IP Library Granted Patent US 7,687,669
Granted Patent B2
US 7,687,669 · App. 12/273,213 · Granted Mar 30, 2010

Method for direct-oxygenation of alkane gases

Assignee: Gas Technologies LLC
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Quick Facts
Patent No.
US 7,687,669
App. No.
12/273,213
Granted
Mar 30, 2010
Kind
B2
Abstract

A method for alkyl oxygenate (e.g., methanol) manufacture via partial oxidation of alkane (methane) uses an injectively-mixed backmixing reaction chamber in fluid communication with a tubular-flow reactor. Alkyl free radicals are induced in the backmixing reaction chamber prior to being fed through a flow-restriction baffle to the tubular-flow reactor. Injective intermixing of feed streams agitates the backmixing reaction chamber. In one embodiment, a variable position flow restriction baffle is axially moved to commensurately modify the backmixing reaction chamber and tubular-flow reactor volumes. In another embodiment, the tubular-flow reactor is quenched with a variable position quenching input. The method further provides for condensing the output stream from the reaction system in a condensing scrubber and also for recycling a portion of the scrubbed output stream to the reactor system.

Claims (9)

1. A method for producing an alkyl oxygenate, the method comprising:

providing a reactor system comprising an injectively-mixed backmixing reaction chamber comprising a first housing in close coupling to a tubular-flow reactor comprising a second housing, wherein the first housing and the second housing are in slideably-sealed interface;

feeding an alkane-containing gas feed stream and an oxygen-containing gas feed stream to said injectively-mixed backmixing reaction chamber;

inducing alkyl free radical formation in said injectively-mixed backmixing reaction chamber to yield an injectively-mixed backmixing reaction chamber product stream comprising oxygen, said alkane, and at least a portion of said alkyl free radicals;

feeding said injectively-mixed backmixing reaction chamber product stream to said tubular-flow reactor; and

reacting said injectively-mixed backmixing reaction chamber product stream to produce at least one alkyl oxygenate through partial oxidation of said alkane;

wherein said alkane is selected from the group consisting of methane, ethane, propane, and butane.

2. The method of claim 1 further comprising modifying the internal volume of the injectively-mixed backmixing reaction chamber from a first internal volume to a second internal volume.

3. A method as set forth in claim 1 wherein feeding of said oxygen-containing feed stream comprises feeding the oxygen-containing stream into a turbulently mixed annular volume from which mixed reacting gases emerge and are conducted axially past an external surface of a converging conical nozzle section of the reactor system toward a tubular flow reactor section, where the induction period is completed.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 10, 2025
From: GAS TECHNOLOGIES LLC
To: GASTECHNO CORP.
Reel/Frame 071374/0823 →
SECURITY AGREEMENT Recorded Apr 12, 2012
From: GAS TECHNOLOGIES LLC
To: PAWLAK, NATHAN; PAWLAK, PAUL; PAWLAK, BETH
Reel/Frame 028034/0741 →
Continuity (10)
Division 1168586700 · Mar 14, 2007
Continuation In Part PCTUS200700455700 · Feb 19, 2007
Continuation In Part PCTUS200700429700 · Feb 19, 2007
Continuation In Part PCTUS200700418500 · Feb 19, 2007
Continuation In Part 1152682400 · Sep 25, 2006
Continuation In Part 1144637100 · Jun 2, 2006
Continuation In Part 1143269200 · May 11, 2006
Continuation In Part 1135153200 · Feb 10, 2006
Continuation In Part 1131909300 · Dec 27, 2005
Related Publication 20090118553A1 · May 7, 2009