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The reaction between ammonia and formaldehyde to produce hexamine is
4NH3 + 6 HCHO ->(CH2)6N4 + 6 H2O
A 0.5 liter CSTR is used for the reaction. Each reactant is fed to the reactor in a separate stream, at the rate of 1.5x10-3 liter/s each. The ammonia concentration is 4.0 mol/liter and the formaldehyde concentration is 6.4 mol/liter. The reactor temperature is 36C. Calculate the concentration of ammonia and formaldehyde in the effluent stream. In kinetics below A is ammonia and B is formaldehyde.
(-rA) = kCACB^2 mole A/liter-s where k = 1,420 exp (-3090/T)
Find out the limiting reactant of the reaction
From the stoichiometry of the reaction
4 mol/L NH3 require = 6 mol/L HCHO
But we have 6.4 mol/L of HCHO
NH3 is the limiting reactant
A = NH3
B = HCHO
Rate constant k = 1,420 exp (-3090/T)
k = 1,420 exp (-3090/(36+273))
= 0.06446 mol2 L-2 s-1
(-rA) = kCACB^2
(-rA) = kCA0(1-X)[CB0 - 1.5 CA0 X]2
(-rA) = 0.06446 * 4 *(1-X)*[6.4 - 1.5 * 4 * X]2
(-rA) = 0.25784 *(1-X)*[6.4 - 6 * X]2
Molar flow rate of A
FA0 = CA0 * vA = 4 mol/L x 1.5x 10^-3 L/s
= 0.006 mol/s
Design equation for CSTR
V/FA0 = X/-rA
0.5/0.006 = X/(0.25784 *(1-X)*[6.4 - 6 * X]2)
21.486 = X/[(1-X)*(40.96 + 36X2 - 76.8X)]
21.486*[(1-X)*(40.96 + 36X2 - 76.8X)] = X
21.486*[40.96 + 36X2 - 76.8X - 40.96X - 36X3 + 76.8X2] = X
880.06 + 2423.6208X2 - 1649.1248 X - 773.496X3 = 0
X = 0.34
Concentration of NH3 in effluent stream
CA = CA0(1-X)
= 4(1-0.34) = 2.64 mol/L
Concentration of HCHO in effluent stream
CB = CBO - 1.5CA0(X)
= 6.4 - 1.5*4*0.34
= 4.36 mol/L