mirror of
https://github.com/CoolProp/CoolProp.git
synced 2026-01-21 03:48:08 -05:00
Merge branch 'master' of https://github.com/CoolProp/CoolProp
This commit is contained in:
Ian Bell
@@ -143,14 +143,18 @@ if (COOLPROP_SHARED_LIBRARY)
|
||||
list(APPEND APP_SOURCES "${CMAKE_SOURCE_DIR}/src/CoolPropLib.cpp")
|
||||
endif()
|
||||
|
||||
if (COOLPROP_STATIC_LIBRARY_MODULE OR COOLPROP_STATIC_LIBRARY)
|
||||
if (COOLPROP_STATIC_LIBRARY_MODULE OR COOLPROP_STATIC_LIBRARY OR COOLPROP_EXTERNC_STATIC_LIBRARY)
|
||||
list(APPEND APP_SOURCES "${CMAKE_SOURCE_DIR}/src/CoolPropLib.cpp")
|
||||
add_library(${app_name} STATIC ${APP_SOURCES})
|
||||
add_dependencies (${app_name} generate_headers)
|
||||
set_target_properties (${app_name} PROPERTIES COMPILE_FLAGS "${COMPILE_FLAGS} -DEXTERNC")
|
||||
install (TARGETS ${app_name} DESTINATION static_library/${CMAKE_SYSTEM_NAME})
|
||||
endif()
|
||||
|
||||
if (COOLPROP_EXTERNC_STATIC_LIBRARY)
|
||||
set_target_properties (${app_name} PROPERTIES COMPILE_FLAGS "${COMPILE_FLAGS} -DEXTERNC")
|
||||
endif()
|
||||
|
||||
|
||||
if (COOLPROP_64BIT_SHARED_LIBRARY_MODULE OR COOLPROP_64BIT_SHARED_LIBRARY)
|
||||
list(APPEND APP_SOURCES "${CMAKE_SOURCE_DIR}/src/CoolPropLib.cpp")
|
||||
add_library(${app_name} SHARED ${APP_SOURCES})
|
||||
@@ -657,15 +661,9 @@ if (COOLPROP_PYTHON_BINARIES)
|
||||
endif()
|
||||
|
||||
if (COOLPROP_PYTHON_PYPI)
|
||||
|
||||
if (DEFINED AND_UPLOAD)
|
||||
set(_AND_UPLOAD upload)
|
||||
else()
|
||||
set(_AND_UPLOAD )
|
||||
endif()
|
||||
|
||||
add_custom_target(CoolProp
|
||||
COMMAND python prepare_pypi.py ${_AND_UPLOAD} --dist-dir=${CMAKE_INSTALL_PREFIX}/Python
|
||||
COMMAND python prepare_pypi.py --dist-dir=${CMAKE_INSTALL_PREFIX}/Python
|
||||
WORKING_DIRECTORY ${CMAKE_SOURCE_DIR}/wrappers/Python/pypi
|
||||
)
|
||||
endif()
|
||||
|
||||
@@ -3,7 +3,7 @@
|
||||
|
||||
@ARTICLE{Abramson-HPR-2011,
|
||||
author = {Evan H. Abramson},
|
||||
title = {Melting curves of argon and methane},
|
||||
title = {{Melting curves of argon and methane}},
|
||||
journal = {High Pressure Research},
|
||||
year = {2011},
|
||||
volume = {31},
|
||||
@@ -13,9 +13,32 @@
|
||||
timestamp = {2014.06.09}
|
||||
}
|
||||
|
||||
@CONFERENCE{Akasaka-Purdue-2014,
|
||||
author = {Ryo Akasaka},
|
||||
title = {{A Thermodynamic Property Model for the R-134a/245fa Mixtures}},
|
||||
booktitle = {15th International Refrigeration and Air Conditioning Conference
|
||||
at Purdue, July 14-17, 2014},
|
||||
year = {2014},
|
||||
owner = {Belli},
|
||||
timestamp = {2014.09.27}
|
||||
}
|
||||
|
||||
@ARTICLE{Akasaka-FPE-2013,
|
||||
author = {Ryo Akasaka},
|
||||
title = {{Thermodynamic property models for the difluoromethane (R-32) + trans-1,3,3,3-tetrafluoropropene
|
||||
(R-1234ze(E)) and difluoromethane + 2,3,3,3-tetrafluoropropene (R-1234yf)
|
||||
mixtures}},
|
||||
journal = {Fluid Phase Equilib.},
|
||||
year = {2013},
|
||||
volume = {358},
|
||||
pages = {98-104},
|
||||
owner = {Belli},
|
||||
timestamp = {2014.09.27}
|
||||
}
|
||||
|
||||
@CONFERENCE{Akasaka-PU-2014,
|
||||
author = {Ryo Akasaka and Yukihiro Higashi},
|
||||
title = {A Thermodynamic Property Model for the R-134a/245fa Mixtures},
|
||||
title = {{A Thermodynamic Property Model for the R-134a/245fa Mixtures}},
|
||||
booktitle = {15 th International Refrigeration and Air Conditioning Conference
|
||||
at Purdue, July 14-17, 2014},
|
||||
year = {2014},
|
||||
@@ -187,7 +210,7 @@
|
||||
}
|
||||
|
||||
@ARTICLE{Avgeri-JPCRD-2014-Benzene,
|
||||
author = {S. Avgeri and M. J. Assael and M. L. Huber and R. A. Perkins},
|
||||
author = {S. Avgeri and M. J. Assael and M. L. Huber and R. A. Perkins},
|
||||
title = {{Reference Correlation of the Viscosity of Benzene from the Triple
|
||||
Point to 675 K and up to 300 MPa}},
|
||||
journal = {J. Phys. Chem. Ref. Data},
|
||||
@@ -351,10 +374,19 @@
|
||||
timestamp = {2010.06.30}
|
||||
}
|
||||
|
||||
@PHDTHESIS{Gernert-Thesis-2013,
|
||||
author = {Georg Johannes Gernert},
|
||||
title = {{A New Helmholtz Energy Model for Humid Gases and CCS Mixtures}},
|
||||
school = {Ruhr-Universit{\:a}t Bochum},
|
||||
year = {2013},
|
||||
owner = {Belli},
|
||||
timestamp = {2014.09.27}
|
||||
}
|
||||
|
||||
@ARTICLE{Gernert-FPE-2014,
|
||||
author = {Johannes Gernert and Andreas J{\"a}ger and Roland Span},
|
||||
title = {Calculation of phase equilibria for multi-component mixtures using
|
||||
highly accurate Helmholtz energy equations of state},
|
||||
title = {{Calculation of phase equilibria for multi-component mixtures using
|
||||
highly accurate Helmholtz energy equations of state}},
|
||||
journal = {Fluid Phase Equilib.},
|
||||
year = {2014},
|
||||
volume = {375},
|
||||
|
||||
2
Doxyfile
2
Doxyfile
@@ -2049,7 +2049,7 @@ TAGFILES =
|
||||
# tag file that is based on the input files it reads. See section "Linking to
|
||||
# external documentation" for more information about the usage of tag files.
|
||||
|
||||
GENERATE_TAGFILE = CoolPropDoxyLink.tag
|
||||
GENERATE_TAGFILE = Web/_static/doxygen/CoolPropDoxyLink.tag
|
||||
|
||||
# If the ALLEXTERNALS tag is set to YES all external class will be listed in the
|
||||
# class index. If set to NO only the inherited external classes will be listed.
|
||||
|
||||
37
Readme.rst
Normal file
37
Readme.rst
Normal file
@@ -0,0 +1,37 @@
|
||||
|
||||
Welcome to CoolProp
|
||||
===================
|
||||
|
||||
CoolProp is a thermophysical property database and wrappers for a selection of programming environments.
|
||||
It offers similar functionality to REFPROP, but CoolProp is open-source and free,
|
||||
It was originally developed by Ian Bell, currently a post-doc at the University of Liege, in Liege, Belgium.
|
||||
|
||||
* CoolProp has flexible licensing terms: Commercial - ok! Academic? - ok! |license|
|
||||
|
||||
* You can get the development binaries for each platform at http://www.coolprop.dreamhosters.com:8010/binaries/.
|
||||
|
||||
* For Python, you can get latest stable version |version| via pip install coolprop |downloads|
|
||||
|
||||
* The development docs for the v5 release are at http://www.coolprop.dreamhosters.com:8010/sphinx/
|
||||
|
||||
* Travis CI helps us to keep track of integration issues |travis|
|
||||
|
||||
* Please, if there are any issues of any kind, file an issue at https://github.com/CoolProp/CoolProp/issues
|
||||
|
||||
* Also, check out our FAQ: https://github.com/CoolProp/CoolProp/blob/master/FAQ.md
|
||||
|
||||
.. |travis| image:: https://travis-ci.org/CoolProp/CoolProp.png?branch=master
|
||||
:target: https://travis-ci.org/CoolProp/CoolProp
|
||||
:alt: travis-ci
|
||||
|
||||
.. |downloads| image:: https://pypip.in/d/CoolProp/badge.png
|
||||
:target: http://pypi.python.org/pypi/CoolProp/
|
||||
:alt: downloads
|
||||
|
||||
.. |version| image:: https://pypip.in/v/CoolProp/badge.png
|
||||
:target: http://pypi.python.org/pypi/CoolProp/
|
||||
:alt: latest stable version
|
||||
|
||||
.. |license| image:: https://pypip.in/license/CoolProp/badge.png
|
||||
:target: http://pypi.python.org/pypi/CoolProp/
|
||||
:alt: license
|
||||
14
Readme.txt
14
Readme.txt
@@ -1,14 +0,0 @@
|
||||
CoolProp is a thermophysical property database and wrappers for a selection of programming environments
|
||||
|
||||
It offers similar functionality to REFPROP, but CoolProp is open-source and free, with flexible licensing terms. Commercial - ok! Academic? - ok!
|
||||
|
||||
It was originally developed by Ian Bell, currently a post-doc at the University of Liege, in Liege, Belgium.
|
||||
|
||||
The development docs for the v5 release are at http://www.coolprop.dreamhosters.com:8010/sphinx/
|
||||
|
||||
The development binaries for each platform are at http://www.coolprop.dreamhosters.com:8010/binaries/.
|
||||
|
||||
Please, if there are any issues of any kind, file an issue at https://github.com/CoolProp/CoolProp/issues
|
||||
|
||||
Also, check out our FAQ: https://github.com/CoolProp/CoolProp/blob/master/FAQ.md
|
||||
|
||||
@@ -9,5 +9,5 @@ REM ~ pdflatex CoolPropdoc.tex
|
||||
REM ~ copy /Y CoolPropdoc.pdf ..\..\_static\
|
||||
REM ~ cd ..\..
|
||||
|
||||
sphinx-apidoc -T -f -o apidoc ../CoolProp
|
||||
sphinx-apidoc -T -f -e -o apidoc C:\\Miniconda\\lib\\site-packages\\coolprop-5.0.0-py2.7-win-amd64.egg\\CoolProp
|
||||
mingw32-make html
|
||||
@@ -1,6 +0,0 @@
|
||||
AbstractState Module
|
||||
====================
|
||||
|
||||
.. automodule:: CoolProp.AbstractState
|
||||
:members: AbstractState
|
||||
:undoc-members:
|
||||
7
Web/apidoc/CoolProp.BibtexParser.rst
Normal file
7
Web/apidoc/CoolProp.BibtexParser.rst
Normal file
@@ -0,0 +1,7 @@
|
||||
CoolProp.BibtexParser module
|
||||
============================
|
||||
|
||||
.. automodule:: CoolProp.BibtexParser
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
7
Web/apidoc/CoolProp.CoolProp.rst
Normal file
7
Web/apidoc/CoolProp.CoolProp.rst
Normal file
@@ -0,0 +1,7 @@
|
||||
CoolProp.CoolProp module
|
||||
========================
|
||||
|
||||
.. automodule:: CoolProp.CoolProp
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
7
Web/apidoc/CoolProp.GUI.CoolPropGUI.rst
Normal file
7
Web/apidoc/CoolProp.GUI.CoolPropGUI.rst
Normal file
@@ -0,0 +1,7 @@
|
||||
CoolProp.GUI.CoolPropGUI module
|
||||
===============================
|
||||
|
||||
.. automodule:: CoolProp.GUI.CoolPropGUI
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
7
Web/apidoc/CoolProp.GUI.PsychScript.rst
Normal file
7
Web/apidoc/CoolProp.GUI.PsychScript.rst
Normal file
@@ -0,0 +1,7 @@
|
||||
CoolProp.GUI.PsychScript module
|
||||
===============================
|
||||
|
||||
.. automodule:: CoolProp.GUI.PsychScript
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
18
Web/apidoc/CoolProp.GUI.rst
Normal file
18
Web/apidoc/CoolProp.GUI.rst
Normal file
@@ -0,0 +1,18 @@
|
||||
CoolProp.GUI package
|
||||
====================
|
||||
|
||||
Submodules
|
||||
----------
|
||||
|
||||
.. toctree::
|
||||
|
||||
CoolProp.GUI.CoolPropGUI
|
||||
CoolProp.GUI.PsychScript
|
||||
|
||||
Module contents
|
||||
---------------
|
||||
|
||||
.. automodule:: CoolProp.GUI
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
7
Web/apidoc/CoolProp.HumidAirProp.rst
Normal file
7
Web/apidoc/CoolProp.HumidAirProp.rst
Normal file
@@ -0,0 +1,7 @@
|
||||
CoolProp.HumidAirProp module
|
||||
============================
|
||||
|
||||
.. automodule:: CoolProp.HumidAirProp
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
7
Web/apidoc/CoolProp.Plots.Common.rst
Normal file
7
Web/apidoc/CoolProp.Plots.Common.rst
Normal file
@@ -0,0 +1,7 @@
|
||||
CoolProp.Plots.Common module
|
||||
============================
|
||||
|
||||
.. automodule:: CoolProp.Plots.Common
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
7
Web/apidoc/CoolProp.Plots.Plots.rst
Normal file
7
Web/apidoc/CoolProp.Plots.Plots.rst
Normal file
@@ -0,0 +1,7 @@
|
||||
CoolProp.Plots.Plots module
|
||||
===========================
|
||||
|
||||
.. automodule:: CoolProp.Plots.Plots
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
7
Web/apidoc/CoolProp.Plots.PsychChart.rst
Normal file
7
Web/apidoc/CoolProp.Plots.PsychChart.rst
Normal file
@@ -0,0 +1,7 @@
|
||||
CoolProp.Plots.PsychChart module
|
||||
================================
|
||||
|
||||
.. automodule:: CoolProp.Plots.PsychChart
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
7
Web/apidoc/CoolProp.Plots.PsychScript.rst
Normal file
7
Web/apidoc/CoolProp.Plots.PsychScript.rst
Normal file
@@ -0,0 +1,7 @@
|
||||
CoolProp.Plots.PsychScript module
|
||||
=================================
|
||||
|
||||
.. automodule:: CoolProp.Plots.PsychScript
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
7
Web/apidoc/CoolProp.Plots.SimpleCycles.rst
Normal file
7
Web/apidoc/CoolProp.Plots.SimpleCycles.rst
Normal file
@@ -0,0 +1,7 @@
|
||||
CoolProp.Plots.SimpleCycles module
|
||||
==================================
|
||||
|
||||
.. automodule:: CoolProp.Plots.SimpleCycles
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
7
Web/apidoc/CoolProp.Plots.Tests.rst
Normal file
7
Web/apidoc/CoolProp.Plots.Tests.rst
Normal file
@@ -0,0 +1,7 @@
|
||||
CoolProp.Plots.Tests module
|
||||
===========================
|
||||
|
||||
.. automodule:: CoolProp.Plots.Tests
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
@@ -1,35 +1,22 @@
|
||||
Plots Package
|
||||
=============
|
||||
CoolProp.Plots package
|
||||
======================
|
||||
|
||||
:mod:`Plots` Package
|
||||
--------------------
|
||||
Submodules
|
||||
----------
|
||||
|
||||
.. toctree::
|
||||
|
||||
CoolProp.Plots.Common
|
||||
CoolProp.Plots.Plots
|
||||
CoolProp.Plots.PsychChart
|
||||
CoolProp.Plots.PsychScript
|
||||
CoolProp.Plots.SimpleCycles
|
||||
CoolProp.Plots.Tests
|
||||
|
||||
Module contents
|
||||
---------------
|
||||
|
||||
.. automodule:: CoolProp.Plots
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
|
||||
:mod:`Plots` Module
|
||||
-------------------
|
||||
|
||||
.. automodule:: CoolProp.Plots.Plots
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
|
||||
:mod:`PsychChart` Module
|
||||
------------------------
|
||||
|
||||
.. automodule:: CoolProp.Plots.PsychChart
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
|
||||
:mod:`SimpleCycles` Module
|
||||
--------------------------
|
||||
|
||||
.. automodule:: CoolProp.Plots.SimpleCycles
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
|
||||
|
||||
7
Web/apidoc/CoolProp.State.rst
Normal file
7
Web/apidoc/CoolProp.State.rst
Normal file
@@ -0,0 +1,7 @@
|
||||
CoolProp.State module
|
||||
=====================
|
||||
|
||||
.. automodule:: CoolProp.State
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
7
Web/apidoc/CoolProp.constants.rst
Normal file
7
Web/apidoc/CoolProp.constants.rst
Normal file
@@ -0,0 +1,7 @@
|
||||
CoolProp.constants module
|
||||
=========================
|
||||
|
||||
.. automodule:: CoolProp.constants
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
@@ -1,9 +1,32 @@
|
||||
CoolProp Module
|
||||
===============
|
||||
CoolProp package
|
||||
================
|
||||
|
||||
.. automodule:: CoolProp.CoolProp
|
||||
:synopsis:
|
||||
Subpackages
|
||||
-----------
|
||||
|
||||
.. toctree::
|
||||
|
||||
CoolProp.GUI
|
||||
CoolProp.Plots
|
||||
CoolProp.tests
|
||||
|
||||
Submodules
|
||||
----------
|
||||
|
||||
.. toctree::
|
||||
|
||||
CoolProp.BibtexParser
|
||||
CoolProp.CoolProp
|
||||
CoolProp.CoolProp
|
||||
CoolProp.HumidAirProp
|
||||
CoolProp.State
|
||||
CoolProp.constants
|
||||
CoolProp.constants
|
||||
|
||||
Module contents
|
||||
---------------
|
||||
|
||||
.. automodule:: CoolProp
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
:exclude-members: State,HAProps,HAProps_Aux,PureFluidClass
|
||||
27
Web/apidoc/CoolProp.tests.rst
Normal file
27
Web/apidoc/CoolProp.tests.rst
Normal file
@@ -0,0 +1,27 @@
|
||||
CoolProp.tests package
|
||||
======================
|
||||
|
||||
Submodules
|
||||
----------
|
||||
|
||||
.. toctree::
|
||||
|
||||
CoolProp.tests.runner
|
||||
CoolProp.tests.test_CoolPropState
|
||||
CoolProp.tests.test_HAProps
|
||||
CoolProp.tests.test_Props
|
||||
CoolProp.tests.test_Props1
|
||||
CoolProp.tests.test_Saturation
|
||||
CoolProp.tests.test_State
|
||||
CoolProp.tests.test_Units_CPState
|
||||
CoolProp.tests.test_consistency
|
||||
CoolProp.tests.test_param_getters
|
||||
CoolProp.tests.test_plots
|
||||
|
||||
Module contents
|
||||
---------------
|
||||
|
||||
.. automodule:: CoolProp.tests
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
7
Web/apidoc/CoolProp.tests.runner.rst
Normal file
7
Web/apidoc/CoolProp.tests.runner.rst
Normal file
@@ -0,0 +1,7 @@
|
||||
CoolProp.tests.runner module
|
||||
============================
|
||||
|
||||
.. automodule:: CoolProp.tests.runner
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
7
Web/apidoc/CoolProp.tests.test_CoolPropState.rst
Normal file
7
Web/apidoc/CoolProp.tests.test_CoolPropState.rst
Normal file
@@ -0,0 +1,7 @@
|
||||
CoolProp.tests.test_CoolPropState module
|
||||
========================================
|
||||
|
||||
.. automodule:: CoolProp.tests.test_CoolPropState
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
7
Web/apidoc/CoolProp.tests.test_HAProps.rst
Normal file
7
Web/apidoc/CoolProp.tests.test_HAProps.rst
Normal file
@@ -0,0 +1,7 @@
|
||||
CoolProp.tests.test_HAProps module
|
||||
==================================
|
||||
|
||||
.. automodule:: CoolProp.tests.test_HAProps
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
7
Web/apidoc/CoolProp.tests.test_Props.rst
Normal file
7
Web/apidoc/CoolProp.tests.test_Props.rst
Normal file
@@ -0,0 +1,7 @@
|
||||
CoolProp.tests.test_Props module
|
||||
================================
|
||||
|
||||
.. automodule:: CoolProp.tests.test_Props
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
7
Web/apidoc/CoolProp.tests.test_Props1.rst
Normal file
7
Web/apidoc/CoolProp.tests.test_Props1.rst
Normal file
@@ -0,0 +1,7 @@
|
||||
CoolProp.tests.test_Props1 module
|
||||
=================================
|
||||
|
||||
.. automodule:: CoolProp.tests.test_Props1
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
7
Web/apidoc/CoolProp.tests.test_Saturation.rst
Normal file
7
Web/apidoc/CoolProp.tests.test_Saturation.rst
Normal file
@@ -0,0 +1,7 @@
|
||||
CoolProp.tests.test_Saturation module
|
||||
=====================================
|
||||
|
||||
.. automodule:: CoolProp.tests.test_Saturation
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
7
Web/apidoc/CoolProp.tests.test_State.rst
Normal file
7
Web/apidoc/CoolProp.tests.test_State.rst
Normal file
@@ -0,0 +1,7 @@
|
||||
CoolProp.tests.test_State module
|
||||
================================
|
||||
|
||||
.. automodule:: CoolProp.tests.test_State
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
7
Web/apidoc/CoolProp.tests.test_Units_CPState.rst
Normal file
7
Web/apidoc/CoolProp.tests.test_Units_CPState.rst
Normal file
@@ -0,0 +1,7 @@
|
||||
CoolProp.tests.test_Units_CPState module
|
||||
========================================
|
||||
|
||||
.. automodule:: CoolProp.tests.test_Units_CPState
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
7
Web/apidoc/CoolProp.tests.test_consistency.rst
Normal file
7
Web/apidoc/CoolProp.tests.test_consistency.rst
Normal file
@@ -0,0 +1,7 @@
|
||||
CoolProp.tests.test_consistency module
|
||||
======================================
|
||||
|
||||
.. automodule:: CoolProp.tests.test_consistency
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
7
Web/apidoc/CoolProp.tests.test_param_getters.rst
Normal file
7
Web/apidoc/CoolProp.tests.test_param_getters.rst
Normal file
@@ -0,0 +1,7 @@
|
||||
CoolProp.tests.test_param_getters module
|
||||
========================================
|
||||
|
||||
.. automodule:: CoolProp.tests.test_param_getters
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
7
Web/apidoc/CoolProp.tests.test_plots.rst
Normal file
7
Web/apidoc/CoolProp.tests.test_plots.rst
Normal file
@@ -0,0 +1,7 @@
|
||||
CoolProp.tests.test_plots module
|
||||
================================
|
||||
|
||||
.. automodule:: CoolProp.tests.test_plots
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
@@ -1,7 +0,0 @@
|
||||
HumidAirProp Module
|
||||
===================
|
||||
|
||||
.. automodule:: CoolProp.HumidAirProp
|
||||
:members: HAProps, HAProps_Aux
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
@@ -1,42 +0,0 @@
|
||||
Plots Package
|
||||
=============
|
||||
|
||||
:mod:`CoolProp.Plots` Package
|
||||
-----------------------------
|
||||
|
||||
.. automodule:: CoolProp.Plots
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
|
||||
:mod:`CoolProp.Plots.Common` Module
|
||||
-------------------------------------
|
||||
|
||||
.. automodule:: CoolProp.Plots.Common
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
|
||||
:mod:`CoolProp.Plots.Plots` Module
|
||||
----------------------------------
|
||||
|
||||
.. automodule:: CoolProp.Plots.Plots
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
|
||||
:mod:`CoolProp.Plots.PsychChart` Module
|
||||
---------------------------------------
|
||||
|
||||
.. automodule:: CoolProp.Plots.PsychChart
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
|
||||
:mod:`SimpleCycles` Module
|
||||
--------------------------
|
||||
|
||||
.. automodule:: CoolProp.Plots.SimpleCycles
|
||||
:members:
|
||||
:undoc-members:
|
||||
:show-inheritance:
|
||||
@@ -1,6 +0,0 @@
|
||||
State Module
|
||||
============
|
||||
|
||||
.. automodule:: CoolProp.State
|
||||
:members: State, PureFluidClass
|
||||
:undoc-members:
|
||||
@@ -1,11 +0,0 @@
|
||||
CoolProp API
|
||||
============
|
||||
|
||||
.. toctree::
|
||||
:maxdepth: 4
|
||||
|
||||
CoolProp
|
||||
HumidAirProp
|
||||
Plots
|
||||
State
|
||||
AbstractState
|
||||
14
Web/conf.py
14
Web/conf.py
@@ -13,6 +13,7 @@
|
||||
# serve to show the default.
|
||||
|
||||
import sys, os
|
||||
|
||||
sys.path.insert(0, os.path.abspath('_ext'))
|
||||
try:
|
||||
import sphinxcontrib.doxylink
|
||||
@@ -20,13 +21,24 @@ except ImportError:
|
||||
|
||||
print('Unable to import sphinxcontrib.doxylink; try to run "pip install sphinxcontrib-doxylink"')
|
||||
|
||||
|
||||
import glob
|
||||
import subprocess
|
||||
|
||||
# This part finds all scripts and runs them
|
||||
scripts = glob.glob(os.path.join('scripts','*.py'))
|
||||
for script in scripts:
|
||||
subprocess.call('python {0}'.format(os.path.basename(script)), cwd='scripts', shell=True)
|
||||
|
||||
|
||||
|
||||
#~ # If your extensions are in another directory, add it here. If the directory
|
||||
#~ # is relative to the documentation root, use os.path.abspath to make it
|
||||
#~ # absolute, like shown here.
|
||||
#~ sys.path.append(os.path.abspath('sphinxext'))
|
||||
|
||||
doxylink = {
|
||||
'cpapi' : ('_static/doxygen/CoolPropDoxyLink.tag', '_static/doxygen/html')
|
||||
'cpapi' : ('_static/doxygen/CoolPropDoxyLink.tag', '../_static/doxygen/html')
|
||||
}
|
||||
|
||||
# -- General configuration -----------------------------------------------------
|
||||
|
||||
@@ -1,15 +1,15 @@
|
||||
import CoolProp5
|
||||
import CoolProp
|
||||
import pandas
|
||||
grouping = dict()
|
||||
grouping2 = []
|
||||
# Group aliases
|
||||
for parameter in CoolProp5.get('parameter_list').split(','):
|
||||
for parameter in CoolProp.get('parameter_list').split(','):
|
||||
|
||||
index = CoolProp5.CoolProp.get_parameter_index(parameter)
|
||||
units = CoolProp5.CoolProp.get_parameter_information(index, 'units').replace('-',' ')
|
||||
IO = CoolProp5.CoolProp.get_parameter_information(index, 'IO')
|
||||
long = CoolProp5.CoolProp.get_parameter_information(index, 'long')
|
||||
short = CoolProp5.CoolProp.get_parameter_information(index, 'short')
|
||||
index = CoolProp.CoolProp.get_parameter_index(parameter)
|
||||
units = CoolProp.CoolProp.get_parameter_information(index, 'units').replace('-',' ')
|
||||
IO = CoolProp.CoolProp.get_parameter_information(index, 'IO')
|
||||
long = CoolProp.CoolProp.get_parameter_information(index, 'long')
|
||||
short = CoolProp.CoolProp.get_parameter_information(index, 'short')
|
||||
|
||||
RHS = (units, IO, long)
|
||||
if RHS not in grouping:
|
||||
|
||||
@@ -1,48 +1,67 @@
|
||||
.. constructed with the build_parameter_table.py script in this folder
|
||||
|
||||
================================= ======= ============ =========================================================
|
||||
Parameter Units Input/Output Description
|
||||
================================= ======= ============ =========================================================
|
||||
``D``, ``Dmass`` kg/m^3 IO Mass density
|
||||
``Delta`` IO Reduced density (rho/rhoc)
|
||||
``Dmolar`` mol/m^3 IO Molar density
|
||||
``H``, ``Hmass`` J/kg IO Mass specific enthalpy
|
||||
``Hmolar`` J/mol IO Molar specific enthalpy
|
||||
``P`` Pa IO Pressure
|
||||
``Q`` mol/mol IO Mass vapor quality
|
||||
``S``, ``Smass`` J/kg/K IO Mass specific entropy
|
||||
``Smolar`` J/mol/K IO Molar specific entropy
|
||||
``T`` K IO Temperature
|
||||
``Tau`` IO Reciprocal reduced temperature (Tc/T)
|
||||
``U``, ``Umass`` J/kg IO Mass specific internal energy
|
||||
``Umolar`` J/mol IO Molar specific internal energy
|
||||
``Bvirial`` O Second virial coefficient
|
||||
``C``, ``Cpmass`` J/kg/K O Mass specific constant presssure specific heat
|
||||
``Cpmolar`` J/mol/K O Molar specific constant presssure specific heat
|
||||
``Cvirial`` O Third virial coefficient
|
||||
``Cvmass``, ``O`` J/kg/K O Mass specific constant volume specific heat
|
||||
``Cvmolar`` J/mol/K O Molar specific constant volume specific heat
|
||||
``FH`` O Flammability hazard
|
||||
``GWP100`` O 100-year gobal warming potential
|
||||
``GWP20`` O 20-year gobal warming potential
|
||||
``GWP500`` O 500-year gobal warming potential
|
||||
``HH`` O Health hazard
|
||||
``L``, ``conductivity`` W/m/K O Thermal conductivity
|
||||
``ODP`` O Ozone depletion potential
|
||||
``PH`` O Physical hazard
|
||||
``T_critical``, ``Tcrit`` K O Temperature at the critical point
|
||||
``T_max`` K O Maximum temperature limit
|
||||
``T_min`` K O Minimum temperature limit
|
||||
``T_reducing`` K O Temperature at the reducing point
|
||||
``T_triple``, ``Ttriple`` K O Temperature at the triple point
|
||||
``V``, ``viscosity`` Pa s O Viscosity
|
||||
``dBvirial_dT`` O Derivative of second virial coefficient with respect to T
|
||||
``dCvirial_dT`` O Derivative of third virial coefficient with respect to T
|
||||
``isothermal_compressibility`` 1/Pa O Isothermal compressibility
|
||||
``molar_mass`` kg/mol O Molar mass
|
||||
``p_critical``, ``pcrit`` Pa O Pressure at the critical point
|
||||
``rhocrit``, ``rhomass_critical`` kg/m^3 O Mass density at critical point
|
||||
``rhomolar_critical`` mol/m^3 O Molar density at critical point
|
||||
``rhomolar_reducing`` mol/m^3 O Molar density at reducing point
|
||||
``speed_of_sound`` m/s O Speed of sound
|
||||
================================= ======= ============ =========================================================
|
||||
====================================================================================== ======= ============ =========================================================
|
||||
Parameter Units Input/Output Description
|
||||
====================================================================================== ======= ============ =========================================================
|
||||
``DELTA``, ``Delta`` IO Reduced density (rho/rhoc)
|
||||
``DMOLAR``, ``Dmolar`` mol/m^3 IO Molar density
|
||||
``D``, ``DMASS``, ``Dmass`` kg/m^3 IO Mass density
|
||||
``GMASS``, ``Gmass`` J/kg IO Mass specific Gibbs energy
|
||||
``GMOLAR``, ``Gmolar`` J/mol IO Molar specific Gibbs energy
|
||||
``HMOLAR``, ``Hmolar`` J/mol IO Molar specific enthalpy
|
||||
``H``, ``HMASS``, ``Hmass`` J/kg IO Mass specific enthalpy
|
||||
``P`` Pa IO Pressure
|
||||
``Q`` mol/mol IO Mass vapor quality
|
||||
``SMOLAR``, ``Smolar`` J/mol/K IO Molar specific entropy
|
||||
``S``, ``SMASS``, ``Smass`` J/kg/K IO Mass specific entropy
|
||||
``TAU``, ``Tau`` IO Reciprocal reduced temperature (Tc/T)
|
||||
``T`` K IO Temperature
|
||||
``UMOLAR``, ``Umolar`` J/mol IO Molar specific internal energy
|
||||
``U``, ``UMASS``, ``Umass`` J/kg IO Mass specific internal energy
|
||||
``ALPHA0``, ``alpha0`` O Ideal Helmholtz energy
|
||||
``ALPHAR``, ``alphar`` O Residual Helmholtz energy
|
||||
``A``, ``SPEED_OF_SOUND``, ``speed_of_sound`` m/s O Speed of sound
|
||||
``BVIRIAL``, ``Bvirial`` O Second virial coefficient
|
||||
``CONDUCTIVITY``, ``L``, ``conductivity`` W/m/K O Thermal conductivity
|
||||
``CP0MASS``, ``Cp0mass`` J/kg/K O Ideal gas mass specific constant presssure specific heat
|
||||
``CP0MOLAR``, ``Cp0molar`` J/mol/K O Ideal gas molar specific constant presssure specific heat
|
||||
``CPMOLAR``, ``Cpmolar`` J/mol/K O Molar specific constant presssure specific heat
|
||||
``CVIRIAL``, ``Cvirial`` O Third virial coefficient
|
||||
``CVMASS``, ``Cvmass``, ``O`` J/kg/K O Mass specific constant volume specific heat
|
||||
``CVMOLAR``, ``Cvmolar`` J/mol/K O Molar specific constant volume specific heat
|
||||
``C``, ``CPMASS``, ``Cpmass`` J/kg/K O Mass specific constant presssure specific heat
|
||||
``DALPHA0_DDELTA_CONSTTAU``, ``dalpha0_ddelta_consttau`` O Derivative of ideal Helmholtz energy with delta
|
||||
``DALPHA0_DTAU_CONSTDELTA``, ``dalpha0_dtau_constdelta`` O Derivative of ideal Helmholtz energy with tau
|
||||
``DALPHAR_DDELTA_CONSTTAU``, ``dalphar_ddelta_consttau`` O Derivative of residual Helmholtz energy with delta
|
||||
``DALPHAR_DTAU_CONSTDELTA``, ``dalphar_dtau_constdelta`` O Derivative of residual Helmholtz energy with tau
|
||||
``DBVIRIAL_DT``, ``dBvirial_dT`` O Derivative of second virial coefficient with respect to T
|
||||
``DCVIRIAL_DT``, ``dCvirial_dT`` O Derivative of third virial coefficient with respect to T
|
||||
``FH`` O Flammability hazard
|
||||
``FUNDAMENTAL_DERIVATIVE_OF_GAS_DYNAMICS``, ``fundamental_derivative_of_gas_dynamics`` O Fundamental_derivative_of_gas_dynamics
|
||||
``GWP100`` O 100-year gobal warming potential
|
||||
``GWP20`` O 20-year gobal warming potential
|
||||
``GWP500`` O 500-year gobal warming potential
|
||||
``HH`` O Health hazard
|
||||
``ISOBARIC_EXPANSION_COEFFICIENT``, ``isobaric_expansion_coefficient`` 1/K O Isobaric expansion coefficient
|
||||
``ISOTHERMAL_COMPRESSIBILITY``, ``isothermal_compressibility`` 1/Pa O Isothermal compressibility
|
||||
``M``, ``MOLAR_MASS``, ``MOLEMASS``, ``molar_mass``, ``molemass`` kg/mol O Molar mass
|
||||
``ODP`` O Ozone depletion potential
|
||||
``PCRIT``, ``P_CRITICAL``, ``p_critical``, ``pcrit`` Pa O Pressure at the critical point
|
||||
``PH`` O Physical hazard
|
||||
``PMAX``, ``P_MAX``, ``P_max``, ``pmax`` Pa O Maximum pressure limit
|
||||
``PRANDTL``, ``Prandtl`` O Prandtl number
|
||||
``PTRIPLE``, ``P_TRIPLE``, ``p_triple``, ``ptriple`` Pa O Pressure at the triple point (pure only)
|
||||
``P_MIN``, ``P_min`` Pa O Minimum pressure limit
|
||||
``RHOCRIT``, ``RHOMASS_CRITICAL``, ``rhocrit``, ``rhomass_critical`` kg/m^3 O Mass density at critical point
|
||||
``RHOMASS_REDUCING``, ``rhomass_reducing`` kg/m^3 O Mass density at reducing point
|
||||
``RHOMOLAR_CRITICAL``, ``rhomolar_critical`` mol/m^3 O Molar density at critical point
|
||||
``RHOMOLAR_REDUCING``, ``rhomolar_reducing`` mol/m^3 O Molar density at reducing point
|
||||
``SURFACE_TENSION``, ``surface_tension`` N/m O Surface tension
|
||||
``TCRIT``, ``T_CRITICAL``, ``T_critical``, ``Tcrit`` K O Temperature at the critical point
|
||||
``TMAX``, ``T_MAX``, ``T_max``, ``Tmax`` K O Maximum temperature limit
|
||||
``TMIN``, ``T_MIN``, ``T_min``, ``Tmin`` K O Minimum temperature limit
|
||||
``TTRIPLE``, ``T_TRIPLE``, ``T_triple``, ``Ttriple`` K O Temperature at the triple point
|
||||
``T_REDUCING``, ``T_reducing`` K O Temperature at the reducing point
|
||||
``V``, ``VISCOSITY``, ``viscosity`` Pa s O Viscosity
|
||||
``Z`` O Compressibility factor
|
||||
====================================================================================== ======= ============ =========================================================
|
||||
|
||||
@@ -67,7 +67,7 @@ Once mono c# is installed, you can run the builder and tests using::
|
||||
# Move into the folder you just created
|
||||
cd CoolProp
|
||||
# Make a build folder
|
||||
mkdir -p build/Csharp && cd build
|
||||
mkdir build && cd build
|
||||
# Build the makefile using CMake
|
||||
cmake .. -DCOOLPROP_CSHARP_MODULE=ON -DBUILD_TESTING=ON
|
||||
# Make the C# files (by default files will be generated in folder install_root/Csharp relative to CMakeLists.txt file)
|
||||
|
||||
@@ -9,7 +9,7 @@ Compilers
|
||||
|
||||
On linux, you need gcc and gfortran, which are easy to install using your package manager.
|
||||
|
||||
On windows, the most reliable mixed compilation seems to be using the mingw-provided gfortran/gcc combination from mingw-get. Theese are the versions used as of June 20, 2014::
|
||||
On windows, the most reliable mixed compilation seems to be using the mingw-provided gfortran/gcc combination from mingw-get. These are the versions used as of June 20, 2014::
|
||||
|
||||
>gfortran --version
|
||||
GNU Fortran (GCC) 4.8.1
|
||||
@@ -30,14 +30,14 @@ On linux/OSX, start in root folder of recursively-cloned CoolProp repo and do::
|
||||
|
||||
mkdir build && cd build
|
||||
mkdir gccstatic && cd gccstatic
|
||||
cmake ../.. -DCOOLPROP_STATIC_LIBRARY=ON
|
||||
cmake ../.. -DCOOLPROP_EXTERNC_STATIC_LIBRARY=ON
|
||||
cmake --build .
|
||||
|
||||
On Windows, the call to CMake should be done using the MinGW generator, but otherwise procedure is the same::
|
||||
On Windows, the call to CMake should be done using the MinGW generator, but otherwise the procedure is the same::
|
||||
|
||||
mkdir build && cd build
|
||||
mkdir gccstatic && cd gccstatic
|
||||
cmake ../.. -G "MinGW Makefiles" -DCOOLPROP_STATIC_LIBRARY=ON
|
||||
cmake ../.. -G "MinGW Makefiles" -DCOOLPROP_EXTERNC_STATIC_LIBRARY=ON
|
||||
cmake --build .
|
||||
|
||||
This will generate the file libCoolProp.a which is a GCC static library that can be linked with GCC/GFORTRAN code. Copy this .a file into the directory with the coolprop FORTRAN example ``cool_fortran_bind.f90``:
|
||||
|
||||
36
Web/coolprop/wrappers/StaticLibrary/index.rst
Normal file
36
Web/coolprop/wrappers/StaticLibrary/index.rst
Normal file
@@ -0,0 +1,36 @@
|
||||
.. _static_library:
|
||||
|
||||
**************
|
||||
Static Library
|
||||
**************
|
||||
|
||||
Static libraries can be used to compile all of CoolProp into one compilation unit, and then link that with user code. This can be advantageous as CoolProp only needs to be compiled once and fast compilation of the user-defined code is then possible.
|
||||
|
||||
When writing your own C++ code, it is advised to compile CoolProp to a static library and then link CoolProp and your own code
|
||||
|
||||
Pre-compiled Binaries
|
||||
=====================
|
||||
Pre-compiled release binaries can be downloaded from :sfdownloads:`static_library`. Development binaries coming from the buildbot server can be found at :bbbinaries:`static_library`. These static libraries are only useful if the compiler used to make the static library agrees with the static library that will be used to build your other code. So best to follow the below instructions to build your own static library.
|
||||
|
||||
User-Compiled Binaries
|
||||
======================
|
||||
|
||||
Common Requirements
|
||||
-------------------
|
||||
Compilation of the static library requires a few :ref:`common wrapper pre-requisites <wrapper_common_prereqs>`
|
||||
|
||||
Compile
|
||||
-------
|
||||
|
||||
You can build the static library using::
|
||||
|
||||
# Check out the sources for CoolProp
|
||||
git clone https://github.com/CoolProp/CoolProp --recursive
|
||||
# Move into the folder you just created
|
||||
cd CoolProp
|
||||
# Make a build folder
|
||||
mkdir -p build && cd build
|
||||
# Build the makefile using CMake
|
||||
cmake .. -DCOOLPROP_STATIC_LIBRARY=ON
|
||||
# Make the static library
|
||||
make VERBOSE=1
|
||||
@@ -9,8 +9,9 @@ CoolProp at its core is a C++ library, but it can be of interest to use this cod
|
||||
Downloads and instructions for each wrapper are included in the page for the wrapper given in the table below.
|
||||
|
||||
======================================= =========================== =======================================
|
||||
Language Operating Systems Notes
|
||||
Target Operating Systems Notes
|
||||
======================================= =========================== =======================================
|
||||
:ref:`Static library <static_library>` linux, OSX, win
|
||||
:ref:`Python <Python>` linux, OSX, win Wrapper is Cython based
|
||||
:ref:`Octave <Octave>` linux, OSX, win Wrapper is SWIG based
|
||||
:ref:`C# <Csharp>` linux, OSX, win Wrapper is SWIG based
|
||||
@@ -90,3 +91,4 @@ OSX should come with a c++ compiler (clang), for git and cmake your best bet is
|
||||
LibreOffice/index.rst
|
||||
Excel/index.rst
|
||||
Maple/index.rst
|
||||
StaticLibrary/index.rst
|
||||
|
||||
@@ -3,6 +3,54 @@
|
||||
Buildbot
|
||||
********
|
||||
|
||||
Buildbot masters and slaves
|
||||
===========================
|
||||
|
||||
Master
|
||||
------
|
||||
|
||||
From the root of the git checkout (this will use the master.cfg from CoolProp)::
|
||||
|
||||
pip install buildbot
|
||||
cd dev/buildbot
|
||||
buildbot create-master master
|
||||
buildbot start master
|
||||
|
||||
The file ``buildbot-private.py`` (which is a python module with the passwords for the slaves as well as the buildbot website), should also be placed in the master folder next to master.cfg. Alternatively, you can put the ``buildbot_private.py`` in another folder on the master's computer and make a soft-link in the master folder to point to the buildbot_private.py file.
|
||||
|
||||
If you want to completely restart the master, you can do::
|
||||
|
||||
buildbot restart master
|
||||
|
||||
but usually a::
|
||||
|
||||
buildbot reconfig master
|
||||
|
||||
will do the job since it will just reparse the configuration file without signing you out of the server
|
||||
|
||||
To ensure that the buildbot server stays online, you can make a script with the contents::
|
||||
|
||||
buildbot start /path/to/master_folder
|
||||
|
||||
and add it to a cron job
|
||||
|
||||
Slaves
|
||||
------
|
||||
|
||||
To start a slave connected to a buildbot master at IP address 10.0.0.2 (default for host for VirtualBox), with a slave named ``example-slave`` and passsword ``pass``, run the command::
|
||||
|
||||
buildslave create-slave slave 10.0.0.2:9989 example-slave pass
|
||||
buildslave start slave
|
||||
|
||||
|
||||
If the master is somewhere else, just change the IP address. As of Sept, 2014, the master was at www.coolprop.dreamhosters.com. The buildbot_private.py on the master holds the required passwords.
|
||||
|
||||
On linux, you can add the following lines to the end of your ``~/.profile`` file (similar ideas apply on other platforms) to autostart the slave when the user logs in::
|
||||
|
||||
# Connect to the buildbot master
|
||||
buildslave start ~/slave
|
||||
|
||||
|
||||
Setting MIME type handler
|
||||
=========================
|
||||
|
||||
|
||||
@@ -3,11 +3,10 @@
|
||||
|
||||
|
||||
@Book{ASHRAE2001,
|
||||
Title = {2001 ASHRAE Handbook: Fundamentals},
|
||||
Author = {American Society of Heating, Refrigerating and Air-Conditioning Engineers},
|
||||
Publisher = {ASHRAE},
|
||||
Title = {{2001 ASHRAE Handbook: Fundamentals}},
|
||||
Author = {{American Society of Heating, Refrigerating and Air-Conditioning Engineers}},
|
||||
Publisher = {{ASHRAE}},
|
||||
Year = {2001},
|
||||
Series = {Ashrae Handbook Fundamentals Systems-international Metric System},
|
||||
Volume = {111},
|
||||
|
||||
ISBN = {9781883413880},
|
||||
@@ -15,22 +14,24 @@
|
||||
Timestamp = {2014.09.17}
|
||||
}
|
||||
|
||||
@Article{Cesar2013,
|
||||
Title = {An amazing title},
|
||||
Author = {Jean C{\'e}sar},
|
||||
Journal = {Nice Journal},
|
||||
Year = {2013},
|
||||
@Manual{Jones2001,
|
||||
Title = {{SciPy}: Open source scientific tools for {Python}},
|
||||
Author = {Eric Jones and Travis Oliphant and Pearu Peterson and others},
|
||||
|
||||
Month = jan,
|
||||
Pages = {12--23},
|
||||
Volume = {12},
|
||||
|
||||
Abstract = {This is an abstract. This line should be long enough to test
|
||||
multilines...},
|
||||
Comments = {A comment},
|
||||
Keywords = {keyword1, keyword2},
|
||||
Owner = {jowr},
|
||||
Timestamp = {2014.09.15}
|
||||
Timestamp = {2014.09.24},
|
||||
Url = {http://www.scipy.org/}
|
||||
}
|
||||
|
||||
@TechReport{Kauffeld2001,
|
||||
Title = {{RP-1166---Behavior of Ice Slurries in Thermal Storage Systems}},
|
||||
Author = {Michael Kauffeld},
|
||||
Institution = {{Danish Technological Institute}},
|
||||
Year = {2001},
|
||||
Note = {{Sponsored by ASHRAE Technical Committee 6.9 Thermal Storage}},
|
||||
|
||||
Owner = {jowr},
|
||||
Timestamp = {2014.09.22}
|
||||
}
|
||||
|
||||
@Book{Melinder2010,
|
||||
@@ -43,10 +44,53 @@
|
||||
Timestamp = {2014.09.17}
|
||||
}
|
||||
|
||||
@Article{Patek2006,
|
||||
Title = {{A computationally effective formulation of the thermodynamic properties of LiBr-H2O solutions from 273 to 500 K over full composition range}},
|
||||
Author = {Jaroslav P\'atek and Jaroslav Klomfar},
|
||||
Journal = {International Journal of Refrigeration},
|
||||
Year = {2006},
|
||||
|
||||
Month = {June},
|
||||
Number = {4},
|
||||
Pages = {566--578},
|
||||
Volume = {29},
|
||||
|
||||
Doi = {10.1016/j.ijrefrig.2005.10.007},
|
||||
Owner = {jowr},
|
||||
Timestamp = {2013.11.22}
|
||||
}
|
||||
|
||||
@InBook{Preisegger2010,
|
||||
Title = {VDI Heat Atlas},
|
||||
Author = {Ewald Preisegger and Felix Flohr and Gernot Krakat and Andreas Gl{\"u}ck and Dietmar Hunold},
|
||||
Chapter = {D4 Properties of Industrial Heat Transfer Media},
|
||||
Editor = {Peter Stephan},
|
||||
Pages = {419--512},
|
||||
Publisher = {Springer},
|
||||
Year = {2010},
|
||||
|
||||
Address = {Berlin Heidelberg},
|
||||
Edition = {2nd},
|
||||
|
||||
Doi = {10.1007/978-3-540-77877-6_20},
|
||||
Owner = {jowr},
|
||||
Timestamp = {2013.06.18}
|
||||
}
|
||||
|
||||
@Book{Schmidt1979,
|
||||
Title = {Properties of Water and Steam in SI-Units},
|
||||
Author = {Ernst Schmidt},
|
||||
Publisher = {Springer},
|
||||
Year = {1979},
|
||||
Edition = {2nd},
|
||||
|
||||
Owner = {jowr},
|
||||
Timestamp = {2014.09.22}
|
||||
}
|
||||
|
||||
@Manual{Skovrup2013,
|
||||
Title = {SecCool Properties},
|
||||
Title = {{SecCool Properties v1.33}},
|
||||
Author = {Morten Juel Skovrup},
|
||||
Edition = {v1.33},
|
||||
Organization = {IPU Refrigeration and Energy Technology},
|
||||
Year = {2013},
|
||||
|
||||
@@ -55,9 +99,29 @@
|
||||
Url = {http://en.ipu.dk/Indhold/refrigeration-and-energy-technology/seccool.aspx}
|
||||
}
|
||||
|
||||
@TechReport{Zavoico2001,
|
||||
Title = {{Solar Power Tower Design Basis Document}},
|
||||
Author = {Alexis B. Zavoico},
|
||||
Institution = {Sandia National Laboratories},
|
||||
Year = {2001},
|
||||
Month = {July},
|
||||
|
||||
Owner = {jowr},
|
||||
Timestamp = {2013.10.23},
|
||||
Url = {http://prod.sandia.gov/techlib/access-control.cgi/2001/012100.pdf}
|
||||
}
|
||||
|
||||
@Manual{Dynalene2014,
|
||||
Title = {{Technical Data Sheet}},
|
||||
Organization = {{Dynalene Inc.}},
|
||||
Year = {2014},
|
||||
|
||||
Owner = {jowr},
|
||||
Timestamp = {2014.09.22}
|
||||
}
|
||||
|
||||
@Manual{Therminol2014,
|
||||
Title = {{Therminol Heat Transfer Reference Disk}},
|
||||
Edition = {v5.1},
|
||||
Title = {{Therminol Heat Transfer Reference Disk v5.1}},
|
||||
Organization = {{Eastman Chemical Company}},
|
||||
Year = {2014},
|
||||
|
||||
@@ -66,3 +130,121 @@
|
||||
Url = {http://www.therminol.com/resources/therminol-reference-disk}
|
||||
}
|
||||
|
||||
@Manual{Paratherm2013,
|
||||
Title = {{Thermal Properties Calculator v6.4}},
|
||||
Organization = {{Paratherm Ltd.}},
|
||||
Year = {2013},
|
||||
|
||||
Owner = {jowr},
|
||||
Timestamp = {2014.09.22},
|
||||
Url = {http://paracalc.paratherm.com}
|
||||
}
|
||||
|
||||
@Manual{Arteco2010,
|
||||
Title = {{Technical Information}},
|
||||
Organization = {{Arteco NV/SA}},
|
||||
Year = {2010},
|
||||
|
||||
Owner = {jowr},
|
||||
Timestamp = {2014.09.22}
|
||||
}
|
||||
|
||||
@Manual{3M2007,
|
||||
Title = {{Technical Information}},
|
||||
Organization = {{3M Company}},
|
||||
Year = {2007},
|
||||
|
||||
Owner = {jowr},
|
||||
Timestamp = {2014.09.22}
|
||||
}
|
||||
|
||||
@Manual{PKS2005,
|
||||
Title = {{Technical Data Sheet}},
|
||||
Organization = {{pro K{\"u}hlsole GmbH}},
|
||||
Year = {2005},
|
||||
|
||||
Owner = {jowr},
|
||||
Timestamp = {2014.09.22}
|
||||
}
|
||||
|
||||
@Manual{Chevron2004,
|
||||
Title = {{Technical Data Sheet}},
|
||||
Organization = {{Chevron Products Company}},
|
||||
Year = {2004},
|
||||
|
||||
Owner = {jowr},
|
||||
Timestamp = {2014.09.22}
|
||||
}
|
||||
|
||||
@Manual{Aspen2001,
|
||||
Title = {{Technical Data Sheet}},
|
||||
Organization = {{Aspen Petroleum AB}},
|
||||
Year = {2001},
|
||||
|
||||
Owner = {jowr},
|
||||
Timestamp = {2014.09.22}
|
||||
}
|
||||
|
||||
@Manual{Clariant2000,
|
||||
Title = {{Technical Data Sheet}},
|
||||
Organization = {{Clariant GmbH}},
|
||||
Year = {2000},
|
||||
|
||||
Owner = {jowr},
|
||||
Timestamp = {2014.09.22}
|
||||
}
|
||||
|
||||
@Manual{Hydro2000,
|
||||
Title = {{Technical Information}},
|
||||
Organization = {{Hydro Chemicals}},
|
||||
Year = {2000},
|
||||
|
||||
Owner = {jowr},
|
||||
Timestamp = {2014.09.22}
|
||||
}
|
||||
|
||||
@Manual{Sulzer1999,
|
||||
Title = {{Technical Information}},
|
||||
Organization = {{Sulzer Chemtech AG}},
|
||||
Year = {1999},
|
||||
|
||||
Owner = {jowr},
|
||||
Timestamp = {2014.09.22}
|
||||
}
|
||||
|
||||
@Manual{Tyfoprop1999,
|
||||
Title = {{Technical Information}},
|
||||
Organization = {{Tyforop Chemie Gmbh}},
|
||||
Year = {1999},
|
||||
|
||||
Owner = {jowr},
|
||||
Timestamp = {2014.09.22}
|
||||
}
|
||||
|
||||
@Manual{Kemira1998,
|
||||
Title = {{Technical Data Sheet}},
|
||||
Organization = {{Kemira Chemicals OY}},
|
||||
Year = {1998},
|
||||
|
||||
Owner = {jowr},
|
||||
Timestamp = {2014.09.22}
|
||||
}
|
||||
|
||||
@Manual{Dow1997,
|
||||
Title = {{Technical Data Sheet}},
|
||||
Organization = {{The Dow Chemical Company}},
|
||||
Year = {1997},
|
||||
|
||||
Owner = {jowr},
|
||||
Timestamp = {2014.09.22}
|
||||
}
|
||||
|
||||
@Manual{Hoechst1995,
|
||||
Title = {{Technical Information}},
|
||||
Organization = {{Hoechst AG}},
|
||||
Year = {1995},
|
||||
|
||||
Owner = {jowr},
|
||||
Timestamp = {2014.09.22}
|
||||
}
|
||||
|
||||
|
||||
@@ -1,11 +1,14 @@
|
||||
|
||||
.. |degC| replace:: :math:`^\circ\!\!` C
|
||||
|
||||
.. _Incompressibles:
|
||||
|
||||
Incompressible Fluids
|
||||
=====================
|
||||
|
||||
|
||||
General Introduction
|
||||
--------------------
|
||||
|
||||
In CoolProp, the incompressible fluids are divided into three major groups.
|
||||
|
||||
* :ref:`Pure fluids <Pure>`.
|
||||
@@ -29,19 +32,44 @@ specific fluid. To get an overview over all the fits, there are also combined
|
||||
documents with all the
|
||||
:download:`pure fluids and all the aqueous solutions</_static/fluid_properties/incompressible/report/all_incompressibles.pdf>`.
|
||||
You can read more about these reports in a dedicated
|
||||
:ref:`section<FittingReports>` called :ref:`Fitting Reports<FittingReports>` below.
|
||||
:ref:`section<FittingReports>` called :ref:`Fitting Reports<FittingReports>`.
|
||||
|
||||
All incompressible fluids have an arbitrary reference state for enthalpy and entropy.
|
||||
During initialisation, the reference state is defined as a temperature of 20 °C
|
||||
and a pressure of 1 atm according to the U.S. National Institute of Standards and
|
||||
Technology (`NIST <http://www.nist.gov>`_).
|
||||
|
||||
.. math::
|
||||
T_\text{ref} &= 293.15\:\text{K} &= 68\:\text{°F} \\
|
||||
p_\text{ref} &= 101325\:\text{Pa} &= 14.696\:\text{psi} \\
|
||||
h_\text{ref} &= 0\:\text{J}\,\text{kg}^{-1} & \\
|
||||
s_\text{ref} &= 0\:\text{J}\,\text{kg}^{-1}\,\text{K}^{-1} & \\
|
||||
|
||||
.. note::
|
||||
If you use a mixture, the reference state gets updated each time you change
|
||||
the composition. Furthermore, not all temperatures can be used as reference
|
||||
temperature since the fraction :math:`T_\text{in,1} / T_\text{in,0}` occurs in the integral used to
|
||||
calculate entropy. The centered fits have a base temperature and setting
|
||||
:math:`T_\text{ref}` equal to :math:`T_\text{base}` yields :math:`T_\text{in,0}=0\:\text{K}`,
|
||||
which obviously is a problem. For non-centred fits, the base temperature is
|
||||
equal to 0 K. Read on :ref:`below<BaseValue>` for more details.
|
||||
|
||||
|
||||
Pure Fluid Examples
|
||||
-------------------
|
||||
|
||||
Incompressible fluids only allow for a limited subset of input variables. The
|
||||
following input pairs are supported: :math:`f(p,T)`, :math:`f(h,p)`, :math:`f(\rho,T)`,
|
||||
:math:`f(p,u)` and :math:`f(p,s)`. All functions iterate on :math:`f(p,T)` calls
|
||||
following input pairs are supported: :math:`f(p,T)`, :math:`f(p,h)`, :math:`f(p,\rho)`,
|
||||
:math:`f(p,u)` and :math:`f(p,s)`. Some fluids also provide saturation state
|
||||
information as :math:`f(Q,T)` with :math:`Q=0`. All functions iterate on :math:`f(p,T)` calls
|
||||
internally, which makes this combination by far the fastest. However, also the
|
||||
other inputs should be fast compared to the full Helmholtz-based EOS implemented
|
||||
for then compressible fluids.
|
||||
|
||||
A call to the top-level function ``PropsSI`` can provide : density, heat capacity,
|
||||
internal energy, enthalpy, entropy, viscosity and thermal conductivity. Hence,
|
||||
the available output keys are: ``D``, ``C``, ``U``, ``H``, ``S``, ``V``, ``L``,
|
||||
``Tmin``, ``Tmax`` and ``Psat``.
|
||||
A call to the top-level function ``PropsSI`` can provide: temperature, pressure,
|
||||
density, heat capacity, internal energy, enthalpy, entropy, viscosity and
|
||||
thermal conductivity. Hence, the available output keys are: ``T``, ``P``, ``D``,
|
||||
``C``, ``U``, ``H``, ``S``, ``V``, ``L``, ``Tmin`` and ``Tmax``.
|
||||
|
||||
.. ipython::
|
||||
|
||||
@@ -53,20 +81,10 @@ the available output keys are: ``D``, ``C``, ``U``, ``H``, ``S``, ``V``, ``L``,
|
||||
#Specific heat capacity of Downtherm Q at 500 K and 1 atm
|
||||
In [1]: PropsSI('C','T',500,'P',101325,'INCOMP::DowQ')
|
||||
|
||||
#Internal energy of Downtherm Q at 500 K and 1 atm
|
||||
In [1]: PropsSI('U','T',500,'P',101325,'INCOMP::DowQ')
|
||||
In [1]: PropsSI('C','D',809.0659,'P',101325,'INCOMP::DowQ')
|
||||
|
||||
#Enthalpy of Downtherm Q at 500 K and 1 atm
|
||||
In [1]: PropsSI('H','T',500,'P',101325,'INCOMP::DowQ')
|
||||
|
||||
#Entropy of Downtherm Q at 500 K and 1 atm
|
||||
In [1]: PropsSI('S','T',500,'P',101325,'INCOMP::DowQ')
|
||||
|
||||
#Viscosity of Downtherm Q at 500 K and 1 atm
|
||||
In [1]: PropsSI('V','T',500,'P',101325,'INCOMP::DowQ')
|
||||
|
||||
#Thermal conductivity of Downtherm Q at 500 K and 1 atm
|
||||
In [1]: PropsSI('L','T',500,'P',101325,'INCOMP::DowQ')
|
||||
#Saturation pressure of Downtherm Q at 500 K
|
||||
In [1]: PropsSI('P','T',500,'Q',0,'INCOMP::DowQ')
|
||||
|
||||
#Minimum temperature for Downtherm Q
|
||||
In [1]: PropsSI('Tmin','T',0,'P',0,'INCOMP::DowQ')
|
||||
@@ -75,65 +93,47 @@ the available output keys are: ``D``, ``C``, ``U``, ``H``, ``S``, ``V``, ``L``,
|
||||
In [1]: PropsSI('Tmax','T',0,'P',0,'INCOMP::DowQ')
|
||||
|
||||
|
||||
.. #Vapour pressure of Downtherm Q at 500 K, note the dummy pressure to work around https://github.com/CoolProp/CoolProp/issues/145
|
||||
In [1]: PropsSI('Psat','T',500,'P',1e8,'INCOMP::DowQ')
|
||||
|
||||
Mixture Examples
|
||||
----------------
|
||||
|
||||
Almost the same syntax can be used for mixtures. Please note that the mixture
|
||||
interface developed for CoolProp 5 has not been ported to the incompressible
|
||||
fluids, yet. For now, you have to use the ``PropsSI`` function with a special
|
||||
composition notation. Depending on your fluid, you have to supply either the
|
||||
:ref:`mass fraction<MassMix>` or the :ref:`volume fraction<VoluMix>` as additional
|
||||
parameter. This is done via the fluid name by appending a dash and the
|
||||
fraction of the substance other than water. The fraction notation can be in the
|
||||
form of percent, ``LiBr-23%``, or as a fraction, ``LiBr[0.23]``, which
|
||||
corresponds to the new mixture syntax in CoolProp5.
|
||||
|
||||
.. In addition to the properties available for the pure fluids (``D``, ``C``,
|
||||
``U``, ``H``, ``S``, ``V``, ``L``,``Tmin`` and ``Tmax``, some mixtures also
|
||||
provide the freezing temperature ``Tfreeze`` as a function of composition.
|
||||
|
||||
|
||||
.. ipython::
|
||||
|
||||
Pure Fluids
|
||||
-----------
|
||||
In [1]: from CoolProp.CoolProp import PropsSI
|
||||
|
||||
For refrigeration applications, 8 fluids were implemented from Aake Melinder's
|
||||
book "Properties of Secondary Working Fluids for Indirect Systems" published in 2010
|
||||
by IIR :cite:`Melinder-BOOK-2010` with coefficients obtained from a fit between
|
||||
-80 |degC| and +100 |degC|: DEB, HCM, HFE, PMS1, PMS2, SAB, HCB and TCO.
|
||||
#Density of a lithium bromide solution at 300 K and 1 atm.
|
||||
In [1]: PropsSI('D','T',300,'P',101325,'INCOMP::LiBr[0.23]')
|
||||
|
||||
Some additional secondary cooling fluids are based on data compiled by Morten
|
||||
Juel Skovrup in his `SecCool software <http://en.ipu.dk/Indhold/refrigeration-and-energy-technology/seccool.aspx>`_
|
||||
provided by his employer `IPU <http://en.ipu.dk>`_. Fits have been made for the
|
||||
manufacturer data stored in the software. The Aspen Temper fluids (AS10, AS20,
|
||||
AS30, AS40, AS55) are a blend of potassium formate and sodiumpropionate and the
|
||||
Zitrec S group (ZS10, ZS25, ZS40, ZS45 and ZS55) consists mainly of potassium
|
||||
acetate and potassium formate.
|
||||
#Specific heat capacity of a lithium bromide solution at 300 K and 1 atm
|
||||
In [1]: PropsSI('C','T',300,'P',101325,'INCOMP::LiBr-0.23%')
|
||||
|
||||
There are also a few high temperature heat transfer fluids with individual
|
||||
temperature ranges. Please refer to the table below for a complete overview.
|
||||
For these fluids, information from commercial data sheets was used to obtain
|
||||
coefficients.
|
||||
#Specific enthalpy of a lithium bromide solution at 300 K and 1 atm
|
||||
In [1]: PropsSI('H','T',300,'P',101325,'INCOMP::LiBr-0.23%')
|
||||
|
||||
.. _Pure:
|
||||
|
||||
.. csv-table:: All incompressible pure fluids included in CoolProp
|
||||
:widths: 10, 35, 25, 15, 15
|
||||
:header-rows: 1
|
||||
:file: ../_static/fluid_properties/incompressible/table/pure-fluids.csv
|
||||
In [1]: PropsSI('T','H',28627,'P',101325,'INCOMP::LiBr-0.23%')
|
||||
|
||||
|
||||
.. warning::
|
||||
Some mixture function have a non-monotonic behaviour, this can lead to misleading
|
||||
results when using other inputs than :math:`f(p,T)`. Keep that in mind and
|
||||
implement a way to validate the results you get from these functions. At the same
|
||||
time, mixture solvers are likely to produce errors due to the same reason...
|
||||
|
||||
Aqueous Mixtures - Solutions and Brines
|
||||
---------------------------------------
|
||||
|
||||
|
||||
.. _MassMix:
|
||||
|
||||
.. csv-table:: All incompressible mass-based binary mixtures included in CoolProp
|
||||
:widths: 10, 30, 20, 10, 10, 10, 10
|
||||
:header-rows: 1
|
||||
:file: ../_static/fluid_properties/incompressible/table/mass-based-fluids.csv
|
||||
|
||||
.. .. _MoleMix:
|
||||
|
||||
.. .. csv-table:: All incompressible mole-based binary mixtures included in CoolProp
|
||||
:widths: 10, 30, 20, 10, 10, 10, 10
|
||||
:header-rows: 1
|
||||
:file: ../_static/fluid_properties/incompressible/table/mole-based-fluids.csv
|
||||
|
||||
.. _VoluMix:
|
||||
|
||||
.. csv-table:: All incompressible volume-based binary mixtures included in CoolProp
|
||||
:widths: 10, 30, 20, 10, 10, 10, 10
|
||||
:header-rows: 1
|
||||
:file: ../_static/fluid_properties/incompressible/table/volume-based-fluids.csv
|
||||
|
||||
|
||||
|
||||
@@ -143,14 +143,14 @@ Fitting Reports
|
||||
---------------------------------------
|
||||
|
||||
A file with all fitting reports for the incompressible fluids can be obtained
|
||||
from :download:`here </_static/fluid_properties/incompressible/report/all_incompressibles.pdf>`. These reports help you to
|
||||
from :download:`here</_static/fluid_properties/incompressible/report/all_incompressibles.pdf>`. These reports help you to
|
||||
get an overview over the different incompressible fluids
|
||||
included in CoolProp. The reports start with some basic information about
|
||||
the fluid. There is the name by which it can be accessed through the
|
||||
interface in the title "Fitting Report for *FluidName*" as well as a description
|
||||
of what the fluid actually is, this could also be a trade name or a commonly
|
||||
used non-scientific name. The next item tells you where we got the data from. This
|
||||
would typically be a data sheet from a manufacturers homepage, some other software
|
||||
the fluid. The fluid name used in CoolProp is in the title "Fitting Report for *FluidName*"
|
||||
and there is also a description of what the fluid actually consists of. The latter
|
||||
could also be a trade name or a commonly used non-scientific name. The next item
|
||||
tells you where we got the data from. This
|
||||
would typically be a data sheet from a manufacturer's homepage, some other software
|
||||
database, a scientific publication or experimental data.
|
||||
|
||||
.. figure:: /_static/fluid_properties/incompressible/report/report2up.jpg
|
||||
@@ -161,10 +161,10 @@ database, a scientific publication or experimental data.
|
||||
fluid and a binary mixture. You can also have a look at the
|
||||
:download:`PDF version</_static/fluid_properties/incompressible/report/report2up.pdf>` of the reports side by side.
|
||||
|
||||
If all data is available, there is a graphs for each of the basic quantities
|
||||
If all data are available, there is a graph for each of the basic quantities:
|
||||
density :math:`\rho`, specific heat capacity :math:`c`, thermal conductivity
|
||||
:math:`\lambda`, dynamic viscosity :math:`\mu`, saturation pressure
|
||||
:math:`p_{sat}`, and freezing temperature :math:`T_{freeze}`. These graphs show
|
||||
:math:`p_\text{sat}`, and freezing temperature :math:`T_\text{freeze}`. These graphs show
|
||||
data points in dark blue, the fitted function from CoolProp as a red line and the
|
||||
relative error in light blue dots. Note that the relative error uses the ordinate
|
||||
on the right hand side while the other two data series refer to the axis on the
|
||||
@@ -173,221 +173,165 @@ that typically lies in the middle of the allowed range. Dashed red lines indicat
|
||||
the limits in terms of concentration as well as the freezing temperature.
|
||||
|
||||
|
||||
.. _Equations:
|
||||
|
||||
Equations
|
||||
----------------------
|
||||
---------
|
||||
|
||||
Exp or log for visc, other poly or log poly
|
||||
|
||||
|
||||
|
||||
Incompressible Liquids
|
||||
----------------------
|
||||
There is also a selection of incompressible liquids implemented. These only allow for calls with
|
||||
temperature and pressure as input and provide only a subset of thermophysical properties, namely:
|
||||
density, heat capacity, internal energy, enthalpy, entropy, viscosity and thermal conductivity.
|
||||
Hence, the available output keys for the ``Props`` function are: "D", "C", "U", "H", "S", "V", "L",
|
||||
"Tmin", "Tmax" and "Psat". An internal iteration allows us to use enthalpy and pressure as inputs,
|
||||
but be aware of the reduced computational efficiency.
|
||||
|
||||
.. ipython::
|
||||
|
||||
In [1]: from CoolProp.CoolProp import PropsSI
|
||||
|
||||
#Density of HFE-7100 at 300 K and 1 atm.
|
||||
In [1]: PropsSI('D','T',300,'P',101325,'INCOMP::HFE')
|
||||
|
||||
|
||||
For refrigeration applications, 8 fluids were implemented from Aake Melinder "Properties of
|
||||
Secondary Working Fluids for Indirect Systems" published in 2010 by IIR and coefficients are
|
||||
obtained from a fit between -80 and +100 degrees Celsius.
|
||||
|
||||
========================== ===================================================
|
||||
Fluid Name Description
|
||||
========================== ===================================================
|
||||
``DEB`` Diethyl Benzene
|
||||
``HCM`` Hydrocarbon Mixture (Therminol D12 Solutia)
|
||||
``HFE`` Hydrofluoroether HFE-7100
|
||||
``PMS1`` Polydimethylsiloxan 1.
|
||||
``PMS2`` Polydimethylsiloxan 2.
|
||||
``SAB`` Synthetic alkyl benzene
|
||||
``HCB`` Hydrocarbon blend (Dynalene MV)
|
||||
``TCO`` Terpene from citrus oils
|
||||
========================== ===================================================
|
||||
|
||||
Some additional secondary cooling fluids are based on data compiled by Morten Juel Skovrup in
|
||||
his `SecCool software <http://en.ipu.dk/Indhold/refrigeration-and-energy-technology/seccool.aspx>`_
|
||||
provided by his employer `IPU <http://en.ipu.dk>`_. Fits have been made according to the manufacturer
|
||||
data stored in the sodtware. The Aspen Temper fluids are a blend of potassium formate and sodiumpropionate
|
||||
and the Zitrec S group consists mainly of potassium acetate and potassium formate.
|
||||
|
||||
========================== ===================================================
|
||||
Fluid Name Description
|
||||
========================== ===================================================
|
||||
``AS10`` Aspen Temper -10 (-10 to +27.5 C)
|
||||
``AS20`` Aspen Temper -20 (-20 to +27.5 C)
|
||||
``AS30`` Aspen Temper -30 (-30 to +27.5 C)
|
||||
``AS40`` Aspen Temper -40 (-40 to +27.5 C)
|
||||
``AS55`` Aspen Temper -55 (-55 to +27.5 C)
|
||||
``ZS10`` Zitrec S -10 (-10 to +85 C)
|
||||
``ZS25`` Zitrec S -25 (-25 to +85 C)
|
||||
``ZS40`` Zitrec S -40 (-40 to +85 C)
|
||||
``ZS45`` Zitrec S -45 (-45 to +85 C)
|
||||
``ZS55`` Zitrec S -55 (-55 to +85 C)
|
||||
========================== ===================================================
|
||||
|
||||
There are also a few high temperature heat transfer fluids with individual temperature ranges. Please
|
||||
refer to the file IncompLiquid.h for a complete overview. For these fluids, information from commercial
|
||||
data sheets was used to obtain coefficients.
|
||||
|
||||
========================== ===================================================
|
||||
Fluid Name Description
|
||||
========================== ===================================================
|
||||
``TD12`` Therminol D12 (-85 to +230 C)
|
||||
``TVP1`` Therminol VP-1 (+12 to +397 C)
|
||||
``T72`` Therminol 72 (-10 to +380 C)
|
||||
``T66`` Therminol 66 (0 to +345 C)
|
||||
``DowJ`` Dowtherm J (-80 to +345 C)
|
||||
``DowQ`` Dowtherm Q (-35 to +360 C)
|
||||
``TX22`` Texatherm 22 (0 to +350 C)
|
||||
``NaK`` Nitrate Salt Blend (+300 to +600 C)
|
||||
``XLT`` Syltherm XLT (-100 to +260 C)
|
||||
``HC10`` Dynalene HC-10 (-10 to +218 C)
|
||||
``HC20`` Dynalene HC-20 (-20 to +210 C)
|
||||
``HC30`` Dynalene HC-30 (-30 to +210 C)
|
||||
``HC40`` Dynalene HC-40 (-40 to +200 C)
|
||||
``HC50`` Dynalene HC-50 (-50 to +210 C)
|
||||
========================== ===================================================
|
||||
|
||||
All fluids are implemented with polynomials for density and heat capacity with typically 4 coefficients
|
||||
and hence a third order polynomial. Thermal conductivity is a second order polynomial and viscosity and
|
||||
vapour pressure are exponential functions.
|
||||
There are only four different equations used to calculate the thermophysical
|
||||
properties of incompressible fluids in CoolProp:
|
||||
|
||||
.. math::
|
||||
|
||||
\rho &= \sum_{i=0}^n C_{\rho}[i] \cdot T^i \\
|
||||
c &= \sum_{i=0}^n C_{c}[i] \cdot T^i \\
|
||||
u &= \int_{0}^{1} c\left( T \right) dT
|
||||
= \sum_{i=0}^n \frac{1}{i+1} \cdot C_{c}[i]
|
||||
\cdot \left( T_1^{i+1} - T_0^{i+1} \right) \\
|
||||
s &= \int_{0}^{1} \frac{c\left( T \right)}{T} dT
|
||||
= C_{c}[0] \cdot \ln\left(\frac{T_1}{T_0}\right)
|
||||
+ \sum_{i=0}^{n-1} \frac{1}{i+1} \cdot C_{c}[i+1]
|
||||
\cdot \left( T_1^{i+1} - T_0^{i+1} \right) \\
|
||||
\lambda &= \sum_{i=0}^n C_{\lambda}[i] \cdot T^i \\
|
||||
\mu &= \exp\left( \frac{C_{\mu}[0]}{T+C_{\mu}[1]} - C_{\mu}[2] \right) \\
|
||||
p_{sat} &= \exp\left( \frac{C_{sat}[0]}{T+C_{sat}[1]} - C_{sat}[2] \right) \\
|
||||
f(T) &= \exp \left( \frac{C[0]}{T+C[1]} - C[2] \right) \text{, } \\
|
||||
f(T) &= \exp \left( \log \left( \sum_{i=0}^l \left( T+C[0] \right)^{-i-1} \right) \cdot C[1] + C[2] \right) \text{, } \\
|
||||
f(T,x)&= \sum_{i=0}^n x^i \cdot \sum_{j=0}^m C[i,j] \cdot T^j \text{ and } \\
|
||||
f(T,x)&= \exp \left( \sum_{i=0}^n x^i \cdot \sum_{j=0}^m C[i,j] \cdot T^j \right) \text{. } \\
|
||||
|
||||
Only the last two are suitable for mixtures with the input parameter :math:`x`
|
||||
denoting the fraction of component other than water. Following the works of
|
||||
Melinder :cite:`Melinder2010` and Skovrup :cite:`Skovrup2013`, the exponents
|
||||
for the polynomials are arranged in a triangular matrix to avoid overfitting.
|
||||
These conditions satisfy :math:`0 \leq i \leq n`, :math:`0 \leq j \leq m`
|
||||
and :math:`i + j \leq \max(n,m)`. It is only for the freezing temperature calculation
|
||||
that the implemented procedures differ from what is presented in Melinder's
|
||||
book :cite:`Melinder2010`. Freezing temperature is only a function of concentration
|
||||
and the dependency on the fluid temperature has been removed. For mixtures,
|
||||
:math:`m=5` and :math:`n=3` are assigned as default values.
|
||||
Omitting the composition term with :math:`n=0` yields the pure fluid formulations
|
||||
for which we selected :math:`l=1` and :math:`m=4`.
|
||||
|
||||
Brines and Solutions
|
||||
--------------------
|
||||
All the brines and solutions can be accessed through the Props function. To use them, the fluid name
|
||||
is something like ``"MEG-20%"`` which is a 20% by mass ethylene glycol solution. Note that these fluids
|
||||
have an arbitrary reference state: Be careful with enthalpy and entropy calculations. Again, only
|
||||
temperature and pressure inputs are supported directly to calculate the same subset of thermophysical
|
||||
properties as above , namely: density, heat capacity, internal energy, enthalpy, entropy, viscosity
|
||||
and thermal conductivity. Hence, the available output keys for the ``Props`` function are: "D", "C",
|
||||
"U", "H", "S", "V", "L", "Tmin", Tmax" and "Tfreeze". An internal iteration allows us to use enthalpy
|
||||
and pressure as inputs, but be aware of the reduced computational efficiency.
|
||||
The standard polynomials are used for the density, heat capacity and thermal
|
||||
conductivity functions, while viscosity, vapour pressure and freezing temperature
|
||||
are exponential functions. For exponential functions of only one variable
|
||||
(:math:`\mu(T)`, :math:`p_\text{sat}(T)`, :math:`T_\text{freeze}(x)`), we start by fitting the
|
||||
first equation. If the fit quality is poor, we try the second exponential function.
|
||||
The exponential polynomial is used as a fall-back function for single variable
|
||||
fits and it is the only function used for multivariate fits, e.g. :math:`\mu(T,x)`.
|
||||
|
||||
.. ipython::
|
||||
If you would like to know more about the fitting procedures, you can have a look
|
||||
at this `Python notebook <http://nbviewer.ipython.org/github/CoolProp/CoolProp/blob/master/dev/incompressible_liquids/LinearAlgebra.ipynb>`_,
|
||||
which describes the basics of the multivariate polynomial fits employed in this
|
||||
software. Non-polynomial functions are fitted using the minimisation routines
|
||||
accessible through SciPy :cite:`Jones2001`. For the extremely curious, the
|
||||
Python module `CPIncomp <https://github.com/CoolProp/CoolProp/tree/master/dev/incompressible_liquids/CPIncomp>`_
|
||||
contains the source code for the fits used in CoolProp as well as the code to
|
||||
generate the fitting reports. Feel free to browse the code.
|
||||
|
||||
In [1]: from CoolProp.CoolProp import PropsSI
|
||||
Using only polynomials for the heat capacity functions, we can derive internal
|
||||
energy and entropy by integrating the specific heat capacity
|
||||
|
||||
#Specific heat 20% mass ethylene glycol solution at 300 K and 1 atm.
|
||||
In [1]: PropsSI('C','T',300,'P',101.325,'INCOMP::MEG-20%')
|
||||
|
||||
For Lithium-Bromide, the publication by Patek and Klomfar from 2005 was implemented based on the
|
||||
source code provided by the authors. The `paper <http://dx.doi.org/10.1016/j.ijrefrig.2005.10.007>`_
|
||||
covering the equations can be found in the
|
||||
`International Journal of Refrigeration <http://dx.doi.org/10.1016/j.ijrefrig.2005.10.007>`_. Data is
|
||||
available for temperatures from 0 C to 225 C and for the full composition range. Use ``LiBr`` to acccess
|
||||
the functions.
|
||||
|
||||
A number of aqueous solutions are implemented using the coefficients from Aake Melinder "Properties of
|
||||
Secondary Working Fluids for Indirect Systems" published in 2010 by IIR. According to the book, 2D
|
||||
polynomials are given in a form that satisfies :math:`0 \leq i \leq 5`, :math:`0 \leq j \leq 3`
|
||||
and :math:`i + j \leq 5` yielding a triangular matrix of coefficients. It is only for the freezing
|
||||
temperature calculation that the implemented procedures differ from what is presented in Melinder's
|
||||
book the dependency on the current temperature is removed. In CoolProp, :math:`T_{freeze}` only depends
|
||||
on concentration.
|
||||
|
||||
========================== =================================================== ================= =================
|
||||
Melinder Fluids Description max. T max. x
|
||||
========================== =================================================== ================= =================
|
||||
``MEG`` Ethylene Glycol (C2H6O2) +100 C 60 %
|
||||
``MPG`` Propylene Glycol (C3H8O2) +100 C 60 %
|
||||
``MEA`` Ethyl Alcohol, Ethanol (C2H6O) +40 C 60 %
|
||||
``MMA`` Methyl Alcohol, Methanol (CH4O) +40 C 60 %
|
||||
``MGL`` Glycerol (C3H8O3) +40 C 60 %
|
||||
``MAM`` Ammonia (NH3) +30 C 30 %
|
||||
``MKC`` Potassium Carbonate (K2CO3) +40 C 40 %
|
||||
``MCA`` Calcium Chloride (CaCl2) +40 C 30 %
|
||||
``MMG`` Magnesium Chloride (MgCl2) +40 C 30 %
|
||||
``MNA`` Sodium Chloride (NaCl) +40 C 23 %
|
||||
``MKA`` Potassium Acetate (CH3CO2K) +40 C 45 %
|
||||
``MKF`` Potassium Formate (CHKO2) +40 C 48 %
|
||||
``MLI`` Lithium Chloride (LiCl) +40 C 24 %
|
||||
========================== =================================================== ================= =================
|
||||
|
||||
Furthermore, there is a number of other secondary fluids that can be accessed in the same way. Most
|
||||
information is based on the data compiled by Morten Juel Skovrup in his `SecCool software <http://en.ipu.dk/Indhold/refrigeration-and-energy-technology/seccool.aspx>`_
|
||||
provided by his employer `IPU <http://en.ipu.dk>`_. The coefficient matrix of the SecCool-based fluids
|
||||
has the same structure as mentioned above.
|
||||
|
||||
For slurry ice, the concentration :math:`x` refers to the solid content and the heat capacity includes the heat of fusion.
|
||||
It might be necessary to adjust the solid content during heat transfer. The implementation is based on the data available
|
||||
in SecCool, which was originally recorded at the `Danish Technological Institute (DTI) <http://www.dti.dk/>`_.
|
||||
|
||||
========================== =================================================== ================= =================
|
||||
SecCool Fluids Description max. T max. x
|
||||
========================== =================================================== ================= =================
|
||||
``ZiAC`` ZitrecAC (corrosion inhibitor) +100 C 50 %
|
||||
``IceEA`` Ethanol-water mixture with slurry ice -10 C 35 %
|
||||
``IcePG`` Propylene glycol-water mixture with slurry ice -10 C 35 %
|
||||
``IceNA`` Sodium chloride-water mixture with slurry ice -5 C 35 %
|
||||
``PK2000`` Pekasol 2000 (Potassium acetate and formate) +100 C 100 %
|
||||
========================== =================================================== ================= =================
|
||||
|
||||
|
||||
|
||||
In both of the above cases, :math:`i` is the exponent for the concentration :math:`x` and :math:`j`
|
||||
is used with the temperature :math:`T`. Properties are modelled with the following polynomials:
|
||||
.. _BaseValue:
|
||||
|
||||
.. math::
|
||||
|
||||
\rho &= \sum_{i=0}^n x^i \cdot \sum_{j=0}^m C_{\rho}[i,j] \cdot T^j \\
|
||||
c &= \sum_{i=0}^n x^i \cdot \sum_{j=0}^m C_{c}[i,j] \cdot T^j \\
|
||||
c &= \sum_{i=0}^n x^i \cdot \sum_{j=0}^m C_{c}[i,j] \cdot T^j \text{ yielding } \\
|
||||
u &= \int_{0}^{1} c\left( x,T \right) dT
|
||||
= \sum_{i=0}^n x^i \cdot \sum_{j=0}^m \frac{1}{j+1} \cdot C_{c}[i,j]
|
||||
\cdot \left( T_1^{j+1} - T_0^{j+1} \right) \\
|
||||
\cdot \left( T_{1}^{j+1} - T_{0}^{j+1} \right) \text{ and } \\
|
||||
s &= \int_{0}^{1} \frac{c\left( x,T \right)}{T} dT
|
||||
= \sum_{i=0}^n x^i \cdot \left(
|
||||
C_{c}[i,0] \cdot \ln\left(\frac{T_1}{T_0}\right)
|
||||
+ \sum_{j=0}^{m-1} \frac{1}{j+1} \cdot C_{c}[i,j+1] \cdot \left( T_1^{j+1} - T_0^{j+1} \right)
|
||||
C_{c}[i,0] \cdot \ln\left(\frac{T_{1}}{T_{0}}\right)
|
||||
+ \sum_{j=0}^{m-1} \frac{1}{j+1} \cdot C_{c}[i,j+1] \cdot \left( T_{1}^{j+1} - T_{0}^{j+1} \right)
|
||||
\right) \\
|
||||
\lambda &= \sum_{i=0}^n x^i \cdot \sum_{j=0}^m C_{\lambda}[i,j] \cdot T^j \\
|
||||
\mu &= \exp \left( \sum_{i=0}^n x^i \cdot \sum_{j=0}^m C_{\mu}[i,j] \cdot T^j \right) \\
|
||||
T_{freeze} &= \sum_{i=0}^n C_{freeze}[i] \cdot x^i \\
|
||||
|
||||
Using a centered approach for the independent variables,
|
||||
the fit quality can be enhanced. Therefore, all solutions have a reference temperature and concentration
|
||||
in the original work by Melinder and Skovrup as well as in CoolProp: :math:`x = x_{real} - x_{ref}`
|
||||
and :math:`T = T_{real} - T_{ref}`, this technique does not affect the calculation
|
||||
According to Melinder :cite:`Melinder2010` and Skovrup :cite:`Skovrup2013`,
|
||||
using a centred approach for the independent variables enhances the fit quality.
|
||||
Therefore, all solutions have a base temperature and concentration in the original
|
||||
works as well as in CoolProp: :math:`x_\text{in} = x - x_\text{base}`
|
||||
and :math:`T_\text{in} = T - T_\text{base}`, this technique does not affect the calculation
|
||||
of the derived quantity internal energy since the formula contains temperature differences.
|
||||
However, integrating :math:`c(x,T)T^{-1}dT` for the entropy requires some changes due to
|
||||
the logarithm. To structure the problem, we introduce a variable :math:`d(j,T_{real})`, which will be expressed by a third sum.
|
||||
As a first step for simplification, one has to expand the the binomial :math:`(T_{real}-T_{ref})^n` to a series.
|
||||
Only containing :math:`j` and :math:`T_{real}`, :math:`d` is independent from :math:`x` and can be
|
||||
computed outside the loop for enhanced computational efficiency. An integration of the expanded binomial
|
||||
then yields the final factor :math:`D` to be multiplied with the other coefficients and the concentration.
|
||||
However, integrating :math:`c(x_\text{in},T_\text{in})T_\text{in}^{-1}dT_\text{in}` for the entropy requires some changes due to
|
||||
the logarithm.
|
||||
|
||||
.. warning::
|
||||
You must **not** use the base temperature :math:`T_\text{base}`
|
||||
as reference temperature for your thermodynamic states. This will lead to an
|
||||
error caused by a division by zero during the integration carried out to
|
||||
obtain the entropy.
|
||||
|
||||
To structure the problem, we introduce a variable :math:`f(j,T)`,
|
||||
which will be expressed by a third sum. As a first step for simplification, one
|
||||
has to expand the the binomial :math:`(T-T_{base})^n` to a series. Only
|
||||
containing :math:`j` and :math:`T`, :math:`f` is independent from :math:`x_\text{in}` and
|
||||
can be computed outside the loop for enhanced computational efficiency. An
|
||||
integration of the expanded binomial then yields the final factor :math:`F` to
|
||||
be multiplied with the other coefficients and the concentration.
|
||||
|
||||
.. math::
|
||||
|
||||
s &= \int_{0}^{1} \frac{c\left( x,T \right)}{T} dT = \sum_{i=0}^n x^i \cdot \sum_{j=0}^m C_{c}[i,j] \cdot D(j,T_0,T_1) \\
|
||||
D &= (-1)^j \cdot \ln \left( \frac{T_1}{T_0} \right) \cdot T_{ref}^j + \sum_{k=0}^{j-1} \binom{j}{k} \cdot \frac{(-1)^k}{j-k} \cdot \left( T_1^{j-k} - T_0^{j-k} \right) \cdot T_{ref}^k
|
||||
s &= \int_{0}^{1} \frac{c\left( x_\text{in},T_\text{in} \right)}{T_\text{in}} dT_\text{in} = \sum_{i=0}^n x_\text{in}^i \cdot \sum_{j=0}^m C_{c}[i,j] \cdot F(j,T_\text{in,0},T_\text{in,1}) \\
|
||||
F &= (-1)^j \cdot \ln \left( \frac{T_\text{in,1}}{T_\text{in,0}} \right) \cdot T_{base}^j + \sum_{k=0}^{j-1} \binom{j}{k} \cdot \frac{(-1)^k}{j-k} \cdot \left( T_\text{in,1}^{j-k} - T_\text{in,0}^{j-k} \right) \cdot T_{base}^k
|
||||
|
||||
|
||||
|
||||
.. bibliography:: ../../CoolPropBibTeXLibrary.bib
|
||||
:style: unsrt
|
||||
The Different Fluids
|
||||
--------------------
|
||||
|
||||
The fluids implemented in CoolProp cover a wide range of industrial heat
|
||||
transfer media. This database has initially been developed with refrigeration
|
||||
systems in mind. That is why the majority of fluids are secondary refrigerants
|
||||
with application temperatures close to the freezing point of water. Besides those,
|
||||
there is also incompressible water, high temperature heat transfer oils and a
|
||||
molten salt mixture for extreme temperatures.
|
||||
|
||||
Besides the different technical data sheets and calculation tools provided by
|
||||
manufactures, two specific publications provided a lot of data used for the
|
||||
incompressible fluids: Åke Melinder's book *Properties of Secondary Working
|
||||
Fluids for Indirect Systems* :cite:`Melinder2010` has inspired both, the work on
|
||||
pure fluids and aqueous solutions. The second major source of inspiration is the
|
||||
`SecCool <http://en.ipu.dk/Indhold/refrigeration-and-energy-technology/seccool.aspx>`_
|
||||
:cite:`Skovrup2013` software, which contains data compiled by Morten Juel
|
||||
Skovrup. It is provided free of charge by his employer `IPU <http://en.ipu.dk>`_.
|
||||
|
||||
|
||||
.. _Pure:
|
||||
|
||||
.. csv-table:: All incompressible pure fluids included in CoolProp
|
||||
:widths: 10, 35, 13, 14, 14, 14
|
||||
:header-rows: 1
|
||||
:file: ../_static/fluid_properties/incompressible/table/pure-fluids.csv
|
||||
|
||||
|
||||
There are also a number of water-based mixtures implemented in CoolProp. Most of them
|
||||
are secondary heat transfer fluids, but there are also aqueous solutions of
|
||||
ammonia :cite:`Melinder2010`, :download:`MAM<../_static/fluid_properties/incompressible/report/MAM_fitreport.pdf>`,
|
||||
and lithium bromide :cite:`Patek2006`, :download:`LiBr<../_static/fluid_properties/incompressible/report/LiBr_fitreport.pdf>`,
|
||||
which can be used to model absorption chillers.
|
||||
|
||||
|
||||
.. _MassMix:
|
||||
|
||||
.. csv-table:: All incompressible mass-based binary mixtures included in CoolProp
|
||||
:widths: 10, 30, 11, 11, 11, 11, 8, 8
|
||||
:header-rows: 1
|
||||
:file: ../_static/fluid_properties/incompressible/table/mass-based-fluids.csv
|
||||
|
||||
.. .. _MoleMix:
|
||||
|
||||
.. .. csv-table:: All incompressible mole-based binary mixtures included in CoolProp
|
||||
:widths: 10, 30, 11, 11, 11, 11, 8, 8
|
||||
:header-rows: 1
|
||||
:file: ../_static/fluid_properties/incompressible/table/mole-based-fluids.csv
|
||||
|
||||
.. _VoluMix:
|
||||
|
||||
.. csv-table:: All incompressible volume-based binary mixtures included in CoolProp
|
||||
:widths: 10, 30, 11, 11, 11, 11, 8, 8
|
||||
:header-rows: 1
|
||||
:file: ../_static/fluid_properties/incompressible/table/volume-based-fluids.csv
|
||||
|
||||
|
||||
For slurry ice, the concentration :math:`x` refers to the solid content and the
|
||||
heat capacity includes the heat of fusion. It might be necessary to adjust the
|
||||
solid content during heat transfer. The implementation is based on the data
|
||||
available in `SecCool <http://en.ipu.dk/Indhold/refrigeration-and-energy-technology/seccool.aspx>`_,
|
||||
which was originally recorded at the Danish Technological Institute `(DTI) <http://www.dti.dk/>`_.
|
||||
|
||||
|
||||
References
|
||||
----------
|
||||
|
||||
.. bibliography:: Incompressibles.bib
|
||||
:filter: docname in docnames
|
||||
:style: unsrt
|
||||
|
||||
@@ -1,12 +1,18 @@
|
||||
.. _mixtures:
|
||||
|
||||
.. contents:: :depth: 2
|
||||
|
||||
********
|
||||
Mixtures
|
||||
********
|
||||
|
||||
Mixtures docs will go here when they are written.
|
||||
Theoretical description
|
||||
-----------------------
|
||||
The mixture modeling used in CoolProp is based on the work of Kunz et al. :cite:`Kunz-BOOK-2007,Kunz-JCED-2012` and Lemmon :cite:`Lemmon-JPCRD-2000,Lemmon-JPCRD-2004,Lemmon-IJT-1999`
|
||||
|
||||
The treatment of mixtures in CoolProp as of v5 is quite rudimentary, though it will be improved in the very near future.
|
||||
A mixture is composed of a number of components, and for each pair of components, it is necessary to have information for the excess Helmholtz energy term as well as the reducing function. See below for what binary pairs are included in CoolProp.
|
||||
|
||||
The numerical methods required for mixtures are far more complicated than those for pure fluids, so the number of flash routines that are currently available are relatively small compared to pure fluids.
|
||||
|
||||
The only types of inputs that are allowed for mixtures right now are
|
||||
|
||||
@@ -14,21 +20,46 @@ The only types of inputs that are allowed for mixtures right now are
|
||||
- Temperature/quality
|
||||
- Temperature/pressure
|
||||
|
||||
.. Used in Python script later on
|
||||
.. role:: raw-html(raw)
|
||||
:format: html
|
||||
|
||||
Binary pairs
|
||||
------------
|
||||
|
||||
.. note::
|
||||
Please hover the mouse pointer over the coefficients to get the full accuracy
|
||||
for the listed coefficients. You can also get more information on references
|
||||
that are not in bibliography.
|
||||
|
||||
.. csv-table:: All binary pairs included in CoolProp
|
||||
:header-rows: 1
|
||||
:file: mixture_binary_pairs.csv
|
||||
|
||||
Phase Envelope
|
||||
--------------
|
||||
.. plot::
|
||||
|
||||
import CoolProp
|
||||
import matplotlib.pyplot as plt
|
||||
|
||||
HEOS = CoolProp.AbstractState('HEOS','R32&R134a')
|
||||
HEOS = CoolProp.AbstractState('HEOS','Methane&Ethane')
|
||||
for x0 in [0.02, 0.2, 0.4, 0.6, 0.8, 0.98]:
|
||||
HEOS.set_mole_fractions([x0, 1 - x0])
|
||||
try:
|
||||
HEOS.build_phase_envelope("dummy")
|
||||
except ValueError as VE:
|
||||
print VE
|
||||
print(VE)
|
||||
PE = HEOS.get_phase_envelope_data()
|
||||
plt.plot(PE.rhomolar_vap, PE.rhomolar_liq, 'o-')
|
||||
plt.plot(PE.T, PE.p, 'o-')
|
||||
|
||||
plt.xlabel('Temperature [K]')
|
||||
plt.ylabel('Pressure [Pa]')
|
||||
plt.tight_layout()
|
||||
plt.tight_layout()
|
||||
|
||||
References
|
||||
----------
|
||||
|
||||
.. bibliography:: ../../CoolPropBibTeXLibrary.bib
|
||||
:filter: docname in docnames
|
||||
:style: unsrt
|
||||
54
Web/scripts/CPWeb/BibtexTools.py
Normal file
54
Web/scripts/CPWeb/BibtexTools.py
Normal file
@@ -0,0 +1,54 @@
|
||||
'''
|
||||
Created on 26 Sep 2014
|
||||
|
||||
@author: jowr
|
||||
'''
|
||||
import os
|
||||
from CoolProp.BibtexParser import BibTeXerClass
|
||||
|
||||
def getPath(filename, search=True):
|
||||
# Path to root
|
||||
coolprop_dir = os.path.abspath(os.path.join(os.path.dirname(__file__),'..','..'))
|
||||
# Test for file
|
||||
fname = filename
|
||||
if os.path.exists(fname): return os.path.abspath(fname)
|
||||
# Test relative to this file
|
||||
fname = os.path.join(os.path.dirname(__file__),filename)
|
||||
if os.path.exists(fname): return os.path.abspath(fname)
|
||||
# Test relative to root notation
|
||||
fname = os.path.join(coolprop_dir,filename)
|
||||
if os.path.exists(fname): return os.path.abspath(fname)
|
||||
# Search in root tree
|
||||
fname = os.path.basename(filename)
|
||||
if search:
|
||||
result = []
|
||||
for root, dirs, files in os.walk(coolprop_dir):
|
||||
if fname in files:
|
||||
result.append(os.path.join(root, fname))
|
||||
if len(result)==1:
|
||||
return os.path.abspath(result[0])
|
||||
elif len(result)>1:
|
||||
print "Found multiple files with the name {0}. Try to specify the path as well.".format(fname)
|
||||
print result
|
||||
return os.path.abspath(result[0])
|
||||
|
||||
raise ValueError("Found no file with the name {0}. Try to specify the path as well.".format(fname))
|
||||
|
||||
|
||||
def getBibtexParser(filename = '../../../CoolPropBibTeXLibrary.bib'):
|
||||
"""Create a parser object that can be used to extract entries from a
|
||||
library in Bibtex format."""
|
||||
fpath = getPath(filename)
|
||||
bibtexer = BibTeXerClass(fpath)
|
||||
return bibtexer
|
||||
|
||||
|
||||
def getCitationOrAlternative(bibtexer, bibtex_key):
|
||||
"""Find the key in the library and convert to a citation, if it is not found,
|
||||
we return a footnote string for sphinx."""
|
||||
bibtex_key = bibtex_key.strip()
|
||||
|
||||
if bibtex_key in bibtexer.library.entries:
|
||||
return u':cite:`{0}`'.format(bibtex_key)
|
||||
else:
|
||||
return u':raw-html:`<span title="{0}">Source</span>`'.format(bibtex_key)
|
||||
69
Web/scripts/CPWeb/UnicodeTools.py
Normal file
69
Web/scripts/CPWeb/UnicodeTools.py
Normal file
@@ -0,0 +1,69 @@
|
||||
'''
|
||||
Created on 26 Sep 2014
|
||||
|
||||
@author: jowr
|
||||
'''
|
||||
import codecs
|
||||
import csv
|
||||
import cStringIO
|
||||
|
||||
class UTF8Recoder:
|
||||
"""
|
||||
Iterator that reads an encoded stream and reencodes the input to UTF-8
|
||||
"""
|
||||
def __init__(self, f, encoding):
|
||||
self.reader = codecs.getreader(encoding)(f)
|
||||
|
||||
def __iter__(self):
|
||||
return self
|
||||
|
||||
def next(self):
|
||||
return self.reader.next().encode("utf-8")
|
||||
|
||||
class UnicodeReader:
|
||||
"""
|
||||
A CSV reader which will iterate over lines in the CSV file "f",
|
||||
which is encoded in the given encoding.
|
||||
"""
|
||||
|
||||
def __init__(self, f, dialect=csv.excel, encoding="utf-8", **kwds):
|
||||
f = UTF8Recoder(f, encoding)
|
||||
self.reader = csv.reader(f, dialect=dialect, **kwds)
|
||||
|
||||
def next(self):
|
||||
row = self.reader.next()
|
||||
return [unicode(s, "utf-8") for s in row]
|
||||
|
||||
def __iter__(self):
|
||||
return self
|
||||
|
||||
class UnicodeWriter:
|
||||
"""
|
||||
A CSV writer which will write rows to CSV file "f",
|
||||
which is encoded in the given encoding.
|
||||
"""
|
||||
|
||||
def __init__(self, f, dialect=csv.excel, encoding="utf-8", **kwds):
|
||||
# Redirect output to a queue
|
||||
self.queue = cStringIO.StringIO()
|
||||
self.writer = csv.writer(self.queue, dialect=dialect, **kwds)
|
||||
self.stream = f
|
||||
self.encoder = codecs.getincrementalencoder(encoding)()
|
||||
|
||||
def writerow(self, row):
|
||||
self.writer.writerow([s.encode("utf-8") for s in row])
|
||||
# Fetch UTF-8 output from the queue ...
|
||||
data = self.queue.getvalue()
|
||||
data = data.decode("utf-8")
|
||||
# ... and reencode it into the target encoding
|
||||
data = self.encoder.encode(data)
|
||||
# write to the target stream
|
||||
self.stream.write(data)
|
||||
# empty queue
|
||||
self.queue.truncate(0)
|
||||
|
||||
def writerows(self, rows):
|
||||
for row in rows:
|
||||
self.writerow(row)
|
||||
|
||||
|
||||
21
Web/scripts/CPWeb/__init__.py
Normal file
21
Web/scripts/CPWeb/__init__.py
Normal file
@@ -0,0 +1,21 @@
|
||||
"""
|
||||
CPWeb - A collection of commonly used routines to produce CoolProp's online documentation
|
||||
=====
|
||||
|
||||
"""
|
||||
from __future__ import division, absolute_import, print_function
|
||||
|
||||
import codecs
|
||||
import csv
|
||||
import cStringIO
|
||||
|
||||
|
||||
|
||||
|
||||
|
||||
def get_version():
|
||||
return 5.0
|
||||
|
||||
if __name__ == "__main__":
|
||||
print('You are using version %s of the Python package for creating CoolProp\' online documentation.'%(get_version()))
|
||||
print()
|
||||
68
Web/scripts/fluid_properties.Mixtures.py
Normal file
68
Web/scripts/fluid_properties.Mixtures.py
Normal file
@@ -0,0 +1,68 @@
|
||||
|
||||
|
||||
from CPWeb.BibtexTools import getCitationOrAlternative, getBibtexParser
|
||||
import CoolProp
|
||||
import os.path
|
||||
|
||||
web_dir = os.path.abspath(os.path.join(os.path.dirname(__file__),'..'))
|
||||
csvfile = os.path.join(web_dir,'fluid_properties','mixture_binary_pairs.csv')
|
||||
|
||||
def merge_args(*args):
|
||||
return " :raw-html:`<br/>` ".join(list(args))
|
||||
|
||||
def printCoeff(number):
|
||||
if number is None or \
|
||||
len(str(number).strip())<1:
|
||||
return " "
|
||||
number = float(number)
|
||||
short = "{0:.4e}".format(number)
|
||||
long = "{0:.14e}".format(number)
|
||||
return u':raw-html:`<span title="{1}">{0}</span>`'.format(short,long)
|
||||
|
||||
class Dossier:
|
||||
def __init__(self):
|
||||
self.data = {}
|
||||
def add(self, key, value):
|
||||
if key not in self.data:
|
||||
self.data[key] = []
|
||||
self.data[key].append(value)
|
||||
|
||||
d = Dossier()
|
||||
|
||||
pairs = CoolProp.get('mixture_binary_pairs_list')
|
||||
for pair in pairs.split(','):
|
||||
CAS1, CAS2 = pair.split('&')
|
||||
d.add('CAS1', CAS1)
|
||||
d.add('CAS2', CAS2)
|
||||
for key in ['name1','name2','F','function','BibTeX','xi','zeta','betaT','betaV','gammaT','gammaV']:
|
||||
try:
|
||||
d.add(key, CoolProp.CoolProp.get_mixture_binary_pair_data(CAS1, CAS2, key))
|
||||
except BaseException as BE:
|
||||
d.add(key, '')
|
||||
|
||||
import pandas
|
||||
df = pandas.DataFrame(d.data)
|
||||
df = df.sort(['BibTeX','name1'], ascending = [0, 1])
|
||||
|
||||
bibtexer = getBibtexParser()#filename = '../../../CoolPropBibTeXLibrary.bib')
|
||||
|
||||
with open(csvfile,'w') as fp:
|
||||
header = 'Ref.,Name1,Name2,function,F,'
|
||||
header += merge_args("xi","zeta,")
|
||||
header += merge_args("betaT","betaV,")
|
||||
header += merge_args("gammaT","gammaV")
|
||||
header += '\n'
|
||||
fp.write(header)
|
||||
|
||||
for index, row in df.iterrows():
|
||||
text = ','.join([ \
|
||||
getCitationOrAlternative(bibtexer,row['BibTeX']),
|
||||
row['name1'],
|
||||
row['name2'],
|
||||
row['function'],
|
||||
row['F'],
|
||||
merge_args(printCoeff(row['xi']),printCoeff(row['zeta'])),
|
||||
merge_args(printCoeff(row['betaT']),printCoeff(row['betaV'])),
|
||||
merge_args(printCoeff(row['gammaT']),printCoeff(row['gammaV']))
|
||||
])+'\n'
|
||||
fp.write(text)
|
||||
@@ -1,90 +0,0 @@
|
||||
from __future__ import print_function
|
||||
|
||||
import json as pyjson
|
||||
from datetime import datetime
|
||||
import struct
|
||||
import os
|
||||
import argparse, textwrap
|
||||
import sys
|
||||
import generate_headers
|
||||
|
||||
# 0: Input file path relative to dev folder
|
||||
# 1: Output file path relative to include folder
|
||||
# 2: Name of variable
|
||||
values = [
|
||||
('all_fluids.json','all_fluids_JSON.h','all_fluids_JSON'),
|
||||
('all_incompressibles.json','all_incompressibles_JSON.h','all_incompressibles_JSON'),
|
||||
('mixtures/mixture_excess_term.json', 'mixture_excess_term_JSON.h', 'mixture_excess_term_JSON'),
|
||||
('mixtures/mixture_reducing_parameters.json', 'mixture_reducing_parameters_JSON.h', 'mixture_reducing_parameters_JSON')
|
||||
]
|
||||
|
||||
def TO_CPP(root_dir, hashes):
|
||||
def to_chunks(l, n):
|
||||
if n<1:
|
||||
n=1
|
||||
return [l[i:i+n] for i in range(0, len(l), n)]
|
||||
|
||||
# Normalise path name
|
||||
root_dir = os.path.normpath(root_dir)
|
||||
|
||||
# First we package up the JSON files
|
||||
import package_json
|
||||
package_json.combine_json(root_dir)
|
||||
|
||||
for infile,outfile,variable in values:
|
||||
|
||||
json = open(os.path.join(root_dir,'dev',infile),'r').read()
|
||||
|
||||
# convert each character to hex and add a terminating NULL character to end the
|
||||
# string, join into a comma separated string
|
||||
if sys.version_info[0] == 2:
|
||||
h = [hex(struct.unpack("b",b)[0]) for b in json] + ['0x00']
|
||||
else:
|
||||
# Encode as ASCII characters
|
||||
json = json.encode('ascii')
|
||||
h = [str(hex(b)) for b in json] + [str('0x00')]
|
||||
|
||||
# Break up the file into lines of 16 hex characters
|
||||
chunks = to_chunks(h, 16)
|
||||
|
||||
# Put the lines back together again
|
||||
# The chunks are joined together with commas, and then EOL are used to join the rest
|
||||
hex_string = ',\n'.join([', '.join(chunk) for chunk in chunks])
|
||||
|
||||
# Check if hash is up to date based on using variable as key
|
||||
if variable not in hashes or (variable in hashes and hashes[variable] != generate_headers.get_hash(hex_string)):
|
||||
|
||||
# Generate the output string
|
||||
output = '// File generated by the script dev/JSON_to_CPP.py on '+ str(datetime.now()) + '\n\n'
|
||||
output += '// JSON file encoded in binary form\n'
|
||||
output += 'const unsigned char '+variable+'_binary[] = {\n' + hex_string + '\n};'+'\n\n'
|
||||
output += '// Combined into a single std::string \n'
|
||||
output += 'std::string {v:s}({v:s}_binary, {v:s}_binary + sizeof({v:s}_binary)/sizeof({v:s}_binary[0]));'.format(v = variable)
|
||||
|
||||
# Write it to file
|
||||
f = open(os.path.join(root_dir,'include',outfile), 'w')
|
||||
f.write(output)
|
||||
f.close()
|
||||
|
||||
# Store the hash of the data that was written to file (not including the header)
|
||||
hashes[variable] = generate_headers.get_hash(hex_string)
|
||||
else:
|
||||
print(outfile + ' is up to date')
|
||||
|
||||
if __name__=='__main__':
|
||||
parser = argparse.ArgumentParser(
|
||||
formatter_class=argparse.RawDescriptionHelpFormatter,
|
||||
description=textwrap.dedent("""CoolProp
|
||||
This program converts the JSON files from dev/fluid etc
|
||||
to header files. It is necessary to give this program the
|
||||
value for --path, this is the root directory where
|
||||
dev/ can be found.""")
|
||||
)
|
||||
|
||||
parser.add_argument('--path', required=False,
|
||||
help='Location of the root folder',
|
||||
default=None)
|
||||
|
||||
args = parser.parse_args()
|
||||
|
||||
TO_CPP(args.path)
|
||||
@@ -1,50 +0,0 @@
|
||||
Buildbot masters and slaves
|
||||
===========================
|
||||
|
||||
Master
|
||||
------
|
||||
|
||||
From the root of the git checkout (this will use the master.cfg from CoolProp)
|
||||
```
|
||||
pip install buildbot
|
||||
cd dev/buildbot
|
||||
buildbot create-master master
|
||||
buildbot start master
|
||||
```
|
||||
|
||||
The file ``buildbot-private.py`` (which is a python module with the passwords for the slaves as well as the buildbot website), should also be placed in the master folder next to master.cfg. Alternatively, you can put the ``buildbot_private.py`` in another folder on the master's computer and make a soft-link in the master folder to point to the buildbot_private.py file.
|
||||
|
||||
If you want to completely restart the master, you can do
|
||||
```
|
||||
buildbot restart master
|
||||
```
|
||||
but usually a
|
||||
```
|
||||
buildbot reconfig master
|
||||
```
|
||||
will do the job since it will just reparse the configuration file without signing you out of the server
|
||||
|
||||
To ensure that the buildbot server stays online, you can make a script with the contents
|
||||
```
|
||||
buildbot start /path/to/master_folder
|
||||
```
|
||||
and add it to a cron job
|
||||
|
||||
Slaves
|
||||
------
|
||||
|
||||
To start a slave connected to a buildbot master at IP address 10.0.0.2 (default for host for VirtualBox), with a slave named ``example-slave`` and passsword ``pass``, run the command
|
||||
|
||||
```
|
||||
buildslave create-slave slave 10.0.0.2:9989 example-slave pass
|
||||
buildslave start slave
|
||||
```
|
||||
|
||||
If the master is somewhere else, just change the IP address.
|
||||
|
||||
On linux, you can add the following lines to the end of your ``~/.profile`` file (similar ideas apply on other platforms) to autostart the slave when the user logs in:
|
||||
|
||||
```
|
||||
# Connect to the buildbot master
|
||||
buildslave start ~/slave
|
||||
```
|
||||
@@ -97,7 +97,7 @@ def sphinx_slave(platform, git_mode = 'incremental'):
|
||||
# Run sphinx build
|
||||
factory.addStep(ShellCommand(command=["python", "-c", "\"import CoolProp; print(CoolProp.__file___)\""], workdir= 'build/wrappers/Python', haltOnFailure = True))
|
||||
# Run doxygen build
|
||||
factory.addStep(ShellCommand(command=' '.join(["doxygen","Doxyfile","&&","mv","CoolPropDoxyLink.tag","Web/_static/doxygen"]), workdir= 'build', haltOnFailure = True))
|
||||
factory.addStep(ShellCommand(command=' '.join(["doxygen","Doxyfile"]), workdir= 'build', haltOnFailure = True))
|
||||
# Run sphinx apidoc
|
||||
#factory.addStep(ShellCommand(command=["sphinx-apidoc","-T","-f","-o","apidoc","../CoolProp"],workdir= 'build/Web', haltOnFailure = True))
|
||||
# Run sphinx build
|
||||
@@ -151,6 +151,25 @@ def python_slave(key, platform, conda_env, cmake_args = [], cmake_env = {}, buil
|
||||
|
||||
return factory
|
||||
|
||||
def python_source_slave(key, platform, conda_env, cmake_args = [], cmake_env = {}, build_args = [], git_mode = 'incremental'):
|
||||
factory = BuildFactory()
|
||||
working_folder = "build/build"
|
||||
|
||||
factory.addStep(ShellCommand(command=cleanCommand, description='fullclean?', workdir=""))
|
||||
# Check out sources
|
||||
factory.addStep(Git(repourl='git://github.com/CoolProp/CoolProp', mode=git_mode, submodules = True, progress=True, haltOnFailure = True))
|
||||
# Remove the temporary folder for installs
|
||||
factory.addStep(RemoveDirectory(dir="build/install_root", haltOnFailure = True))
|
||||
factory.addStep(MakeDirectory(dir=working_folder, haltOnFailure = True))
|
||||
|
||||
factory.addStep(ShellCommand(command = ' '.join(['source',"activate",conda_env,"&&","cmake", "..", "-DCOOLPROP_PYTHON_PYPI=ON","&&","cmake","--build","."]+cmake_args),
|
||||
env = cmake_env,
|
||||
workdir= working_folder,
|
||||
haltOnFailure = True))
|
||||
factory.addStep(DirectoryUpload(slavesrc="install_root", masterdest="public_html/binaries", url="binaries", compress="bz2"))
|
||||
|
||||
return factory
|
||||
|
||||
def deb_slave(git_mode = 'incremental'):
|
||||
factory = BuildFactory()
|
||||
working_folder = "build/wrappers/DEB"
|
||||
@@ -298,7 +317,7 @@ BuilderConfig(name="Javascript-linux",
|
||||
c['builders'].append(
|
||||
BuilderConfig(name="Python-sdist",
|
||||
slavenames=["OSX-slave"],
|
||||
factory = python_slave("PYPI", platform = 'OSX', conda_env = 'py27')
|
||||
factory = python_source_slave("PYPI", platform = 'OSX', conda_env = 'py27')
|
||||
)
|
||||
)
|
||||
|
||||
|
||||
@@ -134,8 +134,6 @@
|
||||
<File Name="../../include/Ice.h"/>
|
||||
<File Name="../../include/IncompressibleFluid.h"/>
|
||||
<File Name="../../include/MatrixMath.h"/>
|
||||
<File Name="../../include/mixture_excess_term_JSON.h"/>
|
||||
<File Name="../../include/mixture_reducing_parameters_JSON.h"/>
|
||||
<File Name="../../include/PlatformDetermination.h"/>
|
||||
<File Name="../../include/PolyMath.h"/>
|
||||
<File Name="../../include/Solvers.h"/>
|
||||
|
||||
@@ -353,22 +353,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 508.1,
|
||||
"T_min": 508.0999999999062,
|
||||
"T_min": 508.09697325761744,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
0.0,
|
||||
0.0,
|
||||
-4.656219323212737e-09,
|
||||
508.10002188423084
|
||||
-1.5123933548972854e-11,
|
||||
-1.7185082712306687e-08,
|
||||
0.0011638028537861549,
|
||||
504.579957217175
|
||||
],
|
||||
"cV": [
|
||||
0.0,
|
||||
0.0,
|
||||
4.64031360324759e-09,
|
||||
508.0999781905261
|
||||
1.9536072269032177e-10,
|
||||
-2.983480058312324e-06,
|
||||
0.015098157455448244,
|
||||
482.76079813563524
|
||||
],
|
||||
"rhomolar_max": 4700.020155407677,
|
||||
"rhomolar_min": 4699.9797791519495
|
||||
"rhomolar_max": 4814.181193727979,
|
||||
"rhomolar_min": 4590.050467927069
|
||||
},
|
||||
"gas_constant": 8.314472,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -506,22 +506,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 150.687,
|
||||
"T_min": 150.68674395835467,
|
||||
"T_min": 150.68697834063298,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
0.0,
|
||||
0.0,
|
||||
-2.124793992189458e-06,
|
||||
150.7154880259892
|
||||
-6.171554333557227e-07,
|
||||
150.69527446806111
|
||||
],
|
||||
"cV": [
|
||||
0.0,
|
||||
0.0,
|
||||
2.1223479463722503e-06,
|
||||
150.65854476919804
|
||||
6.072607995401675e-07,
|
||||
150.67885819354578
|
||||
],
|
||||
"rhomolar_max": 13527.931526630135,
|
||||
"rhomolar_min": 13286.788909807183
|
||||
"rhomolar_max": 13442.525139946354,
|
||||
"rhomolar_min": 13371.76233564158
|
||||
},
|
||||
"gas_constant": 8.31451,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -367,22 +367,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 132.86,
|
||||
"T_min": 132.85999999951312,
|
||||
"T_min": 132.85867131966137,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
0.0,
|
||||
0.0,
|
||||
-4.587508257048314e-09,
|
||||
132.8600497744646
|
||||
3.1174266374072594e-11,
|
||||
-1.0578676813227408e-06,
|
||||
0.011945990965038183,
|
||||
87.96227472439597
|
||||
],
|
||||
"cV": [
|
||||
0.0,
|
||||
0.0,
|
||||
4.611514127080118e-09,
|
||||
132.85994996507173
|
||||
-2.7988602187391993e-11,
|
||||
8.673443114829891e-07,
|
||||
-0.008936706896165105,
|
||||
163.4668663127422
|
||||
],
|
||||
"rhomolar_max": 10850.106136720144,
|
||||
"rhomolar_min": 10849.894418190801
|
||||
"rhomolar_max": 11038.842068491349,
|
||||
"rhomolar_min": 10664.189840198747
|
||||
},
|
||||
"gas_constant": 8.314472,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -1,7 +1,7 @@
|
||||
{
|
||||
"ALIASES": [
|
||||
"Cyclohexane",
|
||||
"CYCLOHEXANE",
|
||||
"CYCLOHEXANE",
|
||||
"CYCLOHEX"
|
||||
],
|
||||
"ANCILLARIES": {
|
||||
@@ -450,22 +450,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 553.6,
|
||||
"T_min": 553.5999997660659,
|
||||
"T_min": 553.5979946139788,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
0.0,
|
||||
0.0,
|
||||
-8.175876311970891e-07,
|
||||
553.602635902523
|
||||
1.56104739484658e-08,
|
||||
-0.00015385588557227471,
|
||||
0.5052887091787223,
|
||||
0.6345188298942561
|
||||
],
|
||||
"cV": [
|
||||
0.0,
|
||||
0.0,
|
||||
8.181583620573008e-07,
|
||||
553.5973622574407
|
||||
-1.5338245208003638e-08,
|
||||
0.0001454870563719106,
|
||||
-0.45981527881664047,
|
||||
1037.8236160527126
|
||||
],
|
||||
"rhomolar_max": 3224.286127290438,
|
||||
"rhomolar_min": 3223.7140723774714
|
||||
"rhomolar_max": 3252.773506033089,
|
||||
"rhomolar_min": 3195.2323910542696
|
||||
},
|
||||
"gas_constant": 8.3144621,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -2,7 +2,7 @@
|
||||
"ALIASES": [
|
||||
"cyclopropane",
|
||||
"Cyclopropane",
|
||||
"CYCLOPROPANE",
|
||||
"CYCLOPROPANE",
|
||||
"CYCLOPRO"
|
||||
],
|
||||
"ANCILLARIES": {
|
||||
|
||||
@@ -2,7 +2,7 @@
|
||||
"ALIASES": [
|
||||
"CycloPentane",
|
||||
"cyclopentane",
|
||||
"CYCLOPENTANE",
|
||||
"CYCLOPENTANE",
|
||||
"CYCLOPEN"
|
||||
],
|
||||
"ANCILLARIES": {
|
||||
@@ -388,22 +388,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 511.72,
|
||||
"T_min": 511.71999999967744,
|
||||
"T_min": 511.7095934234679,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
0.0,
|
||||
0.0,
|
||||
-3.3125554580735164e-08,
|
||||
511.72012653961855
|
||||
-4.880588052926918e-09,
|
||||
5.252717316693226e-05,
|
||||
-0.18764912368477027,
|
||||
734.1005944101676
|
||||
],
|
||||
"cV": [
|
||||
0.0,
|
||||
0.0,
|
||||
3.3109614501400934e-08,
|
||||
511.71987352127263
|
||||
5.250582737174832e-09,
|
||||
-6.357124543112242e-05,
|
||||
0.2558285044919253,
|
||||
169.4290891702673
|
||||
],
|
||||
"rhomolar_max": 3820.0097389577454,
|
||||
"rhomolar_min": 3819.990256554135
|
||||
"rhomolar_max": 3873.2904355172786,
|
||||
"rhomolar_min": 3766.813756733369
|
||||
},
|
||||
"gas_constant": 8.314472,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -352,22 +352,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 645.78,
|
||||
"T_min": 642.4672205036263,
|
||||
"T_min": 645.4997615767367,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
0.0,
|
||||
-6.230392935143472e-05,
|
||||
0.07816508273019042,
|
||||
621.263969382756
|
||||
-1.554702914197144e-07,
|
||||
0.00027871311312902783,
|
||||
-0.16613864293822964,
|
||||
678.7008854032358
|
||||
],
|
||||
"cV": [
|
||||
3.6584356889802007e-07,
|
||||
-0.0006916100001806448,
|
||||
0.43580969539355185,
|
||||
554.2417982977918
|
||||
2.1732433324774884e-07,
|
||||
-0.00042927603672073575,
|
||||
0.28201442644063596,
|
||||
584.1491278422845
|
||||
],
|
||||
"rhomolar_max": 857.8775266580042,
|
||||
"rhomolar_min": 421.67935851484685
|
||||
"rhomolar_max": 725.3981107757561,
|
||||
"rhomolar_min": 542.276230072255
|
||||
},
|
||||
"gas_constant": 8.314472,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -440,22 +440,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 38.34,
|
||||
"T_min": 38.339416735480214,
|
||||
"T_min": 38.3399506598222,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
0.0,
|
||||
0.0,
|
||||
-2.853182978628294e-06,
|
||||
38.389160342721766
|
||||
-8.339819490855398e-07,
|
||||
38.35436950898275
|
||||
],
|
||||
"cV": [
|
||||
0.0,
|
||||
0.0,
|
||||
2.8554684120896426e-06,
|
||||
38.2908002792597
|
||||
8.380089288669903e-07,
|
||||
38.325561106155625
|
||||
],
|
||||
"rhomolar_max": 17434.42590754112,
|
||||
"rhomolar_min": 17025.73770897889
|
||||
"rhomolar_max": 17289.162165151512,
|
||||
"rhomolar_min": 17171.122133543762
|
||||
},
|
||||
"gas_constant": 8.3144621,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -409,22 +409,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 557.0,
|
||||
"T_min": 556.9998876027566,
|
||||
"T_min": 556.9999904919641,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
0.0,
|
||||
0.0,
|
||||
-1.3572331448181178e-06,
|
||||
557.0054289325793
|
||||
-2.1173490191325178e-07,
|
||||
557.0008469396076
|
||||
],
|
||||
"cV": [
|
||||
0.0,
|
||||
0.0,
|
||||
1.2967566129304942e-06,
|
||||
556.9948129735483
|
||||
2.0050706260121842e-07,
|
||||
556.9991979717496
|
||||
],
|
||||
"rhomolar_max": 4082.813512058265,
|
||||
"rhomolar_min": 3913.3243337382946
|
||||
"rhomolar_max": 4044.9053782587557,
|
||||
"rhomolar_min": 3952.580044972171
|
||||
},
|
||||
"gas_constant": 8.314472,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -1,6 +1,6 @@
|
||||
{
|
||||
"ALIASES": [
|
||||
"DIMETHYLETHER",
|
||||
"DIMETHYLETHER",
|
||||
"DME"
|
||||
],
|
||||
"ANCILLARIES": {
|
||||
@@ -390,22 +390,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 400.378,
|
||||
"T_min": 400.37110506132734,
|
||||
"T_min": 400.3774167354802,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
-1.2340856080204133e-11,
|
||||
-3.6668010216655235e-07,
|
||||
0.005662449102513134,
|
||||
382.2672995716492
|
||||
0.0,
|
||||
0.0,
|
||||
-1.846177917829548e-05,
|
||||
400.48766296831906
|
||||
],
|
||||
"cV": [
|
||||
3.2678596450956466e-11,
|
||||
-1.1690463919857066e-06,
|
||||
0.010429215559579295,
|
||||
372.82769480948826
|
||||
0.0,
|
||||
0.0,
|
||||
1.8536722158567707e-05,
|
||||
400.2678918703781
|
||||
],
|
||||
"rhomolar_max": 6048.293446297928,
|
||||
"rhomolar_min": 5831.9191440537215
|
||||
"rhomolar_max": 5971.593082884313,
|
||||
"rhomolar_min": 5908.534646267459
|
||||
},
|
||||
"gas_constant": 8.314472,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -1,7 +1,7 @@
|
||||
{
|
||||
"ALIASES": [
|
||||
"ethylbenzene",
|
||||
"ETHYLBENZENE",
|
||||
"ETHYLBENZENE",
|
||||
"EBENZENE"
|
||||
],
|
||||
"ANCILLARIES": {
|
||||
@@ -382,22 +382,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 617.12,
|
||||
"T_min": 617.1169732576175,
|
||||
"T_min": 617.1197439583547,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
-5.889287007942239e-10,
|
||||
2.7489748115156017e-06,
|
||||
-0.0017958058182523087,
|
||||
613.5170511389289
|
||||
0.0,
|
||||
0.0,
|
||||
-2.3245131740117315e-05,
|
||||
617.1837152780217
|
||||
],
|
||||
"cV": [
|
||||
2.7233018397998547e-10,
|
||||
-4.332169254554028e-06,
|
||||
0.017610902629837312,
|
||||
595.7882622446201
|
||||
0.0,
|
||||
0.0,
|
||||
2.3091817015124984e-05,
|
||||
617.0567049600925
|
||||
],
|
||||
"rhomolar_max": 2778.835947943192,
|
||||
"rhomolar_min": 2703.079602802352
|
||||
"rhomolar_max": 2752.0308502563307,
|
||||
"rhomolar_min": 2729.928018264121
|
||||
},
|
||||
"gas_constant": 8.314472,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -510,22 +510,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 282.35,
|
||||
"T_min": 282.34697325761744,
|
||||
"T_min": 282.3497439583547,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
-5.3490529714823425e-11,
|
||||
1.1806509186406972e-06,
|
||||
-0.008673975227377104,
|
||||
303.55881549532984
|
||||
0.0,
|
||||
0.0,
|
||||
-3.634935446259431e-06,
|
||||
282.37775915135825
|
||||
],
|
||||
"cV": [
|
||||
5.6266047158959514e-11,
|
||||
-1.3340632313871347e-06,
|
||||
0.010531516936650963,
|
||||
254.66645559595844
|
||||
0.0,
|
||||
0.0,
|
||||
3.6437107681563877e-06,
|
||||
282.3221738335621
|
||||
],
|
||||
"rhomolar_max": 7866.912063903078,
|
||||
"rhomolar_min": 7408.049532488636
|
||||
"rhomolar_max": 7707.205098345808,
|
||||
"rhomolar_min": 7566.496505023215
|
||||
},
|
||||
"gas_constant": 8.31451,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -362,22 +362,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 377.921,
|
||||
"T_min": 377.92099999999897,
|
||||
"T_min": 377.88522000242136,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
0.0,
|
||||
0.0,
|
||||
-6.93839214284477e-10,
|
||||
377.9210032250623
|
||||
4.9355266611563965e-11,
|
||||
-1.1363349519029853e-06,
|
||||
0.00736469652648742,
|
||||
363.2831553274167
|
||||
],
|
||||
"cV": [
|
||||
0.0,
|
||||
0.0,
|
||||
5.712986843822467e-10,
|
||||
377.9209973445233
|
||||
-1.6224665103344288e-10,
|
||||
1.8467354481248633e-06,
|
||||
-0.0066516525010036605,
|
||||
385.2331741502011
|
||||
],
|
||||
"rhomolar_max": 4648.142188502035,
|
||||
"rhomolar_min": 4648.138929822613
|
||||
"rhomolar_max": 4935.29110614525,
|
||||
"rhomolar_min": 4335.002308503029
|
||||
},
|
||||
"gas_constant": 8.314472,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -440,22 +440,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 5.1953000000000005,
|
||||
"T_min": 5.141297013055385,
|
||||
"T_min": 5.19073171770731,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
-4.82863868046167e-13,
|
||||
2.5798878786242034e-08,
|
||||
-0.0004593197751427837,
|
||||
7.920274522054607
|
||||
-3.0333435224167437e-13,
|
||||
1.5607506016709e-08,
|
||||
-0.00026681298442982895,
|
||||
6.710133323667334
|
||||
],
|
||||
"cV": [
|
||||
0.0,
|
||||
-1.5275455601862228e-09,
|
||||
5.538880201235252e-05,
|
||||
4.693200509758024
|
||||
-4.479989405503328e-10,
|
||||
1.624444158435496e-05,
|
||||
5.048044137037824
|
||||
],
|
||||
"rhomolar_max": 22647.96434858185,
|
||||
"rhomolar_min": 12184.179354171467
|
||||
"rhomolar_max": 19915.76431162559,
|
||||
"rhomolar_min": 14936.712852945791
|
||||
},
|
||||
"gas_constant": 8.314472,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -412,22 +412,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 33.145,
|
||||
"T_min": 33.144999999992066,
|
||||
"T_min": 33.13810506132737,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
0.0,
|
||||
0.0,
|
||||
-3.5640307070519154e-10,
|
||||
33.145005527098824
|
||||
3.1007578284721566e-12,
|
||||
-1.5869880447859634e-07,
|
||||
0.0026850233556669507,
|
||||
18.107690278950276
|
||||
],
|
||||
"cV": [
|
||||
0.0,
|
||||
0.0,
|
||||
3.1573424275146666e-10,
|
||||
33.14499510359337
|
||||
-2.3396699485553584e-12,
|
||||
9.516798742074658e-08,
|
||||
-0.0012636720187622463,
|
||||
38.58044486815464
|
||||
],
|
||||
"rhomolar_max": 15508.022271289323,
|
||||
"rhomolar_min": 15507.974851755711
|
||||
"rhomolar_max": 16262.923237049079,
|
||||
"rhomolar_min": 14746.877675758724
|
||||
},
|
||||
"gas_constant": 8.314472,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -4,7 +4,7 @@
|
||||
"Isobutane",
|
||||
"ISOBUTANE",
|
||||
"R600A",
|
||||
"R600a",
|
||||
"R600a",
|
||||
"ISOBUTAN"
|
||||
],
|
||||
"ANCILLARIES": {
|
||||
@@ -455,22 +455,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 407.817,
|
||||
"T_min": 406.8534813947396,
|
||||
"T_min": 407.73549293470376,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
-9.941703745512649e-10,
|
||||
1.1401780743865456e-05,
|
||||
-0.04357798580431196,
|
||||
463.3231742084145
|
||||
-5.728389280296945e-10,
|
||||
6.296755366265217e-06,
|
||||
-0.022991762972926447,
|
||||
435.69130219666266
|
||||
],
|
||||
"cV": [
|
||||
0.0,
|
||||
-1.0815601793791963e-06,
|
||||
0.00839238089576816,
|
||||
391.53680162488934
|
||||
5.562666408422913e-10,
|
||||
-6.761233991678565e-06,
|
||||
0.027344254864717768,
|
||||
371.015481302833
|
||||
],
|
||||
"rhomolar_max": 4815.639002152002,
|
||||
"rhomolar_min": 2935.903033135107
|
||||
"rhomolar_max": 4253.160501655689,
|
||||
"rhomolar_min": 3479.687062549918
|
||||
},
|
||||
"gas_constant": 8.314472,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -1,7 +1,7 @@
|
||||
{
|
||||
"ALIASES": [
|
||||
"Isobutene",
|
||||
"ISOBUTENE",
|
||||
"ISOBUTENE",
|
||||
"IBUTENE"
|
||||
],
|
||||
"ANCILLARIES": {
|
||||
@@ -350,22 +350,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 418.09000000000003,
|
||||
"T_min": 418.08999999951317,
|
||||
"T_min": 418.08543171770737,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
0.0,
|
||||
0.0,
|
||||
-2.0580323178237388e-08,
|
||||
418.09008581994766
|
||||
1.0856405178489673e-09,
|
||||
-1.4451084442137125e-05,
|
||||
0.06388776104495195,
|
||||
324.24484504699296
|
||||
],
|
||||
"cV": [
|
||||
0.0,
|
||||
0.0,
|
||||
2.0591910110230444e-08,
|
||||
418.0899141317349
|
||||
-6.230035048466998e-10,
|
||||
6.9227418610441575e-06,
|
||||
-0.02523563018482191,
|
||||
448.11876326463465
|
||||
],
|
||||
"rhomolar_max": 4170.023655555847,
|
||||
"rhomolar_min": 4169.976356154625
|
||||
"rhomolar_max": 4246.188019158735,
|
||||
"rhomolar_min": 4095.5716752458243
|
||||
},
|
||||
"gas_constant": 8.314472,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -2,7 +2,7 @@
|
||||
"ALIASES": [
|
||||
"ipentane",
|
||||
"R601a",
|
||||
"ISOPENTANE",
|
||||
"ISOPENTANE",
|
||||
"IPENTANE"
|
||||
],
|
||||
"ANCILLARIES": {
|
||||
@@ -366,22 +366,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 460.35,
|
||||
"T_min": 460.34999999967744,
|
||||
"T_min": 460.34697325761744,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
0.0,
|
||||
0.0,
|
||||
-1.3800199316984639e-08,
|
||||
460.350045140452
|
||||
8.005022701910341e-10,
|
||||
-8.44526357152168e-06,
|
||||
0.029554133854069683,
|
||||
426.02215187987395
|
||||
],
|
||||
"cV": [
|
||||
0.0,
|
||||
0.0,
|
||||
1.384341277338779e-08,
|
||||
460.34995471819684
|
||||
-5.384468503556533e-10,
|
||||
4.689391032778603e-06,
|
||||
-0.013394755215389163,
|
||||
472.83487531264404
|
||||
],
|
||||
"rhomolar_max": 3271.023375025736,
|
||||
"rhomolar_min": 3270.9766981300554
|
||||
"rhomolar_max": 3346.612383148717,
|
||||
"rhomolar_min": 3197.125647678554
|
||||
},
|
||||
"gas_constant": 8.314472,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -349,22 +349,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 209.48000000000002,
|
||||
"T_min": 209.47999999926515,
|
||||
"T_min": 209.47310506132737,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
0.0,
|
||||
0.0,
|
||||
-9.371176887927681e-09,
|
||||
209.48010167726926
|
||||
6.390300964893231e-11,
|
||||
-2.199509680360674e-06,
|
||||
0.02516089390363733,
|
||||
113.79346021244321
|
||||
],
|
||||
"cV": [
|
||||
0.0,
|
||||
0.0,
|
||||
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|
||||
209.47990160301933
|
||||
-3.436623953002642e-11,
|
||||
1.0066209446840255e-06,
|
||||
-0.009706635600422744,
|
||||
240.19068612286947
|
||||
],
|
||||
"rhomolar_max": 10850.078419187403,
|
||||
"rhomolar_min": 10849.918967439311
|
||||
"rhomolar_max": 11108.82129459245,
|
||||
"rhomolar_min": 10591.412518037536
|
||||
},
|
||||
"gas_constant": 8.314472,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -518,22 +518,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 190.564,
|
||||
"T_min": 190.56361355465157,
|
||||
"T_min": 190.5639673093741,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
0.0,
|
||||
0.0,
|
||||
-2.9498492462244708e-06,
|
||||
190.59390889908818
|
||||
-8.298041773773189e-07,
|
||||
190.57241349076935
|
||||
],
|
||||
"cV": [
|
||||
0.0,
|
||||
0.0,
|
||||
3.00418301102579e-06,
|
||||
190.53354020391578
|
||||
8.001489626516288e-07,
|
||||
190.5558871872486
|
||||
],
|
||||
"rhomolar_max": 10270.133117949952,
|
||||
"rhomolar_min": 10010.492245451042
|
||||
"rhomolar_max": 10178.523590876614,
|
||||
"rhomolar_min": 10098.272325109083
|
||||
},
|
||||
"gas_constant": 8.31451,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -1,6 +1,6 @@
|
||||
{
|
||||
"ALIASES": [
|
||||
"METHYLLINOLEATE",
|
||||
"METHYLLINOLEATE",
|
||||
"MLINOLEA"
|
||||
],
|
||||
"ANCILLARIES": {
|
||||
|
||||
@@ -1,6 +1,6 @@
|
||||
{
|
||||
"ALIASES": [
|
||||
"METHYLLINOLENATE",
|
||||
"METHYLLINOLENATE",
|
||||
"MLINOLEN"
|
||||
],
|
||||
"ANCILLARIES": {
|
||||
|
||||
@@ -1,6 +1,6 @@
|
||||
{
|
||||
"ALIASES": [
|
||||
"METHYLOLEATE",
|
||||
"METHYLOLEATE",
|
||||
"MOLEATE"
|
||||
],
|
||||
"ANCILLARIES": {
|
||||
|
||||
@@ -1,6 +1,6 @@
|
||||
{
|
||||
"ALIASES": [
|
||||
"METHYLPALMITATE",
|
||||
"METHYLPALMITATE",
|
||||
"MPALMITA"
|
||||
],
|
||||
"ANCILLARIES": {
|
||||
@@ -396,22 +396,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 755.0,
|
||||
"T_min": 754.9999999319605,
|
||||
"T_min": 754.9979946139788,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
0.0,
|
||||
0.0,
|
||||
-1.7213757676923328e-06,
|
||||
755.0015440740636
|
||||
-8.453804974988888e-07,
|
||||
0.0022314430347624794,
|
||||
-1.9626065342276378,
|
||||
1330.1589912157262
|
||||
],
|
||||
"cV": [
|
||||
0.0,
|
||||
0.0,
|
||||
1.7239651981209695e-06,
|
||||
754.9984536032173
|
||||
8.346377269227008e-07,
|
||||
-0.002289692013105165,
|
||||
2.0930363910460232,
|
||||
117.46650514532276
|
||||
],
|
||||
"rhomolar_max": 897.0395262628024,
|
||||
"rhomolar_min": 896.9605331088118
|
||||
"rhomolar_max": 903.4045446436754,
|
||||
"rhomolar_min": 890.603960171529
|
||||
},
|
||||
"gas_constant": 8.314472,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -1,6 +1,6 @@
|
||||
{
|
||||
"ALIASES": [
|
||||
"METHYLSTEARATE",
|
||||
"METHYLSTEARATE",
|
||||
"MSTEARAT"
|
||||
],
|
||||
"ANCILLARIES": {
|
||||
|
||||
@@ -427,22 +427,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 44.491800000000005,
|
||||
"T_min": 44.48723171770732,
|
||||
"T_min": 44.49141355465158,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
-1.1025814119387474e-13,
|
||||
1.491524533973909e-09,
|
||||
0.00011741598951019355,
|
||||
42.338817257479654
|
||||
0.0,
|
||||
0.0,
|
||||
-1.5811616648711508e-06,
|
||||
44.52956130288046
|
||||
],
|
||||
"cV": [
|
||||
1.7438239837612905e-13,
|
||||
-1.890874143571898e-08,
|
||||
0.0006047801629533931,
|
||||
38.4577598458307
|
||||
0.0,
|
||||
0.0,
|
||||
1.5834258838542428e-06,
|
||||
44.4539846230418
|
||||
],
|
||||
"rhomolar_max": 24720.30951969461,
|
||||
"rhomolar_min": 23047.532486140095
|
||||
"rhomolar_max": 24126.40596873362,
|
||||
"rhomolar_min": 23637.943519451463
|
||||
},
|
||||
"gas_constant": 8.31434,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -349,22 +349,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 433.74,
|
||||
"T_min": 433.73999999926514,
|
||||
"T_min": 433.73543171770734,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
0.0,
|
||||
0.0,
|
||||
-2.793653710159193e-08,
|
||||
433.7400913524763
|
||||
1.8157110662036835e-09,
|
||||
-1.8874192929720874e-05,
|
||||
0.0651915711809464,
|
||||
358.895660684941
|
||||
],
|
||||
"cV": [
|
||||
0.0,
|
||||
0.0,
|
||||
2.7689755256340264e-08,
|
||||
433.7399094545003
|
||||
-2.2365486585331262e-09,
|
||||
2.089693784319932e-05,
|
||||
-0.06492040004203695,
|
||||
500.7835165371252
|
||||
],
|
||||
"rhomolar_max": 3270.026304880335,
|
||||
"rhomolar_min": 3269.973461489175
|
||||
"rhomolar_max": 3339.892894257803,
|
||||
"rhomolar_min": 3198.06041887194
|
||||
},
|
||||
"gas_constant": 8.314472,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -501,22 +501,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 126.19200000000001,
|
||||
"T_min": 126.19199984500558,
|
||||
"T_min": 126.19199998688855,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
0.0,
|
||||
0.0,
|
||||
-1.7874713257311775e-07,
|
||||
126.19399909031777
|
||||
-1.547800694886972e-07,
|
||||
126.19373104504585
|
||||
],
|
||||
"cV": [
|
||||
0.0,
|
||||
0.0,
|
||||
1.1629442664483669e-08,
|
||||
126.19186993745916
|
||||
9.95463660457675e-10,
|
||||
126.19198886683252
|
||||
],
|
||||
"rhomolar_max": 11184.76858012661,
|
||||
"rhomolar_min": 11170.573704081868
|
||||
"rhomolar_max": 11183.986174852074,
|
||||
"rhomolar_min": 11170.73026187868
|
||||
},
|
||||
"gas_constant": 8.31451,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -417,22 +417,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 38.34,
|
||||
"T_min": 38.33961355465158,
|
||||
"T_min": 38.33996730937413,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
0.0,
|
||||
0.0,
|
||||
-2.3235096620580277e-06,
|
||||
38.38003407147726
|
||||
-6.850188755192064e-07,
|
||||
38.3518028752252
|
||||
],
|
||||
"cV": [
|
||||
0.0,
|
||||
0.0,
|
||||
2.3247053545885936e-06,
|
||||
38.29994532674044
|
||||
6.843466890793785e-07,
|
||||
38.328208706547166
|
||||
],
|
||||
"rhomolar_max": 17396.319664916562,
|
||||
"rhomolar_min": 17063.76588019465
|
||||
"rhomolar_max": 17277.722226405003,
|
||||
"rhomolar_min": 17182.23089934681
|
||||
},
|
||||
"gas_constant": 8.3144621,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -2,7 +2,7 @@
|
||||
"ALIASES": [
|
||||
"Orthohydrogen",
|
||||
"orthohydrogen",
|
||||
"ORTHOHYDROGEN",
|
||||
"ORTHOHYDROGEN",
|
||||
"ORTHOHYD"
|
||||
],
|
||||
"ANCILLARIES": {
|
||||
@@ -380,22 +380,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 33.22,
|
||||
"T_min": 33.21999999998802,
|
||||
"T_min": 33.216973257617425,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
0.0,
|
||||
0.0,
|
||||
-4.57432325893615e-10,
|
||||
33.220007064832
|
||||
4.066468806855226e-12,
|
||||
-2.0485786362827496e-07,
|
||||
0.003417899984425546,
|
||||
14.316580566669387
|
||||
],
|
||||
"cV": [
|
||||
0.0,
|
||||
0.0,
|
||||
4.301031431449862e-10,
|
||||
33.219993357254666
|
||||
-3.379814959674437e-12,
|
||||
1.404217131242082e-07,
|
||||
-0.0019188970430762365,
|
||||
41.812545688089735
|
||||
],
|
||||
"rhomolar_max": 15444.566501913807,
|
||||
"rhomolar_min": 15444.512461229047
|
||||
"rhomolar_max": 15899.98591137461,
|
||||
"rhomolar_min": 14989.857909343546
|
||||
},
|
||||
"gas_constant": 8.314472,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -415,22 +415,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 38.34,
|
||||
"T_min": 38.33961355465158,
|
||||
"T_min": 38.33996730937413,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
0.0,
|
||||
0.0,
|
||||
-2.3234750017306126e-06,
|
||||
38.38003347427982
|
||||
-6.849502299785245e-07,
|
||||
38.35180169246253
|
||||
],
|
||||
"cV": [
|
||||
0.0,
|
||||
0.0,
|
||||
2.3248386159631863e-06,
|
||||
38.29994303064696
|
||||
6.848389037037868e-07,
|
||||
38.32820022568919
|
||||
],
|
||||
"rhomolar_max": 17396.32214598207,
|
||||
"rhomolar_min": 17063.77540885253
|
||||
"rhomolar_max": 17277.727009113827,
|
||||
"rhomolar_min": 17182.26523245882
|
||||
},
|
||||
"gas_constant": 8.3144621,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -2,7 +2,7 @@
|
||||
"ALIASES": [
|
||||
"Parahydrogen",
|
||||
"parahydrogen",
|
||||
"PARAHYDROGEN",
|
||||
"PARAHYDROGEN",
|
||||
"PARAHYD"
|
||||
],
|
||||
"ANCILLARIES": {
|
||||
@@ -420,22 +420,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 32.938,
|
||||
"T_min": 32.93799999997271,
|
||||
"T_min": 32.93599461397884,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
0.0,
|
||||
0.0,
|
||||
-6.176636722223463e-10,
|
||||
32.938009597258144
|
||||
4.253205081213295e-12,
|
||||
-2.116493776473347e-07,
|
||||
0.0034966692458426726,
|
||||
13.749966028178376
|
||||
],
|
||||
"cV": [
|
||||
0.0,
|
||||
0.0,
|
||||
5.786265121310599e-10,
|
||||
32.93799100930126
|
||||
-3.141534424322369e-12,
|
||||
1.338646257848717e-07,
|
||||
-0.0018846003827776433,
|
||||
41.68699310689614
|
||||
],
|
||||
"rhomolar_max": 15538.044190612114,
|
||||
"rhomolar_min": 15537.952830972841
|
||||
"rhomolar_max": 15953.359013823481,
|
||||
"rhomolar_min": 15115.765516662266
|
||||
},
|
||||
"gas_constant": 8.314472,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -459,22 +459,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 364.211,
|
||||
"T_min": 364.20410506132737,
|
||||
"T_min": 364.21041673548024,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
-2.0397446597019764e-10,
|
||||
3.2958687540071058e-06,
|
||||
-0.017748737115287072,
|
||||
396.06517964228243
|
||||
0.0,
|
||||
0.0,
|
||||
-6.505035916897591e-06,
|
||||
364.2464979809985
|
||||
],
|
||||
"cV": [
|
||||
2.0280477994216778e-10,
|
||||
-3.3625914669476956e-06,
|
||||
0.018581444515139024,
|
||||
329.9897393682322
|
||||
0.0,
|
||||
0.0,
|
||||
6.4811926293276935e-06,
|
||||
364.17563213182177
|
||||
],
|
||||
"rhomolar_max": 5722.778431306117,
|
||||
"rhomolar_min": 5189.89767929224
|
||||
"rhomolar_max": 5546.663535640788,
|
||||
"rhomolar_min": 5367.006606323258
|
||||
},
|
||||
"gas_constant": 8.314472,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -376,22 +376,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 487.21000000000004,
|
||||
"T_min": 487.2031050613274,
|
||||
"T_min": 487.20941673548026,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
3.6894468782358206e-10,
|
||||
-4.073513681283046e-06,
|
||||
0.014462353513138904,
|
||||
470.5229580953627
|
||||
0.0,
|
||||
0.0,
|
||||
-2.1155772356204888e-05,
|
||||
487.27322739169836
|
||||
],
|
||||
"cV": [
|
||||
1.1946318431162753e-09,
|
||||
-1.1482911409880193e-05,
|
||||
0.03662536226299625,
|
||||
448.42495860364784
|
||||
0.0,
|
||||
0.0,
|
||||
2.1763182218616364e-05,
|
||||
487.1449572672853
|
||||
],
|
||||
"rhomolar_max": 3085.865073202007,
|
||||
"rhomolar_min": 2900.0292736747374
|
||||
"rhomolar_max": 3016.2291002048787,
|
||||
"rhomolar_min": 2961.858589771953
|
||||
},
|
||||
"gas_constant": 8.314471,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -346,22 +346,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 293.03000000000003,
|
||||
"T_min": 293.02999999985843,
|
||||
"T_min": 293.02697325761744,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
0.0,
|
||||
0.0,
|
||||
-7.658301925164341e-09,
|
||||
293.0300340334938
|
||||
5.973701413916427e-10,
|
||||
-8.378309573561642e-06,
|
||||
0.039073782995767505,
|
||||
232.42219731732985
|
||||
],
|
||||
"cV": [
|
||||
0.0,
|
||||
0.0,
|
||||
7.708669659796271e-09,
|
||||
293.02996574267206
|
||||
-4.2587664193266785e-10,
|
||||
5.257573775768188e-06,
|
||||
-0.02149722855677295,
|
||||
322.1082759616395
|
||||
],
|
||||
"rhomolar_max": 4444.018490179812,
|
||||
"rhomolar_min": 4443.981630049213
|
||||
"rhomolar_max": 4535.77641861197,
|
||||
"rhomolar_min": 4355.023810307573
|
||||
},
|
||||
"gas_constant": 8.314472,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -394,22 +394,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 385.12,
|
||||
"T_min": 385.11310506132736,
|
||||
"T_min": 385.11941673548023,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
1.384320477183494e-11,
|
||||
-6.214242836621232e-07,
|
||||
0.004900765150571461,
|
||||
374.37610683053464
|
||||
0.0,
|
||||
0.0,
|
||||
-1.583911139375003e-05,
|
||||
385.1940127028315
|
||||
],
|
||||
"cV": [
|
||||
1.8819672379934522e-10,
|
||||
-3.0664139289381314e-06,
|
||||
0.01632960178423799,
|
||||
356.56849340248095
|
||||
0.0,
|
||||
0.0,
|
||||
1.5981068543804365e-05,
|
||||
385.04532396245855
|
||||
],
|
||||
"rhomolar_max": 4800.06197048058,
|
||||
"rhomolar_min": 4549.199865356502
|
||||
"rhomolar_max": 4709.605576782584,
|
||||
"rhomolar_min": 4636.284039366143
|
||||
},
|
||||
"gas_constant": 8.314471,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -470,22 +470,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 456.831,
|
||||
"T_min": 456.83099999999655,
|
||||
"T_min": 456.7079808473738,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
0.0,
|
||||
0.0,
|
||||
-1.497293042906961e-09,
|
||||
456.83100538489015
|
||||
-5.2516982254248e-10,
|
||||
4.95822393582125e-06,
|
||||
-0.015285703141563677,
|
||||
472.1032632289936
|
||||
],
|
||||
"cV": [
|
||||
0.0,
|
||||
0.0,
|
||||
1.577833587606056e-09,
|
||||
456.8309943254525
|
||||
5.019316578137991e-10,
|
||||
-6.104407328102757e-06,
|
||||
0.024431712288804266,
|
||||
424.57182248409964
|
||||
],
|
||||
"rhomolar_max": 3596.419300284971,
|
||||
"rhomolar_min": 3596.414813901929
|
||||
"rhomolar_max": 3965.7364882421543,
|
||||
"rhomolar_min": 3221.873367889577
|
||||
},
|
||||
"gas_constant": 8.31451,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -2,7 +2,7 @@
|
||||
"ALIASES": [
|
||||
"R1233zdE",
|
||||
"R1233ZDE",
|
||||
"R1233ZD(E)",
|
||||
"R1233ZD(E)",
|
||||
"R1233ZD"
|
||||
],
|
||||
"ANCILLARIES": {
|
||||
|
||||
@@ -392,22 +392,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 367.85,
|
||||
"T_min": 367.84799461397887,
|
||||
"T_min": 367.84983035809745,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
-6.280447767869642e-11,
|
||||
4.941333351258848e-07,
|
||||
-0.0008447696692286383,
|
||||
367.3343146300655
|
||||
0.0,
|
||||
0.0,
|
||||
-7.28092281910778e-06,
|
||||
367.8803614481557
|
||||
],
|
||||
"cV": [
|
||||
8.488656120290226e-11,
|
||||
-1.3525258087977996e-06,
|
||||
0.006851813473070161,
|
||||
356.6416038903997
|
||||
0.0,
|
||||
0.0,
|
||||
7.273842039048367e-06,
|
||||
367.8196680786972
|
||||
],
|
||||
"rhomolar_max": 4252.211021596844,
|
||||
"rhomolar_min": 4087.906435621643
|
||||
"rhomolar_max": 4193.299505682264,
|
||||
"rhomolar_min": 4146.67781322612
|
||||
},
|
||||
"gas_constant": 8.314472,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -405,22 +405,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 382.52,
|
||||
"T_min": 382.5194167354802,
|
||||
"T_min": 382.5199506598222,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
0.0,
|
||||
0.0,
|
||||
-4.227168461645191e-06,
|
||||
382.53813455270046
|
||||
-7.9305911732753e-07,
|
||||
382.5234022236133
|
||||
],
|
||||
"cV": [
|
||||
0.0,
|
||||
0.0,
|
||||
3.54150649256091e-06,
|
||||
382.5048069371469
|
||||
6.090875342473237e-07,
|
||||
382.51738701447806
|
||||
],
|
||||
"rhomolar_max": 4427.979956342802,
|
||||
"rhomolar_min": 4125.306098974923
|
||||
"rhomolar_max": 4352.215006013345,
|
||||
"rhomolar_min": 4208.993289113025
|
||||
},
|
||||
"gas_constant": 8.314472,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -1,6 +1,6 @@
|
||||
{
|
||||
"ALIASES": [
|
||||
"R1234ZE(Z)",
|
||||
"R1234ZE(Z)",
|
||||
"R1234ZE"
|
||||
],
|
||||
"ANCILLARIES": {
|
||||
@@ -349,22 +349,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 423.27,
|
||||
"T_min": 423.26999999889085,
|
||||
"T_min": 423.26310506132734,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
0.0,
|
||||
0.0,
|
||||
-2.4196343285339583e-08,
|
||||
423.27009972047097
|
||||
-1.0661006391670194e-09,
|
||||
1.2653370461499062e-05,
|
||||
-0.04997314613163001,
|
||||
488.933234607043
|
||||
],
|
||||
"cV": [
|
||||
0.0,
|
||||
0.0,
|
||||
3.019678505019119e-08,
|
||||
423.2698755498882
|
||||
-8.160851613585538e-10,
|
||||
9.267609720003654e-06,
|
||||
-0.03480529660648677,
|
||||
466.4282367596696
|
||||
],
|
||||
"rhomolar_max": 4121.349202957066,
|
||||
"rhomolar_min": 4121.266633051825
|
||||
"rhomolar_max": 4225.213370352157,
|
||||
"rhomolar_min": 4025.0245673273625
|
||||
},
|
||||
"gas_constant": 8.314472,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
@@ -380,22 +380,22 @@
|
||||
],
|
||||
"critical_region_splines": {
|
||||
"T_max": 374.21,
|
||||
"T_min": 373.5716150640238,
|
||||
"T_min": 374.15599701305536,
|
||||
"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
|
||||
"cL": [
|
||||
-3.1676460727923154e-10,
|
||||
4.632248820128229e-06,
|
||||
-0.022560800178147874,
|
||||
410.803318485873
|
||||
-2.358891970526994e-10,
|
||||
3.35250579170572e-06,
|
||||
-0.015826824353177796,
|
||||
399.0175702243528
|
||||
],
|
||||
"cV": [
|
||||
3.734362612529562e-10,
|
||||
-5.680300209122729e-06,
|
||||
0.02879764276811166,
|
||||
325.5497395319938
|
||||
2.033032586375043e-10,
|
||||
-3.2541387283179285e-06,
|
||||
0.017300443262052236,
|
||||
343.6482870886872
|
||||
],
|
||||
"rhomolar_max": 6152.557816507652,
|
||||
"rhomolar_min": 3872.298405322532
|
||||
"rhomolar_max": 5442.556273932187,
|
||||
"rhomolar_min": 4580.218882520725
|
||||
},
|
||||
"gas_constant": 8.314471,
|
||||
"gas_constant_units": "J/mol/K",
|
||||
|
||||
Some files were not shown because too many files have changed in this diff Show More
Reference in New Issue
Block a user