The direct conversion
of CH
4
into fuels and chemicals
produces less waste, requires smaller capital investments, and has
improved energy efficiency compared to multistep processes. While
the methane oxychlorination (MOC) reaction has been given little attention,
it offers the potential to achieve high CH
4
conversion
levels at high selectivities. In a continuing effort to design commercially
interesting MOC catalysts, we have improved the catalyst design of
EuOCl by the partial replacement of Eu
3+
by La
3+
. A set of catalytic solid solutions of La
3+
and Eu
3+
(i.e., La
x
Eu
1–
x
OCl, where
x
= 0, 0.25, 0.50, 0.75,
and 1) were synthesized and tested in the MOC reaction. The La
3+
–Eu
3+
catalysts exhibit an increased CH
3
Cl selectivity (i.e., 54–66 vs 41–52%), a lower
CH
2
Cl
2
selectivity (i.e., 8–24 vs 18–34%),
and a comparable CO selectivity (i.e., 11–28 vs 14–28%)
compared to EuOCl under the same reaction conditions and varying HCl
concentrations in the feed. The La
3+
–Eu
3+
catalysts possessed a higher CH
4
conversion rate than
when the individual activities of LaOCl and EuOCl are summed with
a similar La
3+
/Eu
3+
ratio (i.e., the linear
combination). In the solid solution, La
3+
is readily chlorinated
and acts as a chlorine buffer that can transfer chlorine to the active
Eu
3+
phase, thereby enhancing the activity. The improved
catalyst design enhances the CH
3
Cl yield and selectivity
and reduces the catalyst cost and the separation cost of the unreacted
HCl. These results showcase that, by matching intrinsic material properties,
catalyst design can be altered to overcome reaction bottlenecks.