A process for making a poly alpha-olefin (PAO) having a relatively high vinylidene content (or combined vinylidene and tri-substituted vinylene content) and a relatively low vinyl and/or di-substituted vinylene content, as well as a relatively low molecular weight. The process includes: contacting a feed containing a C.sub.2-C.sub.32 alpha-olefin with a catalyst system comprising activator and a bis-cyclopentadienyl metallocene compound, typically a cyclopentadienyl-benzindenyl group 4 transition metal compound.

A process for making a poly alpha-olefin (PAO) having a relatively high vinylidene content (or combined vinylidene and tri-substituted vinylene content) and a relatively low vinyl and/or di-substituted vinylene content, as well as a relatively low molecular weight. The process includes: contacting a feed containing a C.sub.2-C.sub.32 alpha-olefin with a catalyst system comprising activator and a bis-cyclopentadienyl metallocene compound, typically a cyclopentadienyl-benzindenyl group 4 transition metal compound.

A three step method for the conversion of ethanol into fuels that can be utilized as full-performance military jet or diesel fuels. Embodiments of the invention further describe methods for the selective conversion of ethanol to full performance saturated hydrocarbon fuels that are suitable for both jet and diesel propulsion.

A three step method for the conversion of ethanol into fuels that can be utilized as full-performance military jet or diesel fuels. Embodiments of the invention further describe methods for the selective conversion of ethanol to full performance saturated hydrocarbon fuels that are suitable for both jet and diesel propulsion.

The present disclosure relates to processes to produce a poly alpha-olefin (PAO) composition. In some embodiments, a process includes introducing a first C6-C32 alpha-olefin, a second C6-C32 alpha-olefin different than the first C6-C32 alpha-olefin, and a first catalyst system comprising an activator and a metallocene compound into a first reactor, wherein a molar ratio of the first C6-C32 alpha-olefin to the second C6-C32 alpha-olefin is from about 1:5 to about 5:1, by total moles of the first and second C6-C32 alpha-olefin; obtaining a first effluent including a PAO dimer; introducing the first effluent, a third C6-C32 alpha-olefin, and a second catalyst system to an oligomerization unit, wherein the third C6-C32 alpha-olefin is the same or different than the first C6-C32 alpha-olefin and/or second C6-C32 alpha-olefin; obtaining a second effluent; and hydrogenating the second effluent to form the PAO composition.

The present disclosure relates to processes to produce a poly alpha-olefin (PAO) composition. In some embodiments, a process includes introducing a first C6-C32 alpha-olefin, a second C6-C32 alpha-olefin different than the first C6-C32 alpha-olefin, and a first catalyst system comprising an activator and a metallocene compound into a first reactor, wherein a molar ratio of the first C6-C32 alpha-olefin to the second C6-C32 alpha-olefin is from about 1:5 to about 5:1, by total moles of the first and second C6-C32 alpha-olefin; obtaining a first effluent including a PAO dimer; introducing the first effluent, a third C6-C32 alpha-olefin, and a second catalyst system to an oligomerization unit, wherein the third C6-C32 alpha-olefin is the same or different than the first C6-C32 alpha-olefin and/or second C6-C32 alpha-olefin; obtaining a second effluent; and hydrogenating the second effluent to form the PAO composition.

The selective oligomerization of ethylene to produce a mixture comprising octene and hexene is conducted in the presence of a catalyst system comprising a source of chromium; two different P—N—P ligands and an activator. The phosphorus atoms of both ligands have ortho-fluoro phenyl substituents. The nitrogen atom of the first ligand has an isopropyl substituent. The nitrogen of the second ligand has a larger/bulkier hydrocarbyl substituent on the N atom. The hexene produced by the process of this invention has very high alpha selectivity.

The selective oligomerization of ethylene to produce a mixture comprising octene and hexene is conducted in the presence of a catalyst system comprising a source of chromium; two different P—N—P ligands and an activator. The phosphorus atoms of both ligands have ortho-fluoro phenyl substituents. The nitrogen atom of the first ligand has an isopropyl substituent. The nitrogen of the second ligand has a larger/bulkier hydrocarbyl substituent on the N atom. The hexene produced by the process of this invention has very high alpha selectivity.

Disclosed herein is a method of preparing 1-octene at high activity and high selectivity while stably maintaining reaction activity by tetramerizing ethylene using a chromium-based catalyst system comprising a transition metal or a transition metal precursor, a cocatalyst, and a P—C—C—P backbone structure ligand represented by (R.sup.1)(R.sup.2)P—(R.sup.5)CHCH(R.sup.6)—P(R.sup.3)(R.sup.4).

Disclosed herein is a method of preparing 1-octene at high activity and high selectivity while stably maintaining reaction activity by tetramerizing ethylene using a chromium-based catalyst system comprising a transition metal or a transition metal precursor, a cocatalyst, and a P—C—C—P backbone structure ligand represented by (R.sup.1)(R.sup.2)P—(R.sup.5)CHCH(R.sup.6)—P(R.sup.3)(R.sup.4).