Direct fabrication

Claim 2

A process for the direct fabrication of an article of pre-determined shape from incompatible resins comprising: a) combining particles of a first thermoplastic resin with particles of a second thermoplastic resin which is incompatible with said first resin, this incompatibility being characterized by a difference of at least 2 (J/cm 3 ) 1/2 between the solubility parameters of the first and second resins, said particles having at least one dimension of at least 2 mm, said first resin being present in a major proportion and said second resin being present in a minor proportion, b) melting this combination of particles while mixing them together, c) periodically shearing the resultant melt without degrading the resins therein to disperse the melt of the second resin within the melt of the first resin, the shear rate of this periodic shearing step being at least 300 sec -1 and the shear rate and shear time being effective to result in a number average particle size of the second resin in articles fabricated from the result sheared melt of less than about 1 micron, d) directly injection molding or extrusion blow molding an amount of the resultant sheared melt into a pre-determined shape and obtaining as a result thereof said article of said pre-determined shape directly fabricated from said combined particles.

Claim 3

A process for direct fabrication of an article from incompatible thermoplastic resins, comprising a) feeding particles of a first thermoplastic resin into a molding machine, b) feeding particles of a second thermoplastic resin to said machine simultaneously with the feed of the first resin to said machine thereby obtaining a combination of particles, said second resin being incompatible with the first resin, this incompatibility being characterized by a difference of at least 2 (J/cm 3 ) 1/2 between the solubility parameters of the first and second resins, said particles of resin having at least one dimension which is at least 2 mm, a major proportion of said particles being of said second resin, c) melting the resultant combination of particles while mixing them together within said machine, d) shearing the resultant melt at a shear rate of at least 300 sec -1 within said machine to disperse the melt of the second resin into the melt of the first resin, the melting and shearing steps being carried out by periodic rotation of a plasticating screw within a barrel operating on the resin feeds to the machine, the fine dispersion provided by the periodic rotation of the screw being characterized by a number average particle size of said second resin in the article fabricated from the sheared melt being less than about 1 micron, and e) either (I) forcing an amount of the resultant sheared melt into a pre-determined shape by the rotation of said screw to inject the sheared melt into a mold cavity of the machine, the amount of shear of the resultant melt during rotation of the screw being effective to finely disperse the second resin within the first resin, or (II) the rotation of said screw occurring during rotation of the screw within the barrel to fill the forward end of the barrel with the sheared melt, (i) retarding the retraction of the screw within the barrel so as to extend the shearing time without degrading said first and second resins, the combination of shear and extended shearing time being effective to finely disperse the second resin within the first resin, (ii) ramming the plasticating screw against the sheared melt filling the forward end of the barrel to inject the sheared melt into a mold cavity of the machine, and f) obtaining as a result thereof a directly fabricated article.

Claim 4

A process for direct fabrication of an article from incompatible thermoplastic resins, comprising a) feeding particles of a first thermoplastic resin into a molding machine, b) feeding particles of a second thermoplastic resin to said machine simultaneously with the feed of the first resin to said machine thereby obtaining a combination of particles, said second resin being incompatible with the first resin, this incompatibility being characterized by a difference of at least 2 (J/cm 3 ) 1/2 between the solubility parameters of the first and second resins, said particles of resin having at least one dimension which is at least 2 mm, a major proportion of said particles being of said second resin, c) melting the resultant combination of particles while mixing them together within said machine, d) shearing the resultant melt at a shear rate of at least 300 sec -1 within said machine to disperse the melt of the second resin into the melt of the first resin, the melting and shearing steps being carried out by periodic rotation of a plasticating screw within a barrel operating on the resin feeds to the machine, the fine dispersion provided by the periodic rotation of the screw being characterized by a number average particle size of said second resin in the article fabricated from the sheared melt being less than about 1 micron, and e) either (I) forcing an amount of the resultant sheared melt into a pre-determined shape by the rotation of said screw to inject the sheared melt into a mold cavity of the machine, the amount of shear of the resultant melt during rotation of the screw being effective to finely disperse the second resin within the first resin, or (II) the rotation of said screw occurring during rotation of the screw within the barrel to fill the forward end of the barrel with the sheared melt, (i) retarding the retraction of the screw within the barrel so as to extend the shearing time without degrading said first and second resins, the combination of shear and extended shearing time being effective to finely disperse the second resin within the first resin, (ii) ramming the plasticating screw against the sheared melt filling the forward end of the barrel to inject the sheared melt into a mold cavity of the machine, and f) obtaining as a result thereof a directly fabricated article.

Claim 5

The process of claim 2 wherein the shearing time is at least 15% of the total molding cycle time.

Claim 6

The process of claim 2 wherein retardation of the retraction of the screw is accomplished by applying a back pressure of at lest 1.5 MPa to said screw.

Claim 7

A process for the direct fabrication of an article of pre-determined shape from incompatible resins comprising: a) combining particles of a first thermoplastic resin selected from the group consisting of polyester and polyamide resin with particles of a second thermoplastic resin which is an elastomer and is incompatible with said first resin, said particles having at least one dimension of at least 2 mm, said first resin being present in a major proportion and said second resin being present in a minor proportion, b) melting this combination of particles while mixing them together, c) periodically shearing the resultant melt at a shear rate of at least 300 sec -1 to disperse the melt of the second resin within the melt of the first resin, the shear rate and shear time of this periodic shearing step being effective to result in a number particle size of the second resin in articles fabricated from the resultant sheared melt of less than about 1 micron, d) directly injection molding or extrusion blow molding an amount of the resultant sheared melt into a pre-determined shape and obtaining as a result thereof said article of said pre-determined shape directly fabricated from the combination of particles.

Claim 8

A process for the direct fabrication of an article of pre-determined shape from incompatible resins comprising: a) combining particles of a first thermoplastic resin selected from the group consisting of polyester and polyamide resin with particles of a second thermoplastic resin which is an elastomer and is incompatible with said first resin, said particles having at least one dimension of at least 2 mm, said first resin being present in a major proportion and said second resin being present in a minor proportion, b) melting this combination of particles while mixing them together, c) periodically shearing the resultant melt at a shear rate of at least 300 sec -1 to disperse the melt of the second resin within the melt of the first resin, the shear rate and shear time of this periodic shearing step being effective to result in a number particle size of the second resin in articles fabricated from the resultant sheared melt of less than about 1 micron, d) directly injection molding or extrusion blow molding an amount of the resultant sheared melt into a pre-determined shape and obtaining as a result thereof said article of said pre-determined shape directly fabricated from the combination of particles.

Claim 9

The process of claim 5 wherein the elastomer is selected from the group consisting of ethylene copolymer, styrene copolymer, and block copolyetherester.

Claim 10

The process of claim 5 wherein the impact strength of said articles is at least 300 J/m.

Claim 11

The process of claim 5 wherein the resin is recycle polyester resin flake.

Claim 12

The process of claim 8 wherein the shear rate is at least about 900 sec -1 .

Claim 13

The process of claim 8 wherein the proportions of said flake and said elastomer are about 80 to 90 wt. % and 10 to 20 wt. %, respectively.

Claim 14

A process for the direct fabrication of an article from a major proportion of polyester resin and minor proportion of ethylene/epoxide copolymer elastomer, said copolymer elastomer in combination with said polyester resin in said article providing substantial toughening of said article comprising: a) combining particles of said polyester resin with particles of said copolymer eslastomer, said particles having at least one dimension of at least 2 mm, b) melting this combination of particles while mixing them together, c) periodically shearing the resultant melt at a shear rate of at least 300 sec -1 to finely disperse the melt of the copolymer elastomer within the melt of the polyester resin, and the shear rate and shear time being effective to result in a number average particle size of the copolymer elastomer in article fabricated from the resultant sheared melt of less than 1 micron, and said shearing being carried out in the presence of an effective amount of adjuvant for said toughening of said article said adjuvant having been incorporated into said melt, and d) directly injection molding or extrusion blow molding an amount of the resultant sheared melt into a pre-determined shape and obtaining as a result thereof said substantially toughened article of said pre-determined shape directly fabricated from said combined particles.

Claim 15

A process for the direct fabrication of an article from a major proportion of polyester resin and minor proportion of ethylene/epoxide copolymer elastomer, said copolymer elastomer in combination with said polyester resin in said article providing substantial toughening of said article comprising: a) combining particles of said polyester resin with particles of said copolymer eslastomer, said particles having at least one dimension of at least 2 mm, b) melting this combination of particles while mixing them together, c) periodically shearing the resultant melt at a shear rate of at least 300 sec -1 to finely disperse the melt of the copolymer elastomer within the melt of the polyester resin, and the shear rate and shear time being effective to result in a number average particle size of the copolymer elastomer in article fabricated from the resultant sheared melt of less than 1 micron, and said shearing being carried out in the presence of an effective amount of adjuvant for said toughening of said article said adjuvant having been incorporated into said melt, and d) directly injection molding or extrusion blow molding an amount of the resultant sheared melt into a pre-determined shape and obtaining as a result thereof said substantially toughened article of said pre-determined shape directly fabricated from said combined particles.

Claim 16

The process of claim 11 wherein said polyester resin is recycle flake.

Claim 17

The process of claim 1 wherein the epoxide of said copolymer elastomer is present as glycidyl(meth)acrylate.

Claim 18

The process of claim 11 wherein the amount of said adjuvant is 0.05 to 2.0 wt. % based on the weight of said polyester resin plus said copolymer elastomer.

Claim 19

The process of claim 11 wherein said adjuvant is at least one compound selected from the group consisting of zinc complexes, zinc salts of fatty acids having from 8 to 28 carbon atoms, Zn carbonate, Zn salicylate, tin stearate, copper stearate, and cerium stearate.

Claim 20

The process of claim 15 wherein said adjuvant is zinc stearate.