Continuing this from the other thread so as not to hijack.
Here is what I have so far, after making some adjustments based on advice already received.
Thanks to all in advance.
Hello everyone,
I'm working on a problem in which I am trying to recommend a hard pipe diameter to a customer for a (relatively) high viscosity non-newtonian fluid.
I am treating it as a power law fluid and have obtained constants K and n to describe the viscosity in relation to shear rate. I...
