Hi!
We are going to install a number of pipelines in my facility which will handle a non-newtonian fluid, with lowering viscosity at increasing shear rates.
I am reviewing pressure drop calculations performed in the system, and I am not sure about the pressure drop calculation method that has been used. I would appreciate it if someone could give me a literature reference where I can find the formulas to calculate pressure drop over a pipeline for non-newtonian fluids.
I am very interested as well in seeing a comparison of the pressure drop over a pipeline for newtonian and non-newtonian fluids.
I have found a spreadsheet in the forum for this purpose, but it is locked and it gives me some trouble in the new excel version, and therefore I cannot use it either.
Any help is appreciated!
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Non-Newtonian Fluids' Pressure Drop Calculation
Started by herrani, Sep 13 2012 07:25 AM
4 replies to this topic
Share this topic:
#1
Posted 13 September 2012 - 07:25 AM
#2
Posted 13 September 2012 - 04:35 PM
I use Non-Newtonian Flow and Heat Transfer by A. H. P. Skelland.
#3
Posted 01 December 2012 - 02:19 PM
@herrani
Hope below attached copy helps you.
http://www.eng-tips.....cfm?qid=177111
Regards
Shivshankar
Hope below attached copy helps you.
http://www.eng-tips.....cfm?qid=177111
Regards
Shivshankar
Attached Files
Edited by Shivshankar, 01 December 2012 - 02:32 PM.
#4
Posted 01 December 2012 - 08:45 PM
From internet:
http://www.google.fr...iw=1121&bih=592
Breizh
http://www.google.fr...iw=1121&bih=592
Breizh
Edited by breizh, 01 December 2012 - 08:47 PM.
#5
Posted 02 December 2012 - 05:39 AM
Fyi, OP has not been active since Oct. 3.
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