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May 17, 2018 at 1:33 pm
mrglobetrotter
SubscriberHello everybody
I'm currently working on my Bachelor Thesis for my Mechanical Engineering degree.
The task is to simulate a water spray which is going to be injected into air as ideal gas. Both fluids need to be set as continuous fluid, so it should not be a large breakup model simulation to investigate every single drop. The nozzle diameter is 0.75mm and the injection velocity is 150 m/s.
I've already done my first setup but the result isn't quite comprehensibly. The water spray keeps cylindrical over a whole injection length of 200mm. I expect that the flow will spread after a time.
My question now is if someone has experience in modelling this kind of sprays? Do I need to add some special models or some other sort of physics? If you have some questions, please ask me!
Thanks for all replies in advance.
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May 17, 2018 at 6:05 pm
raul.raghav
SubscriberHow did you come with the geometry for your simulation? And what are the boundary conditions? 2D or 3D? Can you provide a better schematic of the geometry and how you setup the BC's?
Which solver and what model are you using to solve this simulation?
And if you want more information about setting up the simulation, Raef has some really good youtube tutorials on jet flow which would help you immensely:
CFD ANSYS Tutorial - Air jet flow simulation through a nozzle revisited | FLUENT
CFD Tutorial – Converging diverging (CD) nozzle supersonic flow | Fluent ANSYS
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May 17, 2018 at 8:42 pm
mrglobetrotter
SubscriberHi Rahul
Thanks for your answer.
I thought since the inlet is round, I'm going to do also a cylindrical opening. So I can create an ogrid (for the inlet) in an ogrid (for the opening). I meshed everything with hexa and did a refinement on the passage area between liquid and gas fluid. The mesh quality is really good and my supervisor is quite happy with it. So, everything is 3D, see pictures:
My boundary conditions:Â
FLOW: Flow Analysis 1
- ANALYSIS TYPE:
Option = Steady State
EXTERNAL SOLVER COUPLING:
Option = None
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- DOMAIN: Default Domain
Coord Frame = Coord 0
Domain Type = Fluid
Location = BODY - BOUNDARY: Inlet
Boundary Type = INLET
Location = INLET
BOUNDARY CONDITIONS:
FLOW REGIME:
Option = Subsonic
HEAT TRANSFER:
Option = Fluid Dependent
MASS AND MOMENTUM:
Option = Cartesian Velocity Components
U = 0 [m s^-1]
V = 0 [m s^-1]
W = 150 m/s
TURBULENCE:
Option = Low Intensity and Eddy Viscosity Ratio
FLUID: Air
BOUNDARY CONDITIONS:
HEAT TRANSFER:
Option = Static Temperature
Static Temperature = 298 [K]
VOLUME FRACTION:
Option = Value
Volume Fraction = 0
FLUID: Water
BOUNDARY CONDITIONS:
HEAT TRANSFER:
Option = Static Temperature
Static Temperature = 298 [K]
VOLUME FRACTION:
Option = Value
Volume Fraction = 1
- BOUNDARY: Opening
Boundary Type = OPENING
Location = SIDE,BACK
BOUNDARY CONDITIONS:
FLOW DIRECTION:
Option = Normal to Boundary Condition
FLOW REGIME:
Option = Subsonic
HEAT TRANSFER:
Option = Fluid Dependent
MASS AND MOMENTUM:
Option = Opening Pressure and Direction
Relative Pressure = 1 [atm]
TURBULENCE:
Option = Low Intensity and Eddy Viscosity Ratio
FLUID: Air
BOUNDARY CONDITIONS:
HEAT TRANSFER:
Option = Static Temperature
Static Temperature = 298 [K]
VOLUME FRACTION:
Option = Zero Gradient
FLUID: Water
BOUNDARY CONDITIONS:
HEAT TRANSFER:
Option = Static Temperature
Static Temperature = 298 [K]
VOLUME FRACTION:
Option = Zero Gradient
- BOUNDARY: Wall
Boundary Type = WALL
Location = WALL
BOUNDARY CONDITIONS:
HEAT TRANSFER:
Option = Adiabatic
MASS AND MOMENTUM:
Option = Free Slip Wall
FLUID PAIR: Air | Water
BOUNDARY CONDITIONS:
WALL ADHESION:
Option = None
- DOMAIN MODELS:
BUOYANCY MODEL:
Option = Non Buoyant
DOMAIN MOTION:
Option = Stationary
MESH DEFORMATION:
Option = None
REFERENCE PRESSURE:
Reference Pressure = 0 [atm]
FLUID DEFINITION: Air
Material = Air Ideal Gas
MORPHOLOGY:
Option = Continuous Fluid
FLUID DEFINITION: Water
Material = Water
Option = Material Library
MORPHOLOGY:
Option = Continuous Fluid
FLUID MODELS:
COMBUSTION MODEL:
Option = None
FLUID: Air
HEAT TRANSFER MODEL:
Include Viscous Work Term = True
Option = Total Energy
FLUID: Water
HEAT TRANSFER MODEL:
Include Viscous Dissipation Term = On
Option = Thermal Energy
HEAT TRANSFER MODEL:
Homogeneous Model = Off
Option = Fluid Dependent
TURBULENCE MODEL:
Option = SST
TURBULENT WALL FUNCTIONS:
Option = Automatic
FLUID PAIR: Air | Water
Surface Tension Coefficient = 0.072 [N m^-1]
INTERPHASE HEAT TRANSFER:
Heat Transfer Coefficient = 10 [W m^-2 K^-1]
Option = Heat Transfer Coefficient
INTERPHASE TRANSFER MODEL:
Option = Free Surface
MASS TRANSFER:
Option = None
SURFACE TENSION MODEL:
Option = Continuum Surface Force
Primary Fluid = Water
MULTIPHASE MODELS:
Homogeneous Model = On
FREE SURFACE MODEL:
Option = Standard
INITIALISATION:
Option = Automatic
FLUID: Air
    INITIAL CONDITIONS:
       SET!
Does this help? Please feel free to ask for more!
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Thank you very much for the youtube tutorials! They seem quite useful! My only question is, how adaptable is it for CFX? Can I use it as a CFX user?
Â
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- ANALYSIS TYPE:
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July 10, 2020 at 3:41 am
sahil
SubscriberHi mrglobetrotter,
Â
I have seen your question and project. I am working on same kind of project. can you please help me by sharing your work ( Maybe you have completed because your question is from 2018), this would be a great help to me. Thank you in advanceÂ
Sahil
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