CN109630478B - Streamline annular jet pump - Google Patents
Streamline annular jet pump Download PDFInfo
- Publication number
- CN109630478B CN109630478B CN201811440357.6A CN201811440357A CN109630478B CN 109630478 B CN109630478 B CN 109630478B CN 201811440357 A CN201811440357 A CN 201811440357A CN 109630478 B CN109630478 B CN 109630478B
- Authority
- CN
- China
- Prior art keywords
- streamlined
- pipe
- jet pump
- suction chamber
- annular jet
- 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 - Fee Related
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 38
- 238000009792 diffusion process Methods 0.000 claims abstract description 11
- 230000007704 transition Effects 0.000 claims description 17
- 230000004323 axial length Effects 0.000 claims description 3
- 230000008602 contraction Effects 0.000 claims description 2
- 239000007788 liquid Substances 0.000 abstract description 29
- 239000012530 fluid Substances 0.000 abstract description 24
- 238000000034 method Methods 0.000 description 7
- 238000010586 diagram Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000013459 approach Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000005204 segregation Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04F—PUMPING OF FLUID BY DIRECT CONTACT OF ANOTHER FLUID OR BY USING INERTIA OF FLUID TO BE PUMPED; SIPHONS
- F04F5/00—Jet pumps, i.e. devices in which flow is induced by pressure drop caused by velocity of another fluid flow
- F04F5/02—Jet pumps, i.e. devices in which flow is induced by pressure drop caused by velocity of another fluid flow the inducing fluid being liquid
- F04F5/10—Jet pumps, i.e. devices in which flow is induced by pressure drop caused by velocity of another fluid flow the inducing fluid being liquid displacing liquids, e.g. containing solids, or liquids and elastic fluids
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04F—PUMPING OF FLUID BY DIRECT CONTACT OF ANOTHER FLUID OR BY USING INERTIA OF FLUID TO BE PUMPED; SIPHONS
- F04F5/00—Jet pumps, i.e. devices in which flow is induced by pressure drop caused by velocity of another fluid flow
- F04F5/44—Component parts, details, or accessories not provided for in, or of interest apart from, groups F04F5/02 - F04F5/42
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04F—PUMPING OF FLUID BY DIRECT CONTACT OF ANOTHER FLUID OR BY USING INERTIA OF FLUID TO BE PUMPED; SIPHONS
- F04F5/00—Jet pumps, i.e. devices in which flow is induced by pressure drop caused by velocity of another fluid flow
- F04F5/44—Component parts, details, or accessories not provided for in, or of interest apart from, groups F04F5/02 - F04F5/42
- F04F5/46—Arrangements of nozzles
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Fluid Mechanics (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Jet Pumps And Other Pumps (AREA)
Abstract
本发明提供了一种流线型环形射流泵。该流线型环形射流泵是将现有环形射流泵的锥形吸入室、圆柱形喉管和锥形扩散管设计为流线型吸入室和流线型混合管;用流线型连接方式替代原来的折线型连接。从而解决了现有环形射流泵中吸入室与喉管连接处液流产生漩涡造成严重局部水头损失;漩涡中心处低压引起环形射流泵喉管壁面空化、空蚀破坏;喉管中被吸液与工作液不能混合充分造成液流能量损失;喉管与扩散管连接处、扩散管与出水管连接处,混合液突然转向造成局部水头损失。本发明所述流线型环形射流泵较现有环形射流泵工作性能及工作效率具有明显优势,有望在流体机械领域和实际应用中有更进一步推广应用前景。
The invention provides a streamlined annular jet pump. The streamlined annular jet pump is designed by designing the conical suction chamber, cylindrical throat and conical diffusion pipe of the existing annular jet pump into a streamlined suction chamber and a streamlined mixing tube; the original broken line connection is replaced by a streamlined connection. This solves the problem of serious local head loss caused by the vortex generated by the liquid flow at the connection between the suction chamber and the throat pipe in the existing annular jet pump; the cavitation and cavitation damage of the throat surface of the annular jet pump caused by the low pressure at the center of the vortex; Can not fully mix with the working fluid, resulting in loss of fluid flow energy; at the connection between the throat pipe and the diffuser pipe, and the connection between the diffuser pipe and the water outlet pipe, the mixed liquid suddenly turns and causes local head loss. Compared with the existing annular jet pump, the streamlined annular jet pump of the invention has obvious advantages in working performance and working efficiency, and is expected to have further promotion and application prospects in the field of fluid machinery and practical applications.
Description
技术领域technical field
本发明涉及一种射流泵技术,尤其涉及一种流线型环形射流泵,属于流体机械技术领域。The invention relates to a jet pump technology, in particular to a streamlined annular jet pump, which belongs to the technical field of fluid machinery.
背景技术Background technique
射流泵是一种利用高速流体作为工作动力,抽吸、运输流体的输送机械和混合反应设备。射流泵自身没有运动部件,其具有结构简单、安装容易、维护方便、密封性好、工作可靠和成本低廉、便于综合利用等一系列独特的优点。射流泵已被广泛应用于水利、冶金、石油、化工、环境保护、海洋开发、核能利用、航空航天等各领域;特别适合于水下、放射、腐蚀等不宜人员靠近的危险场合。但是由于射流泵内部液流卷吸、混掺,容易产生较大的能量损失,因此其工作效率较低,并且易出现空化、空蚀现象,影响射流泵的运行的同时进一步降低系统的效率,甚至影响整个工作系统的安全运行。Jet pump is a kind of conveying machinery and mixing reaction equipment that uses high-speed fluid as working power to pump and transport fluid. The jet pump itself has no moving parts, and it has a series of unique advantages such as simple structure, easy installation, convenient maintenance, good sealing, reliable operation, low cost, and easy comprehensive utilization. Jet pumps have been widely used in water conservancy, metallurgy, petroleum, chemical industry, environmental protection, marine development, nuclear energy utilization, aerospace and other fields; especially suitable for underwater, radiation, corrosion and other dangerous places that are not suitable for people to approach. However, due to the entrainment and mixing of liquid flow inside the jet pump, it is easy to produce large energy loss, so its working efficiency is low, and cavitation and cavitation are prone to occur, which affects the operation of the jet pump and further reduces the efficiency of the system. , and even affect the safe operation of the entire work system.
射流泵根据其喷嘴和吸水管的位置不同,可分为中心射流泵和环形射流泵两种。环形射流泵的吸水管布置在其管轴中心线处,其环形喷嘴环绕在吸水管管道周围,形成环形射流,如图1所示。所述环形射流泵的高压工作液通过环形喷嘴冲入吸入室,对吸水管中的低压被吸液形成强烈的卷吸作用,两股流体在喉管中剧烈地混掺,经扩散管增压,由出水管排出,从而实现增压过程。现有环形射流泵中吸入室形式为锥形吸入室、喉管形式为圆柱形喉管、扩散管形式为锥形扩散管;同时现有环形射流泵中吸入室、喉管、扩散管、出水管的连接方式均采用折线型连接。环形射流泵的这种结构形式与连接方式存在的不足之处是:第一,在现有环形射流泵中,由于吸入室与喉管的连接处为折线型,导致该处管壁突然转向,高速工作液会脱离壁面流动,喉管中的液流随即填补高速工作液与喉管管壁之间所空出的区域,形成漩涡。漩涡会导致液流内部质点相对运动的加强,使液流内摩擦增加,由于该处工作液流速较快,因此会产生较大的局部水头损失,进而影响环形射流泵输送流体的工作效率。第二,漩涡中心处会形成低压区,导致喉管壁面处离析出微汽泡,随着射流泵出口压力降低、流量比增大,喉管壁面处微汽泡数量不断增加。在工作液与被吸液进行动量交换的同时,喉管内压力逐步升高,喉管壁面处的汽泡溃灭,对喉管壁面会产生空蚀破坏;同时消耗液流的能量,使环形射流泵的性能和运行效率急剧下降,进而缩短射流泵的使用寿命。第三,现有环形射流泵喉管为圆柱形,由于工作液流速较高,为减少管道沿程损失、要求喉管不能太长,因此会导致被吸液与工作液在喉管内混合不充分,喉管出口混合液流动不均匀。第四,在现有环形射流泵中,由于喉管与扩散管、扩散管与出水管的连接处均为折线型,导致这两处管壁突然转向,流线会发生弯曲,同时近壁面混合液流速较高,因此会产生一定的局部水头损失,影响环形射流泵的工作效率。Jet pumps can be divided into central jet pumps and annular jet pumps according to the positions of their nozzles and suction pipes. The suction pipe of the annular jet pump is arranged at the centerline of its tube axis, and its annular nozzle surrounds the suction pipe to form an annular jet, as shown in Figure 1. The high-pressure working fluid of the annular jet pump rushes into the suction chamber through the annular nozzle, forming a strong entrainment effect on the low-pressure sucked liquid in the suction pipe, and the two fluids are vigorously mixed in the throat pipe and pressurized by the diffusion pipe. , discharged from the outlet pipe, so as to realize the pressurization process. In the existing annular jet pump, the suction chamber is in the form of a conical suction chamber, the throat is in the form of a cylindrical throat, and the diffuser is in the form of a conical diffuser; The connection method of the water pipe adopts the broken line connection. The disadvantages of this structure and connection method of the annular jet pump are: first, in the existing annular jet pump, because the connection between the suction chamber and the throat is a broken line, the pipe wall at this place suddenly turns, The high-speed working fluid will flow away from the wall, and the liquid flow in the throat will fill the area vacated between the high-speed working fluid and the throat wall, forming a vortex. The vortex will lead to the strengthening of the relative motion of the particles inside the liquid flow, which will increase the internal friction of the liquid flow. Because the working fluid has a faster flow rate there, a large local head loss will occur, which will affect the working efficiency of the annular jet pump to transport fluid. Second, a low pressure area will be formed at the center of the vortex, resulting in the segregation of micro-bubbles on the wall of the throat. As the outlet pressure of the jet pump decreases and the flow ratio increases, the number of micro-bubbles on the wall of the throat increases continuously. When the working fluid and the sucked fluid exchange momentum, the pressure in the throat gradually increases, the bubbles on the wall of the throat collapse, and cavitation damage will occur to the wall of the throat; at the same time, the energy of the liquid flow is consumed to make the annular jet flow The performance and operating efficiency of the pump drop dramatically, which in turn shortens the life of the jet pump. Third, the throat of the existing annular jet pump is cylindrical. Due to the high flow rate of the working fluid, in order to reduce the loss along the pipeline, the throat should not be too long, which will lead to insufficient mixing of the sucked liquid and the working fluid in the throat. , the flow of the mixture at the outlet of the throat is uneven. Fourth, in the existing annular jet pump, because the joints between the throat pipe and the diffuser pipe, and the diffuser pipe and the water outlet pipe are all broken lines, the two pipe walls suddenly turn, and the streamline will bend, and the near-wall surface will mix. The liquid flow rate is high, so there will be a certain local head loss, which will affect the working efficiency of the annular jet pump.
发明内容SUMMARY OF THE INVENTION
本发明的目的正是为了克服现有环形射流泵结构中所存在的缺陷和不足,提供一种流线型环形射流泵;该流线型环形射流泵是将现有环形射流泵上采用的锥形吸入室、圆柱形喉管和锥形扩散管分别设计为流线型吸入室和流线型混合管;同时将现有环形射流泵中采用的吸入室、喉管、扩散管、出水管的折线型连接方式均设计为流线型的连接方式。从而解决了现有环形射流泵中吸入室与喉管连接处,液流产生漩涡造成的局部水头损失;漩涡中心处的低压引起的环形射流泵喉管壁面空化、空蚀破坏;喉管中被吸液与工作液不能够混合充分造成的液流能量损失;喉管与扩散管连接处、扩散管与出水管连接处,混合液突然转向造成的局部水头损失。The purpose of the present invention is to overcome the defects and deficiencies existing in the existing annular jet pump structure, to provide a streamlined annular jet pump; the streamlined annular jet pump is a conical suction chamber, Cylindrical throat pipe and conical diffuser pipe are designed as streamlined suction chamber and streamlined mixing pipe respectively; at the same time, the polyline connection methods of suction chamber, throat pipe, diffuser pipe and water outlet pipe used in the existing annular jet pump are designed to be streamlined connection method. Therefore, the local water head loss caused by the vortex generated by the liquid flow at the connection between the suction chamber and the throat pipe in the existing annular jet pump is solved; The energy loss of the liquid flow caused by the insufficient mixing of the sucked liquid and the working liquid; the local head loss caused by the sudden turning of the mixed liquid at the connection between the throat pipe and the diffusion pipe, and the connection between the diffusion pipe and the water outlet pipe.
为实现本发明的上述目的,本发明是由以下技术措施构成的技术方案来实现的。In order to achieve the above-mentioned purpose of the present invention, the present invention is realized by a technical solution composed of the following technical measures.
本发明所述一种流线型环形射流泵,包括工作水管,吸水管,环形喷嘴,吸入室,喉管,扩散管和出水管;按照本发明,所述吸入室设计为流线型吸入室;所述喉管和扩散管设计为一体式流线型混合管,即流线型混合管包括流线型喉管和流线型扩散管;且设计一圆弧过渡管将流线型混合管与出水管流线型连接;所述工作水管连接环形喷嘴,环形喷嘴连接所述流线型吸入室,所述吸水管连接流线型吸入室,而流线型吸入室、流线型混合管、圆弧过渡管和出水管依次为流线型连接。The streamlined annular jet pump of the present invention includes a working water pipe, a suction pipe, an annular nozzle, a suction chamber, a throat pipe, a diffuser pipe and a water outlet pipe; according to the present invention, the suction chamber is designed as a streamlined suction chamber; the throat The tube and the diffuser are designed as an integrated streamlined mixing tube, that is, the streamlined mixing tube includes a streamlined throat and a streamlined diffusion tube; and an arc transition tube is designed to streamline the connection between the streamlined mixing tube and the outlet pipe; the working water tube is connected to the annular nozzle, The annular nozzle is connected to the streamlined suction chamber, the water suction pipe is connected to the streamlined suction chamber, and the streamlined suction chamber, the streamlined mixing pipe, the arc transition pipe and the water outlet pipe are sequentially connected in a streamlined manner.
上述技术方案中,所述流线型吸入室内壁面设计为圆弧流线型,所述圆弧起始于环形喷嘴外边缘壁面的出口处并与其壁面相切;所述圆弧末尾处与流线型混合管内壁面相连接并与其内壁面相切。In the above technical solution, the wall surface of the streamlined suction chamber is designed as a circular arc streamlined shape, and the circular arc starts at the outlet of the outer edge wall of the annular nozzle and is tangent to its wall surface; the end of the circular arc is opposite to the inner wall surface of the streamlined mixing tube. connected and tangent to its inner wall.
上述技术方案中,所述流线型吸入室的圆弧流线型中圆弧对应的圆心角角度为α/2,其数学表达式如下:In the above technical solution, the central angle angle corresponding to the circular arc in the circular arc streamline of the streamlined suction chamber is α/2, and its mathematical expression is as follows:
R=L×cot(α/4)R=L×cot(α/4)
式中:α、L分别为已有环形射流泵吸入室的收缩角、长度;R为流线型吸入室的圆弧半径。where α and L are the contraction angle and length of the suction chamber of the existing annular jet pump, respectively; R is the arc radius of the streamlined suction chamber.
上述技术方案中,所述流线型混合管内壁面设计为流线型,所述流线型线形起始于流线型吸入室内壁面的出口处并与其内壁面相切;所述流线型线形末尾处与所述圆弧过渡管内壁面起始处相连接并与其内壁面相切;所述流线型线形的数学表达式如下:In the above technical solution, the inner wall surface of the streamlined mixing pipe is designed to be streamlined, and the streamlined linear shape starts at the outlet of the streamlined suction chamber inner wall surface and is tangent to its inner wall surface; the end of the streamlined linear shape starts from the inner wall surface of the arc transition pipe. connected at the beginning and tangent to its inner wall; the mathematical expression of the streamlined line is as follows:
Ltd=(4~7)Dt β=8°~12° y=±(Dt/2+xn)L td =(4~7)D t β=8°~12° y=±(D t /2+x n )
式中:Ltd为所述流线型混合管的轴向长度;Dt为所述流线型混合管入口处的管道直径;β为流线型混合管出口处的扩散角;y为流线型线形的纵向坐标;x为流线型线形的轴向坐标;n为指数,其取值范围为2.5~5。Where: L td is the axial length of the streamlined mixing tube; D t is the pipe diameter at the inlet of the streamlined mixing tube; β is the diffusion angle at the outlet of the streamlined mixing tube; y is the longitudinal coordinate of the streamlined line; x is the axial coordinate of the streamline; n is the index, and its value ranges from 2.5 to 5.
上述技术方案中,所述圆弧过渡管内壁面设计为圆弧流线型,所述圆弧起始于流线型混合管内壁面末尾处并与其内壁面相切;所述圆弧末尾处与出水管入口处内壁面相连接并与其内壁面相切。In the above technical solution, the inner wall surface of the arc transition pipe is designed as a circular arc streamline, and the arc starts at the end of the inner wall surface of the streamlined mixing pipe and is tangent to its inner wall surface; the end of the arc is in contact with the inner wall surface of the inlet of the water outlet pipe. connected and tangent to its inner wall.
本发明所述流线型环形射流泵,具有以下优点和有益的技术效果:The streamlined annular jet pump of the present invention has the following advantages and beneficial technical effects:
1、本发明所述流线型环形射流泵,将现有环形射流泵的锥形吸入室设计为流线型吸入室,将圆柱形喉管和锥形扩散管设计为流线型混合管;用流线型连接方式替代现有的折线型连接;在流线型吸入室与流线型混合管连接处,高速工作液沿壁面平顺流动,避免发生分离流动形成漩涡,可以减小局部水头损失,进而有助于改善环形射流泵的工作性能。1. The streamlined annular jet pump of the present invention, the conical suction chamber of the existing annular jet pump is designed as a streamlined suction chamber, and the cylindrical throat pipe and the conical diffuser pipe are designed as a streamlined mixing tube; Some folded-line connections; at the connection between the streamlined suction chamber and the streamlined mixing pipe, the high-speed working fluid flows smoothly along the wall to avoid separation and flow to form vortices, which can reduce the local head loss and help improve the working performance of the annular jet pump .
2、本发明所述流线型环形射流泵,其射流泵内的高速工作液在流线型吸入室与流线型混合管连接处不会脱离壁面流动,从而消除了局部低压区,可避免因边界突变导致的环形射流泵壁面空化、空蚀破坏。2. According to the streamlined annular jet pump of the present invention, the high-speed working fluid in the jet pump will not flow away from the wall at the connection between the streamlined suction chamber and the streamlined mixing pipe, thereby eliminating the local low pressure area and avoiding the annular shape caused by the sudden change in the boundary. Cavitation and cavitation damage on the wall of the jet pump.
3、本发明所述流线型环形射流泵,所述流线型混合管中,由于混合液沿壁面平顺流动,可以减小局部水头损失,也有助于提升环形射流泵的工作效率;同时流线型混合管中的被吸液与工作液可以较为充分地混合,因而使出口混合液流动更加均匀,从而减小混合液扩散损失。3. In the streamlined annular jet pump of the present invention, in the streamlined mixing tube, since the mixed liquid flows smoothly along the wall surface, the local water head loss can be reduced, and the working efficiency of the annular jet pump can also be improved; The aspirated liquid and the working liquid can be more fully mixed, so that the mixed liquid at the outlet flows more uniformly, thereby reducing the diffusion loss of the mixed liquid.
4、本发明所述流线型环形射流泵,所述流线型混合管与出水管的连接方式为流线型连接,进而混合管中的混合液可沿圆弧过渡管壁面平顺流入出水管,避免在该处混合液流向急剧变化导致的局部水头损失,同时也有助于改善环形射流泵的工作性能。4. In the streamlined annular jet pump of the present invention, the connection between the streamlined mixing pipe and the water outlet pipe is streamlined connection, and the mixed liquid in the mixing pipe can smoothly flow into the water outlet pipe along the wall of the arc transition pipe to avoid mixing there. The local head loss caused by the sudden change of liquid flow direction also helps to improve the working performance of the annular jet pump.
5、本发明所述流线型环形射流泵,与现有环形射流泵相比较,由于改变原吸入室和扩散管的锥形结构、喉管的圆柱形结构为流线型结构,以及改变原吸入室、喉管、扩散管、出水管的折线型连接方式为流线型连接方式;并且现有的数控加工技术是可以实现的,使本发明的流线型环形射流泵的工作性能改善具有明显优势,有望在流体机械领域和实际应用中有更进一步的推广应用前景。5. Compared with the existing annular jet pump, the streamlined annular jet pump of the present invention has a The broken line connection mode of the pipe, the diffuser pipe and the water outlet pipe is a streamlined connection mode; and the existing numerical control processing technology can be realized, so that the streamlined annular jet pump of the present invention has obvious advantages in improving the working performance, and is expected to be used in the field of fluid machinery. And there are further promotion and application prospects in practical applications.
附图说明Description of drawings
图1为已有环形射流泵的剖面结构示意图;Fig. 1 is the sectional structure schematic diagram of the existing annular jet pump;
图2为本发明所述流线型环形射流泵的剖面结构示意图;Fig. 2 is the sectional structure schematic diagram of the streamlined annular jet pump of the present invention;
图3为图2中所述流线型环形射流泵的流线型混合管的放大剖面结构示意图。FIG. 3 is an enlarged cross-sectional structural schematic diagram of the streamlined mixing tube of the streamlined annular jet pump in FIG. 2 .
图中:1工作水管;2吸水管;3环形喷嘴;4吸入室;5流线型吸入室;6喉管;7扩散管;8流线型混合管;9圆弧过渡管;10出水管。In the figure: 1 working water pipe; 2 suction pipe; 3 annular nozzle; 4 suction chamber; 5 streamlined suction chamber; 6 throat pipe; 7 diffusion pipe; 8 streamlined mixing pipe; 9 arc transition pipe; 10 water outlet pipe.
具体实施方式Detailed ways
下面结合附图并通过具体实施例对本发明做进一步的详细说明,但并不意味着是对本发明保护范围的任何限定。The present invention will be further described in detail below with reference to the accompanying drawings and specific embodiments, but it is not intended to limit the protection scope of the present invention.
本发明所述流线型环形射流泵,其剖面结构如图2所示,包括工作水管1,吸水管2,环形喷嘴3,流线型吸入室5,包括喉管和扩散管为一体式的流线型混合管8,圆弧过渡管9和出水管10;所述工作水管1连接环形喷嘴3,环形喷嘴3连接所述流线型吸入室5,所述吸水管2连接流线型吸入室5,而流线型吸入室5、流线型混合管8、圆弧过渡管9和出水管10依次为流线型连接。The streamlined annular jet pump of the present invention has a cross-sectional structure as shown in Figure 2, including a working water pipe 1, a
所述流线型吸入室5壁面设计为圆弧流线型,所述圆弧起始于环形喷嘴3外边缘壁面的出口处并与其壁面相切,所述圆弧末尾处与流线型混合管8内壁面相连接并与其内壁面相切;所述流线型混合管8内壁面设计为流线型,所述流线型线形起始于流线型吸入室5的出口处并与其内壁面相切,所述流线型线形末尾处与所述圆弧过渡管9中圆弧内壁面起始处相连接并与其内壁面相切;所述流线型混合管8与出水管10之间采用圆弧过渡管9相连接,所述圆弧起始于流线型混合管8内壁面的末尾处并与其内壁面相切,所述圆弧末尾处与出水管10入口处内壁面相连接并与其内壁面相切。The wall surface of the streamlined suction chamber 5 is designed as a circular arc streamlined shape, the circular arc starts at the outlet of the outer edge wall surface of the
图3中,由于将喉管和扩散管设计为一体式的流线型混合管8,所述流线型混合管内壁面设计为流线型,因此混合液可以沿流线型混合管壁面平顺流动,可以减小局部水头损失,有助于提升环形射流泵的工作效率。In Fig. 3, since the throat and the diffuser are designed as an integrated
实施例Example
根据现有环形射流泵实验研究的结果,结合本实施例采用所述流线型环形射流泵工作时,其吸入室4收缩角取为α=20°,射流泵面积比即流线型混合管8入口面积与环形喷嘴3出口面积的比值取为2.22;吸水管2直径取为44mm。According to the experimental research results of the existing annular jet pump, when the streamlined annular jet pump is used in combination with the present embodiment, the constriction angle of the suction chamber 4 is taken as α=20°, and the area ratio of the jet pump, that is, the inlet area of the
所述流线型吸入室5中圆弧所对圆心角角度取为10°,所述吸入室4中吸入室长度L取为43mm,根据前述流线型吸入室5圆弧流线型中圆弧对应的数学表达式R=L×cot(α/4),可得其圆弧半径R取为491.5mm;所述流线型混合管8入口处直径Dt取为40mm;根据前述流线型线形的数学表达式中Ltd=(4~7)Dt,结合实际经验可得流线型混合管8的轴向长度Ltd取为200mm,根据前述流线型线形的数学表达式中β=8°~12°,结合实际经验可得流线型混合管8出口处的扩散角取为β=10°,所述流线型线形的数学表达式y=±(Dt/2+xn)中指数n取为3.25,根据该数学表达式可得流线型混合管8出口处直径Dtd为50.8mm;所述圆弧过渡管9连接流线型混合管8与出水管10;出水管10直径取为60mm。The central angle of the arc in the streamlined suction chamber 5 is taken as 10°, and the suction chamber length L in the suction chamber 4 is taken as 43mm. According to the mathematical expression corresponding to the arc in the aforementioned streamlined suction chamber 5 arc streamlined R=L×cot(α/4), it can be obtained that its arc radius R is taken as 491.5mm; the diameter D t at the inlet of the
本实施例所述流线型环形射流泵的工作过程如下:The working process of the streamlined annular jet pump described in this embodiment is as follows:
如图2所示结构的流线型环形射流泵,该流线型环形射流泵工作时,其高速工作液经环形喷嘴3喷射,喷射出的工作液卷吸吸水管2中的被吸液并且与被吸液在流线型吸入室5相接触,然后沿流线型吸入室壁面平顺进入流线型混合管8并在流线型混合管内混合、进行能量交换,同时逐步使混合液速度降低、压力升高,之后混合液沿圆弧过渡管9壁面平顺进入出水管10,最后经出水管排出。The streamlined annular jet pump with the structure shown in Figure 2, when the streamlined annular jet pump works, its high-speed working fluid is sprayed through the
通过本实施例,所述流线型环形射流泵在流线型吸入室与流线型混合管以流线型方式的连接处,使高速工作液沿壁面平顺流动,从而避免漩涡形成,可以减小局部水头损失,有助于改善环形射流泵的工作性能,以及提升环形射流泵的工作效率;同时环形射流泵内的高速工作液在流线型吸入室与流线型混合管的流线型连接处不会脱离壁面流动,从而消除了局部低压区,可避免因边界突变导致的环形射流泵壁面空化、空蚀破坏,因此有助于提升环形射流泵的空化性能,延长射流泵的使用寿命;所述流线型混合管中的被吸液与工作液可以较为充分地混合,使混合管出口混合液流动更加均匀;此外由于流线型混合管与出水管的连接方式以流线型连接方式替代现有的折线型连接,因而流线型混合管中的混合液可以沿圆弧过渡管壁面平顺流入出水管,从而减小在该处存在的局部水头损失,同样有助于改善环形射流泵的工作性能和提升环形射流泵的工作效率。Through this embodiment, the streamlined annular jet pump makes the high-speed working fluid flow smoothly along the wall at the connection between the streamlined suction chamber and the streamlined mixing tube in a streamlined manner, thereby avoiding the formation of vortices, reducing local head loss, and helping Improve the working performance of the annular jet pump and improve the working efficiency of the annular jet pump; at the same time, the high-speed working fluid in the annular jet pump will not flow away from the wall at the streamlined connection between the streamlined suction chamber and the streamlined mixing tube, thus eliminating the local low pressure area. , which can avoid the cavitation and cavitation damage of the annular jet pump wall caused by the sudden change of the boundary, so it helps to improve the cavitation performance of the annular jet pump and prolong the service life of the jet pump; The working fluid can be fully mixed, so that the mixed liquid at the outlet of the mixing tube flows more uniformly; in addition, because the connection between the streamlined mixing tube and the water outlet pipe is replaced by the existing broken line connection, the mixed liquid in the streamlined mixing tube can be The water flows smoothly into the outlet pipe along the wall of the arc transition pipe, thereby reducing the local head loss there, which also helps to improve the working performance of the annular jet pump and the working efficiency of the annular jet pump.
Claims (5)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811440357.6A CN109630478B (en) | 2018-11-29 | 2018-11-29 | Streamline annular jet pump |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811440357.6A CN109630478B (en) | 2018-11-29 | 2018-11-29 | Streamline annular jet pump |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN109630478A CN109630478A (en) | 2019-04-16 |
| CN109630478B true CN109630478B (en) | 2020-08-14 |
Family
ID=66069714
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811440357.6A Expired - Fee Related CN109630478B (en) | 2018-11-29 | 2018-11-29 | Streamline annular jet pump |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109630478B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN119862665A (en) * | 2024-12-27 | 2025-04-22 | 河海大学 | Venturi device based on vortex analysis and optimal design method |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE4103050A1 (en) * | 1991-02-01 | 1992-08-06 | Koerting Ag | Gas jet pump - has high temperature resistant internal ceramic lining |
| GB2355218A (en) * | 1999-10-12 | 2001-04-18 | Newteam Ltd | Shower water flow booster unit |
| CN201297296Y (en) * | 2008-11-27 | 2009-08-26 | 江苏振华泵业制造有限公司 | Streamline diffusing pipe jet pump |
| CN103233925A (en) * | 2013-04-23 | 2013-08-07 | 武汉大学 | Efficient multi-functional annular jet pump |
| CN203441837U (en) * | 2013-08-27 | 2014-02-19 | 杭州传奇环保工程有限公司 | Jet flow anti-drag energy-saving device |
-
2018
- 2018-11-29 CN CN201811440357.6A patent/CN109630478B/en not_active Expired - Fee Related
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE4103050A1 (en) * | 1991-02-01 | 1992-08-06 | Koerting Ag | Gas jet pump - has high temperature resistant internal ceramic lining |
| GB2355218A (en) * | 1999-10-12 | 2001-04-18 | Newteam Ltd | Shower water flow booster unit |
| CN201297296Y (en) * | 2008-11-27 | 2009-08-26 | 江苏振华泵业制造有限公司 | Streamline diffusing pipe jet pump |
| CN103233925A (en) * | 2013-04-23 | 2013-08-07 | 武汉大学 | Efficient multi-functional annular jet pump |
| CN203441837U (en) * | 2013-08-27 | 2014-02-19 | 杭州传奇环保工程有限公司 | Jet flow anti-drag energy-saving device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN109630478A (en) | 2019-04-16 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101830278B (en) | Serial axial-flow water jet propulsion pump | |
| CN201949953U (en) | High-efficiency energy-saving nozzle and steam injection pump with nozzle | |
| CN106064122B (en) | Sawtooth jet type evacuator | |
| CN104632216B (en) | Bulb apparatus are produced in the self-priming short distance reinforcing of rotating jet for coal-winning machine dust suppression | |
| CN108204382B (en) | Composite jet pump based on combination of central jet flow and annular jet flow | |
| CN201050511Y (en) | Jet pump used in wet desulfurization forced oxidation | |
| CN104772239A (en) | Supersonic speed chrysanthemum-shaped nozzle and gas jet vacuum pump provided with same | |
| CN107269544A (en) | A kind of jet pump | |
| CN201045359Y (en) | A Liquid Jet Pump with Reduced Vibration and Noise | |
| CN109630478B (en) | Streamline annular jet pump | |
| Liu et al. | Effect of sand diameter on the performance of annular jet pumps | |
| CN222989241U (en) | Pipeline mixer of ash conveying system | |
| CN210919593U (en) | Jet pump capable of automatically and uniformly supplementing air and reducing corrosion | |
| CN109404349B (en) | Spiral-flow type jet pump | |
| WO2010054534A1 (en) | Mixing apparatus for ship flow-guiding propulsion system | |
| CN114349110A (en) | A Rotary Hydraulic Cavitation Device that Continues and Stably Produces Cavitation | |
| CN104265697B (en) | Jet pump | |
| CN218902267U (en) | Micro-nano bubble flow guiding structure | |
| CN204553358U (en) | A kind of high pressure annular jet pump being applicable to turbopump-feed system | |
| CN108704599B (en) | Heterogeneous reaction device | |
| CN110685964A (en) | A Jet Pump for Automatic and Uniform Air Supplementation and Corrosion Reduction | |
| CN213451033U (en) | Preposition device for improving cavitation performance of water pump | |
| CN202185267U (en) | Hydraulic cutting type in-ground leaching agent oxygen mixing device | |
| CN206090699U (en) | Full -automatic gas -liquid replacement variable cross section siphon rivers generating device | |
| CN207361901U (en) | Injector aerator with guide vane |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20200814 Termination date: 20211129 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
