imagingcros.blogg.se - Hydrocarbon dew point calculator excel

#HYDROCARBON DEW POINT CALCULATOR EXCEL INSTALL#
#HYDROCARBON DEW POINT CALCULATOR EXCEL 64 BIT#
#HYDROCARBON DEW POINT CALCULATOR EXCEL 32 BIT#

A number of these are only compatible with the 32 bit version, and these calculations are in the main superseded by new standards and calculations.

#HYDROCARBON DEW POINT CALCULATOR EXCEL 64 BIT#

Users of the 64 bit version of Flocalc will lose access to certain calculations which were marked as legacy.

#HYDROCARBON DEW POINT CALCULATOR EXCEL INSTALL#

While there is no significant advantage to either, if you have 64 bit Excel and wish to use FloXL then you must install the 64 bit version of Flocalc. Version 1.8.1 – Released 23 September 2020įrom release 1.8.1 we support both 64 bit and 32 bit installations.

F319 – USM speed of sound bias calculation added.

C219 F073 – When solving for standard density with density entered below 555.56kg/m3 the Ctl calculation failure resolved.

The following changes have also been included:

C306 F108 – option to select AGA 8:1994 compressibility calculation method calculation added.The following calculation has been added: Version 2.0.0.0 – Released 6 January 2023 Various defect fixes within the following calculations -F048,C015,F003,F070.You can use your copy of RefProp if you already bought it from NIST and more easily couple it to your program through the FluidProp interface.SHA1 B7B4177CD3749D959F917B7ABD29F399E984A00A RefProp contains an advanced mixture model for natural gas components, namely the GERG-2008 model. Mixtures can be composed from the list of available pure fluids. Mixture properties can also be calculated using a generalized model described in the RefProp documentation. Technical equations of state are less accurate but quite sufficient for most technical applications. Reference equations of state are able to describe all experimental thermodynamic property data available for a certain fluid within their experimental uncertainty. It implements reference equations of state as well as technical equations of state for pure fluids and mixtures.

RefProp is the thermodynamic property library from the National Institute of Standards and Technologies in the USA. So, even if your particular fluid is not yet available, it will not cost you much to get it into the library. One of the nice features of the StanMix model is that we can easily add extra fluids to those that are already supplied.

These algorithms also reduce computational time.įor mixtures, StanMix uses the Wong and Sandler mixing rules which are suitable for the modeling of highly non-ideal mixtures, and are thermodynamically consistent. convergence problems close to the critical point and for mixtures with polar fluids.

Advanced and efficient algorithms for phase equilibria (bubble and dew point, PT-flash calculations) that avoid e.g.

The critical point of mixtures can be computed directly and very fast, and is much more accurate than in FreeStanMix.

Further advantages of StanMix over FreeStanMix include: Accuracy has also been slightly improved. This feature is relevant to some scientific and industrial applications. StanMix implements the iPRSV equation of state, a recent improvement of the PRSV equation of state that solves the artificial discontinuity in the calculation of properties in the standard PSRV equation of state.