Abstract:
A process for producing an ethylene/α-olefin/unconjugated polyene copolymer, which comprises copolymerizing ethylene, an α-olefin, and an unconjugated polyene in a hydrocarbon solvent with the aid of a transition metal compound catalyst to obtain a solution containing a copolymer and removing the unreacted monomers and the hydrocarbon solvent from the solution without removing the residual catalyst, characterized in that the monomers are copolymerized under the conditions of a polymerization temperature of 100°C or higher and a polymerization pressure of 2.7 MPa or higher while regulating the concentration of the unconjugated polyene in the polymerization mixture solution to a value less than the maximum unconjugated-polyene concentration Cmax (mol/L) shown below: Cmax = 0.050 (mol/L) when the iodine value (IV) of the copolymer is 9.0 to less than 17.0 g/100g, and Cmax = 0.104 (mol/L) when the iodine value (IV) of the copolymer is not lower than 17.0 g/100g.
Abstract:
A polymer characterized by having a melt tension (MT (g)) substantially equal to or lower than that of a polymer which is substantially equal in repeating units of the backbone and in molecular weight, molecular-weight distribution, and crystallinity and by having a flow activation energy (Ea (KJ/mol)) higher by at least 5 KJ/mol than the Ea value of that polymer. A preferred example of the polymer is one which comprises 50 to 100 mol% repeating units derived from ethylene and 0 to 50 mol% repeating units derived from an a-olefin having 3 to 20 carbon atoms, satisfies a specific relationship between flow activation energy (Ea (KJ/mol)) and a-olefin content (C (wt.%)), and satisfies a specific relationship between melt tension (MT (g)) and melt flow rate (MFR (g/10 min)). This branched polyolefin is excellent in moldability and mechanical strength.