Methods and devices for mechanical separation of multilayer interlayers
US-2024217227-A1 · Jul 4, 2024 · US
US9751990B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9751990-B2 |
| Application number | US-201214371102-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 21, 2012 |
| Priority date | Jan 10, 2012 |
| Publication date | Sep 5, 2017 |
| Grant date | Sep 5, 2017 |
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A method for producing a transparent thermoplastic resin pellet comprising a step of kneading a transparent thermoplastic resin with a kneader under a condition under which a damage history calculated according to the following formula is 500 to 2,500: Damage history={Residence time ( tr )}×{Shear rate (γ)} Residence time ( tr )=( W×H×L )/ Q Shear rate (γ)=(π× D×N )/ H in the formulae, W represents a screw groove width (pitch) [cm]; H represents a screw groove depth [cm]; L represents a screw length [cm]; Q represents a resin supply amount [g/s]; D represents a screw diameter [cm]; and N represents a screw rotation number [rps].
Opening claim text (preview).
The invention claimed is: 1. A method for producing a transparent thermoplastic resin pellet, the method comprising kneading a transparent thermoplastic resin with a kneader under a condition under which a damage history calculated according to the following formula is from 500 to 2,500 cm 3 /g: Damage history={Residence time ( tr )}×{Shear rate (γ)} Residence time ( tr )=( W×H×L )/ Q Shear rate (γ)=(π× D×N )/ H wherein W represents a screw groove width (pitch) [cm]; H represents a screw groove depth [cm]; L represents a screw length [cm]; Q represents a resin supply amount [g/s]; D represents a screw diameter [cm]; and N represents a screw rotation number [rps]. 2. The method of claim 1 , wherein the transparent thermoplastic resin is an aromatic polycarbonate. 3. The method of claim 2 , wherein the aromatic polycarbonate has a viscosity average molecular weight (Mv) of from 11,000 to 23,000. 4. The method of claim 1 , wherein the kneader is a twin-screw kneader. 5. The method of claim 1 , wherein the kneader is equipped with a melt filter for removal of extraneous foreign matter. 6. The method of claim 1 wherein the damage history is from 900 to 2,000 cm 3 /g. 7. The method of claim 1 wherein the transparent thermoplastic resin is selected from the group consisting of a polyarylate resin, a polymethyl methacrylate resin, a polystyrene resin and a polycarbonate resin. 8. The method of claim 1 wherein the transparent thermoplastic resin is a polycarbonate prepared from bisphenol A.
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