Method for regenerating adsorbent media used for extracting natural gas liquids from natural gas

US9944872B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-9944872-B2
Application numberUS-201415107678-A
CountryUS
Kind codeB2
Filing dateAug 5, 2014
Priority dateFeb 27, 2014
Publication dateApr 17, 2018
Grant dateApr 17, 2018

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 is disclosed for the separation of ethane and heavier hydrocarbons or propane and heavier hydrocarbons from natural gas to provide a methane-rich natural gas stream and less volatile natural gas liquids (NGLs). This method provides for the use of a regenerable adsorbent media comprising a porous cross-linked polymeric adsorbent, a pyrolized macroporous polymer, or mixtures thereof, which is regenerated by a pressure swing adsorption (PSA) process, temperature swing adsorption (TSA) process, or combination of the two. Said regeneration step may be operated as a batch process, a semi-continuous process, or preferably as a continuous process.

First claim

Opening claim text (preview).

What is claimed is: 1. A process for separating natural gas liquids from a natural gas feedstream comprising methane and one or more of ethane, propane, butane, pentane, or heavier hydrocarbons, comprising the steps of: (a) providing an adsorbent bed comprising an adsorbent media comprising a porous cross-linked polymeric adsorbent which is a polymer of a monovinyl aromatic monomer crosslinked with a polyvinylidene aromatic compound, wherein said adsorbent media adsorbs ethane, propane, butane, pentane, heavier hydrocarbons, and/or mixtures thereof, (b) passing the natural gas feedstream through the adsorbent bed to provide a methane rich natural gas stream and a loaded adsorbent media, (c) recovering, transporting, liquefying, or flaring the methane rich natural gas stream, (d) regenerating the loaded adsorbent media to release the adsorbed ethane, propane, butane, pentane, heavier hydrocarbons, and/or mixtures thereof, (e) recovering, transporting, liquefying, re-injecting, excluding, by-passing, or flaring the ethane, propane, butane, heavier hydrocarbons, and/or pentane individually and/or as mixtures, and (f) reusing the regenerated adsorbent media in step (b), wherein said passing of the natural gas stream through the adsorbent bed is performed in a pressure swing adsorption (PSA) vessel containing said adsorbent media, a temperature swing adsorption (TSA) vessel containing said adsorbent media, or a PSA vessel in combination with a TSA vessel. 2. The process of claim 1 wherein the steps of the process are performed as a continually repeating cycle of steps in a system comprising a plurality of adsorption vessels which each undergo their respective cycle of steps while collectively operated sequentially in parallel with one another. 3. The process of claim 1 wherein the monovinyl aromatic monomer comprises from 92% to 99.25% by weight of said polymer, and said polyvinylidene aromatic compound comprises from 0.75% to 8% by weight of said polymer. 4. The process of claim 1 wherein the cross-linked macroporous polymeric adsorbent is a polymer of a member selected from the group consisting of styrene, vinylbenzene, vinyltoluene, ethylstyrene, and t-butylstyrene; and is crosslinked with a member selected from the group consisting of divinylbenzene, trivinylbenzene, and ethylene glycol dimethacrylate. 5. The process of claim 4 wherein the cross-linked macroporous polymeric adsorbent has a total porosity of from 0.5 to 1.5 cc/g, a surface area of from 150 to 2100 m 2 /g as measured by nitrogen adsorption, and an average pore diameter of from 10 Angstroms to 100 Angstroms.

Assignees

Inventors

Classifications

  • Surface area, e.g. B.E.T specific surface area · CPC title

  • Polymeric adsorbents · CPC title

  • of sorbents or filter aids comprising organic materials · CPC title

  • Pressure swing adsorption · CPC title

  • being more than 1000 m2/g · 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 US9944872B2 cover?
A method is disclosed for the separation of ethane and heavier hydrocarbons or propane and heavier hydrocarbons from natural gas to provide a methane-rich natural gas stream and less volatile natural gas liquids (NGLs). This method provides for the use of a regenerable adsorbent media comprising a porous cross-linked polymeric adsorbent, a pyrolized macroporous polymer, or mixtures thereof, whi…
Who is the assignee on this patent?
Dow Global Technologies Llc
What technology area does this patent fall under?
Primary CPC classification C10L3/101. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Apr 17 2018 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 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).