good day
I need you assistance to calculate oil viscosity at 100 C. i have the viscosity of it at 90 C which is 13.5 cST. the specific gravity of mixture is 1.003. Is there a correlation to calculate viscosity if temperature available
thanks
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Posted 21 March 2017 - 06:00 AM
good day
I need you assistance to calculate oil viscosity at 100 C. i have the viscosity of it at 90 C which is 13.5 cST. the specific gravity of mixture is 1.003. Is there a correlation to calculate viscosity if temperature available
thanks
Posted 21 March 2017 - 12:43 PM
Relation between viscosity and temperature depends on the nature of the oil.
An oil with a s.g. of 1.003 and a viscosity of only 13.5 cSt at 90 oC does not look like a common petroleum oil.
What kind of oil is this?
Posted 21 March 2017 - 11:02 PM
Hi Sir
Its pyrolysis fuel oil. its coming from hydrocarbon paraffin cracking.
thanks
Posted 22 March 2017 - 01:39 AM
gentlemen
I found two viscosity points at two deferant temperature which is as follows
1.13.9 cP at temperature of 90 C
2. 8.83 cP at temperature of 138 C
what I need the viscosity at 100 C
Posted 22 March 2017 - 03:26 AM
For hydrocarbons you can use the ASTM D341 equations or graphs.
JMW has made a spreadsheet available for the calculation:
https://www.cheresou...ity-calculator/
Note however that the ASTM D341 method works with cSt, not cP.
So if you have viscosities in cP as in post #4 then you first convert them to cSt using the SG at the indicated temperatures..
The calculated viscosity at 100 oC is then also in cSt so if you need it to be in cP you have to convert it to cP using the SG at 100 oC.
Posted 22 March 2017 - 03:40 AM
alhamees,
you should have (or estimate) density (or cst) at the 2nd temperture....then you can draw a line
you can easily find the relevant equations/excel files
good luck
Posted 22 March 2017 - 04:39 AM
The graph that gegio posted is from ASTM D341.
Using the graph is easy: just plot the available viscosity points (in cSt) and draw a straight line through them.
The formulas, like in JMW's spreadsheet are more accurate.
In this particular case one could also look at the numbers and say:
hmmm, the viscosity at 100 oC must about 13
Posted 22 March 2017 - 04:50 AM
Alhamees,
Not knowing densities at different temperature, the dynamic viscosity can be estimated from the Arrhenius-type model equation: (http://www.academicj...312_Stanciu.pdf)
ln μ1 = A + B ln T1...(1)
ln μ2 = A + B ln T2...(2)
----------------------------------
ln(μ1/μ2) = B ln(T1/T2) ==> B = ln (μ1/μ2) / ln(T1/T2) ....(3)
A =ln μ1 - B ln T1 = ln μ1 - {ln (μ1/μ2) / ln(T1/T2)} ln T1 or A = ln μ2 - B ln T2 = ln μ2 - {ln (μ1/μ2) / ln(T1/T2)} ln T2 ....(4)
Therefore,
ln μ3 = A + B ln T3...(5)
= ln μ1 - {ln (μ1/μ2) / ln(T1/T2)} ln T1 + {ln (μ1/μ2) / ln(T1/T2)} ln T3 or = ln μ2 - {ln (μ1/μ2) / ln(T1/T2)} ln T2 + {ln (μ1/μ2) / ln(T1/T2)} ln T3
=ln μ1 -{ln (μ1/μ2) / ln(T1/T2)} ln (T1/T3) or = ln μ2 -{ln (μ1/μ2) / ln(T1/T2)} ln (T2/T3) ......(5)
Then
μ3 = exp { ln μ1 -{ln (μ1/μ2) / ln(T1/T2)} ln (T1/T3) } or = exp { ln μ2 -{ln (μ1/μ2) / ln(T1/T2)} ln (T2/T3) }
=μ1 * (T3/T1)^{ ln (μ1/μ2) / ln(T1/T2)} or = μ2 * (T3/T2)^{ ln (μ1/μ2) / ln(T1/T2)} .................(6)
Use dynamic viscosities[Pa*s] for μ1, μ2, μ3 and absolute temperatures[K] for T1, T2, and T3. If you have a log-log sheet, simply locate the previous known data (ln T1, ln μ1) and (ln T2, ln μ2) and connect the two points then find (ln T3, ln μ3) on the straight line (ln μ = A + B ln T).
~ Stefano Kim
Edited by sgkim, 23 March 2017 - 01:52 AM.
Posted 22 March 2017 - 03:16 PM
Hi Alameehs
For your question, use the API Procedure 11A4.1 to calculate the viscosity knowing only one viscosity.
The procedure uses the viscosity in cSt at 100°F.
For your case, I use some tricks for get the viscosity at 100°F, and then with this value I calculate the viscosity at temperature needed of 212 °F (100°C)
Attached the excel file for that. Review the worksheet and try to repeat the procedure that I follow and the PDF file for API procedure 11A4.1
Source: API - Petroleum Refining Technical Data Book pag 11-33 to 11-34.
Good luck
Fausto.
Edited by Profe, 23 March 2017 - 07:56 AM.
Posted 23 March 2017 - 12:29 AM
Thank you very much all of for your help and valuable information that you provide me
Posted 24 March 2017 - 12:05 PM
Alameehs,
I attached related information, from the book Heat Transfer Design Methods by John McKetta.
Napo.
Posted 25 March 2017 - 02:35 AM
Hi ,
The dynamic viscosity ( Po or CPO) should follow this type of model : ln (mu) = A+B/T with mu the dynamic viscosity and T temp in Kelvins .
The coefficients A.B should be identified if you have data to support at 2 different temperature.
In the case you only have the cinematic viscosity you need to get access to the density at the same temperature :
nu (St or Cst) = mu /density .
Hope this helps,
Breizh
Edited by breizh, 25 March 2017 - 02:36 AM.
Posted 06 April 2017 - 01:47 AM
Thank you very much all of you for your assistance
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