Chemical Reaction Engineering
With decrease in temperature, the equilibrium conversion of a reversible endother- mic reaction

Remains unaffected
Increases
Decreases
Increases linearly with temperature

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Chemical Reaction Engineering
A batch reactor is suitable for

Large scale gaseous phase reactions
Liquid phase reactions
Obtaining uniform polymerisation products in highly exothermic reactions
Achieving cent percent conversion of reactants into products

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Chemical Reaction Engineering
A CSTR is to be designed in which an exothermic liquid phase first order reaction of the type, A → R, is taking place. The reactor is to be provided with a jacket in which coolant is flowing. Following data is given: CA0= 5 kmole/m³ ; XA = 0.5; Feed temperature = reactor temperature = 40°C. Rate constant at 40°C = 1 min⁻¹ ; (ΔH) = - 40kJ/mole; ρ = 1000kg/m³ CP = 4 J/gm.°C ; q = 10⁻³ m³/min (ρ and CP are same for the reactant and product streams). The amount of heat to be removed is

2/3 kW
4kW
5/3 kW
1kW

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