JPH0428439B2 - - Google Patents
Info
- Publication number
- JPH0428439B2 JPH0428439B2 JP12490583A JP12490583A JPH0428439B2 JP H0428439 B2 JPH0428439 B2 JP H0428439B2 JP 12490583 A JP12490583 A JP 12490583A JP 12490583 A JP12490583 A JP 12490583A JP H0428439 B2 JPH0428439 B2 JP H0428439B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- chamber
- pump
- cathode
- water supply
- 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
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 76
- 238000004140 cleaning Methods 0.000 claims description 18
- 238000005868 electrolysis reaction Methods 0.000 claims description 10
- 230000002378 acidificating effect Effects 0.000 claims description 7
- 238000007599 discharging Methods 0.000 claims description 5
- 238000005192 partition Methods 0.000 claims description 4
- 230000000694 effects Effects 0.000 claims description 2
- 238000013022 venting Methods 0.000 claims description 2
- 239000007788 liquid Substances 0.000 description 9
- 239000007789 gas Substances 0.000 description 8
- 238000000034 method Methods 0.000 description 7
- 238000005406 washing Methods 0.000 description 5
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 239000000052 vinegar Substances 0.000 description 3
- 235000021419 vinegar Nutrition 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 239000001110 calcium chloride Substances 0.000 description 2
- 229910001628 calcium chloride Inorganic materials 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 229910002114 biscuit porcelain Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 229910001424 calcium ion Inorganic materials 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000007872 degassing Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000035622 drinking Effects 0.000 description 1
- 238000005370 electroosmosis Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
Description
【発明の詳細な説明】
本発明は、主として飲料に適する良質な水を電
気分解作用によつて生成するための水の電解装置
における洗滌装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a washing device in a water electrolysis device for producing high-quality water suitable for drinking mainly by electrolysis.
この種の水の電解装置は、長期的に連続して使
用されるので、陰極室内において、陰電極表面
に、カルシウムなどが析出し、沈着し、通電率を
低下させるという問題をかゝえている。そこで、
一時的に陰電極および陽電極に逆極性の直流電圧
を与えて、陰電極表面から沈着物を剥離させるこ
とがなされている。また、別の方法としては、酢
などを水中に混入し、電解槽内に循環させること
により、化学的に除去する方式が試みられてい
る。この方式の利点は、電極表面から、沈着物を
除去するだけでなく、極室内壁あるいは取出し用
通路内壁に附着したものも、分解除去できる点に
ある。この洗滌の際の循環には、ポンプが使用さ
れるが、この循環系は閉鎖型にすることができな
い。これは、洗滌の際あるいは通常の電解作用の
際に発生したガスを自然に排出しなければならな
いためで、もし、このガスがポンプ内に送り込ま
れると、ポンプが空転し、ノツキング現象をもた
らす。 Since this type of water electrolyzer is used continuously over a long period of time, it suffers from the problem that calcium and other substances precipitate and deposit on the surface of the cathode in the cathode chamber, reducing the current conductivity. . Therefore,
A DC voltage of opposite polarity is temporarily applied to the negative electrode and the positive electrode to remove deposits from the surface of the negative electrode. As another method, attempts have been made to chemically remove the water by mixing vinegar or the like into water and circulating it in the electrolytic cell. The advantage of this method is that not only deposits can be removed from the electrode surface, but also deposits attached to the inner wall of the electrode chamber or the inner wall of the extraction passage can be decomposed and removed. A pump is used for circulation during this washing, but this circulation system cannot be of a closed type. This is because the gas generated during cleaning or normal electrolytic action must be naturally exhausted. If this gas is pumped into the pump, the pump will idle, resulting in a knocking phenomenon.
本発明は上記事情にもとづいてなされたもの
で、循環系内にガスが発生していても、ポンプ側
にもたらすことなく、自然に排出でき、ポンプの
空転がさけられ、円滑な洗滌作用が行なえるよう
にした水の電解装置における洗滌装置を提供しよ
うとするものである。 The present invention has been made based on the above circumstances, and even if gas is generated in the circulation system, it can be naturally discharged without introducing it to the pump side, and idling of the pump can be avoided and a smooth cleaning action can be performed. It is an object of the present invention to provide a cleaning device for a water electrolysis device in which the water is washed.
この目的のため、本発明は、水供給個所より陰
極室および陽極室にそれぞれ水を分配供給し、各
極室に配設した陰電極および陽電極に直流電圧を
印加し、両極室を区切るポーラスな隔壁を介して
電気滲透作用、電気分解作用により陰極室側にア
ルカリイオン水を、陽極室側に酸性水をそれぞれ
生成するものにおいて、上記陰極室からアルカリ
イオン水を排出する通路に切換弁を介してバイパ
ス路を構成し、陽極室から酸性水を排出する通路
に上記バイパス路を連通し、上記バイパス路に設
けたポンプで洗滌時に陰極室および陽極室を水供
給個所を介して循環回路を形成すると共に、上記
酸性水の排出通路は上記バイパス路との連通個所
に上記ポンプのレベルよりも高い頂部を有するガ
ス抜き径路を設けてあることを特徴とする。 For this purpose, the present invention distributes and supplies water from a water supply point to a cathode chamber and an anode chamber, applies a DC voltage to a cathode and an anode disposed in each electrode chamber, and creates a porous tube that separates the two electrode chambers. In a device that generates alkaline ionized water in the cathode chamber side and acidic water in the anode chamber side by electroosmosis and electrolysis through a partition wall, a switching valve is installed in the passage for discharging the alkaline ionized water from the cathode chamber. The above bypass path is connected to a passage for discharging acidic water from the anode chamber, and a circulation circuit is established between the cathode chamber and the anode chamber through the water supply point during cleaning using a pump provided in the bypass path. In addition, the acid water discharge passage is characterized in that a degassing passage having a top portion higher than the level of the pump is provided at a point communicating with the bypass passage.
以下、本発明の一実施例を図面を参照して具体
的に説明する。図において、符号1は電解槽であ
り、ポーラスな、例えば素焼、あるいはミクロフ
イルターなどの電気滲透膜で構成された円筒状隔
壁2(板状でもよい)で、内側に陽極室3を、外
側に陰極室4を仕切つており、上記陰極室4内に
は陰極5を、上記陽極室3内には陽極6をそれぞ
れ配設している。 Hereinafter, one embodiment of the present invention will be specifically described with reference to the drawings. In the figure, reference numeral 1 denotes an electrolytic cell, which has a cylindrical partition wall 2 (it may be plate-shaped) made of a porous, e.g. bisque, or an electropermeable membrane such as a microfilter, with an anode chamber 3 on the inside and an anode chamber 3 on the outside. A cathode chamber 4 is partitioned, and a cathode 5 is disposed within the cathode chamber 4, and an anode 6 is disposed within the anode chamber 3.
上記陰極室4および陽極室3は電解槽1の底部
に構成した給水室7にそれぞれ下端を連通してお
り、上記陰極室4の上端は管路8を介して貯水槽
9に連通され、上記陽極室3の上端は管路10を
介してドレン11へと排出されるようになつてい
る。そして、上記給水室7には電磁開閉式の給水
弁12が浄水器13(活性炭などによるフイルタ
ー)を介して連通され、上記給水弁12は管路1
4を介して水道に連通されている。 The lower ends of the cathode chamber 4 and the anode chamber 3 communicate with a water supply chamber 7 configured at the bottom of the electrolytic cell 1, and the upper end of the cathode chamber 4 communicates with a water storage tank 9 via a conduit 8. The upper end of the anode chamber 3 is adapted to be discharged into a drain 11 via a conduit 10. An electromagnetic open/close type water supply valve 12 is communicated with the water supply chamber 7 via a water purifier 13 (a filter made of activated carbon or the like).
It is connected to the water supply via 4.
また、上記給水室7には、チエツクバルブ15
を介して洗滌液がポンプ16により供給されるよ
うになつており、また、チエツクバルブ17を介
して、塩化カルシウムなどの薬液がポンプ18に
より供給されるようになつている。 In addition, a check valve 15 is provided in the water supply chamber 7.
A cleaning liquid is supplied by a pump 16 through a check valve 17, and a chemical solution such as calcium chloride is supplied by a pump 18 through a check valve 17.
上記管路8には、電磁切換式のスプールバルブ
19が設けてあり、上記管路8をバイパス路20
に連通切換えできるようにしてある。上記バイパ
ス路20は上記管路10に連通され、また、途中
にはポンプ21を具備している。上記ポンプ21
にデリベリ側は管路8に、またサクシヨン側は管
路10に向けられている。また、上記管路10に
は上記バイパス路20との連通個所に、上記ポン
プレベルよりも高い頂部を有するガス抜き径路2
2がもうけられている。 The pipe line 8 is provided with an electromagnetic switching type spool valve 19, and the pipe line 8 is connected to a bypass line 20.
It is possible to switch the communication to The bypass path 20 communicates with the pipe line 10, and is provided with a pump 21 on the way. The above pump 21
The delivery side is directed towards line 8 and the suction side towards line 10. Further, the pipe line 10 has a gas venting line 2 having a top portion higher than the pump level at a point communicating with the bypass line 20.
2 has been produced.
なお、図中、符号23は貯水槽9に設けたレベ
ルセンサであり、上記レベルセンサ23によつて
水レベルを検知し、上限および下限位置で信号を
制御系24に出すようになつている。上記制御系
24では、ポンプ21,16および18、スプー
ルバルブ19、給水弁12などの動作制御を行な
う。 In the figure, reference numeral 23 is a level sensor provided in the water tank 9, and the level sensor 23 detects the water level and outputs a signal to the control system 24 at the upper and lower limit positions. The control system 24 controls the operations of the pumps 21, 16, and 18, the spool valve 19, the water supply valve 12, and the like.
このような構成では、上記電解装置は、次のよ
うにして作動される。先づ、通常の電解について
説明する。レベルセンサ23が貯水槽9の下限レ
ベルを検知して制御系24に信号を送ると、制御
系24は給水弁12を開放する信号を入れると共
に、電極5,4間に直流電圧を印加し、電解槽1
内で水の電解作用、電気滲透作用を行なう。同時
に、ポンプ18を駆動して、塩化カルシウム溶液
など、アルカリイオン水含有のミネラル補給を達
成する。電解過程で、塩化カルシウムなどは水酸
化カルシウム、カルシウムイオンとして、陰極室
4内の水へと滲透される。生成されたアルカリイ
オン生成水は管路8、スプールバルブ19を介し
て貯水槽9に入れられる。一方、陽極室3で生成
された酸性水は管路10を経由して、ドレン11
へと排出される。貯水槽9の水レベルが上限に達
すると、センサ23によつて再び信号が制御系2
4に与えられ、給水弁12が閉じ、電極5,6間
への電流電圧印加が解除される。なお、電解水に
発生した陰極室4内の水素、陽極室3内の酸素な
どは、水と共に排出される。このようにして、水
の所要量につき、連続的に水の電解作用を達成す
るのである。 In such a configuration, the electrolyzer is operated as follows. First, normal electrolysis will be explained. When the level sensor 23 detects the lower limit level of the water tank 9 and sends a signal to the control system 24, the control system 24 inputs a signal to open the water supply valve 12 and applies a DC voltage between the electrodes 5 and 4. Electrolytic cell 1
Inside the chamber, water electrolyzes and electrolyzes. At the same time, the pump 18 is activated to achieve mineral replenishment containing alkaline ionized water, such as calcium chloride solution. During the electrolysis process, calcium chloride and the like permeate into the water in the cathode chamber 4 as calcium hydroxide and calcium ions. The generated alkaline ionized water is put into a water storage tank 9 via a pipe 8 and a spool valve 19. On the other hand, the acidic water generated in the anode chamber 3 passes through the pipe 10 to the drain 11.
is discharged to. When the water level in the water tank 9 reaches the upper limit, the sensor 23 again sends a signal to the control system 2.
4, the water supply valve 12 is closed, and the current and voltage application between the electrodes 5 and 6 is released. Note that hydrogen in the cathode chamber 4, oxygen in the anode chamber 3, etc. generated in the electrolyzed water are discharged together with the water. In this way, water electrolysis is achieved continuously for the required amount of water.
次に、酢(食用酢)などの洗滌液により、陰極
室4などの洗滌を行なう場合について具体的に説
明する。当該装置の使用者によつて、洗滌の開始
をスイツチが操作されると、制御系24は先づ、
給水弁12を閉鎖状態に維持し、ポンプ18を停
止状態に維持すると共に、スプールバルブ19を
切換動作させ、ポンプ16を駆動し、洗滌液を給
水室7に供給する。所要量の洗滌液が給水室7に
供給される間、酸性水の一部は、管路10を経由
して、ドレン11に排出される。この状況下で、
ポンプ21の駆動で、電解槽1内の水は、点線矢
印方向に循環を開始する。したがつて、水は給水
室7から陽極室3、バイパス20、ポンプ21、
管路8、陰極室4、給水室7の順で流れ、洗滌液
がこれらを通り、その過程で陰極5に沈着した付
着物質を溶解し、陰極室4内壁、管路8内壁など
に付着したものも洗滌、剥離するのである。電解
槽1内に残留し、あるいは、洗滌液との化学反応
などで生成されたガスは、循環する溶液中にとも
なわれて管路10に入るが、バイパス20との分
岐個処で経路22に流れ、比重差で浮上し、経路
22の頂部へともたらされる。このため、ポンプ
21へはガスは導入されず、ポンプ21の空転は
さけられ、ノツキング現象はさけられる。洗滌液
が所要量注入された段階でポンプ16の駆動は停
止される。電解槽1内の洗滌が終了する時点(制
御系タイマーなどにより設定した時間経過の後)
で、給水弁12が開放される。これによつて、電
解槽1を含む循環系での水量が増大し、ポンプ2
1による循環の間に、管路10を経由してドレン
11に洗滌水が流れ出す。電解槽1内の洗滌水が
新たに供給された水によつて稀釈されて、通常の
水の状態まで戻つた時点(制御系で時間的に予め
設定)で、ポンプ21が停止され、スプールバル
ブ19が切換り、図の状態に戻し、ポンプ18を
駆動し、電極5,6に直流電圧を印加する状態に
する。すなわち、再び、貯水槽9の水レベル検知
にもとづく、電解制御に戻るのである。 Next, a case in which the cathode chamber 4 and the like are cleaned with a cleaning liquid such as vinegar (edible vinegar) will be specifically described. When the user of the device operates the switch to start washing, the control system 24 first
The water supply valve 12 is maintained in a closed state, the pump 18 is maintained in a stopped state, and the spool valve 19 is operated to switch, the pump 16 is driven, and the cleaning liquid is supplied to the water supply chamber 7. While the required amount of cleaning liquid is supplied to the water supply chamber 7, a portion of the acidic water is discharged to the drain 11 via the pipe line 10. Under this situation,
By driving the pump 21, the water in the electrolytic cell 1 starts circulating in the direction of the dotted arrow. Therefore, water flows from the water supply chamber 7 to the anode chamber 3, the bypass 20, the pump 21,
The cleaning liquid flows in the order of pipe 8, cathode chamber 4, and water supply chamber 7, and the cleaning liquid passes through these, and in the process dissolves the adhering substances deposited on the cathode 5, and adheres to the inner wall of cathode chamber 4, the inner wall of pipe 8, etc. It also cleans and exfoliates things. Gas remaining in the electrolytic cell 1 or generated by a chemical reaction with the cleaning liquid is accompanied by the circulating solution and enters the pipe 10, but at the point where it branches off from the bypass 20, it enters the pipe 22. It flows to the top of the path 22, floats up due to the difference in specific gravity, and is brought to the top of the path 22. Therefore, no gas is introduced into the pump 21, idling of the pump 21 is avoided, and the knocking phenomenon is avoided. When the required amount of cleaning liquid has been injected, the drive of the pump 16 is stopped. The point in time when cleaning inside electrolytic cell 1 ends (after the time set by the control system timer, etc.)
Then, the water supply valve 12 is opened. As a result, the amount of water in the circulation system including the electrolyzer 1 increases, and the pump 2
During the circulation according to 1, the cleaning water flows out via the line 10 into the drain 11. When the cleaning water in the electrolytic cell 1 is diluted by the newly supplied water and returns to the normal water state (time set in advance in the control system), the pump 21 is stopped and the spool valve is closed. 19 is switched back to the state shown in the figure, the pump 18 is driven, and a DC voltage is applied to the electrodes 5 and 6. That is, the process returns to electrolysis control based on water level detection in the water tank 9 again.
本発明は、以上詳述したように、流水状態で電
解してアルカリイオン水を生成する電解装置にお
いて、その洗滌にポンプ循環系を用いる場合、ポ
ンプのサクシヨン側で、酸性水の排出通路(管路
10)にバイパス路20との分岐部分に対して、
ポンプレベルより高い経路22を設けたので、電
解過程で発生し、電解槽内などに残留したガス、
あるいは洗滌液との化学反応により発生したガス
などがポンプに導入されてノツキング現象を起す
おそれがなく、しかも、水の供給で、洗滌水を稀
釈した、通常水の状態に戻すまでの過程では、単
に上記排出通路からの排出でこれを達成でき、特
に切換弁などの制御系を設ける必要がないという
優れた効果が得られるのである。 As described in detail above, in an electrolytic device that generates alkaline ionized water by electrolyzing in flowing water, when a pump circulation system is used for cleaning, the acid water discharge passage (pipe With respect to the branch part of road 10) with bypass road 20,
Since the path 22 is higher than the pump level, gas generated during the electrolysis process and remaining in the electrolytic tank, etc.
In addition, there is no risk of gases generated by chemical reactions with the washing liquid being introduced into the pump and causing a knocking phenomenon, and in the process of returning the washing water to the diluted state of normal water by supplying water. This can be achieved simply by discharging from the above-mentioned discharge passage, and an excellent effect can be obtained in that there is no need to provide a control system such as a switching valve.
図面は本発明の一実施例を示す系統図である。
1……電解槽、2……隔壁、3……陽極室、4
……陰極室、5……陰極、6……陽極、7……給
水室、8……管路、9……貯水槽、10……管
路、11……ドレン、12……給水弁、13……
浄水器、14……管路、15……チエツクバル
ブ、16……ポンプ、17……チエツクバルブ、
18……ポンプ、19……スプールバルブ、20
……バイパス路、21……ポンプ、22……経
路、23……レベルセンサ、24……制御系。
The drawing is a system diagram showing one embodiment of the present invention. 1... Electrolytic cell, 2... Partition wall, 3... Anode chamber, 4
... cathode chamber, 5 ... cathode, 6 ... anode, 7 ... water supply chamber, 8 ... pipe, 9 ... water tank, 10 ... pipe, 11 ... drain, 12 ... water supply valve, 13...
Water purifier, 14...Pipe line, 15...Check valve, 16...Pump, 17...Check valve,
18...Pump, 19...Spool valve, 20
... bypass path, 21 ... pump, 22 ... route, 23 ... level sensor, 24 ... control system.
Claims (1)
れ水を分配供給し、各極室に配設した陰電極およ
び陽電極に直流電圧を印加し、両極室を区切るポ
ーラスな隔壁を介して電気滲透作用、電気分解作
用により陰極室側にアルカリイオン水を、陽極室
側に酸性水をそれぞれ生成するものにおいて、上
記陰極室からアルカリイオン水を排出する通路に
切換弁を介してバイパス路を構成し、陽極室から
酸性水を排出する通路に上記バイパス路を連通
し、上記バイパス路に設けたポンプで洗滌時に陰
極室および陽極室を水供給個所を介して循環回路
を形成するとともに、上記酸性水の排出通路は上
記バイパス路との連通個所に上記ポンプのレベル
よりも高い頂部を有するガス抜き径路を設けてあ
ることを特徴とする水の電解装置における洗滌装
置。1. Water is distributed and supplied from the water supply point to the cathode chamber and the anode chamber, and a DC voltage is applied to the cathode and anode arranged in each electrode chamber, and an electric permeation effect is generated through the porous partition wall that separates the two electrode chambers. , in which alkaline ionized water is generated in the cathode chamber side and acidic water is generated in the anode chamber side by electrolysis, a bypass path is configured through a switching valve in the path for discharging the alkaline ionized water from the cathode chamber, The bypass passage is connected to a passage for discharging acidic water from the anode chamber, and a pump provided in the bypass passage forms a circulation circuit between the cathode chamber and the anode chamber via the water supply point during cleaning, and the acidic water is discharged from the anode chamber through the water supply point. A cleaning device for a water electrolyzer, characterized in that the exhaust passage has a gas venting passage having a top higher than the level of the pump at a point communicating with the bypass passage.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12490583A JPS6019088A (en) | 1983-07-09 | 1983-07-09 | Washing system in electrolytic apparatus of water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12490583A JPS6019088A (en) | 1983-07-09 | 1983-07-09 | Washing system in electrolytic apparatus of water |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6019088A JPS6019088A (en) | 1985-01-31 |
| JPH0428439B2 true JPH0428439B2 (en) | 1992-05-14 |
Family
ID=14897009
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12490583A Granted JPS6019088A (en) | 1983-07-09 | 1983-07-09 | Washing system in electrolytic apparatus of water |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6019088A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01130775A (en) * | 1987-11-17 | 1989-05-23 | Tatsuo Okazaki | Closed circuit for washing liquid |
| JPH02108794U (en) * | 1988-06-21 | 1990-08-29 |
-
1983
- 1983-07-09 JP JP12490583A patent/JPS6019088A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6019088A (en) | 1985-01-31 |
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