I agree Terry and Joe. It seems to me that the way you state the problem Don, it becomes almost a circular argument. Another large issue in looking at these issues are the assumptions that we make in dealing with Bernoulli and Poiseuille for that matter, that are not consistent with what happens in a patient. Such as: 1. The conduit is a rigid tube with a smooth surface and no irregularities. 2. The fluid is Newtonian and incompressible. 3. No energy loss due to heat. 4. there is steady flow. While Reynolds > 2000 usually results in turbulence, we can find many examples of turbulence with much lower numbers and vice versa. My go to book has become Frank Miele for good models of how this stuff works.

Bill

William B Schroedter, BS, RVT, RPhS, FSVU
Technical Director, Quality Vascular Imaging, Inc
4120 Woodmere Park Blvd
Suite 8B
Venice, Florida 34293
(941) 408-8855 office

Sent: Wednesday, October 31, 2012 7:26 AM
Subject: Re: Reynolds

Cross sectional area is pi * r2 . If the radius is doubled then the area quadruples and so velocity would decrease by about 75% to accommodate the same volume flow.  More apropos of what we see in disease if the radius decreases by 50% then the velocity roughly quadruples to accommodate the same volume flow. We are used to thinking of turbulence occurring in stenoses so if the radius decreases velocity must increase much more to accommodate the same volume flow and you can see that this will increase the Reynolds number.

All the best

Joe

Sent: Wednesday, October 31, 2012 5:36 AM
Subject: Re: Reynolds

Don, The answer for your student is in the question.  The Reynolds equation is determining the point at which flow becomes turbulent in a tube.  You can solve that riddle for any diameter tube but once you choose the diameter of the tube you are solving for it is no longer a variable but rather a fixed constant in the formula.  I guess if you were questioning the diameter required to keep a certain fluid of known viscosity and volume from becoming turbulent as you deliver it from point a to b than yes your student question would have some application, but you would first have to determine a starting diameter and it's associated Reynolds number for that specific fluid to be able to apply it.  I think.

I got asked an awkward question by a student today, regarding the Reynolds equation:

Re = V p 2r
n

My primitive school email access won't allow me to make that lower-case p into a rho for density, nor that lower-case n into an eta for viscosity, but you get the idea.

The question was this: since we know from another equation—Q = V x CSA—that a reduction of cross-sectional area means an increase of mean velocity, then why don''t those two balance out in the Reynolds equation?

For example, if the radius is doubled, won't that bring about a decrease to 1/2 of the velocity, leaving Re unchanged?

My clever response: life is complicated. And I'll get back to you.

I'm obviously angling for a bit of perspective from Dr. Beach from up there in Seattle (whence I'm flying Friday, as it happens).

Thanks in advance to anyone with help on this.

Don Ridgway

To unsubscribe or search other topics on UVM Flownet link to:
http://list.uvm.edu/archives/uvmflownet.html

To unsubscribe or search other topics on UVM Flownet link to: http://list.uvm.edu/archives/uvmflownet.html

To unsubscribe or search other topics on UVM Flownet link to: http://list.uvm.edu/archives/uvmflownet.html To unsubscribe or search other topics on UVM Flownet link to: http://list.uvm.edu/archives/uvmflownet.html