Revista: | Brazilian journal of chemical engineering |
Base de datos: | PERIÓDICA |
Número de sistema: | 000308789 |
ISSN: | 0104-6632 |
Autors: | Narimatsu, C.P1 Ferreira, M.C |
Institucions: | 1Universidade Federal de Sao Carlos, Departamento de Engenharia Quimica, Sao Carlos, Sao Paulo. Brasil |
Any: | 2001 |
Període: | Sep |
Volum: | 18 |
Número: | 3 |
Paginació: | 221-232 |
País: | Brasil |
Idioma: | Inglés |
Tipo de documento: | Artículo |
Enfoque: | Experimental, aplicado |
Resumen en inglés | In this work, the effects of particle size and density on the fluid dynamic behavior of vertical gas-solid transport of Group D particles in a 53.4 mm diameter transport tube were studied. For the conditions tested, the experimental curves of pressure gradient versus air velocity presented a minimum pressure gradient point, which is associated with a change in the flow regime from dense to dilute phase. The increases in particle size from 1.00 to 3.68 mm and in density from 935 to 2500 kg/m³ caused an increase in pressure gradient for the dense-phase transport region, but were not relevant in dilute transport. The transition velocity between dense and dilute flow (Umin) also increased with increasing particle density and diameter. An empirical equation was fitted for predicting transition air velocity for the transport of glass spheres. Additional experiments, covering a wider range of conditions and particles properties, are still needed to allow the fitting of a generalized equation for prediction of Umin |
Disciplines | Química |
Paraules clau: | Ingeniería química, Transportadores neumáticos, Partículas gruesas, Régimen de flujo, Velocidad de transición |
Keyword: | Chemistry, Chemical engineering, Pneumatic conveying, Coarse particles, Flow regime, Transition velocity |
Text complet: | Texto completo (Ver HTML) |