Abstract: Disclosed is a process for preparing n-hexenes and high octane blending components from a mixture of C.sub.6 olefin isomers. Also disclosed is a process for preparing 1-hexene from a mixture of C.sub.6 olefin isomers which provides high octane blending components as a by-product.

Abstract: Disclosed is a process for preparing C.sub.5 to C.sub.18 straight chain .alpha.-olefins from the corresponding internal olefins. The process comprises reacting a C.sub.5 to C.sub.18 straight chain olefin reactant with an electrophilic compound containing hydrogen followed by selectively cracking the resulting product.

Abstract: Disclosed is a process for preparing 1-hexene from 1-butene. The 1-butene is metathesized to produce 3-hexene which is then subjected to, e.g., an hydration/dehydration procedure to produce a mixture of n-hexenes containing 1-hexene.

Abstract: Processes are disclosed for recovering n-hexenes from a mixture comprising n-hexenes and at least one branched-chain C.sub.6 olefin isomer by oligomerizing the branched-chain C.sub.6 olefin isomers, but not the n-hexenes, and recovering the n-hexenes from the resulting mixture.

Abstract: Disclosed is a process for preparing C.sub.5 to C.sub.18 straight chain .alpha.-olefins from the corresponding internal olefins. The process comprises reacting a C.sub.5 C.sub.18 straight chain olefin reactant with an electrophilic compound containing hydrogen followed by cracking the resulting product.

Abstract: The present invention provides a process for the preparation of propylene from C.sub.4 or higher feed by a combination of cracking and metathesis wherein higher hydrocarbon is cracked to form ethylene and propylene and at least a portion of the ethylene is metathesized to propylene.

Abstract: The present invention provides a process for the preparation of ethylene from C.sub.4 or higher feed by a combination of cracking and metathesis wherein higher hydrocarbon is cracked to form ethylene and propylene and at least a portion of the propylene is metathesized to ethylene.

Abstract: An improved olefin disproportionation catalyst produced by contacting an inorganic refractory oxide containing a catalytic amount of molybdenum oxide with a promoting amount of at least one elemental metal selected from the group consisting of barium and magnesium.

Abstract: Olefins are converted into other olefins having different numbers of carbon atoms by contact with a catalyst comprising silica containing tungsten oxide and a promoting amount of silver under conditions suitable for silver to promote the activity of tungsten oxide for the disproportionation reaction.

Abstract: A novel process for the conversion of olefins is provided by adding water to said olefin and thereafter contacting said olefin with an acidic alumina catalyst under conditions sufficient to effect the conversion of said olefin.

Abstract: A disproportionation of olefins is disclosed which employs a novel catalyst system consisting essentially of (I) at least one neutral carbene complex and (II) at least one chlorinated or chlorobrominated saturated organic compound containing only carbon and chlorine or carbon, chlorine, and bromine.

Abstract: A process for producing high octane DIP (2,3-dimethylbutane) from mixed C.sub.4 olefins comprising the steps of subjecting the mixed C.sub.4 olefines to double bond isomerization, skeletal isomerization, olefin disproportionation, olefin hydrogenation and fractionation to yield DIP.

Abstract: High octane gasoline is produced from cat cracked gasoline by cleaving the C.sub.5 olefins in the gasoline with ethylene in a first disproportionation zone. The effluent is separated to produce a C.sub.5.sup.+ stream, a first butenes stream and an ethylene-propylene stream. The ethylene-propylene stream is passed to a second disproportionation or cleavage zone along with additional propylene supplied from an external source. The effluent is separated to produce ethylene which is passed to the first disproportionation zone and a second stream of butenes. The butenes stream are combined and passed to an alkylation zone where it is alkylated with isobutane. The alkylate and remaining gasoline (C.sub.5.sup.+ stream) can be combined to produce a product higher in octane value than cat cracked gasoline.

Abstract: Double bond isomerization and disproportionation of olefins is obtained by contact with a catalyst in a single-stage composition containing a support, uranium, and at least one of tungsten, molybdenum, or rhenium.

Abstract: A feed of mixed butenes is subjected to a combination process comprising skeletal isomerization, disproportionation, and appropriate fractionation to yield separate streams of isobutane, normal butane, and isoamylenes which can be dehydrogenated to isoprene.