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Phoenics User Conference on CFD May 2004 Vipac Engineers & Scientists Ltd COMPUTATIONAL FLUID DYNAMICS Simulation of Turbulent Flows and Pollutant Dispersion Around Groups of Buildings presented by Dr. Neihad Al-Khalidy Specialist Consultant Fluid and Thermal Technologies

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Page 1: Phoenics User Conference on CFD May 2004 Vipac Engineers & Scientists Ltd COMPUTATIONAL FLUID DYNAMICS Simulation of Turbulent Flows and Pollutant Dispersion

Phoenics User Conference on CFD May 2004

Vipac Engineers & Scientists Ltd

COMPUTATIONAL FLUID DYNAMICS Simulation of Turbulent Flows and

Pollutant Dispersion Around Groups of Buildings

presented byDr. Neihad Al-KhalidySpecialist Consultant

Fluid and Thermal Technologies

Page 2: Phoenics User Conference on CFD May 2004 Vipac Engineers & Scientists Ltd COMPUTATIONAL FLUID DYNAMICS Simulation of Turbulent Flows and Pollutant Dispersion

Phoenics User Conference on CFD May 2004

Background

The analysis of flow and dispersion of pollutants around buildings is important from an environmental point of view

Examine pollutant problem under different scenarios based on a detailed fluid flow Analysis

Page 3: Phoenics User Conference on CFD May 2004 Vipac Engineers & Scientists Ltd COMPUTATIONAL FLUID DYNAMICS Simulation of Turbulent Flows and Pollutant Dispersion

Phoenics User Conference on CFD May 2004

Strategy

Recommend modifications to the duct heights, dimensions or velocities to achieve the

recommended criteria

Flow Simulation

Pollutant Dispersion Prediction

Probability Analysis

Pollutant sources

Wind data Data

CFD Model Construction

Compliance with Occupational Health & Safety Commission limits at human height

levels and living area

Page 4: Phoenics User Conference on CFD May 2004 Vipac Engineers & Scientists Ltd COMPUTATIONAL FLUID DYNAMICS Simulation of Turbulent Flows and Pollutant Dispersion

Phoenics User Conference on CFD May 2004

Geometry – Proposed Building

Page 5: Phoenics User Conference on CFD May 2004 Vipac Engineers & Scientists Ltd COMPUTATIONAL FLUID DYNAMICS Simulation of Turbulent Flows and Pollutant Dispersion

Phoenics User Conference on CFD May 2004

Geometry – Surrounding buildings

Page 6: Phoenics User Conference on CFD May 2004 Vipac Engineers & Scientists Ltd COMPUTATIONAL FLUID DYNAMICS Simulation of Turbulent Flows and Pollutant Dispersion

Phoenics User Conference on CFD May 2004

Geometry – Surrounding buildings

Page 7: Phoenics User Conference on CFD May 2004 Vipac Engineers & Scientists Ltd COMPUTATIONAL FLUID DYNAMICS Simulation of Turbulent Flows and Pollutant Dispersion

Phoenics User Conference on CFD May 2004

Boundary Condition - Wind Data

Still wind condition

Windy condition At the upwind

free boundary inlet velocity profiles were derived from the Australian Wind Code AS1170.2

Page 8: Phoenics User Conference on CFD May 2004 Vipac Engineers & Scientists Ltd COMPUTATIONAL FLUID DYNAMICS Simulation of Turbulent Flows and Pollutant Dispersion

Phoenics User Conference on CFD May 2004

Boundary Condition - pollutant Data

The maximum pollution emission rate at each stack is 450 l/s

The maximum mass flowrate of Xylene fume is 1200 l/s at each of the two ducts through the roof located near the plant room

A pollution concentration of unity is assumed at the pollutant sources

The pollutants were assumed to be slightly heavier than air at the sources

Page 9: Phoenics User Conference on CFD May 2004 Vipac Engineers & Scientists Ltd COMPUTATIONAL FLUID DYNAMICS Simulation of Turbulent Flows and Pollutant Dispersion

Phoenics User Conference on CFD May 2004

CFD Modelling

Phonics Software Navier-Stokes equations for continuity,

momentum, energy and species concentration

Steady-state Incompressible

Page 10: Phoenics User Conference on CFD May 2004 Vipac Engineers & Scientists Ltd COMPUTATIONAL FLUID DYNAMICS Simulation of Turbulent Flows and Pollutant Dispersion

Phoenics User Conference on CFD May 2004

CFD Modelling

Standard K-є model 680000 unstructured grid cells A Hybrid numerical approach to discretise the

convective term in the governing equations. SIMPLE algorithm for the pressure – velocity

coupling. Relaxation parameter to stabilize the solution

processes convergence 20-32 hours CPU

Page 11: Phoenics User Conference on CFD May 2004 Vipac Engineers & Scientists Ltd COMPUTATIONAL FLUID DYNAMICS Simulation of Turbulent Flows and Pollutant Dispersion

Phoenics User Conference on CFD May 2004

Sensitivity Analysis

Page 12: Phoenics User Conference on CFD May 2004 Vipac Engineers & Scientists Ltd COMPUTATIONAL FLUID DYNAMICS Simulation of Turbulent Flows and Pollutant Dispersion

Phoenics User Conference on CFD May 2004

CFD Flow Results

South-Westerly Wind Conditions

Page 13: Phoenics User Conference on CFD May 2004 Vipac Engineers & Scientists Ltd COMPUTATIONAL FLUID DYNAMICS Simulation of Turbulent Flows and Pollutant Dispersion

Phoenics User Conference on CFD May 2004

CFD Flow Results

South-Westerly Wind Conditions

Page 14: Phoenics User Conference on CFD May 2004 Vipac Engineers & Scientists Ltd COMPUTATIONAL FLUID DYNAMICS Simulation of Turbulent Flows and Pollutant Dispersion

Phoenics User Conference on CFD May 2004

CFD Pollutant Dispersion Results

concentration profile in a horizontal section at the chest level.

Downwash effect

Page 15: Phoenics User Conference on CFD May 2004 Vipac Engineers & Scientists Ltd COMPUTATIONAL FLUID DYNAMICS Simulation of Turbulent Flows and Pollutant Dispersion

Phoenics User Conference on CFD May 2004

CFD Pollutant Dispersion Results

1. concentration profiles in a horizontal section at the 15 m elevation

2. The pollutant dispersed to a wider region and the concentration is increased to 1.7% source concentration.

Page 16: Phoenics User Conference on CFD May 2004 Vipac Engineers & Scientists Ltd COMPUTATIONAL FLUID DYNAMICS Simulation of Turbulent Flows and Pollutant Dispersion

Phoenics User Conference on CFD May 2004

CFD Pollutant Dispersion Results

1. concentration profiles in a horizontal section Through the outlet of the stack

2. The pollution concentrations seen to increase to 3% source concentration near the roof of the building.

Page 17: Phoenics User Conference on CFD May 2004 Vipac Engineers & Scientists Ltd COMPUTATIONAL FLUID DYNAMICS Simulation of Turbulent Flows and Pollutant Dispersion

Phoenics User Conference on CFD May 2004

CFD Pollutant Dispersion Results

Concentration Profile- Iso-surface of 1% Source Concentration – Pollutant Slightly Heavier Than Air

Page 18: Phoenics User Conference on CFD May 2004 Vipac Engineers & Scientists Ltd COMPUTATIONAL FLUID DYNAMICS Simulation of Turbulent Flows and Pollutant Dispersion

Phoenics User Conference on CFD May 2004

CFD Pollutant Dispersion Results

Concentration Profile- Iso-surface of 1% Source Concentration – Pollutant of a Similar Density Than That of Air Was Used

Page 19: Phoenics User Conference on CFD May 2004 Vipac Engineers & Scientists Ltd COMPUTATIONAL FLUID DYNAMICS Simulation of Turbulent Flows and Pollutant Dispersion

Phoenics User Conference on CFD May 2004

CFD Flow Results

North-Easterly Wind Conditions

Page 20: Phoenics User Conference on CFD May 2004 Vipac Engineers & Scientists Ltd COMPUTATIONAL FLUID DYNAMICS Simulation of Turbulent Flows and Pollutant Dispersion

Phoenics User Conference on CFD May 2004

CFD Pollutant Dispersion Results

Concentration Profile in Horizontal Section at 1.5 m Elevation

Page 21: Phoenics User Conference on CFD May 2004 Vipac Engineers & Scientists Ltd COMPUTATIONAL FLUID DYNAMICS Simulation of Turbulent Flows and Pollutant Dispersion

Phoenics User Conference on CFD May 2004

CFD Pollutant Dispersion Results

Concentration Profile in Horizontal Section at 15 m Elevation

Page 22: Phoenics User Conference on CFD May 2004 Vipac Engineers & Scientists Ltd COMPUTATIONAL FLUID DYNAMICS Simulation of Turbulent Flows and Pollutant Dispersion

Phoenics User Conference on CFD May 2004

CFD Pollutant Dispersion Results

North-Easterly Wind Condition

Page 23: Phoenics User Conference on CFD May 2004 Vipac Engineers & Scientists Ltd COMPUTATIONAL FLUID DYNAMICS Simulation of Turbulent Flows and Pollutant Dispersion

Phoenics User Conference on CFD May 2004

CFD Pollutant Dispersion Results

Calm Wind Condition – near the roof of the building

Page 24: Phoenics User Conference on CFD May 2004 Vipac Engineers & Scientists Ltd COMPUTATIONAL FLUID DYNAMICS Simulation of Turbulent Flows and Pollutant Dispersion

Phoenics User Conference on CFD May 2004

Conclusions

Flow fields and pollutant dispersal around a number of buildings to the east and west of a proposed building have been predicted using computational fluid dynamics analysis.

The flow characteristics are seen to be captured well by the two equation k-ε model. The pollutant concentrations were predicted at the chest level and at a range of elevations during near calm wind and windy conditions.

 The CFD analysis has offered a comprehensive range of output including velocity distribution, pressure profile and turbulence levels. Subsequent testing of the modified duct system has validated the approach using CFD analytical tools.

The CFD results will be validated against the measurement data when the proposed building is completed and operated

Page 25: Phoenics User Conference on CFD May 2004 Vipac Engineers & Scientists Ltd COMPUTATIONAL FLUID DYNAMICS Simulation of Turbulent Flows and Pollutant Dispersion

Phoenics User Conference on CFD May 2004

Vipac Engineers & Scientists Ltd

Phone: 1300 7 VIPACwww.vipac.com.au