Method for regenerating adsorbent media used for extracting natural gas liquids from natural gas
US-9944872-B2 · Apr 17, 2018 · US
US10011796B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10011796-B2 |
| Application number | US-201414893306-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 5, 2014 |
| Priority date | Aug 6, 2013 |
| Publication date | Jul 3, 2018 |
| Grant date | Jul 3, 2018 |
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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 passing a natural gas feedstream though a regenerable adsorbent media which adsorbs the NGLs to provides the methane rich natural gas product. The regenerable adsorbent media of the present invention is a cross-linked macroporous polymeric adsorbent media.
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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 consisting of the steps of: (a) providing an adsorbent bed consisting of a cross-linked macroporous polymeric adsorbent media, wherein said adsorbent media adsorbs ethane, propane, butane, pentane, heavier hydrocarbons and/or mixtures thereof; (b) passing the natural gas feedstream through the cross-linked macroporous polymeric adsorbent bed to provide a methane rich natural gas stream and a loaded cross-linked macroporous polymeric adsorbent media; (c) recovering, transporting, liquefying, or flaring the methane rich natural gas stream, (d) regenerating the cross-linked loaded macroporous polymeric adsorbent media for reuse by desorbing the adsorbed ethane, propane, butane, pentane, heavier hydrocarbons, and/or mixtures thereof, and (e) recovering, transporting, liquefying, re-injecting, excluding, by-passing, or flaring the ethane, propane, butane, pentane, and heavier hydrocarbons individually and/or as mixtures, wherein the cross-linked macroporous polymeric adsorbent media is in the form of a particle, a bead, or a sphere. 2. The process of claim 1 wherein the cross-linked macroporous polymeric adsorbent is a polymer of a monovinyl aromatic monomer crosslinked with a polyvinylidene aromatic compound. 3. The process in of claim 2 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 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; and the macroporous resin 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.
Aliphatic hydrocarbons · CPC title
Pore size distribution · CPC title
by adsorption, e.g. preparative gas chromatography {(solid sorbent compositions B01J20/00, preparation of inorganic compounds or elements C01)} · CPC title
Adsorption of impurities during preparation or upgrading of a fuel · CPC title
being less than 2 nm, i.e. micropores or nanopores · CPC title
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