Methane pyrolysis using stacked fluidized beds

Patent metadata

Field	Value
Publication number	US-12358788-B2
Application number	US-202117236418-A
Country	US
Kind code	B2
Filing date	Apr 21, 2021
Priority date	Apr 23, 2020
Publication date	Jul 15, 2025
Grant date	Jul 15, 2025

Abstract

Systems and methods are provided for conversion of methane and/or other hydrocarbons to hydrogen by pyrolysis while reducing or minimizing production of carbon oxides. The conversion of hydrocarbons to hydrogen is performed in one or more pyrolysis or conversion reactors that contain a plurality of sequential fluidized beds. The fluidized beds are arranged so that the coke particles forming the fluidized bed move in a counter-current direction relative to the gas phase flow of feed (e.g., methane) and/or product (H 2 ) in the fluidized beds. By using a plurality of sequential fluidized beds, the heat transfer and management benefits of fluidized beds can be realized while also at least partially achieving the improved reaction rates that are associated with a plug flow or moving bed reactor.

First claim

The invention claimed is:

1. A method for reforming hydrocarbons, comprising:
contacting a hydrocarbon-containing feed with a first portion of coke particles in a first group of fluidized beds to form a heated hydrocarbon-containing feed, the hydrocarbon-containing feed being sequentially passed into each fluidized bed of the first group of fluidized beds;
contacting the heated hydrocarbon-containing feed with a second portion of coke particles in a second group of fluidized beds comprising one or more fluidized beds operating under pyrolysis conditions to form a hydrogen-containing effluent, the one or more fluidized beds operating under pyrolysis conditions being externally heated, the heated hydrocarbon-containing feed comprising 75 vol % or more of C 1 -C 4 alkanes;
contacting the hydrogen-containing effluent with a third portion of coke particles in a third group of fluidized beds to form a cooled hydrogen-containing effluent, the hydrogen-containing effluent being sequentially passed into each fluidized bed of the third group of fluidized beds;
flowing the first portion of coke particles, the second portion of coke particles, and the third portion of coke particles in a counter-current direction to a flow direction of at least one of the hydrocarbon-containing feed and the hydrogen-containing effluent, a fraction of the third portion of coke particles being passed into the second group of fluidized beds, a fraction of the second portion of coke particles being passed into the first group of fluidized beds;
passing a recycle fraction of the first portion of coke particles into the third group of fluidized beds,
wherein a temperature of at least one fluidized bed in the first group of fluidized beds is lower than a temperature of a downstream adjacent fluidized bed, and
wherein a temperature of at least one fluidized bed in the third group of fluidized beds is lower than a temperature of an adjacent upstream fluidized bed.

2. The method of claim 1 , wherein a temperature of each fluidized bed in the first group of fluidized beds is lower than a temperature of a downstream adjacent fluidized bed, and wherein a temperature of each fluidized bed in the third group of fluidized beds is lower than a temperature of an adjacent upstream fluidized bed.

3. The method of claim 1 , wherein the second group of fluidized beds comprises a plurality of fluidized beds operating under pyrolysis conditions.

4. The method of claim 1 , wherein passing a recycle fraction of the first portion of coke particles into the third group of fluidized beds comprises:
passing the recycle fraction of the first portion of coke particles into a coke particle reservoir; and
passing the recycle fraction of the first portion of coke particles from the coke particle reservoir to the third group of fluidized beds.

5. The method of claim 1 , wherein passing a recycle fraction of the first portion of coke particles into the third group of fluidized beds comprises:
pneumatically transporting the recycle fraction of the first portion of coke particles using a pneumatic transport gas; and
separating the recycle fraction of the first portion of coke particles from the pneumatic transport gas.

6. The method of claim 5 , further comprising separating at least a portion of the pneumatic transport gas from the hydrogen-containing effluent prior to the pneumatically transporting.

7. The method of claim 6 , further comprising combining at least a portion the pneumatic transport gas with the hydrogen-containing effluent after the pneumatically transporting.

8. The method of claim 1 , wherein the first group of fluidized beds comprises a first fluidized bed that is upstream adjacent to a fluidized bed in the second group of fluidized beds, and wherein at least a portion of the hydrocarbon-containing feed is converted to hydrogen and carbon in the first fluidized bed.

9. The method of claim 1 , wherein the third group of fluidized beds comprises a second fluidized bed that is downstream adjacent to a fluidized bed in the second group of fluidized beds, wherein the hydrogen-containing effluent comprises C 1 -C 4 hydrocarbon, and wherein at least a portion of the C 1 -C 4 hydrocarbon is converted to hydrogen and carbon in the second fluidized bed.

10. The method of claim 1 , wherein the hydrocarbon-containing feed comprises methane, natural gas, or a combination thereof.

11. The method of claim 1 , wherein the hydrocarbon-containing feed comprises 95 vol % or more of C 1 -C 4 alkanes.

12. The method of claim 1 , wherein the one or more fluidized beds of the second group of fluidized beds are externally heated using electrical resistance heating, induction heating, plasma heating, or a combination thereof.

13. The method of claim 1 , wherein the one or more fluidized beds of the second group of fluidized beds are externally heated using heating tubes, a heated fluid within the heating tubes being heated by combustion of a portion of the hydrogen-containing effluent.

14. The method of claim 1 , wherein the first group of fluidized beds, the second group of fluidized beds, and the third group of fluidized beds comprise sequential fluidized beds.

15. The method of claim 1 , wherein the heat capacity of a flow of coke particles into one or more fluidized beds of the first group of fluidized beds is substantially equal to a heat capacity of a flow of hydrocarbon-containing feed into the one or more fluidized beds of the first group of fluidized beds; or wherein a heat capacity of a flow of coke particles into one or more fluidized beds of the third group of fluidized beds is substantially equal to a heat capacity of a flow of the hydrogen-containing effluent in the one or more fluidized beds of the third group of fluidized beds; or a combination thereof.

16. The method of claim 1 , wherein the second group of fluidized beds comprises at least one fluidized bed that is not externally heated.

17. The method of claim 1 , wherein the heated hydrocarbon-containing feed comprises 95 vol % or more of C 1 -C 4 alkanes.

18. The method of claim 1 , wherein the heated hydrocarbon-containing feed comprises 10 vol % or less of N 2 .

Assignees

• Exxonmobil Technology & Engineering Company

Inventors

• Gupta Ramesh
• Caram Hugo S
• Kovvali Anjaneya S
• Raman Sumathy
• Dankworth David C

Classifications

• C01B3/28 Primary

  using moving solid particles, e.g. fluidised bed technique · CPC title

• C01B2203/0272

  containing a non-catalytic decomposition step · CPC title

• B01J2208/00327

  by direct heat exchange · CPC title

• B01J2208/00176

  outside the reactor · CPC title

• C01B2203/0872

  Methods of cooling · CPC title