Process for preparing polyethylene terephthalate useful for beverage containers
AssigneeCelanese Corporation
InventorsGeorge W. Halek, William T. Freed, Jerome S. Schaul, Raymond W. Rupp, Stanley L. Pauls
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AssigneeCelanese Corporation
InventorsGeorge W. Halek, William T. Freed, Jerome S. Schaul, Raymond W. Rupp, Stanley L. Pauls
Estimating the term…
There is disclosed a process for reducing the acetaldehyde content and the generation rate of acetaldehyde of polyethylene terephthalate chip which has a crystallinity of at least about 30% in order to render the polyethylene terephthalate suitable for making containers which are useful in the carbonated beverage industry. This process comprises stabilizing the polyethylene terephthalate by heating it at an elevated temperature in air and maintaining an air to chip ratio at a predetermined value of at least about 0.8 standard cubic foot of air per minute/pound of resin per hour and at a vapor velocity of at least about 0.5 foot per second. The air used in the stabilization process has a dew point of less than about -30.degree. C. The stabilized polyethylene terephthalate produced by this process has an acetaldehyde level of less than about 2.5 parts per million, a generation rate of acetaldehyde of less than about 3.0 parts per million per minute and an intrinsic viscosity of from about 0.60 to about 0.95 deciliters per gram. There is also disclosed a process for molding a polyethylene terephthalate preform comprising melting the above described polymer, forming it into the desired preform shape, and cooling the molten polymer. This preform may then be reheated above its glass transition temperature and molded into the desired container shape.
A process for reducing the acetaldehyde content and the generation rate of acetaldehyde of polyethylene terephthalate chip which has a crystallinity of at least about 30% in order to render the polyethylene terephthalate suitable for making containers, which process comprises stabilizing said polyethylene terephthalate by heating it at a temperature of about 180.degree. to about 220.degree. C. for from about 2 to about 20 hours in a countercurrent stream of air and maintaining an air to chip ratio at a predetermined value of at least about 0.8 standard cubic foot of air per minute/pound of polyethylene terephthalate per hour and at a vapor velocity of at least about 0.5 foot per second, said air having a dew point of less than about -30.degree. C., in order to reduce the acetaldehyde level of said crystallized polyethylene terephthalate to less than about 2.5 parts per million, to reduce the generation rate of acetaldehyde to less than about 3.0 parts per million per minute, and to increase the intrinsic visocity to a value in the range of from about 0.60 to about 0.95 deciliters per gram calculated from measurements made on an 8% by weight solution in o-chlorophenol at 25.degree. C.
A continuous process for reducing the acetaldehyde content and the generation rate of acetaldehyde of polyethylene terephtalate chip which has a crystallinity of at least about 30% in order to render the polyethylene terephthalate suitable for making containers, which process comprises stabilizing said polyethylene terephthalate by moving it downward and heating it in a stabilization zone at a temperature of about 190.degree. to about 210.degree. C. for from about 6 to about 12 hours in a countercurrent stream of air and maintaining an air to chip ratio at a predetermined value of from about 1.25 to about 2.5 standard cubic feed of air per minute/pound of polyethylene terephthalate per hour and at a vapor velocity of from about 1 to about 2 feet per second, said air having a dew point of from about -40.degree. to about -80.degree. C., in order to reduce the acetaldehyde level of said crystallized polyethylene terephtalate to less than about 1.5 parts per million, to reduce the generation rate of acetaldehyde to a value of from about 2 to about 3 parts per million per minute, and to increase the intrinsic viscosity to a value in the range of from about 0.70 to about 0.80 deciliter per gram calculated from measurements made on an 8% by weight solution in o-chlorophenol at 25.degree. C.
A process for reducing the acetaldehyde content and the generation rate of acetaldehyde of polyethylene terephthalate chip which has an intrinsic viscosity of from about 0.55 to about 0.75 deciliter per gram as calculated from measurements made on an 8 percent by weight solution in o-chlorophenol at 25.degree. C. in order to render the polyethylene terephthalate suitable for making containers, which process comprises
A continuous process for reducing the acetaldehyde content and the generation rate of acetaldehyde of polyethylene terephthalate chip which has an intrinsic viscosity of from about 0.62 to about 0.68 deciliters per gram as calculated from measurements made on an 8% by weight solution in o-chlorophenol at 25.degree. C. in order to render the polyethylene terephthalate suitable for making containers, which process comprises
Dependencies are inferred from the claim text.