Burners for conversion of methane to olefins, aromatics, and nanoparticles

US2022018537A1 · US · A1

Patent metadata
FieldValue
Publication numberUS-2022018537-A1
Application numberUS-202117488763-A
CountryUS
Kind codeA1
Filing dateSep 29, 2021
Priority dateOct 10, 2016
Publication dateJan 20, 2022
Grant date

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

Embodiments of the present disclosure describe burner configurations used in an industrial process to convert methane to olefins, aromatics, and nanoparticles/nanomaterials. Both a vitiated coflow burner and piloted turbulent burner with inhomogeneous inlets are disclosed.

First claim

Opening claim text (preview).

What is claimed is: 1 . A burner for converting injected methane to olefins, aromatics and nanoparticles/nanomaterials, comprising: a plate through which a coflow gas passes including a porous plate or catalytic monolith, with a coflow flame established above the plate; a central tube passing through the plate and having a tip through which methane exits; two concentric tubes with an annulus that supplies premixed methane and oxygen via the porous plate or catalytic monolith; a tube positioner for varying an offset height of the tube tip relative to the plate; and a controller for adjusting the offset height of the tube tip based on material inputs or desired output yield. 2 . The burner of claim 1 further comprising an exit collar surrounding the plate, with said exit collar establishing a shear boundary of combustion products. 3 . The burner of claim 1 , wherein the plate includes a catalytic monolith. 4 . The burner of claim 3 , wherein the catalytic monolith is a ceramic monolith coated by catalytic materials. 5 . The burner of claim 3 , wherein the catalytic monolith is a straight-channel monolith. 6 . The burner of claim 1 , wherein the plate includes the porous plate. 7 . The burner of claim 6 , wherein the porous plate is a perforated plate, a porous metal, or a metal screen. 8 . A method of controlling secondary reactions of a burner of combustion products using injected methane, the method comprising: passing a premixed vitiated coflow of gas through a porous plate or catalytic monolith to establish a premixed flame, wherein the porous plate or catalytic monolith is supplied with the premixed vitiated coflow of gas by an annulus of a coflow burner comprising two concentric tubes, wherein the central tube has a tip; establishing a jet flame in coaxial flow of hot combustion products from the premixed flame, said jet flame established by gas exiting from the central tube of the two concentric tubes; providing a tube positioner to translate the tip of the central tube to an offset height relative to the porous plate or catalytic monolith; and controlling the tube positioner to vary the offset height of the tip of the central tube in a dynamic manner based on chemical inputs, with the controlling step resulting in different secondary reactions of the hot combustion products from the premixed flame, with the gas exiting from the central tube. 9 . The method of claim 8 , wherein the central tube is a blunt-tipped tube and the gas exiting the central tube is methane. 10 . The method of claim 8 , wherein the coflow gas is a combination of methane and oxygen. 11 . The method of claim 8 , wherein offset height of the central tube tip is controlled to provide both a methane/oxygen combustion process and subsequent pyrolysis of methane to form olefins, aromatics or nanoparticles. 12 . The method of claim 11 , wherein the pyrolysis of methane forms nanoparticles selected from carbon black and carbon nanotubes. 13 . The method of claim 11 , wherein the pyrolysis of methane forms ethylene or acetylene. 14 . The method of claim 11 , wherein the pyrolysis of methane forms benzene or naphthalene. 15 . The method of claim 8 , wherein the plate includes a catalytic monolith. 16 . The method of claim 15 , wherein the catalytic monolith is a ceramic monolith coated by catalytic materials. 17 . The method of claim 8 , wherein the plate includes the porous plate. 18 . The method of claim 17 , wherein the porous plate is a perforated plate, a porous metal, or a metal screen.

Assignees

Inventors

Classifications

  • F23D99/004Primary

    for use in particular heating operations · CPC title

  • Coating · CPC title

  • Combustion apparatus adapted for incorporating a fuel reforming device · CPC title

  • with fuel supply in stages · CPC title

  • Apparatus in which combustion takes place in the presence of catalytic material (in a fluidised bed of catalytic particles F23C10/01; radiant gas burners using catalysis for flameless combustion F23D14/18) · CPC title

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Frequently asked questions

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What does patent US2022018537A1 cover?
Embodiments of the present disclosure describe burner configurations used in an industrial process to convert methane to olefins, aromatics, and nanoparticles/nanomaterials. Both a vitiated coflow burner and piloted turbulent burner with inhomogeneous inlets are disclosed.
Who is the assignee on this patent?
Univ King Abdullah Sci & Tech
What technology area does this patent fall under?
Primary CPC classification F23D99/004. Mapped technology areas include Mechanical Engineering.
When was this patent published?
Publication date Thu Jan 20 2022 00:00:00 GMT+0000 (Coordinated Universal Time) (A1). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).