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August 15, 2003, 13:56 |
Multiphase non-Newtonian Flow
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#1 |
Guest
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Hi there,
(CFX 5.6 User ) I am simulating a mixture of one continuous phase (water) and two dispersed solid phasees. Definitely the viscosity of the mixture is dependent on the concentration of two dispersed solid phases. It also is a function of shear rate. For simplicity, I want to try power law model first. But I can not understand how the viscosity of mixture is calculated in CFX particle model. In Fluid Detail, I have to assign the viscosity of both continuous phase and dispersed phase. If I tend to set the power law model for mixture, should I set it for continuous phase or dispersed phases because nowhere can the viscosity of the mixture be assigned in CFX 5.6. Thank you in advance! Jingo |
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September 7, 2003, 06:41 |
Re: Multiphase non-Newtonian Flow
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#2 |
Guest
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dear Jingo for the cfd simulation reguarding the non newtonian fluids with the solid phase as a dispersed or the contineous phase , you can use the fluent software for cfd simulation since whatever the problem u r facing u can get it from fluent.
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September 8, 2003, 10:47 |
Re: Multiphase non-Newtonian Flow
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#3 |
Guest
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Hi Jingo,
The effective viscosity of the mixture will already vary due to the presence of the additional dispersed phases as a result of their momentum transport. Do you expect the viscosity of the individual phases to actually change? -Robin |
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