Method and reactor for pyrolysis conversion of hydrocarbon gases

Patent metadata

Field	Value
Publication number	US-11020719-B2
Application number	US-201916977644-A
Country	US
Kind code	B2
Filing date	Mar 7, 2019
Priority date	Mar 7, 2018
Publication date	Jun 1, 2021
Grant date	Jun 1, 2021

Abstract

A pyrolysis reactor (12) and method for the pyrolysis of hydrocarbon gases (e.g., methane) utilizes a pyrolysis reactor (12) having a unique burner assembly (44) and pyrolysis feed assembly (56) that creates an inwardly spiraling fluid flow pattern of the feed gases to form a swirling gas mixture that passes through a burner conduit (46) with a constricted neck portion or nozzle (52). At least a portion of the swirling gas mixture forms a thin, annular mixed gas flow layer immediately adjacent to the burner conduit (46). A portion of the swirling gas mixture is combusted as the swirling gas mixture passes through the burner conduit (46) and a portion of combustion products circulates in the burner assembly (44). This provides conditions suitable for pyrolysis of hydrocarbons or light alkane gas, such as methane or natural gas.

First claim

We claim:

1. A method of converting light alkanes to pyrolysis products, the method comprising:
providing a pyrolysis reactor comprising:
a pyrolysis reactor vessel having a reactor wall that defines a pyrolysis reaction chamber;
a burner assembly having a burner conduit with a circumferential wall that surrounds a central longitudinal axis and extends from opposite upstream and downstream ends of the burner conduit, the circumferential wall having an annular constricted neck portion located between the downstream and upstream ends of the burner conduit, the downstream end of the burner conduit being in fluid communication with the reaction chamber of the pyrolysis reactor, the upstream end of the burner conduit forming a burner assembly inlet; and
a pyrolysis feed assembly having an annular alkane gas flow space and an annular oxygen gas flow space that discharge into a central mixing chamber that is in fluid communication with the burner assembly inlet;

introducing an alkane-containing gas feed stream of a pyrolysis feed into the annular alkane gas flow space and an oxygen-containing gas feed stream of the pyrolysis feed into the annular oxygen gas flow space so that the alkane-containing gas feed stream and the oxygen-containing gas feed stream pass through said flow spaces perpendicularly to the central longitudinal axis of the burner conduit in an inwardly spiraling fluid flow pattern within said flow spaces that flows about the central longitudinal axis of the burner conduit, with the oxygen-containing gas feed stream from the oxygen gas flow space and alkane-containing gas feed stream from the alkane gas flow space being discharged into the mixing chamber so that the alkane-containing gas and oxygen-containing gas feed streams are mixed together and form a swirling gas mixture within the mixing chamber;
allowing the swirling gas mixture to pass through the burner conduit, with at least a portion of the swirling gas mixture forming a thin, annular mixed gas flow layer immediately adjacent to the burner conduit, and wherein a portion of the swirling gas mixture is combusted as the swirling gas mixture passes through the burner conduit to provide conditions suitable for pyrolysis of the alkane gas from the alkane-containing gas feed stream within the pyrolysis reaction chamber of the reactor vessel, with a portion of the alkane gas being converted to pyrolysis products within the pyrolysis reaction chamber; and
removing pyrolysis products from the reaction chamber of the reactor vessel; and
wherein gas flow through the pyrolysis reactor is at subsonic flow velocities.

2. The method of claim 1 , wherein:
a back flow of flue gases is formed within the pyrolysis reactor that flows upstream and radially inward from the thin, annular mixed gas flow layer along the central longitudinal axis toward the upstream end of the burner conduit.

3. The method of claim 1 , wherein:
the alkane gas of the alkane-containing gas feed stream is a methane gas or natural gas.

4. The method of claim 3 , wherein:
the methane gas or natural gas (NG) of the alkane-containing gas feed stream and oxygen of the oxygen-containing gas feed stream are introduced into the pyrolysis feed assembly in a CH 4 /O 2 or NG/O 2 molar ratio of from 1 to 5.

5. The method of claim 1 , wherein:
pyrolysis products are removed from the reaction chamber and are quenched within a quenching unit.

6. The method of claim 1 , wherein:
the azimuthal-to-radial velocity ratio of each of the alkane-containing gas feed stream and the oxygen-containing gas feed stream within the annular flow spaces is from 0 to 30.

7. The method of claim 1 , wherein:
alkane-containing gas feed stream and the oxygen-containing gas feed stream are each introduced into the respective annular flow spaces in the same rotational direction.

8. The method of claim 1 , wherein:
at least one of the annular alkane gas and oxygen gas flow spaces is provided with circumferentially spaced apart guide vanes oriented to facilitate forming the inwardly spiraling fluid flow pattern within said at least one flow spaces.

9. The method of claim 8 , wherein:
the guide vanes are movable to selected positions to provided selected azimuthal-to-radial velocity ratios of each of the alkane-containing gas feed stream and the oxygen-containing gas feed stream within the annular flow spaces.

10. The method of claim 1 , wherein:
gas flow through the pyrolysis reactor is at flow velocities of from 500 m/s or less.

11. The method of claim 1 , wherein:
the circumferential wall of the burner conduit from the downstream end to the annular constricted neck portion, and optionally an upstream portion of the reactor wall of the pyrolysis reaction chamber that joins the circumferential wall of the burner conduit, is configured as a smooth, continuous wall that follows contour lines of an ellipsoidal cap or spherical cap shape.

12. The method of claim 1 , wherein:
the interior of the reactor wall is a refractory material.

13. The method of claim 1 , wherein:
the annular alkane gas flow space and the annular oxygen gas flow space are defined by planar walls of the pyrolysis feed assembly that are oriented perpendicular to the central longitudinal axis of the burner conduit.

14. The method of claim 1 , wherein:
the annular alkane gas flow space is located at a position along the central longitudinal axis downstream from the annular oxygen gas flow space.

Assignees

• Sabic Global Technologies Bv

Inventors

• Pannala Sreekanth
• Shtern Vladimir
• Chen Lei
• West David

Classifications

• B01J6/008 Primary

  Pyrolysis reactions (of hydrocarbons C10G9/00) · CPC title

• B01J19/2415

  Tubular reactors · CPC title

• B01J4/005

  provided with baffles · CPC title

• C07C2/78

  Processes with partial combustion · CPC title

• B01J19/2405

  provoking a turbulent flow of the reactants, such as in cyclones, or having a high Reynolds-number · CPC title