CN106046681B - A kind of flax fiber element base phosphorus expanding fire retardant and its preparation method and application - Google Patents
A kind of flax fiber element base phosphorus expanding fire retardant and its preparation method and application Download PDFInfo
- Publication number
- CN106046681B CN106046681B CN201610383752.XA CN201610383752A CN106046681B CN 106046681 B CN106046681 B CN 106046681B CN 201610383752 A CN201610383752 A CN 201610383752A CN 106046681 B CN106046681 B CN 106046681B
- Authority
- CN
- China
- Prior art keywords
- flax fiber
- flax
- flame retardant
- carboxyl
- 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.)
- Expired - Fee Related
Links
- 241000208202 Linaceae Species 0.000 title claims abstract description 83
- 235000004431 Linum usitatissimum Nutrition 0.000 title claims abstract description 83
- 239000003063 flame retardant Substances 0.000 title claims abstract description 76
- 239000000835 fiber Substances 0.000 title claims abstract description 69
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 title claims abstract description 19
- 229910052698 phosphorus Inorganic materials 0.000 title claims abstract description 19
- 239000011574 phosphorus Substances 0.000 title claims abstract description 19
- 238000002360 preparation method Methods 0.000 title claims abstract description 13
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 claims abstract description 61
- 239000003822 epoxy resin Substances 0.000 claims abstract description 44
- 229920000647 polyepoxide Polymers 0.000 claims abstract description 44
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 23
- 239000002131 composite material Substances 0.000 claims abstract description 17
- 239000003054 catalyst Substances 0.000 claims abstract description 10
- 239000004114 Ammonium polyphosphate Substances 0.000 claims description 16
- 235000019826 ammonium polyphosphate Nutrition 0.000 claims description 16
- 229920001276 ammonium polyphosphate Polymers 0.000 claims description 16
- 229920000877 Melamine resin Polymers 0.000 claims description 14
- JDSHMPZPIAZGSV-UHFFFAOYSA-N melamine Chemical compound NC1=NC(N)=NC(N)=N1 JDSHMPZPIAZGSV-UHFFFAOYSA-N 0.000 claims description 14
- 239000003795 chemical substances by application Substances 0.000 claims description 13
- 238000000034 method Methods 0.000 claims description 11
- 239000003610 charcoal Substances 0.000 claims description 7
- 229920005989 resin Polymers 0.000 claims description 5
- 239000011347 resin Substances 0.000 claims description 5
- 229920001971 elastomer Polymers 0.000 claims description 3
- 239000005060 rubber Substances 0.000 claims description 3
- GVPFVAHMJGGAJG-UHFFFAOYSA-L cobalt dichloride Chemical compound [Cl-].[Cl-].[Co+2] GVPFVAHMJGGAJG-UHFFFAOYSA-L 0.000 claims description 2
- ARUVKPQLZAKDPS-UHFFFAOYSA-L copper(II) sulfate Chemical group [Cu+2].[O-][S+2]([O-])([O-])[O-] ARUVKPQLZAKDPS-UHFFFAOYSA-L 0.000 claims description 2
- 238000005253 cladding Methods 0.000 claims 2
- 229910021586 Nickel(II) chloride Inorganic materials 0.000 claims 1
- FBAFATDZDUQKNH-UHFFFAOYSA-M iron chloride Chemical compound [Cl-].[Fe] FBAFATDZDUQKNH-UHFFFAOYSA-M 0.000 claims 1
- QMMRZOWCJAIUJA-UHFFFAOYSA-L nickel dichloride Chemical compound Cl[Ni]Cl QMMRZOWCJAIUJA-UHFFFAOYSA-L 0.000 claims 1
- 238000002791 soaking Methods 0.000 claims 1
- 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 abstract description 61
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 47
- 229910052799 carbon Inorganic materials 0.000 abstract description 46
- 229920002678 cellulose Polymers 0.000 abstract description 32
- 239000001913 cellulose Substances 0.000 abstract description 32
- 238000002485 combustion reaction Methods 0.000 abstract description 20
- 239000007789 gas Substances 0.000 abstract description 16
- 238000010521 absorption reaction Methods 0.000 abstract description 12
- 230000015572 biosynthetic process Effects 0.000 abstract description 12
- 238000003756 stirring Methods 0.000 abstract description 11
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 9
- 239000001301 oxygen Substances 0.000 abstract description 9
- 229910052760 oxygen Inorganic materials 0.000 abstract description 9
- 239000002253 acid Substances 0.000 abstract description 6
- 238000005979 thermal decomposition reaction Methods 0.000 abstract description 4
- GCENSIWSRGSXJV-NNIBJMICSA-N 2,2-dimethylpropanoyloxymethyl (2s,5r,6z)-3,3-dimethyl-7-oxo-6-[(e)-4-oxobut-2-enylidene]-4-thia-1-azabicyclo[3.2.0]heptane-2-carboxylate Chemical compound S1C(C)(C)[C@H](C(=O)OCOC(=O)C(C)(C)C)N2C(=O)C(=C/C=C/C=O)/[C@@H]12 GCENSIWSRGSXJV-NNIBJMICSA-N 0.000 description 18
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 15
- 230000000694 effects Effects 0.000 description 13
- 238000006243 chemical reaction Methods 0.000 description 11
- 239000000203 mixture Substances 0.000 description 11
- 239000000243 solution Substances 0.000 description 11
- WXZMFSXDPGVJKK-UHFFFAOYSA-N pentaerythritol Chemical compound OCC(CO)(CO)CO WXZMFSXDPGVJKK-UHFFFAOYSA-N 0.000 description 10
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 9
- 239000012153 distilled water Substances 0.000 description 8
- 239000000463 material Substances 0.000 description 8
- 229920002472 Starch Polymers 0.000 description 7
- 238000007254 oxidation reaction Methods 0.000 description 7
- 239000008107 starch Substances 0.000 description 7
- 235000019698 starch Nutrition 0.000 description 7
- 238000001035 drying Methods 0.000 description 6
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 6
- 239000007800 oxidant agent Substances 0.000 description 6
- 230000003647 oxidation Effects 0.000 description 6
- 239000000047 product Substances 0.000 description 6
- LCFVJGUPQDGYKZ-UHFFFAOYSA-N Bisphenol A diglycidyl ether Chemical compound C=1C=C(OCC2OC2)C=CC=1C(C)(C)C(C=C1)=CC=C1OCC1CO1 LCFVJGUPQDGYKZ-UHFFFAOYSA-N 0.000 description 5
- 239000004841 bisphenol A epoxy resin Substances 0.000 description 5
- 238000004786 cone calorimetry Methods 0.000 description 5
- 230000003247 decreasing effect Effects 0.000 description 5
- 230000001590 oxidative effect Effects 0.000 description 5
- 239000004033 plastic Substances 0.000 description 5
- 229920003023 plastic Polymers 0.000 description 5
- -1 polyethylene Polymers 0.000 description 5
- 230000002195 synergetic effect Effects 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 4
- 230000007423 decrease Effects 0.000 description 4
- 125000002791 glucosyl group Chemical group C1([C@H](O)[C@@H](O)[C@H](O)[C@H](O1)CO)* 0.000 description 4
- LNEPOXFFQSENCJ-UHFFFAOYSA-N haloperidol Chemical compound C1CC(O)(C=2C=CC(Cl)=CC=2)CCN1CCCC(=O)C1=CC=C(F)C=C1 LNEPOXFFQSENCJ-UHFFFAOYSA-N 0.000 description 4
- 239000000779 smoke Substances 0.000 description 4
- 239000012265 solid product Substances 0.000 description 4
- 238000004448 titration Methods 0.000 description 4
- 238000001291 vacuum drying Methods 0.000 description 4
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 238000003763 carbonization Methods 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 150000004676 glycans Chemical class 0.000 description 3
- 239000000383 hazardous chemical Substances 0.000 description 3
- 239000003094 microcapsule Substances 0.000 description 3
- 229920001282 polysaccharide Polymers 0.000 description 3
- 239000005017 polysaccharide Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 238000000967 suction filtration Methods 0.000 description 3
- BFKJFAAPBSQJPD-UHFFFAOYSA-N tetrafluoroethene Chemical group FC(F)=C(F)F BFKJFAAPBSQJPD-UHFFFAOYSA-N 0.000 description 3
- 238000005481 NMR spectroscopy Methods 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 2
- 229920000297 Rayon Polymers 0.000 description 2
- 230000004888 barrier function Effects 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- ORTQZVOHEJQUHG-UHFFFAOYSA-L copper(II) chloride Chemical compound Cl[Cu]Cl ORTQZVOHEJQUHG-UHFFFAOYSA-L 0.000 description 2
- 238000006731 degradation reaction Methods 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- GYCHYNMREWYSKH-UHFFFAOYSA-L iron(ii) bromide Chemical compound [Fe+2].[Br-].[Br-] GYCHYNMREWYSKH-UHFFFAOYSA-L 0.000 description 2
- UAEPNZWRGJTJPN-UHFFFAOYSA-N methylcyclohexane Chemical compound CC1CCCCC1 UAEPNZWRGJTJPN-UHFFFAOYSA-N 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 2
- 239000004810 polytetrafluoroethylene Substances 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 230000004044 response Effects 0.000 description 2
- LPXPTNMVRIOKMN-UHFFFAOYSA-M sodium nitrite Chemical compound [Na+].[O-]N=O LPXPTNMVRIOKMN-UHFFFAOYSA-M 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 229920001187 thermosetting polymer Polymers 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- VNDYJBBGRKZCSX-UHFFFAOYSA-L zinc bromide Chemical compound Br[Zn]Br VNDYJBBGRKZCSX-UHFFFAOYSA-L 0.000 description 2
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 description 2
- 229910021591 Copper(I) chloride Inorganic materials 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 229910021575 Iron(II) bromide Inorganic materials 0.000 description 1
- 229910021578 Iron(III) chloride Inorganic materials 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- 239000005708 Sodium hypochlorite Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 125000003172 aldehyde group Chemical group 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 235000010290 biphenyl Nutrition 0.000 description 1
- 150000004074 biphenyls Chemical class 0.000 description 1
- ODWXUNBKCRECNW-UHFFFAOYSA-M bromocopper(1+) Chemical compound Br[Cu+] ODWXUNBKCRECNW-UHFFFAOYSA-M 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000002775 capsule Substances 0.000 description 1
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 229910000361 cobalt sulfate Inorganic materials 0.000 description 1
- 229940044175 cobalt sulfate Drugs 0.000 description 1
- KTVIXTQDYHMGHF-UHFFFAOYSA-L cobalt(2+) sulfate Chemical compound [Co+2].[O-]S([O-])(=O)=O KTVIXTQDYHMGHF-UHFFFAOYSA-L 0.000 description 1
- BZRRQSJJPUGBAA-UHFFFAOYSA-L cobalt(ii) bromide Chemical compound Br[Co]Br BZRRQSJJPUGBAA-UHFFFAOYSA-L 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 229910000365 copper sulfate Inorganic materials 0.000 description 1
- 229960000355 copper sulfate Drugs 0.000 description 1
- OXBLHERUFWYNTN-UHFFFAOYSA-M copper(I) chloride Chemical compound [Cu]Cl OXBLHERUFWYNTN-UHFFFAOYSA-M 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 229960003280 cupric chloride Drugs 0.000 description 1
- 229940045803 cuprous chloride Drugs 0.000 description 1
- 230000007123 defense Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000001066 destructive effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- USIUVYZYUHIAEV-UHFFFAOYSA-N diphenyl ether Chemical class C=1C=CC=CC=1OC1=CC=CC=C1 USIUVYZYUHIAEV-UHFFFAOYSA-N 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000010292 electrical insulation Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 229940032296 ferric chloride Drugs 0.000 description 1
- 229940032950 ferric sulfate Drugs 0.000 description 1
- 229940046149 ferrous bromide Drugs 0.000 description 1
- 229960002089 ferrous chloride Drugs 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 230000002439 hemostatic effect Effects 0.000 description 1
- 238000002329 infrared spectrum Methods 0.000 description 1
- NMCUIPGRVMDVDB-UHFFFAOYSA-L iron dichloride Chemical compound Cl[Fe]Cl NMCUIPGRVMDVDB-UHFFFAOYSA-L 0.000 description 1
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 description 1
- RUTXIHLAWFEWGM-UHFFFAOYSA-H iron(3+) sulfate Chemical compound [Fe+3].[Fe+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O RUTXIHLAWFEWGM-UHFFFAOYSA-H 0.000 description 1
- 229910000360 iron(III) sulfate Inorganic materials 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 231100000053 low toxicity Toxicity 0.000 description 1
- 229940099596 manganese sulfate Drugs 0.000 description 1
- 239000011702 manganese sulphate Substances 0.000 description 1
- 235000007079 manganese sulphate Nutrition 0.000 description 1
- SQQMAOCOWKFBNP-UHFFFAOYSA-L manganese(II) sulfate Chemical compound [Mn+2].[O-]S([O-])(=O)=O SQQMAOCOWKFBNP-UHFFFAOYSA-L 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- GYNNXHKOJHMOHS-UHFFFAOYSA-N methyl-cycloheptane Natural products CC1CCCCCC1 GYNNXHKOJHMOHS-UHFFFAOYSA-N 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 231100000956 nontoxicity Toxicity 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000012264 purified product Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- JHJLBTNAGRQEKS-UHFFFAOYSA-M sodium bromide Inorganic materials [Na+].[Br-] JHJLBTNAGRQEKS-UHFFFAOYSA-M 0.000 description 1
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 1
- 235000010288 sodium nitrite Nutrition 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 230000001629 suppression Effects 0.000 description 1
- 238000002411 thermogravimetry Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 229940102001 zinc bromide Drugs 0.000 description 1
- 239000011592 zinc chloride Substances 0.000 description 1
- 235000005074 zinc chloride Nutrition 0.000 description 1
- 229960001939 zinc chloride Drugs 0.000 description 1
- NWONKYPBYAMBJT-UHFFFAOYSA-L zinc sulfate Chemical compound [Zn+2].[O-]S([O-])(=O)=O NWONKYPBYAMBJT-UHFFFAOYSA-L 0.000 description 1
- 229910000368 zinc sulfate Inorganic materials 0.000 description 1
- 229960001763 zinc sulfate Drugs 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L63/00—Compositions of epoxy resins; Compositions of derivatives of epoxy resins
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B15/00—Preparation of other cellulose derivatives or modified cellulose, e.g. complexes
- C08B15/02—Oxycellulose; Hydrocellulose; Cellulosehydrate, e.g. microcrystalline cellulose
- C08B15/04—Carboxycellulose, e.g. prepared by oxidation with nitrogen dioxide
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2201/00—Properties
- C08L2201/02—Flame or fire retardant/resistant
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Biochemistry (AREA)
- Materials Engineering (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Reinforced Plastic Materials (AREA)
Abstract
本发明属于含磷膨胀型阻燃剂技术领域,公开了一种亚麻纤维素基磷系膨胀型阻燃剂及其制备方法和应用。该阻燃剂包括2~10重量份的炭源、1~10重量份的酸源和1~10重量份的气源;所述炭源为高羧基含量的羧基亚麻纤维,由包括以下步骤的方法制备得到:将亚麻纤维浸泡水中,加入H2O2及催化剂,搅拌反应,得到高羧基含量的羧基亚麻纤维。本发明还提供一种基于上述阻燃剂的环氧树脂复合材料。本发明阻燃剂以高羧基含量的羧基亚麻纤维素为炭源,成炭率为20~27.2%,热分解释放可燃性气体少。得到的环氧树脂复合材料极限氧指数超过29,垂直燃烧等级为V‑0,燃烧总热释放量下降超过60%,并具有吸水率低、力学性能高等优点。
The invention belongs to the technical field of phosphorus-containing intumescent flame retardants, and discloses a flax cellulose-based phosphorus-based intumescent flame retardant, a preparation method and application thereof. The flame retardant comprises 2 to 10 parts by weight of a carbon source, 1 to 10 parts by weight of an acid source and 1 to 10 parts by weight of a gas source; the carbon source is carboxylated flax fiber with a high carboxyl content, which comprises the following steps Preparation method: Soak flax fiber in water, add H 2 O 2 and catalyst, stir and react to obtain carboxyl flax fiber with high carboxyl content. The present invention also provides an epoxy resin composite material based on the above flame retardant. The flame retardant of the invention uses carboxylated flax cellulose with high carboxyl content as a carbon source, has a char formation rate of 20-27.2%, and releases less combustible gas through thermal decomposition. The obtained epoxy resin composite material has a limiting oxygen index of more than 29, a vertical combustion rating of V-0, a reduction in total combustion heat release of more than 60%, and has the advantages of low water absorption and high mechanical properties.
Description
技术领域technical field
本发明属于含磷膨胀型阻燃剂技术领域,特别涉及一种亚麻纤维素基磷系膨胀型阻燃剂及其制备方法和应用。The invention belongs to the technical field of phosphorus-containing intumescent flame retardants, and in particular relates to a flax cellulose-based phosphorus-based intumescent flame retardant and a preparation method and application thereof.
背景技术Background technique
纤维素是自然界中分布最广、含量最多的一种多糖,占植物界碳含量的50%以上。羧基亚麻纤维作为纤维素衍生物的一种,具有良好的生物相容性、生物可降解性、环境友好和无毒等特点,已被广泛用于不少行业。以过氧化氢(H2O2)制备羧基亚麻纤维因具有绿色、环保和高纯度等优点而备受关注。而纤维素经过氧化之后,其性能较天然纤维素又有了较大的提高。如中国专利申请CN104017090A公开一种采用过氧化氢制备羧基纤维素的方法,其羰基含量高达10.4%,对铅离子的吸附比纯纤维提高10倍以上。Cellulose is the most widely distributed and most abundant polysaccharide in nature, accounting for more than 50% of the carbon content in the plant kingdom. As a kind of cellulose derivative, carboxylated flax fiber has the characteristics of good biocompatibility, biodegradability, environmental friendliness and non-toxicity, and has been widely used in many industries. The preparation of carboxylated flax fiber by hydrogen peroxide (H 2 O 2 ) has attracted much attention due to its advantages of greenness, environmental protection and high purity. After cellulose is oxidized, its performance is greatly improved compared with natural cellulose. For example, Chinese patent application CN104017090A discloses a method for preparing carboxycellulose by using hydrogen peroxide, its carbonyl content is as high as 10.4%, and the adsorption of lead ions is more than 10 times higher than that of pure fiber.
环氧树脂具有多方面优良的性能,如耐腐蚀性能、电绝缘性能、力学性能、可粘结性以及优于其他热固性树脂的加工工艺性。因此无论在高新技术还是在通用技术,无论在国防军事还是在民用工业,甚至在日常生活中都可以看到环氧树脂及其次加工产品的踪迹。环氧树脂是热固性树脂中非常重要的一种,但其阻燃性能较差,氧指数较低(约19.8)。环氧树脂的易燃性及离火后的持续自燃容易引发火灾的缺点限制了它的应用。卤系阻燃剂因其用量少、阻燃效率高且应用范围广,成为市场的主流,但阻燃的同时也产生大量的腐蚀性和有毒气体,由此引发的二口恶英(Dioxin)问题而受到人们的广泛关注。欧盟2003年2月颁布了《限制有害物质指令》(RoHS),2006年7月1日开始实施《关于在电气、电子设备中限制使用某些有害物质指令》(简称ROHS指令),规定了首批实施的有害物质和近期关注环境管理物质名单。在电子电气设备中禁止使用多溴联苯(PBB)、多溴二苯醚(PBOE)和甲醛。含卤阻燃剂的使用受到了很大的冲击。Epoxy resin has many excellent properties, such as corrosion resistance, electrical insulation, mechanical properties, bondability, and better processing than other thermosetting resins. Therefore, whether in high-tech or general-purpose technology, whether in national defense or civilian industry, or even in daily life, traces of epoxy resin and its secondary processed products can be seen. Epoxy resin is a very important kind of thermosetting resin, but its flame retardancy is poor and its oxygen index is low (about 19.8). The flammability of epoxy resin and the disadvantages of continuous spontaneous combustion after leaving the fire are easy to cause fires, which limit its application. Halogenated flame retardants have become the mainstream of the market due to their low dosage, high flame retardant efficiency and wide application range. ) issues have received widespread attention. The European Union promulgated the "Restriction of Hazardous Substances Directive" (RoHS) in February 2003, and the "Restriction of the Use of Certain Hazardous Substances Directive in Electrical and Electronic Equipment" (RoHS Directive for short) began to be implemented on July 1, 2006. The list of hazardous substances that have been implemented in batches and substances of concern for environmental management in the near future. The use of polybrominated biphenyls (PBBs), polybrominated diphenyl ethers (PBOEs) and formaldehyde is prohibited in electrical and electronic equipment. The use of halogenated flame retardants has been hit hard.
所以开发一种新型阻燃环氧树脂替代现有的卤素阻燃环氧树脂迫在眉睫。由此,新型的膨胀形阻燃剂由于其低毒、抑烟以及制备简单等优点而备受关注。添加膨胀阻燃剂的聚合物在燃烧时分解产生不燃气体隔绝氧气带走大量热量,并在材料表面形成一层炭层起到隔绝热量和氧气的作用。膨胀型阻燃剂主要有三大成分:炭源、酸源和气源。随着上世纪对于膨胀型阻燃的研究的深入,典型的炭源如季戊四醇由于价格昂贵已经不能满足大规模生产的需要,所以来源广泛,绿色无污染的淀粉成为了最为普遍的成炭剂。如李斌等人研究了淀粉替代季戊四醇对聚乙烯膨胀阻燃体系的影响(李斌,张秀成,孙才英.淀粉对聚乙烯膨胀阻燃体系热降解和阻燃的影响[J].高分子材料科学与工程.2000(02))。在日常使用时,淀粉容易吸水而迁移出材料外,从而导致不能形成足够多的炭层,进一步影响阻燃效果。而在膨胀型阻燃炭源中,同为多糖类的亚麻纤维却鲜有提及。与淀粉相比,同为天然大分子多糖的亚麻纤维有着更好的耐水性和结构稳定性。Therefore, it is imminent to develop a new type of flame retardant epoxy resin to replace the existing halogen flame retardant epoxy resin. Therefore, new intumescent flame retardants have attracted much attention due to their advantages of low toxicity, smoke suppression and simple preparation. The polymer added with intumescent flame retardant decomposes during combustion to produce non-combustible gas to isolate oxygen and take away a large amount of heat, and forms a layer of charcoal layer on the surface of the material to isolate heat and oxygen. Intumescent flame retardants mainly have three major components: carbon source, acid source and gas source. With the in-depth research on intumescent flame retardant in the last century, typical carbon sources such as pentaerythritol can no longer meet the needs of large-scale production due to its high price, so starch with a wide range of sources, green and pollution-free, has become the most common char-forming agent. For example, Li Bin and others studied the effect of starch replacing pentaerythritol on polyethylene intumescent flame retardant system (Li Bin, Zhang Xiucheng, Sun Caiying. Effect of starch on thermal degradation and flame retardancy of polyethylene intumescent flame retardant system[J]. Polymer Materials Science and Engineering.2000(02)). In daily use, starch is easy to absorb water and migrate out of the material, resulting in the inability to form enough char layers, which further affects the flame retardant effect. However, among the intumescent flame-retardant carbon sources, flax fiber, which is also a polysaccharide, is rarely mentioned. Compared with starch, flax fiber, which is also a natural macromolecular polysaccharide, has better water resistance and structural stability.
为了制备羧基纤维素,章胜红等用NaOH溶液对天然纤维素进行改性以提高其被氧化能力,以TEMPO-NaOCl-NaBr体系作为氧化剂选择性羧基亚麻纤维葡萄糖基环的伯羟基成羧基,以此技术制备的一种纤维素基重金属吸附材料可置于曝气生物滤池的调节池中对Cu2+和Cd2+等重金属离子进行预处理(章胜红,陈季华,曝气生物滤池深度净化有机废水的研究,2006)。公开号为CN1O201899A的专利采用的方法是以粘胶纤维长丝织物为起始原料,采用有机氧化溶剂体系对粘胶纤维长丝织物进行氧化,氧化反应结束后,经洗涤、干燥制成羧基亚麻纤维止血产品,产品的羧基含量可以达到15~24%,采用的有机氧化溶剂为环己烷或是甲基环己烷。美国专利US6627749B1公布了一种采用亚硝酸钠、磷酸和硝酸混合液体对纤维素进行氧化,制备得到羧基含量低于24.5%的羧基亚麻纤维,可用于药物、化工和医用高分子领域中。美国专利US6120554-A公布了一种采用烷基季氨盐为催化剂,以过氧化氢为氧化剂羧基亚麻纤维,从而制备得到羧基亚麻纤维,但是氧化度低,氧化效率差,并且制备过程需要在较高的温度下进行,难为广泛应用。日本专利2011057749A报道了采用极性氧化剂将纤维素C6上的羟基氧化成醛基和羧基,其中得到的羧基亚麻纤维中羧基含量为0.6~2.2mmol/g。德国专利DE102010034782报道了一种氧化度5~50%的纤维素的制备方法,该方法采用次氯酸钠等氧化剂进行氧化处理,反应温度20~160℃下进行。In order to prepare carboxylated cellulose, Zhang Shenghong et al. used NaOH solution to modify natural cellulose to improve its oxidizing ability, and used the TEMPO-NaOCl-NaBr system as an oxidant to selectively convert the primary hydroxyl group of the carboxyl flax fiber glucosyl ring into a carboxyl group. A cellulose-based heavy metal adsorption material prepared by the technology can be placed in the regulating tank of the biological aerated filter to pretreat heavy metal ions such as Cu 2+ and Cd 2+ (Zhang Shenghong, Chen Jihua, Organic aerated deep purification of biological aerated filter Wastewater Research, 2006). The method adopted by the patent whose publication number is CN1O201899A is to use viscose fiber filament fabric as the starting material, and use an organic oxidation solvent system to oxidize the viscose fiber filament fabric. After the oxidation reaction is completed, it is washed and dried to make carboxyl flax Fiber hemostatic product, the carboxyl content of the product can reach 15-24%, and the organic oxidation solvent used is cyclohexane or methylcyclohexane. U.S. Patent No. 6,627,749B1 discloses a method of oxidizing cellulose with a mixed solution of sodium nitrite, phosphoric acid, and nitric acid to prepare carboxylated flax fibers with a carboxyl content lower than 24.5%, which can be used in the fields of medicine, chemical industry, and medical polymers. U.S. Patent US6120554-A discloses a kind of adopting alkyl quaternary ammonium salt as catalyst, taking hydrogen peroxide as oxidant carboxyl flax fiber, thereby prepares carboxy flax fiber, but oxidation degree is low, oxidation efficiency is poor, and preparation process needs relatively It is difficult to be widely used under high temperature. Japanese Patent No. 2011057749A reported the use of polar oxidants to oxidize the hydroxyl groups on cellulose C6 into aldehyde groups and carboxyl groups, wherein the carboxyl group content in the obtained carboxylated flax fibers was 0.6-2.2 mmol/g. German patent DE102010034782 reports a method for preparing cellulose with an oxidation degree of 5-50%. The method uses an oxidizing agent such as sodium hypochlorite for oxidation treatment at a reaction temperature of 20-160°C.
迄今为止,国内外对制备羧基纤维素的报道虽已存在,但是制备的工艺复杂,条件苛刻,须在强酸性或者是碱性介质中制备。所选用的氧化剂不仅对纤维素本身的破坏性大,而且会有副产物遗留,对环境造成一定的影响。本发明采用过氧化氢这种绿色环保的氧化剂,通过设计的反应条件,制备羧基含量最高达40%的羧基亚麻纤维,并将其作为新型膨胀型阻燃剂炭源,与三聚氰胺微胶囊包覆的聚磷酸铵形成的组合物,实现在较低含量下膨胀阻燃环氧树脂具有高阻燃等级、高力学性能及低吸水率等优点。So far, there have been reports on the preparation of carboxycellulose at home and abroad, but the preparation process is complicated and the conditions are harsh, and it must be prepared in a strongly acidic or alkaline medium. The selected oxidizing agent is not only destructive to cellulose itself, but also has by-products left over, which has a certain impact on the environment. The present invention uses hydrogen peroxide, an environmentally friendly oxidant, to prepare carboxy flax fibers with a carboxyl content of up to 40% through designed reaction conditions, and use it as a new type of intumescent flame retardant carbon source, coated with melamine microcapsules The composition formed by ammonium polyphosphate realizes the expansion of flame retardant epoxy resin at a lower content, and has the advantages of high flame retardant grade, high mechanical properties and low water absorption.
发明内容Contents of the invention
为了克服上述现有技术的缺点与不足,本发明的首要目的在于提供一种亚麻纤维素基磷系膨胀型阻燃剂。本发明以高羧基含量的羧基亚麻纤维为材料,与三聚氰胺微胶囊包覆的聚磷酸铵组成膨胀型阻燃剂,利用其高成炭性和低可燃性气体释放量,降低阻燃剂的含量,提高阻燃性能,应用于环氧树脂阻燃中。In order to overcome the above-mentioned shortcomings and deficiencies of the prior art, the primary purpose of the present invention is to provide a flax cellulose-based phosphorus-based intumescent flame retardant. The present invention uses carboxyl flax fiber with high carboxyl content as the material, and ammonium polyphosphate coated with melamine microcapsules to form an intumescent flame retardant, and utilizes its high char formation and low flammable gas release to reduce the content of the flame retardant , to improve the flame retardant properties, used in epoxy resin flame retardant.
本发明另一目的在于提供一种上述亚麻纤维素基磷系膨胀型阻燃剂的制备方法。Another object of the present invention is to provide a method for preparing the flax cellulose-based phosphorus-based intumescent flame retardant.
本发明再一目的在于提供一种基于上述亚麻纤维素基磷系膨胀型阻燃剂的环氧树脂复合材料。Another object of the present invention is to provide an epoxy resin composite material based on the flax cellulose-based phosphorus-based intumescent flame retardant.
本发明再一目的在于提供上述亚麻纤维素基磷系膨胀型阻燃剂在树脂、橡胶中的应用,特别是环氧树脂阻燃中的应用。Another object of the present invention is to provide the application of the flax cellulose-based phosphorus-based intumescent flame retardant in resin and rubber, especially the application in epoxy resin flame retardancy.
本发明的目的通过下述方案实现:The object of the present invention is achieved through the following solutions:
一种亚麻纤维素基磷系膨胀型阻燃剂,包括2~10重量份的炭源、1~10重量份的酸源和1~10重量份的气源;A flax cellulose-based phosphorus-based intumescent flame retardant, comprising 2 to 10 parts by weight of a carbon source, 1 to 10 parts by weight of an acid source and 1 to 10 parts by weight of a gas source;
所述炭源为高羧基含量的羧基亚麻纤维,其由包括以下步骤的方法制备得到:将亚麻纤维浸泡水中,加入H2O2及催化剂,搅拌反应,得到高羧基含量的羧基亚麻纤维。The carbon source is carboxy flax fiber with high carboxyl content, which is prepared by the following steps: soak flax fiber in water, add H 2 O 2 and a catalyst, stir and react to obtain carboxy flax fiber with high carboxyl content.
所用亚麻纤维和H2O2的质量比优选为20:10~20:80。The mass ratio of the used flax fiber to H 2 O 2 is preferably 20:10˜20:80.
所述搅拌反应的条件优选为20~50℃下搅拌反应0.5~72h。The conditions of the stirring reaction are preferably stirring and reacting at 20-50° C. for 0.5-72 hours.
所用催化剂的量为催化量即可,优选为亚麻纤维质量的0.02~2%。The amount of the catalyst used is just a catalytic amount, preferably 0.02-2% of the flax fiber mass.
所述的催化剂可为硫酸铁、硫酸铜、硫酸钴、硫酸锰、硫酸锌、氯化锌、氯化钴、氯化亚铜、氯化亚铁、氯化铁、氯化铜、溴化锌、溴化钴、溴化亚铁、溴化铁和溴化铜中的至少一种。所述催化剂使用前优选先溶解于水中制备得到浓度为0.1mol/L的溶液。Described catalyst can be ferric sulfate, copper sulfate, cobalt sulfate, manganese sulfate, zinc sulfate, zinc chloride, cobalt chloride, cuprous chloride, ferrous chloride, ferric chloride, cupric chloride, zinc bromide , cobalt bromide, ferrous bromide, iron bromide and copper bromide at least one. The catalyst is preferably dissolved in water before use to prepare a solution with a concentration of 0.1 mol/L.
所述亚麻纤维优选在水中浸泡1~5h后再加入H2O2及催化剂反应。所用水的量优选为亚麻纤维质量的两倍或以上。The flax fiber is preferably soaked in water for 1-5 hours, and then added with H 2 O 2 and a catalyst for reaction. The amount of water used is preferably twice or more the mass of flax fiber.
所述搅拌反应后,优选通过分离、洗涤和干燥得到纯化产品。所述洗涤优选利用水冲洗分离后固体至中性。所述干燥优选在50℃~85℃下烘干4~12h。After the stirring reaction, a purified product is preferably obtained by separation, washing and drying. The washing is preferably to use water to rinse the separated solid to neutrality. The drying is preferably performed at 50° C. to 85° C. for 4 to 12 hours.
所述的酸源和气源优选为三聚氰胺包覆的聚磷酸铵(MFAPP),其制备方法可参照文献(Yang L,Cheng W L,Zhou J,et al.Polym Degradation Stab,2014,105(1):150-159.)得到。Described acid source and gas source are preferably melamine-coated ammonium polyphosphate (MFAPP), and its preparation method can refer to literature (Yang L, Cheng W L, Zhou J, et al.Polym Degradation Stab,2014,105(1) :150-159.) to get.
所述酸源和气源的总用量优选为3~10重量份。The total amount of the acid source and the gas source is preferably 3-10 parts by weight.
为了更好地实现本发明,所述亚麻纤维素基磷系膨胀型阻燃剂,包括2~10重量份的炭源、3~10重量份的三聚氰胺包覆的聚磷酸铵;In order to better realize the present invention, the flax cellulose-based phosphorus-based intumescent flame retardant includes 2 to 10 parts by weight of carbon source, and 3 to 10 parts by weight of ammonium polyphosphate coated with melamine;
所述炭源为高羧基含量的羧基亚麻纤维,其由包括以下步骤的方法制备得到:将亚麻纤维浸泡水中,加入H2O2及催化剂,搅拌反应,得到高羧基含量的羧基亚麻纤维。The carbon source is carboxy flax fiber with high carboxyl content, which is prepared by the following steps: soak flax fiber in water, add H 2 O 2 and a catalyst, stir and react to obtain carboxy flax fiber with high carboxyl content.
本发明所述阻燃剂的炭源为高羧基含量的羧基亚麻纤维素,与传统的成炭剂,如季戊四醇、纯淀粉和纯亚麻纤维相比,具有成炭率高、燃烧过程中释放甲醇等可燃性气体少以及耐水性高等优点,其羧基含量为10~40%,在空气气氛中热分解温度为600℃时所得成炭率为20~27.2%,热分解释放甲醇等可燃性气体下降比例50~95%。The carbon source of the flame retardant of the present invention is carboxyl flax cellulose with high carboxyl content, compared with traditional carbon forming agents such as pentaerythritol, pure starch and pure flax fiber, it has high char formation rate and releases methanol during combustion. It has the advantages of less flammable gas and high water resistance. Its carboxyl content is 10-40%. When the thermal decomposition temperature is 600°C in the air atmosphere, the char formation rate is 20-27.2%. The thermal decomposition releases methanol and other flammable gases. The ratio is 50-95%.
本发明还提供一种所述亚麻纤维素基磷系膨胀型阻燃剂的制备方法,通过将2~10重量份的炭源、1~10重量份的酸源和1~10重量份的气源混合制备得到。The present invention also provides a preparation method of the flax cellulose-based phosphorus-based intumescent flame retardant, by adding 2-10 parts by weight of carbon source, 1-10 parts by weight of acid source and Source mixes are prepared.
本发明还提供一种基于上述亚麻纤维素基磷系膨胀型阻燃剂的环氧树脂复合材料,包括100质量份环氧树脂、20~60质量份固化剂、5~20质量份所述亚麻纤维素基磷系膨胀型阻燃剂。其通过将所述组合混合搅拌均匀得到。The present invention also provides an epoxy resin composite material based on the flax cellulose-based phosphorus-based intumescent flame retardant, comprising 100 parts by mass of epoxy resin, 20-60 parts by mass of curing agent, 5-20 parts by mass of the flax Cellulose-based phosphorus-based intumescent flame retardant. It is obtained by mixing and stirring the combination uniformly.
所用固化剂为本领域常规使用的固化剂即可,优选为33质量份。The curing agent used can be the conventional curing agent used in this field, preferably 33 parts by mass.
将上述组分混合搅拌均匀,加入模具中,固化,脱模,得到环氧树脂复合材料。The above components are mixed and stirred evenly, put into the mold, cured, demoulded, and the epoxy resin composite material is obtained.
上述制备得到的环氧树脂复合材料具有优异的阻燃性能,其极限氧指数超过29,垂直燃烧等级为V-0,燃烧总热释放量与纯环氧树脂相比下降最大值超过60%。其中,以羧基含量为32.2%的高羧基含量的羧基亚麻纤维素为炭源制备得到的环氧树脂复合材料具有突出优异的阻燃效果。The epoxy resin composite material prepared above has excellent flame retardancy, its limiting oxygen index exceeds 29, its vertical combustion rating is V-0, and its total heat release in combustion decreases by more than 60% compared with pure epoxy resin. Among them, the epoxy resin composite material prepared by using carboxylated flax cellulose with a high carboxyl content of 32.2% as a carbon source has outstanding and excellent flame retardant effect.
本发明,以高羧基含量的羧基亚麻纤维素为炭源,与三聚氰胺包覆的聚磷酸铵发挥协同作用可应用于树脂、橡胶中作为阻燃剂,特别是环氧树脂阻燃中的应用。其用于环氧树脂膨胀型阻燃剂中,依靠其高成炭性和自身高阻燃性,使得在较低阻燃剂添剂量的情况下,环氧树脂具有良好的阻燃性能,从而推动羧基亚麻纤维应用于膨胀阻燃领域中。In the present invention, carboxylated flax cellulose with high carboxyl content is used as a carbon source, and the melamine-coated ammonium polyphosphate exerts a synergistic effect and can be used as a flame retardant in resins and rubbers, especially in epoxy resin flame retardants. It is used in epoxy resin intumescent flame retardant, relying on its high char formation and high flame retardancy, so that the epoxy resin has good flame retardant performance under the condition of low flame retardant additive amount, thus Promote the application of carboxylated flax fiber in the field of intumescent flame retardant.
本发明的机理为:Mechanism of the present invention is:
本发明制备高羧基含量的亚麻纤维素并将其作为新型炭源与聚磷酸铵发挥协同作用,得到膨胀型阻燃剂。此新型炭源的羧基含量为10~40%,成炭量超过27.2%,燃烧过程中甲醇等可燃性气体量大幅度减少,且膨胀所得的炭层结构均匀致密且膨胀率高,与三聚氰胺微胶囊包覆的聚磷酸铵形成的阻燃剂,具有膨胀性优异,协同阻燃效率高的特点。以100质量份的环氧树脂(固化剂用量为21份)计,当所用的膨胀型阻燃剂中三聚氰胺微胶囊包覆的聚磷酸铵的用量为3~10质量份,炭源的用量为2~10质量份,所得环氧树脂复合材料的极限氧指数超过29,垂直燃烧等级为V-0,燃烧总热释放量下降最大值超过60%,并且具有吸水率低(24小时内吸水率低于4%)、力学性能高(拉伸强度和缺口冲击强度分别不低于纯环氧树脂的85%和130%)等优点,其综合性能远优于以常用炭源季戊四醇和纯淀粉,具有广泛的应用价值。The invention prepares flax cellulose with high carboxyl content and uses it as a novel carbon source to play a synergistic effect with ammonium polyphosphate to obtain an intumescent flame retardant. The carboxyl group content of this new type of carbon source is 10-40%, the amount of char formation exceeds 27.2%, the amount of flammable gases such as methanol is greatly reduced during the combustion process, and the carbon layer obtained by expansion has a uniform and dense structure and a high expansion rate, which is slightly different from melamine. The flame retardant formed by capsule-coated ammonium polyphosphate has the characteristics of excellent expansion and high flame retardant efficiency. Based on 100 parts by mass of epoxy resin (the amount of curing agent is 21 parts), when the amount of ammonium polyphosphate coated with melamine microcapsules in the intumescent flame retardant used is 3 to 10 parts by mass, the amount of carbon source is 2~10 parts by mass, the limiting oxygen index of the obtained epoxy resin composite material exceeds 29, the vertical combustion grade is V-0, the maximum value of the total heat release of combustion decreases by more than 60%, and has low water absorption (water absorption within 24 hours less than 4%), high mechanical properties (tensile strength and notched impact strength are not lower than 85% and 130% of pure epoxy resin, respectively), and its comprehensive performance is far superior to the common carbon source pentaerythritol and pure starch. It has wide application value.
本发明相对于现有技术,具有如下的优点及有益效果:Compared with the prior art, the present invention has the following advantages and beneficial effects:
(1)与现有的技术相比,本发明阻燃剂的碳源,高羧基含量的羧基亚麻纤维,具有成炭率高,炭层结构致密均匀,燃烧产生的可燃性气体少,协同阻燃效率高,可以作为膨胀型阻燃剂的一种新型炭源来使用。(1) Compared with the existing technology, the carbon source of the flame retardant of the present invention, the carboxyl flax fiber of high carboxyl content, has the high char formation rate, and the char layer structure is dense and uniform, and the combustible gas that combustion produces is few, synergistic retardation It has high combustion efficiency and can be used as a new type of carbon source for intumescent flame retardants.
(2)本发明独创性的使用高羧基亚麻纤维做为一种新型成炭剂用于膨胀型阻燃剂中,取得了明显的效果,极大拓宽了亚麻纤维及其衍生物的应用范围。(2) The inventive use of high carboxyl flax fiber as a new type of char-forming agent in the intumescent flame retardant has achieved remarkable results and greatly broadened the application range of flax fiber and its derivatives.
(3)通过对比发现,高羧基含量的羧基亚麻纤维素与聚磷酸铵发挥协同作用,用于环氧树脂的膨胀型阻燃,获得了膨胀程度高,炭层结构致密,阻燃效果良好的膨胀型阻燃剂。(3) Through comparison, it was found that carboxy-flax cellulose with high carboxyl content and ammonium polyphosphate exerted a synergistic effect and was used in the intumescent flame retardant of epoxy resin to obtain a high degree of expansion, a dense carbon layer structure, and a good flame retardant effect. Intumescent flame retardant.
附图说明Description of drawings
图1为实施例1、2和4制备的羧基亚麻纤维素的红外谱图。其中,曲线a为纯亚麻纤维,曲线b为实施例1制备的OLF12.6,曲线c为实施例2制备的OLF27.4,曲线d为实施例4制备的OLF34.5。Fig. 1 is the infrared spectrogram of the carboxyl flax cellulose prepared by embodiment 1, 2 and 4. Wherein, curve a is pure flax fiber, curve b is OLF12.6 prepared in Example 1, curve c is OLF27.4 prepared in Example 2, and curve d is OLF34.5 prepared in Example 4.
图2为实施例1、2和4制备的羧基亚麻纤维素的核磁共振碳谱图。其中,曲线a为纯亚麻纤维,曲线b为实施例1制备的OLF12.6,曲线c为实施例2制备的OLF27.4,曲线d为实施例4制备的OLF34.5。Fig. 2 is the carbon nuclear magnetic resonance spectrogram of the carboxy flax cellulose prepared in embodiment 1, 2 and 4. Wherein, curve a is pure flax fiber, curve b is OLF12.6 prepared in Example 1, curve c is OLF27.4 prepared in Example 2, and curve d is OLF34.5 prepared in Example 4.
图3为实施例1、2和4制备的羧基亚麻纤维素的热重分析谱图。其中,曲线a为纯亚麻纤维,曲线b为实施例1制备的OLF12.6,曲线c为实施例2制备的OLF27.4,曲线d为实施例4制备的OLF34.5。Fig. 3 is the thermogravimetric analysis spectrogram of the carboxyl flax cellulose prepared in embodiment 1, 2 and 4. Wherein, curve a is pure flax fiber, curve b is OLF12.6 prepared in Example 1, curve c is OLF27.4 prepared in Example 2, and curve d is OLF34.5 prepared in Example 4.
图4为实施例1、2和4制备的羧基亚麻纤维素热重红外联用谱图。其中,曲线a为纯亚麻纤维,曲线b为实施例1制备的OLF12.6,曲线c为实施例2制备的OLF27.4,曲线d为实施例4制备的OLF34.5。Fig. 4 is the thermogravimetric infrared spectrogram of carboxy-flax cellulose prepared in Examples 1, 2 and 4. Wherein, curve a is pure flax fiber, curve b is OLF12.6 prepared in Example 1, curve c is OLF27.4 prepared in Example 2, and curve d is OLF34.5 prepared in Example 4.
图5为实例5、6和7锥形量热测试中平均热释放速率(A)、总的热释放量(B)和总的烟密度谱图(C),其中,曲线a为纯环氧树脂,曲线b为对比例2,曲线c为对比例1,曲线d为实施例5,曲线e为实施例6,曲线f为实施例7。Fig. 5 is average heat release rate (A), total heat release (B) and total smoke density spectrum (C) in the cone calorimetry test of example 5, 6 and 7, wherein, curve a is pure epoxy Resin, curve b is comparative example 2, curve c is comparative example 1, curve d is embodiment 5, curve e is embodiment 6, and curve f is embodiment 7.
图6为实例5、6和7锥形量热燃烧测试后样品的炭层外观。Fig. 6 is the appearance of the charcoal layer of the sample after the cone calorimetry combustion test of Examples 5, 6 and 7.
具体实施方式Detailed ways
下面结合实施例和附图对本发明作进一步详细的描述,但本发明的实施方式不限于此。The present invention will be further described in detail below with reference to the examples and drawings, but the implementation of the present invention is not limited thereto.
下列实施例中未注明具体条件的实验方法,通常按照常规条件,例如是《贝尔斯坦有机化学手册》(化学工业出版社,1996年)中的条件,或按照制造厂商所建议的条件。比例和百分比基于重量,除非特别说明。The experimental methods in the following examples that do not specify specific conditions are generally in accordance with conventional conditions, such as the conditions in "Beilstein Organic Chemistry Handbook" (Chemical Industry Press, 1996), or in accordance with the conditions suggested by the manufacturer. Ratios and percentages are by weight unless otherwise indicated.
除非另有定义或说明,本文中所使用的所有专业与科学用语与本领域技术熟练人员所熟悉的意义相同。此外任何与所记载内容相似或均等的方法及材料皆可应用于本发明方法中。Unless otherwise defined or stated, all professional and scientific terms used herein have the same meanings as those familiar to those skilled in the art. In addition, any methods and materials similar or equivalent to those described can be applied to the method of the present invention.
下列实施例中所用试剂均可从商业渠道购买得到。All reagents used in the following examples can be purchased from commercial sources.
对比例1Comparative example 1
27.5g环氧树脂固化剂(D230)和82.5g双酚A型环氧树脂(DGEBA)放置于塑料烧杯中,搅拌混合10min;混合物置于真空干燥箱内40℃放置1小时;随后加入4.11g三聚氰胺包覆的聚磷酸铵(MFAPP)和5.48g季戊四醇(PER)搅拌混合5min,随后利用高速搅拌机,2000rpm下搅拌3min,直到形成均一稳定混合物;倒入聚四氟乙烯模具中,置于真空干燥箱中固化,固化条件为55℃固化45min后升温到85℃继续固化90min,脱模,得到复合材料样品。27.5g of epoxy resin curing agent (D230) and 82.5g of bisphenol A epoxy resin (DGEBA) were placed in a plastic beaker, stirred and mixed for 10min; the mixture was placed in a vacuum oven at 40°C for 1 hour; then 4.11g Melamine-coated ammonium polyphosphate (MFAPP) and 5.48g pentaerythritol (PER) were stirred and mixed for 5 minutes, then stirred at 2000 rpm for 3 minutes using a high-speed mixer until a uniform and stable mixture was formed; poured into a polytetrafluoroethylene mold and placed in vacuum drying Curing in the box, the curing condition is 55°C for 45 minutes, then the temperature is raised to 85°C for 90 minutes, and the mold is demoulded to obtain a composite material sample.
对比例2Comparative example 2
27.5g环氧树脂固化剂(D230)和82.5g双酚A型环氧树脂(DGEBA)放置于塑料烧杯中,搅拌混合10min;混合物置于真空干燥箱内40℃放置1小时;随后加入4.11g三聚氰胺包覆的聚磷酸铵(MFAPP)和5.48g亚麻纤维,搅拌混合5min,随后利用高速搅拌机,2000rpm下搅拌3min,直到形成均一稳定混合物;倒入聚四氟乙烯模具中,置于真空干燥箱中固化,固化条件为55℃固化45min后升温到85℃继续固化90min,脱模,得到复合材料样品。27.5g of epoxy resin curing agent (D230) and 82.5g of bisphenol A epoxy resin (DGEBA) were placed in a plastic beaker, stirred and mixed for 10min; the mixture was placed in a vacuum oven at 40°C for 1 hour; then 4.11g Melamine-coated ammonium polyphosphate (MFAPP) and 5.48g flax fiber were stirred and mixed for 5 minutes, and then stirred at 2000rpm for 3 minutes using a high-speed mixer until a uniform and stable mixture was formed; poured into a polytetrafluoroethylene mold and placed in a vacuum oven Medium curing, the curing condition is 55°C for 45 minutes, then the temperature is raised to 85°C for 90 minutes, and the mold is demoulded to obtain a composite material sample.
实施例1Example 1
将100份亚麻纤维浸置于1500份蒸馏水中,滴入预先配置好的0.1mol/L的CuSO4溶液2份,缓慢加入24.6份的双氧水(H2O2含量30%)溶液,置于30℃恒温搅拌反应72小时,抽滤并用蒸馏水将羧基亚麻纤维洗涤干净,放入80℃干燥箱中烘干12小时。取出后用高速搅拌机粉碎6min,得到固体产物,采用滴定法测试羧基含量约12.6%,标记样品为OLF12.6。Immerse 100 parts of flax fibers in 1500 parts of distilled water, drop 2 parts of pre-configured 0.1mol/L CuSO solution, slowly add 24.6 parts of hydrogen peroxide (H 2 O 2 content 30%) solution, place at 30 ℃ constant temperature stirring reaction for 72 hours, suction filtration and distilled water to wash the carboxy flax fiber, put it in a drying oven at 80 ℃ and dry for 12 hours. After taking it out, it was pulverized with a high-speed mixer for 6 minutes to obtain a solid product. The carboxyl content was measured to be about 12.6% by titration method, and the marked sample was OLF12.6.
实施例2Example 2
将100份亚麻纤维浸置于1500份蒸馏水中,滴入预先配置好的0.05mol/L的FeCl2溶液3份,缓慢加入48.6份的双氧水(H2O2含量30%)溶液,置于35℃恒温搅拌反应60小时,抽滤并用蒸馏水将羧基亚麻纤维洗涤干净,放入85℃干燥箱中烘干12小时。取出后将纤维用高速搅拌机粉碎6min,得到固体产物,采用滴定法测试羧基含量约27.4%,标记样品为OLF27.4。Immerse 100 parts of flax fibers in 1500 parts of distilled water, drop 3 parts of pre-configured 0.05mol/L FeCl solution, slowly add 48.6 parts of hydrogen peroxide (H 2 O 2 content 30%) solution, place at 35 ℃ constant temperature stirring reaction for 60 hours, suction filtration and distilled water to wash the carboxy flax fiber, put it in a drying oven at 85 ℃ and dry for 12 hours. After taking out, the fiber was pulverized with a high-speed mixer for 6 minutes to obtain a solid product. The carboxyl content was measured to be about 27.4% by titration method, and the marked sample was OLF27.4.
实施例3Example 3
将100份亚麻纤维浸置于1500份蒸馏水中,滴入预先配置好的0.05mol/L的CoCl2溶液3份,缓慢加入50.9份的双氧水(H2O2含量30%)溶液,置于40℃恒温搅拌反应70小时,将进行抽滤并用蒸馏水羧基亚麻纤维洗涤干净,放入85℃干燥箱中烘干12小时。取出后将纤维用高速搅拌机粉碎6min,得到固体产物,采用滴定法测试羧基含量约28.4%,标记样品为OLF28.4。Soak 100 parts of flax fibers in 1500 parts of distilled water, drop 3 parts of pre-configured 0.05mol/L CoCl solution , slowly add 50.9 parts of hydrogen peroxide (H 2 O 2 content 30%) solution, place at 40 ℃ constant temperature stirring reaction for 70 hours, will be suction filtered and washed with distilled water carboxy flax fiber, put into 85 ℃ drying oven to dry for 12 hours. After taking it out, the fiber was pulverized with a high-speed mixer for 6 minutes to obtain a solid product. The carboxyl content was measured to be about 28.4% by titration method, and the marked sample was OLF28.4.
实施例4Example 4
将100份亚麻纤维浸置于1500份蒸馏水中,滴入预先配置好的0.05mol/L的NiCl2溶液3份,缓慢加入92.2份的双氧水(H2O2含量30%)溶液,置于40℃恒温搅拌反应70小时,进行抽滤并用蒸馏水将羧基亚麻纤维洗涤干净,放入85℃干燥箱中烘干12小时。取出后将纤维用高速搅拌机粉碎6min,得到固体产物,采用滴定法测试羧基含量约34.5%,标记样品为OLF34.5。Immerse 100 parts of flax fibers in 1500 parts of distilled water, drop 3 parts of pre-configured 0.05mol/L NiCl solution, slowly add 92.2 parts of hydrogen peroxide (H 2 O 2 content 30%) solution, place at 40 ℃ constant temperature stirring reaction for 70 hours, suction filtration and distilled water to wash the carboxy flax fiber, put it in a drying oven at 85 ℃ for 12 hours. After taking it out, the fiber was pulverized with a high-speed mixer for 6 minutes to obtain a solid product. The carboxyl content was measured to be about 34.5% by titration method, and the marked sample was OLF34.5.
对实施例1~4制备得到的羧基亚麻纤维进行红外、核磁共振、热重、及热重红外分析,结果见图1~4。由图1可见,与亚麻相比,OLF在1735cm-1处的新出现一处强烈的吸收峰,归属为C=O伸缩振动峰,随着羧基含量的增加,1735cm-1处吸收峰的强度增加。同时在1640cm-1对应于亚麻纤维吸附水羟基的吸收振动峰,其强度明显下降。红外谱图结果说明,采用H2O2催化氧化亚麻纤维,其产物是羧基亚麻纤维。由图2可见,61ppm归属于葡萄糖环侧链的C6的特征吸收峰,74ppm,73ppm,71ppm分别归属于葡萄糖骨架的C3、C2和C5的特征吸收峰,101ppm则为C1的特征吸收峰。与NLF曲线相比较,曲线OLF12.6,OLF27.4和OLF34.5在173ppm位置出现一个新的特征吸收峰,归属于C6上羟基被氧化为羧基后的响应峰,同时随着羧基含量的提高,响应峰的强度逐渐增强,从图2可以确认C6的伯羟基被选择性的氧化为羧基,而曲线在220~230ppm无新的吸收峰出现,因此判断反应过程C2和C3位置羟基不发生氧化反应。图3说明随着羧基含量的提高,OLF受热分解的残炭量逐渐增加,在膨胀型阻燃体系中,增加炭化率,可降低逸至燃烧区的可燃性挥发产物的量,起到隔热隔氧的作用,降低炭层下材料的可燃性;由图4可见,羧基的存在可以起到催化葡萄糖单元成炭的作用,同时羧基的存在使得在燃烧过程,OLF产生更少量的含碳元素的气体;随着羧基含量的提高,催化成炭效果越明显,含有碳元素的气体释放量越少,有更多的碳元素保留在凝聚相中,从而使得OLF的成炭率逐渐提高。因此,本发明的OLF可作为新型炭源来使用。Carboxylated flax fibers prepared in Examples 1-4 were analyzed by infrared, nuclear magnetic resonance, thermogravimetric, and thermogravimetric infrared, and the results are shown in Figs. 1-4. It can be seen from Figure 1 that compared with flax, OLF has a new strong absorption peak at 1735cm -1 , which is attributed to the C=O stretching vibration peak. With the increase of carboxyl content, the intensity of the absorption peak at 1735cm -1 Increase. At the same time, at 1640cm -1 corresponding to the absorption vibration peak of the flax fiber adsorbed water hydroxyl group, its intensity decreased obviously. The results of infrared spectrum showed that the flax fiber was oxidized by H 2 O 2 and the product was carboxylated flax fiber. As can be seen from Figure 2, 61ppm is attributed to the characteristic absorption peak of C6 of the side chain of the glucose ring, 74ppm, 73ppm, and 71ppm are respectively assigned to the characteristic absorption peaks of C3, C2 and C5 of the glucose skeleton, and 101ppm is the characteristic absorption peak of C1. Compared with the NLF curve, the curves OLF12.6, OLF27.4 and OLF34.5 have a new characteristic absorption peak at 173ppm, which belongs to the response peak after the hydroxyl group on C6 is oxidized to carboxyl group. , the intensity of the response peak gradually increases. From Figure 2, it can be confirmed that the primary hydroxyl group of C6 is selectively oxidized to carboxyl group, and the curve has no new absorption peak at 220-230ppm, so it is judged that the hydroxyl group at positions C2 and C3 does not oxidize during the reaction process. reaction. Figure 3 shows that as the content of carboxyl groups increases, the amount of carbon residue from thermal decomposition of OLF gradually increases. In an intumescent flame retardant system, increasing the carbonization rate can reduce the amount of flammable volatile products that escape into the combustion zone and play a role in heat insulation. The role of oxygen barrier reduces the flammability of materials under the carbon layer; as can be seen from Figure 4, the presence of carboxyl groups can play a role in catalyzing the formation of glucose units into carbon. At the same time, the presence of carboxyl groups makes OLF produce less carbon-containing elements during the combustion process. As the content of carboxyl groups increases, the catalytic char formation effect is more obvious, the release of carbon-containing gas is less, and more carbon elements are retained in the condensed phase, so that the char formation rate of OLF gradually increases. Therefore, the OLF of the present invention can be used as a novel carbon source.
实施例5Example 5
27.5g环氧树脂固化剂(D230)和82.5g双酚A型环氧树脂(DGEBA)放置于塑料烧杯中,搅拌混合10min;混合物置于真空干燥箱内40℃放置1小时;随后加入4.11g三聚氰胺包覆的聚磷酸铵(MFAPP)和5.48g实施例1制备得到的羧基亚麻纤维(OLF12.6)搅拌混合5min,随后利用高速搅拌机,2000rpm下搅拌3min,直到形成均一稳定混合物;倒入聚四氟乙烯模具中,置于真空干燥箱中固化,固化条件为55℃固化45min后升温到85℃继续固化90min,脱模,得到复合材料样品。27.5g of epoxy resin curing agent (D230) and 82.5g of bisphenol A epoxy resin (DGEBA) were placed in a plastic beaker, stirred and mixed for 10min; the mixture was placed in a vacuum oven at 40°C for 1 hour; then 4.11g The ammonium polyphosphate (MFAPP) coated with melamine and the carboxyl flax fiber (OLF12.6) prepared by 5.48g embodiment 1 were stirred and mixed for 5min, then utilized a high-speed stirrer, and stirred for 3min at 2000rpm until a uniform and stable mixture was formed; Place in a tetrafluoroethylene mold and cure in a vacuum drying oven. The curing condition is 55°C for 45 minutes, then raise the temperature to 85°C for 90 minutes, and demould to obtain a composite material sample.
实施例6Example 6
27.5g环氧树脂固化剂(D230)和82.5g双酚A型环氧树脂(DGEBA)放置于塑料烧杯中,搅拌混合10min;混合物置于真空干燥箱内40℃放置1小时;随后加入4.11g三聚氰胺包覆的聚磷酸铵(MFAPP)和5.48g实施例2制备得到的羧基亚麻纤维(OLF27.4)搅拌混合5min,随后利用高速搅拌机,2000rpm下搅拌3min,直到形成均一稳定混合物;倒入聚四氟乙烯模具中,置于真空干燥箱中固化,固化条件为55℃固化45min后升温到85℃继续固化90min,脱模,得到复合材料样品。27.5g of epoxy resin curing agent (D230) and 82.5g of bisphenol A epoxy resin (DGEBA) were placed in a plastic beaker, stirred and mixed for 10min; the mixture was placed in a vacuum oven at 40°C for 1 hour; then 4.11g The ammonium polyphosphate (MFAPP) coated with melamine and the carboxyl flax fiber (OLF27.4) prepared by 5.48g embodiment 2 were stirred and mixed for 5min, then utilized a high-speed stirrer, and stirred for 3min at 2000rpm until a uniform and stable mixture was formed; Place in a tetrafluoroethylene mold and cure in a vacuum drying oven. The curing condition is 55°C for 45 minutes, then raise the temperature to 85°C for 90 minutes, and demould to obtain a composite material sample.
实施例7Example 7
27.5g环氧树脂固化剂(D230)和82.5g双酚A型环氧树脂(DGEBA)放置于塑料烧杯中,搅拌混合10min;混合物置于真空干燥箱内40℃放置1小时;随后加入4.11g三聚氰胺包覆的聚磷酸铵(MFAPP)和5.48g实施例4制备得到的羧基亚麻纤维(OLF34.5)搅拌混合5min,随后利用高速搅拌机,2000rpm下搅拌3min,直到形成均一稳定混合物;倒入聚四氟乙烯模具中,置于真空干燥箱中固化,固化条件为55℃固化45min后升温到85℃继续固化90min,脱模,得到复合材料样品。27.5g of epoxy resin curing agent (D230) and 82.5g of bisphenol A epoxy resin (DGEBA) were placed in a plastic beaker, stirred and mixed for 10min; the mixture was placed in a vacuum oven at 40°C for 1 hour; then 4.11g The ammonium polyphosphate (MFAPP) coated with melamine and the carboxyl flax fiber (OLF34.5) prepared by 5.48g embodiment 4 were stirred and mixed for 5min, then utilized a high-speed stirrer, and stirred for 3min at 2000rpm until a uniform and stable mixture was formed; Place in a tetrafluoroethylene mold and cure in a vacuum drying oven. The curing condition is 55°C for 45 minutes, then raise the temperature to 85°C for 90 minutes, and demould to obtain a composite material sample.
对实施例5~7制备得到的环氧树脂复合材料各项性能指标进行检测,结果见表1和表2,及图5和图6。其中,表1为以不同炭源制备的膨胀阻燃环氧树脂的阻燃性能,表2为纯EP和不同炭源制备的膨胀阻燃环氧树脂的锥形量热参数。Various performance indicators of the epoxy resin composite materials prepared in Examples 5-7 were tested, and the results are shown in Table 1 and Table 2, and Fig. 5 and Fig. 6 . Among them, Table 1 shows the flame retardant properties of intumescent flame retardant epoxy resins prepared with different carbon sources, and Table 2 shows the cone calorimetry parameters of intumescent flame retardant epoxy resins prepared with pure EP and different carbon sources.
由表1可见,炭源为PER、NLF、OLF(用量为5份)对MFAPP/EP阻燃性能的影响,在相同的添加量下(MFAPP用量为3.75份),以PER作为炭源时,EP的LOI只有24.5%,且无阻燃等级,阻燃效果最差。这是由于PER的成炭率仅有0.9%,无法形成有效的膨胀型炭层,起到阻燃效果。当添加5%的OLF作为炭源时,随着羧基含量的增加,EP的阻燃性能逐渐提高,以OLF27.4为炭源的MFAPP/EP阻燃性能最好。随着羧基含量的提高,OLF的热稳定降低,炭化温度下降至与MFAPP的初始分解温度更加匹配;并且残炭量逐渐增大,燃烧释放的可燃性气体逐渐减少,因此提高了EP的阻燃性能。而由于OLF34.4炭化温度降低过多,在MFAPP分解前,已提前分解成炭,最终不能形成多孔炭层,对EP的阻燃性能作用下降。以OLF27.4为炭源阻燃效果明显优于纯亚麻纤维,主要是OLF27.4在燃烧中更容易成炭形成多孔炭层结构,可降低逸至燃烧区的可燃性挥发产物的量,同时燃烧释放的更少量的可燃物等。It can be seen from Table 1 that the carbon source is PER, NLF, OLF (amount of 5 parts) on the flame retardancy of MFAPP/EP. Under the same addition amount (MFAPP dosage is 3.75 parts), when PER is used as a carbon source, The LOI of EP is only 24.5%, and there is no flame retardant grade, and the flame retardant effect is the worst. This is because the char formation rate of PER is only 0.9%, which cannot form an effective intumescent char layer and play a flame retardant effect. When 5% OLF was added as carbon source, the flame retardancy of EP gradually improved with the increase of carboxyl content, and the flame retardancy of MFAPP/EP with OLF27.4 as carbon source was the best. With the increase of carboxyl content, the thermal stability of OLF decreases, and the carbonization temperature drops to match the initial decomposition temperature of MFAPP; and the amount of residual carbon gradually increases, and the flammable gas released by combustion gradually decreases, thus improving the flame retardancy of EP performance. However, because the carbonization temperature of OLF34.4 decreased too much, before the decomposition of MFAPP, it had been decomposed into charcoal in advance, and finally the porous charcoal layer could not be formed, and the flame retardant performance of EP was reduced. The flame retardant effect of using OLF27.4 as a carbon source is obviously better than that of pure flax fiber, mainly because OLF27.4 is more likely to form carbon during combustion to form a porous carbon layer structure, which can reduce the amount of flammable volatile products that escape into the combustion zone, and at the same time A smaller amount of combustibles released by combustion, etc.
表1 以不同炭源制备的膨胀阻燃环氧树脂的阻燃性能Table 1 Flame retardant properties of intumescent flame retardant epoxy resins prepared with different carbon sources
表2 纯EP和不同炭源制备的膨胀阻燃环氧树脂的锥形量热参数Table 2 Cone calorimetry parameters of intumescent flame retardant epoxy resins prepared from pure EP and different carbon sources
由图5的锥形量热谱图中可以看到,纯的环氧树脂热释放速率(PHRR)为1247.3kW/m2,总的热释放量(THR)为49.8MJ/m2,烟密度(TSP)为26.7m2/kg说明环氧树脂是种易燃材料,当引入不同的阻燃剂(MFAPP/PER,MFAPP/NLF和MFAPP/OLF)时,可以降低环氧树脂PHRR和THR的数值。其中MFAPP/OLF27.4降低的最多,PHRR降低为553.5kW/m2,THR降低为19.4MJ/m2。同时,MFAPP/OLF27.4加入到环氧树脂中更极大降低了材料的总的烟释放量(TSP),这是因为OLF27.4和MFAPP发挥了较好的协同阻燃效果,在燃烧过程中能够形成比较连续且致密的炭层,从而阻碍的热量,可燃性气体和氧气向基材内部的传递,起到很好的屏障作用,从而达到较好的阻燃效果。这个推断由图6展示的图片可以得到证实,即当炭源为羧基亚麻纤维时,燃烧后的成炭率更高(最大数值超过41%),便于包覆由MFAPP分解释放的气体,使得体系的膨胀率更好,隔热隔氧的作用更充分,因此阻燃效果更好。It can be seen from the cone calorimetry diagram in Figure 5 that the heat release rate (PHRR) of pure epoxy resin is 1247.3kW/m 2 , the total heat release (THR) is 49.8MJ/m 2 , and the smoke density (TSP) is 26.7m 2 /kg, indicating that epoxy resin is a flammable material. When different flame retardants (MFAPP/PER, MFAPP/NLF and MFAPP/OLF) are introduced, the PHRR and THR of epoxy resin can be reduced. value. Among them, MFAPP/OLF27.4 decreased the most, PHRR decreased to 553.5kW/m 2 , and THR decreased to 19.4MJ/m 2 . At the same time, the addition of MFAPP/OLF27.4 to epoxy resin greatly reduces the total smoke emission (TSP) of the material. This is because OLF27.4 and MFAPP have a better synergistic flame retardant effect. A relatively continuous and dense carbon layer can be formed in the medium, thereby hindering the transfer of heat, flammable gas and oxygen to the interior of the substrate, and playing a good barrier role, thereby achieving a better flame retardant effect. This inference can be confirmed by the picture shown in Figure 6, that is, when the carbon source is carboxylated flax fiber, the char formation rate after combustion is higher (the maximum value exceeds 41%), which is convenient for covering the gas released by the decomposition of MFAPP, making the system The expansion rate is better, and the effect of heat and oxygen insulation is more sufficient, so the flame retardant effect is better.
上述实施例为本发明较佳的实施方式,但本发明的实施方式并不受上述实施例的限制,其他的任何未背离本发明的精神实质与原理下所作的改变、修饰、替代、组合、简化,均应为等效的置换方式,都包含在本发明的保护范围之内。The above-mentioned embodiment is a preferred embodiment of the present invention, but the embodiment of the present invention is not limited by the above-mentioned embodiment, and any other changes, modifications, substitutions, combinations, Simplifications should be equivalent replacement methods, and all are included in the protection scope of the present invention.
Claims (5)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610383752.XA CN106046681B (en) | 2016-06-01 | 2016-06-01 | A kind of flax fiber element base phosphorus expanding fire retardant and its preparation method and application |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610383752.XA CN106046681B (en) | 2016-06-01 | 2016-06-01 | A kind of flax fiber element base phosphorus expanding fire retardant and its preparation method and application |
Publications (2)
Publication Number | Publication Date |
---|---|
CN106046681A CN106046681A (en) | 2016-10-26 |
CN106046681B true CN106046681B (en) | 2018-09-14 |
Family
ID=57172770
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201610383752.XA Expired - Fee Related CN106046681B (en) | 2016-06-01 | 2016-06-01 | A kind of flax fiber element base phosphorus expanding fire retardant and its preparation method and application |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN106046681B (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110054809B (en) * | 2019-04-18 | 2021-04-06 | 宁波一舟塑胶有限公司 | Composite flame retardant, preparation method thereof and application thereof in polypropylene |
CN110564108B (en) * | 2019-09-29 | 2021-08-17 | 国网江苏省电力有限公司镇江供电分公司 | Clean flame-retardant and smoke-suppressing epoxy resin nano composite material and preparation method thereof |
CN112279927A (en) * | 2020-11-04 | 2021-01-29 | 暨南大学 | Carboxy nanocellulose, its preparation method and application |
CN112795140B (en) * | 2021-01-04 | 2021-10-01 | 中变集团上海变压器有限公司 | Epoxy resin coil for transformer and processing technology thereof |
CN113563486B (en) * | 2021-07-01 | 2022-07-05 | 杭州志合新材料有限公司 | Flame-retardant nanocellulose containing phosphorus nitrile group, preparation method and flame-retardant polylactic acid thereof |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103073751A (en) * | 2012-11-22 | 2013-05-01 | 中国科学院宁波材料技术与工程研究所 | Expansive type fire retardant, flame retardation polymer composition containing fire retardant and fiber enhanced polymer-based flame retardation composite material |
CN104017090A (en) * | 2014-05-05 | 2014-09-03 | 华南理工大学 | Method for preparing carboxycellulose by using hydrogen peroxide |
CN104804218A (en) * | 2015-04-28 | 2015-07-29 | 中科院广州化学有限公司南雄材料生产基地 | Nanocellulose surface-modified core-shell structure fire retardant, and preparation method and application of fire retardant |
-
2016
- 2016-06-01 CN CN201610383752.XA patent/CN106046681B/en not_active Expired - Fee Related
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103073751A (en) * | 2012-11-22 | 2013-05-01 | 中国科学院宁波材料技术与工程研究所 | Expansive type fire retardant, flame retardation polymer composition containing fire retardant and fiber enhanced polymer-based flame retardation composite material |
CN104017090A (en) * | 2014-05-05 | 2014-09-03 | 华南理工大学 | Method for preparing carboxycellulose by using hydrogen peroxide |
CN104804218A (en) * | 2015-04-28 | 2015-07-29 | 中科院广州化学有限公司南雄材料生产基地 | Nanocellulose surface-modified core-shell structure fire retardant, and preparation method and application of fire retardant |
Non-Patent Citations (3)
Title |
---|
"Effects of microencapsulated APP-II on the microstructure and flame retardancy of PP/APP-II/PER composites";Lin Yang等;《Polymer Degradation and Stability》;20140425(第105期);第150-159页 * |
"定位氧化淀粉的制备及对环氧树脂膨胀阻燃体系的影响";张水洞等;《高分子材料科学与工程》;20160228;第32卷(第2期);第78-82页 * |
"过氧化氢氧化再生纤维素及其阻燃、吸附性能";张水洞等;《化工学报》;20160301;第67卷(第6期);第2401-2409页 * |
Also Published As
Publication number | Publication date |
---|---|
CN106046681A (en) | 2016-10-26 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN106046681B (en) | A kind of flax fiber element base phosphorus expanding fire retardant and its preparation method and application | |
CN113667277B (en) | A low heat release, low smoke, high flame retardant epoxy resin material and preparation method thereof | |
CN111875648A (en) | Bio-based macromolecular flame retardant and preparation method and application thereof | |
CN113817287A (en) | Bio-based nano synergistic flame retardant and preparation method and application thereof | |
CN101368000A (en) | Sepiolite based flame retarding polymer and method of producing the same | |
Han et al. | Half etching of ZIF-67 towards open hollow nanostructure with boosted absorption ability for toxic smoke and fume in epoxy composites | |
Guo et al. | Flame retardant, high mechanical strength, transparent and water-resistant epoxy composites modified with chitosan derivatives | |
CN101284994A (en) | Polyphosphate pillared hydrotalcite inorganic flame retardant and preparation method thereof | |
Lin et al. | Growing metal–organic framework nanoparticles on short carbon fibers to improve flame retardancy, smoke suppression and mechanical properties of the flame retardant epoxy composites | |
CN105111321A (en) | High-carbonization-rate carboxyl starch, preparation method and application thereof, and intumescent halogen-free flame retardant based on starch | |
CN115232445B (en) | Flame-retardant epoxy resin and preparation method thereof | |
Yang et al. | Preparation of a novel flame retardant based on phosphorus/nitrogen modified lignin with metal–organic framework and its application in epoxy resin | |
Lian et al. | A novel bio-based PAbz@ PBA maize structure for improving fire protection, toxic gas suppression and mechanical performance of intumescent flame-retardant epoxy coatings | |
Yin et al. | A novel P/Fe/Si-doped porphyrin with excellent flame retardancy and ultrastrong toughening effect on epoxy resin | |
CN104945661A (en) | Microencapsulated red phosphorus, flame retardant wood-plastic composite material based on microencapsulated red phosphorus and preparation method of microencapsulated red phosphorus | |
Zuo et al. | Construction of PAN composite fibers with flame retardant, smoke suppression and enhanced mechanical properties based on self-assembled supramolecular network | |
Gao et al. | Preparation of flame retardant and antibacterial polyacrylonitrile based on Cu2+ chelated six-armed star-type flame retardant SCCP and chitosan | |
CN107057302A (en) | Smoke-inhibiting type Flame-retardant PET composite and preparation method thereof | |
CN106674592A (en) | Phosphate melamine salt type nitrogen and phosphorus intumescent flame retardant as well as preparation method and application thereof | |
CN105440525A (en) | Fire-proof and flame-retardant plastic sheet and preparation method thereof | |
CN110551324A (en) | Preparation method and application of nanoscale transition metal oxide loaded expanded graphite particles | |
CN110042652A (en) | A kind of expandable flame retardant coating solution and its application | |
CN116120636A (en) | A kind of modified vermiculite halogen-free phosphorus-free anti-droplet expansion flame retardant and its preparation method and application | |
CN115028984A (en) | Conductive foam material with good flame-retardant property and preparation method thereof | |
CN115613358A (en) | A kind of composite plant fiber flame retardant modifier and its application |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180914 Termination date: 20200601 |
|
CF01 | Termination of patent right due to non-payment of annual fee |