Selective recovery of c2+ hydrocarbons from natural gas for steam cracker feed in an integrated refinery and steam cracker complex using pressure swing adsorption
US-2015376525-A1 · Dec 31, 2015 · US
US9944872B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9944872-B2 |
| Application number | US-201415107678-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 5, 2014 |
| Priority date | Feb 27, 2014 |
| Publication date | Apr 17, 2018 |
| Grant date | Apr 17, 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 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.
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.
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
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