Sequential removal of NGLs from a natural gas stream

Patent metadata

Field	Value
Publication number	US-9976091-B2
Application number	US-201415114962-A
Country	US
Kind code	B2
Filing date	Aug 5, 2014
Priority date	Mar 18, 2014
Publication date	May 22, 2018
Grant date	May 22, 2018

Abstract

Disclosed is a method of sequentially separating and recovering one or more NGLs ( 129, 229 ) from a natural gas feedstream ( 3 ). Specifically, a raw natural gas feedstream ( 3 ) is passed through two or more NGLs separation unit ( 100, 200 ) wherein each separation unit removes one or more NGLs from the natural gas feedstream to provide a methane-rich natural gas supply ( 205 ). Each separation unit employs an adsorption media and has an adsorption step and a media regeneration step wherein the regeneration step may be operated as a batch process, a semi-continuous process, or a continuous process. One embodiment of this method provides for the use of a different regenerable adsorbent media in each separation unit.

First claim

What is claimed is:

1. A method to sequentially remove and recover some or all of the natural gas liquids (NGLs): ethane, propane, butane, pentane, or heavier hydrocarbons, from a natural gas feedstream to provide a methane-rich natural gas supply wherein the NGLs are separated from the natural gas feedstream by means of two or more NGLs separation units each comprising:
(i) an adsorption unit comprising an adsorption bed comprising an adsorbent media which adsorbs one or more NGLs to form a loaded adsorbent media
and
(ii) a regeneration unit comprising a means to regenerate loaded adsorbent media by causing the release of adsorbed NGLs from the loaded adsorbing media and forming regenerated adsorbent media wherein the method comprises the steps of:
(a) passing the natural gas feedstream through a first adsorption unit of the first separation unit at a first flow rate generating a first adsorbent loaded with one or more NGLs and a first treated natural gas supply,
(b) regenerating the first adsorbent loaded with one or more NGLs by releasing the adsorbed NGLs from the first loaded adsorbing media and forming regenerated first adsorbent media,
(c) recovering the released NGLs,
(d) providing the first treated natural gas supply to a second adsorption unit of the second separation unit at a second flow rate generating a second adsorbent loaded with one or more NGLs and a methane-rich natural gas supply,
(e) regenerating the second adsorbent loaded with one or more NGLs by releasing the adsorbed NGLs from the second loaded adsorbing media and forming regenerated second adsorbent media,
(f) recovering the released NGLs,
and
(g) providing the methane-rich natural gas supply to a one or more additional separation unit for further treatment, a natural gas pipeline for transportation, for use as fuel for a combustion process, for flaring, or a combination thereof,
wherein the adsorption media in each separation unit is independently selected from a porous cross-linked polymeric adsorbent, a pyrolized macroporous polymer, or mixtures thereof.

2. The method of claim 1 wherein the methane-rich gas supply is provided to a third separation unit wherein the method further comprises the steps of:
(h) passing the methane-rich natural gas supply through a third adsorption unit of the third separation unit at a third flow rate generating a third adsorbent loaded with one or more contaminant and a treated methane-rich natural gas supply,
(i) regenerating the third adsorbent loaded with contaminant(s) by releasing the adsorbed contaminant(s) from the third loaded adsorbing media and forming regenerated third adsorbent media
(j) recovering, treating, or venting the released contaminant(s),
and
(k) providing the treated methane-rich natural gas supply to a natural gas pipeline for transportation, for use as fuel for a combustion process, for flaring, or a combination thereof.

3. The methods of claim 1 or 2 wherein the adsorption unit/regeneration unit of each separation unit is independently the same unit wherein the adsorption/regeneration steps take place in the same unit or distinct adsorption and regeneration units wherein the adsorption step takes place in a separation unit and the regeneration step takes place in a regeneration unit, which is not the separation unit.

4. The method of claim 1 comprising 3, 4, 5, 6, 7, 8, 9, or 10 NGLs separation units and optionally one or more separation units for the removal of one or more contaminant.

5. The method of claim 1 wherein the source of the natural gas feedstream is from an oil well, a gas well, a condensate well, or a pipeline natural gas containing NGLs.

6. The method of claim 1 wherein the adsorption media in the two or more separation units is independently regenerated by means of reduced pressure over the media, heating the media, or a combination of reduced pressure and heating.

7. The method of claim 1 wherein the loaded adsorption media in the two or more separation units is regenerated by a microwave heating system.

8. The method of claim 1 wherein the first adsorption media is not the same as the second adsorption media.

9. The method of claim 1 wherein the first adsorption media is a porous cross-linked polymeric adsorbent and the second adsorption media is a pyrolized macroporous polymer.

10. The method of claim 1 wherein the first adsorption media is the same as the second adsorption media and the first flow rate is not equal to the second flow rate.

11. The method of claim 1 wherein each regeneration step is operated independently as a batch process, a semi-continuous process, or as a continuous process.

Assignees

• Dow Global Technologies Llc

Inventors

• Matteucci Scott T
• Goltz H Robert
• Badhwar Ajay N
• Shurgott Nicholas J
• Leister Jonathan W

Classifications

• B01D53/04

  with stationary adsorbents {(B01D53/025 takes precedence)} · CPC title

• B01D2253/308

  Pore size · CPC title

• B01D2257/304

  Hydrogen sulfide · CPC title

• B01D2257/504

  Carbon dioxide · CPC title

• C10G5/02 Primary

  with solid adsorbents · CPC title