摘要:
A Dy-alumino-silicate catalyst, useful for hydrocarbon conversion reactions, is chemically characterized by the empirical formula Mx(A102)x(SiO2)y.(H2O)z, where x, y and z are integers, the ratio x:y being usually from 1.0 to 0.2 and where at least 25% (and preferably more than 40%) of the negative charge associated with the aluminum of the alumino-silicate framework is satisfied by a cation of Dy or a cation of an oxide or a hydroxide of Dy. Preferably, upon ignition analysis the catalyst will evolve from 1 to 6 molecules of water (typically 1.5-2.5molecules) for each atom of Dy in the catalyst. Typically the negative charge associated with the zeolite framework is not completely satisfied by cations containing Dy and the balance of cations necessary for electronic equivalency comprise H or cations of metals, metal oxides or metal hydroxides. The zeolite also contains less than one alkali metal cation for every four atoms of aluminum in the framework. The zeolite can be amorphous, but preferably is at least partially crystalline and can adsorb benzene.
摘要:
An improved method of preparing a catalyst comprising a Group VIII metal and a Group VIB metal impregnated on a refractory inorganic oxide support or carrier material, said catalyst being especially useful in the hydrorefining of residual oils, and particularly effective for the conversion of sulfurous components contained therein. A more active catalyst results from the order of metals impregnation on the support or carrier material, and from the nature of the impregnating solution.
摘要:
An improved hydrotreating catalyst is prepared by precipitating the oxides or hydrated oxides of aluminum and silicon from an aqueous solution of water-soluble salts (a mixture of aqueous alkaline aluminate and aqueous alkali metal silicate) at 105*120* F at a pH of 5-9.5 and at an alumina concentration, expressed as Al2O3 of 1.2-5.0 wt. percent. The precipitate is washed, impregnated with Group VI-B and Group VIII metals and the impregnated catalyst is dried. An extrudable slurry is formed and extruded; the extrudate is then dried and calcined. The hydrotreating catalyst contains an oxide of a Group VIB metal and an oxide of a Group VIII metal on an alumina support containing 1-20 wt. percent silica. The conventional spray drying step is omitted in the preparation of the present catalyst.
摘要:
A hydroprocessing catalyst having preferred surface area and pore volume ranges located in pores having diameters ranging from 30-80A and greater than 2000A. Pore volume in the 200-2000A diameter range is kept to a minimum. The catalyst is a mixture of Group VIB and Group VIII metal oxides or sulfides on an alumina support. The catalyst shows exceptional activity maintenance in hydrodesulfurization of heavy hydrocarbon feed stocks containing asphaltenes.
摘要:
Shaped bodies of a molecular sieve zeolite having an improved mechanical hardness greater than 5 kp are produced by spraying an unstable silicic acid sol as the binder on to a zone of the rotating plate of a granulating device and concurrently applying the pulverized zeolite particles to another zone of the rotating plate, while avoiding the formation of a plastic mass, and the thus produced shaped bodies are dried and activated according to the disclosed process. The unstable silicic acid sol has a silicic acid content greater than 10 percent by weight and a BET surface greater than 150 m2/g.
摘要:
Synthetic faujasite is exchanged with a combination of rare earth and transition metal ions. The resulting exchanged faujasites possess high thermal and steam stabilities and find utility as hydrocarbon conversion catalysts.
摘要:
A high specific surface area silica for support of e.g., platinum catalysts is obtained by acid leaching of a ceramic, particularly a corrugated structure, containing a cordierite phase.
摘要:
A process for an improved hydrodesulfurization catalyst comprising incorporation of a molybdenum in a washed alumina hydrogel which is then spray-dried, mix-mulled, extruded, dried and calcined, promoted with an aqueous urea-containing cobalt source, and activated.
摘要:
In order to increase the amount of catalytic metal which can be incorporated in a zeolite catalyst by contact of zeolite with solution of a given amount of chemical containing the catalytic metal, or conversely to reduce the amount of such chemical needed to incorporate a given desired amount of catalytic metal in the catalyst, a zeolite containing a cation, e.g., sodium, replaceable by ammonium ion, is contacted with an aqueous solution of ammonium metalate, e.g., molybdate, and a second ammonium compound, e.g., ammonium chloride, said second ammonium compound providing additional anion for balancing the change of said cation in the solution.
摘要:
A film of a noble metal is deposited on the surface of a carrier without substantial penetration of the carrier by immersing the carrier first in a dilute solution of a salt of the noble metal, removing the carrier and heating and drying it to produce precipitation cores of the noble metal on the surface of the carrier, and then immersing the carrier with the precipitation cores in a solution of a noble metal salt which also contains a reducing agent for the salt and a stabilizer for the solution. The film of noble metal thus produced on the surface is adherent thereto and is highly active as a catalyzer for removing pollutants from the exhaust gas of an automobile.