Oxidative coupling of methane

US11117848B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-11117848-B2
Application numberUS-201816500249-A
CountryUS
Kind codeB2
Filing dateApr 9, 2018
Priority dateApr 10, 2017
Publication dateSep 14, 2021
Grant dateSep 14, 2021

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.

The present invention relates to a process for oxidative coupling of methane (OCM), comprising the steps of: (a) contacting, in a reactor, oxygen and methane with an OCM catalyst, resulting in a reactor effluent comprising ethylene, ethane, methane, carbon dioxide and water; (b) cooling the reactor effluent to obtain a liquid stream comprising water and a gas stream comprising ethylene, ethane, methane and carbon dioxide; (c) removing carbon dioxide from at least a part of the gas stream comprising ethylene, ethane, methane and carbon dioxide resulting in a gas stream comprising ethylene, ethane and methane; (d) passing at least a part of the gas stream comprising ethylene, ethane and methane as obtained in step (c) through a membrane, preferably a membrane comprising metal cations, more preferably a membrane comprising silver (I) ions (Ag+ ions) or copper (I) ions (Cu+ ions), to obtain a stream comprising ethane and a stream comprising ethylene.

First claim

Opening claim text (preview).

That which is claimed is: 1. A process for oxidative coupling of methane (OCM), comprising the steps of: (a) contacting, in a reactor, oxygen and methane with an OCM catalyst, resulting in a reactor effluent comprising ethylene, ethane, methane, carbon dioxide and water; (b) cooling the reactor effluent to obtain a liquid stream comprising water and a gas stream comprising ethylene, ethane, methane and carbon dioxide; (c) removing carbon dioxide from at least a part of the gas stream comprising ethylene, ethane, methane and carbon dioxide resulting in a gas stream comprising ethylene, ethane and methane; (d) passing at least a part of the gas stream comprising ethylene, ethane and methane as obtained in step (c) through a membrane to obtain a stream comprising ethane and methane and a stream comprising ethylene and ethane; (e) feeding the stream comprising ethane and methane as obtained in step (d) to a distillation column to obtain a stream comprising ethane and a stream comprising methane; (f) optionally feeding at least a part of the stream comprising methane as obtained in step (e) to step (a); (g) passing at least a part of the stream comprising ethylene and ethane as obtained in step (d) through a second membrane to obtain a stream comprising ethane and ethylene and a stream comprising ethylene; and (h) optionally feeding at least a part of the stream comprising ethane and ethylene as obtained in step (g) to the membrane used in step (d), or optionally feeding at least a part of the stream comprising ethane and ethylene as obtained in step (g) to step (a). 2. The process according to claim 1 , wherein the membrane comprises metal cations. 3. The process according to claim 2 , wherein the membrane comprises silver(I) ions (Ag+ions) or copper(I) ions (Cu + ions). 4. A process for oxidative coupling of methane (OCM), comprising the steps of: (a) contacting, in a reactor, oxygen and methane with an OCM catalyst, resulting in a reactor effluent comprising ethylene, ethane, methane, carbon dioxide and water; (b) cooling the reactor effluent to obtain a liquid stream comprising water and a gas stream comprising ethylene, ethane, methane and carbon dioxide; (c) removing carbon dioxide from at least a part of the gas stream comprising ethylene, ethane, methane and carbon dioxide resulting in a gas stream comprising ethylene, ethane and methane; (d) passing at least a part of the gas stream comprising ethylene, ethane and methane as obtained in step (c) through a membrane to obtain a stream comprising ethane and methane and a stream comprising ethylene and ethane; (eA) feeding the stream comprising ethane and methane as obtained in step (d) to a Pressure Swing Adsorption (PSA) unit to obtain a stream comprising ethane and a stream comprising methane; and (fA) optionally feeding at least a part of the stream comprising methane as obtained in step (eA) to step (a). 5. The process according to claim 4 , wherein step (d) is followed by the following steps: (gA) passing at least a part of the stream comprising ethylene and ethane as obtained in step (d) through a second membrane to obtain a stream comprising ethane and ethylene and a stream comprising ethylene; and (hA) optionally feeding at least a part of the stream comprising ethane and ethylene as obtained in step (gA) to the membrane used in step (d), that is to say to the first membrane, or optionally feeding at least a part of the stream comprising ethane and ethylene as obtained in step (gA) to step (a). 6. The process according to claim 5 , wherein the second membrane comprises metal cations. 7. The process according to claim 6 , wherein the second membrane comprises silver(I) ions (Ag + ions) or copper(I) ions (Cu + ions). 8. The process according to claim 4 , wherein step (d) is further followed by: (gB) feeding the stream comprising ethylene and ethane as obtained in step (d) to a distillation column to obtain a stream comprising ethane and a stream comprising ethylene; and (hB) optionally feeding at least a part of the stream comprising ethane as obtained in step (gB) to step (a). 9. A process for oxidative coupling of methane (OCM), comprising the steps of: (a) contacting, in a reactor, oxygen and methane with an OCM catalyst, resulting in a reactor effluent comprising ethylene, ethane, methane, carbon dioxide and water; (b) cooling the reactor effluent to obtain a liquid stream comprising water and a gas stream comprising ethylene, ethane, methane and carbon dioxide; (c) removing carbon dioxide from at least a part of the gas stream comprising ethylene, ethane, methane and carbon dioxide resulting in a gas stream comprising ethylene, ethane and methane, wherein at least a part of the gas stream comprising ethylene, ethane and methane is subjected to distillation, resulting in a stream comprising methane and a stream comprising ethylene, ethane and methane, (d)passing at least a part of the gas stream comprising ethylene, ethane and methane as obtained in step (c) through a membrane to obtain a stream comprising ethane and methane and a stream comprising ethylene and ethane; (eA) feeding the stream comprising ethane and methane as obtained in step (d) to a Pressure Swing Adsorption (PSA) unit to obtain a stream comprising ethane and a stream comprising methane; (fA) optionally feeding at least a part of the stream comprising methane as obtained in step (eA) to step (a); and (gC) optionally feeding at least a part of the stream comprising methane as obtained in the distillation to step (a). 10. A process for oxidative coupling of methane (OCM), comprising the steps of: (a) contacting, in a reactor, oxygen and methane with an OCM catalyst, resulting in a reactor effluent comprising ethylene, ethane, methane, carbon dioxide and water; (b) cooling the reactor effluent to obtain a liquid stream comprising water and a gas stream comprising ethylene, ethane, methane and carbon dioxide; (c) removing carbon dioxide from at least a part of the gas stream comprising ethylene, ethane, methane and carbon dioxide resulting in a gas stream comprising ethylene, ethane and methane, wherein at least a part of the gas stream comprising ethylene, ethane and methane is fed to a first Pressure Swing Adsorption (PSA) unit, resulting in a stream comprising methane and a stream comprising ethylene, ethane and methane stream is fed to step (d); (d) passing at least a part of the gas stream comprising ethylene, ethane and methane as obtained in step (c) through a membrane to obtain a stream comprising ethane and methane and a stream comprising ethylene and ethane; (eA) feeding the stream comprising ethane and methane as obtained in step (d) to a second PSA unit to obtain a stream comprising ethane and a stream comprising methane; (fA) optionally feeding at least a part of the stream comprising methane as obtained in step (eA) to step (a); and (gC) optionally feeding at least a part of the stream comprising methane as obtained in the first PSA step to step (a). 11. A process for oxidative coupling of methane (OCM), comprising the steps of: (a) contacting, in a reactor, oxygen and methane with an OCM catalyst, resulting in a reactor effluent comprising ethylene, ethane, methane, carbon dioxide and water; (b) cooling the reactor effluent to obtain a liquid stream comprising water and a gas stream comprising ethylene, ethane, methane and carbon dioxide; (c) removing carbon dioxide from at least a part of the gas stream comprising ethylene, ethane, methane and carbon dioxide resulting in a gas stream comprising ethylene, ethane and methane, wherein at least a part of the gas stream comprising ethylene, ethane and methane is fed to a

Assignees

Inventors

Classifications

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 US11117848B2 cover?
The present invention relates to a process for oxidative coupling of methane (OCM), comprising the steps of: (a) contacting, in a reactor, oxygen and methane with an OCM catalyst, resulting in a reactor effluent comprising ethylene, ethane, methane, carbon dioxide and water; (b) cooling the reactor effluent to obtain a liquid stream comprising water and a gas stream comprising ethylene, ethane,…
Who is the assignee on this patent?
Shell Oil Co
What technology area does this patent fall under?
Primary CPC classification C07C2/84. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Sep 14 2021 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 4 related publications on this page (citations in our corpus or others sharing the same primary CPC).