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
bartleby

Videos

Question
Book Icon
Chapter 13, Problem 13.1P

(a)

Interpretation Introduction

Interpretation:

The mole fraction of benzene in vapour phase, y1and constant total pressure, P at temperature 100°C is to be calculated.

Concept introduction:

Raoult’s Law states that the partial pressure of liquid A above the solution is equal to the mole fraction of the liquid in a solution times the partial pressure of the pure liquid. This holds for ideal solutions. An ideal solution is approached by binary solutions of molecules that have similar properties (e.g. benzene and toluene). The law is mathematically expressed as-

  pA*=xAPAv

Where

  PAv = vapor pressure of A at the given temperature

  xA = mole fraction of the solute A in the liquid

  pA* = equilibrium partial pressure exerted by the solute.

A solution behaves ideally when

  1. The solute and the solvent molecules have similar sizes and similar intermolecular forces,
  2. The excess volume of mixing is zero, and
  3. The heat of mixing is zero when both the solute and the solvent are liquids

(a)

Expert Solution
Check Mark

Answer to Problem 13.1P

(a) y1=0.545059 and P=818.6900256 mm Hg at T=100°C

Explanation of Solution

The Raoult’s law expression for two components A and B to give the equilibrium partial pressure of the components in a binary mixture is written as follows-

pA*=xAPAv

and

pB*=(1xA)PBv

The total pressure: P=pA*+pB*=xAPAv+(1xA)PBv

Where

xA = mole fraction of A in liquid phase in the binary solution

xB = (1xA) = mole fraction of B in liquid phase in the binary solution

  PAv = vapor pressure of A at the given temperature

  PBv = vapor pressure of B at the given temperature

  pA* =equilibrium partial pressure of component A

  pB* = equilibrium partial pressure of component B

The mole fraction of A in the vapor phase is given by -     yA=pA*P=xAPAvP

Similarly, mole fraction of B in vapor phase is given by -     yB=pB*P=xBPBvP

Now vapor pressures PAv and PBv are calculated by using the Antoine equation:

lnPBv or lnPAv=A'B'C'+θ;

PAv and PBv in mm Hg, θ in °C

A', B', C' are constants

Now, For benzene (1) A' =15.9037, B' =2789.01, C' =220.79

And For toluene (2) A' =16.00531, B' =3090.78, C' =219.14

Given x1=0.33 and T=100°C, find y1 and P

Now vapor pressure for benzene (1) can be calculated using Antoine equation as follows: -

  lnP1v=A'B'C'+θ

  lnP1v=15.90372789.01220.79+100

  lnP1v=7.209507

P1v=1352.226183 mm Hg at T=100°C

Now vapor pressure for toluene (2) can be calculated using Antoine equation as follows:

  lnP2v=A'B'C'+θ

  lnP2v=16.005313090.78219.14+100

  lnP2v=6.320594

P2v=555.90356 mm Hg at T=100°C

Using formula P=pA*+pB*=xAPAv+(1xA)PBv we find total pressure P

  P=p1*+p2*=x1P1v+(1x1)P2v

  P=0.33×1352.226183+(10.33)×555.90356

  P=446.2346404+372.4553852

P=818.6900256 mm Hg at T=100°C

Using the formula yA=pA*P=xAPAvP

we find mole fraction of benzene (1) in vapor phase, Introduction to Chemical Engineering Thermodynamics, Chapter 13, Problem 13.1P , additional homework tip  1

  y1=p1*P=x1P1vP=0.33×1352.226183818.6900256=0.545059

Therefore, y1=0.545059 and P=818.6900256 mm Hg at T=100°C

(b)

Interpretation Introduction

Interpretation:

The mole fraction of benzene in liquid phase, x1and constant total pressure, P at temperature 100°C is to be calculated.

Concept introduction:

Raoult’s Law states that the partial pressure of liquid A above the solution is equal to the mole fraction of the liquid in a solution times the partial pressure of the pure liquid. This holds for ideal solutions. An ideal solution is approached by binary solutions of molecules that have similar properties (e.g. benzene and toluene). The law is mathematically expressed as-

  pA*=xAPAv

Where

  PAv = vapor pressure of A at the given temperature

  xA = mole fraction of the solute A in the liquid

  pA* = equilibrium partial pressure exerted by the solute.

A solution behaves ideally when

  1. The solute and the solvent molecules have similar sizes and similar intermolecular forces,
  2. The excess volume of mixing is zero, and
  3. The heat of mixing is zero when both the solute and the solvent are liquids

(b)

Expert Solution
Check Mark

Answer to Problem 13.1P

x1=0.16838 and P=689.9883186 mm Hg at T=100°C

Explanation of Solution

The Raoult’s law expression for two components A and B to give the equilibrium partial pressure of the components in a binary mixture is written as follows-

pA*=xAPAv

and

pB*=(1xA)PBv

The total pressure: P=pA*+pB*=xAPAv+(1xA)PBv

Where

xA = mole fraction of A in liquid phase in the binary solution

xB = (1xA) = mole fraction of B in liquid phase in the binary solution

PAv = vapor pressure of A at the given temperature

PBv = vapor pressure of B at the given temperature

pA* =equilibrium partial pressure of component A

pB* = equilibrium partial pressure of component B

The mole fraction of A in the vapor phase is given by -

yA=pA*P=xAPAvP

Similarly, mole fraction of B in vapor phase is given by -     yB=pB*P=xBPBvP

Now vapor pressures PAv and PBv are calculated by using the Antoine equation:

lnPBv or lnPAv=A'B'C'+θ;

PAv and PBv in mm Hg, θ in °C

A', B', C' are constants

Now, For benzene (1) A' =15.9037, B' =2789.01, C' =220.79

And For toluene (2) A' =16.00531, B' =3090.78, C' =219.14

Given y1=0.33 and T=100°C, find x1 and P

Now vapor pressure for benzene (1) can be calculated using Antoine equation as follows: -

  lnP1v=A'B'C'+θ

  lnP1v=15.90372789.01220.79+100

  lnP1v=7.209507

P1v=1352.226183 mm Hg at T=100°C

Now vapor pressure for toluene (2) can be calculated using Antoine equation as follows:

  lnP2v=A'B'C'+θ

  lnP2v=16.005313090.78219.14+100

  lnP2v=6.320594

P2v=555.90356 mm Hg at T=100°C

Using the formula yA*=pA*P=xAPAvP and P=pA*+pB*=xAPAv+(1xA)PBv

we find mole fraction of benzene (1) in liquid phase, Introduction to Chemical Engineering Thermodynamics, Chapter 13, Problem 13.1P , additional homework tip  2

  y1=x1P1vP=x1P1vx1P1v+(1x1)P2v=x1×1352.226183x1×1352.226183+(1x1)×555.903560.33=x1×1352.226183x1×1352.226183+(1x1)×555.903560.33×x1×1352.226183+0.33×(1x1)×555.90356=x1×1352.2261830.33×555.90356=1352.226183×x1446.2346404×x1+0.33×555.90356×x1183.4481748=1089.439717×x1x1=0.16838

Using formula P=pA*+pB*=xAPAv+(1xA)PBv we find total pressure P

  P=p1*+p2*=x1P1v+(1x1)P2v

  P=0.16838×1352.226183+(10.16838)×555.90356

  P=227.6878+462.3005

P=689.9883186 mm Hg at T=100°C

Therefore, x1=0.16838 and P=689.9883186 mm Hg at T=100°C

(c)

Interpretation Introduction

Interpretation:

The mole fraction of benzene in vapor phase, y1and temperature of the solution, T at total pressure P =120 kPa is to be calculated.

Concept introduction:

Raoult’s Law states that the partial pressure of liquid A above the solution is equal to the mole fraction of the liquid in a solution times the partial pressure of the pure liquid. This holds for ideal solutions. An ideal solution is approached by binary solutions of molecules that have similar properties (e.g. benzene and toluene). The law is mathematically expressed as-

  pA*=xAPAv

Where

  PAv = vapor pressure of A at the given temperature

  xA = mole fraction of the solute A in the liquid

  pA* = equilibrium partial pressure exerted by the solute.

A solution behaves ideally when

  1. The solute and the solvent molecules have similar sizes and similar intermolecular forces,
  2. The excess volume of mixing is zero, and
  3. The heat of mixing is zero when both the solute and the solvent are liquids

(c)

Expert Solution
Check Mark

Answer to Problem 13.1P

y1=0.542392 and T=103.35043°C at P=120

  kPa

Explanation of Solution

The Raoult’s law expression for two components A and B to give the equilibrium partial pressure of the components in a binary mixture is written as follows-

pA*=xAPAv

and

pB*=(1xA)PBv

The total pressure: P=pA*+pB*=xAPAv+(1xA)PBv

Where

xA = mole fraction of A in liquid phase in the binary solution

xB = (1xA) = mole fraction of B in liquid phase in the binary solution

  PAv = vapor pressure of A at the given temperature

  PBv = vapor pressure of B at the given temperature

  pA* =equilibrium partial pressure of component A

  pB* = equilibrium partial pressure of component B

The mole fraction of A in the vapor phase is given by -     yA=pA*P=xAPAvP

Similarly, mole fraction of B in vapor phase is given by -     yB=pB*P=xBPBvP

Now vapor pressures PAv and PBv are calculated by using the Antoine equation:

lnPBv or lnPAv=A'B'C'+θ;

PAv and PBv in mm Hg, θ in °C

A', B', C' are constants

Now, For benzene (1) A' =15.9037, B' =2789.01, C' =220.79

And For toluene (2) A' =16.00531, B' =3090.78, C' =219.14

Given x1=0.33 and P=120kPa, find y1 and T

Now, P=120

kPa=900.07404 mm Hg (as 1 kPa=7.500617 mm Hg)

Using formula P=pA*+pB*=xAPAv+(1xA)PBv we write an equation in θ

  900.07404=0.33×e15.90372789.01220.79+θ+(10.33)×e16.005313090.78219.14+θ

Solving this equation, we find θ=103.35043°C

Now vapor pressure for benzene (1) can be calculated using Antoine equation as follows: -

  lnP1v=A'B'C'+θ

  lnP1v=15.90372789.01220.79+103.35043

  lnP1v=7.299373

P1v=1479.373228 mm Hg at T=103.35043°C

Now vapor pressure for toluene (2) can be calculated using Antoine equation as follows:

  lnP2v=A'B'C'+θ

  lnP2v=16.005313090.78219.14+103.35043

  lnP2v=6.421211

P2v=614.74751 mm Hg at T=103.35043°C

Using the formula yA=pA*P=xAPAvP

we find mole fraction of benzene (1) in vapor phase, Introduction to Chemical Engineering Thermodynamics, Chapter 13, Problem 13.1P , additional homework tip  3

  y1=p1*P=x1P1vP=0.33×1479.373228900.07404=0.542392

Therefore, y1=0.542392 and T=103.35043°C at P=120

  kPa

(d)

Interpretation Introduction

Interpretation:

The mole fraction of benzene in liquid phase, x1and temperature of the solution, T at total pressure P =120 kPa is to be calculated.

Concept introduction:

Raoult’s Law states that the partial pressure of liquid A above the solution is equal to the mole fraction of the liquid in a solution times the partial pressure of the pure liquid. This holds for ideal solutions. An ideal solution is approached by binary solutions of molecules that have similar properties (e.g. benzene and toluene). The law is mathematically expressed as-

  pA*=xAPAv

Where

  PAv = vapor pressure of A at the given temperature

  xA = mole fraction of the solute A in the liquid

  pA* = equilibrium partial pressure exerted by the solute.

A solution behaves ideally when

  1. The solute and the solvent molecules have similar sizes and similar intermolecular forces,
  2. The excess volume of mixing is zero, and
  3. The heat of mixing is zero when both the solute and the solvent are liquids

(d)

Expert Solution
Check Mark

Answer to Problem 13.1P

x1=0.17247 and T=109.17784°C at P=120

  kPa

Explanation of Solution

The Raoult’s law expression for two components A and B to give the equilibrium partial pressure of the components in a binary mixture is written as follows-

pA*=xAPAv

and

pB*=(1xA)PBv

The total pressure: P=pA*+pB*=xAPAv+(1xA)PBv

Where

xA = mole fraction of A in liquid phase in the binary solution

xB = (1xA) = mole fraction of B in liquid phase in the binary solution

  PAv = vapor pressure of A at the given temperature

  PBv = vapor pressure of B at the given temperature

  pA* =equilibrium partial pressure of component A

  pB* = equilibrium partial pressure of component B

The mole fraction of A in the vapor phase is given by -     yA=pA*P=xAPAvP

Similarly, mole fraction of B in vapor phase is given by -     yB=pB*P=xBPBvP

Now vapor pressures PAv and PBv are calculated by using the Antoine equation:

lnPBv or lnPAv=A'B'C'+θ;

PAv and PBv in mm Hg, θ in °C

A', B', C' are constants

Now, For benzene (1) A' =15.9037, B' =2789.01, C' =220.79

And For toluene (2) A' =16.00531, B' =3090.78, C' =219.14

Given y1=0.33 and P=120kPa, find x1 and T

Now, P=120

kPa=900.07404 mm Hg (as 1 kPa=7.500617 mm Hg) Using the formula yA=pA*P=xAPAvP we find mole fraction of benzene (1) in liquid phase, x1

  y1=p1*P=x1P1vP0.33=x1×e15.9037 2789.01 220.79+θ900.07404297.02443=x1×e15.90372789.01220.79+θ

  y2=p1*P=x1P1vP0.67=(1x1)×P2v900.07404603.0496=(1x1)×e16.005313090.78219.14+θ

Solving these two equations, we find θ=109.17784°C and x1=0.17247

Therefore, x1=0.17247 and T=109.17784°C at P=120

  kPa

(e)

Interpretation Introduction

Interpretation:

The mole fraction of benzene in liquid phase, x1and mole fraction of benzene in vapour phase, y1at total pressure P =120 kPa and temperature T=105 °C is to be calculated.

Concept introduction:

Raoult’s Law states that the partial pressure of liquid A above the solution is equal to the mole fraction of the liquid in a solution times the partial pressure of the pure liquid. This holds for ideal solutions. An ideal solution is approached by binary solutions of molecules that have similar properties (e.g. benzene and toluene). The law is mathematically expressed as-

  pA*=xAPAv

Where

  PAv = vapor pressure of A at the given temperature

  xA = mole fraction of the solute A in the liquid

  pA* = equilibrium partial pressure exerted by the solute.

A solution behaves ideally when

  1. The solute and the solvent molecules have similar sizes and similar intermolecular forces,
  2. The excess volume of mixing is zero, and
  3. The heat of mixing is zero when both the solute and the solvent are liquids

(e)

Expert Solution
Check Mark

Answer to Problem 13.1P

x1=0.28296, y1=0.485786 and T=105°C at P=120

  kPa

Explanation of Solution

The Raoult’s law expression for two components A and B to give the equilibrium partial pressure of the components in a binary mixture is written as follows-

pA*=xAPAv

and

pB*=(1xA)PBv

The total pressure: P=pA*+pB*=xAPAv+(1xA)PBv

Where

xA = mole fraction of A in liquid phase in the binary solution

xB = (1xA) = mole fraction of B in liquid phase in the binary solution

  PAv = vapor pressure of A at the given temperature

  PBv = vapor pressure of B at the given temperature

  pA* =equilibrium partial pressure of component A

  pB* = equilibrium partial pressure of component B

The mole fraction of A in the vapor phase is given by -     yA=pA*P=xAPAvP

Similarly, mole fraction of B in vapor phase is given by -     yB=pB*P=xBPBvP

Now vapor pressures PAv and PBv are calculated by using the Antoine equation:

lnPBv or lnPAv=A'B'C'+θ;

PAv and PBv in mm Hg, θ in °C

A', B', C' are constants

Now, For benzene (1) A' =15.9037, B' =2789.01, C' =220.79

And For toluene (2) A' =16.00531, B' =3090.78, C' =219.14

Given T=105°C and P=120kPa, find x1 and y1

Now, P=120

kPa=900.07404 mm Hg (as 1 kPa=7.500617 mm Hg)

Now vapor pressure for benzene (1) can be calculated using Antoine equation as follows: -

  lnP1v=A'B'C'+θ

  lnP1v=15.90372789.01220.79+105

  lnP1v=7.34294

P1v=1545.248474 mm Hg at T=105°C

Now vapor pressure for toluene (2) can be calculated using Antoine equation as follows:

  lnP2v=A'B'C'+θ

  lnP2v=16.005313090.78219.14+105

  lnP2v=6.469985

P2v=645.47453 mm Hg at T=105°C

Using formula P=pA*+pB*=xAPAv+(1xA)PBv we find mole fraction of benzene (1) in liquid phase, x1

  P=p1*+p2*=x1P1v+(1x1)P2v900.07404=x1×1545.2484+(1x1)×645.47453899.77387×x1=254.59951x1=0.28296

Using the formula yA=pA*P=xAPAvP we find mole fraction of benzene (1) in vapor phase, y1

  y1=p1*P=x1P1vPy1=0.28296×1545.2484900.07404y1=0.485786

Therefore, x1=0.28296, y1=0.485786 and T=105°C at P=120

  kPa

(f)

Interpretation Introduction

Interpretation:

The overall mole fraction of benzene is z1=0.33 at total pressure P =120 kPa and temperature T=105 °C is given. The mole fraction of benzene and toluene in vapor phase needs to calculated.

Concept introduction:

Raoult’s Law states that the partial pressure of liquid A above the solution is equal to the mole fraction of the liquid in a solution times the partial pressure of the pure liquid. This holds for ideal solutions. An ideal solution is approached by binary solutions of molecules that have similar properties (e.g. benzene and toluene). The law is mathematically expressed as-

  pA*=xAPAv

Where

  PAv = vapor pressure of A at the given temperature

  xA = mole fraction of the solute A in the liquid

  pA* = equilibrium partial pressure exerted by the solute.

A solution behaves ideally when

  1. The solute and the solvent molecules have similar sizes and similar intermolecular forces,
  2. The excess volume of mixing is zero, and
  3. The heat of mixing is zero when both the solute and the solvent are liquids

(f)

Expert Solution
Check Mark

Answer to Problem 13.1P

Vapor fraction, V is 0.231923 and liquid fraction is 0.768077

Explanation of Solution

The Raoult’s law expression for two components A and B to give the equilibrium partial pressure of the components in a binary mixture is written as follows-

pA*=xAPAv

and

pB*=(1xA)PBv

The total pressure: P=pA*+pB*=xAPAv+(1xA)PBv

Where

xA = mole fraction of A in liquid phase in the binary solution

xB = (1xA) = mole fraction of B in liquid phase in the binary solution

  PAv = vapor pressure of A at the given temperature

  PBv = vapor pressure of B at the given temperature

  pA* =equilibrium partial pressure of component A

  pB* = equilibrium partial pressure of component B

The mole fraction of A in the vapor phase is given by -     yA=pA*P=xAPAvP

Similarly, mole fraction of B in vapor phase is given by -     yB=pB*P=xBPBvP

Now vapor pressures PAv and PBv are calculated by using the Antoine equation:

lnPBv or lnPAv=A'B'C'+θ;

PAv and PBv in mm Hg, θ in °C

A', B', C' are constants

Now, For benzene (1) A' =15.9037, B' =2789.01, C' =220.79

And For toluene (2) A' =16.00531, B' =3090.78, C' =219.14

Given T=105°C and P=120kPa, find x1+y1

Now, P=120

kPa=900.07404 mm Hg (as 1 kPa=7.500617 mm Hg)

Now vapor pressure for benzene (1) can be calculated using Antoine equation as follows: -

  lnP1v=A'B'C'+θ

  lnP1v=15.90372789.01220.79+105

  lnP1v=7.34294

P1v=1545.248474 mm Hg at T=105°C

Now vapor pressure for toluene (2) can be calculated using Antoine equation as follows:

  lnP2v=A'B'C'+θ

  lnP2v=16.005313090.78219.14+105

  lnP2v=6.469985

P2v=645.47453 mm Hg at T=105°C

Using formula P=pA*+pB*=xAPAv+(1xA)PBv we find an equation in x1

  P=p1*+p2*=x1P1v+(1x1)P2v900.07404=x1×1545.2484+(1x1)×645.47453899.77387×x1=254.59951x1=0.28296

Using the formula yA=pA*P=xAPAvP we find mole fraction of benzene (1) in vapor phase, y1

  y1=p1*P=x1P1vPy1=0.28296×1545.2484900.07404y1=0.485786

Now,

  z1=L×x1+V×y1L+V=1z1=L×0.28296+(1L)×0.4857860.33=0.4857860.202826×LL=0.768077V=1L=0.231923

Therefore, vapor fraction, V is 0.231923 and liquid fraction is 0.768077.

(g)

Interpretation Introduction

Interpretation:

To explain why Raoul’s law is likely to be an excellent VLE model for this system at the stated conditions.

Concept introduction:

Raoult’s Law states that the partial pressure of liquid A above the solution is equal to the mole fraction of the liquid in a solution times the partial pressure of the pure liquid. This holds for ideal solutions. An ideal solution is approached by binary solutions of molecules that have similar properties (e.g. benzene and toluene). The law is mathematically expressed as-

  pA*=xAPAv

Where

  PAv = vapor pressure of A at the given temperature

  xA = mole fraction of the solute A in the liquid

  pA* = equilibrium partial pressure exerted by the solute.

A solution behaves ideally when

  1. The solute and the solvent molecules have similar sizes and similar intermolecular forces,
  2. The excess volume of mixing is zero, and
  3. The heat of mixing is zero when both the solute and the solvent are liquids

(g)

Expert Solution
Check Mark

Explanation of Solution

Benzene and toluene are both non-polar. They are similar in shape and size. Therefore, one would expect little chemical interaction between the two substances. Moreover, the temperature is sign enough and the pressure is low, so it is expected to behave ideally.

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!

Chapter 13 Solutions

Introduction to Chemical Engineering Thermodynamics

Ch. 13 - A binary mixture of mole fraction z1is flashed to...Ch. 13 - Humidity, relating to the quantity of moisture in...Ch. 13 - A concentrated binary solution containing mostly...Ch. 13 - Air, even more than carbon dioxide, is inexpensive...Ch. 13 - Helium-laced gases are used as breathing media for...Ch. 13 - A binary system of species 1 and 2 consists of...Ch. 13 - For the system ethyl ethanoate(l)/n-heptane(2) at...Ch. 13 - A liquid mixture of cyclohexanone(1)/phenol(2) for...Ch. 13 - A binary system of species 1 and 2 consists of...Ch. 13 - For the acetone(l)/methanol(2) system, a vapor...Ch. 13 - The following is a rule of thumb: For a binary...Ch. 13 - A process stream contains light species 1 and...Ch. 13 - If a system exhibits VLE, at least one of the...Ch. 13 - Flash calculations are simpler for binary systems...Ch. 13 - Prob. 13.25PCh. 13 - (a) A feed containing equimolar amounts of...Ch. 13 - A binary mixture of benzene(1) and toluene(2) is...Ch. 13 - Ten (10) kmolhr-1 of hydrogen sulfide gas is...Ch. 13 - Physiological studies show the neutral comfort...Ch. 13 - Prob. 13.30PCh. 13 - Prob. 13.31PCh. 13 - Prob. 13.32PCh. 13 - If Eq. (13.24) is valid for isothermal VLE in a...Ch. 13 - Prob. 13.34PCh. 13 - The excess Gibbs energy for binary systems...Ch. 13 - For the ethanol(l )/chloroform(2) system at 50°C,...Ch. 13 - VLE data for methyl tert-butyl...Ch. 13 - Prob. 13.38PCh. 13 - Prob. 13.39PCh. 13 - Following are VLE data for the system...Ch. 13 - Prob. 13.41PCh. 13 - Prob. 13.42PCh. 13 - Problems 13.43 through 13.54 require parameter...Ch. 13 - Problems 13.43 through 13.54 require parameter...Ch. 13 - Prob. 13.45PCh. 13 - Problems 13.43 through 13.54 require parameter...Ch. 13 - Prob. 13.47PCh. 13 - Prob. 13.48PCh. 13 - Prob. 13.49PCh. 13 - Prob. 13.50PCh. 13 - Problems 13.43 through 13.54 require parameter...Ch. 13 - Prob. 13.52PCh. 13 - The following expressions have been reported for...Ch. 13 - Possible correlating equations for In 1 in a...Ch. 13 - Prob. 13.57PCh. 13 - Binary VLE data are commonly measured at constant...Ch. 13 - Consider the following model for GE/RT of a binary...Ch. 13 - A breathalyzer measures volume-% ethanol in gases...Ch. 13 - Table 13.10 gives values of parameters for the...Ch. 13 - Prob. 13.62PCh. 13 - A single P-x1- y1data point is available for a...Ch. 13 - A single P- x1, data point is available for a...Ch. 13 - The excess Gibbs energy for the system...Ch. 13 - Prob. 13.66PCh. 13 - A system formed of methane(l) and a light oil(2)...Ch. 13 - Use Eq. (13.13) to reduce one of the following...Ch. 13 - For one of the following substances, determine...Ch. 13 - Departures from Raoult's law are primarily from...Ch. 13 - The relative volatility a12is commonly used in...Ch. 13 - Prob. 13.74PCh. 13 - Prob. 13.75PCh. 13 - Prob. 13.76P
Knowledge Booster
Background pattern image
Chemical Engineering
Learn more about
Need a deep-dive on the concept behind this application? Look no further. Learn more about this topic, chemical-engineering and related others by exploring similar questions and additional content below.
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
Homogeneous and Heterogeneous Equilibrium - Chemical Equilibrium - Chemistry Class 11; Author: Ekeeda;https://www.youtube.com/watch?v=8V9ozZSKl9E;License: Standard YouTube License, CC-BY