Advanced oxidative coupling of methane
The present disclosure provides a method for generating higher hydrocarbon(s) from a stream comprising compounds with two or more carbon atoms (C 2+ ), comprising introducing methane and an oxidant (e.g., O 2 ) into an oxidative coupling of methane (OCM) reactor that has been retrofitted into a system comprising an ethylene-to-liquids (ETL) reactor. The OCM reactor reacts the methane with the oxidant to generate a first product stream comprising the C 2+ compounds. The first product stream can then be directed to a pressure swing adsorption (PSA) unit that recovers at least a portion of the C 2+ compounds from the first product stream to yield a second product stream comprising the at least the portion of the C 2+ compounds. The second product stream can then be directed to the ETL reactor. The higher hydrocarbon(s) can then be generated from the at least the portion of the C 2+ compounds in the ETL reactor.
1. A method for generating compounds with two or more carbon atoms (C 2+ compounds), comprising:
(a) directing oxygen (O 2 ) and methane (CH 4 ) into an oxidative coupling of methane (OCM) reactor that reacts said O 2 and CH 4 in an OCM process to yield a product stream comprising (i) C 2+ compounds including ethylene (C 2 H 4 ) and (ii) carbon monoxide (CO) and/or carbon dioxide (CO 2 ); and
(b) directing said product stream from said OCM reactor into a separations system that employs a refrigeration unit having a refrigerant that includes methane from said product stream, to enrich said C 2+ compounds in said product stream.
2. The method of claim 1 , wherein said product stream is directed into said separations system through one or more additional units.
3. The method of claim 1 , further comprising separating methane from said product stream for use in said refrigeration unit.
4. The method of claim 1 , further comprising directing CO and/or CO 2 from said product stream to a methanation reactor that reacts said CO and/or CO 2 to yield a methanation product stream comprising methane.
5. The method of claim 4 , further comprising directing at least a portion of said methane in said methanation product stream to said OCM reactor.
6. The method of claim 1 , further comprising separating said product stream into (i) an ethylene product stream comprising ethylene and (ii) a C 3+ product stream comprising compounds with three or more carbon atoms (C 3+ compounds).
7. The method of claim 1 , further comprising directing ethane from said product stream to said OCM reactor.
8. The method of claim 1 , further comprising, prior to directing said product stream into said separations system, compressing said product stream.