Carbon dioxide separation using adsorption with steam regeneration
US-9504955-B2 · Nov 29, 2016 · US
US2017368494A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2017368494-A1 |
| Application number | US-201615536329-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jan 6, 2016 |
| Priority date | Jan 27, 2015 |
| Publication date | Dec 28, 2017 |
| Grant date | — |
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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).
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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.
by applying microwaves · CPC title
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