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Added changelog for v5.0.7

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Jorrit Wronski
2015-02-11 15:58:26 +01:00
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Changelog for CoolProp
======================
5.0.7
-----
New Features:
* Added a Lua wrapper
Issues Closed:
* `#460 <http://github.com/CoolProp/CoolProp/issues/460>`_ : PropsSI ("Q", "P", valueP, "H", valueH, "REFPROP-R410A") only return 0
* `#459 <http://github.com/CoolProp/CoolProp/issues/459>`_ : PropsSI ("D", "P", valueP, "T", valueT, "R407C") return bad result in L+V Phasis
* `#456 <http://github.com/CoolProp/CoolProp/issues/456>`_ : Slave alert
* `#454 <http://github.com/CoolProp/CoolProp/issues/454>`_ : Add density dependency to entropy and enthalpy of incomprerssible fluids
* `#452 <http://github.com/CoolProp/CoolProp/issues/452>`_ : Allow mixtures to have zero mole fractions
* `#450 <http://github.com/CoolProp/CoolProp/issues/450>`_ : Calling PropsSI to get thermal conductivity throws an exception
* `#448 <http://github.com/CoolProp/CoolProp/issues/448>`_ : Retrieving acentric factor through Props1SI fails
* `#443 <http://github.com/CoolProp/CoolProp/issues/443>`_ : Javascript index.html is missing
* `#437 <http://github.com/CoolProp/CoolProp/issues/437>`_ : REFPROP predefined mixtures no longer work
* `#434 <http://github.com/CoolProp/CoolProp/issues/434>`_ : R404A Refprop value differs from Refprop Value in Excel
* `#432 <http://github.com/CoolProp/CoolProp/issues/432>`_ : All the mixture interaction parameters of Gernert are wrong
* `#431 <http://github.com/CoolProp/CoolProp/issues/431>`_ : REFPROP should not be reloaded after every call to PropsSI
* `#430 <http://github.com/CoolProp/CoolProp/issues/430>`_ : HAPropsSI is missing from the SWIG wrapper
* `#429 <http://github.com/CoolProp/CoolProp/issues/429>`_ : Entropy of Melinder fluids giving wrong results
* `#428 <http://github.com/CoolProp/CoolProp/issues/428>`_ : On windows, do not error out if REFPROP fluid files are not found in c:\Program Files\REFPROP
* `#427 <http://github.com/CoolProp/CoolProp/issues/427>`_ : HapropsSi("W","B", 279.15, "T", 293.15, "P", 101325) lead to a "-1.#IND" value
* `#425 <http://github.com/CoolProp/CoolProp/issues/425>`_ : Incompressible viscosity
* `#419 <http://github.com/CoolProp/CoolProp/issues/419>`_ : HapropSI ("T","B",273.15+37,"D",273.15+36.44,"P",101325) lead to an error ...
* `#416 <http://github.com/CoolProp/CoolProp/issues/416>`_ : Sphinx docs
* `#413 <http://github.com/CoolProp/CoolProp/issues/413>`_ : Incompressible entropy
* `#410 <http://github.com/CoolProp/CoolProp/issues/410>`_ : Phase envelope segfaults for pure fluids
* `#409 <http://github.com/CoolProp/CoolProp/issues/409>`_ : Trivial outputs
* `#408 <http://github.com/CoolProp/CoolProp/issues/408>`_ : HapropsSI function issues
* `#403 <http://github.com/CoolProp/CoolProp/issues/403>`_ : Error in new CoolProp version in the function HAPropsSI (variable combination 'PH' and 'W')
* `#401 <http://github.com/CoolProp/CoolProp/issues/401>`_ : Linux/OSX error with refprop 9.1* and mixtures containing R1234YF
* `#400 <http://github.com/CoolProp/CoolProp/issues/400>`_ : HAPropsSI(Output, "B",valueB, "R", 1, "P", 101325) lead to an error
* `#398 <http://github.com/CoolProp/CoolProp/issues/398>`_ : HAPropsSI(Output, "B",252.84, "D";250.85, "P", 101325) lead to an infinite value
* `#387 <http://github.com/CoolProp/CoolProp/issues/387>`_ : Vectorised PropSI breaks plotting functions
* `#386 <http://github.com/CoolProp/CoolProp/issues/386>`_ : Bibtex numbering
* `#307 <http://github.com/CoolProp/CoolProp/issues/307>`_ : Transport Properties for Mixtures
5.0.6
-----