radiative heat transfer and fluid flow simulation in a ... · radiative heat transfer and fluid...
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Radiative Heat Transfer and Fluid Flow
Simulation in a Solar Reactor
Luiz Felipe de Oliveira Campos, Escola de Química, UFRJ;
Luiz Fernando Lopes Rodrigues Silva(*), DEQ, Escola de Química, UFRJ;
Paulo L. C. Lage, LTFD, Programa de Engenharia Química, COPPE/UFRJ
PRESENTATION TOPICS
• Motivation and Introduction;
• Problem Description;
• Simulations;
• Results;
• Conclusion and next steps.
Motivation
• Main current energy source: Fossil fuels
• World oil reserves: 1200 billion barrels (2005)[1]
• World natural gas reserves: 180 trillion m3 (2004)[1]
• Oil: 80 million barrels/day 41 years [2]
• Natural gas: 7.36 billion m3 /day 67 years [2]
• Energy comsumption x Energy demand
[1] Kalogirou, S. – Solar Energy Engineering : Processes and Systems, 2009.
[2]Goswami, Y.D. - Energy: the burning issue, 2007.
Motivation
Global temperature since 1850
Kalogirou, S. – Solar Energy Engineering : Processes and Systems, 2009.
Motivation
CO2 levels in the last 1000 years
Kalogirou, S. – Solar Energy Engineering : Processes and Systems, 2009.
Introduction
• Renewable energy: less pollution
• Wind energy
• Biomass
• Geothermal
• Ocean Energy
• Biggest Investors[3]: China, EUA and Europe
• Brazil?
[3] Jeremy Von Loon – Bloomberg Business Week , 2010.
Problem Description
• “An improved engineering design of a solar chemical reactor
for the thermal dissociation of ZnO at above 2000K is
presented. It features a rotating cavity receiver lined with
ZnO particles that are held by centrifugal force (...).
Concentrated solar radiation enters the cavity through a
3mm thick quartz window, wich is mounted on a water colled
aluminum ring and integrated to the front face of the cavity
via a conical frustum that contains a 60 mm diameter
aperture.”
Schunk et al; 2008 – A Receiver-Reactor for the Solar Thermal Dissociation of ZnO.
Solar reactor
scheme
(1)Cavity;
(2)Aperture;
(3)Quartz window;
(4)Rotating Drum;
(5)Actuation;
(6) Insulation;
(7)Dynamic feeder;
(8)Product outlet port;
(9)Rotary joint;
(10)Cooling Fluids
Problem Description
• Dynamic feeder: Spread of ZnO particles
• Rotating Cavity: Reaction
• Outlet port: Quenching section
• Injecton of Ar: Quartz window protection
Simulations
• Schunk et al; 2008: Optimal flow configuration without
radiative heat transport considerations
• Analysis: Radiative heat transfer effects on the flow,
considering surface radiation (non participating media)
• Monte Carlo simulation with gray difusive surfaces in ANSYS
CFX 12.1 using the SST turbulence model and the thermal
model with the automatic wall treatment and the Kader’s law-
of-the-wall
Simulations – Boundary Conditions
• Fluid: Argon as Ideal gas, fed at 900 K.
• Inlet1: 0.384 Kg/s
• Inlet 2: 0.12 Kg/s
• Outlet: 0 Pa relative pressure (reference pressure: 105 Pa)
• Rotating Cavity: 2000 K
• Frustum: 900 K
• Window: irradiation of 5000 suns modeled by blackbody at
3064 K
• Feeder/Rotatory joint: Adiabatic
Results – Mesh Analysis
Horizontal Line: L , Vertical Line: r
Convergence: Achieved for a number of rays greater than 10 milion.
Number of rays used: 40 milion
Results - Comparison
Velocity w profiles:
Black/White – Without radiation;
Schunk et al.
Colored – With radiation
Results - Comparison
Temperature profiles:
Black/White – Without radiation ;
Schunk et al.
Colored – With radiation
Results
• Experimental observations made by Schunk et al.
• Cavity temperature: 1807 K – 1907 K
• Zn condensation over the window was observed
• Particles deposition at the outlet port
Conclusions
• Radiative heat transfer affects significantly the temperature
and velocity profiles.
• Better agreement with experimental observations.
• Absence of vortices in the frustum region can avoid particles
to be dragged to the window better protection.
• Radiation should’ve been accounted for geometry analysis.