CN104629195B - A kind of hot water pipe polybutene alloy PP Pipe Compound and preparation method thereof - Google Patents
A kind of hot water pipe polybutene alloy PP Pipe Compound and preparation method thereof Download PDFInfo
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- CN104629195B CN104629195B CN201510081974.1A CN201510081974A CN104629195B CN 104629195 B CN104629195 B CN 104629195B CN 201510081974 A CN201510081974 A CN 201510081974A CN 104629195 B CN104629195 B CN 104629195B
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- Prior art keywords
- polybutene
- hot
- parts
- cold water
- water pipes
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- 229920001083 polybutene Polymers 0.000 title claims abstract description 65
- 239000000956 alloy Substances 0.000 title claims abstract description 47
- 229910045601 alloy Inorganic materials 0.000 title claims abstract description 46
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 29
- 238000002360 preparation method Methods 0.000 title abstract description 7
- 150000001875 compounds Chemical class 0.000 title description 3
- 239000000463 material Substances 0.000 claims abstract description 48
- 239000003963 antioxidant agent Substances 0.000 claims abstract description 19
- 230000003078 antioxidant effect Effects 0.000 claims abstract description 18
- 239000002667 nucleating agent Substances 0.000 claims abstract description 12
- 239000006096 absorbing agent Substances 0.000 claims abstract description 10
- 239000004611 light stabiliser Substances 0.000 claims abstract description 9
- 239000004595 color masterbatch Substances 0.000 claims abstract description 8
- 229910052736 halogen Inorganic materials 0.000 claims abstract description 8
- 150000002367 halogens Chemical class 0.000 claims abstract description 8
- 239000004743 Polypropylene Substances 0.000 claims description 37
- -1 polypropylene Polymers 0.000 claims description 33
- 229920001155 polypropylene Polymers 0.000 claims description 32
- 229920005989 resin Polymers 0.000 claims description 22
- 239000011347 resin Substances 0.000 claims description 22
- 238000000034 method Methods 0.000 claims description 8
- 239000000155 melt Substances 0.000 claims description 6
- UEZVMMHDMIWARA-UHFFFAOYSA-M phosphonate Chemical compound [O-]P(=O)=O UEZVMMHDMIWARA-UHFFFAOYSA-M 0.000 claims description 5
- 239000004698 Polyethylene Substances 0.000 claims description 4
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 4
- FQUNFJULCYSSOP-UHFFFAOYSA-N bisoctrizole Chemical compound N1=C2C=CC=CC2=NN1C1=CC(C(C)(C)CC(C)(C)C)=CC(CC=2C(=C(C=C(C=2)C(C)(C)CC(C)(C)C)N2N=C3C=CC=CC3=N2)O)=C1O FQUNFJULCYSSOP-UHFFFAOYSA-N 0.000 claims description 4
- 229920000573 polyethylene Polymers 0.000 claims description 4
- 239000002270 dispersing agent Substances 0.000 claims description 3
- FMZUHGYZWYNSOA-VVBFYGJXSA-N (1r)-1-[(4r,4ar,8as)-2,6-diphenyl-4,4a,8,8a-tetrahydro-[1,3]dioxino[5,4-d][1,3]dioxin-4-yl]ethane-1,2-diol Chemical group C([C@@H]1OC(O[C@@H]([C@@H]1O1)[C@H](O)CO)C=2C=CC=CC=2)OC1C1=CC=CC=C1 FMZUHGYZWYNSOA-VVBFYGJXSA-N 0.000 claims description 2
- GHKOFFNLGXMVNJ-UHFFFAOYSA-N Didodecyl thiobispropanoate Chemical compound CCCCCCCCCCCCOC(=O)CCSCCC(=O)OCCCCCCCCCCCC GHKOFFNLGXMVNJ-UHFFFAOYSA-N 0.000 claims description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 2
- 239000002202 Polyethylene glycol Substances 0.000 claims description 2
- 229920011250 Polypropylene Block Copolymer Polymers 0.000 claims description 2
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims description 2
- 150000001412 amines Chemical class 0.000 claims description 2
- 230000003712 anti-aging effect Effects 0.000 claims description 2
- 239000012965 benzophenone Substances 0.000 claims description 2
- 150000008366 benzophenones Chemical class 0.000 claims description 2
- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical compound [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 claims description 2
- 235000013539 calcium stearate Nutrition 0.000 claims description 2
- 239000008116 calcium stearate Substances 0.000 claims description 2
- 239000003795 chemical substances by application Substances 0.000 claims description 2
- 150000001470 diamides Chemical class 0.000 claims description 2
- 229940087101 dibenzylidene sorbitol Drugs 0.000 claims description 2
- PWWSSIYVTQUJQQ-UHFFFAOYSA-N distearyl thiodipropionate Chemical compound CCCCCCCCCCCCCCCCCCOC(=O)CCSCCC(=O)OCCCCCCCCCCCCCCCCCC PWWSSIYVTQUJQQ-UHFFFAOYSA-N 0.000 claims description 2
- 239000008187 granular material Substances 0.000 claims description 2
- 239000004615 ingredient Substances 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 claims description 2
- 239000000049 pigment Substances 0.000 claims description 2
- 229920001223 polyethylene glycol Polymers 0.000 claims description 2
- 239000011591 potassium Substances 0.000 claims description 2
- 229910052700 potassium Inorganic materials 0.000 claims description 2
- 239000002994 raw material Substances 0.000 claims description 2
- 239000011734 sodium Substances 0.000 claims description 2
- 229910052708 sodium Inorganic materials 0.000 claims description 2
- RYYKJJJTJZKILX-UHFFFAOYSA-M sodium octadecanoate Chemical compound [Na+].CCCCCCCCCCCCCCCCCC([O-])=O RYYKJJJTJZKILX-UHFFFAOYSA-M 0.000 claims description 2
- LVEOKSIILWWVEO-UHFFFAOYSA-N tetradecyl 3-(3-oxo-3-tetradecoxypropyl)sulfanylpropanoate Chemical compound CCCCCCCCCCCCCCOC(=O)CCSCCC(=O)OCCCCCCCCCCCCCC LVEOKSIILWWVEO-UHFFFAOYSA-N 0.000 claims description 2
- 239000004408 titanium dioxide Substances 0.000 claims description 2
- XOOUIPVCVHRTMJ-UHFFFAOYSA-L zinc stearate Chemical compound [Zn+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O XOOUIPVCVHRTMJ-UHFFFAOYSA-L 0.000 claims description 2
- CTPBWPYKMGMLGS-CIAFKFPVSA-N (3s,4s,5s,6r)-1,8-bis(4-methylphenyl)octa-1,7-diene-2,3,4,5,6,7-hexol Chemical compound C1=CC(C)=CC=C1C=C(O)[C@@H](O)[C@@H](O)[C@H](O)[C@@H](O)C(O)=CC1=CC=C(C)C=C1 CTPBWPYKMGMLGS-CIAFKFPVSA-N 0.000 claims 1
- KGRVJHAUYBGFFP-UHFFFAOYSA-N 2,2'-Methylenebis(4-methyl-6-tert-butylphenol) Chemical compound CC(C)(C)C1=CC(C)=CC(CC=2C(=C(C=C(C)C=2)C(C)(C)C)O)=C1O KGRVJHAUYBGFFP-UHFFFAOYSA-N 0.000 claims 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims 1
- 229910052782 aluminium Inorganic materials 0.000 claims 1
- 238000002156 mixing Methods 0.000 abstract description 8
- 230000006353 environmental stress Effects 0.000 abstract description 5
- 239000002861 polymer material Substances 0.000 abstract description 3
- 230000000052 comparative effect Effects 0.000 description 13
- 239000000203 mixture Substances 0.000 description 12
- 239000013078 crystal Substances 0.000 description 7
- 238000009472 formulation Methods 0.000 description 6
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 5
- 229920001577 copolymer Polymers 0.000 description 5
- 238000001125 extrusion Methods 0.000 description 5
- 238000005469 granulation Methods 0.000 description 5
- 230000003179 granulation Effects 0.000 description 5
- 238000011056 performance test Methods 0.000 description 4
- 238000002464 physical blending Methods 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 238000012360 testing method Methods 0.000 description 4
- 238000005452 bending Methods 0.000 description 3
- 239000011159 matrix material Substances 0.000 description 3
- 230000005501 phase interface Effects 0.000 description 3
- 238000006116 polymerization reaction Methods 0.000 description 3
- 239000004640 Melamine resin Substances 0.000 description 2
- 229920000877 Melamine resin Polymers 0.000 description 2
- 239000005062 Polybutadiene Substances 0.000 description 2
- IAQRGUVFOMOMEM-UHFFFAOYSA-N butene Natural products CC=CC IAQRGUVFOMOMEM-UHFFFAOYSA-N 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 239000003484 crystal nucleating agent Substances 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229920001971 elastomer Polymers 0.000 description 2
- 238000011065 in-situ storage Methods 0.000 description 2
- 229920002857 polybutadiene Polymers 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 229920005629 polypropylene homopolymer Polymers 0.000 description 2
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 2
- 239000011342 resin composition Substances 0.000 description 2
- 230000009466 transformation Effects 0.000 description 2
- HDUNAIVOFOKALD-RLCYQCIGSA-N (1s,2s)-1-[(4r)-2-(4-methylphenyl)-1,3-dioxolan-4-yl]-2-[(4s)-2-(4-methylphenyl)-1,3-dioxolan-4-yl]ethane-1,2-diol Chemical compound C1=CC(C)=CC=C1C1O[C@@H]([C@@H](O)[C@H](O)[C@H]2OC(OC2)C=2C=CC(C)=CC=2)CO1 HDUNAIVOFOKALD-RLCYQCIGSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 239000004594 Masterbatch (MB) Substances 0.000 description 1
- JKIJEFPNVSHHEI-UHFFFAOYSA-N Phenol, 2,4-bis(1,1-dimethylethyl)-, phosphite (3:1) Chemical compound CC(C)(C)C1=CC(C(C)(C)C)=CC=C1OP(OC=1C(=CC(=CC=1)C(C)(C)C)C(C)(C)C)OC1=CC=C(C(C)(C)C)C=C1C(C)(C)C JKIJEFPNVSHHEI-UHFFFAOYSA-N 0.000 description 1
- BGYHLZZASRKEJE-UHFFFAOYSA-N [3-[3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoyloxy]-2,2-bis[3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoyloxymethyl]propyl] 3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoate Chemical compound CC(C)(C)C1=C(O)C(C(C)(C)C)=CC(CCC(=O)OCC(COC(=O)CCC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)(COC(=O)CCC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)COC(=O)CCC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)=C1 BGYHLZZASRKEJE-UHFFFAOYSA-N 0.000 description 1
- NCPIYHBOLXSJJR-UHFFFAOYSA-H [Al+3].[Al+3].[O-]P([O-])=O.[O-]P([O-])=O.[O-]P([O-])=O Chemical compound [Al+3].[Al+3].[O-]P([O-])=O.[O-]P([O-])=O.[O-]P([O-])=O NCPIYHBOLXSJJR-UHFFFAOYSA-H 0.000 description 1
- 239000006230 acetylene black Substances 0.000 description 1
- 150000004645 aluminates Chemical class 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229920001400 block copolymer Polymers 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000000806 elastomer Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 229920001903 high density polyethylene Polymers 0.000 description 1
- 239000004700 high-density polyethylene Substances 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 159000000003 magnesium salts Chemical class 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 238000010899 nucleation Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 229920001384 propylene homopolymer Polymers 0.000 description 1
- 239000005060 rubber Substances 0.000 description 1
- 230000035945 sensitivity Effects 0.000 description 1
- 150000004760 silicates Chemical class 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 239000004711 α-olefin Substances 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions 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
- C08L23/18—Homopolymers or copolymers of hydrocarbons having four or more carbon atoms
- C08L23/20—Homopolymers or copolymers of hydrocarbons having four or more carbon atoms having four to nine carbon atoms
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B9/00—Making granules
- B29B9/02—Making granules by dividing preformed material
- B29B9/06—Making granules by dividing preformed material in the form of filamentary material, e.g. combined with extrusion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/92—Measuring, controlling or regulating
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/20—Compounding polymers with additives, e.g. colouring
- C08J3/22—Compounding polymers with additives, e.g. colouring using masterbatch techniques
- C08J3/226—Compounding polymers with additives, e.g. colouring using masterbatch techniques using a polymer as a carrier
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
- F16L—PIPES; JOINTS OR FITTINGS FOR PIPES; SUPPORTS FOR PIPES, CABLES OR PROTECTIVE TUBING; MEANS FOR THERMAL INSULATION IN GENERAL
- F16L9/00—Rigid pipes
- F16L9/12—Rigid pipes of plastics with or without reinforcement
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/9258—Velocity
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/92704—Temperature
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
- C08J2323/02—Characterised 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
- C08J2323/18—Homopolymers or copolymers of hydrocarbons having four or more carbon atoms
- C08J2323/20—Homopolymers or copolymers of hydrocarbons having four or more carbon atoms having four to nine carbon atoms
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- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2423/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
- C08J2423/02—Characterised 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
- C08J2423/18—Homopolymers or copolymers of hydrocarbons having four or more carbon atoms
- C08J2423/20—Homopolymers or copolymers of hydrocarbons having four or more carbon atoms having four to nine carbon atoms
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- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K2201/00—Specific properties of additives
- C08K2201/014—Additives containing two or more different additives of the same subgroup in C08K
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- C08L2201/00—Properties
- C08L2201/08—Stabilised against heat, light or radiation or oxydation
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- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2203/00—Applications
- C08L2203/18—Applications used for pipes
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2205/00—Polymer mixtures characterised by other features
- C08L2205/02—Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group
- C08L2205/025—Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group containing two or more polymers of the same hierarchy C08L, and differing only in parameters such as density, comonomer content, molecular weight, structure
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- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2205/00—Polymer mixtures characterised by other features
- C08L2205/03—Polymer mixtures characterised by other features containing three or more polymers in a blend
- C08L2205/035—Polymer 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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- C08L2205/00—Polymer mixtures characterised by other features
- C08L2205/24—Crystallisation aids
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- C08L2207/00—Properties characterising the ingredient of the composition
- C08L2207/02—Heterophasic composition
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- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2207/00—Properties characterising the ingredient of the composition
- C08L2207/10—Peculiar tacticity
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- C08L2207/00—Properties characterising the ingredient of the composition
- C08L2207/10—Peculiar tacticity
- C08L2207/14—Amorphous or atactic polypropylene
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
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- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- General Engineering & Computer Science (AREA)
- Rigid Pipes And Flexible Pipes (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
本发明涉及一种冷热水管用聚丁烯合金管材专用料及其制备方法,属于高分子材料领域。其组分包括聚丁烯合金、抗氧剂、吸卤素剂、光稳定剂、色母料、成核剂;制备方法是将聚丁烯合金、抗氧剂、吸卤素剂、光稳定剂、成核剂和色母料采用高速搅拌混合机混合均匀,经挤出造粒,得到冷热水管用聚丁烯合金管材专用料。该聚丁烯合金管材专用料在保持聚丁烯抗冲击性能、优异的耐环境应力开裂性和耐热蠕变性的基础上,拉伸强度、弯曲模量有大幅的提高,可以作为冷热水管材及管件材料使用。The invention relates to a special polybutene alloy pipe material for hot and cold water pipes and a preparation method thereof, belonging to the field of polymer materials. Its components include polybutene alloy, antioxidant, halogen absorbing agent, light stabilizer, color masterbatch, and nucleating agent; the preparation method is to mix polybutene alloy, antioxidant, halogen absorbing agent, light stabilizer, The nucleating agent and color masterbatch are uniformly mixed with a high-speed mixing mixer, extruded and granulated to obtain the special material for polybutene alloy pipes for hot and cold water pipes. On the basis of maintaining the impact resistance of polybutene, excellent environmental stress crack resistance and heat creep resistance, the special material for polybutene alloy pipes has greatly improved tensile strength and flexural modulus, and can be used as cold and hot Water pipes and fittings materials used.
Description
技术领域technical field
本发明涉及一种冷热水管材用聚丁烯合金管材专用料及其制备方法和用途,属于高分子材料,特别是高分子材料加工和应用领域。The invention relates to a special polybutene alloy pipe material for hot and cold water pipes, a preparation method and application thereof, and belongs to the field of polymer materials, especially the processing and application of polymer materials.
背景技术Background technique
由于聚丙烯PP质量轻、强度高、室温下不溶于一般溶剂、耐化学腐蚀,且无毒,可回收利用,无环境污染,因此可以作为管道材料用于建筑管道和工业管道领域。但是,聚丙烯属于准韧性材料,缺口敏感性大,常温或低温下冲击性能差,耐高温特性不突出,特别是工作温度和工作压力与其使用寿命直接相关,这大大限制了其在管材领域的应用。Because polypropylene PP is light in weight, high in strength, insoluble in common solvents at room temperature, resistant to chemical corrosion, non-toxic, recyclable, and environmentally friendly, it can be used as a piping material for construction piping and industrial piping. However, polypropylene is a quasi-tough material with high notch sensitivity, poor impact performance at room temperature or low temperature, and low temperature resistance. Especially, the working temperature and working pressure are directly related to its service life, which greatly limits its application in the field of pipes. application.
传统聚丙烯改性技术中,采用橡胶或弹性体与PP共混,可提高其耐冲击性能,但同时大幅降低了拉伸强度和弯曲强度,难以达到强度和韧性的综合平衡。PP的晶体结构中β晶型PP具有优异的冲击性能,并且其它力学性能与α晶型相比下降并不明显,可以作为增韧方面的应用使用,也已成为聚丙烯管道领域发展的一个重要方向。In the traditional polypropylene modification technology, the blending of rubber or elastomer with PP can improve its impact resistance, but at the same time greatly reduce the tensile strength and bending strength, making it difficult to achieve a comprehensive balance of strength and toughness. In the crystal structure of PP, the β crystal form PP has excellent impact properties, and other mechanical properties are not significantly lower than those of the α crystal form. It can be used as a toughening application and has become an important development in the field of polypropylene pipes. direction.
CN 103171068公开了通过控制冷却箱的方法来改善聚丙烯管材的抗冲击性能。CN103930481公开了一种采用单点催化剂和Z-N催化剂体系分别分段聚合制备了聚丙烯共混物及具有β-成核效果的丙烯共聚物,并且得到改善的抗冲击性能。中国发明专利CN201210104449.3、CN201310496215公开了采用嵌段聚丙烯和共聚聚丙烯作为树脂基体制备冷水管材料,并阐明了其填料等配料体系及加工方法。中国发明专利CN201110368990、CN201310112454、CN201019026051、CN200510017644等公开了采用β晶型成核剂、硅酸盐、铝酸盐、镁盐等晶须的方法,使得加工后的聚丙烯具有较多的β晶型PP,使其抗冲击性能得到改善,并可以在管材方面应用。但β晶型成核剂在与聚丙烯进行熔融共混时的分散和相界面问题,是影响均聚丙烯最终性能的主要问题。聚丁烯树脂具有优异的耐蠕变性和耐环境应力开裂性,可以作为冷热水管材或管件来使用。但是由于聚丁烯在熔体中结晶会存在一个晶型II到晶型I的转变,需要时间较长,从而限制了其加工和应用。缩短固化时间的方法很多,日本专利2618469公开了采用添加丙烯均聚物和HDPE的方法缩短转变周期,但是其使用性能变差。中国发明专利ZL 200410032739.7公开了采用乙炔黑作为成核剂,促进1-丁烯均聚物或1-丁烯共聚物固有的晶型转变现象,同时改善了其耐氯水性的组合物。CN 103171068 discloses improving the impact resistance of polypropylene pipes by controlling the cooling box. CN103930481 discloses that a polypropylene blend and a propylene copolymer with β-nucleation effect are prepared by staged polymerization using a single-site catalyst and a Z-N catalyst system, and improved impact resistance is obtained. Chinese invention patents CN201210104449.3 and CN201310496215 disclose the use of block polypropylene and copolymerized polypropylene as the resin matrix to prepare cold water pipe materials, and clarify the ingredient system and processing methods such as fillers. Chinese invention patents CN201110368990, CN201310112454, CN201019026051, CN200510017644, etc. disclose methods of using whiskers such as β crystal nucleating agents, silicates, aluminates, magnesium salts, etc., so that the processed polypropylene has more β crystal forms PP, which improves its impact resistance and can be used in pipes. However, the dispersion and phase interface of the β crystal nucleating agent in melt blending with polypropylene are the main problems affecting the final properties of homopolypropylene. Polybutene resin has excellent creep resistance and environmental stress crack resistance, and can be used as hot and cold water pipes or pipe fittings. However, due to the crystallization of polybutene in the melt, there will be a transformation from crystal form II to crystal form I, which takes a long time, thereby limiting its processing and application. There are many ways to shorten the curing time. Japanese Patent No. 2618469 discloses the method of adding propylene homopolymer and HDPE to shorten the transition period, but its performance becomes worse. Chinese invention patent ZL 200410032739.7 discloses a composition that uses acetylene black as a nucleating agent to promote the inherent crystal transformation phenomenon of 1-butene homopolymer or 1-butene copolymer, while improving its resistance to chlorine water.
中国发明专利01142929.1公开了一种丁烯及丁烯与高级α-烯烃的共聚物和聚丙烯树脂通过熔融捏合的物理共混方式制备了聚丁烯树脂组合物,并生成可以用于冷热水管材及管件领域。Chinese invention patent 01142929.1 discloses a butene and a copolymer of butene and higher α-olefins and polypropylene resin to prepare a polybutene resin composition through melt kneading and physical blending, and produce a polybutene resin composition that can be used for hot and cold water The field of pipes and pipe fittings.
中国发明专利CN2013106486926采用共聚聚丙烯作为基体材料制备了具有抗冲击性能的管材,添加了三聚氰胺树脂等提高其耐水性。中国发明专利CN201210398867公开了聚丙烯与一定含量的聚乙烯和高顺式顺丁橡胶进行物理共混,制备高抗冲聚丙烯管材料。但由于三聚氰胺树脂或顺丁橡胶的加入,对管材料的回收造成很大困难。同时,对两种以上聚合物进行物理共混时,其混合分散效果与聚合物的本体性质、表界面性质和相容性及相形态等有很大的相关程度,在没有解决好相容性的前提下,最终产品性能不能得到有效提高。Chinese invention patent CN2013106486926 uses copolymerized polypropylene as the matrix material to prepare a pipe with impact resistance, and adds melamine resin to improve its water resistance. Chinese invention patent CN201210398867 discloses that polypropylene is physically blended with a certain amount of polyethylene and high-cis-butadiene rubber to prepare a high-impact polypropylene pipe material. However, due to the addition of melamine resin or butadiene rubber, it is very difficult to recycle the pipe material. At the same time, when two or more polymers are physically blended, the mixing and dispersing effect has a great correlation with the bulk properties, surface and interface properties, compatibility and phase morphology of the polymers. Under the premise, the performance of the final product cannot be effectively improved.
中国发明专利ZL 201010198121.3公开了一种新型的聚丁烯合金材料,其包含均聚丙烯、均聚丁烯和丁烯-丙烯共聚物组成。该聚丁烯合金在不影响聚丁烯树脂高温抗蠕变性和柔性的前提下,尽量缩短成型周期,提高其强度及模量等。同时,通过釜内原位聚合制备聚丁烯合金,不仅可以有效改善聚丁烯与聚丙烯物理共混时存在的两相分散及相界面形貌,从而影响聚丁烯合金制品的性能的问题,同时少量共聚物的原位合成可明显改善合金的相界面问题,同时可以通过聚合工艺参数的调节来调节合金的组分含量、分子量及其分布等参数。该专利提及了聚丁烯合金可以在水管或聚丙烯增韧材料领域应用,但是并未涉及具体管材专用料的配方及加工。Chinese invention patent ZL 201010198121.3 discloses a new type of polybutene alloy material, which consists of homopolypropylene, homopolybutene and butene-propylene copolymer. The polybutene alloy shortens the molding cycle as much as possible and improves its strength and modulus without affecting the high temperature creep resistance and flexibility of the polybutene resin. At the same time, the preparation of polybutene alloy by in-situ polymerization in the kettle can not only effectively improve the two-phase dispersion and phase interface morphology existing in the physical blending of polybutene and polypropylene, but also affect the performance of polybutene alloy products. , at the same time, the in-situ synthesis of a small amount of copolymer can significantly improve the phase interface problem of the alloy, and at the same time, parameters such as the component content, molecular weight and distribution of the alloy can be adjusted by adjusting the polymerization process parameters. The patent mentions that polybutene alloys can be used in the field of water pipes or polypropylene toughening materials, but does not involve the formulation and processing of specific pipe materials.
发明内容Contents of the invention
本发明的目的就是提供一种聚丁烯合金作为主要组分的冷热水管材用聚丁烯管材专用料及其制备方法和用途,该聚丁烯合金管材专用料保持了聚丁烯抗冲击性能、优异的耐环境应力开裂性和耐热蠕变性,同时拉伸强度、弯曲模量有大幅的提高,可以作为冷热水管材及管件使用。The object of the present invention is to provide a special polybutene pipe material for cold and hot water pipes with polybutene alloy as the main component, its preparation method and application, the special polybutene alloy pipe material maintains the impact resistance of polybutene , Excellent resistance to environmental stress cracking and thermal creep resistance, while the tensile strength and flexural modulus are greatly improved, it can be used as hot and cold water pipes and pipe fittings.
本发明的具有改善的抗冲击性能、耐环境应力开裂性和耐热蠕变性,以及较高的拉伸强度、弯曲模量的冷热水管材用聚丁烯合金管材专用料的配方,以重量份计:The present invention has improved impact resistance, environmental stress cracking resistance and thermal creep resistance, and a formula of special polybutene alloy pipe material for hot and cold water pipes with higher tensile strength and flexural modulus. Parts by weight:
聚丁烯合金树脂 100份Polybutene alloy resin 100 parts
抗氧剂 0.2~9份Antioxidant 0.2~9 parts
吸卤素剂 0.01~0.2份Halogen absorbing agent 0.01~0.2 parts
光稳定剂 0.01~2份Light stabilizer 0.01~2 parts
色母料 0.1~5份Color masterbatch 0.1~5 parts
成核剂 0.01~6份Nucleating agent 0.01~6 parts
所述聚丁烯合金树脂为多相多组分釜内合金树脂,其中高等规聚丁烯(iPB)的重量百分含量为66~98.98%,高等规聚丙烯(iPP)的重量百分含量为1~25%,聚丁烯-聚丙烯嵌段共聚物的重量百分含量为0.01~5%,无规聚丁烯与无规聚丙烯的重量百分含量为0.01~4%。少量存在的嵌段共聚物和无规聚丁烯、无规聚丙烯可以起到辅助成核剂的作用。The polybutene alloy resin is a heterogeneous and multi-component in-kettle alloy resin, wherein the weight percentage of high isotactic polybutene (iPB) is 66% to 98.98%, and the weight percentage of high isotactic polypropylene (iPP) is The weight percentage of polybutene-polypropylene block copolymer is 0.01-5%, and the weight percentage of random polybutene and random polypropylene is 0.01-4%. A small amount of block copolymer, random polybutene and random polypropylene can play the role of auxiliary nucleating agent.
所述聚丁烯合金树脂在190℃,2.16kg砝码条件下,其熔体质量流动速率为0.5~2g/10min。The melt mass flow rate of the polybutene alloy resin is 0.5-2 g/10 min under the condition of 190° C. and a weight of 2.16 kg.
所述的抗氧剂由主抗氧剂和辅助抗氧剂组成;主抗氧剂BHT、Hostanox3、2246、1010、1076中的一种或多种复配;辅助抗氧剂为168、626、9228、DLTDP、DSTDP、DMTDP、DTDTP中的一种或多种复配;主抗氧剂和辅助抗氧剂的重量比例为1:1~4。抗氧剂的总份数以聚丁烯合金树脂为100重量份计算,为重量0.1~9份,其中优选重量0.3~5份。Described antioxidant is made up of main antioxidant and auxiliary antioxidant; One or more compound in main antioxidant BHT, Hostanox3, 2246, 1010, 1076; Auxiliary antioxidant is 168, 626, One or more compounds of 9228, DLTDP, DSTDP, DMTDP, DTDTP; the weight ratio of primary antioxidant to secondary antioxidant is 1:1-4. The total parts of the antioxidant is calculated based on 100 parts by weight of the polybutene alloy resin, and is 0.1 to 9 parts by weight, preferably 0.3 to 5 parts by weight.
所述成核剂为二苄叉山梨醇、二(对-甲基苄叉)山梨醇、2,2’-亚甲基双(4,6-特丁基苯酚)膦酸铝、2,2’-亚甲基双(4,6-特丁基苯酚)膦酸钠、2,2’-亚甲基双(4,6-特丁基苯酚)膦酸钾、二酰胺类化合物及其衍生物中的一种或两种及两种以上混合。成核剂的用量为以100重量份树脂计算,添加0.01~6重量份,其中优选0.3~1重量份。The nucleating agent is dibenzylidene sorbitol, bis(p-methylbenzylidene) sorbitol, 2,2'-methylenebis(4,6-tert-butylphenol) aluminum phosphonate, 2,2 Sodium '-methylenebis(4,6-tert-butylphenol) phosphonate, potassium 2,2'-methylenebis(4,6-tert-butylphenol)phosphonate, diamide compounds and their derivatives One or a mixture of two or more of them. The nucleating agent is used in an amount of 0.01-6 parts by weight based on 100 parts by weight of the resin, preferably 0.3-1 part by weight.
所述吸卤素剂是硬脂酸钙、硬脂酸钠或硬脂酸锌中的一种或几种。吸卤素剂的用量为0.01~0.2重量份(以100重量份聚丁烯合金树脂计算)。The halogen-absorbing agent is one or more of calcium stearate, sodium stearate or zinc stearate. The amount of the halogen-absorbing agent is 0.01-0.2 parts by weight (calculated on the basis of 100 parts by weight of polybutene alloy resin).
所述光稳定剂为二苯甲酮类或受阻胺类中的一种或几种。其用量为0.01~2重量份(以100重量份聚丁烯合金树脂计算)。The light stabilizer is one or more of benzophenones or hindered amines. The dosage thereof is 0.01-2 parts by weight (calculated on the basis of 100 parts by weight of polybutene alloy resin).
所述色母料包含以下组成:40~95重量份的高等规聚丁烯作为基体树脂、0.1~8重量份的分散剂、0.1~5重量份的钛白粉、0.001~5重量份的颜料和0.01~4重量份的防老剂。分散剂为聚乙烯蜡、聚乙二醇中的一种或两种复配使用。The color masterbatch comprises the following composition: 40-95 parts by weight of high isotactic polybutene as a matrix resin, 0.1-8 parts by weight of dispersant, 0.1-5 parts by weight of titanium dioxide, 0.001-5 parts by weight of pigment and 0.01-4 parts by weight of anti-aging agent. The dispersing agent is one or two kinds of polyethylene wax and polyethylene glycol.
本发明所述的聚丁烯合金管材专用料,其制备方法包括以下步骤:The special material for polybutene alloy pipe material of the present invention, its preparation method comprises the following steps:
(1)按上述质量份数称取各原料,聚丁烯合金、抗氧剂、吸卤素剂、光稳定剂、色母料、成核剂配料;(1) Take each raw material according to the above-mentioned parts by mass, polybutene alloy, antioxidant, halogen absorbing agent, light stabilizer, color masterbatch, nucleating agent batching;
(2)将上述各组分在高速混合机中混合5分钟,使各组分混合均匀;(2) Mix the above-mentioned components in a high-speed mixer for 5 minutes, so that the components are mixed evenly;
(3)将第二步混合均匀的物料,加入到长径比30~50:1的双螺杆挤出机中熔融分散,挤出造粒。(3) Add the homogeneously mixed material in the second step into a twin-screw extruder with an aspect ratio of 30-50:1 to melt and disperse, and extrude to granulate.
所述的双螺杆挤出机的长径比30~50:1。The aspect ratio of the twin-screw extruder is 30-50:1.
所述的挤出造粒工艺为:一区140~160℃,二区160~170℃,三区175~185℃,四区180~200℃,五区190~230℃,机头190~230℃,转速10~30r/min,熔体压力12~20MPa。The extrusion granulation process is as follows: first zone 140-160°C, second zone 160-170°C, third zone 175-185°C, fourth zone 180-200°C, fifth zone 190-230°C, head 190-230°C ℃, rotating speed 10~30r/min, melt pressure 12~20MPa.
本发明制备的冷热水管用聚丁烯合金管材专用料,该聚丁烯合金管材专用料可以提供保持了聚丁烯抗冲击性能、优异的耐环境应力开裂性和耐热蠕变性,同时拉伸强度、弯曲模量有大幅的提高,可以作为冷热水管材及管件使用。The special polybutene alloy pipe material for hot and cold water pipes prepared by the present invention can provide and maintain polybutene impact resistance, excellent environmental stress crack resistance and thermal creep resistance, and at the same time The tensile strength and flexural modulus have been greatly improved, and it can be used as hot and cold water pipes and pipe fittings.
具体实施方式detailed description
以下实施例是为了更好地解释本发明,但并不造成对本发明权利要求书的限制。The following examples are for better explaining the present invention, but do not limit the claims of the present invention.
实施例1Example 1
按表1提供的组分和配方(按照重量百分比计,以下实施例均同)称重物料,在高速搅拌机中混合5分钟后,在长径比45的、直径50的双螺杆挤出机中挤出造粒得到聚丁烯合金树脂管材专用料。所用聚丁烯合金树脂中iPB的质量含量为66%,其熔体流动速率(190℃,负荷2.16kg)为0.5g/10min。挤出机各个区间温度为:一区150℃,二区165℃,三区180℃,四区190℃,五区210℃,机头230℃,挤出机转速20转/分钟,熔体压力15MPa。Components and formulations provided by Table 1 (according to weight percent, the following examples are all the same) weigh the material, after mixing in a high-speed mixer for 5 minutes, in a twin-screw extruder with an aspect ratio of 45 and a diameter of 50 Extrusion granulation to obtain the special material for polybutene alloy resin pipes. The mass content of iPB in the polybutene alloy resin used is 66%, and its melt flow rate (190° C., load 2.16 kg) is 0.5 g/10 min. The temperature of each section of the extruder is: 150°C in zone 1, 165°C in zone 2, 180°C in zone 3, 190°C in zone 4, 210°C in zone 5, 230°C at the head, 20 rpm of extruder, and melt pressure 15MPa.
性能测试结果见表2。The performance test results are shown in Table 2.
对比例1Comparative example 1
按表1提供的组分和配方(按照重量百分比计,以下实施例均同)称重物料,在高速搅拌机中混合5分钟后,在长径比45的、直径50的双螺杆挤出机中挤出造粒得到聚丙烯管材料。所用聚丙烯为等规度大于98%的聚丙烯树脂,其熔体流动速率(230℃,负荷2.16kg)为1.2g/10min。挤出机各个区间温度为:一区150℃,二区165℃,三区180℃,四区190℃,五区210℃,机头230℃,挤出机转速20转/分钟,熔体压力15MPa。Components and formulations provided by Table 1 (according to weight percent, the following examples are all the same) weigh the material, after mixing in a high-speed mixer for 5 minutes, in a twin-screw extruder with an aspect ratio of 45 and a diameter of 50 Extrusion granulation to obtain polypropylene pipe material. The polypropylene used is a polypropylene resin with an isotacticity greater than 98%, and its melt flow rate (230° C., load 2.16 kg) is 1.2 g/10 min. The temperature of each section of the extruder is: 150°C in zone 1, 165°C in zone 2, 180°C in zone 3, 190°C in zone 4, 210°C in zone 5, 230°C at the head, 20 rpm of extruder, and melt pressure 15MPa.
性能测试结果见表2。The performance test results are shown in Table 2.
实施例1和对比例1的区别仅在于所用基体树脂不同,其它所有成分及用料以及生产工艺均完全相同。通过实施例1和对比例1的结果可以看出,与聚丙烯管材专用料相比,聚丁烯合金树脂制备的管材专用料,在弯曲性能和热变形温度降低不大的前提下,缺口冲击强度和收缩率得到大幅度改善。The difference between Example 1 and Comparative Example 1 is only that the base resin used is different, and all other components, materials and production processes are completely the same. From the results of Example 1 and Comparative Example 1, it can be seen that compared with the special material for polypropylene pipes, the special material for pipes made of polybutene alloy resin has a lower notched impact on the premise that the bending performance and heat distortion temperature are not greatly reduced. Strength and shrinkage are greatly improved.
表1实施例1和对比例1的组分及配方Component and formula of table 1 embodiment 1 and comparative example 1
表2实施例1和对比例1所生产材料的性能The performance of the produced material of table 2 embodiment 1 and comparative example 1
实施例2~4Embodiment 2-4
按表3提供的组分和配方(按照重量百分比计,以下实施例均同)称重物料,在高速搅拌机中混合5分钟后,在长径比45的、直径50的双螺杆挤出机中挤出造粒得到聚丁烯合金管材专用料。挤出机各个区间温度为:一区140~160℃,二区160~170℃,三区175~185℃,四区180~200℃,五区190~230℃,机头190~230℃,转速10~30r/min,熔体压力12~20MPa。Components and formulations provided by Table 3 (according to weight percent, the following examples are the same) weigh the material, after mixing in a high-speed mixer for 5 minutes, in a twin-screw extruder with an aspect ratio of 45 and a diameter of 50 Extrusion granulation to obtain special materials for polybutene alloy pipes. The temperature of each section of the extruder is: 140-160°C for the first zone, 160-170°C for the second zone, 175-185°C for the third zone, 180-200°C for the fourth zone, 190-230°C for the fifth zone, 190-230°C for the head, The speed is 10~30r/min, and the melt pressure is 12~20MPa.
性能测试结果见表4。The performance test results are shown in Table 4.
从表4测试结果能够看出,通过适当的配比和优化的加工工艺条件,能够制备出满足冷热水管用管材料使用要求的聚丁烯合金管材专用料。From the test results in Table 4, it can be seen that through proper proportioning and optimized processing conditions, special polybutene alloy pipe materials that meet the requirements for the use of pipe materials for cold and hot water pipes can be prepared.
表3实施例2~4的组分、配方及工艺Components, formula and process of table 3 embodiment 2~4
表4实施例2~4所生产材料的性能The performance of the produced material of table 4 embodiment 2~4
对比例2~4Comparative example 2~4
按表5提供的组分和配方(按照重量百分比计,以下实施例均同)称重物料,在高速搅拌机中混合5分钟后,在长径比45的、直径50的双螺杆挤出机中挤出造粒得到聚丁烯/聚丙烯共混复合管材专用料。所用聚丁烯为等规度98%的均聚丁烯,其熔体流动速率为0.8g/10min;所用聚丙烯聚丙烯为抗冲聚丙烯30R,等规度95%,其熔体流动速率(230℃,负荷2.16kg)为13g/10min。挤出机各个区间温度为:一区140~160℃,二区160~170℃,三区175~185℃,四区180~200℃,五区190~230℃,机头190~230℃,转速10~30r/min,熔体压力12-20MPa。Components and formulations provided by Table 5 (according to weight percent, the following examples are the same) weigh the material, after mixing in a high-speed mixer for 5 minutes, in a twin-screw extruder with an aspect ratio of 45 and a diameter of 50 Extrusion granulation to obtain special material for polybutene/polypropylene blended composite pipe. The polybutene used is homopolybutene with an isotacticity of 98%, and its melt flow rate is 0.8g/10min; the polypropylene polypropylene used is impact polypropylene 30R, with an isotacticity of 95%, and its melt flow rate (230°C, load 2.16kg) is 13g/10min. The temperature of each section of the extruder is: 140-160°C for the first zone, 160-170°C for the second zone, 175-185°C for the third zone, 180-200°C for the fourth zone, 190-230°C for the fifth zone, 190-230°C for the head, The speed is 10~30r/min, and the melt pressure is 12-20MPa.
性能测试结果见表6。The performance test results are shown in Table 6.
通过对比例2~4与实施例2~4的比较可以看出,采用聚丁烯合金制备的冷热水管材专用料,缺口冲击强度和弯曲模量比物理共混制备的聚丁烯/聚丙烯管材料要大很多,并且随着聚丙烯份数的增加,冲击强度降低明显。同时,作为冷热水管使用,物理共混制备的聚丁烯/聚丙烯共混管材料的维卡软化温度低,其使用场合收到限制且使用寿命降低。From the comparison of Examples 2-4 with Examples 2-4, it can be seen that the notched impact strength and flexural modulus ratio of the special material for cold and hot water pipes prepared by polybutene alloy, the ratio of physical blending of polybutene/polyethylene The propylene pipe material is much larger, and as the proportion of polypropylene increases, the impact strength decreases significantly. At the same time, as cold and hot water pipes, the Vicat softening temperature of the polybutene/polypropylene blend pipe material prepared by physical blending is low, and its application occasions are limited and its service life is reduced.
表5对比例2~4的组分、配方及工艺Components, formulations and processes of Table 5 Comparative Examples 2 to 4
表6对比例2~4所生产材料的性能The performance of the produced material of table 6 comparative examples 2~4
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CN111286128B (en) * | 2020-03-26 | 2023-02-10 | 青岛科技大学 | A kind of rapid prototyping polybutene resin and preparation method thereof |
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