Upstream-downstream integrated process for the upgrading of a heavy crude oil with capture of co2 and relative plant for the embodiment thereof
Abstract
The present invention relates to an upstream-downstream integrated process for the upgrading of a heavy crude oil with the capture of CO 2 , comprising the following operative steps: a) production of a heavy crude oil from a reservoir; b) distillation of said heavy crude oil, at atmospheric pressure or under vacuum, with the separation of a distilled fraction and a hydrocarbon residue containing asphaltenes; c) solvent deasphalting of said hydrocarbon residue containing asphaltenes with the formation of a precipitate of asphaltenes and a deasphalted oil (DAO); d1) oxy-combustion of said precipitate of asphaltenes in pure oxygen with the formation of a stream of exhausted gases comprising CO 2 and water vapour; d2) as an alternative to said oxy-combustion, gasification of said precipitate of asphaltenes in pure oxygen with the formation of a stream of syngas which is subsequently transformed into a gas stream comprising CO 2 and H 2 ; e) separation of a substantially pure gaseous stream of CO 2 from said stream of exhausted gases or from said gas stream comprising CO 2 and H 2 ; f) injection of said gaseous stream of CO 2 into the subsoil in order to recover oil or gas, by displacement, from a reservoir and/or to permanently sequester said gaseous stream of CO 2 in a geological formation. The present invention also relates to a plant for the embodiment of the above integrated process.
Claims
exact text as granted — not AI-modified1 . An upstream-downstream integrated process for the upgrading of a heavy crude oil with the capture of CO 2 , comprising the following operative steps:
a. producing a heavy crude oil from a reservoir; b. distilling said heavy crude oil, at atmospheric pressure or under vacuum, to separate a distilled fraction and a hydrocarbon residue containing asphaltenes; c. solvent deasphalting said hydrocarbon residue containing asphaltenes to form a precipitate of asphaltenes and a deasphalted oil (DAO); d1. oxy-combusting of said precipitate of asphaltenes in pure oxygen to form a stream of exhausted gases comprising CO 2 and water vapour; d2. alternatively to said oxy-combustion, gasifying said precipitate of asphaltenes in pure oxygen to form a stream of syngas which is subsequently transformed into a gas stream comprising CO 2 and H 2 ; e. separating a substantially pure gaseous stream of CO 2 from said stream of exhausted gases or from said gas stream comprising CO 2 and H 2 ; f. injecting said gaseous stream of CO 2 into the subsoil in order to recover oil or gas, by displacement, from a reservoir and/or to permanently sequester said gaseous stream of CO 2 in a geological formation.
2 . The process according to claim 1 , further comprising mixing said DAO with at least a part of said distilled fraction to form a reconstituted crude oil.
3 . The process according to claim 1 , wherein said process further comprises producing power by means of the water vapour generated in the oxy-combustion step.
4 . The process according to claim 1 , further comprising injecting water vapour into the subsoil for the displacement of oil from a reservoir.
5 . The process according to claim 1 , wherein the water vapour produced in the oxy-combustion and gasification steps is used for EOR treatment.
6 . The process according to claim 1 , wherein the power produced by the water vapour generated in the oxy-combustion phase, is used for EOR treatment.
7 . The process according to claim 1 , wherein the gaseous stream of CO 2 is injected as displacing fluid into a carbon-bed methane reservoir.
8 . The process according to claim 1 wherein the syngas stream is transformed into a gas stream comprising CO 2 and H 2 by means of a CO-shift reaction.
9 . The process according to claim 1 wherein said solvent is a C 3 -C 6 alkane and/or mixtures thereof.
10 . The process according to claim 1 wherein said gaseous stream of CO 2 is separated from said stream of exhausted gases by cooling the exhausted gas to remove the water present and, optionally, removing the inert gases present.
11 . The process according to claim 1 , wherein the said gaseous stream of CO 2 is permanently sequestered in an exhausted oil or gas reservoir or in a deep reservoir of salt water.
12 . The process according to claim 1 , wherein the H 2 generated in said gasification in pure oxygen of the precipitate of asphaltenes is used in refineries or in upstream-downstream integrated complexes.
13 . A plant for implementing the upstream-downstream integrated process for the upgrading of a heavy crude oil according to claim 1 , comprising:
I) a production well (PP) for producing a heavy crude oil from a reservoir; II) a distillation unit (DF) to distil, at atmospheric pressure or under vacuum, said heavy crude oil with the separation of a distilled fraction and a hydrocarbon residue containing asphaltenes; III). a solvent deasphaltation unit (SDA) for treating said hydrocarbon residue containing asphaltenes with the formation of a precipitate of asphaltenes and a deasphalted oil; IVa) a combustion unit (C) for subjecting said precipitate of asphaltenes to oxy-combustion with the formation of a stream of exhausted gases comprising CO 2 and water vapour; IVb) or, alternatively to the unit defined in IVa), a combustion unit (C) for subjecting said precipitate of asphaltenes to a gasification process in pure oxygen with the formation of a stream of syngas which can be subsequently transformed into a gas stream comprising CO 2 and H 2 ; V) a separation unit (SC) for separating a substantially pure gaseous stream of CO 2 from said exhausted gas stream, or from said gas stream comprising CO 2 and H 2 ; VI) an injection unit (IN) for injecting said gaseous stream of CO 2 or the vapour produced in the process by oxy-combustion, into the subsoil to recover oil or gas, by displacement, from a reservoir and/or for permanently sequestering said gaseous CO 2 stream in a geological formation.Join the waitlist — get patent alerts
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