Release v5.0.7 created by Jorrit Wronski on 11 February 2015, 15:11:58 UTC
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
Target: 173bc5e06d2c6ffe5f7906349e7e92678f38d9e5
Directory: 6958b7052f0a56032817b84b8a27d04e880c5b9b
Directory: 6958b7052f0a56032817b84b8a27d04e880c5b9b
