Calculate the volume required to achieve 95% degradation of a contaminant in a CSTR if the...
Calculate the volume required to achieve 95% degradation of a contaminant in a CSTR if the degradation follows a first order reaction with a rate constant of 0.2 min-1 at a feed flow rate of 100m3/hr.
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Calculate the volume required to achieve 95% degradation of a
contaminant in a CSTR if the...
It's not 840, 5320, or 6.34 Compare the reactor volume required to achieve 95% contaminant removal...
It's not 840, 5320, or 6.34
Compare the reactor volume required to achieve 95% contaminant removal efficiency for a CMFR vs. a PFR for the following conditions: steady-state, first-order reaction, flow rate 14 m3/d, and reaction rate coefficient 0.05 d. Your answers should represent the dimensionless ratio VCMER/VPR
Consider an isothermal CSTR, with the liquid phase inlet feed of: Fao 61 mol/hr benzene Vo 10 L/m...
Consider an isothermal CSTR, with the liquid phase inlet feed of: Fao 61 mol/hr benzene Vo 10 L/min Diphenyl is synthesized by the following irreversible reaction 2benzene-» diphenyl H2 with the rate law: Tbenzene-kCbenzenek 0.2 L/(mol'min) a. Wirite the stoichiometric table for this reaction. b. What volume CSTR is required for the exit concentration of benzene to be 12 mM? c. What is the extent of reaction? d. What is the conversion of benzene?
Consider an isothermal CSTR, with the...
Hi, can you please help me with F? I know that if the volume is the...
Hi, can you please help me
with F? I know that if the volume is the same, negative order
reactions would give PFR a higher yield, however, when I tried to
do it mathematically, the units won't match because of the rate
constant. I don't know how to prove that PFR would give a higher
yield. Can i use the same rate constant but with different
units?
3. Your boss asks you to isothermally carry out a liquid-phase, irreversible reaction...
An acid-catalyzed irreversible liquid-phase reaction A B is carried out adiabatically in a CSTR. The reaction is second...
An acid-catalyzed irreversible liquid-phase reaction A B is carried out adiabatically in a CSTR. The reaction is second order in A. The feed is equimolar A and solvent (S, which contains catalyst), and enters the reactor at a total volumetric flow rate of 10 dm3/min at a concentration of A of 4 mol/L. The feed enters at 300 K. The product and reactant heat capacities are 15 cal/(mol°C), the solvent is 18 cal/(mol°C). The reaction rate constant at 300 K...
The degradation of atrazine can be described by second-order kinetics with k= 5 L∙mg-1min-1 in a...
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.
The reversible liquid reaction 2A ↔ B + C is carried out in an isothermal CSTR...
The reversible liquid reaction 2A ↔ B + C is carried out in an isothermal CSTR with no pressure drop. The feed has an A concentration of 0.1 lbmol/ft3 and T=300K. The forward reaction rate constant is 1800 ft3/lbmol-s and the concentration equilibrium constant is 0.3. a. Determine the equilibrium conversion. b. Determine the reactor volume necessary to achieve 98% of the equilibrium conversion of A if the feed is 10 lb mol/min.
The reversible gas-phase dehydrogenation of ethylbenzene is achieved in an isothermal CSTR with no pressure drop....
The reversible gas-phase dehydrogenation of ethylbenzene is achieved in an isothermal CSTR with no pressure drop. The feed enters at a volumetric flow rate of v0 = 2000 L/hour. On a molar basis the feed consists of half ethyl benzene (A) and half inerts (I) and is well mixed before it enters the reactor. The total pressure in the reactor is 6 bar (PA0 = 3 bar, PI0 = 3 bar). The molar flow rate of A is FA0 =...
The first order irreversible reaction A -> B is carried out in a CSTR. The rate...
The first order irreversible reaction A -> B is carried out in a CSTR. The rate constant is 0.05 s^-1 and the volumetric flowrate is 0.02 m^3 s^-1. What volume of reactor is required in order to achieve a conversion of 80%? Hint:(Conversation of Ca to molar flowrate/volumetric flowrate)
Reaction is A-->B is carried out adiabatically in a CSTR. The reaction is second order in...
Reaction is A-->B
is carried out adiabatically in a CSTR. The reaction is second order in A. The feed, which is equal molar in water (which contains the catalyst) and A, enters the reactor at a temperature of 52 C and a total volumetric flow rate of 10 dm3/min. The concentration of A entering the reactor is 4 molar. a) What is the reactor volume to achieve 80% conversion b) What conversion can be achieved in a 1000 dm3 CSTR?...
26. A 2m3 CSTR processes an aqueous feed containing reactant A. This is a second order...
26. A 2m3 CSTR processes an aqueous feed containing reactant A. This is a second order reaction occurring at a constant temperature of 80 C. Calculate the conversion of reactant A in a CSTR. Round your answer to three decimal places. Data: qo 100 L min-1 Cao = 100 mol L-1 r^--0.02 c^2 (mol L-1 min-1]
It's not 840, 5320, or 6.34
Compare the reactor volume required to achieve 95% contaminant removal efficiency for a CMFR vs. a PFR for the following conditions: steady-state, first-order reaction, flow rate 14 m3/d, and reaction rate coefficient 0.05 d. Your answers should represent the dimensionless ratio VCMER/VPR
Consider an isothermal CSTR, with the liquid phase inlet feed of: Fao 61 mol/hr benzene Vo 10 L/min Diphenyl is synthesized by the following irreversible reaction 2benzene-» diphenyl H2 with the rate law: Tbenzene-kCbenzenek 0.2 L/(mol'min) a. Wirite the stoichiometric table for this reaction. b. What volume CSTR is required for the exit concentration of benzene to be 12 mM? c. What is the extent of reaction? d. What is the conversion of benzene?
Consider an isothermal CSTR, with the...
Hi, can you please help me
with F? I know that if the volume is the same, negative order
reactions would give PFR a higher yield, however, when I tried to
do it mathematically, the units won't match because of the rate
constant. I don't know how to prove that PFR would give a higher
yield. Can i use the same rate constant but with different
units?
3. Your boss asks you to isothermally carry out a liquid-phase, irreversible reaction...
An acid-catalyzed irreversible liquid-phase reaction A B is carried out adiabatically in a CSTR. The reaction is second order in A. The feed is equimolar A and solvent (S, which contains catalyst), and enters the reactor at a total volumetric flow rate of 10 dm3/min at a concentration of A of 4 mol/L. The feed enters at 300 K. The product and reactant heat capacities are 15 cal/(mol°C), the solvent is 18 cal/(mol°C). The reaction rate constant at 300 K...
Reaction is A-->B
is carried out adiabatically in a CSTR. The reaction is second order in A. The feed, which is equal molar in water (which contains the catalyst) and A, enters the reactor at a temperature of 52 C and a total volumetric flow rate of 10 dm3/min. The concentration of A entering the reactor is 4 molar. a) What is the reactor volume to achieve 80% conversion b) What conversion can be achieved in a 1000 dm3 CSTR?...
26. A 2m3 CSTR processes an aqueous feed containing reactant A. This is a second order reaction occurring at a constant temperature of 80 C. Calculate the conversion of reactant A in a CSTR. Round your answer to three decimal places. Data: qo 100 L min-1 Cao = 100 mol L-1 r^--0.02 c^2 (mol L-1 min-1]
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