Nileo2005
Mechanical
- Jul 10, 2008
- 83
Hi all. Fist time posting a question, so try to be nice if I mess this whole thing up. I currently am having a problem mapping the stresses and deformation of a closed pressure vessel.
The current method is to just define an internal pressure amplitude on the fluid elements, and that works just dandy with small to no vessel deformation as the internal pressure over time decays negligibly. The problem is when large expansion of the vessel starts to occur.
With the creep effects over time being the target of this testing, this large volumetric expansion is inevitable. Coupled with this volumetric expansion of the vessel, being a closed system, should be an internal pressure decrease due to the ideal gas law, which is not currently represented with the current method.
Does anyone know a way to define a cavity to a certain pressure with a finite amount of fluid or something of the sort? Or possibly to define the internal pressure of the vessel as a function of the current volume, its cvol output, per step? Those are my first two thoughts, but alas my internet forum and book scouring has yeilded bupkus. Thaks in advance!
Oh. by the way, I'm using a compressible fluid like air, ideal and newtonian.
The current method is to just define an internal pressure amplitude on the fluid elements, and that works just dandy with small to no vessel deformation as the internal pressure over time decays negligibly. The problem is when large expansion of the vessel starts to occur.
With the creep effects over time being the target of this testing, this large volumetric expansion is inevitable. Coupled with this volumetric expansion of the vessel, being a closed system, should be an internal pressure decrease due to the ideal gas law, which is not currently represented with the current method.
Does anyone know a way to define a cavity to a certain pressure with a finite amount of fluid or something of the sort? Or possibly to define the internal pressure of the vessel as a function of the current volume, its cvol output, per step? Those are my first two thoughts, but alas my internet forum and book scouring has yeilded bupkus. Thaks in advance!
Oh. by the way, I'm using a compressible fluid like air, ideal and newtonian.