Scalable multiple-inverse diffusion flame burner for synthesis and processing of carbon-based and other nanostructured materials and films and fuels
US-9388042-B2 · Jul 12, 2016 · US
US11175035B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11175035-B2 |
| Application number | US-201716340566-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 10, 2017 |
| Priority date | Oct 10, 2016 |
| Publication date | Nov 16, 2021 |
| Grant date | Nov 16, 2021 |
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Embodiments of the present disclosure describe burner ( 10 ) 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.
Opening claim text (preview).
What is claimed is: 1. A method of controlling secondary reactions of a burner of combustion products using injected methane, the method comprising: establishing a premixed flame from a gas mixture passing through a porous plate or catalytic monolith, with said premixed flame forming a high temperature zone for pyrolysis and being established by a piloted turbulent burner with inhomogeneous inlets and defining three concentric tubes, wherein an outermost tube of the piloted turbulent burner supplies said gas mixture; providing a tube positioner to translate an innermost one of the three concentric tubes to different positions relative to an intermediate tube, wherein the innermost tube supplies a first gas and the intermediate tube supplies a second gas; and controlling the tube positioner to vary the position of the innermost tube in a dynamic manner based on chemical inputs, with said controlling resulting in different levels of mixing of the first gas and the second gas prior to entering the high temperature zone. 2. The method of claim 1 , wherein the innermost tube is a blunt-tipped tube and the gas exiting the innermost tube is methane. 3. The method of claim 1 , wherein oxygen is supplied via the intermediate tube and a combination of methane and oxygen is supplied by the outermost tube. 4. The method of claim 1 , wherein the position of the innermost tube is controlled to facilitate both a methane/oxygen combustion process and subsequent pyrolysis of methane to form olefins, aromatics or nanoparticles. 5. The method of claim 1 , wherein gas flowing through an outermost tube passes through a porous plate or catalytic monolith to ignite the premixed flame. 6. A burner for converting injected methane to olefins, aromatics and nanoparticles/nanomaterials, comprising: a perforated plate through which a coflow gas passes, with a coflow flame established above the plate; a central tube passing through the plate and having a tip through which methane exits, with a jet flame established above the central tube; an exit ring surrounding the plate, with said exit ring establishing a shear boundary of combustion products; 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, wherein the central tube is one of three concentric tubes for gas delivery, including an innermost tube delivering methane, an intermediate tube delivering oxygen, and an outermost tube delivering a mixture of methane and oxygen, with the mixture of methane and oxygen from the outermost tube passing through the perforated plate, and with said innermost tube being translatable within the intermediate tube to vary the position of the tube tip relative to the perforated plate. 7. The burner of claim 6 , wherein the perforated plate includes a porous plate or catalytic monolith.
for use in particular heating operations · CPC title
using perforated plates · CPC title
in the presence of catalytically active bodies, e.g. porous plates · CPC title
Combustion process using hydrogen, hydrogen peroxide water or brown gas as fuel · CPC title
Provision for adjustment of burner position during operation · CPC title
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