摘要:
Hydrocarbons are converted by contacting them at hydrocarbon conversion conditions with a trimetallic acidic catalytic composite comprising a combination of catalytically effective amounts of a platinum group component, a Group IVA component, a bismuth component and a halogen component with a porous carrier material. The platinum group component, Group IVA metallic component, a halogen component are present in the trimetallic catalyst in amounts respectively, calculated on an elemental basis, corresponding to about 0.01 to about 2 wt. % platinum group metal, about 0.01 to about 5 wt. % Group IVA metal and about 0.1 to about 3.5 wt. % halogen. The bismuth component is present in amounts corresponding to an atomic ratio of bismuth to platinum group metal of about 0.1:1 to about 1:1. Moreover, these metallic components are uniformly dispersed throughout the porous carrier material in carefully controlled oxidation states such that substantially all of the platinum group metal and bismuth components are present therein in the corresponding elemental metallic states while substantially all of the Group IVA metallic component is present therein in an oxidation state above that of the corresponding metal. A specific example of the type of hydrocarbon conversion process disclosed is a process for the catalytic reforming of a low-octane gasoline fraction wherein the gasoline fraction and hydrogen stream are contacted with the novel trimetallic catalyst disclosed herein at reforming conditions.
摘要:
A process for upgrading reformer feedstocks containing alkylcyclopentanes by isomerizing said feedstock components in the presence of hydrogen and a catalyst mixture containing a metal halide, such as tantalum and/or niobium pentafluoride, and a protonic acid, such as hydrogen fluoride so that the alkylcyclopentanes are converted to the corresponding cyclohexane isomers.
摘要:
1. A PROCESS FOR THE PREPARATION OF AN OXYCHLORINATION CATALYST COMPRISING THE STEPS OF FORMING A SILICA-MAGNESIA SUPPORT BY FORMING A SILICA HYDROGEL WITH A COMPOUND SELECTED FROM THE GROUP CONSISTING OF MAGNESIUM CHLORIDE, MAGNESIUM BROMIDE, MAGNESIUM PERCHLORATE AND MIXTURES THEREOF, CALCINING THE RESULTING HYDROGEL AT A TEMPERATURE OF 530 TO 700*C. TO FORM THE SUPPORT, WITH THE COMPOUND BEING EMPLOYED IN AN AMOUNT SUFFICIENT TO PROVIDE A HYDROGEL CONTAINING 10 TO 25% MAGNESIA BASED ON THE CALCINED PARTICLES, AND DEPOSITING ON THE SUPPORT A COPPER CHLORIDE CATALYST.
摘要:
1. AN AQUEOUS HOMOGENEOUS SOLUTION CONSISTING ESSENTIALLY OF (A) A WATER-SOLULBE PALLADIUM (II) SALT, SAID SALT BEING SELECTED FROM THE GROUP CONSISTING OF A CHLORIDE, BROMIDDE, NITRATE, SULFATE, AND LI2PDCL4, HAVING A CONCENTRATION OF METAL ION OF AT LEAST ABOUT 0.00005 TO ABOUT 0.025 MOLE PER LITER, (B) COPPER (ii) CHLORIDE OR BROMIDE, (C) A COPPER (II) SALT SELECTED FROM THE GROUP CONSISTING OF A NITRATE, SULFATE, ALKYLSULFONATE, ARYLSUFONATE, TETRAFLUOROBORATE, PERCHLORATE, TRIFLUOROACETATE, TRICHLOROACETATE AND METHANEPHOSPHONATE, AND (D) THE BALANCE WATER, WHEREIN THE TOTAL CONCENTRATION OF (B) AND (C) IS FROM ABOUT 0.003 TO ABOUT 3 MOLES PER LITER, AND WHEREIN THE COPPER (II) CHLORIDE OR BROMIDE (B) COMPRISES FROM ABOUT 10 TO ABOUT 80 MOLE PERCENT OF THE TOTAL OF (B) AND (C).
摘要:
A SHAPED CATALYST BODY FOR HYDROFLUORINATION COMPRISING A HYDROFLUORINATED BODY COMPOSED OF A MIXTURE OF ALUMINUM OXIDE HYDRATE OR ALUMINUM HYDROXIDE WITH 2 TO 60% BY WEIGHT OF BORON TRIOXIDE RELATIVE TO THE STARTING MIXTURE. THE CATALYST BODY IS MADE BY FORMING THE MIXTURE OF THE ABOVE MATERIALS, SOFTENING THE MIXTURE TO A DEGREE THAT IT CAN BE SHAPED, SHAPING IT AND THEN DRYING THE SHAPED BODY AT A TEMPERATURE BETWEEN 120-200*C. FOLLOWED BY ACTIVATING THE CATALYST WITH HYDROGEN FLUORIDE AT A TEMPERATURE BETWEEN 200-500*C. THE CATALYST IS SUED IN THE HYDROFLUORINATION OF ACETYLENE, HALOGENATED OLEFINS AND SIMILAR COMPOUNDS.
摘要:
GRAPHITE-METAL CHLORIDE INTERCALATION COMPOUNDS ARE MADE BY CONTACTING A MIXTURE OF GRAPHITE AND AT LEAST ONE WATER OF HYDRATION CONTAINING METAL CHLORIDE WITH A STREAM OF CHLORINE AT A TEMPERATURE BETWEEN 200*C. AND THE DECOMPOSITION TEMPERATURE OF THE INTERCALATION COMPOUND AND AT A PRESSURE BETWEEN ATMOSPHERIC AND 5 ATM.
摘要:
AN IMPROVED PROCESS FOR PRODUCING CO-CRYSTALS OF TITANIUM TRICHLORIDE AND ALUMINUM TRICHLORIDE WITH A COMPOSITION OF SUBSTANTIALLY THREE MOLES OF TITANIUM TRICHLORIDE AND ONE MOLE OF ALUMINUM TRICHLORIDE OR OTHER DESIRED RATIO, AND SUBSTANTIALLY FREE OF IMPURITIES IS DESCRIBED. SUCH CRYSTALS ARE OF VALUE AS AN ACTIVE CATALYST, PARTICULARLY, FOR EXAMPLE, FOR PREPARING POLYPROPYLENE. THE IMPROVED PROCESS PROVIDED HEREIN INVOLVES THE REMOVAL OF TRACES OF TITANIUM TETRACHLORIDE FROM ALREADY FORMED CO-CRYSTALS BY BALL MILLING THE CO-CRYSTALS IN THE PRESENCE OF A SUFFICIENT QUANTITY OF ALUMINUM POWDER TO SUBSTANTIALLY QUANTITATIVELY REACT WITH TITANIUM TETRACHLORIDE.
摘要:
ADDITIVES ARE PROVIDED TO A CHROMIC OXIDE CATALYST SYSTEM USED FOR OLEFIN POLYMERIZATION WHICH AFFECT THE COURSE OF REACTION AND/OR THE NATURE OF THE POLYMER PRODUCED, THE ADDITIVES BEING COMPOUNDS OF THE METALS OF GROUP II-A AND GROUP III-B OF THE PERIODIC TABLE.
摘要:
A CATALYST HAVING HIGHER ACTIVITY IN FLORINATION OF ACETYLENE AND OTHER HYDROCARBONS IS OBTAINED BY TREATING AN ACIDIC ACTIVE ALUMINA CONTAINING 2 TO 20% BY WEIGHT OF SILICA WIHT HYDROGEN FLORIDE AT A TEMPERATURE OF 200 TO 430*C.
摘要:
Incorporation of 30-65 percent of a hydrogenation metal component into a hydrogel which would yield on drying and calcining without the hydrogenation metals a xerogel of a high compacted bulk density (0.8-1.6 g/cc) low pore volume (0.15-0.45 cc/g.) alumina results in a catalyst having a very high hydrogenation and dentrification activity. Up to about 10 percent fluoride is added to provide a cracking component. The hydrogenation metal component is selected from the oxides of nickel, molybdenum, tungsten, cobalt and mixtures thereof.