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Calculation Performed at www.codecalculation.com

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Project

Project No:
Project Title:
Document No:
Revision No:
Date :
     

Inputs

Pressure [[ gUL('pressure') ]]

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Temperature [[ gUL('temperature') ]]

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Mixture

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Component Formula Mol.Wt. Mol.Fraction
Air -- 28.966

[[err]]

Oxygen O2 32.000

[[err]]

Nitrogen N2 28.016

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Water Vapor H2O 18.016

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Carbon Monoxide CO 28.010

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Carbon Dioxide CO2 44.010

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Hydrogen Sulfide H2S 34.076

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Hydrogen H2 2.016

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Methane CH4 16.042

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Ethene C2H4 28.052

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Ethane C2H6 30.068

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Propene C3H6 42.078

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n-Propane C3H8 44.094

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i-Butane C4H10 58.120

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n-Butane C4H10 58.120

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i-Pentane C5H12 72.146

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n-Pentane C5H12 72.146

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Hexane+ C6H14 86.000

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Errors

[[ err ]]

Results

MW [[ retSilent(doc, ['result', 'MW', '_val']) ]] [[ gUL('molecularMass') ]]
Critical Pressure [[ retSilent(doc, ['result', 'Pcritical', '_val']) ]] [[ gUL('pressure') ]]
Critical Temperature [[ retSilent(doc, ['result', 'Tcritical', '_val']) ]] [[ gUL('temperature') ]]
Reduced Pressure [[ retSilent(doc, ['result', 'Pr', '_val']) ]]
Reduced Temperature [[ retSilent(doc, ['result', 'Tr', '_val']) ]]
Acentric Factor [[ retSilent(doc, ['result', 'acentric', '_val']) ]]
Z (Peng-Robinson) [[ retSilent(doc, ['result', 'Z_PR', '_val']) ]]
Z (Lee-Kesler) [[ retSilent(doc, ['result', 'Z_LKP', '_val']) ]]
Z (Nelson Obert) [[ retSilent(doc, ['result', 'Z_NO', '_val']) ]]
Cp0 [[ retSilent(doc, ['result', 'Cp0mass', '_val']) ]] [[ gUL('specificHeat') ]]
Cv0 [[ retSilent(doc, ['result', 'Cv0mass', '_val']) ]] [[ gUL('specificHeat') ]]
Cp0 Molar [[ retSilent(doc, ['result', 'Cp0molar', '_val']) ]] [[ gUL('specificHeatMolar') ]]
Cv0 Molar [[ retSilent(doc, ['result', 'Cv0molar', '_val']) ]] [[ gUL('specificHeatMolar') ]]