Process for preparing a polyolefin composition
US-2017341266-A1 · Nov 30, 2017 · US
US9908276B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9908276-B2 |
| Application number | US-201214366576-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 28, 2012 |
| Priority date | Dec 31, 2011 |
| Publication date | Mar 6, 2018 |
| Grant date | Mar 6, 2018 |
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Official abstract text for this publication.
Systems ( 200 ) and methods for making different plastic products ( 202, 204 ) in a single melting process are provided. A method includes melting a plastic resin in a first extruder ( 104 ) to form a melt ( 106 ) and transferring at least a portion of the melt to a second extruder ( 114 ). Any portion of the melt ( 106 ) that is not transferred to the second extruder ( 114 ) is formed into a first plastic product ( 202 ). Additives ( 116 ) are blended with the melt in the second extruder to form a second melt ( 118 ), and a second plastic product ( 204 ) is formed from the second melt ( 118 ).
Opening claim text (preview).
What is claimed is: 1. A system for forming different plastic products from a single melt, comprising: a main extruder system, comprising: a main extruder configured to melt a plastic resin, forming a melt; an additive system configured to feed an additive to the melt in the main extruder; a first die positioned downstream from the main extruder a second product extruder system comprising a second product extruder that is located downstream of the main extruder; a diverter valve positioned downstream from the main extruder and between the main extruder and the first die and the second product extruder, the diverter valve configured to: receive the melt from the main extruder; transfer a first portion of the melt to the first die to form a first plastic product and transfer a second portion of the melt to the second product extruder; and the second product extruder system, comprising: the second product extruder configured to blend the second portion of the melt with an additive, forming a second product melt; an additive feeder configured to feed the product additive to the second product extruder; and a second die configured to form a second plastic product from the second product melt; wherein the second product extruder has a capacity that is about 75% or less than the capacity of the main extruder. 2. The system of claim 1 , wherein the diverter valve is configured to transfer additional portions of the melt to each of a plurality of product extruders. 3. The system of claim 1 , wherein the second product extruder has a capacity that is about 50% or less than the capacity of the main extruder. 4. The system of claim 1 , wherein the second product extruder has a lower power demand than the main extruder for an equivalent amount of material. 5. The system of claim 1 , wherein the main extruder system further comprises a melt pump. 6. The system of claim 1 , wherein the second product extruder system does not comprise a melt pump. 7. The system of claim 1 , wherein the first or second die comprises a pultrusion pipe die. 8. The system of claim 1 , wherein the first or second die comprises a sheet die, a film die, or a combination sheet/film die. 9. The system of claim 1 , wherein the first or second die comprises a blown film die. 10. The system of claim 1 , wherein the additive feeder comprises a liquid injection system. 11. The system of claim 1 , wherein the additive feeder comprises a melt pump feeder. 12. The system of claim 1 , comprising a third product extruder system comprising: a third product extruder that is located downstream of the diverter valve and configured to blend a third portion of the melt with a product additive, forming a third product melt; an additive feeder configured to feed the product additive to the third product extruder; and a third die configured to form a third plastic product from the third product melt. 13. The system of claim 1 , wherein the diverter valve is coupled to a piston and an actuator to control a flow rate of the first portion of the melt from the diverter value and to control a flow rate of the second portion of the melt from the diverter valve.
using two or more parallel screws {or at least two parallel non-intermeshing screws}, e.g. twin screw extruders · CPC title
with consecutive mixers, e.g. with premixing some of the components · CPC title
using a screw extruder and a gear pump · CPC title
flexible, e.g. blown foils · CPC title
containing compounding ingredients (releasing, lubricating or separating agents B29C33/56, fibers B29K2105/08, B29K2105/12; fillers B29K2105/16, recycled material B29K2105/26) · CPC title
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