CN111363251A - Special coloring master batch for PPR pipe and preparation method and application thereof - Google Patents

Special coloring master batch for PPR pipe and preparation method and application thereof Download PDF

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Publication number
CN111363251A
CN111363251A CN202010086272.3A CN202010086272A CN111363251A CN 111363251 A CN111363251 A CN 111363251A CN 202010086272 A CN202010086272 A CN 202010086272A CN 111363251 A CN111363251 A CN 111363251A
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pigment
ppr pipe
master batch
yellow
antioxidant
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刘鹏
雷周桥
许卫民
黎泽顺
卢俊文
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Guangdong Bosi Sci & Tech Co ltd
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Guangdong Bosi Sci & Tech Co ltd
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    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/20Compounding polymers with additives, e.g. colouring
    • C08J3/22Compounding polymers with additives, e.g. colouring using masterbatch techniques
    • C08J3/226Compounding polymers with additives, e.g. colouring using masterbatch techniques using a polymer as a carrier
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    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2323/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2323/02Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
    • C08J2323/10Homopolymers or copolymers of propene
    • C08J2323/14Copolymers of propene
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2423/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2423/02Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
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    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2423/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2423/02Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
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    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2423/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2423/02Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
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    • C08J2423/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2423/02Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
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    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2423/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2423/02Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
    • C08J2423/18Homopolymers or copolymers of hydrocarbons having four or more carbon atoms
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    • C08J2453/00Characterised by the use of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Derivatives of such polymers
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    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
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    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/20Oxides; Hydroxides
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    • C08K2003/2241Titanium dioxide
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Abstract

The invention discloses a special coloring master batch for a PPR pipe, which comprises the following components in percentage by weight: 15-70% of pigment, 20-81.4% of carrier resin, 3-6% of dispersing agent, 0.1-5% of N, N' -dicyclohexyl p-dimethylamide, 0-5% of antioxidant and 0.5-10% of nano zinc oxide. The invention also provides a preparation method and application of the special coloring master batch for the PPR pipe. The addition amount of the special coloring master batch for the PPR pipe in the PPR pipe is 1-4% of the weight of the PPR pipe. The coloring master batch special for the PPR pipe has excellent dispersion performance and easy dilution performance, can ensure that the PPR pipe product has excellent heat resistance and weather resistance, can obviously improve the low-temperature impact performance of the PPR pipe product, improves the low-temperature falling performance of the PPR pipe product, and enhances the hydrostatic pressure resistance strength and slow cracking resistance growth performance of the PPR pipe product.

Description

Special coloring master batch for PPR pipe and preparation method and application thereof
Technical Field
The invention belongs to the technical field of plastic coloring, and particularly relates to a special coloring master batch for a PPR pipe, and a preparation method and application thereof.
Background
The color master batch is a concentrate prepared by carrying a plastic additive in an extraordinary amount in resin, and when a plastic product is manufactured, the plastic additive does not need to be added, but only the corresponding master batch needs to be added. The color master batch is prepared from carrier resin, pigment and dispersant by mixing, melt extruding, and granulating to obtain granular master batch with particle size equal to that of resin. The color master batch is one of the most main forms of plastic auxiliary agent application in the world at present, has simple process and convenient use, is convenient for realizing production automation, improves the labor productivity, avoids environmental pollution and is beneficial to clean and civilized production of workers.
Compared with traditional cast iron pipes, galvanized steel pipes, cement pipes and other pipelines, the PPR pipe has the advantages of material saving, environmental protection, light weight, high strength, corrosion resistance, smooth inner wall, no scale formation, simple and convenient construction and maintenance, long service life and the like, and is widely applied to the construction industry, municipal administration, industry and agricultural field such as building water supply and drainage, urban and rural water supply and drainage, urban gas, electric power and optical cable sheaths, industrial fluid delivery, agricultural irrigation and the like. In recent years, with the increasing market demands of industries such as construction industry, municipal engineering, hydraulic engineering, agriculture and industry, the PPR pipe industry in China shows a high-speed development situation. While the output of plastic pipelines in China is increased, the quality requirements of consumers on the aspects of environmental protection, health, durability and the like of products are continuously improved. The PPR water supply pipe has special requirements on color masterbatch: 1. certain covering power; 2. the pigment has good high temperature resistance; 3. has certain weather resistance.
Patent application CN102850658A discloses a novel high-efficiency cold-resistant toughening color master batch for PPR pipes, which comprises the following raw materials in parts by weight: 5-25 parts of polypropylene, 5-50 parts of pigment, 35-65 parts of cold-resistant modifier and 1-15 parts of reinforcing modifier; the cold-resistant modifier is one or a mixture of more of a styrene-butadiene-styrene ternary block copolymer, an ethylene-vinyl acetate copolymer and an ethylene-octene copolymer, and the reinforcing modifier is one or a mixture of more of nano calcium carbonate, nano silicon and nano barium sulfate. However, the PPR pipe specified by the national standard GB18742-2017 should not contain calcium carbonate, barium sulfate and other components, and the color master batch cannot meet the technical requirements of the new national standard.
Patent application CN104059299A discloses a special coloring master batch for PPR pipes and a preparation method thereof, wherein the master batch is composed of the following raw materials in parts by weight: 40-60 parts of carrier resin, 35-55 parts of pigment, 0.5-5 parts of dispersing agent, 0.1-3 parts of antioxidant and 0.1-3 parts of antibacterial agent. The preferred pigments of the invention are titanium dioxide, carbon black and permanent yellow, although the coloring power of the permanent yellow is strong, the high temperature resistance is poor, and the color change is easy to generate in the processing process, so that the normal color of the pipe is influenced; in addition, the dispersant added in the invention is preferably polyethylene glycol 200 and polyethylene glycol 400, the polyethylene glycol is stable under general conditions, but the polyethylene glycol can react with oxygen in the air at 120 ℃ or higher, so that the dispersion effect of the polyethylene glycol is lost, and the coloring master batch of the invention still cannot solve the existing problems such as: poor light-shielding property, poor dispersibility, easy color change and uneven inner surface to store dirt and dirty.
Patent application CN104497424A discloses a coloring master batch for a PPR pipe and a preparation method thereof, wherein the master batch comprises the following raw materials in percentage by mass: 50-65% of rutile titanium dioxide, 28-40% of PPR resin, 3.9-9% of iron oxide red, 1.0-1.5% of titanium yellow, 0.1-0.5% of carbon black and 0.5-1.5% of polysiloxane; the rutile titanium dioxide has the average particle size of 0.2-0.25 mu m and the refractive index of 2.7, has strong covering power and strong ultraviolet absorption capacity, and can resist the temperature of 300 ℃; the carbon black is pigment carbon black with the average particle size of 10-27 nm produced by a tank method. The coloring master batch disclosed by the invention adopts PPR4220 or PPR2400 as a carrier, so that the melt index is low and the low-temperature falling performance is poor.
Disclosure of Invention
The invention aims to solve the problems of low-temperature drop, poor weather resistance, poor heat resistance and poor dispersibility of the color masterbatch for the PPR pipe in the prior art, and provides the special coloring masterbatch for the PPR pipe. The coloring master batch has good processability and weather resistance, and can meet the requirements of PPR pipe manufacturers.
The invention also aims to provide a preparation method of the special coloring master batch for the PPR pipe.
The invention further aims to provide application of the special coloring master batch for the PPR pipe.
The purpose of the invention is realized by the following technical scheme: the special coloring master batch for the PPR pipe comprises the following components in percentage by weight: 15-70% of pigment, 20-81.4% of carrier resin, 3-6% of dispersing agent, 0.1-5% of N, N' -dicyclohexyl p-dimethylamide, 0-5% of antioxidant and 0.5-10% of nano zinc oxide.
Further, the pigment is an inorganic pigment or/and an organic pigment.
Further, the inorganic pigment is one or a mixture of at least two of rutile titanium dioxide, carbon black, aluminum powder, copper powder, pearl powder, iron oxide red, iron oxide black, iron oxide brown and metal composite inorganic pigments.
Further, the metal composite inorganic pigment is one or a mixture of at least two of pigment yellow 53, pigment yellow 119, pigment yellow 161, pigment yellow 164, pigment yellow 189, pigment brown 24, pigment brown 29, pigment brown 48, pigment blue 28, pigment green 50, pigment violet 47 and pigment black 26.
Further, the organic pigment is pigment yellow 62, pigment yellow 93, pigment yellow 95, pigment yellow 109, pigment yellow 110, pigment yellow 138, pigment yellow 151, pigment yellow 155, pigment yellow 168, pigment yellow 180, pigment yellow 181, pigment yellow 183, pigment yellow 191:1, pigment yellow 214, pigment yellow 215, pigment orange 43, pigment orange 61, pigment orange 64, pigment orange 68, pigment orange 72, pigment orange 73, pigment orange 79, pigment red 122, pigment red 149, pigment red 166, pigment red 170, pigment red 175, pigment red 176, pigment red 177, pigment red 178, pigment red 179, pigment red 185, pigment red 187, pigment red 202, pigment red 220, pigment red 254, pigment red 264, pigment violet 19, pigment violet 23, pigment violet 29, pigment blue 15:1, pigment blue 15:3, pigment blue 15:4, pigment green 7 and pigment green 36.
The pigments used herein have excellent heat, light, weather and chemical resistance.
Further, the carrier resin is one or a mixture of at least two of polypropylene, polyethylene, ethylene propylene copolymer and polyisobutylene.
Further, the polypropylene is block copolymerization polypropylene, random copolymerization polypropylene or homopolymerization polypropylene.
Further, the dispersing agent is one or a mixture of at least two of calcium stearate, calcium heptanedionate stearate, pentaerythritol calcium stearate, lanthanum stearate and pentaerythritol lanthanum stearate. The dispersant can improve the impact resistance and toughness of the PPR pipe while providing pigment dispersion performance, and particularly has more remarkable synergistic effect when the dispersant and N, N' -dicyclohexyl are compounded on the dimethylamide.
Further, the antioxidant is one or a mixture of at least two of antioxidant P-EPQ (tetrakis (2, 4-di-tert-butylphenol) -4,4' -biphenyldiphosphite), antioxidant 3114 (tris (3, 5-di-tert-butyl-4-hydroxybenzyl) isocyanate), antioxidant CPL (P-cresol and dicyclopentadiene copolymer), antioxidant 1330(1,3, 5-trimethyl-2, 4, 6-tris (3, 5-di-tert-butyl-4-hydroxybenzyl) benzene), antioxidant 1790(1,3, 5-tris (4-tert-butyl-3-hydroxy-2, 6-dimethylbenzyl) -1, 3, 5-triazine-2, 4,6- (1H,3H,5H) -trione), antioxidant 4120 (pentaerythritol tetrakis (3-laurylthiopropionate)) . The antioxidant has excellent antioxidant effect and excellent water extraction resistance, and can reduce the water pollution of the antioxidant while ensuring the excellent ageing resistance of the PPR product.
On the other hand, the preparation method of the special coloring master batch for the PPR pipe comprises the following steps:
A. adding 15-70% of pigment, 20-81.4% of carrier resin, 3-6% of dispersing agent, 0.1-5% of N, N' -dicyclohexyl terephthalamide, 0-5% of antioxidant and 0.5-10% of nano zinc oxide into a mixer for mixing to obtain a mixture, and discharging when the temperature of the mixture is 100 ℃ plus 120 ℃; the percentages are weight percentages;
B. transferring the mixture obtained in the step A to a double-screw extruder, carrying out melt extrusion, cooling and granulating to obtain a special coloring master batch for the PPR pipe; the extrusion temperature of the double-screw extruder is 150-230 ℃, and the screw rotating speed is 400-900 rpm.
The special coloring master batch for the PPR pipe is mainly applied to the fields of building industry, municipal administration, industry and agriculture, such as building water supply and drainage, urban and rural water supply and drainage, urban gas, electric power and optical cable sheaths, industrial fluid delivery, agricultural irrigation and the like.
The additive amount of the special coloring master batch for the PPR pipe in the PPR pipe is 1% -4% of the weight of the PPR pipe, and the preferable additive amount is 1.5% -2% of the weight of the PPR pipe.
Compared with the prior art, the invention has the following advantages and effects:
1) the special coloring master batch for the PPR pipe has excellent dispersing performance and easy dilutability.
2) The special coloring master batch for the PPR pipe enables the PPR pipe product to have excellent heat resistance and weather resistance.
3) The special coloring master batch for the PPR pipe can obviously improve the low-temperature impact property of the PPR pipe product, improve the low-temperature drop property of the PPR pipe material, and enhance the hydrostatic strength resistance and slow crack growth resistance of the PPR pipe material.
Detailed Description
The present invention will be described in further detail with reference to examples, but the embodiments of the present invention are not limited thereto.
Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this application belongs. The terminology used herein in the description is for the purpose of describing particular embodiments only and is not intended to be limiting of the application.
In this application, all materials are commercially available unless otherwise specified. As used herein, unless otherwise indicated, "percent" or "%" refers to weight percent of all components.
In this application, the word "about" or "approximately" means within an acceptable range for the specified particular parameter as determined by one of ordinary skill in the art, which will depend in part on the manner in which the value is measured or determined, i.e., the limits of the measurement system. For example, "about" may refer to a range of up to 10% of a given value.
The invention provides a special coloring master batch for a PPR pipe, which comprises the following components in percentage by weight: 15-70% of pigment, 20-81.4% of carrier resin, 3-6% of dispersing agent, 0.1-5% of N, N' -dicyclohexyl p-dimethylamide, 0-5% of antioxidant and 0.5-10% of nano zinc oxide.
Further, the pigment is an inorganic pigment or/and an organic pigment.
Further, the inorganic pigment is one or a mixture of at least two of rutile titanium dioxide, carbon black, aluminum powder, copper powder, pearl powder, iron oxide red, iron oxide black, iron oxide brown and metal composite inorganic pigments.
Further, the metal composite inorganic pigment is one or a mixture of at least two of pigment yellow 53, pigment yellow 119, pigment yellow 161, pigment yellow 164, pigment yellow 189, pigment brown 24, pigment brown 29, pigment brown 48, pigment blue 28, pigment green 50, pigment violet 47 and pigment black 26.
Further, the organic pigment is pigment yellow 62, pigment yellow 93, pigment yellow 95, pigment yellow 109, pigment yellow 110, pigment yellow 138, pigment yellow 151, pigment yellow 155, pigment yellow 168, pigment yellow 180, pigment yellow 181, pigment yellow 183, pigment yellow 191:1, pigment yellow 214, pigment yellow 215, pigment orange 43, pigment orange 61, pigment orange 64, pigment orange 68, pigment orange 72, pigment orange 73, pigment orange 79, pigment red 122, pigment red 149, pigment red 166, pigment red 170, pigment red 175, pigment red 176, pigment red 177, pigment red 178, pigment red 179, pigment red 185, pigment red 187, pigment red 202, pigment red 220, pigment red 254, pigment red 264, pigment violet 19, pigment violet 23, pigment violet 29, pigment blue 15:1, pigment blue 15:3, pigment blue 15:4, pigment green 7 and pigment green 36.
The pigments used herein have excellent heat, light, weather and chemical resistance.
Further, the carrier resin is one or a mixture of at least two of polypropylene, polyethylene, ethylene propylene copolymer and polyisobutylene.
Further, the polypropylene is block copolymerization polypropylene, random copolymerization polypropylene or homopolymerization polypropylene.
Further, the dispersing agent is one or a mixture of at least two of calcium stearate, calcium heptanedionate stearate, pentaerythritol calcium stearate, lanthanum stearate and pentaerythritol lanthanum stearate. The dispersant can improve the impact resistance and toughness of the PPR pipe while providing pigment dispersion performance, and particularly has more remarkable synergistic effect when the dispersant and N, N' -dicyclohexyl are compounded on the dimethylamide.
Further, the antioxidant is one or a mixture of at least two of antioxidant P-EPQ (tetrakis (2, 4-di-tert-butylphenol) -4,4' -biphenyldiphosphite), antioxidant 3114 (tris (3, 5-di-tert-butyl-4-hydroxybenzyl) isocyanate), antioxidant CPL (P-cresol and dicyclopentadiene copolymer), antioxidant 1330(1,3, 5-trimethyl-2, 4, 6-tris (3, 5-di-tert-butyl-4-hydroxybenzyl) benzene), antioxidant 1790(1,3, 5-tris (4-tert-butyl-3-hydroxy-2, 6-dimethylbenzyl) -1, 3, 5-triazine-2, 4,6- (1H,3H,5H) -trione), antioxidant 4120 (pentaerythritol tetrakis (3-laurylthiopropionate)) . The antioxidant has excellent antioxidant effect and excellent water extraction resistance, and can reduce the water pollution of the antioxidant while ensuring the excellent ageing resistance of the PPR product.
On the other hand, the preparation method of the special coloring master batch for the PPR pipe comprises the following steps:
A. adding 15-70% of pigment, 20-81.4% of carrier resin, 3-6% of dispersing agent, 0.1-5% of N, N' -dicyclohexyl terephthalamide, 0-5% of antioxidant and 0.5-10% of nano zinc oxide into a mixer for mixing to obtain a mixture, and discharging when the temperature of the mixture is 100 ℃ plus 120 ℃; the percentages are weight percentages;
B. transferring the mixture obtained in the step A to a double-screw extruder, carrying out melt extrusion, cooling and granulating to obtain a special coloring master batch for the PPR pipe; the extrusion temperature of the double-screw extruder is 150-230 ℃, and the screw rotating speed is 400-900 rpm.
The special coloring master batch for the PPR pipe is mainly applied to the fields of building industry, municipal administration, industry and agriculture, such as building water supply and drainage, urban and rural water supply and drainage, urban gas, electric power and optical cable sheaths, industrial fluid delivery, agricultural irrigation and the like.
The additive amount of the special coloring master batch for the PPR pipe in the PPR pipe is 1% -4% of the weight of the PPR pipe, and the preferable additive amount is 1.5% -2% of the weight of the PPR pipe.
The coloring master batch special for the PPR pipe has excellent dispersion performance and easy dilution performance, can ensure that the PPR pipe product has excellent heat resistance and weather resistance, can obviously improve the low-temperature impact performance of the PPR pipe product, improves the low-temperature falling performance of the PPR pipe product, and enhances the hydrostatic strength resistance and the slow cracking growth resistance of the PPR pipe product.
Example 1
40% of rutile titanium dioxide, 5% of phthalocyanine blue, 1835% of pigment yellow, 1% of carbon black, 3% of calcium pimelate stearate, 3% of lanthanum pentaerythrite stearate, 23% of polyethylene, 5% of N, N' -dicyclohexyl terephthalamide, 13301% of antioxidant, 1% of antioxidant P-EPQ, 31141% of antioxidant, 17901% of antioxidant, 41201% of antioxidant and 10% of nano zinc oxide. Adding the raw materials into a high-speed mixer, mixing at high speed, transferring the mixed materials into a double-screw extruder (extrusion temperature: 150 ℃, screw rotation speed 400rpm) after the temperature of the materials reaches 100 ℃, melting, granulating, drying and packaging to obtain the color master batch.
Example 2
15% of carbon black, 3% of calcium heptanedioate stearate, 40% of block copolymerization polypropylene carrier resin, 41.4% of random copolymerization polypropylene carrier resin, 0.1% of N, N' -dicyclohexyl p-dimethylamide and 0.5% of nano zinc oxide. Adding the raw materials into a high-speed mixer, mixing at high speed, transferring the mixed materials into a double-screw extruder (extrusion temperature: 200 ℃, screw rotation speed 900rpm) after the temperature of the materials reaches 120 ℃, melting, granulating, drying and packaging to obtain the color master batch.
Example 3
15% of rutile titanium dioxide, 10% of gold pearl powder, 6410% of pigment orange, 2% of lanthanum stearate, 3% of lanthanum heptastearate, 27% of homopolymerized polypropylene carrier resin, 8% of ethylene-propylene copolymer, 13% of polyisobutylene, 13302% of antioxidant, P-EPQ 3% of antioxidant, 2% of N, N' -dicyclohexyl P-dimethylamide and 5% of nano zinc oxide. Adding the raw materials into a high-speed mixer, mixing at high speed, transferring the mixed materials into a double-screw extruder (extrusion temperature: 210 ℃, screw rotation speed 600rpm) after the temperature of the materials reaches 110 ℃, melting, granulating, drying and packaging to obtain the color master batch.
Comparative examples
40% of rutile type titanium dioxide, 5% of phthalocyanine blue, 1835% of pigment yellow, 1% of carbon black, 6% of polyethylene wax, 38% of polyethylene, 13301% of antioxidant, 1% of antioxidant P-EPQ, 31141% of antioxidant, 17901% of antioxidant and 41201% of antioxidant. Adding the raw materials into a high-speed mixer, mixing at high speed, transferring the mixed materials into a double-screw extruder (extrusion temperature: 150 ℃, screw rotation speed 400rpm) after the temperature of the materials reaches 100 ℃, melting, granulating, drying and packaging to obtain the color master batch.
The examples and comparative examples were tested as follows, with the masterbatch and PPR being added at 2%. The test results are shown in Table 1.
(1) Dispersing Properties
The dispersion of the pigment or carbon black in the polyolefin pipes, pipes and compounding materials was determined according to the method of GB/T18251-.
(2) Evaluation of Heat-resistant color Difference
Uniformly mixing the prepared coloring master batch with PPR resin; 20 plates were injected consecutively at 230 ℃. The average L, a, b values (symbols L0, a0, b0) were measured as standards, and then the average L, a, b values (symbols L1, a1, b1) were measured by continuously injection molding 3 plates at 200 ℃ for 5 min. Heat-resistant color difference [ (L1-L0)2+(a1-a0)2+(b1-b0)2]1/2
(3) Evaluation of Weathering color difference
According to the standard GB/T16422.2-2014 Plastic laboratory light source exposure test method part 2: xenon arc lamps testing.
(4) Impact performance
Part 1 of the test of the impact performance of the plastic simple supported beam according to the standard GB/T1043.1-2008: non-instrumented impact test.
(5) Antibacterial property
The test was carried out according to the standard "test for antibacterial activity and effect of JIS Z2801-.
TABLE 1
Detecting items Example 1 Example 2 Example 3 Comparative example 1
Dispersibility Level 1 Stage 2 Level 1 Grade 3
Heat resistant color difference 0.51 0.3 0.4 0.6
Weatherproof color difference 1.01 0.47 1.23 1.87
Notched impact (23 ℃ C.) 65.4 43.9 58.6 39.3
Notched impact (-20 ℃ C.) 9.41 5.54 7.92 4.58
Antibacterial property 99.9% 93.4% 99.0% 0%
The experimental result shows that the coloring master batch prepared by the method is obviously superior to a comparative example in the aspects of dispersing performance, weather-proof and heat-resistant performance and low-temperature impact performance, and the coloring master batch prepared by the method also provides excellent antibacterial performance.
The above embodiments are preferred embodiments of the present invention, but the present invention is not limited to the above embodiments, and any other changes, modifications, substitutions, combinations, and simplifications which do not depart from the spirit and principle of the present invention should be construed as equivalents thereof, and all such changes, modifications, substitutions, combinations, and simplifications are intended to be included in the scope of the present invention.

Claims (10)

1. The special coloring master batch for the PPR pipe is characterized by comprising the following components in percentage by weight: 15-70% of pigment, 20-81.4% of carrier resin, 3-6% of dispersing agent, 0.1-5% of N, N' -dicyclohexyl p-dimethylamide, 0-5% of antioxidant and 0.5-10% of nano zinc oxide.
2. The special color masterbatch for PPR pipe according to claim 1, wherein the pigment is inorganic pigment or/and organic pigment.
3. The special color masterbatch for PPR pipe as claimed in claim 2, wherein the inorganic pigment is one or a mixture of at least two of rutile titanium dioxide, carbon black, aluminum powder, copper powder, pearl powder, iron oxide red, iron oxide black, iron oxide brown and metal composite inorganic pigments.
4. The special coloring master batch for the PPR pipe as claimed in claim 3, wherein the metal composite inorganic pigment is one or a mixture of at least two of pigment yellow 53, pigment yellow 119, pigment yellow 161, pigment yellow 164, pigment yellow 189, pigment brown 24, pigment brown 29, pigment brown 48, pigment blue 28, pigment green 50, pigment violet 47 and pigment black 26.
5. The special coloring master batch for the PPR tube as claimed in claim 2, wherein the organic pigment is pigment yellow 62, pigment yellow 93, pigment yellow 95, pigment yellow 109, pigment yellow 110, pigment yellow 138, pigment yellow 151, pigment yellow 155, pigment yellow 168, pigment yellow 180, pigment yellow 181, pigment yellow 183, pigment yellow 191:1, pigment yellow 214, pigment yellow 215, pigment orange 43, pigment orange 61, pigment orange 64, pigment orange 68, pigment orange 72, pigment orange 73, pigment orange 79, pigment red 122, pigment red 149, pigment red 166, pigment red 170, pigment red 175, pigment red 176, pigment red 177, pigment red 178, pigment red 179, pigment red 185, pigment red 187, pigment red 202, pigment red 220, pigment red 254, pigment red 264, pigment violet 19, pigment violet 23, pigment violet 29, pigment blue 15:1, pigment blue 15:3, pigment blue 15:4, One or a mixture of at least two of pigment green 7 and pigment green 36.
6. The special color masterbatch for PPR pipe as claimed in claim 1, wherein the carrier resin is one or a mixture of at least two of polypropylene, polyethylene, ethylene propylene copolymer and polyisobutylene.
7. The special coloring master batch for the PPR pipe as claimed in claim 6, wherein the polypropylene is block co-polypropylene, random co-polypropylene or homo-polypropylene.
8. The special color masterbatch for PPR pipe as claimed in claim 1, wherein the dispersant is one or a mixture of at least two of calcium stearate, calcium pimelic stearate, calcium pentaerythritol stearate, lanthanum stearate and lanthanum pentaerythritol stearate; the antioxidant is one or a mixture of at least two of antioxidant P-EPQ, antioxidant 3114, antioxidant CPL, antioxidant 1330, antioxidant 1790 and antioxidant 4120.
9. The method for preparing the special coloring master batch for the PPR pipe, which is described in any one of claims 1 to 8, is characterized by comprising the following steps:
A. adding 15-70% of pigment, 20-81.4% of carrier resin, 3-6% of dispersing agent, 0.1-5% of N, N' -dicyclohexyl terephthalamide, 0-5% of antioxidant and 0.5-10% of nano zinc oxide into a mixer for mixing to obtain a mixture, and discharging when the temperature of the mixture is 100 ℃ plus 120 ℃; the percentages are weight percentages;
B. transferring the mixture obtained in the step A to a double-screw extruder, carrying out melt extrusion, cooling and granulating to obtain a special coloring master batch for the PPR pipe; the extrusion temperature of the double-screw extruder is 150-230 ℃, and the screw rotating speed is 400-900 rpm.
10. The use of the colored masterbatch for PPR pipe as claimed in any one of claims 1 to 8 in the fields of construction water supply and drainage, urban and rural water supply and drainage, urban gas, electric and optical cable sheathing, industrial fluid transport, and agricultural irrigation; the addition amount of the special coloring master batch for the PPR pipe in the PPR pipe is 1-4% of the weight of the PPR pipe.
CN202010086272.3A 2020-02-11 2020-02-11 Special coloring master batch for PPR pipe and preparation method and application thereof Pending CN111363251A (en)

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Application publication date: 20200703