Experimental and numerical investigation of dynamic heat transfer parameters in packed bed
Contribuinte(s) |
UNIVERSIDADE DE SÃO PAULO |
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Data(s) |
18/10/2012
18/10/2012
2010
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Resumo |
Dynamic experiments in a nonadiabatic packed bed were carried out to evaluate the response to disturbances in wall temperature and inlet airflow rate and temperature. A two-dimensional, pseudo-homogeneous, axially dispersed plug-flow model was numerically solved and used to interpret the results. The model parameters were fitted in distinct stages: effective radial thermal conductivity (K (r)) and wall heat transfer coefficient (h (w)) were estimated from steady-state data and the characteristic packed bed time constant (tau) from transient data. A new correlation for the K (r) in packed beds of cylindrical particles was proposed. It was experimentally proved that temperature measurements using radially inserted thermocouples and a ring-shaped sensor were not distorted by heat conduction across the thermocouple or by the thermal inertia effect of the temperature sensors. CAPES-Coordenacao de Aperfeicoamento de Pessoal de Nivel Superior (Brasilia, Brazil) FAPESP-Fundacao de Amparo a Pesquisa do Estado de Sao Paulo (Sao Paulo, Brazil) |
Identificador |
HEAT AND MASS TRANSFER, v.46, n.11/Dez, p.1355-1365, 2010 0947-7411 http://producao.usp.br/handle/BDPI/18510 10.1007/s00231-010-0659-6 |
Idioma(s) |
eng |
Publicador |
SPRINGER |
Relação |
Heat and Mass Transfer |
Direitos |
restrictedAccess Copyright SPRINGER |
Palavras-Chave | #BOUNDARY CONDITIONS #FIXED-BED #FLOW REACTORS #GAS-FLOW #THERMAL-CONDUCTIVITY #DISPERSION #MODELS #PARTICLES #SPHERES #WALL #Thermodynamics #Mechanics |
Tipo |
article original article publishedVersion |