Zeolite adsorbent material, method of preparation and use for non-cryogenic separation of industrial gases

1. A zeolitic adsorbent material comprising:

a particle size distribution, based on LSX zeolite crystals, that is a Gaussian distribution characterised by a peak width (2σ) in a range from 9.0 to 17.0, limits included, for a number average diameter (d 50 ) in a range from 0.5 μm to 20.0 μm,

the zeolitic adsorbent material having an Si/AI atomic ratio in a range from 1.00 to 1.15, limits included,

the zeolitic adsorbent material having a lithium content, expressed by weight of Li 2 O, in a range from 9% to 12% by weight relative to the total weight of the zeolitic adsorbent material, and

the zeolitic adsorbent material having a non-zeolitic phase (NZP) content such that 0<NZP≤8% by weight relative to the total weight of the zeolitic adsorbent material.

2. The material according to claim 1 , wherein the number-average diameter (d 50 ) of the LSX zeolite crystals is in a range from 1.0 μm to 15.0 μm.

3. The material according to claim 1 , wherein the non-zeolitic phase (NZP) is present in an amount of 0.5%≤NZP≤4% by weight relative to the total weight of the zeolitic adsorbent material.

4. The material according to claim 1 , which is in the form of beads with a volume mean diameter of between 0.05 mm and 5 mm, limits included.

5. The material according to claim 1 , having an apparent density in a range from 0.58 kg/m −3 to 0.80 kg/m −3 .

6. A method for preparing the zeolitic adsorbent material according to claim 1 , comprising:

agglomerating LSX zeolite crystals with an agglomerating binder and a silica source, followed by shaping, drying and calcining of the agglomerated crystals,

zeolitising the binder by the action of a basic alkaline solution,

replacing the major part of the cations at the exchangeable sites of the product obtained in the zeolitising step by lithium cations, followed by washing and drying of the product thus treated, and

optionally drying, and activating the zeolitic adsorbent material obtained.

7. The method according to claim 6 , wherein at the end of the agglomerating step, the amount by weight of LSX zeolite crystals is in a range from 75% to 90% by weight relative to the total weight of said product obtained at the end of the agglomerating step and the amount of zeolitisable clay is in a range from 5% to 25% by weight relative to the total weight of said product obtained at the end of the agglomerating step.

8. The method according to claim 6 , wherein the silica source is added in an amount such that at the end of the agglomerating step, the silica source represents from 0.1% to 10% by weight, relative to the total weight of said product obtained at the end of the agglomerating step.

9. The method according to claim 6 , wherein the agglomerating binder contains at least 80% by weight of zeolitisable clay(s), said zeolitisable clays selected from the group consisting of kaolinites, halloysites, nacrites, dickites, kaolins and/or metakaolins.

10. A nitrogen-adsorbent material or a carbon monoxide-adsorbent material comprising the zeolitic adsorbent material according to claim 1 .

11. A consumable cartridge of zeolitic adsorbent, comprising at least one zeolitic adsorbent material according to claim 1 .

12. An oxygen concentrator for respiratory assistance, which is transportable, mobile, comprising at least one zeolitic adsorbent material according to claim 1 .