CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > Software User Forums > ANSYS > CFX

Waterwheel shaped turbine inside a pipe simulation problem

Register Blogs Community New Posts Updated Threads Search

 
 
LinkBack Thread Tools Search this Thread Display Modes
Prev Previous Post   Next Post Next
Old   December 1, 2014, 10:57
Default Waterwheel shaped turbine inside a pipe simulation problem
  #1
New Member
 
Mohaimin Shahed
Join Date: Nov 2014
Posts: 2
Rep Power: 0
mshahed91 is on a distinguished road
Hello Everyone,

I am very new to CFD and I have carried out a simulation for a undershot waterwheel placed inside a pipeline. Currently I have used a rigid body for my waterwheel, and have two domains, one for the region surrounding the rigid body and another for the remainder of the pipe. I have specified my rotor domain as a subdomain with the option of rigid body solution and have also used a wall boundary condition for the wheel walls with the option of rigid body solution.

To calculate power, I use different external torques (on the opposite direction to rotation) on the rigid body and see what my final angular velocity and try to find the optimum torque for which I have max power (Torque times angular velocity). I have attached several images to help explain what I have done. I would greatly appreciate any suggestions to help improve the accuracy of my simulation since I am not sure I am doing it right.

Best Regards,
Mohaimin

LIBRARY:
COORDINATE FRAME DEFINITIONS:PlotData.png

BackView.JPG

IsoView.JPG

Setupview.jpg

WireframeView.JPG
COORDINATE FRAME: Coord 1
Axis 3 Point = 0.0[m],0.0[m],1.0[m]
Coord Frame Type = Cartesian
Option = Axis Points
Origin Point = 0.0[m],0.0[m],0.0[m]
Plane 13 Point = 1.0[m],0.0[m],0.0[m]
Reference Coord Frame = Coord 0
END
END
MATERIAL: Crude Oil
Material Group = User
Option = Pure Substance
PROPERTIES:
Option = General Material
EQUATION OF STATE:
Density = 870 [kg m^-3]
Molar Mass = 154 [kg kmol^-1]
Option = Value
END
DYNAMIC VISCOSITY:
Dynamic Viscosity = 0.0105 [Pa s]
Option = Value
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 = Transient
EXTERNAL SOLVER COUPLING:
Option = None
END
INITIAL TIME:
Option = Automatic with Value
Time = 0 [s]
END
TIME DURATION:
Option = Total Time
Total Time = 3 [s]
END
TIME STEPS:
Option = Timesteps
Timesteps = 0.025 [s]
END
END
DOMAIN: Rotor
Coord Frame = Coord 1
Domain Type = Fluid
Location = B763
BOUNDARY: Default Fluid Fluid Interface Side 1
Boundary Type = INTERFACE
Location = F583.763
BOUNDARY CONDITIONS:
MASS AND MOMENTUM:
Option = Conservative Interface Flux
END
MESH MOTION:
Option = Stationary
END
TURBULENCE:
Option = Conservative Interface Flux
END
END
END
BOUNDARY: Domain Interface 1 Side 1
Boundary Type = INTERFACE
Location = RotorInterface1
BOUNDARY CONDITIONS:
MASS AND MOMENTUM:
Option = Conservative Interface Flux
END
MESH MOTION:
Option = Stationary
END
TURBULENCE:
Option = Conservative Interface Flux
END
END
END
BOUNDARY: RotorWall
Boundary Type = WALL
Location = RotorWall
BOUNDARY CONDITIONS:
MASS AND MOMENTUM:
Option = No Slip Wall
Wall Velocity Relative To = Mesh Motion
END
MESH MOTION:
Option = Rigid Body Solution
Rigid Body = Rigid Body 1
END
WALL ROUGHNESS:
Option = Smooth Wall
END
END
END
BOUNDARY: Symmetry
Boundary Type = SYMMETRY
Location = F586.763
BOUNDARY CONDITIONS:
MESH MOTION:
Option = Unspecified
END
END
END
DOMAIN MODELS:
BUOYANCY MODEL:
Option = Non Buoyant
END
DOMAIN MOTION:
Option = Stationary
END
MESH DEFORMATION:
Displacement Relative To = Previous Mesh
Option = Regions of Motion Specified
MESH MOTION MODEL:
Option = Displacement Diffusion
MESH STIFFNESS:
Option = Increase near Small Volumes
Stiffness Model Exponent = 2.0
REFERENCE VOLUME:
Option = Mean Control Volume
END
END
END
END
REFERENCE PRESSURE:
Reference Pressure = 1 [atm]
END
END
FLUID DEFINITION: Fluid 1
Material = Crude Oil
Option = Material Library
MORPHOLOGY:
Option = Continuous Fluid
END
END
FLUID MODELS:
COMBUSTION MODEL:
Option = None
END
HEAT TRANSFER MODEL:
Option = None
END
THERMAL RADIATION MODEL:
Option = None
END
TURBULENCE MODEL:
Option = k epsilon
END
TURBULENT WALL FUNCTIONS:
Option = Scalable
END
END
INITIALISATION:
Option = Automatic
INITIAL CONDITIONS:
Velocity Type = Cartesian
CARTESIAN VELOCITY COMPONENTS:
Option = Automatic with Value
U = 0 [m s^-1]
V = 0 [m s^-1]
W = 0 [m s^-1]
END
STATIC PRESSURE:
Option = Automatic with Value
Relative Pressure = 0 [Pa]
END
TURBULENCE INITIAL CONDITIONS:
Option = Medium Intensity and Eddy Viscosity Ratio
END
END
END
SUBDOMAIN: Subdomain 1
Coord Frame = Coord 1
Location = B763
MESH MOTION:
Option = Rigid Body Solution
Rigid Body = Rigid Body 1
END
END
END
DOMAIN: Stator
Coord Frame = Coord 1
Domain Type = Fluid
Location = B640
BOUNDARY: Default Fluid Fluid Interface Side 2
Boundary Type = INTERFACE
Location = F493.640
BOUNDARY CONDITIONS:
MASS AND MOMENTUM:
Option = Conservative Interface Flux
END
TURBULENCE:
Option = Conservative Interface Flux
END
END
END
BOUNDARY: Domain Interface 1 Side 2
Boundary Type = INTERFACE
Location = StatorInterface1
BOUNDARY CONDITIONS:
MASS AND MOMENTUM:
Option = Conservative Interface Flux
END
TURBULENCE:
Option = Conservative Interface Flux
END
END
END
BOUNDARY: Inlet
Boundary Type = INLET
Location = F486.640
BOUNDARY CONDITIONS:
FLOW DIRECTION:
Option = Normal to Boundary Condition
END
FLOW REGIME:
Option = Subsonic
END
MASS AND MOMENTUM:
Mass Flow Rate = 1100 [kg s^-1]
Option = Mass Flow Rate
END
TURBULENCE:
Option = Medium Intensity and Eddy Viscosity Ratio
END
END
END
BOUNDARY: Outlet
Boundary Type = OUTLET
Location = F485.640
BOUNDARY CONDITIONS:
FLOW REGIME:
Option = Subsonic
END
MASS AND MOMENTUM:
Mass Flow Rate = 1100 [kg s^-1]
Option = Mass Flow Rate
END
END
END
BOUNDARY: Symmetry2
Boundary Type = SYMMETRY
Location = F491.640
END
BOUNDARY: Wall
Boundary Type = WALL
Location = Wall
BOUNDARY CONDITIONS:
MASS AND MOMENTUM:
Option = No Slip Wall
END
WALL ROUGHNESS:
Option = Smooth Wall
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: Fluid 1
Material = Crude Oil
Option = Material Library
MORPHOLOGY:
Option = Continuous Fluid
END
END
FLUID MODELS:
COMBUSTION MODEL:
Option = None
END
HEAT TRANSFER MODEL:
Option = None
END
THERMAL RADIATION MODEL:
Option = None
END
TURBULENCE MODEL:
Option = k epsilon
END
TURBULENT WALL FUNCTIONS:
Option = Scalable
END
END
INITIALISATION:
Option = Automatic
INITIAL CONDITIONS:
Velocity Type = Cartesian
CARTESIAN VELOCITY COMPONENTS:
Option = Automatic with Value
U = 0 [m s^-1]
V = 0 [m s^-1]
W = 0 [m s^-1]
END
STATIC PRESSURE:
Option = Automatic with Value
Relative Pressure = 0 [Pa]
END
TURBULENCE INITIAL CONDITIONS:
Option = Medium Intensity and Eddy Viscosity Ratio
END
END
END
END
DOMAIN INTERFACE: Default Fluid Fluid Interface
Boundary List1 = Default Fluid Fluid Interface Side 1
Boundary List2 = Default Fluid Fluid Interface Side 2
Interface Type = Fluid Fluid
INTERFACE MODELS:
Option = General Connection
FRAME CHANGE:
Option = None
END
MASS AND MOMENTUM:
Option = Conservative Interface Flux
MOMENTUM INTERFACE MODEL:
Option = None
END
END
PITCH CHANGE:
Option = None
END
END
MESH CONNECTION:
Option = GGI
END
END
DOMAIN INTERFACE: Domain Interface 1
Boundary List1 = Domain Interface 1 Side 1
Boundary List2 = Domain Interface 1 Side 2
Interface Type = Fluid Fluid
INTERFACE MODELS:
Option = General Connection
FRAME CHANGE:
Option = None
END
MASS AND MOMENTUM:
Option = Conservative Interface Flux
MOMENTUM INTERFACE MODEL:
Option = None
END
END
PITCH CHANGE:
Option = None
END
END
MESH CONNECTION:
Option = GGI
END
END
OUTPUT CONTROL:
MONITOR OBJECTS:
MONITOR BALANCES:
Option = Full
END
MONITOR FORCES:
Option = Full
END
MONITOR PARTICLES:
Option = Full
END
MONITOR POINT: Monitor Point 1
Coord Frame = Coord 1
Expression Value = torque_z@RotorWall
Option = Expression
END
MONITOR RESIDUALS:
Option = Full
END
MONITOR TOTALS:
Option = Full
END
END
RESULTS:
File Compression Level = Default
Option = Standard
END
TRANSIENT RESULTS: Transient Results 1
File Compression Level = Default
Option = Standard
OUTPUT FREQUENCY:
Option = Time Interval
Time Interval = 0.075 [s]
END
END
END
RIGID BODY: Rigid Body 1
Location = RotorWall
Mass = 5.15 [kg]
Rigid Body Coord Frame = Coord 1
DYNAMICS:
DEGREES OF FREEDOM:
ROTATIONAL DEGREES OF FREEDOM:
Option = Z axis
END
TRANSLATIONAL DEGREES OF FREEDOM:
Option = None
END
END
GRAVITY:
Gravity X Component = 0 [m s^-2]
Gravity Y Component = -9.81 [m s^-2]
Gravity Z Component = 0 [m s^-2]
Option = Cartesian Components
END
END
INITIAL CONDITIONS:
ANGULAR VELOCITY:
Option = Automatic with Value
xValue = 0 [radian s^-1]
yValue = 0 [radian s^-1]
zValue = 0 [radian s^-1]
END
CENTRE OF MASS:
Option = Automatic
END
LINEAR VELOCITY:
Option = Automatic with Value
xValue = 0 [m s^-1]
yValue = 0 [m s^-1]
zValue = 0 [m s^-1]
END
END
MASS MOMENT OF INERTIA:
xxValue = 0.048 [kg m^2]
xyValue = 0 [kg m^2]
xzValue = 0 [kg m^2]
yyValue = 0.048 [kg m^2]
yzValue = 0 [kg m^2]
zzValue = 0.051 [kg m^2]
END
END
SOLVER CONTROL:
Turbulence Numerics = First Order
ADVECTION SCHEME:
Option = High Resolution
END
CONVERGENCE CONTROL:
Maximum Number of Coefficient Loops = 10
Minimum Number of Coefficient Loops = 1
Timescale Control = Coefficient Loops
END
CONVERGENCE CRITERIA:
Residual Target = 1.E-4
Residual Type = RMS
END
TRANSIENT SCHEME:
Option = Second Order Backward Euler
TIMESTEP INITIALISATION:
Option = Automatic
END
END
END
END
COMMAND FILE:
Version = 15.0
Results Version = 15.0
END
SIMULATION CONTROL:
EXECUTION CONTROL:
EXECUTABLE SELECTION:
Double Precision = Off
END
INTERPOLATOR STEP CONTROL:
Runtime Priority = Standard
DOMAIN SEARCH CONTROL:
Bounding Box Tolerance = 0.01
END
INTERPOLATION MODEL CONTROL:
Enforce Strict Name Mapping for Phases = Off
Mesh Deformation Option = Automatic
Particle Relocalisation Tolerance = 0.01
END
MEMORY CONTROL:
Memory Allocation Factor = 1.0
END
END
PARALLEL HOST LIBRARY:
HOST DEFINITION: winserv5
Host Architecture String = winnt-amd64
Installation Root = C:\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 = No gap from turbine to wall but same dim.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
mshahed91 is offline   Reply With Quote

 


Posting Rules
You may not post new threads
You may not post replies
You may not post attachments
You may not edit your posts

BB code is On
Smilies are On
[IMG] code is On
HTML code is Off
Trackbacks are Off
Pingbacks are On
Refbacks are On


Similar Threads
Thread Thread Starter Forum Replies Last Post
Frozen Rotor Simulation Trouble with a Hydrokinetic Propeller Turbine PorscheGTIII OpenFOAM Running, Solving & CFD 1 November 3, 2013 10:54
Turbine: Transient Simulation Problem John C. CFX 7 December 5, 2011 08:31
Problem with interface in a wind turbine simulation be_inspired FLUENT 2 March 7, 2011 23:46
Large-scale simulation problem Purushothama Main CFD Forum 0 November 7, 2010 20:12
fluid flow fundas ram Main CFD Forum 5 June 17, 2000 21:31


All times are GMT -4. The time now is 13:59.