Dehumidifier With VOF Model, CFD Simulation ANSYS Fluent Training

$210.00 Student Discount

The present simulation is about a Dehumidifier with VOF Model via ANSYS Fluent, and the results of this simulation have been analyzed.

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The journal file in ANSYS Fluent is used to record and automate simulations for repeatability and batch processing.
editable geometry and mesh allows users to create and modify geometry and mesh to define the computational domain for simulations.
The case and data files in ANSYS Fluent store the simulation setup and results, respectively, for analysis and post-processing.
Geometry, Mesh, and CFD Simulation methodologygy explanation, result analysis and conclusion
The MR CFD certification can be a valuable addition to a student resume, and passing the interactive test can demonstrate a strong understanding of CFD simulation principles and techniques related to this product.

Description

Dehumidifier With VOF Model Description

The present simulation is about a dehumidifier via ANSYS Fluent. A dehumidifier is an air conditioning device that reduces and maintains the level of humidity in the air. This device is used to increase the health and thermal comfort of the people in the environment, eliminate the musty odor, and prevent mildew growth by removing water from humid air.

This project investigates a humidification-dehumidification system with a phase change process. These systems consist of two sections the evaporator and the condenser.

First, the airflow inside the copper pipes is heated and compressed by the compressor and goes to the condenser section. In this section, the air inside the pipes is reduced by temperature due to blowing the fan, and condensation occurs.

The resulting liquid then goes to the evaporator section to evaporate again when it receives heat and turns into a gas phase. This heat is taken from the humid air blown into the pipes. Receiving heat from humid air causes dry air to be obtained. In this study, water vapor is considered humid air. Therefore, a multi-phase model must be defined, consisting of water and vapor.

Then the mass transfer between vapor and water is defined in evaporation-condensation type so that steam becomes liquid water by decreasing the temperature to below saturation temperature.

The amount of water resulting from the phase change between vapor and water indicates the amount of dehumidification. Since the two phases of water and vapor are entirely separate from each other, the volume of fluid (VOF) model is used. So, a chamber is designed with spiral tubes, So that the pipes have a flow of cold water and the chamber contains water vapor.

The vapor enters the chamber with a saturation temperature of 373.15 K and velocity of 0.05 m/s and contacts the surface of a pipe with water flow at a temperature of 358.15 K and a velocity of 0.01 m/s.

CFD

Geometry & Mesh

The present geometry is designed in a 3D model via Design Modeler. The computational zone is the interior of a dehumidifier. This dehumidifier consists of a chamber with spiral tubes. Steam flows inside the chamber, and cold-water flows inside the spiral pipes.

CFD

The mesh of the present model has been done via ANSYS Meshing. Mesh is done unstructured, and the number of production cells is equal to 1522772.

CFD

Set-up & Solution

Assumptions used in this simulation  :

  • Pressure-based solver is used.
  • The present simulation is steady.
  • The effect of gravity on the model is considered, and the gravitational acceleration is defined as 9.81 m/s2.

 

Models
Viscous k-epsilon
k-epsilon model realizable
Near-wall treatment standard wall function
Multiphase VOF
number of eulerian phases 2 (water & vapor)
interface modeling sharp
mass transfer mechanism evaporation-condensation
Energy On
Boundary conditions
Inlet-Wet Air Velocity Inlet
velocity magnitude 0.05 m.s-1
temperature 373.15 K
volume fraction of water 0
volume fraction of vapor 1
Inlet-Cool Water Velocity Inlet
velocity magnitude 0.01 m.s-1
temperature 358.15 K
volume fraction of water 1
volume fraction of vapor 0
Outlet-Dry Air Pressure Outlet
gauge pressure 0 Pascal
Outlet-Cool Water
gauge pressure 0 Pascal
Inner Wall Wall
wall motion stationary wall
thermal condition coupled
Outer Wall Wall
wall motion stationary wall
heat flux 0 W.m-2
Methods
Pressure-Velocity Coupling Coupled
pressure PRESTO
momentum First-order upwind
turbulent kinetic energy First-order upwind
turbulent dissipation rate First-order upwind
volume fraction modified HRIC
energy First-order upwind
Initialization
Initialization methods Standard
gauge pressure 0 Pascal
volume fraction of vapor in chamber 1
volume fraction of vapor in tube (patch) 0
velocity 0 m.s-1
temperature in chamber 373.15 K
temperature in tube (patch) 358.15 K

 

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