“…The forward flux and reverse flux in the other steps are both extreme ly large. For pr~ctical purposes , eq ua tions (5.5), (5,6) and (5,8) are approxi mated: 128 Simultaneous solution fo r each e-term is performed, followed by substi t ution in equation (5,3), which becomes: · k! .k 3 .k 5 ,k 7 .xH 2 Si -k 2 , k 4 .k6,k 8 ,aSi .xH 2 i Flux = --------------------------------------------------k3.k6,k7.aSi+k3,k5.k8,xH2i+k4.k6.k8,xH2i' If the ove ral I ra t e of tra ns fe r is control led by th e rate of the c hem ical reaction, a similar argumen t to that for the adso r ptio n step above may be appli e d, Equation (5,5) Evaluate the 6 1 s and substitute in the equation for the flux, C.kg,k 1 ,k 3 ,k 5 .k 7 ,xH 2 S 00 -C,kg.k 2 .k 4 .k 6 ,k 8 ,a 500 ,xH 2 oo If the resistance is high in the gas or I iquid phase, the same argume nt applied in Appendix 2 may be employed in the i~termediate steps.…”