Composite adsorbent bead, process for its production, gas separation process and gas adsorption bed
Composite adsorbent beads have a porous and non-adsorbent core comprising at least one inorganic material and a porous and adsorbent shell comprising at least one adsorbent layer comprising a porous adsorbent material on the surface of the core. The core preferably comprises agglomerated inorganic particles having a mean particle size equal to or smaller than the mean particle size of the surrounding agglomerated adsorbent particles. The beads preferably are manufactured by calcining together a non-sintered core and the adsorbent layer. The beads can be used at the outlet end of an adsorption column to improve performance.
1. A composite adsorbent bead for the separation of at least one gas component from a gas mixture, the adsorbent bead having at least one porous and non-adsorbent core comprising at least one inorganic material and a porous and adsorbent shell comprising at least one layer comprising a porous adsorbent material on the surface of the core, wherein the inorganic material is in the form of particles having a diameter in the range of 0.01 to 5 μm.
2. The composite adsorbent bead of claim 1 , wherein the core material has a porosity in the range of 10 to 50% and/or a pore volume in the range of 0.02 to 0.3 cm 3 /g.
3. The composite adsorbent bead of claim 1 , wherein the core comprises agglomerated inorganic particles having a mean particle size equal to or smaller than the mean particle size of surrounding agglomerated adsorbent particles forming said layer.
4. The composite adsorbent bead of claim 1 , wherein the core has a particle size distribution ratio D 90 /D 50 of less than 1.6 and a sphericity of 0.7 to 1.
5. The composite adsorbent bead of claim 1 , wherein the core meets one or any combination of the following specifications:
a thermal conductivity in the range of 1 to 450 W/mK
a sphericity of 0.7 to 1
a BET surface of 20 to 400 m 2 /g
a particle size distribution ratio D 90 /D 50 of less than 1.6
a porosity in the range of 10 to 50%
is permeable and/or
a pore volume in the range of 0.02 to 0.3 cm 3 /g.
6. The composite adsorbent bead of claim 1 , wherein the composite adsorbent bead meets one or any combination of the following specifications:
a bulk density in the range of 560 to 2000 kg/m 3
a specific crush strength in the range of 1 to 7 N/mm 2
a diameter of 0.1 to 5 mm
a ratio of the core diameter to the diameter of the composite adsorbent bead in the range of 0.5 to 0.98
an overall porosity greater than 40%
a sphericity of 0.7 to 1
a particle size distribution ratio D 90 /D 50 of less than 1.6
a specific surface in the range of 350 to 800 m 2 g −1 and/or
less than 20% wt of at least one inorganic binder material in the adsorbent layer.
7. The composite adsorbent bead of claim 1 , wherein the at least one core comprises
from 50 to 100 wt % of agglomerated clay particles and
from 0 to 50 wt % of graphite or a metal.
8. The composite adsorbent bead of claim 1 , wherein the at least one adsorbent material is selected from the group consisting of zeolites.
9. The composite adsorbent bead of claim 1 , wherein the at least one layer comprises 2 to 20 wt % of at least one inorganic binder material.
10. The composite adsorbent bead of claim 1 , wherein the core and shell materials have been calcined together.
11. A process for the production of a composite adsorbent bead according to claim 1 , comprising:
a) producing a dried porous non-adsorbent core having a moisture content in the range of 0.1 wt % and 25 wt %, comprising an organic binder,
b) applying a layer comprising adsorbent material, and
c) at least one heating step, whereby the organic binder material is removed.
12. A process of producing composite adsorbent beads comprising forming a non-sintered core comprising an inorganic material having hydroxyl groups and an organic binder; coating the core with a layer comprising an adsorbent material having hydroxyl groups, an organic binder and 2 to 20 wt % inorganic binder; and heating the coated core to remove the organic binder and calcining the core and layer together.
13. The process of claim 12 , wherein the inorganic core material is clay, the adsorbent material is selected from the group consisting of zeolites, and the inorganic binder is selected from the group consisting of silica and clay.
14. A dried porous and non-adsorbent core, suitable as an intermediate product for the production of a composite adsorbent bead comprising agglomerated clay particles, wherein the clay particles have a particle size in the range of 0.05 μm to 5 μm and an organic binder.
15. A gas separation process for the separation of at least one gas component from a gas mixture comprising feeding a gas mixture comprising at least two gas components into an adsorption vessel comprising a bed of the composite adsorbent beads of claim 1 and subjecting the gas mixture to conditions which allow the adsorption of at least one gas component which has to be separated from the gas mixture.
16. A process of conducting an adsorption process comprising contacting a gas mixture to be separated with the adsorbent bead according to claim 1 wherein the adsorbent bead is provided as layered adsorption beds.
17. An adsorption vessel having an adsorption bed comprising composite adsorbent beads according to claim 1 .
18. The adsorption vessel of claim 17 , wherein the adsorption bed comprises the composite adsorbent beads on the outlet end of the adsorption vessel and/or homogeneous adsorbent bead at the inlet end of the vessel.
19. The composite adsorbent bead of claim 2 , wherein the core has a particle size distribution ratio D 90 /D 50 of less than 1.6 and a sphericity of 0.7 to 1.
20. The composite adsorbent bead of claim 3 , wherein the core has a particle size distribution ratio D 90 /D 50 of less than 1.6 and a sphericity of 0.7 to 1.