(a) Interpretation: It should be determined that how many independent material balance may be written for this system. Concept introduction: The independent material balance is when the stoichiometric equation of anyone of them can not be obtained by adding or subtracting multiples of the stoichiometric equation of the others. The material balances are non independent; if two molecular species are in same ratio to each other wherever they appear and if two atomic species are in same ratio to each other wherever they occur.

Question

Advance Statistics and DOL 01 (90%): Use the below experimental regions information and the data given in the below table to run and analyze the Yield of reactor presented below: Factors; Response: Temperature (°C): (150, 250) Pressure (bar): (1.5, 10) Flow Rate (L/min): (10, 30) Yield (%): Hypothetical yield data for each combination of factors. Use 2 factorial, full factorial, Central Composite, and Box-Behnken designs to construct the design tables that are required to run the experiments (real and coded). Then analyze the results using MINITAB software to show the regression model for you think is the Yield and most effective parameters and interaction. Which design do the giving best model fitting based on your results? (Note; use 3 center point). 02 (10%): Use the Hypothetical yield data shown in the below Table to find the variance and standard deviation and the median. Hypothetical Yield Data Run Temperature (°C) Pressure (bar) Flow Rate (L/min) Yield (%) 1 150 1 10 65 2 150 1…

Answer 1

Question

Chapter 4, Problem 4.8P

Interpretation Introduction

(a)

Interpretation:

It should be determined that how many independent material balance may be written for this system.

Concept introduction:

The independent material balance is when the stoichiometric equation of anyone of them can not be obtained by adding or subtracting multiples of the stoichiometric equation of the others.

The material balances are non independent; if two molecular species are in same ratio to each other wherever they appear and if two atomic species are in same ratio to each other wherever they occur.

Interpretation Introduction

(b)

Interpretation:

How many of unknown flow rates and mole fractions must be specified before the other may be calculated?

Concept introduction:

In order to understand different variables and components of a system, the analysis of degree of freedom can work better. If the degree of freedom is zero then the problem is specified.

The degree of freedom is explained as:

F=m−n−p−s

Where, m is total number of independent stream variables, n is number of independent balances, p is total number of specified terms and s is total number of subsidiary relation.

Interpretation Introduction

(c)

Interpretation:

Supposing the values are given for m.1 and x2A, then a series of equations should be given involving only a single unknown for the remaining variables. The variables should be circled for which the problem is solved.

Concept introduction:

In order to understand different variables and components of a system, the analysis of degree of freedom can work better. If the degree of freedom is zero then the problem is specified.

The degree of freedom is explained as:

F=m−n−p−s

Where, m is total number of independent stream variables, n is number of independent balances, p is total number of specified terms and s is total number of subsidiary relation.

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Advance Statistics and DOL 01 (90%): Use the below experimental regions information and the data given in the below table to run and analyze the Yield of reactor presented below: Factors; Response: Temperature (°C): (150, 250) Pressure (bar): (1.5, 10) Flow Rate (L/min): (10, 30) Yield (%): Hypothetical yield data for each combination of factors. Use 2 factorial, full factorial, Central Composite, and Box-Behnken designs to construct the design tables that are required to run the experiments (real and coded). Then analyze the results using MINITAB software to show the regression model for you think is the Yield and most effective parameters and interaction. Which design do the giving best model fitting based on your results? (Note; use 3 center point). 02 (10%): Use the Hypothetical yield data shown in the below Table to find the variance and standard deviation and the median. Hypothetical Yield Data Run Temperature (°C) Pressure (bar) Flow Rate (L/min) Yield (%) 1 150 1 10 65 2 150 1…

Derive the formula boundary-s layer, thickness 5x Rex

Q2] The reaction AR + S is irreversible and first order. It is conducted in a PFR with 50 tubes, each with 0.5 in diameter and 1.0 m of height. 200 kg/h of reactant A (MW-80 g/gmol) with 30% inert is introduced at a pressure of 50 atm at 500°C. The output conversion is 80%. Calculate the average residence time.

Answer 2

Question

Chapter 4, Problem 4.8P

Interpretation Introduction

(a)

Interpretation:

It should be determined that how many independent material balance may be written for this system.

Concept introduction:

The independent material balance is when the stoichiometric equation of anyone of them can not be obtained by adding or subtracting multiples of the stoichiometric equation of the others.

The material balances are non independent; if two molecular species are in same ratio to each other wherever they appear and if two atomic species are in same ratio to each other wherever they occur.

Interpretation Introduction

(b)

Interpretation:

How many of unknown flow rates and mole fractions must be specified before the other may be calculated?

Concept introduction:

In order to understand different variables and components of a system, the analysis of degree of freedom can work better. If the degree of freedom is zero then the problem is specified.

The degree of freedom is explained as:

F=m−n−p−s

Where, m is total number of independent stream variables, n is number of independent balances, p is total number of specified terms and s is total number of subsidiary relation.

Interpretation Introduction

(c)

Interpretation:

Supposing the values are given for m.1 and x2A, then a series of equations should be given involving only a single unknown for the remaining variables. The variables should be circled for which the problem is solved.

Concept introduction:

In order to understand different variables and components of a system, the analysis of degree of freedom can work better. If the degree of freedom is zero then the problem is specified.

The degree of freedom is explained as:

F=m−n−p−s

Where, m is total number of independent stream variables, n is number of independent balances, p is total number of specified terms and s is total number of subsidiary relation.

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Answer 3

Question

Chapter 4, Problem 4.8P

Interpretation Introduction

(a)

Interpretation:

It should be determined that how many independent material balance may be written for this system.

Concept introduction:

The independent material balance is when the stoichiometric equation of anyone of them can not be obtained by adding or subtracting multiples of the stoichiometric equation of the others.

The material balances are non independent; if two molecular species are in same ratio to each other wherever they appear and if two atomic species are in same ratio to each other wherever they occur.

Interpretation Introduction

(b)

Interpretation:

How many of unknown flow rates and mole fractions must be specified before the other may be calculated?

Concept introduction:

In order to understand different variables and components of a system, the analysis of degree of freedom can work better. If the degree of freedom is zero then the problem is specified.

The degree of freedom is explained as:

F=m−n−p−s

Where, m is total number of independent stream variables, n is number of independent balances, p is total number of specified terms and s is total number of subsidiary relation.

Interpretation Introduction

(c)

Interpretation:

Supposing the values are given for m.1 and x2A, then a series of equations should be given involving only a single unknown for the remaining variables. The variables should be circled for which the problem is solved.

Concept introduction:

In order to understand different variables and components of a system, the analysis of degree of freedom can work better. If the degree of freedom is zero then the problem is specified.

The degree of freedom is explained as:

F=m−n−p−s

Where, m is total number of independent stream variables, n is number of independent balances, p is total number of specified terms and s is total number of subsidiary relation.

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Answer 4

Question

Chapter 4, Problem 4.8P

Interpretation Introduction

(a)

Interpretation:

It should be determined that how many independent material balance may be written for this system.

Concept introduction:

The independent material balance is when the stoichiometric equation of anyone of them can not be obtained by adding or subtracting multiples of the stoichiometric equation of the others.

The material balances are non independent; if two molecular species are in same ratio to each other wherever they appear and if two atomic species are in same ratio to each other wherever they occur.

Interpretation Introduction

(b)

Interpretation:

How many of unknown flow rates and mole fractions must be specified before the other may be calculated?

Concept introduction:

In order to understand different variables and components of a system, the analysis of degree of freedom can work better. If the degree of freedom is zero then the problem is specified.

The degree of freedom is explained as:

F=m−n−p−s

Where, m is total number of independent stream variables, n is number of independent balances, p is total number of specified terms and s is total number of subsidiary relation.

Interpretation Introduction

(c)

Interpretation:

Supposing the values are given for m.1 and x2A, then a series of equations should be given involving only a single unknown for the remaining variables. The variables should be circled for which the problem is solved.

Concept introduction:

In order to understand different variables and components of a system, the analysis of degree of freedom can work better. If the degree of freedom is zero then the problem is specified.

The degree of freedom is explained as:

F=m−n−p−s

Where, m is total number of independent stream variables, n is number of independent balances, p is total number of specified terms and s is total number of subsidiary relation.

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Answer 5

Chapter 4, Problem 4.8P

Interpretation Introduction

(a)

Interpretation:

It should be determined that how many independent material balance may be written for this system.

Concept introduction:

The independent material balance is when the stoichiometric equation of anyone of them can not be obtained by adding or subtracting multiples of the stoichiometric equation of the others.

The material balances are non independent; if two molecular species are in same ratio to each other wherever they appear and if two atomic species are in same ratio to each other wherever they occur.

Interpretation Introduction

(b)

Interpretation:

How many of unknown flow rates and mole fractions must be specified before the other may be calculated?

Concept introduction:

In order to understand different variables and components of a system, the analysis of degree of freedom can work better. If the degree of freedom is zero then the problem is specified.

The degree of freedom is explained as:

F=m−n−p−s

Where, m is total number of independent stream variables, n is number of independent balances, p is total number of specified terms and s is total number of subsidiary relation.

Interpretation Introduction

(c)

Interpretation:

Supposing the values are given for m.1 and x2A, then a series of equations should be given involving only a single unknown for the remaining variables. The variables should be circled for which the problem is solved.

Concept introduction:

In order to understand different variables and components of a system, the analysis of degree of freedom can work better. If the degree of freedom is zero then the problem is specified.

The degree of freedom is explained as:

F=m−n−p−s

Where, m is total number of independent stream variables, n is number of independent balances, p is total number of specified terms and s is total number of subsidiary relation.

Answer 6

Chapter 4, Problem 4.8P

Interpretation Introduction

(a)

Interpretation:

It should be determined that how many independent material balance may be written for this system.

Concept introduction:

The independent material balance is when the stoichiometric equation of anyone of them can not be obtained by adding or subtracting multiples of the stoichiometric equation of the others.

The material balances are non independent; if two molecular species are in same ratio to each other wherever they appear and if two atomic species are in same ratio to each other wherever they occur.

Answer 7

Chapter 4, Problem 4.8P

Interpretation Introduction

(a)

Interpretation:

It should be determined that how many independent material balance may be written for this system.

Concept introduction:

The independent material balance is when the stoichiometric equation of anyone of them can not be obtained by adding or subtracting multiples of the stoichiometric equation of the others.

The material balances are non independent; if two molecular species are in same ratio to each other wherever they appear and if two atomic species are in same ratio to each other wherever they occur.

Answer 8

Interpretation Introduction

(b)

Interpretation:

How many of unknown flow rates and mole fractions must be specified before the other may be calculated?

Concept introduction:

In order to understand different variables and components of a system, the analysis of degree of freedom can work better. If the degree of freedom is zero then the problem is specified.

The degree of freedom is explained as:

F=m−n−p−s

Where, m is total number of independent stream variables, n is number of independent balances, p is total number of specified terms and s is total number of subsidiary relation.

Answer 9

Interpretation Introduction

(b)

Interpretation:

How many of unknown flow rates and mole fractions must be specified before the other may be calculated?

Concept introduction:

In order to understand different variables and components of a system, the analysis of degree of freedom can work better. If the degree of freedom is zero then the problem is specified.

The degree of freedom is explained as:

F=m−n−p−s

Where, m is total number of independent stream variables, n is number of independent balances, p is total number of specified terms and s is total number of subsidiary relation.

Answer 10

Interpretation Introduction

(c)

Interpretation:

Supposing the values are given for m.1 and x2A, then a series of equations should be given involving only a single unknown for the remaining variables. The variables should be circled for which the problem is solved.

Concept introduction:

In order to understand different variables and components of a system, the analysis of degree of freedom can work better. If the degree of freedom is zero then the problem is specified.

The degree of freedom is explained as:

F=m−n−p−s

Where, m is total number of independent stream variables, n is number of independent balances, p is total number of specified terms and s is total number of subsidiary relation.

Answer 11

Interpretation Introduction

(c)

Interpretation:

Supposing the values are given for m.1 and x2A, then a series of equations should be given involving only a single unknown for the remaining variables. The variables should be circled for which the problem is solved.

Concept introduction:

In order to understand different variables and components of a system, the analysis of degree of freedom can work better. If the degree of freedom is zero then the problem is specified.

The degree of freedom is explained as:

F=m−n−p−s

Where, m is total number of independent stream variables, n is number of independent balances, p is total number of specified terms and s is total number of subsidiary relation.

Answer 12

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Ch. 4 - Prob. 4.1P Ch. 4 - Rain is falling on a poorly designed 150-m" flat...Ch. 4 - A liquid-phase chemical reaction A -* B takes...Ch. 4 - A stream consisting of 44.6 mole% benzene and...Ch. 4 - Prob. 4.5P Ch. 4 - A liquid mixture of acetone and water contains 35...Ch. 4 - Prob. 4.7P Ch. 4 - Prob. 4.8P Ch. 4 - Inside a distillation column (see Problem 4.8), a...Ch. 4 - Prob. 4.10P

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