Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
288 words
A PROCESS FOR PRODUCING ELASTOMERIC COPOLYMERS OF NONCONJUGATED DIOLEFINS CONTAINING AT LEAST ONE TERMINAL UNSATURATION OF VINYL TYPE AND FROM FIVE TO 15 CARBON ATOMS WITH AT LEAST ONE MONOOLEFIN SELECTED FROM THE GROUP CONSISTING OF ETHYLENE AND ALIPHATIC ALPHA-OLEFINS CONTAINING FROM THREE TO EIGHT CARBON ATOMS, SAID COPOLYMERS BEING ESSENTIALLY LINEAR AND AMORPHOUS UNDER X-RAYS EXAMINATION, COMPLETELY EXTRACTABLE WITH BOILING N-HEPTANE, MADE UP OF MACROMOLECULES CONTAINING COPOLYMERIZED UNITS OF ALL OF THE STARTING MONOMERS AND IN WHICH PRACTICALLY ALL OF THE COPOLYMERIZED DIOLEFIN UNITS ARE POLYMERIZED 1, 2 AND HAVE UNSATRUATIONS IN SIDE GROUPS, SAID COPOLYMERS HAVING A MOLECULAR WEIGHT HIGHER THAN 20,000 AND BEING READILY SULFUR-VULVANIZABLE TO SYNTHETIC RUBBERS HAVING LOW DEFORMATION AT BREAK, WHICH PROCESS COMPRISES COPOLYMERIZING A MIXTURE OF THE MONOMERS, ONE OF WHICH IS A NON-CONJUGATED DIOLEFIN, IN A REACTION MIXTURE WHICH CONSISTS ESSENTIALLY OF THE MONOMERS MIXTURE IN THE LIQUID STATE OR CONSISTS OF AN INERT HYDROCARBON SOLVENT, IN CONTACT WITH A CATALYST PREPARED BY MIXING HYDROCARBONSOLUBLE COMPOUNDS OF VANADIUM SELECTED FROM THE GROUP CONSISTING OF VANADIUM TRIACETYLACETONATE, VANADYL DIACETYLACETONATE, VANADYL HALOGEN-ACETYLACETONATES, TETRAHYDROFURANATES AND DIALKYL ETHERATES OF VANADIUM TRICHLORIDE, VANADIUM TETRACHLORIDE AND VANADYL TRICHLORIDE, AND PYRIDINATES, AMINATES AND QUINOLINATES OF VANADIUM TRICHLORIDE, VANADIUM TETRACHLORIDE AND VANADYL TRICHLORIDE, WITH AT LEAST ONE ALKYL METAL HALIDE SELECTED FROM THE GROUP CONSISTING OF DIALKYL ALUMINUM HALIDES AND ALKYL ALUMINUM DIHALIDES IN WHICH THE ALKYL GROUPS CONTAIN FROM ONE TO SIX CARBON ATOMS, IN A MOLAR RATIO OF THE ALKYL METAL HALIDE TO VANADIUM COMPOUND COMPRISED BETWEEN TWO AND 30, BOTH THE PREPARATION OF THE CATALYST AND THE COPOLYMERIZATION BEING CARRIER OUT AT A TEMPERATURE BETWEEN -80*C AND 0*C, AND THE CONCENTRATION OF THE MONOMERS TO BE COPOLYMERIZED BEING MAINTAINED SUBSTANTIALLY CONSTANT DURING THE COPOLYMERIZATION REACTION.
Claim 2
Dependent Claim
288 words
A PROCESS FOR PRODUCING ELASTOMERIC COPOLYMERS OF NONCONJUGATED DIOLEFINS CONTAINING AT LEAST ONE TERMINAL UNSATURATION OF VINYL TYPE AND FROM FIVE TO 15 CARBON ATOMS WITH AT LEAST ONE MONOOLEFIN SELECTED FROM THE GROUP CONSISTING OF ETHYLENE AND ALIPHATIC ALPHA-OLEFINS CONTAINING FROM THREE TO EIGHT CARBON ATOMS, SAID COPOLYMERS BEING ESSENTIALLY LINEAR AND AMORPHOUS UNDER X-RAYS EXAMINATION, COMPLETELY EXTRACTABLE WITH BOILING N-HEPTANE, MADE UP OF MACROMOLECULES CONTAINING COPOLYMERIZED UNITS OF ALL OF THE STARTING MONOMERS AND IN WHICH PRACTICALLY ALL OF THE COPOLYMERIZED DIOLEFIN UNITS ARE POLYMERIZED 1, 2 AND HAVE UNSATRUATIONS IN SIDE GROUPS, SAID COPOLYMERS HAVING A MOLECULAR WEIGHT HIGHER THAN 20,000 AND BEING READILY SULFUR-VULVANIZABLE TO SYNTHETIC RUBBERS HAVING LOW DEFORMATION AT BREAK, WHICH PROCESS COMPRISES COPOLYMERIZING A MIXTURE OF THE MONOMERS, ONE OF WHICH IS A NON-CONJUGATED DIOLEFIN, IN A REACTION MIXTURE WHICH CONSISTS ESSENTIALLY OF THE MONOMERS MIXTURE IN THE LIQUID STATE OR CONSISTS OF AN INERT HYDROCARBON SOLVENT, IN CONTACT WITH A CATALYST PREPARED BY MIXING HYDROCARBONSOLUBLE COMPOUNDS OF VANADIUM SELECTED FROM THE GROUP CONSISTING OF VANADIUM TRIACETYLACETONATE, VANADYL DIACETYLACETONATE, VANADYL HALOGEN-ACETYLACETONATES, TETRAHYDROFURANATES AND DIALKYL ETHERATES OF VANADIUM TRICHLORIDE, VANADIUM TETRACHLORIDE AND VANADYL TRICHLORIDE, AND PYRIDINATES, AMINATES AND QUINOLINATES OF VANADIUM TRICHLORIDE, VANADIUM TETRACHLORIDE AND VANADYL TRICHLORIDE, WITH AT LEAST ONE ALKYL METAL HALIDE SELECTED FROM THE GROUP CONSISTING OF DIALKYL ALUMINUM HALIDES AND ALKYL ALUMINUM DIHALIDES IN WHICH THE ALKYL GROUPS CONTAIN FROM ONE TO SIX CARBON ATOMS, IN A MOLAR RATIO OF THE ALKYL METAL HALIDE TO VANADIUM COMPOUND COMPRISED BETWEEN TWO AND 30, BOTH THE PREPARATION OF THE CATALYST AND THE COPOLYMERIZATION BEING CARRIER OUT AT A TEMPERATURE BETWEEN -80*C AND 0*C, AND THE CONCENTRATION OF THE MONOMERS TO BE COPOLYMERIZED BEING MAINTAINED SUBSTANTIALLY CONSTANT DURING THE COPOLYMERIZATION REACTION.
Claim 3
Dependent Claim
35 words
The process according to claim 1, characterized in that ethylene, propylene and the non-conjugated diolefin are copolymerized, and a molar ratio of propylene to ethylene of at least 4:1 is maintained in the liquid phase.
Claim 4
Dependent Claim
34 words
The process according to claim 1, characterized in that ethylene, butene-1 and the non-conjugated diolefin are copolymerized, and a butene-1 to ethylene molar ratio of at least 25:1 is maintained in the liquid phase.
Claim 5
Dependent Claim
35 words
The process according to claim 1, further characterized in that the alkyl metal compound is dialkyl aluminum monochloride and the molar ratio between the aluminum compound and vanadium compound is comprised between 2 and 30.
Claim 6
Dependent Claim
18 words
The process according to claim 1, characterized in that the polymerization is carried out in an inert solvent.
Claim 7
Dependent Claim
15 words
The process according to claim 1, characterized in that the polymerization is carried out continuously.
Claim 8
Dependent Claim
40 words
The process according to claim 1, characterized in that the copolymerization is carried out continuously by adding the catalyst components continuously to the copolymerizing system while maintaining constant the ratio between the concentrations of the monomers in the liquid phase.
Claim 9
Dependent Claim
66 words
The process according to claim 1, characterized in that the non-conjugated diolefin contains only one terminal double bond of the vinyl type, both the preparation of the catalyst and the copolymerization are carried out at a temperature between +10*C and -80*C, and the copolymerization is effected in the absence of inert solvents and using the monomers mixture maintained in the liquid state as the copolymerization medium.
Claim 10
Dependent Claim
25 words
The process of claim 1 in which the catalyst is prepared and the copoLymerization is carried out at a temperature of from -50*C to -10*C.