| dc.creator | Pecora, AAB | |
| dc.creator | Parise, MR | |
| dc.date | 2006 | |
| dc.date | OCT-DEC | |
| dc.date | 2014-11-19T19:44:34Z | |
| dc.date | 2015-11-26T16:29:04Z | |
| dc.date | 2014-11-19T19:44:34Z | |
| dc.date | 2015-11-26T16:29:04Z | |
| dc.date.accessioned | 2018-03-28T23:10:08Z | |
| dc.date.available | 2018-03-28T23:10:08Z | |
| dc.identifier | Brazilian Journal Of Chemical Engineering. Brazilian Soc Chemical Eng, v. 23, n. 4, n. 497, n. 506, 2006. | |
| dc.identifier | 0104-6632 | |
| dc.identifier | WOS:000242535500007 | |
| dc.identifier | 10.1590/S0104-66322006000400007 | |
| dc.identifier | http://www.repositorio.unicamp.br/jspui/handle/REPOSIP/54304 | |
| dc.identifier | http://www.repositorio.unicamp.br/handle/REPOSIP/54304 | |
| dc.identifier | http://repositorio.unicamp.br/jspui/handle/REPOSIP/54304 | |
| dc.identifier.uri | http://repositorioslatinoamericanos.uchile.cl/handle/2250/1269637 | |
| dc.description | This work presents an experimental study of a continuous gas-solid fluidized bed with an immersed horizontal tube. Silica sand (254 mu m diameter) was used as solid particles and air was used for fluidization in a 900mm long and 150mm wide heat exchanger. Measurements were made under steady state conditions for a solid particle mass flow rate from 14 to 95kg.h(-1) and a number of baffles from 0 to 8. Results showed that the heat transfer coefficient increases with the solid particle mass flow rate and with the number of baffles, suggesting that these are important factors to be considered in the design of such equipment. An empirical correlation for the heat transfer coefficient is proposed as a function of solid particle and gas mass flow rata, number of baffles and gas velocity. | |
| dc.description | 23 | |
| dc.description | 4 | |
| dc.description | 497 | |
| dc.description | 506 | |
| dc.language | en | |
| dc.publisher | Brazilian Soc Chemical Eng | |
| dc.publisher | Sao Paulo | |
| dc.publisher | Brasil | |
| dc.relation | Brazilian Journal Of Chemical Engineering | |
| dc.relation | Braz. J. Chem. Eng. | |
| dc.rights | aberto | |
| dc.source | Web of Science | |
| dc.subject | shallow fluidized bed | |
| dc.subject | experimental work | |
| dc.subject | heat transfer coefficient | |
| dc.subject | Horizontal Tube | |
| dc.title | An analysis of process heat recovery in a gas-solid shallow fluidized bed | |
| dc.type | Artículos de revistas | |
