초록 ▼

A gas separation process uses a structured particulate bed of adsorbent coated shapes/particles laid down in the bed in an ordered manner to simulate a monolith by providing longitudinally extensive gas passages by which the gas mixture to be separated can access the adsorbent material along the len

A gas separation process uses a structured particulate bed of adsorbent coated shapes/particles laid down in the bed in an ordered manner to simulate a monolith by providing longitudinally extensive gas passages by which the gas mixture to be separated can access the adsorbent material along the length of the particles. The particles can be laid down either directly in the bed or in locally structured packages/bundles which themselves are similarly oriented such that the bed particles behave similarly to a monolith but without at least some disadvantages. The adsorbent particles can be formed with a solid, non-porous core with the adsorbent formed as a thin, adherent coating on the exposed exterior surface. Particles may be formed as cylinders/hollow shapes to provide ready access to the adsorbent. The separation may be operated as a kinetic or equilibrium controlled process.

대표청구항 ▼

1. A gas separation process comprising contacting a gas mixture containing at least one contaminant with an adsorbent bed of structured adsorbent particles comprising a thin film adsorbent coating on the exterior of a low permeability core, wherein the adsorbent particles have: (i) a minimum crossse

1. A gas separation process comprising contacting a gas mixture containing at least one contaminant with an adsorbent bed of structured adsorbent particles comprising a thin film adsorbent coating on the exterior of a low permeability core, wherein the adsorbent particles have: (i) a minimum crosssectional dimension of less than 1 centimeter and greater than 100 microns;(ii) a length to maximum cross-sectional dimension of at least 2:1; and(iii) a longitudinal dimension of at least 20 mm; andwherein the adsorbent particles are positioned in the adsorbent bed with a void fraction not more than 30%, and in an ordered configuration to provide substantially longitudinally extensive, substantially aligned gas channels by which the gas mixture to be separated can access the adsorbent material along the length of at least a proportion of the particles to cause adsorption of at least some of the contaminants and to form a purified gas product having a reduced content of the adsorbed contaminant material. 2. A process according to claim 1, wherein the core is a substantially non-permeable, solid core. 3. A process according to claim 1, wherein the adsorbent coating has a thickness of less than 1000 microns and greater than 1 micron, which coating thickness also has a uniformity such that a thickness standard deviation is less than about 40% of the thickness. 4. A process according to claim 3, wherein the adsorbent coating has a thickness of less than 500 microns and greater than 25 microns. 5. A process according to claim 1, wherein the adsorbent coating comprises a microporous material. 6. A process according to claim 5, wherein the microporous material is selected from zeolites, MOPs (metal organic frameworks), AlPOs, SAPOs, ZIFs, (zeolitic imidazolate frameworks), carbons, and combinations and intergrowths thereof. 7. A process according to claim 6, wherein the microporous material is a zeolite selected from DDR, CHA, MPI, Beta, FAU, and combinations and intergrowths thereof. 8. A process according to claim 1, wherein the adsorbent coating comprises a mixed matrix material. 9. A process according to claim 8, wherein the mixed matrix material is a polymer film comprising a polymer selected from silicone rubber and polyimides, and further comprises particles of zeolite. 10. A process according to claim 9, wherein the zeolite is selected from DDR, CHA, MPI, Beta, FAU, and combinations and intergrowths thereof. 11. A process according to claim 1, wherein the ordered adsorbent bed of particulate adsorbent particles comprises locally structured ordered regions in which the particulate adsorbent particles are laid down in the ordered configuration of substantially longitudinally extensive, substantially aligned gas channels. 12. A process according to claim 11, further comprising adhering the adsorbent particles together with an adhesive to form the locally structured ordered regions and removing the adhesive prior to contact with the gas stream. 13. A process according to claim 12, further comprising applying the adhesive to the adsorbent particles by spraying the adsorbent particles with the adhesive or passing the adsorbent particles through a bath of the adhesive. 14. A process according to claim 11, where an end-to-end dimension of the locally structured ordered regions is from about 5 cm to about 100 cm. 15. A process according to claim 1, wherein the adsorbent particles are in the form of hollow cylinders or hollow prismatic polygonal shapes having a central gas passage. 16. A process according to claim 1, wherein the adsorbent particles are in the form of prismatic polygonal shapes having cross-sectional irregularities that preclude maximal face-to-face contact of the particles in the ordered configuration. 17. A process according to claim 16, wherein the cross-sectional irregularities comprise irregular lengths of polygonal sides and/or irregular vertex angles. 18. A process according to claim 1, wherein the adsorbent particles have surface irregularities in the form of uniform roughness that preclude maximal face-to-face contact of the particles in the ordered configuration. 19. A process according to claim 1, wherein the adsorbent particles have a length to maximum cross-sectional dimension of the particle of at least 5:1. 20. A process according to claim 1, wherein the gas mixture is natural gas and the at least one contaminant is CO2, H2S, or a combination thereof. 21. A process according to claim 1, wherein the at least one contaminant is CO2, H2S, or a combination thereof. 22. A process according to claim 1, further comprising growing an intergrown film of adsorbent crystals directly on the exterior surface of the low permeability core to form the adsorbent coating. 23. A process according to claim 22, wherein the adsorbent crystals are comprised of a zeolite selected from DDR, MPI, CHA, and combinations and intergrowths thereof. 24. A process according to claim 1, wherein the adsorbent particles comprise an exterior longitudinal groove. 25. A process according to claim 1, wherein the adsorbent particles have a central gas passage and an exterior gas passage and the interior and exterior surfaces of the adsorbent particles comprise the adsorbent coating. 26. A process according claim 1, further comprising wash coating individual bound particles on the core to form the adsorbent coating. 27. A process according to claim 1, further comprising forming a porous inorganic oxide film on the surface of the core and imbibing an adsorbent liquid into the pore structure of the inorganic oxide film to form the adsorbent coating.