mirror of
https://github.com/CoolProp/CoolProp.git
synced 2026-01-09 14:08:08 -05:00
* Expansions are fully wrapped, looking good. Next step is the set of expansions that is the 1D approximation * Get 1D approx working via cython * Count solutions * SuperAncillary class is working >1000x speedup for water Time for C++! * Superancillaries are working! In C++, speedup is more than 2000x. In Python, more like 150x because of Python <-> C++ overhead * Add pmax check for PQ superancillary calls * Update tests * Allow T limits to be obtained * Implement get_fluid_parameter_double for getting superanc value * Add tests for getting parameters from superanc * Script for testing superancillaries for sphinx * Microoptimizations; don't help speed The limiting factor remains the clear function, which takes about 30 ns * Add R125 superancillary * Use the release from fastchebpure for the files * Drop a .gitignore in the unzipped folder * Update superancillary injection script * Turn on superancillaries by default * Missing header * Many int conversions in superancillary * Another int cast * More annoying solution for boost iter max * Fix warnings * One more warning * Clear up the calculation of rho * Update docs_docker-build.yml Use arm64 since the containers were built on mac * Superfluous ; * Update backend.py * Get the critical points working for superancillaries * Fix wrapping changes of xmin&xmax methods * squelch warnings * Version 0 of jupyter notebook for docs * Try to add the notebook to the docs * Add jupyter notebook for superancillary * Lots of updates to superancillary notebook * More updates to docs * Skip pseudo-pure for superancillary docs * Fix output of superancillary figures * Add superancillary plots to docs for the page for each fluid * Make a placeholder figure for fluids without superancillary * Add superancillary plots to task list * Bump to release fixing m-xylene * Relax the location of the REFPROP stuff * Change default name for R-1336mzz(E) * No need for figures to be so large * Don't need REFPROP setting * Bump to fastchebpure release with methanol * Benchmark caching options * Benchmark more granularly * Add the fast methods to public API for HEOS class * Back to memset - can memset with 0 but no other value * Fix how caching is managed in Helmholtz class * Close to final implementation Perhaps a tiny bit more optimization possible? * Update function name * Make message more accurate * Fix init order * Expose update_QT_pure_superanc to Python * Fix when _reducing is set for pures * Fix the post_update * Indent * Notebook * Notebook * Make ln(p) construction lazy Only really matters for debug builds * Also make reference non-const * Inject superancillary for methanol * Make the superancillary loading entirely lazy in debug * Fix PH bug for Nitrogen Closes #2470 * Force the clear to be called on SatL and SatV To invalidate them at start * Default is non-lazy superancillary loading * Add CMake option to have lazy-loading superancillaries [skip ci] Not a good idea unless doing very narrow testing
262 lines
10 KiB
Python
262 lines
10 KiB
Python
import CoolProp
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CP = CoolProp.CoolProp
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import os
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import codecs
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web_dir = os.path.abspath(os.path.join(os.path.dirname(__file__), '..', '..'))
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root_dir = os.path.abspath(os.path.join(web_dir, '..'))
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fluid_template = u""".. _fluid_{fluid:s}:
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{fluid_stars:s}
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{fluid:s}
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{fluid_stars:s}
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{references:s}
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{aliases:s}
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Fluid Information
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=================
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.. csv-table::
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:header-rows: 1
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:escape: @
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:widths: 40, 60
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:delim: ;
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:file: {fluid:s}-info.csv
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REFPROP Validation Data
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=======================
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.. note::
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This figure compares the results generated from CoolProp and those generated from REFPROP. They are all results obtained in the form :math:`Y(T,\\rho)`, where :math:`Y` is the parameter of interest and which for all EOS is a direct evaluation of the EOS
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You can download the script that generated the following figure here: :download:`(link to script)<REFPROPplots/{fluid:s}.py>`, right-click the link and then save as... or the equivalent in your browser. You can also download this figure :download:`as a PDF<REFPROPplots/{fluid:s}.pdf>`.
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.. image:: REFPROPplots/{fluid:s}.png
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Consistency Plots
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=================
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The following figure shows all the flash routines that are available for this fluid. A red + is a failure of the flash routine, a black dot is a success. Hopefully you will only see black dots. The red curve is the maximum temperature curve, and the blue curve is the melting line if one is available for the fluid.
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In this figure, we start off with a state point given by T,P and then we calculate each of the other possible output pairs in turn, and then try to re-calculate T,P from the new input pair. If we don't arrive back at the original T,P values, there is a problem in the flash routine in CoolProp. For more information on how these figures were generated, see :py:mod:`CoolProp.Plots.ConsistencyPlots`
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.. note::
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You can download the script that generated the following figure here: :download:`(link to script)<Consistencyplots/{fluid:s}.py>`, right-click the link and then save as... or the equivalent in your browser. You can also download this figure :download:`as a PDF<Consistencyplots/{fluid:s}.pdf>`.
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.. image:: Consistencyplots/{fluid:s}.png
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Superancillary Plots
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====================
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The following figure shows the accuracy of the superancillary functions relative to extended precision calculations carried out in C++ with the teqp library. The results of the iterative calculations with REFPROP and CoolProp are also shown.
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.. note::
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You can download the script that generated the following figure here: :download:`(link to script)<Superancillaryplots/{fluid:s}.py>`, right-click the link and then save as... or the equivalent in your browser. You can also download this figure :download:`as a PDF<Superancillaryplots/{fluid:s}.pdf>`.
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.. image:: Superancillaryplots/{fluid:s}.png
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"""
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table_template = """ Parameter, Value
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**General**;
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Molar mass [kg/mol];{mm:s}
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CAS number; {CAS:s}
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ASHRAE class; {ASHRAE:s}
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Formula; {formula:s}
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Acentric factor; {acentric:s}
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InChI; {inchi:s}
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InChIKey; {inchikey:s}
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SMILES; {smiles:s}
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ChemSpider ID; {ChemSpider_id:s}
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**Limits**;
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Maximum temperature [K];{Tmax:s}
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Maximum pressure [Pa];{pmax:s}
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**Triple point**;
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Triple point temperature [K];{Tt:s}
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Triple point pressure [Pa]; {pt:s}
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**Critical point**;
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Critical point temperature [K]; {Tc:s}
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Critical point density [kg/m3]; {rhoc_mass:s}
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Critical point density [mol/m3]; {rhoc_molar:s}
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Critical point pressure [Pa]; {pc:s}
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{reducing_string:s}
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"""
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reducing_template = """**Reducing point**;
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Reducing point temperature [K]; {Tr:s}
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Reducing point density [mol/m3]; {rhor_molar:s}
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"""
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bibtex_keys = ['EOS', 'CP0', 'CONDUCTIVITY', 'VISCOSITY', 'MELTING_LINE', 'SURFACE_TENSION']
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bibtex_map = {'EOS': 'Equation of State',
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'CP0': 'Ideal gas specific heat',
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'CONDUCTIVITY': 'Thermal Conductivity',
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'VISCOSITY': 'Viscosity',
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'MELTING_LINE': 'Melting Line',
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'SURFACE_TENSION': 'Surface Tension'}
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from pybtex.database.input import bibtex
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parser = bibtex.Parser()
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bibdata = parser.parse_file(os.path.join(root_dir, "CoolPropBibTeXLibrary.bib"))
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from CoolProp.BibtexParser import BibTeXerClass
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BTC = BibTeXerClass(os.path.join(root_dir, "CoolPropBibTeXLibrary.bib"))
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# See http://stackoverflow.com/questions/19751402/does-pybtex-support-accent-special-characters-in-bib-file/19754245#19754245
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import pybtex
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style = pybtex.plugin.find_plugin('pybtex.style.formatting', 'plain')()
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backend = pybtex.plugin.find_plugin('pybtex.backends', 'html')()
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parser = pybtex.database.input.bibtex.Parser()
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def formula2RST(formula):
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"""
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See: https://docutils.sourceforge.io/docs/ref/rst/roles.html#subscript
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"""
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return formula.replace('_{', r'\ :sub:`').replace('}',r'`\ ').replace(r'\ :sub:`1`\ ', '')
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def entry2html(entry):
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for e in entry:
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return e.text.render(backend).replace('{', '').replace('}', '').replace('\n', ' ')
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def generate_bibtex_string(fluid):
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string = ''
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for key in bibtex_keys:
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header_string = ''
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sect_strings = []
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try:
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# get the item
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bibtex_key = CoolProp.CoolProp.get_BibTeXKey(fluid, key).strip()
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for thekey in bibtex_key.split(','):
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if thekey.strip() in bibdata.entries.keys():
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html = BTC.getEntry(key=thekey.strip(), fmt='html')
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if len(sect_strings) == 0:
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sect = bibtex_map[key]
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header_string = sect + '\n' + '-' * len(sect) + '\n\n'
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sect_strings.append('.. raw:: html\n\n ' + html + '\n\n')
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except ValueError as E:
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print("error: %s" % E)
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string += header_string + '\n\n.. raw:: html\n\n <br><br> \n\n'.join(sect_strings)
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return string
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class FluidInfoTableGenerator(object):
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def __init__(self, name):
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self.name = name
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def write(self, path):
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def tos(n):
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''' convert number to nicely formatted string '''
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n = str(n)
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if 'e' in n:
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l, r = n.split('e')
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n = rf' :math:`{l}@\times 10^{{{r}}}`'
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else:
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return n
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return n
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molar_mass = CoolProp.CoolProp.PropsSI(self.name, 'molemass')
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Tt = CoolProp.CoolProp.PropsSI(self.name, 'Ttriple')
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Tc = CoolProp.CoolProp.PropsSI(self.name, 'Tcrit')
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Tr = CoolProp.CoolProp.PropsSI(self.name, 'T_reducing')
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pc = CoolProp.CoolProp.PropsSI(self.name, 'pcrit')
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pt = CoolProp.CoolProp.PropsSI(self.name, 'ptriple')
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if pt is None:
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pt = "Unknown"
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Tmax = CoolProp.CoolProp.PropsSI(self.name, 'Tmax')
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pmax = CoolProp.CoolProp.PropsSI(self.name, 'pmax')
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acentric = CoolProp.CoolProp.PropsSI(self.name, 'acentric')
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rhoc_mass = CoolProp.CoolProp.PropsSI(self.name, 'rhomass_critical')
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rhoc_molar = CoolProp.CoolProp.PropsSI(self.name, 'rhomolar_critical')
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rhor_molar = CoolProp.CoolProp.PropsSI(self.name, 'rhomolar_reducing')
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CAS = CoolProp.CoolProp.get_fluid_param_string(self.name, "CAS")
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ASHRAE = CoolProp.CoolProp.get_fluid_param_string(self.name, "ASHRAE34")
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formula = CoolProp.CoolProp.get_fluid_param_string(self.name, "formula")
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if formula:
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formula = formula2RST(formula)
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else:
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formula = 'Not applicable'
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formula = formula.replace('_{1}', '')
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InChI = CoolProp.CoolProp.get_fluid_param_string(self.name, "INCHI")
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InChiKey = CoolProp.CoolProp.get_fluid_param_string(self.name, "INCHIKEY")
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smiles = CoolProp.CoolProp.get_fluid_param_string(self.name, "SMILES")
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ChemSpider_id = CoolProp.CoolProp.get_fluid_param_string(self.name, "CHEMSPIDER_ID")
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twoDurl = CoolProp.CoolProp.get_fluid_param_string(self.name, "2DPNG_URL")
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# Generate (or not) the reducing data
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reducing_data = ''
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if abs(Tr - Tc) > 1e-3:
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reducing_data = reducing_template.format(Tr=tos(Tr),
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rhor_molar=tos(rhor_molar))
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args = dict(mm=tos(molar_mass),
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Tt=tos(Tt),
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pt=tos(pt),
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Tc=tos(Tc),
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rhoc_mass=tos(rhoc_mass),
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rhoc_molar=tos(rhoc_molar),
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pc=tos(pc),
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acentric=tos(acentric),
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CAS=tos(CAS),
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ASHRAE=tos(ASHRAE),
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Tmax=tos(Tmax),
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pmax=tos(pmax),
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reducing_string=reducing_data,
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formula=formula,
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inchi=InChI,
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inchikey=InChiKey,
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smiles=smiles,
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ChemSpider_id=ChemSpider_id,
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twoDurl=twoDurl
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)
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out = table_template.format(**args)
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with open(os.path.join(path, self.name + '-info.csv'), 'w') as fp:
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print("writing %s" % os.path.join(path, self.name + '-info.csv'))
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fp.write(out)
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class FluidGenerator(object):
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def __init__(self, fluid):
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self.fluid = fluid
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def write(self, path):
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# Write CSV table data for fluid information
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ITG = FluidInfoTableGenerator(self.fluid)
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ITG.write(path)
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del_old = CP.get_config_string(CP.LIST_STRING_DELIMITER)
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CP.set_config_string(CP.LIST_STRING_DELIMITER, '|')
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try:
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aliases = ', '.join(['``' + a.strip() + '``' for a in CoolProp.CoolProp.get_fluid_param_string(self.fluid, 'aliases').strip().split('|') if a])
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finally:
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CP.set_config_string(CP.LIST_STRING_DELIMITER, del_old)
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if aliases:
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aliases = 'Aliases\n=======\n\n' + aliases + '\n'
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references = generate_bibtex_string(self.fluid)
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if references:
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references = 'References\n==========\n' + references + '\n'
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# Write RST file for fluid
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out = fluid_template.format(aliases=aliases,
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fluid=self.fluid,
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fluid_stars='*' * len(self.fluid),
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references=references
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)
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with codecs.open(os.path.join(path, self.fluid + '.rst'), 'w', encoding='utf-8') as fp:
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print("writing %s" % os.path.join(path, self.fluid + '.rst'))
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fp.write(out)
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