CN101260227B - A kind of preparation method of halogen-free flame-retardant polylactic acid - Google Patents
A kind of preparation method of halogen-free flame-retardant polylactic acid Download PDFInfo
- Publication number
- CN101260227B CN101260227B CN2008100365537A CN200810036553A CN101260227B CN 101260227 B CN101260227 B CN 101260227B CN 2008100365537 A CN2008100365537 A CN 2008100365537A CN 200810036553 A CN200810036553 A CN 200810036553A CN 101260227 B CN101260227 B CN 101260227B
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- China
- Prior art keywords
- polylactic acid
- flame retardant
- flame
- retardant
- halogen
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- 239000003063 flame retardant Substances 0.000 title claims abstract description 124
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 title claims abstract description 110
- 229920000747 poly(lactic acid) Polymers 0.000 title claims abstract description 66
- 239000004626 polylactic acid Substances 0.000 title claims abstract description 66
- 238000002360 preparation method Methods 0.000 title claims abstract description 14
- 239000000203 mixture Substances 0.000 claims abstract description 51
- 239000007822 coupling agent Substances 0.000 claims abstract description 23
- 239000003963 antioxidant agent Substances 0.000 claims abstract description 21
- 230000003078 antioxidant effect Effects 0.000 claims abstract description 19
- 239000000463 material Substances 0.000 claims abstract description 19
- 239000004114 Ammonium polyphosphate Substances 0.000 claims description 19
- 229920001276 ammonium polyphosphate Polymers 0.000 claims description 19
- 235000019826 ammonium polyphosphate Nutrition 0.000 claims description 19
- WXZMFSXDPGVJKK-UHFFFAOYSA-N pentaerythritol Chemical compound OCC(CO)(CO)CO WXZMFSXDPGVJKK-UHFFFAOYSA-N 0.000 claims description 16
- -1 phenylene diisodecyl phosphite Chemical compound 0.000 claims description 16
- GUJOJGAPFQRJSV-UHFFFAOYSA-N dialuminum;dioxosilane;oxygen(2-);hydrate Chemical group O.[O-2].[O-2].[O-2].[Al+3].[Al+3].O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O GUJOJGAPFQRJSV-UHFFFAOYSA-N 0.000 claims description 15
- 229910052901 montmorillonite Inorganic materials 0.000 claims description 15
- 239000000654 additive Substances 0.000 claims description 13
- 238000001125 extrusion Methods 0.000 claims description 12
- 229920000877 Melamine resin Polymers 0.000 claims description 10
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims description 10
- JDSHMPZPIAZGSV-UHFFFAOYSA-N melamine Chemical compound NC1=NC(N)=NC(N)=N1 JDSHMPZPIAZGSV-UHFFFAOYSA-N 0.000 claims description 10
- 239000002202 Polyethylene glycol Substances 0.000 claims description 9
- 239000006087 Silane Coupling Agent Substances 0.000 claims description 9
- 229920001223 polyethylene glycol Polymers 0.000 claims description 9
- 238000003756 stirring Methods 0.000 claims description 8
- 239000004632 polycaprolactone Substances 0.000 claims description 7
- 229920001610 polycaprolactone Polymers 0.000 claims description 7
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 6
- 239000005014 poly(hydroxyalkanoate) Substances 0.000 claims description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 5
- JKIJEFPNVSHHEI-UHFFFAOYSA-N Phenol, 2,4-bis(1,1-dimethylethyl)-, phosphite (3:1) Chemical group 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 claims description 5
- 230000000996 additive effect Effects 0.000 claims description 5
- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical compound [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 claims description 5
- 239000008116 calcium stearate Substances 0.000 claims description 5
- 235000013539 calcium stearate Nutrition 0.000 claims description 5
- 150000002148 esters Chemical class 0.000 claims description 5
- 239000010439 graphite Substances 0.000 claims description 5
- 229910002804 graphite Inorganic materials 0.000 claims description 5
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 claims description 5
- 239000000347 magnesium hydroxide Substances 0.000 claims description 5
- 229910001862 magnesium hydroxide Inorganic materials 0.000 claims description 5
- ZQKXQUJXLSSJCH-UHFFFAOYSA-N melamine cyanurate Chemical compound NC1=NC(N)=NC(N)=N1.O=C1NC(=O)NC(=O)N1 ZQKXQUJXLSSJCH-UHFFFAOYSA-N 0.000 claims description 5
- XZZNDPSIHUTMOC-UHFFFAOYSA-N triphenyl phosphate Chemical compound C=1C=CC=CC=1OP(OC=1C=CC=CC=1)(=O)OC1=CC=CC=C1 XZZNDPSIHUTMOC-UHFFFAOYSA-N 0.000 claims description 5
- XOOUIPVCVHRTMJ-UHFFFAOYSA-L zinc stearate Chemical compound [Zn+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O XOOUIPVCVHRTMJ-UHFFFAOYSA-L 0.000 claims description 5
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims description 4
- 229910019142 PO4 Inorganic materials 0.000 claims description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 4
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 4
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims description 4
- 239000010452 phosphate Substances 0.000 claims description 4
- 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 4
- WGKLOLBTFWFKOD-UHFFFAOYSA-N tris(2-nonylphenyl) phosphite Chemical compound CCCCCCCCCC1=CC=CC=C1OP(OC=1C(=CC=CC=1)CCCCCCCCC)OC1=CC=CC=C1CCCCCCCCC WGKLOLBTFWFKOD-UHFFFAOYSA-N 0.000 claims description 4
- 229920002472 Starch Polymers 0.000 claims description 3
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 3
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 claims description 3
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 3
- 239000003795 chemical substances by application Substances 0.000 claims description 3
- 229920000903 polyhydroxyalkanoate Polymers 0.000 claims description 3
- 235000019698 starch Nutrition 0.000 claims description 3
- 239000008107 starch Substances 0.000 claims description 3
- 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 description 2
- YEVQZPWSVWZAOB-UHFFFAOYSA-N 2-(bromomethyl)-1-iodo-4-(trifluoromethyl)benzene Chemical compound FC(F)(F)C1=CC=C(I)C(CBr)=C1 YEVQZPWSVWZAOB-UHFFFAOYSA-N 0.000 claims description 2
- 229910021536 Zeolite Inorganic materials 0.000 claims description 2
- JBTXGEJRJCNRLU-UHFFFAOYSA-N [2-(dihydroxyphosphanyloxymethyl)-3-hydroxy-2-(hydroxymethyl)propyl] dihydrogen phosphite Chemical compound OP(O)OCC(CO)(CO)COP(O)O JBTXGEJRJCNRLU-UHFFFAOYSA-N 0.000 claims description 2
- 229910000410 antimony oxide Inorganic materials 0.000 claims description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 claims description 2
- 239000004567 concrete Substances 0.000 claims description 2
- 239000003431 cross linking reagent Substances 0.000 claims description 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 2
- 239000003822 epoxy resin Substances 0.000 claims description 2
- VTRUBDSFZJNXHI-UHFFFAOYSA-N oxoantimony Chemical compound [Sb]=O VTRUBDSFZJNXHI-UHFFFAOYSA-N 0.000 claims description 2
- 229920000647 polyepoxide Polymers 0.000 claims description 2
- 239000000377 silicon dioxide Substances 0.000 claims description 2
- 235000012239 silicon dioxide Nutrition 0.000 claims description 2
- ISIJQEHRDSCQIU-UHFFFAOYSA-N tert-butyl 2,7-diazaspiro[4.5]decane-7-carboxylate Chemical compound C1N(C(=O)OC(C)(C)C)CCCC11CNCC1 ISIJQEHRDSCQIU-UHFFFAOYSA-N 0.000 claims description 2
- 239000004408 titanium dioxide Substances 0.000 claims description 2
- 235000010215 titanium dioxide Nutrition 0.000 claims description 2
- STCOOQWBFONSKY-UHFFFAOYSA-N tributyl phosphate Chemical compound CCCCOP(=O)(OCCCC)OCCCC STCOOQWBFONSKY-UHFFFAOYSA-N 0.000 claims description 2
- JZZBTMVTLBHJHL-UHFFFAOYSA-N tris(2,3-dichloropropyl) phosphate Chemical compound ClCC(Cl)COP(=O)(OCC(Cl)CCl)OCC(Cl)CCl JZZBTMVTLBHJHL-UHFFFAOYSA-N 0.000 claims description 2
- BIKXLKXABVUSMH-UHFFFAOYSA-N trizinc;diborate Chemical compound [Zn+2].[Zn+2].[Zn+2].[O-]B([O-])[O-].[O-]B([O-])[O-] BIKXLKXABVUSMH-UHFFFAOYSA-N 0.000 claims description 2
- 239000010457 zeolite Substances 0.000 claims description 2
- 238000012360 testing method Methods 0.000 abstract description 22
- 238000000034 method Methods 0.000 abstract description 9
- 239000002861 polymer material Substances 0.000 abstract description 4
- 239000012752 auxiliary agent Substances 0.000 abstract 1
- 238000002485 combustion reaction Methods 0.000 description 12
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 8
- 229910052760 oxygen Inorganic materials 0.000 description 8
- 239000001301 oxygen Substances 0.000 description 8
- 238000002156 mixing Methods 0.000 description 7
- 238000009776 industrial production Methods 0.000 description 5
- 230000004048 modification Effects 0.000 description 5
- 238000012986 modification Methods 0.000 description 5
- 229910052698 phosphorus Inorganic materials 0.000 description 5
- 239000011574 phosphorus Substances 0.000 description 5
- DXZMANYCMVCPIM-UHFFFAOYSA-L zinc;diethylphosphinate Chemical compound [Zn+2].CCP([O-])(=O)CC.CCP([O-])(=O)CC DXZMANYCMVCPIM-UHFFFAOYSA-L 0.000 description 5
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 3
- 238000011161 development Methods 0.000 description 3
- WSQZNZLOZXSBHA-UHFFFAOYSA-N 3,8-dioxabicyclo[8.2.2]tetradeca-1(12),10,13-triene-2,9-dione Chemical compound O=C1OCCCCOC(=O)C2=CC=C1C=C2 WSQZNZLOZXSBHA-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 229920000742 Cotton Polymers 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- WOZVHXUHUFLZGK-UHFFFAOYSA-N dimethyl terephthalate Chemical compound COC(=O)C1=CC=C(C(=O)OC)C=C1 WOZVHXUHUFLZGK-UHFFFAOYSA-N 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000012768 molten material Substances 0.000 description 2
- 229920000728 polyester Polymers 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 235000016936 Dendrocalamus strictus Nutrition 0.000 description 1
- 235000016735 Manihot esculenta subsp esculenta Nutrition 0.000 description 1
- 241000658379 Manihot esculenta subsp. esculenta Species 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 239000007983 Tris buffer Substances 0.000 description 1
- 239000012620 biological material Substances 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- PYFRLDVYGBCYLI-UHFFFAOYSA-N decyl dihydrogen phosphite Chemical compound CCCCCCCCCCOP(O)O PYFRLDVYGBCYLI-UHFFFAOYSA-N 0.000 description 1
- 239000000539 dimer Substances 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 230000026030 halogenation Effects 0.000 description 1
- 238000005658 halogenation reaction Methods 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 229910001853 inorganic hydroxide Inorganic materials 0.000 description 1
- 230000002687 intercalation Effects 0.000 description 1
- 238000009830 intercalation Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 239000002114 nanocomposite Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- XFZRQAZGUOTJCS-UHFFFAOYSA-N phosphoric acid;1,3,5-triazine-2,4,6-triamine Chemical compound OP(O)(O)=O.NC1=NC(N)=NC(N)=N1 XFZRQAZGUOTJCS-UHFFFAOYSA-N 0.000 description 1
- OJMIONKXNSYLSR-UHFFFAOYSA-N phosphorous acid Chemical compound OP(O)O OJMIONKXNSYLSR-UHFFFAOYSA-N 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920000052 poly(p-xylylene) Polymers 0.000 description 1
- 229920000139 polyethylene terephthalate Polymers 0.000 description 1
- 239000005020 polyethylene terephthalate Substances 0.000 description 1
- 238000012667 polymer degradation Methods 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 239000012815 thermoplastic material Substances 0.000 description 1
- 239000002341 toxic gas Substances 0.000 description 1
- 239000013638 trimer Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
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- 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
-
- 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
- B29C2948/9259—Angular 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
-
- 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
- B29C2948/92819—Location or phase of control
- B29C2948/92857—Extrusion unit
- B29C2948/92876—Feeding, melting, plasticising or pumping zones, e.g. the melt itself
- B29C2948/92885—Screw or gear
-
- 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
- B29C2948/92819—Location or phase of control
- B29C2948/92857—Extrusion unit
- B29C2948/92876—Feeding, melting, plasticising or pumping zones, e.g. the melt itself
- B29C2948/92895—Barrel or housing
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Biological Depolymerization Polymers (AREA)
Abstract
本发明属于高分子材料技术领域,具体涉及一种无卤阻燃聚乳酸的制备方法。具体制备步骤为:先将阻燃剂、阻燃助剂、抗氧剂按照一定比例搅拌得到阻燃混合物,再将聚乳酸、阻燃混合物、增容剂、偶联剂按照一定比例混合后熔融共混,物料经冷却、切粒、干燥得到阻燃的聚乳酸。阻燃的聚乳酸具有良好的阻燃性能,能通过UL94级测试,并且具有较少的熔融滴落物,可用于飞机、汽车、电子等对材料阻燃性能要求苛刻的领域。The present invention belongs to the technical field of polymer materials, and specifically relates to a method for preparing halogen-free flame-retardant polylactic acid. The specific preparation steps are: firstly, a flame retardant, a flame retardant auxiliary agent, and an antioxidant are stirred in a certain proportion to obtain a flame retardant mixture, and then polylactic acid, the flame retardant mixture, a compatibilizer, and a coupling agent are mixed in a certain proportion and melt-blended, and the material is cooled, pelletized, and dried to obtain flame-retardant polylactic acid. The flame-retardant polylactic acid has good flame retardant properties, can pass the UL94 test, and has less molten dripping, and can be used in fields such as aircraft, automobiles, and electronics that have strict requirements on the flame retardant properties of materials.
Description
技术领域 technical field
本发明属于高分子材料改性技术领域,具体涉及一种无卤阻燃聚乳酸的制备方法。 The invention belongs to the technical field of polymer material modification, and in particular relates to a preparation method of halogen-free flame-retardant polylactic acid. the
背景技术Background technique
能源问题和环境问题促进了生物材料的发展与应用。聚乳酸是一种原料来源于可再生的非主食农产品(如木薯)淀粉并且可以完全降解成二氧化碳和水的“绿色高分子”材料。聚乳酸不仅可降解,而且还具有许多良好的机械性能和加工性能,被称为最优前景的“绿色塑料”。然而聚乳酸和其它高分子一样,易于燃烧,限制了聚乳酸在航空、电子、汽车等领域的应用,需要通过改性的方法赋予聚乳酸阻燃性能。 Energy issues and environmental issues have promoted the development and application of biomaterials. Polylactic acid is a "green polymer" material whose raw material is derived from renewable non-staple agricultural products (such as cassava) starch and can be completely degraded into carbon dioxide and water. Polylactic acid is not only degradable, but also has many good mechanical properties and processing properties, and is known as the most promising "green plastic". However, polylactic acid, like other polymers, is easy to burn, which limits the application of polylactic acid in aviation, electronics, automobiles and other fields. It is necessary to endow polylactic acid with flame retardant properties by modification. the
添加型阻燃剂与高分子材料共混是材料阻燃改性能的常用方法。含卤阻燃剂具有较高的阻燃性能,常用于热塑性高分子材料的阻燃改性。但随着阻燃技术的发展,人们发现利用含卤阻燃剂阻燃的材料再燃烧时生成卤化氢等有毒气体,同时含卤阻燃剂及其燃烧时的生成物具有致癌作用,因此目前欧美等发达国家已经对部分含卤阻燃剂发布了禁令。阻燃技术的无卤化是未来材料阻燃改性的发展方向。 The blending of additive flame retardants and polymer materials is a common method for flame retardancy modification of materials. Halogenated flame retardants have high flame retardant properties and are often used in the flame retardant modification of thermoplastic polymer materials. However, with the development of flame retardant technology, it has been found that toxic gases such as hydrogen halides are generated when the flame retardant materials are re-burned. At the same time, the halogen-containing flame retardants and their combustion products have carcinogenic effects. Therefore, at present Developed countries such as Europe and the United States have issued bans on some halogenated flame retardants. The non-halogenation of flame retardant technology is the development direction of flame retardant modification of materials in the future. the
可以阻燃聚酯类材料的无卤阻燃剂有:磷系阻燃剂,如红磷、聚磷酸铵、磷酸三聚氰胺;无机氢氧化物,如氢氧化铝、氢氧化镁等;硅系阻燃剂,如层状硅酸盐等。Galina F等(Polym Int,2000,49:1095-1100)把含磷阻燃剂与对苯二甲酸丁二醇酯在高搅机中混合均匀,混合物在230-240℃下熔融切片,最后把得到的产物230-240℃、30吨的压力下热压。所得产物的阻燃性能可以达到UL94 V-0级。在国内,哈尔滨工业大学、四川大学等高校在无卤阻燃聚酯类高聚物方面进行了研究,虽然在阻燃方面取得了一些进展,但是最大的缺点在于工业化生产困难。Junfeng Xiao等(Polymer Degradation and Stability,2006,91:2093-2100)把阻燃剂三聚氰胺、磷酸三苯酯与对苯二甲酸丁二醇酯颗粒经二辊式轧机熔融共混(温度:235℃,转数:100)。当三聚氰胺、磷酸三苯酯在复合材料中的含量为10wt%、20%wt%时,能通过UL94V-0级测试。四川大学2002年申请专利《含磷阻燃聚对苯二甲酸乙二醇酯/层状硅酸盐纳米复合材料及其制备方法和用途》(CN1396206),该专利提到应用层状硅酸盐、反应型含磷阻燃剂及其他助剂阻燃对苯二甲酸二甲酯。所得产物具有阻燃性能、力学性能,但该专利缺点是应用反应型含磷阻燃剂,采用原位插层聚合法,不利于工业化生产。无卤阻燃的热塑性材料在燃烧时伴随有大量的熔融物滴落,特别 是应用磷酸酯类阻燃剂时,随着阻燃剂用量的加大,滴落现象变得相当严重,极大限制了材料的应用范围。 Halogen-free flame retardants that can flame-retardant polyester materials include: phosphorus-based flame retardants, such as red phosphorus, ammonium polyphosphate, melamine phosphate; inorganic hydroxides, such as aluminum hydroxide, magnesium hydroxide, etc.; silicon-based flame retardants Burning agent, such as layered silicate, etc. Galina F et al. (Polym Int, 2000, 49: 1095-1100) mixed the phosphorus-containing flame retardant and butylene terephthalate in a high mixer, and melted the mixture at 230-240°C, and finally The obtained product is hot-pressed at 230-240° C. and a pressure of 30 tons. The flame retardancy of the obtained product can reach UL94 V-0 level. In China, Harbin Institute of Technology, Sichuan University and other universities have conducted research on halogen-free flame-retardant polyester polymers. Although some progress has been made in flame-retardant, the biggest disadvantage is the difficulty in industrial production. Junfeng Xiao et al. (Polymer Degradation and Stability, 2006, 91: 2093-2100) melt-blended the flame retardant melamine, triphenyl phosphate and butylene terephthalate particles through a two-roll mill (temperature: 235°C , number of revolutions: 100). When the content of melamine and triphenyl phosphate in the composite material is 10wt%, 20wt%, it can pass the UL94V-0 level test. In 2002, Sichuan University applied for a patent "Phosphorus-containing flame-retardant polyethylene terephthalate/layered silicate nanocomposite material and its preparation method and application" (CN1396206), which mentioned the application of layered silicate , Reactive phosphorus-containing flame retardants and other additives flame retardant dimethyl terephthalate. The resulting product has flame retardant and mechanical properties, but the disadvantage of this patent is that it uses a reactive phosphorus-containing flame retardant and uses an in-situ intercalation polymerization method, which is not conducive to industrial production. Halogen-free flame-retardant thermoplastic materials are accompanied by a large amount of molten material dripping when burning, especially when phosphoric ester flame retardants are used, as the amount of flame retardants increases, the dripping phenomenon becomes quite serious, which is extremely large. The application range of the material is limited. the
针对这种情况,本专利提供了一种适合工业化生产环境友好、可生物降解的聚乳酸阻燃材料的制备方法,并且通过添加蒙脱土、硬脂酸锌等阻燃助剂来减少材料燃烧时熔融物的滴落。此方法具有工艺简单、生产能力高等特点,具有重要的实际应用价值。 In response to this situation, this patent provides a method for preparing environmentally friendly and biodegradable polylactic acid flame-retardant materials suitable for industrial production, and reduces material combustion by adding flame-retardant additives such as montmorillonite and zinc stearate When the melt drips. This method has the characteristics of simple process and high production capacity, and has important practical application value. the
发明内容Contents of the invention
本发明的目的是提供一种适合工业化生产的无卤阻燃聚乳酸的制备方法。 The purpose of the present invention is to provide a method for preparing halogen-free flame-retardant polylactic acid suitable for industrial production. the
本发明提出的无卤阻燃聚乳酸的制备方法,是先将阻燃剂进行表面改性,再将改性后的阻燃剂、聚乳酸、其它助剂共混挤出得到产品。 The preparation method of the halogen-free flame-retardant polylactic acid proposed by the present invention is to firstly modify the surface of the flame retardant, and then blend and extrude the modified flame retardant, polylactic acid and other additives to obtain a product. the
本发明提出的无卤阻燃聚乳酸的制备方法,具体步骤如下: The preparation method of the halogen-free flame-retardant polylactic acid that the present invention proposes, concrete steps are as follows:
(1)将聚乳酸、阻燃剂分别在30~120℃下真空干燥1~24小时,以除去水分; (1) Vacuum dry the polylactic acid and the flame retardant respectively at 30-120°C for 1-24 hours to remove moisture;
(2)将步骤(1)得到的处理后的阻燃剂与阻燃助剂、抗氧剂按照重量比在干燥的容器内进行搅拌,使其混合均匀,得到阻燃混合物;其各组分的重量百分比为: (2) Stir the treated flame retardant obtained in step (1) with flame retardant aids and antioxidants in a dry container according to the weight ratio to mix them evenly to obtain a flame retardant mixture; its components The weight percentage is:
阻燃剂 69~98.5wt% Flame retardant 69~98.5wt%
阻燃助剂 0.5~30wt% Flame retardant additive 0.5~30wt%
抗氧剂 1~10wt% Antioxidant 1~10wt%
其总重量满足100%; Its total weight satisfies 100%;
(3)将步骤(1)得到的处理后的聚乳酸、步骤(2)得到的阻燃混合物、偶联剂、增容剂按重量比加入到干燥的容器内,混合均匀,然后熔融共混;采用挤出机或双辊开炼机得到所需产品;其中各组成的重量百分比为: (3) Add the treated polylactic acid obtained in step (1), the flame retardant mixture obtained in step (2), coupling agent, and compatibilizer into a dry container by weight ratio, mix well, and then melt blend ; Adopt extruder or two-roll mill to obtain required product; Wherein the weight percent of each composition is:
聚乳酸 59.4~95wt% Polylactic acid 59.4~95wt%
阻燃混合物 2~40wt% Flame retardant mixture 2~40wt%
偶联剂 0.5~8wt% Coupling agent 0.5~8wt%
其余为增容剂,其总重量满足100%; The rest are compatibilizers, the total weight of which satisfies 100%;
本发明中,步骤(3)中所述采用挤出机,其螺杆转速为15~280rpm,挤出温度为100~190℃,物料挤出后经冷却、切粒、干燥即可。 In the present invention, an extruder is used as described in step (3), the screw speed of which is 15-280 rpm, and the extrusion temperature is 100-190° C. After the material is extruded, it can be cooled, pelletized and dried. the
本发明中,步骤(3)中所述采用双辊开炼机,双辊开炼机的前辊温度为80~180℃,后辊温度为60~170℃。 In the present invention, the two-roll mill is adopted as described in step (3), the temperature of the front roll of the two-roll mill is 80-180°C, and the temperature of the rear roll is 60-170°C. the
本发明中,所述聚乳酸的重均分子量为1×105~3×105。 In the present invention, the polylactic acid has a weight average molecular weight of 1×10 5 to 3×10 5 .
本发明中,所述阻燃剂为不含卤素的无卤阻燃剂,具体为蒙脱土、氢氧化铝、磷酸、亚磷酸、聚磷酸铵、磷酸三苯酯、磷酸三辛酯、磷酸三丁酯、磷酸三(2,3一二氯丙基)、 亚磷酸三苯酯、磷酸盐、氰尿酸三聚氰胺、膨胀型石墨或红磷等中的一种或者几种混合使用。 In the present invention, the flame retardant is a halogen-free flame retardant, specifically montmorillonite, aluminum hydroxide, phosphoric acid, phosphorous acid, ammonium polyphosphate, triphenyl phosphate, trioctyl phosphate, phosphoric acid One or more of tributyl phosphate, tris(2,3-dichloropropyl) phosphate, triphenyl phosphite, phosphate, melamine cyanurate, expanded graphite or red phosphorus are used in combination. the
本发明中,所述阻燃助剂为季戊四醇、三聚氰胺、淀粉、二氧化钛、硬脂酸钙、硬脂酸锌、碳酸钙、硼酸锌、氧化锑、沸石、二氧化硅、氢氧化镁、抗滴落剂或交联剂等中的一种或几种。 In the present invention, the flame retardant additives are pentaerythritol, melamine, starch, titanium dioxide, calcium stearate, zinc stearate, calcium carbonate, zinc borate, antimony oxide, zeolite, silicon dioxide, magnesium hydroxide, antidripping One or more of falling agents or cross-linking agents. the
本发明中,所述偶联剂为钛酸脂或硅烷偶联剂等中的一种或多种。 In the present invention, the coupling agent is one or more of titanate or silane coupling agents. the
本发明中,所述增容剂为聚己内酯(PCL)、聚羟基脂肪酸酯(PHA)、聚乙二醇(PEG)或环氧树脂等中一至多种。 In the present invention, the compatibilizer is one or more of polycaprolactone (PCL), polyhydroxyalkanoate (PHA), polyethylene glycol (PEG) or epoxy resin. the
本发明中,所述抗氧剂为亚磷酸三(2,4-二叔丁基苯基)酯、亚磷酸酯三(2,4-二特丁基苯基)酯、亚磷酸苯二异癸酯、三(壬基代苯基)亚磷酸酯或亚磷酸三(壬基苯酯)、季戊四醇双亚磷酸酯二(2,4-二特丁基苯基)酯、多烷基双酚A亚磷酸酯的双聚体或三聚体的复合物等中一至多种。 In the present invention, the antioxidant is tris(2,4-di-tert-butylphenyl) phosphite, tris(2,4-di-tert-butylphenyl) phosphite, diisophenylene phosphite Decyl ester, tris(nonylphenyl)phosphite or tris(nonylphenyl)phosphite, pentaerythritol bisphosphite bis(2,4-di-tert-butylphenyl)ester, polyalkylbisphenol One or more of the dimer or trimer complex of A phosphite. the
本发明的优点在于: The advantages of the present invention are:
(1)选用环境友好的无卤阻燃剂与聚乳酸进行复合,所得的制品完全满足环保的要求。 (1) Select an environment-friendly halogen-free flame retardant to compound with polylactic acid, and the obtained product fully meets the requirements of environmental protection. the
(2)选用无卤阻燃剂与聚乳酸进行复合,所得的制品具有良好的阻燃性能,制品满足UL 94V0或UL 94V1级标准,可应用于航空、汽车、电子等对阻燃性能要求苛刻的领域。 (2) Composite halogen-free flame retardants and polylactic acid, the resulting products have good flame retardant properties, and the products meet UL 94V0 or UL 94V1 standards, and can be used in aviation, automobiles, electronics, etc., which have strict requirements on flame retardant properties field of. the
(3)制备方法简单有效、工艺条件温和,适用于工业化生产。 (3) The preparation method is simple and effective, the process conditions are mild, and it is suitable for industrial production. the
(4)可以根据产品的要求调节阻燃剂的用量、配方,控制生产成本; (4) The dosage and formula of the flame retardant can be adjusted according to the requirements of the product to control the production cost;
具体实施方式Detailed ways
下面通过实施例进一步描述本发明。 The present invention is further described below by way of examples. the
实施例1 Example 1
1.将聚乳酸、聚磷酸铵分别在30℃下真空干燥24小时,以除去水分。 1. Vacuum dry polylactic acid and ammonium polyphosphate at 30°C for 24 hours to remove moisture. the
2.将干燥后的阻燃剂聚磷酸铵与阻燃助剂季戊四醇、三聚氰胺、硬脂酸锌、抗氧剂亚磷酸三(2,4-二叔丁基苯基)酯按重量比在干燥的容器内高速搅拌混合均匀,得到阻燃混合物。其中聚磷酸铵为3份、季戊四醇为2份、三聚氰胺为1份,硬脂酸锌1份、抗氧剂为0.5份。 2. The dried flame retardant ammonium polyphosphate and flame retardant additives pentaerythritol, melamine, zinc stearate, antioxidant tris (2,4-di-tert-butylphenyl) phosphite are dried by weight Stir and mix evenly in a container at high speed to obtain a flame retardant mixture. Wherein ammonium polyphosphate is 3 parts, pentaerythritol is 2 parts, melamine is 1 part, zinc stearate is 1 part, and antioxidant is 0.5 part. the
3.将干燥的聚乳酸与步骤(2)得到的阻燃混合物、增容剂聚己内酯、偶联剂钛酸脂LD-101按照一定的重量比在干燥的容器内进行混合,然后在挤出机中进行共混挤出,其中螺杆转数为250rpm,挤出温度为180℃。其中聚乳酸为90份,阻燃混合物为8.5份,偶联剂为0.5份,增容剂1份。物料挤出后经冷却、切粒、干燥得到阻燃的聚乳酸。 3. Mix the dried polylactic acid with the flame retardant mixture obtained in step (2), compatibilizer polycaprolactone, and coupling agent titanate LD-101 in a dry container according to a certain weight ratio, and then mix them in a dry container Blending and extrusion were carried out in an extruder, wherein the screw rotation speed was 250 rpm, and the extrusion temperature was 180°C. Among them, 90 parts of polylactic acid, 8.5 parts of flame retardant mixture, 0.5 parts of coupling agent, and 1 part of compatibilizer. After the material is extruded, it is cooled, pelletized and dried to obtain flame-retardant polylactic acid. the
阻燃性UL-94V试验: Flame retardant UL-94V test:
UL-94V规格:将长127毫米、宽12.7毫米、厚1.6毫米的试验片垂直放置,经测试炉点火10秒,之后移去火焰,测定试验片着火的自熄时间。其次,火焰熄灭的同时立即二次点火10秒钟,同样测试火焰自熄时间。同时考察落下的火种能否点燃脱脂棉。通过第一次和第二次的着火的时间和脱脂棉着火的有无来评价材料燃烧等级。燃烧等级V-0级最高,其次分别为V-1、V-2。 UL-94V specification: place a test piece with a length of 127 mm, a width of 12.7 mm, and a thickness of 1.6 mm vertically, ignite it in the test furnace for 10 seconds, then remove the flame, and measure the self-extinguishing time of the test piece on fire. Secondly, immediately re-ignite for 10 seconds when the flame is extinguished, and also test the flame self-extinguishing time. At the same time, check whether the falling tinder can ignite the absorbent cotton. The fire grade of the material is evaluated by the time of the first and second fires and the presence or absence of fires of absorbent cotton. The combustion grade V-0 is the highest, followed by V-1 and V-2 respectively. the
产品的极限氧指数大于29,可以通过V-1级燃烧测试。 The limiting oxygen index of the product is greater than 29, which can pass the V-1 level combustion test. the
实施例2 Example 2
1.将聚乳酸、蒙脱土、聚磷酸铵分别在80℃下真空干燥3小时,以除去水分。 1. Vacuum dry polylactic acid, montmorillonite, and ammonium polyphosphate at 80°C for 3 hours to remove moisture. the
2.将干燥后的阻燃剂蒙脱土、聚磷酸铵与阻燃助剂季戊四醇、三聚氰胺、抗氧剂亚磷酸三(2,4-二叔丁基苯基)酯按重量比在干燥的容器内高速搅拌混合均匀,得到阻燃混合物。其中蒙脱土为15份、聚磷酸铵为8份、季戊四醇为4份、三聚氰胺为3份,抗氧剂为1份。 2. the dried flame retardant montmorillonite, ammonium polyphosphate and flame retardant additives pentaerythritol, melamine, antioxidant tris (2,4-di-tert-butylphenyl) ester in dry Stir and mix evenly in the container at high speed to obtain a flame retardant mixture. Wherein montmorillonite is 15 parts, ammonium polyphosphate is 8 parts, pentaerythritol is 4 parts, melamine is 3 parts, and antioxidant is 1 part. the
3.将干燥的聚乳酸与步骤(2)得到的阻燃混合物、增容剂聚己内酯、偶联剂硅烷偶联剂KH550按照一定的重量比在干燥的容器内进行混合,然后在挤出机中进行共混挤出,其中螺杆转数为30rpm,挤出温度为150℃。其中聚乳酸为64份,阻燃混合物为31份,偶联剂为4份,增容剂1份。物料挤出后经冷却、切粒、干燥得到阻燃的聚乳酸。 3. Mix the dried polylactic acid with the flame-retardant mixture obtained in step (2), compatibilizer polycaprolactone, and coupling agent silane coupling agent KH550 in a dry container according to a certain weight ratio, and then Blending and extrusion were carried out in the extruder, wherein the screw rotation speed was 30 rpm, and the extrusion temperature was 150°C. Among them, polylactic acid is 64 parts, flame retardant mixture is 31 parts, coupling agent is 4 parts, and compatibilizer is 1 part. After the material is extruded, it is cooled, pelletized and dried to obtain flame-retardant polylactic acid. the
阻燃性UL-94V试验同实施例1。 The flame retardancy UL-94V test is the same as that in Example 1. the
产品的极限氧指数大于30,可以通过V-1级燃烧测试。 The limiting oxygen index of the product is greater than 30, which can pass the V-1 level combustion test. the
实施例3 Example 3
1.将聚乳酸、硬脂酸钙在80℃下真空干燥3小时,以除去水分。 1. Dry polylactic acid and calcium stearate in vacuum at 80°C for 3 hours to remove moisture. the
2.将阻燃剂磷酸三本酯与阻燃助剂硬脂酸钙、抗氧剂亚磷酸苯二异癸酯按重量比在干燥的容器内高速搅拌混合均匀,得到阻燃混合物。其中磷酸三本酯为15份、硬脂酸钙为3份,抗氧剂为1份。 2. Stir and mix the flame retardant tripenyl phosphate, the flame retardant additive calcium stearate, and the antioxidant phenylene diisodecyl phosphite in a dry container at high speed according to the weight ratio to obtain a flame retardant mixture. Among them, 15 parts of tripenyl phosphate, 3 parts of calcium stearate, and 1 part of antioxidant. the
3.将干燥的聚乳酸与步骤(2)得到的阻燃混合物、增容剂聚乙二醇、偶联剂硅烷偶联剂KH550按照一定的重量比在干燥的容器内进行混合,然后在挤出机中进行共混挤出,其中螺杆转数为130rpm,挤出温度为190℃。其中聚乳酸为77.9份,阻燃混合物为19份,偶联剂为3份,增容剂0.1份。物料挤出后经冷却、切粒、干燥得到阻燃的聚乳酸。 3. Mix the dry polylactic acid with the flame retardant mixture obtained in step (2), the compatibilizer polyethylene glycol, and the coupling agent silane coupling agent KH550 in a dry container according to a certain weight ratio, and then extrude Blending and extrusion were carried out in the extruder, wherein the screw rotation speed was 130 rpm, and the extrusion temperature was 190°C. Among them, the polylactic acid is 77.9 parts, the flame retardant mixture is 19 parts, the coupling agent is 3 parts, and the compatibilizer is 0.1 part. After the material is extruded, it is cooled, pelletized and dried to obtain flame-retardant polylactic acid. the
阻燃性UL-94V试验同实例1。 Flame retardancy UL-94V test is the same as Example 1. the
产品的极限氧指数大于29,可以通过V-2级燃烧测试。 The limiting oxygen index of the product is greater than 29, which can pass the V-2 level combustion test. the
实施例4 Example 4
1.将聚乳酸、聚磷酸铵分别在70℃下真空干燥10小时,以除去水分。 1. Vacuum dry polylactic acid and ammonium polyphosphate at 70°C for 10 hours to remove moisture. the
2.将干燥的阻燃剂聚磷酸铵与阻燃助剂氢氧化镁、季戊四醇、抗氧剂亚磷酸苯二异癸酯,按重量比在干燥的容器内高速搅拌混合均匀,得到阻燃混合物。其中氢氧化镁为5份、聚磷酸铵为12份、季戊四醇为6份,抗氧剂为1份。 2. Mix the dry flame retardant ammonium polyphosphate with flame retardant additives magnesium hydroxide, pentaerythritol, and antioxidant phenylene diisodecyl phosphite at high speed in a dry container according to the weight ratio to obtain a flame retardant mixture . Wherein magnesium hydroxide is 5 parts, ammonium polyphosphate is 12 parts, pentaerythritol is 6 parts, and antioxidant is 1 part. the
3.将干燥的聚乳酸与步骤(2)得到的阻燃混合物、增容剂聚乙二醇、偶联剂硅烷偶联剂KH560按照一定的重量比在干燥的容器内进行混合,然后在挤出机中进行共混挤出,其中螺杆转数为150rpm,挤出温度为170℃。其中聚乳酸为75.5份,阻燃混合物为24份,偶联剂为2份,增容剂0.5份。物料挤出后经冷却、切粒、干燥得到阻燃的聚乳酸。 3. Mix the dried polylactic acid with the flame retardant mixture obtained in step (2), compatibilizer polyethylene glycol, and coupling agent silane coupling agent KH560 in a dry container according to a certain weight ratio, and then extrude Blending and extrusion were carried out in the extruder, wherein the screw rotation speed was 150 rpm, and the extrusion temperature was 170°C. Among them, the polylactic acid is 75.5 parts, the flame retardant mixture is 24 parts, the coupling agent is 2 parts, and the compatibilizer is 0.5 parts. After the material is extruded, it is cooled, pelletized and dried to obtain flame-retardant polylactic acid. the
阻燃性UL-94V试验同实施例1。 The flame retardancy UL-94V test is the same as that in Example 1. the
样品的极限氧指数大于31,可以通过V-0级燃烧测试。 The limiting oxygen index of the sample is greater than 31, which can pass the V-0 level combustion test. the
实施例5 Example 5
1.将聚乳酸、膨胀型石墨分别在60℃下真空干燥20小时,以除去水分。 1. Vacuum dry polylactic acid and expanded graphite at 60°C for 20 hours to remove moisture. the
2.将干燥的阻燃剂膨胀型石墨与阻燃剂红磷、阻燃助剂季戊四醇、抗氧剂戊四醇双亚磷酸酯二(2,4-二特丁基苯基)酯,按重量比在干燥的容器内高速搅拌混合均匀,得到阻燃混合物。其中膨胀型石墨为5份、红磷为3份、季戊四醇为1份,抗氧剂为1份。 2. With dry flame retardant expanded graphite and flame retardant red phosphorus, flame retardant additive pentaerythritol, antioxidant pentylene glycol bisphosphite bis (2,4-di-tert-butylphenyl) ester, press Stir and mix evenly at high speed in a dry container to obtain a flame retardant mixture. Among them, 5 parts of expanded graphite, 3 parts of red phosphorus, 1 part of pentaerythritol, and 1 part of antioxidant. the
3.将干燥的聚乳酸与步骤(2)得到的阻燃混合物、增容剂聚乙二醇、偶联剂硅烷偶联剂KH560按照一定的重量比在干燥的容器内进行混合,然后在挤出机中进行共混挤出,其中螺杆转数为70rpm,挤出温度为180℃。其中聚乳酸为88.9份,阻燃混合物为10份,偶联剂为1为份,增容剂0.1份。物料挤出后经冷却、切粒、干燥得到阻燃的聚乳酸。 3. Mix the dried polylactic acid with the flame retardant mixture obtained in step (2), compatibilizer polyethylene glycol, and coupling agent silane coupling agent KH560 in a dry container according to a certain weight ratio, and then extrude Blending and extrusion were carried out in the extruder, wherein the screw rotation speed was 70 rpm, and the extrusion temperature was 180°C. Among them, 88.9 parts of polylactic acid, 10 parts of flame retardant mixture, 1 part of coupling agent, and 0.1 part of compatibilizer. After the material is extruded, it is cooled, pelletized and dried to obtain flame-retardant polylactic acid. the
阻燃性UL-94V试验同实施例1。 The flame retardancy UL-94V test is the same as that in Example 1. the
产品的极限氧指数大于27,可以通过V-2级燃烧测试。 The limiting oxygen index of the product is greater than 27, which can pass the V-2 level combustion test. the
实施例6 Example 6
1.将聚乳酸、聚磷酸铵、蒙脱土在50℃下真空干燥10小时,以除去水分。 1. Dry polylactic acid, ammonium polyphosphate, and montmorillonite in vacuum at 50°C for 10 hours to remove moisture. the
2.将干燥后的聚磷酸铵、蒙脱土与季戊四醇、三聚氰胺、增容剂聚己内酯、抗氧剂亚磷酸苯二异癸酯按重量比在干燥的容器内高速搅拌混合均匀,得到阻燃混合物。其中蒙脱土为25份,聚磷酸铵为45份、季戊四醇为18份、三聚氰胺为8份、聚己内酯3为份、抗氧剂亚磷酸苯二异癸酯为1份。 2. Mix the dried ammonium polyphosphate, montmorillonite, pentaerythritol, melamine, compatibilizer polycaprolactone, and antioxidant phenylene diisodecyl phosphite at a high speed in a dry container by weight ratio to obtain Flame retardant compound. Wherein 25 parts of montmorillonite, 45 parts of ammonium polyphosphate, 18 parts of pentaerythritol, 8 parts of melamine, 3 parts of polycaprolactone, and 1 part of antioxidant phenylene diisodecyl phosphite. the
3.将干燥的聚乳酸与步骤(2)得到的阻燃混合物、增容剂聚乙二醇、偶联剂硅烷偶联剂KH560按照一定的重量比在双辊开炼机上进行共混,得到阻燃聚乳酸。其中前辊温度为140℃,后辊温度100℃,聚乳酸为60.2份,阻燃混合物为38份,增容剂为0.8份,偶联剂为1份。 3. the dry polylactic acid is blended with the flame retardant mixture obtained in step (2), compatibilizer polyethylene glycol, coupling agent silane coupling agent KH560 on a two-roll mill according to a certain weight ratio, to obtain Flame retardant polylactic acid. Among them, the temperature of the front roll is 140°C, the temperature of the back roll is 100°C, the polylactic acid is 60.2 parts, the flame retardant mixture is 38 parts, the compatibilizer is 0.8 parts, and the coupling agent is 1 part. the
阻燃性UL-94V试验同实施例1。 The flame retardancy UL-94V test is the same as that in Example 1. the
产品的极限氧指数大于27,样品可以通过V-0级燃烧测试。 The limiting oxygen index of the product is greater than 27, and the sample can pass the V-0 level combustion test. the
实施例7 Example 7
1.将聚乳酸、聚磷酸铵、蒙脱土在100℃下真空干燥5小时,以除去水分。 1. Dry polylactic acid, ammonium polyphosphate, and montmorillonite in vacuum at 100°C for 5 hours to remove moisture. the
2.将干燥后的聚磷酸铵、蒙脱土与季戊四醇、增容剂聚羟基脂肪酸酯(PHA)、抗氧剂亚磷酸苯二异癸酯按重量比在干燥的容器内高速搅拌混合均匀,得到阻燃预混料。其中蒙脱土为15份,聚磷酸铵为55份、季戊四醇为23份、聚羟基脂肪酸酯为5份、抗氧剂亚磷酸苯二异癸酯为2份。 2. Stir and mix the dried ammonium polyphosphate, montmorillonite and pentaerythritol, compatibilizer polyhydroxyalkanoate (PHA), antioxidant phenylene diisodecyl phosphite at high speed in a dry container according to the weight ratio , to obtain a flame retardant premix. Wherein 15 parts of montmorillonite, 55 parts of ammonium polyphosphate, 23 parts of pentaerythritol, 5 parts of polyhydroxyalkanoate, and 2 parts of antioxidant phenylene diisodecyl phosphite. the
3.将干燥的聚乳酸与步骤(2)得到的阻燃预混阻燃混合物、增容剂聚乙二醇、偶联剂硅烷偶联剂KH550按照一定的重量比在双辊开炼机上进行共混,得到阻燃聚乳酸。其中前辊温度为130℃,后辊温度120℃,聚乳酸为65份,阻燃混合物为33.2份,增容剂为1份,偶联剂为0.8份。 3. Dry polylactic acid and the flame-retardant premixed flame-retardant mixture obtained in step (2), compatibilizer polyethylene glycol, and coupling agent silane coupling agent KH550 are carried out on a double-roll mill according to a certain weight ratio Blending to obtain flame-retardant polylactic acid. Among them, the temperature of the front roll is 130°C, the temperature of the back roll is 120°C, the polylactic acid is 65 parts, the flame retardant mixture is 33.2 parts, the compatibilizer is 1 part, and the coupling agent is 0.8 parts. the
阻燃性UL-94V试验同实施例1。 The flame retardancy UL-94V test is the same as that in Example 1. the
样品的极限氧指数大于28,样品可以通过V-0级燃烧测试。 The limiting oxygen index of the sample is greater than 28, and the sample can pass the V-0 level combustion test. the
实施例8 Example 8
1.将聚乳酸、氰尿酸三聚氰胺、蒙脱土在120℃下真空干燥1小时,以除去水分。 1. Dry polylactic acid, melamine cyanurate, and montmorillonite in vacuum at 120°C for 1 hour to remove moisture. the
2.将干燥后的氰尿酸三聚氰胺、蒙脱土与季戊四醇、增容剂聚羟基脂肪酸酯(PHA)、抗氧剂亚磷酸苯二异癸酯按重量比在干燥的容器内高速搅拌混合均匀,得到阻燃预混料。其中蒙脱土为20份,氰尿酸三聚氰胺为46份、季戊四醇为24份、聚羟基脂肪酸酯为8份、抗氧剂亚磷酸苯二异癸酯为2份。 2. Stir and mix the dried melamine cyanurate, montmorillonite and pentaerythritol, compatibilizer polyhydroxyalkanoate (PHA), antioxidant phenylene diisodecyl phosphite at high speed in a dry container according to the weight ratio , to obtain a flame retardant premix. Wherein 20 parts of montmorillonite, 46 parts of melamine cyanurate, 24 parts of pentaerythritol, 8 parts of polyhydroxyalkanoate, and 2 parts of antioxidant phenylene diisodecyl phosphite. the
3.将干燥的聚乳酸与步骤(2)得到的阻燃混合物、增容剂聚乙二醇、偶联剂硅烷偶联剂KH570按照一定的重量比在双辊开炼机上进行共混,得到阻燃聚乳酸。其中前辊温度为135℃,后辊温度125℃,聚乳酸为85份,阻燃混合物为15份,增容剂为0.9份,偶联剂为0.9份。 3. the dry polylactic acid is blended with the flame retardant mixture obtained in step (2), compatibilizer polyethylene glycol, coupling agent silane coupling agent KH570 on a two-roll mill according to a certain weight ratio, to obtain Flame retardant polylactic acid. The temperature of the front roll is 135°C, the temperature of the back roll is 125°C, the polylactic acid is 85 parts, the flame retardant mixture is 15 parts, the compatibilizer is 0.9 parts, and the coupling agent is 0.9 parts. the
阻燃性UL-94V试验同实施例1。 The flame retardancy UL-94V test is the same as that in Example 1. the
产品的极限氧指数大于28,样品可以通过V-1级燃烧测试,燃烧时熔融物滴落极少。 The limiting oxygen index of the product is greater than 28, and the sample can pass the V-1 level combustion test, and the molten material drips very little when burning. the
此外,与只用无卤阻燃剂(如聚磷酸铵、磷酸三苯酯等)阻燃的聚乳酸相比,用本发明制备的样品在燃烧过程中具有较少的熔融滴落物。 In addition, compared with polylactic acid flame-retardant only with halogen-free flame retardants (such as ammonium polyphosphate, triphenyl phosphate, etc.), the samples prepared with the present invention have less molten drips during combustion. the
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