METHOD AND SYSTEM FOR EXTRACTING PURE HELIUM

Abstract

The invention relates to a method (200-400) for extracting pure helium using a first membrane separation stage (1), a second membrane separation stage (2), and a third membrane separation stage (3), in which a first helium-containing feed mixture is supplied to the first membrane separation stage (1), a second helium-containing feed mixture is supplied to the second membrane separation stage (2), and a third helium-containing feed mixture is supplied to the third membrane separation stage (3), and in which a first permeate and a first retentate are formed in the first membrane separation stage (1), a second permeate and a second retentate are formed in the second membrane separation stage (2), and a third permeate and a third retentate are formed in the third membrane separation stage (3). According to the invention, the first feed mixture is formed using at least one portion of a helium-containing starting mixture, the second feed mixture is formed using at least one portion of the first permeate, the third feed mixture is formed using at least one portion of the second retentate, the second permeate is at least partially processed by pressure-swing adsorption in order to obtain the pure helium and a remaining mixture, and at least one portion of the third permeate and/or at least one portion of the third retentate is guided back into the method (200). The invention also relates to a corresponding system.

Claims

1. Method (100-400) for extracting pure helium using a first membrane separation stage (1), a second membrane separation stage (2), and a third membrane separation stage (3), wherein a first helium-containing feed mixture is supplied to the first membrane separation stage (1), a second helium-containing feed mixture is supplied to the second membrane separation stage (2), and a third helium-containing feed mixture is supplied to the third membrane separation stage (3), and wherein a first permeate and a first retentate are formed in the first membrane separation stage (1), a second permeate and a second retentate are formed in the second membrane separation stage (2), and a third permeate and a third retentate are formed in the third membrane separate stage (3), wherein the first feed mixture is formed using at least one portion of a helium-containing starting mixture, that the second feed mixture is formed using at least one portion of the first permeate, that the third feed mixture is formed using at least one portion of the second retentate, that the second permeate is at least partially processed by pressure switch adsorption in order to obtain the pure helium and a remaining mixture, and that at least one portion of the third permeate and/or at least one portion of the third retentate is guided back into the method, wherein at least one portion of the remaining mixture is used in the formation of the second feed mixture, and at least one portion of the third permeate is used in the formation of the second feed mixture, wherein the remaining mixture or its portion used in the formation of the second feed mixture, the first permeate or its portion used in the formation of the second feed mixture, and the third permeate or its portion used in the formation of the second feed mixture are combined and jointly compressed and subjected to carbon dioxide removal after they are combined and jointly compressed, or wherein the remaining mixture or its portion used in the formation of the second feed mixture and the third permeate or its portion used in the formation of the second feed mixture are combined and jointly compressed, separately from the first permeate or its portion used in the formation of the second feed mixture, and subjected to carbon dioxide removal after they are combined and jointly compressed, or wherein the third permeate or its portion used in in the formation of the second feed mixture and the first permeate or its portion used in the formation of the second feed mixture are combined and jointly compressed, separately from the remaining mixture or its portion used in the formation of the second feed mixture, and subjected to carbon dioxide removal after they are combined and jointly compressed, characterized in that the carbon dioxide removal is carried out using an adsorption process in which at least one rinsing and displacement gas is used, and at least one portion of the second or third retentate is used as the or one of the rinsing and displacement gases.

2. Method (100-400) according to claim 1, in which at least one portion of the third retentate is used in the formation of the first feed mixture.

3. Method (200-400) according to claim 1, in which the second permeate or its portion processed by pressure-swing adsorption is subjected to hydrogen removal.

4. Method (200-400) according to claim 1, in which either the first membrane separation stage (1) is operated at a pressure level of 10 to 120 bar, the second membrane separation stage (2) is operated at a pressure level of 10 to 120 bar, and the third membrane separation stage (3) is operated at a pressure level of 10 to 120 bar, or in which the first membrane separation stage (1) is operated at a pressure level of 30 to 100 bar, the second membrane separation stage (2) is operated at a pressure level of 30 to 100 bar, and the third membrane separation stage (3) is operated at a pressure level of 30 to 100 bar.

5. System (200-400) for extracting pure helium, having a first membrane separation stage (1), a second membrane separation stage (2), and a third membrane separation stage (3), wherein means are provided which are configured to supply a first helium-containing feed mixture to the first membrane separation stage (1), a second helium-containing feed mixture to the second membrane separation stage (2), and a third helium-containing feed mixture to the third membrane separation stage (3), wherein the first membrane separation stage (1) is configured to form a first permeate and a first retentate, wherein the second membrane separation stage (2) is configured to form a second permeate and a second retentate, and wherein the third membrane separation stage (3) is configured to form a third permeate and a third retentate, wherein a means is provided which are configured to form the first feed mixture using at least one portion of a helium-containing starting mixture, to form the second feed mixture using at least one portion of the first permeate, to form the third feed mixture using at least one portion of the second retentate, to process the second permeate at least partially in order to obtain the pure helium and a remaining mixture through pressure-swing adsorption, and to guide at least one portion of the third permeate and/or at least one portion of the third retentate back into the method (200), wherein at least one portion of the remaining mixture and at least one portion of the third permeate are guided back into the first permeate, and wherein the remaining mixture, the third permeate are combined with the first permeate and subjected to carbon dioxide removal after they are combined, characterized in that the carbon dioxide removal is an adsorption process in which at least one rinsing and displacement gas is introduced, and wherein at least one portion of the second or third retentate is introduced as the or one of the rinsing and displacement gases in the adsorption process.

Description

[0043] Embodiments of the invention are described in more detail below with reference to the accompanying drawings. Brief description of the drawings

[0044] FIG. 1 shows a method according to an embodiment of the invention in the form of a schematic process flow diagram.

[0045] FIG. 2 shows a method according to an embodiment of the invention in the form of a schematic process flow diagram.

[0046] FIG. 3 shows a method according to an embodiment of the invention in the form of a schematic process flow diagram.

DETAILED DESCRIPTION OF THE DRAWINGS

[0047] In the figures, elements functionally or structurally corresponding to one another are indicated by reference signs corresponding to one another and are not explained repeatedly for the sake of clarity. The following explanations relate to methods and corresponding systems in the same way. It is understood that corresponding systems or methods can, in practice, also comprise optional or obligatory further components or method steps. These are not shown in the following figures, only for the sake of clarity.

[0048] In FIG. 1, a method according to an embodiment of the invention is shown in the form of a schematic process flow diagram and is designated as a whole by 200. The core of the method is, in particular, a first membrane separation stage 1, a second membrane separation stage 2, and a third membrane separation stage 3.

[0049] In the method 200, a starting mixture A of the kind previously explained is supplied, and, optionally, prepared in any desired preparation steps (not shown). The starting mixture A is combined with a stream M (see below) and supplied to an optional heating 4. Thus, using the starting mixture A or a portion thereof, a first feed mixture B is formed, which is supplied to the first membrane separation stage 1.

[0050] In the first membrane separation stage 1, a first permeate C and a first retentate D are formed. Using the first permeate or a portion thereof, a second feed mixture E is formed by compression 5 and supplied to the second membrane separation stage 2.

[0051] In the second membrane separation stage 2, a second permeate F and a second retentate G are formed. In the example shown, the second permeate F, after a compression 6 and hydrogen removal 7, is at least partially subjected to a pressure-swing adsorption 8. In this, pure helium H as a product and a remaining mixture I are formed.

[0052] At the same time, the retentate G of the second membrane separation stage 2 is supplied to the third membrane separation stage 3, i.e., a third feed mixture K is formed using at least one portion of the second retentate G. In the third membrane separation stage 3, a third permeate L and a third retentate M are formed.

[0053] In the example shown, the remaining mixture I and the third permeate L are now combined with one another and with the first permeate C, and subjected to the compression 5. Thus, the second feed mixture E is formed using the remaining mixture I, the third permeate L, and the first permeate C.

[0054] Further, in the illustrated embodiment, the third retentate M is used in the formation of the first feed mixture B andin particular, as part thereofsubjected to the optional heating 4. In particular, if required, a corresponding compression 9 can take place, which likewise effects a heating.

[0055] In addition, carbon dioxide removal 10 is shown here. In the carbon dioxide removal 10, a rinsing and displacement gas M may be used, which is formed using at least one portion of the second and/or the third retentates G and M, respectively.

[0056] In FIG. 2, a method of a further embodiment of the present invention is shown in the form of a schematic process flow diagram and is designated as a whole by 300. The method 300 according to FIG. 2 differs from the method 200 according to FIG. 1, in particular, in the positioning of the carbon dioxide removal 10. While, in the method 200 according to FIG. 1, the carbon dioxide removal 10 takes place upstream of the second membrane separation stage 2, and the explained first and third permeates C and L, along with the remaining mixture I, are thereby processed, in the method 300 illustrated in FIG. 2, carbon dioxide removal 10 takes place from only the remaining mixture I and the third permeate L, which are supplied separately from the second permeate C to the carbon dioxide removal 10 for this purpose and are subjected separately therefrom to compression 11. Compression 5 therefore does not have to take place. Optionally, however, a feeding to an intermediate stage of a compressor used in the compression 5 can also take place.

[0057] In FIG. 3, a method according to a further embodiment of the present invention is shown in the form of a schematic process flow diagram and is designated as a whole by 400. The method 400 according to FIG. 3 represents a variant compared to the methods 200 or 300. The carbon dioxide removal 10 takes place here from the remaining mixture I of the pressure-swing adsorption 8. A corresponding separate compression 12 takes place for this purpose.

[0058] It is understood that the method variants shown in the previously explained figures may also be used in combination and independently from one another, as long as the scope of the present invention, which is defined by the appended claims, is not departed from.