PROCESS FOR CRYSTALLIZING POLYETHYLENE NAPHTHALATE

Abstract: Polyethylene naphthalate pellets coated with an alkylene carbonate such as ethylene carbonate or propylene carbonate crystallize more quickly and at lower temperature than uncoated pellets, reducing the tendency of the pellets to stick together during the crystallization process prior to solid-state polymerization.

Description: PROCESS FOR CRYSTALLIZING POLYETHYLENE NAPHTHALATE Polyethylene naphthalate (PEN) is a polyester useful in film, fiber and packaging applications. High molecular weight PEN is produced in a two-step process involving (a) melt polymerization to a relatively low molecular weight, amorphous polymer and (b) solid-state polymerization of this polymer to a high molecular weight polyester. The amorphous polymer is generally formed into the shape of pellets or chips for favorable solid-state reaction rates. It is desirable to convert the amorphous PEN polymer to the crystalline state prior to solid-state polymerization, because the sticking temperature of the crystalline polymer is higher than that of the amorphous polymer, and use of the crystalline material will thus reduce the tendency of the pellets to stick together as a solid mass during solid-state polymerization. The crystallization process involves heating the amorphous PEN polymer to its crystallization temperature (about 180-200°C) . As the temperature is raised, however, the polymer passes through its sticking temperature (about 140°C) . In comparison with other polyesters such as polyethylene terephthalate, PEN pellets crystallize rather slowly, and clumping of the pellets will often occur before the crystallization process is complete. It has now been discovered that coating with an alkylene carbonate, such as ethylene carbonate or propylene carbonate, causes PEN pellets to crystallize more rapidly and at a lower temperature, reducing the tendency of the pellets to stick together during the crystallization process. Accordingly, the present invention provides a process for crystallizing an amorphous naphthalate-based aromatic polyester which comprises mixing pellets of said polyester with an alkylene carbonate; and heating the mixture of alkylene carbonate and polyester pellets to a temperature of at least 80°C. The invention process is designed for treatment of naphthalate-based aromatic polyesters, by which is meant polyesters having aromatic groups in the polymer chain at least a portion of which are naphthalate units. The invention process is particularly suitable for two classes of polyethylene naphthalates: those having 75 or more mole percent naphthalate units and those having 25 or less mole percent naphthalate units, based on total aromatic units in the polyester. PEN polyesters can be prepared by condensation polymerization of the esterification reaction product of one or more aromatic dicarboxylic acids, at least one of which is a naphthalate-based acid such as 2, 6-naphthalene dicarboxylic acid, and an alkylene diol such as ethylene glycol. Alternatively, the polymerization starting material can be prepared by the transesterification reaction of a naphthalate-based ester such as 2,6-dimethyl naphthalate and an alkylene diol, catalyzed with a suitable catalyst such as manganese acetate. PEN copolyesters can be prepared by including other acids and/or diols in the polymerization mixture, such as an alkylene diol such as 1, 3-propylene diol, 1,4-butylene diol, diethylene glycol and the like, and an aromatic acid (or alkyl ester thereof) such as terephthalic acid or isophthalic acid. The currently preferred PEN's are polyethylene naphthalate homopolyesters and polyethylene naphthalate/terephthalate copolyesters. As used herein, "polyethylene naphthalates" (or "PEN") refers to polyesters and copolyesters which have aromatic units which include, but are not necessarily limited to, naphthalate groups and alkylene groups which include, but are not necessarily limited to, ethylene groups. The amorphous, relatively low molecular weight polymer (referred to herein as the "feed polymer" to solid-state polymerization) can be prepared under condensation polymerization conditions, generally in the presence of a polycondensation catalyst such as antimony trioxide or an organotitanate, at an elevated temperature and in a reduced pressure environment. The reaction is generally carried out to the point at which the reaction product can be easily pelletized, and then the reaction product is extruded in the desired pellet, cube, chip or other small particle form, which will be collectively referred to herein as "pellets." The feed polymer pellets are then mixed with an alkylene carbonate such as, for example, ethylene carbonate or propylene carbonate. Preferably, the mixing conditions are such that the alkylene carbonate is distributed on the surface of the pellets. Although a uniform coating of the alkylene carbonate on the pellet surfaces is not required, it is desirable that mixing is accomplished so as to distribute the alkylene carbonate on the surface of essentially all the pellets. The alkylene carbonate will normally be present on the pellets in an amount effective to reduce the crystallization temperature of the polyester, generally within the range of 0.1 to 10, preferably 0.5 to 3, weight percent, based on the weight of the polyester. The alkylene carbonate can be applied, for example, by placing the pellets in an aqueous solution of the alkylene carbonate and then removing the water by, for example, flash evaporation; by spraying the alkylene carbonate on the pellets; or by stirring a mixture of the pellets and solid alkylene carbonate. The preferred technique is to introduce the alkylene carbonate as an aqueous solution into the solid-state polymerization vessel, add the amorphous PEN feed polymer pellets, and blend the mixture while evaporating off the water. This process can be carried out prior to or simultaneously with devolatilization of the PEN polymer under reduced pressure and/or inert gas flow at an elevated temperature lower than the polymer crystallization temperature. Crystallization of the feed polymer is carried out by heating the coated chips, preferably with stirring, to the crystallization temperature of the particular PEN, generally a temperature within the range of 80 to 180°C, preferably 120 to 170°C. In order to accomplish the objective of reducing the tendency of the pellets to stick together, it is generally sufficient for crystallization to occur at the pellet surface, characterized by haziness of the surface of the pellets. The presence of the alkylene carbonate generally reduces the time required for crystallization of the PEN polyester, so that crystallization can usually be accomplished within 20 to 60 minutes. Solid-state polymerization is carried out by heating the crystalline pellets in a suitable solid-state reactor to a temperature greater than 210°C under reduced pressure and/or inert gas flow for a period which can vary widely depending upon the particular polymer but will generally be greater than 7 hours, often greater than 20 hours for PEN copolyesters, to achieve an intrinsic viscosity greater than that of the feed polymer, e.g., greater than about 0.5 dl/g for high-naphthalate polyesters and greater than about 0.6 for low-naphthalate copolyesters. In general, the crystallization process of this invention will not affect solid-stating conditions or the properties of the final polyester. The solid-stated polyester can be used in a wide variety of applications, including molded bottles and trays. Example 1_ This experiment illustrates the effect of coating PEN polyester pellets with ethylene carbonate and subjecting the pellets to crystallization conditions. lOg of polyethylene terephthalate/naphthalate (10/90 T/N) pellets were coated with ethylene carbonate by mixing the PET/PEN with 0.15g of ethylene carbonate in 0.85g of water and boiling off the water. The coated pellets were introduced into a glass reactor heated to 141°C and the pellets were stirred slowly. After five minutes, the pellets turned hazy, indicating crystallization. No sticking was observed. In a control experiment, uncoated pellets of PET/PEN were stirred slowly at 141°C. The pellets had not crystallized after 5 minutes, and there was noticeable sticking together of the pellets. Example 2_ lOg of PET/PEN (10/90 T/N) pellets were coated with propylene carbonate by mixing the pellets with O.lg of propylene carbonate in 0.4g of water and boiling off the water. The coated pellets were introduced into a glass reactor and were stirred slowly at 150°C. After 5 minutes, the pellets turned hazy, indicating crystallization. The pellets were not sticking together. In a control experiment, uncoated pellets of PET/PEN were stirred slowly at 150°C. The pellets had not crystallized after 5 minutes, and there was noticeable sticking together of the pellets. Example _3 This experiment demonstrates solid-state polymerization of coated and uncoated pellets of PEN. A solid-state polymerization was run in an 85 litre blender using pelletized PET/PEN (10/90 T/N) feed polymer. 225g of ethylene carbonate as an aqueous solution were charged to the blender, after which the feed polymer was charged. The feed polymer was devolatilized for 2 hours at 120°C and then crystallized at 165°C for 1 hour. The temperature of the blender was raised to 230°C and held for 30 hours for solid-state polymerization. In a control experiment, 22.7kg of PET/PEN (10/90 T/N) were charged to the blender with no ethylene carbonate. After devolatilization for 2 hours at 120°C and crystallization at 165°C for 1 hour, it was necessary to continue for another 1.5 hour at 190°C to complete crystallization. The polymer was then solid-stated for 30 hours at 230°C. Polymerization rates were similar for the two polyesters, but there was very heavy sticking in the control . Example 4_ This experiment demonstrates crystallization of PET/PEN pellets coated with ethylene carbonate. 33g of PET/PEN (10/90 T/N) pellets were coated with 0.17g of ethylene carbonate by mixing in a rotary flask of an evaporator/blender. The flask was immersed in a hot oil bath at 165°C. After 25 minutes, the pellets were signif cantly crystallized and there was little sticking. The same experiment was carried out using uncoated PET/PEN pellets. Under the same conditions, there was less crystaliinity and heavy sticking of the pellets. Example 5_ This experiment demonstrates crystallization of PET/PEN pellets coated with propylene carbonate. 34g of PET/PEN (10/90 T/N) pellets were coated with 0.17g of propylene carbonate by mixing in a rotary flask. The flask was immersed in a hot oil bath at 150°C. After 30 minutes, there was some crystallization and little sticking. The same experiment was carried out using uncoated PET/PEN pellets. There was little crystallization and considerable sticking of the pellets. Example _6 This experiment demonstrates crystallization of PET/PEN pellets coated with ethylene carbonate, in which the PET/PEN contains a relatively small molar quantity of naphthalate units. 30g of PET/PEN (90/10 T/N) pellets were coated with 0.3g of ethylene carbonate by mixing in a -rotary flask of an evaporator/blender. The flask was immersed in a hot oil bath at 125°C. After 15 minutes, the pellets were significantly crystallized and there was little sticking. The same experiment was carried out using uncoated PET/PEN pellets. Under the same conditions, there was less crystaliinity and heavy sticking of the pellets.

Claims: C L A I M S 1. A process for crystallizing an amorphous naphthalate- based aromatic polyester which comprises mixing pellets of said polyester with an alkylene carbonate; and heating the mixture of alkylene carbonate and polyester pellets to a temperature of at least 80°C. 2. A process as claimed in claim 1 in which the alkylene carbonate is present in an amount within the range of 0.1 to 10 weight percent, based on the weight of the polyester. 3. A process as claimed in claim 2 in which the alkylene carbonate is present in an amount within the range of 0.5 to 3 weight percent, based on the weight of the polyester. 4. A process as claimed in claim 1, 2 or 3 in which the alkylene carbonate is ethylene carbonate or propylene * carbonate. 5. A process as claimed in claim 1, 2, 3 or 4 in which the mixture of alkylene carbonate and polyester pellets is heated to a temperature between 120 to 170°C for between 20 to 60 minutes. 6. A process as claimed in any one of the preceding claims in which the aromatic polyester comprises at least 75 mole percent naphthalate units, based on moles of aromatic units. 7. A process as claimed in any one of claims 1-5 in which the aromatic polyester comprises an amount of naphthalate units, based on moles of aromatic units, within the range of 1 to 25 percent. 8. Naphthalate-based aromatic polyester pellets in which at least the outer part is crystalline, when prepared by a process as claimed in any one of the preceding claims. 9. Process for preparing a high molecular weight naphthalate-based aromatic polyester, which comprises heating at least partially crystalline pellets as claimed in claim 8 to a temperature between 210 and 265°C. 10. High molecular weight naphthalate-based aromatic polyester prepared by a process as claimed in claim 9.

Inventors: MOATS SAMUEL MARTIN, PESATA PATRICK JOSEPH, TUNG WILLIAM CHUNG TSING, MOATS, SAMUEL, MARTIN, PESATA, PATRICK, JOSEPH, TUNG, WILLIAM, CHUNG, TSING
Applicants: SHELL CANADA LTD, SHELL INT RESEARCH, SHELL CANADA LIMITED, SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.
Application year: 1996
Main classification: C08G63
IPC codes: C08F2, C08G63, C08L67