aali94
Mechanical
- Oct 28, 2013
- 9
Hi,
I am trying to model the sloughing of paraffin wax deposits from the walls of oil pipelines due to the flow of crude oil. One of the parameters I require is the interfacial tension between crude oil and the wax deposit. I have varied the interfacial tension in my CFD simulations from 10 to 1000 mN/m. The results show that low surface tension values result in a wavy surface, while high surface tension does not produce a wavy surface (see attachment). However, I have not been able to find any values in literature for the interfacial tension between oil and solid wax. I have found that the interfacial tension between oil and water can only be as high as 50 dyn/cm. Could you please let me know what values of surface tension I should be using.
Also, I am modelling the wax as a highly viscous fluid with a viscosity of 100,000 cP. I am not sure if this is the best way to model wax sloughing. I am modelling the crude oil as a Newtonian fluid above the Wax Appearance Temperature (WAT) with two viscosities: 4.3 cP and 29.5 cP. Below the WAT I am modelling the crude oil as a shear thinning fluid with a behaviour index of 0.6.
I would be grateful if you could provide any insight?
I am trying to model the sloughing of paraffin wax deposits from the walls of oil pipelines due to the flow of crude oil. One of the parameters I require is the interfacial tension between crude oil and the wax deposit. I have varied the interfacial tension in my CFD simulations from 10 to 1000 mN/m. The results show that low surface tension values result in a wavy surface, while high surface tension does not produce a wavy surface (see attachment). However, I have not been able to find any values in literature for the interfacial tension between oil and solid wax. I have found that the interfacial tension between oil and water can only be as high as 50 dyn/cm. Could you please let me know what values of surface tension I should be using.
Also, I am modelling the wax as a highly viscous fluid with a viscosity of 100,000 cP. I am not sure if this is the best way to model wax sloughing. I am modelling the crude oil as a Newtonian fluid above the Wax Appearance Temperature (WAT) with two viscosities: 4.3 cP and 29.5 cP. Below the WAT I am modelling the crude oil as a shear thinning fluid with a behaviour index of 0.6.
I would be grateful if you could provide any insight?