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Registro Completo |
Biblioteca(s): |
Embrapa Agroindústria de Alimentos. |
Data corrente: |
13/01/2011 |
Data da última atualização: |
30/11/2012 |
Tipo da produção científica: |
Artigo em Periódico Indexado |
Autoria: |
PARK, K. J. B.; ALONSO, L. F. T.; CORNEJO, F. E. P.; DAL FABBRO, I. M.; PARK, K. J. |
Afiliação: |
KIL JIN BRANDINI PARK; LUÍS FELIPE TORO ALONSO; FELIX EMILIO PRADO CORNEJO, CTAA; INÁCIO MARIA DAL FABBRO, UNICAMP; KIL JIN PARK, UNICAMP. |
Título: |
Drying system designs: global balance and costs. |
Ano de publicação: |
2010 |
Fonte/Imprenta: |
Journal of Food Process Engineering, 16 sep. 2010. |
DOI: |
10.1111/j.1745-4530.2009.00573.x |
Idioma: |
Inglês |
Conteúdo: |
When designing drying systems, heat and mass balance should be studied as well as constructing and operating costs. These designs, which differ by type of dryer, depend on the heat-mass relationship. The heat and mass balance on drying systems depend on the type of dryer, the drying process and the drying rate. One of the biggest problems involving dryers? selection consists in obtaining the required quality of the product with a great variety of drying equipments and processes. Many methods are presented in literature, those based on phenomenological concepts and those based on cost aspects. Consequently the criteria to classify and design dryers are also in a large number and different for each drying system. Drying system simulation models can also be used to design the dryer. Equations for dryer designs and the costs and area calculations are presented to help food engineers. The case study with specific software using these equations will be presented in future articles. |
Palavras-Chave: |
Sistema de secagem. |
Categoria do assunto: |
X Pesquisa, Tecnologia e Engenharia |
Marc: |
LEADER 01531naa a2200193 a 4500 001 1872884 005 2012-11-30 008 2010 bl uuuu u00u1 u #d 024 7 $a10.1111/j.1745-4530.2009.00573.x$2DOI 100 1 $aPARK, K. J. B. 245 $aDrying system designs$bglobal balance and costs. 260 $c2010 520 $aWhen designing drying systems, heat and mass balance should be studied as well as constructing and operating costs. These designs, which differ by type of dryer, depend on the heat-mass relationship. The heat and mass balance on drying systems depend on the type of dryer, the drying process and the drying rate. One of the biggest problems involving dryers? selection consists in obtaining the required quality of the product with a great variety of drying equipments and processes. Many methods are presented in literature, those based on phenomenological concepts and those based on cost aspects. Consequently the criteria to classify and design dryers are also in a large number and different for each drying system. Drying system simulation models can also be used to design the dryer. Equations for dryer designs and the costs and area calculations are presented to help food engineers. The case study with specific software using these equations will be presented in future articles. 653 $aSistema de secagem 700 1 $aALONSO, L. F. T. 700 1 $aCORNEJO, F. E. P. 700 1 $aDAL FABBRO, I. M. 700 1 $aPARK, K. J. 773 $tJournal of Food Process Engineering, 16 sep. 2010.
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