Process and apparatus to recover helium

Patent metadata

Field	Value
Publication number	US-2024217821-A1
Application number	US-202218570557-A
Country	US
Kind code	A1
Filing date	Jun 16, 2022
Priority date	Jun 17, 2021
Publication date	Jul 4, 2024
Grant date	—

Abstract

An apparatus and a process to recover high purity helium from a low helium content feed stream are disclosed. The apparatus includes a first dual reflux pressure swing adsorption (DRPSA) unit and a second DRPSA unit, each unit comprising a high pressure adsorption column and a low pressure adsorption column configured in fluid communication with the high pressure adsorption column. The first DRPSA unit is arranged to receive and separate the feed stream into a first reflux product and a first heavy product and circulate the first reflux product and the first heavy product between the high and low pressure adsorption columns to produce an intermediate helium-enriched stream. The second DRPSA unit is arranged to receive and separate the intermediate helium-enriched stream into a second reflux product and a second heavy product and circulate the second reflux product and the second heavy product between the high and low pressure adsorption columns to produce a high purity helium stream and a waste stream containing helium. The waste stream from the second DRPSA unit is recycled to one of a plurality of locations in the first DRPSA unit to increase helium recovery in the high purity helium stream produced in the second DRPSA unit.

First claim

1 . A non-cryogenic process for recovering high purity helium from a feed stream comprising a low helium content gas, the process comprising:
a) introducing the feed stream into a high pressure adsorption column or a low pressure adsorption column of a first dual reflux pressure swing adsorption (DRPSA) unit; b) separating the feed stream by adsorption into a first reflux product and a first heavy product and circulating the first reflux product and the first heavy product in said first DRPSA unit to produce an intermediate helium-enriched stream; c) withdrawing the intermediate helium-enriched stream from the first DRPSA unit and introducing the intermediate helium-enriched stream to a high pressure adsorption column or a low pressure adsorption column of a second DRPSA unit; d) separating the intermediate helium-enriched stream by adsorption into a second reflux product and a second heavy product and circulating the second reflux product and the second heavy product in said second DRPSA unit to produce a high purity helium stream and a waste stream containing helium; and e) withdrawing the waste stream containing helium from the second DRPSA unit and recycling thereof to one of a plurality of locations in the first DRPSA unit to increase helium recovery in the high purity helium stream produced in the second DRPSA unit.

2 . A non-cryogenic process for separately recovering high purity helium and high purity methane from a feed stream comprising methane, nitrogen and helium, the process comprising:
a) introducing the feed stream into a high pressure adsorption column or a low pressure adsorption column of a first dual reflux pressure swing adsorption (DRPSA) unit; b) separating the feed stream by adsorption into a first reflux product and a first heavy product and circulating the first reflux product and the first heavy product thereof in said first DRPSA unit to produce an intermediate helium-enriched stream and a high purity methane stream; c) withdrawing the intermediate helium-enriched stream from first DRPSA unit and introducing the intermediate helium-enriched stream to a high pressure adsorption column or a low pressure adsorption column of a second DRPSA unit; d) separating the intermediate helium-enriched stream by adsorption into a second reflux product and a second heavy product and circulating the second reflux product and the second heavy product thereof in said second DRPSA unit to produce a high purity helium stream and a waste stream containing helium; and e) withdrawing the waste stream containing helium from the second DRPSA unit and recycling thereof to one of a plurality of locations in the first DRPSA unit to increase helium recovery in the high purity helium stream produced in the second DRPSA unit.

3 . The process according to claim 1 , wherein the feed stream is introduced to the high pressure adsorption column of the first DRPSA unit.

4 . The process according to claim 1 , wherein the intermediate helium-enriched stream is introduced to the high pressure adsorption column of the second DRPSA unit.

5 . The process according to claim 1 , wherein the intermediate helium-enriched stream is withdrawn from the high pressure adsorption column of the first DRPSA unit.

6 . The process according to claim 1 , wherein the waste stream containing helium is withdrawn from the low pressure adsorption column of the second DRPSA unit.

7 . The process according to claim 1 , wherein the process further comprises compressing the intermediate helium-enriched stream prior to introducing the intermediate helium-enriched stream to the high pressure adsorption column of the second DRPSA unit or compressing the waste stream containing helium prior to introducing said waste stream to the high pressure adsorption column of the first DRPSA unit.

8 . The process according to claim 1 , wherein circulating said reflux products and heavy products in said respective first and second DRPSA unit comprises reducing a pressure of said reflux product prior to feeding thereof to the low pressure adsorption column and compressing said heavy product prior to feeding thereof to the high pressure adsorption column.

9 . The process according to claim 1 , wherein said reflux products and heavy products in said DRPSA units may be circulated up to five times before withdrawing streams produced therein.

10 . The process according to claim 1 , wherein the feed stream is introduced into an intermediate portion of the high pressure adsorption column of the first DRPSA unit.

11 . The process according to claim 1 , wherein the intermediate helium-enriched stream is introduced into an intermediate portion of the high pressure adsorption column of the second DRPSA unit.

12 . The process according to claim 1 , wherein recycling the waste stream containing helium may comprise introducing said waste stream to an intermediate portion of the low pressure adsorption column of the first DRPSA unit, an intermediate portion of the high pressure adsorption column of the first DRPSA unit, or combining the waste stream with the feed stream prior to introducing the feed stream into the high pressure adsorption column of the first DRPSA unit.

13 . The process according to claim 1 , wherein the first and second DRPSA units are operated at a temperature maintained in a range of from 273 K to 333 K.

14 . The process according to claim 1 , wherein the high pressure adsorption columns are operated at a pressure of from 100 kPa to 1000 kPa and the low pressure adsorption columns are operated at a pressure of between about 0.01 kPa to about 500 kPa.

15 . The process according to claim 1 , wherein said adsorption columns comprise an adsorbent having a selectivity for methane over nitrogen.

16 . The process according to claim 15 , wherein the adsorbent has a selectivity for methane over nitrogen greater than 2.

17 . The process according to claim 15 , wherein the adsorbent in the adsorptions columns of the first DRPSA is the same or different to the adsorbent in the adsorption columns of the second DRPSA.

18 . The process according to claim 1 , wherein the feed stream comprises a hydrocarbon gas.

19 . The process according to claim 18 , wherein the feed stream comprises from about 0.01 mol % He to about 10 mol % He, optionally from about 1 mol % methane to about 99 mol % methane, with the balance being made up by nitrogen and/or one or more other gases such as argon, carbon dioxide, oxygen, hydrogen sulphide, ethane, propane.

20 . The process according to claim 1 , wherein the intermediate helium-enriched stream comprises from about 5 mol % to about 30 mol % He.

21 . The process according to claim 1 , wherein the waste stream comprises less than 20 mol % He.

22 . The process according to claim 21 , wherein the waste stream comprises from about 1 mol % to about 10 mol % helium.

23 . The process according to claim 1 , the high purity helium stream comprises >99 mol % He.

24 . The process according to claim 1 , wherein recovery of high purity helium is >90%.

25 . The process according to claim 1 , wherein the high purity methane stream comprises >96 mol % methane.

26 . The process according to claim 1 , wherein recovery of high purity methane is >90%.

27 . An apparatus to recover high purity helium from a feed stream comprising low helium content, the apparatus comprising:
a first dual reflux pre

Assignees

• Univ Western Australia

Inventors

• May Eric Freemantle
• Weh Roman
• Xiao Gongkui

Classifications

• C01B2210/0046

  Nitrogen · CPC title

• C01B2210/0031

  Helium · CPC title

• C01B2210/0028

  Separation of the specific gas from gas mixtures containing a minor amount of this specific gas · CPC title

• C01B2210/0014

  by adsorption in solids · CPC title

• C01B2210/007

  Hydrocarbons · CPC title