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Advanced oxidation processes can be employed to remove organic and inorganic contaminants during the treatment of water and wastewater. The reaction between the hydroxyl radical (HO), the material responsible for removing contaminants during treatemnt, and the target compound, R, is represented as follows: HO. + R → byproducts The second order rate law for decay of the target compound, rR, corresponding to this reaction is: TR KRCHO-CR Estimate the volume of a PFR reactor needed to achieve 95 percent reduction of chlorobenzene, by advanced oxidation, using HO concentrations of 10-9 moles/L ; 10-10 moles/L; and 10-11 moles/L, if the flowrate is 3800 m³/day, k is 4.3*10⁹ L/mol-s and the initial concentration of chlorobenzene is 25 µg/L for each reactor.

Advanced oxidation processes can be employed to remove organic and inorganic contaminants during the treatment of water and wastewater. The reaction between the hydroxyl radical (HO), the material responsible for removing contaminants during treatemnt, and the target compound, R, is represented as follows: HO. + R → byproducts The second order rate law for decay of the target compound, rR, corresponding to this reaction is: TR KRCHO-CR Estimate the volume of a PFR reactor needed to achieve 95 percent reduction of chlorobenzene, by advanced oxidation, using HO concentrations of 10-9 moles/L ; 10-10 moles/L; and 10-11 moles/L, if the flowrate is 3800 m³/day, k is 4.3*10⁹ L/mol-s and the initial concentration of chlorobenzene is 25 µg/L for each reactor.

Structural Analysis
Structural Analysis
6th Edition
ISBN:9781337630931
Author:KASSIMALI, Aslam.
Publisher:KASSIMALI, Aslam.
Chapter2: Loads On Structures
Section: Chapter Questions
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Advanced oxidation processes can be employed to remove organic and inorganic contaminants during the treatment of water and wastewater. The reaction between the hydroxyl radical (HO), the material responsible for removing contaminants during treatemnt, and the target compound, R, is represented as follows: HO. + R → byproducts The second order rate law for decay of the target compound, rR, corresponding to this reaction is: TR KRCHO-CR Estimate the volume of a PFR reactor needed to achieve 95 percent reduction of chlorobenzene, by advanced oxidation, using HO concentrations of 10-9 moles/L ; 10-10 moles/L; and 10-11 moles/L, if the flowrate is 3800 m³/day, k is 4.3*10⁹ L/mol-s and the initial concentration of chlorobenzene is 25 µg/L for each reactor.
Transcribed Image Text:Advanced oxidation processes can be employed to remove organic and inorganic contaminants during the treatment of water and wastewater. The reaction between the hydroxyl radical (HO), the material responsible for removing contaminants during treatemnt, and the target compound, R, is represented as follows: HO. + R → byproducts The second order rate law for decay of the target compound, rR, corresponding to this reaction is: TR KRCHO-CR Estimate the volume of a PFR reactor needed to achieve 95 percent reduction of chlorobenzene, by advanced oxidation, using HO concentrations of 10-9 moles/L ; 10-10 moles/L; and 10-11 moles/L, if the flowrate is 3800 m³/day, k is 4.3*10⁹ L/mol-s and the initial concentration of chlorobenzene is 25 µg/L for each reactor.
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Could you please explain how we got this integration equation , and why we substitute the values in the underlined part and what they stand for ? 

Given, Molecular weight of chlorobenzene = 112.56 g/mol R+ chlorobenzene = 25 μg/l { in all 3 reactors} Molor Concentration of R 251g/l 112-56 g/mol Cro = 0.22x15² mollet Concentration of Ho in all 3 reactor : Cao 10 molled → 100 mollet 10" mollet Volumetric flow rate ری دارد second order rate low: V 1 VR кр сно ср = ra K≤ 4-3 x 189 llnd-see = CA 109 S- 0.95 S 109 = 25 ug/l { in all vatansy alt For 951. Conversion, XAS =0.95 79 slov ход S s dxA less 0.95 109 109 S D dxA кса се 0.95 (VA) S = 3800 m³/day s0.0416 m³/sec where, CA CR s 10 Frustelfel loter Asidorgyd dxa K CAO (XA) (Ceo CAO XA) = dxA Catt сво KCAU (I-XA) CRO [1-(AU XA] CRO dx A KCAO (RO (1-XA) (1-MYA) stab noves ی کو دور (3:2) enefeodaralds wom' al- nudushooned of publem 0038 = etorcida zlomil 01x8. nodrodno je masenviros bitme Спо-своха Cao - CAO XA ON woll andscaulov (orvoo) yote 15-9972 word sw
Transcribed Image Text:Given, Molecular weight of chlorobenzene = 112.56 g/mol R+ chlorobenzene = 25 μg/l { in all 3 reactors} Molor Concentration of R 251g/l 112-56 g/mol Cro = 0.22x15² mollet Concentration of Ho in all 3 reactor : Cao 10 molled → 100 mollet 10" mollet Volumetric flow rate ری دارد second order rate low: V 1 VR кр сно ср = ra K≤ 4-3 x 189 llnd-see = CA 109 S- 0.95 S 109 = 25 ug/l { in all vatansy alt For 951. Conversion, XAS =0.95 79 slov ход S s dxA less 0.95 109 109 S D dxA кса се 0.95 (VA) S = 3800 m³/day s0.0416 m³/sec where, CA CR s 10 Frustelfel loter Asidorgyd dxa K CAO (XA) (Ceo CAO XA) = dxA Catt сво KCAU (I-XA) CRO [1-(AU XA] CRO dx A KCAO (RO (1-XA) (1-MYA) stab noves ی کو دور (3:2) enefeodaralds wom' al- nudushooned of publem 0038 = etorcida zlomil 01x8. nodrodno je masenviros bitme Спо-своха Cao - CAO XA ON woll andscaulov (orvoo) yote 15-9972 word sw
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