scholarly journals Effect of ultrasound pre-treatment on the drying kinetics of brown seaweed Ascophyllum nodosum

2015 ◽  
Vol 23 ◽  
pp. 302-307 ◽  
Author(s):  
Shekhar U. Kadam ◽  
Brijesh K. Tiwari ◽  
Colm P. O’Donnell
2014 ◽  
Vol 50 (5) ◽  
pp. 670-675 ◽  
Author(s):  
Shekhar U. Kadam ◽  
Brijesh K. Tiwari ◽  
Shane O’Connell ◽  
Colm P. O’Donnell

2020 ◽  
Vol 44 (11) ◽  
Author(s):  
Muhammad Heikal Ismail ◽  
Khursheed Alam Khan ◽  
Ngadisih Ngadisih ◽  
Mami Irie ◽  
Sze Pheng Ong ◽  
...  

2020 ◽  
Vol 8 (10) ◽  
pp. 35-44
Author(s):  
Mamadou Lamine Coly ◽  
◽  
Mamadou Seck Gueye ◽  
Boucounta Mbaye ◽  
Waly Faye ◽  
...  

This work is part of a study for the conservation of fish products through solar drying. The grey seabream is dried after a pre-treatment of 16 hours in a salt brine under two conditions: on a rack in open air and in a solar dryer. The tests were carried out under average irradiance conditions of 592.76 W/m², an average ambient temperature of 30°C and an average air temperature in the dryer of 50°C. The results obtained, allowed us to reach a final humidity of 32% from an initial humidity of 65% in a wet basis. The drying was processed in 15 hours, (i.e. two days in the dryer) and 24 hours (i.e. three days in the open air). The modeling of the drying kinetics of the grey sea bream is carried out from empirical or semi-empirical models taken from the previous works. Several criteria were defined for the choice of the two-term model as being the one that can describe in the best way, the drying of the fish in both conditions. The effective diffusivity was determined using Ficks diffusive model whose solution is given by Crank, so that the logarithm of the reduced moisture allows us to find effective diffusivities for fish of 9.88823 10-7 (m²/s) and 1.72534 10-6 (m²/s) for open-air and in dryer drying respectively.


2006 ◽  
Vol 9 (3) ◽  
pp. 541-549 ◽  
Author(s):  
C. González-Martínez ◽  
M. Cháfer ◽  
K. Xue ◽  
A. Chiralt

Author(s):  
Elham Azarpahzooh ◽  
Hosahalli S. Ramaswamy

The effect of microwave-osmotic dehydration pre-treatment under continuous flow medium spray (MWODS) conditions on the second stage air-drying kinetics of apple (Red Gala) cylinders was evaluated. MWODS pre-treatment was carried out using a response surface methodology involving 5-levels of sucrose concentration (33-66.8°B), temperature (33-66.8°C) and contact time (5-55 min). Drying time and coefficient of moisture diffusion (Dm) and coefficient of moisture infusion (Im) during rehydration were evaluated as responses and the results were compared with their air-dried (AD) (worst scenario) and freeze-dried (FD) (best scenario) counterparts without the osmotic treatments. The diffusion and infusion coefficients were based on the solution of Fick's diffusion model. Empirical models developed for all response variables were significant (P ? 0.001) and the lack of fit was not significant (P > 0.05). MWODS pre-treatments significantly influenced the Dm values and reduced the air-drying time of apples by 30-65 percent in comparison with untreated apple thereby providing opportunity for better energy savings. On the other hand, the values of Im during the rehydration process were highest for the freeze-dried samples followed by apples air-dried after MWODS treatment, and the least for the untreated air-dried samples.


2009 ◽  
Vol 27 (No. 2) ◽  
pp. 88-94 ◽  
Author(s):  
S. Jokić ◽  
D. Velić ◽  
M. Bilić ◽  
J. Lukinac ◽  
M. Planinić ◽  
...  

The aim of this research was to determine the influence of the process parameters and pre-treatment methods on the quality and drying kinetics of apple samples of the Florina variety using standard analytical methods: thermo-gravimetry, rehydration, colorimetry. The Apple samples were dried in a laboratory tray drier at different temperatures (50, 60, and 70°C), airflow velocities (1.5 m/s and 2.75 m/s), and pre-treatment methods (dipping in 0.5% ascorbic acid solution; 0.3% L-cysteine solution; 0.1% 4-hexyl resorcinol solution; 0.5% sodium metabisulfite solution; mixed solution of 0.05% 4-hexyl resorcinol and 0.5% sodium metabisulfite; blanching in hot water at 85°C). According to the drying time, rehydration and colour characteristics, the optimal drying parameters found were: temperature of 60°C and airflow velocity of 2.75 m/s. The drying kinetic equations were estimated using Page’s mathematical model. The results of the estimation showed a good agreement with the experimental data. The best results were achieved when the samples were pre-treated with 4-hexyl resorcinol. Blanching in hot water resulted in a higher drying rate and higher rehydration ratio, but also in unacceptable changes in the colour appearance of the apple samples.


Author(s):  
Marianne S Brooks ◽  
Abdel E Ghaly ◽  
Nabiha H Abou El-Hana

The air-drying kinetics of plum tomato pieces pre-treated with different osmotic solutions were investigated. Four pre-treatment solutions (comprised of salt, sugar and/or calcium lactate), three sample geometries (halves, quarters and eighths) and two air-drying temperatures (55 and 65°C) were studied. In general, the rate of drying over time appeared to fit an exponential curve (R2 values between 0.74 and 0.99). A closer look at the data indicated that the rate of drying appeared to follow two separate falling rate periods. The change from one falling rate period to another was observed for samples at a transition moisture ratio of ~ 0.2, for all geometries and temperatures. Thus, modeling the process was improved by including the two falling rate periods. The drying constant (K) for the two falling rate periods ranged between 0.05 to 0.3 h-1. Moisture diffusivity values ranged from 2.5 x 10-9 to 9 x 10-9 m2 s-1 and were relatively constant during the first falling rate period. During the second falling rate period, the diffusivity increased as the moisture ratio decreased, though this change was less pronounced as the sample size decreased from halves to eighths. The untreated samples had lower diffusivities than those with osmotic pre-treatment but there were no differences amongst the various pre-treatment solutions. In general, moisture diffusivities showed a dependence on the sample size, as the larger tomato samples had higher values of diffusivity. The greater diffusivity seen in the larger samples may be due to the collapse of cell walls in the skin.


2014 ◽  
Vol 7 (9) ◽  
pp. 2516-2527 ◽  
Author(s):  
Lijun Liu ◽  
Yuxin Wang ◽  
Dandan Zhao ◽  
Kejing An ◽  
Shenghua Ding ◽  
...  

2018 ◽  
Vol 237 ◽  
pp. 110-117 ◽  
Author(s):  
R. Ostermeier ◽  
P. Giersemehl ◽  
C. Siemer ◽  
S. Töpfl ◽  
H. Jäger

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