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[Sponsors] |
December 28, 2007, 04:28 |
Biomass Gasifier
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#1 |
Guest
Posts: n/a
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Dear All,
I intend to simulate a down draft biomass gasifier considering it as a porous bed. I would also like to get the pressure drop & temperature across the bed. I would also like to know the gas composition, CV and the temperature of the gas at the outlet. I could model the cold porous bed and get the pressure drop and velocity profiles in the reactor. Further help me out to initiate the chemical reactions. Kindly help me out; your inputs are highly valuable to me. |
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April 1, 2011, 04:52 |
CFD modelling of downdraft gasifier
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#2 |
New Member
Keran.kp
Join Date: Sep 2010
Posts: 3
Rep Power: 16 |
To, N K Ram
I am Keran patel from Ahmedabad,Studying M tech in Thermal Engg.I've ur thesis of M Tech. which u submitted in 2006-08 under the guidence of Dr. S Maji and Dr. B .B. Arora.. My Project is similiar to urs with a l'ii bit change in model.Bt i can not initiate the combustioin in my model.I kindly request u to help me out.My settings of the model are as below:- Settings : Solver -Pressure Based Formulation -implicit Space -2D Velocity Formulation -Absolute Gradient Option -Green-Gauss Cell Based Porous Formulation -Superficial Velocity Multiphase Multiphase Model : Off Number of phase -1 Energy -Energy Equation Viscous Model Model -k-epsilon (2 eqn) k-epsilon Model -Realizable Near-Wall Treatment -Standard Wall Functions k-epsilon Multiphase Model -Mixture Model Constants C2-Epsilon: 1.9, TKE Prandtl Number: 1, TDR Prandtl Number: 1.2, Disperion Prandtl number: 0.75, Energy Prandtl Number: 0.85, Turb. Schmidt Number: 0.7, Species Model Model -Species Transport Reactions -Volumetric & Particle Surface Options -Inlet Diffusion & Diffusion Energy Source Turbulent -Chemistry Interaction -Finite-Rate/Eddy-Dissipation Operating Condition Pressure: Operating Pressure(pascal)-101325 Gravity: Gravity- Off Hope for the Help ! Thanks in advance |
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