{"text_format":"1","workbook":"xlsx","n_sheets":7,"sheets":["Summary","Examples","Fluids","User Information","Excel Hints","Sample calcs.","Check Sheet"],"not_rendered":{"charts":1,"images":2,"macros":1,"external_links":0,"defined_names":0,"comments":4,"pivot_tables":0},"unopened":[],"bounds":{"document_bytes":16777216,"sheet_cells":100000,"rows_first":2000,"rows_last":500,"rows_between":2000,"halvings":0,"cell_chars":16384,"cell_head_chars":4096},"cells_cut":0,"cells_raw":0,"read":"whole","date_system":"1900"}

{"sheet":"Summary","index":0,"n_rows":27,"n_cols":5,"rows_kept":27,"cut":false,"hidden":false,"merged":[]}
[]
[]
[null,"Sample Workbook to demonstrate the use of REFPROP in a Spreadsheet."]
[]
[]
[]
[]
[]
[]
[null,null,"Dr. Eric W. Lemmon",null,"Dr. Mark O. McLinden"]
[null,null,"Physical and Chemical Properties Division",null,"Physical and Chemical Properties Division"]
[null,null,"Theory and Modeling of Fluids Group",null,"Experimental Properties of Fluids Group"]
[null,null,"325 Broadway",null,"325 Broadway"]
[null,null,"Boulder, CO 80305, U.S.A.",null,"Boulder, CO 80305, U.S.A."]
[null,"Phone: ","+1-303-497-7939","Phone: ","+1-303-497-3580"]
[null,"Fax: ","+1-303-497-5224","Fax: ","+1-303-497-5224"]
[null,"Web: ","http://www.boulder.nist.gov/div838/theory.html","Web: ","http://FluidProperties.NIST.Gov"]
[]
[]
[null,null,"Dr. Marcia L. Huber"]
[null,null,"Physical and Chemical Properties Division"]
[null,null,"Theory and Modeling of Fluids Group"]
[null,null,"325 Broadway"]
[null,null,"Boulder, CO 80305, U.S.A."]
[null,"Phone: ","+1-303-497-5252"]
[null,"Fax: ","+1-303-497-5224"]
[null,"Web: ","http://www.boulder.nist.gov/div838/theory.html"]

{"sheet":"Examples","index":1,"n_rows":109,"n_cols":17,"rows_kept":109,"cut":false,"hidden":false,"merged":[]}
["***Do not save your work as REFPROP.XLS, but rename it.  This will avoid losing the file if you ever uninstall or reinstall the program.***"]
["The REFPROP.xls file can be saved as a template file (REFPROP.xlt).  When a new Excel file is created (under File/New) using this template file, a suffix number is appended so that the saved material will not overwrite the original file."]
["Text of user-specified values in the input cells is blue."]
["Macros must be enabled to calculate properties."]
["See the help file in the REFPROP graphical interface for additional information on calculating properties."]
["Most properties shown here use the default units of \"Molar SI\"; other available sets:  \"SI\", \"SI with C\", \"Molar SI\", \"E\", \"cgs\", \"mks\", \"M\" (these all need quotes).  The \"SI with C\" set can also be labeled as just \"C\"."]
["(See the \"REFPROP with Instructions and Help.XLS\" file for definitions of these sets)"]
["All unit systems use a mass basis for properties and a mole basis for compositions, except \"Molar SI\", which uses a mole basis for properties."]
["To use mass basis for compositions, add the word \"mass\" to the end of the composition string; see the example at the bottom of this sheet."]
["To permanently change the default units to English, search for \"DefaultUnits = 0\" in the Visual Basic code (press Alt-F11) and change the value to 3."]
["To use predefined mixtures, the extension \".MIX\" must be included in the fluid name, see the example below."]
["For information on making these functions available to any Excel worksheet, see the help file or visit http://www.fontstuff.com/vba/vbatut08.htm for information on how to use these functions in a vba file."]
["A screen shot of REFPROP can be inserted into a worksheet by clicking the \"Print Screen\" key (top row) to copy what is displayed on the monitor when REFPROP.exe is running.  This can then be pasted into a worksheet."]
["NOTE:  The units used here have changed slightly from those used in REFPROP 7.0.  \"SI\" now refers to SI units on a mass basis, while \"Molar SI\" will return the same results as those given in version 7.0."]
[]
["An environment variable can be set to specify the locations of the fluid files.  This new variable should be called RPPrefix and be given the value of \"C:\\Program Files\\REFPROP\" (or the directory where REFPROP is located)."]
["(Environment variables can be set under Start/Settings/Control Panel/System/Advanced/Environment Variables, under the \"User variables\" option.)"]
["The environment variable for the path (located under the \"System variables\") can also be modified by adding \";c:\\program files\\REFPROP\" (or whatever location is used) to the end so that the file REFPROP.DLL can be found from any location."]
["Alternatively, the comments at the beginning of the Visual Basic code (press Alt-F11) tell how to change the working directories in order for REFPROP to locate the fluid files and the DLL."]
[]
[]
["Example:",null,null,"Units:","Molar SI"]
["Pure Fluid Calculations",null,null,"Critical Temp. (K):",{"$f":"Temperature($B$25,\"Crit\",$E$22)","v":126.19199999999999},null,"Triple Point Temp. (K):",{"$f":"Temperature($B$25,\"Trip\",$E$22)","v":63.151000000000003},null,"Critical Temp. (C):",{"$f":"Temperature($B$25,\"Crit\",\"c\")","v":-146.95799999999997}]
[null,null,null,"Crit. Press. (MPa):",{"$f":"Pressure($B$25,\"crit\",$E$22)","v":3.3958000000000004},null,"Trp Pressure (MPa):",{"$f":"Pressure($B$25,\"trip\",$E$22)","v":1.25197818481261E-2},null,"Triple Point Temp. (C):",{"$f":"Temperature($B$25,\"Trip\",\"c\")","v":-209.99899999999997}]
["Fluid:  ","nitrogen",null,"Crit. Dens. (mol/L):",{"$f":"Density($B$25,\"crit\",$E$22)","v":11.1839},null,"Trp Density (mol/L):",{"$f":"Density($B$25,\"trip\",$E$22)","v":30.957306220703618}]
["T","P","r","h","s","Quality"]
["K","MPa","mol/L","J/mol","J/mol-K","—"]
[200,2,{"$f":"Density($B$25,\"TP\",$E$22,A28,B28)","v":1.2552496616383777},{"$f":"Enthalpy($B$25,\"TP\",$E$22,A28,B28)","v":5535.1578078021512},{"$f":"Entropy($B$25,\"TP\",$E$22,A28,B28)","v":154.04335710832169},{"$f":"Quality($B$25,\"TD\",$E$22,A28,C28)","v":"#Superheated vapor with T>Tc"}]
[100,2,{"$f":"Density($B$25,\"TP\",$E$22,A29,B29)","v":24.874424581850569},{"$f":"Enthalpy($B$25,\"TP\",$E$22,A29,B29)","v":-2045.4779477486795},{"$f":"Entropy($B$25,\"TP\",$E$22,A29,B29)","v":94.135503417189454},{"$f":"Quality($B$25,\"TD\",$E$22,A29,C29)","v":-5.2096232091741518E-4}]
[{"$f":"Temperature($B$25,\"PS\",$E$22,B30,E30)","v":103.74691221887008},1,{"$f":"Density($B$25,\"PS\",$E$22,B30,E30)","v":11.156421762179916},{"$f":"Enthalpy($B$25,\"PD\",$E$22,B30,C30)","v":-1483.318336269873},100,{"$f":"Quality($B$25,\"TD\",$E$22,A30,C30)","v":7.4816226934408592E-2}]
[{"$f":"Temperature($B$25,\"PH\",$E$22,B31,D31)","v":66.72859296662682},1,{"$f":"Density($B$25,\"PH\",$E$22,B31,D31)","v":30.493246736524753},-4000,{"$f":"Entropy($B$25,\"TP\",$E$22,A31,B31)","v":70.885113296869108},{"$f":"Quality($B$25,\"TD\",$E$22,A31,C31)","v":-3.0069026118529577E-6},null,"If the phase is known for given inputs of T and P, the following examples show how to obtain much faster calculations:"]
[100,{"$f":"Pressure($B$25,\"Tmelt\",$E$22,A32)","v":204.58751325654546},{"$f":"Density($B$25,\"TP\",$E$22,A32,B32)","v":34.751176352143681},"(Melting point given temperature)",null,null,null,"These examples also show how to force the calculation to search only in the liquid or only in the vapor state (for example, for metastable states.)"]
[{"$f":"Temperature($B$25,\"Pmelt\",$E$22,B33)","v":99.295456674886367},200,{"$f":"Density($B$25,\"TP\",$E$22,A33,B33)","v":34.688726014805965},"(Melting point given pressure)",null,null,null,{"$f":"Density(\"Water\",\"TPL\",\"C\",30,4)","v":997.38009631027921},"(Input state is known to be in the liquid)"]
[60,{"$f":"Pressure($B$25,\"TSUBL\",$E$22,A34)","v":6.2977503272662596E-3},{"$f":"Density($B$25,\"Tsubl\",$E$22,A34)","v":1.2693575669104487E-2},"(Sublimation point given temperature)",null,null,null,{"$f":"Enthalpy(\"Water\",\"TPV\",\"C\",30,0.004)","v":2555.659174409886},"(Input state is known to be in the vapor)"]
[{"$f":"Temperature($B$25,\"Psubl\",$E$22,B35)","v":62.083839302903264},0.01,{"$f":"Density($B$25,\"Psubl\",$E$22,B35)","v":1.9526041494479601E-2},"(Sublimation point given pressure)"]
[]
["Two-Phase Calculations"]
["Compute properties from given temperature and density.",null,null,null,null,null,null,null,null,null,"Liquid","Vapor ","Liquid","Vapor"]
["T","P","r","u","h","s","Quality","rSL","rSV","Surf. Tens.","Viscosity","Viscosity","Th. Cnd.","Th. Cnd.","Z","Z"]
["K","MPa","mol/L","J/mol","J/mol","J/mol-K","—","mol/L","mol/L","mN/m","mPa-s","mPa-s","mW/(m-K)","mW/(m-K)","-","-"]
[100,{"$f":"Pressure($B$25,\"TD\",$E$22,A41,C41)","v":0.7782748802395455},15,{"$f":"Energy($B$25,\"TD\",$E$22,A41,C41)","v":-1962.2969826792892},{"$f":"Enthalpy($B$25,\"TD\",$E$22,A41,C41)","v":-1910.4119906633177},{"$f":"Entropy($B$25,\"TD\",$E$22,A41,C41)","v":95.979925436459368},{"$f":"Quality($B$25,\"TD\",$E$22,A41,C41)","v":3.1141187878215702E-2},{"$f":"LiquidDensity($B$25,\"TD\",$E$22,A41,C41)","v":24.607885592902882},{"$f":"VaporDensity($B$25,\"TD\",$E$22,A41,C41)","v":1.1409208869722482},{"$f":"SurfaceTension($B$25,\"TD\",$E$22,A41,C41)","v":4.0504202917983196},{"$f":"viscosity($B$25,\"TD\",$E$22,A41,H41)","v":75.757589870211206},{"$f":"viscosity($B$25,\"TD\",$E$22,A41,I41)","v":7.4285254313167384},{"$f":"ThermalConductivity($B$25,\"TD\",$E$22,A41,H41)","v":100.11174896483813},{"$f":"ThermalConductivity($B$25,\"TD\",$E$22,A41,I41)","v":10.725845587703468},{"$f":"CompressibilityFactor($B$25,\"TD\",$E$22,A41,H41)","v":3.8038383646434193E-2},{"$f":"CompressibilityFactor($B$25,\"TD\",$E$22,A41,I41)","v":0.82042865863779435}]
[" ",null,null,null,null,null,"Latent heat"]
["Calculate properties given only the saturation pressure.",null,null,null,null,null,"J/mol"]
[{"$f":"Temperature($B$25,\"Pliq\",$E$22,B44)","v":87.907263111350602},0.3,{"$f":"Density($B$25,\"Pliq\",$E$22,B44)","v":26.976716083824989},{"$f":"Energy($B$25,\"Pvap\",$E$22,B44)","v":1688.6917289329886},{"$f":"Enthalpy($B$25,\"Pvap\",$E$22,B44)","v":2351.9811192981997},{"$f":"Entropy($B$25,\"Pvap\",$E$22,B44)","v":145.40314612374249},{"$f":"LatentHeat($B$25,\"P\",$E$22,B44)","v":5153.4118916845337}]
[]
["Calculate properties given only the saturation temperature."]
["(note that some of the following calculations use \"TD&\" to define the input properties, see the \"Mixture Example\" sheet for more information."]
[100,{"$f":"Pressure($B$25,\"Tliq\",$E$22,A48)","v":0.7782748802395455},{"$f":"VaporDensity($B$25,\"Tvap\",$E$22,A48)","v":1.1409208869722482},{"$f":"Energy($B$25,\"TD&\",$E$22,A48,C48)","v":1776.4940736375966},{"$f":"Enthalpy($B$25,\"TD&\",$E$22,A48,C48)","v":2458.6403022906493},{"$f":"Entropy($B$25,\"TD&\",$E$22,A48,C48)","v":139.67044836599902},{"$f":"LatentHeat($B$25,\"T\",$E$22,A48)","v":4509.4829486928202}]
[null,null,{"$f":"LiquidDensity($B$25,\"Tliq\",$E$22,A48)","v":24.607885592902882},{"$f":"Energy($B$25,\"TD&\",$E$22,A48,C49)","v":-2082.4696985233822},{"$f":"Enthalpy($B$25,\"TD&\",$E$22,A48,C49)","v":-2050.8426464021709},{"$f":"Entropy($B$25,\"TD&\",$E$22,A48,C49)","v":94.575618879070831}]
[]
[]
["Example:"]
["Unit Conversions"]
["Unit system:  ","cgs"]
["T","P","r","v","u","h","s","Cv","Cp","w","h","l","Z","Prandtl"]
["K","MPa","g/cm3","cm3/g","J/g","J/g","J/g-K","J/g-K","J/g-K","cm/s","mPa-s","mW/(m-K)","-","Number"]
[100,1,{"$f":"Density($B$25,\"TP\",B54,A57,B57)","v":0.69076560475959148},{"$f":"volume($B$25,\"TP\",B54,A57,B57)","v":1.4476690690875267},{"$f":"Energy($B$25,\"TP\",B54,A57,B57)","v":-74.631102130499315},{"$f":"Enthalpy($B$25,\"TP\",B54,A57,B57)","v":-73.183433061411677},{"$f":"Entropy($B$25,\"TP\",B54,A57,B57)","v":3.3731192342648764},{"$f":"IsochoricHeatCapacity($B$25,\"TP\",B54,A57,B57)","v":0.98330928390286432},{"$f":"IsobaricHeatCapacity($B$25,\"TP\",B54,A57,B57)","v":2.3047524002211635},{"$f":"SpeedOfSound($B$25,\"TP\",B54,A57,B57)","v":60942.495648971541},{"$f":"viscosity($B$25,\"TP\",B54,A57,B57)","v":76.255021984613691},{"$f":"ThermalConductivity($B$25,\"TP\",B54,A57,B57)","v":100.58319809371577},{"$f":"CompressibilityFactor($B$25,\"TP\",B54,A57,B57)","v":4.8775271800144619E-2},{"$f":"Prandtl($B$25,\"TP\",B54,A57,B57)","v":1.7472992336573596}]
[]
["Other Properties"]
["Unit system:  ","E","Isothermal","Volume","Isentropic","Isothermal","Adiabatic","Adiabatic Bulk","Isothermal Bulk"]
["T","P","Compressibility","Expansivity","Expansion","Expansion","Compressibility","Modulus","Modulus"]
["F","psia","1/psia","1/R","Coefficient","Coefficient","1/psia","psia","psia"]
[-200,1000,{"$f":"IsothermalCompressibility($B$25,\"TP\",$B$60,$A$63,$B$63)","v":1.3097386321007211E-3},{"$f":"VolumeExpansivity($B$25,\"TP\",$B$60,$A$63,$B$63)","v":2.0948027959346572E-2},{"$f":"IsentropicExpansionCoef($B$25,\"TP\",$B$60,$A$63,$B$63)","v":3.2797784953024332},{"$f":"IsothermalExpansionCoef($B$25,\"TP\",$B$60,$A$63,$B$63)","v":0.76351111243933867},{"$f":"AdiabaticCompressibility($B$25,\"TP\",$B$60,$A$63,$B$63)","v":3.048986391709931E-4},{"$f":"AdiabaticBulkModulus($B$25,\"TP\",$B$60,$A$63,$B$63)","v":3279.7784953024357},{"$f":"IsothermalBulkModulus($B$25,\"TP\",$B$60,$A$63,$B$63)","v":763.51111243933917}]
[]
[]
["Example:"]
["Mixture Calculations (maximum number of components in a mixture is 20)"]
["System:  ",{"$f":"B73&\" \"&A73&\" + \"&B74&\" \"&A74&\" + \"&B75&\" \"&A75","v":"0,6 nitrogen + 0,05 argon + 0,35 oxygen"}]
[]
[{"$f":"CONCATENATE(A73,\";\",B73,\";\",A74,\";\",B74,\";\",A75,\";\",B75)","v":"nitrogen;0,6;argon;0,05;oxygen;0,35"}]
[]
["Components","Mole Fractions"]
["nitrogen",0.6]
["argon",0.05]
["oxygen",0.35]
["Total",{"$f":"SUM(B73:B75)","v":1}]
[]
[]
["Mixture properties:"]
["r (100 K, 0.1 MPa)",{"$f":"Density($A$70,\"TP\",\"SI\",100,0.1)","v":3.6867629279031009},"kg/m3"]
["r (100 K, 1 MPa)",{"$f":"Density($A$70,\"TP\",\"SI\",100,1)","v":848.20996216600327},"kg/m3"]
[]
[]
["Example:",null,null,"Mole Fraction 1","Mole Fraction 2","Mass Fraction 1","Mass Fraction 2"]
["Predefined Mixture:",null,"r410a.mix",{"$f":"MoleFraction($C$85,1)","v":0.69761469937586296},{"$f":"MoleFraction($C$85,2)","v":0.30238530062413799},{"$f":"MassFraction($C$85,1)","v":0.49999999999999983},{"$f":"MassFraction($C$85,2)","v":0.50000000000000011}]
[null,null,"In addition to the predefined mixtures in REFPROP, any mixture with a \".mix\" extension that you save in the mixtures directory while running the REFPROP graphical interface will be available to the Excel file here."]
["Mixture properties:"]
["r (300 K, 10 MPa)",{"$f":"Density($C$85,\"TP\",\"SI\",300,10)","v":1113.5604396543629},"kg/m3"]
[null,null,null,null,"Properties of the liquid and vapor at the equilibrium compositions (not the R410A composition):"]
["Two phase state point at 300 K, 200 kg/m3:",null,null,null,"Liquid Phase","Liquid Phase","Vapor Phase","Vapor Phase","Liquid","Vapor","Liquid","Vapor ","Liquid","Vapor","Liquid phase","Liquid phase"]
["T","P","r","Quality","Mole Frac.","Mole Frac.","Mole Frac.","Mole Frac.","Density","Density","Viscosity","Viscosity","Th. Cnd.","Th. Cnd.","mass fract.","mass fract."]
["K","MPa","kg/m3","(molar basis)","R32","R125","R32","R125","kg/m3","kg/m3","mPa-s","mPa-s","mW/(m-K)","mW/(m-K)","R32","R125"]
[300,{"$f":"Pressure($C$85,\"TD\",\"SI\",A93,C93)","v":1.7391009650867044},200,{"$f":"Quality($C$85,\"TD\",\"SI\",A93,C93)","v":0.30258014136786227},{"$f":"LiquidMoleFraction($C$85,\"TD\",\"SI\",A93,C93,1)","v":0.69127353003764624},{"$f":"LiquidMoleFraction($C$85,\"TD\",\"SI\",A93,C93,2)","v":0.30872646996235376},{"$f":"VaporMoleFraction($C$85,\"TD\",\"SI\",A93,C93,1)","v":0.71223052175865542},{"$f":"VaporMoleFraction($C$85,\"TD\",\"SI\",A93,C93,2)","v":0.28776947824134463},{"$f":"LiquidDensity($C$85,\"TD\",\"SI\",A93,C93)","v":1050.882047629857},{"$f":"VaporDensity($C$85,\"TD\",\"SI\",A93,C93)","v":68.883394340789451},{"$f":"viscosity($E$94,\"TQ\",\"SI\",A93,0)","v":115.30342144328678},{"$f":"viscosity($E$95,\"TQ\",\"SI\",A93,1)","v":13.799058798537807},{"$f":"ThermalConductivity($E$94,\"TQ\",\"SI\",A93,0)","v":87.501455606567987},{"$f":"ThermalConductivity($E$95,\"TQ\",\"SI\",A93,1)","v":15.803399208651594},{"$f":"mole2mass($C$85,1,E93,F93)","v":0.4925293080198766},{"$f":"mole2mass($C$85,2,E93,F93)","v":0.50747069198012351}]
[null,"Liquid phase composition string:",null,null,{"$f":"CONCATENATE(E92,\";\",E93,\";\",F92,\";\",F93)","v":"R32;0,691273530037646;R125;0,308726469962354"},null,null,null,null,null,null,null,null,null,{"$f":"mass2mole($C$85,1,O93,P93)","v":0.69127353003764624},{"$f":"mass2mole($C$85,2,O93,P93)","v":0.30872646996235381},"(These two cells are just for checking mass to mole conversions)"]
[null,"Vapor phase composition string:",null,null,{"$f":"CONCATENATE(G92,\";\",G93,\";\",H92,\";\",H93)","v":"R32;0,712230521758655;R125;0,287769478241345"}]
[]
[null,null,null,null,"Properties of the liquid and vapor at the equilibrium compositions (not the R410A composition for the liquid):"]
["Dew point at 300 K with equilibrium liquid properties",null,null,null,"Liquid Phase","Liquid Phase",null,null,"Liquid","Vapor","Liquid","Vapor ","Liquid","Vapor"]
["T","P","r","Equilibrium","Mole Frac.","Mole Frac.",null,null,"Enthalpy","Enthalpy","Viscosity","Viscosity","Th. Cnd.","Th. Cnd."]
["K","MPa","kg/m3","Liquid Density","R32","R125",null,null,"kJ/kg","kJ/kg","mPa-s","mPa-s","mW/(m-K)","mW/(m-K)"]
[300,{"$f":"Pressure($C$85,\"TVAP\",\"SI\",A101)","v":1.7351590873846998},{"$f":"Density($C$85,\"TVAP\",\"SI\",A101)","v":69.707325679818339},{"$f":"LiquidDensity($C$85,\"TVAP\",\"SI\",A101)","v":1055.0920653081682},{"$f":"LiquidMoleFraction($C$85,\"TVAP\",\"SI\",A101,,1)","v":0.67501327086585061},{"$f":"LiquidMoleFraction($C$85,\"TVAP\",\"SI\",A101,,2)","v":0.32498672913414944},null,null,{"$f":"Enthalpy($E$102,\"TD&\",\"SI\",A101,D101)","v":242.6534462140776},{"$f":"Enthalpy($C$85,\"TD&\",\"SI\",A101,C101)","v":426.27974829784193},{"$f":"viscosity($E$102,\"TD&\",\"SI\",A101,D101)","v":115.75277638326537},{"$f":"viscosity($C$85,\"TD&\",\"SI\",A101,C101)","v":13.814398966003438},{"$f":"ThermalConductivity($E$102,\"TD&\",\"SI\",A101,D101)","v":86.250977347800671},{"$f":"ThermalConductivity($C$85,\"TD&\",\"SI\",A101,C101)","v":15.8142798620084}]
[null,"Liquid phase composition string:",null,null,{"$f":"CONCATENATE(E100,\";\",E101,\";\",F100,\";\",F101)","v":"R32;0,675013270865851;R125;0,324986729134149"}]
[]
[]
["Alternative method for specifying a mixture setup",null,null,null,"To specify mass composition, add the word \"mass\" at the end of the input"]
["R32/R125 (0.5/0.5)",null,null,null,"R32/R125 (0.5/0.5) mass"]
["T","P","r",null,"T","P","r"]
["K","MPa","kg/m3",null,"K","MPa","kg/m3"]
[300,{"$f":"Pressure($A$106,\"TVAP\",\"SI\",A109)","v":{"$error":"#VALUE!"}},{"$f":"Density($A$106,\"TVAP\",\"SI\",A109)","v":{"$error":"#VALUE!"}},null,300,{"$f":"Pressure($E$106,\"TVAP\",\"SI\",E109)","v":{"$error":"#VALUE!"}},{"$f":"Density($E$106,\"TVAP\",\"SI\",E109)","v":{"$error":"#VALUE!"}}]

{"sheet":"Fluids","index":2,"n_rows":87,"n_cols":10,"rows_kept":87,"cut":false,"hidden":false,"merged":[]}
[null,"Index of pure fluids included in the REFPROP database",null,null,null,null,null,"Index of mixtures included in the REFPROP database"]
["Short Name","File Name","CAS number","Full Chemical Name","EOS Temperature and ",null,"ASHRAE ",null,"Composition","Composition"]
[null,null,null,null,"Pressure Limits",null,"Designation","Components","(mass percentages)","(mole fractions)"]
["acetone","acetone.fld","67-64-1","propanone","178.5-550 K, 700 MPa",null,"air","N2/Ar/O2","75.57/1.27/23.16","0.78120/0.00920/0.20960"]
["ammonia","ammonia.fld","7664-41-7","ammonia","195.495-700 K, 1000 MPa",null,"R401A","R22/R152a/R124","53/13/34","0.57885/0.18587/0.23527"]
["argon","argon.fld","7440-37-1","argon","83.8058-2000 K, 1000 MPa",null,"R401B","R22/R152a/R124","61/11/28","0.65492/0.15461/0.19047"]
["benzene","benzene.fld","71-43-2","benzene","278.7-635 K, 78 MPa",null,"R401C","R22/R152a/R124","33/15/52","0.38559/0.22945/0.38496"]
["butane","butane.fld","106-97-8","n-butane","134.895-575 K, 69 MPa",null,"R402A","R125/Propane/R22","60/2/38","0.50766/0.04606/0.44628"]
["butene","1butene.fld","106-98-9","1-butene","87.8-525 K, 70 MPa",null,"R402B","R125/Propane/R22","38/2/60","0.29986/0.04296/0.65719"]
["carbon dioxide","co2.fld","124-38-9","carbon dioxide","216.592-2000 K, 800 MPa",null,"R403A","Propane/R22/R218","5/75/20","0.10430/0.79785/0.09785"]
["carbon monoxide","co.fld","630-08-0","carbon monoxide","68.16-500 K, 100 MPa",null,"R403B","Propane/R22/R218","5/56/39","0.11708/0.66873/0.21418"]
["carbonyl sulfide","cos.fld","463-58-1","carbon oxide sulfide","134.3-650 K, 50 MPa",null,"R404A","R125/R134a/R143a","44/4/52","0.35782/0.03826/0.60392"]
["cis-butene","c2butene.fld","590-18-1","cis-2-butene","134.3-525 K, 50 MPa",null,"R405A","R22/R152a/R142b/RC318","45/7/5.5/42.5","0.58240/0.11860/0.06125/0.23776"]
["cyclohexane","cyclohex.fld","110-82-7","cyclohexane","279.47-700 K, 80 MPa",null,"R406A","R22/Isobutane/R142b","55/4/41","0.57156/0.06184/0.36660"]
["cyclopropane","cyclopro.fld","75-19-4","cyclopropane","273-473 K, 28 MPa",null,"R407A","R32/R125/R134a","20/40/40","0.34642/0.30032/0.35326"]
["decane","decane.fld","124-18-5","decane","243.5-675 K, 800 MPa",null,"R407B","R32/R125/R134a","10/70/20","0.19787/0.60036/0.20177"]
["deuterium","d2.fld","7782-39-0","deuterium","18.71-423 K, 320 MPa",null,"R407C","R32/R125/R134a","23/25/52","0.38111/0.17956/0.43933"]
["dimethylether","dme.fld","115-10-6","ethylene oxide","131.65-525 K, 40 MPa",null,"R407D","R32/R125/R134a","15/15/70","0.26227/0.11368/0.62405"]
["dodecane","c12.fld","112-40-3","dodecane","263.6-700 K, 700 MPa",null,"R407E","R32/R125/R134a","25/15/60","0.40261/0.10471/0.49268"]
["ethane","ethane.fld","74-84-0","ethane","90.368-675 K, 900 MPa",null,"R408A","R125/R143a/R22","7/46/47","0.05075/0.47628/0.47297"]
["ethanol","ethanol.fld","64-17-5","ethyl alcohol","250-650 K, 280 MPa",null,"R409A","R22/R124/R142b","60/25/15","0.67609/0.17848/0.14543"]
["ethylene","ethylene.fld","74-85-1","ethene","103.986-450 K, 300 MPa",null,"R409B","R22/R124/R142b","65/25/10","0.72671/0.17709/0.09620"]
["fluorine","fluorine.fld","7782-41-4","fluorine","53.4811-300 K, 20 MPa",null,"R410A","R32/R125","50/50","0.69761/0.30239"]
["heavy water","d2o.fld","7789-20-0","deuterium oxide","276.97-800 K, 100 MPa",null,"R410B","R32/R125","45/55","0.65369/0.34631"]
["helium","helium.fld","7440-59-7","helium-4","2.1768-1500 K, 100 MPa",null,"R411A","Propylene/R22/R152a","1.5/87.5/11","0.02936/0.83347/0.13717"]
["heptane","heptane.fld","142-82-5","heptane","182.55-600 K, 100 MPa",null,"R411B","Propylene/R22/R152a","3/94/3","0.05922/0.90305/0.03773"]
["hexane","hexane.fld","110-54-3","hexane","177.83-600 K, 100 MPa",null,"R412A","R22/R218/R142b","70/5/25","0.74619/0.02451/0.22930"]
["hydrogen (normal)","hydrogen.fld","1333-74-0","hydrogen (normal)","13.957-1000 K, 2000 MPa",null,"R413A","R218/R134a/Isobutane","9/88/3","0.04976/0.89658/0.05366"]
["hydrogen sulfide","h2s.fld","7783-06-04","hydrogen sulfide","187.7-760 K, 170 MPa",null,"R414A","R22/R124/Isobutane/R142b","51/28.5/4/16.5","0.57172/0.20242/0.06671/0.15915"]
["isobutane","isobutan.fld","75-28-5","2-methylpropane","113.73-575 K, 35 MPa",null,"R414B","R22/R124/Isobutane/R142b","50/39/1.5/9.5","0.58744/0.29031/0.02622/0.09603"]
["isobutene","ibutene.fld","115-11-7","2-methyl-1-propene","132.4-550 K, 50 MPa",null,"R415A","R22/R152a","82/18","0.77678/0.22322"]
["isohexane","ihexane.fld","107-83-5","2-methylpentane","119.6-550 K, 1000 MPa",null,"R415B","R22/R152a","25/75","0.20295/0.79705"]
["isopentane","ipentane.fld","78-78-4","2-methylbutane","112.65-500 K, 1000 MPa",null,"R416A","R134a/R124/Butane","59/39.5/1.5","0.64718/0.32393/0.02888"]
["krypton","krypton.fld","7439-90-9","krypton","115.775-750 K, 200 MPa",null,"R417A","R125/R134a/Butane","46.6/50/3.4","0.41446/0.52310/0.06244"]
["methane","methane.fld","74-82-8","methane","90.6941-625 K, 1000 MPa",null,"R418A","Propane/R22/R152a","1.5/96/2.5","0.02878/0.93920/0.03202"]
["methanol","methanol.fld","67-56-1","methanol","175.61-620 K, 800 MPa",null,"R419A","R125/R134a/DME","77/19/4","0.70146/0.20360/0.09494"]
["neon","neon.fld","7440-01-09","neon","24.556-700 K, 700 MPa",null,"R420A","R134a/R142b","88/12","0.87839/0.12161"]
["neopentane","neopentn.fld","463-82-1","2,2-dimethylpropane","256.6-550 K, 200 MPa",null,"R421A","R125/R134a","58/42","0.54001/0.45999"]
["nitrogen","nitrogen.fld","7727-37-9","nitrogen","63.151-2000 K, 2200 MPa",null,"R421B","R125/R134a","85/15","0.82810/0.17190"]
["nitrogen triflouride","nf3.fld","7783-54-2","nitrogen trifluoride","85-500 K, 50 MPa",null,"R422A","R125/R134a/Isobutane","85.1/11.5/3.4","0.80550/0.12804/0.06646"]
["nitrous oxide","n2o.fld","10024-97-2","dinitrogen monoxide","182.33-525 K, 50 MPa",null,"R422B","R125/R134a/Isobutane","55/42/3","0.49729/0.44670/0.05601"]
["nonane","nonane.fld","111-84-2","nonane","219.7-600 K, 800 MPa",null,"R422C","R125/R134a/Isobutane","82/15/3","0.77476/0.16671/0.05853"]
["octane","octane.fld","111-65-9","octane","216.37-600 K, 100 MPa",null,"R422D","R125/R134a/Isobutane","65.1/31.5/3.4","0.59629/0.33940/0.06431"]
["oxygen","oxygen.fld","7782-44-7","oxygen","54.361-2000 K, 82 MPa",null,"R423A","R134a/R227ea","52.5/47.5","0.64812/0.35188"]
["parahydrogen","parahyd.fld","1333-74-0p","parahydrogen","13.803-1000 K, 2000 MPa",null,"R424A","R125/R134a/Isobutane/Butane/ Isopentane","50.5/47.9/1/0.6","0.45615/0.49939/0.01679/0.01865/ 0.00902"]
["pentane","pentane.fld","109-66-0","pentane","143.47-600 K, 100 MPa",null,"R425A","R32/R134a/R227ea","18.5/69.5/12","0.32113/0.61513/0.06373"]
["perfluorobutane","c4f10.fld","355-25-9","decafluorobutane","189-500 K, 30 MPa",null,"R426A","R125/R134a/Butane/Isopentane","5.1/93/1.3/0.6","0.04315/0.92568/0.02272/0.00845"]
["perfluoropentane","c5f12.fld","678-26-2","dodecafluoropentane","200-500 K, 30 MPa",null,"R427A","R32/R125/R143a/R134a","15/25/10/50","0.26078/0.18839/0.10762/0.44321"]
["propane","propane.fld","74-98-6","propane","85.53-625 K, 1000 MPa",null,"R428A","R125/R143a/Propane/Isobutane","77.5/20/0.6/1.9","0.69433/0.25589/0.01463/0.03515"]
["propylene","propylen.fld","115-07-1","propene","87.953-575 K, 1000 MPa",null,"R500","R12/R152a","73.8/26.2","0.60610/0.39390"]
["propyne","propyne.fld","74-99-7","propyne","273-474 K, 32 MPa",null,"R501","R22/R12","75/25","0.80751/0.19249"]
["sulfur dioxide","so2.fld","7446-09-05","sulfur dioxide","197.7-525 K, 35 MPa",null,"R502","R22/R115","48.8/51.2","0.62999/0.37001"]
["sulfur hexafluoride","sf6.fld","2551-62-4","sulfur hexafluoride","223.555-625 K, 150 MPa",null,"R503","R23/R13","40.1/59.9","0.49970/0.50030"]
["toluene","toluene.fld","108-88-3","methylbenzene","178-700 K, 500 MPa",null,"R504","R32/R115","48.2/51.8","0.73424/0.26576"]
["trans-butene","t2butene.fld","624-64-6","trans-2-butene","167.6-525 K, 50 MPa",null,"R507A","R125/R143a","50/50","0.41184/0.58816"]
["trifluoroiodomethane","cf3i.fld","2314-97-8","trifluoroiodomethane","120-420 K, 20 MPa",null,"R508A","R23/R116","39/61","0.55758/0.44242"]
["water","water.fld","7732-18-5","water","273.16-2000 K, 1000 MPa",null,"R508B","R23/R116","46/54","0.62675/0.37325"]
["xenon","xenon.fld","7440-63-3","xenon","161.405-750 K, 700 MPa",null,"R509A","R22/R218","44/56","0.63079/0.36921"]
["R11","r11.fld","75-69-4","trichlorofluoromethane","162.68-625 K, 30 MPa"]
["R12","r12.fld","75-71-8","dichlorodifluoromethane","116.099-525 K, 200 MPa"]
["R13","r13.fld","75-72-9","chlorotrifluoromethane","92-403 K, 35 MPa"]
["R14","r14.fld","75-73-0","tetrafluoromethane","120-623 K, 51 MPa"]
["R21","r21.fld","75-43-4","dichlorofluoromethane","200-473 K, 138 MPa"]
["R22","r22.fld","75-45-6","chlorodifluoromethane","115.73-550 K, 60 MPa"]
["R23","r23.fld","75-46-7","trifluoromethane","118.02-475 K, 120 MPa"]
["R32","r32.fld","75-10-5","difluoromethane","136.34-435 K, 70 MPa"]
["R41","r41.fld","593-53-3","fluoromethane","129.82-425 K, 70 MPa"]
["R113","r113.fld","76-13-1","1,1,2-trichloro-1,2,2-trifluoroethane","236.93-525 K, 200 MPa"]
["R114","r114.fld","76-14-2","1,2-dichloro-1,1,2,2-tetrafluoroethane","273.15-507 K, 21 MPa"]
["R115","r115.fld","76-15-3","chloropentafluoroethane","173.75-550 K, 60 MPa"]
["R116","r116.fld","76-16-4","hexafluoroethane","173.1-425 K, 50 MPa"]
["R123","r123.fld","306-83-2","2,2-dichloro-1,1,1-trifluoroethane","166-600 K, 40 MPa"]
["R124","r124.fld","2837-89-0","1-chloro-1,2,2,2-tetrafluoroethane","120-470 K, 40 MPa"]
["R125","r125.fld","354-33-6","pentafluoroethane","172.52-500 K, 60 MPa"]
["R134a","r134a.fld","811-97-2","1,1,1,2-tetrafluoroethane","169.85-455 K, 70 MPa"]
["R141b","r141b.fld","1717-00-6","1,1-dichloro-1-fluoroethane","169.68-500 K, 400 MPa"]
["R142b","r142b.fld","75-68-3","1-chloro-1,1-difluoroethane","142.72-470 K, 60 MPa"]
["R143a","r143a.fld","420-46-2","1,1,1-trifluoroethane","161.34-650 K, 100 MPa"]
["R152a","r152a.fld","75-37-6","1,1-difluoroethane","154.56-500 K, 60 MPa"]
["R218","r218.fld","76-19-7","octafluoropropane","125.45-440 K, 20 MPa"]
["R227ea","r227ea.fld","431-89-0","1,1,1,2,3,3,3-heptafluoropropane","146.35-475 K, 60 MPa"]
["R236ea","r236ea.fld","431-63-0","1,1,1,2,3,3-hexafluoropropane","242-500 K, 60 MPa"]
["R236fa","r236fa.fld","690-39-1","1,1,1,3,3,3-hexafluoropropane","179.52-500 K, 40 MPa"]
["R245ca","r245ca.fld","679-86-7","1,1,2,2,3-pentafluoropropane","200-500 K, 60 MPa"]
["R245fa","r245fa.fld","460-73-1","1,1,1,3,3-pentafluoropropane","171.05-440 K, 200 MPa"]
["R365mfc","r365mfc.fld","406-58-6","1,1,1,3,3-pentafluorobutane","239-500 K, 35 MPa"]
["RC318","rc318.fld","115-25-3","octafluorocyclobutane","233.35-623 K, 60 MPa"]

{"sheet":"User Information","index":3,"n_rows":56,"n_cols":37,"rows_kept":56,"cut":false,"hidden":false,"merged":[[12,6,13,9]]}
["Available functions:",null,"Function Syntax:",null,null,null,"Dimensions",null,null,null,null,null,null,"L3 : U41","Dimensions based on REFPROP.xls"]
[null,null,{"$f":"VLOOKUP(A3,N3:W41,10,FALSE)","v":"Density(FluidName, InpCode, Units, Prop1, Prop2)"},null,null,null,null,"Units Input Code","Units",null,null,null,null,null,"Functions ","US  \"E\"","\"SI\"","\"SI with C\"","Molar SI","mks","cgs","Mixed","Argument definitions are at the beginning  (See the Refprop help file for more details.)",null,null,null,null,null,null,null,null,"Bolded Functions are available in REFPROP.exe and REFPROP.xls          Unbolded functions are in REFPROP.exe ONLY",null,null,null,null,".xls functions"]
[3,null,null,null,null,null,{"$f":"VLOOKUP(A3,N3:W41,3,FALSE)","v":"lbm/ft³"},"\"E\"","English",null,null,null,null,1,"Temperature","°F","K"," °C    ","K","K","K","K","Temperature(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,"(Definition for all of these properties are given in the REFPROP.HLP file)"]
[null,null,"Arguments:  (FluidName, InpCode, Units, Prop1, Prop2, i)",null,null,null,{"$f":"VLOOKUP(A3,N3:W41,4,FALSE)","v":"kg/m³"},"\"SI\"","SI",null,null,null,null,2,"Pressure","psia","MPa","MPa","MPa","kPa","MPa","psia","Pressure(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,"Temperature","Therm. Cond.","Isothrm. Compress.","(Z - 1)/d",null,"Temperature"]
[null,null,"FluidName = text, fluid must be either in Fluids or Mixtures sub directories.  ",null,null,null,{"$f":"VLOOKUP(A3,N3:W41,5,FALSE)","v":"kg/m³"},"\"C\"","SI with °C",null,null,null,null,3,"Density","lbm/ft³","kg/m³","kg/m³","mol/dm³","kg/m³","g/cm³","g/cm³","Density(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,"Pressure","Viscosity","Vol. Expansivity","Exergy",null,"Pressure"]
[null,null,null,"Predefined mixtures must contain .mix suffix   eg:    \"air.mix\"",null,null,{"$f":"VLOOKUP(A3,N3:W41,6,FALSE)","v":"mol/dm³"},"\"Molar SI\"","Molar SI",null,null,null,null,4,"CompressibilityFactor","dimLess","dimLess","dimLess","dimLess","dimLess","dimLess","dimLess","CompressibilityFactor(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,"Density","Kin. Viscosity","Isentropic Expansion","Spec. Heat Input",null,"Density"]
[null,null,"InpCode   = name and order of Prop1 and Prop2.",null,null,null,{"$f":"VLOOKUP(A3,N3:W41,7,FALSE)","v":"kg/m³"},"\"mks\"","mks",null,null,null,null,5,"LiquidDensity","lbm/ft³","kg/m³","kg/m³","mol/dm³","kg/m³","g/cm³","g/cm³","LiquidDensity(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,"Volume","Therm. Diff.","Isothermal Expansion","Cv2phase",null,"CompressibilityFactor"]
[null,null,"            \"TP\" would mean Prop1 is Temperature, Prop2 is Pressure (need quotes)",null,null,null,{"$f":"VLOOKUP(A3,N3:W41,8,FALSE)","v":"g/cm³"},"\"cgs\"","cgs",null,null,null,null,6,"VaporDensity","lbm/ft³","kg/m³","kg/m³","mol/dm³","kg/m³","g/cm³","g/cm³","VaporDensity(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,"Int. Energy","Prandtl","Adi. Compress.","Fpv",null,"LiquidDensity"]
[null,null,"            Valid InpCodes:  TP,TD,TH,TS,TE,TQ,PD,PH,PS,PE,PQ,DH,DS,DE,HS",null,null,null,{"$f":"VLOOKUP(A3,N3:W41,9,FALSE)","v":"g/cm³"},"\"M\"","Mixed",null,null,null,null,7,"Volume","ft³/lbm","m³/kg","m³/kg","dm³/mol","m³/kg","cm³/g","cm³/g","Volume(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,"Enthalpy","Surf. Tension","Adi. Bulk Modulus","Crit. Flow Fact.",null,"VaporDensity"]
[null,null,"            To define saturated liquid or vapor inputs:  TLIQ, TVAP, PLIQ, PVAP instead of T and P",null,null,null,null,null,null,null,null,null,null,8,"Energy","Btu/lbm","kJ/kg","kJ/kg","J/mol","kJ/kg","J/g","J/g","Energy(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,"Entropy","Dielec. Const.","Isothrm. Bulk Modulus","p = p(T,rho)",null,"Volume"]
[null,null,null,"                 Other:  Crit, Trip, TMelt, PMelt, TSubl, PSubl",null,null,null,null,null,null,null,null,null,9,"Enthalpy","Btu/lbm","kJ/kg","kJ/kg","J/mol","kJ/kg","J/g","J/g","Enthalpy(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,"Cv",null,"Iso. Thrott. Coef.","h = h(T,rho)",null,"Energy"]
[null,null,"Units      = \"E\", \"SI\", \"SI with C\" or \"C\", \"Molar SI\", \"mks\", \"cgs\", \"M\" (need quotes)  If blank, then SI is default. (Unless DefaultUnits changed in VBA )",null,null,null,null,null,null,null,null,null,null,10,"Entropy","Btu/lbm-°R","kJ/kg-K","kJ/kg-K","J/mol-K","kJ/kg-K","J/g-K","J/g-K","Entropy(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,"Cp",null,"Gruneisen","s = s(T,rho)",null,"Enthalpy"]
[null,null,"Prop1     = numerical value of the first input property (in the units of the previous line)",null,null,null,"All unit systems use a mass basis for properties and a mole basis for compositions,  except \"Molar SI\" which uses a mole basis for properties",null,null,null,null,null,null,11,"IsochoricHeatCapacity","Btu/lbm-°R","kJ/kg-K","kJ/kg-K","J/mol-K","kJ/kg-K","J/g-K","J/g-K","IsochoricHeatCapacity(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,"Cp0",null,"dp/d(rho)","a = a(T,rho)",null,"Entropy"]
[null,null,"Prop2     = numerical value of the second input property (if required).",null,null,null,null,null,null,null,null,null,null,12,"Cv","Btu/lbm-°R","kJ/kg-K","kJ/kg-K","J/mol-K","kJ/kg-K","J/g-K","J/g-K","Cv(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,"Cp/Cv",null,"d²p/d(rho)²","g = g(T,rho)",null,"IsochoricHeatCapacity"]
[null,null,null,null,null,null,"Define new fluid mixture (FluidName in H21 this worksheet) ",null,null,null,null,null,null,13,"IsobaricHeatCapacity","Btu/lbm-°R","kJ/kg-K","kJ/kg-K","J/mol-K","kJ/kg-K","J/g-K","J/g-K","IsobaricHeatCapacity(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,"Csat",null,"dp/dT","Z = Z(T,rho)",null,"Cv"]
[null,null,"Mixture functions require the index i, which is the component number in the mixture (ranging from 1 to 20).",null,null,null,"CONCATENATE(H22,\";\",H23,\";\",H24,\";\",H25)",null,null,null,null,null,null,14,"Cp","Btu/lbm-°R","kJ/kg-K","kJ/kg-K","J/mol-K","kJ/kg-K","J/g-K","J/g-K","Cp(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,"Sound Speed",null,"dp/dT [sat]","Internal Pressure",null,"IsobaricHeatCapacity"]
[null,null,"FluidName, InpCode, Units  are text.  Use quotes when entering into function.",null,null,null,"Refprop fluid name, \";\", Mole Fraction",null,null,null,null,null,null,15,"SpeedOfSound","ft/s","m/s","m/s","m/s","m/s","cm/s","m/s","SpeedOfSound(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,"Comp. Factor",null,"dh/dZ [sat]","Ideal Gas Density",null,"Cp"]
[null,null,null,"Prop1 and Prop2 are numbers",null,null,null,null,null,null,null,null,null,16,"Sound","ft/s","m/s","m/s","m/s","m/s","cm/s","m/s","Sound(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,"Joule-Thom.",null,"d(rho)/dT","Ideal Gas Enthalpy",null,"SpeedOfSound"]
[null,null,null,"Cell references may be used to assign argument(s)",null,null,"Note   \";\",        (semi-colon in quotes and comma)",null,null,null,null,null,null,17,"LatentHeat","Btu/lbm","kJ/kg","kJ/kg","J/mol","kJ/kg","J/g","J/g","LatentHeat(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,"Quality",null,"d(rho)/dp","Ideal Gas Entropy",null,"Sound"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,18,"HeatOfVaporization","Btu/lbm","kJ/kg","kJ/kg","J/mol","kJ/kg","J/g","J/g","HeatOfVaporization(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,"2nd Virial Coef.",null,"dB/dT","Ideal Gas Gibbs",null,"LatentHeat"]
[null,null,null,null,null,null,"New mixture",{"$f":"CONCATENATE(H22,\";\",H23,\";\",H24,\";\",H25)","v":"argon;0,25;pentane;0,75"},null,null,null,null,null,19,"JouleThompson","°F/psia","K/MPa","K/MPa","K/MPa","K/MPa","K/MPa"," K/psia  ","JouleThompson(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,"3rd Virial Coef.",null,"dh/dT [rho]","Ideal Gas Helmholtz",null,"HeatOfVaporization"]
[null,null,null,null,null,null,"Component 1","argon",null,null,null,null,null,20,"IsentropicExpansionCoef","Cp/Cv","Cp/Cv","Cp/Cv","Cp/Cv","Cp/Cv","Cp/Cv","Cp/Cv","IsentropicExpansionCoef(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,"Helmholtz",null,"dh/dT [p]",null,null,"JouleThompson"]
[null,null,null,null,null,null,"Mole Fraction of 1",0.25,null,null,null,null,null,21,"IsothermalCompressibility","1/psia","1/MPa","1/MPa","1/MPa"," 1/kPa  ","1/MPa"," 1/psia  ","IsothermalCompressibility(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,"Gibbs",null,"dh/d(rho) [T]",null,null,"IsentropicExpansionCoef"]
[null,null,null,null,null,null,"Component 2","pentane",null,null,null,null,null,22,"VolumeExpansivity","1/°R","1/K","1/K"," 1/K  "," 1/K  "," 1/K  "," 1/K  ","VolumeExpansivity(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,"Heat of Vapor.",null,"dh/d(rho) [p]",null,null,"IsothermalCompressibility"]
[null,null,null,null,null,null,"Mole Fraction of 2",0.75,null,null,null,null,null,23,"AdiabaticCompressibility","1/psia","1/MPa","1/MPa"," 1/MPa  "," 1/kPa  "," 1/MPa  "," 1/psia  ","AdiabaticCompressibility(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,"Fugacity",null,"dh/dp [T]",null,null,"VolumeExpansivity"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,24,"AdiabaticBulkModulus","psia","MPa","MPa","MPa"," kPa  ","MPa","psia","AdiabaticBulkModulus(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,"Fugacity Coef.",null,"dh/dp [rho]",null,null,"AdiabaticCompressibility"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,25,"IsothermalExpansionCoef","dimLess","dimLess","dimLess","dimLess","dimLess","dimLess","dimLess","IsothermalExpansionCoef(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,"K value",null,null,null,null,"AdiabaticBulkModulus"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,26,"IsothermalBulkModulus","psia","MPa","MPa"," MPa  "," kPa  "," MPa  "," psia  ","IsothermalBulkModulus(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,"Molar Mass",null,null,null,null,"IsothermalExpansionCoef"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,27,"Quality","lbm/lbm","kg/kg","kg/kg"," mol/mol  "," kg/kg  "," g/g  "," g/g  ","Quality(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,null,null,null,null,null,"IsothermalBulkModulus"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,28,"Viscosity","lbm/ft-s","µPa-s","µPa-s"," µPa-s  "," µPa-s  "," µPa-s  "," µPa-s  ","Viscosity(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,null,null,null,null,null,"Quality"]
["Mole & Mass Fractions of i",null,null,null,null,null,null,null,null,null,null,null,null,29,"ThermalConductivity","Btu/h-ft-°F","mW/m-K","mW/m-K"," mW/m-K  "," W/m-K  "," mW/m-K  "," mW/m-K  ","ThermalConductivity(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,null,null,null,null,null,"Viscosity"]
["Mole2Mass",null,null,null,null,null,null,null,null,null,null,null,null,30,"Prandtl","dimLess","dimLess","dimLess","dimLess","dimLess","dimLess","dimLess","Prandtl(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,null,null,null,null,null,"ThermalConductivity"]
["Mass2Mole",null,null,null,null,null,null,null,".",null,null,null,null,31,"SurfaceTension","lbf/ft","mN/m","mN/m"," mN/m  "," mN/m  "," dyn/cm  "," mN/m  ","SurfaceTension(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,null,null,null,null,null,"Prandtl"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,32,"DielectricConstant","dimLess","dimLess","dimLess","dimLess","dimLess","dimLess","dimLess","DielectricConstant(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,null,null,null,null,null,"SurfaceTension"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,33,"MolarMass","lbm/lbmole","kg/kgmole","kg/kgmole"," kg/kgmole  "," kg/kgmole  "," g/gmole  "," g/gmole  ","MolarMass(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,null,null,null,null,null,"DielectricConstant"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,34,"EOSMax",null,null,null,null,null,null,null,"EOSMax(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,null,null,null,null,null,"MolarMass"]
["The following systems of units can be used in either the REFPROP.exe graphical interface or the REFPROP.xls Excel spreadsheet",null,null,null,null,null,null,null,null,null,null,null,null,35,"EOSMin",null,null,null,null,null,null,null,"EOSmin(FluidName, InpCode, Units, Prop1, Prop2)",null,null,null,null,null,null,null,null,null,null,null,null,null,"EOSMax"]
["The code for DefaultUnits can be set in the REFPROP.xls VBA code  (see the VBA code by pressing F-11 and looking under the \"Modules\" section)",null,null,null,null,null,null,null,null,null,null,null,null,36,"MassFraction           (mix)","lbm/lbm","kg/kg","kg/kg"," mol/mol  "," kg/kg  "," g/g  "," g/g  ","MassFraction(FluidName, i)",null,null,null,null,null,null,null,null,null,null,null,null,null,"EOSmin"]
["The characters in quotes are the acceptable values that the user must insert into the Excel REFPROP functions.",null,null,null,null,null,null,null,null,null,null,null,null,37,"MoleFraction            (mix)","mole/mole","mole/mole","mole/mole","mole/mole","mole/mole","mole/mole","mole/mole","MoleFraction(FluidName, i)",null,null,null,null,null,null,null,null,null,null,null,null,null,"MassFraction           (mix)"]
["If the User does not input any characters in the function code, then the DefaultUunits will be used (currently set to 0)",null,null,null,null,null,null,null,null,null,null,null,null,38,"LiquidMoleFraction   (mix)","mole/mole","mole/mole","mole/mole","mole/mole","mole/mole","mole/mole","mole/mole","LiquidMoleFraction(FluidName, InpCode, Units, Prop1, Prop2, i)",null,null,null,null,null,null,null,null,null,null,null,null,null,"MoleFraction            (mix)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,39,"VaporMoleFraction   (mix)","mole/mole","mole/mole","mole/mole","mole/mole","mole/mole","mole/mole","mole/mole","VaporMoleFraction(FluidName, InpCode, Units, Prop1, Prop2, i)",null,null,null,null,null,null,null,null,null,null,null,null,null,"LiquidMoleFraction   (mix)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"VaporMoleFraction   (mix)"]
["REFPROP units and dimensions",null,null,null,null,null,null,null,null,null,null,null,null,null,"'In the following, i is the component number in the mixture"]
[null,null,null,"DefaultUnits  (code)",null,null,null,null,null,null,null,null,null,null,"'Function MoleFraction          (FluidName, i)"]
[null,null,null,0,5,6,1,2,3,4,null,null,null,null,"'Function MassFraction          (FluidName, i)"]
["REFPROP Functions",null,"Default Units in DLL","\"SI\"","\"SI with C\" or \"C\"","\"Molar SI\"","\"mks\"","\"cgs\"","\"E\"  (English)","\"M\" (Mixed)",null,null,null,null,"'Function LiquidMoleFraction    (FluidName, InpCode, Units, Prop1, Prop2, i)"]
["Temperature",null,"  K","K","  C","K","K","K","  °F","  K",null,null,null,null,"'Function VaporMoleFraction     (FluidName, InpCode, Units, Prop1, Prop2, i)"]
["Pressure",null,"  kPa","  MPa","  MPa","  MPa","  kPa","  MPa","  psia","  psia"]
["Density",null,"  mol/dm^3","  kg/m^3","  kg/m^3","  mol/dm^3","  kg/m^3","  g/cm^3","  lbm/ft^3","  g/cm^3"]
["Volume",null,"  dm^3/mol","  m^3/kg","  m^3/kg","  dm^3/mol","  m^3/kg","  cm^3/g","  ft^3/lbm","  cm^3/g"]
["Energy, Enthalpy",null,"  J/mol","  kJ/kg","  kJ/kg","  J/mol","  kJ/kg","  J/g","  Btu/lbm","  J/g"]
["Entropy, Heat Capacities",null,"  J/mol-K","  kJ/kg-K","  kJ/kg-K","  J/mol-K","  kJ/kg-K","  J/g-K","  Btu/lbm-°R","  J/g-K"]
["Speed of Sound",null,"  m/s","  m/s","  m/s","  m/s","  m/s","  cm/s","  ft/s","  m/s"]
["Viscosity",null,"  uPa-s","  uPa-s","  uPa-s","  uPa-s","  uPa-s","  uPa-s","  lbm/ft-s","  uPa-s"]
["Thermal Conductivity",null,"  W/m-K","  mW/m-K","  mW/m-K","  mW/m-K","  W/m-K","  mW/m-K","  Btu/h-ft-°F","  mW/m-K"]
["Surface Tension",null,"  N/m","  mN/m","mN/m","  mN/m","  mN/m","  dyn/cm","  lbf/ft","  mN/m"]

{"sheet":"Excel Hints","index":4,"n_rows":61,"n_cols":21,"rows_kept":61,"cut":false,"hidden":false,"merged":[]}
[]
[]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Argument definitions are listed at the bottom    (See the Refprop help file for more details.)"]
[]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,1,"Temperature","Temperature(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,2,"Pressure","Pressure(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,3,"Density","Density(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,4,"CompressibilityFactor","CompressibilityFactor(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,5,"LiquidDensity","LiquidDensity(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,6,"VaporDensity","VaporDensity(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,7,"Volume","Volume(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,8,"Energy","Energy(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,9,"Enthalpy","Enthalpy(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,10,"Entropy","Entropy(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,11,"IsochoricHeatCapacity","IsochoricHeatCapacity(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,12,"Cv","Cv(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,13,"IsobaricHeatCapacity","IsobaricHeatCapacity(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,14,"Cp","Cp(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,15,"SpeedOfSound","SpeedOfSound(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,null,null,null,null,null,null,null,null,"Sample List Box",null,null,null,null,null,null,null,null,16,"Sound","Sound(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,"The list box displays a list of cells.  The cells can be anyplace in the workbook",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,17,"Quality","Quality(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,"It reports the selected item in the cell of your choice",null,null,null,null,null,null,null,null,4,{"$f":"VLOOKUP(K22,S5:U45,3,FALSE)","v":"CompressibilityFactor(FluidName, InpCode, Units, Prop1, Optional Prop2)"},null,null,null,null,null,null,18,"LatentHeat","LatentHeat(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,19,"HeatOfVaporization","HeatOfVaporization(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,"Cell range is T5:T45",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,20,"JouleThompson","JouleThompson(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,"K22 is selected as the \"reporting cell\" (hidden by the list box)",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,21,"IsentropicExpansionCoef","IsentropicExpansionCoef(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,"VLOOKUP uses the reporting cell to point to another cell that has a value of interest",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,22,"IsothermalCompressibility","IsothermalCompressibility(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,23,"VolumeExpansivity","VolumeExpansivity(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,"Cell L22 contains the VLOOKUP function (Excel)",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,24,"AdiabaticCompressibility","AdiabaticCompressibility(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,"VLOOKUP looks for a cell that is associated with the Lookup Value cell",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,25,"AdiabaticBulkModulus","AdiabaticBulkModulus(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,26,"IsothermalExpansionCoef","IsothermalExpansionCoef(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,null,null,"Lookup value",null,"K22",null,null,null,null,null,null,null,null,null,null,null,null,27,"IsothermalBulkModulus","IsothermalBulkModulus(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,null,null,"Table Array",null,"S5:U45",null,null,null,null,null,null,null,null,null,null,null,null,28,"Viscosity","Viscosity(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,null,null,"Column index number",null,3,"The third column of the array has the function data",null,null,null,null,null,null,null,null,null,null,null,29,"ThermalConductivity","ThermalConductivity(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,null,null,"Range Lookup",null,false,"only uses the value in the reference cell",null,null,null,null,null,null,null,null,null,null,null,30,"Prandtl","Prandtl(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,31,"SurfaceTension","SurfaceTension(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,32,"DielectricConstant","DielectricConstant(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,33,"MolarMass","MolarMass(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
["Using these vba functions in another workbook's vba code requires References to be set in the new workbook.",null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,34,"EOSMax","EOSMax(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,35,"EOSMin","EOSMin(FluidName, InpCode, Units, Prop1, Optional Prop2)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,36,"MoleFraction","MoleFraction(FluidName, i)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,37,"MassFraction","MassFraction(FluidName, i)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,38,"LiquidMoleFraction","LiquidMoleFraction(FluidName, Optional InpCode, Optional Units, Optional Prop1, Optional Prop2, Optional i)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,39,"VaporMoleFraction","VaporMoleFraction(FluidName, Optional InpCode, Optional Units, Optional Prop1, Optional Prop2, Optional i)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,40,"Mole2Mass","Mole2Mass(FluidName, i, Prop1, Prop2, Optional Prop3, Optional Prop4, Optional Prop5, Optional Prop6, Optional Prop7, Optional Prop8, Optional Prop9, Optional Prop10, Optional Prop11, Optional Prop12, Optional Prop13, Optional Prop14, Optional Prop15, Optional Prop16, Optional Prop17, Optional Prop18, Optional Prop19, Optional Prop20)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,41,"Mass2Mole","Mass2Mole(FluidName, i, Prop1, Prop2, Optional Prop3, Optional Prop4, Optional Prop5, Optional Prop6, Optional Prop7, Optional Prop8, Optional Prop9, Optional Prop10, Optional Prop11, Optional Prop12, Optional Prop13, Optional Prop14, Optional Prop15, Optional Prop16, Optional Prop17, Optional Prop18, Optional Prop19, Optional Prop20)"]
[]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Arguments:  (FluidName, InpCode, Units, Prop1, Prop2)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"FluidName = text,  fluid must be either in Fluids or Mixtures sub directories."]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"InpCode   = name and order of Prop1 and Prop2."]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"            \"TP\" would mean Prop1 is Temperature, Prop2 is Pressure (need quotes)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"            Valid InpCodes:  TP,TD,TH,TS,TE,TQ,PD,PH,PS,PE,PQ,DH,DS,DE,HS"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"            To define saturated liquid or vapor inputs:  TLIQ, TVAP, PLIQ, PVAP"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"            Other:  Crit, Trip, TMelt, PMelt, TSubl, PSubl"]
[]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"            The word \"Optional\" appears in the argument listings to indicate that"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"            PROP2 is not always required depending on the InpCode argument."]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"            In some cases, PROP1 is also optional."]
[]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Units     = \"SI\", \"SI with C\" (or just \"C\"), \"Molar SI\", \"E\", \"cgs\", \"mks\", \"M\" (need quotes).  \"SI\" is used by default if no input is given. (Unless DefaultUnits changed in VBA code)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Prop1     = numerical value of the first input property (in the units of the previous line)"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Prop2     = numerical value of the second input property (if required)."]

{"sheet":"Sample calcs.","index":5,"n_rows":77,"n_cols":11,"rows_kept":77,"cut":false,"hidden":false,"merged":[]}
["McCabe-Theile  Benzene - Toluene binary system",null,null,null,null,"Define new fluid mixture (in D16 on this worksheet) "]
[null,null,null,null,null,"CONCATENATE(H16,\";\",H17,\";\",G19,\";\",H19,\";\",G20,\";\",H20)"]
[null,null,null,null,null,null,"Refprop fluid name ( I )"]
[null,null,null,null,null,null,"Mole Fraction ( I )"]
[null,null,null,null,null,"Note   \";\"        (semi-colon)"]
[]
[]
[null,null,null,null,null,"VaporMoleFraction(FluidName, InpCode, Units, Prop1, Prop2, i)"]
[]
[null,null,null,null,null,"MoleFraction(FluidName, i)"]
[]
[null,null,null,null,null,"REFPROP values"]
[null,null,null,null,"Pressure >>",20,20,15,15,30,30]
[null,"Benzene","Toluene",null,"Benzene","Benzene","Toluene","Benzene","Toluene","Benzene","Toluene"]
[null,"Liquid Mole Fraction","Liquid Mole Fraction","REFPROP fluid name inputs","Liquid Mole Fraction","Vapor Mole Fraction","Vapor Mole Fraction","Vapor Mole Fraction","Vapor Mole Fraction","Vapor Mole Fraction","Vapor Mole Fraction"]
[null,0,1,{"$f":"CONCATENATE($B$14,\";\",B16,\";\",$C$14,\";\",C16)","v":"Benzene;0;Toluene;1"},0,{"$f":"VaporMoleFraction($D16,\"Pliq\",\"E\",F$13,,1)","v":0},{"$f":"VaporMoleFraction($D16,\"Pliq\",\"E\",G$13,,2)","v":1},0,{"$f":"VaporMoleFraction($D16,\"Pliq\",\"E\",I$13,,2)","v":1},0,{"$f":"VaporMoleFraction($D16,\"Pliq\",\"E\",K$13,,2)","v":1}]
[null,0.05,0.95,"Benzene;0,05;Toluene;0,95",0.05,0.1192698256233114,{"$f":"VaporMoleFraction($D17,\"Pliq\",\"E\",G$13,,2)","v":0.88073017437668855},0.12430942896247059,{"$f":"VaporMoleFraction($D17,\"Pliq\",\"E\",I$13,,2)","v":0.87569057103752945},0.11226431580779565,{"$f":"VaporMoleFraction($D17,\"Pliq\",\"E\",K$13,,2)","v":0.88773568419220439}]
[null,0.1,0.9,"Benzene;0,1;Toluene;0,9",0.1,0.22080627327325353,0.77919372672674658,0.22892065430354169,0.7710793456964582,0.20939553939898883,0.79060446060101119]
[null,0.15,0.85,"Benzene;0,15;Toluene;0,85",0.15,0.30823583313521463,0.69176416686478537,0.31810670529342128,0.68189329470657878,0.29421615986454847,0.70578384013545148]
[null,0.2,0.8,"Benzene;0,2;Toluene;0,8",0.2,0.38435880870624362,0.6156411912937565,0.39509778085387226,0.60490221914612763,0.36897423506638621,0.63102576493361373]
[null,0.25,0.75,"Benzene;0,25;Toluene;0,75",0.25,0.45134793365536735,0.54865206634463271,0.46235443556920741,0.53764556443079259,0.43546176899912908,0.56453823100087097]
[null,0.3,0.7,"Benzene;0,3;Toluene;0,7",0.3,0.51090092532653719,0.48909907467346281,0.52176870018774635,0.47823129981225371,0.49511246265644554,0.5048875373435544]
[null,0.35,0.65,"Benzene;0,35;Toluene;0,65",0.35,0.56435520631368108,0.43564479368631887,0.5748103166128059,0.42518968338719404,0.54907944196613467,0.45092055803386544]
[null,0.4,0.6,"Benzene;0,4;Toluene;0,6",0.4,0.61277352574920763,0.38722647425079232,0.62263287880136298,0.37736712119863691,0.5982959431800039,0.40170405681999621]
[null,0.45,0.55000000000000004,"Benzene;0,45;Toluene;0,55",0.45,0.65700782753727494,0.34299217246272512,0.66615116148699949,0.33384883851300046,0.6435223172867599,0.35647768271323999]
[null,0.5,0.5,"Benzene;0,5;Toluene;0,5",0.5,{"$f":"VaporMoleFraction($D26,\"Pliq\",\"E\",F$13,,1)","v":0.69774705212732147},0.30225294787267859,0.70609783371125079,0.29390216628874916,0.68538235784733192,0.31461764215266802]
[null,0.55000000000000004,0.45,"Benzene;0,55;Toluene;0,45",0.55000000000000004,0.73555311226342956,0.26444688773657038,0.7430653944876785,0.25693460551232156,0.72439141207568269,0.27560858792431725]
[null,0.6,0.4,"Benzene;0,6;Toluene;0,4",0.6,0.77088813542055257,0.22911186457944743,0.77753747157981634,0.22246252842018366,0.76097820397943161,0.23902179602056833]
[null,0.65,0.35,"Benzene;0,65;Toluene;0,35",0.65,0.80413534632705685,0.19586465367294315,0.80991231262324948,0.19008768737675052,0.79550185893483061,0.20449814106516928]
[null,0.7,0.3,"Benzene;0,7;Toluene;0,3",0.7,0.83561494128439517,0.16438505871560477,0.84052081482567642,0.15947918517432363,0.82826524081920128,0.17173475918079867]
[null,0.75,0.25,"Benzene;0,75;Toluene;0,25",0.75,0.86559659725741211,0.13440340274258789,0.86964010898333277,0.13035989101666715,0.85952547924408629,0.14047452075591368]
[null,0.8,0.2,"Benzene;0,8;Toluene;0,2",0.8,0.89430913365485198,0.10569086634514795,0.89750426524655535,0.10249573475344466,0.88950231330856788,0.11049768669143217]
[null,0.85,0.15,"Benzene;0,85;Toluene;0,15",0.85,0.92194813554076882,7.8051864459231263E-2,0.92431253288000237,7.568746711999759E-2,0.91838474707818663,8.1615252921813375E-2]
[null,0.9,0.1,"Benzene;0,9;Toluene;0,1",0.9,0.94868200202362751,5.1317997976372348E-2,0.9502358672637784,4.9764132736221732E-2,0.94633640897476201,5.3663591025237989E-2]
[null,0.95,0.05,"Benzene;0,95;Toluene;0,05",0.95,0.97465677439205811,2.5343225607941777E-2,0.97542208801144104,2.4577911988559041E-2,0.97349983354025882,2.6500166459741206E-2]
[null,1,0,"Benzene;1;Toluene;0",1,1,0,1,0,1,0]
[]
[]
[]
[]
[null,null,null,null,"Determine the accuracy of the Mcad data to REFPROP"]
[]
[]
[null,null,null,null,"Pressure =",20]
[null,null,null,null,null,null,null,"Percent Error"]
[null,null,null,null,"Liquid Mole Fraction","REFPROP Benzene Vapor Mole Fraction","Mcad Benzene Vapor Mole FR. Curve","(Mcad - Refprop)    Refprop"]
[null,null,null,null,0,0,{"$f":"$F$70+$F$71*E47+$F$72*E47^2+$F$73*E47^3+$F$74*E47^4+$F$75*E47^5+$F$76*E47^6+$F$77*E47^7","v":7.5918815000000003E-6}]
[null,null,null,null,0.05,0.11926982562426808,0.1192496288462675,{"$f":"(G48-F48)/F48*100","v":-1.693368619839019E-2}]
[null,null,null,null,0.1,0.22080627327097127,0.22081074167363501,{"$f":"(G49-F49)/F49*100","v":2.0236755946963403E-3}]
[null,null,null,null,0.15,0.30823583313303343,0.30825131742087775,5.0235197144100482E-3]
[null,null,null,null,0.2,0.38435880870645456,0.38436618040438009,1.917920900613185E-3]
[null,null,null,null,0.25,0.45134793365718678,0.45134192342141705,-1.331619205839274E-3]
[null,null,null,null,0.3,0.51090092531768994,0.51088828634094519,-2.4738606094500005E-3]
[null,null,null,null,0.35,0.56435520631916103,0.56434605245227987,-1.6220045068539911E-3]
[null,null,null,null,0.4,0.61277352575345334,0.61277393296053995,6.6453113506330808E-5]
[null,null,null,null,0.45,0.65700782753172948,0.65701691001773532,1.3824014913127718E-3]
[null,null,null,null,0.5,0.69774705213458843,0.69775850867837519,1.6419336709069738E-3]
[null,null,null,null,0.55000000000000004,0.73555311226370002,0.73555946816847806,8.640986860191654E-4]
[null,null,null,null,0.6,0.77088813541248646,0.77088528285686009,-3.7003496296509096E-4]
[null,null,null,null,0.65,0.8041353463203802,0.80412508331757748,-1.2762780357405057E-3]
[null,null,null,null,0.7,0.83561494128607683,0.83560432787240513,-1.2701321083806593E-3]
[null,null,null,null,0.75,0.86559659725947713,0.86559377500222723,-3.260476368364771E-4]
[null,null,null,null,0.8,0.89430913365473186,0.89431720701622008,9.0274841041067515E-4]
[null,null,null,null,0.85,0.92194813554041244,0.92196037536769826,1.3276047549731053E-3]
[null,null,null,null,0.9,0.94868200202345887,0.94868363800551458,1.7244788582738429E-4]
[null,null,null,null,0.95,0.97465677439233167,0.97464075914988224,-1.6431674072562377E-3]
[null,null,null,null,1,1,1.0000063418814997,6.3418814997273643E-4]
[]
[null,null,null,null,"Coefficients"]
[null,null,null,null,"a",7.5918815000000003E-6]
[null,null,null,null,"b",2.5899366000000001]
[null,null,null,null,"c",-4.4191336999999997]
[null,null,null,null,"d",6.7166641]
[null,null,null,null,"e",-7.7493600000000002]
[null,null,null,null,"f",6.2001622999999997]
[null,null,null,null,"g",-2.9656709000000001]
[null,null,null,null,"h",0.62740035000000005]

{"sheet":"Check Sheet","index":6,"n_rows":30,"n_cols":5,"rows_kept":30,"cut":false,"hidden":false,"merged":[]}
["This worksheet can be used to verify that the user's computer is returning proper calculations"]
["The values in the columns on the left are calculated from your copy of the Refprop DLL."]
["The values in the middle column were calculated at NIST."]
["The values in the right column show the differences, and should all be zero (or very near zero)"]
["If the \"Total sum of errors\" below is not (nearly) zero, please check carefully to determine the source of the problem(s)."]
[]
[null,"Total Sum of Errors:",{"$f":"SUM(C10:C30)","v":{"$error":"#VALUE!"}},null,"To recalculate, press Ctrl-Alt-F9 (or Ctrl-Alt-Shift-F9 for some users)"]
[]
["From DLL","From NIST","Difference"]
[{"$f":"MolarMass(\"Air\")","v":28.958600656000002},28.958600656000002,{"$f":"ABS(A10-B10)","v":0}]
[{"$f":"Temperature(\"argon\",\"PD\",\"SI\",2,15)","v":637.37758865785702},637.37758865785702,{"$f":"ABS(A11-B11)","v":0}]
[{"$f":"Pressure(\"r134a\",\"TD\",\"SI\",400,50)","v":1.4569189278973724},1.4569189278973724,0]
[{"$f":"Enthalpy(\"ethylene\",\"TS\",\"SI\",300,3)","v":651.51370313035648},651.51370313035648,0]
[{"$f":"viscosity(\"oxygen\",\"TP\",\"SI\",100,1)","v":153.88668066375217},153.88668066375217,0]
[{"$f":"ThermalConductivity(\"nitrogen\",\"Tliq\",\"SI\",100)","v":100.11174896483813},100.11174896483813,0]
[{"$f":"Density(\"air\",\"TP\",\"E\",70,14.7)","v":7.4915638466684184E-2},7.4915638466684184E-2,0]
[{"$f":"Enthalpy(\"R32;0.3;R125;0.7\",\"PS\",\"molar si\",10,110)","v":{"$error":"#VALUE!"}},23643.993567366797,{"$error":"#VALUE!"}]
[{"$f":"Temperature(\"ethane;0.5;butane;0.5 mass\",\"DH\",\"E\",30,283)","v":{"$error":"#VALUE!"}},298.43132031104824,{"$error":"#VALUE!"}]
[{"$f":"SpeedOfSound(\"ammonia;0.4;water;0.6\",\"TP\",\"E\",300,10000)","v":{"$error":"#VALUE!"}},5536.7914493159169,{"$error":"#VALUE!"}]
[{"$f":"Density(\"r218;.1;r123;.9\",\"PH\",\"cgs\",7,180)","v":{"$error":"#VALUE!"}},1.60040403481075,{"$error":"#VALUE!"}]
[{"$f":"Quality(\"methane;40;ethane;60 mass\",\"TD\",\"mks\",200,300)","v":5.0092690346257185E-2},5.0092690346257185E-2,0,null,"(note:  quality is returned on a molar basis, not mass basis)"]
[{"$f":"heatofvaporization(\"octane\",\"tliq\",\"c\",100)","v":319.16749987056795},319.16749987056795,0]
[{"$f":"SurfaceTension(\"nitrogen\",\"tl\",,100)","v":4.0504202917983196},4.0504202917983196,0]
[{"$f":"viscosity(\"butane;.25;hexane;.75\",\"TH\",,300,-21)","v":{"$error":"#VALUE!"}},283.7248366681759,{"$error":"#VALUE!"}]
[{"$f":"ThermalConductivity(\"carbon dioxide,.5,nitrogen,.5 mass\",\"TH\",\"SI\",200,126)","v":{"$error":"#VALUE!"}},101.79478262055925,{"$error":"#VALUE!"}]
[{"$f":"dielectricconstant(\"ethane;.5;propane;.5\",\"tvap\",,300)","v":{"$error":"#VALUE!"}},1.0370580639065157,{"$error":"#VALUE!"}]
[{"$f":"MoleFraction(\"R410A.MIX\",1)","v":0.69761469937586296},0.69761469937586296,0]
[{"$f":"mole2mass(\"R410A.MIX\",1,A27,1-A27)","v":0.50000000000000067},0.50000000000000067,0]
[{"$f":"mass2mole(\"R410A.MIX\",1,0.5,0.5)","v":0.69761469937586251},0.69761469937586251,0]
[{"$f":"LiquidDensity(\"methane;.7;ethane;.2;propane;.05;butane;.05\",\"TD\",,150,200)","v":{"$error":"#VALUE!"}},481.27615729800686,{"$error":"#VALUE!"}]