Abstract: Semipermeable membranes useful for the separation of gases from a mixture containing at least two fractions into enriched fractions of each, the membrane formed from at least one polymer containing a preponderance of arylene units of the formula ##STR1## where each R is independently a C.sub.1 -C.sub.8 aliphatic or a C.sub.5 -C.sub.7 cycloaliphatic hydrocarbon radical, an aryl radical, an aralkyl radical or an alkaryl radical, each radical being free of a tertiary alpha-carbon atom; each Q is a radical of the formula ##STR2## where R' is a C.sub.1 -C.sub.20 linear or branched hydrocarbon or a nonpolymeric aryl radical; X is a divalent oxygen or sulfur atom or a carbonate group; m is an integer of 0-2; and n is 0-1 with the proviso that n is 1 in at least 10 percent of the arylene units of the polymer. A process is also provided whereby a mixture of gases is separated with the foregoing semipermeable membrane.

Abstract: Semipermeable membranes prepared from at least one cellulosic polymer, such as cellulose triacetate, and containing at least one silicon compound, such as tetraethoxy silane, are useful for the separation of various gaseous mixtures into their constituent parts, such as separating natural gas into enriched fractions of carbon dioxide and methane.

Abstract: Semipermeable membranes useful for separating gaseous mixtures of carbon dioxide and methane into enriched fractions of each are prepared from at least one polymer containing a preponderance of arylene units, such as polyxylene oxide, the arylene units containing pendent sulfone groups substituted with an aromatic group, such as phenyl.

Abstract: Copper sulfide ores are processed by a unique series of steps to produce blister copper, while attaining long sought advantages. An initial smelting step is carried out in any desired manner, e.g. according to conventional practice, to produce a molten, copper sulfide matte or white metal. This matte or white metal is then solidified and subjected to a size-reduction step to produce solid particles capable of being injected into a converting vessel in a stream of oxygen, either pure oxygen or air significantly enriched with oxygen. With the matte or white metal injected in this manner, the converting reaction may be carried out on an autogenous basis, with continuous evolution of substantially undiluted SO.sub.2 gas capable of being liquified for use in the production of elemental sulfur or sulfuric acid or for disposal so as to avoid atmospheric contamination.

Abstract: A process for the impact modification of a plastic with a rubbery polymer to form a thermoplastic resin in a reactor extruder is provided. The process includes the steps of dissolving a rubbery polymer in at least one ethylenically unsaturated monomer to form a feed solution, introducing the feed solution into the feed section of a twin screw reactor extruder, heating the feed solution under pressure to a temperature sufficient for polymerization to begin, shearing the feed solution until the solids content formed is equal to at least about twice the rubber content in the feed solution so as to produce a phase inversion product wherein discrete particles of rubber become encapsulated in a continuous phase of plastic polymer formed from the ethylenically unsaturated monomer, thereafter reacting the phase inversion product until at least about 70 weight percent of the feed solution has been converted to a thermoplastic resin, and extruding the said thermoplastic resin through a die.

Abstract: The change in the crush strength of a catalyst particle as it is transformed from a catalyst precursor to a finished catalyst by calcination is controlled by the method comprising:1. Preparing a catalyst precursor containing at least one metal element,2. Adjusting the volatile portion of the catalyst precursor to a predetermined level,3. Adjusting the water content of the volatile-adjusted precursor of (2) to a predetermined level,4. Forming the catalyst particle from the water-adjusted precursor of (3), and5. Transforming the catalyst precursor particle of (4) into a finished catalyst particle by calcination.

Abstract: The octane number of unleaded gasoline is improved by the addition of a mixture of etherified phenols obtained from crude shale oil.

Abstract: The coextrusion device (20) of the present invention can be used with conventional extruders (24-26) and extrusion dies (90) for forming layered products (91) from at least two materials. It includes a manifold (21) for receiving a plurality of extruded feed materials (A, B, C) and a feedblock (22) receiving the feed materials from the manifold. The feedblock includes first and second faces (43, 52), entrance ports (40, 41, 42) in the first face corresponding to the number of feed materials, channel means (50, 60, 70) passing through the feedblock between the first and second faces directing each feed material into at least one separate profile, and exit ports (51, 61, 71) in the second face corresponding to the number of channel means, defining a first profile for each feed material.

Abstract: Cyclohexenyl and alkenyl aromatic compounds, such as cyclohexene and styrene, are prepared by a process comprising contacting a corresponding cyclohexyl or alkyl aromatic carboxylic acid, such as cyclohexyl carboxylic acid or 2-phenyl propionic acid, with a decarboxylation catalyst of the formulaM.sub.a M'.sub.b O.sub.xwherem is copper or a combination of copper and molybdenum, andM' is at least one promoter element, such as a Group IA element.

Abstract: The present invention relates to the oxidation of monoolefins with molecular oxygen to the corresponding olefin oxides, in the liquid phase in the presence of a catalyst comprising an organo-monovalent aurous complex.

Abstract: 2-phenyl propanal is converted to 2-indanone by contact at conversion conditions, typically vapor-phase conditions, with a catalyst of the formula Mo.sub.12 Cu.sub.0.1-10 V.sub.0.1-5 W.sub.0.1-3 M.sub.0-3 O.sub.x where M is an optional promoter, such as Sn, Sb, Te or a Group VIII element.

Abstract: Mononuclear aromatic hydrocarbons, e.g. benzene and analogs, are converted by hydroalkylation to the corresponding cycloalkyl aromatics by contacting the mononuclear aromatic hydrocarbons in the presence of hydrogen with a catalyst comprising a rare earth-exchanged Y-type zeolite support carrying a promoter comprising at least one of ruthenium, iridium, rhodium and palladium, the catalyst being calcined in an oxygen-containing atmosphere at a temperature of 250.degree. to 600.degree. C. prior to the hydroalkylation reaction.

Abstract: Water-in-oil microemulsions useful as fire-resistant hydraulic fluids are prepared from an oil, such as mineral oil, water, emulsifiers, and an aliphatic diol, such as 2-ethyl-1,3-hexanediol.

Abstract: Isobutyraldehyde is oxidized to methacrylic acid by contacting gaseous isobutyraldehyde with molecular oxygen at oxidative conditions in the presence of a catalyst of the empirical formula:Mo.sub.12 P.sub.0.1-3 Cu.sub.0.01-2 V.sub.0.01-3 M.sub.0.1-3 M'.sub.0.01-2 O.sub.xwhereM is at least one of K, Rb, Cs and Tl;M' is at least one of Be, Mg, Ca, Sr, Ba, Nb and Sb; andx is a positive number that satisfies the valence requirements of the other elements present.

Abstract: Compositions of the empirical formula:Mo.sub.12 P.sub.0.1-3 Te.sub.0.01-2 M.sub.0.1-3 M'.sub.0.01-3 X.sub.a O.sub.b (I)whereM is at least one of K, Rb and Cs;M' is at least one of Cu and V;X is at least one of Ba, Zn, Ga, Nb, Cd, Ti, Ca, Mg, Ta, Zr, Bi, Ce, Ni, Co, Cr, Fe and Tl when a >0;a is a number of 0 to about 2; andb is a number that satisfies the valence requirements of the other elements present,are excellent catalysts for the oxidation of methacrolein to methacrylic acid.

Abstract: Compositions of the empirical formula:Mo.sub.12 P.sub.0.1- Te.sub.0.01-2 M.sub.0.1-3 M'.sub.0.01-3 X.sub.a O.sub.bwhereM is at least one of K, Rb and Cs;M' is at least one of Cu and V;X is at least one of Ba, Zn, Ga, Nb, Cd, Ti, Ca, Bi, Mg, Ta, Zr, Ce, Ni, Co, Cr, Fe and Tl when a>0;a is a number of 0 to about 2; andb is a number that satisfies the valence requirements of the other elements present,are excellent catalysts for the oxydehydrogenation of saturated, lower aliphatic acids and esters to the corresponding unsaturated acids and esters.

Abstract: Dehydrogenatable hydrocarbons are dehydrogenated by contacting them at dehydrogenation conditions in the presence of a complex oxide catalyst comprising molybdenum, copper and tin and at least one element selected from the group consisting of Li, Na, K, Rb, Cs, Mg, Ca, Sr, Ba, La, Ce, Th and U. For example, an alkyl aromatic hydrocarbon, e.g. ethylbenzene, can be dehydrogenated to an alkenyl aromatic hydrocarbon, e.g. styrene, in the presence of an oxide complex catalyst comprising molybdenum, copper, tin and at least one element selected from the group consisting of K, Cs, Ba, Mg and Ca.

Abstract: Aldehydes, such as isobutyraldehyde, are isomerized to ketones, such as methyl ethyl ketone, by contact at isomerization conditions, typically vapor-phase conditions, with a catalyst of the formula M.sub.0.15-15 M'.sub.0.05-12 O.sub.x where M is at least one of Mo and Cu and M' is a promoter, such as a Group IIB or VIII element.

Abstract: The present invention relates to a process for the manufacture of furan compounds by the direct oxidation of conjugated diolefins with air or oxygen in the liquid phase in the presence of a transition metal catalyst system.

Abstract: Cyclohexenyl and alkenyl aromatic compounds, such as cyclohexene and styrene, are prepared by a process comprising contacting a corresponding cyclohexyl or alkyl aromatic carboxylic acid, such as cyclohexyl carboxylic acid or 2-phenyl propionic acid, with a decarboxylation catalyst of the formulaM.sub.a M'.sub.b O.sub.xwhereM is copper or a combination of copper and molybdenum, andM' is at least one promoter element, such as a Group IA element.