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3. Three CSTR's are to be used in series. The second reactor has a volume twice...
1. A reactor system consists of a series arrangement of a plug flow reactor and a mixed flow rector (continuous stirred tank reactor). The mixed flow reactor has 10 times the volume of the plug flow reactor. Assume the rate equation for the reaction that occurs is given by: r = 2.4 C2 where c is the concentration of the reacting species. The reaction occurs to 96% conversion. The inlet concentration of C is Cao1. You may assume the density...
1. A reactor system consists of a series arrangement of a plug flow reactor and a mixed flow rector (continuous stirred tank reactor). The mixed flow reactor has 10 times the volume of the plug flow reactor. Assume the rate equation for the reaction that occurs is given by: r = 2.4 C2 where c is the concentration of the reacting species. The reaction occurs to 96% conversion. The inlet concentration of C is Cao1. You may assume the density...
You are designing a plug flow reactor that uses chlorine to destroy pathogens in water. You want to reduce the pathogen concentration from 100 pathogens/L to below 1 pathogen/L through a first-order decay process with the constant decay rate of k = 0.15/ min. You plan on treating water at a rate of 1,000 gal/min. (a) What is the minimum contact time you need to achieve this reduction (in minutes)? And what is the minimum volume (in gallons) of the...
Q2- The conversion attained with a plug flow reactor having a volume VR is 98%,. If the reaction taking place is a 2nd order and the initial concentration is 5 mole /litter. Chemical engineer Mohamad Al afree proposed : 1-to replace the existing plug with a series of 4 mixed flow reactors (with total volume=VR of the plug flow reactor) . How will this proposal affect the conversion ? If we want to keep the conversion constant ,how will these...
5. (40 points) A set of reactors processes 20 cfm through two basins in series: one of these basins has dimensions of 10' deep x 20' wide x 50' long, while the other has dimensions of 10' deep x 20' wide x 100' long. One of these will operate as an ideal plug flow operation, and the other as an ideal continuously stirred tank reactor (CSTR). A reaction will be performed in this sequence of reactors, for which k 0.05...
The degradation of atrazine can be described by second-order kinetics with k= 5 L∙mg-1min-1 in a reactor. Calculate the volume of a PFR and CSTR required to remove atrazine to the MCL if the flow rate is 2 m3/min and C0 is 0.06 mg/L. Assume steady-state. If it costs $1/gal of tank and $4/gal of tank for a CSTR and a PFR, respectively, determine which type of reactor would be cheaper to construct.
1. An industry produces a degradable waste at flow rate of 0.72 m/day. Concentration of pollutant in the raw waste is 850 mg/L with first-order reaction rate constant of 2.5/day. The industry splits the flow into three parallel continuous stirred tank reactors at 0.25 m/day to reactor one, 0.3 m/day to reactor two and the remaining 0.17 m®/day to reactor three. If each reactor must achieve removal efficiency of 90%, what is the required detention time and the volume for...
(30 points) A completely mixed activated sludge system comprised of an aerated reactor and a secondary clarifier with sludge return is going to treat 15,000 m/d of industrial wastewater. The primary effluent going to the reactor has a BODs of 1,100 mg/L that must be reduced to 150 mg/L prior to discharge to a municipal sewer. The pilot study was conducted and generated the following results: 3. Mean cell residence time- 5 day, MLSS concentration in the reactor 7.200 mg/L...
completely mixed activated-sludge plant is to treat 10 000 m3/d ofindustrial wastewater. The wastewater has a BOD5 of 1200 mg/L that must be reduced to 200 mg/L prior to discharge to a municipal sewer. Pilot-plant analysis indicates that a mean cell-residence time of 5 d maintaining MLSS concentration of 5000 mg/L produces the desired results. The vaue for Y is determined to be 0.7 kg/kg and the value for kd is found to be 0.03 d-1Determinea) The volume of the...
2. (40 pts) A wastewater treatment plant has an activated sludge system. The aeration tank is 252 ft long, 25 ft wide, and 18 ft deep. An engineer will model the steady-state performance as first order (k= 8.3 d ?) as a series of 9 equal-volume CFSTRs. The flow rate is 3.1 MGD and the influent BODS is 165 mg/L. a) If the engineer's model is correct, what is the outlet BOD5 concentration (mg/L)? b) If the model is correct,...