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By C. M. Rodkiewicz (eds.)

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E. the fluid ap- pears as newtonian. e. a newtonian behaviour. 4D) will involve the same characteristic timeT (as a relaxation time for thixotropic buildup of the structure at y= 0) since nr = nr ( tr) in this case. In fact, critical tube Reynolds number, pVR/n is found 1 at least two orders in magnitude lower than the usual critical value for ordinary fluids. In the case of more complex systems, each additional variable requires a new dimensionless variable in the viscosity equation, as shown in the following examples.

A brief survey of the operating principles and main characteristics of usual viscometers will follow. 3 Viscometry Steady measurements of blood rheological properties concern mainly its shear viscosity. Two types of viscometers are currently used, capillary (tube) viscometers and rotational viscometers. A. Tube viscometers Fluid flows down a tube from a reservo~r. 1). Onerecords the time interval during which a fixed volume of fluid flows through the tube under a given pressure gradient P = ~p/L.

It must be kept in mind that this actual packing $p will be usually different from the true one, $M , owing to structural modifications which would occur during the (true) rising of the tion. Therefore, the ~p ( ~M) = ~M $-dependent value , $p =$p($) concentr~ must verify • It appears closely related to the inverse of the "ralati ve sediment volume", as ROBINSON (1949) introduced. The previous detailed discussion has been given to stress on (i) the large applicability of eq. 20) as a very simple viscosity equation, 44 D.

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