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# -*- coding: utf-8 -*- |
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""" |
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Example that illustrates how to use component `GenericCHP` can be used. |
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In this case it is used to model a combined cycle extraction turbine. |
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This file is part of project oemof (github.com/oemof/oemof). It's copyrighted |
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by the contributors recorded in the version control history of the file, |
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available from its original location |
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oemof/tests/test_scripts/test_solph/test_generic_caes/test_generic_caes.py |
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SPDX-License-Identifier: MIT |
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""" |
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import os |
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import pandas as pd |
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import pytest |
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from oemof.solph import EnergySystem |
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from oemof.solph import Model |
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from oemof.solph import processing |
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from oemof.solph import views |
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from oemof.solph.buses import Bus |
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from oemof.solph.components import Sink |
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from oemof.solph.components import Source |
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from oemof.solph.components.experimental import GenericCAES |
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from oemof.solph.flows import Flow |
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def test_gen_caes(): |
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# read sequence data |
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full_filename = os.path.join(os.path.dirname(__file__), "generic_caes.csv") |
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data = pd.read_csv(full_filename) |
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# select periods |
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periods = len(data) |
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# create an energy system |
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idx = pd.date_range("1/1/2017", periods=periods, freq="h") |
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es = EnergySystem(timeindex=idx, infer_last_interval=True) |
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# resources |
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bgas = Bus(label="bgas") |
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es.add(bgas) |
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es.add(Source(label="rgas", outputs={bgas: Flow(variable_costs=20)})) |
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# power |
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bel_source = Bus(label="bel_source") |
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es.add(bel_source) |
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es.add( |
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Source( |
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label="source_el", |
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outputs={bel_source: Flow(variable_costs=data["price_el_source"])}, |
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) |
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) |
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bel_sink = Bus(label="bel_sink") |
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es.add(bel_sink) |
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es.add( |
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Sink( |
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label="sink_el", |
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inputs={bel_sink: Flow(variable_costs=data["price_el_sink"])}, |
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) |
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) |
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# dictionary with parameters for a specific CAES plant |
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# based on thermal modelling and linearization techniques |
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concept = { |
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"cav_e_in_b": 0, |
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"cav_e_in_m": 0.6457267578, |
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"cav_e_out_b": 0, |
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"cav_e_out_m": 0.3739636077, |
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"cav_eta_temp": 1.0, |
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"cav_level_max": 211.11, |
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"cmp_p_max_b": 86.0918959849, |
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"cmp_p_max_m": 0.0679999932, |
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"cmp_p_min": 1, |
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"cmp_q_out_b": -19.3996965679, |
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"cmp_q_out_m": 1.1066036114, |
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"cmp_q_tes_share": 0, |
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"exp_p_max_b": 46.1294016678, |
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"exp_p_max_m": 0.2528340303, |
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"exp_p_min": 1, |
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"exp_q_in_b": -2.2073411014, |
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"exp_q_in_m": 1.129249765, |
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"exp_q_tes_share": 0, |
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"tes_eta_temp": 1.0, |
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"tes_level_max": 0.0, |
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} |
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# generic compressed air energy storage (caes) plant |
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es.add( |
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GenericCAES( |
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label="caes", |
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electrical_input={bel_source: Flow()}, |
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fuel_input={bgas: Flow()}, |
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electrical_output={bel_sink: Flow()}, |
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params=concept, |
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) |
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) |
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# create an optimization problem and solve it |
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om = Model(es) |
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# solve model |
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om.solve(solver="cbc") |
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# create result object |
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results = processing.results(om) |
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data = ( |
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views.node(results, "caes", keep_none_type=True)["sequences"] |
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.sum(axis=0) |
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.to_dict() |
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) |
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test_dict = { |
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(("caes", None), "cav_level"): 25658.82964382, |
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(("caes", None), "exp_p"): 5020.801997000007, |
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(("caes", None), "exp_q_fuel_in"): 5170.880360999999, |
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(("caes", None), "tes_e_out"): 0.0, |
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(("caes", None), "exp_st"): 226.0, |
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(("bgas", "caes"), "flow"): 5170.880360999999, |
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(("caes", None), "cav_e_out"): 1877.5972265299995, |
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(("caes", None), "exp_p_max"): 17512.352336, |
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(("caes", None), "cmp_q_waste"): 2499.9125993000007, |
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(("caes", None), "cmp_p"): 2907.7271520000004, |
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(("caes", None), "exp_q_add_in"): 0.0, |
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(("caes", None), "cmp_st"): 37.0, |
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(("caes", None), "cmp_q_out_sum"): 2499.9125993000007, |
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(("caes", None), "tes_level"): 0.0, |
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(("caes", None), "tes_e_in"): 0.0, |
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(("caes", None), "exp_q_in_sum"): 5170.880360999999, |
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(("caes", None), "cmp_p_max"): 22320.76334300001, |
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(("caes", "bel_sink"), "flow"): 5020.801997000007, |
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(("bel_source", "caes"), "flow"): 2907.7271520000004, |
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(("caes", None), "cav_e_in"): 1877.597226, |
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} |
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for key in test_dict.keys(): |
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assert data[key] == pytest.approx(test_dict[key]) |
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