Abstract:
AN IMPROVED METHOD OF LUBRICATION OF A CONTROLLED-SLIP DIFFERENTIAL COMPRISES USING A LUBRICANT COMPRISING (A) SYNTHETIC SULFURIZED OIL CONSISTING ESSENTIALLY OF A SULFURIZED BLEND OF LARD OIL AND A C12-24 MONOOLEFIN AND (B) A HYDROCARBON BASE STOCK HAVING A KINEMATIC VISCOSITY AT 210*F. IN THE RANGE OF 1.5-200.0 CS. AND CONTAINING AT BLEND OF AT LEAST ONE C13-C29 NAPHTHENE AND FORM 0.120 PARTS BY WEIGHT, BASED ON SAID NAPHTHENE OF AT LEAST ONE MEMBER FROM AT LEAST ONE OF THE FOLLOWING GROUPS (A), (B), (C) AND (D): (A) A SYNTHETIC LIQUID C3-C4 OLEFIN HOMOPOLYMER COPOLYMER, OR TERPOLYMER; (B) A MEMBER FROM GROUP (A) ABOVE WHICH IS AT LEAST PARTIALLY HYDROGENATED; (C) A SEVERLY HYDROREFINED NAPHTHENIC LUBE CONTAINING LESS THAN 1% OF GEL AROMATIC HYDROCARBONS; AND (D) A SEVERLY HYDROREFINED PARAFFINIC LUBE CONTAINING LESS THAN 1% OF GEL AROMATIC HYDROCARBONS; AND WHEREIN THE AMOUNT OF SAID BLEND WHICH IS PRESENT IN SAID BASE STOCK IS SUFFICIENT TO PROVIDE A GREATER COEFFICIENT OF TRACTION, MEASURED T 600 F./MIN., 200*F., 400,000 P.S.I., THAN WOULD BE PROVIDED BY SUBSTITUTION OF THE SAME AMOUNT OF ASTM OIL NO. 3 FOR SAID BLEND IN SAID BASE STOCK AND WHEREIN SAID LUBRICANT CONTAINS 0.5-10 VOLUMES OF SYNTHETIC SULFURIZED OIL FOR EACH 100 VOLUMES OF SAID BASE STOCK. THE PREFERRED LUBRICANT ALSO CONTINS AN EXTREME PRESSURE ADDITIVE (E.G. TRICRESYL PHOSPHATE) AND AN ADDITIVE WHICH LOWERS THE STATIC FRICTION OF THE LUBRICANT (E.G. A SURFACE-ACTIVE, ORGANIC PHOSPHATE ESTER OF A LINEAR ALIPHATIC, ETHOXYLATED ALCOHOL).
Abstract:
A THERMAL PROCESS FOR THE GENERATION OF SODIUM METAL FROM SODIUM CARBONATE AND COKE BY FEEDING PARTICULATE COKE AND SODIUM CARBONATE TO SODIUM GENERATOR, CONDUCTING MOLTEN SODIUM CARBONATE CONTAINING UNREACTED COKE BY GRAVITY FLOW FROM THE UPPER PORTION OF THE GENERATOR TO THE BOTTOM OF A FURNACE, SAID FURNACE BEING FED WITH A SOURCE OF OXYGEN TO OBTAIN ESSENTIALLY COMPLETE COMBUSTION OF THE COKE, RECIRCULATING THE MOLTEN SODIUM CARBONATE BY GRAVITY FLOW FROM AN UPPER PORTION OF THE FURNACE TO THE BOTTOM OF THE GENERATOR, CONDUCTING VAPORS OF CARBON MONOXIDE AND SODIUM FROM THE GENERATOR TO A QUENCH SYSTEM, RECOVERING CONDENSED LIQUID SODIUM FROM THE BOTTOM OF THE QUENCH SYSTEM, THE CARBON MONOXIDE EXITING FROM THE QUENCH SYSTEM BEING RETURNED TO THE FURNACE OF COMBUSTION TO CARBON DIOXIDE.
Abstract:
A system for the irradiation of a target with electromagnetic energies covering the region between approximately the infra-Xray and the trans-infrared portions of the spectrum comprises: light associated with a shock wave front aligned to strike a tape valve comprising a movable tape, impervious to said shock wave, having a mirror-like surface and also at least one aperture in spaced relation to said surface and means for moving said tape at a speed such that said light strikes the mirror-like surface and said shock wave front passes through said aperture; a shock sensitive irradiable target optically coupled to said mirror-like surface and said movable member, whereby to provide via said movable member a light-coupling between said target and light source.
Abstract:
Process of dehydrocyclizing C6-C10 hydrocarbons using a lithium, sodium or potassium zeolite X or a lithium, sodium or potassium zeolite Y which zeolite has been impregnated with from 0.10 to 1.2 wt. percent platinum and from 0.10 to 1.2 wt. percent rhenium and then reduced with hydrogen to the free metal. The dehydrocyclization reaction is carried out at from 500* to 560* C. and preferably from 510* to 555* C. using a partial pressure of hydrogen of from 10 to 300 p.s.i.g. and preferably from 50 to 200 p.s.i.g. to form benzene and alkylbenzenes.
Abstract:
A PROCESS FOR MAKING NITRILES FROM ALKYL SUBSTITUTED AROMATIC HYDROCARBONS BY CONTACTING VAPORS OF SAID ALKYL AROMATIC HYDROCARBONS AND VAPORIZED AMMONIUM POLYSULFIDE AT A TEMPERATURE OF ABOUT 300* TO ABOUT 500* C., AT ESSENTIALLY ATMOSPHERIC PRESSURE, AND IN THE PRESENCE OF A CATALYST COMPRISING AHIGHER OXIDE OF ELEMENTS OF GROUPSV-B, VI-B, THE LANTHANIDE GROUP, AND THE ACTINIDE GROUP.
WHERE R1 ABD R2 ARE HYDROGEN OR HYDROCARBYL RADICALS HAVING 1 TO 20 CARBON ATOMS AND N REPRESENTS THE NUMBER OF REPEATING UNITS. THESE RESINS ARE VALUABLE IN THE MANUFACTURE OF COATINGS, MOLDING RESINS, ADHESIVES, POTTING AND ENCAPSULATION APPLICATIONS AND THE LIKE.
Abstract:
SELECTIVE ADSORPTION OF P-XYLENE FROM A FLUID MIXTURE CONTAINING M-XYLENE CAB BE OBTAINED WITH COPPER-EXCHANGED MOLECULAR SIEVES (CRYSTALLINE ALUMINO-SILICATE ZEOLITES) WHICH HAVE A WATER LOSS ON IGNITION AT 800* C. IN THE RANGE OF 8-20 WT. PERCENT AND PREFERABLY, HAVE BEEN PARTIALLY DEHYDRATED AT A TEMPERATURE IN THE RANGE OF 50-300* C. PREFERABLY THE AL/SI RATIO IN THE ZEOLITE FRAMEWORK IS IN THE RANGE OF 0.2-0.65. FOR EXAMPLE, P-XYLENE CAN BE SEPARATED FROM M-XYLENE BY SELECTIVE ADSORPTION AT 100* C. OF THE P-XYLENE ON CUY ZEOLITE WHICH WAS PARTIALLY DEHYDRATED AT 82* C. AND CONTAINED ABOUT 15 WT. PERCENT WATER BY IGNITION ANALYSIS.
Abstract:
ADDITIVES FOR INCREASING THE OCTANE RATING OF GASOLINE MAY BE OBTAINED FRON C1-6 ALDEHYDES OR C3-6 KETONES BY CONVERTING THEM INTO HIGHER MOLECULAR WEIGHT UNSATURATED CORBOYYL COMPOUNDS FOLOWED BY PARTIAL ISOMERIZATION OF THE DOUBLE BOND AND OR PARTIAL ISOMZATION OF FROM A FURAN RING. THESE STEPS PROVIDE A MIXTURE OF COMPOUNDS WHICH NEED NOT BE SEPARATED INTO THEIR PURE COMPONENTS AMD WHICH POSSESS A HIGHER BVON THAN THE STARTING MATERIAL.
Abstract:
A PROCESS FOR PREPARING 2-PYRROLIDINONE WHICH COMPRISES REACTING SUCCINONITRILE IN AQUEOUS SOLUTION AND IN THE ABSENCE OF ADDED AMMONIA WITH HYDROGEN IN THE PRESENCE OF A RANEY COBALT CATALYST, AT A TEMPERATURE OF FROM ABOUT 250*C. TO ABOUT 300*C. AND AT A HYDROGEN PRESSURE OF FROM ABOUT 2000 TO ABOUT 3500 P.S.I.G.
Abstract:
SELECTIVE ADSORPTION OF 2,6-DIMETHYLNAPHTHALENE FROM A EUTECTIC MIXTURE WITH 1,5-DIMETHYLNAPHTHALENE CAN BE OBTAINED WITH PARTIALLY DEHYDRATED MOLECULAR SIEVES (CRYSTALLINE ALUMINO-SILICATE ZEOLITE). PREFERABLY THE AL-SI RATIO IN THE ZELOITE FRAMWORK IS IN THE RANGE OF 0.2-0.65, MORE PREFEREED 0.2-0.35 (EG., TYPE L). THE UNADSORBED RAFFINIATE FRACTION CAN BE FED TO AN ISOMERIZATION STEP.