EVALUATING SHEAR RATES FOR POWER LAW FLUIDS IN MIXER VISCOMETRY

被引:27
作者
CASTELLPEREZ, ME
STEFFE, JF
机构
[1] MICHIGAN STATE UNIV,DEPT AGR ENGN,E LANSING,MI 48824
[2] MICHIGAN STATE UNIV,DEPT FOOD SCI & HUMAN NUTR,E LANSING,MI 48824
关键词
D O I
10.1111/j.1745-4603.1990.tb00493.x
中图分类号
TS2 [食品工业];
学科分类号
0832 ;
摘要
Established mixer viscometry methods, the viscosity matching and the slope methods, were evaluated for determining average shear rates when agitating time-independent, non-Newtonian fluids. Results indicate that the use of a constant value of the mixer proportionally constant, k', is not valid for all ranges of fluid rheological properties, system geometry (impeller and cup) and impeller rotational speed. A small impeller-to-cup diameter ratio and impeller rotational speeds greater than .33 rev/s (20 rpm) provide the optimum operating parameters for evaluation of k'.
引用
收藏
页码:439 / 453
页数:15
相关论文
共 13 条
  • [1] BECKNER JL, 1966, TRANS INST CHEM ENG, V44, pT224
  • [2] CALDERBANK PH, 1961, T I CHEM ENG-LOND, V39, P338
  • [3] CASTELLPEREZ ME, 1990, THESIS MICHIGAN STAT
  • [4] CASTELLPEREZ ME, 1991, VISCOELASTIC PROPERT, pCH10
  • [5] EFFECTS OF SHEAR-THINNING BEHAVIOR ON MIXER VISCOMETRY TECHNIQUES
    MACKEY, KL
    MORGAN, RG
    STEFFE, JF
    [J]. JOURNAL OF TEXTURE STUDIES, 1987, 18 (03) : 231 - 240
  • [6] MAGNUSSON K, 1952, IVA, V23, P86
  • [7] AGITATION OF NON-NEWTONIAN FLUIDS
    METZNER, AB
    OTTO, RE
    [J]. AICHE JOURNAL, 1957, 3 (01) : 3 - 10
  • [8] Nagata S., 1975, MIXING PRINCIPLES AP
  • [9] RAO M A, 1975, Journal of Texture Studies, V6, P533
  • [10] Rao M. A., 1984, Journal of Texture Studies, V15, P327, DOI 10.1111/j.1745-4603.1984.tb00390.x