Abstract:
Hydroperoxides, such as cyclohexylbenzene hydroperoxide, are manufactured by the oxidation of aryl compounds, such as cyclohexylbenzene, in the presence of a catalyst selected from the group consisting of C.sub.6 -C.sub.18 primary amines and polyvinylpyrrolidone.
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:
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.
Abstract:
Hydroperoxides are catalytically decomposed using a novel metal complex of the formula: ##STR1## wherein M is a positively charged metal or metal compound;Z is S, O, P, S-P, or S-S;L is C, P, or N; andA is selected from the group consisting of halogens; hydrogen; N-R wherein R is selected from the group consisting of H, C.sub.1-30 alkyls and 4 to 8 membered aryls optionally substituted with one or more C.sub.1-20 alkyls and C.sub.1-20 alkoxys; and hydrocarbon groups containing up to 30 carbon atoms optionally substituted with halogen atoms, C.sub.1-12 hydroxy groups, C.sub.1-12 acid groups, C.sub.1-12 aldehyde groups, C.sub.1-12 ketone groups, and C.sub.1-10 nitrile groups; andwhereinn is 1 or 2; andb is 1, 2 or 3.These catalysts are especially effective in decomposing either cumene hydroperoxide or cyclohexylbenzene hydroperoxide to phenol.
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:
This invention relates to an improved process for the dehydrogenation of diarylethanes to the corresponding diarylethylenes in the presence of oxygen and in the presence of a metal phosphate catalyst.
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:
Hydroperoxidizable hydrocarbons are hydroperoxidized by contacting them at hydroperoxidation conditions in the presence of a catalyst comprising a polymer containing maleimide linkages. For example, cumyl hydroperoxide can be produced by contacting cumene and oxygen with a catalyst comprising polymaleimide.
Abstract:
Aromatic hydrocarbons, e.g., benzene and analogs thereof, are converted by alkylation to the corresponding alkyl aromatics by contacting the mononuclear aromatic hydrocarbon with an alkylating agent in the presence of a coated zeolite catalyst. This coated catalyst consists of an essentially inert base support having a strongly adherent outer coating containing an active catalytic zeolite material.
Abstract:
Substituted or unsubstituted cyclohexylbenzene is dehydrogenated to substituted or unsubstituted biphenyl in the absence of oxygen over an oxide complex catalyst. The oxide complex catalyst comprises at least one element selected from the group consisting of Group VB and Group VIII elements, optionally promoted with at least one element selected from the group consisting of Group IA, Group IB, Group IIB, Group VIIB and Group VIB.