Ethylene polymers for extrusion coating

1. A low density polyethylene having a melt flow rate (MFR) according to ISO 1133 (190° C., 2.16 kg) which is higher than 4.0 g/10 min, a storage modulus G′, measured at a loss modulus G″ of 5 kPa, which is above 3000 Pa, a vinylidene content which is at least 24/100 k C, and a molecular weight distribution Mw/Mn which is at least 22 and not higher than 30.

2. A low density polyethylene according to claim 1 , wherein the low density polyethylene is produced in a tubular reactor.

3. A low density polyethylene according to claim 1 , wherein the low density polyethylene has a vinylidene content which is at least 28/100 k C.

4. A composition comprising the low density polyethylene according to claim 1 , wherein the composition, optionally, may be useful in extrusion coating.

5. A composition according to claim 4 , which comprises the low density polyethylene in an amount of 5 to 40 wt %, based on the total weight of the composition, and may further comprise at least one olefin polymer prepared in the presence of a transition metal catalyst, which at least one olefin polymer may be selected from homo- or copolymers of polyethylene, polypropylene or poly-1-butene.

6. A process for production of the low density polyethylene according to claim 1 , in a tubular reactor by radical initiated polymerization under a pressure from 1000 to 3000 bar where the polymerization is performed by reacting a reaction mixture, comprising ethylene monomers, under action of one or more radical initiators, such as peroxides, oxygen or combinations thereof, wherein the amount of used radical initiators, i.e. the amount of used active oxygen, is at least 0.20 kg/ton PE, and, optionally, wherein inlet temperature of the reaction mixture into the first reaction zone of the reactor is 135° C. or lower.

7. A process according to claim 6 , wherein a radical initiator cocktail is used, which is composed of the following radical initiators, where the 0.1 hours half life temperature (T½) is given for each radical initiator: Initiator A (T½ 0.1 h at 75-90° C. in chlorobenzene), Initiator B (T½ 0.1 h at 80-95° C. in chlorobenzene), Initiator C (T½ 0.1 h at 105-125° C. in chlorobenzene), Initiator D (T½ 0.1 h at 125-140° C. in chlorobenzene), Initiator E (T½ 0.1 h at 130-145° C. in chlorobenzene) and Initiator F (T½ 0.1 h at 155-175° C. in chlorobenzene).

8. A method for an extrusion coating process, which method comprises extrusion coating a flat substrate by extruding the low density polyethylene according to claim 1 .

9. A method for an extrusion coating process, which method comprises extrusion coating a flat substrate by extruding the composition according to claim 4 , in a molten state through a flat die onto said substrate.

10. An article selected from an extrusion article, an extrusion coating article or an extrusion lamination article, film blowing article, film casting article, wire and cable extrusion article, injection molding article, blow molding article or pipe extrusion article, comprising the low density polyethylene according to claim 1 .

11. An article selected from an extrusion article, an extrusion coating article or an extrusion lamination article, film blowing article, film casting article, wire and cable extrusion article, injection molding article, blow molding article or pipe extrusion article, comprising the composition according to claim 4 .