ELEMENTS OF CHEM. REACTION ENGR
ELEMENTS OF CHEM. REACTION ENGR
5th Edition
ISBN: 9780135486498
Author: Fogler
Publisher: INTER PEAR
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Chapter 18, Problem 18.3P

The second-order liquid-phase reaction

A B + C

is to be carried out isothermally. The entering concentration of A is 1.0 mol/dm3. The specific reaction rate is 1.0 dm3/mol·min. A number of used reactors (shown below) are available, each of which has been characterized by an RTD. There are two crimson and white reactors, and three maize and blue reactors available.

Chapter 18, Problem 18.3P, The second-order liquid-phase reaction AB+C is to be carried out isothermally. The entering

  1. (a) You have $50,000 available to spend. What is the greatest conversion you can achieve with the available money and reactors?
  2. (b) How would your answer to (a) change if you had an extra $75.000 available to spend?
  3. (c) From which cities do you think the various used reactors came from?

(a)

Expert Solution
Check Mark
Interpretation Introduction

Interpretation:

The greatest amount of the conversion that can be attained with the available money and reactors is to be stated.

Concept introduction:

The conversion, X can be defined as the moles of any species A that are reacted per mole of A fed in the reactor.

Answer to Problem 18.3P

The greatest amount of the conversion that can be attained with the available money and reactors is 0.86 that is present in both orange and blue reactor and silver and black reactor.

Explanation of Solution

It is given that some bromine present in a glass battery jar is dissolved in water and placed in the sunlight directly for the photochemical decay.

The given second-order liquid-phase reaction is as follows.

    AB+C

The initial entering concentration of reactant A, CA0, is 1.0mol/dm3.

The given specific rate constant of the reaction, k, is 1.0dm3/molmin.

The given reactors with their space time and area are shown as follows.

Reactorsσ(min)τ(min)Cost
Maize and blue22$25,000
Green and white44$50,000
Scarlet and gray3.054$50,000
Orange and blue2.314$50,000
Purple and white5.174$50,000
Silver and black2.54$50,000
Crimson and white2.52$25,000

The expression to calculate the number of tanks is given as follows.

    n=τ2σ2

Where,

  • n is the number of tanks.
  • τ is the specific time.
  • σ is the cross-sectional area.

Thus, the new table for the reactors with calculated number of tanks is given as follows.

Reactorsσ(min)τ(min)CostNumber of tanks, n=τ2σ2
Maize and blue22$25,0001
Green and white44$50,0001
Scarlet and gray3.054$50,0002
Orange and blue2.314$50,0003
Purple and white5.174$50,0001
Silver and black2.54$50,0003
Crimson and white2.52$25,0001

The conversion for the second order reaction is calculated by the expression given below.

    X=2Da4Da+12Da

Where,

  • Da is the equals to kτCA0.
  • CA0 is the initial concentration of A.

The expression to calculate the final concentration is as follows.

    CA=CA0(1X)

The single tank reactors are maize and blue; green and white; purple and white; and crimson and white.

The values of conversion and the final concentration corresponding to the single tank reactor are given in the table as follows.

Reactorsσ(min)τ(min)Number of tanks, n=τ2σ2Da=kτCA0X1=2Da4Da+12DaCA1=CA0(1X)
Maize and blue22120.50.5
Green and white44140.610.39
Purple and white5.174140.610.39
Crimson and white2.52120.50.5

The double and triple tank reactors are scarlet and gray; orange and blue; and silver and black.

The values of conversion and the final concentration corresponding to the single tank reactor are given in the table as follows.

Reactorsσ(min)τ(min)Number of tanks, n=τ2σ2Da=kτCA0X1=2Da4Da+12DaCA1=CA0(1X)
Scarlet and gray3.054240.610.39
Orange and blue2.314340.610.39
Silver and black2.54340.610.39

The final concentration, CA1, for the tank-1 of scarlet and gray reactor is 0.39dm3/mol.

For the second tank of scarlet and gray reactor, the value of Da2 is calculated as follows.

    Da1=kτCA1

Substitute the value of k as 1.0dm3/molmin, τ as 4 and CA1 as 0.39dm3/mol in the above equation.

    Da1=1.0dm3/molmin×4min×0.39dm3/mol=1.56

For the second tank of scarlet and gray reactor, the value of X2 that is conversion is calculated as follows.

    X2=2Da14Da1+12Da1

Substitute the value of Da1 as 1.56 in the above equation.

    X2=2×1.564×1.56+12×1.56=0.46

Thus, the final concentration for the second tank of the reactor is calculated by the expression below.

    CA2=CA1(1X2)

Substitute the value of CA1 as 0.39dm3/mol and X2 as 0.46 in the above equation.

    CA2=0.39dm3/mol(10.46)=0.21dm3/mol

The overall conversion of the scarlet and gray reactor is calculated by expression below.

    Xoverall=1CA2CA0

Substitute the value of CA2 as 0.21dm3/mol and CA0 as 1.0mol/dm3 in the above equation.

    Xoverall=10.21dm3/mol1.0mol/dm3=0.79

Thus, the total conversion for scarlet and gray reactor is 0.79.

The final concentration, CA2, for the tank-2 of orange and blue reactor is 0.21dm3/mol.

For the third tank of orange and blue reactor, the value of Da2 is calculated as follows.

    Da2=kτCA2

Substitute the value of k as 1.0dm3/molmin, τ as 4 and CA2 as 0.21dm3/mol in the above equation.

    Da2=1.0dm3/molmin×4min×0.21dm3/mol=0.84

For the third tank of orange and blue reactor, the value of X2 that is conversion is calculated as follows.

    X2=2Da24Da2+12Da2

Substitute the value of Da2 in the above equation.

    X2=2×0.844×0.84+12×0.84=0.35

Thus, the final concentration for the third tank of the reactor is calculated by the expression below.

    CA3=CA2(1X2)

Substitute the value of CA1 as 0.39dm3/mol and X2 as 0.35 in the above equation.

    CA3=0.21dm3/mol(10.35)=0.14dm3/mol

The overall conversion of the orange and blue reactor is calculated by expression below.

    Xoverall=1CA3CA0

Substitute the value of CA3 as 0.14dm3/mol and CA0 as 1.0mol/dm3 in the above equation.

    Xoverall=10.14dm3/mol1.0mol/dm3=0.86

Thus, the total conversion for orange and blue reactor is 0.86.

For silver and black reactors, they contain three tanks as well. Thus, the overall conversion of silver and black is also 0.86.

The table that is showing the overall conversion and cost of all the reactors is as follows.

ReactorsnCostXoverall
Maize and blue1$25,0000.5
Green and white1$50,0000.61
Scarlet and gray2$50,0000.79
Orange and blue3$50,0000.86
Purple and white1$50,0000.61
Silver and black3$50,0000.86
Crimson and white1$25,0000.5

The available money to spend is $50,000.

According to the above table, the greatest conversion corresponds to the orange and blue reactor and silver and black reactor which is 0.86.

(b)

Expert Solution
Check Mark
Interpretation Introduction

Interpretation:

The greatest amount of the conversion that can be attained if an individual had the availability of extra $75000 to spend is to be stated.

Concept introduction:

The conversion, X can be defined as the moles of any species A that are reacted per mole of A fed in the reactor.

Answer to Problem 18.3P

The greatest conversion can be attained with availability of extra $75000 to spend by the help of both maize and blue reactor and orange and blue reactor.

Explanation of Solution

The table that is showing the overall conversion and cost of all the reactors is as follows.

ReactorsnCostXoverall
Maize and blue1$25,0000.5
Green and white1$50,0000.61
Scarlet and gray2$50,0000.79
Orange and blue3$50,0000.86
Purple and white1$50,0000.61
Silver and black3$50,0000.86
Crimson and white1$25,0000.5

The previous available money to spend is $50,000.

The available money to spend is $75,000.

As, $25,000 extra money available, thus, with the help of orange and blue reactor having cost $50,000 and maize and blue reactor having cost $25,000, the greatest conversion can be achieved.

(c)

Expert Solution
Check Mark
Interpretation Introduction

Interpretation:

The cities from which different types of used reactors came are to be stated.

Concept introduction:

The conversion, X can be defined as the moles of any species A that are reacted per mole of A fed in the reactor.

Answer to Problem 18.3P

The cities from which different types of used reactors came are stated below.

Explanation of Solution

The cities from which different types of used reactors came are follows.

  • Evanston, Illinois
  • Columbus, OR
  • Ann Arbor, Michigan
  • East Lansing, Michigan
  • Urbana, Illinois
  • West Lafayette, Indiana
  • Madison, Wisconsin

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