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Performances of falling film evaporators

Published online by Cambridge University Press:  01 June 2009

R. Selwyn Jebson
Affiliation:
Food Technology Department, Massey University, Palmerston North, New Zealand
Mani Iyer
Affiliation:
Food Technology Department, Massey University, Palmerston North, New Zealand

Summary

The performances of falling film evaporators used in the New Zealand dairy industry for concentrating skim milk, whole milk and buttermilk were evaluated by determining (1) the kg steam used per kg water evaporated, and (2) the heat transfer coefficient of each pass in the evaporators. A computer program was used to calculate the results. The heat transfer coefficients varied from 0·3 to 3·2 kW/m2 per °C and the steam consumption from 0·4 to 0·09 kg steam/kg evaporation. The viscosity of the feed and the momentum of the vapours passing down the tubes were found to be the main factors controlling the heat transfer coefficient. A correlation between the heat transfer coefficient and these factors is presented. Other factors likely to have an influence on the performance are discussed.

Type
Original articles
Copyright
Copyright © Proprietors of Journal of Dairy Research 1991

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References

REFERENCES

Agarwala, S. P. & Ojha, T. P. 1976 Heat transfer studies in single tube single effect falling film skim milk evaporator. Indian Journal of Dairy Research 29 231233Google Scholar
Angeletti, S. & Moresi, M. 1983 Modelling of multiple-effect falling-film evaporators. Journal of Food Technology 18 539563CrossRefGoogle Scholar
Bloore, C. G. & Boag, I. F. 1981 Some factors affecting the viscosity of concentrated skim milk. New Zealand Journal of Dairy Science and Technology 16 143154Google Scholar
Buckingham, J. H. 1978 Kinematic viscosities of New Zealand skim-milk. Journal of Dairy Research 45 2535CrossRefGoogle Scholar
Cooper, J. R. & Le Fevre, E. J. 1969 Thermophysical Properties of Water Substance. London: Edward ArnoldGoogle Scholar
Jebson, R. S. 1988 The performances of falling film evaporators. Proceedings, IPENZ (Institution of Professional Engineers of New Zealand) Annual Conference vol. 2 pp. 195204Google Scholar
Kessler, H. G. 1981 Food Engineering and Dairy Technology p. 235Freising: Verlag A. KesslerGoogle Scholar
Mincowycz, W. J. & Sparrow, E. M. 1966 Condensation heat transfer in the presence of noncondensables, interfacial resistance, superheating, variable properties, and diffusion. International Journal of Heat and Mass Transfer 9 11251144CrossRefGoogle Scholar
Ministry of Agriculture and Fisheries 1978 Chemistry, Standard Methods of Analysis 1.12.0. Wellington, NZ: Ministry of Agriculture and FisheriesGoogle Scholar
Narayana Murthy, V. & Sarma, P. K. 1977 Falling film evaporators–a design equation for heat transfer rates. Canadian Journal of Chemical Engineering 55 732735CrossRefGoogle Scholar
Sparrow, E. M., Mincowycz, W. J. & Saddy, M. 1967 Forced convection condensation in the presence of noncondensables and interfacial resistance. International Journal of Heat and Mass Transfer 10 18291845CrossRefGoogle Scholar