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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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Optimising the quality of safe food: Computational modelling of a continuous sterilisation process

TL;DR: Results have shown that the conservative approach used in the food industry can lead to significant overprocessing and thus unnecessary deterioration of the overall product quality.
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Residence time distribution in twisted pipe flows: helically coiled system and chaotic system

TL;DR: In this paper, residence time distributions in a helically coiled tube and a spatially chaotic system are compared by modeling the residence time distribution, experimentally determined by means of a two-measurement-point technique, using the axial dispersion plug-flow model.
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Minimisation of axial dispersion by use of secondary flow in helical tubes

TL;DR: In this article, the authors considered the problem of attaining plug flow in continuous flow systems and showed that helical coils are far superior to straight tubes or packed beds in minimizing axial dispersion and approaching plug flow.
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TL;DR: In this article, a tube friction chart for single-phase fluid flow through curved tubes is introduced, which covers both laminar flow (0 Recrit) and single phase fluid flow.
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Chaotic heat transfer for heat exchanger design and comparison with a regular regime for a large range of Reynolds numbers

TL;DR: In this article, an experimental comparison is made over a large range of Reynolds numbers (from 30 to 30,000) between two shell-and-tube heat exchangers having the same heat-transfer area and same number of bends, but different configurations: one has a helical configuration (regular flow), the other has a chaotic one (chaotic advection flow).
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