Oxygen storage and catalytic alkane conversion
AssigneeExxonMobil Chemical Patents Inc.
InventorsJuan D. Henao, Paul F. Keusenkothen
Life of this patent
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Abstract
The inventing relates to hydrocarbon conversion, and more particularly to catalytically converting alkane in the presence of oxygen released from an oxygen storage material. Conversion products include C2 hydrocarbon, such as C2+ olefin. The hydrocarbon conversion process can be an oxidative coupling reaction, which refers to the catalytic conversion of methane in the presence of oxidant to produce the olefin product. Flow-through reactors can be used to carry out oxygen storage and the oxidative coupling reaction. Reverse-flow reactors are examples of flow-through reactors, which can be used to carry out oxygen storage and the oxidative coupling reaction.
Claims12
A process for producing a C2+ composition, comprising:
- (a) providing a reverse-flow reactor comprising (i) an oxidative coupling catalyst, (ii) and an oxygen storage material, and (iii) at least one thermal mass;
- (b) during a first time interval,
- i. passing a heating fluid comprising an oxidant and a hydrocarbon fuel through the reverse-flow reactor, wherein the oxidant is present in the heating fluid in a stoichiometric excess of that needed for substantially complete combustion with the hydrocarbon fuel,
- ii. exothermically combusting at least a first portion of the heating fluid's oxygen with the heating fluid's fuel to produce a heated combustion gas, storing at least a second portion of the heating fluid's oxidant with the oxygen storage material, and transferring heat from the heated combustion gas to the thermal mass, and
- iii. lessening or discontinuing the passing of the oxidant and fuel through the reverse-flow reactor;
- and
- (c) during a second time interval,
- i. passing a hydrocarbon reactant comprising methane through the reverse-flow reactor,
- ii. releasing at least a portion of the stored oxygen and reacting at least a portion of the released oxygen with at least a portion of the hydrocarbon reactant's methane in the presence of the oxidative coupling catalyst to produce a reaction mixture comprising a C2+ composition which includes ethane and/or ethylene;
- (d) non-cryogenically separating from the C2+ composition within the reverse-flow reactor at least a portion of the ethane and/or at least a portion of the ethylene, and conducting at least a portion of the separated ethane and/or at least a portion of the separated ethylene away from the reverse-flow reactor.
Dependencies are inferred from the claim text.