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:
* #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