge valve E is located above.
A single or plural pieces of material 5 are vertically supported from the liquid intake chamber 4 above the partition plate 2 into the excess liquid storage tank 3. C is a pressurized gas valve provided in the excess stock solution storage tank 3. The air valve D, like the pressurized gas valve C, shall be installed in the raw liquid storage tank 3, and the air valve D shall be installed in the liquid intake chamber 4.
In addition to the liquid discharge valve E, an atmosphere release or pressurization valve F is also provided. The material 5 is composed of a perforated core material 6, such as a tube whose entire surface is perforated, as shown in FIG. 6, so that liquid can be ingested from any part of the outer circumferential surface, and a cloth 7 is coated on the surface of the perforated core material 6. Use porous materials such as stainless steel.

上記の上部集液式加圧過機本体1に於いて、
過運転状態は第1図の如きであり、各バルブは
原液供給バルブA、液排出バルブEが開放の他
皆閉塞状態に在り、運転停止の為には原液供給バ
ルブAを閉塞し、次いで加圧ガスバルブCを開放
すると原液貯留槽3内の原液は前記原液供給バル
ブAが閉塞されているものにも拘らず加圧ガスに
より強制過が動作して液となり液排出バル
ブEへ導かれる。加圧ガスによる強制過は第2
図の状態を経て遂には第3図に示す如く状態迄進
行して材5の最下端位に原液面が達すると強制
過機能は停止する。第1〜3図の状況変化の間
も絶えず材5表面に付着した滓には加圧状態
を継続していることにより剥離脱落を発生させな
いという効果をもたらすことが出来る。第3図状
態に於ける原液の残液は内外差圧を保ちながらド
レンバルブBを開放して抜き取る。次に液の回
収方法及び同装置は第2実施例として添附図面の
第4図に従つて説明する。
In the above-mentioned upper liquid collection type pressurizing machine main body 1,
The over-operating state is as shown in Figure 1, in which all valves are closed except for the stock solution supply valve A and the liquid discharge valve E, which are open.To stop the operation, the stock solution supply valve A is closed, and then the stock solution supply valve E is closed. When the pressurized gas valve C is opened, the stock solution in the stock solution storage tank 3 becomes a liquid due to the pressurized gas and is guided to the liquid discharge valve E even though the stock solution supply valve A is closed. Forced overflow by pressurized gas is the second
The condition progresses through the state shown in the figure and finally reaches the state shown in FIG. 3, and when the raw liquid level reaches the lowest end of the material 5, the forced overfunction stops. By continuing to pressurize the slag adhering to the surface of the material 5 even during the situation changes shown in FIGS. 1 to 3, it is possible to prevent the slag from peeling off. The residual liquid in the state shown in FIG. 3 is drained by opening the drain valve B while maintaining the pressure difference between the inside and outside. Next, a liquid recovery method and apparatus will be described as a second embodiment with reference to FIG. 4 of the accompanying drawings.

上記第1実施例の構成に対し、液排出バルブ
Eに通ずる材5の内空下端まで回収管9を臨ま
せた液回収管集合部8を液摂取室4に付加設
置せしめて構成し、前記第1実施例により原液貯
留槽3の原液は液となつて排出バルブEから取
出すのであるが、材5及び過摂取室4の滞留
液は前記の原液の回収方法では回収不能である
ことは勿論であり、液回収バルブGを開放して
加圧ガスを原液貯留槽3を微低圧例えば実験値と
して0.1〜1.2Kg/cm2Gにて送気することにより、
該槽内は加圧状態となり、直接原液に圧力をかけ
原液を強制過して第4図の状態となり液摂取
室4は液の液圧が高まつて逃げ道が無い為回収
管9、回収管集合部8を経由して原液が材5の
最下部に到る迄液を外部に回収し得る。
In contrast to the configuration of the first embodiment, a liquid recovery tube collection section 8 is additionally installed in the liquid intake chamber 4, with the recovery tube 9 facing up to the lower end of the inner space of the material 5 leading to the liquid discharge valve E. According to the first embodiment, the undiluted solution in the undiluted solution storage tank 3 becomes a liquid and is taken out from the discharge valve E. However, it goes without saying that the remaining liquid in the material 5 and the overdose chamber 4 cannot be recovered by the above-mentioned method for recovering the undiluted solution. By opening the liquid recovery valve G and supplying pressurized gas to the raw liquid storage tank 3 at a very low pressure, for example, 0.1 to 1.2 Kg/cm 2 G as an experimental value,
The inside of the tank becomes pressurized, and the undiluted solution is directly pressurized and the undiluted solution is forced to pass through, resulting in the state shown in Fig. 4. The liquid intake chamber 4 is closed to the recovery pipe 9, as there is no escape route due to the increased liquid pressure. The liquid can be collected to the outside via the collection part 8 until the liquid reaches the lowest part of the material 5.

その後、ガス圧を例えば0.5Kg/cm2G程度に上
昇させた加圧ガスを供給することにより、ガスは
液摂取室4に徐々に流れ、該屋4はガスのみで
充満し、液はガス圧によつて第5図の如く回収
管9、回収管集合部8を軽由して液を外部に回
収する。この場合原液は微低圧ガス送気時に於け
る材5の最下部位の侭である。そして内外差圧
を保ちながらドレンバルブBを開放して原液の残
液を抜き取ることにより完全に機体内の原液及び
液を回収出来る。
After that, by supplying pressurized gas whose gas pressure has been increased to, for example, about 0.5 kg/cm 2 G, the gas gradually flows into the liquid intake chamber 4, and the chamber 4 is filled only with gas, and the liquid is filled with gas. As shown in FIG. 5, the pressure releases the recovery tube 9 and the recovery tube collecting section 8, and the liquid is recovered to the outside. In this case, the stock solution is the lowest part of the material 5 when the very low pressure gas is supplied. Then, by opening the drain valve B and draining the remaining stock solution while maintaining the internal and external pressure difference, the stock solution and liquid inside the machine can be completely recovered.

次に前記の微低圧送気の場合に対し、最初から
つまり直接原液に0.5Kg/cm2G程度の加圧ガスを
送気することにより、原液は強制過されると共
に、ガスは液摂取室4に流れ、前記の両現象が
相俟つて液は回収管9、回収管集合部8を経由
して液回収バルブGより液を外部に回収す
る。前記にて説明した如く大気開放又は加圧バル
ブFを設けることによつて、このバルブFを開放
して液摂取室4への加圧を併用すると液回収
管集合部8からの回収作業が迅速となる。然し、
当該加圧ガス圧は、原液貯留槽3の加圧ガス圧よ
り低く設定することを条件とする。尚前述のエア
抜きバルブDは、上記構成の過機に於いて、前
記大気開放又は加圧バルブFから洗浄の為送気し
た場合原液貯留槽3のエア抜き作用をする。
Next, in the case of extremely low pressure air supply described above, by supplying pressurized gas of about 0.5 kg/cm 2 G directly to the stock solution from the beginning, the stock solution is forcibly passed through, and the gas is transferred to the liquid intake chamber. 4, and as a result of both of the above-mentioned phenomena, the liquid passes through the recovery pipe 9 and recovery tube collection section 8, and is recovered to the outside from the liquid recovery valve G. As explained above, by providing the atmosphere release or pressurizing valve F, when this valve F is opened and the liquid intake chamber 4 is pressurized, the recovery work from the liquid recovery pipe collection section 8 can be speeded up. becomes. However,
The condition is that the pressurized gas pressure is set lower than the pressurized gas pressure of the stock solution storage tank 3. The above-mentioned air bleed valve D functions to bleed air from the stock solution storage tank 3 when air is blown to the atmosphere or from the pressurized valve F for cleaning in the above-mentioned permeator.

本発明の過原液及び液から成る機体内の液
の脱液方法及び同装置は上記の如く、過原液貯
留槽3に対し加圧ガスを供給継続して絶えず加圧
状態を保つている為原液の強制過を行いながら
材5表面に付績した滓は剥離脱落することな
く付績姿勢を保つた侭原液の回収が可能となるば
かりでなく液回収管集合部8を付設することに
より液の回収までも略完全に回収効果が得られ
ることによつて、メツキ液等高価な過原液の変
更に際して切換作業にともなう従来技術に於ける
不可抗力的損失を全面的に解消し得る有益なる発
明である、尚前記加圧ガスの圧力及び液回収管
集合部8の径等の設定値は過機本体1の機能仕
様に基づきテストにより作動値を選定することが
望ましい。
As described above, in the method and device for removing the liquid in the machine body made of excess stock solution and liquid of the present invention, pressurized gas is continuously supplied to the excess stock solution storage tank 3 to constantly maintain the pressurized state. The slag deposited on the surface of the material 5 during forced filtration does not peel off and fall, and the undiluted solution that remains in the deposition position can be recovered.In addition, by adding a liquid collection pipe collection part 8, the liquid can be removed. This is a useful invention that can completely eliminate the force majeure losses that occur in the prior art due to switching work when changing expensive overstock solutions such as plating solution by achieving a recovery effect almost completely. It is preferable to select operating values for the pressure of the pressurized gas, the diameter of the liquid recovery tube collecting section 8, etc. through tests based on the functional specifications of the filter main body 1.

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

第1〜3図は第1実施例を示す縦断面図、第
4、5図は第2実施例を示す同図、第6図は材
の断面図である。 1……過機本体、2……中間仕切板、3……
過原液貯留槽、4……液摂取室、5……
材、6……有孔芯材、7……布、8……液回
収管集合部、9……回収管、A……原液供給バル
ブ、B……ドレンバルブ、C……加圧ガスバル
ブ、D……エア抜きバルブ、E……液排出バル
ブ、F……大気開放又は加圧バルブ、G……液
回収バルブ。
1 to 3 are longitudinal sectional views showing the first embodiment, FIGS. 4 and 5 are the same figures showing the second embodiment, and FIG. 6 is a sectional view of the material. 1... Main body of the machine, 2... Intermediate partition plate, 3...
Excess liquid storage tank, 4...Liquid intake chamber, 5...
Material, 6... Perforated core material, 7... Cloth, 8... Liquid recovery tube gathering part, 9... Recovery pipe, A... Stock solution supply valve, B... Drain valve, C... Pressurized gas valve, D... ...Air bleed valve, E...Liquid discharge valve, F...Atmospheric release or pressurization valve, G...Liquid recovery valve.

Claims (1)

【特許請求の範囲】 1 中間仕切板2の下方を、最下部にドレンバル
ブB及び原液供給バルブAを設けた過原液貯留
槽3とし、同上方は、管路を介して液排出バル
ブEを設けた液摂取室4にして、単数又は複数
本の材5を、該液摂取室4から過原液貯留
槽3内に垂設支持し且つ該過原液貯留槽3に加
圧ガスバルブCを設けた上部集液式加圧過機本
体に於いて、 前記原液供給バルブA及び前記液排出バルブ
Eが解放の他皆閉塞状態にある過運転に対し、
原液供給バルブAを閉塞し、次いで前記加圧ガス
バルブCを解放して前記材5の最下端位に原液
面が達する迄加圧強制過を行なつた後、前記ド
レンバルブBを解放して原液の残液を回収し、更
に材5の内空まで回収管9の下端を臨ませ、該
回収管9の上端に連通する液回収管集合部8
に、外部からの管路を介して接続した液回収バ
ルブGを解放すると共に前記液排出バルブEと
前記液摂取室4との間の管路に連通した、大気
開放又は加圧するための加圧バルブFを開放し
て、液摂取室4への加圧を併用することによつ
て、該液摂取室4の液を外部に回収すること
を特徴とする上部集液式加圧過機に於ける機体
内液の脱液方法。 2 中間仕切板2の下方を、最下部にドレンバル
ブB及び原液供給バルブAを設けた過原液貯留
槽3とし、同上方は、管路を介して液排出バル
ブEを設けた液摂取室4にして、単数又は複数
本の材5を、該液摂取室4から過原液貯留
槽3内に垂設支持し且つ該貯留槽3に加圧ガスバ
ルブCを設けた上部集液式加圧過機本体に於い
て、 前記液排出バルブEと前記液摂取室4との
管路に連通して設けた、大気開放又は加圧するた
めの加圧バルブFと、前記材5の内空まで臨ま
せた回収管9と、該回収管9の上端に連通して設
けた液回収管集合部8と、該液回収管集合部
8に連通する外部からの管路に設けた液回収バ
ルブGとを備えたことを特徴とする上部集液式加
圧過機に於ける機体内液の脱液装置。
[Scope of Claims] 1 The lower part of the intermediate partition plate 2 is an excess stock solution storage tank 3 which is provided with a drain valve B and a stock solution supply valve A at the lowest part, and a liquid discharge valve E is connected to the upper part through a pipe line. A liquid intake chamber 4 is provided, and one or more pieces of material 5 are vertically supported from the liquid intake chamber 4 into the excess stock solution storage tank 3, and a pressurized gas valve C is provided in the excess stock solution storage tank 3. In the main body of the upper liquid collecting type pressurizing machine, in case of over-operation in which the raw liquid supply valve A and the liquid discharge valve E are all closed except in the open state,
The stock solution supply valve A is closed, and then the pressurized gas valve C is released to carry out forced overpressure until the stock solution level reaches the lowest end of the material 5, and then the drain valve B is released to supply the stock solution. The remaining liquid is recovered, and the lower end of the recovery tube 9 is exposed to the inner space of the material 5, and the liquid recovery tube gathering part 8 communicates with the upper end of the recovery tube 9.
Then, the liquid recovery valve G connected via a pipe line from the outside is released, and a pressurization valve connected to the pipe line between the liquid discharge valve E and the liquid intake chamber 4 is opened to the atmosphere or pressurized. In the upper liquid collection type pressurizing machine, the liquid in the liquid intake chamber 4 is recovered to the outside by opening the valve F and pressurizing the liquid intake chamber 4. How to remove fluids inside the aircraft. 2 The lower part of the intermediate partition plate 2 is an excess stock solution storage tank 3 equipped with a drain valve B and a stock solution supply valve A at the lowest part, and the upper part is a liquid intake chamber 4 equipped with a liquid discharge valve E via a conduit. An upper liquid collection type pressurizing machine in which one or more pieces of material 5 are vertically supported from the liquid intake chamber 4 into the excess stock liquid storage tank 3, and a pressurized gas valve C is provided in the storage tank 3. In the main body, there is a pressurizing valve F for opening to the atmosphere or pressurizing, which is provided in communication with the pipe line between the liquid discharge valve E and the liquid intake chamber 4, and a pressurizing valve F that communicates with the pipe line between the liquid discharge valve E and the liquid intake chamber 4, and a pressurizing valve F for opening to the atmosphere or pressurizing the liquid, and a pressure valve F that communicates with the pipe line between the liquid discharge valve E and the liquid intake chamber 4. It includes a recovery pipe 9, a liquid recovery tube collection part 8 provided in communication with the upper end of the recovery pipe 9, and a liquid collection valve G provided in a pipe line from the outside communicating with the liquid collection pipe collection part 8. A device for removing fluid inside the machine in an upper liquid collection type pressurizing machine.
JP15779684A 1984-07-28 1984-07-28 Method and apparatus for draining liquid in machine body in upper part liquid collection type filter press Granted JPS6135815A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15779684A JPS6135815A (en) 1984-07-28 1984-07-28 Method and apparatus for draining liquid in machine body in upper part liquid collection type filter press

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15779684A JPS6135815A (en) 1984-07-28 1984-07-28 Method and apparatus for draining liquid in machine body in upper part liquid collection type filter press

Publications (2)

Publication Number Publication Date
JPS6135815A JPS6135815A (en) 1986-02-20
JPH0435202B2 true JPH0435202B2 (en) 1992-06-10

Family

ID=15657471

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15779684A Granted JPS6135815A (en) 1984-07-28 1984-07-28 Method and apparatus for draining liquid in machine body in upper part liquid collection type filter press

Country Status (1)

Country Link
JP (1) JPS6135815A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02218409A (en) * 1989-02-21 1990-08-31 Japan Organo Co Ltd Method for recovering residual filtered liquid in filter cylinder in solid-liquid separation-recovery process
JP2009148680A (en) * 2007-12-19 2009-07-09 Fujiwara Techno-Art Co Ltd Method for recovering stock solution in filtration apparatus
GB0918149D0 (en) 2009-10-16 2009-12-02 Jagotec Ag Improved medicinal aerosol formulation

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4946264A (en) * 1972-08-21 1974-05-02
JPS5823126A (en) * 1981-07-31 1983-02-10 シャープ株式会社 Flat thin switch board

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4946264A (en) * 1972-08-21 1974-05-02
JPS5823126A (en) * 1981-07-31 1983-02-10 シャープ株式会社 Flat thin switch board

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