Method of electrolysing hydrogen bromide after h2so4 synthesis

Patent metadata

Field	Value
Publication number	US-2025257477-A1
Application number	US-202318998221-A
Country	US
Kind code	A1
Filing date	Jul 24, 2023
Priority date	Jul 25, 2022
Publication date	Aug 14, 2025
Grant date	—

Abstract

A method of electrolysing hydrogen bromide comprising the steps i) synthesizing sulfuric acid such that hydrogen bromide is produced, ii) providing an electrolytic cell comprising an anode, a cathode, and a membrane sandwiched between the anode and the cathode, iii) feeding a first composition comprising hydrogen bromide and water to the anode, iv) feeding a second composition comprising hydrogen bromide and water to the cathode, and v) operating the electrolytic cell to produce hydrogen at the cathode.

First claim

1 . A method of electrolysing hydrogen bromide comprising the following steps:
i) synthesizing sulfuric acid such that hydrogen bromide is produced, ii) providing an electrolytic cell comprising an anode, a cathode, and a membrane sandwiched between the anode and the cathode, iii) feeding a first composition comprising hydrogen bromide and water to the anode, iv) feeding a second composition comprising hydrogen bromide and water to the cathode, wherein the hydrogen bromide concentration of the second composition is at least 4 mol/kg, and v) operating the electrolytic cell to produce hydrogen at the cathode, wherein the hydrogen bromide produced in step i) is used to prepare the first composition fed in step iii) or both the first composition and the second composition fed in steps iii) and iv).

2 . A method of electrolysing hydrogen bromide comprising the following steps:
(i) providing a stream containing hydrogen bromide obtained from the synthesis of sulfuric acid, ii) providing an electrolytic cell comprising an anode, a cathode, and a membrane sandwiched between the anode and the cathode, iii) feeding a first composition comprising hydrogen bromide and water to the anode, iv) feeding a second composition comprising hydrogen bromide and water to the cathode, wherein the hydrogen bromide concentration of the second composition is at least 4 mol/kg, and v) operating the electrolytic cell to produce hydrogen at the cathode, wherein the stream containing hydrogen bromide provided in step i) is used to prepare the first composition fed in step iii) or both the first composition and the second composition fed in steps iii) and iv).

3 . The method according to claim 1 , wherein the hydrogen bromide concentration of the second composition is ranging from 4 to 10 mol/kg; preferably from 4 to 8 mol/kg.

4 . The method according to claim 1 , wherein the electrolytic cell is operated in step v) at an operational voltage U op of at most 1900 mV, preferably at an operational voltage U op of at most 1700 mV.

5 . The method according to claim 1 , wherein the electrolytic cell is operated in step v) at an operational temperature T op of at least 70° C., wherein T op is below the boiling point of the second composition, preferably at an operational temperature T op ranging from 70° C. to 122° C.

6 . The method according to claim 1 , wherein the first composition and the second composition are both a liquid composition.

7 . The method according to claim 1 , wherein the electrolytic cell is operated at an operational pressure p op which increases from the anode to the cathode.

8 . The method according to claim 1 , wherein the electrolytic cell is operated in step v) at least partially at an operational pressure p op above 0.1 MPa.

9 . The method according to claim 1 , wherein the electrolytic cell is operated in step v) at an operational current density J op of at least 3 kA/m 2 , preferably at an operational current density J op of at least 5 kA/m 2 .

10 . The method according to claim 1 , wherein the membrane is a fluoropolymer membrane having a glass transition temperature T g of at least 110° C. as determined according to DIN EN ISO 11357-2: 2020-08, preferably having a glass transition temperature T g of at least 120° C.

11 . The method according to claim 1 , wherein in step i) nitrogen oxide is converted into nitric acid and/or ammonia is converted into nitrogen.

12 . The method according to claim 1 , wherein in step v) bromine is produced at the anode.

13 . The method according to claim 1 , which does not occur in a flow battery.

14 . The method according to claim 1 , which occurs in the absence of hydrogen fluoride, hydrogen chloride, and/or hydrogen iodide.

15 . The method according to claim 1 is characterized in that the membrane is a fluoropolymer membrane comprising —(CF 2 —CF 2 )— repeat units.

16 . The method according to claim 1 is characterized in that the membrane is a sulfonated fluoropolymer membrane.

Assignees

• Totalenergies Onetech

Inventors

• Kettner Miroslav
• Veryasov Gleb
• Turek Thomas
• Kunz Ulrich
• Grimm Heiner

Classifications

• C01B17/69

  Sulfur trioxide; Sulfuric acid · CPC title

• C01B7/093

  Hydrogen bromide · CPC title

• C25B13/08

  based on organic materials · CPC title

• C25B1/24

  Halogens or compounds thereof · CPC title

• C25B1/04

  by electrolysis of water · CPC title