Abstract:
The loading of a gas generating bed such as activated charcoal with a fluid such as dinitrogen tetroxide by exposing the bed to an atmosphere of the fluid.
Abstract:
A METHOD FOR PREPARING A SUPPORTED CATALYST FOR USE IN OXIDIZING ETHYLENE TO ETHYLENE OXIDE, SAID SUPPORTED CATALYST CONSISTING ESSENTIALLY OF SILVER TO THE EXTENT OF 7 TO 30% BY WEIGHT WITH RESPECT TO THE SUPPORT, AND OF A MEMBER SELECTED FROM THE GROUP CONSISTING OF PLATINUM, PALLADIUM AND GOLD TO AN EXTENT OF FROM 0.01 TO 1.0% BY WEIGHT WITH RESPECT TO SAID SILVER, WHICH COMPRISES: (A) IMPREGNATING A SOLID, INERT SUBDIVIDED SUPPORT, AT A TEMPERATURE OF FROM 60* C.TO 115* C., WITH A SOLUTION OF SILVER LACTATE IN LACTIC ACID CONTAINING IN SUSPENSION, CARBON AND AT LEAST ONE METAL SELECTED FROM THE GROUP CONSISTING OF PALLADIUM, PLATINUM AND GOLD, SAID LACTIC ACID BEING PRESENT IN A MOLAR EXCESS OF FROM 20% TO 200% WITH RESPECT TO THE NUMBER OF MOLS REQUIRED FOR COMPLETE SALIFICATION OF SAID SILVER. (B) DRYING THE PARTICLES THUS IMPREGNATED IN A STREAM OF AIR AT A TEMPERATURE RISING TO A MAXIMUM, BUT NOT EXCEEDING 130* C. FOR A PERIOD OF FROM 1 TO 3 HOURS, AND (C) SUBJECTING THE PARTICLES THUS IMPREGNATED TO A HEAT TREATMENT, SAID TEMPERATURE BEING RAISED GRADUALLY TO A MAXIMUM LEVEL OF BETWEEN 230* C. AND 360* C. OVER A PERIOD OF 10 TO 15 HOURS.
Abstract:
A CATALYST FOR INCREASING THE RATE OF HYDROGENATION REACTIONS INCLUDING A COMPLEX SALT OF THE CHLORIDE, BROMIDE OR IODINE OF ZINC, TIN, ANTIMONY, BISMUTH, CADMIUM, GALLIUM, MERCURY OR ARSENIC, AND THE CORRESPONDING AMMONIUM HALIDE.
Abstract:
SOLID PHOSPHORIC ACID IS THE NAME WHICH HAS COME INTO USE FOR A CALCINED MIXTURE OF AN ACID OF PHOSPHOROUS AND A POROUS SILICEOUS MATERIAL. SOLID PHOSPHORIC ACID CATALYSTS HAVE FOR YEARS BEEN VIRTUALLY THE ONLY CATALYST EFFECTIVE IN MANY REACTIONS INVOLVING OLEFINS, PARTICULARLY THE POLYMERIZATION OF OLEFINS TO FORM HIGH OCTAN FUELS. THESE CATALYSTS ARE WIDELY USE DESPITE THEIR LACK OF STRENGTH AND POOR WEARING QUALITIES. HIGH STRENGTH SOLID PHOSPHORIC ACID CATALYSTS ARE PROVIDED HEREIN, THE UNIQUENESS OF THE CATALYST BEING ATTRIBUTABLE TO THE METHOD OR PREPARATION. P2O5 IS DRY BLENDED WITH THE SILICA MATERIAL TO FORM THE PRECURSOR. THE PRECURSOR IS THEN SUBJECTED TO A STEAM-AIR TREATMENT TO BRING ABOUT THE HYDRATION OF THE P2O5. THIS FORMS A SILICO-PHOSPHOROUS MATRIX. THID MATRIX IS PRESERVED BY NOT PHYSICALLY CHANGING THE CATALYST DURING ITS PREPARATION. THIS IS ACCOMPLISHED BY FORMING SPHERES OF THE CATALYST MATERIAL BY TUMBLING AND SPRAYING THE TUMING MASS WITH PHOSPHORIC ACID.
Abstract:
POROUS, ABRASION-RESISTANT BEAD-LIKE CATALYST SUPPORTS FOR REACTIONS IN FLUIDISED BEDS CONTAINING IN A MATRIX OF A SILICON DIOXIDE GELMIXED WITH 0.1 TO 3% BY WEIGHT OF MAGNESIUM OXIDE A SILICON DIOXIDE FILLER WITH A SPECIFIC SURFACE AREA OF 20 TO 200 M.2/G. ACCORDING TO BET IN QUANTITIES OF FROM 20 TO 60% BY WEIGHT AND AN ARGILLACEOUS MINERAL FROM THE GROUP COMPRISING KAOLINITE, MONTMORILLONITE AND ATTAPULGITE IN QUANTITIES OF FROM 5 TO 30% BY WEIGHT, BOTH QUANTITIES BEING RELATED TO THE DRY GRANULATED MATERIAL. THE CATALYST SUPPORTS ARE OBTAINED BY SUSPENDING THE SILICON DIOXIDE FILLER AND THE ARGILLACEOUS MINERAL IN THE AFORESAID QUANTITIES IN AN AQUEOS, STABLE SILICON DIOXIDE SOL WITH A SPECIFIC SURFACE AREA OF 150 TO 400 M.2/G. ACCORDING TO BET AND GELLING THE LIQUID SUSPENSION BY THE ADDITION OF HYDRATED FINALLY DIVIDED MAGNESIUM OXIDE IN QUANTITIES OF 0.1 TO 3% BY WEIGHT AND FEEDING THIS GELLABLE MIXTURE IN DROPLET FORM INTO A LIQUID WHICH IS IMMISCIBLE WITH WATER AND FINALLY SEPARATING THE SULPHATED GRANULATED MATERIAL FROM THE LIQUID AND DRIVING AND HARDENING THE BEAD-LIKE GRANULATED MATERIAL FOR AT LEAST 10 MINUTES AT A TEMPERATURE OF FROM 500 TO 1000*C.
Abstract:
A method of manufacturing an extruded catalyst composite of a Group VIII metal, a Group VIB metal and a refractory inorganic oxide-boron phosphate carrier material. A refractory inorganic oxide hydrogel is prepared and formed into a slurry with an aqueous solution of boric and phosphoric acids. The liquid level of the slurry is adjusted to form an extrudable mass comprising from about 15 to about 45 weight percent solids. The material is then extruded, impregnated with a metal of Group VIII and a metal of Group VIB, dried and calcined in an oxidizing atmosphere.
Abstract:
THE INSTANT PRODUCT IS A REMANUFACTURED CATALYST. USED OR SPENT BISMUTH PHOSPHOMOLYBDATE CATALYST IS REFORMULATED WITH THE ADDITION OF IRON BY COMMUNUTING SAID CATALYST WITH SUFFICIENT WATER TO FORM A PASTE, ADDING AQUEOUS AMMONIUM HEPTAMOLYBDATE SOLUTION TO SAID PASTE TO FORM A SLURRY, ADDING SAID SLURRY TO A SILICA DISPERSION IN WATER ACIDIFIED WITH PHOSPHORIC ACID, ADDING AN IRON SALT IN ACIDIC SOLUTION TO SAID SLURRY AND HOMOGENEOUSLY DISPERSING IT THEREIN TO FORM A SMOOTH MIXTURE, SPRAY-DRYING SAID MIXTURE AND CALCINING THE SPRAY-DRIED PRODUCT.
Abstract:
Producing a precipitate from an aqueous solution of a vanadium compound and a phosphoric acid compound, drying the precipitate, calcining the product, which is not yet finally moulded, at temperatures between about 300* and 650* C. in the presence of air, then grinding and finally moulding it without applying elevated temperatures.
Abstract:
This invention relates to an alkali treated calcium dihydrogen orthophosphate monohydrate adsorbent. Further, it concerns an alkali and trimetaphosphate treated calcium dihydrogen orthophosphate monohydrate adsorbent. Still further, it relates to the processes for the preparation of these adsorbents and to their use in virus purification.
Abstract:
DEHYDROGENATION CATALYSTS OF IMPROVED SELECTIVITY ARE PREPARED BY PRECIPITATING CALCIUM NICKEL PHOSPHATE AT A PH ABOVE 7 IN THE PRESENCE OF A SMALL AMOUNT OF MANGANESE, FOR EXAMPLE 0.1 MOLE PERCENT BASED ON THE COMBINED CALCIUM PLUS NICKEL. ADVANTAGEOUSLY, THE PRECIPITATION MAY BE CARRIED OUT AT A CONSTANT PH. THE RESULTING CALCIUM NICKEL PHOSPHATES ARE ESSENTIALLY IN THE FORM OF B-TRICALCIUM PHOSPHATE AND ARE SUBSTANTIALLY FREE FROM UNDESIRABLE HYDROXYAPATITE.