Brookfield DV-III Ultra Rheometer Manual de usuario Pagina 104

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Brookeld 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
specic shear that it starts at, only an approximate region of shear depending on the uid.
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