Method for production and upgrading of oil
Abstract
An integrated process for production and upgrading of heavy and extra-heavy crude oil, comprising (a) reforming of hydrocarbons such as natural gas to produce hydrogen, CO2 and steam (b) separating the produced hydrogen from the CO2, steam and any other gases to give a hydrogen rich fraction and a CO2 rich fraction and steam, (c) injecting the steam alone or in combination with the CO2 rich fraction into a reservoir containing heavy or extra heavy oil to increase the oil recovery, and (d) upgrading/refining of the heavy or extra heavy oil to finished products by extensive hydroprocessing, comprising several steps of hydrocracking and hydrotreating (sulfur, nitrogen and metals removal as well as hydrogenation of olefins and aromatics), using the hydrogen rich fraction.
Claims
exact text as granted — not AI-modified1 . An integrated process for production and upgrading of heavy and extra-heavy crude oil, comprising (a) reforming of hydrocarbons to produce gases comprised of hydrogen, CO 2 and steam (b) separating the produced hydrogen from the CO 2 , steam and any other gases to give a hydrogen rich fraction and a CO 2 rich fraction and steam, (c) injecting the steam alone or in combination with the CO 2 rich fraction into a reservoir containing one of heavy or extra heavy oil to increase the oil recovery, and (d) one or both of upgrading and refining of the heavy or extra heavy oil to finished products by extensive hydroprocessing, comprising a plurality of steps of hydrocracking and hydrotreating, using the hydrogen rich fraction.
2 . The process of claim 1 , wherein the reforming in step (a) is steam reforming.
3 . The process of claim 2 , wherein the reforming is performed under supercritical conditions.
4 . The process of claim 1 , wherein the reforming in step (a) is one of autothermal reforming or partial oxidation.
5 . The process of claim 4 , wherein air is used as oxidizer in the autothermal reformer or in the partial oxidation reactor.
6 . The process of claim 3 , comprising the additional step of air separation to produce purified oxygen comprising more than 95%, oxygen, that is used as oxidizer in the reforming.
7 . The process of claim 6 , wherein purified nitrogen co-produced with the purified oxygen is injected into the reservoir together with the CO 2 rich fraction in step (d) to stimulate the oil production.
8 . The process according to claim 7 wherein CO 2 produced during the reforming process is reacted in a water gas shift reaction to produce additional CO 2 and H 2 .
9 . The process according to claim 1 wherein the heavy or extra heavy oil is partially upgraded in the reservoir by hydrogen injection.
10 . The process according to claim 1 wherein the heavy or extra heavy oil is partially upgraded in a downhole upgrading unit.
11 . The process according to claim 1 wherein the heavy or extra heavy oil is upgraded on one of an offshore or onshore upgrading facility, employing particular compact process unit design.
12 . The process according to claim 1 wherein at least a part of the heat to increase recovery of the heavy or extra heavy oil is generated by in-situ combustion.
13 . The process according to claim 1 wherein geothermal heat is used to increase recovery and transport of the heavy or extra heavy oil.
14 . The process of claim 3 comprising the additional step of air separation to produce purified oxygen comprising more than 98% oxygen that is used as oxidizer in the reforming.
15 . The process of claim 1 wherein the hydrocarbon reformed is natural gas.
16 . The process according to claim 15 wherein CO 2 produced during the reforming process is reacted in a water gas shift reaction to produce additional CO 2 and H 2 .
17 . The process according to claim 1 wherein CO 2 produced during the reforming process is reacted in a water gas shift reaction to produce additional CO 2 and H 2 .
18 . The process according to claim 5 wherein CO 2 produced during the reforming process is reacted in a water gas shift reaction to produce additional CO 2 and H 2 .
19 . The process according to claim 7 wherein the heavy or extra heavy oil is partially upgraded in the reservoir by hydrogen injection.
20 . The process according to claim 19 wherein the heavy or extra heavy oil is partially upgraded in a downhole upgrading unit.
21 . The process according to claim 8 wherein the heavy or extra heavy oil is partially upgraded in a downhole upgrading unit.
22 . The process according to claim 7 wherein the heavy or extra heavy oil is upgraded on one of an offshore or onshore upgrading facility employing a compact process unit design.
23 . The process according to claim 21 wherein the heavy or extra heavy oil is upgraded on one of an offshore or onshore upgrading facility employing a compact process unit design.
24 . The process of claim 23 wherein the compact process unit design is compact gas reforming.
25 . The process according to claim 23 wherein at least a part of the heat to increase recovery of the heavy or extra heavy oil is generated by in-situ combustion.
26 . The process according to claim 25 wherein geothermal heat is used to increase recovery and transport of the heavy or extra heavy oil.
27 . The process according to claim 7 wherein at least a part of the heat to increase recovery of the heavy or extra heavy oil is generated by in-situ combustion.
28 . The process according to claim 7 wherein geothermal heat is used to increase recovery and transport of the heavy or extra heavy oil.
29 . The process according to claim 11 wherein the particular compact process unit design is compact gas reforming.Cited by (0)
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