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 13.4P

(a)

Interpretation Introduction

Interpretation:

The flow rate of the coolant at 2h after the starting the reaction 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.

A batch reactor is a closed system with no continuous flow of reactants entering the system or products leaving the system while the reaction takes place.

In most batch reactors, the longer a reactant stays in the reactor, the more the reactant is converted to product until either equilibrium is reached or the reactant is exhausted. Consequently, in batch systems the conversion X is a function of the time the reactants spend in the reactor.

(b)

Interpretation Introduction

Interpretation:

The rate of solvent evaporation as function of time is to be stated. The flow rate of the solvent at the end of 2h 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.

A batch reactor is a closed system with no continuous flow of reactants entering the system or products leaving the system while the reaction takes place.

In most batch reactors, the longer a reactant stays in the reactor, the more the reactant is converted to product until either equilibrium is reached or the reactant is exhausted. Consequently, in batch systems the conversion X is a function of the time the reactants spend in the reactor.

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(30) 6. In a process design, the following process streams must be cooled or heated: Stream No mCp Temperature In Temperature Out °C °C kW/°C 1 5 350 270 2 9 270 120 3 3 100 320 4 5 120 288 Use the MUMNE algorithm for heat exchanger networks with a minimum approach temperature of 20°C. (5) a. Determine the temperature interval diagram. (3) (2) (10) (10) b. Determine the cascade diagram, the pinch temperatures, and the minimum hot and cold utilities. c. Determine the minimum number of heat exchangers above and below the pinch. d. Determine a valid heat exchange network above the pinch. e. Determine a valid heat exchange network below the pinch.
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