Abstract: 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 R5 is a (C1-C15) alkyl group, a (C3-C15) cyclohydrocarbyl group, a (C3-C15) cycloheterohydrocarbyl group, or a (C1-C15) aryl group, and RA, RB, RC, RD, RE, RF, RG, RH, R1, R2, R3, R4, R6, R7, R8, and R9 are independently chosen from a hydrogen atom, a (C1-C50) hydrocarbyl group, or a (C1-C50) heterohydrocarbyl group.

Abstract: 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 R5, R6, and R7 are each independently chosen from a (C1-C50) hydrocarbyl group or a (C1-C50) heterohydrocarbyl group, and wherein the (C1-C50) hydrocarbyl or (C1-C50) heterohydrocarbyl groups of R5, R6, and R7 have greater than 10 carbon atoms combined and RA, RB, RC, and RD and R1, R2, R3, and R4, are independently chosen from a hydrogen atom or a (C1-C50) hydrocarbyl group.

Abstract: Catalyst systems suitable for tetramerizing ethylene to form 1-octene may include a catalyst comprising a chromium compound coordinated with a ligand and a co-catalyst comprising an organoaluminum compound. The ligand may include have a chemical structure according to formula (I), wherein at least one of R1, R2, R3, R4, R5, R6, R7, R8, R9, R10, R11, and R12 have the structure according to formula (II) wherein RA, RB, RC, and RD and the remainder of R1, R2, R3, R4, R5, R6, R7, R8, R9, R10, R11, and R12 are independently chosen from a hydrogen or a (C1-C50) hydrocarbyl group.

Abstract: A system for upgrading pyrolysis oil may include a pyrolysis upgrading unit having a mixed metal oxide catalyst and a separation unit operable to separate used mixed metal oxide catalyst from a reaction effluent. A method for upgrading pyrolysis oil may include contacting the pyrolysis oil with hydrogen in the presence of the mixed metal oxide catalyst at reaction conditions to produce a reaction effluent. The pyrolysis oil may include multi-ring aromatic compounds. The mixed metal oxide catalyst may include a plurality of catalyst particles and each of the plurality of catalyst particles having a plurality of metal oxides. Contacting the pyrolysis oil with hydrogen in the presence of the mixed metal oxide catalyst at the reaction conditions may convert at least a portion of the multi-ring aromatic compounds in the pyrolysis oil to the light aromatic compounds.

Abstract: A system for upgrading pyrolysis oil may include a pyrolysis upgrading unit having a mixed metal oxide catalyst and a separation unit operable to separate used mixed metal oxide catalyst from a reaction effluent. A method for upgrading pyrolysis oil may include contacting the pyrolysis oil with hydrogen in the presence of the mixed metal oxide catalyst at reaction conditions to produce a reaction effluent. The pyrolysis oil may include multi-ring aromatic compounds. The mixed metal oxide catalyst may include a plurality of catalyst particles and each of the plurality of catalyst particles having a plurality of metal oxides. Contacting the pyrolysis oil with hydrogen in the presence of the mixed metal oxide catalyst at the reaction conditions may convert at least a portion of the multi-ring aromatic compounds in the pyrolysis oil to the light aromatic compounds.

Abstract: A system for upgrading pyrolysis oil may include a pyrolysis upgrading unit having a mixed metal oxide catalyst and a separation unit operable to separate used mixed metal oxide catalyst from a reaction effluent. A method for upgrading pyrolysis oil may include contacting the pyrolysis oil with hydrogen in the presence of the mixed metal oxide catalyst at reaction conditions to produce a reaction effluent. The pyrolysis oil may include multi-ring aromatic compounds. The mixed metal oxide catalyst may include a plurality of catalyst particles and each of the plurality of catalyst particles having a plurality of metal oxides. Contacting the pyrolysis oil with hydrogen in the presence of the mixed metal oxide catalyst at the reaction conditions may convert at least a portion of the multi-ring aromatic compounds in the pyrolysis oil to the light aromatic compounds.