# US 2018/0022918 A1 · A method of quenching a melt polycarbonate > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 2018/0022918 A1 - Document ID: US20180022918A1 - Status: Published application - Kind: A1 - Application number: 15/548,822 - Filed: 2016-02-11 - Published: 2018-01-25 - Earliest claimed: 2015-02-17 - Assignees: Sabic Global Technologies B.V. - Applicants: Sabic Global Technologies B.V. - Inventors: Ignacio Vic Fernandez - Web page: https://patentgrep.com/patent/US20180022918A1 ## CPC - C08L 69/00: Compositions of polycarbonates; Compositions of derivatives of polycarbonates - C08G 64/40: Post-polymerisation treatment - C08L 2205/025: containing two or more polymers of the same hierarchy C08L, and differing only in parameters such as density, comonomer content, molecular weight, structure - C08L: COMPOSITIONS OF MACROMOLECULAR COMPOUNDS (compositions based on polymerisable monomers C08F, C08G; artificial filaments or fibres D01F; textile treating compositions D06) - C08G: MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS ## Abstract In an embodiment, a process for forming a quenched composition comprises mixing an unquenched melt polycarbonate and a quenched melt polycarbonate to form the quenched composition; wherein the quenched polycarbonate was formed from a first melt polymerization, wherein the first melt polymerization comprises adding a quencher to form the quenched polycarbonate, wherein the unquenched polycarbonate was formed from a second melt polymerization, wherein the unquenched melt polycarbonate comprises an active catalyst used during the second melt polymerization, and wherein the second melt polymerization is free of a quencher addition. ## Claims ### Claim 1 A process for forming a quenched composition comprising: mixing 40 to 95 wt % of an unquenched melt polycarbonate and 5 to 60 wt % of a quenched melt polycarbonate to form the quenched composition, wherein the weight percentage is based upon a total weight of the quenched composition; wherein the quenched melt polycarbonate was formed from a first melt polymerization, and wherein the quenched melt polycarbonate comprises greater than or equal to 0.5 ppm of free quencher; wherein the unquenched melt polycarbonate was formed from a second melt polymerization, wherein the unquenched melt polycarbonate comprises an active catalyst that is capable of further polymerizing the unquenched melt polycarbonate and that was used during the second melt polymerization. ### Claim 2 (depends on 1) The process of claim 1, wherein the quenched melt polycarbonate is free of an additive with a reactive OH group, where reactivity is with respect to the quenched melt polycarbonate and the unquenched melt polycarbonate. ### Claim 3 (depends on 2) The process of claim 2, wherein the quenched melt polycarbonate consists essentially of the melt polymerized polycarbonate, a quenched catalyst, the quencher, and optionally one or more of unreacted monomer, phenol, and ester-substituted phenol. ### Claim 4 (depends on 1) The process of claim 1, further comprising adding an additive with a reactive group after greater than or equal to 30 seconds of starting the mixing, or greater than or equal to 60 seconds of starting the mixing; wherein the additive with the reactive group optionally comprises 2-(2H-benzotriazol-2-yl)-4-(1,1,3,3-tetramethylbutyl)-phenol, glycerol monostearate, or a combination comprising one or both of the foregoing. ### Claim 5 (depends on 1) The process of claim 1, further comprising receiving a first shipment of the quenched melt polycarbonate from a first source prior to mixing the unquenched melt polycarbonate and the quenched melt polycarbonate. ### Claim 6 (depends on 5) The process of claim 5, further comprising receiving a second shipment of the unquenched melt polycarbonate from a second source prior to mixing the unquenched melt polycarbonate and the quenched melt polycarbonate, wherein the second source is different than the first source. ### Claim 7 (depends on 1) The process of claim 1, wherein one of the quenched melt polycarbonate and the unquenched melt polycarbonate has a melt flow rate of greater than or equal to 10 g/10 min and the other has a melt flow rate of less than or equal to 8 g/10 min as determined by ASTM D1238-04 at 250° C., 1.5 kilograms. ### Claim 8 (depends on 1) The process of claim 1, wherein one or both of the quenched melt polycarbonate and the unquenched melt polycarbonate was derived from a diaryl carbonate comprising a metal compound, wherein the metal compound comprises less than or equal to 500 ppb of molybdenum; less than or equal to 33 ppb of vanadium; less than or equal to 33 ppb of chromium; less than or equal to 75 ppb of titanium; less than or equal to 375 ppb of niobium; less than or equal to 33 ppb of nickel; less than or equal to 10 ppb of zirconium; and less or equal to 10 ppb iron; all based on the total weight of the diaryl carbonate and the metal compound. ### Claim 9 (depends on 1) The process of claim 1, wherein the quenched melt polycarbonate comprises 0.5 to 20 ppm of free quencher based on the total weight of the quenched melt polycarbonate. ### Claim 10 (depends on 1) The process of claim 1, wherein the mixture comprises 5 to 10 wt % of the quenched melt polycarbonate based on the total weight of the mixture. ### Claim 11 (depends on 1) The process of claim 1, wherein the unquenched melt polycarbonate comprises greater than or equal to 10 wt % active catalyst, based upon a total weight of catalyst used during second melt polymerization, and wherein less than 1 ppm quencher has been added during second melt polymerization. ### Claim 12 (depends on 1) The process of claim 1, wherein the mixing occurs for less than or equal to 5 minutes. ### Claim 13 (depends on 1) The process of claim 1, wherein the mixing does not melt a component with a melting temperature of 60° C. ### Claim 14 (depends on 1) The process of claim 1, wherein the mixing occurs at a tipspeed of 1 to 5 m/s. ### Claim 15 (depends on 1) The process of claim 1, wherein the mixing occurs in a double shaft mixer rotating in opposite directions. ### Claim 16 (depends on 1) The process of claim 1, wherein the quencher comprises n-butyl tosylate. ### Claim 17 (depends on 1) The process of claim 1, wherein the quenched composition comprises mixing 40 to 60 wt % of an unquenched the unquenched melt polycarbonate and 40 to 60 wt % of the quenched melt polycarbonate. ### Claim 18 (depends on 1) The process of claim 1, wherein the alkali catalyst comprises a metal compound, wherein the metal comprises at least one of sodium, potassium, cesium; wherein if the metal compound comprises sodium sulfate, the amount of sodium is 0 to 1,690 ppm; if the metal compound comprises cesium sulfate, the amount of cesium is 0 to 275 ppm; if the metal compound comprises sodium hydroxide, the amount of sodium is 0 to 35 ppm; if the metal compound comprises potassium hydroxide, the amount of potassium is 0 to 50 ppm; if the metal compound comprises cesium hydroxide, the amount of cesium is 0 to 140 ppm; all based on the total weight of the alkali compound and metal compound. ### Claim 19 (depends on 1) The process of claim 1, wherein one or both of the quenched melt polycarbonate and the unquenched melt polycarbonate has terminal have terminal hydroxyl groups in an amount of less than or equal to 20 mol % based on the molar total of all terminal groups of the polycarbonate. ### Claim 20 (depends on 1) The process of claim 1, wherein the quenched composition comprises glycerol tristearate.