CFD Online Discussion Forums

CFD Online Discussion Forums (https://www.cfd-online.com/Forums/)
-   FLUENT (https://www.cfd-online.com/Forums/fluent/)
-   -   superficial velocity (https://www.cfd-online.com/Forums/fluent/36238-superficial-velocity.html)

Taskin April 2, 2005 05:48

superficial velocity
 
hi,

I couldn't find what the exact difference between superficial velocity and physical velocity is. Fluent user guide 6.1 always defines it using porous medium, however my model do not consist of any porous medium. Moreover physical velocity condition gives a much better solution when compared to superficial. can anyone make a short description of their difference?

Thanks for any help

Taskin

ap April 2, 2005 15:18

Re: superficial velocity
 
The superficial velocity in a monophasic flow is equal to its mean velocity, while in multiphase flows it's defined as the ratio of the velocity and the volume fraction of the considered phase in a multiphase system.

Best regards, ap

pUl| April 3, 2005 00:31

Re: superficial velocity
 
ap is right. However, some people prefer to call it as the "Actual velocity" of a phase.

For Instance:

Actual velocity of gas phase = (Superficial velocity of gas phase) / (volume fraction of gas phase)

When you feed velocities and a guess for the volume fraction for a phase in fluent, you use the above equation to determine the 'Actual velocity' and enter this in the "Velocity inlet" panel. For the dispersed phase volume fraction you will have to enter the volume fraction guess that you used to calculate 'Actual velocity'.

Taskin April 3, 2005 17:00

Re: superficial velocity
 
hi, you mean in superficial velocity, it doesn't make a varying velocity distrubution along the cross section. It just takes a mean value, but physical velocity models the real situtation, I mean varying velocity distribution. did I understand correctly? Thanks for your help

Regards, Taskin

pUl| April 4, 2005 02:16

Re: superficial velocity
 
Well, no. If you wish to specify a distribution profile for velocity across a boundary, you can either you ASCII profile definitions or UDF's to do it. Simply inserting values into the "Velocity inlet" panel just means a uniform constant distribution across the boundary, not a profile.

Taskin April 5, 2005 06:48

Re: superficial velocity
 
hi, I mean, varying velocity distribution due to viscous effects. I give a constant velocity but, due to viscous effects, it should have a bell shaped profile after the flow is fully-developed. so is that what superficial velocity takes as a mean? Thanks for you help, Regards, Taskin


pUl| April 5, 2005 13:50

Re: superficial velocity
 
Superficial velocity is simply a number (defined as):

Volumetric flow rate

-------------------------

Cross section area

Taskin April 5, 2005 15:41

Re: superficial velocity
 
hmm I got it I think.. Thanks for your help Regards Taskin

waqasiqbal August 15, 2010 15:10

superficial velocity
 
Superficial velocity is nothing but the velocity of a fluid in a pipe,conduit,column etc in the absence of packing or obstruction. like in packed columns the actual velocity of the fluid through it is actually the volumetric flow rate divided by the cross sectional area. so the velocity achieved by the same fluid in the same column in absence of the packing is called superficial velocity.

chriss August 16, 2017 14:22

In single phase flows in absence of porous medium, the superficial velocity is Q/A, where Q is the volumetric flow rate and A refers to the cross-sectional area.

In multiphase flows, here assuming a gas-liquid two-phase flow, we have:

physical velocities...vg and vl
superficial velocities...Jg=alpha*vg and Jl=(1-alpha)*vl where alpha represents the void fraction and (1-alpha) is the liquid holdup, HL. Thus: alpha+HL=1.

Now, considering a gas-liquid two-phase flow in porous medium, we have:
First, defining the porosity as "por"......por=(V_total-V_solids)/V_total
So,

superficial velocities........vsg=por*alpha*vg and vsl=por*(1-alpha)*vl.

With kind regards,
Chris


All times are GMT -4. The time now is 11:57.