Vapor Pressure of a Liquid Solution

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Vapor Pressure of a Liquid Solution created by Christopher Haslego, author of the Chemical Engineers' Resource Page (http://www.cheres Instructions for this spreadsheet: This spreadsheet will t ake the following inputs: Temperature Liquid Composition of one component Critical Temperatures and Pressures Molar Volumes Simply input the data into the yellow cells and click on the "Solve Spreadsheet" button.** The vapor pressure of the two liquid solution will appear at the top of the sheet. The true vapor pressure of each component (also called fugacity) in labeled f 0 The error associated with this method is +/- 1.00% **The spreads he et doe s not hav e t o sol ved to ge t the vapor pressure of th e sol ut io n, onl y t o get the co This value only influenced the activity coefficients and has no bearing on t he vapor pressure of the solu ie. If y ou don 't n eed the act ivi ty coe ffici ent s or th e compressibl ity fact or, don 't b other s olv ing the spr ead your inputs

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Vapor Pressure of a Liquid Solutioncreated by Christopher Haslego, author of the Chemical Engineers' Resource Page (http://www.cheres

Instructions for this spreadsheet:

This spreadsheet will take the following inputs: Temperature

Liquid Composition of one component

Critical Temperatures and Pressures

Molar Volumes

Simply input the data into the yellow cells and click on the "Solve Spreadsheet" button.**

The vapor pressure of the two liquid solution will appear at the top of the sheet.

The true vapor pressure of each component (also called fugacity) in labeled f 0

The error associated with this method is +/- 1.00%

**The spreadsheet does not have to solved to get the vapor pressure of the solution, only to get the co

This value only influenced the activity coefficients and has no bearing on the vapor pressure of the solu

ie. If you don't need the activity coefficients or the compressiblity factor, don't bother solving the spreadyour inputs

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urces.com)

pressibility factor.

ion.

sheet, just change

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Vapor Pressure of a Liquid SolutionCreated by Christopher Haslego, author of the Chemical Engineers' Resource Page (http://www.cheresources.com)

Chemical 1= Water  Vapor PressChemical 2= MEG

<--enter data at yellow cells

T (0C)

Mole Fraction of

Chemical 1 in Liquid

Mole Fraction of

Chemical 1 in Vapor 

Mole Fraction of

Chemical 2 in Liquid

Mole Fraction of

Chemical 2 in Vapor 

100 0.5 0.979195199 0.500 0.021

C1 (kPa-1/2

) C2 (kPa-1/2

) D1 (kPa-1

) D2 (kPa-1

)

0.003333 0.004943 0.00000099 0.00000259

-FP(1+FP) (E P)(FP) Compressibility Actvity Coeff. 1 Actvity Coeff. 2

0.001044846 0.000000119 0.9990 0.998975 0.998039

Constants: 

Critical Pressure of Substance 1 in kPa =

0.0000 Critical Pressure of Substance 2 in kPa =

Critical Temp of Substance 1 in Celsius=

Critical Temp of Substance 2 in Celsius=

Molar Volume of Substance 1 (m3/mol)=

Molar Volume of Substance 2 (m3/mol)=

Pressure of Distillation Process (kPa)=

 Antoine Equation ConstantsChemical 1

 A= 7.96681

B= 1668.210

C= 228.000

Solve Spreadsheet

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re of Solut ion=  51.7005 kPa 

vapor pressure of each comp Reduced Temperatures

Pv1 (kPa) Pv2 (kPa) Tr1 (0C) Tr2 (

0C)

50.661 1.076 0.576 0.648

E (kPa-1

) F (kPa-1

)

0.0033665 0.0000010

f 01 (kPa) f  02 (kPa)

50.6243 1.0762

22129.38

7520

374.15

303

0.000018

0.00005558

101.325

Chemical 2

8.091

2088.900

203.500

correct or "real"values..also called

fugacity.

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**Note that only chemicals marked "Eq 1" are for use on the spreadsheet.

Water 1 0-60 8.10765 1750.286 235

1 60-150 7.96681 1668.21 228

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