Hollow polystyrene body obtained by injection stretch blow moulding
A blow molding having capacity of at least 250 ml, having a shell which is composed of impact-resistant polystyrene and which is produced via injection stretch blow molding where an average aspect ratio of rubber particles derived from longitudinal section and an average aspect ratio of rubber particles derived from cross section measured in transmission electron micrographs is greater than 4 respectively, and a biaxial orientation of the rubber particles, given by the ratio of the aspect ratio derived from cross section to the aspect ratio derived from longitudinal section is smaller than 3.
1. A blow molding having capacity of at least 250 ml, having a shell which is composed of impact-resistant polystyrene and which is produced via injection stretch blow molding where an average aspect ratio of rubber particles derived from longitudinal section and an average aspect ratio of rubber particles derived from cross section measured in transmission electron micrographs is greater than 4 respectively, and a biaxial orientation of the rubber particles, given by the ratio of the aspect ratio derived from cross section to the aspect ratio derived from longitudinal section is smaller than 3.
2. The blow molding according to claim 1 , wherein the shell has less than 30 ppm sulfur content.
3. The blow molding according to claims 1 , wherein the shell has also been additionally equipped with a plastic with a barrier property.
4. The blow molding according to claim 3 , wherein the plastic with a barrier property comprises polyamide, polyvinylidene chloride or styrene-acrylonitrile copolymers.
5. The blow molding according to claim 1 , where the shell has been covered with a shrink film.
6. The blow molding according to claim 5 , where the shrink film is composed of a styrene-butadiene block copolymer.
7. A process for production of blow molding according to claim 1 , which comprises
i) melting pellets composed of impact-resistant polystyrene and injection molding said melted pellets to give a parison,
ii) transferring the resultant parison to a second mold, where it is stretched and blown.
8. The process according to claim 7 , wherein the prevailing temperatures in step i) are from 150 to 260° C. and in step ii) are from 120 to 145° C.
9. The process according to claim 7 , wherein the preblowing pressure set in step ii) is smaller than 5 bar and the subsequent blowing pressure set is smaller than 15 bar.
10. A process for the storage of dairy products which comprises utilizing the blow molding according to claim 1 .