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INTRODUCTION (
abstract of PhD dissertation)
The aim of the research work is to increase the
efficiency of the methane
oxycondensation process and to develop an energy and resource saving technology
for the production of ethylene by catalytic oxycondensation of methane.
The object of research work is natural gas, air, bentonite, ethylene.
The scientific novelty of the research is:
for the first time a catalyst with a new composition (Mn
2
O
3
)
x
∙ (Na
2
MoO
4
)
y
∙
(ZrO
2
)
z
have been created for the process of catalytic oxycondensation of methane,
characterized by reduced coking and having high productivity and selectivity;
the kinetic regularities of the reaction established
under the conditions of a
differential reactor (the rate of change of the initial substances, the kinetic model of
the reaction, the influence of various factors on the conversion rate and the choice
of the optimal process mode), the optimal conditions
for the process were
determined;
the physicochemical foundations of equipping with effective technology and
equipment for the process of methane oxycondensation were created based on the
optimization of the operating parameters of
the membrane reactor;
on the basis of the mechanisms of the methane oxycondensation reaction,
kinetic equations were selected that reflect the processes and the efficiency of the
process in a membrane
adiabatic device was proved;
the optimal technological parameters for the synthesis of ethylene from
methane were determined, as well as this process and the catalyst used were tested
on a semi-industrial equipment at JSC “Navoiazot”, based on the results obtained,
a technological scheme for the synthesis of ethylene from methane was developed.
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