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An adsorption vessel comprising a packed bed region of adsorbent particles contiguously arranged, comprising a perforated adsorbent particles, a gas separation process using the perforated adsorbent particles, and methods for making the perforated adsorbent particles. The perforated adsorbent partic

An adsorption vessel comprising a packed bed region of adsorbent particles contiguously arranged, comprising a perforated adsorbent particles, a gas separation process using the perforated adsorbent particles, and methods for making the perforated adsorbent particles. The perforated adsorbent particles each comprise an adsorbent material where the perforated adsorbent particles each have at least 10 channels extending through the particle. The equivalent diameter of the channels may range from 0.05 mm to 1.5 mm, and the void fraction of the channels may range from 0.05 to 0.5.

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1. An adsorption vessel comprising: a packed bed region of adsorbent particles contiguously arranged, comprising a plurality of perforated adsorbent particles,wherein each perforated adsorbent particle comprises an adsorbent material capable of preferentially adsorbing at least one more strongly ads

1. An adsorption vessel comprising: a packed bed region of adsorbent particles contiguously arranged, comprising a plurality of perforated adsorbent particles,wherein each perforated adsorbent particle comprises an adsorbent material capable of preferentially adsorbing at least one more strongly adsorbable gaseous component in a mixture comprising at least two gaseous components comprising the at least one more strongly adsorbable component and at least one less strongly adsorbable component, wherein the adsorbent material is a material selected from the group consisting of activated alumina, activated carbon, zeolites, mesopore-structured materials, carbon molecular sieve, metal-organic framework materials, silica gel, and combinations thereof;wherein each perforated adsorbent particle defines a respective plurality of channels numbering at least 10, the respective plurality of channels extending through each perforated adsorbent particle in a lengthwise direction from a first end to a second end, andwherein each channel of the plurality of channels has an equivalent diameter, d, ranging from 0.05 mm to 1.5 mm, where d=2⁢Aπ, where A is the cross-sectional area normal to the lengthwise direction for each respective channel. 2. The adsorption vessel of claim 1 wherein the plurality of perforated adsorbent particles number at least 100; and wherein the packed bed region has an interparticle void fraction ranging from 0.09 to 0.5. 3. The adsorption vessel of claim 1 wherein the adsorbent particles are irregularly arranged in the packed bed region. 4. The adsorption vessel of claim 1 wherein the adsorbent particles are contiguously arranged in a horizontal and a vertical direction of the packed bed region. 5. The adsorption vessel of claim 1 wherein each adsorbent particle of the adsorbent particles in the packed bed region lies beside at least a portion of at least one neighboring adsorbent particle of the adsorbent particles in the packed bed region and lies above or below at least a portion of at least one other neighboring adsorbent particle of the adsorbent particles in the packed bed region. 6. The adsorption vessel of claim 1 wherein each of the adsorbent particles has an upper end portion facing upward and a lower end portion facing downward, the upper end portion of a first group of adsorbent particles of the plurality of perforated adsorbent particles being in contact with the lower end portion of a second group of adsorbent particles of the packed bed region and/or the lower end portion of the first group of adsorbent particles being in contact with the upper end portion of a third group of adsorbent particles of the packed bed region. 7. The adsorption vessel of claim 6, wherein the second adsorbent particles and/or the third adsorbent particles are perforated adsorbent particles of the plurality of perforated adsorbent particles. 8. The adsorption vessel of claim 1 wherein each channel of the plurality of channels has a respective distance of travel through the channel from the first end to the second end where the respective distance of travel is less than 150% of a respective straight-line distance from the first end to the second end for each channel. 9. The adsorption vessel of claim 1 wherein the channels of the plurality of channels do not intersect one another. 10. The adsorption vessel of claim 1 wherein each perforated adsorbent particle of the plurality of perforated adsorbent particles has a respective void fraction, VCVT, ranging from 0.05 to 0.5, where VC is the void volume in each perforated adsorbent particle formed by a respective total number of channels in each respective perforated adsorbent particle, and VT is the total volume of the perforated adsorbent particle including the void volume, each perforated adsorbent particle having no more and no less than its respective total number of channels. 11. The adsorption vessel of claim 1 wherein each adsorbent particle of the plurality of adsorbent particles has a longest spatial dimension wherein the longest spatial dimension is from 1 mm to 50 mm. 12. A process for separating a gaseous mixture comprising at least two gaseous components, the process comprising: passing the gaseous mixture to an adsorption unit, the adsorption unit comprising one or more adsorption vessels of claim 1; andseparating the at least one more strongly adsorbable component from an at least one less strongly adsorbable component in the gaseous mixture in the adsorption unit to form a first product stream enriched in the at least one less strongly adsorbable component and a second product stream enriched in the at least one more strongly adsorbable component. 13. The process of claim 12 wherein the plurality of perforated adsorbent particles number at least 100; and wherein the packed bed region has an interparticle void fraction ranging from 0.09 to 0.5. 14. The process of claim 12 wherein each adsorbent particle of the plurality of adsorbent particles has a respective void fraction, VCVT, ranging from 0.05 to 0.5, where VC is the void volume in the adsorbent particle formed by a respective total number of channels in each respective adsorbent particle, and VT is the total volume of the adsorbent particle including the void volume, each adsorbent particle having no more and no less than its respective total number of channels. 15. A method for making a plurality of adsorbent particles, the method comprising: (a) forming a composite rope comprising a precursor for forming an adsorbent material and fibers embedded in the precursor such that the fibers extend in a lengthwise direction of the composite rope, wherein the adsorbent material is a material selected from the group consisting of activated alumina, activated carbon, zeolites, mesopore-structured materials, carbon molecular sieve, metal-organic framework materials, silica gel, and combinations thereof;(b) forming dried particle intermediates by drying and dividing the composite rope or by dividing the composite rope to form particle intermediates and drying the particle intermediates; and(c) removing the fibers from the particle intermediates by chemically dissolving the fibers and/or firing to burn out the fibers to form the plurality of channels in each adsorbent particle of the plurality of adsorbent particles;wherein step (a) comprises extruding a paste comprising the fibers and the precursor through an orifice to form the composite rope. 16. A method for making a plurality of the adsorbent particles, the method comprising: (a) forming a composite rope comprising a precursor for forming an adsorbent material and fibers embedded in the precursor such that the fibers extend in a lengthwise direction of the composite rope, wherein the adsorbent material is a material selected from the group consisting of activated alumina, activated carbon, zeolites, mesopore-structured materials, carbon molecular sieve, metal-organic framework materials, silica gel, and combinations thereof;(b) forming dried particle intermediates by drying and dividing the composite rope or by dividing the composite rope to form particle intermediates and drying the particle intermediates; and(c) removing the fibers from the particle intermediates by chemically dissolving the fibers and/or firing to burn out the fibers to form the plurality of channels in each adsorbent particle of the plurality of adsorbent particles;wherein step (a) comprises coating the fibers with a suspension containing the precursor to form a plurality of fibrous unit cells and drawing the plurality of fibrous unit cells together to form the composite rope. 17. The method of claim 16 wherein the fibers are coated by spray-coating and/or dip-coating.