S. Schenck , S. Barrios , A. Ferrari , P. Lema , S.M. Goñi
{"title":"Macroscopic modelling and parameter estimation of blueberries freeze-drying","authors":"S. Schenck , S. Barrios , A. Ferrari , P. Lema , S.M. Goñi","doi":"10.1016/j.fbp.2025.05.007","DOIUrl":null,"url":null,"abstract":"<div><div>This work aimed to enhance comprehension of the processes involved in the primary stage of blueberry freeze-drying by applying and evaluating two mathematical models to whole fruits, assuming spherical geometry. This approach represents a novel contribution to the modeling of freeze-drying of whole solid plant foods. Blueberries were modeled as spheres with dried and icy layers delimited by the icy core radius. Two models were proposed, to predict the evolution of key state variables - interface temperature, internal temperature, interface pressure, surface pressure and total sublimation time during the process. Model 1 includes five parameters and a detailed representation of heat and mass transfer resistances, and assumes spherical symmetry, neglects shrinkage and desorption, and describes a one-dimensional heat and mass transfer in series. Model 2 is a simplified version of Model 1, represented with three parameters, by unifying mass and heat transfer coefficients. Experimental data from pressure rise tests (PRT) at 20 Pa chamber pressure (<span><math><msub><mrow><mi>P</mi></mrow><mrow><mi>vc</mi></mrow></msub></math></span>) and shelf temperatures (<span><math><msub><mrow><mi>T</mi></mrow><mrow><mi>s</mi></mrow></msub></math></span>) of −20, 0, 10 and 20 °C were used for parameter estimation and validation. Particle swarm optimization was employed to determine heat and mass transfer parameters by minimizing mean square error (MSE) and mean absolute percentage error (MAPE). Performance metrics including MSE, MAPE and coefficient of determination (<span><math><mrow><msup><mrow><mi>R</mi></mrow><mrow><mn>2</mn></mrow></msup><mo>)</mo><mspace></mspace></mrow></math></span>were considered to evaluate the models. The two models achieved errors below 10 % for PRT. The major contribution to overall mass transfer resistance lies in the blueberry skin layer. When models were used to predict sublimation rate, Model 2 significantly outperformed Model 1 in predicting the initial slope of PRT curves (<span><math><msup><mrow><mi>R</mi></mrow><mrow><mn>2</mn></mrow></msup></math></span> = 0.96 vs. 0.73). Model 2 was used to simulate the effects of control variables (<span><math><msub><mrow><mi>P</mi></mrow><mrow><mi>vc</mi></mrow></msub></math></span> and <span><math><msub><mrow><mi>T</mi></mrow><mrow><mi>s</mi></mrow></msub></math></span>) and blueberry initial radius on sublimation time. This work enhances the understanding of heat and mass transfer mechanisms in blueberry freeze-drying, providing a valuable tool for process optimization.</div></div>","PeriodicalId":12134,"journal":{"name":"Food and Bioproducts Processing","volume":"152 ","pages":"Pages 191-206"},"PeriodicalIF":3.5000,"publicationDate":"2025-05-15","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Food and Bioproducts Processing","FirstCategoryId":"97","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0960308525000951","RegionNum":2,"RegionCategory":"农林科学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"BIOTECHNOLOGY & APPLIED MICROBIOLOGY","Score":null,"Total":0}
引用次数: 0
Abstract
This work aimed to enhance comprehension of the processes involved in the primary stage of blueberry freeze-drying by applying and evaluating two mathematical models to whole fruits, assuming spherical geometry. This approach represents a novel contribution to the modeling of freeze-drying of whole solid plant foods. Blueberries were modeled as spheres with dried and icy layers delimited by the icy core radius. Two models were proposed, to predict the evolution of key state variables - interface temperature, internal temperature, interface pressure, surface pressure and total sublimation time during the process. Model 1 includes five parameters and a detailed representation of heat and mass transfer resistances, and assumes spherical symmetry, neglects shrinkage and desorption, and describes a one-dimensional heat and mass transfer in series. Model 2 is a simplified version of Model 1, represented with three parameters, by unifying mass and heat transfer coefficients. Experimental data from pressure rise tests (PRT) at 20 Pa chamber pressure () and shelf temperatures () of −20, 0, 10 and 20 °C were used for parameter estimation and validation. Particle swarm optimization was employed to determine heat and mass transfer parameters by minimizing mean square error (MSE) and mean absolute percentage error (MAPE). Performance metrics including MSE, MAPE and coefficient of determination (were considered to evaluate the models. The two models achieved errors below 10 % for PRT. The major contribution to overall mass transfer resistance lies in the blueberry skin layer. When models were used to predict sublimation rate, Model 2 significantly outperformed Model 1 in predicting the initial slope of PRT curves ( = 0.96 vs. 0.73). Model 2 was used to simulate the effects of control variables ( and ) and blueberry initial radius on sublimation time. This work enhances the understanding of heat and mass transfer mechanisms in blueberry freeze-drying, providing a valuable tool for process optimization.
期刊介绍:
Official Journal of the European Federation of Chemical Engineering:
Part C
FBP aims to be the principal international journal for publication of high quality, original papers in the branches of engineering and science dedicated to the safe processing of biological products. It is the only journal to exploit the synergy between biotechnology, bioprocessing and food engineering.
Papers showing how research results can be used in engineering design, and accounts of experimental or theoretical research work bringing new perspectives to established principles, highlighting unsolved problems or indicating directions for future research, are particularly welcome. Contributions that deal with new developments in equipment or processes and that can be given quantitative expression are encouraged. The journal is especially interested in papers that extend the boundaries of food and bioproducts processing.
The journal has a strong emphasis on the interface between engineering and food or bioproducts. Papers that are not likely to be published are those:
• Primarily concerned with food formulation
• That use experimental design techniques to obtain response surfaces but gain little insight from them
• That are empirical and ignore established mechanistic models, e.g., empirical drying curves
• That are primarily concerned about sensory evaluation and colour
• Concern the extraction, encapsulation and/or antioxidant activity of a specific biological material without providing insight that could be applied to a similar but different material,
• Containing only chemical analyses of biological materials.