Francesco Witte

Some considerations to be collected below - Td_bp then needs to refer to Q=0 in case of subcooling and Q=1 in case of superheating - A method to access bubble...

Implement compressor part load efficiency models

3

At the [Carnot2024](https://www.labothap.uliege.be/cms/c_11689223/en/carnot-2024-belgian-symposium-of-thermodynamics?id=c_11689223&id=c_11689223) conference, an interesting approach suitable for implementation in tespy was presented on a poster. 

A discretization method for heat exchangers might be useful

1

I have received multiple requests for finding/imposing the minimum pinch inside a heat exchanger. For that, a discretization approach must be taken. The `MovingBoundaryHeatExchanger` does this already by assuming, that...

This is essentially a precalculation, because pressure can directly be calculated. Usually, you could just do that using CoolProp API in your script and pass the value to tespy. This...

In case the user applies - a Desuperheater, - a Condenser, - a Drum, - a DropletSeparator the pressure values at the hot side inlet and outlet should be forced...

It has been recommended to me recently, would be a nice addition!

They should be the same style as the access for components and connections: - `Network.get_ude` - `Network.get_bus`

Implement guesses based on Temperature or Quality

2

Users should be able to specify a temperature or a quality guess, and based on this together with the pressure guess at the same point, the starting value of enthalpy...