Method and arrangement for recovering helium

Patent metadata

Field	Value
Publication number	US-2022314163-A1
Application number	US-202017597288-A
Country	US
Kind code	A1
Filing date	Aug 6, 2020
Priority date	Aug 20, 2019
Publication date	Oct 6, 2022
Grant date	—

Abstract

A method for recovering helium from a feed gas mixture comprising helium, carbon dioxide and at least one of methane and nitrogen, and wherein at least a part of the feed gas mixture is subjected to a separation sequence including a membrane-based separation and an adsorption-based separation forming a helium product, wherein the the membrane based separation is performed using a first membrane separation step and a second membrane separation step, the membrane based separation and the separation sequence includes no further membrane separation steps, the adsorption based separation is performed using a pressure swing adsorption step, at least a part of the feed gas mixture is subjected to the first membrane separation step forming a first retentate and a first permeate. A corresponding arrangement is also provided.

First claim

1 - 12 . (canceled)

13 . A method for recovering helium from a feed gas mixture comprising helium, carbon dioxide and at least one of methane and nitrogen, wherein the feed gas mixture is subjected to a separation sequence including a membrane based separation and an adsorption based separation forming a helium product wherein the membrane based separation is performed using a first membrane separation step and a second membrane separation step, that the membrane based separation and the separation sequence includes no further membrane separation steps, that the adsorption based separation is performed using a pressure swing adsorption step, that at least a part of the feed gas mixture is subjected to the first membrane separation step forming a first retentate and a first permeate, that at least a part of the first permeate is subjected to a carbon dioxide removal step forming a gas mixture depleted in carbon dioxide, that at least a part of the gas mixture depleted in carbon dioxide is subjected to the second membrane separation step forming a second retentate and a second permeate, that at least a part of the second permeate is subjected to the pressure swing adsorption step forming a tail gas and the helium product, and that at least a part of the tail gas is recycled to a position between the first membrane separation step and the second membrane separation step in the separation sequence.

14 . The method according to claim 13 , wherein the feed gas mixture is obtained by submitting a starting gas mixture to a pretreatment comprising at least one of a removal of particles, a removal of liquids, a removal of heavy hydrocarbons, a removal of water, a removal of trace components including mercury, sulfur components and/or other trace components.

15 . The method according to claim 13 , wherein the starting gas mixture or the feed gas mixture is natural gas or obtained therefrom.

16 . The method according to claim 13 , wherein at least a part of the first retentate and/or at least a part of the second retentate are used in forming a further gas product poor in helium.

17 . The method according to claim 13 , wherein the first permeate or the part thereof being subjected to the carbon dioxide removal step is subjected to a first compression step and/or wherein the gas mixture depleted in carbon dioxide is or the part thereof subjected to the second membrane separation step is subjected to a second compression step and/or wherein the second permeate or the part thereof being subjected to the pressure swing adsorption step is subjected to a third compression step.

18 . The method according to claim 17 , wherein the tail gas or the part thereof being recycled is combined with the first permeate or with the part thereof being subjected to the carbon dioxide removal step is also subjected to the first compression step after being combined with the first permeate or with the part thereof being subjected to the carbon dioxide removal step.

19 . The method according to claim 17 , wherein the tail gas or the part thereof being recycled is subjected to a further compression step separate from the first compression step and is thereafter combined with the first permeate or with the part thereof being subjected to the carbon dioxide removal step.

20 . The method according to claim 13 , wherein the helium product is subjected to a compression and/or a liquefaction.

21 . The method according to claim 16 , wherein the further gas product is subjected to a compression and/or a liquefaction.

22 . The method according to claim 13 , wherein the feed gas mixture contains 0.1 to 5 mol-% helium and/or 0.5 to 60 mol-% of carbon dioxide and further comprises, in the part not formed by helium and carbon dioxide, at least 50 mol-% methane and/or nitrogen, wherein the first retentate and the second retentate contain less than 200 ppm helium, wherein the second permeate contains 20 to 40 mol-% helium and wherein the helium product contains 90 to 99.9999 mol-% helium.

23 . An arrangement for recovering helium from a feed gas mixture comprising helium and carbon dioxide and at least one of methane and nitrogen, the arrangement comprising means for subjecting at least a part of the feed gas mixture to a separation sequence including a membrane based separation and an adsorption based separation forming a helium product wherein the membrane based separation comprises a first membrane separation step and a second membrane separation step, that the membrane based separation and the separation sequence includes no further membrane separation steps, that the adsorption based separation comprises a pressure swing adsorption step, that means are provided which are adapted to subject at least a part of the feed gas mixture to the first membrane separation step and to form a first retentate and a first permeate, that means are provided which are adapted to subject at least a part of the first permeate to a carbon dioxide removal step forming as gas mixture depleted in carbon dioxide, that means are provided to subject at least a part of the gas mixture depleted in carbon dioxide to the second membrane separation step and to form a second retentate and a second permeate, that means are provided which are adapted to subject at least a part of the second permeate to the pressure swing adsorption step and to form a tail gas and the helium product, and in that means are provided which are adapted to recycle a part of the tail gas at a position between the first membrane separation step and the second membrane separation step in the separation sequence.

24 . The arrangement according to claim 11 , comprising means adapted to perform a method for recovering helium from a feed gas mixture comprising helium, carbon dioxide and at least one of methane and nitrogen, wherein the feed gas mixture is subjected to a separation sequence including a membrane based separation and an adsorption based separation forming a helium product wherein the membrane based separation is performed using a first membrane separation step and a second membrane separation step, that the membrane based separation and the separation sequence includes no further membrane separation steps, that the adsorption based separation is performed using a pressure swing adsorption step, that at least a part of the feed gas mixture is subjected to the first membrane separation step forming a first retentate and a first permeate, that at least a part of the first permeate is subjected to a carbon dioxide removal step forming a gas mixture depleted in carbon dioxide, that at least a part of the gas mixture depleted in carbon dioxide is subjected to the second membrane separation step forming a second retentate and a second permeate, that at least a part of the second permeate is subjected to the pressure swing adsorption step forming a tail gas and the helium product, and that at least a part of the tail gas is recycled to a position between the first membrane separation step and the second membrane separation step in the separation sequence.

Assignees

• Linde Gmbh

Inventors

• Salazar Duarte Gabriel
• Bauer Martin
• Pleintinger Stefan
• Kramer Verena
• Johannink Matthias

Classifications

• C01B2210/007

  Hydrocarbons · CPC title

• C01B2210/0071

  Sulfur oxides · CPC title

• B01D2257/102

  Nitrogen · CPC title

• B01D2257/504

  Carbon dioxide · CPC title

• C01B2210/0051

  Carbon dioxide · CPC title