초록 ▼

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 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.

대표청구항 ▼

What is claimed as new and desired to be protected by Letters Patent is set forth in the appended claims. 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 c

What is claimed as new and desired to be protected by Letters Patent is set forth in the appended claims. 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.