Use of carboxylates for carbon sequestration, improved oil recovery, and hydrogen storage and reproduction
View Patent ↗Described herein are compositions, techniques, methods, and systems for sequestering carbon, for producing oil, for improved oil recovery, and for storing hydrogen by way of injecting aqueous mixtures into subterranean reservoirs. The aqueous mixtures include one or more carboxylates, which can represent a form of carbon dioxide and/or a form of hydrogen. The aqueous mixtures including carboxylates may also or alternatively be useful for increasing a viscosity of a fluid within the reservoir or modifying the wettability of rock within the reservoir to improve the availability and production of hydrocarbons contained within pores of the rock.
1 . A method for carbon capture and/or storage, the method comprising:
capturing carbon dioxide from the atmosphere or from an industrial process;
converting carbon dioxide to a carboxylate by way of an electroreduction reaction;
obtaining an aqueous mixture comprising water and the carboxylate, wherein a concentration of the carboxylate in the aqueous mixture is from 1 wt. % to 45 wt. %; and
injecting the aqueous mixture comprising the carboxylate into a subterranean reservoir, to thereby capture and/or store carbon in the subterranean reservoir.
2 . The method of claim 1 , wherein the aqueous mixture has a pH within 1 pH unit of an aqueous fluid in the subterranean reservoir.
3 . The method of claim 1 , wherein injecting the aqueous mixture comprises sequestering carbon or carbon dioxide in the form of the carboxylate in the subterranean reservoir.
4 . The method of claim 1 , wherein obtaining the aqueous mixture comprises preparing the carboxylate from a member selected from the group of CO2 gas, carbonate ions, and bicarbonate ions.
5 . The method of claim 1 , wherein obtaining the aqueous mixture comprises adjusting a pH of the aqueous mixture by adding an acid or a base to the aqueous mixture.
6 . The method of claim 1 , wherein the concentration of the carboxylate is within a solubility limit of the carboxylate in the aqueous mixture at a temperature and a pressure of the subterranean reservoir.
7 . The method of claim 1 , wherein the concentration of the carboxylate is above a solubility limit of the carboxylate in the aqueous mixture at a temperature and a pressure of the subterranean reservoir or wherein the aqueous mixture is saturated or a supersaturated solution of the carboxylate.
8 . The method of claim 1 , wherein the aqueous mixture comprises a plurality of different carboxylates, and wherein concentrations of each of the plurality of different carboxylates in the aqueous mixture are from 0.5 wt. % to 44.5 wt. %.
9 . The method of claim 1 , wherein the subterranean reservoir is a member selected from the group consisting of an oil or gas reservoir, a saline aquifer, a fresh water aquifer, a geothermal reservoir, and a cavern.
10 . The method of claim 1 , wherein the aqueous mixture comprises fresh water, seawater, reservoir connate water, produced water, river water, pond water, or brine.
11 . The method of claim 1 , wherein the aqueous mixture or a component thereof contacts rock surfaces in the subterranean reservoir and increases a water wettability character of the rock surfaces, or wherein the aqueous mixture or a component thereof increases a viscosity of a fluid in the subterranean reservoir.
12 . The method of claim 1 , wherein the aqueous mixture further comprises one or more of a surfactant, a solvent, an acid, a base, a salt, an inorganic compound, a polymer, a chelating agent, a nanomaterial, an amino acid, a biocide, a hydrocarbon, nitrogen, or carbon dioxide.
13 . The method of claim 1 , wherein obtaining the aqueous mixture comprises preparing the carboxylate from either (i) CO 2 and water or (ii) carbonate ions together with H 2 O.
14 . The method of claim 1 , wherein obtaining the aqueous mixture comprises preparing the carboxylate from bicarbonate ions and H 2 O using an electrochemical reduction process.
15 . The method of claim 1 , wherein the subterranean reservoir comprises sandstone, carbonate, volcanic rock, or a combination thereof.
16 . The method of claim 1 , wherein the subterranean reservoir comprises one or more minerals including quartz, calcite, carbonate, dolomite, anhydrite, gypsum, feldspar, siderite, zeolites, kaolinite, illite, chlorite, or smectite.
17 . The method of claim 1 , wherein a salinity of the aqueous mixture is greater than or about equal to a salinity of brine in the subterranean reservoir.
18 . The method of claim 1 , wherein a salinity of the aqueous mixture is less than or about equal to a salinity of brine in the subterranean reservoir.
19 . The method of claim 1 , wherein injecting the aqueous mixture comprises storing hydrogen in the form of the carboxylate in the subterranean reservoir, the method further comprising:
producing a fluid from the subterranean reservoir,
wherein the fluid comprises H 2 or
wherein the fluid comprises the carboxylate and the method further comprises generating H 2 using the carboxylate from the fluid, wherein generating the H 2 using the carboxylate comprises dehydrogenating the carboxylate from the fluid.
20 . The method of claim 19 , further comprising generating H 2 in the subterranean reservoir using the carboxylate in the subterranean reservoir, and wherein generating H 2 in the subterranean reservoir comprises injecting catalysts including nano-catalysts or pH modifiers into the subterranean reservoir.
21 . The method of claim 1 , further comprising producing hydrocarbons from the subterranean reservoir; wherein:
a rate of producing the hydrocarbons from the subterranean reservoir is greater after injecting the aqueous mixture as compared to a rate of producing the hydrocarbons from the subterranean reservoir before injecting the aqueous mixture; or
the hydrocarbons comprise crude oil, tarmat, bitumen, kerogen, heavy oil, tight oil, shale oil, gas condensate, wet gas, dry gas, or any combination of these.
22 . The method of claim 21 , wherein producing the hydrocarbons from the subterranean reservoir includes producing the hydrocarbons from one or more wells in the subterranean reservoir, wherein producing the hydrocarbons from the subterranean reservoir includes recovering at least a portion of the aqueous mixture injected into the subterranean reservoir, or wherein the method further comprises producing brine from the subterranean reservoir.
23 . The method of claim 22 , wherein producing the hydrocarbons from the subterranean reservoir includes producing the brine from the subterranean reservoir, wherein the carboxylate is present as a tracer in the brine produced from the subterranean reservoir, or wherein the method further comprises identifying the carboxylate as a tracer in the brine produced from the subterranean reservoir.
24 . The method of claim 21 , wherein injecting the aqueous mixture and producing the hydrocarbons comprises a flooding process or a huff-n-puff process, or wherein injecting the aqueous mixture and producing the hydrocarbons comprises a continuous injection process, a cyclic injection process, or a slug injection process.
25 . A system for carbon capture and or storage, the system comprising:
a capture element for carbon dioxide from the atmosphere or an industrial process;
a vessel for converting carbon dioxide to a carboxylate by an electroreduction reaction;
a source of an aqueous mixture, wherein the aqueous mixture comprises water and the carboxylate, and wherein a concentration of the carboxylate in the aqueous mixture is from 1 wt. % to 45 wt. %; and
an injection system in fluid communication with the source and a subterranean reservoir for injecting the aqueous mixture comprising the carboxylate into the subterranean reservoir, thereby capturing and or storing carbon in the subterranean reservoir.
26 . The system of claim 25 , wherein:
the carboxylate comprises a carboxylic acid, a carboxylate salt, a carboxylate ion, or any combination of these; or
a salinity of the aqueous mixture is from about 0 ppm to about 243000 ppm; or
the aqueous mixture has a pH of from 5 to 9 or a pH within 1 pH unit of an aqueous fluid in the subterranean reservoir; or
the aqueous mixture comprises fresh water, seawater, reservoir connate water, produced water, river water, pond water, or brine; or
the carboxylate is not an amino acid; or
the carboxylate has a formula of:
wherein R is H or a C 1 -C 3 alkyl group, and wherein X is H or an alkali metal; or
the carboxylate is formate, formic acid, acetate, acetic acid, propionate, or propionic acid; or
the subterranean reservoir comprises an oil or gas reservoir, a saline aquifer, a fresh water aquifer, or a geothermal reservoir; or
the source of the aqueous mixture comprises an electrochemical reduction reactor for generating the carboxylate from CO 2 and H 2 O; or
the fluid comprises H 2 ; or
the system further comprises a fluid production system in fluid communication with the subterranean reservoir for producing fluid from the subterranean reservoir, wherein:
the fluid comprises hydrocarbons, or
the fluid comprises the carboxylate and the system further comprises a dehydrogenation reactor in fluid communication with the fluid production system for generating H 2 from the carboxylate in the fluid.