Abstract:
NEUTRAL S-2-HYDROCARBYLTHIOALKYL ESTERS OF THIOPHOSPHOROUS ACIDS ARE PREPARED THROUGH THE DISPLACEMENT REACTION OF A 2-HYDROCARBYL-2-HYDROCARBYLTHIOETHYL HALIDE ALONE OR IN ADMIXTURE WITH THE CORRESPONDING ISOMERIC SECONDARY HALIDE COMPOUND WITH A DIORGANO THIOPHOSPHATE, THIOPHOSPHONATE OR THIOPHOSPHINATE SALT, THE DISPLACEMENT REACTIONS ARE CONDUCTED AT MODERATE TEMPERATURES AND PRESSURE, PREFERABLY IN THE PRESSENCE OF A POLAR DILUENT. THE PERFERRED THIOPHOSPHORUS ACID AND DIALKYL MONOTHIOPHOSPHORIC ACIDS. THE PREFERRED HALIDE REACTANTS ARE 2-ALKYL-2-ALKYTHIOETHYL CHLORIDES ALONE OR IN COMBINATION WITH 1-ALKYL-2-ALKYLTHIOETHYL CHLORIDES. THE COMPOUNDS DERIVED FROM THE DISPLACEMENT REACTIONS POSSES PARTICULARLY GOOD PESTICIDAL ACTIVITY.
Abstract:
A SATURATED C3-C4 HYDROCARBON FEED IS DEHYDROGENATED WITH AN OXYGEN-CONTAINING GAS AND A FLUIDIZED CATALYST, SUCH AS, BISMUTH PHOSPHATE ON ACTIVATED ALUMINA, VANADIUM OXIDE OR BISMUTH OXIDE, TO FORM C3 AND C4 MONO OLEFINS. THE OLEFIN FRACTION IS THAN ALKAYLATED WITH ISOPARAFFIN AND A CATALYST, SUCH AS H2SO4, HF OR ZEOLITES. THE OLEFIN FRACTION MAY BE HYDROGENATED PRIOR TO ALKYLATION TO CONVERTE ANY BUTADIENE FORMED IN THE DEHYDROGENATION REACTION TO BUTENE.
Abstract:
AN ETHYLENE GROWTH PROCESS FOR OBTAINING REACTION PRODUCT MIXTURES RICH IN LINEAR C22 TO C200 WAX RANG OLEFINS, ESPECIALLY LINEAR ALPHA OLEFINS OF THE C40 TO C100 CARBON NUMBER RANGE. AN ETHYLENE OLIGOMERIZATION REACTION IS CONDUCTED IN A DILUENT IN THE PRESENCE OF AN OLIGMERIZATION CATALYST MIXTURE CONSISTING OF A TRANSITION METAL HALIDE AND AN ORGANOLAUMINUM HALIDE, PREVIOUSLY MODIFIED BY TREATMENT WITH A PI BASE COMPOUND, PARTICULARLY A PIBASE AROMATIC COMPOUND, TO YIELD SAID WAX RANGE WITHOUT SUBSTANTIALY PRODUCTION OF HIGH MOLECULAR WEIGHT POLYMERS. PRESSURES AND TEMPERATURES ARE SELECTED TO MAINTAIN A MOLAR RATIO OF ETHYLENE TO PRODUCTS OLEFINS SUFFICIENT TO MINIMI ZE COPOLYMERIZABLE OF THE PRODUCT OLEFINS.
Abstract:
DIORGANO THIOPHOSPHORUS ACIDS, SUCH AS DIHYDROCARBYL DITHIO-AND MONOTHIOPHOSPHORIC ACIDS, O-ALKYL DITHIOPHOSPHONIC ACIDS, DIHYDROCARBYL DITHIOPHOSPHINIC ACIDS, ETC., CAN BE READILY ADDED TO N-VINYL COMPOUNDS. ON ADDITION THE CORRESPONDING MARKOVNIKOV TYPE ADDUCTS, E.E. NEUTRAL S-SUBSTITUTED A-AMINOETHYL PHOSPHORUS ESTERS ARE FORMED IN THE PRESENCE AND IN THE ABSENCE OF ADDED IONIC CATALYSTS. THE ADDUCTS ARE USEFUL AS PESTICIDES, PARTICULARLY FOR THE CONTROL OF ANIMAL AND PLANT PESTS SUCH AS INSECTS, MITES AND FUNGI. THE PESTICIDAL EFFECTIVENESS OF THE ADDUCTS DERIVED FROM N-VINYL SUBSTITUTED CYCLIC IMIDES AND AMIDES IS SURPRISINGLY SUPERIOR TO STRUCTURALLY RELATED KNOWN PESTICIDES.
Abstract:
CORROSION OF FERROUS METALS BY CORROSIVE ACIDS AT ELEVATED TEMPERATURES IS INHIBITED BY ADDING TO THE CORROSIVE ACID A COMPOSITION COMPRISING EFFECTIVE AMOUNTS OF AT LEAST 2 ACETYLENIC ALCOHOLS, A QUINOLINE QUATERNARY COMPOUND AND AN ORGANIC FLUORIDE HAVING THE STRUCTURE:
1-Y,2-(CNF(2N+1)-)-2-IMIDAZOLINIUM (X.3H2O)(-)
WHERE N IS AN INTEGER FROM 3 TO 10; X IS SELECTED FROM THE GROUP CONSISTING OF BROMINE AND IODINE; AND Y IS A GLYCOL HAVING 3 TO 10 CARBON ATOMS. THE COMPOSITION MAY CONTAIN A TERPENE ALCOHOL, AN ALIPHATIC ALCOHOL AND A DISPERSING AGENT SUCH ASS AN ETHOXYLATED OLEATE AND THE LIKE.
Abstract:
A process for upgrading and improving the color, odor and stability of petroleum oils to render the latter suitable for use in specialty applications. Raw distillates and semi-refined oils of suitable boiling range and viscosity are refined, or further refined, in a hydrogenation process, at suitable conditions, in the presence of a catalyst which comprises a support and a transition metal complexed with an organometallic compound, to yield colorless mineral oils, i.e., white oils. These highly refined oils are used in pharmaceuticals and cosmetics and similar compositions requiring oil components that meet certain high quality standards.
Abstract:
An improved process for dewaxing and deoiling a petroleum oil stock with a liquid, normally gaseous solvent in which the oil feed is chilled prior to autorefrigeration by dilution with cold recycled filtrate from the final filtration of the wax-oilsolvent mixture.
Abstract:
Mineral lubricating oil compositions containing oil-soluble overbased alkaline earth metal hydrocarbon sulfonates, employed in internal combustion engines, are improved as to their antirust, sludge inhibiting and/or antiwear properties by incorporating into such compositions, in colloidal form, small amounts, for example 0.01 to 10.0 wt. percent, of the total oil composition, of in situ formed oil-insoluble inorganic alkaline earth metal phosphorus salts derived from the lower oxy or thio acids of phosphorus or from the corresponding oxides or sulfides of phosphorus which, upon hydrolysis, yield the lower oxy or thio acids of phosphorus. The preferred process of preparing such compositions involves the treatment of the neutral or overbased alkaline earth metal sulfonates, either of petroleum origin or of synthetic long chain alkaryl origin, or mineral oil concentrates thereof, and which have been in the past, conventionally employed as oil additives, with up to the stoichiometric amount of the phosphorus acid, thio acid, oxide or sulfide required to at least partially neutralize the free alkalinity of the overbased sulfonate, filtering therefrom any precipitate formed as a result of such treatment of the sulfonate or oil concentrate thereof, and recovering an oil-soluble alkaline earth metal sulfonate product, or oil concentrate thereof, containing colloidal oilinsoluble alkaline earth metal phosphorus compounds of reducing nature formed in situ.
Abstract:
AN IMPROVED FLUIDIZED CATALYTIC CRACKING PROCESS IS PROVIDED WHICH COMPRISES FEEDING A SUBSTANTIALLY LIQUID HYDROCARBON OIL FEEDSTOCK TO AT LEAST ONE FEED INJECTION ZONE OF A FLUIDIZED CATALYTIC CRACKING REACTION ZONE, CONCURRENTLY FEEDING STEAM TO SAID INJECTION ZONE IN A VOLUMETRIC RATIO OF STEAM TO LIQUID HYDROCARBON RANGING FROM ABOUT 3 TO ABOUT 75, THEREBY IMPARTING TO THE RESULTING MIXTURE AN EXIT VELOCITY RELATIVE TO THE FLUIDIZED CATALYST OF AT LEAST ABOUT 100 FEET PER SECOND, WHEREBY THE OIL FEEDSTOCK IS ESSENTIALLY COMPLETELY ATOMIZED FORMING DROPLETS LESS THAN ABOUT 350 MICRONS IN DIAMETER.
Abstract:
THIS INVENTION RELATES TO A FLUID COKING-STEAM CRACKING FURNACE COMBINATION PROCESS FOR PRODUCING COKE AND GASEOUS HYDROCARBONS FROM A HEAVY HYDROCARBON FEEDSTOCK WHEREIN A SUBSTANTIAL PORTION OF THE HEAT REQUIREMENTS FOR THE ENDOTHERMIC-CRACKING REACTION IN THE FLUID COKING VESSEL ARE MET BY PASSING STEAM THROUGH A FURNACE, PREFERABLY A STEAM CRACKING FURNACE, AND THEREAFTER INTRODUCING SAID HEATED STEAM INTO THE BOTTOM OF THE FLUIDIZED BED OF THE COKER VESSEL. IN ONE EMBODIMENT, STEAM IS FIRST HEATED IN A STEAM CRACKING FURNACE AND INTRODUCED INTO THE BOTTOM OF THE FLUID BED TO PROVIDE A SUBSTANTIAL PORTION OF THE HEAT REQUIREMENTS FOR THE CRACKING REACTION. THE REMAINING PORTION OF THE HEAT REQUIREMENTS FOR THE CRACKING REACTION ARE SUPPLIED BY EMPLOYING HEAT TRANSFER SURFACES WITHIN THE FLUID BED OF THE COKER VESSEL. HEAT IS SUPPLIED TO THE HEAT TRANSFER SURFACES BY PASSING A HOT MOLTEN MEDIUM, SUCH AS MOLTEN LEAD, OR HOT COMBUSTION GASES WITHIN SAID HEAT TRANSFER SURFACES. IN ANOTHER EMBODIMENT, THE HEAT REQUIREMENTS FOR THE ENDOTHERMIC CRACKING REACTION ARE SUPPLIED BY INTRODUCING STEAM, WHICH HAS BEEN HEATED IN A STEAM CRACKING FURNACE, INTO THE BOTTOM OF THE FLUID BED, AND WITHDRAWING CARBONACEOUS MATERIAL FROM THE FLUID BED AND CONTACTING SAID MATERIAL WITH HEAT TRANSFER SURFACES LOCATED IN AN EXTERNAL HEAT EXCHANGER TO PROVIDE THE REMAINING PORTION OF THE HEAT REQUIRED FOR THE CRACKING REACTION. THE INTRODUCTION OF STEAM INTO THE BOTTOM OF THE FLUID BED, IN ADDITION TO SUPPLYING A SUBSTANTIAL PORTION OF THE HEAT REQUIREMENTS TO THE FLUID BED, FUNCTIONS TO FLUIDIZE THE BED AND TO PROVIDE THE DILUENT MEDIUM FOR THE VAPORIZED HYDROCARBONS RECOVERED FROM THE FLUID BED COKING ZONE WHICH ARE THEN PASSED TO A STEAM CRACKING FURNACE TO PRODUCE THE LOW MOLECULAR WEIGHT UNSATURATED PRODUCTS.