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Disclosed are silica bound zeolite adsorbent particles which possess high volumetric gas adsorption capacity for the adsorption and/or desorption of gases. The adsorbent are highly effective as a gas source in volumetrically constrained applications. The silica-bound zeolite adsorbents possess a rel

Disclosed are silica bound zeolite adsorbent particles which possess high volumetric gas adsorption capacity for the adsorption and/or desorption of gases. The adsorbent are highly effective as a gas source in volumetrically constrained applications. The silica-bound zeolite adsorbents possess a relatively high zeolite content simultaneously with a relatively low intra-particle pore volume as compared to the clay bound zeolite aggregates heretofore used as a gas source in volumetrically constrained environments, e.g. instant beverage carbonation processes, devices or systems.

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1. A plurality of adsorbent particles, wherein the particles comprise zeolite powders bound with a silica binder, wherein the zeolite has a silica to alumina (SiO2/Al2O3) ratio of less than 6 and wherein the silica binder content in the particles is at least 5 wt %, based on the total weight of the

1. A plurality of adsorbent particles, wherein the particles comprise zeolite powders bound with a silica binder, wherein the zeolite has a silica to alumina (SiO2/Al2O3) ratio of less than 6 and wherein the silica binder content in the particles is at least 5 wt %, based on the total weight of the particles; wherein the adsorbent particles have a mean diameter of greater than 800 microns and a) a zeolite crystal density within a loose bed sufficient to provide an effective zeolite crystal mass loading within the bed of at least 52 g/100 cc, and/orb) a zeolite crystal density within a loose bed sufficient to provide an effective zeolite crystal volume loading within the bed of at least 36 cc/100 cc, orc) a volumetric capacity for CO2 of at least 13.4 g CO2/100 cc of adsorbent. 2. The adsorbent particles of claim 1 wherein the particles have an intra-pore volume of no greater than 0.28 cc/g. 3. The adsorbent particles of claim 1 wherein at least 75% of an adsorbed gas can desorbed from the adsorbent particles containing a desired gas within 30 seconds when the adsorbent particles are wetted with a volume of water in excess of the volume of the gas containing adsorbent. 4. Adsorbent particles of claim 1 wherein the silica binder is selected from the group consisting of colloidal silica, silicic acid, alkali metal silicate and combinations thereof. 5. Adsorbent particles of any one of claim 1 wherein the particles have an average crush strength of at least about 2.0 lbf. 6. Adsorbent particles of claim 1 wherein the particles have a bulk density of at least about 0.5 g/cc. 7. Adsorbent particles of claim 1 wherein the particles have an Attrition Index of less than about 0.15, as measured by the SUT test. 8. Adsorbent particles of claim 1 wherein the particles are spherical in shape. 9. Adsorbent particles of claim 1 wherein the particles have a mean diameter ranging from about 850 to about 3000 microns. 10. Adsorbent particles of claim 1 wherein the particles have a pore volume, as determined by mercury porosimetry, of ranging from about 0.15 to about 0.28 cc/g. 11. Adsorbent particles of claim 1 wherein the zeolite comprises X-zeolite, Y-zeolite, A-zeolite, omega zeolite, beta zeolite, ZSM-4, ZSM-5, ZSM-10, ZSM-12, ZSM-20, REY, USY, RE-USY, LZ-210, LZ-210-A, LZ-210-M, LZ-210-T, SSZ-24, ZZA-26, SSZ-31, SSZ-33, SSZ-35, SSZ-37, SSZ-41, SSZ-42, SSZ-44, mordenite, faujasite, or combinations thereof. 12. Adsorbent particles of any one of claims 1 to 11 having a gas reversibly adsorbed therein, wherein the gas is H2O, CO2, NH3, SO2, SOx, NOx, CH4, C2-C8 hydrocarbons, N2, O2, H2S, He, Kr, Ar, Ne, Xe, desflurane, diethyl ether.methoxypropane, vinyl ether, halogenated ethers, enflurane, isoflurane, methoxyflurane, sevoflurane, chloroform, halothane, trichloroethylene or combinations thereof. 13. Adsorbent particles of claim 12 wherein the adsorbent particles are contained in a container. 14. A plurality of adsorbent particles according to claim 1 wherein in c) the zeolite of the particles has a silica to alumina (SiO2/Al2O3) ratio of less than 3 and wherein the adsorbent particles have a volumetric capacity volumetric capacity of at least 13.4 g CO2/100 cc of adsorbent. 15. An instant beverage carbonation device or system comprising the adsorbent of claim 1. 16. A portable medical gas delivery device or system comprising the adsorbent of claim 1. 17. A method of manufacturing dense adsorbent particles having a high volumetric capacity, the process comprising: mixing zeolite powder, a silica binder and water in an amount sufficient to form a homogeneous mixture;forming the zeolite/silica mixture to provide dense adsorbent particles having a mean particle diameter of greater than 800 microns;drying the particles; andcalcining the dried particles to provide silica bound zeolite particles having at least 5 wt %, based on the total weight of the particles, of a silica binder, a mean diameter of greater than 800 microns and a zeolite crystal density when poured loosely into a bed sufficient to provide an effective zeolite crystal mass loading within the bed of at least 52 g/100 cc. 18. The method of claim 17 wherein the silica binder is colloidal silica, silicic acid, alkali metal silicate or combinations thereof. 19. The method of claim 17 wherein the silica binder is in an aqueous slurry, wherein the pH of the aqueous slurry of silica binder is adjusted to a pH of 8 or less prior to mixing with the zeolite powder. 20. The method of claim 17 wherein the zeolite powder and silica binder are mixed below incipient wetness. 21. The method of claim 17 wherein the adsorbent particles are formed by agglomeration and compaction, wherein the adsorbent particles are in the form of beads or pellets. 22. The method of claim 17 wherein the adsorbent particles when poured loosely in a bed have an effective zeolite crystal volume loading with the bed of at least 36 g/100 cc, and/or wherein the adsorbent particles have an average crush strength ranging from about 2 to about 8 lbf, and/or the particles have bulk density of at least about 0.5 glee, and/or the particles have an Attrition Index of less than about 0.15, as measured by the SUT Attrition test. 23. The method of any one of claim 17 wherein the zeolite, binder and water is mixed with a high intensity mixer.