Mathematical Modelling of Food Processing

A special issue of Foods (ISSN 2304-8158). This special issue belongs to the section "Food Engineering and Technology".

Deadline for manuscript submissions: closed (29 February 2024) | Viewed by 1037

Special Issue Editors


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Guest Editor
Department of Food Engineering, Faculty of Engineering, King Mongkut's University of Technology Thonburi, 126 Pracha u‐tid Road, Tungkru, Bangkok 10140, Thailand
Interests: drying; novel food proceesing; food property characterization; mathematical modeling of food processing operations

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Guest Editor
Department of Chemical Engineering, Faculty of Engineering, King Mongkut’s University of Technology Thonburi, Bangkok, Thailand
Interests: food drying; fruits and grains

Special Issue Information

Dear Colleagues,

Modelling is an important tool for devising and improving food processing systems since it allows the generation of valuable data necessary for such activities without having to heavily rely on tedious and, in most cases, expensive experiments. This would lead in turn to the availability of higher-efficiency devices, equipment and optimal operating processing conditions. Modelling can be performed either through the use of analytical, numerical or empirical tools and can include the prediction and understanding of complex transport processes, physicochemical property changes and even oral mastication as well as gastro-intestinal digestion. Modelling is beneficial in understanding the nature of a process and determining the relevant effective and/or optimal process parameters and conditions. Simulation strategies in modelling could be beneficial in the visualization of the effects of process parameters, determination of the optimal process conditions or design parameters for the scaling-up of industrial lines, and their validation.

This Special Issue aims to serve as an outlet for high-quality, state-of-the art articles dealing with all aspects of mathematical modelling as related to foods. Potential topics include, but are not limited to, numerical methods in mathematical modelling, computational simulations, trends in modelling procedures for food processing, modelling-based optimization and design of food processing operations/systems and their validation, and life cycle analysis.

Prof. Dr. Sakamon Devahastin
Dr. Somkiat Prachayawarakorn
Guest Editors

Manuscript Submission Information

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Keywords

  • modelling
  • computational
  • numerical
  • optimization
  • transport phenomena
  • quality
  • human-food relations
  • equipment
  • scale-up

Published Papers (1 paper)

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Research

15 pages, 4404 KiB  
Article
Analysis of Mass Transfer and Shrinkage Characteristics of Chinese Cabbage (Brassica rapa L. ssp. pekinensis) Leaves during Osmotic Dehydration
by Timilehin Martins Oyinloye and Won Byong Yoon
Foods 2024, 13(2), 332; https://doi.org/10.3390/foods13020332 - 20 Jan 2024
Viewed by 649
Abstract
The mass transfer and shrinkage characteristics of Chinese cabbage (CC) during osmotic dehydration (OD) were investigated. The leaves were grouped into four sections and analyzed based on their morphological characteristics (i.e., maturity, width, and thickness). The sections were immersed in 2.0 mol/m3 [...] Read more.
The mass transfer and shrinkage characteristics of Chinese cabbage (CC) during osmotic dehydration (OD) were investigated. The leaves were grouped into four sections and analyzed based on their morphological characteristics (i.e., maturity, width, and thickness). The sections were immersed in 2.0 mol/m3 NaCl for 120 h at 25 ± 2 °C. The diffusion coefficient (D) of the leaf blade was not significantly different with respect to the sections that were formed, but it was significantly different in the midrib in the increasing order of P1, P4, P3, and P2, with values of 1.12, 1.61, 1.84, and 2.06 (× 10−6), respectively, after a 1 h soaking period due to the different characteristics in morphology and structure, such as porosity (0.31, 0.41, 0.42, and 0.38 for positions 1, 2, 3, and 4, respectively) and fiber contents. Numerical simulation (NS) for CC was conducted with and without the consideration of shrinkage during OD. The shrinkage effect on the NaCl uptake analyzed using NS indicated no significant difference between 0 to 48 h for both models. However, changes in the NaCl concentration were observed from 48 h onwards, with a lesser concentration in the model with shrinkage for all sections. The difference in NaCl concentration for the models with and without shrinkage was within the standard error range (±0.2 mol/m3) observed during experimental analysis. This implies that the shrinkage effect can be overlooked during the modeling of CC to reduce computational power. Full article
(This article belongs to the Special Issue Mathematical Modelling of Food Processing)
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