Dear All,
I've several questions about outflow boundary conditions for boundary 
regions and conditions specified below for a pipe flow problem:
*/<BOUNDARYREGIONS>/**/
/**/            <B ID="0"> C[2] </B> <!-- Inlet -->/**/
/**/            <B ID="1"> C[3] </B> <!-- Outlet -->/**/
/**/            <B ID="2"> C[1] </B> <!-- Wall -->/**/
/**/        </BOUNDARYREGIONS>/**/
/**/
/**/        <BOUNDARYCONDITIONS>/**/
/**/            <REGION REF="0">/**/
/**/                <D VAR="u" VALUE="0" />/**/
/**/                <D VAR="v" VALUE="0" />/**/
/**/                <D VAR="w" VALUE="1" />/**/
/**/                <N VAR="p" USERDEFINEDTYPE="H" VALUE="0" />/**/
/**/            </REGION>/**/
/**/            <REGION REF="1">/**/
/**/                <N VAR="u" VALUE="0" />/**/
/**/                <N VAR="v" VALUE="0" />/**/
/**/                <N VAR="w" VALUE="0" />/**/
/**/                <D VAR="p" VALUE="0" />/**/
/**/            </REGION>/**/
/**/            <REGION REF="2">/**/
/**/                <D VAR="u" VALUE="0" />/**/
/**/                <D VAR="v" VALUE="0" />/**/
/**/                <D VAR="w" VALUE="0" />/**/
/**/                <N VAR="p" USERDEFINEDTYPE="H" VALUE="0" />/**/
/**/            </REGION>/**/
/**/        </BOUNDARYCONDITIONS>/*
1) What is the meaning of */<N VAR="p" USERDEFINEDTYPE="H" VALUE="0" /> 
/*and why do we specify such a BC at the wall of the pipe? What happens 
if I don't specify any pressure BC at the wall of the pipe?*/
/*2) Is there any other option to specify pressure BC at the outlet 
other than*//**/*/<D VAR="p" VALUE="0" />/*/* ?*/*//*/*For example is it 
possible to apply the pressure BC at the outlet given below which is 
specified in a paper (Direct numerical simulation of stenotic flows. 
Part 1. Steady flow, SONU S. VARGHESE, STEVEN H. FRANKEL AND PAUL F. 
FISCHER) ?
/*In turbulent flows, it is possible to have vortices strong enough to 
yield a (locally) negative flux at the outflow boundary. Since no flow 
characteristics are specified on these boundaries, a negative flux 
condition typically leads to instabilities with catastrophic results. 
One way to ensure that the characteristics at the exit are always 
pointing outwards is to force the exit flow through a nozzle, 
effectively adding a mean axial component to the velocity field. In 
contrast, schemes based on viscous *//*buffer zones require knowledge of 
the anticipated space and time scales to ensure that vortical structures 
are adequately damped as they pass through the buffer zone.*//*
*//*This nozzle effect can be imposed numerically without having to 
change the mesh geometry by imparting a positive divergence to the flow 
field near the exit (in the spirit of a supersonic nozzle). In the 
current study, this is done by identifying the layer of elements 
adjacent to the outflow and imposing a divergence function D(x) that is 
zero at the upstream end of the layer and ramps to a fixed positive 
value at the exit. Specifically, we set D(x)=C[1−(x⊥/L⊥)2], where x⊥ is 
the distance normal to the boundary and L⊥ is the maximum thickness of 
the last layer of elements. A net gain in mean velocity is obtained over 
the extent of the layer by integrating the expression for D from x⊥/L⊥=1 
to 0. The constant C is chosen such that the gain is equal to the mean 
velocity prior to the correction.*//*
*/*/
/*Regards,
Kamil