TY - JOUR
T1 - The determination of global solutions from local ones in catalytic systems showing steady-state multiplicity
AU - Sheintuch, Moshe
PY - 1987
Y1 - 1987
N2 - The problem of constructing the steady-state solutions of the global (in the physical space) system, when local steady-state multiplicity is possible, repeats itself on various scales in heterogeneous catalytic reactors. This work presents a qualitative analysis that classifies this relation according to the physical system, the origin of steady-state multiplicity (thermokinetic, isothermal or truly kinetic) and the shape of the rate curve. A systematic approach for drawing the global observable bifurcation set from the local one is presented. The global features of a catalytic wire exposed to uniform conditions are usually identical to the local ones, i.e. inhomogeneities propagate out of the system. The existence of a global gradient in the adiabatic or isothermal heterogeneous plug-flow reactor or in the heterogeneous model of the catalytic pore adds one or even two stationary-front solutions. The latter problem, which accounts for adsorbate and fluid phases, applies only with truly kinetic multiplicity, and has not been considered earlier in the literature.
AB - The problem of constructing the steady-state solutions of the global (in the physical space) system, when local steady-state multiplicity is possible, repeats itself on various scales in heterogeneous catalytic reactors. This work presents a qualitative analysis that classifies this relation according to the physical system, the origin of steady-state multiplicity (thermokinetic, isothermal or truly kinetic) and the shape of the rate curve. A systematic approach for drawing the global observable bifurcation set from the local one is presented. The global features of a catalytic wire exposed to uniform conditions are usually identical to the local ones, i.e. inhomogeneities propagate out of the system. The existence of a global gradient in the adiabatic or isothermal heterogeneous plug-flow reactor or in the heterogeneous model of the catalytic pore adds one or even two stationary-front solutions. The latter problem, which accounts for adsorbate and fluid phases, applies only with truly kinetic multiplicity, and has not been considered earlier in the literature.
UR - http://www.scopus.com/inward/record.url?scp=0023563627&partnerID=8YFLogxK
U2 - 10.1016/0009-2509(87)85031-5
DO - 10.1016/0009-2509(87)85031-5
M3 - 文章
AN - SCOPUS:0023563627
SN - 0009-2509
VL - 42
SP - 2103
EP - 2114
JO - Chemical Engineering Science
JF - Chemical Engineering Science
IS - 9
ER -