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Estimating Liquid Mixture Viscosity


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#1 alex91ro

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Posted 17 January 2017 - 03:47 PM

Hello,

 

 

Is there any reliable correlation for estimating the viscosity of a blend? I read about Refutas, Kendal-Monroe, Chevron correlation and others but I have no idea which one give better results, I didn't find anything about a range of viscosities where they are efficient.

 

Thank you! 

 

(PS: I hope you can understand my bad English)

 



#2 Art Montemayor

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Posted 17 January 2017 - 09:50 PM

When trying to estimate a liquid's viscosity in the past I always arrived at the unfortunate conclusion that there is no reliable method to estimate the viscosity of a pure liquid.  Only very approximate empirical rules were available.  Perhaps this has improved markedly in recent times, but I doubt it.  From a good and detailed explanation on the subject as well as sample calculations and results, go to:  http://www.owlnet.ri.../proj02/beckys/

 

Additionally, you can read the material found in Wikipedia: https://en.wikipedia...ends_of_liquids



#3 alex91ro

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Posted 18 January 2017 - 02:32 AM

So the only solution is to make several blends and see what proportions give the desired viscosity?

#4 latexman

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Posted 18 January 2017 - 07:55 AM

That will work.



#5 gegio1960

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Posted 18 January 2017 - 10:41 AM

Alex, once acknowledged Art's valuable words I'd like to add my 2 cents of experience in the (limited) oil refining world.

Since you're asking about blending rules and their best ranges of application, you can use the following:

- refutas for residual fuel oils

- chevron correlation for ligher cuts (eg gasoils)

Good luck!



#6 Profe

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Posted 18 January 2017 - 12:06 PM

Hi Alex

For your question, use procedure API 11A4.5: Liquid viscosity blending of hydrocarbon mixtures.



#7 alex91ro

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Posted 18 January 2017 - 12:50 PM

gegio1960:

 

This equations are giving almost similar results, Chevron is always a little higher.  The problem is that Kendal-Monroe equation gives higher values of the mixture viscosity (2-3 x results of Refutas/Chevron) when there are big differences between the viscosities of the two liquids: Liquid 1 under 20 cst + Liquid 2 over 500 cst.  Which numbers are better?

 

 

@Profe

Do you have link? I can't find it.

 

 

Thank you all for your answers.



#8 gegio1960

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Posted 18 January 2017 - 11:36 PM

Alex, with reference to #7

- This equations are giving almost similar results   YES, THAT'S GOOD

- The problem is that Kendal-Monroe equation gives higher values    DON'T USE IT



#9 Profe

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Posted 19 January 2017 - 08:17 AM

Alex

 

Review a mesage that I send you about the  API procedure. Study it and review its aplication example

 

And attached I send an example of this method.

 

I Hope this will be useful.

 

Fausto.

Attached Files






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