Daniel Lohmeier

In our changes to the net comparison, we realized that some errors occur when saving and restoring nets with SQLite, which remained undiscovered in the old version. The test is...

The latter would implement our internal naming convention correctly.

In some calculations (derivatives) we need certain fluid properties (i.e. state values) that could change with the propagation along a branch, but must be used to derive other values (e.g....

Disregard disconnected flow controllers

1

**Describe the bug** In case the connectivity check sets parts of the network out of service, flow controllers (and heat consumers) might prevail in the pit structure, even though connected...

Do we need a loss coefficient for pressure controllers?

1

I just came to realize that "loss_coefficient" is one of the pressure controller's input entries. However, I fail to see a need for this parameter. This parameter is usually used...

It appears that there is quite a variety of how pressure increasing units are modeled in pandapipes. Technically, there are pumps for liquids and compressors for gases, but the underlying...

Feature request: Check for boundary conditions and correct system setup

2

The complexity of piping grid simulation, especially in case of heating networks, requires a very thorrow model and understanding of how to use different components in a specific setup. We...

Transient heat transfer: further TODOs

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With PR #533 , a lot of changes and further development has been implemented on the transient heat transfer branch. Before we can release the transient heat transfer simulation, there...

I built a test for running a simulation of a district heating grid model with a circulation pump and an external grid: net = pandapipes.create_empty_network("net", add_stdtypes=False) j1, j2, j3, j4,...