Gas to hydrogen process with co-production of carbon

Patent metadata

Field	Value
Publication number	US-11891706-B2
Application number	US-202117915958-A
Country	US
Kind code	B2
Filing date	Mar 29, 2021
Priority date	Mar 30, 2020
Publication date	Feb 6, 2024
Grant date	Feb 6, 2024

Abstract

The disclosure relates in its first aspect to a process of conversion of a gaseous stream comprising methane into hydrogen ( 51 ) and carbon ( 25 ), the process is remarkable in that it comprises a step (a) of providing a first gaseous stream ( 3, 7 ); a step (b) of bromination and synthesis in which the first gaseous stream ( 3, 7 ) is put in contact with a second stream ( 53 ) comprising bromine resulting in the formation of a third stream ( 15 ) comprising methyl bromides and hydrogen bromide, and of a fourth stream ( 25 ) comprising carbon including graphite and/or carbon black; a step (c) of separation performed on the third stream ( 15 ) to recover a hydrogen bromide-rich stream ( 41 ) which is then oxidized in a step (d) to produce a stream ( 51 ) comprising hydrogen. The second aspect relates to the installation for performing the process of the first aspect and the third aspect concerns the use of bromine in such process.

First claim

The invention claimed is:

1. A process of conversion of gaseous stream comprising methane into hydrogen ( 51 , 63 ) and carbon ( 25 ), said process is characterized in that it comprises the following steps:
a step (a) of providing a first gaseous stream ( 3 , 7 ) comprising methane;
a step (b) of bromination and synthesis of carbon wherein the first gaseous stream ( 3 , 7 ) comprising methane of step (a) is put in contact with a second stream ( 53 , 95 , 127 ) comprising bromine under operating conditions resulting in the formation of a third stream ( 15 ) comprising methyl bromides and hydrogen bromide, and of a fourth stream ( 25 ) comprising carbon including graphite and/or carbon black;
a step (c) of separation performed on the third stream ( 15 ) to recover a hydrogen bromide-rich stream ( 33 , 41 , 107 ) and a methyl bromides-rich stream ( 23 ), wherein the process comprises a step of recycling the methyl bromides-rich stream ( 23 ) into step (b) of bromination and synthesis of carbon; and
a step (d) of converting said hydrogen bromide-rich stream ( 33 , 41 , 107 ) into a stream ( 51 , 63 ) comprising hydrogen and a stream ( 53 , 95 , 127 ) comprising bromine.

2. The process according to claim 1 , characterized in that said step (c) is performed by non-aqueous extraction and in that said step (d) of converting said hydrogen bromide-rich stream ( 33 , 41 ) is performed by electrolysis of said hydrogen bromide-rich stream ( 33 , 41 ).

3. The process according to claim 1 , characterized in that said step (c) is performed by aqueous extraction and in that said step (d) of converting said hydrogen bromide-rich stream ( 107 ) is performed by electrolysis carried out in aqueous phase to produce a stream comprising bromine ( 109 , 127 ).

4. The process according to claim 1 , characterized in that said step (c) is performed by non-aqueous extraction and in that said step (d) of converting said hydrogen bromide-rich stream ( 41 ) is carried out in presence of an oxygen stream ( 62 ), to produce a bromine-rich stream ( 69 , 91 , 95 ).

5. The process according to claim 4 , wherein said step (d) of converting said hydrogen bromide-rich stream ( 33 , 41 , 107 ) into a stream ( 51 , 63 ) comprising hydrogen and a stream ( 53 , 95 , 127 ) comprising bromine further produces thermal energy ( 55 ), further wherein said thermal energy ( 55 ) is converted into electrical energy ( 79 ).

6. The process according to claim 5 , characterized in that said electrical energy ( 79 ) is used in an electrolysis reaction of water to produce a hydrogen stream ( 63 , 67 ) and/or an oxygen stream ( 62 ) which is optionally used in said step (d) of converting said hydrogen bromide-rich stream ( 33 , 41 , 107 ) into a stream ( 51 , 63 ) comprising hydrogen and a stream ( 53 , 95 , 127 ) comprising bromine.

7. The process according to claim 1 , characterized in that step (c) of separation comprises at least one step of separation of hydrogen bromide to produce a hydrogen bromide-rich stream ( 27 ), wherein said hydrogen bromide-rich stream ( 27 ) is subjected to one or more further steps of separation.

8. The process according to claim 1 , characterized in that the operating conditions of step (b) include one or more of a temperature ranging from 500° C. to 1000° C., a pressure ranging from 0.1 MPa to 2.0 MPa, and being performed without catalyst.

9. The process according to claim 1 , characterized in that step (c) of separation is performed at a temperature lower than the temperature used in step (b) of bromination and synthesis of carbon.

10. The process according to claim 1 , characterized in that step (c) of separation comprises at least one step of separation of a stream ( 39 ) comprising unreacted methane.

11. The process according to claim 1 , characterized in that the process comprises a step of recycling the stream ( 53 , 95 , 127 ) comprising bromine obtained in step (d) into step (b) of bromination and synthesis of carbon.

12. The process according to claim 1 , characterized in that step (a) of providing a first gaseous stream ( 3 ) comprising methane comprises providing a natural gas comprising methane at a content of at least 75 mol. % of the total molar content of said natural gas.

13. The process according to claim 1 , characterized in that step (a) of providing a first gaseous stream ( 3 ) comprising methane comprises providing natural gas and purifying the natural gas to remove one or more selected from sulphur, nitrogen, water, oxygen and carbon dioxide.

14. The process according to claim 1 , characterized in that in step (b) comprises a carbonization step performed on the fourth stream at a temperature ranging from 500° C. to 3500° C.

Assignees

• Totalenergies Onetech
• Sulzer Management Ag

Inventors

• Coupan Romuald
• Nesterenko Nikolai
• Veryasov Gleb

Classifications

• B01D3/009

  in combination with chemical reactions · CPC title

• B01J8/02

  with stationary particles, e.g. in fixed beds · CPC title

• B01J8/24

  according to "fluidised-bed" technique (B01J8/20 takes precedence) · CPC title

• C07C17/10

  of hydrogen atoms (combined with addition of halogens to unsaturated hydrocarbons C07C17/06) · CPC title

• C01B32/205

  Preparation · CPC title