CSTR reactor 1) 0 th reactor (CAo=3mol/L, Kf=0.03, time constant=70min) What is the formula for t...
CSTR reactor
1) 0 th reactor (CAo=3mol/L, Kf=0.03, time constant=70min)
What is the formula for the conversion(XA)?
What is concentration(CA)?
2) A=B basic reaction reversible (CAo=3mol/L, Kf=0.03, Kb=0.01, time constant=70min)
What is the formula for the conversion(XA)?
What is concentration(CA)?
3) A=B basic reaction reversible(CAo=3mol/L, Kf=0.03, Kb=0.01)
What is the formula for the equilibrium conversion(XA)?
What is equilibrium concentration(CA)?
4) 1th reaction(-KCA, CAo=3mol/L, K=0.03, time constant=70min)
What is the formula for the conversion(XA)?
What is concentration(CA)?
5) 2th reaction(-KCA^2, CAo=3mol/L, K=0.03, time constant=70min)
What is the formula for the conversion(XA)?
What is concentration(CA)?
Homework Answers
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CSTR reactor 1) 0 th reactor (CAo=3mol/L, Kf=0.03, time constant=70min) What is the formula for t...
For a constant volume batch reactor, solve for the temporal concentration profiles, e.g., CA(t) and CBt)...
For a constant volume batch reactor, solve for the temporal concentration profiles, e.g., CA(t) and CBt) at each initial condition (IC). Given) Reversible elementary reaction kA (forward) B kB (backward) dC - -k^C4kCB dt dC = k,C-k,C B dt k 0.0001(s) k 0.00005(s1) = 0 (mol/dm at t 0, CAo = 0.5 (mol/dm') and CBo IC 1. at t-0, CAO 0.5 (mol/dm2) and CB0 = 0.2 (mol/dm' 2. IC Using any ODE solver, solve the coupled ODES for two initial...
2 of 6 04-Chem-A4/Dec 2012 1. A first-order, homogeneous, liquid-phase reaction (A - B) occurs in...
2 of 6 04-Chem-A4/Dec 2012 1. A first-order, homogeneous, liquid-phase reaction (A - B) occurs in a CSTR that operates adiabatically at steady state. The reaction is exothermic. Data are as follows and should be considered as exact quantities CA G, 1.75 molA/L (Inlet concentration of A) 2.5 J/g-K (The heat capacity of the reacting fluid; assumed constant at all conversions.) AH, -27 000 J/molA q-30 L/min (Flow into the CSTR.) (-rA) = 1.8( 1013)e(-84000 RDCA (The rate of reaction...
1. Pure butanol (A) is fed to a semibatch reactor containing pure ethyl acetate (8) to...
1. Pure butanol (A) is fed to a semibatch reactor containing pure ethyl acetate (8) to produce butyl acetate (C) and ethanol (D). The liquid- phase reaction, A + B ㈠ C + D, is elementary and reversible and is carried out isothermally at 300 K. At this temperature, the equilibrium constant, Kc, is 1.08 and the specific reaction rate, k is 9 x 10 5 L mo s1.Initilly, there is 200 L of ethyl acetate in the reactor, and...
P8-3B The following reactions D ku[CA-CD 1A. 1A. ka [CA-C, T/K take place in a batch...
P8-3B The following reactions D ku[CA-CD 1A. 1A. ka [CA-C, T/K take place in a batch reactor. Additional information: k1 31.0 min-1, K1A 10 k2 100 2A CAO- 1 mol/dm3 (Adapted from a problem by John Falconer, University of Colorado.) (a) Plot and analyze conversion and the concentrations of A, D, and U as a function of time. When would you stop the reaction to maximize the concentration of D? Describe what you find. (b) When does the maximum concentration...
reply ma as soon as possible 120 points total Due: October 23, 2019 Budget your time...
reply ma as soon as possible
120 points total Due: October 23, 2019 Budget your time carefully TRUE OR FALSE (45 points - 3 points cach): Mark whether the statements as written are "true" or "false". If the statement is false, make minor changes to the statement so that the statement is true. The primary adverse health effect resulting from the disposal of mercury wastes into Minamata Bay was dysentery The flow regime in horizontal velocity grit chambers approaches continuous...
For a constant volume batch reactor, solve for the temporal concentration profiles, e.g., CA(t) and CBt) at each initial condition (IC). Given) Reversible elementary reaction kA (forward) B kB (backward) dC - -k^C4kCB dt dC = k,C-k,C B dt k 0.0001(s) k 0.00005(s1) = 0 (mol/dm at t 0, CAo = 0.5 (mol/dm') and CBo IC 1. at t-0, CAO 0.5 (mol/dm2) and CB0 = 0.2 (mol/dm' 2. IC Using any ODE solver, solve the coupled ODES for two initial...
2 of 6 04-Chem-A4/Dec 2012 1. A first-order, homogeneous, liquid-phase reaction (A - B) occurs in a CSTR that operates adiabatically at steady state. The reaction is exothermic. Data are as follows and should be considered as exact quantities CA G, 1.75 molA/L (Inlet concentration of A) 2.5 J/g-K (The heat capacity of the reacting fluid; assumed constant at all conversions.) AH, -27 000 J/molA q-30 L/min (Flow into the CSTR.) (-rA) = 1.8( 1013)e(-84000 RDCA (The rate of reaction...
1. Pure butanol (A) is fed to a semibatch reactor containing pure ethyl acetate (8) to produce butyl acetate (C) and ethanol (D). The liquid- phase reaction, A + B ㈠ C + D, is elementary and reversible and is carried out isothermally at 300 K. At this temperature, the equilibrium constant, Kc, is 1.08 and the specific reaction rate, k is 9 x 10 5 L mo s1.Initilly, there is 200 L of ethyl acetate in the reactor, and...
P8-3B The following reactions D ku[CA-CD 1A. 1A. ka [CA-C, T/K take place in a batch reactor. Additional information: k1 31.0 min-1, K1A 10 k2 100 2A CAO- 1 mol/dm3 (Adapted from a problem by John Falconer, University of Colorado.) (a) Plot and analyze conversion and the concentrations of A, D, and U as a function of time. When would you stop the reaction to maximize the concentration of D? Describe what you find. (b) When does the maximum concentration...
reply ma as soon as possible
120 points total Due: October 23, 2019 Budget your time carefully TRUE OR FALSE (45 points - 3 points cach): Mark whether the statements as written are "true" or "false". If the statement is false, make minor changes to the statement so that the statement is true. The primary adverse health effect resulting from the disposal of mercury wastes into Minamata Bay was dysentery The flow regime in horizontal velocity grit chambers approaches continuous...
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