Mathematical model, validation and analysis of the drying treatment on quality attributes of chicory root cubes considering variable properties and shrinkage

被引:14
作者
Florencia Balzarini, Maria [1 ,2 ]
Agustina Reinheimer, Maria [1 ,3 ]
Cristina Ciappini, Maria [2 ]
Jose Scenna, Nicolas [1 ,3 ]
机构
[1] Univ Tecnol Nacl, CAIMI, Fac Reg Rosario, FRRo, Zeballos 1346,S2000BQA, Rosario, Sante Fe, Argentina
[2] Univ Tecnol Nacl, Ctr Invest Tecnol Alimentos CIDTA, Fac Reg Rosario, FRRo, Zeballos 1346,S2000BQA, Rosario, Sante Fe, Argentina
[3] Consejo Nacl Invest Cient & Tecn, Buenos Aires, DF, Argentina
关键词
3-D; Drying; Chicory roots; First-principles modeling; GAMS; Quality attributes; MASS-TRANSFER; DIFFUSION-COEFFICIENT; SIMULTANEOUS HEAT; MOISTURE-CONTENT; KINETICS; DENSITY; SLICES; REHYDRATION; TEMPERATURE; POROSITY;
D O I
10.1016/j.fbp.2018.07.005
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
This work presents an exhaustive three dimensional mathematical model to describe chicory root cubes drying process (Cichorium intybus L.) using a Fick's diffusion model considering a variable diffusion path length in three dimensions. Experimental data obtained at laboratory scale is used to validate the proposed model. Experiments are conducted using a forced convection laboratory dryer at temperatures of 60 degrees C and 80 degrees C and air velocities of 0.2 and 0.7 m/s to dry chicory root cubes of 1 cm of side. Mathematical modeling is firstly used to represent the performance of the drying process with the temporal variations of the average humidity content, to determine diffusion coefficients, and afterwards, to obtain useful predictions on how the volumetric contraction of the cubes behaves under different operating conditions. The good agreements between experimental and predicted values prove that the proposed model can be applied to the precise description of experimental drying curves for chicory roots in three dimensions (3-D). In the ranges covered, the values of the effective moisture diffusivity were obtained between 5.63 x 10(-5) and 8.21 x 10(-5) cm(2)/s. Results from the analysis of rehydration and browning aspects illustrate that drying conditions have effects on the quality attributes of the dried samples. (C) 2018 Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:114 / 128
页数:15
相关论文
共 47 条
  • [1] Afaghi N., 2013, Int. J. Adv. Biol. Biomed. Res, V1, P1660
  • [2] Aguilera J.M., 1999, Microstructural principles of food processing and engineering
  • [3] Drying and Rehydration of Oyster Mushroom
    Apati, Giannini Pasiznick
    Furlan, Sandra Aparecida
    Laurindo, Joao Borges
    [J]. BRAZILIAN ARCHIVES OF BIOLOGY AND TECHNOLOGY, 2010, 53 (04) : 945 - 952
  • [4] Heat and mass transfer in apple cubes in a microwave-assisted fluidized bed drier
    Askari, G. R.
    Emam-Djomeh, Z.
    Mousavi, S. M.
    [J]. FOOD AND BIOPRODUCTS PROCESSING, 2013, 91 (C3) : 207 - 215
  • [5] Moisture diffusivity and drying kinetic equation of convective drying of grapes
    Azzouz, S
    Guizani, A
    Jomaa, W
    Belghith, A
    [J]. JOURNAL OF FOOD ENGINEERING, 2002, 55 (04) : 323 - 330
  • [6] Modelling of drying kinetic of potatoes taking into account shrinkage
    Bacelos, Marcelo S.
    Almeida, Paulo I. F.
    [J]. 11TH INTERNATIONAL CONGRESS ON ENGINEERING AND FOOD (ICEF11), 2011, 1 : 713 - 721
  • [7] Simultaneous heat and mass transfer in shrinkable apple slab during drying
    Bialobrzewski, I
    [J]. DRYING TECHNOLOGY, 2006, 24 (05) : 551 - 559
  • [8] Mass transfer in the celery slice: Effects of temperature, moisture content, and density on water diffusivity
    Bialobrzewski, I
    Markowski, M
    [J]. DRYING TECHNOLOGY, 2004, 22 (07) : 1777 - 1789
  • [9] Chandra M.V.P., 2010, INT J HEAT MASS TRAN, V53, P4638, DOI DOI 10.1016/J.IJHEATMASSTRANSFER.2010.06.029
  • [10] Choi Y., 1986, Food Engineering and Process Applications