Abstract: A method and composition for dimerization of olefins containing 2 to 4 carbon atoms, wherein at least one of said olefins is mixed, in a medium of hydrocarbon or halogenated hydrocarbon solvents at a temperature ranging from 0.degree. to 100.degree. C. under a pressure of from 1 to 40 atm with a two-component catalyst consisting of:(1) a complex of a nickel salt with a tertiary phosphine or tertiary phosphite;(2) an organoaluminum compound comprising a natural or synthetic carbochain rubber, swellable in said solvents, containing 2 to 50 mol. % of AlRX units, wherein R is an alkyl with at most 8 carbon atoms, X is a halogen; atomic ratio Al/Ni being varied within the range of from 1 to 100.The catalyst employed in the method according to the present invention features high stability (retaining its original activity for a long time); it is not crushed and can be readily regenerated.

Abstract: A catalyst for the (co)polymerization of ethylene, .alpha.-olefines, conjugated and non-conjugated dienes, a method of preparation, and a mode of using same. The catalyst contains from 0.1 to 50 wt.% of a compound of a transition metal of the IV-VIII Groups chemically combined and distributed over the surface and within the volume of a rubber-like polymeric carrier containing from 1 to 50 wt.% of electron-donor and/or electron-acceptor groups and is in the form of a gel which is swellable, but insoluble in the reaction medium.A co-catalyst comprising an organic compound of a metal of Groups I-III is employed chemically combined and/or non-combined with the catalyst.The catalyst is prepared by mixing the metal compound with said carrier swollen or dissolved in a solvent, and by extracting the resulting compound with a solvent.(Co)polymerization is effected in a solvent such as a hydrocarbon or a hologenated hydrocarbon derivative at a temperature not exceeding 200.degree. C.

Abstract: A catalyst for the (co)polymerization of ethylene, .alpha.-olefines, conjugated and non-conjugated dienes, a method of preparation and a mode of using same. The catalyst contains from 0.1 to 50 wt.% of a compound of a transition metal of the IV-VIII Groups chemically combined and distributed over the surface and within the volume of a rubber-like polymeric carrier containing from 1 to 50 wt.% of electron donor and/or electron-acceptor groups and is in the form of a gel which is swellable, but insoluble in the reaction medium.A co-catalyst comprising an organic compound of a metal of Groups I-III is employed chemically combined and/or non-combined with the catalyst.The catalyst is prepared by mixing the metal compound with said carrier swollen or dissolved in a solvent, and by extracting the resulting compound with a solvent.(Co)polymerization is effected in a solvent such as a hydrocarbon or a hologenatedhydrocarbon derivative at a temperature not exceeding 200.degree. C.