Abstract:
A solid catalyst component for the (co)polymerization of α-olefins having general formula (I): ZrnMAlxClyMgp (I) wherein: M represents titanium (Ti), vanadium (V), or mixtures thereof; n is a number ranging from 0.01 to 2; x is a number ranging from 0.1 to 4; y is a number ranging from 5 to 53; p is a number ranging from 0 to 15; obtained by means of a process comprising putting at least one zirconium arene in contact with at least one metal compound and, optionally, with at least one compound of magnesium. Said solid catalyst component can be advantageously used as a solid component in a catalyst for the (co)polymerization of α-olefins.Said catalyst can be advantageously used in a process for the (co)polymerization of α-olefins.
Abstract:
A solid catalyst component for the (co)polymerization of α-olefins having general formula (I): ZrnMAlxClMgp (I) wherein: M represents titanium (Ti), vanadium (V), or mixtures thereof; n is a number ranging from 0.01 to 2; x is a number ranging from 0.1 to 4; y is a number ranging from 5 to 53; p is a number ranging from 0 to 15; obtained by means of a process comprising putting at least one zirconium arene in contact with at least one metal compound and, optionally, with at least one compound of magnesium. Said solid catalyst component can be advantageously used as a solid component in a catalyst for the (co)polymerization of α-olefins. Said catalyst can be advantageously used in a process for the (co)polymerization of α-olefins.
Abstract:
The particle size is increased and particle size range is decreased without loss of compactness in a Ziegler-type catalyst, by carrying out the reduction reaction in the presence of a preformed catalyst at a reduction rate which minimizes formation of new nuclei. The reduction of TiCl4 with diethylaluminum, ethyl aluminum dichloride, triethyl aluminum, and mixtures thereof, is exemplary. The preformed catalyst is mixed with the reactants at a low temperature at which the rate of reduction is negligible (e.g. -40* to -5* C.), and the reactants are slowly heated (0.2* C/min to 2.0* C/min) while in a well-mixed zone until a holding temperature of +25* C. to +45* C. is reached. The reactants are held at the holding temperature for 0 to 120 minutes, after which the catalyst is activated by heating at 160* C. for 1 hour. If the reduction step is to be repeated, the catalyst is not activated, but is cooled to -30* C. for repetition of the reduction step. Preferably, the reduction step is repeated three times, the catalyst in the reduction zone during the holding step providing the preformed catalyst for the following reduction procedure.
Abstract:
A solid catalyst component for the (co)polymerization of α-olefins having general formula (I): ZrnMAlxClyMgp (I) wherein: M represents titanium (Ti), vanadium (V), or mixtures thereof; n is a number ranging from 0.01 to 2; x is a number ranging from 0.1 to 4; y is a number ranging from 5 to 53; p is a number ranging from 0 to 15; obtained by means of a process comprising putting at least one zirconium arene in contact with at least one metal compound and, optionally, with at least one compound of magnesium. Said solid catalyst component can be advantageously used as a solid component in a catalyst for the (co)polymerization of α-olefins.Said catalyst can be advantageously used in a process for the (co)polymerization of α-olefins.
Abstract:
A solid catalyst component for the (co)polymerization of α-olefins having general formula (I): ZrnMAlxClMgp (I) wherein: M represents titanium (Ti), vanadium (V), or mixtures thereof; n is a number ranging from 0.01 to 2; x is a number ranging from 0.1 to 4; y is a number ranging from 5 to 53; p is a number ranging from 0 to 15; obtained by means of a process comprising putting at least one zirconium arene in contact with at least one metal compound and, optionally, with at least one compound of magnesium. Said solid catalyst component can be advantageously used as a solid component in a catalyst for the (co)polymerization of α-olefins. Said catalyst can be advantageously used in a process for the (co)polymerization of α-olefins.
Abstract:
A process for manufacturing a thermoplastic elastomeric material includes at least one elastomeric phase and at least one thermoplastic phase by the following steps: surface-treating a vulcanized rubber in a subdivided form with an effective amount of at least one organometallic polymerization catalyst; and polymerizing at least one ethylenically unsaturated monomer in the presence of the surface-treated vulcanized rubber in a subdivided form to obtain at least one thermoplastic phase.
Abstract:
A CATALYST, USEFUL FOR THE POLYMERIZATION OF OLEFINS, WHICH CONTAINS VIOLET TICL3 AND HAS A HIGH STEROSPECIFICITY IS PREPARED BY CONTACTING BROWN TICL3 WITH TICL4 AT A TEMPERATURE BELOW 100*C.