Zeolitic granular material having a connected structure
View Patent ↗The present invention relates to a zeolitic granular material having a connected zeolitic structure across the entire volume thereof, having high mechanical resistance to crushing in the bed, and optimised material transfer in the macro-mesopores. The invention also relates to the method for preparing said zeolitic granular material, as well as to the use thereof as an adsorbent material in co-current or counter-current liquid phase separation methods, typically in a simulated mobile bed.
1. A zeolitic granular material having a particle size of from 0.1 mm to 1 mm, wherein
the zeolitic granular material has a mechanical bulk crushing strength of greater than or equal to 1.0 MPa,
the zeolitic granular material contains a zeolite structure that has a three-dimensionally connected surface,
the proportion of connected surface represents at least 50% of the surface occupied by the zeolitic granular material when ten images of polished sections of the zeolitic granular material are examined with a scanning electron microscope at a magnification of from 5,000 to 10,000,
the zeolitic granular material comprises at least one zeolite selected from the group consisting of zeolite LSX, zeolite MSX and zeolite X, and
the pore distribution satisfies the inequalities 1), 2) and 3) below:
Vme
Vme
+
Vma
≤
0.1
;
1
)
0.4
≤
Vmi
Vma
+
Vme
+
Vmi
;
2
)
and
0.25
≤
Vma
+
Vme
Vg
≤
0.35
;
3
)
wherein
Vma represents the macropore volume,
Vme represents the mesopore volume,
Vmi represents the micropore volume, and
Vg represents the total volume of the granular material.
2. The zeolitic granular material of claim 1 , comprising more than 94% by weight of zeolite(s), relative to the total weight of the zeolitic granular material.
3. The zeolitic granular material of claim 1 , wherein
0.01
≤
Vme
Vme
+
Vma
≤
0.1
.
4. The zeolitic granular material of claim 1 , wherein
0.01
≤
Vme
Vme
+
Vma
≤
0.06
.
5. The zeolitic granular material of claim 1 , wherein
0.4
≤
Vmi
Vma
+
Vme
+
Vmi
≤
0.6
.
6. The zeolitic granular material of claim 1 , wherein
0.45
≤
Vmi
Vma
+
Vme
+
Vmi
≤
0.55
.
7. The zeolitic granular material of claim 1 , having a size between 0.3 mm and 0.8 mm, limits inclusive.
8. The zeolitic granular material of claim 1 , having a mechanical bulk crushing strength greater than or equal to 2.0 MPa.
9. The zeolitic granular material of claim 1 , comprising zeolite X.
10. The zeolitic granular material of claim 1 , comprising between 96% and 98% by weight of zeolite(s), limits inclusive, relative to the total weight of the zeolitic granular material.
11. A process for preparing the zeolitic granular material of claim 1 , comprising:
a) mixing crystals of at least one zeolite with a clay binder containing at least 80% by weight of zeolitizable clay, and, optionally, a source of silica to form a mixture,
b) placing the mixture in contact with an alkaline basic solution to form a suspension,
c) bringing the suspension to a temperature between 80° C. and 600° C., in a closed and leaktight container, at a pressure at least equal to the autogenous pressure to obtain a zeolitic granular material,
d) optionally, carrying out cationic exchange of the cations contained in the reaction medium of step c) by placing the reaction medium in contact with a solution of barium ions, or of barium ions and potassium ions,
e) washing and drying of the zeolitic granular material thus obtained, and, optionally, at least one step of forming the zeolitic granular material to a desired size, and
f) activating the zeolitic granular material obtained in e) by heating to a temperature between 100° C. and 400° C.
12. The process of claim 11 , wherein the clay binder contains at least 80% by weight of clay, wherein the clay comprises at least one member selected from the group consisting of kaolins, kaolinites, nacrites, dickites, halloysite and metakaolins, and wherein the clay binder may optionally comprise at least one other mineral binder.
13. A process for separating aromatic fractions comprising mixtures of isomers containing 8 carbon atoms, comprising contacting an aromatic fraction comprising mixtures of isomers containing 8 carbon atoms with the zeolitic granular material of claim 1 .
14. The process of claim 13 , wherein the process is a liquid-phase process for separating xylenes in a simulated mobile bed.
15. The process of claim 13 , wherein the aromatic fraction contains xylenes.