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  • v6.4.1
  • v6.4.0
  • v6.3.0
    ba41b143 · Just a typo ·
  • v6.2.1
    Bugfix release for Javascript
  • v6.2.0
    * Added a new EoS for heavy water
    * Added pre-built wheels for Python 3.6 and Python 3.7
    * The MATLAB wrappers have been abandoned in favour of Python-based calls
    * Add phase specification to high-level interface
    * LabVIEW VIs can now call PropsSI and Props1SI
    * Added a wrapper for Android
  • v6.1.0
    7864c261 · One more try at #1288 ·
  • v6.0.0
    New features:
    
    * MathCAD wrapper working again (thanks to Jeff Henning)
    * Added binary interaction parameters for more than 400 mixtures
    * Added a cubic backend supporting PR and SRK for some calculations
    * Added new non-iterative viscosity model for a few refrigerants (especially R32 and R245fa)
    * Implemented EOS for HCl, D4, ethylene oxide, and dichloroethane from M. Thol
    * ... and a lot of little bugfixes (see issues)
    
    Contributors to this release:
    ibell, jowr, henningjp, bilderbuchi, dinojr, mapipolo, Mol3culo, stefann82, arashsk, pypamart, milesabarr, wahlenkus, saha84, EmiCas, Heathckliff, Tom0310, dizzux, davideziviani, paarfi
    
    Issues Closed:
    
    * `#1056 <http://github.com/CoolProp/CoolProp/issues/1056>`_ : Added "set_reference_state" wrapper for Mathcad and Updated Example Worksheets
    * `#1053 <http://github.com/CoolProp/CoolProp/issues/1053>`_ : Align Tmax with REFPROP values
    * `#1049 <http://github.com/CoolProp/CoolProp/issues/1049>`_ : apply_simple_mixing_rule should be implemented for HEOS instances
    * `#1048 <http://github.com/CoolProp/CoolProp/issues/1048>`_ : Calling set_binary_interaction_double on AbstractState instance has no effect
    * `#1047 <http://github.com/CoolProp/CoolProp/issues/1047>`_ : Mathcad Wrapper Updates for CoolProp 5.x and 6
    * `#1044 <http://github.com/CoolProp/CoolProp/issues/1044>`_ : Manylinux build integration
    * `#1041 <http://github.com/CoolProp/CoolProp/issues/1041>`_ : Fixed Minor MSVC Compiler Warnings
    * `#1034 <http://github.com/CoolProp/CoolProp/issues/1034>`_ : Strange behaviour of densities at critical point
    * `#1033 <http://github.com/CoolProp/CoolProp/issues/1033>`_ : Python builder issues
    * `#1032 <http://github.com/CoolProp/CoolProp/issues/1032>`_ : Rewrite mixture derivatives tests to use new format
    * `#1031 <http://github.com/CoolProp/CoolProp/issues/1031>`_ : Fixes STRING conflict between Mathcad library and cppformat
    * `#1030 <http://github.com/CoolProp/CoolProp/issues/1030>`_ : Add pass-throughs for testing derivatives
    * `#1029 <http://github.com/CoolProp/CoolProp/issues/1029>`_ : Sphinx builder
    * `#1028 <http://github.com/CoolProp/CoolProp/issues/1028>`_ : ALTERNATIVE_REFPROP_PATH ignored for predefined mixtures
    * `#1026 <http://github.com/CoolProp/CoolProp/issues/1026>`_ : Add REFPROP version to REFPROP comparison script
    * `#1025 <http://github.com/CoolProp/CoolProp/issues/1025>`_ : Phase envelopes construction failing for example in docs
    * `#1024 <http://github.com/CoolProp/CoolProp/issues/1024>`_ : VLE calcs failing for SRK & PR backends
    * `#1023 <http://github.com/CoolProp/CoolProp/issues/1023>`_ : AbstractState.update fails for mixtures containing specific refrigerants using REFPROP backend
    * `#1020 <http://github.com/CoolProp/CoolProp/issues/1020>`_ : Add target_link_libraries to CMakeLists.txt
    * `#1014 <http://github.com/CoolProp/CoolProp/issues/1014>`_ : Figure out how to make coolprop static library a clean cmake dependency
    * `#1012 <http://github.com/CoolProp/CoolProp/issues/1012>`_ : Residual Helmholtz energy not work
    * `#1011 <http://github.com/CoolProp/CoolProp/issues/1011>`_ : Update references
    * `#1010 <http://github.com/CoolProp/CoolProp/issues/1010>`_ : Derivative of residual Helmholtz energy with delta
    * `#1009 <http://github.com/CoolProp/CoolProp/issues/1009>`_ : Can't compute densities at the triple point
    * `#1007 <http://github.com/CoolProp/CoolProp/issues/1007>`_ : 'error: key [Ar] was not found in string_to_index'
    * `#1006 <http://github.com/CoolProp/CoolProp/issues/1006>`_ : Use c++14 when building on MINGW
    * `#1005 <http://github.com/CoolProp/CoolProp/issues/1005>`_ : Derivative of the saturation enthalpy cair_sat = d(hsat)/dT
    * `#1003 <http://github.com/CoolProp/CoolProp/issues/1003>`_ : Fix bug in Chung estimation model
    * `#1002 <http://github.com/CoolProp/CoolProp/issues/1002>`_ : Add python 3.5 wheel
    * `#1001 <http://github.com/CoolProp/CoolProp/issues/1001>`_ : DmolarP broken for Air
    * `#1000 <http://github.com/CoolProp/CoolProp/issues/1000>`_ : Fix setting of BIP function
    * `#999 <http://github.com/CoolProp/CoolProp/issues/999>`_ : Abbreviate all journal names
    * `#998 <http://github.com/CoolProp/CoolProp/issues/998>`_ : Refine phase envelope better on liquid side
    * `#997 <http://github.com/CoolProp/CoolProp/issues/997>`_ : Abbreviate IECR in CoolProp reference
    * `#996 <http://github.com/CoolProp/CoolProp/issues/996>`_ : Update references for R245fa and R1234ze(E)
    * `#995 <http://github.com/CoolProp/CoolProp/issues/995>`_ : Check double_equal in CPnumerics.h
    * `#994 <http://github.com/CoolProp/CoolProp/issues/994>`_ : Find a way to simplify includes
    * `#993 <http://github.com/CoolProp/CoolProp/issues/993>`_ : Test/Add example for DLL calling from C
    * `#992 <http://github.com/CoolProp/CoolProp/issues/992>`_ : Fix reference for R1234ze(E) again
    * `#987 <http://github.com/CoolProp/CoolProp/issues/987>`_ : Multiple EOS paper refs run together
    * `#986 <http://github.com/CoolProp/CoolProp/issues/986>`_ : Air lookup in Excel v5.1.2
    * `#982 <http://github.com/CoolProp/CoolProp/issues/982>`_ : Reorganize CoolPropTools.h into smaller modules
    * `#981 <http://github.com/CoolProp/CoolProp/issues/981>`_ : Saturation states
    * `#976 <http://github.com/CoolProp/CoolProp/issues/976>`_ : Add high-level functions to Julia wrapper
    * `#975 <http://github.com/CoolProp/CoolProp/issues/975>`_ : Correct get_parameter_information_string, fixes #974
    * `#973 <http://github.com/CoolProp/CoolProp/issues/973>`_ : Remove warnings when using Julia 0.4 realease
    * `#971 <http://github.com/CoolProp/CoolProp/issues/971>`_ : Fix bug in PhaseEnvelopeRoutines::evaluate
    * `#970 <http://github.com/CoolProp/CoolProp/issues/970>`_ : Props1SI function missing in Mathematica wrapper on OSX
    * `#968 <http://github.com/CoolProp/CoolProp/issues/968>`_ : Update index.rst
    * `#967 <http://github.com/CoolProp/CoolProp/issues/967>`_ : SO2 ancillaries broken
    * `#964 <http://github.com/CoolProp/CoolProp/issues/964>`_ : Update index.rst
    * `#963 <http://github.com/CoolProp/CoolProp/issues/963>`_ : Update index.rst
    * `#962 <http://github.com/CoolProp/CoolProp/issues/962>`_ : Update sample.sce
    * `#960 <http://github.com/CoolProp/CoolProp/issues/960>`_ : Update index.rst
    * `#953 <http://github.com/CoolProp/CoolProp/issues/953>`_ : Remap CoolPropDbl to double
    * `#952 <http://github.com/CoolProp/CoolProp/issues/952>`_ : Switch string formatting to use the cppformat library; see #907
    * `#951 <http://github.com/CoolProp/CoolProp/issues/951>`_ : Allow gibbs as input to first_partial_deriv()
    * `#950 <http://github.com/CoolProp/CoolProp/issues/950>`_ : Wrong units for residual entropy
    * `#949 <http://github.com/CoolProp/CoolProp/issues/949>`_ : Fix {} in bibtex to protect title capitalization
    * `#948 <http://github.com/CoolProp/CoolProp/issues/948>`_ : Update reference for  EOS-CG
    * `#947 <http://github.com/CoolProp/CoolProp/issues/947>`_ : Add Fij to REFPROPMixtureBackend::get_binary_interaction_double
    * `#945 <http://github.com/CoolProp/CoolProp/issues/945>`_ : Add EOS for R245ca
    * `#944 <http://github.com/CoolProp/CoolProp/issues/944>`_ : Update reference for R1233ze(E)
    * `#941 <http://github.com/CoolProp/CoolProp/issues/941>`_ : CoolProp returns same value for p_critical and p_triple for R503
    * `#937 <http://github.com/CoolProp/CoolProp/issues/937>`_ : Allow ability to get refprop version
    * `#934 <http://github.com/CoolProp/CoolProp/issues/934>`_ : Memory access violation on mixture update at very low pressures using tabular backend
    * `#933 <http://github.com/CoolProp/CoolProp/issues/933>`_ : ValueError: Bad phase to solver_rho_Tp_SRK (CoolProp 5.1.2)
    * `#932 <http://github.com/CoolProp/CoolProp/issues/932>`_ : Fix EOS reference for oxygen
    * `#931 <http://github.com/CoolProp/CoolProp/issues/931>`_ : Remap CoolPropDbl to double permanently
    * `#930 <http://github.com/CoolProp/CoolProp/issues/930>`_ : Phase envelopes should be begin at much lower pressure
    * `#929 <http://github.com/CoolProp/CoolProp/issues/929>`_ : PT should start with Halley's method everywhere
    * `#928 <http://github.com/CoolProp/CoolProp/issues/928>`_ : Add EOS for HCl, D4, ethylene oxide, and dichloroethane
    * `#927 <http://github.com/CoolProp/CoolProp/issues/927>`_ : Add ability to use Henry's Law to get guesses for liquid phase composition
    * `#926 <http://github.com/CoolProp/CoolProp/issues/926>`_ : hydrogen formula is wrong
    * `#925 <http://github.com/CoolProp/CoolProp/issues/925>`_ : Fix HS inputs
    * `#921 <http://github.com/CoolProp/CoolProp/issues/921>`_ : Tabular calcs with mixtures often return Dew T< Bubble T using PQ input pair
    * `#920 <http://github.com/CoolProp/CoolProp/issues/920>`_ : Cant find temperature at pressure and entropy
    * `#917 <http://github.com/CoolProp/CoolProp/issues/917>`_ : Fix errors in docs
    * `#907 <http://github.com/CoolProp/CoolProp/issues/907>`_ : Replace string formatting with C++ format library
    * `#905 <http://github.com/CoolProp/CoolProp/issues/905>`_ : Using conda recipes
    * `#885 <http://github.com/CoolProp/CoolProp/issues/885>`_ : Duplicate critical points found
    * `#854 <http://github.com/CoolProp/CoolProp/issues/854>`_ : Coolprop R448A, R449A or R450A
    * `#816 <http://github.com/CoolProp/CoolProp/issues/816>`_ : Issue with viscosity of R245FA
    * `#808 <http://github.com/CoolProp/CoolProp/issues/808>`_ : Implement tangent plane distance
    * `#665 <http://github.com/CoolProp/CoolProp/issues/665>`_ : Viscosity convergence issue
    * `#279 <http://github.com/CoolProp/CoolProp/issues/279>`_ : Rebuild MathCAD wrapper with v5 support
    * `#186 <http://github.com/CoolProp/CoolProp/issues/186>`_ : Convert cubics to HE
    
    Pull Requests merged:
    
    * `#1062 <http://github.com/CoolProp/CoolProp/pull/1062>`_ : Export first_partial_deriv, see #946 #1062
    * `#1056 <http://github.com/CoolProp/CoolProp/pull/1056>`_ : Added "set_reference_state" wrapper for Mathcad and Updated Example Worksheets
    * `#1053 <http://github.com/CoolProp/CoolProp/pull/1053>`_ : Align Tmax with REFPROP values
    * `#1047 <http://github.com/CoolProp/CoolProp/pull/1047>`_ : Mathcad Wrapper Updates for CoolProp 5.x and 6
    * `#1041 <http://github.com/CoolProp/CoolProp/pull/1041>`_ : Fixed Minor MSVC Compiler Warnings
    * `#1031 <http://github.com/CoolProp/CoolProp/pull/1031>`_ : Fixes STRING conflict between Mathcad library and cppformat
    * `#1020 <http://github.com/CoolProp/CoolProp/pull/1020>`_ : Add target_link_libraries to CMakeLists.txt
    * `#982 <http://github.com/CoolProp/CoolProp/pull/982>`_ : Reorganize CoolPropTools.h into smaller modules
    * `#981 <http://github.com/CoolProp/CoolProp/pull/981>`_ : Saturation states
    * `#976 <http://github.com/CoolProp/CoolProp/pull/976>`_ : Add high-level functions to Julia wrapper
    * `#975 <http://github.com/CoolProp/CoolProp/pull/975>`_ : Correct get_parameter_information_string, fixes #974
    * `#973 <http://github.com/CoolProp/CoolProp/pull/973>`_ : Remove warnings when using Julia 0.4 realease
    * `#968 <http://github.com/CoolProp/CoolProp/pull/968>`_ : Update index.rst
    * `#964 <http://github.com/CoolProp/CoolProp/pull/964>`_ : Update index.rst
    * `#963 <http://github.com/CoolProp/CoolProp/pull/963>`_ : Update index.rst
    * `#962 <http://github.com/CoolProp/CoolProp/pull/962>`_ : Update sample.sce
    * `#960 <http://github.com/CoolProp/CoolProp/pull/960>`_ : Update index.rst
    * `#953 <http://github.com/CoolProp/CoolProp/pull/953>`_ : Remap CoolPropDbl to double
    * `#952 <http://github.com/CoolProp/CoolProp/pull/952>`_ : Switch string formatting to use the cppformat library; see #907
    
  • v5.1.2
  • v5.1.1
  • v5.1.0
    ba23ccbf · Bump revision to 5.1.1 ·
  • v5.0.8
  • v5.0.7
    5.0.7
    -----
    
    New Features:
    
    * Added a Lua wrapper
    
    Issues Closed:
    
    * #460: PropsSI ("Q", "P", valueP, "H", valueH, "REFPROP-R410A") only return 0
    * #459: PropsSI ("D", "P", valueP, "T", valueT, "R407C") return bad result in L+V Phasis
    * #454: Add density dependency to entropy and enthalpy of incomprerssible fluids
    * #452: Allow mixtures to have zero mole fractions
    * #450: Calling PropsSI to get thermal conductivity throws an exception
    * #448: Retrieving acentric factor through Props1SI fails
    * #443: Javascript index.html is missing
    * #437: REFPROP predefined mixtures no longer work
    * #434: R404A Refprop value differs from Refprop Value in Excel
    * #432: All the mixture interaction parameters of Gernert are wrong
    * #431: REFPROP should not be reloaded after every call to PropsSI
    * #430: HAPropsSI is missing from the SWIG wrapper
    * #429: Entropy of Melinder fluids giving wrong results
    * #428: On windows, do not error out if REFPROP fluid files are not found in c:\Program Files\REFPROP
    * #427: HapropsSi("W","B", 279.15, "T", 293.15, "P", 101325) lead to a "-1.#IND" value
    * #425: Incompressible viscosity
    * #419: HapropSI ("T","B",273.15+37,"D",273.15+36.44,"P",101325) lead to an error ...
    * #416: Sphinx docs
    * #413: Incompressible entropy
    * #410: Phase envelope segfaults for pure fluids
    * #409: Trivial outputs
    * #408: HapropsSI function issues
    * #403: Error in new CoolProp version in the function HAPropsSI (variable combination 'PH' and 'W')
    * #401: Linux/OSX error with refprop 9.1* and mixtures containing  R1234YF
    * #400: HAPropsSI(Output, "B",valueB, "R", 1, "P", 101325) lead to an error
    * #398: HAPropsSI(Output, "B",252.84, "D";250.85, "P", 101325) lead to an infinite value
    * #387: Vectorised PropSI breaks plotting functions
    * #386: Bibtex numbering
    * #307: Transport Properties for Mixtures
  • v5.0.6
    fa2d50d9 · Version 5.0.6 release ·
  • v5.0.5
    f9d01990 · Touchup to changelog ·
    * Added Mathematica wrapper
    * Added ``Prandtl()`` function to ``AbstractState``
    * Added vectorized ``PropsSImulti`` function that can return a matrix of outputs for vectors of state inputs and desired outputs
    
    Removed Features:
    
    * All the ``PropsSI`` overloads.  For all other types of inputs, the ``PropsSImulti`` function is now used
    
    Issues Closed:
    
    * #375: If one input and one output to PropsSI, bubble error cleanly
    * #373: Move predefined mixture parsing to HelmholtzEOS initializer function
    * #372: Prandtl number is missing from AbstractState
    * #371: Parse inputs to PropsSI/PropsSI(vectorized) and turn into a vector of inputs
    * #370: Docs are missing all the fluid files
    * #368: CoolProp on iOS
    * #367: Python module architecture
    * #366: Get value of universal gas constant
    * #365: REFPROP_lib.h is missed in 5.0.4 source code zip
    * #364: Liquid and vapor saturation pressures are not the same for some fluids
    * #363: Revision synchronisation
    * #359: Add high-level function that allows for multiple outputs
    * #357: Vector functions and state class
    * #349: Host v4 docs
  • v5.0.4
    BUGFIX: Lots of bugs squashed.
    
    New features:
    
    * Julia wrapper added
    * Derivatives along the saturation line for pure fluids implemented
    * Exposed the configuration getter/setter through SWIG (except for MATLAB)
    * Added transport properties for xylenes and Ethylbenzene
    * Surface tension for HFC pseudo-pures added
    
    Issues Closed:
    
    * #355: In MSVC, too many symbols are exported in SWIG+MATLAB
    * #354: REFPROP headers
    * #353: Using HAPropsSI within circular reference on Mac Excel 2011 causes div/0 error!
    * #350: Python module docs
    * #347: Implement calc_melting_line for incompressibles
    * #346: Memory sanitizer is reporting errors with RPVersion function call
    * #344: skip typeerror in Excel to make 32-bit xlam work in 64-bit excel
    * #342: Refprop mixture with 4 components error
    * #339: Some SWIG tests fail due to the inclusion of rapidjson header
    * #337: ECS not yielding the proper values for eta and lambda
    * #332: Make the REFPROP wrapper code 1% more sane
    * #331: Excel wapper shouts errors (in Excel 2013)
    * #330: Implement ECS model for viscosity of xylenes and ethylbenzene
    * #326: expose configuration through SWIG
    * #325: Implement the generalized derivatives for REFPROP as well
    * #324: SetPath for Refprop
    * #322: Add method to AbstractState to return mixture component names
    * #321: Add more R-number aliases
    * #320: HAPropsSI("T", "V", 0.83, "R", 1, "P", 101325) & lead to infinite value
    * #319: Error in entropy calculation with TH inputs
    * #314: Add surface tension reference information to docs
    * #312: Small examples of the use of derivatives should be in docs
    * #309: MEG properties
    * #308: Set maximum states for saturation curves for pseudo-pures properly
    * #306: Surface Tension for HFC Pseudo-Pure is missing
    * #304: Develop some docs about hooking up with Julia code
    * #294: Add the clang sanitize tests to buildbot
    * #247: Implement thermal conductivity for o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene
    * #238: add a function to retrieve derivatives along the saturation curve
  • v5.0.3
    Bugfix, with some new functionality
    
    The most important fix is for users of Microsoft Excel on windows. It is imperative to download a new CoolProp.dll, there was a serious bug in how Excel and CoolProp interact that has been fixed.
    
    Issues Closed:
    
    * #293: Requirement for zipped source code file
    * #292: Update CycloHexane EOS
    * #289: Two-phase states don't work for DY flash
    * #288 : Some calls in Excel throw FPU exceptions which throw error messages
    * #287: Predefined mixtures cannot be used in PropsSI
    * #285: Cannot solve for conductivity and viscosity
    * #284: Create build steps on the master that allow us to automate the releasing even more
    * #283: Change fullclean logic to use git pull to wipe the folder completely
    * #282: SWIG wrappers not converting errors in PropsSI to exceptions
    * #280: Describe the predefined mixtures with examples on website
  • v5.0.2
    46083a25 · Release notes for 5.0.2 ·
    Bugfix release
    
    Issues closed:
  • v5.0.1
    Released version 5.0.1 to test release script and to fix minor bugs
  • v5.0.0
    7f1c3665 · Fixed CP online docs ·
  • v0.0
    dcb3cfa9 · Update index.rst ·