Process and systems for carbon-negative and water-positive hydrogen production

Patent metadata

Field	Value
Publication number	US-2024217817-A1
Application number	US-202318392615-A
Country	US
Kind code	A1
Filing date	Dec 21, 2023
Priority date	Dec 29, 2022
Publication date	Jul 4, 2024
Grant date	—

Abstract

The disclosed technology provides processes for producing hydrogen that is renewable, has negative carbon intensity, and is associated with net water production. The hydrogen is economically, environmentally, and socially superior to conventional hydrogen via steam reforming of natural gas or electrolysis of water. Some variations provide a process for manufacturing carbon-negative hydrogen and optionally activated carbon, comprising: feeding biomass into a first heated vessel or zone to generate dried biomass and a first recovered water stream; feeding the dried biomass into a second heated vessel or zone to pyrolyze the dried biomass, generating a biocatalyst and a biogas; feeding the biocatalyst, the first recovered water stream, and biogas to a third heated vessel or zone for biocatalytic conversion, thereby generating H2, CO, and optionally activated carbon; and recovering the hydrogen. The H2 is carbon-negative hydrogen characterized by a carbon intensity less than 0 kg CO2e per metric ton H2.

First claim

What is claimed is:

1 . A system for manufacturing carbon-negative hydrogen, the system comprising:
a first heated vessel or zone configured for drying a biomass and generating dried biomass and a first recovered water stream; a second heated vessel or zone configured for pyrolyzing the dried biomass and generating a biocatalyst and a biogas, wherein the second heated vessel or zone is in flow communication with the first heated vessel or zone; a third heated vessel or zone configured for (i) receiving the biocatalyst, (ii) optionally receiving a first portion of the biogas, and (iii) generating H 2 and CO, wherein the third heated vessel or zone is in flow communication with the second heated vessel or zone, and wherein the third heated vessel or zone comprises means for recovering the H 2 ; and a thermal oxidizer configured for oxidizing at least a portion of the biogas and generating heat, wherein the thermal oxidizer is in thermal communication with the first heated vessel or zone, the second heated vessel or zone, and the third heated vessel or zone, wherein the system is mass-integrated and heat-integrated such that the system is capable of generating carbon-negative hydrogen characterized by a carbon intensity less than 0 kg CO 2 e per metric ton of the H 2 .

2 . The system of claim 1 , wherein the third heated vessel or zone is configured for receiving the first portion of the biogas, and wherein the third heated vessel or zone is configured for converting a portion of the biogas into the H 2 and CO.

3 . The system of claim 1 , wherein the system further comprises a separation unit configured for separating out a second recovered water stream from the biogas.

4 . The system of claim 3 , wherein the third heated vessel or zone is configured with an inlet for receiving the second recovered water stream.

5 . The system of claim 1 , wherein the first heated vessel or zone, the second heated vessel or zone, and the third heated vessel or zone are spatially arranged sequentially such that operation of the system is capable of operating continuously.

6 . The system of claim 1 , wherein the first heated vessel or zone, the second heated vessel or zone, and the third heated vessel or zone are each configured to operate countercurrently with respect to solid and vapor phases.

7 . The system of claim 1 , wherein the first heated vessel or zone, the second heated vessel or zone, and the third heated vessel or zone are each configured as vertical, solids-downflow vessels.

8 . The system of claim 1 , wherein the first heated vessel or zone, the second heated vessel or zone, and the third heated vessel or zone are each configured with an internal vessel lining.

9 . The system of claim 1 , wherein the system further comprises a fourth heated vessel or zone configured for reducing, using the H 2 or the CO, a metal oxide to a pure metal or a less-reduced metal oxide.

10 . The system of claim 9 , wherein the first heated vessel or zone, the second heated vessel or zone, the third heated vessel or zone, and the fourth heated vessel or zone are spatially arranged sequentially such that operation of the system is capable of operating continuously.

11 . The system of claim 1 , wherein the system further comprises a fourth heated vessel or zone configured for reducing a metal oxide, using the biocatalyst, to a pure metal or a less-reduced metal oxide.

12 . The system of claim 11 , wherein the first heated vessel or zone, the second heated vessel or zone, the third heated vessel or zone, and the fourth heated vessel or zone are spatially arranged sequentially such that operation of the system is capable of operating continuously.

13 . The system of claim 1 , wherein the system further comprises a dried-biomass pelletizer configured for pelletizing the dried biomass, and wherein the dried-biomass pelletizer is in flow communication with the first heated vessel or zone and with the second heated vessel or zone.

14 . The system of claim 1 , wherein the system further comprises a biocatalyst pelletizer configured for pelletizing the biocatalyst, and wherein the biocatalyst pelletizer is in flow communication with the second heated vessel or zone and with the third heated vessel or zone.

15 . The system of claim 1 , wherein the system further comprises an electricity generation unit configured to combust a portion of the biogas to generate electricity, and wherein the electricity generation unit configured to supply the electricity to components within the system.

16 . A system for manufacturing carbon-negative hydrogen and activated carbon, the system comprising:
a first heated vessel or zone configured for drying a biomass and generating dried biomass and a first recovered water stream; a second heated vessel or zone configured for pyrolyzing the dried biomass and generating a biocatalyst and a biogas, wherein the second heated vessel or zone is in flow communication with the first heated vessel or zone; a third heated vessel or zone configured for (i) receiving the biocatalyst, (ii) optionally receiving a first portion of the biogas, and (iii) generating H 2 , CO, and activated carbon, wherein the third heated vessel or zone is in flow communication with the second heated vessel or zone, wherein the third heated vessel or zone comprises means for recovering the H 2 , and wherein the third heated vessel or zone comprises means for recovering the activated carbon; and a thermal oxidizer configured for oxidizing a second portion of the biogas and generating heat, wherein the thermal oxidizer is in thermal communication with the first heated vessel or zone, the second heated vessel or zone, and the third heated vessel or zone, wherein the system is mass-integrated and heat-integrated such that the system is capable of generating carbon-negative hydrogen characterized by a carbon intensity less than 0 kg CO 2 e per metric ton of the H 2 .

17 . The system of claim 16 , wherein the third heated vessel or zone is configured for receiving the first portion of the biogas, and wherein the third heated vessel or zone is configured for converting a portion of the biogas into the H 2 and CO.

18 . The system of claim 16 , wherein the system further comprises a separation unit configured for separating out a second recovered water stream from the biogas.

19 . The system of claim 18 , wherein the third heated vessel or zone is configured with an inlet for receiving the second recovered water stream.

20 . The system of claim 16 , wherein the first heated vessel or zone, the second heated vessel or zone, and the third heated vessel or zone are spatially arranged sequentially such that operation of the system is capable of operating continuously.

21 . The system of claim 16 , wherein the first heated vessel or zone, the second heated vessel or zone, and the third heated vessel or zone are each configured to operate countercurrently with respect to solid and vapor phases.

22 . The system of claim 16 , wherein the first heated vessel or zone, the second heated vessel or zone, and the third heated vessel or zone are each configured as vertical, solids-downflow vessels.

23 . The system of claim 16 , wherein the first heated vessel or zone, the second heated vessel or zone, and the third heated vessel or zone are each configured with an internal vessel lining.

24 . The system of claim 16 , wherein the system further comprises a four

Assignees

• Carbon Tech Holdings Llc

Inventors

• Mennell James A
• Daugaard Daren
• Slack Dustin

Classifications

• C21B13/0073

  Selection or treatment of the reducing gases · CPC title

• B01J2219/00045

  Green chemistry · CPC title

• B01J2219/0004

  Processes in series · CPC title

• B01J2219/00033

  Continuous processes · CPC title

• C01B2203/1041

  Composition of the catalyst · CPC title