Separation of hydrocarbons using regenerable macroporous alkylene-bridged adsorbent

US2017368494A1 · US · A1

Patent metadata
FieldValue
Publication numberUS-2017368494-A1
Application numberUS-201615536329-A
CountryUS
Kind codeA1
Filing dateJan 6, 2016
Priority dateJan 27, 2015
Publication dateDec 28, 2017
Grant date

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Abstract

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A method for separating natural gas liquids (NGLs) from a hydrocarbon gas mixture containing natural gas liquids and methane, comprising the steps of: i) providing a bed of adsorbent selective for NGLs over methane; ii) passing a hydrocarbon gas mixture containing methane and NGL through the bed of adsorbent to at least partially remove NGLs from the gas mixture to produce: (a) NGL-loaded adsorbent and (b) NGL-depleted hydrocarbon gas mixture; iii) recovering the NGL-depleted hydrocarbon gas mixture; iv) regenerating the NGL-loaded adsorbent by at least partially removing NGLs from the adsorbent; and v) sequentially repeating steps (ii) and (iii) using regenerated adsorbent from step (iv).

First claim

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1 - 10 . (canceled) 11 . A method for separating methane or ethane from a hydrocarbon gas mixture comprising methane or ethane, or a combination of methane and ethane, along with C3 and heavier paraffins, wherein the method comprises the steps of: i) providing a bed of a macroporous alkylene-bridged adsorbent selective for C 3 and heavier paraffins over methane and ethane; ii) passing a hydrocarbon gas mixture through the bed of adsorbent to at least partially remove C 3 and heavier paraffins from the gas mixture to produce: (a) C 3 and heavier paraffins-loaded adsorbent and (b) C 3 and heavier paraffins-depleted hydrocarbon gas mixture; iii) recovering the C 3 and heavier paraffins-depleted hydrocarbon gas mixture; iv) regenerating the C 3 and heavier-loaded adsorbent by at least partially removing C 3 and heavier paraffins from the adsorbent; and v) sequentially repeating steps (ii) and (iii) using regenerated adsorbent from step (iv). 12 . The method of claim 11 for separating methane from a hydrocarbon gas mixture comprising methane and natural gas liquids (NGLs) that comprise ethane and heavier paraffins, wherein the method comprises the steps of: i) providing a bed of adsorbent selective for NGLs over methane; ii) passing a hydrocarbon gas mixture through the bed of adsorbent to at least partially remove NGLs from the gas mixture to produce: (a) NGLs-loaded adsorbent and (b) NGLs-depleted hydrocarbon gas mixture; iii) recovering the NGLs-depleted hydrocarbon gas mixture; iv) regenerating the NGLs-loaded adsorbent by at least partially removing NGLs from the adsorbent; and v) sequentially repeating steps (ii) and (iii) using regenerated adsorbent from step (iv). 13 . The method of claim 12 wherein step (i) occurs in an adsorption chamber, and step (iv) occurs in a desorption chamber, and wherein NGL-loaded adsorbent is continuously transferred from the adsorption chamber to the desorption chamber, and regenerated adsorbent is continuously transferred from the desorption chamber to the adsorption chamber. 14 . The method of claim 13 wherein the adsorbent located in the adsorption chamber forms a packed moving bed. 15 . The method of claim 12 wherein the step of regenerating the NGL-loaded adsorbent comprises irradiating the adsorbent with microwaves. 16 . The method of claim 11 wherein the adsorbent comprises a functionalized macroporous alkylene-bridged adsorbent. 17 . The method of claim 16 wherein the macroporous alkylene-bridged adsorbent comprises an amine or a sulfur containing functional group. 18 . The method of claim 12 wherein the step of regeneration comprises exposing the adsorbent to lower pressure.

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What does patent US2017368494A1 cover?
A method for separating natural gas liquids (NGLs) from a hydrocarbon gas mixture containing natural gas liquids and methane, comprising the steps of: i) providing a bed of adsorbent selective for NGLs over methane; ii) passing a hydrocarbon gas mixture containing methane and NGL through the bed of adsorbent to at least partially remove NGLs from the gas mixture to produce: (a) NGL-loaded adsor…
Who is the assignee on this patent?
Dow Global Technologies Llc
What technology area does this patent fall under?
Primary CPC classification B01D53/08. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Thu Dec 28 2017 00:00:00 GMT+0000 (Coordinated Universal Time) (A1). 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).