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classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J37-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G47-16
filingDate 2010-05-14-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_dd5023f1a9f7ebf5bcc37e8aa5413680
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publicationDate 2010-12-22-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber CZ-302215-B6
titleOfInvention A method for producing an aluminosilicate hydrocracking catalyst
abstract The process for producing the aluminosilicate hydrocracking catalyst consists in that the aqueous solution of sodium aluminate containing at least one dissolved metal compound VI of the periodic system of the element is present. An aqueous solution containing at least one dissolved metal compound (VIII) from a group of periodic elements is formed at least to form a suspension. One activator is silicon dioxide in the form of silica gel silica sol or siloxide. Other activators are fluorine and phosphorus compounds. the slurry filtering the resulting filter cake is washed with water then dried and then milled thereafter until the dried milled portion is dried. The filter wheel is mixed with up to 40 parts by weight of the composition comprising alumina and up to 50 parts by weight of the composition. the weight of silicon oxide in the form of silica gel silica sol or siloxide and up to part by weight of the nickel nitrate solution by the concentration of silicon dioxide. @@ to @@@ Thereafter, the mixture is peptized to up to about 50 parts by weight of the acetic acid solution to a concentration by weight of the acetic acid solution. It is then dried at a temperature of about 0 ° C to about 0 ° C to about 0 ° C to about 0 ° C to about 50 ° C to 50 ° C. Thereafter, the intermediate product is heated at a rate of up to 0 hours per hour at a temperature of about 0 ° C to about 0 ° C. which is annealed for up to hours
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