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Articles de revues sur le sujet « Gas/particle »

Auteur : Grafiati

Publié le 9 mars 2023

Mis à jour le 31 juillet 2025

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1

Chubb, Donald L. "Gas Particle Radiator." Journal of Thermophysics and Heat Transfer 1, no. 3 (1987): 285–88. http://dx.doi.org/10.2514/3.56213.

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2

Zhou, Lixing, and Zhuoxiong Zeng. "Studies on gas turbulence and particle fluctuation in dense gas-particle flows." Acta Mechanica Sinica 24, no. 3 (2008): 251–60. http://dx.doi.org/10.1007/s10409-008-0156-z.

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3

ASBACH, C., T. KUHLBUSCH, and H. FISSAN. "Investigation on the gas particle separation efficiency of the gas particle partitioner." Atmospheric Environment 39, no. 40 (2005): 7825–35. http://dx.doi.org/10.1016/j.atmosenv.2005.08.032.

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4

Yang, Xiaojian, Chang Liu, Xing Ji, Wei Shyy null, and Kun Xu. "Unified Gas-Kinetic Wave-Particle Methods VI: Disperse Dilute Gas-Particle Multiphase Flow." Communications in Computational Physics 31, no. 3 (2022): 669–706. http://dx.doi.org/10.4208/cicp.oa-2021-0153.

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5

Sinclair, J. L., and R. Jackson. "Gas-particle flow in a vertical pipe with particle-particle interactions." AIChE Journal 35, no. 9 (1989): 1473–86. http://dx.doi.org/10.1002/aic.690350908.

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6

Zeng, Zhuo Xiong, Zhang Jun Wang, and Yun Ni Yu. "Effect of Particle Finite Size on Gas Turbulent Flow." Advanced Materials Research 516-517 (May 2012): 752–57. http://dx.doi.org/10.4028/www.scientific.net/amr.516-517.752.

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Dynamic mesh and moving wall technique were employed to simulate the unsteady flow field of moving particle with finite size. For freely moving particle, it does not come into being particle wake. Middle particle can move straightforward outlet, but left and right particles move disorderly in a restricted region. Vortex location varies with the change of particle location. Turbulence energy and pressure is decreased gradually from inlet to outlet. But for moving particle with slip velocity between gas and particle, particle wake comes into being. Turbulence enhancement by particle wake effect

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7

Zhuo, C. F., W. J. Yao, X. S. Wu, F. Feng, and P. Xu. "Research on the Muzzle Blast Flow with Gas-Particle Mixtures Based on Eulerian-Eulerian Approach." Journal of Mechanics 32, no. 2 (2015): 185–95. http://dx.doi.org/10.1017/jmech.2015.44.

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ABSTRACTThe issue on the muzzle blast flow with gas-particle mixtures was numerically investigated in this paper. The propellant gas in the cannon was assumed to be gas-particle mixtures consisting of a variety of gaseous species and particles. The model made use of the Eulerian-Eulerican approach, where the particle were modeled as a second fluid with parameters like bulk density, velocity and temperature, interacting with the gas flow. A high-resolution upwind scheme(AUSMPW+) and detailed reaction kinetics model were employed to solve the chemical non-equilibrium Euler equations for gas phas

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8

Li, Jie, and J. A. M. Kuipers. "Gas-particle interactions in dense gas-fluidized beds." Chemical Engineering Science 58, no. 3-6 (2003): 711–18. http://dx.doi.org/10.1016/s0009-2509(02)00599-7.

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9

Knoop, Claas, and Udo Fritsching. "Gas/particle Interaction in Ultrasound Agitated Gas Flow." Procedia Engineering 42 (2012): 770–81. http://dx.doi.org/10.1016/j.proeng.2012.07.469.

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10

Li, Jie, and J. A. M. Kuipers. "Effect of competition between particle–particle and gas–particle interactions on flow patterns in dense gas-fluidized beds." Chemical Engineering Science 62, no. 13 (2007): 3429–42. http://dx.doi.org/10.1016/j.ces.2007.01.086.

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11

Veyssiere, Bernard. "Detonations in Gas-Particle Mixtures." Journal of Propulsion and Power 22, no. 6 (2006): 1269–88. http://dx.doi.org/10.2514/1.18378.

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12

Buehler, M. G., L. D. Bell, and M. H. Hecht. "Alpha‐particle gas‐pressure sensor." Journal of Vacuum Science & Technology A: Vacuum, Surfaces, and Films 14, no. 3 (1996): 1281–87. http://dx.doi.org/10.1116/1.579942.

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13

Ullah, S. M. Rahmat, Masaki Takeuchi, and Purnendu K. Dasgupta. "Versatile Gas/Particle Ion Chromatograph." Environmental Science & Technology 40, no. 3 (2006): 962–68. http://dx.doi.org/10.1021/es051722z.

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14

Sabdenov, K. O. "Bubbling of gas-particle mixtures." Fluid Dynamics 33, no. 4 (1998): 559–66. http://dx.doi.org/10.1007/bf02698221.

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15

Hanley, H. J. M. "Particle dispersion in a gas." International Journal of Thermophysics 18, no. 4 (1997): 947–55. http://dx.doi.org/10.1007/bf02575240.

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16

Connolly, Christine. "Gas sensing and particle detection." Sensor Review 28, no. 4 (2008): 294–98. http://dx.doi.org/10.1108/02602280810902587.

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17

Feng, Y. Q., B. H. Xu, S. J. Zhang, A. B. Yu, and P. Zulli. "Discrete particle simulation of gas fluidization of particle mixtures." AIChE Journal 50, no. 8 (2004): 1713–28. http://dx.doi.org/10.1002/aic.10169.

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18

Yang, Xiaojian, Wei Shyy, and Kun Xu. "Unified gas-kinetic wave–particle method for gas–particle two-phase flow from dilute to dense solid particle limit." Physics of Fluids 34, no. 2 (2022): 023312. http://dx.doi.org/10.1063/5.0081105.

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19

Shen, Zhi Yuan, Li Jun Yang, Meng Xi Liu, Chun Xi Lu, and Xiao Na Liu. "Particle Velocity Distribution in a Novel Draft Tube-Lifted Gassolid Air Loop Reactor." Advanced Materials Research 396-398 (November 2011): 639–47. http://dx.doi.org/10.4028/www.scientific.net/amr.396-398.639.

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The hydrodynamics in a gas-solid draft tube-lifted air-loop reactor (GSALR) was investigated systematically using experimental measurements. To demonstrate the gas-solid flow pattern, the upward particle velocity, downward particle velocity and time-averaged particle velocity in four regions of the GSALR were measured by optical fiber probe under different superficial gas velocities. The experimental results show that the downward particle velocity distributes uniformly along the radius in the four regions, but the radial distributions of upward particle velocity and time-averaged particle vel

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20

Gusev, V. N., and Yu V. Nikol'skii. "Modeling gas dynamic particle interaction in rarefied gas flows." Fluid Dynamics 22, no. 1 (1987): 129–35. http://dx.doi.org/10.1007/bf01050863.

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21

Li, Qian, Xiaonan Wu, Siying Yu, Lianqing Li, and Xinxin Wang. "Deposition of naphthalene particle in horizontal straight pipe of manufactured gas pipeline." Advances in Mechanical Engineering 10, no. 8 (2018): 168781401879356. http://dx.doi.org/10.1177/1687814018793568.

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After long time operation of the manufactured gas pipeline, the naphthalene in the gas will jam the pipeline and threaten the safety of the pipeline seriously. To study the naphthalene particle deposition law in the manufactured gas pipeline, a horizontal straight pipe of Kunming manufactured gas pipeline is taken as an example; based on Reynolds stress model and discrete phase model, ANSYS Fluent software is used to carry out the numerical simulation in different pipe diameters, particle size, inlet velocity, temperature, and pressure conditions. The main conclusion can be obtained as follows

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22

RAHMAN, KHURRAM, and CHARLES S. CAMPBELL. "Particle pressures generated around bubbles in gas-fluidized beds." Journal of Fluid Mechanics 455 (March 25, 2002): 103–27. http://dx.doi.org/10.1017/s002211200100725x.

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The particle pressure is the surface force in a particle/fluid mixture that is exerted solely by the particle phase. This paper presents measurements of the particle pressure on the faces of a two-dimensional gas-fluidized bed and gives insight into the mechanisms by which bubbles generate particle pressure. The particle pressure is measured by a specially designed ‘particle pressure transducer’. The results show that, around single bubbles, the most significant particle pressures are generated below and to the sides of the bubble and that these particle pressures steadily increase and reach a

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23

Xu, Lijun, Chang Liu, Zhang Cao, and Xiaomin Li. "Particle size influence on effective permittivity of particle–gas mixture with particle clusters." Particuology 11, no. 2 (2013): 216–24. http://dx.doi.org/10.1016/j.partic.2012.07.003.

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24

Ocone, R., S. Sundaresan, and R. Jackson. "Gas-Particle flow in a duct of arbitrary inclination with particle-particle interactions." AIChE Journal 39, no. 8 (1993): 1261–71. http://dx.doi.org/10.1002/aic.690390802.

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25

Cheng, Cheng, Xiao-Yu Cheng, Han Gao, Wen-Ping Yue, and Chao Liu. "Prediction of Gas Emissions in the Working Face Based on the Desorption Effects of Granular Coal: A Case Study." Sustainability 14, no. 18 (2022): 11353. http://dx.doi.org/10.3390/su141811353.

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The aim of the study in this paper is to establish a prediction model of gas emission in the working face. The gas desorption variation characteristics of coal with different particle sizes were assessed using physical tests and based on the coal body of No. 2 coal seam in Wangjialing Coal Mine, Shanxi, China, to reveal the influence law of coal particle size on coal gas desorption. The gas desorption characteristics in the working face, the law of gas emission of coal cutting, coal caving, coal wall, and remnant coal in the goaf of the production process were then analyzed after establishing

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26

Lee, Chuan Ping, Mihnea Surdu, David M. Bell, et al. "High-frequency gaseous and particulate chemical characterization using extractive electrospray ionization mass spectrometry (Dual-Phase-EESI-TOF)." Atmospheric Measurement Techniques 15, no. 12 (2022): 3747–60. http://dx.doi.org/10.5194/amt-15-3747-2022.

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Abstract. To elucidate the sources and chemical reaction pathways of organic vapors and particulate matter in the ambient atmosphere, real-time detection of both the gas and particle phase is needed. State-of-the-art techniques often suffer from thermal decomposition, ionization-induced fragmentation, high cut-off size of aerosols or low time resolution. In response to all these limitations, we developed a new technique that uses extractive electrospray ionization (EESI) for online gas and particle chemical speciation, namely the dual-phase extractive electrospray ionization time-of-flight mas

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27

Sikovskii, D. F. "Relations for particle deposition in turbulent gas-particle channel flows." Fluid Dynamics 45, no. 1 (2010): 74–84. http://dx.doi.org/10.1134/s0015462810010096.

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28

Pratsinis, Sotiris E. "Particle production by gas-to-particle conversion in turbulent flows." Journal of Aerosol Science 20, no. 8 (1989): 1461–64. http://dx.doi.org/10.1016/0021-8502(89)90862-8.

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29

Schmitt, R. G., and P. B. Butler. "Influence of particle melting on a shocked particle-laden gas." Powder Technology 70, no. 2 (1992): 163–73. http://dx.doi.org/10.1016/0032-5910(92)85043-u.

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30

Sommerfeld, M. "Modelling of particle-wall collisions in confined gas-particle flows." International Journal of Multiphase Flow 18, no. 6 (1992): 905–26. http://dx.doi.org/10.1016/0301-9322(92)90067-q.

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31

Oesterle, B., and A. Petitjean. "Simulation of particle-to-particle interactions in gas solid flows." International Journal of Multiphase Flow 19, no. 1 (1993): 199–211. http://dx.doi.org/10.1016/0301-9322(93)90033-q.

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32

Bartley, Paul C., Aziz Amoozegar, William C. Fonteno, and Brian E. Jackson. "Particle Densities of Horticultural Substrates." HortScience 57, no. 3 (2022): 379–83. http://dx.doi.org/10.21273/hortsci16319-21.

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The heterogeneity of horticultural substrates makes basic physical characteristics, such as total porosity and particle density, difficult to estimate. Due to the material source, inclusion of occluded pores, and hydrophobicity, particle density values reported from using liquid pyknometry, vary widely. Gas pycnometry was used to determine the particle density of coir, peat, perlite, pine bark, and wood substrates. Further precision was examined by gas species and separation by particle size. The calculated particle densities for each material determined by He, N2, and air were relatively cons

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33

YAMAMOTO, Y., M. POTTHOFF, T. TANAKA, T. KAJISHIMA, and Y. TSUJI. "Large-eddy simulation of turbulent gas–particle flow in a vertical channel: effect of considering inter-particle collisions." Journal of Fluid Mechanics 442 (August 24, 2001): 303–34. http://dx.doi.org/10.1017/s0022112001005092.

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The interaction between a turbulent gas flow and particle motion was investigated by numerical simulations of gas–particle turbulent downward flow in a vertical channel. In particular the effect of inter-particle collision on the two-phase flow field was investigated. The gas flow field was obtained by large-eddy simulation (LES). Particles were treated by a Lagrangian method, with inter-particle collisions calculated by a deterministic method. The spatial resolution for LES of gas–solid two-phase turbulent flow was examined and relations between grid resolution and Stokes number are presented

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34

Shaffer, F. D., and R. A. Bajura. "Analysis of Venturi Performance for Gas-Particle Flows." Journal of Fluids Engineering 112, no. 1 (1990): 121–27. http://dx.doi.org/10.1115/1.2909359.

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In recent years, use of the venturi for measurement of gas-particle flows has received considerable attention. The technology for the venturi as a single-phase flowmeter has matured to the point that application is routine. Much more research, however, is required to establish the venturi as an acceptable gas-particle flowmeter. The first part of this paper consists of a discussion of the basic principles of venturi pressure-flow performance for gas-particle flows. This is followed by a description of the experimental calibration of a venturi for measurement of gas-particle flows with particle

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35

Ishii, R., Y. Umeda, and M. Yuhi. "Numerical analysis of gas-particle two-phase flows." Journal of Fluid Mechanics 203 (June 1989): 475–515. http://dx.doi.org/10.1017/s0022112089001552.

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This paper is concerned with a numerical analysis of axisymmetric gas-particle two-phase flows. Underexpanded supersonic free-jet flows and supersonic flows around a truncated cylinder of gas-particle mixtures are solved numerically on the super computer Fujitsu VP-400. The gas phase is treated as a continuum medium, and the particle phase is treated partly as a discrete one. The particle cloud is divided into a large number of small clouds. In each cloud, the particles are approximated to have the same velocity and temperature. The particle flow field is obtained by following these individual

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36

Thien Chi, Nguyen Doan. "GAS–PARTICLE PARTITIONING OF POLYCYCLIC AROMATIC HYDROCARBONS - PAHs IN AMBIENT AIR IN HOCHIMINH CITY." Vietnam Journal of Science and Technology 55, no. 4C (2018): 97. http://dx.doi.org/10.15625/2525-2518/55/4c/12136.

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This research conducted an analysis of 14 Polycyclic Aromatic Hydrocarbons (PAHs) in gas and particle-phase in ambient air in Hochiminh City to investigate their occurence and the gas/particle distribution. Gas and particle samples were collected from June to August 2015 in Hochiminh City and PAHs were treated and analyzed using high performance liquid chromatography with fluorescence detection (HPLC/FLD). Results showed that average concentration of 14 PAHs were from 6.4 to 29.8 ng/m3 and from 50.7 to 133 ng/m3 in particle-phase and in gas-phase, respectively. The concentration of PAHs in the

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37

Mohanarangam, K., and J. Y. Tu. "Numerical Study of Particle Interaction in Gas-Particle and Liquid-Particle Flows: Part II Particle Response." Journal of Computational Multiphase Flows 1, no. 3 (2009): 245–62. http://dx.doi.org/10.1260/1757-482x.1.3.245.

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In this paper the numerical model, which was presented in the first paper (Mohanarangam & Tu; 2009) of this series of study, is employed to study the different particle responses under the influence of two carrier phases namely the gas and the liquid. The numerical model takes into consideration the turbulent behaviour of both the carrier and the dispersed phases, with additional equations to take into account the combined fluid particle behaviour, thereby effecting a two-way coupling. The first paper in this series showed the distinct difference in particulate response both at the mean as

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38

Cheng, De Zhu, Ai Ling Du, Shan Chao Jiang, and Ai Qin Du. "Gas Desorption of Different Particle Size Coal under the Effect of Electromagnetic Radiation." Advanced Materials Research 953-954 (June 2014): 1205–9. http://dx.doi.org/10.4028/www.scientific.net/amr.953-954.1205.

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Many factors can influence coal gas desorption. In this paper, the impact of coal particle size on coal gas desorption under the effect of microwave radiation was mainly studied. Infrared (IR) spectroscopy and optical fiber sensor were used to on-line detect and the qualitative and quantitative analysis of the desorbed gas. The analysis results of the infrared spectrogram showed that under the effect of electromagnetic radiation (2450Hz, 1.5μT), different particle sizes of coal sample could desorb gas which contained carbon dioxide, carbon monoxide and methane. The comparison of gas content de

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39

Campbell, Charles S., and David G. Wang. "Particle pressures in gas-fluidized beds." Journal of Fluid Mechanics 227 (June 1991): 495–508. http://dx.doi.org/10.1017/s0022112091000216.

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The particle pressure is the surface force that is exerted due to the motion of particles and their interactions. This paper describes measurements of the particle pressure exerted on the sidewall of a gas-fluidized bed. As long as the bed remains in a packed state, the particle pressure decreases with increasing gas velocity as progressively more of the bed is supported by fluid forces. It appropriately reaches a minimum fluidization and then begins to rise again when the bed is fluidized, reflecting the agitation of the bed by bubbles. In this fully fluidized region, the particle pressure sc

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40

Liu, Chuan Shao, Jiang Wei Cheng, and Jian Xin Zheng. "Numerical Simulation of Gas-Particle Two Phase Flow in the Process of Cold Spraying Aluminum Zinc-Base Alloy Powder." Applied Mechanics and Materials 37-38 (November 2010): 735–38. http://dx.doi.org/10.4028/www.scientific.net/amm.37-38.735.

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The gas velocity and particle velocity in and out of the nozzle have great influence on the coating effect in the process of cold spray. An axis-symmetric two-dimensional mathematical model was presented to study the flow field in and out of cold spray nozzle, and the effect of different pressure, temperature, spraying distance and particle diameter on gas axial velocity and particle velocity were researched. The simulation results showed that the gas axial velocity and particle velocity increased when the gas pressure and temperature were increased, spray distance had little effect on the flo

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41

Wang, Guoming, Jiahua Shen, Demao Liu, Sung-Wook Kim, and Gyung-Suk Kil. "Green gas for grid as an eco-friendly alternative insulation gas to SF6: From the perspective of PD initiated by metallic particles under DC." Journal of Electrical Engineering 71, no. 1 (2020): 43–48. http://dx.doi.org/10.2478/jee-2020-0006.

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AbstractThis paper dealt with characteristics of partial discharge (PD) initiated by metallic particles under DC voltage in green gas for grid (g3), which is an emerging and promising eco-friendly alternative insulation gas to SF6. Experimental setup was configured to simulate PD under DC in gas-insulated power facilities. Two types of particle, namely rectangle particle and sphere particle were used. The results indicated that the discharge inception voltages in g3 gas were 90.1-92.5% of that in SF6. In two particles, PD occurred with higher average apparent charge and discharge repetition ra

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42

Zhang, Ma, Kim, and Lin. "Numerical Analysis of Supersonic Impinging Jet Flows of Particle-Gas Two Phases." Processes 8, no. 2 (2020): 191. http://dx.doi.org/10.3390/pr8020191.

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Supersonic impinging jet flows always occur when aircrafts start short takeoff and vertical landing from the ground. Supersonic flows with residues produced by chemical reaction of fuel mixture have the potential of reducing aircraft performance and landing ground. The adverse flow conditions such as impinging force, high noise spectrum, and high shear stress always take place. Due to rare data on particle-gas impinging jet flows to date, three-dimensional numerical simulations were carried out to investigate supersonic impinging jet flows of particle-gas two phases in the present studies. A c

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43

Ishii, R., Y. Umeda, and K. Kawasaki. "Nozzle flows of gas–particle mixtures." Physics of Fluids 30, no. 3 (1987): 752. http://dx.doi.org/10.1063/1.866325.

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44

Malyshev, Oleg B. "Gas dynamics modelling for particle accelerators." Vacuum 86, no. 11 (2012): 1669–81. http://dx.doi.org/10.1016/j.vacuum.2012.03.047.

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45

Cohen, Douglas L. "Hot Particle Drag in Compressible Gas." Aerosol Science and Technology 13, no. 2 (1990): 213–19. http://dx.doi.org/10.1080/02786829008959439.

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46

Ishii, R., and Y. Umeda. "Freejet flows of gas-particle mixtures." Journal of Thermophysics and Heat Transfer 2, no. 1 (1988): 17–24. http://dx.doi.org/10.2514/3.56.

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47

Wagner, Ayten Yilmaz, Hans Livbjerg, Per Gravers Kristensen, and Peter Glarborg. "Particle Emissions from Domestic Gas Cookers." Combustion Science and Technology 182, no. 10 (2010): 1511–27. http://dx.doi.org/10.1080/00102202.2010.486015.

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48

Ogi, Takashi. "2.1 Particle Generation in Gas Phase." Journal of the Society of Powder Technology, Japan 59, no. 10 (2022): 519–20. http://dx.doi.org/10.4164/sptj.59.519.

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49

Rhodes, Martin, Shihui Zhou, and Hadj Benkreira. "Flow of dilute gas-particle suspensions." AIChE Journal 38, no. 12 (1992): 1913–15. http://dx.doi.org/10.1002/aic.690381207.

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50

Lesniewski, T. K., and S. K. Friedlander. "Particle nucleation in turbulent gas jets." AIChE Journal 43, S11 (1997): 2698–703. http://dx.doi.org/10.1002/aic.690431314.

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