ELEMENTS OF CHEM. REACTION ENGR
ELEMENTS OF CHEM. REACTION ENGR
5th Edition
ISBN: 9780135486498
Author: Fogler
Publisher: INTER PEAR
Question
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Chapter 13, Problem 13.7P

(a)

Interpretation Introduction

Interpretation:

The temperature and the concentrations of A, B and C are to be plotted and analyzed as a function of time for an adiabatic operation.

Concept introduction:

The real reactor is defined as the process vessel which is used to perform a chemical reaction. It is modeled by various combinations of ideal reactors. The conversion, X can be defined as the moles of any species A that are reacted per mole of A fed in the reactor.

Semibatch reactor is defined as a reactor in which one reactor can be added continuously to the other reactor that is present in the vessel as the reaction continues.

(b)

Interpretation Introduction

Interpretation:

The temperature and the concentrations of A, B and C are to be plotted and analyzed as a function of time for the values of UA which are equal to 10,000,40,000 and 100,000J/minK.

Concept introduction:

The real reactor is defined as the process vessel which is used to perform a chemical reaction. It is modeled by various combinations of ideal reactors. The conversion, X can be defined as the moles of any species A that are reacted per mole of A fed in the reactor.

Semibatch reactor is defined as a reactor in which one reactor can be added continuously to the other reactor that is present in the vessel as the reaction continues.

(c)

Interpretation Introduction

Interpretation:

The temperature and the concentrations of A, B and C are to be plotted and analyzed as a function of time for the value of UA equals to 40,000J/minK and for different initial reactor temperatures.

Concept introduction:

The real reactor is defined as the process vessel which is used to perform a chemical reaction. It is modeled by various combinations of ideal reactors. The conversion, X can be defined as the moles of any species A that are reacted per mole of A fed in the reactor.

Semibatch reactor is defined as a reactor in which one reactor can be added continuously to the other reactor that is present in the vessel as the reaction continues.

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15.6. We want to model the flow of fluid in a flow channel. For this we locate three measuring points A, B, and C, 100 m apart along the flow channel. We inject tracer upstream of point A, fluid flows past points A, B, and C with the following results: At A the tracer width is 2 m At B the tracer width is 10 m At C the tracer width is 14 m What type of flow model would you try to use to represent this flow: dispersion, convective, tanks-in-series, or none of these? Give a reason for your answer.
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15.4. Aqueous A (CAO (p = 1000 kg/m³, = 1 mol/liter) with physical properties close to water = 10-9 m²/s) reacts by a first-order homogeneous 1 reaction (AR, k = 0.2 s¹) as it flows at 100 mm/s through a tubular 50 mm, L = 5 m). Find the conversion of A in the fluid reactor (d, leaving this reactor.
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