For instance, R is the refrigerant number for ammonia. Number of rows to include in the fluid tables for the vapor phase. The fluid tables are stored in a structure array the output fluidTables. The properties are those required of a two-phase fluid model—among them specific volume, specific entropy, kinematic viscosity, and thermal conductivity. You can also use any of the aliases of the fluids that are the listed on the fluid page. Get the properties of Ra from CoolProp and save them as tables in a structure named raTables. Lower and upper bounds of the specific internal energy range onto which to map the fluid properties.

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The function queries the database indicated in the installPath argument for the fluid named in the substance argument. Number of rows to include in the fluid tables for the liquid phase.

Contents of the fluidTables Structure Array.

Assume the CoolProp root folder to be C: Furthermore, there is a number of other secondary fluids that can be accessed in the same way. For Lithium-Bromide, the publication by Patek and Klomfar from was implemented based on the source code provided by the authors.

The fluid name is set up like this: Therefore, all solutions have a reference temperature and concentration in the original work by Melinder and Skovrup as well as in CoolProp: Click here to see To view all translated materials including this page, select Country from the country navigator on the bottom of this refprop 7 software.


Lower and upper bounds refprop 7 software the specific internal energy range onto which to map the fluid properties. CoolProp import Props Density of dry air at 1 atm. Props ‘D”T’, ‘P’ The property tables are formatted as matrices with mLiquid or mVapor rows spanning the specific internal energies given in uRange and n columns spanning the pressures given in pRange.

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Created using Sphinx 1. Number of rows to include in the fluid tables for the vapor phase. Output Arguments collapse all fluidTables — Name of the structure in which to save the fluid tables structure array.

Please follow the instructions from https: Number of columns to include in the fluid tables. These only allow for calls with temperature and pressure as input and provide only a subset of thermophysical properties, namely: The root folder of the installation should contain a DLL file refprp All the brines and solutions can be accessed through the Props refprop 7 software.

Select the block and get its path name: Data is available for temperatures from 0 C to C and for the full composition range. To use one of these fluids, do something like. Number of elements in the pressure vector below the critical pressure.


CoolProp is compatible with Windows, Linux, and Macintosh systems. The upper bound can be above the critical pressure of the fluid. Props ‘D”Q’1’P’ The number of columns is the same whether for the liquid or vapor phase. Trial Software Product Updates.

CoolProp Fluid Information — CoolProp documentation

For these fluids, information from commercial data sheets was used to obtain coefficients. Use LiBr to acccess the functions. Refprop 7 software, the available output keys for the Props function are: Refer to the database documentation for a list of valid fluid names. Each row gives the fluid properties at a fixed value of the normalized specific internal energy, with the normalized specific internal energy increasing from left to right between the vapor saturation value and the upper bound of uRange.

It might be necessary to adjust the solid content during heat transfer.