Zeolitic and molecular organic framework materials as catalysts suitable for generating branched olefins from linear olefins, thereby increasing the octane of a composition comprising the linear olefins. In particular, catalyst may exhibit selectivity for methyl-shift isomerization over cracking, alkylation, and oligomerization.

Isomerized olefin products are produced by contacting an olefin feed containing a C.sub.10 to C.sub.20 normal alpha olefin, a solid acid catalyst, and a C.sub.2 to C.sub.15 primary ester to form the isomerized olefin product. Typical primary esters used in the processes include formates and acetates. Linear olefin compositions are produced that contain at least 80 wt. % C.sub.10 to C.sub.20 linear internal olefins, less than 8 wt. % C.sub.10 to C.sub.20 normal alpha olefins, less than 8 wt. % dimers of C.sub.10 to C.sub.20 olefins, less than 15 wt. % C.sub.10 to C.sub.20 branched olefins, and at least 1 wt. % C.sub.2 to C.sub.15 primary ester and less than 8 wt. % secondary esters.

Provided herein are cinchonium betaine catalysts and methods of promoting asymmetric imine isomerization reactions using the same.

A homogeneous catalytic reaction method and a catalyst for isomerization and hydroformylation of long-chain internal olefins are disclosed. A rhodium-ruthenium metal complex is used as a catalyst; and the ligands are tetradentate phosphine ligands. By means of the catalytic system, homogeneous internal olefin isomerization aid hydroformylation can be performed under a certain temperature and pressure to obtain aldehyde products having high normal to iso ratios. The present invention is applicable to not only long-chain internal olefins (C8) but also internal olefins having a carbon number less than 8.

Multi-reactor systems with aromatization reactor vessels containing a catalyst with low surface area and pore volume, followed in series by aromatization reactor vessels containing a catalyst with high surface area and pore volume, are disclosed. Related reforming methods using the different aromatization catalysts also are described.

Multi-reactor systems with aromatization reactor vessels containing a catalyst with low surface area and pore volume, followed in series by aromatization reactor vessels containing a catalyst with high surface area and pore volume, are disclosed. Related reforming methods using the different aromatization catalysts also are described.

Provided herein are cinchonium betaine catalysts and methods of promoting asymmetric imine isomerization reactions using the same.

Catalytic processes employing rhodium complexes are disclosed, wherein the catalytic processes involve an initial step of activation of a CH bond present within a hydrocarbon substrate. In contrast to prior art techniques, the catalytic processes of the invention can be conducted at low temperatures, and the catalytic compounds are themselves highly recyclable. Also disclosed are the rhodium complexes themselves and processes of making them.

Provided herein are cinchonium betaine catalysts and methods of promoting asymmetric imine isomerization reactions using the same.

Provided herein are cinchonium betaine catalysts and methods of promoting asymmetric butenolide isomerization reactions using the same.