Non-Newtonian Flow Between 2 Concentric Cylinders, Eulerian, ANSYS Fluent

Price: $24

The present problem simulates a non-Newton two-phase flow between two concentric cylinders using ANSYS Fluent software.

Audio: English
Subtitles: English, Spanish, Arabic, Turkish, French, Portuguese
Intermediate
1 Lesson
33m 16s
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  • Non-Newtonian Flow

    Non-Newtonian Flow Between 2 Concentric Cylinders, Eulerian, ANSYS Fluent

    Price: $24

    The present problem simulates a non-Newton two-phase flow between two concentric cylinders using ANSYS Fluent software.

    Audio: English
    Subtitles: English, Spanish, Arabic, Turkish, French, Portuguese
    Intermediate
    1 Lesson
    33m 16s

    Non-Newtonian Flow Project Description

    The present problem simulates a non-Newton two-phase flow between two concentric cylinders using ANSYS Fluent software. Fluids are divided into two categories in terms of viscosity: Newtonian and non-Newtonian fluids. Viscosity is a parametric fluid that indicates the degree of resistance of that fluid to flow. Newtonian fluids are fluids that follow Newton's law of viscosity (shear stress in a Newtonian fluid changes linearly with strain rate) and also their viscosity depends only on the temperature and pressure of the fluid, and by applying a force to them in a constant temperature and pressure, their viscosity does not change.

    Non-Newtonian fluids, on the other hand, are fluids that do not follow Newton's law of fluids, and their viscosity changes with the application of force. In this simulation, a two-phase flow is defined using the Eulerian model, the base fluid of which is a non-Newtonian fluid with a soluble fluid flowing through it. The base fluid has a density of 998.2 kg.m-3 and its viscosity is defined as non-Newtonian, which is non-Newtonian-power-law. The relation to the non-Newtonian viscosity value is as follows; So that k is equal to the criterion for measuring the average viscosity of the fluid and n is the criterion for the deviation of the fluid from the Newtonian state.

    In this simulation, k is defined as 0.021 and n is defined as 0.75, and the minimum and maximum viscosity are 0.0001 kg.m-1.s-1 and 2000 kg.m-1.s-1, respectively. The soluble fluid in non-Newtonian fluid also has a density equal to 2000 kg.m-3 and a viscosity equal to 0.00111 kg.m-1.s-1.

    Geometry & Mesh

    The present model is designed in three dimensions using Design Modeler software. The model is a cylindrical channel with a length of 1 m and an inner diameter of 0.0225 m and an outer diameter of 0.03125 m.

    non-newtonian

    We carry out the model's meshing using ANSYS Meshing software. The mesh type is structured. The element number is 1396224. The following figure shows the mesh.

    non-newtonian

    Non-Newtonian Flow CFD Simulation

    We consider several assumptions to simulate the present model:

    • We perform a pressure-based solver.
    • The simulation is steady.
    • The gravity effect on the fluid is ignored.

    The following table represents a summary of the defining steps of the problem and its solution:

    Models (Non-Newtonian)
    Viscousk-epsilon
    k-epsilon modelstandard
    near wall treatmentstandard wall functions
    Multiphase ModelEulerian
    number of eulerian phases2
    formulationimplicit
    Boundary conditions (Non-Newtonian)
    InletVelocity Inlet
    gauge pressure0 Pascal
    velocity magnitude1.3566 m.s-1
    volume fraction - primary phase0.87
    volume fraction - secondary phase0.13
    OutletPressure Outlet
    gauge pressure0 pascal
    Inner wallwall motionRotating wall (100 rpm)
    Outer wallwall motionstationary wall
    Methods (Non-Newtonian)
    Pressure-Velocity CouplingCoupled
    PressurePRESTO
    momentumfirst order upwind
    turbulent kinetic energyfirst order upwind
    turbulent dissipation ratefirst order upwind
    volume fractionfirst order upwind
    Initialization (Non-Newtonian)
    Initialization methodsStandard
    gauge pressure0 Pascal
    velocity (x,y,z)0 m.s-1
    volume fraction - primary1
    volume fraction - secondary0

    Results & Discussions

    At the end of the solution process, two-dimensional and three-dimensional contours related to pressure, velocity, volume fraction of non-Newtonian base fluid and volume fraction of soluble fluid were obtained.