Multilayer Blow Molded Container and Production Process Thereof
AssigneeKureha Corporation
InventorsTakashi Sato, Satoru Suzuki, Daisuke Itoh
Life of this patent
Estimating the term…
Loading patent…
AssigneeKureha Corporation
InventorsTakashi Sato, Satoru Suzuki, Daisuke Itoh
Estimating the term…
A multilayer blow molded container having a layer structure that a polyglycolic acid layer is provided as a core layer, and thermoplastic polyester resin layers are arranged as inner and outer layers, wherein the melt viscosity x of a polyglycolic acid forming the polyglycolic acid layer is 300 to 900 Pa·s as measured at a temperature of 270° C. and a shear rate of 122 sec−1, the melt viscosity y of a thermoplastic polyester resin forming the thermoplastic polyester resin layers is 250 to 600 Pa·s as measured at a temperature of 290° C. and a shear rate of 122 sec−1, and a melt viscosity ratio x/y between both melt viscosities is 0.85 to 1.80, and a production process thereof.
A multilayer blow molded container having a layer structure that a polyglycolic acid layer is provided as a core layer, and thermoplastic polyester resin layers are arranged as inner and outer layers, wherein the melt viscosity x of a polyglycolic acid forming the polyglycolic acid layer is 300 to 900 Pa·s as measured at a temperature of 270° C. and a shear rate of 122 sec−1, the melt viscosity y of a thermoplastic polyester resin forming the thermoplastic polyester resin layers is 250 to 600 Pa·s as measured at a temperature of 290° C. and a shear rate of 122 sec−1, and a melt viscosity ratio x/y between both melt viscosities is 0.85 to 1.80.
A process for producing a multilayer blow molded container, which comprises co-injection molding a polyglycolic acid and a thermoplastic polyester resin to form a bottomed multilayer preform having a layer structure that a polyglycolic acid layer is provided as a core layer, and thermoplastic polyester resin layers are arranged as inner and outer layers, and then subjecting the multilayer preform to stretch blow molding, wherein the melt viscosity x of the polyglycolic acid is 300 to 900 Pa·s as measured at a temperature of 270° C. and a shear rate of 122 sec−1, the melt viscosity y of the thermoplastic polyester resin is 250 to 600 Pa·s as measured at a temperature of 290° C. and a shear rate of 122 sec1, and a melt viscosity ratio x/y between both melt viscosities is 0.85 to 1.80.
Dependencies are inferred from the claim text.