Add a few closed issues to changelog

Bump revision to 5.1.1

Merge branch 'release' of https://github.com/coolprop/coolprop into r…

…elease

5.0.7

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New Features:

* Added a Lua wrapper

Issues Closed:

* CoolProp#460: PropsSI ("Q", "P", valueP, "H", valueH, "REFPROP-R410A") only return 0
* CoolProp#459: PropsSI ("D", "P", valueP, "T", valueT, "R407C") return bad result in L+V Phasis
* CoolProp#454: Add density dependency to entropy and enthalpy of incomprerssible fluids
* CoolProp#452: Allow mixtures to have zero mole fractions
* CoolProp#450: Calling PropsSI to get thermal conductivity throws an exception
* CoolProp#448: Retrieving acentric factor through Props1SI fails
* CoolProp#443: Javascript index.html is missing
* CoolProp#437: REFPROP predefined mixtures no longer work
* CoolProp#434: R404A Refprop value differs from Refprop Value in Excel
* CoolProp#432: All the mixture interaction parameters of Gernert are wrong
* CoolProp#431: REFPROP should not be reloaded after every call to PropsSI
* CoolProp#430: HAPropsSI is missing from the SWIG wrapper
* CoolProp#429: Entropy of Melinder fluids giving wrong results
* CoolProp#428: On windows, do not error out if REFPROP fluid files are not found in c:\Program Files\REFPROP
* CoolProp#427: HapropsSi("W","B", 279.15, "T", 293.15, "P", 101325) lead to a "-1.#IND" value
* CoolProp#425: Incompressible viscosity
* CoolProp#419: HapropSI ("T","B",273.15+37,"D",273.15+36.44,"P",101325) lead to an error ...
* CoolProp#416: Sphinx docs
* CoolProp#413: Incompressible entropy
* CoolProp#410: Phase envelope segfaults for pure fluids
* CoolProp#409: Trivial outputs
* CoolProp#408: HapropsSI function issues
* CoolProp#403: Error in new CoolProp version in the function HAPropsSI (variable combination 'PH' and 'W')
* CoolProp#401: Linux/OSX error with refprop 9.1* and mixtures containing  R1234YF
* CoolProp#400: HAPropsSI(Output, "B",valueB, "R", 1, "P", 101325) lead to an error
* CoolProp#398: HAPropsSI(Output, "B",252.84, "D";250.85, "P", 101325) lead to an infinite value
* CoolProp#387: Vectorised PropSI breaks plotting functions
* CoolProp#386: Bibtex numbering
* CoolProp#307: Transport Properties for Mixtures

Version 5.0.6 release

Signed-off-by: Ian Bell <[email protected]>

* 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:

* CoolProp#375: If one input and one output to PropsSI, bubble error cleanly
* CoolProp#373: Move predefined mixture parsing to HelmholtzEOS initializer function
* CoolProp#372: Prandtl number is missing from AbstractState
* CoolProp#371: Parse inputs to PropsSI/PropsSI(vectorized) and turn into a vector of inputs
* CoolProp#370: Docs are missing all the fluid files
* CoolProp#368: CoolProp on iOS
* CoolProp#367: Python module architecture
* CoolProp#366: Get value of universal gas constant
* CoolProp#365: REFPROP_lib.h is missed in 5.0.4 source code zip
* CoolProp#364: Liquid and vapor saturation pressures are not the same for some fluids
* CoolProp#363: Revision synchronisation
* CoolProp#359: Add high-level function that allows for multiple outputs
* CoolProp#357: Vector functions and state class
* CoolProp#349: Host v4 docs

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:

* CoolProp#355: In MSVC, too many symbols are exported in SWIG+MATLAB
* CoolProp#354: REFPROP headers
* CoolProp#353: Using HAPropsSI within circular reference on Mac Excel 2011 causes div/0 error!
* CoolProp#350: Python module docs
* CoolProp#347: Implement calc_melting_line for incompressibles
* CoolProp#346: Memory sanitizer is reporting errors with RPVersion function call
* CoolProp#344: skip typeerror in Excel to make 32-bit xlam work in 64-bit excel
* CoolProp#342: Refprop mixture with 4 components error
* CoolProp#339: Some SWIG tests fail due to the inclusion of rapidjson header
* CoolProp#337: ECS not yielding the proper values for eta and lambda
* CoolProp#332: Make the REFPROP wrapper code 1% more sane
* CoolProp#331: Excel wapper shouts errors (in Excel 2013)
* CoolProp#330: Implement ECS model for viscosity of xylenes and ethylbenzene
* CoolProp#326: expose configuration through SWIG
* CoolProp#325: Implement the generalized derivatives for REFPROP as well
* CoolProp#324: SetPath for Refprop
* CoolProp#322: Add method to AbstractState to return mixture component names
* CoolProp#321: Add more R-number aliases
* CoolProp#320: HAPropsSI("T", "V", 0.83, "R", 1, "P", 101325) & lead to infinite value
* CoolProp#319: Error in entropy calculation with TH inputs
* CoolProp#314: Add surface tension reference information to docs
* CoolProp#312: Small examples of the use of derivatives should be in docs
* CoolProp#309: MEG properties
* CoolProp#308: Set maximum states for saturation curves for pseudo-pures properly
* CoolProp#306: Surface Tension for HFC Pseudo-Pure is missing
* CoolProp#304: Develop some docs about hooking up with Julia code
* CoolProp#294: Add the clang sanitize tests to buildbot
* CoolProp#247: Implement thermal conductivity for o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene
* CoolProp#238: add a function to retrieve derivatives along the saturation curve

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:

* CoolProp#293: Requirement for zipped source code file
* CoolProp#292: Update CycloHexane EOS
* CoolProp#289: Two-phase states don't work for DY flash
* CoolProp#288 : Some calls in Excel throw FPU exceptions which throw error messages
* CoolProp#287: Predefined mixtures cannot be used in PropsSI
* CoolProp#285: Cannot solve for conductivity and viscosity
* CoolProp#284: Create build steps on the master that allow us to automate the releasing even more
* CoolProp#283: Change fullclean logic to use git pull to wipe the folder completely
* CoolProp#282: SWIG wrappers not converting errors in PropsSI to exceptions
* CoolProp#280: Describe the predefined mixtures with examples on website

Bugfix release

Issues closed:

Released version 5.0.1 to test release script and to fix minor bugs