Introduction to Chemical Engineering Thermodynamics
Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN: 9781259696527
Author: J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher: McGraw-Hill Education
Question
Book Icon
Chapter 1, Problem 1.2P
Interpretation Introduction

Interpretation:

The relation between the parameters of Antoine equation which is written in two different forms should be determined.

Expert Solution & Answer
Check Mark

Answer to Problem 1.2P

The relation between the parameters of Antoine equation which is written in two different forms is:

A = 2.303a
B = 2.303b
C = c-273.15

And, log10psat/kpa=10.88log10psat/torr     

Explanation of Solution

Given information:

Antoine equation can be expressed in following two forms-

log10Psat/torr=ab[t/°C+c] ......... (1)

And
lnPsat/kPa=AB[t/K+C] .......... (2)

Where Psat − Liquid/vapor saturation pressure

And a, b, c, A, B, C are substance specific constants

  • Antoine Equation relates the Vapor pressure of the substance to the temperature.
  • The given two forms of equation differ in terms of units of pressure and temperature. Hence to find the relation b/w a, b, c and A, B, C, we must convert the equation1 so that it has the same unit as that of equation 2.

Calculation:

We have equation 1 as-

  log10Psat/torr=ab[t/°C+c] ......... (1)

  • Consider Left hand side of equation (1)- First convert log10into ln by multiplying equation (1) by 2.303:
  •   2.303log10Psat/torr=lnPsat/torr

  • Now convert the unit of Pressure from torr to KPa:

1 torr = 133.32 Pa = 133.32×103KPa

  2.303log10Psat/torr=lnPsat/torr                                 = ln Psat/(torr×133.32× 10 3 KPa1 torr)                                 = ln Psat/133.32×103 KPa   

Therefore,

  2.303log10Psat/torr= ln Psat/133.32×103 KPa                                   = ln (7.50 Psat)/KPa 

Now we know that, ln(ab)=lna+lnb

Thus,

   ln (7.50 Psat/KPa)=ln(7.50)+ln(Psat/KPa)                                = 0.88+ln(Psat/KPa)                

Finally,

  2.303log10Psat/torr=0.88+lnPsat/KPalog10Psat/torr=12.303(0.88+lnPsat/KPa)        ...... (3)

  • Now consider the right hand side of the equation (1) and convert the temperature into Kelvin(K)

  (T273.15)/K=t/°C

  ab[t/°C+c]=ab[(T273.15)/K+c]                     =ab[T/K+c273.15]            ......(4)

Thus, putting equation (3) and (4) in equation (1), we get

  12.303(0.88+lnPsat/KPa)=ab[T/K+c273.15]          (0.88+lnPsat/KPa)=2.303(ab[T/K+c273.15])                                  =2.303a2.303b[T/K+c273.15]        ......(5)

Hence, by comparing equation (2) and equation (5), we can relate a, b, c and A,B,C as:

A = 2.303a
B = 2.303b
C = c-273.15

And, log10psat/kpa=10.88log10psat/torr     

Conclusion

The relation between the parameters of Antoine equation which is written in two different forms is:

A = 2.303a
B = 2.303b
C = c-273.15

And, log10psat/kpa=10.88log10psat/torr     

Want to see more full solutions like this?

Subscribe now to access step-by-step solutions to millions of textbook problems written by subject matter experts!
Students have asked these similar questions
give me solution math not explin
Example (6): An evaporator is concentrating F kg/h at 311K of a 20wt% solution of NaOH to 50wt %. The saturated steam used for heating is at 399.3K. The pressure in the vapor space of the evaporator is 13.3 KPa abs. The 5:48 O Transcribed Image Text: Example (7): Determine the
14.9. A forward feed double-effect vertical evaporator, with equal heating areas in each effect, is fed with 5 kg/s of a liquor of specific heat capacity of 4.18 kJ/kg K. and with no boiling point rise, so that 50 per cent of the feed liquor is evaporated. The overall heat transfer coefficient in the second effect is 75 per cent of that in the first effect. Steam is fed at 395 K and the boiling point in the second effect is 373 K. The feed is heated by an external heater to the boiling point in the first effect. It is decided to bleed off 0.25 kg/s of vapour from the vapour line to the second effect for use in another process. If the feed is still heated to the boiling point of the first effect by external means, what will be the change in steam consumption of the evaporator unit? For the purpose of calculation, the latent heat of the vapours and of the steam may both be taken as 2230 kJ/kg
Knowledge Booster
Background pattern image
Similar questions
SEE MORE QUESTIONS
Recommended textbooks for you
Text book image
Introduction to Chemical Engineering Thermodynami...
Chemical Engineering
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:McGraw-Hill Education
Text book image
Elementary Principles of Chemical Processes, Bind...
Chemical Engineering
ISBN:9781118431221
Author:Richard M. Felder, Ronald W. Rousseau, Lisa G. Bullard
Publisher:WILEY
Text book image
Elements of Chemical Reaction Engineering (5th Ed...
Chemical Engineering
ISBN:9780133887518
Author:H. Scott Fogler
Publisher:Prentice Hall
Text book image
Process Dynamics and Control, 4e
Chemical Engineering
ISBN:9781119285915
Author:Seborg
Publisher:WILEY
Text book image
Industrial Plastics: Theory and Applications
Chemical Engineering
ISBN:9781285061238
Author:Lokensgard, Erik
Publisher:Delmar Cengage Learning
Text book image
Unit Operations of Chemical Engineering
Chemical Engineering
ISBN:9780072848236
Author:Warren McCabe, Julian C. Smith, Peter Harriott
Publisher:McGraw-Hill Companies, The