Fast cycle gas phase simulated moving bed apparatus and process

Patent metadata

Field	Value
Publication number	US-10500538-B2
Application number	US-201815877419-A
Country	US
Kind code	B2
Filing date	Jan 23, 2018
Priority date	Feb 15, 2017
Publication date	Dec 10, 2019
Grant date	Dec 10, 2019

Abstract

Systems and processes for use of concentric adsorbent beds with rotary valve assemblies are provided.

First claim

The invention claimed is:

1. An adsorbent bed system for use in swing adsorption processes comprising:
a rotary valve assembly comprising
a feed stator having at least two annular tracks, each of the annular tracks having at least one opening to permit gas to flow there through;
a feed rotor being connected to the feed stator, the feed rotor having at least two annular tracks, each of the annular tracks having an opening to permit gas to flow there through;
product rotor having at least two annular tracks, each of the annular tracks having an opening to permit gas to flow there through; and
a product stator having at least two annular tracks, each of the annular tracks having an opening to permit gas to flow there through;

a first adsorbent bed of material capable of selectively removing a target gas from a gaseous mixture, which adsorbent bed is substantially cylindrical shape; and
a second adsorbent bed of material capable of selectively removing a target gas from a gaseous mixture, which second adsorbent bed has a substantially annular shape and being disposed about the first adsorbent bed of material and has a different face cross-sectional area than the face cross-sectional area of the first adsorbent bed; the first and second adsorbent beds being in fluid communication with the feed rotor, product rotor, and each other.

2. The adsorbent bed system of claim 1 , further comprising:
a third adsorbent bed of material capable of selectively removing a target gas from a gaseous mixture and being substantially annular in shape and being disposed about the second adsorbent bed, the third adsorbent bed having a different face cross-sectional area than the face cross-sectional area of the first and second adsorbent beds;
wherein the feed stator and feed rotor have at least three annular tracks, each of the annular tracks having an opening to permit gas flow through; and
wherein the product rotor and product stator have at least three annular tracks, each of the annular tracks having an opening to permit gas flow through.

3. The adsorbent bed system of claim 2 , further comprising:
a fourth adsorbent bed of material capable of selectively removing a target gas from a gaseous mixture and being substantially annular in shape and being disposed about the third adsorbent bed, the fourth adsorbent bed having a different face cross-sectional area than the face cross-sectional area of the first, second and third adsorbent beds;
wherein the feed stator and feed rotor have at least four annular tracks, each of the annular tracks having an opening to permit gas flow through; and
wherein the product rotor and product stator have at least four annular tracks, each of the annular tracks having an opening to permit gas flow through.

4. The adsorbent bed system of claim 2 , wherein the gaseous mixture flows through the feed stator, through the feed rotor, into the first adsorbent bed, then into the second adsorbent bed, then into the third adsorbent bed, through the product rotor, and through the product stator, wherein flow through the first, second, and third adsorbent bed is in the axial plane, wherein flow through the second adsorbent bed is in the opposite direction from the first adsorbent bed and the third adsorbent bed, wherein the face cross-sectional area of the first adsorbent bed is greater than the second adsorbent bed, wherein the face cross-sectional area of the second adsorbent bed is greater than the third adsorbent bed.

5. The adsorbent bed system of claim 2 , wherein the gaseous mixture flows through the feed stator, through the feed rotor, into the third adsorbent bed, then into the second adsorbent bed, then into the first adsorbent bed, through the product rotor, and through the product stator, wherein flow through the first, second, and third adsorbent bed is in the axial plane, wherein flow through the second adsorbent bed is in the opposite direction from the first adsorbent bed and the third adsorbent bed, wherein the face cross-sectional area of the third adsorbent bed is greater than the second adsorbent bed, wherein the face cross-sectional area of the second adsorbent bed is greater than the first adsorbent bed.

6. The adsorbent bed system of claim 2 , wherein the feed stator includes three rings of annular tracks, each ring aligned with one of the first, second, and third adsorbent bed, each ring containing annular tracks for a feedstream, a blowdown stream, a purge stream, and pressure equalization with a neighboring adsorbent bed.

7. The adsorbent bed system of claim 1 , wherein there is an equal volume of adsorbent material in the first adsorbent bed and the second adsorbent bed.

8. The adsorbent bed system of claim 1 , wherein the adsorbent material in the first adsorbent bed and the adsorbent material in the second adsorbent bed is loaded to different heights.

9. The adsorbent bed system of claim 1 , wherein the first adsorbent bed is offset from the second adsorbent bed in the axial plane.

10. An adsorption process comprising:
providing a feedstream containing a first concentration of a product gas and first concentration of a target gas;
feeding the feedstream to the first adsorbent bed in the adsorption system of claim 2 ;
in the first adsorbent bed, adsorbing the target gas onto the material capable of selectively removing a target gas from a gaseous mixture;
recovering a stream from the first adsorbent bed that has a higher concentration of product gas and a lower concentration of target gas than the feedstream;
reducing the pressure in the first adsorbent bed by equalizing the first adsorbent bed with one of the second and third adsorbent beds;
further reducing the pressure in the first adsorbent bed by outputting a blowdown stream from at least one end of the first adsorbent bed;
purging the first adsorbent bed with a purge gas to produce a target gas recovery stream that as higher concentration of target gas and a lower concentration of product gas than the feedstream.

11. The adsorption process of claim 10 , wherein during feeding of the first adsorbent bed, the second adsorbent bed equalizes with the third adsorbent bed and undergoes a repressurization step and the third adsorbent bed equalizes with the second adsorbent bed and undergoes a blowdown step and a purge step.

12. The adsorption process of claim 11 , wherein the feedstream passes sequentially from the first adsorbent bed to the second adsorbent bed to the third adsorbent bed, wherein the first adsorbent bed has a greater face cross-sectional area than the second adsorbent bed, wherein the second adsorbent bed has a greater cross-sectional area than the third adsorbent bed.

13. The adsorption process of claim 10 , wherein the product gas is N 2 and the target gas is CO 2 .

14. The adsorption process of claim 10 , wherein the product gas is H 2 and the target gas is CO 2 .

15. The adsorption process of claim 10 , wherein the feedstream comprises nitrogen and oxygen.

16. The adsorption process of claim 10 , wherein the feedstream comprises olefins and paraffins.

17. The adsorption process of claim 16 , wherein the feedstream comprises ethylene and ethane.

18. The adsorption process of claim 16 , wherein the feedstream comprises propylene and propane.

19. The adsorption process of claim 10 , wherein the feedstream comprises a mixture of xylenes.

20. An adsorption process for storage and use of a target gas, comprising:
providing a feedstream consisting essentially of a target gas;
feeding the feedstream to the fi

Assignees

• Exxonmobil Res & Eng Co

Inventors

• Sundaram Narasimhan

Classifications

• B01D2257/7022

  Aliphatic hydrocarbons · CPC title

• F17C11/00

  Use of gas-solvents or gas-sorbents in vessels {(absorbing compositions for acetylene C10L3/04; absorbing compositions for hydrogen C01B3/0005)} · CPC title

• B01D2257/504

  Carbon dioxide · CPC title

• B01D2259/40005

  using rotary valves · CPC title

• B01J20/165

  Natural alumino-silicates, e.g. zeolites · CPC title