Abstract: Oxygen is separated from an oxygen-containing gas by introducing the gas into a first zone of a gas separation apparatus, the apparatus comprising first and second zones separated by a mixed metal oxide membrane, the membrane having a first surface open to the first zone, a second surface open to the second zone, and an empirical formula ofBiA.sub.x M.sub.y M'.sub.z O.sub.nwhere A is at least one of Mg, Ca, Sr, Ba, Y, Th, U, and the lanthanide elements; M is at least one of Sc, Ti, Cr, Mn, Fe, Ni, Cu and Zn; and M' is at least one of Co, Rh, Pd, Pt or Ru. The oxygen separated from the oxygen-containing gas can be recovered from the second surface of the membrane either as molecular oxygen, or it can be reacted with an oxygen-consuming substance, such as a hydrocarbon gas, which can be introduced into the second zone of the separation apparatus and brought in contact with the second surface of the membrane.

Abstract: The present invention provides for a process for converting a feedstock comprising ethylene and/or acetylene to a product comprising liquid hydrocarbons. The process comprises maintaining said feedstock at a temperature in the range of about 700.degree. C. to about 1000.degree. C. for about 100 to about 1000 milliseconds to provide for said conversion. In one embodiment, the feedstock further comprises hydrogen. In another embodiment the feedstock comprises the product made by the process comprising heating a gaseous mixture comprising (i) hydrogen and (ii) natural gas and/or at least one light hydrocarbon at a temperature of at least about 1250.degree. C. for an effective period of time to provide said feedstock. In still another embodiment, the feedstock further comprises natural gas and/or at least one light hydrocarbon in addition to said ethylene and/or acetylene.

Abstract: A catalyst is disclosed which comprises a molybdenum-tungsten-containing complex represented by the formulaMo.sub.a W.sub.b M.sub.c A.sub.d O.sub.

Abstract: The invention relates to a process for converting light hydrocarbon feedstocks such as methane and/or natural gas, to higher molecular weight hydrocarbon products that are more readily handleable and transportable. The process comprises heating a gaseous mixture comprising said light hydrocarbon feedstocks and a minor, effective amount of at least one ether or thioether compound at a temperature of at least about 800.degree. C. for a period of time effective to provide said higher molecular weight liquid hydrocarbon product. The invention also relates to the higher molecular weight liquid products obtained by the process of the invention.

Abstract: A catalyst is disclosed which comprises a molybdenum-tungsten-containing complex represented by the formulaMo.sub.a W.sub.b M.sub.c A.sub.d O.sub.

Abstract: In a process for the production of hydrogen by the reaction of steam with carbon, a catalyst system is employed comprising a supported Group VIIIA metal and, as modifier for the suppression of methane, an effective amount of an oxide of molybdenum or tungsten.

Abstract: An alcohol such as methanol is decomposed to form hydrogen and carbon monoxide at elevated temperature in the presence of mixed metal oxide catalyst containing copper and a metal L selected from the group consisting of Th, Be, Zr, Ce, Mg and U.The catalyst can contain a further metal M selected from the group consisting of Ca, Mo, Mn, Pt, Ce, Cr, Zn, Al, Ti, La, V, U, Ru, Re and Pd.The catalysts are particularly effective at relatively low temperatures for example 200.degree.-200.degree. C.

Abstract: A process for converting .alpha.-hydroxycarboxylic acids to hydroxy free aliphatic carboxylic acids and aldehydes in the presence of a catalyst of the formula:M.sub.a M'.sub.b O.sub.xwhereinM is at least one of an element selected from Group IB, VIB, IVA; andM' is at least one of an element selected from Groups IA, IIA, IVA, VA, VIA, VIIIB, VB.

Abstract: Fly ash is activated by heating a screened magnetic fraction of the ash in a steam atmosphere and then reducing, oxidizing and again reducing the hydrothermally treated fraction. The activated fly ash can be used as a carbon monoxide disproportionating catalyst useful in the production of hydrogen and methane.

Abstract: A process for producing HCN by contacting CO and NH.sub.3 with a catalyst comprising a porous catalyst support, a Group VIII metal which is at least one of Fe, Ni, Co and Ru, and carbon, wherein the metal is disposed on the pore surfaces of the support and the carbon is randomly bonded to the metal.

Abstract: Aryl ethers, e.g., cumylmethylether and anisole, are particularly effective additives for improving the octane number of motor fuels. These aryl ethers are especially useful in increasing the octane number of unleaded gasolines.

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: 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: A fixed-bed catalytic material comprises iron impregnated Alundum carrying a coating of copper oxide on its outside surfaces. By means of the coating, the growth of carbon fibers as a result of the disproportionation of carbon monoxide is restricted to the interior surfaces of the catalyst particles.

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: 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 invention herein is directed toward a process for the conversion of oxides of nitrogen to nitrogen gas by employing a reactant carbon fiber or inter host carbon material at a temperature of about 550.degree. C. The reactant material can be utilized alone or on a support material; in reactors such as fixed bed, fluid bed and radial flow; and, if desired, can be regenerated during the conversion process.

Abstract: 1,1-diphenylethane or 1,1-diphenylethylene is oxidized to benzophenone by contacting the 1,1-diphenylethane or 1,1-diphenylethylene and oxygen with an antimonate catalyst.