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3) An exothermic liquid phase reaction between two reactants is carried out in a CSTR operating constant volume of 1 m³. The density and specific heats remain constant during the reaction. If the feed enters at a volumetric flow rate of 0.02 m³/s at 20 °C and the reactor operates adiabatically. What is the possible steady-state of temperature and conversion? $-r_A = 0.7 \exp[27.63 - \frac{9680}{T(K)}]C_AC_B$, $\left[\frac{mol}{dm^3.s}\right]$ $C_{A0} = 2 \frac{mol}{dm^3}$ $C_{B0} = 3 \frac{mol}{dm^3}$ $-\Delta H^0_{rxn}(T_R) = 210 \frac{kJ}{mol_A}$ $C_{pmix} = 15 \frac{J}{g^oC} (\Delta C_p \approx 0)$ $\rho_{mix} = 780 \frac{g}{dm^3}$

          3) An exothermic liquid phase reaction between two reactants is carried out in a
CSTR operating constant volume of 1 m³.
The density and specific heats remain constant during the reaction. If the feed
enters at a volumetric flow rate of 0.02 m³/s at 20 °C and the reactor operates
adiabatically.
What is the possible steady-state of temperature and conversion?
$-r_A = 0.7 \exp[27.63 - \frac{9680}{T(K)}]C_AC_B$, $\left[\frac{mol}{dm^3.s}\right]$
$C_{A0} = 2 \frac{mol}{dm^3}$
$C_{B0} = 3 \frac{mol}{dm^3}$
$-\Delta H^0_{rxn}(T_R) = 210 \frac{kJ}{mol_A}$
$C_{pmix} = 15 \frac{J}{g^oC} (\Delta C_p \approx 0)$
$\rho_{mix} = 780 \frac{g}{dm^3}$

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3) An exothermic liquid phase reaction between two reactants is carried out in a
CSTR operating constant volume of 1 m³.
The density and specific heats remain constant during the reaction. If the feed
enters at a volumetric flow rate of 0.02 m³/s at 20 °C and the reactor operates
adiabatically.
What is the possible steady-state of temperature and conversion?
-rA = 0.7 [27.63 - (9680)/(T(K))]CACB, [(mol)/(dm^3.s)]
CA0 = 2 (mol)/(dm^3)
CB0 = 3 (mol)/(dm^3)
-Δ H^0rxn(TR) = 210 (kJ)/(molA)
Cpmix = 15 (J)/(g^oC) (Δ Cp ≈ 0)
ρmix = 780 (g)/(dm^3)

Added by Ignacio C.

Chemistry: Structure and Properties

Nivaldo Tro 2nd Edition

Instant Answer

Solved by Expert Adi S

03/07/2023

Step 1

02 m^3/s Molar concentration of reactant A in the feed (Cao) = 2 mol/dm^3 Molar concentration of reactant B in the feed (Cbo) = 3 mol/dm^3 To calculate the molar flow rate (F) of the feed, we can use the formula: F = Q * C Where Q is the volumetric flow rate and Show more…

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Texts: An exothermic liquid-phase reaction between two reactants is carried out in a CSTR operating at a constant volume of 1 m3. The density and specific heats remain constant during the reaction. If the feed enters at a volumetric flow rate of 0.02 m3/s at 20°C and the reactor operates adiabatically, what is the possible steady-state temperature and conversion? 3) An exothermic liquid-phase reaction between two reactants is carried out in a CSTR operating at a constant volume of 1 m3. The density and specific heats remain constant during the reaction. If the feed enters at a volumetric flow rate of 0.02 m3/s at 20°C and the reactor operates adiabatically, what is the possible steady-state temperature and conversion? 96801 mol -ra = 0.7 exp[27.63 CACB, T(K)] [dm3.s] Cao = 2 mol/dm3 CBo = 3 mol/dm3 -Hxn(Tr) = 210 kJ/molA Cpmix = 15 J/g°C (Cp~O) Pmix = 780 g/dm3

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