Polyester vessel and package

Claim 2

In a polyester vessel having mouth, side wall and bottom portions formed of a polyester composed mainly of ethylene terephthalate units, the improvement wherein said polyester is a thermoplastic polyester containing (i) a catalyst residue comprising Ge or Ti in an amount smaller than 1000 ppm as the metal and (ii) a phosphoric acid type stabilizer in an amount larger than 15 ppm as P in the case of the Ge-catalyst or in an amount larger than 55 ppm as P in the case of the Ti-catalyst, the upper limit of the amount of the phosphoric acid type stabilizer being smaller than 500 ppm as P, and in the thermoplastic polyester constituting the bottom portion of the vessel, the ratio of the thermal crystallization degree (V) represented by the following formula: V=100×(Q.sub.DC -Q.sub.AC)/Q.sub.DC ( 1) wherein Q AC stands for the heat quantity of crystallization at elevation of the temperature and Q DC stands for the heat quantity of crystallization at lowering of the temperature, is lower than 90%.

Claim 3

A vessel as set forth in claim 1, wherein the ratio of the thermal crystallization ratio is lower than 85%.

Claim 4

A vessel as set forth in claim 1, wherein the ratio of the thermal crystallization degree is lower than 50%.

Claim 5

A vessel as set forth in claim 1, wherein the amount of the catalyst residue is smaller than 900 ppm as the metal.

Claim 6

A vessel as set forth in claim 1, wherein the polyester is a polyester composed mainly of ethylene terephthalate units, which has an intrinsic viscosity (IV) of 0.55 to 1.40 dl/g and a diethylene glycol unit content of 0.01 to 5.0% by weight.

Claim 7

A vessel as set forth in claim 1, wherein at least the side wall portion of the vessel is molecularly oriented in both the axial direction of the vessel and the circumferential direction of the vessel.

Claim 8

In a polyester package comprising a polyester vessel having mouth, side wall and bottom portions formed of a thermoplastic polyester composed mainly of ethylene terephthalate units and an edible oil filled and sealed in the polyester vessel, the improvement wherein said polyester is a thermoplastic polyester containing (i) a catalyst residue comprising Ge or Ti in an amount smaller than 1000 ppm as the metal and (ii) a phosphoric acid type stabilizer in an amount larger than 15 ppm as P in the case of the Ge-catalyst or in an amount larger than 55 ppm as P in the case of the Ti-catalyst, the upper limit of the amount of the phosphoric acid type stabilizer being smaller than 500 ppm as P, and in the thermoplastic polyester constituting the bottom portion of the vessel, the ratio of the thermal crystallization degree (V) represented by the following formula: V=100×(Q.sub.DC -Q.sub.AC)/Q.sub.DC ( 1) wherein Q AC stands for the heat quantity of crystallization at elevation of the temperature and Q DC stands for the heat quantity of crystallization at lowering of the temperature, is lower than 90%.

Claim 9

In a polyester package comprising a polyester vessel having mouth, side wall and bottom portions formed of a thermoplastic polyester composed mainly of ethylene terephthalate units and an edible oil filled and sealed in the polyester vessel, the improvement wherein said polyester is a thermoplastic polyester containing (i) a catalyst residue comprising Ge or Ti in an amount smaller than 1000 ppm as the metal and (ii) a phosphoric acid type stabilizer in an amount larger than 15 ppm as P in the case of the Ge-catalyst or in an amount larger than 55 ppm as P in the case of the Ti-catalyst, the upper limit of the amount of the phosphoric acid type stabilizer being smaller than 500 ppm as P, and in the thermoplastic polyester constituting the bottom portion of the vessel, the ratio of the thermal crystallization degree (V) represented by the following formula: V=100×(Q.sub.DC -Q.sub.AC)/Q.sub.DC ( 1) wherein Q AC stands for the heat quantity of crystallization at elevation of the temperature and Q DC stands for the heat quantity of crystallization at lowering of the temperature, is lower than 90%.

Claim 10

A vessel as set forth in claim 5, wherein the polyester has an intrinsic viscosity (IV) of 0.65 to 1.25 dl/g and a diethylene glycol unit content of 0.05 to 3.5% by weight.

Claim 11

A vessel as set forth in claim 6, wherein the draw ratio in the axial direction of the vessel is 1.1 to 3.0 and the draw ratio in the circumferential direction of the vessel is 3.0 to 5.0.

Claim 12

In a polyester vessel having mouth, side wall and bottom portions formed of a polyester composed mainly of ethylene terephthalate units, the improvement wherein said polyester is a thermoplastic polyester containing (i) a catalyst residue comprising Ge, Ti or Sb in an amount smaller than 1000 ppm as the metal and (ii) a phosphoric acid type stabilizer in an amount larger than 15 ppm as P in case of the Ge-catalyst, in an amount larger than 55 ppm as P in the case of the Ti-catalyst, or in an amount larger than 95 ppm as P in the case of the Sb-catalyst, the upper limit of the amount of the phosphoric acid type stabilizer being smaller than 500 ppm as P; in the thermoplastic polyester constituting the bottom portion of the vessel, the ratio of the thermal crystallization degree (V) represented by the following formula: V=100×(Q.sub.DC -Q.sub.AC)/Q.sub.DC ( 1) wherein Q AC stands for the heat quantity of crystallization at elevation of the temperature and Q DC stands for the heat quantity of crystallization at lowering of the temperature, is lower than 90%; and the bottom portion has a higher concentration of the phosphoric acid type stabilizer than the phosphoric acid type stabilizer concentration in the side wall portion.

Claim 13

In a polyester vessel having mouth, side wall and bottom portions formed of a polyester composed mainly of ethylene terephthalate units, the improvement wherein said polyester is a thermoplastic polyester containing (i) a catalyst residue comprising Ge, Ti or Sb in an amount smaller than 1000 ppm as the metal and (ii) a phosphoric acid type stabilizer in an amount larger than 15 ppm as P in case of the Ge-catalyst, in an amount larger than 55 ppm as P in the case of the Ti-catalyst, or in an amount larger than 95 ppm as P in the case of the Sb-catalyst, the upper limit of the amount of the phosphoric acid type stabilizer being smaller than 500 ppm as P; in the thermoplastic polyester constituting the bottom portion of the vessel, the ratio of the thermal crystallization degree (V) represented by the following formula: V=100×(Q.sub.DC -Q.sub.AC)/Q.sub.DC ( 1) wherein Q AC stands for the heat quantity of crystallization at elevation of the temperature and Q DC stands for the heat quantity of crystallization at lowering of the temperature, is lower than 90%; and the bottom portion has a higher concentration of the phosphoric acid type stabilizer than the phosphoric acid type stabilizer concentration in the side wall portion.