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Part of the book series: Food Engineering Series ((FSES))

Abstract

Mixing is fundamental to food processing operations, such as in the preparation of ingredients, the addition of solids to liquids and the development of structure and incorporation of air in the dough mixing process. Chapters 2 and 5 have described the basics of fluid mechanics and of food rheology. Rheology is crucial in mixing; it is obviously more straightforward to mix a fluid such as water than it is to ensure the homogeneity of a highly viscous and non-Newtonian fluid such as a starch solution.

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References and further reading

  • Bates, R.L., Fondy, P.L. and Corpstein, R.R. (1963) An examination of some geometric parameters of impeller power. Industrial and Engineering Chemistry, Process Design and Development, 2, 310–314.

    Article  CAS  Google Scholar 

  • Bruijn, W., Van’t Riet, K. and Smith, J.M. (1974) Power consumption with aerated Rushton turbines. Transactions of the Institution of Chemical Engineers, 52, 88–104.

    Google Scholar 

  • Calderbank, P.H. (1958) Physical rate processes in industrial fermentation. Transactions of the Institution of Chemical Engineers, 36, 443–463.

    Google Scholar 

  • Danckwerts, P.V. (1953) The definition and measurement of some characteristics of mixtures. Applied Scientific Research, 3, 279–296.

    Google Scholar 

  • Donaldson, R. (1985) in Mixing in the Process Industries (eds N. Harnby, M.F. Edwards and A.W. Nienow), Butterworth, London, Ch. 15.

    Google Scholar 

  • Edwards, M.F. (1985) in Mixing in the Process Industries (eds N. Harnby, M.F. Edwards and A.W. Nienow), Butterworth, London, Ch. 7.

    Google Scholar 

  • Edwards, M.F. and Ayazi-Shamlou, P. (1983) in Low Reynolds Number Flow Heat Exchangers (ed. Spacek, S), Hemisphere.

    Google Scholar 

  • Geldart, D. (1973) Types of gas fluidisation. Powder Technology, 7, 285–292.

    Article  CAS  Google Scholar 

  • Greaves, M. and Barigou, M. (1986) Estimation of gas holdup and impeller power in a stirred vessel, in Fluid Mixing III, Institution of Chemical Engineers Symposium Series 108, pp. 235-256.

    Google Scholar 

  • Greaves, M. and Kobbacy, K.A.H. (1981) Power consumption and impeller dispersion efficiency in gas-liquid mixing, in Fluid Mixing I, Institution of Chemical Engineers Symposium Series 64, paper L1-L23.

    Google Scholar 

  • Harnby, N. (1967) A comparison of the performance of industrial solids mixers using segregating materials. Powder Technology, 1, 94–102.

    Article  Google Scholar 

  • Harnby, N. (1985) in Mixing in the Process Industries (eds N. Harnby, M.F. Edwards and A.W. Nienow), Butterworth, London, Ch. 3.

    Google Scholar 

  • Hoogendorn, C.J. and den Hartog, A.P. (1967) Model studies on mixers in the viscous flow region. Chemical Engineering Science, 22, 1689–1699.

    Article  Google Scholar 

  • Joshi, J.B., Pandit, A.B. and Sharma, M.M. (1982) Mechanically agitated gas-liquid reactors. Chemical Engineering Science, 37, 813–844.

    Article  CAS  Google Scholar 

  • Kay, J.M. and Nedderman, R.M. (1985) Fluid Mechanics and Heat Transfer, Cambridge University Press, Cambridge.

    Google Scholar 

  • Laufhutte, H.D. and Mersmann, A.B. (1985) Dissipation of power in stirred vessels, in Proceedings Fifth European Conference on Mixing, BHRA Fluid Engineering, Cranfield, paper 33, 331–340.

    Google Scholar 

  • Lee, J.C., Tasakorn, P. and Belghazi, A. (1984) Fundamentals of drop breakage in the formation of liquid-liquid dispersions, in Proceedings Institution of Chemical Engineers Symposium on Formation of Liquid-Liquid Dispersions, London.

    Google Scholar 

  • Mann, R. (1983) Gas-liquid contacting in mixing vessels. Institution of Chemical Engineers Research Fellowship report, Rugby.

    Google Scholar 

  • McManamey, W.J. (1979) Sauter mean and maximum drop diameters of liquid-liquid dispersions in turbulent agitated vessels at low dispersed phase hold up. Chemical Engineering Science, 34, 432–433.

    Article  CAS  Google Scholar 

  • Metzner, A.B. and Otto, R.E. (1957) Agitation of non-Newtonian fluids. American Institution of Chemical Engineers Journal, 3, 3–10.

    Article  CAS  Google Scholar 

  • Michel, B.J. and Miller, S.A. (1962) Power requirements of gas-liquid agitated systems. American Institution of Chemical Engineers Journal, 8, 262–271.

    Article  Google Scholar 

  • Middleton, J.C. (1985) in Mixing in the Process Industries (eds N. Harnby, M.F. Edwards and A.W. Nienow), Butterworth, London, Ch. 17.

    Google Scholar 

  • Nagata, S. (1975) Mixing. Principles and Applications, HaLsted Press, Tokyo.

    Google Scholar 

  • Nienow, A.W. (1968) Suspension of solid particles in turbine agitated baffled vessels. Chemical Engineering Science, 23, 1453–1459.

    Article  CAS  Google Scholar 

  • Nienow, A.W. (1985) in Mixing in the Process Industries (eds N. Harnby, M.F. Edwards and A.W. Nienow), Butterworth, London, Ch. 16.

    Google Scholar 

  • Nienow, A.W. and Elson, T.P. (1988) Aspects of mixing in Theologically complex fluids. Chemical Engineering Research and Design, 66, 16–21.

    Google Scholar 

  • Nienow, A.W. and Miles, D. (1968) The effect of impeller/tank configurations on fluid-particle mass transfer. Chemical Engineering Journal, 15, 13–24.

    Google Scholar 

  • Nienow, A.W., Wisdom, D.J. and Middleton, J.C. (1978) The effect of scale and geometry on flooding, recirculation and power in gassed, stirred vessels, in Second European Conference on Mixing, BHRA Fluid Engineering, Cranfield, pp. F1–F16.

    Google Scholar 

  • Poux, M., Fayolle, P., Bertrand, J. and Bridoux, D. (1991) Powder mixing: some practical rules applied to agitated systems. Powder Technology, 68, 213–234.

    Article  CAS  Google Scholar 

  • Prochazka, J. and Landau, J. (1961) Homogenisation of miscible liquids in the turbulent regime. Collection of Czech Chemical Communications, 26, 2961–2973.

    CAS  Google Scholar 

  • Revill, B.K. (1982) Pumping capacity of disc turbine agitators — a literature review. Fourth European Conference on Mixing, BHRA Fluid Engineering, Cranfield, paper R1, 11–24.

    Google Scholar 

  • Rielly, C.D. and Pandit A.B. (1988) Mixing of Newtonian liquids with large density and viscosity differences in mechanically agitated contactors, in Sixth European Conference on Mixing, BHRA Fluid Engineering, Cranfield, pp. 69–71.

    Google Scholar 

  • Rowe, P.N., Claxton, K.T. and Lewis, J.B. (1965) Heat and Mass transfer from a single sphere in an extensive flowing fluid. Transactions of the Institution of Chemical Engineers, 43, T14–T31.

    CAS  Google Scholar 

  • Smith, J.M. & Warmoeskerken, M.M.C.G. (1986) The dispersion of gases in liquids with turbines, in Fifth European Conference on Mixing, BHRA Fluid Engineering, Cranfield, paper 13, 115–126.

    Google Scholar 

  • Smith, J.M., Middleton, J.C. and van’t Riet, K. (1977) in Second European Conference on Mixing, BHRA Fluid Engineering, Cranfield, paper F4, 51–66.

    Google Scholar 

  • Streiff, F.A. (1979) Adapted motionless mixer design, in Third European Conference on Mixing, BHRA Fluid Engineering, Cranfield, pp. 171–188.

    Google Scholar 

  • Uhl, V.W. and Gray, J.B. (1966) Mixing Theory and Practice, Vols I and II, Academic Press.

    Google Scholar 

  • Van Dierendonck, L.L., Fortuin, J.M.H. and Venderbos, D. (1968) The specific contact area in gas-liquid reactors. Fourth European Conference on Chemical Reactor Engineering, pp. 205-215.

    Google Scholar 

  • Van’t Riet, K. and Smith, J.M. (1973) Chemical Engineering Science, 28, 1031.

    Article  CAS  Google Scholar 

  • Voit, H. and Mersmann, A.B. (1986) General statement for the minimum stirrer speed during suspension. German Chemical Engineering, 9, 101–106.

    Google Scholar 

  • Warmoeskerken, M.M.C.G. and Smith, J.M. (1984) The flooding transition with gassed Rushton turbines, in Fluid Mixing II, Institution of Chemical Engineers Symposium Series 89, 59-67.

    Google Scholar 

  • Wilkinson, W.L. and Cliff, M.J. (1977) An investigation into the performance of a static in-line mixer, in Proceedings Second European Conference on Mixing, BHRA Fluid Engineering, Cranfield, paper A2–A15.

    Google Scholar 

  • Zwietering, T.N. (1958) Suspending of solid particles in liquid by agitators. Chemical Engineering Science, 8, 244–253.

    Article  CAS  Google Scholar 

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© 1997 Springer Science+Business Media Dordrecht

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Rielly, C.D. (1997). Mixing in food processing. In: Fryer, P.J., Pyle, D.L., Rielly, C.D. (eds) Chemical Engineering for the Food Industry. Food Engineering Series. Springer, Boston, MA. https://doi.org/10.1007/978-1-4615-3864-6_10

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  • DOI: https://doi.org/10.1007/978-1-4615-3864-6_10

  • Publisher Name: Springer, Boston, MA

  • Print ISBN: 978-1-4613-6724-6

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