CN112126170A - PVC tray and preparation method thereof - Google Patents
PVC tray and preparation method thereof Download PDFInfo
- Publication number
- CN112126170A CN112126170A CN202010887199.XA CN202010887199A CN112126170A CN 112126170 A CN112126170 A CN 112126170A CN 202010887199 A CN202010887199 A CN 202010887199A CN 112126170 A CN112126170 A CN 112126170A
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- China
- Prior art keywords
- pvc
- tray
- filler
- type
- parts
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
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- 238000002360 preparation method Methods 0.000 title abstract description 14
- 239000004800 polyvinyl chloride Substances 0.000 claims abstract description 86
- 229920000915 polyvinyl chloride Polymers 0.000 claims abstract description 85
- 229920005989 resin Polymers 0.000 claims abstract description 43
- 239000011347 resin Substances 0.000 claims abstract description 43
- 239000000945 filler Substances 0.000 claims abstract description 24
- 239000004609 Impact Modifier Substances 0.000 claims abstract description 17
- 239000003963 antioxidant agent Substances 0.000 claims abstract description 15
- 230000003078 antioxidant effect Effects 0.000 claims abstract description 15
- 239000007822 coupling agent Substances 0.000 claims abstract description 15
- 239000012760 heat stabilizer Substances 0.000 claims abstract description 15
- 238000005187 foaming Methods 0.000 claims abstract description 13
- 239000004088 foaming agent Substances 0.000 claims abstract description 13
- 239000003999 initiator Substances 0.000 claims abstract description 13
- 239000000314 lubricant Substances 0.000 claims abstract description 13
- 229920001577 copolymer Polymers 0.000 claims abstract description 8
- 239000000203 mixture Substances 0.000 claims description 37
- 239000000843 powder Substances 0.000 claims description 28
- 238000002156 mixing Methods 0.000 claims description 20
- 238000006116 polymerization reaction Methods 0.000 claims description 18
- 238000001816 cooling Methods 0.000 claims description 15
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 claims description 15
- 229910052737 gold Inorganic materials 0.000 claims description 15
- 239000010931 gold Substances 0.000 claims description 15
- 239000012768 molten material Substances 0.000 claims description 15
- -1 bis (2-ethyl) hexyl peroxydicarbonate Chemical compound 0.000 claims description 14
- 150000002978 peroxides Chemical group 0.000 claims description 14
- 239000002994 raw material Substances 0.000 claims description 11
- HVLLSGMXQDNUAL-UHFFFAOYSA-N triphenyl phosphite Chemical compound C=1C=CC=CC=1OP(OC=1C=CC=CC=1)OC1=CC=CC=C1 HVLLSGMXQDNUAL-UHFFFAOYSA-N 0.000 claims description 10
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2-(2-cyanopropan-2-yldiazenyl)-2-methylpropanenitrile Chemical compound N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 claims description 9
- QTKPMCIBUROOGY-UHFFFAOYSA-N 2,2,2-trifluoroethyl 2-methylprop-2-enoate Chemical group CC(=C)C(=O)OCC(F)(F)F QTKPMCIBUROOGY-UHFFFAOYSA-N 0.000 claims description 8
- 229920000459 Nitrile rubber Polymers 0.000 claims description 8
- ANISOHQJBAQUQP-UHFFFAOYSA-N octyl prop-2-enoate Chemical compound CCCCCCCCOC(=O)C=C ANISOHQJBAQUQP-UHFFFAOYSA-N 0.000 claims description 8
- IHBCFWWEZXPPLG-UHFFFAOYSA-N [Ca].[Zn] Chemical group [Ca].[Zn] IHBCFWWEZXPPLG-UHFFFAOYSA-N 0.000 claims description 7
- 239000006084 composite stabilizer Substances 0.000 claims description 7
- 150000001875 compounds Chemical class 0.000 claims description 7
- 239000004156 Azodicarbonamide Substances 0.000 claims description 6
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 claims description 6
- 235000021355 Stearic acid Nutrition 0.000 claims description 6
- XOZUGNYVDXMRKW-AATRIKPKSA-N azodicarbonamide Chemical compound NC(=O)\N=N\C(N)=O XOZUGNYVDXMRKW-AATRIKPKSA-N 0.000 claims description 6
- 235000019399 azodicarbonamide Nutrition 0.000 claims description 6
- CQEYYJKEWSMYFG-UHFFFAOYSA-N butyl acrylate Chemical compound CCCCOC(=O)C=C CQEYYJKEWSMYFG-UHFFFAOYSA-N 0.000 claims description 6
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 claims description 6
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 claims description 6
- 239000008117 stearic acid Substances 0.000 claims description 6
- 239000004372 Polyvinyl alcohol Substances 0.000 claims description 5
- 238000001125 extrusion Methods 0.000 claims description 5
- 238000000465 moulding Methods 0.000 claims description 5
- 229920002451 polyvinyl alcohol Polymers 0.000 claims description 5
- 238000007493 shaping process Methods 0.000 claims description 5
- BAPJBEWLBFYGME-UHFFFAOYSA-N Methyl acrylate Chemical compound COC(=O)C=C BAPJBEWLBFYGME-UHFFFAOYSA-N 0.000 claims description 4
- 229920002749 Bacterial cellulose Polymers 0.000 claims description 3
- YIVJZNGAASQVEM-UHFFFAOYSA-N Lauroyl peroxide Chemical compound CCCCCCCCCCCC(=O)OOC(=O)CCCCCCCCCCC YIVJZNGAASQVEM-UHFFFAOYSA-N 0.000 claims description 3
- 239000004698 Polyethylene Substances 0.000 claims description 3
- TXQVDVNAKHFQPP-UHFFFAOYSA-N [3-hydroxy-2,2-bis(hydroxymethyl)propyl] octadecanoate Chemical compound CCCCCCCCCCCCCCCCCC(=O)OCC(CO)(CO)CO TXQVDVNAKHFQPP-UHFFFAOYSA-N 0.000 claims description 3
- 239000005016 bacterial cellulose Substances 0.000 claims description 3
- BLCKNMAZFRMCJJ-UHFFFAOYSA-N cyclohexyl cyclohexyloxycarbonyloxy carbonate Chemical compound C1CCCCC1OC(=O)OOC(=O)OC1CCCCC1 BLCKNMAZFRMCJJ-UHFFFAOYSA-N 0.000 claims description 3
- GVGUFUZHNYFZLC-UHFFFAOYSA-N dodecyl benzenesulfonate;sodium Chemical compound [Na].CCCCCCCCCCCCOS(=O)(=O)C1=CC=CC=C1 GVGUFUZHNYFZLC-UHFFFAOYSA-N 0.000 claims description 3
- 238000000034 method Methods 0.000 claims description 3
- SSDSCDGVMJFTEQ-UHFFFAOYSA-N octadecyl 3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoate Chemical compound CCCCCCCCCCCCCCCCCCOC(=O)CCC1=CC(C(C)(C)C)=C(O)C(C(C)(C)C)=C1 SSDSCDGVMJFTEQ-UHFFFAOYSA-N 0.000 claims description 3
- 229920000573 polyethylene Polymers 0.000 claims description 3
- BWJUFXUULUEGMA-UHFFFAOYSA-N propan-2-yl propan-2-yloxycarbonyloxy carbonate Chemical compound CC(C)OC(=O)OOC(=O)OC(C)C BWJUFXUULUEGMA-UHFFFAOYSA-N 0.000 claims description 3
- 229940080264 sodium dodecylbenzenesulfonate Drugs 0.000 claims description 3
- NDLIRBZKZSDGSO-UHFFFAOYSA-N tosyl azide Chemical compound CC1=CC=C(S(=O)(=O)[N-][N+]#N)C=C1 NDLIRBZKZSDGSO-UHFFFAOYSA-N 0.000 claims description 3
- QQQSFSZALRVCSZ-UHFFFAOYSA-N triethoxysilane Chemical compound CCO[SiH](OCC)OCC QQQSFSZALRVCSZ-UHFFFAOYSA-N 0.000 claims description 3
- BEQKKZICTDFVMG-UHFFFAOYSA-N 1,2,3,4,6-pentaoxepane-5,7-dione Chemical compound O=C1OOOOC(=O)O1 BEQKKZICTDFVMG-UHFFFAOYSA-N 0.000 claims description 2
- WPMYUUITDBHVQZ-UHFFFAOYSA-N 3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoic acid Chemical compound CC(C)(C)C1=CC(CCC(O)=O)=CC(C(C)(C)C)=C1O WPMYUUITDBHVQZ-UHFFFAOYSA-N 0.000 claims description 2
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical compound C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-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
- 239000003508 Dilauryl thiodipropionate Substances 0.000 claims description 2
- 239000004721 Polyphenylene oxide Substances 0.000 claims description 2
- 235000019400 benzoyl peroxide Nutrition 0.000 claims description 2
- 235000019304 dilauryl thiodipropionate Nutrition 0.000 claims description 2
- 229920000570 polyether Polymers 0.000 claims description 2
- 229920002545 silicone oil Polymers 0.000 claims description 2
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 claims 1
- 239000000463 material Substances 0.000 abstract description 8
- 230000002035 prolonged effect Effects 0.000 abstract description 2
- 230000002195 synergetic effect Effects 0.000 abstract description 2
- 230000000052 comparative effect Effects 0.000 description 13
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 11
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 8
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 7
- 229910052681 coesite Inorganic materials 0.000 description 7
- 229910052593 corundum Inorganic materials 0.000 description 7
- 229910052906 cristobalite Inorganic materials 0.000 description 7
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 7
- 239000000377 silicon dioxide Substances 0.000 description 7
- 229910052682 stishovite Inorganic materials 0.000 description 7
- 239000000126 substance Substances 0.000 description 7
- 229910052905 tridymite Inorganic materials 0.000 description 7
- 229910001845 yogo sapphire Inorganic materials 0.000 description 7
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 6
- QVQLCTNNEUAWMS-UHFFFAOYSA-N barium oxide Chemical compound [Ba]=O QVQLCTNNEUAWMS-UHFFFAOYSA-N 0.000 description 6
- 239000011734 sodium Substances 0.000 description 4
- KKCBUQHMOMHUOY-UHFFFAOYSA-N Na2O Inorganic materials [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 description 3
- MCMNRKCIXSYSNV-UHFFFAOYSA-N ZrO2 Inorganic materials O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 3
- 238000009776 industrial production Methods 0.000 description 3
- RVTZCBVAJQQJTK-UHFFFAOYSA-N oxygen(2-);zirconium(4+) Chemical compound [O-2].[O-2].[Zr+4] RVTZCBVAJQQJTK-UHFFFAOYSA-N 0.000 description 3
- 239000011787 zinc oxide Substances 0.000 description 3
- 229920003023 plastic Polymers 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 235000017166 Bambusa arundinacea Nutrition 0.000 description 1
- 235000017491 Bambusa tulda Nutrition 0.000 description 1
- 241001330002 Bambuseae Species 0.000 description 1
- 241000238631 Hexapoda Species 0.000 description 1
- 235000015334 Phyllostachys viridis Nutrition 0.000 description 1
- XBDQKXXYIPTUBI-UHFFFAOYSA-M Propionate Chemical compound CCC([O-])=O XBDQKXXYIPTUBI-UHFFFAOYSA-M 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 239000011425 bamboo Substances 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000003889 chemical engineering Methods 0.000 description 1
- 238000012824 chemical production Methods 0.000 description 1
- 229920006026 co-polymeric resin Polymers 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- NFHFRUOZVGFOOS-UHFFFAOYSA-N palladium;triphenylphosphane Chemical compound [Pd].C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1.C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1.C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1.C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1 NFHFRUOZVGFOOS-UHFFFAOYSA-N 0.000 description 1
- WXZMFSXDPGVJKK-UHFFFAOYSA-N pentaerythritol Chemical group OCC(CO)(CO)CO WXZMFSXDPGVJKK-UHFFFAOYSA-N 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 230000007306 turnover Effects 0.000 description 1
- 239000002023 wood 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
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/04—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
- C08J9/06—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent
- C08J9/10—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent developing nitrogen, the blowing agent being a compound containing a nitrogen-to-nitrogen bond
- C08J9/106—Azides
-
- 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
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/0014—Use of organic additives
- C08J9/0023—Use of organic additives containing oxygen
-
- 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
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/0014—Use of organic additives
- C08J9/0038—Use of organic additives containing phosphorus
-
- 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
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/0061—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof characterized by the use of several polymeric components
-
- 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
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/0066—Use of inorganic compounding ingredients
-
- 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
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/009—Use of pretreated compounding ingredients
-
- 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
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/0095—Mixtures of at least two compounding ingredients belonging to different one-dot groups
-
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- 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
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/04—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
- C08J9/06—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent
- C08J9/10—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent developing nitrogen, the blowing agent being a compound containing a nitrogen-to-nitrogen bond
- C08J9/102—Azo-compounds
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- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/04—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
- C08J9/06—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent
- C08J9/10—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent developing nitrogen, the blowing agent being a compound containing a nitrogen-to-nitrogen bond
- C08J9/102—Azo-compounds
- C08J9/103—Azodicarbonamide
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- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/04—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
- C08J9/06—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent
- C08J9/10—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent developing nitrogen, the blowing agent being a compound containing a nitrogen-to-nitrogen bond
- C08J9/104—Hydrazines; Hydrazides; Semicarbazides; Semicarbazones; Hydrazones; Derivatives thereof
- C08J9/105—Hydrazines; Hydrazides; Semicarbazides; Semicarbazones; Hydrazones; Derivatives thereof containing sulfur
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- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2203/00—Foams characterized by the expanding agent
- C08J2203/04—N2 releasing, ex azodicarbonamide or nitroso compound
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- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
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- C08J2203/00—Foams characterized by the expanding agent
- C08J2203/18—Binary blends of expanding agents
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- C08J2203/00—Foams characterized by the expanding agent
- C08J2203/20—Ternary blends of expanding agents
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- 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
- C08J2327/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers
- C08J2327/02—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment
- C08J2327/04—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment containing chlorine atoms
- C08J2327/06—Homopolymers or copolymers of vinyl chloride
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- C08J2401/00—Characterised by the use of cellulose, modified cellulose or cellulose derivatives
- C08J2401/02—Cellulose; Modified cellulose
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- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
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- 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
- C08J2423/04—Homopolymers or copolymers of ethene
- C08J2423/08—Copolymers of ethene
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Abstract
The invention belongs to the technical field of PVC materials, and particularly relates to a PVC tray and a preparation method thereof. The material comprises, by mass, 70-80 parts of polyvinyl chloride resin, 20-30 parts of PCV scrap, 3.5-4.0 parts of ethylene-octene copolymer, 0.5-0.8 part of foaming agent, 4.0-6.0 parts of foaming regulator, 0.5-1.0 part of impact modifier, 0.1-0.5 part of initiator, 3.0-4.5 parts of filler, 1.0-3.0 parts of antioxidant, 0.5-1.5 parts of lubricant, 2.0-3.0 parts of coupling agent and 1.5-3.0 parts of heat stabilizer. The PVC tray provided by the invention adopts the synergistic cooperation of the ethylene-octene copolymer and the impact modifier, the impact resistance of the tray is enhanced, the filler is modified by using the coupling agent, the compatibility of the filler and PVC resin is increased, and the service life of the tray is prolonged by adding the antioxidant and the heat stabilizer.
Description
Technical Field
The invention belongs to the technical field of PVC materials, and particularly relates to a PVC tray and a preparation method thereof.
Background
Polyvinyl chloride (PVC) section bar is produced by adopting a polyvinyl chloride material, and is produced by taking polyvinyl chloride and copolymer resin thereof as main raw materials, adding auxiliary materials such as a filler, a plasticizer, a stabilizer and the like, and coating or rolling, extruding or extruding on a flaky continuous base material. Because of the advantages of water resistance, flame resistance, acid and alkali resistance, moth resistance, light weight, smooth and flat surface, no deformation, easy processing, recyclability and the like, the PVC section becomes a common thermal forming material, can replace part of stainless steel and other corrosion-resistant synthetic materials, and is widely applied to the fields of building engineering, municipal engineering, chemical engineering, industrial production and the like.
The pallet is an indispensable carrying tool in chemical and industrial production, is a medium for converting static goods into dynamic goods, is a carrying platform, and is a movable platform or a movable ground. Even if the goods are put on the ground and lose flexibility, the goods can be immediately moved after being loaded with the pallets, and the goods become flexible and mobile goods. At present, the types of the trays classified according to the materials mainly include: wooden pallets, bamboo pallets, multi-ply board pallets, plastic pallets, steel pallets, paper pallets, plastic-wood pallets, molded pallets, etc., but all suffer from some drawbacks. The wooden tray is not fireproof and waterproof, is easy to damp, is easy to grow insects and decay, is easy to generate burrs at corners and has low bearing capacity. The plastic tray has the advantages of no water absorption, high turnover rate, convenient recycling and the like as a substitute of the traditional tray, plays a bigger and bigger role in the field of warehouse logistics, but has the defects of low strength, poor impact resistance, easy occurrence of scratches on the surface when placing some heavier objects and the like.
Disclosure of Invention
The purpose of the invention is: a PVC pallet is provided. The PVC tray has the advantages of high strength, strong impact resistance, no scratch after long-term use and the like; the invention also provides a preparation method thereof.
The PVC tray comprises the following raw materials in parts by weight:
wherein:
the polyvinyl chloride resin is a compound of SG-5 and SG-8, the mass ratio of SG-8 type PVC resin powder to SG-5 type PVC resin powder is 3.5-5.5:1, the average polymerization degree of SG-5 type PVC resin powder is 1000-type 1100, and the average polymerization degree of SG-8 type PVC resin powder is 700-type 750.
The foaming agent is at least two of p-toluenesulfonyl azide, 4' -oxybis-benzenesulfonyl hydrazide, azobisisobutyronitrile or azodicarbonamide.
The foaming regulator is one or more of methyl methacrylate, methyl acrylate or butyl acrylate.
The impact modifier is a composition of trifluoroethyl methacrylate, nitrile rubber and n-octyl acrylate.
The initiator is peroxide, and the peroxide is one or more of diisopropyl peroxydicarbonate, dibenzoyl peroxide, dicyclohexyl peroxydicarbonate, lauroyl peroxide, diphenoxyethyl peroxydicarbonate or bis (2-ethyl) hexyl peroxydicarbonate.
The filler is one or two of red mud, gold tailings or bacterial cellulose, preferably a mixture of the red mud and the gold tailings, and the weight ratio of the red mud to the gold tailings is 1: 1.
The antioxidant is one or more of octadecyl-3- (3, 5-di-tert-butyl-4-hydroxyphenyl) propionate, triphenyl phosphite, tetra [ beta- (3, 5-di-tert-butyl-4-hydroxyphenyl) propionic acid ] pentaerythritol ester or dilauryl thiodipropionate.
The lubricant is one or more of pentaerythritol stearate, stearic acid, polyethylene wax or Fischer-Tropsch wax.
The coupling agent is one or more of 3-glycidyl ether oxypropyl triethoxysilane, gamma-glycidyl propyl methyldimethoxysilane, sodium dodecyl benzene sulfonate, polyether silicone oil or polyvinyl alcohol.
The heat stabilizer is a calcium-zinc composite stabilizer.
The preparation method of the PVC tray comprises the following steps:
(1) carrying out polymerization reaction on the ethylene-octene copolymer, the impact modifier and the initiator at the temperature of 140 ℃ and 150 ℃;
(2) adding the filler into the coupling agent and mixing at the temperature of 100-120 ℃;
(3) putting the products obtained in the step (1) and the step (2), polyvinyl chloride resin, PCV scrap, a foaming agent, a foaming regulator, a filler, an antioxidant, a lubricant and a heat stabilizer into a mixer according to a ratio for mixing, wherein the mixing temperature is kept at 190 ℃ and the mixing time is 20-30 min;
(4) and taking out the mixture for extrusion molding, obtaining a molten material through an extruder, carrying out vacuum negative pressure cooling and shaping on the molten material, cooling and molding the molten material through a cooling system to obtain a tray, and carrying out post-treatment on the molded tray to obtain the PVC tray.
Compared with the prior art, the invention has the following beneficial effects:
(1) the PVC tray provided by the invention adopts the synergistic cooperation of the ethylene-octene copolymer and the impact modifier, the impact resistance of the tray is enhanced, the filler is modified by using the coupling agent, the compatibility of the filler and PVC resin is increased, and the service life of the tray is prolonged by adding the antioxidant and the heat stabilizer.
(2) The PVC tray provided by the invention has the advantages of high surface hardness, strong scratch resistance, excellent impact resistance, and high tensile strength and bending strength.
(3) The preparation method of the PVC tray has the advantages of easily available raw materials, simple process, easy realization of industrial production, good performance of the prepared tray and long service life.
Detailed Description
The present invention is further described below with reference to examples.
Example 1
The PVC tray described in this embodiment 1 comprises the following raw materials in parts by mass:
wherein:
the polyvinyl chloride resin is a compound of SG-5 and SG-8, the mass ratio of SG-8 type PVC resin powder to SG-5 type PVC resin powder is 4.5:1, the average polymerization degree of SG-5 type PVC resin powder is 1000-type 1100, and the average polymerization degree of SG-8 type PVC resin powder is 700-type 750.
The foaming agent is a mixture of p-toluenesulfonyl azide and azobisisobutyronitrile.
The foaming regulator is methyl methacrylate.
The impact modifier is a composition of trifluoroethyl methacrylate, nitrile rubber and n-octyl acrylate.
The initiator is peroxide, and the peroxide is a mixture of diisopropyl peroxydicarbonate and dicyclohexyl peroxydicarbonate.
The filler is red mud, and the chemical composition of the red mud is SiO2 12.3%、Al2O3 33.5%、Fe2O3 7.6%、CaO 21.3%、MgO 1.2%、TiO2 3.5%、K2O 0.5%、Na23.7% of O and 16.4% of loss on ignition.
The antioxidant is octadecyl-3- (3, 5-di-tert-butyl-4-hydroxyphenyl) propionate.
The lubricant is a mixture of pentaerythritol stearate and Fischer-Tropsch wax.
The coupling agent is 3-glycidyl ether oxypropyl triethoxysilane.
The heat stabilizer is a calcium-zinc composite stabilizer.
The preparation method of the PVC tray described in this embodiment 1 comprises the following steps:
(1) polymerizing the ethylene-octene copolymer, the impact modifier and the initiator at 145 ℃;
(2) adding the filler into the coupling agent and mixing at 110 ℃;
(3) putting the products obtained in the steps (1) and (2), polyvinyl chloride resin, PCV scrap, a foaming agent, a foaming regulator, a filler, an antioxidant, a lubricant and a heat stabilizer into a mixer according to a ratio for mixing, wherein the mixing temperature is kept at 170 ℃, and the mixing time is 25 min;
(4) and taking out the mixture for extrusion molding, obtaining a molten material through an extruder, carrying out vacuum negative pressure cooling and shaping on the molten material, cooling and molding the molten material through a cooling system to obtain a tray, and carrying out post-treatment on the molded tray to obtain the PVC tray.
Example 2
The PVC tray described in this embodiment 2 is composed of the following raw materials in parts by mass:
wherein:
the polyvinyl chloride resin is a compound of SG-5 and SG-8, the mass ratio of SG-8 type PVC resin powder to SG-5 type PVC resin powder is 5.5:1, the average polymerization degree of SG-5 type PVC resin powder is 1000-type 1100, and the average polymerization degree of SG-8 type PVC resin powder is 700-type 750.
The foaming agent is a mixture of 4, 4' -oxybis-benzenesulfonyl hydrazide, azodiisobutyronitrile and azodicarbonamide.
The foaming regulator is a mixture of methyl methacrylate and butyl acrylate.
The impact modifier is a composition of trifluoroethyl methacrylate, nitrile rubber and n-octyl acrylate.
The initiator is peroxide, and the peroxide is bis (2-ethyl) hexyl peroxydicarbonate.
The filler is a mixture of red mud and gold tailings, and the weight ratio of the red mud to the gold tailings is 1: 1; the chemical composition of the red mud is SiO2 12.3%、Al2O3 33.5%、Fe2O3 7.6%、CaO 21.3%、MgO 1.2%、TiO23.5%、K2O0.5%、Na23.7 percent of O and 16.4 percent of loss on ignition; the chemical composition of the gold tailings is SiO270.5%、Al2O3 17%、K2O 3%、Na2O 3%、CaO 2%、MgO 0.2%、Fe2O3 1%、TiO20.1% and traces of zirconium dioxide, zinc oxide and barium oxide.
The antioxidant is triphenyl phosphite.
The lubricant is stearic acid.
The coupling agent is a mixture of gamma-glycidylpropylmethyldimethoxysilane and polyvinyl alcohol.
The heat stabilizer is a calcium-zinc composite stabilizer.
The preparation method of the PVC tray described in this embodiment 2 comprises the following steps:
(1) carrying out polymerization reaction on the ethylene-octene copolymer, the impact modifier and the initiator at 150 ℃;
(2) adding the filler into the coupling agent and mixing at 120 ℃;
(3) putting the products obtained in the steps (1) and (2), polyvinyl chloride resin, PCV scrap, a foaming agent, a foaming regulator, a filler, an antioxidant, a lubricant and a heat stabilizer into a mixer according to a ratio for mixing, wherein the mixing temperature is kept at 190 ℃ and the mixing time is 30 min;
(4) and taking out the mixture for extrusion molding, obtaining a molten material through an extruder, carrying out vacuum negative pressure cooling and shaping on the molten material, cooling and molding the molten material through a cooling system to obtain a tray, and carrying out post-treatment on the molded tray to obtain the PVC tray.
Example 3
The PVC tray described in this embodiment 3 is composed of the following raw materials in parts by mass:
wherein:
the polyvinyl chloride resin is a compound of SG-5 and SG-8, the mass ratio of SG-8 type PVC resin powder to SG-5 type PVC resin powder is 3.5:1, the average polymerization degree of SG-5 type PVC resin powder is 1000-type 1100, and the average polymerization degree of SG-8 type PVC resin powder is 700-type 750.
The foaming agent is a mixture of azodiisobutyronitrile and azodicarbonamide.
The foaming regulator is butyl acrylate.
The impact modifier is a composition of trifluoroethyl methacrylate, nitrile rubber and n-octyl acrylate.
The initiator is peroxide, and the peroxide is lauroyl peroxide.
The filler is bacterial cellulose.
The antioxidant is pentaerythritol tetrakis [ beta- (3, 5-di-tert-butyl-4-hydroxyphenyl) propionate ].
The lubricant is a mixture of stearic acid and polyethylene wax.
The coupling agent is sodium dodecyl benzene sulfonate.
The heat stabilizer is a calcium-zinc composite stabilizer.
The preparation method of the PVC tray described in this embodiment 3 comprises the following steps:
(1) carrying out polymerization reaction on the ethylene-octene copolymer, the impact modifier and the initiator at 140 ℃;
(2) adding the filler into the coupling agent and mixing at 10 ℃;
(3) putting the products obtained in the steps (1) and (2), polyvinyl chloride resin, PCV scrap, a foaming agent, a foaming regulator, a filler, an antioxidant, a lubricant and a heat stabilizer into a mixer according to a ratio for mixing, wherein the mixing temperature is kept at 180 ℃, and the mixing time is 30 min;
(4) and taking out the mixture for extrusion molding, obtaining a molten material through an extruder, carrying out vacuum negative pressure cooling and shaping on the molten material, cooling and molding the molten material through a cooling system to obtain a tray, and carrying out post-treatment on the molded tray to obtain the PVC tray.
Comparative example 1
The PVC tray of comparative example 1 comprises the following raw materials in parts by mass:
wherein:
the polyvinyl chloride resin is a compound of SG-5 and SG-8, the mass ratio of SG-8 type PVC resin powder to SG-5 type PVC resin powder is 5.5:1, the average polymerization degree of SG-5 type PVC resin powder is 1000-type 1100, and the average polymerization degree of SG-8 type PVC resin powder is 700-type 750.
The foaming agent is a mixture of 4, 4' -oxybis-benzenesulfonyl hydrazide, azodiisobutyronitrile and azodicarbonamide.
The foaming regulator is a mixture of methyl methacrylate and butyl acrylate.
The impact modifier is a composition of trifluoroethyl methacrylate, nitrile rubber and n-octyl acrylate.
The initiator is peroxide, and the peroxide is bis (2-ethyl) hexyl peroxydicarbonate.
The filler is a mixture of red mud and gold tailings, and the weight ratio of the red mud to the gold tailings is 1: 1; the chemical composition of the red mud is SiO2 12.3%、Al2O3 33.5%、Fe2O3 7.6%、CaO 21.3%、MgO 1.2%、TiO23.5%、K2O0.5%、Na23.7 percent of O and 16.4 percent of loss on ignition; the chemistry of the gold tailingsHas the composition of SiO270.5%、Al2O3 17%、K2O 3%、Na2O 3%、CaO 2%、MgO 0.2%、Fe2O3 1%、TiO20.1% and traces of zirconium dioxide, zinc oxide and barium oxide.
The antioxidant is triphenyl phosphite.
The lubricant is stearic acid.
The coupling agent is a mixture of gamma-glycidylpropylmethyldimethoxysilane and polyvinyl alcohol.
The heat stabilizer is a calcium-zinc composite stabilizer.
The preparation method described in this comparative example 1 is the same as that of example 2.
Comparative example 2
The PVC tray of comparative example 2 comprises the following raw materials in parts by mass:
wherein:
the polyvinyl chloride resin is a compound of SG-5 and SG-8, the mass ratio of SG-8 type PVC resin powder to SG-5 type PVC resin powder is 5.5:1, the average polymerization degree of SG-5 type PVC resin powder is 1000-type 1100, and the average polymerization degree of SG-8 type PVC resin powder is 700-type 750.
The foaming agent is a mixture of 4, 4' -oxybis-benzenesulfonyl hydrazide, azodiisobutyronitrile and azodicarbonamide.
The foaming regulator is a mixture of methyl methacrylate and butyl acrylate.
The impact modifier is a composition of trifluoroethyl methacrylate and nitrile rubber.
The initiator is peroxide, and the peroxide is bis (2-ethyl) hexyl peroxydicarbonate.
The filler is red mud and gold tailThe weight ratio of the red mud to the gold tailings is 1: 1; the chemical composition of the red mud is SiO2 12.3%、Al2O3 33.5%、Fe2O3 7.6%、CaO 21.3%、MgO 1.2%、TiO23.5%、K2O0.5%、Na23.7 percent of O and 16.4 percent of loss on ignition; the chemical composition of the gold tailings is SiO270.5%、Al2O3 17%、K2O 3%、Na2O 3%、CaO 2%、MgO 0.2%、Fe2O3 1%、TiO20.1% and traces of zirconium dioxide, zinc oxide and barium oxide.
The antioxidant is triphenyl phosphite.
The lubricant is stearic acid.
The coupling agent is a mixture of gamma-glycidylpropylmethyldimethoxysilane and polyvinyl alcohol.
The heat stabilizer is a calcium-zinc composite stabilizer.
The preparation method described in this comparative example 2 is the same as that of example 2.
Comparative example 3
The raw materials for the PVC pallet and the preparation method thereof described in comparative example 3 are the same as those of comparative example 2, except that the impact modifier is a combination of nitrile rubber and n-octyl acrylate.
Comparative example 4
The raw materials for the PVC pallet and the preparation method thereof described in comparative example 4 are the same as those of comparative example 2, except that the impact modifier is a combination of trifluoroethyl methacrylate and n-octyl acrylate.
The PVC trays prepared in examples 1 to 3 and comparative examples 1 to 4 were subjected to performance tests, and the results are shown in table 1 below:
Claims (10)
2. the PVC tray of claim 1, wherein: the polyvinyl chloride resin is a compound of SG-5 and SG-8, the mass ratio of SG-8 type PVC resin powder to SG-5 type PVC resin powder is 3.5-5.5:1, the average polymerization degree of SG-5 type PVC resin powder is 1000-type 1100, and the average polymerization degree of SG-8 type PVC resin powder is 700-type 750.
3. The PVC tray of claim 1, wherein: the foaming agent is at least two of p-toluenesulfonyl azide, 4' -oxybis-benzenesulfonyl hydrazide, azodiisobutyronitrile or azodicarbonamide; the foaming regulator is one or more of methyl methacrylate, methyl acrylate or butyl acrylate.
4. The PVC tray of claim 1, wherein: the impact modifier is a composition of trifluoroethyl methacrylate, nitrile rubber and n-octyl acrylate.
5. The PVC tray of claim 1, wherein: the initiator is peroxide, and the peroxide is one or more of diisopropyl peroxydicarbonate, dibenzoyl peroxide, dicyclohexyl peroxydicarbonate, lauroyl peroxide, diphenoxyethyl peroxydicarbonate or bis (2-ethyl) hexyl peroxydicarbonate.
6. The PVC tray of claim 1, wherein: the filler is one or two of red mud, gold tailings, bacterial cellulose or expanded perlite powder.
7. The PVC tray of claim 6, wherein: the filler is a mixture of red mud and gold tailings, and the weight ratio of the red mud to the gold tailings is 1: 1.
8. The PVC tray of claim 1, wherein: the antioxidant is one or more of octadecyl-3- (3, 5-di-tert-butyl-4-hydroxyphenyl) propionate, triphenyl phosphite, tetra [ beta- (3, 5-di-tert-butyl-4-hydroxyphenyl) propionic acid ] pentaerythritol ester or dilauryl thiodipropionate; the heat stabilizer is a calcium-zinc composite stabilizer.
9. The PVC tray of claim 1, wherein: the lubricant is one or more of pentaerythritol stearate, stearic acid, polyethylene wax or Fischer-Tropsch wax; the coupling agent is one or more of 3-glycidyl ether oxypropyl triethoxysilane, gamma-glycidyl propyl methyldimethoxysilane, sodium dodecyl benzene sulfonate, polyether silicone oil or polyvinyl alcohol.
10. A method for preparing the PVC tray of claim 1, characterized in that: the method comprises the following steps:
(1) carrying out polymerization reaction on the ethylene-octene copolymer, the impact modifier and the initiator at the temperature of 140 ℃ and 150 ℃;
(2) adding the filler into the coupling agent and mixing at the temperature of 100-120 ℃;
(3) putting the products obtained in the step (1) and the step (2), polyvinyl chloride resin, PCV scrap, a foaming agent, a foaming regulator, a filler, an antioxidant, a lubricant and a heat stabilizer into a mixer according to a ratio for mixing, wherein the mixing temperature is kept at 190 ℃ and the mixing time is 20-30 min;
(4) and taking out the mixture for extrusion molding, obtaining a molten material through an extruder, carrying out vacuum negative pressure cooling and shaping on the molten material, cooling and molding the molten material through a cooling system to obtain a tray, and carrying out post-treatment on the molded tray to obtain the PVC tray.
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Application publication date: 20201225 |