CN108570180A - A kind of polyethylene water-feeding pipes and preparation method thereof having excellent weather resistance - Google Patents

A kind of polyethylene water-feeding pipes and preparation method thereof having excellent weather resistance Download PDF

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CN108570180A
CN108570180A CN201810415211.XA CN201810415211A CN108570180A CN 108570180 A CN108570180 A CN 108570180A CN 201810415211 A CN201810415211 A CN 201810415211A CN 108570180 A CN108570180 A CN 108570180A
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陈云
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Zhengzhou Dewei Machinery Equipment Co Ltd
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Zhengzhou Dewei Machinery Equipment Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/04Homopolymers or copolymers of ethene
    • C08L23/06Polyethene
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/24Acids; Salts thereof
    • C08K3/26Carbonates; Bicarbonates
    • C08K2003/265Calcium, strontium or barium carbonate
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K2201/00Specific properties of additives
    • C08K2201/011Nanostructured additives
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2201/00Properties
    • C08L2201/08Stabilised against heat, light or radiation or oxydation
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2203/00Applications
    • C08L2203/18Applications used for pipes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/03Polymer mixtures characterised by other features containing three or more polymers in a blend
    • C08L2205/035Polymer mixtures characterised by other features containing three or more polymers in a blend containing four or more polymers in a blend

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Abstract

The present invention relates to a kind of polyethylene water-feeding pipes and preparation method thereof having excellent weather resistance, and the tubing is made of following raw material:Polyethylene, modified poly ethylene, aerosil, calcium stearate, modified poly ethylene is by polyethylene powder, modified SEBS, polyvinyl alcohol, polymethyl methacrylate and makrolon reaction are made, modified SEBS is by SEBS, ethylene propylene diene rubber, polyester hot-melt adhesive and modified nano calcium carbonate reaction are made, modified nano calcium carbonate is by nano-calcium carbonate, ethyl alcohol, water, hydroxy silicon oil 107 and the reactions of hydroxy silicon oil JF M30 203 are made, aerosil is by tetraethyl orthosilicate, ethyl alcohol, water, nonionic surfactant Lutensol XP 50 and nonionic surfactant Lutensol XP 70 reactions are made.Tubing provided by the invention has excellent weatherability and oxidation induction performance.

Description

A kind of polyethylene water-feeding pipes and preparation method thereof having excellent weather resistance
Technical field
The present invention relates to polyethylene pipe fields, and in particular to a kind of polyethylene water-feeding pipes having excellent weather resistance and its system Preparation Method.
Background technology
Polyethylene is one of the most frequently used synthetic plastic tubing resin.Polyethylene have excellent elongation at break, toughness, The advantages such as the burn into of resistance to industrial chemicals resistance to pressure, electrical insulating property, processing performance, low-density, nontoxic, mechanical strength.Polyethylene is wide It is general to be applied to the necks such as water supply and sewerage pipeline, chemical industry blow-off line, tap water conveyance conduit, industrial chemicals conveyance conduit, electric wire Domain.
Currently, polythene material needs further to be promoted in weatherability and oxidation induction performance.The present invention using polyethylene, Modified poly ethylene, aerosil, calcium stearate are prepared for the polyethylene water-feeding pipes having excellent weather resistance, prepared by this method The polyethylene water-feeding pipes having excellent weather resistance have excellent weatherability and oxidation induction performance.
Invention content
The purpose of the present invention is to provide a kind of preparation method for the polyethylene water-feeding pipes having excellent weather resistance, this method is logical Change reactant feed and technology mode are crossed, the material of preparation has excellent weatherability and oxidation induction performance.
To achieve the goals above, technical scheme is as follows.
A kind of polyethylene water-feeding pipes and preparation method thereof having excellent weather resistance, specifically include following steps:(1), by silicon Sour tetra-ethyl ester, ethyl alcohol, nonionic surfactant Lutensol XP-50 and nonionic surfactant Lutensol XP-70 It is 90 according to quality parts ratio:185~225:8~19:9~17 are added in reaction kettle, and mixing speed is 400~550r/ Min reacts 50min under the conditions of 25~33 DEG C of maintenance system temperature, by quality parts ratio be 9~23 water according to 0.05 mass Part/min is added in reaction kettle, and after the completion of to be added, the 40min that maintains under above-mentioned reaction condition that the reaction was continued shifts product Into hydrothermal reaction kettle, 2~6h is reacted under the conditions of 185~200 DEG C of maintenance system temperature, product subtracts through 125 DEG C, -0.08MPa Pressure distillation 1h, product wash 5 times through 1L EtOH Sonicates, are dried in vacuo 15min in 75 DEG C, -0.07MPa, grinding obtains titanium dioxide Silica aerogel;(2), it is 70 according to quality parts ratio by nano-calcium carbonate, ethyl alcohol, water:55~67:7~15 to be added to hydro-thermal anti- Answer in kettle, under the conditions of 115~128 DEG C of maintenance system temperature react 30~45min, product through filtering, 56 DEG C, -0.05MPa it is true The dry 9min of sky, is 18~27 by product and quality parts ratio:14~25 hydroxy silicon oil 107 and hydroxy silicon oil JF-M30-203 It is added in hydrothermal reaction kettle, 1~2h is reacted under the conditions of 175~198 DEG C of maintenance system temperature, product shakes through filtering, 2L ethyl alcohol Washing 3 times is swung, 11min is dried in vacuo in 70 DEG C, -0.08MPa, obtains modified nano calcium carbonate;(3), by SEBS, EPDM Rubber, polyester hot-melt adhesive and modified nano calcium carbonate are 80 according to quality parts ratio:13~25:11~20:35~41 are added to In ball mill, drum speed is 15~31 r/min, and 21~33min is reacted under the conditions of 0~10 DEG C of maintenance system temperature, with squeezing Go out machine in 185~197 DEG C of extruding pelletizations of temperature, crushes to get to modified SEBS;(4), by polyethylene powder, modified SEBS, poly- second Enol, polymethyl methacrylate and makrolon are 30 according to quality parts ratio:19~27:9~22:7~16:6~14 add Enter and crushed into pulverizer, transferred the material into ball mill, drum speed be 18~30r/min, maintenance system temperature 10~ 20~35min is reacted under the conditions of 19 DEG C, with extruder in 195~210 DEG C of extruding pelletizations of temperature, is crushed to get to the poly- second of modification Alkene;(5), it is 90 according to quality parts ratio by polyethylene, modified poly ethylene, aerosil, calcium stearate:18~32: 16~30:2~6 are added in ball mill, and drum speed is 21~38 r/min, anti-under the conditions of -5~5 DEG C of maintenance system temperature 27~39min is answered, with extruder in 185~197 DEG C of extrusion moldings of temperature to get to the polyethylene feed pipe having excellent weather resistance Material.
The preparation method of the polyethylene water-feeding pipes of the present invention having excellent weather resistance, includes the following steps:
(1), by tetraethyl orthosilicate, ethyl alcohol, nonionic surfactant Lutensol XP-50 and nonionic surfactant Lutensol XP-70 are 90 according to quality parts ratio:185~225:8~19:9~17 are added in reaction kettle, mixing speed For 400~550r/min, 50min is reacted under the conditions of 25~33 DEG C of maintenance system temperature, the water for being 9~23 by quality parts ratio It is added in reaction kettle according to 0.05 mass parts/min, after the completion of to be added, maintains under above-mentioned reaction condition that the reaction was continued Product is transferred in hydrothermal reaction kettle by 40min, and 2~6h, product warp are reacted under the conditions of 185~200 DEG C of maintenance system temperature 125 DEG C, -0.08MPa vacuum distillation 1h, product are washed 5 times through 1L EtOH Sonicates, are dried in vacuo in 75 DEG C, -0.07MPa 15min, grinding, obtains aerosil;The nonionic surfactant Lutensol XP-50 and nonionic table The purpose of face activator Lutensol XP-70 improves silica airsetting to improve the dispersing uniformity of System forming drop The porosity of glue.
(2), it is 70 according to quality parts ratio by nano-calcium carbonate, ethyl alcohol, water:55~67:7~15 are added to hydro-thermal reaction In kettle, 30~45min is reacted under the conditions of 115~128 DEG C of maintenance system temperature, product is through filtering, 56 DEG C, -0.05MPa vacuum Product and quality parts ratio are 18~27 by dry 9min:14~25 hydroxy silicon oil 107 and hydroxy silicon oil JF-M30-203 adds It adds in hydrothermal reaction kettle, 1~2h is reacted under the conditions of 175~198 DEG C of maintenance system temperature, product is vibrated through filtering, 2L ethyl alcohol Washing 3 times is dried in vacuo 11min in 70 DEG C, -0.08MPa, obtains modified nano calcium carbonate;The hydroxy silicon oil 107 and hydroxyl The purpose of base silicone oil JF-M30-203 induces performance to improve the oxidation of polyethylene feed pipe.
(3), it is 80 according to quality parts ratio by SEBS, ethylene propylene diene rubber, polyester hot-melt adhesive and modified nano calcium carbonate: 13~25:11~20:35~41 are added in ball mill, and drum speed is 15~31 r/min, maintenance system temperature 0~10 21~33min is reacted under the conditions of DEG C, with extruder in 185~197 DEG C of extruding pelletizations of temperature, is crushed to get to modified SEBS;Institute The purpose of the ethylene propylene diene rubber and polyester hot-melt adhesive stated is in order to improve to the weather-proof of the wellability of raw material and polyethylene feed pipe Property.
(4), by polyethylene powder, modified SEBS, polyvinyl alcohol, polymethyl methacrylate and makrolon according to mass parts Number is than being 30:19~27:9~22:7~16:6~14 are added in pulverizer and crush, and transfer the material into ball mill, cylinder Rotating speed is 18~30r/min, and 20~35min is reacted under the conditions of 10~19 DEG C of maintenance system temperature, with extruder temperature 195~ 210 DEG C of extruding pelletizations crush to get to modified poly ethylene;Polyvinyl alcohol, polymethyl methacrylate and the makrolon Purpose in order to improve dispersion and the mixing uniformity of storeroom.
(5), it is 90 according to quality parts ratio by polyethylene, modified poly ethylene, aerosil, calcium stearate:18 ~32:16~30:2~6 are added in ball mill, and drum speed is 21~38 r/min, -5~5 DEG C of items of maintenance system temperature Under part react 27~39min, with extruder 185~197 DEG C of extrusion moldings of temperature to get to the polyethylene having excellent weather resistance to Water pipe material.
The beneficial effects of the present invention are:
1, tetraethyl orthosilicate is in nonionic surfactant Lutensol XP-50 and nonionic surfactant Lutensol In the presence of XP-70 emulsifiers, by the small sized drop of material shape and it can be dispersed in ethanol solution, under hydrothermal conditions Improve the porosity of the stability and aerosil of drop;The aerosil of preparation can improve polyethylene water supply The resistance to oxidation of pipe induces performance;
2, after nano-calcium carbonate is surface-treated by ethanol water, by hydro-thermal reaction, hydroxy silicon oil 107 and hydroxyl silicon Oily JF-M30-203 is surface modified nano-calcium carbonate, can improve the resistance to oxidation induction performance of nano-calcium carbonate;It prepares Modified nano calcium carbonate can improve the resistance to oxidation induction performance of polyethylene feed pipe;
3, ethylene propylene diene rubber and polyester hot-melt adhesive at high temperature, have excellent wellability to material surface, can be to material table Face is infiltrated, and the compatibility and dispersion stabilization of storeroom are improved, and the modified SEBS of preparation can improve polyethylene feed pipe Weatherability and resistance to oxidation inductivity;
4, polyvinyl alcohol, polymethyl methacrylate and makrolon have larger rigidity and hardness, by crushing and ball milling Processing, while capable of significantly improving fineness of materials, improves the mixing uniformity of storeroom;The modified poly ethylene of preparation can improve object Mixing uniformity between material, to which the weatherability and resistance to oxidation for improving polyethylene feed pipe induce performance;
5, under polyethylene, modified poly ethylene, aerosil synergistic effect, the polyethylene water supply having excellent weather resistance is assigned The excellent weatherability of tubing and resistance to oxidation induce performance.
Specific implementation mode
The specific implementation mode of the present invention is described with reference to embodiment, to be better understood from the present invention.
Embodiment 1
A kind of polyethylene water-feeding pipes having excellent weather resistance, preparation method includes the following steps:
(1), 90 parts of tetraethyl orthosilicates, 195 parts of ethyl alcohol, 12 parts of nonionic surfactant Lutensol XP-50 and 11 parts are weighed Nonionic surfactant Lutensol XP-70 are added in reaction kettle, mixing speed 470r/min, maintenance system temperature 50min is reacted under the conditions of 28 DEG C, 13 parts of water are added to according to 0.05 part/min in reaction kettle, after the completion of to be added, in maintenance The 40min that states under reaction condition that the reaction was continued, product is transferred in hydrothermal reaction kettle, anti-under the conditions of 195 DEG C of maintenance system temperature 2.5h, product is answered to be evaporated under reduced pressure 1h through 125 DEG C, -0.08MPa, product washs 5 times through 1L EtOH Sonicates, in 75 DEG C, -0.07MPa It is dried in vacuo 15min, grinding obtains aerosil;
(2), it weighs 70 parts of nano-calcium carbonates, 62 parts of ethyl alcohol, 10 parts of water to be added in hydrothermal reaction kettle, maintenance system temperature 122 37min is reacted under the conditions of DEG C, product is dried in vacuo 9min through filtering, 56 DEG C, -0.05MPa, by product and 22 parts of hydroxy silicon oils 107 and 18 parts of hydroxy silicon oil JF-M30-203 are added in hydrothermal reaction kettle, are reacted under the conditions of 188 DEG C of maintenance system temperature 1.4h, product are dried in vacuo 11min in 70 DEG C, -0.08MPa, obtain modified Nano carbon through filtering, 2L ethyl alcohol oscillation washing 3 times Sour calcium;
(3), 80 parts of SEBS, 17 parts of ethylene propylene diene rubbers, 16 parts of polyester hot-melt adhesives and 38 parts of modified nano calcium carbonates are weighed to be added Into ball mill, drum speed is 21 r/min, 26min is reacted under the conditions of 3 DEG C of maintenance system temperature, with extruder in temperature 189 DEG C of extruding pelletizations crush to get to modified SEBS;
(4), weigh 30 parts of polyethylene powders, 23 parts of modified SEBSs, 14 parts of polyvinyl alcohol, 2488,10 parts of polymethyl methacrylates and 8 parts of makrolon are added in pulverizer and crush, and transfer the material into ball mill, drum speed 25r/min, maintenance system 27min is reacted under the conditions of 12 DEG C of temperature, with extruder in 203 DEG C of extruding pelletizations of temperature, is crushed to get to modified poly ethylene;
(5), 90 parts of polyethylene, 22 parts of modified poly ethylenes, 19 parts of aerosils, 4 parts of calcium stearates are weighed and are added to ball In grinding machine, drum speed is 28 r/min, reacts 32min under the conditions of 0 DEG C of maintenance system temperature, with extruder in 194 DEG C of temperature Extrusion molding is to get to the polyethylene water-feeding pipes having excellent weather resistance.
Embodiment 2
A kind of polyethylene water-feeding pipes having excellent weather resistance, preparation method includes the following steps:
(1), it is non-that 90 parts of tetraethyl orthosilicates, 185 parts of ethyl alcohol, 8 parts of nonionic surfactant Lutensol XP-50 and 9 parts are weighed Ionic surfactant Lutensol XP-70 are added in reaction kettle, mixing speed 400r/min, maintenance system temperature 25 50min is reacted under the conditions of DEG C, 9 parts of water are added to according to 0.05 part/min in reaction kettle, after the completion of to be added, remains above-mentioned anti- The reaction was continued under the conditions of answering 40min, product is transferred in hydrothermal reaction kettle, is reacted under the conditions of 185 DEG C of maintenance system temperature 6h, product are evaporated under reduced pressure 1h through 125 DEG C, -0.08MPa, and product washs 5 times through 1L EtOH Sonicates, in 75 DEG C, -0.07MPa vacuum Dry 15min, grinding obtain aerosil;
(2), it weighs 70 parts of nano-calcium carbonates, 55 parts of ethyl alcohol, 7 parts of water to be added in hydrothermal reaction kettle, maintenance system temperature 115 45min is reacted under the conditions of DEG C, product is dried in vacuo 9min through filtering, 56 DEG C, -0.05MPa, by product and 18 parts of hydroxy silicon oils 107 and 14 parts of hydroxy silicon oil JF-M30-203 are added in hydrothermal reaction kettle, react 2h under the conditions of 175 DEG C of maintenance system temperature, Product is dried in vacuo 11min in 70 DEG C, -0.08MPa, obtains modified nano calcium carbonate through filtering, 2L ethyl alcohol oscillation washing 3 times;
(3), 80 parts of SEBS, 13 parts of ethylene propylene diene rubbers, 11 parts of polyester hot-melt adhesives and 35 parts of modified nano calcium carbonates are weighed to be added Into ball mill, drum speed is 15 r/min, 33min is reacted under the conditions of 0 DEG C of maintenance system temperature, with extruder in temperature 185 DEG C of extruding pelletizations crush to get to modified SEBS;
(4), 30 parts of polyethylene powders, 19 parts of modified SEBSs, 9 parts of polyvinyl alcohol, 2488,7 parts of polymethyl methacrylates and 6 are weighed Part makrolon, which is added in pulverizer, to be crushed, and is transferred the material into ball mill, drum speed 18r/min, maintenance system 35min is reacted under the conditions of 10 DEG C of temperature, with extruder in 195 DEG C of extruding pelletizations of temperature, is crushed to get to modified poly ethylene;
(5), 90 parts of polyethylene, 18 parts of modified poly ethylenes, 16 parts of aerosils, 2 parts of calcium stearates are weighed and are added to ball In grinding machine, drum speed is 21 r/min, 39min is reacted under the conditions of -5 DEG C of maintenance system temperature, with extruder in temperature 185 DEG C extrusion molding is to get to the polyethylene water-feeding pipes having excellent weather resistance.
Embodiment 3
A kind of polyethylene water-feeding pipes having excellent weather resistance, preparation method includes the following steps:
(1), 90 parts of tetraethyl orthosilicates, 225 parts of ethyl alcohol, 19 parts of nonionic surfactant Lutensol XP-50 and 17 parts are weighed Nonionic surfactant Lutensol XP-70 are added in reaction kettle, mixing speed 550r/min, maintenance system temperature 50min is reacted under the conditions of 33 DEG C, 23 parts of water are added to according to 0.05 part/min in reaction kettle, after the completion of to be added, in maintenance The 40min that states under reaction condition that the reaction was continued, product is transferred in hydrothermal reaction kettle, anti-under the conditions of 200 DEG C of maintenance system temperature Answer 2h, product is evaporated under reduced pressure 1h through 125 DEG C, -0.08MPa, and product washs 5 times through 1L EtOH Sonicates, in 75 DEG C, -0.07MPa it is true The dry 15min of sky, grinding obtain aerosil;
(2), it weighs 70 parts of nano-calcium carbonates, 67 parts of ethyl alcohol, 15 parts of water to be added in hydrothermal reaction kettle, maintenance system temperature 128 30min is reacted under the conditions of DEG C, product is dried in vacuo 9min through filtering, 56 DEG C, -0.05MPa, by product and 27 parts of hydroxy silicon oils 107 and 25 parts of hydroxy silicon oil JF-M30-203 are added in hydrothermal reaction kettle, react 1h under the conditions of 198 DEG C of maintenance system temperature, Product is dried in vacuo 11min in 70 DEG C, -0.08MPa, obtains modified nano calcium carbonate through filtering, 2L ethyl alcohol oscillation washing 3 times;
(3), 80 parts of SEBS, 25 parts of ethylene propylene diene rubbers, 20 parts of polyester hot-melt adhesives and 41 parts of modified nano calcium carbonates are weighed to be added Into ball mill, drum speed is 31 r/min, 21min is reacted under the conditions of 10 DEG C of maintenance system temperature, with extruder in temperature 197 DEG C of extruding pelletizations crush to get to modified SEBS;
(4), weigh 30 parts of polyethylene powders, 27 parts of modified SEBSs, 22 parts of polyvinyl alcohol, 2488,16 parts of polymethyl methacrylates and 14 parts of makrolon are added in pulverizer and crush, and transfer the material into ball mill, drum speed 30r/min, maintain body It is to react 20min under the conditions of 19 DEG C of temperature, with extruder in 210 DEG C of extruding pelletizations of temperature, crushes to get to modified poly ethylene;
(5), 90 parts of polyethylene, 32 parts of modified poly ethylenes, 30 parts of aerosils, 6 parts of calcium stearates are weighed and are added to ball In grinding machine, drum speed is 38 r/min, reacts 27min under the conditions of 5 DEG C of maintenance system temperature, with extruder in 197 DEG C of temperature Extrusion molding is to get to the polyethylene water-feeding pipes having excellent weather resistance.
Embodiment 4
A kind of polyethylene water-feeding pipes having excellent weather resistance, preparation method includes the following steps:
(1), 90 parts of tetraethyl orthosilicates, 190 parts of ethyl alcohol, 15 parts of nonionic surfactant Lutensol XP-50 and 10 parts are weighed Nonionic surfactant Lutensol XP-70 are added in reaction kettle, mixing speed 420r/min, maintenance system temperature 50min is reacted under the conditions of 29 DEG C, 16 parts of water are added to according to 0.05 part/min in reaction kettle, after the completion of to be added, in maintenance The 40min that states under reaction condition that the reaction was continued, product is transferred in hydrothermal reaction kettle, anti-under the conditions of 188 DEG C of maintenance system temperature 3.9h, product is answered to be evaporated under reduced pressure 1h through 125 DEG C, -0.08MPa, product washs 5 times through 1L EtOH Sonicates, in 75 DEG C, -0.07MPa It is dried in vacuo 15min, grinding obtains aerosil;
(2), it weighs 70 parts of nano-calcium carbonates, 61 parts of ethyl alcohol, 10 parts of water to be added in hydrothermal reaction kettle, maintenance system temperature 127 39min is reacted under the conditions of DEG C, product is dried in vacuo 9min through filtering, 56 DEG C, -0.05MPa, by product and 22 parts of hydroxy silicon oils 107 and 17 parts of hydroxy silicon oil JF-M30-203 are added in hydrothermal reaction kettle, are reacted under the conditions of 186 DEG C of maintenance system temperature 1.8h, product are dried in vacuo 11min in 70 DEG C, -0.08MPa, obtain modified Nano carbon through filtering, 2L ethyl alcohol oscillation washing 3 times Sour calcium;
(3), 80 parts of SEBS, 21 parts of ethylene propylene diene rubbers, 17 parts of polyester hot-melt adhesives and 38 parts of modified nano calcium carbonates are weighed to be added Into ball mill, drum speed is 19 r/min, 23min is reacted under the conditions of 4 DEG C of maintenance system temperature, with extruder in temperature 192 DEG C of extruding pelletizations crush to get to modified SEBS;
(4), 30 parts of polyethylene powders, 23 parts of modified SEBSs, 15 parts of polyvinyl alcohol, 2488,9 parts of polymethyl methacrylates and 7 are weighed Part makrolon, which is added in pulverizer, to be crushed, and is transferred the material into ball mill, drum speed 20r/min, maintenance system 26min is reacted under the conditions of 17 DEG C of temperature, with extruder in 199 DEG C of extruding pelletizations of temperature, is crushed to get to modified poly ethylene;
(5), 90 parts of polyethylene, 23 parts of modified poly ethylenes, 19 parts of aerosils, 5 parts of calcium stearates are weighed and are added to ball In grinding machine, drum speed is 31 r/min, reacts 29min under the conditions of 4 DEG C of maintenance system temperature, with extruder in 187 DEG C of temperature Extrusion molding is to get to the polyethylene water-feeding pipes having excellent weather resistance.
Embodiment 5
A kind of polyethylene water-feeding pipes having excellent weather resistance, preparation method includes the following steps:
(1), 90 parts of tetraethyl orthosilicates, 193 parts of ethyl alcohol, 9 parts of nonionic surfactant Lutensol XP-50 and 11 parts are weighed Nonionic surfactant Lutensol XP-70 are added in reaction kettle, mixing speed 500r/min, maintenance system temperature 50min is reacted under the conditions of 32 DEG C, 22 parts of water are added to according to 0.05 part/min in reaction kettle, after the completion of to be added, in maintenance The 40min that states under reaction condition that the reaction was continued, product is transferred in hydrothermal reaction kettle, anti-under the conditions of 192 DEG C of maintenance system temperature 4.5h, product is answered to be evaporated under reduced pressure 1h through 125 DEG C, -0.08MPa, product washs 5 times through 1L EtOH Sonicates, in 75 DEG C, -0.07MPa It is dried in vacuo 15min, grinding obtains aerosil;
(2), it weighs 70 parts of nano-calcium carbonates, 61 parts of ethyl alcohol, 9 parts of water to be added in hydrothermal reaction kettle, maintenance system temperature 121 34min is reacted under the conditions of DEG C, product is dried in vacuo 9min through filtering, 56 DEG C, -0.05MPa, by product and 23 parts of hydroxy silicon oils 107 and 20 parts of hydroxy silicon oil JF-M30-203 are added in hydrothermal reaction kettle, are reacted under the conditions of 191 DEG C of maintenance system temperature 1.7h, product are dried in vacuo 11min in 70 DEG C, -0.08MPa, obtain modified Nano carbon through filtering, 2L ethyl alcohol oscillation washing 3 times Sour calcium;
(3), 80 parts of SEBS, 16 parts of ethylene propylene diene rubbers, 17 parts of polyester hot-melt adhesives and 36 parts of modified nano calcium carbonates are weighed to be added Into ball mill, drum speed is 27 r/min, 30min is reacted under the conditions of 1 DEG C of maintenance system temperature, with extruder in temperature 191 DEG C of extruding pelletizations crush to get to modified SEBS;
(4), weigh 30 parts of polyethylene powders, 22 parts of modified SEBSs, 21 parts of polyvinyl alcohol, 2488,12 parts of polymethyl methacrylates and 11 parts of makrolon are added in pulverizer and crush, and transfer the material into ball mill, drum speed 20r/min, maintain body It is to react 34min under the conditions of 11 DEG C of temperature, with extruder in 207 DEG C of extruding pelletizations of temperature, crushes to get to modified poly ethylene;
(5), 90 parts of polyethylene, 28 parts of modified poly ethylenes, 27 parts of aerosils, 5.2 parts of calcium stearates are weighed to be added to In ball mill, drum speed is 36 r/min, 36min is reacted under the conditions of -4 DEG C of maintenance system temperature, with extruder in temperature 192 DEG C of extrusion moldings are to get to the polyethylene water-feeding pipes having excellent weather resistance.
Embodiment 6
A kind of polyethylene water-feeding pipes having excellent weather resistance, preparation method includes the following steps:
(1), 90 parts of tetraethyl orthosilicates, 210 parts of ethyl alcohol, 18 parts of nonionic surfactant Lutensol XP-50 and 15 parts are weighed Nonionic surfactant Lutensol XP-70 are added in reaction kettle, mixing speed 510r/min, maintenance system temperature 50min is reacted under the conditions of 28 DEG C, 17 parts of water are added to according to 0.05 part/min in reaction kettle, after the completion of to be added, in maintenance The 40min that states under reaction condition that the reaction was continued, product is transferred in hydrothermal reaction kettle, anti-under the conditions of 193 DEG C of maintenance system temperature 3.4h, product is answered to be evaporated under reduced pressure 1h through 125 DEG C, -0.08MPa, product washs 5 times through 1L EtOH Sonicates, in 75 DEG C, -0.07MPa It is dried in vacuo 15min, grinding obtains aerosil;
(2), it weighs 70 parts of nano-calcium carbonates, 59 parts of ethyl alcohol, 13 parts of water to be added in hydrothermal reaction kettle, maintenance system temperature 117 36min is reacted under the conditions of DEG C, product is dried in vacuo 9min through filtering, 56 DEG C, -0.05MPa, by product and 26 parts of hydroxy silicon oils 107 and 19 parts of hydroxy silicon oil JF-M30-203 are added in hydrothermal reaction kettle, are reacted under the conditions of 197 DEG C of maintenance system temperature 1.1h, product are dried in vacuo 11min in 70 DEG C, -0.08MPa, obtain modified Nano carbon through filtering, 2L ethyl alcohol oscillation washing 3 times Sour calcium;
(3), 80 parts of SEBS, 22 parts of ethylene propylene diene rubbers, 14 parts of polyester hot-melt adhesives and 40 parts of modified nano calcium carbonates are weighed to be added Into ball mill, drum speed is 19 r/min, 30min is reacted under the conditions of 3 DEG C of maintenance system temperature, with extruder in temperature 192 DEG C of extruding pelletizations crush to get to modified SEBS;
(4), weigh 30 parts of polyethylene powders, 21 parts of modified SEBSs, 16 parts of polyvinyl alcohol, 2488,13 parts of polymethyl methacrylates and 10 parts of makrolon are added in pulverizer and crush, and transfer the material into ball mill, drum speed 21r/min, maintain body It is to react 27min under the conditions of 16 DEG C of temperature, with extruder in 199 DEG C of extruding pelletizations of temperature, crushes to get to modified poly ethylene;
(5), 90 parts of polyethylene, 22 parts of modified poly ethylenes, 24 parts of aerosils, 4.3 parts of calcium stearates are weighed to be added to In ball mill, drum speed is 28 r/min, 33min is reacted under the conditions of -2 DEG C of maintenance system temperature, with extruder in temperature 194 DEG C of extrusion moldings are to get to the polyethylene water-feeding pipes having excellent weather resistance.
Embodiment 7
A kind of polyethylene water-feeding pipes having excellent weather resistance, preparation method includes the following steps:
(1), 90 parts of tetraethyl orthosilicates, 220 parts of ethyl alcohol, 11 parts of nonionic surfactant Lutensol XP-50 and 15 parts are weighed Nonionic surfactant Lutensol XP-70 are added in reaction kettle, mixing speed 515r/min, maintenance system temperature 50min is reacted under the conditions of 31 DEG C, 20 parts of water are added to according to 0.05 part/min in reaction kettle, after the completion of to be added, in maintenance The 40min that states under reaction condition that the reaction was continued, product is transferred in hydrothermal reaction kettle, anti-under the conditions of 195 DEG C of maintenance system temperature 5.5h, product is answered to be evaporated under reduced pressure 1h through 125 DEG C, -0.08MPa, product washs 5 times through 1L EtOH Sonicates, in 75 DEG C, -0.07MPa It is dried in vacuo 15min, grinding obtains aerosil;
(2), it weighs 70 parts of nano-calcium carbonates, 62 parts of ethyl alcohol, 11 parts of water to be added in hydrothermal reaction kettle, maintenance system temperature 127 40min is reacted under the conditions of DEG C, product is dried in vacuo 9min through filtering, 56 DEG C, -0.05MPa, by product and 20 parts of hydroxy silicon oils 107 and 24 parts of hydroxy silicon oil JF-M30-203 are added in hydrothermal reaction kettle, are reacted under the conditions of 194 DEG C of maintenance system temperature 1.4h, product are dried in vacuo 11min in 70 DEG C, -0.08MPa, obtain modified Nano carbon through filtering, 2L ethyl alcohol oscillation washing 3 times Sour calcium;
(3), 80 parts of SEBS, 23 parts of ethylene propylene diene rubbers, 17 parts of polyester hot-melt adhesives and 40 parts of modified nano calcium carbonates are weighed to be added Into ball mill, drum speed 18r/min reacts 32min under the conditions of 4 DEG C of maintenance system temperature, with extruder in temperature 196 DEG C of extruding pelletizations crush to get to modified SEBS;
(4), weigh 30 parts of polyethylene powders, 22 parts of modified SEBSs, 20 parts of polyvinyl alcohol, 2488,13 parts of polymethyl methacrylates and 11 parts of makrolon are added in pulverizer and crush, and transfer the material into ball mill, drum speed 25r/min, maintain body It is to react 25min under the conditions of 14 DEG C of temperature, with extruder in 206 DEG C of extruding pelletizations of temperature, crushes to get to modified poly ethylene;
(5), 90 parts of polyethylene, 27 parts of modified poly ethylenes, 29 parts of aerosils, 3.2 parts of calcium stearates are weighed to be added to In ball mill, drum speed is 26 r/min, 38min is reacted under the conditions of -3 DEG C of maintenance system temperature, with extruder in temperature 193 DEG C of extrusion moldings are to get to the polyethylene water-feeding pipes having excellent weather resistance.
Embodiment 8
A kind of polyethylene water-feeding pipes having excellent weather resistance, preparation method includes the following steps:
(1), 90 parts of tetraethyl orthosilicates, 208 parts of ethyl alcohol, 15 parts of nonionic surfactant Lutensol XP-50 and 13 parts are weighed Nonionic surfactant Lutensol XP-70 are added in reaction kettle, mixing speed 460r/min, maintenance system temperature 50min is reacted under the conditions of 30 DEG C, 22 parts of water are added to according to 0.05 part/min in reaction kettle, after the completion of to be added, in maintenance The 40min that states under reaction condition that the reaction was continued, product is transferred in hydrothermal reaction kettle, anti-under the conditions of 196 DEG C of maintenance system temperature 3.8h, product is answered to be evaporated under reduced pressure 1h through 125 DEG C, -0.08MPa, product washs 5 times through 1L EtOH Sonicates, in 75 DEG C, -0.07MPa It is dried in vacuo 15min, grinding obtains aerosil;
(2), it weighs 70 parts of nano-calcium carbonates, 60 parts of ethyl alcohol, 14 parts of water to be added in hydrothermal reaction kettle, maintenance system temperature 123 37min is reacted under the conditions of DEG C, product is dried in vacuo 9min through filtering, 56 DEG C, -0.05MPa, by product and 22 parts of hydroxy silicon oils 107 and 17 parts of hydroxy silicon oil JF-M30-203 are added in hydrothermal reaction kettle, are reacted under the conditions of 187 DEG C of maintenance system temperature 1.6h, product are dried in vacuo 11min in 70 DEG C, -0.08MPa, obtain modified Nano carbon through filtering, 2L ethyl alcohol oscillation washing 3 times Sour calcium;
(3), 80 parts of SEBS, 21 parts of ethylene propylene diene rubbers, 17 parts of polyester hot-melt adhesives and 40 parts of modified nano calcium carbonates are weighed to be added Into ball mill, drum speed is 28 r/min, 31min is reacted under the conditions of 7 DEG C of maintenance system temperature, with extruder in temperature 195 DEG C of extruding pelletizations crush to get to modified SEBS;
(4), weigh 30 parts of polyethylene powders, 21 parts of modified SEBSs, 20 parts of polyvinyl alcohol, 2488,11 parts of polymethyl methacrylates and 13 parts of makrolon are added in pulverizer and crush, and transfer the material into ball mill, drum speed 26r/min, maintain body It is to react 29min under the conditions of 12 DEG C of temperature, with extruder in 201 DEG C of extruding pelletizations of temperature, crushes to get to modified poly ethylene;
(5), 90 parts of polyethylene, 30 parts of modified poly ethylenes, 23 parts of aerosils, 4 parts of calcium stearates are weighed and are added to ball In grinding machine, drum speed is 34 r/min, 33min is reacted under the conditions of -2 DEG C of maintenance system temperature, with extruder in temperature 192 DEG C extrusion molding is to get to the polyethylene water-feeding pipes having excellent weather resistance.
Reference examples 1
In this reference examples, aerosil is not added, other components and preparation method are same as Example 1.
Reference examples 2
In this reference examples, modified nano calcium carbonate is not added, other components and preparation method are same as Example 1.
Reference examples 3
In this reference examples, modified SEBS is not added, other components and preparation method are same as Example 1.
Reference examples 4
In this reference examples, modified poly ethylene is not added, other components and preparation method are same as Example 1.
Reference examples 5
The aerosil in general silica aeroge alternate embodiment 1 is selected in this reference examples, in formula, it is other Component is same as Example 1 with preparation method.
Reference examples 6
The modified nano calcium carbonate in common nano-calcium carbonate alternate embodiment 1, other components are selected in this reference examples, in formula It is same as Example 1 with preparation method.
Reference examples 7
Select the modified SEBS in common SEBS alternate embodiments 1 in this reference examples, in formula, other components and preparation method with Embodiment 1 is identical.
Reference examples 8
The modified poly ethylene in common polythene pellet alternate embodiment 1, other components and system are selected in this reference examples, in formula Preparation Method is same as Example 1.
Elongation at break, longitudinal direction to the polyethylene water-feeding pipes having excellent weather resistance made from Examples 1 to 8 and reference examples 1~8 The performances such as relaxation shrinkage, oxidation induction time, weatherability are tested, and test method is as follows, and test result sees below Tables 1 and 2.
The elongation at break for the polyethylene water-feeding pipes having excellent weather resistance, longitudinal welds, oxidation induction time, weatherability Etc. performances tested according to GB/T 13663-2000 standards.
The performance parameter for the polyethylene water-feeding pipes having excellent weather resistance made from 1 Examples 1 to 8 of table
The performance parameter for the polyethylene water-feeding pipes having excellent weather resistance made from 2 embodiment 1 of table and reference examples 1~8
By upper Tables 1 and 2 it is found that the tubing that various embodiments of the present invention are prepared oxidation induction performance it is more excellent, this show with There is the tubing that raw material provided by the invention is prepared preferable oxidation to induce performance;In contrast, the raw material of each reference examples The oxidation induction performance for the tubing being prepared is poor.In addition, the tubing that various embodiments of the present invention are prepared has preferably Elongation at break and longitudinal welds.
The above is the preferred embodiment of the present invention, it is noted that for those skilled in the art For, various improvements and modifications may be made without departing from the principle of the present invention, these improvements and modifications are also considered as Protection scope of the present invention.

Claims (4)

1. a kind of preparation method for the polyethylene water-feeding pipes having excellent weather resistance, it is characterised in that:Including following raw material components:It is poly- Ethylene, modified poly ethylene, aerosil, calcium stearate, the polyethylene, modified poly ethylene, silica airsetting Glue, calcium stearate quality parts ratio be 90:18~32:16~30:2~6, wherein the modified poly ethylene is by polyethylene Powder, modified SEBS, polyvinyl alcohol, polymethyl methacrylate and makrolon reaction are made, the polyethylene powder, modification SEBS, polyvinyl alcohol, polymethyl methacrylate and makrolon quality parts ratio be 30:19~27:9~22:7~16:6 ~14, the modified SEBS is reacted by SEBS, ethylene propylene diene rubber, polyester hot-melt adhesive and modified nano calcium carbonate to be made, institute The quality parts ratio of SEBS, ethylene propylene diene rubber, polyester hot-melt adhesive and the modified nano calcium carbonate stated is 80:13~25:11~ 20:35~41, the modified nano calcium carbonate is by nano-calcium carbonate, ethyl alcohol, water, hydroxy silicon oil 107 and hydroxy silicon oil JF- M30-203 reactions are made, the matter of the nano-calcium carbonate, ethyl alcohol, water, hydroxy silicon oil 107 and hydroxy silicon oil JF-M30-203 It is 70 to measure portion rate:55~67:7~15:18~27:14~25, the aerosil is by tetraethyl orthosilicate, second Alcohol, water, nonionic surfactant Lutensol XP-50 and nonionic surfactant Lutensol XP-70 reactions are made, Tetraethyl orthosilicate, ethyl alcohol, water, nonionic surfactant Lutensol XP-50 and the nonionic surfactant The quality parts ratio of Lutensol XP-70 is 90:185~225:9~23:8~19:9~17.
2. a kind of preparation method for the polyethylene water-feeding pipes having excellent weather resistance according to claim 1, it is characterised in that:Institute The polyethylene water-feeding pipes having excellent weather resistance stated are made from following preparation method:(1), by tetraethyl orthosilicate, ethyl alcohol, non- Ionic surfactant Lutensol XP-50 and nonionic surfactant Lutensol XP-70 are according to quality parts ratio 90:185~225:8~19:9~17 are added in reaction kettle, and mixing speed is 400~550r/min, maintenance system temperature 25 50min is reacted under the conditions of~33 DEG C, the water that quality parts ratio is 9~23 is added to reaction kettle according to 0.05 mass parts/min In, after the completion of to be added, product is transferred in hydrothermal reaction kettle, maintains by the 40min that maintains under above-mentioned reaction condition that the reaction was continued 2~6h is reacted under the conditions of 185~200 DEG C of system temperature, product is evaporated under reduced pressure 1h through 125 DEG C, -0.08MPa, and product is through 1L ethyl alcohol Supersound washing 5 times is dried in vacuo 15min in 75 DEG C, -0.07MPa, and grinding obtains aerosil;(2), by nano-sized carbon Sour calcium, ethyl alcohol, water are 70 according to quality parts ratio:55~67:7~15 are added in hydrothermal reaction kettle, maintenance system temperature 115 30~45min is reacted under the conditions of~128 DEG C, product is dried in vacuo 9min through filtering, 56 DEG C, -0.05MPa, by product and quality Portion rate is 18~27:14~25 hydroxy silicon oil 107 and hydroxy silicon oil JF-M30-203 is added in hydrothermal reaction kettle, is maintained Under the conditions of 175~198 DEG C of system temperature react 1~2h, product through filtering, 2L ethyl alcohol oscillation washing 3 times, in 70 DEG C ,- 0.08MPa is dried in vacuo 11min, obtains modified nano calcium carbonate;(3), by SEBS, ethylene propylene diene rubber, polyester hot-melt adhesive and Modified nano calcium carbonate is 80 according to quality parts ratio:13~25:11~20:35~41 are added in ball mill, drum speed For 15~31r/min, 21~33min is reacted under the conditions of 0~10 DEG C of maintenance system temperature, with extruder in 185~197 DEG C of temperature Extruding pelletization crushes to get to modified SEBS;(4), by polyethylene powder, modified SEBS, polyvinyl alcohol, poly-methyl methacrylate Ester and makrolon are 30 according to quality parts ratio:19~27:9~22:7~16:6~14 are added in pulverizer and crush, will Material is transferred in ball mill, and drum speed is 18~30r/min, and reaction 20 under the conditions of 10~19 DEG C of maintenance system temperature~ 35min is crushed with extruder in 195~210 DEG C of extruding pelletizations of temperature to get to modified poly ethylene;(5), by polyethylene, change Property polyethylene, aerosil, calcium stearate according to quality parts ratio be 90:18~32:16~30:2~6 are added to ball In grinding machine, drum speed is 21~38r/min, reacts 27~39min under the conditions of -5~5 DEG C of maintenance system temperature, uses extruder In 185~197 DEG C of extrusion moldings of temperature to get to the polyethylene water-feeding pipes having excellent weather resistance.
3. wanting a kind of 1 preparation method for the polyethylene water-feeding pipes having excellent weather resistance according to right, it is characterised in that:It is described Polyvinyl alcohol be polyvinyl alcohol 2488.
4. wanting a kind of 1 preparation method for the polyethylene water-feeding pipes having excellent weather resistance according to right, it is characterised in that:It is described Polyethylene be recycling grade polyethylene.
CN201810415211.XA 2018-05-03 2018-05-03 A kind of polyethylene water-feeding pipes and preparation method thereof having excellent weather resistance Withdrawn CN108570180A (en)

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WO2006062278A1 (en) * 2004-12-07 2006-06-15 Lg Chem. Ltd. Pipe having barrier property
CN101514769A (en) * 2009-01-06 2009-08-26 福建恒杰塑业新材料有限公司 Non-digging PE-specialized service tube
CN104390069A (en) * 2014-11-05 2015-03-04 广西金盛科技发展有限公司 Polyethylene water feeding pipe

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Publication number Priority date Publication date Assignee Title
WO2006062278A1 (en) * 2004-12-07 2006-06-15 Lg Chem. Ltd. Pipe having barrier property
CN101514769A (en) * 2009-01-06 2009-08-26 福建恒杰塑业新材料有限公司 Non-digging PE-specialized service tube
CN104390069A (en) * 2014-11-05 2015-03-04 广西金盛科技发展有限公司 Polyethylene water feeding pipe

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