Processing additives and uses of same in rotational molding
The cycle time of polymer compositions subjected to a rotomolding process is improved (i.e., reduced), while the processing window is simultaneously enlarged through the use of a polymer-stabilizing amount of a processing stabilizer system having at least one chroman-based compound according to Formula V:
1. A process for producing a stabilized polymeric hollow article in a rotational molding operation, the process comprising:
a) filling a mold with a polyolefin and 0.01 to 10% by weight of the total weight of the polyolefin of a stabilizer composition, wherein said stabilizer composition comprises:
i) vitamin E acetate;
ii) a phosphite or phosphonite compound; and
iii) at least one basic co-additive selected from calcium stearate, zinc stearate, magnesium behenate, magnesium stearate, sodium ricinoleate, or potassium palmitate;
b) rotating the mold around at least one axis while heating the mold in an oven for a time interval sufficient to achieve sintering and laydown of the polyolefin, thereby spreading the polyolefin to the walls of the mold;
c) cooling the heated mold; and
d) opening the mold to remove a resulting product in the form of a stabilized polymeric hollow article;
wherein the polyolefin comprises linear low density polyethylene (LLDPE), medium density polyethylene (MDPE), high density polyethylene (HDPE), or polypropylene; and
wherein the polyolefin, phosphite or phosphonite compound, and at least one basic co-additive, and amounts of the vitamin E acetate, phosphite or phosphonite compound, and at least one basic co-additive are selected to reach maximum mean failure energy (MFE) of the article at a shorter time interval of the rotational molding operation, to retain a higher MFE of the article over a longer heating time of the rotational molding operation, and to enlarge a processing window of the rotational molding operation to a peak internal air temperature (PIAT) of up to 452° F. with yellowness index of the article remaining substantially unchanged up to a PIAT of 452° F., even in the absence of a sterically hindered amine light stabilizer (HALS).
2. The process of claim 1 , wherein the polyolefin is linear low density polyethylene (LLDPE).
3. The process of claim 1 , wherein the phosphite or phosphonite compound is a phosphite compound.
4. The process of claim 3 , wherein the phosphite compound is selected from tris(2,4-di-tert-butylphenyl)phosphite and bis(2,4-dicumylphenyl)pentaerythritol diphosphate.
5. The process of claim 1 , wherein the at least one basic co-additive is zinc stearate.
6. The process of claim 1 , wherein 0.05% by weight of the vitamin E acetate, 0.06% by weight of the phosphite, and either 0.035% or 0.05% by weight of the zinc stearate are present based on the total weight of the polyolefin.
7. The process of claim 1 , wherein the article has a ⅛″ to ¼″ thickness.
8. The process of claim 1 , wherein the polyolefin and amounts of the vitamin E acetate, the phosphite or phosphonite compound, and the basic co-additive in the stabilizer composition are further selected to reduce a heating time of the rotational molding operation for achieving optimal cure without compromising physical and/or mechanical properties of the article.