Numerical and experimental studies on drying behavior of radio frequency assisted convective drying for thin-layer corn kernels

2021 ◽  
Vol 191 ◽  
pp. 106520
Author(s):  
Shuo Wei ◽  
Weijun Xie ◽  
Zhaohui ZHeng ◽  
Deyong Yang
2012 ◽  
Vol 58 (No. 2) ◽  
pp. 73-82 ◽  
Author(s):  
R. Amiri Chayjan ◽  
K. Salari ◽  
B. Shadidi

Thin layer drying properties of high moisture garlic sheets under semi fluidized and fluidized bed conditions with high initial moisture content (about 154.26% d.b.) were studied. Air temperatures of 50, 60, 70 and 80&deg;C were applied to garlic samples. Among the applied models, Page model was the best to predict the thin layer drying behavior of garlic sheets. Using this model, correlation coefficient (R<sup>2</sup>) was high for all drying cases. The computed values of D<sub>eff</sub> were between 3.38 &times; 10<sup>&ndash;10</sup> and 2.54 &times; 10<sup>&ndash;9</sup> m<sup>2</sup>/s during the falling rate drying. Values of D<sub>eff</sub> for garlic sheets were also increased with increasing in input air temperature. Activation energy values were varied between 51.32 and 60.58 kJ/mol for 50 to 80&deg;C, respectively. The specific energy consumption (SEC) for garlic specimens was placed in the range of 0.316 &times; 10<sup>6</sup> and 0.979 &times; 10<sup>6</sup> kJ/kg from 50 to 80&deg;C, respectively. An increase in air temperature caused decrease in SEC value. Application of semi fluidized bed convective drying with temperature between 50 and 60&deg;C was suitable to produce dried garlic. &nbsp; &nbsp;


2016 ◽  
Vol 599 ◽  
pp. 49-53 ◽  
Author(s):  
P. Svarnas ◽  
M.A. Botzakaki ◽  
G. Skoulatakis ◽  
S. Kennou ◽  
S. Ladas ◽  
...  

2015 ◽  
Vol 33 (11) ◽  
pp. 1302-1308 ◽  
Author(s):  
Laurent Fraikin ◽  
Benjamin Herbreteau ◽  
Thierry Salmon ◽  
François Nicol ◽  
Michel Crine ◽  
...  

2019 ◽  
Vol 874 ◽  
pp. 235-262 ◽  
Author(s):  
Thomas D. Nevins ◽  
Douglas H. Kelley

The mixing of a reactive scalar by a fluid flow can have a significant impact on reaction dynamics and the growth of reacted regions. However, experimental studies of the fluid mechanics of reactive mixing present significant challenges and puzzling results. The observed speed at which reacted regions expand can be separated into a contribution from the underlying flow and a contribution from reaction–diffusion dynamics, which we call the chemical front speed. In prior work (Nevins & Kelley, Chaos, vol. 28 (4), 2018, 043122), we were surprised to observe that the chemical front speed increased where the underlying flow in a thin layer was faster. In this paper, we show that the increase is physical and is caused by smearing of reaction fronts by vertical shear. We show that the increase occurs not only in thin-layer flows with a free surface, but also in Hele-Shaw systems. We draw these conclusions from a series of simulations in which reaction fronts are located according to depth-averaged concentration, as is common in laboratory experiments. Where the front profile is deformed by shear, the apparent front speed changes as well. We compare the simulations to new experimental results and find close quantitative agreement. We also show that changes to the apparent front speed are reduced approximately 80 % by adding a lubrication layer.


Heliyon ◽  
2020 ◽  
Vol 6 (4) ◽  
pp. e03220
Author(s):  
Vasudha Agnihotri ◽  
Priyanka Adhikari ◽  
Neha Pandey ◽  
Priyanka Sati ◽  
Anita Pandey

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