Study of heat transfer coefficients and temperature distribution in a continuous flow pasteurizer with helical tubes using model fluids in laminar flow

被引:2
作者
Russo, Guilherme [3 ]
Gut, Jorge Andrey Wilhelms [1 ,2 ]
机构
[1] Univ Sao Paulo, Escola Politecn, Dept Chem Engn, BR-05424970 Sao Paulo, Brazil
[2] Univ Sao Paulo, FoRC, Food Res Ctr, Sao Paulo, Brazil
[3] Univ Sao Paulo, Escola Politecn, Dept Chem Engn, Av Prof Luciano Gualberto,Trav 3,380, BR-05508010 Sao Paulo, SP, Brazil
基金
巴西圣保罗研究基金会;
关键词
heat exchanger; heat transfer; mathematical modeling; pasteurization; thermal processing; RESIDENCE TIME DISTRIBUTION; NON-NEWTONIAN FLUIDS; TRANSFER ENHANCEMENT; TUBULAR REACTORS; EXCHANGERS; FOOD; JUICE;
D O I
10.1515/ijfe-2021-0340
中图分类号
TS2 [食品工业];
学科分类号
0832 ;
摘要
Modeling of continuous pasteurization is useful for predicting time-temperature history of the product and lethality. The use of helical tubes in the heat exchangers and holding tube can simplify modeling in laminar flow due to the narrowing of the residence time distribution. To present this approach, three model fluids (water, 80% glycerol/water and 1% carboxymethylcellulose) were processed in 25 conditions in a pilot scale unit and the overall heat transfer coefficients of the heater, cooler and holding tube were correlated with Reynolds and Prandtl numbers. For heater and cooler, 3-7 parameters were needed for a fair adjustment, while in the holding tube an average value was obtained. Using these correlations, a simple unidimensional model was simulated to predict the time-temperature history and lethality distribution. Simulation examples for processing at 90 degrees C provided the F-value contribution of each step showing that this model can be useful for process analysis and design.
引用
收藏
页码:559 / 570
页数:12
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