5.0.7
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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