METHOD AND ARRANGEMENT FOR PROCESSING A GAS MIXTURE

Abstract

A method for processing a nitrogen-containing starting gas mixture by vacuum pressure swing adsorption, in which the starting gas mixture is temporarily guided under pressure in a main flow direction through an adsorption unit filled with an adsorbent material. The adsorbent material is provided, in a first region along the main flow direction, predominantly or exclusively in the form of first adsorption bodies; the adsorbent material is provided, in a second region along the main flow direction and downstream of the first region in the form of second adsorption bodies; that at least the second adsorption bodies are provided as composite bodies that have an inner core of a non-porous, non-adsorbent material and an outer layer formed from the adsorbent material; and that the second adsorption bodies have a lower proportion of the adsorbent material, in the body volume, than the first adsorption bodies.

Claims

1. A method for processing a gaseous, nitrogen-containing starting gas mixture by pressure swing adsorption, in which the starting gas mixture is temporarily guided under pressure in a main flow direction through an adsorption unit filled with an adsorbent material, wherein the adsorbent material is provided, in a first region along the main flow direction, predominantly or exclusively in the form of first adsorption bodies, that the adsorbent material is provided, in a second region along the main flow direction and downstream of the first region, predominantly or exclusively in the form of second adsorption bodies, that at least the second adsorption bodies are provided as composite bodies that have an inner core of a non-porous, non-adsorbent material and an outer layer having or formed from the adsorbent material, and that the second adsorption bodies have a lower proportion of the adsorbent material, in the body volume, than the first adsorption bodies.

2. The method according to claim 1, in which the first adsorption bodies are also provided as composite bodies having an inner core of a non-porous, non-adsorbent material and an outer layer having or formed from the adsorbent material, wherein the outer layer assumes a greater proportion of the body volume in the first adsorption bodies than in the second adsorption bodies.

3. The method according to claim 2, in which the volumetric proportion of the porous, adsorbent material is 50 to 60% of the body volume in the second adsorption bodies and more than 70% of the body volume in the first adsorption bodies.

4. The method according to claim 1, in which the first adsorption bodies are provided in the form of homogeneous adsorption bodies having the adsorbent material or formed from the adsorbent material.

5. The method according to claim 4, in which the first adsorption bodies have a diameter of more than 2 mm.

6. The method according to claim 1, in which the adsorbent material is selected from the group consisting of activated aluminum oxide, zeolites, materials with mesopores, carbon molecular sieves and mixtures thereof.

7. The method according to claim 1, in which the inner core contains a material selected from the group consisting of metals, metal oxide, mixed oxides, dense ceramic oxides such as corderite, perovskite, sintered clays such as kaolin, attapulgite, silicas, aluminum oxides, silica-aluminum oxide, silica-magnesium oxide, silica-zirconium oxide, silica-purium oxide, silica-beryllium oxide, and silica-titanium oxide, as well as ternary compositions such as silica-aluminum oxide-thorium oxide, silica-aluminum oxide, zirconium oxide, and mixtures thereof.

8. The method according to claim 1, in which the first region and the second region together have a length of which the first region comprises 40 to 80%.

9. The method according to claim 1, in which the first region is dimensioned such that it corresponds to an equilibration zone for nitrogen in the adsorption unit, and in which the second region is dimensioned such that it corresponds to a mass transfer zone for nitrogen in the adsorption unit.

10. The method according to claim 9, comprising experimentally and/or simulatively determining a length of the equilibration zone and a length of the mass transfer zone.

11. The method according to claim 1, in which the first and/or second composite bodies are each spherical and/or have a minimum diameter of 2 mm.

12. The method according to claim 1, in which air is used as the starting gas mixture.

13. The method according to claim 9, in which the first and second zones are part of a nitrogen removal layer which adjoins a water removal layer in the adsorption unit.

14. The method according to claim 1, which is carried out as a vacuum pressure swing adsorption method.

15. An arrangement for processing a nitrogen-containing starting gas mixture by pressure swing adsorption, having an adsorption unit filled with an adsorbent material and having means which are designed to temporarily guide the starting gas mixture under pressure in a main flow direction through the adsorption unit, wherein the adsorbent material is provided, in a first region along the main flow direction, predominantly or exclusively in the form of first adsorption bodies, that the adsorbent material is provided, in a second region along the main flow direction and downstream of the first region, predominantly or exclusively in the form of second adsorption bodies, that at least the second adsorption bodies are provided as composite bodies that have an inner core of a non-porous, non-adsorbent material and an outer layer having or formed from the adsorbent material, and that the second adsorption bodies (121) have a lower proportion of the adsorbent material, in the body volume, than the first adsorption bodies.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0050] FIG. 1 shows an adsorption unit during use for processing air.

[0051] FIG. 2 shows a concentration gradient of nitrogen in an adsorption unit according to an embodiment of the invention.

[0052] FIG. 3 shows charging with nitrogen in an adsorption unit according to an embodiment of the invention.

[0053] FIG. 4 shows an adsorption body designed as a composite body in a simplified schematic representation.

DETAILED DESCRIPTION OF THE DRAWINGS

[0054] In the figures, components corresponding functionally or structurally to one another are indicated by identical reference signs and for the sake of clarity are not explained repeatedly. It is self-evident that, when components of arrangements and systems according to embodiments of the present invention are described below, these explanations relate to methods according to the invention and their embodiments in the same way.

[0055] The drawings respectively relate to embodiments in which the first adsorption bodies are designed as homogeneous adsorption bodies, i.e., not as core-in-shell or composite bodies. However, as mentioned, the present invention can also relate to such a case.

[0056] FIG. 1 schematically illustrates an adsorption unit during use for processing air according to an embodiment of the present invention and is designated as a whole by 100.

[0057] The adsorption unit 100 can in particular be part of an arrangement 10, which is indicated here only schematically and in which a plurality of adsorption units 100 can be arranged and can be operated in a manner known in principle. In the example shown, a starting gas mixture, in particular air, designated E is supplied to the adsorption unit 100.

[0058] The adsorption unit 100 is shown here in an adsorption phase of the type explained above so that a product mixture P is extracted therefrom. In a subsequent desorption or regeneration phase, however, adsorbed components are desorbed, in particular under a sub-atmospheric pressure level in the case of VPSA, from the adsorption material contained in the adsorption unit 100. By using the adsorption unit 100, the starting gas mixture E can be depleted of components which adsorb well to the adsorbent material, in the present case nitrogen, so that a product mixture P is enriched in oxygen or represents pure oxygen.

[0059] A first layer 101 and a second layer 102 are formed in the adsorption unit 100. The first layer 101 is a water removal layer previously explained several times and is equipped with a suitable adsorbent material for this purpose. The second layer 102 forms a nitrogen removal layer. The latter is considered in detail below.

[0060] In operation, an equilibration zone 110 and a mass transfer zone 120 form in the nitrogen removal layer 102, as is generally known from the field of adsorption technology. The equilibration zone 110 is characterized in particular by a constant or substantially constant nitrogen partial pressure, whereas the nitrogen partial pressure in the mass transfer zone 120 is reduced in the form of a steep gradient.

[0061] FIG. 2 schematically illustrates a concentration gradient of nitrogen, at the end of the adsorption phase, in an adsorption unit according to an embodiment of the invention, for example adsorption unit 100 according to FIG. 1, in the form of a concentration diagram. In the diagram shown in FIG. 2, a length of the adsorption unit or of a corresponding adsorbent bed is shown on the abscissa against a nitrogen concentration in arbitrary units on the ordinate. Again, the water removal layer 101 and the equilibration zone 110 and the mass transfer zone 120 of the nitrogen removal layer 102 (not designated separately here) are shown. The nitrogen concentration curve is denoted by 201. As again illustrated separately here, homogeneous adsorption bodies 111 having an adsorbent material or formed from the adsorbent material are provided in the equilibration zone of the adsorption unit 100, whereas composite bodies 121 are provided in the second region, that is, in the mass transfer zone, wherein the composite bodies 121 comprise an inner core C of a non-porous, non-adsorbent material and an outer layer S having or formed from the adsorption material.

[0062] As can be seen in FIG. 2, the nitrogen concentration and thus the nitrogen partial pressure, at the end of the adsorption, is substantially constant in the gas phase in the equilibration zone 110 of the nitrogen removal layer 102. Since this nitrogen partial pressure represents the impelling force for the adsorption of nitrogen, it is sufficiently high for kinetic effects, as mentioned, to play a smaller role here and therefore for nitrogen simply to be adsorbed. This is in particular also clear from FIG. 3. On the other hand, the nitrogen concentration or the corresponding partial pressure in the mass transfer zone 120 is much lower and therefore rapid kinetics are required. As mentioned, the composite bodies used here meet these requirements.

[0063] FIG. 3 illustrates the charging of an adsorption unit with nitrogen according to an embodiment of the invention in the form of a corresponding diagram. In the diagram according to FIG. 3, a length of an adsorption unit or of an adsorbent bed is again shown on the abscissa, but now against a value characterizing the charging of the adsorbent material on the ordinate. Again, the water removal layer 101 as well as the equilibration zone 110 and the mass transfer zone 120 of the nitrogen removal layer, which is also not designated separately here, are illustrated. A curve corresponding to the charging of the adsorbent material is indicated by 301. As can be seen in particular from FIG. 3, complete or almost complete charging of the entire equilibration zone with the adsorbent material is possible under the present conditions.

[0064] FIG. 4 shows an adsorption body designed as a composite body in a simplified schematic representation. This is designated as above by 121 and comprises an inner core C and an outer layer S. D denotes the diameter of the composite body 121, which defines the “body volume” within the meaning explained above. The diameter of the inner core C is denoted by d. This results in the thickness of the outer layer S to h.