Antistatic laminated foam sheet and process for producing same

1. An extruded laminated foam sheet comprising a foam layer containing a polyethylene-based resin (PE-1), and an antistatic layer laminated on at least one side of the foam layer,

said antistatic layer having a basis weight of 1 to 20 g/m 2 and containing a polyethylene-based resin (PE-2), an ionomer resin having an antistatic property and a polyalkylene glycol,

wherein the ionomer resin is contained in the antistatic layer in an amount of 5 to 50% by weight based on the total weight of the polyethylene-based resin (PE-2) and the ionomer resin,

wherein the polyethylene-based resin (PE-2) forms a continuous phase, and the ionomer resin forms dispersed phases dispersed in the continuous phase, and

wherein, on a vertical cross-section of the antistatic layer, which is taken along the extrusion direction of the laminated foam sheet, a number-based median value S 50 of cross-sectional areas of the dispersed phases is 1×10 2 to 5×10 5 nm 2 , and

wherein a weight ratio of the polyalkylene glycol to the ionomer resin is 0.03 to 0.6.

2. The extruded laminated foam sheet according to claim 1 , wherein, on the vertical cross-section of the antistatic layer, an aspect ratio LM 50 /LT 50 of a number-based median value LM 50 of diameters in the extrusion direction of the dispersed phases to a number-based median value LT 50 of diameters in the thickness direction of the dispersed phases is 2 or more.

3. The extruded laminated foam sheet according to claim 1 , wherein the polyalkylene glycol is present in the antistatic layer in an amount of 0.3 to 6% based on the weight of the antistatic layer.

4. The extruded laminated foam sheet according to claim 1 , wherein a difference (Tmp−Tmi) between a melting point Tmp of the polyethylene-based resin (PE-2) and a melting point Tmi of the ionomer resin is 5 to 30° C.

5. The extruded laminated foam sheet according to claim 1 , wherein the antistatic layer has a surface resistivity of 1×10 13 Ω or less.

6. The extruded laminated foam sheet according to claim 1 , wherein the extruded laminated foam sheet has a thickness of 0.05 to 2 mm.

7. The extruded laminated foam sheet according to claim 1 , wherein the extruded laminated foam sheet has an apparent density of 15 to 200 kg/m 3 .

8. A process for producing a laminated foam sheet having a polyethylene-based resin foam layer and a polyethylene-based resin antistatic layer laminated on at least one side of the foam layer, comprising the steps of:

providing a first melt containing a polyethylene-based resin (PE-1) and a physical blowing agent,

providing a second melt containing a polyethylene-based resin (PE-2), an ionomer resin having an antistatic property, a polyalkylene glycol and a volatile plasticizer, and

coextruding the first and second melts to form the laminated foam sheet in which the polyethylene-based resin foam layer and the polyethylene-based resin antistatic layer are formed from the first and second melts, respectively,

wherein the ionomer resin is present in the second melt in an amount of 5 to 50% by weight based on the total weight of the polyethylene-based resin (PE-2) and the ionomer resin, wherein a weight ratio of the polyalkylene glycol to the ionomer resin is 0.03 to 0.6,

wherein the antistatic layer having a basis weight of 1 to 20 g/m 2 ,

wherein the polyethylene-based resin (PE-2) forms a continuous phase, and the ionomer resin forms dispersed phases dispersed in the continuous phase, and

wherein, on a vertical cross-section of the antistatic layer, which is taken along the extrusion direction of the laminated foam sheet, a number-based median value S 50 of cross-sectional areas of the dispersed phases is 1×10 2 to 5×10 5 nm 2 .

9. The process according to claim 8 , wherein the volatile plasticizer is present in the second melt in an amount of 1 to 60 parts by weight per 100 parts by weight of the total weight of the polyethylene-based resin (PE-2) and the ionomer resin and wherein a weight ratio of the volatile plasticizer to polyalkylene glycol is 5 to 100.

10. The process according to claim 8 , wherein the volatile plasticizer is at least one selected from the group consisting of saturated hydrocarbons having 3 to 5 carbon atoms, dialkyl ethers in which each alkyl has 1 to 3 carbon atoms, and alcohols.

11. The process according to claim 8 , wherein the volatile plasticizer is n-butane, isobutane or a mixture thereof.