Abstract: A method is disclosed for converting methane to higher hydrocarbon product by contacting the methane with a solid which comprises a reducible metal oxide which when contacted with methane at a temperature within the range of about 500.degree. to 1000.degree. C. is reduced and produces higher hydrocarbon products and water, the improvement comprising recycling C.sub.2 + alkanes recovered during subsequent processing of the effluent produced by the contacting to the contacting step.

Abstract: A method is disclosed for converting methane to higher hydrocarbon product by contacting methane with a contact solid which comprises a reducible metal oxide which when contacted with methane at a temperature within the range of about 500.degree. to 1000.degree. C. is reduced and produces higher hydrocarbon products and water; and a promoting amount of at least one halogen component.

Abstract: An improved process for the production of a contact agent comprising digesting a reducible oxide of at least one metal, the oxide of which forms a reduced metal oxide, and a support in the presence of a silicon component, drying the precipitate of the reducible oxide and calcining the precipitate to form the contact agent.

Abstract: A method is disclosed for converting methane to higher hydrocarbon product by contacting methane with a solid which comprises a reducible metal oxide which when contacted with methane at a temperature within the range of about 500.degree. to 1000.degree. C. is reduced and produces higher hydrocarbon products and a promoting amount of at least one chalcogen component. The preferred chalcogen components are selected from a group consisting of sulfur, selenium, tellurium, and compounds thereof.

Abstract: An improved method for converting methane to higher hydrocarbon products by contacting a gas comprising methane with a contact agent at a selected temperature, the agent comprising a reducibile metal oxide, a support of at least two oxides, and an alkali metal.

Abstract: A process for the low temperature oxydehydrogenation of ethane to ethylene uses a calcined oxide catalyst containing Mo, V, Nb, Sb, and at least one metal from a given group of metals.

Abstract: An improved method for converting methane to higher hydrocarbon products by contacting a hydrocarbon gas comprising methane, an oxygen-containing gas and a reducible metal oxide under synthesis conditions, the improvement which comprises contacting methane and oxygen with a contact solid which comprises at least one manganese silicate.

Abstract: An improved method for converting methane to higher hydrocarbon products by contacting a hydrocarbon gas comprising methane, an oxygen-containing gas and a reducible metal oxide under synthesis conditions, the improvement which comprises contacting methane and oxygen with a contact solid which also contains a promoting amount of alkali metal, alkaline earth metal, and/or compounds thereof. Sodium is a particularly effective promoter. Stability of the promoted contact agent is enhanced by the presence of minor amounts of phosphorus.

Abstract: A method for converting methane to higher hydrocarbon products by contacting, at conditions to convert said hydrocarbons, at least one reducible oxide of at least one metal, associated with a hydroxylated magnesia support (that is, magnesia derived from magnesium hydroxide or a magnesium-containing component contacted with hydroxyl-containing material), which support is calcined prior to the addition of the reducible oxide.

Abstract: A catalyst for removing acetylenic impurities from gaseous organic product streams, comprising at least Fe and Ni, other elements from Groups 8, 1b, 2b, 4b, 6b and 7b of the Periodic Table, an alkaline earth metal and an alkali metal.

Abstract: A method for dehydrogenating dehydrogenatable hydrocarbons which comprises contacting hydrocarbon with an oxide of Tb having combined therewith an amount of alkali and/or alkaline earth metal which is sufficient to improve the selectivity to dehydrogenated hydrocarbon products. The oxide is reduced by the contact which is carried at about 500.degree. to 1000.degree. C. Reducible oxides of Tb are regenerated by oxidizing the reduced composition with molecular oxygen. Solids prepared from the oxide Tb.sub.4 O.sub.7 are particularly effective in the process.

Abstract: An improved method for converting methane to higher hydrocarbon products by contacting a gas comprising methane and an oxidative synthesizing agent at synthesizing conditions, the improvement which comprises contacting methane with an oxidative synthesizing agent containing a promoting amount of alkali metal and/or compounds thereof. Sodium is a particularly effective promoter. Stability of the promoted contact agent is enhanced by the presence of phosphorus.

Abstract: A paraffin or mixture of paraffins having from 2 to 5 carbon atoms is oxidatively dehydrogenated in the presence of a cobalt based catalyst composition which has been calcined in the absence of oxygen. The catalyst composition comprises cobalt; phosphorus; at least one promoter selected from the group consisting of zinc, titanium, zirconium, niobium, indium, lead and bismuth; at least one alkali metal and oxygen. The catalyst composition may also contain sulfur and/or a halogen. If the feed to the oxidative dehydrogenation process contains paraffins having more than two carbon atoms, some cracking of such paraffins will also occur at the conditions at which the oxidative dehydrogenation process is carried out.

Abstract: An improved method for converting methane to higher hydrocarbon products by contacting a gas comprising methane and an oxidative synthesizing agent under systhesis conditions, the improvement which comprises contacting methane with an oxidative synthesizing agent containing a promoting amount of alkaline earth metal and/or compounds thereof. Magnesium is a particularly effective promoter. Stability of the promoted contact agent is enhanced by the presence of phosphorus.

Abstract: An alkane is reacted with oxygen and available chlorine in the presence of a solid solution catalyst containing iron cations to yield unsaturated hydrocarbons and chlorinated saturated and unsaturated hydrocarbons. In a preferred embodiment of the process, ethane is reacted with oxygen and available chlorine in the presence of a solid solution catalyst containing iron cations to yield vinyl chloride, ethylene, and other valuable by-products. The conversion of ethane to products approaches 100 percent, vinyl chloride is prepared in up to 40 mole percent yield, and the combined yield of vinyl chloride, ethylene dichloride, ethyl chloride, and ethylene is up to 90 mole percent.

Abstract: An alkane is reacted with oxygen and available chlorine in the presence of a solid solution catalyst containing iron cations to yield unsaturated hydrocarbons and chlorinated saturated and unsaturated hydrocarbons. In a preferred embodiment of the process, ethane is reacted with oxygen and available chlorine in the presence of a solid solution catalyst containing iron cations to yield vinyl chloride, ethylene, and other valuable by-products. The conversion of ethane to products approaches 100 percent, vinyl chloride is prepared in up to 40 mole percent yield, and the combined yield of vinyl chloride, ethylene dichloride, ethyl chloride, and ethylene is up to 90 mole percent.

Abstract: A method for synthesizing hydrocarbons from a methane source which comprises contacting methane with an oxide of tin at a temperature of about 500.degree. to 1000.degree. C. The oxide is reduced by the contact and coproduct water is formed. A reducible oxide of tin is regenerated by oxidizing the reduced composition with molecular oxygen. The oxide SnO.sub.2 is a particularly effective synthesizing agent.

Abstract: A method for synthesizing hydrocarbons from a methane source which comprises contacting methane with an oxide of bismuth at a temperature of about 500.degree. to 850.degree. C. The oxide is reduced by the contact and coproduct water is formed. A reducible oxide of bismuth is regenerated by oxidizing the reduced composition with molecular oxygen. The oxide Bi.sub.2 O.sub.3 is a particularly effective solid synthesizing agent.

Abstract: A method for synthesizing hydrocarbons from a methane source which comprises contacting methane with an oxide of germanium at a temperature of 500.degree. to 800.degree. C. The oxide is reduced by the contact and coproduct water is formed. A reducible oxide of germanium is regenerated by oxidizing the reduced composition with molecular oxygen. The oxide GeO.sub.2 is a particularly effective synthesizing agent.

Abstract: A method for synthesizing hydrocarbons from a methane source which comprises contacting methane with an oxide of antimony at a temperature of about 500.degree. to 1000.degree. C. The oxide is reduced by the contact and coproduct water is formed. A reducible oxide of antimony is regenerated by oxidizing the reduced composition with molecular oxygen. The oxide Sb.sub.2 O.sub.3 is a particularly effective synthesizing agent.

Abstract: A method for synthesizing hydrocarbons from a methane source which comprises contacting methane with an oxide of manganese at a temperature of about 500.degree. to 1000.degree. C. The oxide is reduced by the contact and coproduct water is formed. A reducible oxide of manganese is regenerated by oxidizing the reduced composition with molecular oxygen. The oxide Mn.sub.3 O.sub.4 is a particularly effective synthesizing agent.

Abstract: A method for synthesizing hydrocarbons from a methane source which comprises contacting methane with an oxide of indium at a temperature of about 500.degree. to 850.degree. C. The oxide is reduced by the contact and coproduct water is formed. A reducible oxide of indium is regenerated by oxidizing the reduced composition with molecular oxygen. The oxide In.sub.2 O.sub.3 is a particularly effective solid synthesizing agent.

Abstract: A method for synthesizing hydrocarbons from a methane source which comprises contacting methane with an oxide of lead at a temperature of about 500.degree. to 1000.degree. C. The oxide is reduced by the contact and coproduct water is formed. A reducible oxide of lead is regenerated by oxidizing the reduced composition with molecular oxygen. The oxide PbO is a particularly effective synthesizing agent.

Abstract: The invention herein is directed toward a process for the oxydehydrogenation of ethane in fixed-bed or fluid-bed reactors at temperatures of less than about 600.degree. C. The process includes the step of contacting ethane and an oxygen-containing gas with a catalyst composition having the formula V.sub.1.0 P.sub.a O.sub.x. The catalyst can be employed in supported or unsupported form. A promoter metal can optionally be present in the catalyst.

Abstract: A multiple reaction zone process for dehydrogenating light hydrocarbons, preferably propane, is disclosed. The feed stream and intermediate streams are first heated by indirect heat exchange to temperatures slightly below the desired inlet temperature of the dehydrogenation catalyst beds. These streams are then transported to a location which is in close proximity of the dehydrogenation catalyst bed and further heated by the selective combustion of hydrogen present in these streams through the use of beds of oxidation catalyst. This eliminates lengthy high temperature reactant residence times in transfer lines extending between fired heaters and the dehydrogenation catalyst beds, thereby reducing thermal cracking of the feed and increasing the selectivity of the process. The process has special utility with stacked moving bed reactors, which have larger volume reactant transfer lines.

Abstract: An alkane is reacted with oxygen and available chlorine in the presence of a solid solution catalyst containing iron cations to yield unsaturated hydrocarbons and chlorinated saturated and unsaturated hydrocarbons. In a preferred embodiment of the process, ethane is reacted with oxygen and available chlorine in the presence of a solid solution catalyst containing iron cations to yield vinyl chloride, ethylene, and other valuable by-products. The conversion of ethane to products approaches 100 percent, vinyl chloride is prepared in up to 40 mole percent yield, and the combined yield of vinyl chloride, ethylene dichloride, ethyl chloride, and ethylene is up to 90 mole percent.

Abstract: The preparation of a compound of formula R.sup.1 --C(R.sup.2).dbd.CH.sub.2 (R.sup.1 and R.sup.2 are a phenyl, alkyl or alkenyl group or a hydrogen atom) by contacting a mixture of steam and a compound of formula R.sup.1 --C(R.sup.2)(H)--CH.sub.3 at elevated temperature under non-oxidative dehydrogenation conditions with a catalyst having a spinel structure allows lower ratios steam to compound of formula R.sup.1 --C(R.sup.2)(H)--CH.sub.3, a higher selectivity to the compound of formula R.sup.1 --C(R.sup.2).dbd.CH.sub.2 and a lower temperature when lithium is present in the spinel structure.

Abstract: The catalytic dehydrogenation of at least one dehydrogenatable organic compound which has at least one ##STR1## grouping is carried out in the presence of a zinc silicate catalyst and in the substantial absence of free oxygen.

Abstract: The catalytic oxidative dehydrogenation of paraffins having from 2 to 5 carbon atoms is carried out in the presence of a catalyst composition comprising cobalt; phosphorus; at least one promoter selected from the group consisting of zinc, titanium, zirconium, niobium, indium, lead and bismuth; and oxygen. The catalyst composition also comprises at least one alkali metal and/or at least one halogen selected from the group consisting of chlorine, bromine and iodine. The selectivity of the catalyst composition is improved by the presence of the at least one alkali metal. The conversion of the catalyst composition is improved by the presence of the at least one halogen.

Abstract: The present invention is a reactor that consists of a single shell that contains a reaction zone and a regeneration zone. The reaction zone and regeneration zone are arranged in such a manner that (a) a particulate solid may be transferred by flow of gases from the regeneration zone to the reaction zone by a first route and then back to the regeneration zone by a second route; and (b) the gases passing through the regeneration zone are not transferred to the reaction zone and the gases passing through the reaction zone are not transferred to the regeneration zone.

Abstract: Improved oxidative dehydrogenation catalysts are prepared by modifying a preformed zinc ferrite oxidative dehydrogenation catalyst with zinc oxide. The resulting catalyst compositions exhibit higher conversions and yields.

Abstract: Ethane is catalytically oxydehydrogenated to ethylene in a gas phase reaction, in the presence or absence of water, at temperatures of .ltoreq.550.degree. C. using a catalyst comprising oxides of the elementsMo.sub.a X.sub.b Y.sub.cwhereinX=Cr, Mn, Nb, Ta, Ti, V and/or W,Y=Bi, Ce, Co, Cu, Fe, K, Mg, Ni, P, Pb, Sb, Si, Sn, Tl and/or U,a=1,b=0 to 2,c=0 to 2,with the proviso that the total value of c for Co, Ni and and/or Fe is <0.5.Acetic acid is also produced.

Abstract: A process for producing unsaturated hydrocarbons which comprises contacting a paraffin, monoolefin and/or alkylaromatic compounds with a catalyst at a temperature within the range of from 400.degree. to 700.degree. C. in the presence of an inert gas and/or steam. The catalyst comprises a carrier having deposited thereonto an oxide of molybdenum in an amount of from 5 to 35% by weight of the catalyst. As the carrier, use is made of a granulated porous crystalline silica modified with magnesia in an amount of from 1 to 20% by weight of the carrier; a granulated magnesium-titanium carrier consisting of 50 to 95% by weight of MgO and 50 to 5% by weight of TiO.sub.2, or a granulated magnesium-aluminum carrier consisting of 70 to 95% by weight of MgO and 5 to 30% by weight of Al.sub.2 O.sub.3. Through the spent catalyst an oxygen-containing gas is passed at a temperature within the range of from 400.degree. to 700.degree. until catalytic activity is restored to the catalyst.

Abstract: The process for preparing butadiene (divinyl) according to the present invention comprises dehydrogenation of n-butane or a mixture thereof with n-butene at a temperature ranging from 550.degree. to 650.degree. C. in the presence of oxygen, an inert diluent and a catalyst having the following composition, percent by weight:antimony oxide: 5.0-20.0vanadium oxide: 2.0-10.0nickel oxide: 4.0-20.0thorium oxide: 0.1-1.0titanium oxide: 0.1-1.0carrier: the balance.The process of this invention makes it possible to increase simultaneously the yield and selectivity of the formation of divinyl.

Abstract: The present invention provides a highly efficient process for use in the high pressure catalytic vapor phase reaction for the high yield conversion of lower aliphatic hydrocarbons such as n-butane to corresponding monocarboxylic acids such as acetic acid. The oxidation reaction takes place under hydrocarbon rich conditions. The increased efficiency in this process is realized by the judicious use of steam and the catalyst systems set forth in the instant invention.

Abstract: Hydrocarbon feedstocks are dehydrogenated to compounds having the same number of carbon atoms and a higher degree of unsaturation by contacting the feedstock in the vapor phase in the presence of molecular oxygen with a catalyst consisting essentially of nickel, lead, phosphorus and combined oxygen, and optionally, an alkali metal. Representative of such conversions is the oxidative dehydrogenation of butane to butenes and butadiene.