Visualization and Measurement of Swirling Flow of Dry Ice Particles in Cyclone Separator-Sublimator

The dry ice sublimation process of carbon dioxide (CO<sub>2</sub>) is a unique, environmentally friendly technology that can achieve a temperature of −56 °C or lower, which is a triple point of CO<sub>2</sub> in CO<sub>2</sub> refrigeration systems. In this study,...

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Main Authors: Haruhiko Yamasaki, Hiroyuki Wakimoto, Takeshi Kamimura, Kazuhiro Hattori, Petter Nekså, Hiroshi Yamaguchi
Format: Article
Language:English
Published: MDPI AG 2022-06-01
Series:Energies
Subjects:
Online Access:https://www.mdpi.com/1996-1073/15/11/4128
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author Haruhiko Yamasaki
Hiroyuki Wakimoto
Takeshi Kamimura
Kazuhiro Hattori
Petter Nekså
Hiroshi Yamaguchi
author_facet Haruhiko Yamasaki
Hiroyuki Wakimoto
Takeshi Kamimura
Kazuhiro Hattori
Petter Nekså
Hiroshi Yamaguchi
author_sort Haruhiko Yamasaki
collection DOAJ
description The dry ice sublimation process of carbon dioxide (CO<sub>2</sub>) is a unique, environmentally friendly technology that can achieve a temperature of −56 °C or lower, which is a triple point of CO<sub>2</sub> in CO<sub>2</sub> refrigeration systems. In this study, a cyclone separator-evaporator was proposed to separate dry ice particles in an evaporator. As an initial step before introducing the cyclone separator-evaporator into an actual refrigeration system, a prototype cyclone separator-evaporator was constructed to visualize dry ice particles in a separation chamber. A high-speed camera was used to visualize the non-uniform flow of dry ice particles that repeatedly coalescence and collision in a swirl section. Consequently, the dry ice particle size and the circumferential and axial velocities of dry ice were measured. The results show that the equivalent diameter of the most abundant dry ice particles in the cyclone separation chamber is 2.0 mm. As the inner diameter of the separation section decreases, dry ice particles coalesce and grow from an equivalent diameter of 4 mm to a maximum of 40 mm. In addition, the comparison of the experimental and simulation results shows that the drag force due to CO<sub>2</sub> gas flow is dominant in the circumferential velocity of dry ice particles.
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spelling doaj.art-5b8c2cafa6d44065b1f0dcf1f009fd062023-11-23T14:00:49ZengMDPI AGEnergies1996-10732022-06-011511412810.3390/en15114128Visualization and Measurement of Swirling Flow of Dry Ice Particles in Cyclone Separator-SublimatorHaruhiko Yamasaki0Hiroyuki Wakimoto1Takeshi Kamimura2Kazuhiro Hattori3Petter Nekså4Hiroshi Yamaguchi5Department of Mechanical Engineering, Osaka Prefecture University, 1-1 Gakuen-Cho, Naka-ku, Sakai 599-8531, JapanDepartment of Mechanical Engineering, Osaka Prefecture University, 1-1 Gakuen-Cho, Naka-ku, Sakai 599-8531, JapanMayekawa MFG. Co., Ltd., 3-14-15 Botan, Koto-ku, Tokyo 135-8482, JapanMayekawa MFG. Co., Ltd., 3-14-15 Botan, Koto-ku, Tokyo 135-8482, JapanSINTEF Energy Research, Sem Sælands vei 11, 7034 Trondheim, NorwayDepartment of Mechanical Engineering, Doshisha University, Kyotanabe city, Kyoto 610-0321, JapanThe dry ice sublimation process of carbon dioxide (CO<sub>2</sub>) is a unique, environmentally friendly technology that can achieve a temperature of −56 °C or lower, which is a triple point of CO<sub>2</sub> in CO<sub>2</sub> refrigeration systems. In this study, a cyclone separator-evaporator was proposed to separate dry ice particles in an evaporator. As an initial step before introducing the cyclone separator-evaporator into an actual refrigeration system, a prototype cyclone separator-evaporator was constructed to visualize dry ice particles in a separation chamber. A high-speed camera was used to visualize the non-uniform flow of dry ice particles that repeatedly coalescence and collision in a swirl section. Consequently, the dry ice particle size and the circumferential and axial velocities of dry ice were measured. The results show that the equivalent diameter of the most abundant dry ice particles in the cyclone separation chamber is 2.0 mm. As the inner diameter of the separation section decreases, dry ice particles coalesce and grow from an equivalent diameter of 4 mm to a maximum of 40 mm. In addition, the comparison of the experimental and simulation results shows that the drag force due to CO<sub>2</sub> gas flow is dominant in the circumferential velocity of dry ice particles.https://www.mdpi.com/1996-1073/15/11/4128dry icecarbon dioxidecyclone separator-sublimatorswirling flowvisualization
spellingShingle Haruhiko Yamasaki
Hiroyuki Wakimoto
Takeshi Kamimura
Kazuhiro Hattori
Petter Nekså
Hiroshi Yamaguchi
Visualization and Measurement of Swirling Flow of Dry Ice Particles in Cyclone Separator-Sublimator
Energies
dry ice
carbon dioxide
cyclone separator-sublimator
swirling flow
visualization
title Visualization and Measurement of Swirling Flow of Dry Ice Particles in Cyclone Separator-Sublimator
title_full Visualization and Measurement of Swirling Flow of Dry Ice Particles in Cyclone Separator-Sublimator
title_fullStr Visualization and Measurement of Swirling Flow of Dry Ice Particles in Cyclone Separator-Sublimator
title_full_unstemmed Visualization and Measurement of Swirling Flow of Dry Ice Particles in Cyclone Separator-Sublimator
title_short Visualization and Measurement of Swirling Flow of Dry Ice Particles in Cyclone Separator-Sublimator
title_sort visualization and measurement of swirling flow of dry ice particles in cyclone separator sublimator
topic dry ice
carbon dioxide
cyclone separator-sublimator
swirling flow
visualization
url https://www.mdpi.com/1996-1073/15/11/4128
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