HOW TO MEASURE POWER REQUIREMENTS FOR AGITATION OF NON-NEWTONIAN LIQUIDS IN THE LAMINAR REGION

[1] Calderbank P. H., 1959, T I CHEM ENGRS LONDO, V37, P26, DOI [10.1016/j.cherd.2017.01.018, DOI 10.1016/J.CHERD.2017.01.018]

[2] The flow due to a rotating disc. [J]. PROCEEDINGS OF THE CAMBRIDGE PHILOSOPHICAL SOCIETY, 1934, 30 : 365 - 375

[3] DUNCAN WJ, 1953, PHYSICAL SIMILARITY, P72

[4] DIRECT DETERMINATION OF THE FLOW CURVES OF NON-NEWTONIAN FLUIDS .2. SHEARING RATE IN THE CONCENTRIC CYLINDER VISCOMETER [J]. JOURNAL OF APPLIED PHYSICS, 1953, 24 (02) : 134 - 139

[5] LEE ER, 1957, IND ENG CHEM, V49, P1849

[6] LYONS EJ, 1948, CHEM ENG PROG, V44, P341

[7] NORMAL STRESS EFFECT IN POLYISOBUTYLENE SOLUTIONS .1. MEASUREMENTS IN A CONE AND PLATE INSTRUMENT [J]. TRANSACTIONS OF THE SOCIETY OF RHEOLOGY, 1957, 1 : 25 - 36

[8] AGITATION OF NON-NEWTONIAN FLUIDS [J]. AICHE JOURNAL, 1957, 3 (01) : 3 - 10

[9] METZNER AB, 1958, AICHE ANN M CINCINNA

[10] REINER M, 1949, DEFORMATION FLOW

[1] Calderbank P. H., 1959, T I CHEM ENGRS LONDO, V37, P26, DOI [10.1016/j.cherd.2017.01.018, DOI 10.1016/J.CHERD.2017.01.018]

[2] The flow due to a rotating disc. [J]. PROCEEDINGS OF THE CAMBRIDGE PHILOSOPHICAL SOCIETY, 1934, 30 : 365 - 375

[3] DUNCAN WJ, 1953, PHYSICAL SIMILARITY, P72

[4] DIRECT DETERMINATION OF THE FLOW CURVES OF NON-NEWTONIAN FLUIDS .2. SHEARING RATE IN THE CONCENTRIC CYLINDER VISCOMETER [J]. JOURNAL OF APPLIED PHYSICS, 1953, 24 (02) : 134 - 139

[5] LEE ER, 1957, IND ENG CHEM, V49, P1849

[6] LYONS EJ, 1948, CHEM ENG PROG, V44, P341

[7] NORMAL STRESS EFFECT IN POLYISOBUTYLENE SOLUTIONS .1. MEASUREMENTS IN A CONE AND PLATE INSTRUMENT [J]. TRANSACTIONS OF THE SOCIETY OF RHEOLOGY, 1957, 1 : 25 - 36

[8] AGITATION OF NON-NEWTONIAN FLUIDS [J]. AICHE JOURNAL, 1957, 3 (01) : 3 - 10

[9] METZNER AB, 1958, AICHE ANN M CINCINNA

[10] REINER M, 1949, DEFORMATION FLOW