3 Katalytische Performance der Mo/V(/W)-Mischoxide - tuprints

190 Anhang
418MOXO(x)^1+18Acr(x)3CO(x)^1+2H2O(x)^1+4MOX(x)^1, k_co, 0
d/dt Acr(x,t) = Dax * d^2/dx^2 Acr(x,t)
d/dt 18Acr(x,t) = Dax * d^2/dx^2 18Acr(x,t)
d/dt Acs(x,t) = Dax * d^2/dx^2 Acs(x,t)
d/dt 18Acs(x,t) = Dax * d^2/dx^2 18Acs(x,t)
d/dt 1618Acs(x,t) = Dax * d^2/dx^2 1618Acs(x,t)
d/dt H2O(x,t) = Dax * d^2/dx^2 H2O(x,t)
d/dt CO2(x,t) = Dax * d^2/dx^2 CO2(x,t)
d/dt CO(x,t) = Dax * d^2/dx^2 CO(x,t)
d/dt 16O2(x,t) = Dax * d^2/dx^2 16O2(x,t)
d/dt 18O2(x,t) = Dax * d^2/dx^2 18O2(x,t)
d^2/dx^2 Acr(xMax,t) = k_neumann
d^2/dx^2 18Acr(xMax,t) = k_neumann
d^2/dx^2 /dx Acs(xMax,t) = k_neumann
d^2/dx^2 /dx 18Acs(xMax,t) = k_neumann
d^2/dx^2 /dx 1618Acs(xMax,t) = k_neumann
d^2/dx^2 /dx H2O(xMax,t) = k_neumann
d^2/dx^2 /dx CO2(xMax,t) = k_neumann
d^2/dx^2 /dx CO(xMax,t) = k_neumann
d^2/dx^2 /dx 16O2(xMax,t) = k_neumann
d^2/dx^2 /dx 18O2(xMax,t) = k_neumann
Acr(x) + (x) ---> (x), w, PDE:Konvektion
18Acr(x) + (x) ---> (x), w, PDE:Konvektion
Acs(x) + (x) ---> (x), w, PDE:Konvektion
18Acs(x) + (x) ---> (x), w, PDE:Konvektion
1618Acs(x) + (x) ---> (x), w, PDE:Konvektion
H2O(x) + (x) ---> (x), w, PDE:Konvektion
CO2(x) + (x) ---> (x), w, PDE:Konvektion
CO(x) + (x) ---> (x), w, PDE:Konvektion
16O2(x) + (x) ---> (x), w, PDE:Konvektion
18O2(x) + (x) ---> (x), w, PDE:Konvektion