Surface Catalyzed Reactions
Surface Catalyzed Reactions |
These are heterogeneous reactions. These reactions consist of solid phase catalyst and liquid/gas phase reactants. They take place at the surface of solid catalyst and thus called surface catalyzed reactions. Reactants react in adsorbed form. In below equations “ g” = gaseous phase and “ad” = adsorbed phase. And the catalyst in the very first equation if platinum.
CO(g) + O2(g) → CO2(g)
CO(g) → CO(ad)
O2(g) → O2(ad)
CO(ad) + O2(ad) → CO2(g)
Steps involved in surface catalyzed
reactions
Surface catalyzed reactions takes
place in 5 steps. (It is a complex mechanism)
1) Diffusion of reactants to the
surface of catalyst.
2) Adsorption of reactants at the
surface of catalyst.
3) Reaction between adsorbed reactants.
This step is chemical reaction step.
4) Desorption of product from the
surface.
5) Diffusion of product away from
the surface of catalyst.
Out of these five steps, one is rate
determining step.
If step (3) is slow (rate
determining) then the surface catalyzed reaction is called kinetic controlled reactions or true reactions.
If steps other than (3) are slow (i.e.
rate determining) then the reaction is called diffusion controlled reaction.
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All steps other than (3) are physical processes. Rate of reaction depends upon the concentration of reactants in adsorbed form. Adsorbed concentration of reactant can be expressed in terms of Fraction of catalyst surface covered “θ”.
A → P eq.23.1
A(g) → A(ad)
A(ad) → P(ad)
P(ad) → P(g)
θ = fraction of catalyst surface
covered by reactant
θA fraction of catalyst
surface covered by reactant A
For θ,
adsorption isotherms are
used.
Rate ∝ θA
Rate = k θA eq.23.2
Most common adsorption isotherms
are:
1) Langmuir adsorption isotherm
2) Frendlich adsorption isotherm
3) Tempkin adsorption isotherm.
(4) BET (Brunauer-Emmett-Teller) theory
Here we will discuss Langmuir Adsorption isotherm.
From eq.23.1 we have reactant = A and product = P. The value of θ here is
here b = adsorption equation constant.. Reactants will be adsorbate and Catalyst will be adsorbent. For θA the equation will be
At low pressure for A, 1 + bAPA ~ 1. So eq.23.3 will become
θA = bAPA eq.23.4
Now we can put this value of θA in eq.23.2
Rate = k θA
Rate = k bAPA
Here, k and bA are constants so, KbA = apparent rate constant and can be written as "Kap". Hence eq.23.5 becomes
Integrating the above equation we will get,
Following the integration rule
, the above equation will becomes,
-ln PA = Kap t + z eq.25.6
To find the value of z, consider that if t = 0 then PA= Pi
-ln Pi = Kap (0) = z or z = -ln Pi
Putting the value of z in eq.23.6 we got
-ln PA = Kap t - ln Pi
ln Pi - ln PA = Kap t
ln Pi/PA = Kap t eq.23.7
Above is a rate equation for surface catalyzed reaction. The graphical representation will be
The above discussed method was for systems having one reactants. For systems having more than one reactants we have three cases:
Case I : All reactants in gaseous form
A(g) + B(g) → P
Case II: One reactant in gaseous form and one in liquid form.
A(g) + B(l) → P
Case III: All reactants in liquid form
A(l) + B(l) → P
For these types of reaction there will be two types of mechanism to occur.
1. Langmuir - Hinshelwood Mechanism
Both reactants will react in adsorbed form.
A(g) → A(ad)
B(g) → B(ad)
A(ad) + B(ad) → P
2. Eley Rideal Mechanism
One of the reactant is in adsorbed form and the other in fluid form. The fluid can be gaseous of liquid.
A + B → P
A(g) → A(ad)
A(ad) + B(g) → P
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