Mathematical modeling on the thin layer drying kinetics of cassava chips in a multipurpose convective-type tray dryer heated by a gas burner

2018 ◽  
Vol 32 (7) ◽  
pp. 3427-3435 ◽  
Author(s):  
Bambang Dwi Argo ◽  
Sandra Sandra ◽  
Ubaidillah Ubaidillah
2015 ◽  
Vol 52 (3) ◽  
pp. 407-419 ◽  
Author(s):  
Amira Belghith ◽  
Soufien Azzouz ◽  
Afif ElCafsi

2012 ◽  
Vol 38 (2) ◽  
pp. 728-736 ◽  
Author(s):  
Antonio Vega-Gálvez ◽  
Luis Puente-Díaz ◽  
Roberto Lemus-Mondaca ◽  
Margarita Miranda ◽  
María José Torres

2016 ◽  
Vol 64 ◽  
pp. 59-66
Author(s):  
Fidel Ivan Labutong ◽  
Janet Stephanie Pastores ◽  
Angelyn Yeung ◽  
Lola Domnina Pestaño

2011 ◽  
Vol 12 (11) ◽  
pp. 7885-7897 ◽  
Author(s):  
Irene Montero ◽  
Teresa Miranda ◽  
Jose Ignacio Arranz ◽  
Carmen Victoria Rojas

2015 ◽  
Vol 39 (3) ◽  
pp. 291-300 ◽  
Author(s):  
Daniele Penteado Rosa ◽  
Denis Cantú-Lozano ◽  
Guadalupe Luna-Solano ◽  
Tiago Carregari Polachini ◽  
Javier Telis-Romero

Drying of orange seeds representing waste products from juice processing was studied in the temperatures of 40, 50, 60 and 70 °C and drying velocities of 0.6, 1.0 and 1.4 m/s. Experimental drying kinetics of orange seeds were obtained using a convective air forced dryer. Three thin-layer models: Page model, Lewis model, and the Henderson-Pabis model and the diffusive model were used to predict the drying curves. The Henderson-Pabis and the diffusive models show the best fitting performance and statistical evaluations. Moreover, the temperature dependence on the effective diffusivity followed an Arrhenius relationship, and the activation energies ranging from 16.174 to 16.842 kJ/mol


2012 ◽  
Vol 51 (7) ◽  
pp. 1294-1301 ◽  
Author(s):  
R. K. Gupta ◽  
Alka Sharma ◽  
Pradeep Kumar ◽  
R. K. Vishwakarma ◽  
R. T. Patil

2009 ◽  
Vol 102 (2) ◽  
pp. 153-161 ◽  
Author(s):  
C.L. Hii ◽  
C.L. Law ◽  
M. Cloke ◽  
S. Suzannah

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