초록 ▼

The invention relates to a method of preparing a thermoplastic vulcanizate comprising: a) melt processing a blend of thermoplastic polymer and vulcanizable elastomer in a multi-screw extruder having at least three intermeshing screws, wherein said screws have 3-170 mixing zones, and said extruder ha

The invention relates to a method of preparing a thermoplastic vulcanizate comprising: a) melt processing a blend of thermoplastic polymer and vulcanizable elastomer in a multi-screw extruder having at least three intermeshing screws, wherein said screws have 3-170 mixing zones, and said extruder having a L/D ratio of 15-100, and a screw profile that has 3 to 17 meshes per L/D; b) adding at least one curing agent to the melt-processed blend of a) in at least one location in the first 46% of the length of said extruder, or adding at least one curing agent to the melt-processed blend of a) in a second extruder, so as to initiate curing of the blend: and, curing at least partially said elastomer by reactive melt processing. Improved processing, reaction kinetics and efficiencies are achieved, as well as thermoplastic vulcanizate products having decreased weight gain when placed in mineral oils.

대표청구항 ▼

What is claimed is: 1. A method for preparing a thermoplastic vulcanizate within a ring extruder having a length and a diameter defined by a length to diameter ratio of 15-100, the extruder including at least three screws having a length and including intermeshing elements disposed along the length

What is claimed is: 1. A method for preparing a thermoplastic vulcanizate within a ring extruder having a length and a diameter defined by a length to diameter ratio of 15-100, the extruder including at least three screws having a length and including intermeshing elements disposed along the length to achieve a screw profile that has 3 to 17 meshes per unit of length to diameter of the extruder, and where the extruder includes at least two screws including blocking elements disposed in the first ¼ portion of the length of the extruder defined from the feed throat of the extruder to prevent cross-over of material and thereby create at least two mixing portions within the first ¼ portion of the extruder, the method comprising: i. charging thermoplastic polymer to the extruder; ii. charging vulcanizable polymer to the extruder; iii. charging curative for the vulcanizable polymer to the extruder; iv. melt mixing the thermoplastic polymer and curative within a first mixing portion of the first ¼ portion of the length of the extruder; v. masticating the vulcanizable polymer within a second mixing portion of the first ¼ portion of the length of the extruder, where said step of melt mixing the thermoplastic polymer and curative and said step of masticating the vulcanizable polymer occurs simultaneously; vi. preventing the cross-over of the curative and thermoplastic polymer contained in the first mixing portion to the vulcanizable polymer contained in the second mixing portion for at least a portion of the first ¼ portion of the length of the extruder by using the blocking elements; vii. melt mixing the curative, thermoplastic polymer, and vulcanizable polymer after said step vi and viii. dynamically vulcanizing the vulcanizable polymer after said step vi to thereby form a thermoplastic vulcanizate. 2. The method of claim 1, where the screw profile has 9 to 17 meshes/L/D. 3. The method of claim 1, wherein said curing agent is a silicon-hydride containing composition with a platinum catalyst. 4. The method of claim 1 , wherein said curing agent is selected from the group consisting of phenolic resins and organic peroxide compositions and wherein said curing agent is added in the first 25% of the length of said first or second extruder. 5. The method of claim 1, where said steps of melt mixing and masticating takes place by rotating said screws at 100 to 1200 RPM and where said step of charging thermoplastic polymer and vulcanizable polymer takes place at a rate of 1.91-22.9 Kg/(Hr×cm2 free cross sectional area). 6. The method of claim 1, where said steps of melt mixing and masticating takes place by rotating said screws at 500 to 850 RPM and where said step of charging thermoplastic polymer and vulcanizable polymer takes place at a rate of 9.54- 16.22 Kg/(Hr×cm2 free cross sectional area). 7. The method of claim 1, further comprising the step of charging oil to the extruder within the first ¼ portion of the length of the extruder. 8. The method of claim 7, further comprising the step of charging oil to the extruder after said step of dynamically vulcanizing. 9. The method of claim 1, further comprising the step of charging additional thermoplastic polymer after said step of melt mixing the thermoplastic polymer and curative. 10. The method of claim 1, further comprising the step of charging additional thermoplastic polymer after said step of dynamically vulcanizing, and where the amount of thermoplastic polymer added is 2.4% to 85% of said thermoplastic vulcanizate. 11. The method of claim 10, further comprising multiple steps of charging an oil to the extruder. 12. the method of claim 11, where the oil is charged before, during, and after said step of dynamically vulcanizing. 13. The method of claim 12, where the amount of oil charged in said steps of charging oil results in an oil to thermoplastic polymer ratio in the thermoplastic vulcanizate of 160:1 to 1:20.