Unit Operations of Chemical Engineering
Unit Operations of Chemical Engineering
7th Edition
ISBN: 9780072848236
Author: Warren McCabe, Julian C. Smith, Peter Harriott
Publisher: McGraw-Hill Companies, The
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Chapter 17, Problem 17.1P

(a)

Interpretation Introduction

Interpretation:

Molal flux of CO2 for the given process of diffusion is to be determined.

Concept Introduction:

The formula to calculate molal flux for the equimolar diffusion of gas A through gas B is:

NA=DvρMBT(yAiyA) ...... (1)

Here, BT is the thickness of the film over which the flux is to be determined, yA is the mole fraction of A at the outer edge of the film, yAi is the mole fraction of A at the inner edge or the interface of the film, Dv is the volumetric diffusivity of A in the mixture with species B, and ρM is the molar density of the gas mixture at the given temperature and pressure conditions.

(a)

Expert Solution
Check Mark

Answer to Problem 17.1P

Molal flux of CO2 for the given process of diffusion is, NCO2=1.387×104kg-molm2h .

Explanation of Solution

Given information:

Diffusion of CO2 through N2 takes place in one direction.

Pressure, P=1 atm

Temperature, T=0C

Mole fraction of CO2 at point A, yA=0.2

Mole fraction of CO2 at point B, yB=0.02

Distance between point A and B, BT=3 m

Volumetric diffusivity, Dv=0.144cm2s

The whole gas phase is stationary.

Nitrogen diffuses at the same rate as carbon dioxide in opposite direction.

For an ideal gas at standard temperature and pressure (1 atm, 0C) , the molar volume is taken as 22.4m3/kg-mol . The given pressure and temperature of the system is same as STP. Calculate the molar density of the gas as:

ρM=1VM

  =122.4kmolm3

  =0.0446kmolm3

Use equation (1) to calculate the molal flux of CO2 as:

NCO2=DvρMBT(yAyB)

  =(0.144cm2s×104 m2cm2×3600 sh)(0.0446kg-molm3)3 m(0.20.02)

  =1.387×104kg-molm2h

(b)

Interpretation Introduction

Interpretation:

The net mass flux for the given process of diffusion is to be determined.

Concept Introduction:

The formula to calculate mass flux for the equimolar diffusion of gas A through gas B is:

mA=MANA ...... (2)

The formula to calculate mass flux for the equimolar diffusion of gas B through gas A is:

mB=MBNB ...... (3)

Total mass flux will be:

mNet=mA+mB ...... (4)

Here, MA and MB are the molar mass of gases A and B respectively.

(b)

Expert Solution
Check Mark

Answer to Problem 17.1P

The net mass flux for the given process of diffusion is, mNet=2.2192×103kgm2h .

Explanation of Solution

From part (a), the molar flux of CO2 through N2 is calculated as:

NCO2=1.387×104kg-molm2h

Molar flux of N2 is equal as that of CO2 but in opposite direction. Thus,

NN2=1.387×104kg-molm2h

Molar masses of CO2 and N2 are taken as:

MCO2=44kgkg-mol

  MN2=28kgkg-mol

Use equations (2) and (3) to calculate the mass flux of CO2 and N2 as:

mCO2=MCO2NCO2

  =(44kgkg-mol)(1.387×104kg-molm2h)

  =6.1028×103kgm2h

  mN2=MN2NN2

  =(28kgkg-mol)(1.387×104kg-molm2h)

  =3.8836×103kgm2h

Use equation (4) to calculate the net mass flux as:

mNet=mCO2+mN2

  =(6.1028×103kgm2h)+(3.8836×103kgm2h)

  =2.2192×103kgm2h

(c)

Interpretation Introduction

Interpretation:

The speed of the observer at which the net mass flux relative to the observer becomes zero is to be determined.

Concept Introduction:

The formula that relates the molar flux of A with its concentration and velocityis:

NA=cAuA ...... (5)

The formula that relates the molar flux of B with its concentration and velocity is:

NB=cBuB ...... (6)

Concentration of a species is defined as:

ci=yiρM ...... (7)

(c)

Expert Solution
Check Mark

Answer to Problem 17.1P

The speed of the observer from point A at which the net mass flux relative to the observer becomes zero is, u0,A=4.43×107ms .

The speed of the observer from point B at which the net mass flux relative to the observer becomes zero is, u0,B=4.89×107ms .

Explanation of Solution

From part (a), the molar flux of CO2 through N2 is calculated as:

NCO2=1.387×104kg-molm2h

Molar flux of N2 is equal as that of CO2 but in opposite direction. Thus,

NN2=1.387×104kg-molm2h

Calculate the concentration of CO2 and N2 at point A and at point B as:

cCO2,A=yAρM

  =(0.2)(0.0446kmolm3)

  =8.92×103kmolm3

  cN2,A=(1yA)ρM

  =(10.2)(0.0446kmolm3)

  =3.568×102kmolm3

  cCO2,B=yBρM

  =(0.02)(0.0446kmolm3)

  =8.92×104kmolm3

  cN2,B=(1yB)ρM

  =(10.02)(0.0446kmolm3)

  =4.3708×102kmolm3

Calculate the velocities of CO2 and N2 at point A and at point B. Use the numerical values of the flux.

uCO2,A=NCO2cCO2,A

  =1.387×104kg-molm2h×h3600 s8.92×103kmolm3

  =4.32×106ms

  uN2,A=NN2cN2,A

  =1.387×104kg-molm2h×h3600 s3.568×102kmolm3

  =1.0798×106ms

  uCO2,B=NCO2cCO2,B

  =1.387×104kg-molm2h×h3600 s8.92×104kmolm3

  =4.32×105ms

  uN2,B=NN2cN2,B

  =1.387×104kg-molm2h×h3600 s4.3708×102kmolm3

  =8.815×107ms

The mass flux of CO2 and N2 through a reference plane in terms of the velocity of the moving observer (u0) is written as:

mCO2=cCO2MCO2(uCO2u0)

  mN2=cN2MN2(uN2u0)

Since the velocity of the observer at the point of zero net mass flux is to be calculated, mass flux of CO2 must be equal to the mass flux of N2. Thus,

mCO2=mN2

  cCO2MCO2(uCO2u0)=cN2MN2(uN2u0)

  u0=cCO2MCO2uCO2cN2MN2uN2cCO2MCO2+cN2MN2

  u0=NCO2MCO2NN2MN2cCO2MCO2+cN2MN2

  u0=NCO2(MCO2MN2)cCO2MCO2+cN2MN2

Now, use the above equation to calculate the observer velocity for point A as well as point B as:

   u 0,A = N CO 2 ( M CO 2 M N 2 ) c CO 2 ,A M CO 2 + c N 2 ,A M N 2

   = ( 1.387× 10 4 kg-mol m 2 h × h 3600 s )( ( 44 kg kmol )( 28 kg kmol ) ) ( 8.92× 10 3 kmol m 3 )( 44 kg kmol )+( 3.568× 10 2 kmol m 3 )( 28 kg kmol )

   =4.43× 10 7 m s u 0,B = N CO 2 ( M CO 2 M N 2 ) c CO 2 ,B M CO 2 + c N 2 ,B M N 2

   = ( 1.387× 10 4 kg-mol m 2 h × h 3600 s )( ( 44 kg kmol )( 28 kg kmol ) ) ( 8.92× 10 4 kmol m 3 )( 44 kg kmol )+( 4.3708× 10 2 kmol m 3 )( 28 kg kmol )

   =4.89× 10 7 m s

(d)

Interpretation Introduction

Interpretation:

The speed of the observer at which the nitrogen is stationary relative to the observer is to be determined.

Concept Introduction:

The formula that relates the molar flux of A with its concentration and velocity is:

NA=cAuA ...... (5)

The formula that relates the molar flux of B with its concentration and velocity is:

NB=cBuB ...... (6)

Concentration of a species is defined as:

ci=yiρM ...... (7)

(d)

Expert Solution
Check Mark

Answer to Problem 17.1P

The speed of the observer from point A at which the nitrogen is stationary relative to the observer is, u0,A=1.0789×106ms .

The speed of the observer from point B at which the nitrogen is stationary relative to the observer is, u0,B=83.815×107ms .

Explanation of Solution

For the nitrogen phase to appear stationary to the observer, the speed of the observer must be equal to the speed of nitrogen and in the direction of the diffusion of nitrogen.

At point A,

uo,A=uN2,A

  =1.0798×106ms

At point B,

uo,B=uN2,B

  =8.815×107ms

(e)

Interpretation Introduction

Interpretation:

Molal flux of CO2 relative to the observer in part (d) is to be estimated.

Concept Introduction:

The molal flux of A through a reference plane in terms of the velocity of the moving observer (u0) is written as:

NA=cA(uAu0) ...... (8)

(e)

Expert Solution
Check Mark

Answer to Problem 17.1P

Molal flux of CO2 relative to the observer in part (d) at point A is, NCO2,A=4.82×108kmolm2s .

Molal flux of CO2 relative to the observer in part (d) at point B is, NCO2,B=9.93×108kmolm2s .

Explanation of Solution

Velocity of the observer at points A and B from part (d) is:

uo,A=1.0798×106ms

  uo,B=8.815×107ms

The molar flux of CO2 through a reference plane in terms of the velocity of the moving observer (u0) with respect to stationary nitrogen is written as:

NCO2=cCO2(uCO2(u0))

  NCO2=cCO2(uCO2+u0)

At point A, the molar flux of CO2relative to the observer is calculated as:

NCO2,A=cCO2,A(uCO2,A+u0,A)

  =(8.92×103kmolm3)(4.32×106ms+1.0798×106ms)

  =4.82×108kmolm2s

At point B, the molar flux of CO2 relative to the observer is calculated as:

NCO2,B=cCO2,B(uCO2,B+u0,B)

  =(8.92×104kmolm3)(4.32×105ms+8.815×107ms)

  =9.93×108kmolm2s

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Chapter 17 Solutions

Unit Operations of Chemical Engineering

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