HEAT TRANSFER IN TWO-PHASE SOLID-LIQUID FOOD FLOWS: A REVIEW
暂无分享,去创建一个
[1] D. Damiano. Issues involved in producing a multiphase food product : Workshop targets continuous multiphase aseptic processing of foods , 1997 .
[2] J. E. Marcy. Biological validation : Workshop targets continuous multiphase aseptic processing of foods , 1997 .
[3] Romeo T. Toledo,et al. Heat Transfer and Simulated Sterilization of Particulate Solids in a Continuously Flowing System , 1989 .
[4] R. K. Singh,et al. Determination of fluid-particle convective heat transfer coefficient , 1995 .
[5] J H Hills. Process engineering in the food industry Edited by R. W. Field & J. A. Howell. Elsevier Science Publishers, London, 1989. 317 pp. Price £46·00. , 1989, Meat science.
[6] Sudhir K. Sastry,et al. Convective Heat Transfer at Particle‐Liquid Interface in Continuous Tube Flow at Elevated Fluid Temperatures , 1994 .
[7] F. Kreith,et al. Principles of heat transfer , 1962 .
[8] Sudhir K. Sastry,et al. Convective heat transfer coefficients for irregular particles immersed in non-newtonian fluid during tube flow☆ , 1990 .
[9] H. Johnstone,et al. Heat and mass transfer in packed beds , 1955 .
[10] F. W. Wheaton,et al. Particle/fluid interface heat transfer under UHT conditions at low particle/fluid relative velocities , 1990 .
[11] Daryl Lund,et al. THE LETHALITY‐FOURIER NUMBER METHOD. HEATING RATE VARIATIONS AND LETHALITY CONFIDENCE INTERVALS FOR FORCED‐CONVECTION HEATED FOODS IN CONTAINERS , 1978 .
[12] H. Kramers,et al. Heat transfer from spheres to flowing media , 1946 .
[13] D. I. Chandarana,et al. SENSITIVITY ANALYSIS of ASEPTIC PROCESS SIMULATIONS FOR FOODS CONTAINING PARTICULATES1 , 1990 .
[14] Sudhir K. Sastry,et al. Use of liquid crystals as temperature sensors in food processing research , 1995 .
[15] Frank Kreith,et al. Convection heat transfer and flow phenomena of rotating spheres , 1963 .
[16] Christian Trägårdh,et al. Heat transfer in tubular heat exchangers for particulate containing liquid foods , 1996 .
[17] Romeo T. Toledo,et al. Simultaneous Determination of Thermal Diffusivity and Heat Transfer Coefficient during Sterilization of Carrot Dices in a Packed Bed , 1990 .
[18] F. C. W. Olson,et al. Sterilization in food technology , 1957 .
[19] Howard H. Hu. Direct simulation of flows of solid-liquid mixtures , 1996 .
[20] D. I. Chandarana,et al. Residence time distribution of particulate foods at aseptic processing temperatures , 1996 .
[21] Mostafa Barigou,et al. The Fluid Mechanics of Two-Phase Solid-Liquid Food Flows: A Review , 1997 .
[22] W. David Kelton,et al. Statistical design and analysis , 1986, WSC '86.
[23] Henry Fraser Johnstone,et al. Heat transfer to clouds of falling particles , 1941 .
[24] Paolo Masi,et al. Biological validation of mathematical modeling of the thermal processing of particulate foods: The influence of heat transfer coefficient determination , 1994 .
[25] D. I. Chandarana,et al. Establishing Thermal Processes for Heterogeneous Foods to be Processed Aseptically: A Theoretical Comparison of Process Development Methods , 1989 .
[26] W. P. Segner,et al. BIOLOGICAL EVALUATION of A HEAT TRANSFER SIMULATION FOR STERILIZING LOW-ACID LARGE PARTICULATE FOODS FOR ASEPTIC PACKAGING , 1989 .
[27] R. G. Evans,et al. Spatial Distribution and Uniformity Evaluations for Chemigation with Center Pivots , 1995 .
[28] Nikolaos G. Stoforos. An Overview of Aseptic Processing of Particulate Foods , 1992 .
[29] I J Pflug,et al. Measuring Sterilizing Values In Containers of Food Using Thermocouples and Biological Indicator Units 1, 2. , 1980, Journal of food protection.
[30] Sudhir K. Sastry,et al. DETERMINATION of CONVECTIVE HEAT TRANSFER COEFFICIENT BETWEEN FLUID and CUBIC PARTICLES IN CONTINUOUS TUBE FLOW USING NONINVASIVE EXPERIMENTAL TECHNIQUES , 1994 .
[31] Paul Tobback,et al. Fluid-to-particle heat transfer coefficient determination of heterogeneous foods : a review , 1992 .
[32] H. S. Ramaswamy,et al. Comparison of two methods for evaluating fluid-to-surface heat transfer coefficients , 1995 .
[33] J. A. G. Rees,et al. Processing and Packaging of Heat Preserved Foods , 1990 .
[34] Nikolaos G. Stoforos,et al. Measurement of Heat Transfer Coefficients in Rotating Liquid/Particulate Systems , 1991 .
[35] Peter J. Fryer,et al. A heterogeneous flow model for the effect of slip and flow velocities on food steriliser design , 1997 .
[36] Ashim K. Datta,et al. Heat transfer to particles in shear flow: Application in aseptic processing , 1993 .
[37] P. Fryer,et al. The effect of particle slip on the sterilisation of solid-liquid food mixtures , 1995 .
[38] A. T. Jones,et al. EFFECT OF FILL WEIGHT ON THE F-VALUE DELIVERED TO TWO STYLES OF GREEN BEANS PROCESSED IN A STERILMATIC RETORT , 1980 .
[39] J. W. Larkin,et al. Statistical design and analysis : Workshop targets continuous multiphase aseptic processing of foods , 1997 .
[40] Y.-M. Choi,et al. Microbiological and chemical investigation of ohmic heating of particulate foods using a 5 kW ohmic system , 1996 .
[41] Pradeep K. Agarwal,et al. Transport phenomena in multi-particle systems—II. Particle-fluid heat and mass transfer , 1988 .
[42] J. C. Jaeger,et al. Conduction of Heat in Solids , 1952 .
[43] J. E. Manson,et al. THERMAL PROCESS SIMULATION FOR ASEPTIC PROCESSING OF FOODS CONTAINING DISCRETE PARTICULATE MATTER , 1974 .
[44] D. L. Parrott,et al. Use of ohmic heating for aseptic processing of food particulates : Dielectric and ohmic sterilization , 1992 .
[45] Sudhir K. Sastry,et al. Liquid-to-particle heat transfer during continuous tube flow: influence of flow rate and particle to tube diameter ratio , 1990 .
[46] Thomas Ohlsson,et al. A computer simulation program for evaluation of the continuous heat treatment of particulate food products. Part 2: Utilisation , 1993 .
[47] E. J. Hinch,et al. The elastohydrodynamic collision of two spheres , 1986, Journal of Fluid Mechanics.
[48] Jorge C. Oliveira,et al. Dimensionless analysis of fluid-to-particle heat transfer coefficients , 1997 .
[49] Sudhir K. Sastry,et al. Mathematical evaluation of process schedules for aseptic processing of low-acid foods containing discrete particulates , 1986 .
[50] Peter J. Fryer,et al. AN EXPERIMENTAL STUDY OF PARTICLE FLOW VELOCITIES IN SOLID-LIQUID FOOD MIXTURES , 1993 .
[51] S. Whitaker. Forced convection heat transfer correlations for flow in pipes, past flat plates, single cylinders, single spheres, and for flow in packed beds and tube bundles , 1972 .
[52] S. K. Sastry. Measuring residence time and modeling the system : Workshop targets continuous multiphase aseptic processing of foods , 1997 .
[53] Robert V. Dail. Calculation of Required Hold Time of Aseptically Processed Low Acid Foods Containing Particulates Utilizing the Ball Method , 1985 .
[54] Anthony G. Dixon,et al. Fluid-phase radial transport in packed beds of low tube-to-particle diameter ratio , 1984 .
[55] W. Ranz. Evaporation from drops : Part II , 1952 .
[56] Christian Trägårdh,et al. Heat transfer and food products , 1988 .
[57] Sudhir K. Sastry,et al. Liquid-to-particle convective heat transfer in non-Newtonian carrier medium during continuous tube flow , 1994 .
[58] Göran Bark,et al. Heat transfer between fluid and particles in aseptic processing , 1994 .
[59] Sudhir K. Sastry,et al. Velocity distributions of food particle suspensions in holding tube flow : distribution characteristics and fastest-particle velocities , 1990 .
[60] D. J. Gunn,et al. Thermal dispersion and wall heat transfer in packed beds , 1975 .
[61] C. Sizer,et al. Aseptic process validated for foods containing particulates , 1997 .
[62] W. E. Ranz,et al. Evaporation from drops , 1952 .
[63] Y. Jaluria,et al. An Introduction to Heat Transfer , 1950 .
[64] H. S. Ramaswamy,et al. SURFACE HEAT TRANSFER COEFFICIENTS ASSOCIATED WITH HEATING of FOOD PARTICLES IN CMC SOLUTIONS , 1993 .
[65] R. K. Singh,et al. Fluid to particle heat transfer coefficient determination in a continuous system , 1994 .
[66] Mohammad Jamialahmadi,et al. PREDICTION OF HEAT-TRANSFER TO LIQUID-SOLID FLUIDIZED-BEDS , 1995 .
[67] Ho-mu Lin,et al. Antimicrobial Effect of Pressurized Carbon Dioxide on Listeria monocytogenes , 1994 .
[68] Neal R. Amundson,et al. Solid-Fluid Interactions in Fixed and Moving Beds Fixed Beds with Small Particles , 1956 .
[69] S. Holdsworth. Thermal processing of packaged foods , 1997 .
[70] P. Noordsij,et al. Mass transfer coefficients to a rotating and to a vibrating sphere , 1967 .
[71] Koichi Asano,et al. NUMERICAL ANALYSIS OF HEAT AND MASS TRANSFER FROM A SPHERE WITH SURFACE MASS INJECTION OR SUCTION , 1984 .
[72] Peter J. Fryer,et al. Measurements of particle-liquid heat transfer in systems of varied solids fraction , 1997 .
[73] M. Hendrickx,et al. Evaluation of the integrated time-temperature effect in thermal processing of foods. , 1995, Critical reviews in food science and nutrition.
[74] A. T. Jones,et al. PERFORMANCE OF BACTERIAL SPORES IN A CARRIER SYSTEM IN MEASURING THE Fo‐VALUE DELIVERED TO CANS OF FOOD HEATED IN A STERITORT , 1980 .
[75] A. B. McKenna,et al. Computer modelling for the control of particulate sterilization under dynamic flow conditions , 1991 .
[76] Peter J. Fryer,et al. Electrical resistance heating of foods , 1993 .
[77] R. K. Singh,et al. Thermal Time Distributions in Tubular Heat Exchangers during Aseptic Processing of Fluid Foods , 1994 .