Relevant bibliographies by topics / Gas/particle

Contents

  1. Journal articles
  2. Dissertations / Theses
  3. Books
  4. Book chapters
  5. Conference papers
  6. Reports

Academic literature on the topic 'Gas/particle'

Author: Grafiati
Published: 9 March 2023
Last updated: 10 March 2023

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Journal articles on the topic "Gas/particle"

1

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

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Zhou, Lixing, and Zhuoxiong Zeng. "Studies on gas turbulence and particle fluctuation in dense gas-particle flows." Acta Mechanica Sinica 24, no. 3 (May 8, 2008): 251–60. http://dx.doi.org/10.1007/s10409-008-0156-z.

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

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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 (June 2022): 669–706. http://dx.doi.org/10.4208/cicp.oa-2021-0153.

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

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

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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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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 (July 2007): 3429–42. http://dx.doi.org/10.1016/j.ces.2007.01.086.

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

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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 (May 1996): 1281–87. http://dx.doi.org/10.1116/1.579942.

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Dissertations / Theses on the topic "Gas/particle"

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Strömgren, Tobias. "Modelling of turbulent gas-particle flow." Licentiate thesis, KTH, Mechanics, 2008. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-4639.

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An Eulerian-Eulerian model for dilute gas-particle turbulent flows is

developed for engineering applications. The aim is to understand the effect of particles on turbulent flows. The model is implemented in a finite element code which is used to perform numerical simulations. The feedback from the particles on the turbulence and the mean flow of the gas in a vertical channel flow is studied. In particular, the influence of the particle response time and particle volume fraction on the preferential concentration of the particles near the walls, caused by the turbophoretic effect is explored. The study shows that the particle feedback decreases the accumulation of particles on the walls. It is also found that even a low particle volume fraction can have a significant impact on the turbulence and the mean flow of the gas. A model for the particle fluctuating velocity in turbulent gas-particle flow is derived using a set of stochastic differential

equations. Particle-particle collisions were taken into account. The model shows that the particle fluctuating velocity increases with increasing particle-particle collisions and that increasing particle response times decrease the fluctuating velocity.

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Strömgren, Tobias. "Modelling of turbulent gas-particle flow /." Stockholm : Mekanik, Kungliga Tekniska högskolan, 2008. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-4639.

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Götz, Christian Walter. "Gas-particle partitioning and particle-bound deposition of semivolatile organic chemicals /." Zürich : ETH, 2007. http://e-collection.ethbib.ethz.ch/show?type=diss&nr=17506.

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Zhang, Yonghao. "Particle-gas interactions in two-fluid models of gas-solid flows." Thesis, University of Aberdeen, 2001. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.367375.

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Modelling gas-solid two-phase flows using a two-fluid approach has two main difficulties: formulating constitutive laws for the particulate stresses and modelling the gas turbulence modulation. Due to the complex nature of the gas-particle interactions, there is no universal model covering every flow regime. In this thesis, three flow regimes with distinctive characteristics are studied, i.e. the very dense regime where the solid volume fraction, v2>5%, the dense flow regime where 5%≥1%, and the relatively dilute regime where 1%≥v2>0.1%. In the very dense flow regime, where the interstitial gas is normally neglected, the gas flow is assumed laminar and causes a viscous energy dissipation in the particulate phase. Numerical results for granular materials flowing down an inclined chute show that the interstitial gas may have a considerable effect in these flows. In the dense regime, where the inter-particle collisions are very important, a fluctuational energy transfer rate between the two phases is postulated, similar to that in a dilute Stokes flow. Consequently, the numerical solutions relax the restriction of elastic inter-particle collisions and show good agreement with experimental measurements. In the above two regimes, the kinetic theory of dry granular flow is adopted for the particulate stresses because the inter-particle collisions dominate the flows. The interstitial gas influence on the constitutive flow behaviour of the particulate phase is considered in the relatively dilute flow regime also, and a k-equation with a prescribed turbulent length scale is first used to address the gas turbulence modulation. Numerical results show that the gas turbulence has a significant effect on the microscopic flow behaviour of the particulate phase. The k-equation of Crowe & Gillandt (1998) has the best performance in predicting the experimentally observed phenomena. Finally, the influence of the particles on the k-Ε model coefficients are studied and the turbulent motion is considered to be restricted by the particles, thereby reducing the turbulent length scale directly. The simulation results indicate that these coefficients should be modified in order to incorporate the effect of particles.
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Choi, Moon Kyu Gavalas George R. Gavalas George R. "Particle shape effects on gas-solid reactions /." Diss., Pasadena, Calif. : California Institute of Technology, 1992. http://resolver.caltech.edu/CaltechETD:etd-07232007-152302.

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Strömgren, Tobias. "Model predictions of turbulent gas-particle shear flows." Doctoral thesis, KTH, Mekanik, 2010. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-12135.

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A turbulent two-phase flow model using kinetic theory of granularflows for the particle phase is developed and implmented in afinite element code. The model can be used for engineeringapplications. However, in this thesis it is used to investigateturbulent gas-particle flows through numerical simulations.  The feedback from the particles on the turbulence and the meanflow of the gas in a vertical channel flow is studied. In particular,the influence of the particle response time, particle volumefraction and particle diameter on the preferential concentration ofthe particles near the walls, caused by the turbophoretic effect isexplored. The study shows that when particle feedback is includedthe accumulation of particles near the walls decreases. It is also foundthat even at low volume fractions particles can have a significant impacton the turbulence and the mean flow of the gas. The effect of particles on a developing turbulent vertical upward pipeflow is also studied. The development length is found to substantiallyincrease compared to an unladen flow. To understand what governs thedevelopment length a simple estimation was derived, showing that itincreases with decreasing particle diameters in accordance with themodel simulations. A model for the fluctuating particle velocity in turbulentgas-particle flow is derived using a set of stochastic differentialequations taking into account particle-particle collisions. Themodel shows that the particle fluctuating velocity increases whenparticle-particle collisions become more important and that increasingparticle response times reduces the fluctuating velocity. The modelcan also be used for an expansion of the deterministic model for theparticle kinetic energy.
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Mansoorzadeh, Shahriar. "Numerical modelling of gas particle fluidised bed dynamics." Thesis, Imperial College London, 1999. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.313654.

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Slater, Shane Anthony. "Particle transport in laminar and turbulent gas flows." Thesis, University of Cambridge, 1999. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.624527.

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Forsyth, Peter. "High temperature particle deposition with gas turbine applications." Thesis, University of Oxford, 2017. http://ora.ox.ac.uk/objects/uuid:61556237-feed-43cb-9f4a-d0aed00ca3f8.

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This thesis describes validated improvements in the modelling of micron-sized particle deposition within gas turbine engine secondary air systems. The initial aim of the research was to employ appropriate models of instantaneous turbulent flow behaviour to RANS CFD simulations, allowing the trajectory of solid particulates in the flow to be accurately predicted. Following critical assessment of turbophoretic models, the continuous random walk (CRW) model was chosen to predict instantaneous fluid fluctuating velocities. Particle flow, characterised by non-dimensional deposition velocity and particle relaxation time, was observed to match published experimental vertical pipe flow data. This was possible due to redefining the integration time step in terms of Kolmagorov and Lagrangian time scales, reducing the disparity between simulations and experimental data by an order of magnitude. As no high temperature validation data for the CRW model were available, an experimental rig was developed to conduct horizontal pipe flow experiments under engine realistic conditions. Both the experimental rig, and a new particulate concentration measurement technique, based on post test aqueous solution electrical conductivity, were qualified at ambient conditions. These new experimental data compare well to published data at non-dimensional particle relaxation times below 7. Above, a tail off in the deposition rate is observed, potentially caused by a bounce or shear removal mechanism at higher particle kinetic energy. At elevated temperatures and isothermal conditions, similar behaviour is observed to the ambient data. Under engine representative thermophoretic conditions, a negative gas to wall temperature gradient is seen to increase deposition by up to 4.8 times, the reverse decreasing deposition by a factor of up to 560 relative to the isothermal data. Numerical simulations using the CRW model under-predict isothermal deposition, though capturing relative thermophoretic effects well. By applying an anisotropic Lagrangian time scale, and cross trajectory effects of the external gravitational force, good agreement was observed, the first inclusion of the effect within the CRW model. A dynamic mesh morphing method was then developed, enabling the effect of large scale particle deposition to be included in simulations, without continual remeshing of the fluid domain. Simulation of an impingement jet array showed deposition of characteristic mounds up to 30% of the hole diameter in height. Simulation of a passage with film-cooling hole off-takes generated hole blockage of up to 40%. These cases confirmed that the use of the CRW generated deposition locations in line with scant available experimental data, but widespread airline fleet experience. Changing rates of deposition were observed with the evolution of the deposits in both cases, highlighting the importance of capturing changing passage geometry through dynamic mesh morphing. The level of deposition observed, was however, greater than expected in a real engine environment and identifies a need to further refine bounce-stick and erosion modelling to complement the improved prediction of impact location identified in this thesis.
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Swar, Rohan. "Particle Erosion of Gas Turbine Thermal Barrier Coating." University of Cincinnati / OhioLINK, 2009. http://rave.ohiolink.edu/etdc/view?acc_num=ucin1259075518.

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Books on the topic "Gas/particle"

1

Astrup, Poul. Turbulent gas-particle flow. Roskilde: Risø National Laboratory, 1992.

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Varaksin, Aleksej Y., ed. Turbulent Particle-Laden Gas Flows. Berlin, Heidelberg: Springer Berlin Heidelberg, 2007. http://dx.doi.org/10.1007/978-3-540-68054-3.

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United States. National Aeronautics and Space Administration., ed. Analysis of the gas particle radiator. [Washington, D.C.]: National Aeronautics and Space Administration, 1986.

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Varaksin, A. Y. Collisions in particle-laden gas flows. New York: Begell House, 2013.

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Dall, Henrik. Development of a Computer Model for Stationary Turbulent 3-D Gas-Particle Flows: Characteristics parameters of gas-particle flow. Roskilde, Denmark: Riso National Laboratory, 1988.

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Lock, G. D. Gas density and particle concentration measurements in shock-induced dusty-gas flows. [S.l.]: [s.n.], 1989.

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Backman, Ulrika. Studies on nanoparticle synthesis via gas-to-particle conversion. [Espoo, Finland]: VTT Technical Research Centre of Finland, 2005.

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A, Lane Douglas, ed. Gas and particle phase measurements of atmospheric organic compounds. Australia: Gordon and Breach, 1999.

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P, Astrup. Development of a computer model for stationary turbulent 3-D gas-particle flow: Numerical prediction of a turbulent gas-particle duct flow. Roskilde: Riso Library, 1989.

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Garrick, Sean C., and Michael Bühlmann. Modeling of Gas-to-Particle Mass Transfer in Turbulent Flows. Cham: Springer International Publishing, 2018. http://dx.doi.org/10.1007/978-3-319-59584-9.

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Book chapters on the topic "Gas/particle"

1

Fauchais, Pierre L., Joachim V. R. Heberlein, and Maher I. Boulos. "Gas Flow–Particle Interaction." In Thermal Spray Fundamentals, 113–226. Boston, MA: Springer US, 2013. http://dx.doi.org/10.1007/978-0-387-68991-3_4.

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Michoud, Vincent. "Particle-Gas Multiphasic Interactions." In Atmospheric Chemistry in the Mediterranean Region, 185–97. Cham: Springer International Publishing, 2022. http://dx.doi.org/10.1007/978-3-030-82385-6_11.

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Yoshida, Hideto, and Hisao Makino. "Particle Sampling in Gas Flow." In Powder Technology Handbook, 567–74. Fourth edition. | Boca Raton, FL : Taylor & Francis Group, LLC, 2020.: CRC Press, 2019. http://dx.doi.org/10.1201/b22268-69.

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Zhang, Fan. "Detonation of Gas-Particle Flow." In Shock Wave Science and Technology Reference Library, 87–168. Berlin, Heidelberg: Springer Berlin Heidelberg, 2009. http://dx.doi.org/10.1007/978-3-540-88447-7_2.

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Seville, J. P. K., and R. Clift. "Gas cleaning at high temperatures: gas and particle properties." In Gas Cleaning in Demanding Applications, 1–14. Dordrecht: Springer Netherlands, 1997. http://dx.doi.org/10.1007/978-94-009-1451-3_1.

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Charlson, R. J. "Gas-to-Particle Conversion and CCN Production." In Dimethylsulphide: Oceans, Atmosphere and Climate, 275–86. Dordrecht: Springer Netherlands, 1993. http://dx.doi.org/10.1007/978-94-017-1261-3_29.

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Gori-Giorgi, Paola. "Uniform Electron Gas from Two-Particle Wavefunctions." In Electron Correlations and Materials Properties 2, 379–87. Boston, MA: Springer US, 2002. http://dx.doi.org/10.1007/978-1-4757-3760-8_22.

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Valiveti, Prabhu, and Donald L. Koch. "Instability of Sedimenting Bidisperse Particle Gas Suspensions." In In Fascination of Fluid Dynamics, 275–303. Dordrecht: Springer Netherlands, 1998. http://dx.doi.org/10.1007/978-94-011-4986-0_16.

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Kawano, A., and K. Kusano. "Continuum/particle interlocked simulation of gas detonation." In Shock Waves, 215–20. Berlin, Heidelberg: Springer Berlin Heidelberg, 2009. http://dx.doi.org/10.1007/978-3-540-85168-4_33.

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Mazzei, Luca. "Recent Advances in Modeling Gas-Particle Flows." In Handbook of Multiphase Flow Science and Technology, 1–43. Singapore: Springer Singapore, 2016. http://dx.doi.org/10.1007/978-981-4585-86-6_8-1.

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Conference papers on the topic "Gas/particle"

1

Tsuji, Yutaka. "TURBULENCE IN GAS-PARTICLE FLOW." In Third Symposium on Turbulence and Shear Flow Phenomena. Connecticut: Begellhouse, 2003. http://dx.doi.org/10.1615/tsfp3.10.

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Kocsis, M. "Gas-filled micro void particle detector." In 2003 IEEE Nuclear Science Symposium. Conference Record (IEEE Cat. No.03CH37515). IEEE, 2003. http://dx.doi.org/10.1109/nssmic.2003.1352065.

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Horton, Tom. "Gas strippers for neutral particle beam systems." In 32nd Aerospace Sciences Meeting and Exhibit. Reston, Virigina: American Institute of Aeronautics and Astronautics, 1994. http://dx.doi.org/10.2514/6.1994-255.

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Zhang, Xinyu, and Goodarz Ahmadi. "Particle Effects on Gas-Liquid-Solid Flows." In ASME 2011 International Mechanical Engineering Congress and Exposition. ASMEDC, 2011. http://dx.doi.org/10.1115/imece2011-65695.

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A numerical simulation is carried out to study the role of particles in gas-liquid-solid flows in bubble columns. An Eulerian-Lagrangian model is used and the liquid flow is modeled using a volume-averaged system of governing equations, while motions of bubbles and particles are evaluated using Lagrangian trajectory analysis. It is assumed that the bubbles remain spherical. The interactions between bubble-liquid and particle-liquid are included in the study. The discrete phase equations include drag, lift, buoyancy, and virtual mass forces. Particle-particle interactions and bubble-bubble interactions are accounted for by the hard sphere model approach. The bubble coalescence is also included in the model. Neutrally buoyant particles are used in the study. A parcel approach is used and a parcel represents a certain number of particles of same size, velocity, and other properties. Variation of particle loading is modeled by changing the corresponding number of particles in every parcel. In a previous work, the predicted results were compared with the experimental data, and good agreement was obtained. The transient flow characteristics of the three-phase flow are studied and the effects of particle loading on flow characteristics are discussed. The simulations show that the transient characteristics of the three-phase flow in a column are dominated by time-dependent vortices. The particle loading can affect the characteristics of the three-phase flows and flows with high particle loading evolve faster.
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Boyd, Iain, and Quanhua Sun. "Particle simulation of micro-scale gas flows." In 39th Aerospace Sciences Meeting and Exhibit. Reston, Virigina: American Institute of Aeronautics and Astronautics, 2001. http://dx.doi.org/10.2514/6.2001-876.

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ISHII, R., and Y. UMEDA. "Free-jet flows of gas-particle mixtures." In 4th Thermophysics and Heat Transfer Conference. Reston, Virigina: American Institute of Aeronautics and Astronautics, 1986. http://dx.doi.org/10.2514/6.1986-1317.

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Mesyats, Gennady A. "High-power particle beams for gas lasers." In Optics, Electro-Optics, and Laser Applications in Science and Engineering, edited by G. Glen McDuff. SPIE, 1991. http://dx.doi.org/10.1117/12.43613.

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Ward, Sayed A., M. A. Abd Allah, and Amr A. Youssef. "Multi-particle initiated breakdown of gas mixtures inside compressed gas devices." In 2012 IEEE Conference on Electrical Insulation and Dielectric Phenomena - (CEIDP 2012). IEEE, 2012. http://dx.doi.org/10.1109/ceidp.2012.6378793.

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Chen, Huajun, Yitung Chen, Hsuan-Tsung Hsieh, and Nathan Siegel. "CFD Modeling of Gas Particle Flow Within a Solid Particle Solar Receiver." In ASME 2006 International Solar Energy Conference. ASMEDC, 2006. http://dx.doi.org/10.1115/isec2006-99044.

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A detailed three dimensional computational fluid dynamics (CFD) analysis on gas-particle flow and heat transfer inside a solid particle solar receiver, which utilizes free-falling particles for direct absorption of concentrated solar radiation, is presented. The two-way coupled Euler-Lagrange method is implemented and includes the exchange of heat and momentum between the gas phase and solid particles. A two band discrete ordinate method is included to investigate radiation heat transfer within the particle cloud and between the cloud and the internal surfaces of the receiver. The direct illumination energy source that results from incident solar radiation was predicted by a solar load model using a solar ray tracing algorithm. Two kinds of solid particle receivers, each having a different exit condition for the solid particles, are modeled to evaluate the thermal performance of the receiver. Parametric studies, where the particle size and mass flow rate are varied, are made to determine the optimal operating conditions. The results also include detailed information for the particle and gas velocity, temperature, particle solid volume fraction, and cavity efficiency.
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Lock, Gary D., and James J. Gottlieb. "Gas density and particle concentration measurements in shock-induced dusty-gas flows." In Current topics in shock waves 17th international symposium on shock waves and shock tubes Bethlehem, Pennsylvania (USA). AIP, 1990. http://dx.doi.org/10.1063/1.39465.

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Reports on the topic "Gas/particle"

1

Fowler, T. K. Particle transport and gas feed during gun injection. Office of Scientific and Technical Information (OSTI), March 1999. http://dx.doi.org/10.2172/9633.

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Durham, M. D. Flue gas conditioning for improved particle collection in electrostatic precipitators. Office of Scientific and Technical Information (OSTI), April 1992. http://dx.doi.org/10.2172/7205354.

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Sankaran Sundaresan. Closures for Course-Grid Simulation of Fluidized Gas-Particle Flows. Office of Scientific and Technical Information (OSTI), February 2010. http://dx.doi.org/10.2172/1007990.

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Durham, M. D. Flue gas conditioning for improved particle collection in electrostatic precipitators. Office of Scientific and Technical Information (OSTI), January 1993. http://dx.doi.org/10.2172/7045530.

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Durham, M. D. Flue gas conditioning for improved particle collection in electrostatic precipitators. Office of Scientific and Technical Information (OSTI), October 1992. http://dx.doi.org/10.2172/7045559.

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Durham, M. D. Flue gas conditioning for improved particle collection in electrostatic precipitators. Office of Scientific and Technical Information (OSTI), April 1993. http://dx.doi.org/10.2172/6552831.

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Durham, M. D. Flue gas conditioning for improved particle collection in electrostatic precipitators. Office of Scientific and Technical Information (OSTI), January 1992. http://dx.doi.org/10.2172/5794372.

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Anderson, Iver, and Jordan Tiarks. CONCENTRIC RING GAS ATOMIZATION DIE DESIGN FOR OPTIMIZED PARTICLE PRODUCTION. Office of Scientific and Technical Information (OSTI), August 2021. http://dx.doi.org/10.2172/1853951.

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Reed, D. T., J. Hoh, J. Emery, S. Okajima, and T. Krause. Gas production due to alpha particle degradation of polyethylene and polyvinylchloride. Office of Scientific and Technical Information (OSTI), July 1998. http://dx.doi.org/10.2172/303944.

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Turner, J. E., R. N. Hamn, S. R. Hunter, W. A. Gibson, G. S. Hurst, and H. A. Wright. Optical imaging of charged particle tracks in a gas. Final report. Office of Scientific and Technical Information (OSTI), September 1995. http://dx.doi.org/10.2172/114038.

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