Modeling the Drying of Wheat Seeds in a Fluidized Bed Using a Spatially Resolved Model

2019 ◽  
Vol 35 (4) ◽  
pp. 551-559
Author(s):  
Mohamed - Hemis ◽  
Dennis G. Watson ◽  
Vijaya G. S. Raghavan

Abstract. A mathematical model for simulating heat and mass transfer during fluidized-bed drying of wheat grains has been developed, combining two transfer steps; a movement of moisture inside the grain and outside the grain. Empirical equations have been used for material properties as well as for transfer processes. The developed model is composed of two models coupled to each other; the distributed parameter model (DPM or Luikov model) and the convective model. The coupled mathematical model was solved numerically by a finite difference method after discretization of equilibrium equations distributed in space. The DPM model made it possible to predict the quantity of water extracted from the grain under the effect of known drying conditions. Results showed that the drying rate of wheat increased when air temperature was increased; and that the rates were higher in the first few minutes of drying, achieving 2.6 × 10-5and 1.7 × 10-5 kg water kg-1[d.b.]·s-1 for temperatures of 66.7°C and 58.6°C, respectively. A comparison of experimental and predicted results gave good agreement, and the use of the distributed model improved the predictive capabilities of wheat grain drying in fluidized beds. Keywords: Canada Western Red Spring, Distributed parameter model, Fluidized-bed dryer, Mathematical modeling, Wheat seeds.

Processes ◽  
2018 ◽  
Vol 6 (12) ◽  
pp. 245 ◽  
Author(s):  
Der-Sheng Chan ◽  
Meng-I Kuo

The development of an effective drying performance of the fluidized bed dryer (FBD) is crucial to reduce drying costs. The objective of this study was to investigate the drying performance of wheat germ (WG) with different time-temperature combinations in the FBD. The WG was dried at different set temperatures of 80, 100 and 120 °C. The moisture content (MC) and water activity (WA) of WG were measured. A mathematical model was proposed to develop an optimal drying condition. The changes in the MC of WG during drying in the FBD could be divided into the decreased period, the dynamic equilibrium period and the increased period. The product temperature of 45 °C and WA of 0.3 of WG drying could be attained by different time-temperature combinations. The mathematical model, which was developed in conjunction with different time-temperature combinations, could predict the dehydration time and the condensation time of WG for optimization the drying conditions. The WG dehydration at the heating stage and the WG condensation at the cooling stage could also be evaluated by the dehydration flux and the condensation flux, respectively. The optimal drying performance of WG exists in a compromise between promoting dehydration and reducing condensation. Information obtained from the analysis of dehydration flux and condensation flux with experimental data and simulation gave the guidelines for performing an effective drying of WG in the FBD.


2006 ◽  
Vol 24 (11) ◽  
pp. 1457-1467 ◽  
Author(s):  
Somchart Soponronnarit ◽  
Somkiat Prachayawarakorn ◽  
Wathanyoo Rordprapat ◽  
Adisak Nathakaranakule ◽  
Warunee Tia

2017 ◽  
Vol 8 (1) ◽  
pp. 57-65 ◽  
Author(s):  
T. Poós ◽  
V. Szabó

Fluidized bed dryers are widely used in several fields of industry. Sufficiently accurate thermal models provide an opportunity to increase the effectiveness of dryers. The required size of a fluidized bed dryer can be defined with the application of mathematical model. This work is aimed at developing mathematical model to investigate the influence of operating parameters in a fluidized bed dryer using volumetric heat transfer coefficient. After the defining the input parameters of the differential equations, the required entry length of the dryer which effective heat and mass transfer between gas and particles takes place can be estimated. The correct estimation of the entry length is useful in optimal design of a fluidized bed dryer. Using the model the impact of the drying parameters can be determined to the required length.


2020 ◽  
Vol 53 (2) ◽  
pp. 7765-7770
Author(s):  
Simon Bachler ◽  
Jens Wurm ◽  
Frank Woittennek

Author(s):  
Sebastian Alexander Pérez Cortés ◽  
Yerko Rafael Aguilera Carvajal ◽  
Juan Pablo Vargas Norambuena ◽  
Javier Antonio Norambuena Vásquez ◽  
Juan Andrés Jarufe Troncoso ◽  
...  

Foods ◽  
2019 ◽  
Vol 8 (5) ◽  
pp. 147 ◽  
Author(s):  
Saheeda Mujaffar ◽  
Sheena Ramsumair

Pumpkin seeds are a major agricultural waste from the fresh-cut produce industry. The objective of this study was to investigate the drying behavior of untreated, whole pumpkin seeds in a fluidized bed dryer at 50–80 °C (2.87 m/s), with a view to producing a high-quality pumpkin powder from dried seeds. Seeds were dried at 50–80 °C to an average equilibrium moisture value of 0.035 to 0.006 g H2O/g DM (3.4 to 0.6% wb). Drying occurred in the falling rate period only and drying rate constants ranged from 0.0226 to 0.0900 1/min with corresponding diffusivity values for the first falling-rate period ranging from 4.68 to 18.63 × 10−10 m2/s. The activation energy (Ea)—for the first falling rate period was determined to be 43.9 kJ/mol. Of the nineteen thin layer models tested, the Alibas model could be successfully used as a general model to predict the Moisture Ratio (MR) data for all temperatures investigated. After drying, seeds were blended to produce powders, which were found to be high in fat, crude protein and fiber.


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