Abstract: A new and improved wood frame construction in which the artwork may be end-loaded into a frame in which three of the four sides are permanently interconnected with the fourth side being removable to accommodate the loading of the artwork into the frame. In particular the new and improved frame construction has a very narrow front profile making the frame quite attractive and comparatively unique in its appearance.

Abstract: An alpha-olefin oligomer synthetic lubricant having an improved viscosity-volatility relationship is prepared from an alpha-olefin such as 1-decene.

Abstract: A process for the conversion of aromatic hydrocarbons, e.g., reacting an alkylating agent, preferably an olefin, with an aromatic hydrocarbon. The process uses a novel catalyst prepared by subjecting alumina to an anhydrous tetravalent titanium flouride complex of an organic compound selected from the group of organic compounds containing at least one methoxy group per molecule or organic compounds having at least one electron donor atom and double bond per molecule, and heat treating the resulting impregnated alumina in an inert atmosphere.

Abstract: The present process is particularly adapted to those situations where a refiner lacks sufficient isobutane to completely alkylate an olefin feedstock. A field butane stream is admixed with an olefin stream, and the mixture is fractionated to provide an isobutane-olefin concentrate and a normal butane concentrate. The former is increased in pressure and reacted in contact with a hydrofluoric acid alkylation catalyst. The latter is introduced into the reaction zone wherein it is vaporized via indirect contact with the warm reaction mixture contained therein. Vaporous normal butane is recycled into the fractionation facility whereby the exothermic heat of the alkylation reaction is utilized to fractionate the first mentioned field butanes-olefin mixture. Alkylation reactions can thus be conducted at subambient temperatures resulting in improved alkylate product quality.

Abstract: Isomerizable light paraffinic hydrocarbon feeds are isomerized in an improved process using a particular super-chlorided reforming catalyst under isomerizing conditions. A chloride source in the feed stabilizes the catalyst. This process provides for a material octane improvement of the feed without excessive loss thereof to normally gaseous hydrocarbons.

Abstract: Isomerization process for petroleum light hydrocarbons with a boiling point within the range of from about 100.degree. F. (38.degree. C.) to about 210.degree. F. (99.degree. C.) wherein said process comprises contacting said hydrocarbons with a catalyst consisting essentially of an ultrastable, large pore crystalline zeolite aluminosilicate material containing less than 1 (wt)% alkali metal and characterized by well-defined hydroxyl infra-red bands and a maximum unit cubic cell dimension of 24.55 A and a metal component selected from the metals, oxides or sulfides of the Group VIII elements of the Periodic Table, under suitable isomerization conditions.

Abstract: Alkylation of aromatic hydrocarbons, especially toluene methylation, is carried out in the presence of a catalyst comprising an aluminosilicate zeolite of the ZSM-5 type in which some or all of the protons of the zeolite have been replaced by monovalent cations. Preferably, the replacement cations are sodium ions, the catalyst preferably containing more than 2% by weight of sodium.

Abstract: Olefins are oxidized to carbonyl compounds, for example, 2-hexene to a mixture of 2-hexanone and 3-hexanone, with a palladium/copper/boric acid catalyst and a suitable surfactant or phase transfer agent. The reaction takes place in a diluent system comprising at least two liquid phases, wherein at least one liquid phase is an aqueous phase, and in the presence of free oxygen. The catalyst system can be used to oxidize internal olefins, as well as terminal olefins, at reasonable rates. The catalyst system can also be used for the selective oxidation of linear olefins in a mixed stream containing linear and branched olefins.

Abstract: This invention relates to a process for the production of alkylbenzenes, which comprises reacting benzene with at least one aromatic hydrocarbon substituted by alkyl groups and containing 9 or more carbon atoms, in the presence of an acid leached hydrogen form mordenite catalyst having a silica (SiO.sub.2)/alumina (Al.sub.2 O.sub.3) molar ratio of 15 to 21 and a sodium content of 0.05 weight % or less as Na.sub.2 O.

Abstract: Isomerization of xylenes in admixture with ethylbenzene by contact with a zeolite catalyst such as ZSM-5 is improved by use of zeolite which has been steamed at high temperature to reduce activity, the reaction being at a temperature above about 700.degree. F. At these conditions, conversion of ethylbenzene follows a different reaction path which permits high conversion of ethylbenzene to benzene without loss of xylenes of disproportionation.

Abstract: Hydrocarbons are converted by contacting them at hydrocarbon conversion conditions with a novel attenuated superactive multimetallic catalytic composite comprising a combination of a catalytically effective amount of a pyrolyzed rhenium carbonyl component with a porous carrier material containing a uniform dispersion of a catalytically effective amount of a platinum group component, which is maintained in the elemental metallic state during the incorporation of the rhenium carbonyl component, and of a bismuth component. In a highly preferred embodiment, this novel catalytic composite also contains a catalytically effective amount of a halogen component. The platinum group component, pyrolyzed rhenium carbonyl component, bismuth component and optional halogen component are preferably present in the multimetallic catalytic composite in amounts, calculated on an elemental basis, corresponding to about 0.01 to about 2 wt. % platinum group metal, about 0.01 to about 5 wt. % rhenium, about 0.

Abstract: A continuous process for alkylating an alkylatable hydrocarbon with an alkylating agent in the presence of an acid-type catalyst in which the alkylatable hydrocarbon is contacted with the alkylating agent in the presence of the catalyst at a temperature and for a time sufficient to alkylate the alkylatable hydrocarbon, the reaction product is separated into an alkylate product phase and a catalyst phase, containing catalyst-soluble oil, the catalyst phase is cooled to maintain a preselected temperature in the exothermic alkylation zone, the cooled catalyst phase is recycled to the alkylation reaction and a predetermined concentration of catalyst-soluble oil is maintained in the catalyst phase by at least periodically heating an alkylating agent to a temperature above the reaction temperature, contacting the heated alkylating agent with one of the separated recycle catalyst, separated rerun catalyst, fresh catalyst or mixture thereof and combining the resultant reaction product with separated recycle catalyst

Abstract: An alcohol which can be straight chain or branch-chain and can contain from 2 to about 20 carbon atoms per molecule is dehydrated in the presence of gamma-alumina, which may be base-treated, employing an inert carrier gas. 3-Methyl-1-butanol was dehydrated over gamma-alumina employing nitrogen as the carrier gas to obtain yields well in excess of 90 percent with correspondingly high selectivities. 3-Methyl-1-butene having a 97.7 weight percent purity was obtained with base-treated gamma-alumina.

Abstract: A process for the production of the internal isomers (3-phenyl, 4-phenyl and higher) from linear phenylalkane mixtures via selective cracking of the 2-phenylalkane isomer over crystalline zeolite catalysts having a silica to alumina ratio of at least about 12 and a constraint index, as herein defined, of about 1 to 12.

Abstract: An improvement is disclosed in a process for the acid-catalyzed alkylation of an isoparaffin with an olefin alkylating agent. The improvement relates to an alkylation process wherein the hydrocarbon phase of the alkylation reaction mixture is introduced into a common fractionation column with a field butane stream comprising olefinic materials. The improvement comprises initially clay-treating said field butane stream.

Abstract: Hexachlorocyclopentadiene is produced by the use of a molten salt mixture of cuprous and cupric chloride, with the reaction effluent including the product, chlorine, hydrogen chloride, unreacted feed and organic byproduct, as well as entrained molten salt. The effluent is cooled at a temperature and pressure to effect condensation of organics, with the salt being present in the condensate. The salt is then separated from the organics for re-use in the process. Hydrogen chloride and chlorine present in the effluent are also recovered for re-use in the process.

Abstract: The object of the present invention is the preparation of ethene in the presence of catalysts using adiabatic reactors at high temperature. Such adiabatic reactors may be used in parallel or be disposed in series or arranged in parallel series assemblies or only a single reactor may be used.The process of the invention allows the use of ethyl alcohol diluted with a sensible heat carrying fluid as feeding material. Said sensible heat carrying fluid is introduced into the reactor simultaneously with the feed, supplying the heat necessary for the performance of the reaction.

Abstract: A method for dehydrogenating an alkyl aromatic compound, particularly, ethylbenzene or ethyl toluene, to its corresponding vinyl aromatic derivative, styrene or methyl styrene, respectively, in which the alkyl aromatic compound and its normally attendant diluent, stream or water, are preheated to a temperature below which any substantial thermal reaction temperature of the alkyl aromatic compound occurs, viz., 450.degree. to about 500.degree. C., and introduced into a catalytic bed of a reactor and thereafter contacted and mixed in said catalytic bed with a quantity of steam in an amount and at a temperature to raise the alkyl aromatic compound to the catalytic dehydrogenation temperature. The steam introduced into the catalyst bed, in a ratio less than 3 to 1 to about 0.7 to 1, steam to hydrocarbon passes through the bed in heat exchange relationship to the catalyst and the reacting gases prior to contacting and mixing with the alkyl aromatic compound in the bed.

Abstract: An improvement as described for the recovery of ethylene oligomers from the reaction product obtained when ethylene is oligomerized by contact in the liquid phase at elevated temperatures and pressures with a nickel complexed catalyst dissolved in an aliphatic diol solvent. In this improved process, the liquid oligomer product phase, after separation from gaseous and dissolved ethylene and liquid diol solvent, is subject to an aqueous acid wash followed optionally and preferably by a water wash to hydrolyze and extract diol solvent degradation products which carry through from the oligomerization reaction zone.

Abstract: Novel acid systems are disclosed which are characterized as being capable of stabilizing high concentrations of tertiary cations, e.g., t-butyl cation, and further characterized as capable of forming carbonium ion salts containing both dimeric and monomeric anions. The ions undergo hydride and halide exchange with other alkanes and halides. The hydride transfer reaction renders them useful in isomerization and alkylation reactions.