Zeolitic agglomerated material, preparation process and use for non-cryogenic gas separation
The present invention relates to new zeolitic adsorbent materials which are particularly specific and adapted for the non-cryogenic separation of gases, and more particularly for the separation of nitrogen by adsorption in gas streams such as air, and also for the purification of hydrogen by adsorption of carbon monoxide (CO) and/or nitrogen (N 2 ), and also to the use thereof especially for the preparation of medical oxygen in oxygen concentrators for respiratory assistance.
1. A zeolitic agglomerated material in the form of a zeolite agglomerate particle comprising zeolite crystals and at least one binder,
wherein the zeolitic agglomerated material has a ratio of the volume-average diameter of the zeolite agglomerate particle relative to the number-average diameter of the zeolite crystals of between 4 and 70,
wherein the zeolite crystals have a number average diameter (d 50 ) of between 5.0 μm and 15 μm, and
wherein the zeolitic agglomerated material has a mass adsorption capacity of nitrogen (N 2 ), measured under 1 bar at 25° C., of greater than 20 Ncm 3 ·g −1 .
2. The zeolitic agglomerated material as claimed in claim 1 , comprising FAU-type zeolite crystals, the material having an Si/Al atomic ratio of between 1 and 2.5, measured by X-ray fluorescence, with a measurement uncertainty of ±0.05.
3. The zeolitic agglomerated material as claimed in claim 1 , having a lithium content, expressed by weight of Li 2 O, of between 8.0% and 12.0% by weight, limits included, relative to the total weight of the zeolitic agglomerated material.
4. The material as claimed in claim 1 , wherein the amount of non-zeolite phase (NZP) is such that 0<NZP≤25%, measured by X-ray diffraction (XRD), by weight relative to the total weight of the zeolitic agglomerated material.
5. The material as claimed in claim 1 , having a bulk density of between 0.50 kg·m −3 and 0.80 kg·m −3 .
6. A process for preparing the zeolitic agglomerated material as claimed in claim 1 , comprising the following steps:
a) agglomerating zeolite crystals, with an agglomeration binder, followed by shaping, drying and calcining the resulting zeolitic agglomerate,
b) optionally subjecting at least a portion of the binder to zeolitization,
c) subjecting the agglomerate to cationic exchange,
d) optional drying the agglomerate, and
e) activating the zeolitic agglomerated material obtained.
7. The process as claimed in claim 6 , wherein the optional zeolitization step may be carried out by immersing the agglomerate in an alkaline basic solution.
8. A method for separating nitrogen gas from industrial gases containing nitrogen gas and from the air, the method comprising treating the industrial gases or the air with the material as claimed in claim 1 .
9. The method as claimed in claim 8 , wherein the material is present in oxygen concentrators for respiratory assistance.
10. A consumable cartridge of zeolitic adsorbent, comprising at least one zeolitic agglomerated material as claimed in claim 1 .
11. The cartridge as claimed in claim 10 , further comprising at least one resin.
12. An oxygen concentrator for respiratory assistance, which is transportable, mobile, comprising at least one zeolitic agglomerated material as claimed in claim 1 .