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Rxn Eng Exam ( 2 0 2 2 0 4 2 0 ) [ 1 0 ] Explain contacting patterns of 3 representative ideal reactors.
Rxn Eng Exam
Explain contacting patterns of representative ideal reactors. Firstly, you should give the names of the reactors,
and add the explanation for each.
In a PFR plug flow reactor under steady state, the following gas reaction takes place. This reaction follows the
firstorder irreversible kinetics at
denotes gas phase rate equation
The temperature, total pressure, and the total molar flow rate at the inlet of the reactor are kPa, and
respectively. There are A and inert gas at the inlet. What size of plug flow reactor operating at
and kPa can produce conversion Note: Write down the corresponding performance equation, integrate the
PFR performance equation with the given rate equation to find the reactor volume
A chemical reaction below took place in a batch reactor. The conversion of A was Temperature, pressure, and
volume at initial stage were and respectively. Initially, there were inert I, and no products. The initial
compositions of and I inert were same. Before reaction, the mixture was found to be an ideal gas mixture. During
the reaction, you could denote temperature, pressure and volume as and respectively. During the reaction, the
gaseous mixture did not seem to be an ideal gas mixture due to relatively high pressure.
Reaction:
a Derive the relationship between the volume at the end of reaction and the initial volume
b Express in gaseous phase. Do it by using stoichiometric coefficients and conversion of
c Experimentalists carried out additional reaction at a lower reaction temperature than the original reaction
temperature. In this experiment the product totally condensed due to its boiling point. Experimentalists noticed that
the liquid fraction of the product was so small that they could disregard the liquid fraction in the volume of reaction
mixture. Derive the relationship between the gaseous volume and the end of reaction and the initial volume
d In the c experiment, derive the expression in terms of stoichiometric coefficients and conversion of
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