JPH0312400Y2 - - Google Patents
Info
- Publication number
- JPH0312400Y2 JPH0312400Y2 JP1983129413U JP12941383U JPH0312400Y2 JP H0312400 Y2 JPH0312400 Y2 JP H0312400Y2 JP 1983129413 U JP1983129413 U JP 1983129413U JP 12941383 U JP12941383 U JP 12941383U JP H0312400 Y2 JPH0312400 Y2 JP H0312400Y2
- Authority
- JP
- Japan
- Prior art keywords
- cylinder
- air
- water
- water pump
- stage water
- 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
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
Description
【考案の詳細な説明】
(産業上の利用分野)
この考案は水深の大きいダム又は湖沼等におい
て、上層部と下層部とを夫々別個に対流撹拌させ
ると共に、曝気することを目的とした二段揚水筒
に関するものである。[Detailed explanation of the invention] (Industrial application field) This invention is a two-stage design for the purpose of separately convective stirring and aeration of the upper and lower parts of dams, lakes, etc. with large water depths. This relates to water pumps.
(従来の技術)
この種二段揚水筒については、先に出願人が提
案したが(特願昭56−170951号又は実願昭57−
124874号)、前者は下部揚水筒で使用した空気を
上部揚水筒で再び使用するものでないので、後者
はこれを改良したものである。(Prior Art) This type of two-stage water pump was previously proposed by the applicant (Japanese Patent Application No. 170951/1983 or Utility Application No. 170951/1983).
124874), the former does not reuse the air used in the lower pumping tube in the upper pumping tube, so the latter is an improvement on this.
(考案により解決すべき課題)
前記従来の装置において、実願昭57−124874号
は、下部筒体内を上昇する気泡の粉砕が不十分に
なり易く、かつ酸素不足を改善するのには空気量
不足になる問題点があつた。(Problems to be Solved by Invention) In the conventional device, Utility Application No. 124874/1985, the air bubbles rising inside the lower cylinder tend to be insufficiently pulverized, and the amount of air is insufficient to improve the oxygen deficiency. There was a problem with the shortage.
(課題を解決する為の手段)
然るにこの考案は、下部筒体に空気補給装置を
設けたので、不足酸素を補給し、前記従来の問題
点を解決したのである。また、この考案は前記実
願昭57−124874号を更に改良して気泡粉砕装置を
高能率化し又は上部筒体を下部筒体より大径にす
るなど、実用性を一層向上させたものである。(Means for Solving the Problems) However, in this invention, an air supply device is provided in the lower cylinder, thereby replenishing insufficient oxygen and solving the above-mentioned conventional problems. Furthermore, this invention further improves the practicality of the above-mentioned Utility Application No. 124874/1985 by making the bubble crusher more efficient and making the upper cylinder larger in diameter than the lower cylinder. .
即ちこの考案は、下部に空気間欠供給用の空気
室を備え、上部に気泡粉砕装置を内蔵した下部筒
体の上部へ、下部に、前記下部筒体内を上昇する
空気を分離する装置と、該空気を捕集して再び間
欠供給するようにした空気室とを備え、上部に浮
子を有する上部筒体を縦に連設し、前記下部筒体
の下部へ空気補給装置を設けてなる二段揚水筒で
ある。また、気泡粉砕装置は円筒内壁へ固定した
撹拌翼および突起としたものである。次に、空気
を分離する装置は、複数の截頭円錐を所定間隔で
重層させたものである。更に、上部筒体は下部筒
体と同径又は大径としたものである。また、空気
補給装置は筒体の周壁へ多数の気孔を設け、その
外側へ散気管を周繞したものである。 That is, this invention includes a device for separating the air rising in the lower cylinder from the upper part of the lower cylinder, which has an air chamber for intermittent supply of air in the lower part and a built-in bubble crusher in the upper part; A two-stage structure comprising an air chamber that collects air and re-supplies it intermittently, an upper cylinder having a float on the upper part connected vertically, and an air supply device provided at the bottom of the lower cylinder. It is a water pump. Further, the bubble crushing device has stirring blades and protrusions fixed to the inner wall of the cylinder. Next, the device for separating air is constructed by stacking a plurality of truncated cones at predetermined intervals. Furthermore, the upper cylinder has the same diameter or a larger diameter than the lower cylinder. Further, the air replenishing device has a large number of air holes provided in the peripheral wall of a cylindrical body, and a diffuser tube surrounding the air holes on the outside thereof.
前記粉砕装置は、例えば案内羽根によつて水流
に渦を発生させ、水と空気とを流動中に激突させ
て粉砕させるもので、定置羽根による粉砕作用の
為に、長時間連続運転しても故障を生じるおそれ
はない。また筒壁に突起を設けることによつて、
局部的に急激な流速変動を生じさせることによ
り、粉砕効果を一層向上させることができる。 The crushing device generates a vortex in the water flow using guide vanes, for example, and causes the water and air to collide during the flow to crush it, and because of the crushing action by the stationary blades, it can be operated continuously for long periods of time. There is no risk of malfunction. Also, by providing protrusions on the cylinder wall,
The pulverizing effect can be further improved by locally causing rapid fluctuations in flow velocity.
尚、下部筒体内で粉砕された気泡は水に混入さ
れて下部層の水中へ可及的に酸素を補給する。こ
の水は下部層内で独立して対流するので(主とし
て温度差によつて上層と下層とは分離される)、
低温の下層水が温度の高い上層水と混入するおそ
れはない。また下層水は酸欠になり易いが、上層
水は水面より酸素補給を受ける為に一般的に溶存
酸素量が多い。従つて下層水には可及的に酸素補
給の考慮を要するが、上層水は比較的水面に近い
部分の水と、水面から若干離れている付近の水と
を対流により混合させることにより、必要な溶存
酸素量を得ることができる。 Note that the air bubbles crushed in the lower cylinder are mixed into the water to supply as much oxygen as possible to the water in the lower layer. Since this water convects independently within the lower layer (the upper and lower layers are separated primarily by temperature differences),
There is no risk of the low temperature lower layer water mixing with the higher temperature upper layer water. In addition, lower layer water is prone to oxygen deficiency, but upper layer water generally has a higher amount of dissolved oxygen because it receives oxygen supply from the water surface. Therefore, it is necessary to consider oxygen supplementation for the lower layer water as much as possible, but for the upper layer water, the necessary oxygen supply is achieved by mixing the water relatively close to the water surface and the water slightly farther from the water surface by convection. The amount of dissolved oxygen can be obtained.
(作用)
この考案は、上部筒体と下部筒体に夫々間欠空
気供給用の空気室を備えたので、夫々の筒体内を
気泡が間欠的に上昇して、夫々の筒体内を気泡が
間欠的に上昇して、夫々の筒体の下方の水を上昇
させるが、水の上昇速度は変動する。また、下部
筒体の下部に空気補給装置を設けたので、この空
気の酸素を溶解するので、下部筒体上から放出さ
れる水は、吸入された水より溶存酸素量が多くな
る。(Function) This device has an air chamber for intermittent air supply in the upper cylinder and the lower cylinder, so air bubbles rise intermittently within each cylinder, and air bubbles intermittently rise inside each cylinder. The water below each cylinder rises, but the rising speed of the water fluctuates. Furthermore, since the air supply device is provided at the bottom of the lower cylinder, the oxygen in this air is dissolved, so that the water discharged from above the lower cylinder has a higher amount of dissolved oxygen than the inhaled water.
(実施例)
即ちこの考案の実施例を添付図面について説明
すれば次の通りである。(Embodiment) An embodiment of this invention will be described below with reference to the accompanying drawings.
ガラス繊維強化プラスチツク製の円筒1の下部
に空気室2を装着固定し、下端に散気管3を周繞
固定すると共に、上部に円筒1より若干大径の粉
砕装置4を連結して下部筒体Aを構成する。また
円筒1と同材質の円筒5の下端に分離装置6を連
結し、その上部の円筒外周に空気室7を装着し、
上端部外周へ浮子8を装着して上部筒体Bを構成
する。前記下部筒体Aの上部へ上部筒体Bを縦に
連結し、この考案の二段揚水筒を構成する。前記
空気室2は円筒9(円筒1と同質かつ同径)の外
側へ所定の間隙を保つて中間円筒10,11を順
次遊嵌し、中間円筒11の外側へ所定の間隙を保
つて外筒12を遊嵌し、円筒9の上部、中間円筒
10,11の上下部へ通気孔13,14,15
夫々穿設し、前記外筒12の下端と中間円筒11
の下端との間は環状間隙16として開放したもの
である(第3図)。前記実施例において、第1図
は上下部筒体がほぼ等径であり、第2図は上部筒
体を大径としたものである。上部筒体と下部筒体
の設置深さが相違するので、同一空気量を使用す
れば(若干は水中に溶けて少なくなるとしても)
上部筒体内を上昇する空気容積は水深に比例して
増加するので、これを考慮して上部筒体の直径を
大きくした方が合理的である。特に上部筒体の空
気室の容積との関係で、空気が連続して出るよう
になると、上部筒体による対流力が弱くなるの
で、上部筒体の直径はその中を上昇する空気団の
上昇間隔および空気団の容積に適した大きさにし
なければならない。 An air chamber 2 is attached and fixed to the lower part of a cylinder 1 made of glass fiber reinforced plastic, a diffuser pipe 3 is fixed around the lower end, and a crushing device 4 having a slightly larger diameter than the cylinder 1 is connected to the upper part to form a lower cylinder. Configure A. In addition, a separation device 6 is connected to the lower end of a cylinder 5 made of the same material as the cylinder 1, and an air chamber 7 is attached to the outer circumference of the upper cylinder.
A float 8 is attached to the outer periphery of the upper end to constitute an upper cylinder B. The upper cylinder B is vertically connected to the upper part of the lower cylinder A to constitute a two-stage water pump of this invention. The air chamber 2 is formed by loosely fitting intermediate cylinders 10 and 11 one after another while keeping a predetermined gap to the outside of a cylinder 9 (same quality and the same diameter as the cylinder 1), and forming an outer cylinder by keeping a predetermined gap to the outside of the intermediate cylinder 11. 12 loosely fit into the upper part of the cylinder 9 and the upper and lower parts of the intermediate cylinders 10 and 11 through the ventilation holes 13, 14, 15.
The lower end of the outer cylinder 12 and the intermediate cylinder 11 are respectively bored.
An annular gap 16 is opened between the lower end and the lower end (FIG. 3). In the embodiment described above, FIG. 1 shows that the upper and lower cylindrical bodies have approximately the same diameter, and FIG. 2 shows that the upper cylindrical body has a larger diameter. Since the installation depths of the upper and lower cylinders are different, if you use the same amount of air (even if some of it dissolves in the water and becomes smaller)
Since the volume of air rising inside the upper cylinder increases in proportion to the water depth, it is more rational to take this into account and increase the diameter of the upper cylinder. In particular, in relation to the volume of the air chamber in the upper cylinder, when air comes out continuously, the convection force by the upper cylinder becomes weaker, so the diameter of the upper cylinder is reduced by the rise of the air mass rising inside it. It shall be sized appropriately for the spacing and volume of the air mass.
前記実施装置において送気管17より(第3図
中)矢示18のように加圧空気を供給すると、空
気は中間円筒10,11および外筒12の相互間
隔に溜り、空気室内の水位を逐次低下させる。か
くて水位が第3図中鎖線19の位置に達すると、
空気室2内に溜つた空気は、通気孔13,14,
15を矢示21,22,23,24,25のよう
に流動し筒体9内へ一団となつて排出され(サイ
フオンによる)、空気団20となつて上昇する。
この空気団20が上昇することにより下部筒体1
の下端より水が矢印26のように流入する。前記
のようにして空気団20が上昇し、粉砕装置24
に入ると、水と空気は撹拌羽根27によつて急激
に方向変換されると共に(矢示8)突起29によ
り流速も変化して空気を微細化し、水に混入する
ので、空気中の酸素は水の中へ溶出する。このよ
うにして生じた空気粒と水との混合物は、第4図
中矢示30のように上昇し、内筒31の下端に衝
突して水は矢示2のように下降し、気泡は矢示3
3のように外筒34と、中間筒35の間を上昇
し、空気室7内へ溜る。このように上昇した気泡
は、中間筒35,36、外筒34の間隙部に溜
り、空気室7の水位を逐次下降させる。この水位
が第4図中鎖線37の位置に達すると、空気室7
内の空気は通気間隙38と通気孔39,40を経
て内つ31の内側へ排出され、空気団41となつ
て円筒5内を上昇する。そこで空気団41の上昇
に伴い、吸水管42から水を矢示43のように吸
入し、水と空気団とは円筒5内を矢示44のよう
に上昇し、その上端から矢示45のように排出さ
れる。従つて水は吸入管42から吸入され、円筒
の上端から排出されるので、円筒5の周囲には上
下対流を生じ、上部円筒体によつて上層水は撹拌
される。前記における空気団の上昇は必然的に間
欠的であるから、上部筒体の上端より排出される
水も間欠的に流速を変えることになる。例えば勢
力の強い水とその貫性力による流出とに分れるの
で、勢力の強い水の場合には上部筒体の上端付近
の水を押し分けるが、貫性力による流出は押し分
け力が殆んどないので、上部筒体付近の水は再び
矢示46,46のようにもどされ、結局上昇した
水と付近の水とは混合し、混合水の温度は上部筒
体の下端付近の水温より高くなる。例えば上部筒
体上端付近の水温が25℃で下端付近の水が17℃と
すれば、混合水は23℃位となる。従つて水温差に
よる比重差が少なくなり、上部筒体付近で下降す
ることなく水面付近を水平方向へ拡散し、徐々に
下降することになるので、対流循環範囲が著しく
広大となる。尚、下部筒体Aの下端(分離装置の
下部)および空気室7の外側には案内板47,4
8が設けられており、下部筒体Aより上昇し、気
泡分離した水が円筒1と直角の方向へ拡散するよ
うに案内する。この水は水底の冷たい円筒上部の
比較的温度の高い水が混合して中間位の温度(例
えば水底7℃で円筒上部が13℃ならば混合水は11
℃位となる)になるので、直ちに下降することな
く、徐々に比重下降するが、円筒1から排出され
た当初の水は混合状態が不十分の為に、或程度混
合するまでは案内板で案内することが望ましい。
また、下部筒体の空気室2から供給される空気だ
けでは必要な空気量(従つて供給酸素量)に不足
を来すと判断される場合にはホース49より矢示
50のように散気管3へ加圧空気を送入し、散気
管3より気孔51を経て微小空気を矢示噴出させ
れば多量の空気を補給することができる。 When pressurized air is supplied from the air pipe 17 in the direction indicated by the arrow 18 (in FIG. 3) in the above-mentioned implementation device, the air accumulates between the intermediate cylinders 10, 11 and the outer cylinder 12, and the water level in the air chamber is gradually increased. lower. Thus, when the water level reaches the position indicated by the chain line 19 in Figure 3,
The air accumulated in the air chamber 2 is discharged through the ventilation holes 13, 14,
15 flows as indicated by arrows 21, 22, 23, 24, and 25, is discharged as a group into the cylinder 9 (by the siphon), and rises as an air mass 20.
As this air mass 20 rises, the lower cylinder 1
Water flows in from the lower end as shown by arrow 26. The air mass 20 rises as described above, and the crushing device 24
When water and air enter the water, the direction is rapidly changed by the stirring blade 27 (arrow 8), and the flow velocity is also changed by the protrusion 29, making the air fine and mixing with the water, so that the oxygen in the air is Elutes into water. The mixture of air particles and water thus generated rises as shown by arrow 30 in FIG. Show 3
3, it rises between the outer cylinder 34 and the intermediate cylinder 35 and accumulates in the air chamber 7. The air bubbles that have risen in this way accumulate in the gaps between the intermediate cylinders 35, 36 and the outer cylinder 34, and gradually lower the water level in the air chamber 7. When this water level reaches the position indicated by the chain line 37 in Fig. 4, the air chamber 7
The air inside the cylinder 5 is discharged to the inside of the cylinder 31 through the ventilation gap 38 and the ventilation holes 39 and 40, and becomes an air mass 41 and rises inside the cylinder 5. Therefore, as the air mass 41 rises, water is sucked in from the water suction pipe 42 as shown by the arrow 43, and the water and air mass rise within the cylinder 5 as shown by the arrow 44, and from the upper end as shown by the arrow 45. It is discharged like this. Therefore, water is sucked in through the suction pipe 42 and discharged from the upper end of the cylinder, so that vertical convection occurs around the cylinder 5, and the upper layer water is stirred by the upper cylinder. Since the rise of the air mass in the above is necessarily intermittent, the flow velocity of the water discharged from the upper end of the upper cylinder also changes intermittently. For example, water can be separated into water with a strong force and outflow due to its penetrating force, so in the case of water with a strong force, the water near the upper end of the upper cylinder is separated, but in the case of outflow due to a penetrating force, there is almost no force to separate it. As a result, the water near the upper cylinder is returned again as shown by arrows 46 and 46, and the rising water eventually mixes with the nearby water, and the temperature of the mixed water is lower than the water temperature near the lower end of the upper cylinder. It gets expensive. For example, if the water temperature near the top end of the upper cylinder is 25°C and the water near the bottom end is 17°C, the mixed water will be about 23°C. Therefore, the difference in specific gravity due to the difference in water temperature is reduced, and the water spreads horizontally near the water surface without descending near the upper cylinder and gradually descends, so the range of convective circulation becomes significantly wider. Note that guide plates 47 and 4 are provided at the lower end of the lower cylinder A (lower part of the separation device) and on the outside of the air chamber 7.
8 is provided, which rises from the lower cylinder A and guides the bubble-separated water to diffuse in a direction perpendicular to the cylinder 1. This water is mixed with relatively high-temperature water at the top of the cylinder, which is cold at the bottom, and has an intermediate temperature (for example, if the bottom of the water is 7°C and the top of the cylinder is 13°C, the mixed water is 11°C).
℃), so the specific gravity does not drop immediately, but gradually decreases.However, since the initial water discharged from the cylinder 1 is not sufficiently mixed, it is kept on the guide plate until it is mixed to a certain extent. It is desirable to provide guidance.
In addition, if it is determined that the air supplied from the air chamber 2 of the lower cylinder is insufficient for the required amount of air (therefore, the amount of oxygen supplied), the hose 49 is connected to the diffuser pipe as shown by the arrow 50. A large amount of air can be replenished by supplying pressurized air to the air diffuser 3 and ejecting fine air from the air diffuser 3 through the pores 51 in the direction of the arrow.
(考案の効果)
即ちこの考案によれば、空気室と粉砕装置とを
有する下部筒体と、分離装置と空気室を有する上
部筒体とを上下に縦に連結し、下部筒体に供給し
た空気を利用して下部筒体内および上部筒体内へ
水を間欠的に上昇させ、各筒体外に上下対流を発
生させると共に、下部筒体内を上昇する空気団を
粉砕して微粉化し、これに含まれた酸素を効率よ
く溶解させて下層水中の溶存酸素量を増大させる
効果がある。(Effect of the invention) That is, according to this invention, a lower cylinder having an air chamber and a crushing device, and an upper cylinder having a separating device and an air chamber are vertically connected, and the powder is supplied to the lower cylinder. Using air, water is intermittently raised into the lower cylinder and upper cylinder to generate vertical convection outside each cylinder, and the air particles rising inside the lower cylinder are pulverized and pulverized. It has the effect of efficiently dissolving the absorbed oxygen and increasing the amount of dissolved oxygen in the lower water.
また、撹拌翼および突起による気泡粉砕装置を
通過すれば、気泡は一層微細になる効果があり、
下部筒体の下部に空気補給装置を設けたので、下
部筒体を上昇する水は、当該空気の酸素が溶解
し、溶存酸素量を増大する効果がある。 In addition, if the bubbles pass through a bubble crusher using stirring blades and protrusions, the bubbles will become even finer.
Since the air supply device is provided at the bottom of the lower cylinder, the water rising up the lower cylinder has the effect of dissolving oxygen in the air and increasing the amount of dissolved oxygen.
第1図はこの考案の実施例の一部を切断した正
面図、第2図は同じく上部筒体を下部筒体より大
径にした実施例の一部省略し一部切断した正面
図、第3図は同じく下部の空気室の拡大断面図、
第4図は同じく上部の空気室の断面拡大図であ
る。
1,5……円筒、2,7……空気室、3……散
気管、4……粉砕装置、6……分離装置、A……
下部筒体、B……上部筒体。
Fig. 1 is a partially cutaway front view of an embodiment of this invention, and Fig. 2 is a partially omitted and partially cutaway front view of an embodiment in which the upper cylinder has a larger diameter than the lower cylinder. Figure 3 is an enlarged sectional view of the lower air chamber,
FIG. 4 is an enlarged cross-sectional view of the upper air chamber. 1, 5...Cylinder, 2,7...Air chamber, 3...Diffuser pipe, 4...Crushing device, 6...Separation device, A...
Lower cylindrical body, B...upper cylindrical body.
Claims (1)
に気泡粉砕装置を内蔵した下部筒体の上部へ、
下部に、前記下部筒体内を上昇する空気を分離
する装置と、該空気を捕集して再び間欠供給す
るようにした空気室とを備え、上部に浮子を有
する上部筒体を縦に連設し、前記下部筒体の下
部へ空気補給装置を設けてなる二段揚水筒。 2 気泡粉砕装置は円筒内壁へ固定した撹拌翼お
よび突起とした実用新案登録請求の範囲第1項
記載の二段揚水筒。 3 空気を分離する装置は、複数の截頭円錐を所
定間隔で重層させた実用新案登録請求の範囲第
1項記載の二段揚水筒。 4 上部筒体は下部筒体と同径又は大径とした実
用新案登録請求の範囲第1項記載の二段揚水
筒。 5 空気補給装置は筒体の周壁へ多数の気孔を設
け、その外側へ散気管を周繞した実用新案登録
請求の範囲第1項記載の二段揚水筒。[Scope of Claim for Utility Model Registration] 1. To the upper part of the lower cylindrical body, which has an air chamber for intermittent supply of air in the lower part and a built-in bubble crusher in the upper part,
The lower part is equipped with a device for separating the air rising inside the lower cylinder, and an air chamber that collects the air and supplies it again intermittently, and the upper cylinder has a float at the upper part and is connected vertically. and a two-stage water pump comprising an air supply device provided at the bottom of the lower cylinder. 2. The two-stage water pump according to claim 1, wherein the bubble crushing device is a stirring blade and a protrusion fixed to the inner wall of the cylinder. 3. The air separating device is a two-stage water pump according to claim 1, which is a utility model registration, and includes a plurality of truncated cones layered at predetermined intervals. 4. The two-stage water pump as set forth in claim 1 of the utility model registration claim, in which the upper cylinder has the same diameter or a larger diameter than the lower cylinder. 5. The air replenishing device is a two-stage water pump according to claim 1, which is a utility model, in which a large number of air holes are provided in the peripheral wall of the cylinder, and a diffuser pipe is surrounded on the outside thereof.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1983129413U JPS6039399U (en) | 1983-08-22 | 1983-08-22 | two-stage water pump |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1983129413U JPS6039399U (en) | 1983-08-22 | 1983-08-22 | two-stage water pump |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6039399U JPS6039399U (en) | 1985-03-19 |
| JPH0312400Y2 true JPH0312400Y2 (en) | 1991-03-25 |
Family
ID=30293235
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1983129413U Granted JPS6039399U (en) | 1983-08-22 | 1983-08-22 | two-stage water pump |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6039399U (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63400U (en) * | 1986-06-17 | 1988-01-05 |
-
1983
- 1983-08-22 JP JP1983129413U patent/JPS6039399U/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6039399U (en) | 1985-03-19 |
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