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Dynamic Model of the Reactor Consider the following Ordinary Differential Equations model of the ammonia reactor: d T f d x = - u S

Dynamic Model of the Reactor
Consider the following Ordinary Differential Equations model of the ammonia reactor:
dTfdx=-uS1WCpf(Tg-Tf)
dTgdx=-uS1WCpg(Tg-Tf)+(-H)S2WCpg
dNN2dx=-
where =f(k1pN2pH21.5pNH3-k2pNH3pH21.5)
k1=1.78954104exp(-20800RTg)
k2=2.57141016exp(-47400RTg)
pN2=286NN22.598NN2,0+2NN2
pH2=3pN2
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(C) Department of Chemical Engineering, University College London, 2024
pNH3=286(2.23NN2,0-2NN2)2.598NN2,0+2NN2
NN2 is the molar flowrate of N2 per area catalyst in kg moles m-2h-1,Tf is temperature of feed gas in K,Tg is
temperature of reacting gas in K,x is reactor length in m. The constant parameters in the model are Cpf(heat
capacity of the feed gas, 0.707kcalkg-1K-1),Cpg(heat capacity of reacting gas, 0.719kcalkg-1K-1), catalyst
activity, 1),H(heat of reaction, -26000kcalkgmolN2,p(partial pressure of a component, psi),R(ideal gas
constant, 1.987kcalkgmol-1K-1),Sl(surface area of catalyst tubes per unit length of reactor, 10m),S2(cross
sectional area of catalyst zone, 0.78m2),u(overall heat transfer coefficient, 500kcalh-1m-2K-1),W(total
mass flowrate, 264000kgh-1).
Q3: Steady-state operation: Assume that the reactor is operating at steady-state, i.e., ODE equations (1)-(3)
and can be replaced by the following algebraic equations:
0=-uS1WCpf(Tg-Tf)
0=-uS1WCpg(Tg-Tf)+(-H)S2WCpg
0=-
Solve these nonlinear algebraic equations for NN2,0=701.2kmolm-2h-1, using the CNS solver in GAMS.
Submit the GAMS (.gms) file and report the solution obtained. Do not submit the .lst file.
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