CAVITATION AND SUCTION VORTICES BEHAVIOR
小学上册第十四次英语第1单元期中试卷(有答案)

小学上册英语第1单元期中试卷(有答案)英语试题一、综合题(本题有100小题,每小题1分,共100分.每小题不选、错误,均不给分)1.The chemical symbol for nickel is _____.2.I make _____ (晚餐) for my family.3.We are going to the ___. (beach) this summer.4.The rabbit hops over the ______.5.What do you call a collection of poetry published together?A. AnthologyB. CollectionC. VolumeD. Book答案: A6. A _______ (小鲸鱼) can sing songs underwater.7. A _____ (植物研究计划) can address global challenges.8.I enjoy making ________ (生日蛋糕) for friends.9.My mom is a great __________ (家长) who supports us.10.The __________ (悬崖) is dangerous but beautiful.11. A __________ is a type of chemical bond formed by sharing electrons.12. A saturated fat is ______ at room temperature.13.My grandpa enjoys gardening ____.14.My teacher is _______ (友好的).15.Solids have tightly packed ______.16.The classroom is _____ (clean/dirty).17.What do you call the process of plants making their own food?A. PhotosynthesisB. RespirationC. FermentationD. Transpiration答案:A18.We have a ______ (丰富的) calendar of events.19. A jellyfish has a gelatinous ______ (身体).20._____ (温带) plants can survive in seasonal changes.21.My dad is a strong __________ (支持者) of my education.22. A cat's purring can soothe ______ (焦虑) feelings.23.The antelope gracefully moves through the grasslands, a testament to speed and ____.24.My aunt is very _______ (形容词). 她总是 _______ (动词).25.Many flowers are ______ (一年生) and die after one season.26.The capital of the Cayman Islands is __________.27.I enjoy playing in the ______ (秋天) leaves when they turn bright ______ (颜色).28.They are ___ a movie. (watching)29.I enjoy ______ (探索) the world around me.30.The element with the chemical symbol Fe is _______.31.I find _____ (乐趣) in reading.32.The chemical formula for silver acetate is _______.33. (Renaissance) artists were supported by wealthy patrons. The ____34.I have _____ (three/four) pets.35.What is the coldest season of the year?A. SpringB. SummerC. FallD. Winter答案:D.Winter36.What is the name of the sweet food made from chocolate and cream?A. GanacheB. FrostingC. MousseD. Pudding答案: C37. A ____(community development) focuses on improving living conditions.38.The process of combining elements to form compounds is called ______.39. A hamster can run for hours on its ______ (轮子).40. A __________ is a common example of a base.41.The museum is very _______ (有教育意义的).42.What is the main ingredient in sushi?A. NoodlesB. RiceC. BreadD. Potatoes答案: B43.I can ______ (dance) with my friends.44.What is the name of the famous landmark in the USA?A. Statue of LibertyB. Washington MonumentC. Golden Gate BridgeD. All of the above答案: D. All of the above45.She is a friendly ________.46.I want a pet _______ (fish).47.I like to _______ (paint) with watercolors.48. A __________ is a narrow valley.49.The __________ helps some animals to glide through the air.50.The chemical formula for boric acid is ______.51.The playground is ________ (适合孩子们).52.She is a _____ (历史学家) who studies ancient civilizations.53.I go to school by ______.54.What is the name of the famous painting by Van Gogh?A. The Starry NightB. The ScreamC. Girl with a Pearl EarringD. The Mona Lisa答案:A.The Starry Night55.The chemical name for HO is _______.56.What do we call the famous American holiday celebrated on July 4th?A. ThanksgivingB. Independence DayC. Memorial DayD. Labor Day 答案:B58.The ancient Egyptians kept _______ as pets. (猫)59.The ancient Romans had a system of laws known as ________.60.The ancient Romans built _____ to celebrate their victories.61.I love to explore ________ (村庄) during vacations.62.I think animals are very _______ (形容词). They bring joy and _______ (快乐) to our lives.63. A __________ is a small body of water, usually smaller than a lake.64. (Magna Carta) was signed in 1215 to limit the power of the king. The ____65.The ancient Greeks believed in the importance of ________ (艺术).66.What is 60 ÷ 3?A. 15B. 20C. 25D. 30答案:b67.What do you call the person who helps you in a gym?A. TrainerB. ChefC. DoctorD. Teacher答案: A68.The apples are _______ (ripe) and ready to eat.69. A ______ has a unique pattern on its fur.70. (18) is the imaginary line that divides the Earth into northern and southern halves. The ____71.The chemical formula for magnesium oxide is _____.72.Which animal lives in a den?A. WolfB. EagleC. FishD. Frog答案:A73.The penguin waddles across the ______ (冰).74.My mom enjoys __________ (与朋友聚会).75.In _____ (日本), sushi is a popular dish.76.My brother is my best _______ who plays games with me.78.In the garden, I planted _____ (多种) vegetables like carrots and tomatoes.79.The ______ teaches us about climate change.80.Carbon dioxide is produced when we __________ (呼吸).81.The crow is known for its ________________ (智慧).82. A squirrel's diet consists mainly of ______ (坚果) and grains.83.The chemical formula for glucose is ______.84.The chemical symbol for promethium is _____.85.How many colors are in a standard rainbow?A. 5B. 6C. 7D. 8答案:C86.n Wall fell in _____. The Berl87.The reaction between an acid and a base produces ______.88.The forecast says it might ______ (下雨) this evening.89.My teacher teaches us . (我的老师教我们。
小学下册第十四次英语第六单元测验试卷

小学下册英语第六单元测验试卷英语试题一、综合题(本题有50小题,每小题1分,共100分.每小题不选、错误,均不给分)1 The water cycle involves the processes of evaporation, condensation, and ______.2 The nurse supports patients' _____ (健康) and well-being.3 What is the name of the process by which plants lose water through their leaves?a. Photosynthesisb. Transpirationc. Respirationd. Evaporation答案:b4 I want to _______ (了解)生态系统.5 What is the color of a typical carrot?A. GreenB. OrangeC. YellowD. Red答案:B6 __________ are used in the production of cosmetics.7 What is the capital of Japan?a. Beijingb. Tokyoc. Seould. Bangkok答案:b8 What is the term for a baby lobster?a. Fryb. Larvac. Pupad. Juvenile答案:b9 What do we call the study of human societies and cultures?a. Anthropologyb. Sociologyc. Psychologyd. Geography答案:a10 The cake is _____ for the party. (ready)11 What do we call a sweet food typically eaten for breakfast?A. PancakeB. WaffleC. MuffinD. All of the above12 A _______ can help to visualize the principles of magnetism.13 A compound that can donate electrons is called an ______.14 Astronauts experience weightlessness due to being in free ______.15 A ______ reaction absorbs heat from the surroundings.16 A ______ is a cold-blooded animal that lives in water.17 The chemical formula for arachidic acid is ______.18 The __________ (植物的形态与结构) varies widely among species.19 We have a ______ (充满乐趣的) sports day at school.20 The __________ (古代文明) often engaged in trade with each other.21 In my garden, there are many ________ (花). The ________ (玫瑰) smell very good.22 A group of wolves is called a ______.23 A tectonic plate boundary where plates collide is called a ______ boundary.24 What do you call a young chicken?A. CubB. ChickC. DucklingD. Gosling25 What is the name of the famous landmark in Paris?A. ColosseumB. Eiffel TowerC. Statue of LibertyD. Big Ben答案: B26 The _____ (弹珠) are colorful and fun to play with.27 The __________ (历史的价值观念) evolve with society.28 My brother is interested in ____ (engineering).29 What do we call a person who translates languages?A. InterpreterB. TranslatorC. LinguistD. Polyglot30 My friend is very ________.31 What is the capital of Kenya?A. NairobiB. KampalaC. Addis AbabaD. Dar es Salaam答案:A32 Which vegetable is known for making people cry?A. CarrotB. OnionC. PotatoD. Lettuce答案: B. Onion33 The __________ (环境保护) is everyone's responsibility.34 The _____ (fire) is warm.35 The ________ (水资源管理) is critical for sustainability.36 The __________ are very clear tonight. (星星)37 Penguins are birds that cannot __________.38 My family has a ________ that we take care of.39 My ________ (朋友) is planning a birthday party this weekend.40 What is the sound of a frog?A. RibbitB. QuackC. BarkD. Chirp41 The __________ (历史的理解) fosters empathy.42 The playground is ___. (fun)43 What do bees make?A. ButterB. HoneyC. JamD. Syrup答案:B. Honey44 The ________ (气候带) varies across different regions.45 What do we call the person who teaches in school?A. DoctorB. TeacherC. ChefD. Artist46 Which planet is known for its strong winds and storms?A. EarthB. SaturnC. JupiterD. Venus47 We can _______ (一起) watch a movie.48 I like to watch the ______ (云彩) change shapes.49 The main component of natural gas is _______.50 We are going to the ___. (concert) tonight.51 In winter, it often ________ (下雪). I like to make a ________ (雪人) and have snowball ________ (战争) with my friends.52 My aunt makes __________ for us. (蛋糕)53 I love to collect ______ (邮票) from different countries.54 Which animal is known for its striped fur?A. LionB. TigerC. BearD. Leopard答案: B. Tiger55 George Washington led the American _______ War.56 What do we call a person who studies stars?A. BiologistB. AstronomerC. GeologistD. Chemist57 The sky is clear and ______ (蓝色) today.58 A chemical change usually cannot be __________ back easily.59 The ____ is known for its colorful feathers and can talk.60 The teacher cultivates ______ (创造力) in her classroom.61 The tree has many ______.62 Dwarf planets include Pluto, Eris, and ______.63 The peacock has beautiful _______ (羽毛).64 What is the main ingredient in a smoothie?A. MilkB. YogurtC. FruitD. All of the above答案:D65 Which season comes after winter?A. SpringB. SummerC. AutumnD. Fall66 I enjoy attending concerts because I love listening to __________ live.67 A reaction that produces a solid precipitate indicates a ______ change.68 What is the term for an animal that only eats meat?A. HerbivoreB. CarnivoreC. OmnivoreD. Insectivore答案: B69 The capital of Antigua is __________.70 A ____(community safety initiative) promotes public well-being.71 My ______ travels around the world for work.72 What is the capital city of Burkina Faso?A. OuagadougouB. Bobo DioulassoC. BanforaD. Koudougou73 I love going to science fairs to see innovative __________.74 We go to bed at ___ (eight/nine).75 My _____ (爷爷) loves to garden. He grows vegetables and flowers. 我爷爷喜欢园艺。
A sharp interface approach for cavitation modeling using volume-of-fluid and ghost-fluid methods

9172017,29(6):917-925DOI: 10.1016/S1001-6058(16)60806-5A sharp interface approach for cavitation modeling using volume-of-fluid and ghost-fluid methods *Thad Michael 1, Jianming Yang 2, Frederick Stern 31. NSWC Carderock Division, 9500 MacArthur Blvd., West Bethesda, MD 20817, USA, E-mail:thad.michael@2. Fidesi Solutions LLC, PO Box 734, Iowa City, IA 52244, USA3. IIHR -Hydroscience and Engineering, University of Iowa, Iowa City, IA 52242, USA(Received September 20, 2017, Revised September 22, 2017)Abstract: This paper describes a novel sharp interface approach for modeling the cavitation phenomena in incompressible viscous flows. A one-field formulation is adopted for the vapor-liquid two-phase flow and the interface is tracked using a volume of fluid (VOF) method. Phase change at the interface is modeled using a simplification of the Rayleigh-Plesset equation. Interface jump conditions in velocity and pressure field are treated using a level set based ghost fluid method. The level set function is constructed from the volume fraction function. A marching cubes method is used to compute the interface area at the interface grid cells. A parallel fast marching method is employed to propagate interface information into the field. A description of the equations and numerical methods is presented. Results for a cavitating hydrofoil are compared with experimental data.Key words: Incompressible flow, two-phase flow, cavitation modeling, sharp interface method, ghost fluid method, volume of fluid method, level set method, parallel fast marching method, marching cubes methodIntroductionCavitation is the term for the change of state from liquid to vapor when it is caused by a low- pressure region within the flow field at an ambient temperature. Although the physical mechanism is the same, in contrast the term boiling is used to describe the change of state from liquid to vapor when it is caused by a local increase in temperature at the ambient pressure. For cavitation, the phase change rate is governed by the local pressure, while for boiling it is governed by the local temperature.Cavitation degrades the performance of lifting surfaces found on ships, such as propeller blades and rudders. In addition to reducing lift, the violent collapse of cavitation bubbles can also remove mate- rial leading to further degradation and possible failure.Potential flow cavitation models have been deve- loped for propellers in Refs.[1,2]. The cavity is treated* Biography: Thad Michael (1975-), Male, Ph. D., Naval ArchitectCorresponding author: Jianming Yang, E-mail: jmyang@as additional thickness and the location is solved iteratively. A number of cavitation models for viscous flows have been developed, primarily for homogenous mixture models. Some examples are Refs.[3,4]. A more recent model in Ref.[5] adds the effect of non- condensable gas within the bubbles. Recent compu- tations in Refs.[6-9] using models of this type have compared well with hydrofoil experiments. For visua- lization, the cavity interface is assumed to be at a constant volume fraction, typically 0.5. For summaries of recent research on cavitation models, especially, homogeneous mixture models, and their applications, the reader is referred to [10-13].Sharp interface phase change models have been used to compute film boiling in Refs.[14,15]. Here we seek to apply similar techniques to the problem of cavitation, with the development of a suitable model for phase change due to cavitation.The focus of this paper is the development of a model for predicting the phase change rate suitable for use with a sharp interface and the necessary models and methods to support this combination. The model is implemented in a two-phase incompressible viscous flow solver with a sharp interface approach. Results918are presented for a cavitating hydrofoil. The results are analyzed to reveal details of the physics of the reentrant jet and cavity shedding. The averaged results are compared with experimental data.1. Mathematical model1.1 Incompressible viscous flowThe Navier-Stokes equations for the incom- pressible viscous flow of the liquid and vapor phases are written as follows:=0∇⋅u (1)1+(+)+u p t ρ∂⋅∇-∇⋅-∂I u u T g(2)where I is the identity matrix and=μT S(3)where μ is the viscosity of the fluid andT 1=[+()]2∇∇S u u(4)1.2 Phase changeWith phase change, a volume source must be added due to the different densities of liquid and vapor. The volume source satisfies the requirement for mass conservation and results in a jump in the fluid velocity at the interface so that Eq.(1) becomes11=lv m ρρ⎛⎫∇⋅- ⎪⎝⎭ u (5)where mis the mass flux between phases and the subscripts l and v stand for liquid and vapor, res- pectively.1.3 Interface trackingA volume of fluid (VOF) method described in Ref.[16] with the addition of a velocity component due to phase change is used to track the interface posi- tion. Without phase change, the boundary between liquid and vapor moves with a velocity which is con- tinuous across the interface. Phase change introduces a velocity discontinuity at the interface which is pro- portional to the phase change rate and the difference in density across the interface. The VOF equation is +=0FF T ∂∇⋅∂U(6) where U is the interface velocity, defined relative to the local liquid or vapor velocity by=+f mρ fn U u(7)where f u is the fluid velocity, and ρf is the fluid density and f is liquid or vapor. This satisfies the conservation of mass between the phases at the interface.1.4 Modeling mass flux between phasesThe rates of vaporization and condensation are determined by a simplification of the Rayleigh-Plesset equation which assumes a spherical bubble subject to uniform pressure variations320vap 032=+42l g R S R RR +R p p p R R R γρμ∞⎛⎫⎛⎫--- ⎪ ⎪⎝⎭⎝⎭(8)where vap p is the vapor pressure, 0g p is the initial partial pressure of non-condensable gasses, 0R is the initial radius of the bubble, S is the surface tension, and γ is the ratio of the gas heat capacities. The third term on the right-hand side represents the effect of the non-condensable gasses. The last two terms on the right represent the effects of surface tension and viscosity, respectively.The surface tension can be neglected for all but the smallest bubbles and the viscous effects can be neglected for the Reynolds numbers of interest in ship flows. By also neglecting the non-condensable gasses, the equation can be integrated with respect to time and simplified to yield=R(9)This simplification is the foundation of several ca- vitation models used with two-phase mixture models where further assumptions about bubble number or size are utilized to arrive at a surface area and mass flux.With a sharp interface method, the bubble must be larger than the cell to be accurately modeled. If the radius is sufficiently large, it is reasonable to represent it by a plane within the cell, as in the volume of fluid method. Then, the velocity is=lmρ n(10)919where n is the interface normal. Because a local pressure will be used in place of the far field pressure, a constant is needed for correlation. With this addition, and a simplification, the mass flux can be expressed:=m C ,vapp p <(11a)=m C ,vapp p ≥(11b)where e C and c C are the coefficients of evapora- tion and condensation, respectively. See Ref.[17] for a more detailed derivation.2. Numerical methods2.1 Flow solverThe CFD code CFDShip-Iowa v6.2[18] is the foundation for this development. It is an incom- pressible Navier-Stokes solver utilizing an orthogonal curvilinear grid. The velocity components are defined at the centers of cell faces while other quantities are defined at the cell centers. A finite difference approach is used, except for the pressure Poisson equation which is solved with a finite volume approach. For cavitation modeling, a first-order Euler method is used for time advancement for simplicity. Hypre library [19] is used for the parallel solution of the Poisson equation. With the volume source due to phase change, the Poisson equation is+1111()=+n i i i i vl u Grad p m x t x ρρ*⎡⎤⎛⎫∂∂-⎢⎥ ⎪∂∆∂⎢⎥⎝⎭⎣⎦ (12)where ()i Grad p is collocated with the velocity com- ponents and incorporates the jump conditions due to surface tension and gravity as described in Ref.[20]. For stability, the phase change rate from Eq.(11) is modeled semi-implicitly, as described in Ref.[17], resulting in this pressure Poisson equation+1+11()=n n i i ii Ep u Grad p x t x *⎛⎫∂∂∂∆∂ ⎝(13)where E is a constant related to the fluid densities1=v E ρ⎛- ⎝(14) For the momentum equation, a ghost fluid method is employed. This method was also used in Refs.[14,15] to model boiling with a sharp interface phase change model. CFDShip-Iowa v6.2 includes surface tension, density, and viscosity changes at the interface [20]. The ghost fluid method is used only to account for the velocity jump normal to the interface due to the volume source.Fig.1 Hydrofoil geometry with six-degree angle-of-attackFig.2 Leading edge of the foil and grid resolutionFig.3 Pressure distribution on the foil without cavitation, 2-D calculation. Experimental data is from Ref.[23]A parallel fast marching method developed in Ref.[21] was also modified to extend the velocity components from one side of the interface to the other such that the velocity normal to the interface is constant. The extended velocity field is not conser- vative. However, only the extended values that are close to the interface are used to solve the momentum equation in the phase of interest and the approxima- tion is reasonable near the interface. The momentum equation is solved separately for each phase and the intermediate velocity fields are then combined using the level set function to discriminate between phases.9202.2 Volume of fluid and level setThe VOF method is used for interface recon- struction and advection as described in Ref.[16]. Anoperator splitting strategy is used to advect theinterface separately in each coordinate direction. Thevelocity used for VOF advection is the interface velocity field computed by applying Eq.(11) to thetwo-phase velocity field.The level set scalar is reinitialized from the VOFusing a parallel fast marching method described in Ref.[21].2.3 Interface area and location In the earlier implementation of this cavitation model described in Ref.[17], some discrepancies arose between the definition of the interface location usedfor the ghost fluid method and the volume source. The ghost fluid velocity extension utilizes the level set function interpolated to the face centers where the ve-Fig.4 (Color online) Cavity evolution at 1.25 cavitation number (=0.625)p , time series from a-h921Fig.5 (Color online) Cavity trailing edge showing stagnationpoint and reentrant jetFig.6 (Color online) Middle of cavity showing bulge wherereentrant jet begins to push outward into cavity. (For clarity, vectors are only shown at every other point.)locity is defined. Previously, the volume source was determined by the interface area from the VOF inter- face reconstruction. However, the two methods could lead to contradictions when the interface was close to a cell face. To eliminate this problem, a marching cubes method has been implemented following the method in Ref.[22]. By interpolating the level set function from cell centers to face centers, edge centers, and corners, a triangulated surface is obtained which is consistent with the interface used for the velocity extension in the ghost fluid method. The interface area can then be determined directly from the area of the triangles in each cell and used in the finite volume implementation of the pressure Poisson equation with a volume source. The triangulated surface is also useful for visualization. 3. Results and discussion 3.1 Two dimensions Previous computations with simple 2-D bubble cases showed that the velocity jump is well repre-sented and the pressure and velocity distributions around the bubble follow the analytical solutions [17].Computations have been made for a hydrofoiltested in Ref.[23]. The thickness of the hydrofoil is 9% of the chord length with a NACA 66 distribution. The camber is 2% of the chord length with a NACA =0.8a distribution. In the experiment, the span of the foil was equal to the chord. The angle-of-attack is o 6.Here, a 2-D slice of the foil is modeled with an O-grid with 2 048 cells wrapping around the foil and 256 cells in the surface normal direction. The radius of the O-grid is about 10 chord lengths. Upstream, the inlet velocity is specified. Downstream, the pressure is specified. The geometry is shown in Fig.1 and Fig.2 shows a detail of the mesh near the leading edge.The cells near the surface of the foil are approxi- mately square and approximately constant size. The fixed resolution is important to accurately capture the bubbles.A calculation without cavitation verifies the pressure distribution is accurately predicted on the foil, as shown in Fig.3. The computed lift coefficient of 0.824 is 3.3% greater than the experimentally mea- sured value at the Reynolds number of 2×106.With the cavitation number set to 1.25 to match the experiment, a time series of the initial cavity development is shown in Fig.4. Note that the contour legend shown in Fig.4 applies to all figures with pressure contours and that p in the figures is norma-lized with 2U ρ. so that the vapor pressure is =p 0.625-. The sequence shows that as the cavity grows downstream, a thin layer of liquid remains on the foil surface. This is because the downstream growth of the cavity is driven mainly by advection and there is a no-slip condition on the surface of the foil. The stagnation point at the downstream end ofthe cavity causes a high pressure at that location which tends to force liquid back upstream, underneath the cavity, as shown in Fig.5. This flow characteristic is often called the reentrant jet. As shown in Fig.5, the vapor flow at the outer surface of the cavity follows the liquid flow on the other side of the interface downstream. Drops of liquid from under the cavity are carried downstream and collect in the downstream portion of the cavity. A short distance from the stagnation point, the pressure in and under the cavity is equal and the liquid under the cavity can easily find its way into the cavity, as shown in Fig.6. Figure 7 shows a time series near the middle of the cavity. The liquid under the cavity is pushed up into the cavity by the flow of the reentrant jet from downstream (a, b). As the finger of liquid approachesand touches the outer surface of the cavity, it is drawndownstream (c, d), stretches (e, f) and breaks up into separate regions (g, h).If sufficient liquid collects in the downstream end of the cavity, or if a finger of liquid from the reentrant jet destabilizes the cavity enough to allow a high pres-922sure to develop between the upstream and downstreamportions of the cavity, the downstream portion of the cavity will be shed downstream and will gradually disappear as the vapor becomes liquid again.The current model does not capture the effect of the non-condensable gasses that diffuse into the cavity and will remain in the bubble after the vapor becomes liquid again.Figure 8 is a time sequence showing the flow field where,qualitatively, the downstream portion ofthe cavity begins to separate from the upstream por- tion before moving downstream while the upstream cavity sheds some additional vapor regions and shrinks. There is no sudden shift in the flow patterns. It appears that liquid accumulates under and among the cavities until the liquid displaces the cavities sufficiently high into the flow field for them to be swept downstream.Following shedding, the development of the new cavity is more complex than the initial developmentFig.7 (Color online) Reentrant jet flow under and into cavity, time series from a-h923 shown in Fig.4. There is not a single vapor-filledcavity, but instead a group of them occupying a similar extent to that shown in Fig,4(h) and Fig.8. The physical processes appear to be similar, including the recirculation or the reentrant jet and increasing liquid fraction.Fig.8(Color online) Shedding. The first image is an overview of the cavity shape at shedding, the arrow indicates the location shown in the other images. The other images show the flow at the point where shedding appears to initiate at times just before, during, and after shedding Fig.9Grid near foil leading edge. The similar discretization in all three directions is important for capturing bubbleswith a sharp interface methodFig.10 Pressure distribution on the foil without cavitation, 3-D calculation averaged across span. Experimental data isfrom Ref.[23]3.2 Three dimensionsThe same hydrofoil is modeled in three dimen- sions with an O-grid of 1 024 cells wrapping around the foil, 1 024 cells in the spanwise direction, and 128 cells in the surface normal direction. In the area of interest near the foil surface on the suction side, the cells are approximately cubes. The surface grid near the foil leading edge and a cut through the grid in a plane normal to the span is shown in Fig.9.Fig.11 (Color online) Inception bubbles near the leading edge of the foilThree calculations have been made: (1) the non-cavitating foil, (2) the cavitating foil initialized with a 2-D cavitating solution, and (3) the cavitating foil from inception.924Fig.12 (Color online) Close up of inception bubbles near the leading edge of the foilFig.13 (Color online) Close up near the leading edge of the foil showing bubble growth, merging, and advectionAs expected, the non-cavitating 3-D pressure dis- tribution is similar to the 2-D wetted pressure distribu- tion. However, there are some variations due to the fineness of the grid. The fine grid results in a DNS- like unsteady behavior, with vortices shed from the leading edge on the suction side. Averaging over the span of the foil shows the expected results, shown in Fig.10.A 3-D cavitating calculation has been initiated. Figures 11 through 13 show cavitation inception near the leading edge of the foil. The inception model generates a bubble of fixed radius, large enough to include several cells. The bubbles are then free to evolve and merge. It is clear from the calculations that the evolution of the bubbles is dominated by advec- tion.The pattern in the initial spanwise spacing, clearly visible in Fig.12, is due to one of the criteria in the inception model. The inception model requires that the center of a new bubble be a bit more than one radius from the nearest interface. Consequently, the model tends to create a line of bubbles along the low-pressure region at the leading edge.Only the initial startup of the 3-D calculation has been completed. As the bubbles stretch, break up, and interact with others, it is found that the stability of the computation is affected. A major reason might be the under-resolved bubbles generated in the process. A bubble model may be required to improve the nume- rical stability. On the other hand, Refs.[24,25] pro- posed a multi-scale approach to smoothly bridge large size cavities captured by level sets and small bubbles described by a discrete singularity model. Future work will require a closer look into similar models.4. conclusionsA sharp interface cavitation model has been developed and implemented. The method utilizes a simplification of the Rayleigh-Plesset equation to compute the interface velocity used to advect the interface between the liquid and vapor phases.The method has been demonstrated in two dimensions with a hydrofoil and found to offer insight into the mechanism of cavity evolution. The results show the formation of the reentrant jet and how instabilities in the reentrant jet perturb the cavity. Increasing liquid content, particularly near the leading edge of the cavity seems to gradually lead to cavity shedding.The method in three dimensions has proved to be more challenging. Of course, complex geometries and moving boundaries in 3-D will pose additional diffi- culties to the current approach with the orthogonal curvilinear grid requirement. It is believed that toge- ther with unstructured mesh approaches or immersed boundary approaches[26] this method will lead to viable high-fidelity cavitation calculations in the near future.AcknowledgmentsThis research was supported by the NSWC Carderock ILIR program and by the US Office of Naval Research (Grant No. N000141-01-00-1-7), with Dr. Ki-Han Kim as the program manager. The computations were performed on computers at AFRL and Navy DoD Supercomputing Resource Centers. References[1]Lee C. S. Prediction of steady and unsteady performanceof marine propellers with or without cavitation by numeri- cal lifting surface theory [D]. Doctoral Thesis, Cambridge, Massachusetts, USA: Massachusetts Institute of Tech- nology, 1979.[2]Kerwin J. E., Kinnas S. A., Lee J. T. et al. A surface panelmethod for the hydrodynamic analysis of ducted pro- pellers [J]. SNAME Transactions, 1987, 95: 93-122.[3]Merkle C. L., Feng J. Z., Buelow P. E. O. Computationalmodeling of the dynamics of sheet cavitation [C]. Third International Symposium on Cavitation. Grenoble, France, 1998.[4]Kunz R. F., Boger D. A., Chyczewski T. S. et al. Multi-phase CFD analysis of natural and ventilated cavitation about submerged bodies [C]. Proceedings of FEDSM ’99,9253rd ASME/JSME Joint Fluids Engineering Conference.San Francisco, California, USA, 1999.[5]Singhal A. K., Athavale M. M., Li H. et al. Mathematicalbasis and validation of the full cavitation model [J].Journal of Fluids Engineering, 2002, 124(3): 617-624. [6]Kim S. E., Brewton S. A multiphase approach to turbulentcavitating flows [C]. Proceedings of the 27th Symposium on Naval Hydrodynamics. Seoul, Korea, 2008.[7]Kim S. E., Schroeder S., Jasak H. A multi-phase CFDframework for predicting performance of marine propul- sors [C]. The 13th International Symposium on Transport Phenomena and Dynamics of Rotating Machinery.Honolulu, Hawaii, USA, 2010.[8]Kim S. E., Schroeder S. Numerical study of thrust-break-down due to cavitation on a hydrofoil, a propeller, and a waterjet [C]. Proceedings of the 28th Symposium on Naval Hydrodynamics. Pasedena, California, USA, 2010.[9]Bensow R. E., Huuva T., Bark G. Large eddy simulationof cavitating propeller flows [C]. 27th Symposium on Naval Hydrodynamics. Seoul, Korea, 2008.[10] Zhang, L. X., Zhang N., Peng X. X. et al. A review ofstudies of mechanism and prediction of tip vortex cavita- tion inception [J]. Journal of Hydrodynamics, 2015, 27(4): 488-495.[11]Luo X. W., Jin B., Tsujimoto Y. A review of cavitation inhydraulic machinery [J]. Journal of Hydrodynamics, 2016, 28(3): 335-358.[12] Chen Y., Lu C. J., Chen X. et al. Numerical investigationof the time-resolved bubble cluster dynamics by using the interface capturing method of multiphase flow approach [J]. Journal of Hydrodynamics, 2017, 29(3): 485-494. [13]Zhang D. S., Shi W. D., Zhang G. J. et al. Numericalanalysis of cavitation shedding flow around a three-dimen- sional hydrofoil using an improved filter-based model [J]. Journal of Hydrodynamics, 2017, 29(2): 361-375. [14] Son G., Dhir V. K. A level set method for analysis of filmboiling on an immersed solid surface [J]. Numerical Heat Transfer, Part B: Fundamentals, 2007, 52(2): 153-177. [15]Gibou F., Chen L., Nguyen D. et al. A level set basedsharp interface method for the multiphase incompressible Navier-Stokes equations with phase change [J]. Journal of Computational Physics, 2007, 222: 536-555. [16]Wang Z., Yang J., Stern F. A new volume-of-fluid methodwith a constructed distance function on general structured grids [J]. Journal of Computational Physics, 2012, 231(9): 3703-3722.[17] Michael T., Yang J., Stern F. Sharp interface cavitationmodeling using volume-of-fluid and level set methods [J].Proceedings of the ASME 2013 Fluids Engineering Summer Meeting. Incline Village, Nevada, USA, 2013. [18] Suh J., Yang J., Stern F. The effect of air-water interfaceon the vortex shedding from a vertical circular cylinder [J].Journal of Fluids and Structures, 2011, 27(1): 1-22. [19]Falgout R. D., Jones J. E., Yang U. M. The design and im-plementation of hypre, a library of parallel high perfor- mance preconditioners (Bruaset A. M., Tveito A.Numerical solution of partial differential equations on pa- rallel computers) [M]. Berlin, Germany: Springer-Verlag, 2006, 51: 267-294.[20]Yang J., Stern F. Sharp interface immersed-boundary/level-set method for wave-body interactions [J]. Journalof Computational Physics, 2009, 228(17): 6590-6616. [21]Yang J., Stern F. A highly scalable massively parallel fastmarching method for the Eikonal equation [J]. Journal of Computational Physics, 2017, 332: 333-362.[22]Lewiner T., Lopes H., Vieira A. W. et al. Efficientimplementation of Marching Cubes’ cases with topologi- cal guarantees [J]. Journal of Graphics Tools,2003, 8(2): 1-15.[23]Shen Y. T., Dimotakis P. E. The influence of surfacecavitation on hydrodynamic forces [C]. 22nd American Towing Tank Conference. St Johns, Newfoundland, Canada, 1989.[24]Hsiao C. T., Ma J., Chahine G. L. Multiscale two-phaseflow modeling of sheet and cloud cavitation [J]. InternationalJournal of Multiphase Flow, 2017, 90: 102-117.[25]Ma J., Hsiao C. T., Chahine G. L. A physics basedmultiscale modeling of cavitating flows [J]. Computersand Fluids, 2017, 145: 68-84.[26]Yang J. Sharp interface direct forcing immersed boundarymethods: A summary of some algorithms and applications [J]. Journal of Hydrodynamics, 2016, 28(5): 713-730.。
一些特殊的食物英语作文

When it comes to discussing special foods in English,we can explore a variety of topics,from regional delicacies to unique ingredients.Heres a detailed look at some special foods that might be featured in an English composition.Regional Delicacies1.Poutine Originating from Quebec,Canada,poutine is a dish that combines French fries with cheese curds and gravy.Its a hearty and indulgent snack that has become a cultural icon.2.Croissant A French pastry that is flaky,buttery,and often enjoyed with a cup of coffee. Its a staple in French bakeries and has variations such as almond croissants or pain au chocolat.3.Sushi A Japanese dish that has gained international popularity.Sushi is typically made with vinegared rice combined with a variety of ingredients,such as seafood,vegetables, and sometimes tropical fruits.4.Feijoada A traditional Brazilian dish that is a stew of black beans with beef and pork. Its often served with rice,collard greens,and farofa toasted cassava flour.Unique Ingredients1.Truffles These are a type of edible fungus that is highly prized for its unique flavor. Truffles are often used in gourmet dishes and can be found in regions like France,Italy, and Australia.2.Wasabi A pungent green paste made from the wasabi plant,native to Japan.Its commonly served with sushi and sashimi to add a sharp,spicy flavor.3.Caviar A luxury food product obtained from fish eggs,particularly sturgeon.Beluga, Osetra,and Sevruga are some of the most soughtafter types of caviar.4.Durian Known as the king of fruits in Southeast Asia,durian is notorious for its strong odor and unique taste.Its a divisive fruit,with some people loving it and others avoiding it.Traditional Dishes1.Peking Duck A famous dish from Beijing,China,known for its crispy skin and tendermeat.Its often served with pancakes,scallions,and hoisin sauce.2.Ratatouille A vegetable stew originating from Nice,France.Its made with eggplant, zucchini,bell peppers,and tomatoes,and is a staple in Provençal cuisine.3.Chiles en Nogada A Mexican dish that is a play on the colors of the Mexican flag.It consists of poblano chiles filled with a mixture of shredded meat and fruits,topped with a walnutbased cream and pomegranate seeds.4.Moussaka A Greek dish that is similar to lasagna,made with layers of eggplant, minced meat,and a bechamel sauce,topped with grated cheese.Modern Fusion Cuisine1.Molecular Gastronomy A modern culinary movement that uses scientific techniques to create innovative dishes.Examples include foams,gels,and spheres that transform the texture and presentation of food.2.Nutritional Yeast A popular ingredient in vegan cooking,nutritional yeast is a deactivated yeast that is rich in vitamins and has a cheesy flavor.3.AçaíBowls A trendy health food that originated in Brazil,açaíbowls are made with açaípulp,often blended with other fruits and topped with granola and fresh fruit.4.Vegan Cheese With the rise of plantbased diets,vegan cheese alternatives made from nuts,soy,or root vegetables are becoming more common and sophisticated in flavor and texture.In conclusion,the world of special foods is vast and diverse,offering a culinary adventure for the taste buds.Whether its traditional dishes,unique ingredients,or modern fusion cuisine,theres always something new and exciting to discover in the world of food.。
CAV2009-final13

Proceedings of the 7th International Symposium on CavitationCAV2009 – Paper No. 13August 17-22, 2009, Ann Arbor, Michigan, USA Quantification of Cavitation Impacts with Acoustic Emissions TechniquesMr Anne Boorsma Lloyd's Register ODS, UKPatrick Fitzsimmons Lloyd's Register ODS, UKABSTRACTCavitation erosion on propellers and rudders remains a problem in the marine industry. The consequences of failing to detect the risk of erosion damage during the design phase, and early in the service life of a vessel, include reducing the speed of the vessel, unscheduled dry-dockings and repairs or replacement of the propellers or rudders. The associated costs are borne by the builder and owner and may harm their reputations within the industry.Lloyd’s Register has developed and tested a unique measurement system, based on acoustic emission techniques, which is capable of detecting the onset of erosion damage on propellers and rudders. The system uses high frequency transducers to quantify the impulsive energy transmitted from imploding cavitation events through the material paths of rudder, propeller and shafting configurations. The acoustic emission signals from such events have been synchronised with visual observations using high speed video equipment and borescopes.INTRODUCTIONCavitation erosion on propellers and appendages, in particular rudders [1], remains a problem in the marine industry. Erosion damage requires increased maintenance including more frequent monitoring of the damage, dry-dockings and repairs and can limit the operational profile of a vessel. The associated additional costs are borne by the ship owner and ship builder.Erosion damage occurs as a result of failures to identify erosive cavitation characteristics during the project design phase. It is difficult to assess the erosive potential of cavitation from calculations and model tests, even when using the current, qualitative, paint and observational techniques [2].When a vessel enters service, (underwater) inspections may not identify erosion damage until after the incubation period, when the surfaces have started to break up. Therefore, damage may not be discovered until or after the guarantee dry-docking limiting palliative action by both builder and owner. Moreover, when erosion occurs it can be difficult to answer some of the questions that would help to create a better understanding of and allow better control of erosion. If the exact conditions and phenomena that lead to erosion were known, full scale observations and model tests could be interpreted to modify the design and avoid erosive cavitation. Alternatively, this information could be used to change the operating profile in order to minimize erosion damage. To this end Lloyd's Register has developed a condition monitoring capability for erosion damage from cavitation which is based on acoustic emission techniques.MEASUREMENT TECHNIQUELloyd's Register has been using and developing acoustic emission techniques over the past 12 years [3]. This technique relies on high frequency sensors that detect wide band stress waves travelling through a structure, referred to as acoustic emissions. Typical sources of acoustic emissions include crack growth and metal to metal contact, hence Lloyd’s Register has used this technique extensively to monitor crack growth in, mainly, metallic structures and for the condition monitoring of rotating machinery. However, it was found that cavitation impacts also give rise to such acoustic emissions which travel through physical connections to locations inside the ship. Acoustic emission sensors can easily be installed inside the ship and used to monitor and quantify such cavitation impacts. LICHTAROWICZ CELLThe feasibility of using acoustic emission techniques to detect cavitation erosion was first shown in tests in a Lichtarowicz cavitation cell in work carried out for the EROCA V project. In a Lichtarwicz cell, shown in Figure 1, a cavitating jet impinges on a specimen causing erosion. By varying jet and chamber pressures and the distance between nozzle and target, different impact intensities can be created.The Lichtarowicz cell was fitted with a primary acoustic emission sensor at the back of the target specimen, and a number of secondary sensors on the walls of the cylindrical tank. Acoustic emission energy was recorded at a number ofdifferent conditions and compared with mass loss rates measured by Momma [4].The results, inFigure 2, show there is a correlation between acoustic emission energy and mass loss rate and therefore acoustic emission techniques can be used to quantify the erosive potential of cavitation impacts. Furthermore, using the arrival times of acoustic bursts, it was possible to locate the impacts at the target surface giving confidence that recorded signals were a result from cavitation impacts.SIGNAL ATTENUATIONDuring in-service measurements it is seldom possible to install sensors directly at the impact location as in the Lichtarowicz cell. However, as the acoustic emission travels from its origin to the measurement location, its amplitude willreduce. This attenuation can be measured using a Hsu-Nielsen source which generates a signal of known magnitude at a known location. This distance amplitude correction was measured for typical structures subject to cavitation erosion such as rudders and propellers. A propeller test set up and the result of such a test are shown in Figure 3.Figure 1, Test set up in Lichtarowicz cavitation cellFigure 3, Test set up and measured attenuation curveFigure 2, Correlation of acoustic emission energy anderosion rate EROSION OF APPENDAGESThe erosion detection system was first used in-service on a number of rudder horns since these are easily accessible from inside a ship. Rudder horns are nearly always subject to impacts from vortex cavitation from the propeller tip and sometimes erosion occurs where this vortex meets the rudder horn leading edge.Figure 4 shows an acoustic emission measurement and observation test set up to quantify the erosive potential of the impact of propeller tip vortex cavitation (TVC). Acoustic emission sensors are installed on the rudder horn inside the ship and a borescope observation position is located several metres off the ship centre line to provide a good view of the passing tip vortex.The acoustic emission time series in Figure 5 exhibits aburst at every blade passage and is hence likely related to theinteraction of the passing, consecutive, tip vortices (TVC) andthe rudder leading edge. Simultaneous observations, alsoshown in Figure 5, suffered from a lack of light but still showthat the instant the tip vortex is expected to impinge on therudder horn (Image C) coincides with the acoustic emissionburst. Therefore the burst will be a result of cavitation impacton the leading edge of the rudder horn. Furthermore, byinstalling several sensors on the rudder horn and using thearrival times of the acoustic emission, it was possible to locatethe impact at the site where erosion damage was observed.These findings were consistent over tests carried out on anumber of ships.Figure 4, measurement and observation of tip vortex impactSHAFT-MOUNTED EROSION-DETECTION SYSTEMTo measure acoustic emissions from cavitation impact on apropeller a shaft-mounted erosion-detection system wasdeveloped. This system, consisting of an acoustic emissionsensor, a signal conditioning unit and a telemetry set, is shownin Figure 6 together with a schematic of the measurement setup.Figure 6, Shaft-mounted erosion-detection system Figure 5, Simultaneous video observations and acousticemission measurementsThe ship’s engine room, due to the associated acoustic emission sources other than cavitation impact, is a challenging place for acoustic emission measurements, further complicated by the significant attenuation caused by the large distance between emission source and sensor. To evaluate this, an attenuation test was performed with a specifically designed Hsu-Nielsen source, capable of creating an acoustic emission equivalent to one from cavitation impact. These tests were performed on a berthed containership where the propeller tips only were not immersed. The majority of the blade and hub were submerged to simulate the actual conditions at which measurements would be performed. These measurements indicated that cavitation impacts on the propeller tips could be detected on the shaft inside the ship and an attenuation curve, as shown in Figure 3, was determined for a propeller and shaft combination.ASSESSMENT OF PROPELLER EROSION RISKThe viability of the system to quantify cavitation impacts on a propeller was investigated on a tanker with known erosion problems. Erosion of the propeller occurred towards the “ear” of the blade on the suction side, as shown in Figure 7, and had grown to a depth of approximately 10mm in the first 12 months of service.A propeller erosion-detection system was mounted on the shaft of the tanker, as shown in Figures 6, and measurements were performed in ballast and loaded condition over a range of shaft speeds. Simultaneously, high speed video observationswere performed with two synchronized borescope systems from port and starboard.Two examples of acoustic emission time series, recorded at 62RPM and 74RPM in ballast condition, are shown in Figure 8. At both shaft speeds the signal was periodic with the blade passing frequency which suggests that cavitation impacts on the blade were the likely source of acoustic emission. Furthermore, the direction of travel of the acoustic emission, determined by two sensors located along the shaft line, was away from the propeller which also indicated the propeller as the origin of the emission.Figure 8, Recorded acoustic emissions from propeller cavitation impact TELESuction SideOrange P eelAreas of Major P ittingMissing P iece495 mmFigure 7, Erosion damage on a tanker propeller.At 62RPM the signal for every blade passage showed some repeatable features with the suggestion of a burst occurring twice per blade passage. In this low power condition the cavitation volumes are likely to be small and, possibly, more susceptible to temporal variations in the wakefield. This might suppress repeatable cavitation phenomena and lead to a less periodic acoustic emission signal. With increasing shaft speed the signal amplitude increased and at 74 RPM there were twodistinct bursts with every blade passage. The increasedamplitude is consistent with the increased energy supplied to the cavitation, although the cavitation collapse and the accompanying impact pressures will also depend on local cavitation dynamics.Images of the propeller were only obtained in the loaded condition since entrained air obscured the view in the ballast condition. Two high speed videos (up to 400fps) simultaneously recorded images of propeller cavitation from locations forward of the propeller, to port and starboard. A series of consecutive stills from these recordings is shown in Figure 9.Figure 9, Recorded acoustic emissions from propeller cavitation impactImages A show the blade in the 12 o’clock position where the sheet cavity extent is largest. A cavitating vortex emanates from the tip of the blade. As the blade rotates further a streak of cavitation develops as a series of cloud-like structures at the lower extent of the sheet cavity, as shown in Images B. The path of these clouds is consistent with the lower edge of the sheet cavity, Images C, and collapse occurs in a focused manner on the “ear” of the blade, which coincides with the area where erosion damage was observed in Figure 7. The EROCA V guidelines [2] suggest that such a separate development of cavitation contains a high risk of erosion because of its repeated and focused collapse. The cavitation moves off the blade via the blade trailing edge, Images D, as the blade leaves the wake peak.Approximately 5 blade passages of simultaneous recorded time series of acoustic emission are also shown in Figure 9. In a similar manner to the measurements on the rudder horn, Figure 5, the peak in the acoustic emission signal corresponds to the moment when cavitation impact on the blade is observed, Images C, which gives confidence that the acoustic emission signals are indeed the result of cavitation impact. The cavitation collapse of the third blade passage in Figure 9 gives rise to a significantly larger acoustic emission than other blade passages. Interestingly, in this sequence it was only during the third blade passage that the separate streak of cloud cavitation, thought to be responsible for erosion, was prominent. High acoustic emission amplitudes were accompanied by the separate cloud cavitation throughout the recorded data set.The measured acoustic emissions, resulting from cavitation impact, provide information to quantify the erosive potential of cavitation. Counting the maximum peak for each blade passage in the time series signals (Figures 8 and 9), results in amplitude histograms as shown in Figures 10 and 11. These amplitude histograms reflect the energy present in the cavitation impacts at a given condition, where energy is proportional to the sum of the number of impacts times their amplitudes.Figure 10 shows the amplitude histograms for signals recorded in the ballast condition at shaft speeds between 62RPM and 74RPM. Up to 70RPM there is a steady increase of energy, however, at shaft speeds over 70RPM the impact energy increases markedly. Relating this to the observations in Figure 9, one could postulate that, in the ballast condition, the separated streak of cloud cavitation that resulted in the potentially erosive cavitation impacts only develops at shaft speeds over 70RPM.histograms in Figure 11, are very similar at shaft speeds up to 70RPM. However, at shaft speeds in excess of 70RPM there are significantly more bursts with large amplitudes in the ballast condition. This suggests that the potentially erosive cavitation, as observed in Figure 8, occurs more frequently in the ballast condition thus making this the more erosive condition, a result which is consistent with a more dynamic cavitation due to the reduced static pressure at the propeller. This effect is not offset by a reduction in power since the ship’s staff indicated a similar power was absorbed by the propeller in ballast and loadedcondition.CONCLUSIONSA system to monitor cavitation erosion on rudders and propellers has been successfully developed by Lloyd's Register. The development process included feasibility studies in a Lichtarowicz cell, attenuation tests in dry-dock and afloat, together with in-service measurements on ships. In the case of a tanker, suffering from erosion, the acoustic emission system has determined the operating conditions which have produced high levels of erosive cavitation. Furthermore, the use of simultaneous high speed video recordings synchronised with acoustic emissions signals has determined with greater certainty the type of cavitation phenomena which has proved erosive.Figure 11, Impact energy in ballast and loaded draught.Thus far, Lloyd’s Register has performed work primarily on ship’s rudders and propellers. However, this technique can easily be applied to other industrial equipment suffering from cavitation erosion such as turbines, pumps and waterjets.As further full scale work is performed, and the techniques adapted for model scale testing, it is anticipated that better ship-model-CFD correlations will be obtained and improved design guidance delivered to propeller and rudder designers.REFERENCES[1] Friesch, J. 2006, Rudder Erosion Damages Caused byCavitation, CA V2006 symposium, Wageningen, The Netherlands.[2] Bark, G. Berchiche, N. Grekula, M. 2004, Application ofprinciples for observation and analysis of eroding cavitation . Chalmers University of Technology [3] Rogers, L.M. 2001, Structural and EngineeringMonitoring by Acoustic Emission Methods – Fundamentals and Applications. Lloyd’s Register Technical Association[4] Momma, T. 1991, Cavitation Loading and ErosionProduced by a Cavitating Jet ., PhD thesis to Nottingham University, UK。
What's cavitation

From Wikipedia, the free encyclopediaCavitation is the formation of gas bubbles 气泡of a flowing liquid in a region where the pressure of the liquid falls below its vapor pressure蒸汽压力. Cavitation is usually divided into two classes of behavior: inertial (or transient) cavitation惯性空化, and noninertial cavitation非惯性空化.Inertial cavitation is the process where a void or bubble in a liquid rapidly collapses, producing a shock wave.液体中气泡迅速破裂,产生冲击波 Inertial cavitation occurs in nature in the strikes of mantis shrimps and pistol shrimps, as well as in the vascular tissues of plants. In artifacts, it can occur in control valves, pumps, propellers and impellers.在调节阀,泵,螺旋桨,叶轮中出现。
Noninertial cavitation is the process in which a bubble in a fluid is forced to oscillate in size or shape due to some form of energy input, 由于某种能量的输入,流体中的气泡发生大小和形状的改变。
journal of fluid mechanics 文献
标题: Two-dimensional and axisymmetric viscous flow in apertures作者: Dabiri, Sadegh; Sirignano, William A.; Joseph, Daniel D.Flow Visualization Using Cavitation Within Blade Passage of an Axial Waterjet Pump RotorDavid Y. Tan,Rinaldo L. Miorini,Jens Keller and Joseph KatzCAVITATION PHENOMENA WITHIN REGIONS OF FLOW SEPARATION.Katz, Joseph Source:Journal of Fluid Mechanics, v 140, p 397-436, Mar 1984Two-dimensional and axisymmetric viscous flow in apertures作者: Dabiri, Sadegh; Sirignano, William A.; Joseph, Daniel D.Interaction between a cavitation bubble and shear flow作者: Dabiri, Sadegh; Sirignano, William A.; Joseph, Daniel D.Direct numerical evidence of stress-induced cavitation作者: Falcucci, G.; Jannelli, E.; Ubertini, S.; 等.标题: Non-spherical bubble dynamics in a compressible liquid. Part 1. Travelling acoustic wave作者: Wang, Q. X.; Blake, J. R.标题: Cavitation in linear bubbles作者: Brenner, Michael P.标题: Numerical simulations of non-spherical bubble collapse作者: Johnsen, Eric; Colonius, Tim标题: Simulation ofcavitationbubbles in a convergent-divergent nozzlewaterjet作者: Qin, Z.; Bremhorst, K.; Alehossein, H.; 等.The influence of the sleeve's orifices geometric patterns on the fluid flow through a hydraulic resistance作者:Sfarlea, I (Sfarlea, I.)[ 1 ] ; Bode, F (Bode, F.)[ 1 ] ; Opruta, D (Opruta, D.)[ 1 ]标题: NUMERICAL SIMULATION OF ORIFICE CAVITATING FLOWS USING TWO-FLUID AND THREE-FLUID CAVITATION MODELS作者: Darbandi, Masoud; Sadeghi, HamedFlow instability due to cryogenic cavitation in the downstream of orifice 作者: Lee, Changjin; Roh, Tae-Seong来源出版物: JOURNAL OF MECHANICAL SCIENCE AND TECHNOLOGY标题: A STUDY ON FLOW THROUGH AN ORIFICE WITH PREDICTIONOF CAVITATION AND HYDRAULIC FLIP作者: Darbandi, Masoud; Sadeghi, Hamed书籍团体作者: ASME标题: ANALYSIS OF THERMAL EFFECTS IN ACAVITATING ORIFICE USING RAYLEIGH EQUATION AND EXPERIMENTS 作者: Grazia, De Giorgi Maria; Daniela, Bello; Ficarella, Antonio书籍团体作者: ASME会议: 17th International Conference on Nuclear Engineering 会议地点: Brussels, BELGIUM会议日期: JUL 12-16, 2009标题: Simulations of cavitation in orifice and venturis作者: Ahuja, Vineet; Hosangadi, Ashvin丛书编者: Moatamedi, M会议: Joint Conference of the ASME Pressure Vessels and Piping Division/8th International Conference on Creep and Fatigue at Elevated Temperatures会议地点: San Antonio, TX会议日期: JUL 22-26, 2007标题: Effects on pipe vibrations of cavitation in an orifice and inglobe-style valves作者: Caillaud, Sebastien; Gibert, Rene-Jean; Moussou, Pierre; 等.丛书编者: Paidoussis, MP会议: 6th Symposium on Fluid-Structure Interactions, Aeroelasticity and Flow-Induced Vibration and Noise 会议地点: Vancouver, CANADA会议日期: JUL 23-27, 2006会议赞助商: ASME, Pressure Vessels & Piping Div标题: Flow and cavitation characteristics of a damping orifice in water hydraulics作者: Liu Yinshui; Zhu Bihai; Zhu Yuquan; 等.来源出版物: PROCEEDINGS OF THE INSTITUTION OF MECHANICAL ENGINEERS PART A-JOURNAL OF POWER AND ENERGY 卷: 220期: A8页: 933-942 DOI: 10.1243/09576509JPE323出版年: DEC 2006标题: Investigation of cavitation near the orifice of hydraulic valves作者: Gao, H.; Lin, W.; Tsukiji, T.来源出版物: PROCEEDINGS OF THE INSTITUTION OF MECHANICAL ENGINEERS PART G-JOURNAL OF AEROSPACE ENGINEERING 卷: 220期: G4页:253-265 DOI: 10.1243/09544100JAER O26出版年: AUG 2006标题: Effects of orifice internal flow on breakup characteristics oflike-doublet injectors作者: Jung, K; Khil, T; Yoon, Y来源出版物: JOURNAL OF PROPULSION AND POWER 卷: 22期: 3页: 653-660 DOI: 10.2514/1.20362出版年: MAY-JUN 2006被引频次: 6 (来自所有数据库)标题: Visualization of cavitation in high-pressure diesel fuel injectororifices作者: Li, Haiyun; Collicott, Steven H.来源出版物: ATOMIZATION AND SPRAYS 卷: 16期: 8页: 875-886 DOI: 10.1615/AtomizSpr.v16.i8.20出版年: 2006被引频次: 8 (来自所有数据库)标题: Experimental study of thermal cavitation in an orifice作者: De Giorgi, Maria Grazia; Chiara, Fabio; Ficarella, Antonio书籍团体作者: ASME会议: 8th Biennial Conference on Engineering Systems Design and Analysis 会议地点: Turin, ITALY会议日期: JUL 04-07, 2006会议赞助商: ASME来源出版物: Proceedings of the 8th Biennial Conference on Engineering Systems Design and Analysis, Vol 1 页: 523-529出版年: 2006被引频次: 0 (来自所有数据库)Cavitation Inception and Head Loss Due to Liquid Flow Through Perforated Plates of Varying ThicknessD. Maynes,G. J. Holt and J. BlotterToward Improved Closure Relations for the Turbulent Kinetic Energy Equation in Bubble-Driven Flows1. Martin Wörner*,2. SercanErdoganArticle first published online: 17 MAY 2013DOI: 10.1002/cite.201200243A TRANSPORT EQUATION MODEL FOR SIMULATINGCAVITATION FLOWS IN MINIATURE MACHINESYAO ZHANG∙State Key Laboratory of Hydroscience& Engineering, TsinghuaUniversity, Beijing, 100084, ChinaXIANWU LUO∙Corresponding author.∙State Key Laboratory of Hydroscience& Engineering, TsinghuaUniversity, Beijing, 100084, ChinaSHUHONG LIU∙State Key Laboratory of Hydroscience& Engineering, TsinghuaUniversity, Beijing, 100084, ChinaHONGYUAN XU∙State Key Laboratory of Hydroscience& Engineering, TsinghuaUniversity, Beijing, 100084, ChinaDevelopment of Cavitation in Refrigerant (R-123) Flow InsideRudimentary Microfluidic SystemsThermodynamic analysis of capillary flows in the presence ofhydrodynamic slip1. A. Laouir1,*,2. D. Tondeur2A Series Pressure Drop Representation for Flow Through Orifice TubesT. A. Jankowski,S. P. Ashworth,E. N. Schmierer and F. C. Prenger[+] Author and Article InformationEstimation of Cavitation Limits From Local Head Loss CoefficientRaúl Sánchez, Francisco V. Laguna, Leonor Rodríguez-Sinobas and Luis Juana[+] Author and Article InformationI mpact of Orifice Length/Diameter Ratio on 90 deg Sharp-Edge Orifice FlowWith Manifold Passage Cross FlowW. H. Nurick, D. G. Talley, P. A. Strakey and T. Ohanian[+] Author and Article InformationNumerical simulation and extended validation of two-phasecompressible flow in diesel injector nozzles1. F J Salvador*2. S Hoyas3. R Novella4. J Martínez-LópezX. Yang, A. Holke, S. A. Jacobson, J. H. Lang, M. A. Schmidt, and S.D. Umans, “An electrostatic, on/off microvalve designed for gas fuel deliveryfor the MIT microengine,”J. Microelectromech. Syst.13, 660 (2004).D. J. Laser and J. G. Santiago, ―A review of micropumps,‖J. Micromech.4.P. Woias, ―Micropumps—summarizing the first two decades,‖Proc.SPIE4560, 39 (2001).5.N.-T. Nguyen, X. Huang, and T. K , Chuan, ―A review of micropumps,‖J. Fluids Eng.124, 384 (2002)./10.1115/1.145907519.C. -M. Ho and Y.-C. Tai, ―Micro-electro-mechanical-systems (MEMS) and fluidflows,‖Annu. Rev. Fluid Mech.30, 579 (1998)./10.1146/annurev.fluid.30.1.57920.P. Gravesen, J. Branebjerg, and O. S. Jensen, ―Microfluidics—a review,‖J.Micromech. Microeng.3, 168 (1993)./10.1088/0960-1317/3/4/00221.H. A. Stone, A. D. Strooch, and A. Ajdari, ―Engineering flows in small devices:Microfluidics toward a lab-on-a-chip,‖Annu. Rev. Fluid Mech.36, 381 (2004)./10.1146/annurev.fluid.36.050802.12212422.T. Hasegawa, M. Suganuma, and H. Watanabe, ―Anomaly of excess pressure drops of the flow through very small orifices,‖Phys. Fluids9, 1 (1997)./10.1063/1.86917023.G. Stemme, G. Kittilsland, and B. Norden, ―A sub-micron particle filter insilicon,‖Sens. Actuators, A21–23, 904 (1990).24.G. M. Mala and D. Li, ―Flow characteristics of water in microtubes,‖Int. J. HeatFluid Flow20, 142 (1999)./10.1016/S0142-727X(98)10043-7G. L. Morini, “Single-phase convective heat transfer in microchannels: A review of experimental results,”Int. J. Therm. Sci.43,631 (2004).26. Cavitation Enhanced Heat Transfer in MicrochannelsBrandon Schneider,Chandan Mishra,Gregory S. Cole,Yoav Peles,Robert P. Scaringe,Ali Koşar and Chih-Jung Kuo26.C. Mishra and Y. Peles, ―Cavitation in flow through a micro-orifice inside a silicon microchannel,‖Phys. Fluids17, 013601(2005)./10.1063/1.182760227.C. Mishra and Y. Peles, ―Size scale effects on cavitating flows through micro-orifices entrenched in rectangular microchannels,‖J. Microelectromech. Syst.14, 987 (2005).28. R. E. A. Arndt, ―Cavitation in fluid machinery and hydraulic structures,‖Annu. Rev. Fluid Mech.13, 273 (1981)./10.1146/annurev.fl.13.010181.00142129. R. T. Knapp, J. W. Daily, and F. G. Hammit, Cavitation (McGraw-Hill, NewYork, 1970).30.C. E. Brennen, Cavitation and Bubble Dynamics (Oxford University Press, Oxford, UK, 1995).31. J. W. Holl, ―Nuclei and cavitation,‖J. Basic Eng.92, 681 (1970).35.F. R. Young, Cavitation (McGraw-Hill, New York, 1989).S. Pennathur, Y. Peles, and A. H. Epstein, Cavitation at Micro-Scale in MEMS Fluid Machinery,” Proc. ASME Int. Mech. Engg. Congress and Expos, New Orleans, LA, 2002, p. 87.39.D. P. Schmidt, C. J. Rutland, and M. L. Corradini, ―Fully compressible,two-dimensional model of small, high-speed, cavitating nozzles,‖Atomization Sprays9, 255 (1999).40. W. Yuan and G. H. Schnerr, ―Numerical simulation of two-phase flow in injection nozzles: Interaction of cavitation and external jet formation,‖J. FluidsEng.125, 963 (2003)./10.1115/1.162568739.D. P. Schmidt, C. J. Rutland, and M. L. Corradini, ―Fully compressible,two-dimensional model of small, high-speed, cavitating nozzles,‖Atomization Sprays9, 255 (1999).40. W. Yuan and G. H. Schnerr, ―Numerical simulation of two-phase flow in injection nozzles: Interaction of cavitation and external jet formation,‖J. FluidsEng.125, 963 (2003)./10.1115/1.162568741. L. C. Ganippa, G. Bark, S. Andersson, and J. Chomiak, ―Cavitation: A contributory factor in the transition from symmetric to asymmetric jets in cross-flow nozzles,‖Exp. Fluids36, 627 (2004).43.B. Freudig, S. Tesch, and H. Schubert, ―Production of emulsions in high-pressure homogenizers—Part II: Influence of cavitation on droplet breakup,‖LifeSci.3, 266 (2003).44. Y. Tomita and A. Shima, ―Mechanisms of impulsive pressure generation and damage pit formation by bubble collapse,‖J. Fluid Mech.169, 535 (1986).42. W. Y. Lee, M. Wong, and Y. Zohar, ―Pressure loss in constriction microchannels,‖J. Microelectromech. Syst.11, 236 (2002)./10.1109/JMEMS.2002.100740245. J. P. Tullis, Hydraulics of Pipelines (Wiley, New York, 1989).43.B. Freudig, S. Tesch, and H. Schubert, ―Production of emulsions in high-pressure homogenizers—Part II: Influence of cavitation on droplet breakup,‖LifeSci.3, 266 (2003).44. Y. Tomita and A. Shima, ―Mechanisms of impulsive pressure generation and damage pit formation by bubble collapse,‖J. Fluid Mech.169, 535 (1986).49. Y. Yan and R. B. Thorpe, ―Flow regime transitions due to cavitation in the flow through an orifice,‖Int. J. Multiphase Flow16,1023 (1990)./10.1016/0301-9322(90)90105-R50. J. W. Ball, J. P. Tullis, and T. Stripling, ―Predicting cavitation in sudden enlargements,‖J. Hydraul. Div., Am. Soc. Civ. Eng.101,857 (1975).51. J. P. Tullis, ―Cavitation scale effects for valves,‖J. Hydraul. Div., Am. Soc. Civ. Eng.99, 1109 (1973).52. K. Ramamurthi and K. Nandakumar, ―Characteristics of flow through smallsharp-edged cylindrical orifices,‖Flow Meas. Instrum.10, 133 (1999)./10.1016/S0955-5986(99)00005-9标题: Experimental study on cavitation characteristics of waterhydraulic orifice作者: Liu, YS; Wu, ZJ; Yang, YS; 等.丛书编者: Lu, YX; Wang, QF; Wei, L会议: 6th International Conference on Fluid Power Transmission and Control (ICFP 2005) 会议地点: Zhejiang Univ, Hangzhou, PEOPLES R CHINA会议日期: APR 05-08, 2005标题: Numerical study of inlet and geometry effects on discharge coefficients for liquid jet emanating from a plain-orifice atomizer作者: Yeh, CL来源出版物: CHINESE JOURNAL OF MECHANICS-SERIES A 卷: 18期: 3页: 153-161出版年: SEP 2002标题: Experimental investigation of the flow characteristics of small orifices and valves in water hydraulics作者: Zhu, BK; Huang, Y; Zhang, TH; 等.来源出版物: PROCEEDINGS OF THE INSTITUTION OF MECHANICAL ENGINEERS PART E-JOURNAL OF PROCESS MECHANICAL ENGINEERING 卷: 216期:E4页: 235-245出版年: 2002标题: Hydraulic characteristics of multistage orifice tunnels作者: Zhang, QY; Chai, BQ来源出版物: JOURNAL OF HYDRAULIC ENGINEERING-ASCE 卷: 127期: 8页: 663-668 DOI: 10.1061/(ASCE)07 33-9429(2001)127:8(663)出版年: AUG 2001被引频次: 3 (来自所有数据库)标题: Unstable cavitation behavior in a circular-cylindrical orifice flow作者: Sato, K; Saito, Y来源出版物: JSME INTERNATIONAL JOURNAL SERIES B-FLUIDS AND THERMALENGINEERING 卷: 45期: 3页: 638-645 DOI: 10.1299/jsmeb.45.638出版年: AUG 2002标题: Simulations of turbulent, cavitating flows in an injector slot/orifice 作者: Xu, C; Blaisdell, GA; Heister, SD丛书编者: Power, H; Brebbia, CA会议: 1st International Conference on Computational Methods in Multiphase Flow 会议地点: ORLANDO, FL会议日期: MAR 14-16, 2001会议赞助商: WessexInstTechnol; Univ Cent Florida标题: Visualization of internal flow in a cavitating slot orifice作者: Henry, ME; Collicott, SH来源出版物: ATOMIZATION AND SPRAYS 卷: 10期: 6页: 545-563出版年: NOV-DEC 2000被引频次: 12 (来自所有数据库)标题: Prediction of noise generated by orifice plates in liquid systems using a modified form of IEC 534-8-4 : 1994作者: Cairns, C; Whitson, RJ; Strachan, P; 等.丛书编者: Rahman, M; Brebbia, CA会议: 3rd International Conference on Advances in Fluid Mechanics 会议地点: MONTREAL, CANADA会议日期: MAY, 2000会议赞助商: WessexInstTechnol; Dalhousie Univ标题: Compromise orifice geometry to minimize pressure drop作者: Zhang, ZJ; Cai, JM来源出版物: JOURNAL OF HYDRAULIC ENGINEERING-ASCE 卷: 125期: 11页: 1150-1153 DOI: 10.1061/(ASCE )0733-9429(1999)125:11(1150)出版年: NOV 1999标题: Characteristics of flow through small sharp-edged cylindrical orifices作者: Ramamurthi, K; Nandakumar, K来源出版物: FLOW MEASUREMENT AND INSTRUMENTATION 卷: 10期: 3页: 133-143 DOI: 10.1016/S0955-5986( 99)00005-9出版年: SEP 1999被引频次: 43 (来自所有数据库)标题: The effect of manifold cross-flow on the discharge coefficient of sharp-edged orifices作者: Strakey, PA; Talley, DG来源出版物: ATOMIZATION AND SPRAYS 卷: 9期: 1页: 51-68出版年: JAN-FEB 1999被引频次: 8 (来自所有数据库)标题: The effect of oil type on flow and cavitation properties in orifices and annular clearances作者: Koivula, T; Ellman, A; Vilenius, M丛书编者: Burrows, CR; Edge, KA会议: Bath Workshop on Power Transmission and Motion Control (PTMC 99) 会议地点: UNIV BATH, BATH, ENGLAND会议日期: SEP 08-10, 1999会议赞助商: Univ Bath; CtrPowrTransmiss& Motion Control来源出版物: BATH WORKSHOP ON POWER TRANSMISSION AND MOTION CONTROL (PTMC 99) 页: 151-165出版年: 1999标题: Some characteristics of variable orifice nozzle geometrics for diesel injection作者: Soteriou, C; Smith, M; Andrews, R; 等.书籍团体作者: PROFESSIONAL ENGINEERING PUBLISHING LIMITED FOR INST OF MECHANICAL ENGINEERS; PROFESSIONAL ENGINEERING PUBLISHING LIMITED FOR INST OF MECHANICAL ENGINEERS会议: Conference on Fuel Injection Systems 会议地点: INST MECH ENGN, LONDON, ENGLAND会议日期: DEC 01-02, 1999会议赞助商: InstMechEngn, Combust Engines Grp; Lucas Diesel Syst来源出版物: FUEL INJECTION SYSTEMS 丛书: INSTITUTION OF MECHANICAL ENGINEERS SEMINAR卷: 1999期: 17页: 135-161出版年: 1999被引频次: 0 (来自所有数据库)标题: Diesel injection - laser light sheet illumination of the developmentof cavitation in orifices作者: Soteriou, C; Smith, M; Andrews, R书籍团体作者: INST MECH ENGINEERS会议: International Conference on Combustion Engines and Hybrid Vehicles 会议地点: INST MECH ENGINEERS HEADQUARTERS, LONDON, ENGLAND会议日期: APR 28-30, 1998会议赞助商: InstMech Engineers, Automobile Div; InstMech Engineers, Combust Engines Grp; Lucas Varity; SAE, UK; SociedadTecnicosAutomocion; Inst Marine Engines; Inst Elect Engineers; Japan SocMech Engineers来源出版物: INTERNATIONAL CONFERENCE ON COMBUSTION ENGINES AND HYBRID VEHICLES 丛书: IMECHE CONFERENCE TRANSACTIONS卷: 1998期: 4页: 137-158出版年: 1998标题: Effect of cavitation on flow and turbulence in plain orifices forhigh-speed atomization作者: He, L; Ruiz, F来源出版物: ATOMIZATION AND SPRAYS 卷: 5期: 6页: 569-584出版年: NOV-DEC 1995被引频次: 41 (来自所有数据库)Thompson, A. S., 2009, ―Experi mental Characterization of Flow Induced Vibration in Turbulent Pipe Flow,‖ M.S. thesis, Brigham Young University, Provo, UT.21Holt, G. J., 2011, ―Experimental Characterization of Baffle Plate Influence on Turbulent and Cavitation Induced Vibrations in Pipe Flow,‖ M.S. thesis, Brigham Young University, Provo, UT.Gilbarg, D., 1960, “Jets andCavities,”Handbuch der Physik, Band IX, Stromungsmechanik III, S.Fluuge, andC.Truesdell, eds., Springer-Verlag, Berlin, pp. 310–445.Pressure Losses and Limiting Reynolds Numbers for Non-Newtonian Fluids in Short Square-Edged Orifice PlatesButteurNtambaNtamba and Veruscha Fester[+] Author and Article InformationDissipation and Cavitation Characteristics of Single-Hole OrificesTullis, J. P., and Govindarajan, R., 1973, “Cavitation and Size Scale Effects for Orifices,” ASCE J. Hydr. Div., 99, pp. 417–430.umachi, F., Yamabe, M., and Oba, R., 1960, “Cavitation Effect on the Discharge Coefficient of the Sharp-Edged Orifice Plate,” ASME J. Basic Eng., 82(1), pp. 1–6. [CrossRef]Kolodzie, P. A., and Van Winkle, M., 1957, “Discharge Coefficients Through Perforated Plates,”AICHE J., 3, pp. 305–312. [CrossRef]Brennen, C. E., 1995, Cavitation and Bubble Dynamics, Oxford University Press, Oxford.9Holl, J. W., 1970, ―Nuclei and Cavitation,‖ ASME J. Basic Eng., 92(4), pp. 681–688. [CrossRef]Au-Yang, M. K., 2001, Flow Induced Vibration of Power and Process Plant Components: A Practical Workbook, ASME Press, New York.7Blevins, R. D., 1984, Applied Fluid Dynamics Handbook, Van Nostrand Reinhold Company, New York.Arndt, R. E. A., 1981, “Cavitation in Fluid Machinery and Hydraulic Structures,” Ann. Rev. Fluid Mech., 13, pp. 273–326. [CrossRef]Tullis, J. P., Powers, J. J., III, Shiers, P. F., and Hall, W. W., 1980, “Perforated Plates as Hydraulic Energy Dissipators,”Computer and Physical Modeling in Hydraulic Engineering, G.Ashton, ed., ASCE, Reston, VA, pp. 62–73.1Weaver, D. S., Ziada, S., Au-Yang, M. K., Chen, S. S., Padoussis, M. P., and Pettigrew, M. J., 2000, ―Flow-Induced Vibrations in Power and Process Plant Components: Progress and Prospects,‖ ASME J. Pressure Vessel Technol., 122(3), pp. 339–348. [CrossRef]2Testud, P., Moussou, P., Hirschberg, A., and Auregan, Y., 2007, ―Noise Generated by Cavitating Single-Hole and Multi-Hole Orifices in a Water Pipe,‖ J. Fluids Struct., 23, pp. 163–189. [CrossRef]Bohra, L. K., Mincks, L. M., and Garimella, S., 2004, “Pressure Drop Characteristics of Viscous Fluid Flow Through Orifices,” ASME Heat Transfer/Fluids Engineering Summer Conference, Charlotte, NC, July. Johansen, F. C., 1930, ―Flow Through Pipe Orifices at Low Reynolds Numbers,‖ Proc. R. Soc. London, Ser. A, 126 (801), pp. 231–245. [CrossRef]2Medaugh, F. W., and Johnson, G. D., 1940, ―Investigation of the Discharge and Coefficients of Small Circular Orifices,‖ Civil Engineering, 7 (7), pp. 422–424.3Alvi, S. H., Sridharan, K., and Lakshmana Rao, N. S., 1978, ―Loss Characteristics of Orifices and Nozzles,‖ ASM E J. Fluids Eng., 100 (3), pp. 299–307. [CrossRef]4Lakshmana Rao, N. S., Sridharan, K., and Alvi, S. H., 1977, ―Critical Reynolds Number for Orifice and Nozzle Flows in Pipes,‖ J. Hydraul. Res., 15 (2), pp. 167–178. [CrossRef]5Telis-Romero, J., Polizelli, M. A., Gabas, A. L., and TelisV. R. N., 2005, ―Friction Losses in Valves and Fittings for Viscoplastic Fluids,‖ Can. J. Chem. Eng., 83 , pp. 186–193. [CrossRef]6Bohra, L. K., Mincks, L. M., and Garimella, S., 2004, ―Pressure Drop Characteristics of Viscous Fluid Flow Through Orifices,‖ ASME Heat Tran sfer/Fluids Engineering Summer Conference, Charlotte, NC, July.7Edwards, M. F., Jadallah, M. S. M., and Smith, R., 1985, ―Head Losses in Pipe Fittings at Low Reynolds Numbers,‖ Chem. Eng. Res. Des., 63 , pp. 43–50. Available at /cgi-bin/somsid.cgi?type=header&record=17488Samanta, A. K., Banerjee, T. K., and Das, S. K., 1999, ―Pressure Losses in Orifices for the Flow of Gas-Non-Newtonian Liquids,‖ Can. J. Chem. Eng., 77 (3), pp. 579–583. [CrossRef]9ESDU International PLC, 2007, ―Incompressible Flow Through Orifice Plates–A Review of the Data in the Literature,‖ Data Item No. TN 07007.10Benedict, R. P., 1977, ―Loss Coefficients for Fluid Meters,‖ ASME J. Fluid s Eng., 99 (1) pp. 245–248. [CrossRef]11Ginsburg, I. P., 1963, "Applied Fluid Dynamics", Israel Program for Scientific Translations, Jerusalem.12Ward-Smith, A. J., 1971, "Pressure Losses in Ducted Flows", Butterworths, London.13McNeil, D. A., and Stuart, A. D., 2005, ―Highly Viscous Liquid Flow in Pipeline Components,‖ Proc. Inst. Mech. Eng., Part C: J. Mech. Eng. Sci., 219 (3), pp. 267–281. [CrossRef]14McNally Institute, 2010, ―Pump, Centrifugal Pumps, PD Pumps, Seals and Mechanical Seals Data,‖15White, F. M., 1999, "Fluid Mechanics", 4th ed., McGraw-Hill, New York.16Acheson, D. J., 1990, "Elementary Fluid Mechanics", Oxford University Press, New York.17Swamee, P. K., 2005, ―Discharge Equations for Venturimeter and Orificemeter,‖ J. Hydraul. Res., 43 (4), pp. 417–420. [CrossRef]18Miller, D. S., 1978, "Internal Flow Systems", BHRA Fluid Engineering, Cranfield, Bedfordshire.19Hooper, W. B., 1981, ―The Two-K Method Predicts Head Losses in Pipe Fittings,‖ Chem. Eng., August 24 , pp. 96–100.20Polizelli, M. A., Menegalli, F. C., Telis, V. R. N., and Telis-Romero, J., 2003, ―Friction Losses in Valves and Fittings for Power-Law Fluids,‖ Braz. J. Chem. Eng.,20 (4), pp. 455–463. [CrossRef]21Slatter, P. T., 1996, ―The Laminar/Turbulent Transition—An Industrial Problem Solved,‖ British Hydromechanics Research Group 13th International Conference on Slurry Handling and Pipeline Transport (Hydrotransport 13), Johannesburg, South Africa, Sept. 3–5.22Fester, V. G., Mbiya, B., and Slatter, P., 2008, ―Energy Losses of Non-Newtonian Fluids in Sudden Pipe Contractions,‖ Chem. Eng. J., 145 , pp. 57–63. [CrossRef]23ANSI/API, 1995, ―Manual of Petroleum Measurement Standards. Chapter 14—Natural Gas Fluids Measurement, Section 3—Concentric, Square-Edged Orifice Meters,‖ Aga Report No. 3, Part 1, Gpa 8185-90, ANSI/API 2530-1991, Parts 1, 2, 3, and 4.24Massey, B. S., 1970, "Mechanics of Fluids", 2nd ed., Van Nostrand Reinhold, New York.25Slatter, P. T., and Pienaar, V. G., 1999, ―Establishing Dynamic Similarity for Non-Newtonian Fittings Loss,‖ British Hydromechanics Research Group 14th International Conference on Slurry Handling and Pipeline Transport (Hydrotransport 14), Maastricht, The Netherlands, pp. 245–254.26Govier, G. W., and Aziz, K., 1972, "The Flow of Complex Mixture in Pipes", Van Nostrand Reinhold, New York.27Hanks, R. W., 1979, ―The Axial Laminar Flow of Yield Pseudoplastic Fluids in a Concentric Annulus,‖ Ind. Eng. Chem. Process Des. Dev., 18 (3), pp. 488–493. [CrossRef]28Lazarus, J. H., and Slatter, P. T., 1987, ―A Method for Rheological Characterization of Tube Viscometer Data,‖ J. Pipelines, 7 , pp. 165–176.29Miller, D. S., 1996, "Internal Flow: A Guide to Losses in Pipe and Duct Systems", BHRA Group, Cranfield, Bedfordshire.30Lakshmana Rao, N. S., and Sridharan, K., 1972, ―Orifice Losses for Laminar Approach Flow,‖ J. Hydraul. Div., 98 (11), pp. 2015–2034. Available at/cgi/WWWdisplay.cgi?12791731Rangaraju, K. G. and Jain, A. K., 1978, ―Energ y Loss Due to Sharp Edged Orifice Meters,‖ Irrig. Power, 35 (3) pp. 401–406. Available at /Record/IND7903051232Shima, N., 1984, ―Loss and Discharge Characteristics of a Flow of Polymer Solutions Through Pipes Orifices,‖ Bu ll. JSME, 27 (225), pp. 443–449. [CrossRef]33Humpherys, A. S., 1987, ―Energy Dissipation in Low Pressure Irrigation Pipelines: II Orifices,‖ Trans. ASAE, 30 (1), pp. 176–182. Available at /473/1/596.pdfY. Tomita and A. Shima, “Mechanisms of impulsive pressure generation and damage pit formation by bubble collapse,”J. Fluid Mech.169, 535 (1986).C.-T. Hsiao, G. L. Chahine, and H.-L. Liu, ―Scaling effect on prediction of cavitation inception in a line vortex flow,‖J. Fluids Eng.125, 53 (2003)./10.1115/1.1521956Y. Kuhn de Chizelle, S. L. Ceccio, and C. E. Brennen, “Observations and scaling of traveling bubble cavitation,”J. Fluid Mech.293, 99 (1995).Cavitation Bubbles Near BoundariesAnnual Review of Fluid MechanicsS. Gopalan, J. Katz and O. Knio, ―The flow structure in the near field of jets and its effect on cavitation inception,‖J. Fluid Mech.398, 1 (1999)./10.1017/S0022112099006072G. L. Chahine and Y. T. Shen, “Cavitation bubbles near boundaries.”J. Fluids Eng.108, 99 (1986).标题: Growth, oscillation and collapse of vortex cavitation bubbles作者: Choi, Jaehyug; Hsiao, Chao-Tsung; Chahine, Georges; 等.来源出版物: JOURNAL OF FLUID MECHANICS 卷: 624页: 255-279 DOI: 10.1017/S0022112008005430出版年: APR 10 2009标题: Prediction of tip vortex cavitation inception using coupled spherical and nonspherical bubble models and Navier-Stokes computations作者: Hsiao, CT; Chahine, G79.I. D. Pearce and A. Lichtarowicz, ―Discharge performance of long orifices with cavitating flow,‖ Proceedings of Second Fluid Power Symposium, Guildford,UK, 1971.A. Yamaguchi and T. Suzuki, “Cavitation in hydraulic fluids. Part 3: Oncavitation in long orifices,”J. Fluid Control12, 21 (1980).J. P. Tullis, “Cavitation scale effects for valves,”J. Hydraul. Div., Am. Soc. Civ. Eng.99, 1109 (1973).Flow characteristics of a micro-orificeAmmourah, S.A.a, Benim, A.C.b, Maqableh, A.M.c, Khadrawi, A.F.c, Al-Nimr, M.A.dA criterion for flow mechanisms through vertical sharp-edged orifice and model for the orifice discharge coefficientCao, R., Liu, Y., Yan, C.Flow characteristics of a micro-orificeAmmourah, S.A.a, Benim, A.C.b, Maqableh, A.M.c, Khadrawi, A.F.c, Al-Nimr, M.A.dCharacteristics of R-123 two-phase flow through micro-scale short tube orifice for design of a small cooling systemJin, S.a, Sung, T.a, Seo, T.b, Kim, J.a∙Experimental study of discharge coefficient and cavitation for different nozzle geometries ∙Kim, S.R., Ku, K.W., Hong, J.G., Lee, C.W.CFD analysis of flowfield and cavitation in aSharp-Edged circular orificeKyparissis, S.D.a, Margaris, D.P.bOFFICE CAVITATION AND ITS EFFECT ON SPRAY MIXING.(1976) Journal of Fluids Engineering, Transactions of the ASME, 98 Ser 1 (4), pp.681-687. Cited 154 times.Cavitation indices for high pressure orifice plate energydissipators(1988) International Journal of Mechanical Sciences, 30 (9), pp. 637-657.The effect of orifice plate geometry upon discharge coefficient (1990) Flow Measurement and Instrumentation, 1 (3), pp. 133-140. Cited 12 times.Flow regime transitions due to cavitation in the flow through an orifice(1990) International Journal of Multiphase Flow, 16 (6), pp. 1023-1045. Cited 46 times.Andrews, K.A., Sabersky, R.H.Flow Through an Orifice From a Transverse Stream(1990) Journal of Fluids Engineering, 112 (4), pp. 524-526. Cited 4 times.DecemberAlajbegovic, A.Three-Dimensional Cavitation Calculations in Nozzles(1999) 2nd Annual Meeting Institute ForMultifluid Science and TechnologySanta Barbara, California, USA, MarchYuan, W., Sauer, J., Schnerr, G.H.Modeling and computation of unsteady cavitation flows in injection nozzles(2001) Mecaniqueet Industries, 2 (5), pp. 383-394. Cited 36 times.doi: 10.1016/S1296-2139(01)01120-4Sato, K., Saito, Y.(2001) Unstable Cavitation Behavior In a Circular-Cylindrical Orifice Flow4th International Symposium on Cavitation, Pasadena, California, USA, JuneBorutzky, W., Barnard, B., Thoma, J.An orifice flow model for laminar and turbulent conditions(2002) Simulation Modelling Practice and Theory, 10 (3-4), pp. 141-152. Cited 38 times. Archer, A.A predictive model for cavitation erosion downstream orifices (2002) American Society of Mechanical Engineers, Fluids Engineering Division (Publication) FED, 257 (1 A), pp. 403-409.doi: 10.1115/FEDSM2002-31012Vortmann, C., Schnerr, G.H., Seelecke, S.Thermodynamic modeling and simulation of cavitating nozzle flow (2003) International Journal of Heat and Fluid Flow, 24 (5), pp. 774-783. Cited 29 times.doi: 10.1016/S0142-727X(03)00003-1Yagi, Y., Murase, M., Sato, K., Hattori, S.Mechanism of cavitation erosion at the exit of a long orifice(2003) Proceedings of the ASME/JSME Joint Fluids Engineering Conference, 1 B, pp. 1359-1364. Cited 2 times.ISBN: 0791836967Chen, Y., Lu, C.-J., Wu, L.Modelling and computation of unsteady turbulent cavitation flows (2006) Journal of Hydrodynamics, 18 (5), pp. 559-566. Cited 21 times.doi: 10.1016/S1001-6058(06)60135-2De Giorgi, G.M., Chiara, F., Ficarella, A.Experimental Study of Thermal Cavitation in an Orifice(2006) 8th ASME Conference On Engineering Systems Design and Analysis, 1, pp. 523-529.。
Aquatic Animal Embryonic Stage
Aquatic Animal Embryonic Stage Embryonic development in aquatic animals is a fascinating and complex process that plays a crucial role in the survival and evolution of these species. From the moment of fertilization to hatching, aquatic animal embryos undergo a series of intricate changes that ultimately determine their growth and development into mature individuals. In this discussion, we will explore the various stages of embryonic development in aquatic animals, the factors that influence this process, and the significance of understanding these stages for conservation and research purposes. The first stage of embryonic development in aquatic animals begins with fertilization, where sperm and egg cells unite to form a zygote. This initial step is crucial for the creation of a genetically unique individual and sets the foundation for all subsequent developmental processes. In many aquatic species, fertilization occurs externally, in the water, while others may have internal fertilization mechanisms. The timing and location of fertilization can varygreatly among different aquatic animals, depending on their reproductivestrategies and environmental conditions. Following fertilization, the zygote undergoes rapid cell division through a process known as cleavage. During this stage, the embryo does not increase in size but instead divides into smaller cells called blastomeres. Cleavage is essential for the formation of a multicellular embryo and sets the stage for the next developmental processes, including gastrulation and organogenesis. The timing and pattern of cleavage can vary among different aquatic animals, reflecting their evolutionary history and ecological adaptations. Gastrulation is a critical stage in embryonic development where the three primary germ layers – ectoderm, mesoderm, and endoderm – are established. This process involves the migration and rearrangement of cells to form distinct tissue layers that will give rise to different organs and structures in the developing embryo. The formation of these germ layers is essential for the differentiation and specialization of cells, ultimately leading to the development of complex body structures in aquatic animals. The precise mechanisms of gastrulation can vary among different species, reflecting their unique developmental pathways and evolutionary relationships. Organogenesis is the next stage in embryonic development, where the rudimentary organs and structures beginto form and take shape. During this process, the cells within the germ layers differentiate and specialize to give rise to specific tissues and organs, such as the nervous system, muscles, and digestive system. Organogenesis is a highly coordinated and regulated process that is influenced by a combination of genetic and environmental factors. Disruptions or abnormalities during organogenesis can lead to developmental defects and impairments in aquatic animals, highlighting the importance of understanding the underlying mechanisms of this stage. As the embryo continues to develop, it undergoes further growth and maturation, leading up to the final stage of hatching or birth. The timing and process of hatching can vary greatly among different aquatic animals, depending on their species-specific adaptations and environmental conditions. Some aquatic animals may hatch fromtheir eggs as larvae, while others may undergo direct development and emerge as miniature versions of the adult. The hatching process is a critical transition point in the life cycle of aquatic animals, marking the beginning of their independent existence outside the protective confines of the egg. In conclusion, embryonic development in aquatic animals is a complex and dynamic process that shapes the growth and evolution of these species. From fertilization to hatching, aquatic animal embryos undergo a series of intricate stages that determine their ultimate form and function. Understanding the mechanisms and factors that influence embryonic development in aquatic animals is essential for conservation efforts, research initiatives, and the overall appreciation of the diversity and complexity of life in aquatic environments. By studying and preserving the embryonic stages of aquatic animals, we can gain valuable insights into their biology, behavior, and ecological roles, ultimately contributing to the conservation and sustainability of these fascinating creatures.。
声动力疗法的机制研究进展
·综述·声动力疗法(sonodynamic therapy,SDT)是一种组织穿透性良好、精度高、副作用小的无创治疗手段,其通过靶向照射病灶区的声敏剂触发特定效应,以物理和化学的机制诱导线粒体功能障碍、细胞程序性死亡、组织或细胞膜间隙的改变和调节免疫微环境[1-2]。
具体指利用超声局部定位的性质,将能量聚焦于恶性肿瘤发生部位,激活肿瘤细胞中的声敏剂,对于肿瘤的治疗具有较高选择性且对周围正常组织损伤较小,与传统放化疗相比展现出显著的优越性。
目前,对SDT机制的研究主要认为是通过空化效应和声敏剂促进活性氧(ROS)的产生和钙超载的出现,进而激活下游信号通路。
本文就空化效应和机械力效应产生ROS诱导钙超载途径进行综述。
一、空化效应空化效应是一种物理作用,其在超声波作用下引起微气泡压力持续变化,通过收缩和膨胀来动态响应压力变化。
当以足够振幅激发时,气泡半径和外部压力呈不均匀状态,提示气泡可能在坍塌时出现反弹,或表现出膨胀或完全内爆,此过程即空化效应,主要分为惯性空化和稳定(非惯性)空化。
1.惯性空化:是指高强度超声波引起空化微泡的迅速膨胀和急剧收缩,在短时间内微泡大量破裂,从而产生强烈的喷射、冲击波和局部高温高压。
其主要应用于消融术等靶向治疗手段,如原发性或帕金森性震颤患者的无创丘脑切开术[3]。
其具体作用机制为:气泡的坍塌引起流体动力流动的不对称性,导致液体射流优先指向表面。
射流不仅造成了机械损伤,而且在非对称坍塌过程中产生的旋涡环也会出现声致光现象。
声致光可以产生自由基,因此在气泡周围的大分子中,这是一个机械和化学反应的交叉区域。
2.稳定空化:是指低强度超声波引起空化微泡小范围内的持续震荡,从而增强核心气体向外扩散的速率,有利于载体转运至胞内。
其具体作用机制为:低强度超声波导致气泡周围产生微流。
这种微流将驱散气泡附近的边界层,化学物质将迅速声动力疗法的机制研究进展蒋恩琰王丹张照霞张梓宸王韫智梁子彬刘飞陈磊摘要声动力疗法是一种组织穿透性良好、精度高、副作用小的无创治疗手段。
小学上册第十四次英语第2单元测验试卷
小学上册英语第2单元测验试卷英语试题一、综合题(本题有100小题,每小题1分,共100分.每小题不选、错误,均不给分)1.My _______ (猫) enjoys chasing after toys.2.The bear searches for food in the _____.3. A star's brightness is measured in _____.4.I enjoy ______ (painting) pictures.5.The __________ (历史的多元性) enrich dialogue.6.My dad is a great __________ (听众) when I talk.7.What is the name of the famous festival celebrated in Mexico?A. Day of the DeadB. Cinco de MayoC. Independence DayD. Thanksgiving8. A kangaroo can jump very ______ (高).9. A _______ is a type of bond formed by the attraction between oppositely charged ions.10. A ________ (社区花园) fosters cooperation.11.I believe that sharing is caring. I like to share __________ with my friends.12.What is the capital of Mongolia?A. UlaanbaatarB. ErdenetC. DarkhanD. Choibalsan13.What do you call the person who teaches you in school?A. DoctorB. TeacherC. FarmerD. Engineer答案:B14.My sister is good at playing ____ (board games).15.The capital of Jamaica is ________ (金斯顿).16.What do we call a scientist who studies plants?A. BotanistB. ZoologistC. EcologistD. Geologist答案:A17.The tortoise's shell protects it from ______ (捕食者).18.What do we call a story with a moral lesson, often featuring animals?A. FableB. MythC. TaleD. Novel答案:A19.What is the opposite of 'happy'?A. JoyfulB. SadC. ExcitedD. Angry答案:B20.What do you call a person who travels in space?A. AstronautB. PilotC. ScientistD. Explorer答案:A21.I love my _____ (玩具车) collection.22.The main role of enzymes in the body is to act as ______.23.What is your name in English?A. NameB. TitleC. IdentityD. Label24.What color do you get when you mix blue and yellow?A. GreenB. OrangeC. PurpleD. Brown答案:A25.What is the name of the famous musician known for his "Sgt. Pepper's Lonely Hearts Club Band"?A. Elvis PresleyB. The BeatlesC. Michael JacksonD. Bob Dylan答案:B26.The main product of combustion is _______.27. (Norse) mythology features gods like Odin and Thor. The ____28.What is the capital of Brazil?A. Rio de JaneiroB. BrasíliaC. São PauloD. Salvador答案:B29.I like to play with my ______ (玩具车) in the living room. It goes ______ (快).30. A ______ is an animal that has feathers.31.What is the shape of a ball?A. SquareB. TriangleC. CircleD. Rectangle答案:C32.The __________ (种植者) carefully watered the seedlings.33.My uncle tells the best __________ (笑话).34.The country known for its coffee is ________ (巴西).35.The _____ (植物发展战略) can lead to sustainable practices.36.The stars are _____ (twinkling/shining) in the sky.37.The _____ (花色) varies depending on the species.38.We have a ______ (快乐的) family gathering every month.39.I hope to one day see the ________ (大堡礁).40.We are going to the ______ (mall) tomorrow.41.The weather is ___ (nice) today.42.What is the name of the place where we watch movies?A. TheaterB. MuseumC. GalleryD. Library答案:A43. A _______ is a substance that donates protons in a reaction.44.My favorite subject is ________ (science).45. A solution that can dissolve more solute is called a _______ solution.46.She is wearing a fancy ___. (dress)47.The Earth's surface is made up of various ______.48.The main gas produced during fermentation is _______.49.Martin Luther King Jr. fought for __________ (平等权利) for African Americans.50.My grandmother tells the best __________ (故事).51.The ________ (植物健康) is monitored closely.52.The _____ (飞机) flies high.53.The ancient Romans were skilled in _____ and law.54.________ (植物可持续性) is vital for future.55.The __________ is an area of high elevation. (高原)56.The chemical symbol for manganese is ______.57.The __________ (历史的影响力) can shift over time.58.What do we call the frozen form of water?A. SteamB. IceC. LiquidD. Gas答案:B59.The invention of the microscope advanced the field of _____.60.How many constellations are officially recognized by astronomers?A. 48B. 88C. 100D. 12061.The ice cream is _____ (melting/frozen).62.The ________ was a major conflict fought in the 20th century.63.What do you call a baby elephant?A. CalfB. CubC. PupD. Kid64. (Titanic) sank in 1912 after hitting an iceberg. The ____65.I can ______ (担任) a leadership role.66.The ________ was a significant period in the history of Russia.67.Baking soda is a ______ used in cooking.68.The _______ (The Holocaust) resulted in the genocide of millions during WWII.69.My ________ (玩具名称) is a fun way to express my thoughts.70.The main source of protein is _____.71.I enjoy baking ______ (蛋糕) for my friends’ birthdays.72. A ______ (蜜蜂) is essential for pollination.73.The __________ (历史的旅程) is ongoing.74.We will go ______ to see the fireworks. (outside)75.What do you call an animal that only eats plants?A. CarnivoreB. OmnivoreC. HerbivoreD. Insectivore答案:C76.The frog's skin can absorb ______ (水).77. A strong base can cause chemical ______.78.I want to _____ (visit) the zoo.79.What is the name of the famous painting by Leonardo da Vinci?A. The Starry NightB. The Mona LisaC. The Last SupperD. The Scream80. (Medieval) Church played a significant role in European life. The ____81.Galaxies can collide and form larger ______.82.The _____ (children/adults) are playing outside.83.The cake is ________ chocolate.84.Do you like _______ (冰淇淋)?85.What do you call the main character in a story?A. ProtagonistB. AntagonistC. Supporting CharacterD. Narrator答案:A86.What is the capital of South Korea?A. SeoulB. BusanC. IncheonD. Daegu答案:A87. A ____ is known for its hopping abilities.88. A beam of light can be ______ by a mirror.89.The jellyfish has a _______ (透明) body.90. A dragonfly is known for its ______ flying ability.91.The visible spectrum of light can be separated using a ______.92.The capybara is a social ________________ (动物).93.How many bones are there in the adult human body?A. 206B. 210C. 202D. 200答案:A94.What do you call the time it takes for the Earth to rotate once on its axis?A. MonthB. YearC. DayD. Hour95.Many galaxies are moving away from us, suggesting the universe is ______.96.What is the name of the longest river in the world?A. AmazonB. NileC. YangtzeD. Mississippi97.The _____ (藤蔓) grows on the fence.98.I think that connecting with nature helps us appreciate its __________.99.The ______ of an element is determined by the number of protons.100.What do we call the seasons that occur after summer?A. WinterB. SpringC. FallD. Autumn答案:C。
- 1、下载文档前请自行甄别文档内容的完整性,平台不提供额外的编辑、内容补充、找答案等附加服务。
- 2、"仅部分预览"的文档,不可在线预览部分如存在完整性等问题,可反馈申请退款(可完整预览的文档不适用该条件!)。
- 3、如文档侵犯您的权益,请联系客服反馈,我们会尽快为您处理(人工客服工作时间:9:00-18:30)。
Won-Tae Kang Changwon National University 9 Sarim-dong, Changwon 641-773, Korea
Ki Han Yu Hyosung Goodsprings, Inc. 43-1, Ungnam-dong, Changwon 641-290, Korea
Copyrigh the other hand, due to the high cost for design and
physical model test CFD analysis has recently considered as an effective tool to evaluate the flow around the suction intake in pumps. Iwano et al.[5] made a trial of an application of a numerical prediction method of a submerged vortex to the flow in pump sumps in order to increase the vortex resolution by the conventional code based on the Reynolds Averaged NavierStokes equations. Detailed vortex flow phenomena including vortex cavitation, submerged vortex, vortex breakdown and vortex filament were investigated at the flow simulation around bell mouth with and without baffle plate in the single intake. Chen and Guo[6] calculated a turbulent flow in the multiintakes sump of the pump station with several water intakes at different flow rate as well as water levels by using the FLUENT software. By imposing a reasonable boundary condition for the flow in the sump, they showed that predicted velocity profiles at several sections of sump could be compared well with experiments. Regarding the CFD prediction and model experiment on suction vortices in pump sump, recently Okamura et al.[7] performed a benchmark test by using several CFD commercial codes and reviewed the results to check their applicability to the design of the pump station instead of the expensive conventional experimental method. Kim et al.[8] studied about the characteristics of the subsurface vortex in the three-different pump sump and showed the usefulness of CFD to predict the subsurface vortex generation. Like this, many parametric studies to increase hydraulic performance of pump intakes have made as reviewed so far. Unfortunately, however, detailed behavior of free surface and subsurface vortices, minimum water levels incepting the vortices, swirling angle and so on are not investigated yet.
heads. However, during pump operation, cavitation, flow separation, pressure loss, vibration and noise occur often by flow unsteadiness and abnormality. Especially, air-entrained free and subsurface vortices observed in sump pumps seriously damage to pump system. According to the HI standard of Hydraulic Institute HI[1] or JSME criteria for a pump sump design[2], therefore, these vortices should be prevented and their disappearance must be verified by sump pump model test in the construction of pump station.
INTRODUCTION Pump system is one of the most important fluid machine
system which delivers the energy to fluid by impeller. This system is used commonly in the industry because it has simple structure and covers a wide range of discharge flow rates and
To reduce these vortices and for the advanced pump sump design with high performance, it is very important to know the detailed flow information in sump system. For this purpose, to date many researchers have made experimental and numerical studies on the flow in pump sump. For instance, Johansson et al.[3] did a model study of sump by a physical test and a CFD, and presented advancements that have been made in the field of hydraulic modeling of pump intakes. How hydraulic models are used to identify unacceptable flow conditions such as surface vortices, any high swirl, pre-rotation and non-uniform axial velocity distribution at the bell mouth, and used to derive modifications to improve the hydraulic performance for both circulating water and cooling water pump intakes were shown. A detailed velocity distribution around the submerged vortex cavitation in a pump intake were investigated by means of PIV (particle image velocimetry) by Nagahara et al.[4]. As an apparatus, a pressure tank was used to control the mean inlet velocity, the circulation and the pressure at the pump intake bell mouth with the model suction. Measured data such as velocities around vortex and core radii of cavitating vortices were compared with CFD predictions and discussed about this
ABSTRACT A numerical and an experimental investigation on a suction
vortices including cavitation, free vortices and subsurface vortices behavior in the model sump system with multi-intakes is performed at several flow rates and water levels. A test model sump and piping system were designed based on Froude similitude for the prototype of the recommended structure layout by HI-9.8 American National Standard for Pump Intake Design of the Hydraulic Institute. An experiment is performed according to the sump model test procedure of Hyosung Goodsprings, Inc. A numerical analysis of three dimensional multiphase flows through the model sump is performed by using the finite volume method of the CFX code with multi-block structured grid systems. A k-ω Shear Stress Transport turbulence model and the Rayleigh-Plesset cavitation model are used for solving turbulence cavitating flow. Several types of free surface and submerged vortex which occurs with each different water level are identified through the experimental investigation. From the numerical analysis, the vortices are reproduced and their formation, growing, shedding and detailed vortex structures are investigated. To reduce abnormal vortices, an anti-vortex device is considered and its effect is investigated and discussed.