- #141
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yes. All you are doing is adding output to what you already have from the lumped model. Nothing about the model itself changes. We are just looking at one additional output parameter from the model.casualguitar said:Yep I have effectively nothing to add to this summary, other than we will need to calculate ##\frac{d\rho}{dh}## before \frac{d_{m1}}{dt}, which we can do with your liquid/vapour/liquid-vapour enthalpy density/temperature equationsI guess I'll still need equations 2 and 3 here? Or are you describing a simpler model?
So the idea would be to not calculate mass flow/enthalpy at each point, but assume it is constant throughout the vessel (as we did previously). Then we can use the mass equations to calculate the hold-up mass and the mass flow out at any time?