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koff - LEPA

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Γ /Γ eq<br />

1.0<br />

0.8<br />

0.6<br />

0.4<br />

0.2<br />

0.0<br />

0<br />

2000<br />

4000<br />

Kinetic-Steady state diffusion<br />

Diffusion control<br />

Kinetic-Time dependent<br />

diffusion layer thickness<br />

t /s<br />

6000<br />

8000<br />

10000<br />

Fig. 8. Comparison between stirred and unstirred diffusion controlled reactions . ( K=10 9 M –1 ,<br />

kon=10 6 M –1 ·s –1 , c bulk = 0.1 pM, D=10 –10 m 2 ·s –1 , δ = 100 µm and ! max " 10 #9 mol·m #2 ).<br />

This figure shows that the perturbation theory gives a rather good approximation to the exact<br />

solution eq.(38).<br />

3.4 Steady-state approximation for kinetic-diffusion control - General case<br />

Eq.(26) can be more generally written as<br />

d!(t)<br />

dt<br />

= konc surf ! max ( 1"! ) " <strong>koff</strong>! max! = " J = D<br />

or in terms of surface coverage<br />

d!(t)<br />

dt<br />

= konc surf ( 1!! ) ! <strong>koff</strong>! =<br />

D<br />

!" max<br />

( ) (40)<br />

! cbulk " c surf<br />

c bulk ! c surf ( ) (41)<br />

from which we can as before obtain an expression for the surface concentration<br />

c surf<br />

( )<br />

( )<br />

= cbulk + Da ! / K<br />

1+ Da 1!!<br />

The differential equation (41) now reads<br />

or<br />

d!(t)<br />

dt<br />

=<br />

( )<br />

konc bulk ( + Da<strong>koff</strong> ! ) ( 1!! )<br />

( )<br />

1+ Da 1!!<br />

" 1+ Da 1!! %<br />

$<br />

'd! =<br />

# ! !" ( ! +1)<br />

&<br />

dt<br />

td ( )<br />

! <strong>koff</strong>! = koncbulk !! konc bulk + <strong>koff</strong> 1+ Da 1!!<br />

( )<br />

We can integrate this expression explicitly assuming no initial coverage to get<br />

Da! ! 1+ Da " % " " " +1%<br />

%<br />

#<br />

$ " +1&<br />

' ln 1!!<br />

#<br />

$<br />

#<br />

$ " &<br />

'<br />

&<br />

'<br />

( )<br />

t " +1<br />

=<br />

td (42)<br />

(43)<br />

(44)<br />

12

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