Viscosity is the property of a fluid to resist the relative displacement of adjoining layers (internal friction). It is necessary to differentiate between dynamic and kinematic viscosity. The physical definition of viscosity originates in the NEWTONian formulation of shear stress (NEWTONian liquid).
The viscosity curve in the shear stress diagram (τ = f(∂vx/∂y)) is, therefore, a line through the origin, see Fig. 1 Pulp pumping. All other curves denote non-NEWTONian liquids handled in pulp pumping applications, whose effects on the operation of centrifugal pumps cannot easily be calculated by the usual methods.
However, in practice it is normal to specify the viscosity-density ratio (kinematic viscosity).
The SI unit of dynamic viscosity is Ns/m2 = Pas, the SI unit of kinematic viscosity is m²/s.
The term "dynamic viscosity" is derived from the Greek "dynamis", which means force, since the SI unit contains a unit of force (N). The SI unit for kinematic viscosity, on the other hand, contains only kinematic dimensions for length (m) and time (s).
The dependence of kinematic viscosity ν on temperature t is shown both for water,
see Fig. 1 under Vapour pressure,
and for mineral oil distillates; with the axes being partitioned in such a way as to provide straight lines. See Fig. 1 Viscosity
As the temperature increases, almost all liquids become thinner, i.e. their viscosity decreases. See Fig. 2 Viscosity
Dynamic viscosity η can be measured for all liquids using a rotational viscometer, in order to record the viscosity curve, as follows: a cylinder with freely^selectable rotational speed rotates in a cylindrical pot filled with the liquid to be tested. Drive torque, circumferential speed, the size of the wetted cylinder surface and the wall clearance in the pot are measured at several rotational speeds. Viscometry also includes other processes, e.g. falling sphere and flow measuring methods.
Effect on the characteristic curves of pumps
The characteristic curves of centrifugal pumps show noticeable effects only at a kinematic viscosity of
ν > 20 ·10 –6 m2/s and must be converted using empirically calculated conversion factors only after this limit is reached. The two most well-known techniques are those according to the Standards of the Hydraulic Institute (HI) and according to KSB. Both techniques use diagrams to illustrate the conversion factors, which - though they are used in a similar way - differ in that the KSB technique includes the influencing variables Q , H and ν as well as being clearly influenced by the specific rotational speed ns in addition. The HI technique, see Fig. 3 Viscosity
was measured only at ns = 15 to 20 rpm and, in this narrow application range, leads to similar results to the KSB technique see Fig. 4 Viscosity, which was measured in the ns range from 6.5 to 45 rpm and at viscosities of up to νz = 4000 · 10–6 m2/s. The use of the two diagrams is explained by means of the depicted examples.
The capacity Q, the head H and the efficiency η of a single-stage centrifugal pump, which are known for operation with water (subscript W), can now be converted for operation with a viscous liquid (subscript Z) as follows:
The f factors are called k in the HI technique; both are illustrated graphically in Figures 3 and 4; in Fig. 4 Viscosity, in addition, the pump rotational speed n must be read in and the specific rotational speed ns of the pump impeller must be known.
With these factors, the operating data known for water mode can then be converted for liquids of a higher viscosity; the conversion applies in the load range:
0.8 Qopt < Q < 1.2 Qopt
Thus simplified at three flow rates 0.8 and 1.0 and 1.2 Qopt, with the only exception:
Q = 0.8 Qopt For Hz = 1.03 • fH • HW
t flow rate Q = 0, put simply:
Hz = Hw and ŋz =ŋw = 0
A calculation scheme simplifies the conversion. See Fig. 5 Viscosity
all characteristic curves can then each be plotted from either 4 or 3 calculated points over Qz. See Fig. 6 Viscosity
If the terms of reference are reversed so that it is not the water values that are given, but the data for operation with a higher-viscosity liquid (e. g. to determine a suitable pump for a required duty point), the water values are first estimated and the solution is then approximated using the conversion factorsfQ , fH and fη iteratively in two (or, if necessary, three) steps.
Above a specific rotational speed of ns ≈ 20 rpm, the better adapted KSB calculation technique leads to lower drive ratings; below this limit the drive ratings calculated according to HI are too small!
Effect on the characteristic curves of the system
Since all hydrodynamic laws remain valid without restriction for NEWTONian liquids, all the calculation formulae and diagrams for the pipe friction coefficients and for the loss coefficients in valves also continue to apply. It is only when calculating the REYNOLDS number Re = v · d/ν that, instead of the kinematic viscosity νw of water, νz, that of the respective higher-viscosity liquid must now be used, resulting in a lower Re number and consequently a greater pipe friction coefficient λz (see also head losses).