Production of blend of polyolefin and organopolysiloxane
US-9527988-B2 · Dec 27, 2016 · US
US2016319084A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016319084-A1 |
| Application number | US-201615211747-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jul 15, 2016 |
| Priority date | Mar 15, 2013 |
| Publication date | Nov 3, 2016 |
| Grant date | — |
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Provided is a process for preparing an improved compounded product and a compounded product prepared by the described process.
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1 . A process for preparing a compounded polyamide, comprising introducing a molten polyamide feedstock directly to one or more polymer compounding devices, where the molten feedstock is prepared by a polymerization process, wherein the polymerization process is a continuous process or a batch process. 2 .- 3 . (canceled) 4 . The process according to claim 1 , wherein the molten polyamide feedstock is a molten nylon66 feedstock. 5 . The process according to claim 1 , wherein the polymer compounding device is an extruder. 6 . The process according to claim 5 , wherein the extruder is a twin-screw extruder. 7 . The process according to claim 6 , wherein the twin-screw extruder contains at least 2 vent ports. 8 . The process according to claim 6 , wherein the twin-screw extruder contains at least 3 vent ports. 9 . The process according to claim 7 , wherein the vent ports are at atmospheric pressure. 10 . The process according to claim 7 , wherein the vent ports are subjected to vacuum conditions. 11 . The process according to claim 6 , wherein the twin-screw extruder has a length to diameter ratio of the screw shaft in the range of 24:1 to 56:1. 12 . The process according to claim 6 , wherein the twin-screw extruder has a length to diameter ratio of the screw shaft in the range of 36:1 to 48:1. 13 . The process according to claim 1 , wherein only a portion of the molten feedstock is sent directly to the one or more polymer compounding devices. 14 . The process according to claim 1 , further comprising introducing one or more additives, fillers, reinforcing agents and modifiers into the one or more polymer compounding devices. 15 . The process according to claim 1 , wherein the polymer polymerization process occurs less than 50 feet from the one or more polymer compounding devices. 16 . The process according to claim 1 , wherein the compounded polyamide has a relative viscosity (RV) range between samples of less than about 3 units. 17 . The process according to claim 16 , wherein the compounded polyamide has a relative viscosity (RV) range between samples of less than about 2 units. 18 . The process according to claim 1 , wherein the compounded polyamide has a relative viscosity (RV) range between samples of less than about 1 unit. 19 .- 28 . (canceled)
using two or more parallel screws {or at least two parallel non-intermeshing screws}, e.g. twin screw extruders · CPC title
Pre-melted polymers · CPC title
Preparatory processes · CPC title
Homopolymers or copolymers of amides or imides · CPC title
with glass fibres · CPC title
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