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Journal articles on the topic 'Solid-liquid flow'

Author: Grafiati

Published: 4 June 2021

Last updated: 12 February 2022

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1

TIEN, R. H. "Liquid flow accompanying liquid solid transition." Transactions of the Iron and Steel Institute of Japan 25, no. 2 (1985): 127–32. http://dx.doi.org/10.2355/isijinternational1966.25.127.

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2

SHIKHMURZAEV, YULII D. "Moving contact lines in liquid/liquid/solid systems." Journal of Fluid Mechanics 334 (March 10, 1997): 211–49. http://dx.doi.org/10.1017/s0022112096004569.

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A general mathematical model which describes the motion of an interface between immiscible viscous fluids along a smooth homogeneous solid surface is examined in the case of small capillary and Reynolds numbers. The model stems from a conclusion that the Young equation, σ1 cos θ = σ2 − σ3, which expresses the balance of tangential projection of the forces acting on the three-phase contact line in terms of the surface tensions σi and the contact angle θ, together with the well-established experimental fact that the dynamic contact angle deviates from the static one, imply that the surface tensi

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3

Fan, L. S., R. Lau, C. Zhu, et al. "Evaporative liquid jets in gas–liquid–solid flow system." Chemical Engineering Science 56, no. 21-22 (2001): 5871–91. http://dx.doi.org/10.1016/s0009-2509(01)00283-4.

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4

TAKAHASHI, Hiroshi, Susumu ISHIHARA, Tadashi MASUYAMA, and Karoku NODA. "Flow Behavior and Pressure Fluctuations in Solid-Liquid Flow." JAPANESE JOURNAL OF MULTIPHASE FLOW 3, no. 1 (1989): 31–49. http://dx.doi.org/10.3811/jjmf.3.31.

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5

Doron, P., and D. Barnea. "Flow pattern maps for solid-liquid flow in pipes." International Journal of Multiphase Flow 22, no. 2 (1996): 273–83. http://dx.doi.org/10.1016/0301-9322(95)00071-2.

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6

Zhao, Tong, Masahiro TAKEI, and Tsuyoshi ITAGAWA. "OS10-4 An electric measurement of Liquid-Solid Two-Phase Flow in a mini-channel." Proceedings of the National Symposium on Power and Energy Systems 2007.12 (2007): 73–74. http://dx.doi.org/10.1299/jsmepes.2007.12.73.

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7

OGATA, Satoshi. "Flow Visualization near the Solid-Liquid Interface." Journal of the Visualization Society of Japan 33, no. 129 (2013): 2–7. http://dx.doi.org/10.3154/jvs.33.129_2.

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8

Dunne, Peter, Takuji Adachi, Arvind Arun Dev, et al. "Liquid flow and control without solid walls." Nature 581, no. 7806 (2020): 58–62. http://dx.doi.org/10.1038/s41586-020-2254-4.

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9

Laocharoensuk, Rawiwan, Kumaranand Palaniappan, Nickolaus A. Smith, et al. "Flow-based solution–liquid–solid nanowire synthesis." Nature Nanotechnology 8, no. 9 (2013): 660–66. http://dx.doi.org/10.1038/nnano.2013.149.

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10

Wang, Steven, Guy Metcalfe, Robert L. Stewart, et al. "Solid–liquid separation by particle-flow-instability." Energy Environ. Sci. 7, no. 12 (2014): 3982–88. http://dx.doi.org/10.1039/c4ee02841d.

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A robust separation strategy using novel particle-flow-instability physics is successfully developed for adifficult-to-separate suspensionin which there is some combination of a small density difference between solid and liquid, high viscosity, and small-sized particles.

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11

KAWAI, Hideki, and Hiroshi TAKAHASHI. "Solid-liquid separation by Taylor vortex flow." Proceedings of Conference of Hokkaido Branch 2002.42 (2002): 40–41. http://dx.doi.org/10.1299/jsmehokkaido.2002.42.40.

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12

KITAHARA, Hiroyuki, and Kunio YOSHIDA. "Flow Patterns for Gas-Liquid and Gas-Liquid-Solid Flows in a Vertical Pipe." JAPANESE JOURNAL OF MULTIPHASE FLOW 3, no. 2 (1989): 145–54. http://dx.doi.org/10.3811/jjmf.3.145.

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13

Guo, S., P. Xu, Z. Zheng, and Y. Gao. "Estimation of flow velocity for a debris flow via the two-phase fluid model." Nonlinear Processes in Geophysics 22, no. 1 (2015): 109–16. http://dx.doi.org/10.5194/npg-22-109-2015.

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Abstract. The two-phase fluid model is applied in this study to calculate the steady velocity of a debris flow along a channel bed. By using the momentum equations of the solid and liquid phases in the debris flow together with an empirical formula to describe the interaction between two phases, the steady velocities of the solid and liquid phases are obtained theoretically. The comparison of those velocities obtained by the proposed method with the observed velocities of two real-world debris flows shows that the proposed method can estimate the velocity for a debris flow.

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14

Guo, S., P. Xu, Z. Zheng, and Y. Gao. "Estimation of flow velocity for a debris flow via the two-phase fluid model." Nonlinear Processes in Geophysics Discussions 1, no. 1 (2014): 999–1021. http://dx.doi.org/10.5194/npgd-1-999-2014.

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Abstract. The two-phase fluid model is applied in this study to calculate the steady velocity of a debris flow along a channel bed. By using the momentum equations of the solid and liquid phases in the debris flow together with an empirical formula to describe the interaction between two phases, the steady velocities of the solid and liquid phases are obtained theoretically. The comparison of those velocities obtained by the proposed method with the observed velocities of two real-world debris flows shows that the proposed method can estimate accurately the velocity for a debris flow.

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15

TODA, Masayuki, and Hirotaka KONNO. "Fundamentals of Gas-Liquid-Solid Three Phase Flow." JAPANESE JOURNAL OF MULTIPHASE FLOW 1, no. 2 (1987): 139–56. http://dx.doi.org/10.3811/jjmf.1.139.

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16

Coiado, Evaldo Miranda, and Victor Emanuel M. G. Diniz. "Two-Phase (Solid-Liquid) Flow in Inclined Pipes." Journal of the Brazilian Society of Mechanical Sciences 23, no. 3 (2001): 347–62. http://dx.doi.org/10.1590/s0100-73862001000300007.

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17

Doron, P., M. Simkhis, and D. Barnea. "Flow of solid-liquid mixtures in inclined pipes." International Journal of Multiphase Flow 23, no. 2 (1997): 313–23. http://dx.doi.org/10.1016/s0301-9322(97)80946-9.

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18

Rozenblit, R., M. Simkhis, G. Hetsroni, D. Barnea, and Y. Taitel. "Heat transfer in horizontal solid–liquid pipe flow." International Journal of Multiphase Flow 26, no. 8 (2000): 1235–46. http://dx.doi.org/10.1016/s0301-9322(99)00089-0.

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19

Roy, Shantanu, and M. P. Dudukovic. "Flow Mapping and Modeling of Liquid−Solid Risers." Industrial & Engineering Chemistry Research 40, no. 23 (2001): 5440–54. http://dx.doi.org/10.1021/ie010181t.

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20

Shen, Chen, Artin Afacan, Jing-Li Luo, Jaganathan Ulaganathan, and Stan J. Klimas. "Solid-Liquid Mass Transfer under Flow Boiling Condition." Journal of The Electrochemical Society 163, no. 7 (2016): H618—H624. http://dx.doi.org/10.1149/2.0081608jes.

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21

Roco, M. C., and N. Balakrishnam. "Multi‐Dimensional Flow Analysis of Solid‐Liquid Mixtures." Journal of Rheology 29, no. 4 (1985): 431–56. http://dx.doi.org/10.1122/1.549819.

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22

Cai, Jie, Chuan-Yu Wu, Yu Guo, Jiecheng Yang, and Xiaobao Zhao. "Mechanistic analysis of solid–liquid flow during injection." Particuology 44 (June 2019): 136–45. http://dx.doi.org/10.1016/j.partic.2018.05.008.

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23

Liu, Xiao Xing, Qi Ying Pan, and Hao Su. "Study on Cross-Flow Solid-Liquid Separation Technology." Advanced Materials Research 712-715 (June 2013): 748–54. http://dx.doi.org/10.4028/www.scientific.net/amr.712-715.748.

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The technology, device current situation , theory ,applied prospect of cross-flow solid-liquid separation have been summarized. It has been studied to making several cuneiform slots on the rotator of traditional crossflow filter, allowing the rotator forms convergence space with canister's inside wall. When suspending liquid fill into the cuneiform convergence space, it will cause kinetic press and improve the efficiency of filtrating. .

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24

RASTEIRO, M. G., M. M. FIGUEIREDO, and H. FRANCO. "PRESSURE DROP FOR SOLID/LIQUID FLOW IN PIPES." Particulate Science and Technology 11, no. 3-4 (1993): 147–55. http://dx.doi.org/10.1080/02726359308906630.

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25

Pordesimo, L. O., C. A. Zuritz, and M. G. Sharma. "Flow behavior of coarse solid-liquid food mixtures." Journal of Food Engineering 21, no. 4 (1994): 495–511. http://dx.doi.org/10.1016/0260-8774(94)90069-8.

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26

Sprunt, Eve S., Tony B. Mercer, and Nizar F. Djabbarah. "Streaming potential from multiphase flow." GEOPHYSICS 59, no. 5 (1994): 707–11. http://dx.doi.org/10.1190/1.1443628.

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In trying to understand the affect of electrokinetics on the spontaneous potential (SP) log, the focus has generally been on the solid‐brine streaming potential. Within the accuracy of the measurements, the streaming‐potential coupling coefficient is shown to be independent of the permeability of the rock. The solid‐brine streaming potential is of much smaller magnitude than the electrostatic potentials from gas‐liquid and liquid‐liquid flow. Air bubbles were found to increase the streaming potential coupling coefficient by more than two orders of magnitude over the value for single‐phase brin

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27

Toppaladoddi, S., and J. S. Wettlaufer. "The combined effects of shear and buoyancy on phase boundary stability." Journal of Fluid Mechanics 868 (April 17, 2019): 648–65. http://dx.doi.org/10.1017/jfm.2019.153.

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We study the effects of externally imposed shear and buoyancy driven flows on the stability of a solid–liquid interface. A linear stability analysis of shear and buoyancy-driven flow of a melt over its solid phase shows that buoyancy is the only destabilizing factor and that the regime of shear flow here, by inhibiting vertical motions and hence the upward heat flux, stabilizes the system. It is also shown that all perturbations to the solid–liquid interface decay at a very modest shear flow strength. However, at much larger shear-flow strength, where flow instabilities coupled with buoyancy m

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28

Sassi, Paolo, Youssef Stiriba, Julia Lobera, Virginia Palero, and Jordi Pallarès. "Experimental Analysis of Gas–Liquid–Solid Three-Phase Flows in Horizontal Pipelines." Flow, Turbulence and Combustion 105, no. 4 (2020): 1035–54. http://dx.doi.org/10.1007/s10494-020-00141-1.

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AbstractThe dynamics of three-phase flows involves phenomena of high complexity whose characterization is of great interest for different sectors of the worldwide industry. In order to move forward in the fundamental knowledge of the behavior of three-phase flows, new experimental data has been obtained in a facility specially designed for flow visualization and for measuring key parameters. These are (1) the flow regime, (2) the superficial velocities or rates of the individual phases; and (3) the frictional pressure loss. Flow visualization and pressure measurements are performed for two and

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29

Hua, Hong, Xiao Lin Wang, Hui Yan Wang, and Xiao Bing Liu. "Analysis of Solid-Liquid Two-Phase Flow in Axial Flow Pump." Applied Mechanics and Materials 229-231 (November 2012): 559–64. http://dx.doi.org/10.4028/www.scientific.net/amm.229-231.559.

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The liquid-solid two-phase turbulent flow in an axial flow pump was numerically simulated by using the SIMPLEC algorithm based Navier-Stoker and RNG k-ε turbulent model and after the secondary development of the software Fluent. The distributions of solid concentration, velocity and pressure on the impellers of the axial flow pump were analyzed at different volume concentrations at the pump inlet. The numerical results show that the head and the efficiency of the pump will reduce with the increasing of the sediment concentration in sandy rivers. This research shows that the numerical simulatio

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30

Toyoshi, Takuya, Yoshitaka Wada, and Masanori Kikuchi. "Solid-Liquid Flows Simulation for Debris Avalanche Analysis." Key Engineering Materials 462-463 (January 2011): 855–60. http://dx.doi.org/10.4028/www.scientific.net/kem.462-463.855.

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From a view point of engineering application, solid-liquid flow is one of the most practical phenomena, however MPS and other particle methods usually premises a constant size of all particles in the model. In a realistic phenomenon, the size of those particles is different. Koshizuka et al. has proposed new algorithm for solid-liquid flow simulation which is multi-scale DEM-MPS method. The method can calculate solid -liquid flow with a large difference of the particle scale. However, its program code requires a DEM part and a MPS part, and actual phenomenon includes various scales of particle

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31

Hua, Hong, Xiao Bing Liu, Shun Bing Ou, and Yong Zhong Zeng. "Numerical Simulation of 3D Solid-Liquid Two-Phase Turbulence Flow in Axial-Flow Pump Impeller." Applied Mechanics and Materials 212-213 (October 2012): 1237–43. http://dx.doi.org/10.4028/www.scientific.net/amm.212-213.1237.

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With the use of the RNG k-ε turbulence model and the SIMPLEC algorithm, as well as after the secondary development of the software Fluent, the velocity field and pressure field of a axial flow impeller were numerically simulated in the single-phase (clear water) and the solid-liquid two-phase conditions. The distributions of pressure, velocity and solid concentration in the impeller under the single-phase flow and the solid-liquid two-phase flow conditions were compared. This study has shown that the numerical simulation results are the same as the actual situation.

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32

Li, Junye, Ningning Su, Lili Wei, Xinming Zhang, Yanlu Yin, and Weihong Zhao. "Study on the surface forming mechanism of the solid–liquid two-phase grinding fluid polishing pipe based on large eddy simulation." Proceedings of the Institution of Mechanical Engineers, Part B: Journal of Engineering Manufacture 233, no. 14 (2019): 2505–14. http://dx.doi.org/10.1177/0954405419841814.

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To study the surface forming mechanism of the solid–liquid two-phase abrasive flow processing, the large eddy simulation method was used. Taking a 90° stainless steel elbow as the research object, the action mechanism of the dynamic pressure, wall shear force, flow state of the abrasive flow at different cross-sections, formation of the vortex, and trajectory of the abrasive flow on the inner surface of the elbow with abrasive flow composed of solid-phase silicon carbide and liquid-phase hydraulic oil are discussed. This study explores the distribution characteristics of the flow pattern of so

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33

Jianping, Wen, Huang Lin, Zhu Yong, Li Chao, and Chen Yunlin. "Solid–liquid mass transfer in a gas–liquid–solid three-phase reversed flow jet loop reactor." Chemical Engineering Journal 78, no. 2-3 (2000): 231–35. http://dx.doi.org/10.1016/s1385-8947(00)00147-9.

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34

TAKAHASHI, Hiroshi, Seiji KIRYU, and Tadashi MASUYAMA. "Fluctuations of in-situ Solid Concentration and Pressure in Solid-Liquid Flow." JAPANESE JOURNAL OF MULTIPHASE FLOW 4, no. 3 (1990): 192–209. http://dx.doi.org/10.3811/jjmf.4.192.

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35

Yamasaki, H., X. D. Niu, and H. Yamaguchi. "Measurement of solid-phase concentration in solid-liquid flow using magnetic fluid." Magnetohydrodynamics 49, no. 3-4 (2013): 407–10. http://dx.doi.org/10.22364/mhd.49.3-4.29.

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36

Ovchinnikov, A. A., A. A. Shadrin, D. V. Alekseev, and N. A. Nikolaev. "Separation of liquid-liquid and liquid-solid heterogeneous systems in single-flow vortex separators." Theoretical Foundations of Chemical Engineering 40, no. 4 (2006): 411–15. http://dx.doi.org/10.1134/s0040579506040117.

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37

Lee, Y. J., and J. H. Kim. "A Review of Holography Applications in Multiphase Flow Visualization Study." Journal of Fluids Engineering 108, no. 3 (1986): 279–88. http://dx.doi.org/10.1115/1.3242575.

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Holographic techniques are used in many fields of science and engineering including flow observation. The purpose of this paper is to review applications of holography to multiphase flow study with emphasis on gas-solid and gas-liquid two-phase flows. The application of holography to multiphase flow has been actively explored in the areas of particle sizing in particulate flows and nuclei population measurements in cavitation study. It is also recognized that holography holds great potential as a means of visualizing dynamic situations inherent in multiphase flows. This potential has been demo

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38

Chang, K. H., and L. C. Witte. "Liquid-Solid Contact During Flow Film Boiling of Subcooled Freon-11." Journal of Heat Transfer 112, no. 2 (1990): 465–71. http://dx.doi.org/10.1115/1.2910401.

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Liquid-solid contacts were measured for flow film boiling of subcooled Freon-11 over an electrically heated cylinder equipped with a surface microthermocouple probe. No systematic variation of the extent of liquid-solid contact with wall superheat, liquid subcooling, or velocity was detected. Only random small-scale contacts that contribute negligibly to overall heat transfer were detected when the surface was above the homogeneous nucleation temperature of the Freon-11. When large-scale contacts were detected, they led to an unexpected intermediate transition from local film boiling to local

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39

Shalimov, S. L. "On effect of precession-induced flows in the liquid core for early Earth's history." Nonlinear Processes in Geophysics 13, no. 5 (2006): 525–29. http://dx.doi.org/10.5194/npg-13-525-2006.

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Abstract. Secondary and tertiary flow patterns seen in experiments simulating flow in the Earth's liquid core induced by luni-solar precession of the solid mantle (Vanyo et al., 1995) hint at the development of non-axisymmetric columnar periodic structures. A simple interpretation of the structure formation is presented in a hydrodynamic approach. It is suggested that if similar flow patterns can occur in the Earth's liquid core enclosed into precessing and rotating mantle then kinematic of the flows may be regarded as a possible geodynamo mechanism for early Earth's history (before the solid

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40

Bianchi, Pauline, Jason D. Williams, and C. Oliver Kappe. "Oscillatory flow reactors for synthetic chemistry applications." Journal of Flow Chemistry 10, no. 3 (2020): 475–90. http://dx.doi.org/10.1007/s41981-020-00105-6.

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Abstract Oscillatory flow reactors (OFRs) superimpose an oscillatory flow to the net movement through a flow reactor. OFRs have been engineered to enable improved mixing, excellent heat- and mass transfer and good plug flow character under a broad range of operating conditions. Such features render these reactors appealing, since they are suitable for reactions that require long residence times, improved mass transfer (such as in biphasic liquid-liquid systems) or to homogeneously suspend solid particles. Various OFR configurations, offering specific features, have been developed over the past

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41

Liedtke, Anne-Kathrin, Frederik Scheiff, Frédéric Bornette, Régis Philippe, David W. Agar, and Claude de Bellefon. "Liquid–Solid Mass Transfer for Microchannel Suspension Catalysis in Gas–Liquid and Liquid–Liquid Segmented Flow." Industrial & Engineering Chemistry Research 54, no. 17 (2015): 4699–708. http://dx.doi.org/10.1021/ie504523y.

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42

Wang, Feng Lan, Yuan Jun Yao, Fa Yun Gong, Fang Ping Ye, and Wen Jie Qi. "Liquid-Solid Coupling Characteristics in the Fluidized Bed Evaporator for Tobacco Refined Liquid." Applied Mechanics and Materials 686 (October 2014): 522–28. http://dx.doi.org/10.4028/www.scientific.net/amm.686.522.

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Consider a two-phase liquid-solid coupling effect, using Euler - Euler two-fluid model is solved using standard viscous term with k-ε model and the velocity pressure coupling a simple algorithm to simulate liquid-solid two-phase flow characteristics of the fluid flow method bed, the applicability of the model to assess the drag. Different effects of a two-stage flow characteristics of fluidized bed flow characteristics, fluid and operating conditions affect the physical properties of the paper. We found from the simulation is the use of different drag coefficient models will greatly affect the

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43

UEMATSU, Junichi, Kazuya ABE, Xiaoran YU, Tatsuya HAZUKU, Masaki OSHIMA, and Tomoji TAKAMASA. "Flow Structures in Vertical Solid-liquid Two-phase Flow under Microgravity Environment." Journal of the Visualization Society of Japan 27, Supplement1 (2007): 109–10. http://dx.doi.org/10.3154/jvs.27.supplement1_109.

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44

Duo-min, Lin, and Tsai Shu-tang. "The mixing of gas-liquid flow with vapor and gas-solid flow." Applied Mathematics and Mechanics 11, no. 6 (1990): 513–18. http://dx.doi.org/10.1007/bf02016336.

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45

Kim, Young-Ju, Young-Hun Kim, and Nam-Sub Woo. "Study on Solid-liquid Mixture Flow in Inclined Annulus." Journal of Ocean Engineering and Technology 25, no. 5 (2011): 15–20. http://dx.doi.org/10.5574/ksoe.2011.25.5.015.

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46

Nouchi, Taihei, Kanji Takeda, and A. B. Yu. "Solid Flow Caused by Buoyancy Force of Heavy Liquid." ISIJ International 43, no. 2 (2003): 187–91. http://dx.doi.org/10.2355/isijinternational.43.187.

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47

Sherwood, J. D. "Liquid–solid relative motion during squeeze flow of pastes." Journal of Non-Newtonian Fluid Mechanics 104, no. 1 (2002): 1–32. http://dx.doi.org/10.1016/s0377-0257(02)00011-3.

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48

Joubert, Rita, and Willie Nicol. "Multiplicity Behavior of Trickle Flow Liquid−Solid Mass Transfer." Industrial & Engineering Chemistry Research 48, no. 18 (2009): 8387–92. http://dx.doi.org/10.1021/ie9002552.

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49

Cartland Glover, G. M., and S. C. Generalis. "Gas–liquid–solid flow modelling in a bubble column." Chemical Engineering and Processing: Process Intensification 43, no. 2 (2004): 117–26. http://dx.doi.org/10.1016/s0255-2701(03)00009-6.

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50

Voinov, O. V. "Flow structure in a liquid wetting a solid surface." Doklady Physics 53, no. 1 (2008): 43–47. http://dx.doi.org/10.1134/s1028335808010114.

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