Thermoplastic resin composition for refrigerant transporting piping, and method for producing same
US-12071541-B2 · Aug 27, 2024 · US
US2017342222A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2017342222-A1 |
| Application number | US-201515513291-A |
| Country | US |
| Kind code | A1 |
| Filing date | Sep 22, 2015 |
| Priority date | Sep 26, 2014 |
| Publication date | Nov 30, 2017 |
| Grant date | — |
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Process for preparing a masterbatch comprising 20-90 wt % of a polymer additive dispersed in 10-80 wt % of a thermoplastic polymer, said process comprising the steps of: —providing the additive in liquid form, —optionally heating the additive, —adding solid particles of the thermoplastic polymer to the liquid additive, —heating the resulting mixture to a temperature in or above the melting temperature of the polymer, —treating the mixture with shaping equipment to form solid particles.
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1 . Process for preparing a masterbatch comprising 20-90 wt % of a polymer additive dispersed in 10-80 wt % of a thermoplastic polymer, said process comprising the steps of: providing the additive in liquid form, optionally heating the additive, adding solid particles of the thermoplastic polymer to the liquid additive, heating the resulting mixture to a temperature in or above the melting temperature of the polymer, treating the mixture with shaping equipment to form solid particles. 2 . Process according to claim 1 wherein in the process is performed under inert atmosphere. 3 . Process according to claim 1 or 2 wherein the addition of solid particles of thermoplastic polymer to the liquid additive and the heating of the resulting mixture are performed in a stirred vessel. 4 . Process according to claim 3 wherein the residence time of the mixture in said vessel is at least 0.5 hour. 5 . Process according to claim 4 wherein the residence time is at least 1 hour. 6 . Process according to any one of the preceding claims wherein the additive is heated to a temperature in the range 80-150° C., preferably 100-130° C. prior to the addition of solid particles of thermoplastic polymer. 7 . Process according to any one of the preceding claims wherein the polymer additive is selected from alkoxylated amines, amides, alkoxylated amides, glycerol esters, alkoxylated glycerol esters, and alkylated sorbitan esters. 8 . Process according to claim 7 wherein the polymer additive is an alkoxylated amine having the general formula wherein R 1 is a saturated or unsaturated hydrocarbon chain with 11 to 21 carbon atoms, optionally substituted with —OH; —O—; —(C═O)—O—; —NH—; —Si—; —S—; —P—; —SO 2 —; —S═O—; or —SO 3 H containing groups, and R 2 is independently selected from H, ethylene oxide chains, propylene oxide chains, and ethylene oxide-propylene oxide bock- or random copolymer chains, provided that at least one R 2 -group is other than H, and the total number of ethylene oxide and propylene oxide per chain is in the range 1-30. 9 . Process according to claim 8 wherein the polymer additive is an alkoxylated monoamide having the general formula wherein R 1 is a saturated or unsaturated hydrocarbon chain with 11 to 21 carbon atoms, optionally substituted with —OH; —O—; —(C═O)—O—; —NH—; —Si—; —S—; —P—; —SO 2 —; —S═O—; or —SO 3 H containing groups, and R 2 is independently selected from H, ethylene oxide chains, propylene oxide chains, and ethylene oxide-propylene oxide bock- or random copolymer chains, provided that not every R 2 in each formula is H, and the total number of ethylene oxide and propylene oxide per chain is in the range 1-30. 10 . Process according to claim 9 wherein the polymer additive is an alkoxylated bisamide having the general formula wherein R 2 is independently selected from H, ethylene oxide chains, propylene oxide chains, and ethylene oxide-propylene oxide bock- or random copolymer chains, provided that at least one R 2 -group is other than H, the total number of ethylene oxide and propylene oxide per chain is in the range 1-30, and R 3 is a linear or branched alkanediyl chain with 2 to 6 carbon atoms, optionally substituted with —OH; —O—; ═O; —S—; —SO 2 —; —Si—; or —P— containing groups. 11 . Process according to claim 10 wherein the polymer additive is an alkoxylated glycerol ester having the formula wherein R 1 is a saturated or unsaturated hydrocarbon chain with 11 to 21 carbon atoms, optionally substituted with —OH; —O—; —(C═O)—O—; —NH—; —Si—; —S—; —P—; —SO 2 —; —S═O—; or —SO 3 H containing groups, and R 2 is independently selected from H, ethylene oxide chains, propylene oxide chains, and ethylene oxide-propylene oxide bock- or random copolymer chains, provided that at least one R 2 -group is other than H, the total number of ethylene oxide and propylene oxide per chain is in the range 1-30, and n is an integer in the range 1-8. 12 . Process according to claim 11 wherein the polymer additive is an alkoxylated sorbitan ester have the formula wherein R 1 is a saturated or unsaturated hydrocarbon chain with 11 to 21 carbon atoms, optionally substituted with —OH; —O—; —(C═O)—O—; —NH—; —Si—; —S—; —P—; —SO 2 —; —S═O—; or —SO 3 H containing groups, and R 2 is independently selected from H, ethylene oxide chains, propylene oxide chains, and ethylene oxide-propylene oxide bock- or random copolymer chains, provided that at least one R 2 -group is other than H, the total number of ethylene oxide and propylene oxide per chain is in the range 1-30. 13 . Process according to any one of the preceding claims wherein the masterbatch contains 50-80 wt % of the polymer additive and 20-50 wt % of the thermoplastic polymer. 14 . Process according to any one of the preceding claims wherein the mixture of thermoplastic polymer and liquid polymer additive is heated to a temperature in the range 150-250° C. 15 . Process according to any one of the preceding claims wherein the thermoplastic polymer is selected from polypropylene, polyethylene, polystyrene, polybutadiene, ethylene-vinyl acetate copolymer, and styrene acrylonitrile.
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