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Commit b63cfd4c authored by Jakob Randow's avatar Jakob Randow Committed by HBShaoUFZ
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test case for server communication 


keep false in test input file. 


Update Tests

Update Tests

Update Tests and delete ogs.exe
parent a1cc159a
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ProcessLib/HeatTransportBHE/Tests.cmake
View file @ b63cfd4c
......@@ -99,6 +99,38 @@ if("${Python3_VERSION}" VERSION_LESS 3.9)
3bhes_1U_ts_10_t_600.000000.vtu 3bhes_1U_ts_10_t_600.000000.vtu temperature_BHE2 temperature_BHE2 1e-10 1e-13
3bhes_1U_ts_10_t_600.000000.vtu 3bhes_1U_ts_10_t_600.000000.vtu temperature_BHE3 temperature_BHE3 1e-10 1e-13
)
AddTest(
NAME HeatTransportBHE_1U_3D_beier_sandbox_server_communication
PATH Parabolic/T/3D_Beier_sandbox_SimX
EXECUTABLE ogs
EXECUTABLE_ARGS beier_sandbox.prj
WRAPPER time
TESTER vtkdiff
REQUIREMENTS OGS_USE_PYTHON AND NOT OGS_USE_MPI
RUNTIME 50
PYTHON_PACKAGES "pandas"
DIFF_DATA
beier_sandbox_ts_10_t_600.000000.vtu beier_sandbox_ts_10_t_600.000000.vtu temperature_BHE1 temperature_BHE1 0 5e-15
beier_sandbox_ts_10_t_600.000000.vtu beier_sandbox_ts_10_t_600.000000.vtu temperature_soil temperature_soil 0 1e-13
)
AddTest(
NAME HeatTransportBHE_3D_3BHEs_array_server_communication
PATH Parabolic/T/3D_3BHEs_array_SimX
RUNTIME 50
EXECUTABLE ogs
EXECUTABLE_ARGS 3bhes_1U.prj
WRAPPER time
TESTER vtkdiff
REQUIREMENTS OGS_USE_PYTHON AND NOT OGS_USE_MPI
PYTHON_PACKAGES "TESPy=0.3.2"
DIFF_DATA
3bhes_1U_ts_10_t_600.000000.vtu 3bhes_1U_ts_10_t_600.000000.vtu temperature_soil temperature_soil 1e-12 1e-13
3bhes_1U_ts_10_t_600.000000.vtu 3bhes_1U_ts_10_t_600.000000.vtu temperature_BHE1 temperature_BHE1 1e-9 1e-12
3bhes_1U_ts_10_t_600.000000.vtu 3bhes_1U_ts_10_t_600.000000.vtu temperature_BHE2 temperature_BHE2 1e-9 1e-12
3bhes_1U_ts_10_t_600.000000.vtu 3bhes_1U_ts_10_t_600.000000.vtu temperature_BHE3 temperature_BHE3 1e-9 1e-12
)
endif()
AddTest(
......
Tests/Data/Parabolic/T/3D_3BHEs_array_SimX/3bhes_1U.gml 0 → 100644
View file @ b63cfd4c
<?xml version="1.0" encoding="ISO-8859-1"?>
<?xml-stylesheet type="text/xsl" href="OpenGeoSysGLI.xsl"?>
<OpenGeoSysGLI xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:noNamespaceSchemaLocation="http://www.opengeosys.org/images/xsd/OpenGeoSysGLI.xsd" xmlns:ogs="http://www.opengeosys.org">
<name>3bhes_1U</name>
<points>
<point id="0" x="-25.0" y="0.0" z="0.0" name="TOP_left_down"/>
<point id="1" x="-25.0" y="50.0" z="0.0" name="TOP_left_upper"/>
<point id="2" x="25.0" y="50.0" z="0.0" name="TOP_right_upper"/>
<point id="3" x="25.0" y="0.0" z="0.0" name="TOP_right_down"/>
<point id="4" x="-25.0" y="0.0" z="-72.0" name="bottom_left_down"/>
<point id="5" x="-25.0" y="50.0" z="-72.0" name="bottom_left_upper"/>
<point id="6" x="25.0" y="50.0" z="-72.0" name="bottom_right_uppert"/>
<point id="7" x="25.0" y="0.0" z="-72.0" name="bottom_right_down"/>
<point id="8" x="0.0" y="25.0" z="-52.0" name="BHE1_BOTTOM"/>
<point id="9" x="0.0" y="25.0" z="-2.0" name="BHE1_TOP"/>
<point id="10" x="-6.0" y="25.0" z="-52.0" name="BHE2_BOTTOM"/>
<point id="11" x="-6.0" y="25.0" z="-2.0" name="BHE2_TOP"/>
<point id="12" x="0.0" y="25.0" z="-52.0" name="BHE3_BOTTOM"/>
<point id="13" x="0.0" y="25.0" z="-2.0" name="BHE3_TOP"/>
</points>
<polylines>
<polyline id="0" name="BHE_1">
<pnt>9</pnt>
<pnt>8</pnt>
</polyline>
<polyline id="1" name="BHE_2">
<pnt>11</pnt>
<pnt>10</pnt>
</polyline>
<polyline id="2" name="BHE_3">
<pnt>13</pnt>
<pnt>12</pnt>
</polyline>
</polylines>
<surfaces>
<surface id="0" name="top">
<element p1="0" p2="1" p3="2"/>
<element p1="0" p2="3" p3="2"/>
</surface>
</surfaces>
</OpenGeoSysGLI>
Tests/Data/Parabolic/T/3D_3BHEs_array_SimX/3bhes_1U.prj 0 → 100644
View file @ b63cfd4c
<?xml version="1.0" encoding="ISO-8859-1"?>
<OpenGeoSysProject>
<mesh>3bhes_1U.vtu</mesh>
<geometry>3bhes_1U.gml</geometry>
<python_script>bcs_tespy_and_serverCommunication.py</python_script>
<processes>
<process>
<name>HeatTransportBHE</name>
<type>HEAT_TRANSPORT_BHE</type>
<integration_order>2</integration_order>
<process_variables>
<process_variable>temperature_soil</process_variable>
<process_variable>temperature_BHE1</process_variable>
<process_variable>temperature_BHE2</process_variable>
<process_variable>temperature_BHE3</process_variable>
</process_variables>
<use_server_communication>true</use_server_communication>
<borehole_heat_exchangers>
<borehole_heat_exchanger>
<type>1U</type>
<use_bhe_pipe_network>true</use_bhe_pipe_network>
<flow_and_temperature_control>
<type>TemperatureCurveConstantFlow</type>
<flow_rate>2.0e-4</flow_rate>
<temperature_curve>inflow_temperature</temperature_curve>
</flow_and_temperature_control>
<borehole>
<length>50.0</length>
<diameter>0.126</diameter>
</borehole>
<grout>
<density>2190.0</density>
<porosity>0.0</porosity>
<specific_heat_capacity>1735.160</specific_heat_capacity>
<thermal_conductivity>0.806</thermal_conductivity>
</grout>
<pipes>
<inlet>
<diameter> 0.013665</diameter>
<wall_thickness>0.003035</wall_thickness>
<wall_thermal_conductivity>0.39</wall_thermal_conductivity>
</inlet>
<outlet>
<diameter>0.013665</diameter>
<wall_thickness>0.003035</wall_thickness>
<wall_thermal_conductivity>0.39</wall_thermal_conductivity>
</outlet>
<distance_between_pipes>0.053</distance_between_pipes>
<longitudinal_dispersion_length>0.001</longitudinal_dispersion_length>
</pipes>
<refrigerant>
<density>992.92</density>
<viscosity>0.00067418</viscosity>
<specific_heat_capacity>4198</specific_heat_capacity>
<thermal_conductivity>0.62863</thermal_conductivity>
<reference_temperature>298.15</reference_temperature>
</refrigerant>
</borehole_heat_exchanger>
<borehole_heat_exchanger>
<type>1U</type>
<use_bhe_pipe_network>true</use_bhe_pipe_network>
<flow_and_temperature_control>
<type>TemperatureCurveConstantFlow</type>
<flow_rate>2.0e-4</flow_rate>
<temperature_curve>inflow_temperature</temperature_curve>
</flow_and_temperature_control>
<borehole>
<length>50.0</length>
<diameter>0.126</diameter>
</borehole>
<grout>
<density>2190.0</density>
<porosity>0.0</porosity>
<specific_heat_capacity>1735.160</specific_heat_capacity>
<thermal_conductivity>0.806</thermal_conductivity>
</grout>
<pipes>
<inlet>
<diameter> 0.013665</diameter>
<wall_thickness>0.003035</wall_thickness>
<wall_thermal_conductivity>0.39</wall_thermal_conductivity>
</inlet>
<outlet>
<diameter>0.013665</diameter>
<wall_thickness>0.003035</wall_thickness>
<wall_thermal_conductivity>0.39</wall_thermal_conductivity>
</outlet>
<distance_between_pipes>0.053</distance_between_pipes>
<longitudinal_dispersion_length>0.001</longitudinal_dispersion_length>
</pipes>
<refrigerant>
<density>992.92</density>
<viscosity>0.00067418</viscosity>
<specific_heat_capacity>4198</specific_heat_capacity>
<thermal_conductivity>0.62863</thermal_conductivity>
<reference_temperature>298.15</reference_temperature>
</refrigerant>
</borehole_heat_exchanger>
<borehole_heat_exchanger>
<type>1U</type>
<use_bhe_pipe_network>true</use_bhe_pipe_network>
<flow_and_temperature_control>
<type>TemperatureCurveConstantFlow</type>
<flow_rate>2.0e-4</flow_rate>
<temperature_curve>inflow_temperature</temperature_curve>
</flow_and_temperature_control>
<borehole>
<length>50.0</length>
<diameter>0.126</diameter>
</borehole>
<grout>
<density>2190.0</density>
<porosity>0.0</porosity>
<specific_heat_capacity>1735.160</specific_heat_capacity>
<thermal_conductivity>0.806</thermal_conductivity>
</grout>
<pipes>
<inlet>
<diameter> 0.013665</diameter>
<wall_thickness>0.003035</wall_thickness>
<wall_thermal_conductivity>0.39</wall_thermal_conductivity>
</inlet>
<outlet>
<diameter>0.013665</diameter>
<wall_thickness>0.003035</wall_thickness>
<wall_thermal_conductivity>0.39</wall_thermal_conductivity>
</outlet>
<distance_between_pipes>0.053</distance_between_pipes>
<longitudinal_dispersion_length>0.001</longitudinal_dispersion_length>
</pipes>
<refrigerant>
<density>992.92</density>
<viscosity>0.00067418</viscosity>
<specific_heat_capacity>4198</specific_heat_capacity>
<thermal_conductivity>0.62863</thermal_conductivity>
<reference_temperature>298.15</reference_temperature>
</refrigerant>
</borehole_heat_exchanger>
</borehole_heat_exchangers>
</process>
</processes>
<media>
<medium id="0">
<phases>
<phase>
<type>AqueousLiquid</type>
<properties>
<property>
<name>phase_velocity</name>
<type>Constant</type>
<value>0 0 0</value>
</property>
<property>
<name>specific_heat_capacity</name>
<type>Constant</type>
<value>4068</value>
</property>
<property>
<name>density</name>
<type>Constant</type>
<value>992.92</value>
</property>
</properties>
</phase>
<phase>
<type>Solid</type>
<properties>
<property>
<name>specific_heat_capacity</name>
<type>Constant</type>
<value>1780</value>
</property>
<property>
<name>density</name>
<type>Constant</type>
<value>1120</value>
</property>
</properties>
</phase>
<phase>
<type>Gas</type>
<properties>
<property>
<name>specific_heat_capacity</name>
<type>Constant</type>
<value>1000</value>
</property>
<property>
<name>density</name>
<type>Constant</type>
<value>2500</value>
</property>
</properties>
</phase>
</phases>
<properties>
<property>
<name>porosity</name>
<type>Constant</type>
<value>0</value>
</property>
<property>
<name>thermal_conductivity</name>
<type>Constant</type>
<value>2.4</value>
</property>
<property>
<name>thermal_longitudinal_dispersivity</name>
<type>Constant</type>
<value>0</value>
</property>
<property>
<name>thermal_transversal_dispersivity</name>
<type>Constant</type>
<value>0</value>
</property>
</properties>
</medium>
</media>
<time_loop>
<processes>
<process ref="HeatTransportBHE">
<nonlinear_solver>basic_picard</nonlinear_solver>
<convergence_criterion>
<type>DeltaX</type>
<norm_type>NORM2</norm_type>
<reltol>1.e-5</reltol>
</convergence_criterion>
<time_discretization>
<type>BackwardEuler</type>
</time_discretization>
<time_stepping>
<type>FixedTimeStepping</type>
<t_initial> 0.0 </t_initial>
<t_end> 600 </t_end>
<!-- use the following for full simulation -->
<!-- <t_end> 15552000 </t_end> -->
<timesteps>
<pair>
<repeat>10</repeat>
<delta_t>60</delta_t>
</pair>
<!-- use the following for full simulation -->
<!-- <pair><repeat>10</repeat><delta_t>60</delta_t></pair> -->
<!-- <pair><repeat>1</repeat><delta_t>3000</delta_t></pair> -->
<!-- <pair><repeat>5</repeat><delta_t>3600</delta_t></pair> -->
<!-- <pair><repeat>1</repeat><delta_t>10800</delta_t></pair> -->
</timesteps>
</time_stepping>
</process>
</processes>
<output>
<type>VTK</type>
<prefix>3bhes_1U</prefix>
<timesteps>
<pair>
<repeat> 10</repeat>
<each_steps> 1 </each_steps>
</pair>
<!-- use the following for full simulation -->
<!-- <pair><repeat> 1</repeat><each_steps> 94 </each_steps></pair> -->
<!-- <pair><repeat> 1</repeat><each_steps> 80 </each_steps></pair> -->
</timesteps>
<variables>
<variable>temperature_soil</variable>
<variable>temperature_BHE1</variable>
<variable>temperature_BHE2</variable>
<variable>temperature_BHE3</variable>
</variables>
<suffix>_ts_{:timestep}_t_{:time}</suffix>
</output>
</time_loop>
<parameters>
<parameter>
<name>T0</name>
<type>Constant</type>
<value>315.15</value>
</parameter>
<parameter>
<name>T0_BHE</name>
<type>Constant</type>
<values>305.36 305.13 305.23 305.115</values>
</parameter>
</parameters>
<process_variables>
<process_variable>
<name>temperature_soil</name>
<components>1</components>
<order>1</order>
<initial_condition>T0</initial_condition>
<boundary_conditions>
<boundary_condition>
<geometrical_set>3bhes_1U</geometrical_set>
<geometry>top</geometry>
<type>Dirichlet</type>
<parameter>T0</parameter>
</boundary_condition>
</boundary_conditions>
</process_variable>
<process_variable>
<name>temperature_BHE1</name>
<components>4</components>
<order>1</order>
<initial_condition>T0_BHE</initial_condition>
</process_variable>
<process_variable>
<name>temperature_BHE2</name>
<components>4</components>
<order>1</order>
<initial_condition>T0_BHE</initial_condition>
</process_variable>
<process_variable>
<name>temperature_BHE3</name>
<components>4</components>
<order>1</order>
<initial_condition>T0_BHE</initial_condition>
</process_variable>
</process_variables>
<nonlinear_solvers>
<nonlinear_solver>
<name>basic_picard</name>
<type>Picard</type>
<max_iter>100</max_iter>
<linear_solver>general_linear_solver</linear_solver>
</nonlinear_solver>
</nonlinear_solvers>
<linear_solvers>
<linear_solver>
<name>general_linear_solver</name>
<lis>-i cg -p jacobi -tol 1e-16 -maxiter 10000</lis>
<eigen>
<solver_type>BiCGSTAB</solver_type>
<precon_type>ILUT</precon_type>
<max_iteration_step>1000</max_iteration_step>
<error_tolerance>1e-16</error_tolerance>
</eigen>
<petsc>
<prefix>gw</prefix>
<parameters>-gw_ksp_type cg -gw_pc_type bjacobi -gw_ksp_rtol 1e-16 -gw_ksp_max_it 10000</parameters>
</petsc>
</linear_solver>
</linear_solvers>
<curves>
<curve>
<name>inflow_temperature</name>
<coords>0 933120000
</coords>
<values>295.3611111 295.3611111
</values>
</curve>
</curves>
</OpenGeoSysProject>
Tests/Data/Parabolic/T/3D_3BHEs_array_SimX/3bhes_1U.vtu 0 → 100644
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Tests/Data/Parabolic/T/3D_3BHEs_array_SimX/3bhes_1U_ts_10_t_600.000000.vtu 0 → 100644
View file @ b63cfd4c
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Tests/Data/Parabolic/T/3D_3BHEs_array_SimX/README.md 0 → 100644
View file @ b63cfd4c
# How to run
You need to install the modules used in the python script and build OGS with `OGS_USE_PYTHON=ON`.
Tests/Data/Parabolic/T/3D_3BHEs_array_SimX/bcs_tespy_and_serverCommunication.py 0 → 100644
View file @ b63cfd4c
###
# Copyright (c) 2012-2021, OpenGeoSys Community (http://www.opengeosys.org)
# Distributed under a Modified BSD License.
# See accompanying file LICENSE.txt or
# http://www.opengeosys.org/project/license
###
import sys
print(sys.version)
import os
import numpy as np
from pandas import read_csv
import OpenGeoSys
from tespy.networks import load_network
# User setting ++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
# parameters
# refrigerant density
rho_f = 992.92 # kg/m3
# switch for special boundary conditions
# switch of the function for manually specified dynamic flowrate
switch_dyn_frate = "off" # 'on','off'
# switch of the function for manually specified dynamic thermal demand
switch_dyn_demand = "on" # 'on','off'
# network status setting
def network_status(t):
nw_status = "on"
# month for closed network
timerange_nw_off_month = [] # No month for closed network
# t-1 to avoid the calculation problem at special time point,
# e.g. t = 2592000.
t_trans = int((t - 1) / 86400 / 30) + 1
t_trans_month = t_trans
if t_trans_month > 12:
t_trans_month = t_trans - 12 * (int(t_trans / 12))
if t_trans_month in timerange_nw_off_month:
nw_status = "off"
return nw_status
# dynamic consumer thermal load
def consumer_demand(t): # dynamic thermal demand from consumer
# time conversion
t_trans = int((t - 1) / 86400 / 30) + 1
if t_trans > 12:
t_trans = t_trans - 12 * (int(t_trans / 12))
# thermal demand in each month (assumed specific heat extraction rate*
# length of BHE* number of BHE)
month_demand = [
-25 * 50 * 3,
-25 * 50 * 3,
-25 * 50 * 3,
-25 * 50 * 3,
-25 * 50 * 3,
-25 * 50 * 3,
-25 * 50 * 3,
-25 * 50 * 3,
-25 * 50 * 3,
-25 * 50 * 3,
-25 * 50 * 3,
-25 * 50 * 3,
]
return month_demand[t_trans - 1]
# dynamic hydraulic flow rate at the network inlet
def dyn_frate(t):
# time conversion
t_trans = int((t - 1) / 86400 / 30) + 1
if t_trans > 12:
t_trans = t_trans - 12 * (int(t_trans / 12))
# flow rate in kg / s time curve in month
month_frate = []
return month_frate[t_trans - 1]
# End User setting +++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++
# create network dataframe
def create_dataframe():
# return dataframe
df_nw = read_csv(
"./pre/bhe_network.csv", delimiter=";", index_col=[0], dtype={"data_index": str}
)
return df_nw
# TESPy calculation process
def get_tespy_results(t):
# bhe network boundary conditions re parametrization
# if network exist dynamic flowrate
if switch_dyn_frate == "on":
cur_frate = dyn_frate(t)
localVars["inlet_name"].set_attr(m=cur_frate)
# if network exist dynamic thermal demand
if switch_dyn_demand == "on":
# consumer thermal load:
cur_month_demand = consumer_demand(t)
nw.busses[bus_name].set_attr(P=cur_month_demand)
# T_out re parametrization:
for i in range(n_BHE):
localVars["outlet_BHE" + str(i + 1)].set_attr(
T=df.loc[data_index[i], "Tout_val"]
)
# solving network
nw.solve(mode="design")
# get Tin_val and flow rate
for i in range(n_BHE):
# get Tin_val
df.loc[df.index[i], "Tin_val"] = (
localVars["inlet_BHE" + str(i + 1)].get_attr("T").val
)
# get flowrate
df.loc[df.index[i], "flowrate"] = (
localVars["inlet_BHE" + str(i + 1)].get_attr("m").val / rho_f
)
return df["Tin_val"].tolist(), df["flowrate"].tolist()
# OGS setting
# Dirichlet BCs
class BC(OpenGeoSys.BHENetwork):
def initializeDataContainer(self):
# initialize network and get data from the network
nw.solve(mode="design")
get_tespy_results(0)
# convert dataframe to column list
t = 0 # 'initial time'
data_col_1 = df["Tin_val"].tolist() # 'Tin_val'
data_col_2 = df["Tout_val"].tolist() # 'Tout_val'
data_col_3 = df["Tout_node_id"].astype(int).tolist() # 'Tout_node_id'
data_col_4 = df["flowrate"].tolist() # 'BHE flow rate'
return (t, data_col_1, data_col_2, data_col_3, data_col_4)
def tespySolver(self, t, Tin_val, Tout_val):
# network status:
nw_status = network_status(t)
# if network closed:
if nw_status == "off":
df.loc[:, "flowrate"] = 0
cur_flowrate = df["flowrate"].tolist()