Method and system for producing methanol using an integrated oxygen transport membrane based reforming system

US9839899B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-9839899-B2
Application numberUS-201615043867-A
CountryUS
Kind codeB2
Filing dateFeb 15, 2016
Priority dateApr 26, 2013
Publication dateDec 12, 2017
Grant dateDec 12, 2017

How to read this patent

A practical reading order for non-experts. Skip the full description unless you need deep technical detail.

  1. Title

    What the patent document calls the invention.

  2. Abstract

    A short plain-language summary of the technical disclosure.

  3. Assignees and inventors

    Who owns or filed the patent and who is credited as inventor.

  4. Key dates

    Filing, priority, publication, and grant dates set the timeline.

  5. First independent claim

    The legal scope of protection — read this for what is actually claimed.

  6. CPC / IPC classifications

    Technology tags used to group this patent with similar filings.

  7. Citations and related patents

    Prior art links and similar publications in this corpus.

Abstract

Official abstract text for this publication.

A method and system for producing methanol that employs an integrated oxygen transport membrane based reforming system is disclosed. The integrated oxygen transport membrane based reforming system carries out a primary reforming process, a secondary reforming process, and synthesis gas conditioning to produce synthesis gas having a desired module of between about 2.0 and 2.2 for a methanol production process thereby optimizing the efficiency and productivity of the methanol plant.

First claim

Opening claim text (preview).

What is claimed is: 1. A system for producing methanol using an oxygen transport membrane based reforming system comprising: an oxygen transport membrane based reforming system configured to reform a combined feed stream of natural gas and steam to produce a synthesis gas stream, wherein said system comprises at least one reforming reactor and at least one oxygen transport membrane reactor in close proximity to said at least one reforming reactor, wherein the oxygen transport membrane reactor comprises one or more oxygen transport membrane tubes wherein said tubes contain both a combustion catalyst and a reforming catalyst disposed therein; a module management system configured to produce a supplemental hydrogen stream from a portion of the produced synthesis gas stream or a portion of a methanol purge stream or both, and wherein a portion of the supplemental hydrogen stream is combined with the produced synthesis gas stream to yield a modified synthesis gas product stream having a module between about 2.0 to 2.2; a duct burner disposed within or proximate to the oxygen transport membrane based reforming system, wherein the duct burner is configured to combust a supplemental fuel stream wherein a portion of said supplemental fuel stream is comprised of synthesis gas generated by the module management system; a methanol synthesis reactor configured to receive the modified synthesis gas product stream and produce crude methanol and the methanol purge stream; and a methanol purification system configured to purify the crude methanol. 2. The system of claim 1 wherein a portion of the supplemental hydrogen stream is combined with the combined feed stream. 3. The system of claim 1 wherein the oxygen transport membrane reactor comprises one or more oxygen transport membrane tubes, wherein said tubes are configured as multilayered dual phase ceramic tubes capable of conducting oxygen ions at an elevated operational temperature. 4. The system of claim 3 wherein said multilayered dual phase ceramic tubes comprise a dense layer, a porous support and an intermediate porous layer capable of conducting oxygen ions at an elevated operational temperature. 5. The system of claim 4 wherein said combustion catalyst is disposed in or proximate to the porous support layer of said ceramic tubs and proximate to the permeate side of the oxygen transport membrane tubes to facilitate reaction of a portion of the reformed synthesis gas stream contacting the permeate side of the oxygen transport membrane tubes with the permeated oxygen stream. 6. The system of claim 5 wherein the retentate side of the oxygen transport membrane tubes is the exterior surface of the ceramic tubes exposed to the heated oxygen containing stream and the permeate side is the interior surface of the ceramic tubes.

Assignees

Inventors

Classifications

  • containing a CO-shift step, i.e. a water gas shift step · CPC title

  • Methanol · CPC title

  • Membrane reactors · CPC title

  • the reforming step being an autothermal reforming step, e.g. secondary reforming processes · CPC title

  • Regenerative adsorption process in two or more beds, one for adsorption, the other for regeneration · CPC title

Patent family

Related publications grouped by family.

External sources

Frequently asked questions

Answers are generated from the same data shown on this page.

What does patent US9839899B2 cover?
A method and system for producing methanol that employs an integrated oxygen transport membrane based reforming system is disclosed. The integrated oxygen transport membrane based reforming system carries out a primary reforming process, a secondary reforming process, and synthesis gas conditioning to produce synthesis gas having a desired module of between about 2.0 and 2.2 for a methanol prod…
Who is the assignee on this patent?
Stuckert Ines C, Chakravarti Shrikar, Drnevich Raymond F, and 1 more
What technology area does this patent fall under?
Primary CPC classification B01J19/2475. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Tue Dec 12 2017 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 9 related publications on this page (citations in our corpus or others sharing the same primary CPC).