JPH0441999A - Jet pump - Google Patents
Jet pumpInfo
- Publication number
- JPH0441999A JPH0441999A JP14658890A JP14658890A JPH0441999A JP H0441999 A JPH0441999 A JP H0441999A JP 14658890 A JP14658890 A JP 14658890A JP 14658890 A JP14658890 A JP 14658890A JP H0441999 A JPH0441999 A JP H0441999A
- Authority
- JP
- Japan
- Prior art keywords
- piping
- diameter
- jet pump
- cylinder
- outer tube
- 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.)
- Pending
Links
- 239000007787 solid Substances 0.000 abstract description 11
- 230000007423 decrease Effects 0.000 abstract description 4
- 239000012530 fluid Substances 0.000 description 9
- 238000007664 blowing Methods 0.000 description 2
- 238000005086 pumping Methods 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
Landscapes
- Jet Pumps And Other Pumps (AREA)
Abstract
Description
【発明の詳細な説明】
「産業上の利用分野]
この発明はジェットポンプに関し、特に固形物を含有す
る流体の搬送に適したジェットポンプに関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a jet pump, and particularly to a jet pump suitable for conveying a fluid containing solids.
「従来の技術及び発明が解決しようとする課題1従来よ
りジェットポンプは第2図に示すように、駆動流配管5
を被駆動流配管6の内部に同軸に配置していたから、被
駆動流配管6の流路6bは環状となっていたにの中心流
ジェットポンプでは、被駆動流配管6の入口端6aの流
路は一般には円形に形成されているから、入口端6aか
らジエ・ントボンプ部の環状流路6bに至る被駆動流配
管6の流路断面積を同一に形成すると5入口端6aをち
ょうど通過できる球体はジェットポンプ部の環状流路6
bを通過することができない、したがつて例えば沈砂池
の揚砂ポンプのように、搬送する対象が固形物を含有す
るときにはポンプの閉塞を来すおそれがあった。またこ
の中心流ジェットポンプではキャビテーションを起こす
おそれが強いために、一般には空気を吹き込んでキャビ
テーションの発生を防止する必要があり、他方、空気を
吹き込むと被駆動流の揚水量が小さくなるという問題点
も有していた。``Problems to be solved by the prior art and the invention 1 Conventionally, jet pumps have a driving flow piping 5, as shown in Fig. 2.
In the center flow jet pump, the flow path 6b of the driven flow piping 6 is annular because the flow path 6b of the driven flow piping 6 is arranged coaxially inside the driven flow piping 6. is generally formed in a circular shape, so if the flow path cross-sectional area of the driven flow pipe 6 from the inlet end 6a to the annular flow path 6b of the die pump section is made the same, a sphere that can just pass through the inlet end 6a. is the annular flow path 6 of the jet pump section
b.Therefore, when the object to be conveyed contains solids, such as in a sand pump for a sand settling basin, there is a risk of blockage of the pump. In addition, since there is a strong risk of cavitation occurring in this central flow jet pump, it is generally necessary to blow air to prevent cavitation from occurring.On the other hand, there is the problem that blowing air reduces the pumping amount of the driven flow. It also had
また特公昭63−25200号公報には、被駆動流配管
の終端外周に設けた多数のノズルから駆動流を噴出した
ジェットポンプが開示されている。Further, Japanese Patent Publication No. 63-25200 discloses a jet pump that ejects a driving flow from a number of nozzles provided on the outer periphery of the terminal end of a driven flow pipe.
この構成は被駆動流配管の終端、すなわち駆動流と被駆
動流との混合領域の始端において、流路断面積がステッ
プ状に拡大しているが、ジェットポンプの効率を高める
ためには一般には拡径した混合領域を絞る必要があり、
管径を絞るとやはりその部分で固形物による流路の閉塞
を招く危険性を生じてしまう6またこの技術は多数の中
心流ジェットポンプを環状に配置した構成となっている
がら空気導入管を設けざるを得す、しかもその結果揚水
量が小さくなるのを免れず、結局のところ中心流ジェッ
トポンプにおける上記問題点を解決するには至っていな
い、
したがって本発明は、固形物を含有する流体を搬送する
ときにも固形物による閉塞を招くおそれが全くなく、ま
た空気導入管を設ける必要もなく、したがって揚水量の
低下を来さないジェットポンプを提供することを目的と
する6
[課題を解決するための手段〕
本発明は上記目的を達成するために成されたものであり
、すなわち実質的に同一の内径を有する配管を設け、該
配管と軸線を共有する第1及び第2の円錐形が前記配管
と交差する位置をそれぞれ内壁及び外壁とする環状テー
パ状の開口を前記配管に設け、該開口に駆動流配管を取
付けたジェットポンプである。In this configuration, the cross-sectional area of the flow passage expands in a stepwise manner at the end of the driven flow piping, that is, at the beginning of the mixing region of the driving flow and the driven flow, but in order to increase the efficiency of the jet pump, generally It is necessary to narrow down the expanded mixing area,
If the pipe diameter is narrowed, there is a risk that the flow path will be blocked by solid matter at that part6.Furthermore, although this technology has a structure in which a number of central flow jet pumps are arranged in a ring, it is difficult to connect the air introduction pipe. However, as a result, the amount of pumped water is inevitably reduced, and the above-mentioned problems in the central flow jet pump have not been solved.Therefore, the present invention is directed to It is an object of the present invention to provide a jet pump that has no risk of clogging due to solid matter during conveyance, does not require the provision of an air introduction pipe, and therefore does not cause a decrease in pumped water.6 [Problems solved] [Means for achieving the above object] The present invention has been made to achieve the above object, that is, a pipe having substantially the same inner diameter is provided, and first and second conical shapes sharing an axis with the pipe are provided. In this jet pump, an annular tapered opening is provided in the piping and a driving flow piping is attached to the opening, the inner wall and the outer wall being the positions where the piping intersects with the piping.
[作用]
被駆動流配管すなわち開口を設けた部分以前の配管と、
混合領域すなわち開口を設けた部分以降の配管とは実質
的に同一の内径に形成されているから、固形物を含有す
る流体を搬送するときにも固形物による閉塞を招くおそ
れは全くない。また本発明の一実施例による実験結果で
は、空気を吹き込まなくともキャビテーションは全く生
じなかった。この理由は第1に、配管に拡径部も縮径部
もないこと、及び第2に、開口を形成する内壁も外壁も
円錐形に形成されているから、開口部での駆動流は管軸
に平行な成分を持たず、すなわち駆動流のいずれの微小
流塊も配管の軸芯に向がって流れるために、径方向の圧
力勾配が生じにくいことによるものと思われる。[Operation] The driven flow piping, that is, the piping before the part where the opening is provided,
Since the mixing region, that is, the piping after the opening is formed to have substantially the same inner diameter, there is no risk of blockage due to solids even when transporting a fluid containing solids. Further, according to the experimental results according to one embodiment of the present invention, cavitation did not occur at all even without blowing air. The reason for this is, firstly, that the piping has no expanding or decreasing diameter portions, and secondly, since both the inner and outer walls forming the opening are formed in a conical shape, the driving flow at the opening is This seems to be due to the fact that there is no component parallel to the axis, that is, any minute flow mass of the driving flow flows toward the axis of the piping, making it difficult for pressure gradients to occur in the radial direction.
[実施例]
本発明を図面によって説明する。第1図は本発明による
ジェットポンプの一実施例の縦断面図であり、均一な内
径の内筒1の中央後部外周面にはおねじlaが刻設され
ており、内筒1の外面前端1bは、内筒1と軸線を共有
する円錐状に、前端に向って縮径している。[Example] The present invention will be explained with reference to the drawings. FIG. 1 is a longitudinal cross-sectional view of an embodiment of a jet pump according to the present invention, in which a male thread la is carved on the outer peripheral surface of the central rear part of an inner cylinder 1 having a uniform inner diameter, and a front end 1b of the outer surface of the inner cylinder 1 is formed. has a conical shape that shares an axis with the inner cylinder 1, and its diameter decreases toward the front end.
内筒1を嵌入するように配置した外筒2の後部には、内
筒のおねじ1aと螺合するめねじ2aが刻設されており
、内筒のおねし1aにはまた、内筒lと外筒2との上記
螺合のゆるみを防止するためのベアリングナツト3が螺
着している。外筒2の前部は、内筒1と実質的に同一の
内径に形成されており、外筒2の中間部内面前端2bは
、外筒2と軸線を共有する円錐状に、前端に向って縮径
している6内筒の外面前端1bの縮径の角度と、外筒の
中間部内面前端2bの縮径の角度とは、必ずしも同一に
形成する必要はないが、本実施例では同一に形成されて
おり、したがって内筒の外面前l!1ii1bと外筒の
中間部内面前端2bとによって形成される流路の断面積
は、前方に向って縮小することとなる。外筒2の中間部
内面と内筒1外面との間には環状領域4が形成されてお
り、該環状領域4の後部と連通ずるように、駆動流配管
5が取付けられている6
本実施例は以上のように構成されており、ベアリングナ
ツト3によって内筒の外面前端1bと外筒の中間部内面
前端2bとの間の間隔を調節し、駆動流配管5より高圧
流体を流すと、高圧流体は内筒の外面前端1bと外筒の
中間部内面前端2bとの間より流入して駆動流となり、
内筒1内の被駆動流体を駆動する。しかしてこのジェッ
トポンプでは被駆動流体が流れる部分の管径は全て実質
的に同径に形成されているから、被駆動流体が固形物を
含有するときにも固形物による閉塞を招くおそれが全く
ない、また本実施例の実験結果ではキャビテーションは
全く生じなかった。The rear part of the outer cylinder 2, which is arranged to fit the inner cylinder 1, is provided with a female thread 2a that engages with the male thread 1a of the inner cylinder. A bearing nut 3 is screwed into the outer cylinder 2 to prevent loosening of the screw connection between the outer cylinder 2 and the outer cylinder 2. The front part of the outer cylinder 2 is formed to have substantially the same inner diameter as the inner cylinder 1, and the front end 2b of the inner surface of the intermediate part of the outer cylinder 2 has a conical shape that shares an axis with the outer cylinder 2 and extends toward the front end. Although the diameter reduction angle of the outer surface front end 1b of the inner cylinder 6 and the diameter reduction angle of the intermediate inner surface front end 2b of the outer cylinder are not necessarily formed to be the same, in this example, are identically formed and therefore the outer surface of the inner cylinder l! The cross-sectional area of the flow path formed by 1ii1b and the front end 2b of the inner surface of the intermediate portion of the outer cylinder decreases toward the front. An annular region 4 is formed between the inner surface of the intermediate part of the outer cylinder 2 and the outer surface of the inner cylinder 1, and a driving flow pipe 5 is attached so as to communicate with the rear part of the annular region 4. The example is configured as described above, and when the distance between the front end 1b of the outer surface of the inner cylinder and the front end 2b of the inner surface of the intermediate part of the outer cylinder is adjusted by the bearing nut 3, and high pressure fluid is caused to flow from the drive flow pipe 5, The high-pressure fluid flows in from between the front end 1b of the outer surface of the inner cylinder and the front end 2b of the inner surface of the intermediate part of the outer cylinder, and becomes a driving flow.
The driven fluid in the inner cylinder 1 is driven. However, in this jet pump, all pipe diameters in the portion through which the driven fluid flows are formed to have substantially the same diameter, so even when the driven fluid contains solids, there is no risk of blockage due to solids. No, and the experimental results of this example showed that no cavitation occurred at all.
次に内筒の外面前端1bと、外筒の中間部内面前端2b
との円錐状の頂角を同一に形成し、その頂角を20°、
30°及び40°に変更したときの実験結果の一例を第
1表に示す。この実験では第1表
内筒】の内径を呼び径50Aの配管と同径に形成し、こ
のジェットポンプの内筒後端に呼び径50Aの配管を、
外筒前端に呼び径100Aの配管を接続した。第1表か
ら明らかなように、頂角が30°程度のときが被駆動流
体の流量及びポンプ効率がもっとも大きくなり、少なく
とも頂角は20〜40°に形成することが好ましいこと
が解った。Next, the outer front end 1b of the inner cylinder and the inner front end 2b of the intermediate part of the outer cylinder.
The apex angle of the cone is the same as that of 20°,
Table 1 shows an example of the experimental results when the angle was changed to 30° and 40°. In this experiment, the inner diameter of the inner cylinder in Table 1 was formed to be the same diameter as the piping with a nominal diameter of 50A, and the piping with a nominal diameter of 50A was installed at the rear end of the inner cylinder of this jet pump.
A pipe with a nominal diameter of 100A was connected to the front end of the outer cylinder. As is clear from Table 1, when the apex angle is about 30°, the flow rate of the driven fluid and the pump efficiency are the highest, and it was found that it is preferable to set the apex angle to at least 20 to 40°.
[発明の効果]
本発明では配管は実質的に同一の内径に形成されている
から、固形物を含有する流体を搬送するときにも固形物
による閉塞を招くおそれが全くなく、また駆動流は管軸
に平行な成分を持たないから空気導入管を設ける必要が
なく、したがって被駆動流の揚水量の低下を来さないジ
ェットポンプが得られた6[Effects of the Invention] In the present invention, since the pipes are formed to have substantially the same inner diameter, there is no risk of blockage due to solids even when conveying a fluid containing solids, and the driving flow is Since there is no component parallel to the pipe axis, there is no need to provide an air introduction pipe, and therefore a jet pump that does not cause a drop in the pumping amount of the driven flow has been obtained6.
第1図は本発明の一実施例の縦断面図、第2図は従来例
の縦断面図である。
1・・・内筒 1a・・・おねじ 1b・・・外面前端
2・・外筒 2a・・・めねじ 2b・・・中間部内面
前端3・・・ベアリングナツト 4・・・環状領域
5・・・駆動流配管FIG. 1 is a vertical cross-sectional view of one embodiment of the present invention, and FIG. 2 is a vertical cross-sectional view of a conventional example. 1...Inner tube 1a...Male thread 1b...Outer surface front end 2...Outer tube 2a...Female thread 2b...Intermediate inner surface front end 3...Bearing nut 4...Annular region 5 ... Drive flow piping
Claims (4)
と軸線を共有する第1及び第2の円錐形が前記配管と交
差する位置をそれぞれ内壁及び外壁とする環状テーパ状
の開口を前記配管に設け、該開口に駆動流配管を取付け
たジェットポンプ。(1) Pipes having substantially the same inner diameter are provided, and first and second conical shapes that share an axis with the piping have an annular tapered opening whose inner and outer walls are the positions where the piping intersects with the piping, respectively. A jet pump provided in the piping and having a driving flow piping attached to the opening.
じを刻設し、前記内筒の外面前端を該内筒と軸線を共有
する第1の円錐形に縮径し、前記内筒を嵌入する外筒の
後部に前記おねじと螺合するめねじを刻設し、前記外筒
の前部を前記内筒と実質的に同一の内径に形成し、前記
外筒の中間部内面前端を該外筒と軸線を共有する第2の
円錐形に縮径して前記内筒の外面前端と対向配置し、前
記外筒の中間部内面と前記内筒外面との間に環状領域を
形成し、該環状領域の後部を駆動流配管と連通したジェ
ットポンプ。(2) A thread is carved on the outer circumferential surface of an inner cylinder having substantially the same inner diameter, and the front end of the outer surface of the inner cylinder is reduced in diameter into a first conical shape that shares an axis with the inner cylinder; A female thread that engages with the male thread is carved in the rear part of the outer cylinder into which the inner cylinder is inserted, a front part of the outer cylinder is formed to have substantially the same inner diameter as the inner cylinder, and a middle part of the outer cylinder is formed. an annular region between the inner surface of the intermediate portion of the outer cylinder and the outer surface of the inner cylinder; A jet pump having an annular region having a rear portion thereof communicating with a driving flow piping.
に形成した請求項1又は2記載のジェットポンプ。(3) The jet pump according to claim 1 or 2, wherein the first and second conical shapes have substantially the same apex angle.
た請求項3記載のジェットポンプ。(4) The jet pump according to claim 3, wherein the substantially same apex angle is 20 to 40 degrees.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14658890A JPH0441999A (en) | 1990-06-05 | 1990-06-05 | Jet pump |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14658890A JPH0441999A (en) | 1990-06-05 | 1990-06-05 | Jet pump |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0441999A true JPH0441999A (en) | 1992-02-12 |
Family
ID=15411112
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP14658890A Pending JPH0441999A (en) | 1990-06-05 | 1990-06-05 | Jet pump |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0441999A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001056000A (en) * | 1999-08-12 | 2001-02-27 | Yoshihiro Kawasaki | Air jet pump and jet nozzle used therein, and jetting method for jet nozzle |
| JP2006314445A (en) * | 2005-05-11 | 2006-11-24 | San-Ei Faucet Mfg Co Ltd | Nose laveur |
| JP2012502784A (en) * | 2008-09-16 | 2012-02-02 | ビーエーエスエフ ソシエタス・ヨーロピア | Adjustable solid particle delivery system |
-
1990
- 1990-06-05 JP JP14658890A patent/JPH0441999A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001056000A (en) * | 1999-08-12 | 2001-02-27 | Yoshihiro Kawasaki | Air jet pump and jet nozzle used therein, and jetting method for jet nozzle |
| JP2006314445A (en) * | 2005-05-11 | 2006-11-24 | San-Ei Faucet Mfg Co Ltd | Nose laveur |
| JP2012502784A (en) * | 2008-09-16 | 2012-02-02 | ビーエーエスエフ ソシエタス・ヨーロピア | Adjustable solid particle delivery system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4487553A (en) | Jet pump | |
| EP0044494A1 (en) | Nozzle for ring jet pump | |
| CN106122120B (en) | Compound two-stage multichannel gas-liquid jet pump | |
| BRPI0618015A2 (en) | clamping sleeve for an ejector, and mounting procedure | |
| US5429156A (en) | Pneumatic transmission apparatus | |
| EP3163093B1 (en) | High vacuum ejector | |
| US3537543A (en) | Noise muffled air ejector | |
| US20100150742A1 (en) | Reconfigurable jet pump | |
| JPS6325200B2 (en) | ||
| JPH0441999A (en) | Jet pump | |
| JPH10141299A (en) | Ejector for ejecting powder | |
| JPS63262339A (en) | Multi-step coanda spiral flow generating device | |
| CN111306959B (en) | A steam jet heater | |
| CN111558309B (en) | A kind of multi-channel jet and agent adding system | |
| CN213611297U (en) | Improved generation chemical industry tower | |
| JP2021152361A (en) | Aspirator | |
| US4565499A (en) | Ejector | |
| JP3342886B2 (en) | Coanda bend tube | |
| US2668504A (en) | Jet nozzle | |
| US20130256425A1 (en) | Self cleaning eductor | |
| RU2228462C2 (en) | Jet pump | |
| CN205977827U (en) | Composite two-stage multi-channel gas-liquid jet pump | |
| EP4368296A1 (en) | Multi-channel mist head | |
| CN116407986A (en) | Fixed-gap chamber device of high-pressure homogenizer and processing method for difficult-to-disperse materials | |
| CN220294457U (en) | Pipe connection for a mixer and mixer |