Inverse estimation of fluid-to-particle heat transfer coefficient in aseptic processing of particulate foods

被引:8
作者
Vidyarthi, Sriram K. [1 ,2 ]
Mishra, Dharmendra K. [3 ]
Dolan, Kirk D. [4 ]
Muramatsu, Yoshiki [5 ]
机构
[1] Morning Star Co, Woodland, CA 95695 USA
[2] Univ Calif Davis, Dept Biol & Agr Engn, Davis, CA 95616 USA
[3] Purdue Univ, Dept Food Sci, Smith Hall, W Lafayette, IN 47907 USA
[4] Michigan State Univ, Dept Food Sci & Human Nutr, E Lansing, MI 48824 USA
[5] Tokyo Univ Agr, Dept Bioprod & Environm Engn, Setagaya Ku, Tokyo 1568502, Japan
基金
美国食品与农业研究所;
关键词
Mathematical modelling; Inverse method; Particulate food; Fluid-to-liquid heat transfer; Aseptic processing; RESIDENCE TIME DISTRIBUTION; LOW-ACID FOODS; MODEL; LETHALITY; TOMATO;
D O I
10.1016/j.biosystemseng.2020.08.012
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
This study proposes and implements inverse methods to estimate fluid-to-particulate heat transfer coefficient (h(fp)) of liquid-particulate solution (sweet potato puree and chickpea) during aseptic processing. The other physical and thermal properties of food were computed using forward techniques. A statistical analysis was conducted to assess the accuracy of the estimated results and performance of the inverse method. The inverse technique successfully estimated the h(fp) with a good correlation with simulated and predicted temperature of the centre of the fastest moving solid particle, zero mean and uncorrelated errors in residuals, higher scaled sensitivity coefficient, and consistent sequential estimation curve. The good fitting between the simulated experimental and the estimated results confirms the robustness of the proposed inverse method in estimating accurate h(fp) to achieve sufficient lethality of the liquid-particulate food product. The study can be useful in facilitating the optimisation of the carrier fluid rheological specifications, the design of the processing equipment, and the process settings for the commercial aseptic system. Published by Elsevier Ltd on behalf of IAgrE.
引用
收藏
页码:210 / 222
页数:13
相关论文
共 40 条
[1]  
Balasubramaniam V. M., 1993, THESIS
[2]   LIQUID-TO-PARTICLE CONVECTIVE HEAT-TRANSFER IN NON-NEWTONIAN CARRIER MEDIUM DURING CONTINUOUS TUBE FLOW [J].
BALASUBRAMANIAM, VM ;
SASTRY, SK .
JOURNAL OF FOOD ENGINEERING, 1994, 23 (02) :169-187
[4]  
Berk Z, 2018, FOOD PROCESS ENGINEERING AND TECHNOLOGY, 3RD EDITION, P1, DOI 10.1016/C2016-0-03186-8
[5]   Food Hygiene in aseptic processing and packaging system: A survey in the Italian food industry [J].
Betta, Giampaolo ;
Barbanti, Davide ;
Massini, Roberto .
TRENDS IN FOOD SCIENCE & TECHNOLOGY, 2011, 22 (06) :327-334
[6]   Estimation of local heat transfer coefficient in coiled tubes under inverse heat conduction problem approach [J].
Bozzoli, Fabio ;
Cattani, Luca ;
Rainieri, Sara ;
Pagliarini, Giorgio .
EXPERIMENTAL THERMAL AND FLUID SCIENCE, 2014, 59 :246-251
[7]   Residence time distribution of particulate foods at aseptic processing temperatures [J].
Chandarana, DI ;
Unverferth, JA .
JOURNAL OF FOOD ENGINEERING, 1996, 28 (3-4) :349-360
[8]   Calculation of the convective heat transfer coefficient and thermal diffusivity of cucumbers using numerical simulation and the inverse method [J].
da Silva, Wilton Pereira ;
e Silva, Cleide M. D. P. S. .
JOURNAL OF FOOD SCIENCE AND TECHNOLOGY-MYSORE, 2014, 51 (09) :1750-1761
[9]  
Farid M.M., 2010, Mathematical modeling of food processing
[10]   Modeling heat and mass transfer in immersion frying .1. Model development [J].
Farkas, BE ;
Singh, RP ;
Rumsey, TR .
JOURNAL OF FOOD ENGINEERING, 1996, 29 (02) :211-226