Initiator-tightened compositions
US-9481778-B2 · Nov 1, 2016 · US
US2016244587A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016244587-A1 |
| Application number | US-201415029686-A |
| Country | US |
| Kind code | A1 |
| Filing date | Oct 17, 2014 |
| Priority date | Oct 18, 2013 |
| Publication date | Aug 25, 2016 |
| Grant date | — |
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The invention relates to a process for production of expanded thermoplastic elastomer, said process comprising the steps of: (e) adding monomers and/or oligomers used for producing the thermoplastic elastomer with or without further starting materials into a first stage of a polymer-processing machine, (f) mixing the monomers and/or oligomers and also the optionally added further starting materials and reacting the monomers and/or oligomers to give a polymer melt in the first stage of the polymer-processing machine, (g) passing the polymer melt into a second stage of a polymer-processing machine and adding a physical blowing agent with or without further starting materials to obtain a polymer melt comprising a blowing agent, (h) molding the polymer melt comprising a blowing agent into an expanded thermoplastic elastomer.
Opening claim text (preview).
1 .- 15 . (canceled) 16 . A process for production of expanded thermoplastic elastomer, said process comprising the steps of: (a) adding monomers and/or oligomers used for producing the thermoplastic elastomer with or without further starting materials into a first stage of a polymer-processing machine, (b) mixing the monomers and/or oligomers and also the optionally added further starting materials and reacting the monomers and/or oligomers to give a polymer melt in the first stage of the polymer-processing machine, (c) passing the polymer melt into a second stage of the polymer-processing machine and adding a physical blowing agent with or without further starting materials to obtain a polymer melt comprising a blowing agent, (d) molding the polymer melt comprising a blowing agent into an expanded thermoplastic elastomer. 17 . The process according to claim 16 , wherein the polymer-processing machine is a screw-plunger machine. 18 . The process according to claim 17 , wherein the first stage of the screw-plunger machine and the second stage of the screw-plunger machine are sectors of an extruder. 19 . The process according to claim 17 , wherein the first stage of the screw-plunger machine is a first extruder of a tandem extruder and the second stage of the screw-plunger machine is a second extruder of the tandem extruder. 20 . The process according to claim 17 , wherein the second stage of the polymer-processing machine comprises a melt pump, optionally with a melt sieve or a static mixer. 21 . The process according to claim 16 , wherein the expanded thermoplastic elastomer is an expanded pellet material. 22 . The process according to claim 21 , wherein the pellet material is obtained by forcing the polymer melt in step (d) through a pelletizing die regulated to a temperature in the range from 150 to 280° C., using a cutting device to cut the polymer melt forced through the temperature-regulated pelletizing die into individual expanding pellets and using a stream of liquid to export the pellets from the pelletizing chamber. 23 . The process according to claim 22 , wherein a temperature-regulated liquid flowing through the pelletizing chamber as a stream has a temperature in the range from 10 to 60° C. and a pressure in the range from 0.7 to 20 bar above ambient pressure. 24 . The process according to claim 21 , wherein the expanded pellet material has a bead weight in the range from 1 to 40 mg. 25 . The process according to claim 16 , wherein the blowing agent comprises carbon dioxide, nitrogen or a mixture of carbon dioxide and nitrogen. 26 . The process according to claim 25 , wherein the blowing agent comprises 50 wt % to 100 wt % carbon dioxide and 0 wt % to 50 wt % nitrogen and no further blowing agent. 27 . The process according to claim 16 , wherein the blowing agent comprises an organic blowing agent selected from alkanes, halogenated hydrocarbons or a mixture thereof. 28 . The process according to claim 16 , wherein the thermoplastic elastomer is a thermoplastic polyurethane. 29 . The process according to claim 16 , wherein the expanded thermoplastic elastomer has a density in the range from 30 to 350 g/l. 30 . The process according to claim 16 , wherein the expanded thermoplastic elastomer has an uninterrupted skin.
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