Apparatus and method for molding of polyester articles directly from a melt

Claim 3

The apparatus of claim 1 wherein the pumping means comprises a gear pump mounted at the outlet of the barrel.

Claim 4

The apparatus of claim 1 further comprising a flow control valve positioned between the pumping means and each molding device.

Claim 5

The apparatus of claim 1 comprising a plurality of molding devices in polymer flow communication with the pumping means for continuously receiving molten polymer from the pumping means and forming molded articles from the polymer.

Claim 6

The apparatus of claim 1 wherein each molding device comprises a mold; an accumulator reservoir for receiving molten polymer from the pumping means; and a ram for injecting molten polymer from the accumulator reservoir to the mold.

Claim 7

The apparatus of claim 5 further comprising a flow control valve positioned between the accumulator reservoir and the mold.

Claim 8

The apparatus of claim 1 comprising a plurality of molding devices in polymer flow communication with the pumping means for continuously receiving molten polymer from the pumping means and forming molded articles from the polymer, wherein the pumping means comprises a gear pump mounted at the outlet of the barrel; a plurality of flow control valves, one flow control valve positioned between the pumping means and each molding device; wherein each molding device comprises a mold, an accumulator reservoir for receiving molten polymer from the pumping means, a ram for injecting molten polymer from the accumulator reservoir to the mold; and a flow control valve positioned between the accumulator reservoir and the mold.

Claim 9

A process for the continuous production of molded polyester articles which comprises: a) reacting polyester homopolymer or copolymer precursors in a reactor under conditions sufficient to produce a stream of molten polyester homopolymer or copolymer; b) mixing the stream of molten polyester with a stream of a gas which is substantially inert to the polyester under a pressure of from about 1000 to about 3000 psig to thereby form a mixture; c) reducing the pressure of the mixure to subatmospheric pressure thereby causing the mixture to foam, and thereafter separating the gas in the mixture from the polyester by means of a vacuum; d) blending the degassed polyester with an acetaldehyde reducing agent to form a blend; e) forming a solid molded article from the blend without solidifying the polyester prior to forming the solid molded article.

Claim 10

A process for the continuous production of molded polyester articles which comprises: a) reacting polyester homopolymer or copolymer precursors in a reactor under conditions sufficient to produce a stream of molten polyester homopolymer or copolymer; b) mixing the stream of molten polyester with a stream of a gas which is substantially inert to the polyester under a pressure of from about 1000 to about 3000 psig to thereby form a mixture; c) reducing the pressure of the mixure to subatmospheric pressure thereby causing the mixture to foam, and thereafter separating the gas in the mixture from the polyester by means of a vacuum; d) blending the degassed polyester with an acetaldehyde reducing agent to form a blend; e) forming a solid molded article from the blend without solidifying the polyester prior to forming the solid molded article.

Claim 11

A process for the continuous production of molded polyester articles which comprises: A) reacting polyester homopolymer or copolymer precursors in a reactor under conditions sufficient to produce a stream of molten polyester homopolymer or copolymer; B) providing an extruder, said extruder comprising a) a cylindrical barrel having a plurality of serially connected zones along the interior of the barrel; at least one screw shaft along the interior of the barrel through said zones; and means for turning the shaft; b) a molten thermoplastic polymer inlet and a gas injection port at a first mixing zone of the barrel; said first mixing zone having means for mixing a molten thermoplastic polymer and a gas therein under a pressure of from about 1000 to about 3000 psig to thereby form a mixture; c) means for causing a flow of the mixture through a pressure reduction zone to a degassing zone; d) a degassing zone capable of being maintained at subatmospheric pressure and having a vacuum gas vent capable of removing gas from the polymer and conveying degassed polymer to a second mixing zone; e) a second mixing zone having an inlet port, capable of mixing and conveying the polymer to an outlet of the barrel; f) pumping means at the outlet of the barrel for pumping the polymer to a molding device; C) continuously flowing the stream of molten polyester into the first mixing zone of the extruder without solidifying the polyester prior to entry into the extruder and mixing the stream of molten polyester with an injected stream of a gas which is substantially inert to the polyester to thereby form a mixture under a pressure of from about 1000 to about 3000 psig; D) flowing the mixture through a pressure reduction zone to a degassing zone; E) degassing the mixture in the degassing zone which is maintained at subatmospheric pressure and removing the gas from the polymer by means of vacuum gas vent; F) mixing the degassed polymer with an acetaldehyde reducing agent in a second mixing zone; G) conveying the polymer to an outlet of the barrel and pumping the polymer out of the barrel to a molding device; and H) continuously forming molded articles from the polymer.

Claim 12

A process for the continuous production of molded polyester articles which comprises: A) reacting polyester homopolymer or copolymer precursors in a reactor under conditions sufficient to produce a stream of molten polyester homopolymer or copolymer; B) providing an extruder, said extruder comprising a) a cylindrical barrel having a plurality of serially connected zones along the interior of the barrel; at least one screw shaft along the interior of the barrel through said zones; and means for turning the shaft; b) a molten thermoplastic polymer inlet and a gas injection port at a first mixing zone of the barrel; said first mixing zone having means for mixing a molten thermoplastic polymer and a gas therein under a pressure of from about 1000 to about 3000 psig to thereby form a mixture; c) means for causing a flow of the mixture through a pressure reduction zone to a degassing zone; d) a degassing zone capable of being maintained at subatmospheric pressure and having a vacuum gas vent capable of removing gas from the polymer and conveying degassed polymer to a second mixing zone; e) a second mixing zone having an inlet port, capable of mixing and conveying the polymer to an outlet of the barrel; f) pumping means at the outlet of the barrel for pumping the polymer to a molding device; C) continuously flowing the stream of molten polyester into the first mixing zone of the extruder without solidifying the polyester prior to entry into the extruder and mixing the stream of molten polyester with an injected stream of a gas which is substantially inert to the polyester to thereby form a mixture under a pressure of from about 1000 to about 3000 psig; D) flowing the mixture through a pressure reduction zone to a degassing zone; E) degassing the mixture in the degassing zone which is maintained at subatmospheric pressure and removing the gas from the polymer by means of vacuum gas vent; F) mixing the degassed polymer with an acetaldehyde reducing agent in a second mixing zone; G) conveying the polymer to an outlet of the barrel and pumping the polymer out of the barrel to a molding device; and H) continuously forming molded articles from the polymer.

Claim 13

The process of claim 9 wherein the pumping means comprises a gear pump mounted at the outlet of the barrel.

Claim 14

The process of claim 9 further comprising a flow control valve positioned between the pumping means and each molding device.

Claim 15

The process of claim 9 comprising a plurality of molding devices in polymer flow communication with the pumping means for continuously receiving molten polymer from the pumping means and forming molded articles from the polymer.

Claim 16

The process of claim 9 wherein each molding device comprises a mold; an accumulator reservoir for receiving molten polymer from the pumping means; and a ram for injecting molten polymer from the accumulator reservoir to the mold.

Claim 17

The process of claim 13 further comprising a flow control valve positioned between the accumulator reservoir and the mold.

Claim 18

The process of claim 9 comprising a plurality of molding devices in polymer flow communication with the pumping means for continuously receiving molten polymer from the pumping means and forming molded articles from the polymer, wherein the pumping means comprises a gear pump mounted at the outlet of the barrel; a plurality of flow control valves, one flow control valve positioned between the pumping means and each molding device; wherein each molding device comprises a mold, an accumulator reservoir for receiving molten polymer from the pumping means, a ram for injecting molten polymer from the accumulator reservoir to the mold; and a flow control valve positioned between the accumulator reservoir and the mold.

Claim 19

The process of claim 9 wherein the reduced pressure of step (E) is less than about 100 mmHg.

Claim 20

The process of claim 9 wherein the degassed polymer resulting from step (E) is substantially free of the inert gas and acetaldehyde.

Claim 21

The process of claim 9 wherein the acetaldehyde reducing agent is selected from the group consisting of polyamides; polyesteramides; ethylenediaminetetraacetic acid alkoxylated polyols, bis(4-β-hydroxyethoxyphenyl)sulfone, zeolite compounds, 5-hydroxyisophthalic acid, poly(ethylene isophthalate), supercritical carbon dioxide and protonic acid catalysts.

Claim 22

The process of claim 15 wherein molded articles are formed by conveying the polymer sequentially to each molding device one at a time while polymer is shutoff by the flow control valves to other molding devices.

Claim 23

The process of claim 9 wherein the molten polyester is maintained at a temperature that is no more than about 20° C. above the melting point of the polyester.

Claim 24

The process of claim 9 wherein the formed molding articles have an acetaldehyde concentration of no more than about 5 ppm based on the weight of the article.