Abstract: Semiconductor substrate materials, such as silicon, useful in the manufacture of electronic devices, such as integrated circuits, employing low temperature, i.e., below 1025.degree. C. processing cycles are provided with a 0.05 to 2.0 micron thick layer of polysilicon on the backside to improve gettering capabilities of defects, contaminants and impurities away from the active device region of the substrate.

Abstract: Process for increasing silicon deposition rates from silicon halide-hydrogen reaction gases wherein electronic-grade silicon bodies are produced from the deposition of silicon upon silicon slim rods heated and introduced into and pulled through a chemical vapor deposition chamber, the increased silicon deposition rates resulting from introducing small percentages by weight of silane to the silicon halide-hydrogen reaction gases, for example, silicon tetrachloride and/or trichlorosilane.

Abstract: A wafer workpiece polishing temperature control method and apparatus are provided wherein wafers are mounted upon a rotatable pressure plate assembly positioned in rotatable contact with a turntable assembly supported polishing pad, the turntable assembly having internal fluid cooling means, the wafer polishing temperature control being achieved through responsive closed loop electromechanical means activated by variation of polishing pressure upon the wafers and the polishing pad.

Abstract: A process for producing electronic-grade silicon bodies is disclosed wherein continuously-pulled slim rods which can be formed in situ from the reaction of a seed crystal and a molten silicon source, are pulled into and through a chemical vapor deposition chamber, having in combination different gas curtains along the chamber inner wall, the slim rod surfaces being preheated before entry into the deposition chamber where the rods are simultaneously exposed to heating and thermally decomposable gaseous silicon compounds in order to provide suitable surface reaction conditions on the slim rods for the decomposition of the gaseous silicon compounds resulting in deposition growth upon the surfaces of the rods.

Abstract: Oxygen concentration and distribution within silicon crystal rods drawn according to the Czochralski process from silicon melt contained in a silica crucible, are regulated through variation of both the magnitude and relative sense of direction of seed and crucible rotation rates with uniform distribution of the oxygen being accomplished by increasing crucible rotation rate to preselected values as a function of crystal rod growth and melt consumption.

Abstract: Disclosed herein are catalysts useful for oxidation and ammoxidation of hydrocarbons. Such catalysts have the empirical formulaBiMo.sub.a V.sub.b Sb.sub.c M.sub.d O.sub.xwherein a is 0.5-2, b is 0.12-3, c is 0.12-10, d is 0-0.5 and x is selected to satisfy the valence requirements of the other elements present. In such catalysts, M is one or more elements selected from Groups I-A, II-A, III-A, V-A, VI-A, I-B, IV-B, VI-B and VII-B of the Periodic Table.Catalysts according to the invention are prepared by forming a slurry of vanadium antimonate component, a bismuth molybdate component, and optionally the compound M and/or a support material, drying the slurry, and calcining to form the catalyst.Such catalysts are specifically useful for production of acrylonitrile from propylene, ammonia and an oxygen-containing gas.

Abstract: Maleic anhydride is recovered in high yields from gaseous mixtures containing the maleic anhydride in the vapor phase by cooling the gaseous mixture containing the maleic anhydride to a temperature above the dew point of water in the gaseous mixture, and then scrubbing the gaseous mixture with a solvent which comprises a phthalate ester, preferably dibutyl phthalate, and up to 10 weight percent phthalic anhydride. Thereafter, the maleic anhydride is stripped from the solvent in a one-step operation, and the solvent is thereafter recycled to the scrubbing step.

Abstract: The present invention provides a process for the production of a polyester having an acid number which is not greater than 65 which comprises reacting an acid anhydride with a monoterminal epoxide in the presence of a solvent for the polyester in such a way that a self-sustaining reaction is initiated within 200 seconds of the reactants being mixed together and said reaction results in the attainment of a maximum peak temperature within 200 seconds of initiation.

Abstract: In a method for preparing a phosphorus-vanadium-oxygen catalyst wherein a pentavalent vanadium compound and a trivalent phosphorus compound are brought together in a liquid reaction zone under conditions to provide a substantial amount of tetravalent vanadium and to form a phosphorus-vanadium-oxygen catalyst precursor having a phosphorus to vanadium atom ratio between about 0.9:1 and about 2:1, the improvement of this invention comprises adding a sufficient amount of a surfactant to the liquid reaction zone to form a dispersion which comprises a liquid, the surfactant and a dispersoid of the phosphorus-vanadium-oxygen catalyst precursor.

Abstract: The productivity of phosphorus-vanadium-oxygen catalysts useful for converting saturated hydrocarbons containing from 4 to 10 carbon atoms to maleic anhydride can be increased by the order of preparatory steps used to prepare such catalysts. Phosphorus-vanadium-oxygen catalysts are prepared by mixing phosphorus and vanadium compounds to form precursors, shaping precursors and then calcining the precursors to form the catalysts. The catalysts are particularly beneficial for the conversion of butane to maleic anhydride.

Abstract: The invention provides a process for the production of a polyester which comprises initiating a reaction between a poly-terminal epoxide, a mono-terminal epoxide and a cyclic diacid anhydride in the presence of a catalytically effective quaternary salt heating to a point at which the reaction becomes a self-sustaining exothermic reaction and controlling the reaction such that the temperature of the mixture is not reduced until after the exothermic reaction has begun to subside.

Abstract: The prior art discloses that phosphorus-vanadium-oxygen catalysts wherein the phosphorus to vanadium atom ratio is between about 1:2 and about 2:1, and wherein at least about 20 atom percent of the vanadium is in the tetravalent state, are useful for the conversion of aliphatic hydrocarbons to maleic anhydride. It has now been found that when the pore volume of the catalysts from pores having diameters between about 0.8 micron and about 10 microns is greater than 0.02 cc/g, the catalyst is particularly useful for the conversion of saturated hydrocarbons, such as butane, to maleic anhydride.

Abstract: A process for the production of unsaturated primary amines which comprises reacting, in the substantial absence of molecular oxygen, an amine having the formula (R.sub.1 HC=CR.sub.2 CH.sub.2)m N H (3-m), wherein m is 2 or 3 and R.sub.1 and R.sub.2 are hydrogen or C.sub.1 - C.sub.3 alkyl groups, with ammonia in the presence of a catalyst comprising palladium or platinum atoms bearing phosphorus-containing ligands, the reaction being carried out at a temperature of from 0.degree. to 250.degree. C in the presence of a solvent for the amine and the catalyst.

Abstract: Bitumen filled polyester foams are provided through a process which comprises forming a solution of a bitumen having a softening point of at least about 80.degree. C. and a cyclic diacid anhydride at a temperature above the softening point of a bitumen, the bitumen solution is then mixed with a monoterminal epoxide and a polyterminal epoxide in the presence of a blowing agent resulting in the initiation of an exothermic reaction. The process for producing bitumen filled polyester foams through the in situ polymerization of polyesters in a solution of bitumen and the foams produced by the process constitute the invention.

Abstract: The present invention provides a process for the production of allylic amines which comprises reacting a pi-allyl palladium complex with ammonia or an amine having a reactive hydrogen attached to the nitrogen atom and a cupric salt, the reaction taking place at a temperature below the decomposition temperature of the complex and in solution in a solvent for the pi-allyl palladium complex.

Abstract: A process for the regeneration of a spent molybdenum-containing ammoxidation catalyst which comprises heating the catalyst at atmospheric pressure or higher and at 400.degree. C or higher for at least 1 hour in an atmosphere comprising 20-45% by volume of steam, the balance being air or a gas inert to the catalyst under the above conditions.

Abstract: A process for the production of an (amm)oxidation catalyst which comprises forming an aqueous slurry consisting essentially of the molybdate of at least one of the elements in the group consisting of cobalt, nickel and iron, a bismuth oxide or salt, and optionally a phosphate radical and an ion of an element selected from the group consisting of sodium, potassium and calcium, and thereafter separating the solid phase from the slurry and calcining said solid phase to form the catalyst.

Abstract: An oxidation/ammoxidation catalyst contains the elements antimony, uranium, iron, bismuth, and molybdenum, and optionally, nickel and/or cobalt, in a catalytic active oxidized state.

Abstract: A process for the production of a catalyst for the synthesis of isoprene from isobutylene and formaldehyde which comprises providing a catalyst precursor comprising silica and alumina and modifying the catalyst precursor by treatment with an alkali metal hydroxide and subsequently neutralizing by treatment with a mineral acid, depositing a transition metal on the treated catalyst precursor and calcining to form the catalyst.

Abstract: Method of ammoxidizing paraffin hydrocarbons to unsaturated nitriles in a transported bed reactor at a temperature of from 350.degree. to 550.degree. C. using a catalyst comprising antimony and uranium.