http://rdf.ncbi.nlm.nih.gov/pubchem/patent/AR-066861-A1

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filingDate 2008-06-04^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_56b7c3d7508aabf51a29adad7322f71e
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publicationDate 2009-09-16^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber AR-066861-A1
titleOfInvention SPHERICAL AGRICULTURE BASED ON ZEOLITE (S), ITS OBTAINING PROCEDURE AND ITS USE IN ADSORTION PROCEDURES OR CATALYSIS
abstract This refers to spherical agglomerates based on zeolite (s) and clay (s), of dominated dimension and morphology, especially dimension less than or equal to 600 um, very good sphericity, high content of zeolitic material, as well as its obtaining procedure These agglomerates are particularly adapted for use in adsorption processes in the gas and / or liquid phase. Claim 7: Method of obtaining agglomerates according to any one of claims 1 to 5, characterized in that it comprises the following steps: 1 / mixing and suspending in crystallites of one or more natural or synthetic powdered zeolites, at least one binder based on a clay or a mixture of clays, possibly up to 5%, preferably between 0.1% and 1%, of the total mass of solids in calcined equivalents of one or more additive (s), preferably organic, which facilitate dispersion, maintenance in suspension, and possibly up to 5% of the total mass of solids in calcined equivalents of a source of liquid and / or solid silica, which preferably represents between 1% and 5% of the total mass of said solids; 2 / atomization conformation of the suspension obtained in 1 / to produce spherical agglomerates in a hot gas at an inlet temperature of between 110 ° C and 300 ° C, preferably between 130 ° C and 250 ° C, possibly followed by a stage sieving and / or spinning; 3 / calcination of the agglomerates obtained in 2 / at a temperature between 500 ° C and 600 ° C, possibly preceded by a post-atomization drying phase; 4 / possibly contacting the resulting product of 3 / with an alkaline basic aqueous solution followed by washing; 5 / possibly partial or total ionic change of the zeolitic agglomerates obtained in 3 / or 4 /, followed by washing; 6 / drying and activation at a temperature between 200 ° C and 600 ° C of the product from stage 4 / or 5 /.
priorityDate 2007-06-04^^<http://www.w3.org/2001/XMLSchema#date>
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