Pressure drop in dairy evaporators: Experimental study and friction factor modelling

被引:8
|
作者
Mura, Ernesto [1 ]
Gourdon, Mathias [1 ]
机构
[1] Chalmers, Environm & Energy Dept, Div Ind Energy Syst & Technol, SE-41296 Gothenburg, Sweden
关键词
Drying process; Falling film; Annular two-phase flow; Vapour pressure losses; FALLING-FILM EVAPORATION; HEAT-TRANSFER; ANNULAR-FLOW;
D O I
10.1016/j.jfoodeng.2016.09.020
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The pressure drop that occurs during the falling film evaporation of dairy products is related to the downward co-flowing vapour and directly affects the saturation temperature of the product, resulting in a non-constant thermal driving force of the process along the evaporator. Frictional forces are the major contributor to the pressure drop, and the friction factor is a crucial parameter in reliably estimating the pressure drop. In the present study, the absolute vapour flow pressure losses during falling film evaporation of dairy products were measured using an experimental internal tube evaporator set-up. To simulate real industrial conditions, experiments were conducted by varying the co-flow inlet velocity (from 0 to 37 ms(-1)) over a wide range of product dry solid content DC (from DC = 0%-50%). Results obtained at DC = 0% show that the experimental approach is consistent when measurements are compared to the well-known Wallis correlation. A large number of experimental data has been obtained for DC between 13 and 40% for which the pressure losses have a strong dependence from the co-flowing vapour rate; in some specific cases, the influence of the surface bubbling phenomena has been put in evidence. The presented results, have been used to calibrate a new accurate correlation for the friction factor (4f(tv)) coefficient showing a squared residual of R-2 = 0.93. (C) 2016 Elsevier Ltd. All rights reserved.
引用
收藏
页码:128 / 136
页数:9
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