Systems and processes for upgrading natural gas liquids from shale gas
Systems and processes for upgrading natural gas liquids (NGL). A natural gas, preferably a shale gas, comprising methane and one or more natural gas liquids can be converted to one or more liquid hydrocarbons. Methane can be separated from the one or more liquid hydrocarbons using a liquid absorbent to provide a first separated stream comprising the methane from the converted stream and a second separated stream comprising the one or more liquid hydrocarbons from the converted stream. At least a portion of the one or more liquid hydrocarbons can be recycled as the liquid absorbent.
1. A process for upgrading natural gas liquids (NGL), comprising:
a) providing a natural gas comprising methane and one or more natural gas liquids;
b) converting at least a portion of the natural gas liquids to one or more liquid hydrocarbons;
c) separating the methane from the one or more liquid hydrocarbons using a liquid absorbent to provide a first separated stream comprising the methane from the converted stream and a second separated stream comprising the one or more liquid hydrocarbons from the converted stream; and
d) recycling at least a portion of the one or more liquid hydrocarbons as the liquid absorbent.
2. The process of claim 1 , wherein the one or more liquid hydrocarbons comprises C2+ alkenes.
3. The process of claim 1 , wherein the one or more liquid hydrocarbons comprises C2+ alkenes derived from the dehydrogenation of the natural gas liquids.
4. The process of claim 3 , wherein the one or more liquid hydrocarbons comprises one or more C4 to C26 oligomers derived from the oligomerization of the C2+ alkenes.
5. The process of claim 1 , wherein the natural gas is derived from shale gas.
6. The process of claim 1 , wherein the natural gas is a sweet and dry natural gas.
7. The process of claim 1 , wherein converting at least a portion of the natural gas liquids to one or more liquid hydrocarbons comprises dehydrogenating any C2+ hydrocarbons in the natural gas to provide one or more C2+ olefins and then oligomerizing the one or more C2+ olefins to provide one or more 4 to C26 oligomers.
8. The process of claim 7 , wherein separating the methane from the one or more liquid hydrocarbons using a liquid absorbent occurs after the dehydrogenation and the oligomerization.
9. The process of claim 7 , wherein separating the methane from the one or more liquid hydrocarbons using a liquid absorbent occurs before the dehydrogenation and the oligomerization.
10. The process of claim 7 , wherein separating the methane from the one or more liquid hydrocarbons using a liquid absorbent occurs after the dehydrogenation and before the oligomerization.
11. The process of claim 10 , wherein the second separated stream is further separated into a light hydrocarbon gas stream that is recycled for dehydrogenation and a concentrated liquid product stream.
12. The process of claim 11 , wherein the second separated stream is separated using a flash drum.
13. The process of claim 11 , wherein the second separated stream is separated using a distillation column.
14. The process of claim 11 , wherein at least a portion of the concentrated liquid product stream is recycled as the absorbent.
15. A process for upgrading natural gas liquids (NGL), comprising:
a) providing a natural gas comprising methane and one or more C 2+ hydrocarbons;
b) dehydrogenating at least a portion of the one or more C 2+ hydrocarbons into one or more C 2+ olefinic hydrocarbons to provide a first converted stream comprising methane and the one or more C 2+ olefinic hydrocarbons;
c) oligomerizing the first converted stream to provide a second converted stream comprising methane and one or more C4 to C26 oligomers;
d) separating the methane from the second converted stream using a liquid absorbent to provide a first separated stream comprising the methane from the second converted stream and a second separated stream comprising the one or more C4 to C26 oligomers from the second converted stream; and
e) recycling at least a portion of the one or more C4 to C26 oligomers as the liquid absorbent.
16. The process of claim 15 , further comprising separating hydrogen from the first separated stream.
17. The process of claim 15 , further comprising separating hydrogen from the second converted stream using the absorbent.
18. The process of claim 1 , wherein the natural gas is derived from shale gas.
19. The process of claim 1 , wherein the natural gas is a sweet and dry natural gas.
20. A process for upgrading natural gas liquids (NGL), comprising:
a) providing a sweet and dry shale gas comprising at least 50 mol % methane and 5 mol % to 40 mol % one or more C 2+ paraffins;
b) dehydrogenating at least a portion of the one or more C 2+ paraffins into one or more C 2+ olefins to provide a first converted stream comprising methane and the one or more C 2+ olefins;
c) oligomerizing the first converted stream to provide a second converted stream comprising methane and one or more C4 to C26 oligomers;
d) absorbing the methane from the second converted stream using a liquid absorbent to provide a first separated stream comprising the methane from the second converted stream and a second separated stream comprising the one or more C4 to C26 oligomers from the second converted stream;
e) separating hydrogen from the methane in the first separated stream;
f) separating gas from the one or more C4 to C26 oligomers in the second separated stream to provide an oligomer product comprising the one or more C4 to C26 oligomers; and
g) recycling at least a portion of the oligomer product as the liquid absorbent.