By R.P. Chhabra and J.F. Richardson (Auth.)
, Pages xi-xiii
, Page xv
Chapter 1 - Non-Newtonian fluid behaviour
, Pages 1-36
Chapter 2 - Rheometry for non-Newtonian fluids
, Pages 37-72
Chapter three - circulate in pipes and in conduits of non-circular cross-sections
, Pages 73-161
Chapter four - stream of multi-phase combos in pipes
, Pages 162-205
Chapter five - Particulate systems
, Pages 206-259
Chapter 6 - warmth move features of non-Newtonian fluids in pipes
, Pages 260-288
Chapter 7 - Momentum, warmth and mass move in boundary layers
, Pages 289-323
Chapter eight - Liquid mixing
, Pages 324-392
, Pages 393-421
, Pages 423-436
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Extra info for Non-Newtonian Flow in the Process Industries. Fundamentals and Engineering Applications
Both types are usually supplied with the same range of measuring geometries, principally the concentric cylinder, cone-and-plate and parallel plate systems. , see Waiters, 1975; Whorlow, 1992; Macosko, 1994) and so only their most basic aspects are covered here. 1 The concentrfc cylinder geometry It is appropriate to begin by considering this geometry as it was the basis of the first practical rotational rheometer. 3). Typically the outer 'cup' rotates and the torque T on the inner cylinder, which is usually suspended from a torsion wire or bar, is measured.
Engineering Rheology. Oxford University Press, Oxford (1988). I. , Rheology: An Historical Perspective, Elsevier, Amsterdam (1998). Tirtaatmadja, V. , J. Rheol. 37 (1993) 1081. , Proc. Roy. Soc. AT/(1906) 426. , Rheometry. Chapman and Hall, London (1975). , Nature 159 (1947) 310. 1 Introduction The rheological characterisation of non-Newtonian fluids is widely acknowledged to be far from straightforward. In some non-Newtonian systems, such as concentrated suspensions, theological measurements may be complicated by non-linear, dispersive, dissipative and thixotropic mechanical properties; and the rheometrical challenges posed by these features may be compounded by an apparent yield stress.
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