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Brookfield DV-III Ultra Rheometer User Manual

Page 30

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Brookfield Engineering Laboratories, Inc.

Page 30

Manual No. M98-211-E0912

III.3 Selecting a Spindle/Speed

The DV-III Ultra has the capability of measuring viscosity over an extremely wide range (for example,

the RVDV-III Ultra can measure fluids within the range of 100-40,000,000 cP) (see Appendix B).

This range is achieved through the use of several spindles over many speeds. When measuring

yield stress with vane spindles, a broad measurement range is also possible through the choice of

multiple spindles.

The process of selecting a spindle and speed for an unknown fluid is normally trial and error. An

appropriate selection will result in measurements made between 10-100 on the instrument %

torque scale. Two general rules will help in the trial and error process.

1) Viscosity range is inversely proportional to the size of the spindle.

2) Viscosity range is inversely proportional to the rotational speed.

In other words: to measure high viscosity, choose a small spindle and/or a slow speed. If the chosen

spindle/speed results in a reading above 100%, then reduce the speed or choose a smaller spindle.

Experimentation may reveal that several spindle/speed combinations will produce satisfactory results

between 10-100%. When this circumstance occurs, any of the spindles may be selected.

Non-Newtonian fluid behavior can result in the measured viscosity and yield stress changing if the

spindle and/or speed is changed. See our publication, "More Solutions to Sticky Problems," for

more detail.

When viscosity and/or yield stress data must be compared, be sure to use the same test

methodology: namely the same instrument, spindle, speed, container, temperature and test

time.

III.4 Multiple Data Points

The majority of viscosity and yield stress measurements are made at the quality control level and

often consist of a single data point. The test is conducted with one spindle at one speed. The data

point is a useful bench mark for the go/no-go decision in a production setting. The DV-III Ultra

can be used for single point measurement.

Many fluids exhibit a characteristic change in viscosity and yield stress with a change in applied

force. This non-Newtonian flow behavior is commonly seen in paints, coatings and food products

as a decrease in viscosity as shear rate increases or an increase in yield stress as rotational speed

increases. This behavior cannot be detected or evaluated with the single point measurement.

Non-Newtonian flow is analyzed through the collection of viscosity data over a range of shear

rates and the generation of a graph of viscosity versus shear rate (a rheogram). The same applies to

yield stress determination by analyzing torque vs. time behavior at different rotational speeds. This

information will allow for a more complete characterization of a fluid and may help in formulating

and production of the product. The DV-III Ultra is capable of collecting multiple data points for

comprehensive analysis of flow behavior. See Section IV on Programming and Analysis.

More information on flow behavior, shear rate and rheograms is available in our publication, "More

Solutions to Sticky Problems."