Reverse flow reactor with integrated partial oxidation

Patent metadata

Field	Value
Publication number	US-12570524-B2
Application number	US-202318499472-A
Country	US
Kind code	B2
Filing date	Nov 1, 2023
Priority date	Nov 2, 2022
Publication date	Mar 10, 2026
Grant date	Mar 10, 2026

Abstract

Systems and methods are provided for performing both reforming and partial oxidation as part of the reaction step of a reaction cycle in a cyclic reaction environment such as a reverse flow reaction environment, where heat is provided by direct heating during a regeneration step. In some aspects, performing a combination of reforming and partial oxidation can allow for higher conversion of hydrocarbons than reforming alone while reducing or minimizing the peak temperatures within the cyclic reaction environment. In some aspects, performing both reforming and partial oxidation can also allow for an improved molar ratio of H 2 to CO in the resulting effluent from the conversion reaction (relative to partial oxidation) while still maintaining high total conversion.

First claim

The invention claimed is:

1 . A method for converting hydrocarbons in a cyclic flow reaction system, comprising:
mixing a fuel flow and a first O 2 -containing flow in a mixing zone of a reactor system to form a mixture comprising an O 2 content of 0.1 vol % or more, the reactor system comprising a reforming zone, a mixing zone adjacent to the reforming zone, and a recuperation zone adjacent to an opposing side of the mixing zone; reacting the mixture to heat one or more surfaces in the reforming zone to a reforming temperature, at least a portion of the reforming zone comprising a reforming catalyst; exposing a reactant stream comprising one or more hydrocarbons to the reforming catalyst in the reforming zone under reforming conditions to form a reforming effluent, a direction of flow of the reactant stream being reversed relative to a direction of flow for the mixture; mixing at least a portion of the reforming effluent with a second O 2 -containing stream in the mixing zone; and exposing the mixture of the at least a portion of the reforming effluent and the second O 2 -containing stream to partial oxidation conditions in the recuperation zone to form a partial oxidation effluent, the partial oxidation effluent comprising 2.0 vol % or less of hydrocarbons.

2 . The method of claim 1 , wherein the reforming conditions comprise a peak temperature in the reforming zone of 1000° C. or less.

3 . The method of claim 1 , wherein a peak temperature in the reforming zone during the reacting the mixture is lower than a peak temperature in the recuperation zone during the exposing the mixture of the at least a portion of the reforming effluent and the second O 2 -containing stream to partial oxidation conditions.

4 . The method of claim 1 , wherein a peak temperature in the recuperation zone during the exposing the mixture of the at least a portion of the reforming effluent and the second O 2 -containing stream to partial oxidation conditions is 1200° C. or more.

5 . The method of claim 1 , wherein the reforming zone comprises a heat sink, the heat sink comprising an average heat sink reforming catalyst density that is 10% or less of an average catalyst density for the reforming zone.

6 . The method of claim 1 , wherein an O 2 content of the second O 2 -containing stream is 5.0% to 30% of a stoichiometric need for combustion of the one or more hydrocarbons in the reactant stream.

7 . The method of claim 1 , wherein the second O 2 -containing stream comprises air.

8 . The method of claim 1 , wherein the second O 2 -containing stream comprises 50 vol % or more combined of CO 2 and O 2 , or wherein the second O 2 -containing stream comprises 25 vol % or less of N 2 , or a combination thereof.

9 . The method of claim 1 , wherein a combined conversion of the one or more hydrocarbons during the exposing the reactant stream and during the exposing the mixture is 98 wt % or more.

10 . The method of claim 1 , wherein the second O 2 -containing stream enters the reactor system in the mixing zone.

11 . The method of claim 1 , wherein a hydrocarbon content of the fuel flow at an end of the reacting is greater than a hydrocarbon content of the fuel flow at a beginning of the reacting.

12 . The method of claim 1 , wherein the reforming conditions comprise conversion of 85 wt % or less of the one or more hydrocarbons.

13 . The method of claim 1 , wherein the partial oxidation effluent comprises a molar ratio of H 2 to CO of 2.2 or more.

14 . The method of claim 1 , wherein the recuperation zone comprises one or more monoliths, the one or more monoliths comprising channels that monotonically increase in size from the end of the regeneration zone at the end of the reaction system to the interface of the regeneration zone with the mixing zone.

15 . A reverse flow reactor system, comprising:
a reaction zone comprising a reforming catalyst and a heat sink, the reaction zone comprising an average reforming catalyst density, the reaction zone further comprising a reactant inlet and a flue gas outlet; a mixing zone adjacent to the reaction zone, the reaction zone comprising at least one reaction zone flow path providing fluid communication between the reactant inlet and the mixing zone; and a recuperation zone adjacent to the mixing zone, the mixing zone providing fluid communication between the reaction zone and the recuperation zone, the recuperation zone comprising a fuel inlet, an oxidant inlet, and a reaction effluent outlet, the recuperation zone comprising at least one recuperation zone flow path providing fluid communication between the fuel inlet and the mixing zone, the recuperation zone further comprising one or more channels for providing fluid communication between the oxidant inlet and the mixing zone that are separate from the at least one flow path, the reactor system comprising a second oxidant inlet and at least one additional flow path providing fluid communication between the second oxidant inlet and the mixing zone, the at least one additional flow path being separate from the at least one reaction zone flow path.

16 . The system of claim 15 , wherein the heat sink comprises a heat sink average reforming catalyst density that is 10% or less of the average catalyst density.

17 . The system of claim 15 , wherein the mixing zone comprises the second oxidant inlet.

18 . The system of claim 15 , wherein the recuperation zone comprises one or more monoliths, an open frontal area of the one or more monoliths varying within the recuperation zone.

19 . The system of claim 15 , wherein the recuperation zone comprises one or more monoliths, the one or more monoliths comprising channels that monotonically increase in cross-sectional area from the end of the regeneration zone at the end of the reaction system to the interface of the regeneration zone with the mixing zone.

20 . The system of claim 15 , wherein the mixing zone comprises one or more mixing structures.

Assignees

• Exxonmobil Technology & Engineering Company

Inventors

• O'Neal Everett J
• Dankworth David C
• Han Lu
• Feicht Sarah E
• Skoulidas Anastasios I

Classifications

• C01B2203/1235

  Hydrocarbons · CPC title

• C01B2203/06

  Integration with other chemical processes · CPC title

• C01B2203/0238

  the reforming step being a carbon dioxide reforming step · CPC title

• B01J19/2485

  Monolithic reactors · CPC title

• B01J19/0066

  Stirrers (mixing per se B01F) · CPC title