-
Notifications
You must be signed in to change notification settings - Fork 87
Add BadPointPressureLiftController tutorial notebook for district heating network #711
New issue
Have a question about this project? Sign up for a free GitHub account to open an issue and contact its maintainers and the community.
By clicking “Sign up for GitHub”, you agree to our terms of service and privacy statement. We’ll occasionally send you account related emails.
Already on GitHub? Sign in to your account
base: develop
Are you sure you want to change the base?
Changes from 11 commits
5cbe9a7
abe6a37
a5269ab
a595d70
5e6281a
a6913ca
7a7813f
b7361cc
a1ada19
2ec057f
03f323f
6b750f5
21fad29
4c3de27
8f99a6f
51c0b0c
286731c
f35bf41
bd56886
File filter
Filter by extension
Conversations
Jump to
Diff view
Diff view
There are no files selected for viewing
| Original file line number | Diff line number | Diff line change |
|---|---|---|
| @@ -0,0 +1 @@ | ||
| from pandapipes.control.controller.bad_point_pressure_lift_controller import BadPointPressureLiftController |
| Original file line number | Diff line number | Diff line change |
|---|---|---|
| @@ -0,0 +1,144 @@ | ||
| 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. | ||
| """ | ||
| 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 | ||
|
Collaborator
There was a problem hiding this comment. Choose a reason for hiding this commentThe reason will be displayed to describe this comment to others. Learn more. why not using:
Contributor
Author
There was a problem hiding this comment. Choose a reason for hiding this commentThe reason will be displayed to describe this comment to others. Learn more. 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: |
||
|
|
||
| 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 | ||
|
Collaborator
There was a problem hiding this comment. Choose a reason for hiding this commentThe reason will be displayed to describe this comment to others. Learn more. 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.
Contributor
Author
There was a problem hiding this comment. Choose a reason for hiding this commentThe reason will be displayed to describe this comment to others. Learn more. In my understanding: For this application we need to adjust both p_flow_bar If we only adjust plift_bar while keeping p_flow_bar constant, increasing plift_bar would 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.
Collaborator
There was a problem hiding this comment. Choose a reason for hiding this commentThe reason will be displayed to describe this comment to others. Learn more. Yes, we should discuss this first I guess. |
||
|
|
||
| return super(BadPointPressureLiftController, self).control_step(net) | ||
| Original file line number | Diff line number | Diff line change |
|---|---|---|
| @@ -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 | ||
| } |
There was a problem hiding this comment.
Choose a reason for hiding this comment
The reason will be displayed to describe this comment to others. Learn more.
Could you adapt the docstrings to Sphinx / reStructuredText (reST) style