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5cbe9a7
add BadPointPressureLiftController tutorial notebook for district hea…
JonasPfeiffer123 May 22, 2025
abe6a37
Merge branch 'e2nIEE:develop' into Tutorials-Examples-District-Heatin…
JonasPfeiffer123 Aug 28, 2025
a5269ab
Create MinimumSupplyTemperatureController.ipynb
JonasPfeiffer123 Aug 28, 2025
a595d70
The previous commit was an accident in this branch.
JonasPfeiffer123 Aug 28, 2025
5e6281a
Added BadPointPressureController reference in the documentation
JonasPfeiffer123 Sep 2, 2025
a6913ca
Merge branch 'e2nIEE:develop' into Tutorials-Examples-District-Heatin…
JonasPfeiffer123 Nov 4, 2025
7a7813f
feat: Add BadPointPressureLiftController as standalone controller module
JonasPfeiffer123 Nov 4, 2025
b7361cc
style: Remove trailing whitespace in BadPointPressureLiftController
JonasPfeiffer123 Nov 4, 2025
a1ada19
fix: Remove unnecessary whitespace in BadPointPressureLiftController
JonasPfeiffer123 Nov 4, 2025
2ec057f
Merge branch 'develop' into Tutorials-Examples-District-Heating-Contr…
EPrade Nov 5, 2025
03f323f
Merge branch 'develop' into Tutorials-Examples-District-Heating-Contr…
SimonRubenDrauz Nov 7, 2025
6b750f5
test: Add test suite for BadPointPressureLiftController
JonasPfeiffer123 Nov 7, 2025
21fad29
test: Organize controller test in control subdirectory
JonasPfeiffer123 Nov 7, 2025
4c3de27
Merge branch 'develop' into Tutorials-Examples-District-Heating-Contr…
EPrade Nov 7, 2025
8f99a6f
refactor: Improve BadPointPressureLiftController implementation
JonasPfeiffer123 Nov 7, 2025
51c0b0c
Merge branch 'Tutorials-Examples-District-Heating-Controllers-' of ht…
JonasPfeiffer123 Nov 7, 2025
286731c
docs: Convert controller docstrings to Sphinx reST format
JonasPfeiffer123 Nov 7, 2025
f35bf41
refactor: Clean up whitespace in BadPointPressureLiftController press…
JonasPfeiffer123 Nov 7, 2025
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Add dual-mode operation to BadPointPressureLiftController
JonasPfeiffer123 Nov 24, 2025
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11 changes: 10 additions & 1 deletion doc/source/controller/controller_classes.rst
Original file line number Diff line number Diff line change
Expand Up @@ -23,4 +23,13 @@ This is used to read the data from a DataSource and write it to a network.

.. _ConstControl:
.. autoclass:: pandapower.control.controller.const_control.ConstControl
:members:
:members:

Custom Controller Example: BadPointPressureLiftController
==========================================================

A practical example of a custom controller implementation is provided in the Jupyter Notebook
`BadPointPressureLiftController.ipynb <https://github.com/e2nIEE/pandapipes/tree/develop/tutorials/BadPointPressureLiftController.ipynb>`_.
This notebook demonstrates how to create a controller that maintains a minimum pressure difference at the worst point in a district heating network, which is a common requirement in district heating systems.

The BadPointPressureLiftController is now available as a standalone controller class in :code:`pandapipes.control` and serves as both a template for user-defined controllers and as an important tool for operating thermal grids with pandapipes.
1 change: 1 addition & 0 deletions src/pandapipes/control/__init__.py
Original file line number Diff line number Diff line change
Expand Up @@ -3,3 +3,4 @@
# Use of this source code is governed by a BSD-style license that can be found in the LICENSE file.

from pandapipes.control.run_control import run_control
from pandapipes.control.controller import BadPointPressureLiftController
1 change: 1 addition & 0 deletions src/pandapipes/control/controller/__init__.py
Original file line number Diff line number Diff line change
@@ -0,0 +1 @@
from pandapipes.control.controller.bad_point_pressure_lift_controller import BadPointPressureLiftController
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from pandapower.control.basic_controller import BasicCtrl

class BadPointPressureLiftController(BasicCtrl):
"""
A controller for maintaining the pressure difference at the worst point (German: Differenzdruckregelung im Schlechtpunkt) in the network.

The BadPointPressureLiftController is a custom controller designed for district heating networks
modeled with pandapipes. Its main purpose is to maintain a minimum pressure difference at the
network's "worst point"—the heat exchanger with the lowest pressure difference (Schlechtpunktregelung).

Key Features:
- **Automatic Worst Point Detection:** Identifies the heat exchanger with the lowest pressure difference where heat flow is present.
- **Pressure Regulation:** Adjusts the circulation pump's lift and flow pressures to ensure the pressure difference at the worst point meets a specified minimum target.
- **Proportional Control:** Uses a proportional gain to determine the adjustment magnitude based on the deviation from the target pressure difference.
- **Standby Mode:** If no heat flow is detected, the controller switches the pump to a standby mode with minimum lift and flow pressures.
- **Convergence Check:** Determines if the pressure difference is within a specified tolerance of the target, signaling convergence.

Args:
net (pandapipesNet): The pandapipes network.
circ_pump_pressure_idx (int, optional): Index of the circulation pump. Defaults to 0.
target_dp_min_bar (float, optional): Target minimum pressure difference in bar. Defaults to 1.
tolerance (float, optional): Tolerance for pressure difference. Defaults to 0.2.
proportional_gain (float, optional): Proportional gain for the controller. Defaults to 0.2.
min_plift (float, optional): Minimum lift pressure in bar. Defaults to 1.5.
min_pflow (float, optional): Minimum flow pressure in bar. Defaults to 3.5.
**kwargs: Additional keyword arguments.

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Could you adapt the docstrings to Sphinx / reStructuredText (reST) style

"""
def __init__(self, net, circ_pump_pressure_idx=0, target_dp_min_bar=1, tolerance=0.2,
proportional_gain=0.2, min_plift=1.5, min_pflow=3.5, **kwargs):
super(BadPointPressureLiftController, self).__init__(net, **kwargs)
self.circ_pump_pressure_idx = circ_pump_pressure_idx
self.target_dp_min_bar = target_dp_min_bar
self.tolerance = tolerance
self.proportional_gain = proportional_gain

self.min_plift = min_plift # Minimum pressure in bar
self.min_pflow = min_pflow # Minimum lift pressure in bar

self.iteration = 0 # Add iteration counter

self.dp_min, self.heat_consumer_idx = self.calculate_worst_point(net)

def calculate_worst_point(self, net):
"""
Calculate the worst point in the heating network, defined as the heat exchanger with the lowest pressure difference.

Args:
net (pandapipesNet): The pandapipes network.

Returns:
tuple: The minimum pressure difference and the index of the worst point.
"""

dp = []

for idx, qext, p_from, p_to in zip(net.heat_consumer.index, net.heat_consumer["qext_w"],
net.res_heat_consumer["p_from_bar"], net.res_heat_consumer["p_to_bar"]):
if qext != 0:
dp_diff = p_from - p_to
dp.append((dp_diff, idx))

if not dp:
return 0, -1

# Find the minimum delta p where the heat flow is not zero
dp_min, idx_min = min(dp, key=lambda x: x[0])

return dp_min, idx_min

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why not using:
diff = net.res_heat_consumer["p_from_bar"] - net.res_heat_consumer["p_to_bar"]
diff.min(), diff.idxmin()

@JonasPfeiffer123 JonasPfeiffer123 Nov 7, 2025

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Good point! Old implementation of mine, never optimized it. I'm going to simplify the code to use pandas operations instead of the manual loop:
diff = net.res_heat_consumer["p_from_bar"] - net.res_heat_consumer["p_to_bar"]
Then filtering with active_consumers = qext != 0 and using diff.min() and diff.idxmin().


def time_step(self, net, time_step):
"""
Reset the iteration counter at the start of each time step.

Args:
net (pandapipesNet): The pandapipes network.
time_step (int): The current time step.

Returns:
int: The current time step.
"""
self.iteration = 0 # reset iteration counter
self.dp_min, self.heat_consumer_idx = self.calculate_worst_point(net)

return time_step

def is_converged(self, net):
"""
Check if the controller has converged.

Args:
net (pandapipesNet): The pandapipes network.

Returns:
bool: True if converged, False otherwise.
"""

if all(net.heat_consumer["qext_w"] == 0):
return True

current_dp_bar = net.res_heat_consumer["p_from_bar"].at[self.heat_consumer_idx] - \
net.res_heat_consumer["p_to_bar"].at[self.heat_consumer_idx]

# Check if the pressure difference is within tolerance
dp_within_tolerance = abs(current_dp_bar - self.target_dp_min_bar) < self.tolerance

if dp_within_tolerance:
return dp_within_tolerance

def control_step(self, net):
"""
Adjust the pump pressure to maintain the target pressure difference.

Args:
net (pandapipesNet): The pandapipes network.
"""
# Increment iteration counter
self.iteration += 1

# Adjust the pump pressure or switch to standby mode when heat flow is zero
if all(net.heat_consumer["qext_w"] == 0):
# Switch to standby mode
print("No heat flow detected. Switching to standby mode.")
net.circ_pump_pressure["plift_bar"].iloc[:] = self.min_plift # Minimum lift pressure
net.circ_pump_pressure["p_flow_bar"].iloc[:] = self.min_pflow # Minimum flow pressure
return super(BadPointPressureLiftController, self).control_step(net)

# Check whether the heat flow in the heat exchanger is zero
current_dp_bar = net.res_heat_consumer["p_from_bar"].at[self.heat_consumer_idx] - \
net.res_heat_consumer["p_to_bar"].at[self.heat_consumer_idx]
current_plift_bar = net.circ_pump_pressure["plift_bar"].at[self.circ_pump_pressure_idx]
current_pflow_bar = net.circ_pump_pressure["p_flow_bar"].at[self.circ_pump_pressure_idx]

dp_error = self.target_dp_min_bar - current_dp_bar

plift_adjustment = dp_error * self.proportional_gain
pflow_adjustment = dp_error * self.proportional_gain

new_plift = current_plift_bar + plift_adjustment
new_pflow = current_pflow_bar + pflow_adjustment

net.circ_pump_pressure["plift_bar"].at[self.circ_pump_pressure_idx] = new_plift
net.circ_pump_pressure["p_flow_bar"].at[self.circ_pump_pressure_idx] = new_pflow

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This seems to me a bit random and error prone. Usually you keep one pressure fixed: flow or return and only adapt the pressure lift accordingly.

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In my understanding: For this application we need to adjust both p_flow_bar
and plift_bar together. The reason is that p_flow_bar sets the absolute pressure at the
pump outlet (supply), and plift_bar sets the pressure increase across the pump.

If we only adjust plift_bar while keeping p_flow_bar constant, increasing plift_bar would
actually decrease the return pressure (since p_flow = p_return + plift), which is
would be restricted by the pressure maintenance in place, right?

By adjusting both pressures with the same proportional gain, we make sure, that the return pressure stays in place.

If that's not the case, I'd like to discuss it, before finishing this pull request.

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Yes, we should discuss this first I guess.


return super(BadPointPressureLiftController, self).control_step(net)
175 changes: 175 additions & 0 deletions tutorials/BadPointPressureLiftController.ipynb
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@@ -0,0 +1,175 @@
{
"cells": [
{
"cell_type": "markdown",
"metadata": {},
"source": [
"# Building a bad point pressure lift Controller for a district heating network"
]
},
{
"cell_type": "markdown",
"metadata": {},
"source": [
"## BadPointPressureLiftController: Pressure Control at the Worst Point\n",
"\n",
"The `BadPointPressureLiftController` is a custom controller designed for district heating networks modeled with pandapipes. Its main purpose is to maintain a minimum pressure difference at the network's \"worst point\"—the heat exchanger with the lowest pressure difference (Schlechtpunktregelung).\n",
"\n",
"### Key Features\n",
"\n",
"- **Automatic Worst Point Detection:** Identifies the heat exchanger with the lowest pressure difference where heat flow is present.\n",
"- **Pressure Regulation:** Adjusts the circulation pump's lift and flow pressures to ensure the pressure difference at the worst point meets a specified minimum target.\n",
"- **Proportional Control:** Uses a proportional gain to determine the adjustment magnitude based on the deviation from the target pressure difference.\n",
"- **Standby Mode:** If no heat flow is detected, the controller switches the pump to a standby mode with minimum lift and flow pressures.\n",
"- **Convergence Check:** Determines if the pressure difference is within a specified tolerance of the target, signaling convergence.\n",
"\n",
"### Usage\n",
"\n",
"- **Initialization:** The controller is initialized with the network, pump index, target pressure difference, tolerance, proportional gain, and minimum pressure settings.\n",
"- **Integration:** It can be integrated into a simulation loop, automatically adjusting pump pressures at each time step to maintain optimal network operation.\n",
"\n",
"This controller is particularly useful for ensuring reliable and efficient operation in district heating systems, where maintaining a minimum pressure difference at the most critical point is essential for system stability and performance."
]
},
{
"cell_type": "code",
"execution_count": null,
"metadata": {},
"outputs": [],
"source": [
"from pandapipes.control import BadPointPressureLiftController"
]
},
{
"cell_type": "markdown",
"metadata": {},
"source": [
"## Example Usage of the BadPointPressureLiftController\n",
"\n",
"To demonstrate the usage of the `BadPointPressureLiftController`, we provide an example with a simple test network. The network is initialized using a `initialize_test_net` function, which sets up a district heating system with two heat consumers, a circulation pump, and several pipes and junctions.\n",
"\n",
"The controller is instantiated and added to the network as follows:\n",
"\n",
"```python\n",
"net = initialize_test_net()\n",
"\n",
"dp_controller = BadPointPressureLiftController(net)\n",
"net.controller.loc[len(net.controller)] = [dp_controller, True, -1, -1, False, False]\n",
"```\n",
"\n",
"This function performs the following steps:\n",
"- Creates a pandapipes network with water as the working fluid.\n",
"- Adds junctions for the pump, pipes, and heat exchangers.\n",
"- Installs a circulation pump with specified flow and lift pressures.\n",
"- Adds two heat consumers with configurable heat extraction and return temperatures.\n",
"- Connects all components with pipes.\n",
"- Runs an initial pipeflow calculation.\n",
"- Instantiates the `BadPointPressureLiftController` and registers it in the network's controller table.\n",
"\n",
"Once the network is initialized, the controller will automatically regulate the pump pressures during simulation to maintain the minimum pressure difference at the worst point (the heat exchanger with the lowest pressure difference). This ensures reliable operation and helps prevent under-supply at critical points in the network.\n",
"\n",
"In my implementation, a dp_min of 1 bar is used in the Controller."
]
},
{
"cell_type": "code",
"execution_count": null,
"metadata": {},
"outputs": [],
"source": [
"import pandapipes as pp\n",
"import numpy as np\n",
"\n",
"def initialize_test_net(qext_w=np.array([100000, 200000]),\n",
" return_temperature=np.array([55, 60]),\n",
" supply_temperature=85, \n",
" flow_pressure_pump=4,\n",
" lift_pressure_pump=1.5,\n",
" pipetype=\"110/202 PLUS\"):\n",
" \n",
" print(\"Running the test network initialization script.\")\n",
" net = pp.create_empty_network(fluid=\"water\")\n",
"\n",
" k = 0.1 # roughness defaults to 0.1\n",
"\n",
" suply_temperature_k = supply_temperature + 273.15\n",
" return_temperature_k = return_temperature + 273.15\n",
"\n",
" # Junctions for pump\n",
" j1 = pp.create_junction(net, pn_bar=1.05, tfluid_k=suply_temperature_k, name=\"Junction 1\", geodata=(0, 10))\n",
" j2 = pp.create_junction(net, pn_bar=1.05, tfluid_k=suply_temperature_k, name=\"Junction 2\", geodata=(0, 0))\n",
"\n",
" # Junctions for connection pipes forward line\n",
" j3 = pp.create_junction(net, pn_bar=1.05, tfluid_k=suply_temperature_k, name=\"Junction 3\", geodata=(10, 0))\n",
" j4 = pp.create_junction(net, pn_bar=1.05, tfluid_k=suply_temperature_k, name=\"Junction 4\", geodata=(60, 0))\n",
"\n",
" # Junctions for heat exchangers\n",
" j5 = pp.create_junction(net, pn_bar=1.05, tfluid_k=suply_temperature_k, name=\"Junction 5\", geodata=(85, 0))\n",
" j6 = pp.create_junction(net, pn_bar=1.05, tfluid_k=suply_temperature_k, name=\"Junction 6\", geodata=(85, 10))\n",
"\n",
" # Junctions for connection pipes return line\n",
" j7 = pp.create_junction(net, pn_bar=1.05, tfluid_k=suply_temperature_k, name=\"Junction 7\", geodata=(60, 10))\n",
" j8 = pp.create_junction(net, pn_bar=1.05, tfluid_k=suply_temperature_k, name=\"Junction 8\", geodata=(10, 10))\n",
"\n",
" pump1 = pp.create_circ_pump_const_pressure(net, j1, j2, p_flow_bar=flow_pressure_pump, plift_bar=lift_pressure_pump, \n",
" t_flow_k=suply_temperature_k, type=\"auto\", name=\"pump1\")\n",
"\n",
" pipe1 = pp.create_pipe(net, j2, j3, std_type=pipetype, length_km=0.01, k_mm=k, name=\"pipe1\", sections=5, text_k=283)\n",
" pipe2 = pp.create_pipe(net, j3, j4, std_type=pipetype, length_km=0.05, k_mm=k, name=\"pipe2\", sections=5, text_k=283)\n",
" pipe3 = pp.create_pipe(net, j4, j5, std_type=pipetype, length_km=0.025, k_mm=k, name=\"pipe3\", sections=5, text_k=283)\n",
"\n",
" heat_consumer1 = pp.create_heat_consumer(net, from_junction=j5, to_junction=j6, loss_coefficient=0, qext_w=qext_w[0], \n",
" treturn_k=return_temperature_k[0], name=\"heat_consumer_1\")\n",
" \n",
"\n",
" heat_consumer2 = pp.create_heat_consumer(net, from_junction=j4, to_junction=j7, loss_coefficient=0, qext_w=qext_w[1], \n",
" treturn_k=return_temperature_k[1], name=\"heat_consumer_2\")\n",
" \n",
" pipe4 = pp.create_pipe(net, j6, j7, std_type=pipetype, length_km=0.25, k_mm=k, name=\"pipe4\", sections=5, text_k=283)\n",
" pipe5 = pp.create_pipe(net, j7, j8, std_type=pipetype, length_km=0.05, k_mm=k, name=\"pipe5\", sections=5, text_k=283)\n",
" pipe6 = pp.create_pipe(net, j8, j1, std_type=pipetype, length_km=0.01, k_mm=k, name=\"pipe6\", sections=5, text_k=283)\n",
"\n",
" pp.pipeflow(net, mode=\"bidirectional\", iter=100)\n",
"\n",
" return net\n",
"\n",
"net = initialize_test_net()\n",
"\n",
"dp_controller = BadPointPressureLiftController(net)\n",
"net.controller.loc[len(net.controller)] = [dp_controller, True, -1, -1, False, False]\n",
"\n",
"pp.pipeflow(net, mode=\"bidirectional\", iter=100)"
]
},
{
"cell_type": "markdown",
"metadata": {},
"source": [
"You can now proceed to run time-series simulations or further analyses, and the controller will handle pressure adjustments as needed. \n",
"\n",
"Suggestions for improvements or alternative approaches are appreciated. Please feel free to contribute."
]
}
],
"metadata": {
"kernelspec": {
"display_name": "Python 3",
"language": "python",
"name": "python3"
},
"language_info": {
"codemirror_mode": {
"name": "ipython",
"version": 3
},
"file_extension": ".py",
"mimetype": "text/x-python",
"name": "python",
"nbconvert_exporter": "python",
"pygments_lexer": "ipython3",
"version": "3.11.9"
}
},
"nbformat": 4,
"nbformat_minor": 2
}