Racing shock oil

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A non-Newtonian fluid is a fluid whose flow properties are not described by a single constant value of viscosity. Many polymer solutions and molten polymers are non-Newtonian fluids, as are many commonly found substances such as ketchup, starch suspensions, paint, blood and shampoo. In a Newtonian fluid, the relation between the shear stress and the strain rate is linear, the constant of proportionality being the coefficient of viscosity. In a non-Newtonian fluid, the relation between the shear stress and the strain rate is nonlinear, and can even be time-dependent.Therefore a constant coefficient of viscosity can not be defined. A ratio between shear stress and rate of strain (or shear-dependent viscosity) can be defined, this concept being more useful for fluids without time-dependent behavior.

Although the concept of viscosity is commonly used to characterize a material, it can be inadequate to describe the mechanical behavior of a substance, particularly non-Newtonian fluids. They are best studied through several other rheological properties which relate the relations between the stress and strain rate tensors under many different flow conditions, such as oscillatory shear, or extensional flow which are measured using different devices or rheometers. The properties are better studied using tensor-valued constitutive equations, which are common in the field of continuum mechanics.
 
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So you guys are saying that viscosity cannot be measured in a non-newtonian fluid ?

Must be the Hutchison effect.
 
what i'm saying is that you are not gonna get a measurement from blackstoned or any uoa shop because a hths setup can't do it.

to expand on this:

lets take a shock. any shock. don't have to be a bike shock.

now, if the viscosity of the fuild changes AS the speed of the shock shaft increases or decreases, please o please tell me how you measure that?
especially when blackstoned cant even do 2 voa's in the same month from the same bottle and come up with the same results!!!
 
Ditto what Shannow said.

The blender should have that sort of info on the TDS, a temp/viscosity/shear rate graph shouldn't be that hard, surely.
Even the viscous coupling fluid I've bought has a 'viscosity' on it to differentiate the different grades.
A non-newtonian fluid still has an apparent viscosity at a certain temp. How hard is that to print ?

An example.
In car dampers, transients (roll, squat, pitch) occur under 4"/sec.
Often times teams are measuring and controlling at 1"/sec or less. On a 'normal' shimmed stack damper this is all controlled by the bleeds.

If you have been using a fluid that gives you the forces you require at, say 80*C you really would like to know that the fluid you are about to tip in will still feed through the bleeds and not pack up, instantly opening the stack, or worse.
Conversely it may run through the bleeds like water, yet pack up the main stack at reasonable shaft speeds.
As a rebuilder, you'd really like to know where you are starting from.

If you have the funds and a dyno, you might just buy the stuff and run it and if it hydraulics the damper on the dyno, well, so be it, but not everyone can afford that approach.
 
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