It is intended to produce Propylene Glycol, PG (CH₂(OH)CH(OH)CH3) by the hydrolysis of Propylene Oxide, PO (CH₂OCHCH3) in CSTR. The acid-catalyzed liquid-phase exothermic reaction is shown below: CH₂OCHCH₂ + H₂O CH₂(OH)CH(OH)CH₂ The feed, containing 3 mol/L of Propylene Oxide and 30 mol/L of water, enters the well-mixed adiabatic reactor at 303 K at a total volumetric flowrate of 10 L/min. Propylene Oxide is a volatile substance, and you cannot exceed an operating temperature of 80°C. Assume that you operate the system at this maximum temperature. Additional Information: AHxn(298K) = -18,000 cal/mol k at 298 K = 2.77x10 min¹ Gas law constant = 1.987 cal/K.mol. E = 15,000 cal/mol Cp (PO) 35 cal/molk = Cp (H20) 18 cal/mol K Cp (PG) = 46 cal/mol K The reaction is dependent in Propylene Oxide concentration and independent of water concentration. It can be treated as a first order and also second order reaction. Analyse and justify the effect of reaction order on the conversion of reaction and volume of reactor.

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It is intended to produce Propylene Glycol, PG (CH2(OH)CH(OH)CH3) by the hydrolysis of
Propylene Oxide, PO (CH20CHCH3) in CSTR. The acid-catalyzed liquid-phase exothermic
reaction is shown below:
CH20CHCH, + H20 - CH2(OH)CH(OH)CH,
The feed, containing 3 mol/L of Propylene Oxide and 30 mol/L of water, enters the well-mixed
adiabatic reactor at 303 K at a total volumetric flowrate of 10 L/min. Propylene Oxide is a
volatile substance, and you cannot exceed an operating temperature of 80°C. Assume that
you operate the system at this maximum temperature.
Additional Information:
AHxn(298K) = -18,000 cal/mol
k at 298 K = 2.77x10-4 min-
Gas law constant = 1.987 cal/K.mol.
E = 15,000 cal/mol
Cp (PO) = 35 cal/molK
Cp (H20) = 18 cal/mol K
Cp (PG) = 46 cal/mol K
%3D
The reaction is dependent in Propylene Oxide concentration and independent of water
concentration. It can be treated as a first order and also second order reaction. Analyse and
justify the effect of reaction order on the conversion of reaction and volume of reactor.
Transcribed Image Text:It is intended to produce Propylene Glycol, PG (CH2(OH)CH(OH)CH3) by the hydrolysis of Propylene Oxide, PO (CH20CHCH3) in CSTR. The acid-catalyzed liquid-phase exothermic reaction is shown below: CH20CHCH, + H20 - CH2(OH)CH(OH)CH, The feed, containing 3 mol/L of Propylene Oxide and 30 mol/L of water, enters the well-mixed adiabatic reactor at 303 K at a total volumetric flowrate of 10 L/min. Propylene Oxide is a volatile substance, and you cannot exceed an operating temperature of 80°C. Assume that you operate the system at this maximum temperature. Additional Information: AHxn(298K) = -18,000 cal/mol k at 298 K = 2.77x10-4 min- Gas law constant = 1.987 cal/K.mol. E = 15,000 cal/mol Cp (PO) = 35 cal/molK Cp (H20) = 18 cal/mol K Cp (PG) = 46 cal/mol K %3D The reaction is dependent in Propylene Oxide concentration and independent of water concentration. It can be treated as a first order and also second order reaction. Analyse and justify the effect of reaction order on the conversion of reaction and volume of reactor.
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