Environmental Engineering Reference
In-Depth Information
limited because it requires eight electrons to fully oxide carbon in CO
2
to
methane, which requires catalysts to achieve acceptable rates and selectivi-
ties [48]. Common catalysts for this reaction include Ni, Ru, and Rh sup-
ported on various oxides such as SiO
2
, TiO
2
, Al
2
O
3
, and CeO
2
. Figure 6.15
shows representative TEM and EDS images of Pd-Mg/SiO
2
catalysts [48].
The results show that the as-synthesized Pd-Mg/SiO
2
catalyst after calcina-
tion at 550°C in air for 6 hours contains well-dispersed electron-dense par-
ticles identified as containing Pd by EDS within a matrix of less dense,
noncrystalline silica shells, with a certain degree of aggregation of Pd par-
ticles. After reaction with CO
2
and hydrogen for 10 hours, the particles
remain well dispersed even though more larger Pd particles appeared, indi-
cating sintering of some particles that are probably not fully encapsulated by
the Mg/Si oxide.
The reaction mechanism is still not well established and the proposed
mechanisms fall into two general categories. The first one involves the con-
version of CO
2
to CO before methanation [49-51], while the second one
involves direct hydrogenation of CO
2
to methane without forming CO as an
intermediate [52, 53]. Even for mathanation of CO, there is no consensus on
the kinetics and mechanism. It has been suggested that the rate-limiting step
is either the formation of a CH
x
O intermediate and its hydrogenation or the
formation of surface carbon via CO dissociation and its interaction with
hydrogen [51, 54].
To gain insight into the reaction mechanism, it is useful to determine
reaction intermediates. For instance, kinetic studies based on steady-state
transient measurements conducted on Ru/TiO
2
catalyst have identified
several reaction intermediates [50]. Hydrogenation of CO as a key intermedi-
ate leads to methane formation. Formates, as intermediates for CO formation,
are bound strongly on the support in equilibrium and become active
species at the metal and support interface. A proposed mechanism for
the formation of the formate thorough a carbonate species is shown in
Figure 6.16.
Similarly, other hydrocarbons can be produced based on reaction between
CO
2
and hydrogen. The reactions are often divided into two categories:
methanol mediated and nonmethanol mediated. In the methanol-mediated
approach, CO
2
and H
2
react over Cu-Zn-based catalysts to produce metha-
nol, which is subsequently converted into other hydrocarbons such as gaso-
line. Light alkanes are usually generated as major products due to further
catalytic hydrogenation of the alkenes. In the nonmethanol-mediated
approach, CO
2
hydrogenation proceeds in two steps: RWGS reaction, which
converts CO
2
into CO, and then the Fisher-Tropsch (FT) reaction, which
converts CO into hydrocarbons via further hydrogenation.
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