Vertical centrifugal thin film evaporator and monomer purification method
US-2015038736-A1 · Feb 5, 2015 · US
US11384206B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11384206-B2 |
| Application number | US-201616321566-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 4, 2016 |
| Priority date | Aug 4, 2016 |
| Publication date | Jul 12, 2022 |
| Grant date | Jul 12, 2022 |
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Volatile siloxanes, particularly those of a cyclic nature, are removed from high viscosity silicone polymers and high viscosity silicone compositions by evaporation in a short path evaporator.
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The invention claimed is: 1. A method for removing volatile constituents from a high-viscosity silicone polymer having a viscosity of 1000 to 20,000 Pa*s or a silicone composition having a viscosity of 100 to 20,000 Pa*s, comprising: introducing the high viscosity silicone polymer or the silicone composition into a short path evaporator which comprises a vertically disposed cylinder having a heating jacket which heats the inner wall of the cylinder; a rotor, and an internal condenser, wherein mounted on the rotor are wiper elements and conveying elements, which distribute the silicone polymers or silicone composition in the form of a thin layer on the heated inner wall and convey the silicone polymers or silicone composition toward an outlet, wherein the silicone polymers or silicone compositions are fed by a feed at the top of the cylinder onto the inner wall, and evaporating volatile constituents and collecting a high viscosity silicone polymer or silicone composition containing less volatiles, wherein the viscosities are measured at 25° C. in accordance with DIN 54458. 2. The method of claim 1 , wherein the volatiles comprise D3 to D30 cyclic polysiloxanes and linear polysiloxanes having 2 to 30 silicon atoms. 3. The method of claim 1 , wherein the silicone polymer is a silicone polymer containing no functional groups, a silicone base polymer having condensable end groups, a silicone base polymer having unsaturated alkyl groups, or Si—H, Si-vinyl, phenyl-containing or fluorine-containing silicone base polymers. 4. The method of claim 1 , wherein the silicone composition comprises an RTV-1, RTV-2, or LSR composition. 5. The method of claim 1 , wherein the high-viscosity silicone composition contains at least 40 wt % of organopolysiloxane. 6. The method of claim 1 , wherein the high-viscosity silicone composition comprises fillers. 7. The method of claim 1 , wherein the absolute pressure in the short path evaporator is 0.01 Pa to 500 Pa. 8. The method of claim 1 , wherein the temperature of the high-viscosity silicone polymer or high viscosity silicone composition in the short path evaporator is 150° C. to 240° C. 9. The method of claim 1 , wherein the high-viscosity silicone polymer or high viscosity silicone compositions are heated before being fed into the short path evaporator. 10. The method of claim 1 , wherein the silicone polymers or high viscosity silicone compositions are degassed before entry into the short path evaporator. 11. The method of claim 9 , wherein heating is effected by exposing the high viscosity silicone polymer or high viscosity silicone composition to high shear. 12. The method of claim 1 , wherein volatiles are removed from a high viscosity silicon composition containing a filler selected from the group consisting of silica, carbon black, silicon-aluminum oxides, and mixtures thereof.
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