The present disclosure relates to a continuous process for the preparation of ethylene homopolymers or ethylene copolymers comprising polymerizing ethylene or copolymerizing ethylene and one or more other olefins in the presence of a chromium catalyst in a gas-phase polymerization reactor which is equipped with a cycle gas line for withdrawing reactor gas from the reactor, leading the reactor gas through a heat-exchanger for cooling and feeding the reactor gas back to the reactor, wherein the polymerization is carried out at a temperature from 30? C. to 130? C. and a pressure of from 0.1 to 10 MPa and an aliphatic carboxylic acid ester having from 8 to 24 carbon atoms is added.

The present disclosure relates to a continuous process for the preparation of ethylene homopolymers or ethylene copolymers comprising polymerizing ethylene or copolymerizing ethylene and one or more other olefins in the presence of a chromium catalyst in a gas-phase polymerization reactor which is equipped with a cycle gas line for withdrawing reactor gas from the reactor, leading the reactor gas through a heat-exchanger for cooling and feeding the reactor gas back to the reactor, wherein the polymerization is carried out at a temperature from 30? C. to 130? C. and a pressure of from 0.1 to 10 MPa and an aliphatic carboxylic acid ester having from 8 to 24 carbon atoms is added.

Catalyst systems and methods for making and using the same are described herein. A catalyst system can include at least three catalysts. The three catalysts include a metallocene catalyst, a first non-metallocene including a ligand complexed to a metal through two or more nitrogen atoms, and a second non-metallocene including a ligand complexed to a metal through one or more nitrogen atoms and an oxygen atom.

Catalyst systems and methods for making and using the same are described herein. A catalyst system can include at least three catalysts. The three catalysts include a metallocene catalyst, a first non-metallocene including a ligand complexed to a metal through two or more nitrogen atoms, and a second non-metallocene including a ligand complexed to a metal through one or more nitrogen atoms and an oxygen atom.

The present invention relates to a process for the (co)polymerization of olefins to make polyethylene (co)polymers having sporadic long chain branches in high molecular weight fractions and a high molecular weight tail along with reversed comonomer composition distribution for improving processability, melt strength and optical properties. Such polyethylene (co)polymers have been prepared with a process comprising the reaction of at least the following components: (a) an advanced Ziegler-Natta catalyst precursor comprising titanium; (b) an activator comprising organohalogenous aluminum compounds; (c) ethylene; and (d) one or more alpha-olefins.

The present invention relates to a process for the (co)polymerization of olefins to make polyethylene (co)polymers having sporadic long chain branches in high molecular weight fractions and a high molecular weight tail along with reversed comonomer composition distribution for improving processability, melt strength and optical properties. Such polyethylene (co)polymers have been prepared with a process comprising the reaction of at least the following components: (a) an advanced Ziegler-Natta catalyst precursor comprising titanium; (b) an activator comprising organohalogenous aluminum compounds; (c) ethylene; and (d) one or more alpha-olefins.

Catalyst systems and methods for making and using the same are described herein. A catalyst system can include at least three catalysts. The three catalysts include a metallocene catalyst, a first non-metallocene including a ligand complexed to a metal through two or more nitrogen atoms, and a second non-metallocene including a ligand complexed to a metal through one or more nitrogen atoms and an oxygen atom.

Catalyst systems and methods for making and using the same are described herein. A catalyst system can include at least three catalysts. The three catalysts include a metallocene catalyst, a first non-metallocene including a ligand complexed to a metal through two or more nitrogen atoms, and a second non-metallocene including a ligand complexed to a metal through one or more nitrogen atoms and an oxygen atom.

A polyethylene composition having the following features: 1) a density from 0.957 to 0.968 g/cm.sup.3; 2) a ratio MIF/MIP from 12 to 30; 3) a MIF from 41 to 60 g/10 min.; 4) a long-chain branching index, LCBI, equal to or greater than 0.45; and 5) a ratio (?.sub.0.02/1000)/LCBI from 45 to 75.

A polyethylene composition having the following features: 1) a density from 0.957 to 0.968 g/cm.sup.3; 2) a ratio MIF/MIP from 12 to 30; 3) a MIF from 41 to 60 g/10 min.; 4) a long-chain branching index, LCBI, equal to or greater than 0.45; and 5) a ratio (?.sub.0.02/1000)/LCBI from 45 to 75.