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June 13, 2011, 01:06 |
Basic Nozzle-Expander Design
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#1 |
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Hi all,
I am proceeding towards design of a nozzle-expander system. Please help me in understanding the output and correct geometry if needed. I have uploaded images showing my input in Vista-RTD, input in CFX and final results of velocity profile. Expander design 1. I input required parameters as shown in Vista-RTD for the expander and created the Expander geometry in BladeGen. I have included input of each step from Vista-RTD. Nozzle design 2. I used the nozzle assumption on Pic 1 from Vista-RTD to create a nozzle in BladeGen. 3. I used the inlet velocity triangle on Pic 4 to match the RELATIVE INLET FLOW ANGLE (W2) = 40.66 degrees required by expander to match the nozzle ABSOLUTE FLOW ANGLE. CFX Input 4.I brought in CFX-MESH for both expander and nozzle and show my input in Pic 6. I input same inlet pressure and temperature as in Vista-RTD and same outlet mass flowrate (0.23 kg/s divided by 13 blade passages = 0.0176 kg/s) as in Vista-RTD. I used conditions at inlet of expander to be same as inlet of nozzle for the time being since I didn't analyze the nozzle separately (I hope this doesn't affect the flow angle problem I am witnessing in the results!) CFX-Post 5.I have attached the velocity profile I obtain in Pic 7. As I interpret it I can see separation and possibly the inlet flow angle to the expander is not correct?. Question- 6. Please help understand the interpretation from the velocity profile I obtained how to correct the geometry or any input I have mistaken. Thank you all for your previous help to familiarize myself with the programs and now I need help to understand results and interprete to create a proper geometry. Karmavatar |
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June 15, 2011, 02:24 |
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#2 |
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Anybody please to help me on this topic.
Mr. Glenn Horrocks if you could help me please. Thank you, |
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June 15, 2011, 08:48 |
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#3 |
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Glenn Horrocks
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But what are you trying to do? Looks like a blade geometry with lots of big separations to me so it does not appear to be operating well.
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June 16, 2011, 02:31 |
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#4 |
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Glenn,
Yes, there are lot of separations. But I am not able to understand how to correct it. I matched nozzle absolute velocity direction to rotor relative velocity direction and I have see big separation. Please give me some direction what to check and look for to correct this. Thank you, Karmavatar |
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June 16, 2011, 09:02 |
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#5 |
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Glenn Horrocks
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I have no experience in rotating machinery design. Looks like you need to get some textbooks on rotating machinery design.
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June 17, 2011, 20:52 |
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#6 |
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Thanks Glenn.
Anybody who is working on either turbine or compressor blade geometry and simulation, I would appreicate if you could give me a direction on this. Thank you, Karmavatar |
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July 2, 2015, 22:01 |
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#7 |
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soong young
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hI karmavatar
I have some difficulties in creating a nozzle in Ansys ,I found you had made it . Did you create the nozzle in the VISTA RTD or you design it in the Bladegen ? Thank you |
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January 15, 2016, 00:23 |
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#8 |
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Hello,
Please help with my questions. How to correct blade geometry by looking at results. Blade geometry was created for certain input by Bladegen. But, CFD results don't match with inputs. Thanks in advance. |
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January 15, 2016, 00:48 |
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#9 |
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Glenn Horrocks
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How to fix a blade design - look in a turbomechinery design textbook.
Inaccurate results - This is an FAQ: http://www.cfd-online.com/Wiki/Ansys..._inaccurate.3F |
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January 15, 2016, 03:49 |
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#10 |
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Thomas
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Hi, I've got expierences about turbomachinery. Could you upload your CCL from Solver? Then it will be easier to help you And also put here more images, for example view from preprocessor to see how you set up boundary conditions.
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January 15, 2016, 14:58 |
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#11 |
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Thank you tomson199 for replying.
I will upload CCL solver in next few days. I have background in turbomachinery and have extensive course work using books like Dixon, Wilson, Aungier etc. and for CFD like Anderson and understand the equations, terminology and the language. I understand inverse solver and equations for creating geometry like BladeGen. I understand pros and cons of different types of meshing in CFD. Except I haven't been able to go through the CFD software portion of it, successfully yet.. not even once.... due to lack of a guide or guidance. I simply want to know and understand if it is traditional or typical method or usual practice to look at output characteristics (flow separations, pressure, entropy etc.) of the impeller/diffuser etc. and then go back manually to edit the blade profile. Is this iterative process typically done by trial and error?. As Bladegen created the geometry using those inputs, I was expecting CFD outputs to be close (not exact) to those inputs, and that I would need to make minimal changes to the blade profile (for next iterations). But, the results are so off. I will check my inputs to CFX again. Thank you very much for extending help. |
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January 20, 2016, 18:47 |
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#12 |
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Hello Thomas,
Please find below CCL details. I will post pictures if required. Thank you, +--------------------------------------------------------------------+ | | | CFX Command Language for Run | | | +--------------------------------------------------------------------+ LIBRARY: MATERIAL: Air Ideal Gas Material Description = Air Ideal Gas (constant Cp) Material Group = Air Data, Calorically Perfect Ideal Gases Option = Pure Substance Thermodynamic State = Gas PROPERTIES: Option = General Material EQUATION OF STATE: Molar Mass = 28.96 [kg kmol^-1] Option = Ideal Gas END SPECIFIC HEAT CAPACITY: Option = Value Specific Heat Capacity = 1.0044E+03 [J kg^-1 K^-1] Specific Heat Type = Constant Pressure END REFERENCE STATE: Option = Specified Point Reference Pressure = 1 [atm] Reference Specific Enthalpy = 0. [J/kg] Reference Specific Entropy = 0. [J/kg/K] Reference Temperature = 25 [C] END DYNAMIC VISCOSITY: Dynamic Viscosity = 1.831E-05 [kg m^-1 s^-1] Option = Value END THERMAL CONDUCTIVITY: Option = Value Thermal Conductivity = 2.61E-2 [W m^-1 K^-1] END ABSORPTION COEFFICIENT: Absorption Coefficient = 0.01 [m^-1] Option = Value END SCATTERING COEFFICIENT: Option = Value Scattering Coefficient = 0.0 [m^-1] END REFRACTIVE INDEX: Option = Value Refractive Index = 1.0 [m m^-1] END END END END FLOW: Flow Analysis 1 SOLUTION UNITS: Angle Units = [rad] Length Units = [m] Mass Units = [kg] Solid Angle Units = [sr] Temperature Units = [K] Time Units = [s] END ANALYSIS TYPE: Option = Steady State EXTERNAL SOLVER COUPLING: Option = None END END DOMAIN: Expander Coord Frame = Coord 0 Domain Type = Fluid Location = PassageBody1 BOUNDARY: Expander Blade Boundary Type = WALL Frame Type = Rotating Location = Blade1 BOUNDARY CONDITIONS: HEAT TRANSFER: Option = Adiabatic END MASS AND MOMENTUM: Option = No Slip Wall END WALL ROUGHNESS: Option = Smooth Wall END END END BOUNDARY: Expander Hub Boundary Type = WALL Coord Frame = Coord 0 Frame Type = Rotating Location = Hub1 BOUNDARY CONDITIONS: HEAT TRANSFER: Option = Adiabatic END MASS AND MOMENTUM: Option = No Slip Wall END WALL ROUGHNESS: Option = Smooth Wall END END END BOUNDARY: Expander Outlet Boundary Type = OUTLET Frame Type = Stationary Location = Outflow1 BOUNDARY CONDITIONS: FLOW REGIME: Option = Subsonic END MASS AND MOMENTUM: Mass Flow Rate = 0.216154 [kg s^-1] Option = Mass Flow Rate END END END BOUNDARY: Expander Shroud Boundary Type = WALL Coord Frame = Coord 0 Frame Type = Rotating Location = Shroud1 BOUNDARY CONDITIONS: HEAT TRANSFER: Option = Adiabatic END MASS AND MOMENTUM: Option = No Slip Wall WALL VELOCITY: Option = Counter Rotating Wall END END WALL ROUGHNESS: Option = Smooth Wall END END END BOUNDARY: Expander to Expander Periodic 1 Side 1 Boundary Type = INTERFACE Location = PeriodicA1 BOUNDARY CONDITIONS: HEAT TRANSFER: Option = Conservative Interface Flux END MASS AND MOMENTUM: Option = Conservative Interface Flux END TURBULENCE: Option = Conservative Interface Flux END END END BOUNDARY: Expander to Expander Periodic 1 Side 2 Boundary Type = INTERFACE Location = PeriodicB1 BOUNDARY CONDITIONS: HEAT TRANSFER: Option = Conservative Interface Flux END MASS AND MOMENTUM: Option = Conservative Interface Flux END TURBULENCE: Option = Conservative Interface Flux END END END BOUNDARY: Expander to Nozzle Interface Side 2 Boundary Type = INTERFACE Location = Inflow1 BOUNDARY CONDITIONS: HEAT TRANSFER: Option = Conservative Interface Flux END MASS AND MOMENTUM: Option = Conservative Interface Flux END TURBULENCE: Option = Conservative Interface Flux END END END DOMAIN MODELS: BUOYANCY MODEL: Option = Non Buoyant END DOMAIN MOTION: Alternate Rotation Model = true Angular Velocity = 30000 [rev min^-1] Option = Rotating AXIS DEFINITION: Option = Coordinate Axis Rotation Axis = Coord 0.3 END END MESH DEFORMATION: Option = None END REFERENCE PRESSURE: Reference Pressure = 1 [atm] END END FLUID DEFINITION: Air Ideal Gas Material = Air Ideal Gas Option = Material Library MORPHOLOGY: Option = Continuous Fluid END END FLUID MODELS: COMBUSTION MODEL: Option = None END HEAT TRANSFER MODEL: Option = Total Energy END THERMAL RADIATION MODEL: Option = None END TURBULENCE MODEL: Option = k epsilon END TURBULENT WALL FUNCTIONS: High Speed Model = Off Option = Scalable END END END DOMAIN: Nozzle Coord Frame = Coord 0 Domain Type = Fluid Location = PassageBody1 2 BOUNDARY: Expander to Nozzle Interface Side 1 Boundary Type = INTERFACE Location = Outflow1 2 BOUNDARY CONDITIONS: HEAT TRANSFER: Option = Conservative Interface Flux END MASS AND MOMENTUM: Option = Conservative Interface Flux END TURBULENCE: Option = Conservative Interface Flux END END END BOUNDARY: Nozzle Blade Boundary Type = WALL Location = Blade1 2 BOUNDARY CONDITIONS: HEAT TRANSFER: Option = Adiabatic END MASS AND MOMENTUM: Option = No Slip Wall END WALL ROUGHNESS: Option = Smooth Wall END END END BOUNDARY: Nozzle Hub Boundary Type = WALL Location = Hub1 2 BOUNDARY CONDITIONS: HEAT TRANSFER: Option = Adiabatic END MASS AND MOMENTUM: Option = No Slip Wall END WALL ROUGHNESS: Option = Smooth Wall END END END BOUNDARY: Nozzle Inlet Boundary Type = INLET Location = Inflow1 2 BOUNDARY CONDITIONS: FLOW DIRECTION: Option = Normal to Boundary Condition END FLOW REGIME: Option = Subsonic END HEAT TRANSFER: Option = Total Temperature Total Temperature = 390 [K] END MASS AND MOMENTUM: Option = Total Pressure Relative Pressure = 1580 [kPa] END TURBULENCE: Option = Medium Intensity and Eddy Viscosity Ratio END END END BOUNDARY: Nozzle Shroud Boundary Type = WALL Location = Shroud1 2 BOUNDARY CONDITIONS: HEAT TRANSFER: Option = Adiabatic END MASS AND MOMENTUM: Option = No Slip Wall END WALL ROUGHNESS: Option = Smooth Wall END END END BOUNDARY: Nozzle to Nozzle Periodic 1 Side 1 Boundary Type = INTERFACE Location = PeriodicA1 2 BOUNDARY CONDITIONS: HEAT TRANSFER: Option = Conservative Interface Flux END MASS AND MOMENTUM: Option = Conservative Interface Flux END TURBULENCE: Option = Conservative Interface Flux END END END BOUNDARY: Nozzle to Nozzle Periodic 1 Side 2 Boundary Type = INTERFACE Location = PeriodicB1 2 BOUNDARY CONDITIONS: HEAT TRANSFER: Option = Conservative Interface Flux END MASS AND MOMENTUM: Option = Conservative Interface Flux END TURBULENCE: Option = Conservative Interface Flux END END END DOMAIN MODELS: BUOYANCY MODEL: Option = Non Buoyant END DOMAIN MOTION: Option = Stationary END MESH DEFORMATION: Option = None END REFERENCE PRESSURE: Reference Pressure = 1 [atm] END END FLUID DEFINITION: Air Ideal Gas Material = Air Ideal Gas Option = Material Library MORPHOLOGY: Option = Continuous Fluid END END FLUID MODELS: COMBUSTION MODEL: Option = None END HEAT TRANSFER MODEL: Option = Total Energy END THERMAL RADIATION MODEL: Option = None END TURBULENCE MODEL: Option = k epsilon END TURBULENT WALL FUNCTIONS: High Speed Model = Off Option = Scalable END END END DOMAIN INTERFACE: Expander to Expander Periodic 1 Boundary List1 = Expander to Expander Periodic 1 Side 1 Boundary List2 = Expander to Expander Periodic 1 Side 2 Interface Type = Fluid Fluid INTERFACE MODELS: Option = Rotational Periodicity AXIS DEFINITION: Option = Coordinate Axis Rotation Axis = Coord 0.3 END END MESH CONNECTION: Option = Automatic END END DOMAIN INTERFACE: Expander to Nozzle Interface Boundary List1 = Expander to Nozzle Interface Side 1 Boundary List2 = Expander to Nozzle Interface Side 2 Interface Type = Fluid Fluid INTERFACE MODELS: Option = General Connection FRAME CHANGE: Option = Frozen Rotor END MASS AND MOMENTUM: Option = Conservative Interface Flux MOMENTUM INTERFACE MODEL: Option = None END END PITCH CHANGE: Option = Value Pitch Ratio = 1 END END MESH CONNECTION: Option = GGI END END DOMAIN INTERFACE: Nozzle to Nozzle Periodic 1 Boundary List1 = Nozzle to Nozzle Periodic 1 Side 1 Boundary List2 = Nozzle to Nozzle Periodic 1 Side 2 Interface Type = Fluid Fluid INTERFACE MODELS: Option = Rotational Periodicity AXIS DEFINITION: Option = Coordinate Axis Rotation Axis = Coord 0.3 END END MESH CONNECTION: Option = Automatic END END OUTPUT CONTROL: MONITOR OBJECTS: EFFICIENCY OUTPUT: Inflow Boundary = Nozzle Inlet Option = Output To Solver Monitor Outflow Boundary = Expander Outlet END MONITOR BALANCES: Option = Full END MONITOR FORCES: Option = Full END MONITOR PARTICLES: Option = Full END MONITOR RESIDUALS: Option = Full END MONITOR TOTALS: Option = Full END END RESULTS: File Compression Level = Default Option = Standard END END SOLVER CONTROL: Turbulence Numerics = First Order ADVECTION SCHEME: Option = High Resolution END CONVERGENCE CONTROL: Length Scale Option = Conservative Maximum Number of Iterations = 100 Minimum Number of Iterations = 1 Timescale Control = Auto Timescale Timescale Factor = 1.0 END CONVERGENCE CRITERIA: Residual Target = 1.E-4 Residual Type = RMS END DYNAMIC MODEL CONTROL: Global Dynamic Model Control = On END END END COMMAND FILE: Version = 13.0 Results Version = 13.0 END SIMULATION CONTROL: EXECUTION CONTROL: EXECUTABLE SELECTION: Double Precision = Off END INTERPOLATOR STEP CONTROL: Runtime Priority = Standard MEMORY CONTROL: Memory Allocation Factor = 1.0 END END PARALLEL HOST LIBRARY: HOST DEFINITION: Host Architecture String = winnt Installation Root = D:\Program Files\ANSYS Inc\v%v\CFX END END PARTITIONER STEP CONTROL: Multidomain Option = Independent Partitioning Runtime Priority = Standard EXECUTABLE SELECTION: Use Large Problem Partitioner = Off END MEMORY CONTROL: Memory Allocation Factor = 1.0 END PARTITIONING TYPE: MeTiS Type = k-way Option = MeTiS Partition Size Rule = Automatic END END RUN DEFINITION: Run Mode = Full Solver Input File = CFX.def END SOLVER STEP CONTROL: Runtime Priority = Standard MEMORY CONTROL: Memory Allocation Factor = 1.0 END PARALLEL ENVIRONMENT: Number of Processes = 1 Start Method = Serial END END END END |
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January 21, 2016, 02:33 |
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#13 |
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Screenshots 1 through 5
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January 21, 2016, 02:34 |
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#14 |
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Screenshots 6 through 10
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January 21, 2016, 02:36 |
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#15 |
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Screenshots 11 through 15
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January 22, 2016, 13:14 |
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#16 |
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Thomas
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Hi karmavatar.
In the first look I think that you did mistake in this turbine design. Are you compare your desing with hand made calculations? Because you used a cp=1712 J/kgK and gas constant R=317 J/kgK and then you use in CFX air as ideal gas when those parameters are different. Secondly why you applied expansion ratio 9? This is too big, because you cannot expand gas above 2,58 pressure ratio if you don't use convergent-divergent nozzle. The last think is pitch ratio. You have 9 blades of nozzle and 13 blades of expander, and you cannot apply this values. In the one side it should be 360/13 and the second side you should use 360/9. |
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January 22, 2016, 17:07 |
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#17 |
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Hey,
I do not fully understand your questions. Are you asking why there are big flow separations in the plot? To see more details accurately, you need to see the relative Mach contours along near the hub and midspan and near the shroud, at least 3 sections. The rotor inlet (2) velocity triangle cartoon implies a CW rotation, but the nozzle cartoon itself shows a CCW rotation of the rotor. The nozzle outlet angle should be aligned with V2 (rotor absolute inlet flow), not with W2 (rotor relative inlet flow). By the combination of blade velocity U2, the relative inlet velocity W2 is found to be aligned with the rotor incidence angle. Every your velocity triangle does not match with those pictures. Because of the wrong design, in the CFX velocity contours you can see the wrong direction of velocity vector at the rotor inlet. The correct design should show the flow vector from top to bottom at the rotor inlet. Please compare yours with what I attached here (found from web). Why do your rotor parts look apart in the velocity contour plot, BTW? What you are dealing with is called the radial-inflow turbine which we can easily see in turbochargers. Last edited by turbo; January 23, 2016 at 00:29. |
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January 26, 2016, 16:27 |
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#18 |
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Thank you Thomas, Thank you Turbo
Turbo has identified a fundamental problem with velocity diagram with my Bladegen. What I need is a CCW rotating Radial Turbine, for which velocity diagrams should be as in attached picture, but Bladegen velocity diagram is opposite, although the 3D geometry of the expander wheel appear correct. I am trying to figure out how to correct this velocity triangle (from forums and Bladegen help files), but Turbo if you know already, please help. I also understood that "The nozzle outlet angle should be aligned with V2 (rotor absolute inlet flow), not with W2 (rotor relative inlet flow)". Thank you |
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January 26, 2016, 16:53 |
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#19 |
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Why don't you go back to the starting line? Your meanline design (Vista whatever) was totally wrong.
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March 20, 2016, 00:29 |
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#20 |
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Please suggest software to create impeller geometry other than Ansys.
I have seen demo of Axstream and looking for similar software names. Thank you |
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