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Question no. 7733

Pollutant P undergoes first-order degradation. An aqueous stream containing 2 kmole/m3 of P at 1 m3/h requires volume V in a mixed reactor to reach 0.5 kmole/m3. If inlet concentration doubles and flow rate triples while outlet concentration remains 0.5 kmole/m3, by what factor must the mixed reactor volume be scaled up_______________?

Select your answer for: Pollutant P undergoes first-order degradation. An aqueous stream containing 2 kmole/m3 of P at 1 m3/h requires volume V in a mixed reactor to reach 0.5 kmole/m3. If inlet concentration doubles and flow rate triples while outlet concentration remains 0.5 kmole/m3, by what factor must the mixed reactor volume be scaled up_______________?
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Answer: A. 7

Explanation

CSTR design equations for first-order reactions relate volume, flow rate, and concentrations. Doubling inlet concentration and tripling flow rate alters mass balance requirements. Solving the steady-state reactor design equation yields a volume scale-up factor of 7. Continuous stirred tank reactor mass balances assume perfect mixing and uniform composition. Space time is calculated as reactor volume divided by volumetric feed rate. First-order degradation kinetics simplify algebraic reactor design calculations.

Environmental engineering relies on CSTR models to design wastewater treatment aeration basins. Industrial pollutant degradation units must scale up when influent loading rates increase. Reactor volume scaling calculations prevent undersizing biological or chemical treatment systems. Alternative scale-up factors fail to satisfy the stoichiometric mass balance equations. Simple proportional scaling ignores the non-linear nature of CSTR kinetics. Rigorous mathematical derivation confirms a scale-up factor of 7 is required.

Subject
Engineering
Topic
—
Difficulty
medium

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