The present invention relates to a method for olefin oligomerization and comprising i) injecting an olefin monomer and a solvent into a continuous stirred tank reactor (CSTR); ii) injecting an oligomerization catalyst system comprising a ligand compound, a transition metal compound, and a co-catalyst into the continuous stirred tank reactor; and iii) performing a multimerization reaction of the olefin monomer, wherein a ratio of the flowing rates of the olefin monomer and the solvent is from 1:1 to 2:1. In the method for olefin oligomerization according to the present invention, high linear alpha-olefin selectivity may be attained even with a small amount of a solvent used by controlling reaction conditions during the multimerization reaction of olefin by a continuous reaction using a continuous stirred tank reactor.

An object of the present invention is to provide a method for suppressing the precipitation of polymers with a high concentration dissolved in a solvent in the operation termination step and suppressing the blockage of the apparatus by the polymers even when the polymers with a high concentration are precipitated, and the invention relates to a method for producing an α-olefin low polymer comprising a production operation step and an operation termination step, wherein the supply position of a supply liquid to a distillation column in the operation termination step is changed to a position lower than the supply position of a supply liquid to the distillation column in the production operation step.

A method for producing an olefin oligomer is disclosed, in which an olefin oligomerization reaction is performed in the presence of an olefin oligomerization catalyst comprising (A) a chromium compound, (B) an amine compound of the general formula (1): ##STR00001##
(R.sup.1 to R.sup.4 represent a group such as a hydrocarbon group, Y represents a structure represented by —CR.sup.5R.sup.6—, R.sup.5 and R.sup.6 represent a group such as a hydrogen atom, and Z represents an integer of 1 to 10),
and (C) a compound such as an organometal compound; and the olefin oligomerization catalyst.

The present invention encompasses a catalyst composition that includes a heterogeneous oligomerization catalyst including a metal-organic framework, the metal-organic framework including a plurality of first metal ions coordinated to one or more ligands, wherein each of the one or more ligands has only one N-heterocyclic aromatic group. The present invention further includes a method of oligomerization that comprises contacting one or more olefins with the heterogeneous oligomerization catalyst to form one or more oligomers, wherein the heterogeneous catalyst comprises the said metal-organic framework and an optional support.

Methods of polymer and/or oligomer depolymerization are described herein which, in some embodiments, enable facile polymer and/or oligomer decomposition under mild, non-energy intensive conditions. Briefly, a method of depolymerization comprises providing a reaction mixture comprising a transition metal catalyst, and a polymer or oligomer having a backbone including cyclobutane units, and decomposing the polymer or oligomer to provide diene monomer or alkene monomer.

Disclosed herein are processes and reaction systems for controlling a temperature of an oligomerization reaction zone using a heat exchange system.

Disclosed herein are processes and reaction systems for controlling a temperature of an oligomerization reaction zone using a heat exchange system.

The invention relates to oligomerization of olefins, such as ethylene, to higher olefins, such as a mixture of 1-hexene and 1-octene, using a catalyst system that comprises a) a source of chromium b) one or more activators and c) a phosphacycle-containing ligating compound. Additionally, the invention relates to a phosphacycle-containing ligating compound and a process for making said compound.

Catalyst systems for tetramerizing ethylene to form 1-octene may include a catalyst which may include a chromium compound coordinated with a ligand and a co-catalyst which may include an organoaluminum compound. The ligand may have a chemical structure according to Chemical Structure (I), wherein R.sub.5, R.sub.6, and R.sub.7 are each independently chosen from a (C.sub.1-C.sub.50) hydrocarbyl group or a (C.sub.1-C.sub.50) heterohydrocarbyl group, and wherein the (C.sub.1-C.sub.50) hydrocarbyl or (C.sub.1-C.sub.50) heterohydrocarbyl groups of R.sub.5, R.sub.6, and R.sub.7 have greater than 10 carbon atoms combined and R.sub.A, R.sub.B, R.sub.C, and R.sub.D and R.sub.1, R.sub.2, R.sub.3, and R.sub.4, are independently chosen from a hydrogen atom or a (C.sub.1-C.sub.50) hydrocarbyl group.

A process comprising a heterogenous reaction between a solid metal organic framework supported heteropolyacid catalyst and a hydrocarbon feed to form a modified hydrocarbon stream. The modified hydrocarbon stream comprises essentially of C6+ hydrocarbons.