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The dual Viscometer Method:
This method is based on the use of the ASTM D341 equation for temperature Vs viscosity:
Log10.log10(+0.7) = A-
Where is the kinematic viscosity (cst) at temperature TC.
To solve the equation the values of “A” and “B” must both be found as they usually vary significantly, even with small changes in quality.
The values of “A” and “B” can be found by substituting the viscosity of the fluid at two different temperatures.
Once “A” and “B” are known the equation can then be solved to find the viscosity at the reference temperature.
How it Works:
In this method, two viscometers are used, each measuring the viscosity at a different temperature by virtue of an intervening heat exchanger.
The values of “A” and “B” are determined in real time and at each calculation up-
It is quite independent of any variation in fluid properties as there are no assumptions
to be made. It is especially suitable for lubricating oils, for example, where the
different Viscosity Index Values from one oil to another preclude using the equation
This system provides accurate base viscosity determination with a typical control response of less than 20 seconds.
In process control the degree to which quality can be controlled depends on two factors,
the accuracy of the measurement which in this case is comparable to the process capillary
viscosity analyser, and the speed of the control response. In this case the speed
of response is much better than the capillary system for so long the oil industry
standard and this means that quality can be more accurately controlled with significant
savings in “give-
It can deliver a high level of confidence in the measurement with minimal operator or instrument engineer intervention.
Indeed, this method can be used where all that is known is that the fluids are hydrocarbons.
In refinery operations this system can be very powerful.
Of all the methods available this is the most universal in application.
There are very few limitations on this method.
However, although the most universally applicable solution, because it is more complex, it is not usual to consider it where other solutions are viable except where the cost to benefit ratio justifies its use.
It is generally the scale of operations in refineries and in large terminals or where high value refined products are to be measured (such as lubricants) that provide the optimum cost to benefit ratios.
A dual viscometer using an electric heater to increase the fluid temperature to the second viscometer.
This system was designed for a crude oil cut-
A schematic of the installation.