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Residence Time Distribution of Multiple Particles in Four Configurations of Holding Tubes

Zeynep Tanyel
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TLDR
In this paper, the authors investigated the residence time distributions of multiple particles (as affected by process and system parameters) during non-Newtonian tube flow during polystyrene and acrylic particles were used as model food particles.
Abstract
Residence time distributions of multiple particles (as affected by process and system parameters) were investigated during non-Newtonian tube flow. Process parameters included flow rate, particle type, carrier fluid viscosity, and particle concentration. The system parameter of interest was the holding tube configuration. Polystyrene and acrylic particles were used as model food particles. Digital imaging analysis was used to obtain residence time data of particles. A novel type of holding tube (chaotic holding tube) was constructed. Comparisons among the straight, single helical, double helical, and chaotic holding tube were performed in terms residence time distribution (RTD) of particles. In addition, the effect of inclination angle (0 º and 45 º) of the chaotic holding tube was investigated. It was found that the narrowest RTD of particles was obtained in the single helical holding tube. RT std in the chaotic holding tube was greater than that in the single helical holding tube, but lower than those in the straight and double helical holding tubes. The most significant process parameter affecting RTD was flow rate. The effect of flow rate was more pronounced for high density (acrylic) particles. Carrier fluid viscosity, particle type, and particle concentration did not have significant effects on the overall RT std. Trends observed in the chaotic holding tube were similar to those observed in the single helical holding tube. However, there were some cases where use of chaotic holding tube resulted in narrower RTD of particles. Changing the inclination angle from 0 º to 45 º in the chaotic holding tube resulted in wider RTD of both types of particles. Denizli, a small town in the Aegean region of Turkey. In 1993, her family moved to the capital city, Ankara, where she attended high school and college. She graduated from Middle East Technical University in 2002, with a B.S degree in Food Engineering. In the summer of 2002, she was admitted to the graduate school at North Carolina State University where she began her Master of Science degree in the Department of Food Science. She currently works as a research assistant in the same department. iii ACKNOWLEDGEMENTS

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Aseptic Processing of Foods Containing Particulates

A.R. Isaacs, +1 more
TL;DR: Aseptic processing involves sterilising the product and package separately, and filling under sterile conditions as discussed by the authors, which can provide better product quality compared with canned products, lower transport and storage costs compared with frozen products, and virtually no restriction on package size.
References
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Journal ArticleDOI

Modelling non‐Newtonian two‐phase flow in conventional and helical‐holding tubes

TL;DR: In this article, a finite difference FORTRAN program (using the fourth-order, four-stage explicit Runge-Kutta method) was written by the authors to compute the velocity of fluid elements and particles during fully 3D flow in conventional and helical-holding tubes.
Journal ArticleDOI

Residence Time Distribution of Particles during Two-Phase Non-Newtonian Flow in Conventional as compared with Helical Holding Tubes

TL;DR: In this article, the residence times of multiple particles during the flow of a non-Newtonian suspension through a conventional holding tube assembly were compared with that in a helical hold tube assembly of identical length and tube diameter.
Journal ArticleDOI

Residence Time Distribution of Multiple Particles in Non-Newtonian Holding Tube Flow: Statistical Analysis

TL;DR: In this paper, residence times of multiple particles in aqueous solutions of carboxy-methylcellulose (CMC) in a holding tube arrangement were measured at different conditions of fluid viscosity, suspension flow rate, particle sizes and particle concentrations.
Journal ArticleDOI

Residence time distribution of food and simulated particles in a model horizontal swept surface heat exchanger

TL;DR: In this paper, the authors investigated the residence time distribution of food and inert particles flowing in a swept surface heat exchanger at room temperature, and the effects of selected experimental conditions on RTD include particle shape (cube, cylinder, and sphere), particle concentration (10, 20, and 30% w/v), particle type (potato, carrot, turkey, green peas, and polystyrene), fluid viscosity (water, 0.5%, 1.0% CMC), bulk flow rate (5.8 x 10 -4, 7.28 x
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