
Brookeld Engineering Laboratories, Inc. Page 104 Manual No. M98-211-E0912
In taking viscosity measurements with the DV-III Ultra Rheometer there are two considerations which
pertain to the low viscosity limit of effective measurement.
1) Viscosity measurements should be accepted within the equivalent % Torque Range from
10% to 100% for any spindle/speed combination.
2) Viscosity measurements should be taken under laminar ow conditions, not under turbulent
ow conditions.
The rst consideration has to do with the precision of the instrument. All DV-III Ultra Rheometers
have a full scale range precision of (+/-) 1% of any spindle/speed combination. We discourage taking
readings below 10% of range because the potential viscosity error of (+/-) 1% is a relatively high number
compared to the instrument reading.
The second consideration involves the mechanics of uid ow. All rheological measurements of
uid ow properties should be made under laminar ow conditions. Laminar ow is ow wherein all
particle movement is in layers directed by the shearing force. For rotational systems, this means all uid
movement must be circumferential. When the inertial forces on the uid become too great, the uid can
break into turbulent ow wherein the movement of uid particles becomes random, and the ow can
not be analyzed with standard math models. This turbulence creates a falsely high Rheometer reading,
with the degree of non-linear increase in reading being directly related to the degree of turbulence in
the uid.
For the following geometries, we have found that an approximate transition point to turbulent ow
occurs:
1) No. 1 LV Spindle: 15 cP at 60 RPM
2) No. 1 RV Spindle: 100 cP at 50 RPM
3) UL Adapter: 0.85 cP at around 70 RPM
4) SC4-18/13R: 1.25 cP at around 240 RPM
Turbulent conditions will exist in these situations whenever the RPM/cP ratio exceeds the values listed
above. The viscosity at which turbulence starts is still at best a guess. Because it is a relationship
between viscous and inertial forces, it can vary dramatically from uid to uid. Turbulence starts as a
small deviation or increase in viscosity for a Newtonian uid and grows quickly. Basically there is no
specic shear that it starts at, only an approximate region of shear depending on the uid.
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