By R.P. Chhabra and J.F. Richardson (Auth.)
Content material:
Preface
, Pages xi-xiii
Acknowledgements
, Page xv
Chapter 1 - Non-Newtonian fluid behaviour
, Pages 1-36
Chapter 2 - Rheometry for non-Newtonian fluids
, Pages 37-72
Chapter three - circulation in pipes and in conduits of non-circular cross-sections
, Pages 73-161
Chapter four - move of multi-phase combinations 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
Problems
, Pages 393-421
Index
, Pages 423-436
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Additional info for Non-Newtonian Flow in the Process Industries. Fundamentals and Engineering Applications
Example text
Fluid Mech. 27 (1995) 169. , Levan, J. N. AIChEJ. 36 (1990) 321. , J. Non. Newt. Fluid Mech. 3 (1976) 87. , Nature 265 (1977) 126. V. , Rheo/ogical Phenomena in Focus. Elsevier, Amsterdam (1992). , Trans. Soc. Rheol. 16 (1972) 99. , Dekee, D. , Rheology of Polymeric Systems: Principles and Applications. Hanser, Munich (1997). , J. Rheol. 36 (1992) 1313. Freundlich, H. , Trans. Faraday Soc. 31 (1935) 920. D. I. Longman, London (1990) Chapter 2. W. , The Flow of Complex Mixtures in Pipes. Krieger, Malabar, FL (1982).
60%) solids volume fraction, and can involve fluctuating torque in a rotational viscometer under steady Rheometry for non-Newtonian fluids 53 rotation [Cheng and Richmond, 1978; Cheng, 1986]. Given that conventional smooth walled rotational devices tend to slip when in contact with many systems which display an apparent yield stress, several workers have adopted the vane measuring geometry [Nguyen and Boger, 1985]. Typically, the vane geometry consists of a small number (usually 4) of thin blades arranged around a cylindrical shaft of small diameter.
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