Residence time distribution of food and simulated particles in a model horizontal swept surface heat exchanger

Journal of Food Process Engineering

Volumn 21, Issue 2, 1998, Pages 145-180

  Alhamdan, Abdullah ^a   Sastry, Sudhir K ^a  

^a OHIO STATE UNIVERSITY   (United States)

Author keywords

[No Author keywords available]

Indexed keywords

FLOW OF FLUIDS; FOOD PRODUCTS; HEAT EXCHANGERS; PARTICLES (PARTICULATE MATTER); POLYSTYRENES; SHAFTS (MACHINE COMPONENTS); VISCOSITY OF LIQUIDS; WATER;

MEAN PARTICLE NORMALIZED RESIDENCE TIME (MNPRT); RESIDENCE TIME DISTRIBUTION (RTD);

FOOD PROCESSING;

EID: 0032071489     PISSN: 01458876     EISSN: None     Source Type: Journal    
DOI: 10.1111/j.1745-4530.1998.tb00445.x     Document Type: Article

References (40)

1. ABDELRAHIM, K.A., RAMASWAMY, H.S., MARCOTTE, M. and TOUPIN, C. 1993. Residence time distribution of carrot cubes in starch solutions in a pilot scale aseptic processing system. Food Res. Intl. 26, 431-441.
2. ABICHANDANI, H. and SARMA, S.C. 1987. Residence time distributions in horizontal thin film scraped-surface heat exchanger. J. Food Process Engineering 10, 71-80.
3. ALCAIRO, E.R. and ZURITZ, C.A. 1990. Residence time distributions of spherical particles suspended in non-Newtonian flow in a scraped-surface heat exchanger. Trans. of the ASAE 33, 1621-1628.
4. BALASUBRAMANIAM, V.M. and SASTRY, S.K. 1996. Fluid-to-particle convective heat transfer coefficient in a horizontal scraped surface heat exchanger determined from relative velocity measurement. J. Food Process Engineering 19, 75-95.
5. BOTT, T.R., AZOORY, S. and PORTER, K.E. 1968. Scraped-surface heat exchangers Part I-hold-up and residence time studies. Trans. Inst. Chem. Engrs. T33-T37.
6. BRADY, J. and BOSSIS, G. 1985. The rheology of concentrated suspensions of spheres in simple shear flow by numerical simulation. J. Fluid Mech. 155, 105.
7. BRODKEY, R. and HERSHEY, H. 1988. Transport Phenomena, a Unified Approach. McGraw-Hill Book Co., New York.
8. BROWN, L.F. and FOGLER, H.S. 1986. Distributions of residence time for chemical reactors. In Elements of Chemical Reaction Engineering. (H.S. Fogler, ed.) pp. 629-679, Prentice-Hall, Englewood Cliffs, NJ.
9. BURFOOT, D. and SELF, K.P. 1988. Prediction of heating times for cubes of beef during water cooking. J. Food Sci. 23, 247-257.
10. CHANDARANA, D. and UNVERFERTH, J. 1996. Residence time distribution of particulate foods at aseptic processing temperatures. J. Food Eng. 28, 349-360.
11. CHEN, A.C. and ZAHRADNIK, J.W. 1967. Residence time distribution in a swept surface heat exchanger. Transactions of the ASAE. 10(4), 508-511.
12. CHHABRA, R. and SRINIVAS, B. 1991. Non-Newtonian (purely viscous) fluid flow through packed beds: Effect of particle shape. Powder Technol. 67, 15.
13. CLARK, N., TURTON, R. and FLEMMER, R. 1989. The effect of particle shape on fluid-particle interactions. Particulate Sci. Technol. 7, 399.
14. DAWSON, P.L., SHELDON, B.W. and MILES, J. 1991. Effect of aseptic processing on the texture of chicken meat. Poultry Sci. 70, 2359-2367.
15. DIGNAN, D.M., BERRY, M.R., PFLUG, I.J. and GARDINE, T.D. 1989. Safety considerations in establishing aseptic processes for low-acid foods containing particulate. Food Technol. 43(3), 118-121, 131.
16. DUTTA, B. and SASTRY, S. 1990a. Velocity distributions of food particle suspensions in holding tube flow: Experimental and modeling studies on average particle velocities. J. Food Sci. 55(5), 1448-1453.
17. DUTTA, B. and SASTRY, S. 1991b. Velocity distributions of food particle suspensions in holding tube flow: Distribution characteristics and fastest-particle velocities. J. Food Sci. 55(6), 1703-1710.
18. FLEMMER, R., PICKETT, J. and CLARK, N. 1993. An experimental study on the effect of particle shape on fluidization behavior. Powder Technol. 77, 12.
19. FOUST, A., WENZEL, L., CLUMP, C., MAUS, L. and ANDERSEN, L. 1990. Principles of Unit Operations. John Wiley & Sons, New York.
20. HAHN, G.J. and SHAPIRO, S.S. 1967. Statistical Models in Engineering. John Wiley & Sons, New York.
21. HÄRRÖD, M. 1986. Scraped surface heat exchangers - a literature survey of flow patterns, mixing effects, residence time distribution, heat transfer and power requirements. J. Food Process Engineering 9(1), 1-6.
22. HÄRRÖD, M. 1990. Methods to distinguish between laminar and vortical flow in scraped surface heat exchangers. J. Food Process Engineering 13(1), 39-57.
23. KONANAYAKAM, M. and SASTRY, S. 1988. Kinetics of shrinkage of mushrooms during blanching. J. Food Sci. 53, 1406-1410.
24. LAREO, C., FRYER, P.J. and BARIGOU, M. 1997. The fluid mechanics of two-phase solid-liquid food flows. Food and Bioproducts Proc., Trans. IChemE, Part C. 75(C2), 73-105.
25. LEE, J.H. and SINGH, R.K. 1991a. Particle residence time distributions in a model horizontal scraped-surface heat exchanger. J. Food Process Engineering 14, 125-146.
26. LEE, J.H. and SINGH, R.K. 1991b. Process parameters effects on particle residence time in a vertical scraped-surface heat exchanger. J. Food Sci. 56, 869.
27. LEE, J.H. and SINGH, R.K. 1991c. Scraped-surface heat exchanger orientation influence on particle residence time distributions. J. Food Sci. 56, 1446-1447.
28. LEE, J.H., SINGH, R.K. and LINEBACK, D.S. 1995. Particle concentration influence on liquid residence time distribution in a model aseptic processing system. J. Food Process Engineering 18(2), 119-133.
29. LEVENSPIEL, O. 1972. Non-ideal flow. In Chemical Reaction Engineering. pp. 253-325, John Wiley & Sons, New York.
30. LIU, Y. and ZURITZ, C.A. 1995. Mathematical modeling of particulate two-phase flow in a helical pipe. J. Food Process Engineering 18(3), 321-341.
31. McCOY, S., ZURITZ, C. and SASTRY, S. 1987. Residence time distribution of simulated food particles in a holding tube. ASAE Paper No. 87-6536. ASAE, St. Joseph, MI.
32. MILTON, J.L. and ZAHRADNIK, J.W. 1973. Residence time distribution of a votator pilot plant using a non-Newtonian fluid. Transactions of the ASAE 16(6), 1186-1189.
33. RAMASWAMY, H.S., ABDELRAHIM, K.A., MARCOTTE, M. and CLAVIER, P. 1995a. Residence time distribution (RTD) characteristics of meat and carrot cubes in starch solutions in a vertical scraped-surface heat exchanger. Food Res. Intl. 28(4), 331-342.
34. RAMASWAMY, H.S., ABDELRAHIM, K.A., SIMPSON, B.K. and SMITH, J.P. 1995b. Residence time distribution in aseptic processing of particulate foods: a review. Food Res. Intl. 28(3), 291-310.
35. RAO, M. and LONCIN, M. 1973. Residence time distribution and its role in continuous pasteurization. Part I and II. Lebensm.-Wiss. u. Technol. 7(1), 5-17.
36. SCHOWALTER, W.R. 1978. In Mechanics of non-Newtonian Fluids. Pergamon Press, London, U.K.
37. TAEYMANS, D., ROELANS, E. and LENGES, J. 1986. Residence time distribution in a horizontal SSHE used for UHT processing of liquids containing solids. In Food Engineering and Process Applications. Transport Phenomenon, (M. Le Maguer and P. Jelen, eds.) pp. 247-258, Elsevier Applied Science, New York.
38. TROMMELEN, A.M. and BEEK, W.J. 1971. Flow phenomenon in a scraped surface heat exchanger. Chem. Eng. Sci. 26(11), 1933-1934.
39. YANG, B. and SWARTZEL, K. 1991. Photo-sensor methodology for determining residence time distribution of particles in continuous flow thermal processing systems. J. Food Sci. 56, 1076.
40. YANG, B. and SWARTZEL, K. 1992. Particle residence time distribution in Two-phase flow in straight round conduit. J. Food Sci. 57, 497.