From db178fe5fd03be68383c41224b71dad5eb14241d Mon Sep 17 00:00:00 2001 From: Ian Bell Date: Fri, 19 Dec 2014 17:46:47 -0600 Subject: [PATCH] Added release notes for v5.0.4 Signed-off-by: Ian Bell --- Web/coolprop/changelog.rst | 41 +++++++++++++++++++++++++++++++++++++- 1 file changed, 40 insertions(+), 1 deletion(-) diff --git a/Web/coolprop/changelog.rst b/Web/coolprop/changelog.rst index e5038d96..814c0737 100644 --- a/Web/coolprop/changelog.rst +++ b/Web/coolprop/changelog.rst @@ -4,9 +4,48 @@ Changelog for CoolProp 5.0.4 ----- +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: -* `#309 `_ : Heat capacity of Ethylene-Glycol mixture is off by a factor of 1e3 +* `#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 + 5.0.3 -----