Backdrop: Designing a dust extraction system (LEV) with a branched junction.
What principles allow for the calculation of volume flow rate and pressure at the inlets if the volume flow rate and pressure is known at the outlet using a compressible fluid?
I am familiar with Continuity and Bernoulli equations using incompressible fluids but clearly in this state they are inadequate here.
Alternatively is anyone aware of simple approximations for such calculations?

