摘要:
Compounds having the perovskite-type AB03 structure wherein 1 to 20% of the B site cations are Ru or Pt, the remainder consisting essentially of cobalt, preferably partially tetravalent and the A sites being occupied by a mixture of lanthanide ions and ions of Group IA, IIA, and IVA of the Periodic Table having an ionic radius of about 0.9 to about 1.65 A are useful catalysts for reduction and oxidation reactions, particularly for the cleanup of exhaust gases of internal combustion engines.
摘要:
Catalysts for the oxidative purification of exhaust gases such as the exhaust gases from internal combustion engines, are prepared by applying a suspension whose solid content consists essentially of boehmite to a ceramic support body thereby forming an intermediate coating which is adapted to receive one or more metals of the platinum group or alloys thereof in finely divided form. The thus treated support body is thereafter heated. The coating suspension also can contain dissolved aluminum nitrate. The intermediate coating of boehmite on the support body is converted to active aluminum oxide prior to impregnation with one or more metals of the platinum group or alloys thereof in finely divided form or the conversion can take place after such impregnation, for example, by heating upon exposure to the hot exhaust gases of an internal combustion engine.
摘要:
A process for hydrocracking a hydrocarbonaceous charge stock using a catalytic composite of an alumina-containing, porous carrier material and a nickel component. The composite is prepared via coextrusion, and contains from about 6.5 to about 10.5% by weight of nickel, calculated as the element, within which range maximum hydrocracking activity and stability are attained.
摘要:
1. A PROCESS FOR THE PREPARATION OF A CATALYST MASS HAVING A CATALYTICALLY ACTIVE COMPONENT PRECIPITATED ONTO A FINELY DEVIDED PARTICULATE, INORGANIC SUPPORTING CARRIER MATERIAL, WHEREIN SAID CATALYTICALLY ACTIVE COMPONENT IS IN THE FORM OF MO.FE2O3 WHERE M REPRESENTS A BIVALENT METAL SELECTED FROM THE GROUP CONSISTING OF IRON, NICKEL, COBALT, ZINC AND MANGANESE, SAID PROCESS COMPRISING: FORMING A SUSPENSION OF SAID FINELY DIVIDED PARTICULATE, INOTGANIC SUPPORTING CARRIER MATERIAL IN AN AQUEOUS SOLUTION CONTAINING IRON IONS IN THE BIVALENT STATE AND IONS OF AT LEAST ONE OF SAID FINELY DIVIDED PARTICULATE, GRADUALLY AND HOMOGENEOUSLY CONVERTING AT LEAST A PORTION OF SAID IRON IONS IN THE BIVALENT STATE TO THE TRIVALENT STATE WHILW AGITATING SAID SUPERSION IN THE ABSENCE OF MOLECULAR OXYGEN, AND SUSPENSION IN THE PH OF SIAD AQUEOUS SOLUTION IN THE RANGE OF 2 TO 6.5, SAID GRADUAL AND HOMOGENEOUS CONVERSION PROCEEDING AT A RATE SUCH THAT THE INCREASE IN THE AMOUNT OF SAID IRON IONS IN THE TRIVALENT STATE IN SAID SUSPENSION IS NO GREATER THAN 0.5 MOLES PER LITER PER MINUTE; AND THE DIFFERENCE IN CONCENTRATION OF SAID IRON IONS IN THE TRIVALENT STATE IN SAID SUSPENSION IS NO SAID AQUEOUS SOLUTION DOES NOT EXCEES 0.001 MOLES PER LITER OF SOLUTION; WHERENY SAID CATALYTICALLY ACTIVE COMPONENT IS CAUSED TO PRECITATE ONTO SAID SUPPORTING CARRIER MATERISL FORMING SAIS PARTICULATE CATALYST MASS, SAID PARTICULATWE CATALYST MASS BEING THEREAFTER SEPARATED FROM SAID AQUEOUS SOLUTION AND DRIED.
摘要:
AN ALKYLAROMATIC HYDROCARBON IS DEALKYLATED BY CONTACTING IT, IN THE PRESENCE OF STEAM AND AT A TEMPERATURE RANGING FROM 350 TO 500* C., WITH A CATALYST COMPRISING NICKEL, AND AT LEAST ONE METAL SELECTED FROM PALLADIUM, IRON, IRIDIUM, RHODIUM, THALLIUM, CERIUM, SELENIUM, ANTIMONY, CADMIUM, TUNGSTEN, BARIUM, SODIUM, POTASSIUM, AND RHENIUM, SUPPORTED ON A CARRIER, PREFERABLY ALUMINA.
摘要:
ORGANIC COMPOUNDS ARE OXIDATIVELY DEHYDROGENATED IN THE PRESENCE OF A SOLID CATALYST COMPRISING COBALT, PHOSPHORUS, COMBINED OXYGEN AND AT LEAST ONE METAL FOROM THE GROUP INDIUM, MAGNESIUM, ALUMINUM THORIUM, YTTRIUM, CADIMIUM, LEAD, BERYLLINUM, ZINC, MANGANESE, SILVER, CERIUM, ZIRCONIUM, BORON AND CALCIUM.
摘要:
IMPROVED OXIDATIVE DEHYDROGENATION CATALYST CAN BE PREPARED BY MODIFYING METAL FERRITE OXIDATIVE DEHYDROGENATION CATALYSTS WITH TITANIUM OR ZIRCONIUM. FOR EXAMPLE, AA PROMOTING AMOUNT OF ZIRCONIUM OXIDE, 10% CAN BE ADDED TO MANGANESE FERRITE. THE IMPROVEMENT MAY BE IN CONVERSION, SELECTIVELY OR YIELD OR IN TEMPERATURE OF OPERATION.
摘要:
A partially deactivated metal ferrite oxidative dehydrogenation catalyst can be reactivated by contacting the catalyst with a relatively large amount of halogen. For example the yield from a Mg ferrite used in the oxidative dehydrogenation of n-butenes to butadiene had declined from 55.1 to 52.4 percent after 1,350 hours on stream. The catalyst was treated with up to 6,800 ppm of chlorine and after termination of the halogen and removal of residual halogen the yield was 55.9 percent. It was not necessary to remove the catalyst for activation or to stop the oxidative dehydrogenation.