IP Library Granted Patent US 12,366,138
Granted Patent B2
US 12,366,138 · App. 17/993,688 · Granted Jul 22, 2025

Hydrogen production, storage and recovery

Inventors: Eva Vinegar (Austin, TX); Harold J. Vinegar (West Lake Hills, TX)
Assignee: TerraH2 LLC
E21B43/006B65G5/00E21B21/068E21B41/0057E21B43/12E21B43/164E21B43/2605E21B49/0875E21B49/088
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 12,366,138
App. No.
17/993,688
Granted
Jul 22, 2025
Kind
B2
Abstract

A method for operating a kerogen-rich unconventional gas reservoir characterized by there being multiple hydraulically-fractured wells drilled thereinto comprises: recovering a methane-containing gas from a first hydraulically-fractured well drilled into the gas reservoir, steam-methane reforming the recovered methane-containing gas to yield a hydrogen gas and an inorganic carbon-containing gas, injecting at least a portion of the hydrogen gas into a second hydraulically-fractured well drilled into the gas reservoir, and injecting at least a portion of the inorganic carbon-containing gas into a third hydraulically-fractured well drilled into the gas reservoir.

Claims (29)

1. A method of storing hydrogen gas in a kerogen-rich geological formation, the method comprising:

a. injecting a fracturing fluid through a horizontal wellbore into the geological formation to cause fracturing within the geological formation;

b. recovering a methane-containing gas through the wellbore, the recovering characterized by a maximum flow rate FLOW MAX ;

c. monitoring a current flow rate FLOW CURRENT of the recovered methane-containing gas over time;

d. determining a flow-rate trigger criterion FLOW TRIGGER at or below which hydrogen injected into the geological formation is subsequently recoverable in a hydrogen-containing gas having an H 2 molar fraction of at least 85%;

e. responsively to and contingent upon the monitored FLOW CURRENT being equal to or below FLOW TRIGGER , ceasing the recovering of the methane-containing gas and injecting a hydrogen gas through the wellbore into the geological formation at a pressure higher than a current shut-in gas pressure at the wellbore; and

f. subsequent to the injecting, recovering, through the wellbore, the hydrogen-containing gas having the H 2 molar fraction of at least 85%.

2. The method of claim 1 , wherein FLOW TRIGGER is equal to at least 10% of FLOW MAX and not more than 20% of FLOW MAX .

3. The method of claim 1 , wherein FLOW TRIGGER is determined based at least in part on a kerogen concentration in the geological formation.

4. The method of claim 1 , wherein FLOW TRIGGER is determined based at least in part on a fluid flow regime of the geological formation.

5. The method of claim 1 , wherein the injecting of the hydrogen gas is at a pressure that is less than a calculated hydrogen fracture extension pressure H2FRAC EXT within the geological formation.

6. The method of claim 1 , wherein the monitoring of the current flow rate FLOW CURRENT includes determining the flow regime in the geological formation.

7. The method of claim 1 , wherein (i) the determining includes determining the flow-rate trigger criterion FLOW TRIGGER at or below which hydrogen injected into the geological formation is subsequently recoverable in a hydrogen-containing gas having an H 2 molar fraction of at least 90%, and (ii) the recovered hydrogen-containing gas has an H 2 molar fraction of at least 90%.

8. The method of claim 1 , wherein the kerogen concentration of the kerogen-rich geological formation is at least 2% by volume.

9. A method of storing and subsequently recovering a hydrogen gas, the method comprising:

a. injecting the hydrogen gas through a horizontal wellbore into a hydraulically-fractured, kerogen-rich, and partially-depleted reservoir of a methane-containing gas, at a pressure higher than a current shut-in gas pressure at the wellbore, the partial depletion of the reservoir being by a methane-containing-gas recovery process characterized by a maximum flow rate of FLOW MAX ,

b. determining a flow-rate trigger criterion FLOW TRIGGER below which hydrogen injected into the reservoir is subsequently recoverable in a hydrogen-containing gas having an H 2 molar fraction of at least 85%; and

c. recovering a portion of the hydrogen gas through the wellbore, the recovered portion of the hydrogen gas having an H 2 molar fraction of at least 85%,

wherein FLOW TRIGGER is equal to at least 10% of FLOW MAX and not more than 20% of FLOW MAX .

10. The method of claim 9 , additionally comprising a step, performed before the injecting of the hydrogen gas, of selecting the reservoir based on a kerogen concentration in the reservoir.

11. The method of claim 9 , additionally comprising a step, performed before the injecting of the hydrogen gas, of selecting the reservoir based on a fluid flow regime of the reservoir.

12. The method of claim 9 , wherein (i) the determining includes determining the flow-rate trigger criterion FLOW TRIGGER at or below which hydrogen injected into the reservoir is subsequently recoverable in a hydrogen-containing gas having an H 2 molar fraction of at least 90%, and (ii) the recovered hydrogen-containing gas has an H 2 molar fraction of at least 90%.

13. The method of claim 9 , wherein the kerogen concentration in the reservoir is at least 2% by volume.

14. A system configured for storing and subsequently recovering a hydrogen-containing gas by performing the method of claim 9 , the system comprising:

a. pumping arrangements for injecting hydrogen-containing gas, disposed in fluid communication with the hydraulically-fractured, kerogen-rich and partially-depleted reservoir of a methane-containing gas and operative to inject the hydrogen gas through a horizontal wellbore into the reservoir at a pressure higher than a shut-in gas pressure at the wellbore; and

b. gas-recovery equipment disposed in fluid communication with the reservoir and operative to recover the portion of the hydrogen-containing gas through the wellbore.

15. The system of claim 14 , wherein the fluid flow regime of the reservoir is substantially characterized by diffusional processes.

16. The system of claim 14 , wherein the fluid flow regime of the reservoir is substantially Knudsen diffusion.

17. The system of claim 14 , additionally comprising equipment for monitored by a delta (C13) isotope ratio in the recovered methane to determine a fluid flow regime in the reservoir.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 11, 2024
From: VINEGAR, EVA; VINEGAR, HAROLD J.
To: TERRAH2 LLC
Reel/Frame 069551/0949 →
Continuity (7)
Continuation 17665707 · Feb 7, 2022
Provisional Application 63301503 · Jan 21, 2022
Provisional Application 63294139 · Dec 28, 2021
Provisional Application 63240961 · Sep 5, 2021
Provisional Application 63195151 · May 31, 2021
Provisional Application 63146847 · Feb 8, 2021
Related Publication 20230167719A1 · Jun 1, 2023
References Cited (58)
US 4709577A · Thompson · 1987 [cited by examiner]
US 5085274A · Puri · 1992 [cited by examiner]
US 7121342B2 · Vinegar · 2006 [cited by examiner]
US 7152675B2 · Heard · 2006 [cited by examiner]
US 8230929B2 · Kaminsky · 2012 [cited by applicant]
US 8760657B2 · Pope · 2014 [cited by examiner]
US 9810064B2 · Garcia · 2017 [cited by examiner]
US 10131593B2 · Okada · 2018 [cited by applicant]
US 11680466B2 · Vinegar et al. · 2023 [cited by applicant]
US 11959364B2 · Vinegar et al. · 2024 [cited by applicant]
US 20040200393A1 · Zauderer · 2004 [cited by applicant]
US 20050109504A1 · Heard · 2005 [cited by applicant]
US 20050220704A1 · Morrow et al. · 2005 [cited by applicant]
US 20090115190A1 · Devine · 2009 [cited by applicant]
US 20090255181A1 · Rhinesmith et al. · 2009 [cited by applicant]
US 20110000133A1 · Rhinesmith et al. · 2011 [cited by applicant]
US 20110223100A1 · Monereau et al. · 2011 [cited by applicant]
US 20110229780A1 · Kershaw · 2011 [cited by applicant]
US 20130240369A1 · McAlister · 2013 [cited by examiner]
US 20140102885A1 · Devine · 2014 [cited by applicant]
US 20140161533A1 · Oates · 2014 [cited by applicant]
US 20140245827A1 · Pope · 2014 [cited by examiner]
US 20150285032A1 · Vinegar et al. · 2015 [cited by applicant]
US 20150321846A1 · Strybos et al. · 2015 [cited by applicant]
US 20160010220A1 · Bower · 2016 [cited by applicant]
US 20160046443A1 · Oates · 2016 [cited by applicant]
US 20160060038A1 · Oates · 2016 [cited by applicant]
US 20160060738A1 · Nagao et al. · 2016 [cited by applicant]
US 20160251217A1 · Fujisawa et al. · 2016 [cited by applicant]
US 20160354622A1 · James · 2016 [cited by applicant]
US 20160354625A1 · James · 2016 [cited by applicant]
US 20170341936A1 · Wasserscheid et al. · 2017 [cited by applicant]
US 20180312935A1 · Nagao et al. · 2018 [cited by applicant]
US 20190219558A1 · Villar De Andrade E Silva · 2019 [cited by examiner]
US 20210404439A1 · Kinsella · 2021 [cited by applicant]
US 20220034448A1 · Meheen et al. · 2022 [cited by applicant]
US 20220064770A1 · Nagao · 2022 [cited by applicant]
US 20220146048A1 · Ewan et al. · 2022 [cited by applicant]
US 20220251935A1 · Vinegar et al. · 2022 [cited by applicant]
US 20230077276A1 · Vinegar et al. · 2023 [cited by applicant]
US 20230160284A1 · Vinegar et al. · 2023 [cited by applicant]
US 20230167719A1 · Vinegar et al. · 2023 [cited by applicant]
US 20230167720A1 · Vinegar et al. · 2023 [cited by applicant]
RU 2493366C2 · 2013 [cited by applicant]
Evans, M. (2016). Unconventional Hydrocarbons and the US Technology Revolution. In R. Grafton, I. Cronshaw, & M. Moore (Eds.), Risks, Rewards and Regulation of Unconventional Gas: A Global Perspective (pp. 59-91). Cambr… [cited by applicant]
Li W, Lu S, Li J, Zhang P, Wang S, Feng W, Wei Y. 2020. Carbon isotope fractionation during shale gas transport: Mechanism, characterization and significance. Science China Earth Sciences, 63: 674-689. [cited by applicant]
Ziarani, A.S., Aguilera, R. Knudsen's Permeability Correction for Tight Porous Media. Transp Porous Med 91, 239-260 (2012). [cited by applicant]
Zhang, T., Ellis, G. S., Ruppel, S. C., Milliken, K., & Yang, R. (2012). Effect of organic-matter type and thermal maturity on methane adsorption in shale-gas systems. Organic geochemistry, 47, 120-131. [cited by applicant]
Londe, L. F. (Dec. 2021). Four Ways to Store Large Quantities of Hydrogen. In Abu Dhabi International Petroleum Exhibition & Conference. OnePetro. [cited by applicant]
Mohammad, A. K., & Sabeeh, N. S. (2018). Comparative study for adsorption of hydrogen-methane mixtures on activated carbon and 5A molecular sieve. Brazilian Journal of Chemical Engineering, 35, 795-804. [cited by applicant]
Ehlig-Economides, Christine , and Dimitrios G. Hatzignatiou. “Blue Hydrogen Economy—A New Look at an Old Idea.” Paper presented at the SPE Annual Technical Conference and Exhibition, Dubai, UAE, Sep. 2021. [cited by applicant]
Wang, X., & Sheng, J. (2017). Gas sorption and non-Darcy flow in shale reservoirs. Petroleum Science, 14(4), 746-754. [cited by applicant]
Osawa, S., Kusumi, S., & Ogino, Y. (1976). Physical adsorption of gases at high pressure: IV. an improvement of DA equation. J. Colloidal Interface Sci, 56, 83-91. [cited by applicant]
Underground Sun Storage: Final Report Public Jan. 13, 2020, Seite 1 von 172. [cited by applicant]
Kobos, Peter Holmes, Lord, Anna Snider, Borns, David James, & Klise, Geoffrey T. A life cycle cost analysis framework for geologic storage of hydrogen : a user's tool . . . United States. https://doi.org/10.2172/1029761… [cited by applicant]
Search report and written opinion of PCT/US22/15486 filed on Feb. 7, 2022 [Search report mailed by the PCT search authority ISA/US on Jun. 24, 2022. [cited by applicant]
RU2493366C2 Machine Translation (by google patents)—published Sep. 20, 2013; BP Exploration Operating Company. [cited by applicant]
Pichler, Assesment of Hydrogen—Rock Interactions During Geological Storage of CH4—H2 Mixtures, Masters thesis; Department Mineral Resources & Petroleum Engineering Chair of Reservoir Engineering; 2013. [cited by applicant]