CN101503490B - A kind of synthetic method of low molecular weight styrene/maleic anhydride alternating copolymer - Google Patents
A kind of synthetic method of low molecular weight styrene/maleic anhydride alternating copolymer Download PDFInfo
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- CN101503490B CN101503490B CN2009100794908A CN200910079490A CN101503490B CN 101503490 B CN101503490 B CN 101503490B CN 2009100794908 A CN2009100794908 A CN 2009100794908A CN 200910079490 A CN200910079490 A CN 200910079490A CN 101503490 B CN101503490 B CN 101503490B
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- 238000010189 synthetic method Methods 0.000 title claims description 3
- WOLATMHLPFJRGC-UHFFFAOYSA-N furan-2,5-dione;styrene Chemical compound O=C1OC(=O)C=C1.C=CC1=CC=CC=C1 WOLATMHLPFJRGC-UHFFFAOYSA-N 0.000 title abstract description 27
- 229920005603 alternating copolymer Polymers 0.000 title abstract description 26
- 229920001577 copolymer Polymers 0.000 claims abstract description 38
- 239000003999 initiator Substances 0.000 claims abstract description 19
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 claims abstract description 17
- 238000000034 method Methods 0.000 claims abstract description 14
- 150000001335 aliphatic alkanes Chemical class 0.000 claims abstract description 7
- -1 azo compound Chemical class 0.000 claims abstract description 5
- XYLMUPLGERFSHI-UHFFFAOYSA-N alpha-Methylstyrene Chemical compound CC(=C)C1=CC=CC=C1 XYLMUPLGERFSHI-UHFFFAOYSA-N 0.000 claims abstract description 3
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 claims description 25
- 238000003756 stirring Methods 0.000 claims description 25
- 239000006185 dispersion Substances 0.000 claims description 18
- 239000000178 monomer Substances 0.000 claims description 14
- 238000009826 distribution Methods 0.000 claims description 12
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 11
- 238000006243 chemical reaction Methods 0.000 claims description 10
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 claims description 7
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical group CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 claims description 7
- 239000004342 Benzoyl peroxide Substances 0.000 claims description 6
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical group C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-N 0.000 claims description 6
- 125000000217 alkyl group Chemical group 0.000 claims description 6
- 235000019400 benzoyl peroxide Nutrition 0.000 claims description 6
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 claims description 4
- XEKOWRVHYACXOJ-UHFFFAOYSA-N ethyl acetate Substances CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims description 4
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- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 claims description 3
- 239000002245 particle Substances 0.000 claims description 3
- 229920000642 polymer Polymers 0.000 claims description 3
- 229910052757 nitrogen Inorganic materials 0.000 claims description 2
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- BEQKKZICTDFVMG-UHFFFAOYSA-N 1,2,3,4,6-pentaoxepane-5,7-dione Chemical compound O=C1OOOOC(=O)O1 BEQKKZICTDFVMG-UHFFFAOYSA-N 0.000 claims 1
- WYGWHHGCAGTUCH-UHFFFAOYSA-N 2-[(2-cyano-4-methylpentan-2-yl)diazenyl]-2,4-dimethylpentanenitrile Chemical compound CC(C)CC(C)(C#N)N=NC(C)(C#N)CC(C)C WYGWHHGCAGTUCH-UHFFFAOYSA-N 0.000 claims 1
- YIVJZNGAASQVEM-UHFFFAOYSA-N Lauroyl peroxide Chemical compound CCCCCCCCCCCC(=O)OOC(=O)CCCCCCCCCCC YIVJZNGAASQVEM-UHFFFAOYSA-N 0.000 claims 1
- WPYMKLBDIGXBTP-UHFFFAOYSA-N benzoic acid Chemical compound OC(=O)C1=CC=CC=C1 WPYMKLBDIGXBTP-UHFFFAOYSA-N 0.000 claims 1
- 238000005119 centrifugation Methods 0.000 claims 1
- LSXWFXONGKSEMY-UHFFFAOYSA-N di-tert-butyl peroxide Chemical compound CC(C)(C)OOC(C)(C)C LSXWFXONGKSEMY-UHFFFAOYSA-N 0.000 claims 1
- 238000001035 drying Methods 0.000 claims 1
- 238000005502 peroxidation Methods 0.000 claims 1
- VVWRJUBEIPHGQF-UHFFFAOYSA-N propan-2-yl n-propan-2-yloxycarbonyliminocarbamate Chemical compound CC(C)OC(=O)N=NC(=O)OC(C)C VVWRJUBEIPHGQF-UHFFFAOYSA-N 0.000 claims 1
- 238000006116 polymerization reaction Methods 0.000 abstract description 14
- 238000012673 precipitation polymerization Methods 0.000 abstract description 9
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 abstract description 7
- 239000012429 reaction media Substances 0.000 abstract description 4
- 239000012986 chain transfer agent Substances 0.000 abstract description 3
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 150000001451 organic peroxides Chemical class 0.000 abstract description 3
- 238000000710 polymer precipitation Methods 0.000 abstract description 2
- 239000012046 mixed solvent Substances 0.000 abstract 1
- 230000002194 synthesizing effect Effects 0.000 abstract 1
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2-(2-cyanopropan-2-yldiazenyl)-2-methylpropanenitrile Chemical compound N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 description 30
- 239000002904 solvent Substances 0.000 description 16
- 238000005227 gel permeation chromatography Methods 0.000 description 13
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 9
- 238000002360 preparation method Methods 0.000 description 9
- 230000015572 biosynthetic process Effects 0.000 description 8
- MLFHJEHSLIIPHL-UHFFFAOYSA-N isoamyl acetate Chemical compound CC(C)CCOC(C)=O MLFHJEHSLIIPHL-UHFFFAOYSA-N 0.000 description 8
- 239000000203 mixture Substances 0.000 description 8
- 238000003786 synthesis reaction Methods 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 229910001873 dinitrogen Inorganic materials 0.000 description 7
- 239000000843 powder Substances 0.000 description 7
- 239000000463 material Substances 0.000 description 6
- 238000001228 spectrum Methods 0.000 description 5
- DKPFZGUDAPQIHT-UHFFFAOYSA-N Butyl acetate Natural products CCCCOC(C)=O DKPFZGUDAPQIHT-UHFFFAOYSA-N 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 4
- FUZZWVXGSFPDMH-UHFFFAOYSA-N hexanoic acid Chemical compound CCCCCC(O)=O FUZZWVXGSFPDMH-UHFFFAOYSA-N 0.000 description 4
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- 239000011259 mixed solution Substances 0.000 description 4
- 239000011877 solvent mixture Substances 0.000 description 4
- 125000004432 carbon atom Chemical group C* 0.000 description 3
- HNAGHMKIPMKKBB-UHFFFAOYSA-N 1-benzylpyrrolidine-3-carboxamide Chemical compound C1C(C(=O)N)CCN1CC1=CC=CC=C1 HNAGHMKIPMKKBB-UHFFFAOYSA-N 0.000 description 2
- XINCECQTMHSORG-UHFFFAOYSA-N Isoamyl isovalerate Chemical compound CC(C)CCOC(=O)CC(C)C XINCECQTMHSORG-UHFFFAOYSA-N 0.000 description 2
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical group SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 description 2
- CRZQGDNQQAALAY-UHFFFAOYSA-N Methyl benzeneacetate Chemical compound COC(=O)CC1=CC=CC=C1 CRZQGDNQQAALAY-UHFFFAOYSA-N 0.000 description 2
- QUKGYYKBILRGFE-UHFFFAOYSA-N benzyl acetate Chemical compound CC(=O)OCC1=CC=CC=C1 QUKGYYKBILRGFE-UHFFFAOYSA-N 0.000 description 2
- OBNCKNCVKJNDBV-UHFFFAOYSA-N butanoic acid ethyl ester Natural products CCCC(=O)OCC OBNCKNCVKJNDBV-UHFFFAOYSA-N 0.000 description 2
- XUPYJHCZDLZNFP-UHFFFAOYSA-N butyl butanoate Chemical compound CCCCOC(=O)CCC XUPYJHCZDLZNFP-UHFFFAOYSA-N 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- MTZQAGJQAFMTAQ-UHFFFAOYSA-N ethyl benzoate Chemical compound CCOC(=O)C1=CC=CC=C1 MTZQAGJQAFMTAQ-UHFFFAOYSA-N 0.000 description 2
- PPXUHEORWJQRHJ-UHFFFAOYSA-N ethyl isovalerate Chemical compound CCOC(=O)CC(C)C PPXUHEORWJQRHJ-UHFFFAOYSA-N 0.000 description 2
- FKRCODPIKNYEAC-UHFFFAOYSA-N ethyl propionate Chemical compound CCOC(=O)CC FKRCODPIKNYEAC-UHFFFAOYSA-N 0.000 description 2
- PQLMXFQTAMDXIZ-UHFFFAOYSA-N isoamyl butyrate Chemical compound CCCC(=O)OCCC(C)C PQLMXFQTAMDXIZ-UHFFFAOYSA-N 0.000 description 2
- QPJVMBTYPHYUOC-UHFFFAOYSA-N methyl benzoate Chemical compound COC(=O)C1=CC=CC=C1 QPJVMBTYPHYUOC-UHFFFAOYSA-N 0.000 description 2
- 238000004513 sizing Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- JLIDRDJNLAWIKT-UHFFFAOYSA-N 1,2-dimethyl-3h-benzo[e]indole Chemical compound C1=CC=CC2=C(C(=C(C)N3)C)C3=CC=C21 JLIDRDJNLAWIKT-UHFFFAOYSA-N 0.000 description 1
- LGJCFVYMIJLQJO-UHFFFAOYSA-N 1-dodecylperoxydodecane Chemical compound CCCCCCCCCCCCOOCCCCCCCCCCCC LGJCFVYMIJLQJO-UHFFFAOYSA-N 0.000 description 1
- HFZLSTDPRQSZCQ-UHFFFAOYSA-N 1-pyrrolidin-3-ylpyrrolidine Chemical compound C1CCCN1C1CNCC1 HFZLSTDPRQSZCQ-UHFFFAOYSA-N 0.000 description 1
- AVMSWPWPYJVYKY-UHFFFAOYSA-N 2-Methylpropyl formate Chemical compound CC(C)COC=O AVMSWPWPYJVYKY-UHFFFAOYSA-N 0.000 description 1
- MLLAPOCBLWUFAP-UHFFFAOYSA-N 3-Methylbutyl benzoate Chemical compound CC(C)CCOC(=O)C1=CC=CC=C1 MLLAPOCBLWUFAP-UHFFFAOYSA-N 0.000 description 1
- FERIUCNNQQJTOY-UHFFFAOYSA-M Butyrate Chemical compound CCCC([O-])=O FERIUCNNQQJTOY-UHFFFAOYSA-M 0.000 description 1
- NHTMVDHEPJAVLT-UHFFFAOYSA-N Isooctane Chemical compound CC(C)CC(C)(C)C NHTMVDHEPJAVLT-UHFFFAOYSA-N 0.000 description 1
- RJUFJBKOKNCXHH-UHFFFAOYSA-N Methyl propionate Chemical compound CCC(=O)OC RJUFJBKOKNCXHH-UHFFFAOYSA-N 0.000 description 1
- XBDQKXXYIPTUBI-UHFFFAOYSA-M Propionate Chemical compound CCC([O-])=O XBDQKXXYIPTUBI-UHFFFAOYSA-M 0.000 description 1
- 229940072049 amyl acetate Drugs 0.000 description 1
- 150000008064 anhydrides Chemical class 0.000 description 1
- PGMYKACGEOXYJE-UHFFFAOYSA-N anhydrous amyl acetate Natural products CCCCCOC(C)=O PGMYKACGEOXYJE-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- DULCUDSUACXJJC-UHFFFAOYSA-N benzeneacetic acid ethyl ester Natural products CCOC(=O)CC1=CC=CC=C1 DULCUDSUACXJJC-UHFFFAOYSA-N 0.000 description 1
- UDEWPOVQBGFNGE-UHFFFAOYSA-N benzoic acid n-propyl ester Natural products CCCOC(=O)C1=CC=CC=C1 UDEWPOVQBGFNGE-UHFFFAOYSA-N 0.000 description 1
- 229940007550 benzyl acetate Drugs 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000012662 bulk polymerization Methods 0.000 description 1
- XSIFPSYPOVKYCO-UHFFFAOYSA-N butyl benzoate Chemical group CCCCOC(=O)C1=CC=CC=C1 XSIFPSYPOVKYCO-UHFFFAOYSA-N 0.000 description 1
- PWLNAUNEAKQYLH-UHFFFAOYSA-N butyric acid octyl ester Natural products CCCCCCCCOC(=O)CCC PWLNAUNEAKQYLH-UHFFFAOYSA-N 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- BLCKNMAZFRMCJJ-UHFFFAOYSA-N cyclohexyl cyclohexyloxycarbonyloxy carbonate Chemical compound C1CCCCC1OC(=O)OOC(=O)OC1CCCCC1 BLCKNMAZFRMCJJ-UHFFFAOYSA-N 0.000 description 1
- JVSWJIKNEAIKJW-UHFFFAOYSA-N dimethyl-hexane Natural products CCCCCC(C)C JVSWJIKNEAIKJW-UHFFFAOYSA-N 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- WNAHIZMDSQCWRP-UHFFFAOYSA-N dodecane-1-thiol Chemical compound CCCCCCCCCCCCS WNAHIZMDSQCWRP-UHFFFAOYSA-N 0.000 description 1
- 238000004043 dyeing Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000007720 emulsion polymerization reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- WBJINCZRORDGAQ-UHFFFAOYSA-N formic acid ethyl ester Natural products CCOC=O WBJINCZRORDGAQ-UHFFFAOYSA-N 0.000 description 1
- LYQXSZBJOLZHSM-UHFFFAOYSA-N formic acid pentyl acetate Chemical compound C(=O)O.C(C)(=O)OCCCCC LYQXSZBJOLZHSM-UHFFFAOYSA-N 0.000 description 1
- 238000010528 free radical solution polymerization reaction Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- MNWFXJYAOYHMED-UHFFFAOYSA-M heptanoate Chemical compound CCCCCCC([O-])=O MNWFXJYAOYHMED-UHFFFAOYSA-M 0.000 description 1
- GJRQTCIYDGXPES-UHFFFAOYSA-N iso-butyl acetate Natural products CC(C)COC(C)=O GJRQTCIYDGXPES-UHFFFAOYSA-N 0.000 description 1
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- FGKJLKRYENPLQH-UHFFFAOYSA-M isocaproate Chemical compound CC(C)CCC([O-])=O FGKJLKRYENPLQH-UHFFFAOYSA-M 0.000 description 1
- OQAGVSWESNCJJT-UHFFFAOYSA-N isovaleric acid methyl ester Natural products COC(=O)CC(C)C OQAGVSWESNCJJT-UHFFFAOYSA-N 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229940095102 methyl benzoate Drugs 0.000 description 1
- 229940017219 methyl propionate Drugs 0.000 description 1
- OLXYLDUSSBULGU-UHFFFAOYSA-N methyl pyridine-4-carboxylate Chemical compound COC(=O)C1=CC=NC=C1 OLXYLDUSSBULGU-UHFFFAOYSA-N 0.000 description 1
- UUIQMZJEGPQKFD-UHFFFAOYSA-N n-butyric acid methyl ester Natural products CCCC(=O)OC UUIQMZJEGPQKFD-UHFFFAOYSA-N 0.000 description 1
- 239000012860 organic pigment Substances 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- BWJUFXUULUEGMA-UHFFFAOYSA-N propan-2-yl propan-2-yloxycarbonyloxy carbonate Chemical compound CC(C)OC(=O)OOC(=O)OC(C)C BWJUFXUULUEGMA-UHFFFAOYSA-N 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 229920005604 random copolymer Polymers 0.000 description 1
- 238000010557 suspension polymerization reaction Methods 0.000 description 1
- GJBRNHKUVLOCEB-UHFFFAOYSA-N tert-butyl benzenecarboperoxoate Chemical compound CC(C)(C)OOC(=O)C1=CC=CC=C1 GJBRNHKUVLOCEB-UHFFFAOYSA-N 0.000 description 1
- 125000000999 tert-butyl group Chemical group [H]C([H])([H])C(*)(C([H])([H])[H])C([H])([H])[H] 0.000 description 1
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- 231100000331 toxic Toxicity 0.000 description 1
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Abstract
一种低分子量苯乙烯/马来酸酐交替共聚物的合成方法属于高分子沉淀聚合领域。现有沉淀聚合制备苯乙烯/马来酸酐共聚物的方法中所使用的介质和链转移剂均存在弊端。本发明通过以有机酸烷基酯与烷烃的混合溶剂作为沉淀聚合反应介质,以α-甲基苯乙烯或乙酸乙烯酯为分子量调节剂,以有机过氧化物或偶氮化合物为引发剂引发单体苯乙烯与苯乙烯共聚反应,制得低分子量苯乙烯/马来酸酐交替共聚物。本发明工艺简单、合成的共聚物性能好,具有经济环保等优点。The invention discloses a method for synthesizing low-molecular-weight styrene/maleic anhydride alternating copolymers, belonging to the field of polymer precipitation polymerization. Both the medium and the chain transfer agent used in the existing method for preparing styrene/maleic anhydride copolymer by precipitation polymerization have disadvantages. In the present invention, the mixed solvent of organic acid alkyl ester and alkane is used as the precipitation polymerization reaction medium, α-methylstyrene or vinyl acetate is used as the molecular weight regulator, and organic peroxide or azo compound is used as the initiator to initiate the single polymerization reaction. Bulk styrene and styrene are copolymerized to produce low molecular weight styrene/maleic anhydride alternating copolymers. The invention has the advantages of simple process, good performance of the synthesized copolymer, economy and environmental protection.
Description
技术领域technical field
本发明属于高分子沉淀聚合领域,具体涉及一种沉淀聚合制备低分子量苯乙烯/马来酸酐交替共聚物的方法。The invention belongs to the field of polymer precipitation polymerization, in particular to a method for preparing low molecular weight styrene/maleic anhydride alternating copolymers by precipitation polymerization.
背景技术Background technique
低分子量苯乙烯/马来酸酐交替共聚物是一种具有广泛用途的聚合物,在造纸、纺织、印染、涂料、化工等行业可分别用作纸张表面施胶剂、有机颜料分散剂、乳液聚合的保护胶体等。Low-molecular-weight styrene/maleic anhydride alternating copolymer is a polymer with a wide range of uses. It can be used as paper surface sizing agent, organic pigment dispersant, and emulsion polymerization in papermaking, textile, printing and dyeing, coating, chemical and other industries. protective colloid etc.
目前,苯乙烯/马来酸酐共聚物的制备方法主要有溶液聚合,少量的本体聚合、本体-悬浮聚合、沉淀聚合。其中,沉淀聚合与其他聚合方法相比,具有后处理工艺简单,成本低等优点。At present, the preparation methods of styrene/maleic anhydride copolymer mainly include solution polymerization, a small amount of bulk polymerization, bulk-suspension polymerization, and precipitation polymerization. Among them, compared with other polymerization methods, precipitation polymerization has the advantages of simple post-treatment process and low cost.
如,张国运在“SMA型表面施胶剂的制备与应用”(《造纸化学品》,2005,17(3),pp.30-32)一文中以过氧化苯甲酰(BPO)为引发剂,甲苯为溶剂,通过沉淀聚合的方法合成了苯乙烯/马来酸酐无规共聚物。王荣伟、郁剑乙等在“低分子量SMA交替共聚物的合成”(《石油化工》,1994,23,pp.706-410)一文中选用沉淀聚合法,以十二烷基硫醇为链转移剂,以甲苯为溶剂制备了低分子量的苯乙烯/马来酸酐交替共聚物。For example, Zhang Guoyun used benzoyl peroxide (BPO) as the trigger in the article "Preparation and Application of SMA Surface Sizing Agent" ("Paper Chemicals", 2005, 17(3), pp.30-32). agent, toluene as solvent, synthesized styrene/maleic anhydride random copolymer by precipitation polymerization. Wang Rongwei, Yu Jianyi, etc. chose the precipitation polymerization method in the article "Synthesis of Low Molecular Weight SMA Alternating Copolymer" ("Petrochemical Industry", 1994, 23, pp.706-410), using dodecyl mercaptan as the chain transfer agent, A low molecular weight styrene/maleic anhydride alternating copolymer was prepared with toluene as solvent.
但目前所报道的沉淀聚合普遍采用毒性溶剂甲苯作为反应介质,不利于环保。另外,使用硫醇类链转移剂,导致所制得的共聚物具有刺激性臭味,影响共聚物的使用性能。However, the currently reported precipitation polymerization generally uses the toxic solvent toluene as the reaction medium, which is not conducive to environmental protection. In addition, the use of mercaptan chain transfer agents causes the prepared copolymer to have a pungent odor, which affects the performance of the copolymer.
发明内容Contents of the invention
本发明的目的在于解决现有技术的问题,而提供一种环保,无刺激性臭味的低分子量苯乙烯/马来酸酐交替共聚物的沉淀聚合法。The purpose of the present invention is to solve the problems of the prior art, and provide a kind of environmental protection, the precipitation polymerization method of the low molecular weight styrene/maleic anhydride alternating copolymer without irritating odor.
本发明所提供的低分子量苯乙烯/马来酸酐交替共聚物的合成方法,包括以下步骤:The synthetic method of low molecular weight styrene/maleic anhydride alternating copolymer provided by the present invention may further comprise the steps:
在氮气保护和搅拌的条件下,将单体马来酸酐(MAH)和引发剂加入到介质中溶解,并加热至60~80℃时,滴加单体苯乙烯(St)和分子量调节剂,滴加完毕后继续搅拌反应1~8h,得到低分子量苯乙烯/马来酸酐聚合物粒子的分散体系,将分散体系离心分离、干燥,得到低分子量苯乙烯/马来酸酐交替共聚物;Under the condition of nitrogen protection and stirring, monomer maleic anhydride (MAH) and initiator are added to the medium to dissolve, and when heated to 60-80 °C, monomer styrene (St) and molecular weight regulator are added dropwise, After the dropwise addition, continue to stir and react for 1 to 8 hours to obtain a dispersion system of low molecular weight styrene/maleic anhydride polymer particles, centrifuge and dry the dispersion system to obtain a low molecular weight styrene/maleic anhydride alternating copolymer;
其中,所述的引发剂为有机过氧化物或偶氮化合物;所述的介质为有机酸烷基酯与烷烃或环己烷的混合溶液;所述的分子量调节剂为α-甲基苯乙烯(AMS)或乙酸乙烯酯(VAC);Wherein, the initiator is an organic peroxide or an azo compound; the medium is a mixed solution of an organic acid alkyl ester and alkane or cyclohexane; the molecular weight regulator is α-methylstyrene (AMS) or vinyl acetate (VAC);
马来酸酐和苯乙烯的用量关系,按摩尔比为1∶0.90~0.96;反应体系(两种单体、引发剂、介质与分子量调节剂的质量之和)中两种单体苯乙烯和马来酸酐的质量浓度之和为2.0~7.5%;反应体系中引发剂的质量浓度为0.05~0.35%;反应体系中分子量调节剂的质量浓度为0.10~0.45%;有机酸烷基酯与烷烃的混合溶液中有机酸烷基酯的体积分数为20~80%。The consumption relationship of maleic anhydride and styrene is 1: 0.90~0.96 by molar ratio; Two kinds of monomer styrene and horse The sum of the mass concentration of toic anhydride is 2.0~7.5%; the mass concentration of initiator in the reaction system is 0.05~0.35%; the mass concentration of molecular weight regulator in the reaction system is 0.10~0.45%; the organic acid alkyl ester and alkane The volume fraction of organic acid alkyl ester in the mixed solution is 20-80%.
其中,所述的引发剂均为常规的热分解型引发剂,对于本专业的技术人员所熟知的有机过氧化物有过氧化苯甲酰(BPO)、过氧化二异丙苯、过氧化二特丁基、过氧化十二酰、过氧化苯甲酸特丁酯、过氧化二碳酸二异丙基酯或过氧化二碳酸二环己酯等。偶氮化合物有偶氮二异丁腈(AIBN)或偶氮二异庚腈等。Wherein, described initiator is conventional pyrolysis type initiator, has benzoyl peroxide (BPO), dicumyl peroxide, dicumyl peroxide for the well-known organic peroxide of those skilled in the art. tert-butyl, lauryl peroxide, tert-butyl peroxybenzoate, diisopropyl peroxydicarbonate or dicyclohexyl peroxydicarbonate, etc. Azo compounds include azobisisobutyronitrile (AIBN) or azobisisoheptanonitrile.
所述的有机酸烷基酯的结构通式为:式中,R1为H、C原子数为1~8的烷基,R2为C原子数为1~5的烷基,具体可包括甲酸乙酯、甲酸丙酯、甲酸异丁酯、甲酸戊酯、乙酸乙酯、乙酸丁酯、乙酸异丁酯、乙酸仲丁酯、乙酸戊酯、乙酸异戊酯、乙酸苄酯、丙酸甲酯、丙酸乙酯、丙酸丁酯、丁酸甲酯、丁酸乙酯、丁酸丁酯、丁酸异戊酯、异戊酸乙酯、异戊酸异戊酯、苯甲酸甲酯、苯甲酸乙酯、苯甲酸丙酯、苯甲酸丁酯、苯甲酸异戊酯、苯乙酸甲酯或苯乙酸乙酯等。而考虑到介质应具有适度的极性、溶解度参数和粘度,有机酸烷基酯结构通式中,R1优选C原子数为1~8的烷基。The structural general formula of described organic acid alkyl ester is: In the formula, R1 is H, an alkyl group with 1 to 8 C atoms, and R2 is an alkyl group with 1 to 5 C atoms, which may specifically include ethyl formate, propyl formate, isobutyl formate, formic acid Amyl acetate, ethyl acetate, butyl acetate, isobutyl acetate, sec-butyl acetate, amyl acetate, isoamyl acetate, benzyl acetate, methyl propionate, ethyl propionate, butyl propionate, butyl Methyl Butyrate, Ethyl Butyrate, Butyl Butyrate, Isoamyl Butyrate, Ethyl Isovalerate, Isoamyl Isovalerate, Methyl Benzoate, Ethyl Benzoate, Propyl Benzoate, Benzoic Acid Butyl, isopentyl benzoate, methyl phenylacetate or ethyl phenylacetate, etc. And considering that the medium should have moderate polarity, solubility parameter and viscosity, in the general formula of organic acid alkyl ester, R 1 is preferably an alkyl group with 1 to 8 C atoms.
所述的烷烃为正己烷、正庚烷、正戊烷、正辛烷或异辛烷。The alkane is n-hexane, n-heptane, n-pentane, n-octane or isooctane.
所述的低分子量苯乙烯/马来酸酐交替共聚物的数均分子量范围为3000~12000g/mol,分子量分布范围为1.36~2.0。The number average molecular weight range of the low molecular weight styrene/maleic anhydride alternating copolymer is 3000-12000 g/mol, and the molecular weight distribution range is 1.36-2.0.
本发明中可采用水浴或油浴加热反应体系,根据公知的技术,聚合反应温度由引发剂的分解温度确定,为降低共聚物的分子量,尽可能采用大于引发剂的分解温度,但又低于溶剂沸点的温度加热反应体系。Can adopt water bath or oil bath heating reaction system among the present invention, according to known technology, polymerization reaction temperature is determined by the decomposition temperature of initiator, in order to reduce the molecular weight of copolymer, adopt as far as possible greater than the decomposition temperature of initiator, but lower than The reaction system is heated at the temperature of the boiling point of the solvent.
本发明的关键在于反应介质的选择,选择原则如下:1)介质对两种单体MAH和S t与引发剂具有一定的溶解作用,以保证反应前为均相体系;2)介质不能溶解所生成的低分子量苯乙烯/马来酸酐共聚物,当共聚物分子链达到一定的临界长度后便可从介质中沉析出来。Key of the present invention is the selection of reaction medium, and selection principle is as follows: 1) medium has certain dissolving effect to two kinds of monomers MAH and St and initiator, is homogeneous system before guaranteeing reaction; 2) medium can not dissolve all The resulting low molecular weight styrene/maleic anhydride copolymer can be precipitated from the medium when the molecular chain of the copolymer reaches a certain critical length.
本发明具有以下有益效果:The present invention has the following beneficial effects:
1)本发明采用低毒溶剂为反应介质,反应完成后,无需加入沉淀剂,共聚物便以粒子的形式从介质中沉析出来,后处理工艺简单,且溶剂可回收利用。1) The present invention uses a low-toxic solvent as the reaction medium. After the reaction is completed, the copolymer is precipitated from the medium in the form of particles without adding a precipitant. The post-treatment process is simple, and the solvent can be recycled.
2)本发明所采用的分子量调节剂可有效调节共聚物的分子量的同时避免了硫醇类链转移剂对共聚物性能的影响。2) The molecular weight regulator used in the present invention can effectively regulate the molecular weight of the copolymer while avoiding the influence of the mercaptan chain transfer agent on the properties of the copolymer.
附图说明Description of drawings
图1、实施例1制备的共聚物的凝胶渗透色谱(GPC)谱图。The gel permeation chromatography (GPC) spectrogram of the copolymer prepared in Fig. 1, embodiment 1.
图2、实施例3制备的共聚物的凝胶渗透色谱(GPC)谱图。The gel permeation chromatography (GPC) spectrogram of the copolymer prepared in Fig. 2, embodiment 3.
图3、实施例4制备的共聚物的凝胶渗透色谱(GPC)谱图。The gel permeation chromatography (GPC) spectrogram of the copolymer prepared in Fig. 3, embodiment 4.
图4、实施例7制备的共聚物的凝胶渗透色谱(GPC)谱图。The gel permeation chromatography (GPC) spectrogram of the copolymer prepared in Fig. 4, embodiment 7.
以下结合附图及具体实施方式对本发明作进一步描述。The present invention will be further described below in conjunction with the accompanying drawings and specific embodiments.
具体实施方式Detailed ways
下述实施例中采用型号为waters1515,规格为300PSI/0.001-10ML/min/1-1.75RIV/1的液相色谱仪测定所制得的共聚物的数均分子量及其分布。In the following examples, the number-average molecular weight and distribution of the prepared copolymers were measured by a liquid chromatograph with a model of waters 1515 and a specification of 300PSI/0.001-10ML/min/1-1.75RIV/1.
实施例1Example 1
备料:单体MAH 1.7658g、St 1.6892g,二者的摩尔配比为1∶0.90;引发剂AIBN 0.1831g;溶剂乙酸异戊酯9mL和环己烷36mL的混合液;分子量调节剂AMS 0.2132g。Material preparation: monomer MAH 1.7658g, St 1.6892g, the molar ratio of the two is 1:0.90; initiator AIBN 0.1831g; solvent mixture of isoamyl acetate 9mL and cyclohexane 36mL; molecular weight regulator AMS 0.2132g .
共聚物的合成:将MAH、AIBN和溶剂置于带有搅拌装置和通有氮气的四口瓶中,常温搅拌15min后,采用80℃的恒温水浴锅加热15min,而后在1h内匀速滴加完毕St与AMS的混合物,滴加完毕后继续搅拌反应1h,得到苯乙烯/马来酸酐交替共聚物的分散体系,将分散体系离心分离、干燥,得到苯乙烯/马来酸酐交替共聚物的白色粉末。Synthesis of copolymer: put MAH, AIBN and solvent in a four-neck flask equipped with a stirring device and nitrogen gas, stir at room temperature for 15 minutes, heat for 15 minutes in a constant temperature water bath at 80°C, and then drop them at a constant speed within 1 hour The mixture of St and AMS, after the dropwise addition, continue to stir and react for 1h to obtain a dispersion system of styrene/maleic anhydride alternating copolymer, centrifuge the dispersion and dry to obtain a white powder of styrene/maleic anhydride alternating copolymer .
聚合收率(Cp)、共聚物的数均分子量(Mn)及其分布(PDI)结果见表1,共聚物的GPC谱图见图1。The results of polymerization yield (C p ), number average molecular weight (Mn) and distribution (PDI) of the copolymer are shown in Table 1, and the GPC spectrum of the copolymer is shown in Fig. 1 .
实施例2Example 2
备料:单体MAH 0.4420g、St 0.557g,二者的摩尔配比为1∶0.90;引发剂AIBN 0.0459g;溶剂为9mL乙酸丁酯和36mL环己烷的混合液;分子量调节剂AMS 0.0542g。Preparation: monomer MAH 0.4420g, St 0.557g, the molar ratio of the two is 1:0.90; initiator AIBN 0.0459g; solvent is a mixture of 9mL butyl acetate and 36mL cyclohexane; molecular weight regulator AMS 0.0542g .
共聚物的合成:将MAH、AIBN和溶剂置于带有搅拌装置和通有氮气的四口瓶中,常温搅拌15min后,采用80℃的恒温水浴锅加热15min,而后在0.5h内匀速滴加完毕St与AMS的混合物,滴加完毕后继续搅拌反应8h,得到苯乙烯/马来酸酐交替共聚物的分散体系,将分散体系离心分离、干燥,得到苯乙烯/马来酸酐交替共聚物的白色粉末。Synthesis of copolymers: put MAH, AIBN and solvent in a four-neck flask with a stirring device and nitrogen gas, stir at room temperature for 15 minutes, heat for 15 minutes in a constant temperature water bath at 80°C, and then drop them at a constant speed within 0.5 hours Complete the mixture of St and AMS, continue to stir and react for 8 hours after the dropwise addition, and obtain the dispersion system of styrene/maleic anhydride alternating copolymer, centrifuge and dry the dispersion system to obtain the white color of styrene/maleic anhydride alternating copolymer powder.
聚合收率(Cp)、共聚物的数均分子量(Mn)及其分布(PDI)结果见表1。The results of polymerization yield (C p ), number average molecular weight (Mn) and distribution (PDI) of the copolymer are shown in Table 1.
实施例3Example 3
备料:单体MAH 1.3245g、St 1.2685g,二者的摩尔配比为1∶0.96;引发剂AIBN 0.1360g;溶剂乙酸异戊酯36mL和正己烷9mL的混合液;分子量调节剂VAC 0.1175g。Material preparation: monomer MAH 1.3245g, St 1.2685g, the molar ratio of the two is 1:0.96; initiator AIBN 0.1360g; solvent mixture of isoamyl acetate 36mL and n-hexane 9mL; molecular weight regulator VAC 0.1175g.
共聚物的合成:将MAH、AIBN和溶剂置于带有搅拌装置和通有氮气的四口瓶中,常温搅拌15min后,采用60℃的恒温水浴锅加热15min,而后在1h内匀速滴加完毕St与VAC的混合物,滴加完毕后继续搅拌反应6h,得到苯乙烯/马来酸酐交替共聚物的分散体系,将分散体系离心分离、干燥,得到苯乙烯/马来酸酐交替共聚物的白色粉末。Synthesis of copolymer: put MAH, AIBN and solvent in a four-neck flask with a stirring device and nitrogen gas, stir at room temperature for 15 minutes, heat in a constant temperature water bath at 60°C for 15 minutes, and then drop them at a constant speed within 1 hour The mixture of St and VAC, after the dropwise addition, continue to stir and react for 6 hours to obtain a dispersion system of styrene/maleic anhydride alternating copolymer, centrifuge the dispersion system and dry to obtain a white powder of styrene/maleic anhydride alternating copolymer .
聚合收率(Cp)、共聚物的数均分子量(Mn)及其分布(PDI)结果见表1,共聚物的GPC谱图见图2。The results of polymerization yield (C p ), number average molecular weight (Mn) and distribution (PDI) of the copolymer are shown in Table 1, and the GPC spectrum of the copolymer is shown in Figure 2.
实施例4Example 4
备料:单体MAH 1.3240g、St 1.2664g,二者的摩尔配比为1∶0.9;引发剂AIBN 0.1354g;溶剂乙酸丁酯9mL和正己烷36mL的混合液;分子量调节剂VAC 0.1168g。Material preparation: monomer MAH 1.3240g, St 1.2664g, the molar ratio of the two is 1:0.9; initiator AIBN 0.1354g; solvent butyl acetate 9mL and n-hexane 36mL mixed solution; molecular weight regulator VAC 0.1168g.
共聚物的合成:将MAH、AIBN和溶剂置于带有搅拌装置和通有氮气的四口瓶中,常温搅拌15min后,采用70℃的恒温水浴锅加热15min,而后在1h内匀速滴加完毕St与VAC的混合物,滴加完毕后继续搅拌反应5h,得到苯乙烯/马来酸酐交替共聚物的分散体系,将分散体系离心分离、干燥,得到苯乙烯/马来酸酐交替共聚物的白色粉末。Synthesis of copolymer: put MAH, AIBN and solvent in a four-neck flask with a stirring device and nitrogen gas, stir at room temperature for 15 minutes, heat for 15 minutes in a constant temperature water bath at 70°C, and then drop them at a constant speed within 1 hour The mixture of St and VAC, after the dropwise addition, continue to stir and react for 5 hours to obtain a dispersion system of styrene/maleic anhydride alternating copolymer, centrifuge the dispersion system and dry to obtain a white powder of styrene/maleic anhydride alternating copolymer .
聚合收率(Cp)、共聚物的数均分子量(Mn)及其分布(PDI)结果见表1,共聚物的GPC谱图见图3。The results of polymerization yield (C p ), number average molecular weight (Mn) and distribution (PDI) of the copolymer are shown in Table 1, and the GPC spectrum of the copolymer is shown in Fig. 3 .
实施例5Example 5
备料:单体MAH 1.3239g、St 1.3501g,二者的摩尔配比为1∶0.96;引发剂AIBN 0.0272g;溶剂乙酸丁酯9mL和环己烷36mL的混合液;分子量调节剂AMS 0.0643g。Material preparation: monomer MAH 1.3239g, St 1.3501g, the molar ratio of the two is 1:0.96; initiator AIBN 0.0272g; solvent butyl acetate 9mL and cyclohexane 36mL mixed solution; molecular weight regulator AMS 0.0643g.
共聚物的合成:将MAH、AIBN和溶剂置于带有搅拌装置和通有氮气的四口瓶中,常温搅拌15min后,采用80℃的恒温水浴锅加热15min,而后在1h内匀速滴加完毕St与AMS的混合物,滴加完毕后继续搅拌反应5h,得到苯乙烯/马来酸酐交替共聚物的分散体系,将分散体系离心分离、干燥,得到苯乙烯/马来酸酐交替共聚物的白色粉末。Synthesis of copolymer: put MAH, AIBN and solvent in a four-neck flask equipped with a stirring device and nitrogen gas, stir at room temperature for 15 minutes, heat for 15 minutes in a constant temperature water bath at 80°C, and then drop them at a constant speed within 1 hour The mixture of St and AMS, after the dropwise addition, continue to stir and react for 5 hours to obtain a dispersion system of styrene/maleic anhydride alternating copolymer, centrifuge the dispersion system and dry to obtain a white powder of styrene/maleic anhydride alternating copolymer .
聚合收率(Cp)、共聚物的数均分子量(Mn)及其分布(PDI)结果见表1,共聚物的GPC谱图见图3。The results of polymerization yield (C p ), number average molecular weight (Mn) and distribution (PDI) of the copolymer are shown in Table 1, and the GPC spectrum of the copolymer is shown in Fig. 3 .
实施例6Example 6
备料:单体MAH 1.3244g、St 1.2673g,二者的摩尔配比为1∶0.9;引发剂AIBN 0.1372g;溶剂乙酸异戊酯22.5mL和环己烷22.5mL的混合液;分子量调节剂AMS 0.1603g。Material preparation: monomer MAH 1.3244g, St 1.2673g, the molar ratio of the two is 1:0.9; initiator AIBN 0.1372g; solvent mixture of isoamyl acetate 22.5mL and cyclohexane 22.5mL; molecular weight regulator AMS 0.1603g.
共聚物的合成:将MAH、AIBN和溶剂置于带有搅拌装置和通有氮气的四口瓶中,常温搅拌15min后,采用80℃的恒温水浴锅加热15min,而后在1h内匀速滴加完毕St与AMS的混合物,滴加完毕后继续搅拌反应5h,得到苯乙烯/马来酸酐交替共聚物的分散体系,将分散体系离心分离、干燥,得到苯乙烯/马来酸酐交替共聚物的白色粉末。Synthesis of copolymer: put MAH, AIBN and solvent in a four-neck flask equipped with a stirring device and nitrogen gas, stir at room temperature for 15 minutes, heat for 15 minutes in a constant temperature water bath at 80°C, and then drop them at a constant speed within 1 hour The mixture of St and AMS, after the dropwise addition, continue to stir and react for 5 hours to obtain a dispersion system of styrene/maleic anhydride alternating copolymer, centrifuge the dispersion system and dry to obtain a white powder of styrene/maleic anhydride alternating copolymer .
聚合收率(Cp)、共聚物的数均分子量(Mn)及其分布(PDI)结果见表1。The results of polymerization yield (C p ), number average molecular weight (Mn) and distribution (PDI) of the copolymer are shown in Table 1.
实施例7Example 7
备料:单体MAH 1.3246g、St 1.2668g,二者的摩尔配比为1∶0.9;引发剂BPO 0.0826g;溶剂丁酸乙酯9mL和环己烷36mL的混合液;分子量调节剂AMS 0.1615g。Material preparation: monomer MAH 1.3246g, St 1.2668g, the molar ratio of the two is 1:0.9; initiator BPO 0.0826g; solvent mixture of ethyl butyrate 9mL and cyclohexane 36mL; molecular weight regulator AMS 0.1615g .
共聚物的合成:将MAH、AIBN和溶剂置于带有搅拌装置和通有氮气的四口瓶中,常温搅拌15min后,采用80℃的恒温水浴锅加热15min,而后在1h内匀速滴加完毕St与AMS的混合物,滴加完毕后继续搅拌反应5h,得到苯乙烯/马来酸酐交替共聚物的分散体系,将分散体系离心分离、干燥,得到苯乙烯/马来酸酐交替共聚物的白色粉末。Synthesis of copolymer: put MAH, AIBN and solvent in a four-neck flask equipped with a stirring device and nitrogen gas, stir at room temperature for 15 minutes, heat for 15 minutes in a constant temperature water bath at 80°C, and then drop them at a constant speed within 1 hour The mixture of St and AMS, after the dropwise addition, continue to stir and react for 5 hours to obtain a dispersion system of styrene/maleic anhydride alternating copolymer, centrifuge the dispersion system and dry to obtain a white powder of styrene/maleic anhydride alternating copolymer .
聚合收率(Cp)、共聚物的数均分子量(Mn)及其分布(PDI)结果见表1,共聚物的GPC谱图见图4。The results of polymerization yield (C p ), number average molecular weight (Mn) and distribution (PDI) of the copolymer are shown in Table 1, and the GPC spectrum of the copolymer is shown in Figure 4.
表1实施例1-7中制备的低分子量苯乙烯/马来酸酐交替共聚物的分子量、分子量分布及聚合收率The molecular weight, molecular weight distribution and polymerization yield of the low molecular weight styrene/maleic anhydride alternating copolymer prepared in the embodiment 1-7 of table 1
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CN101979417B (en) * | 2010-10-22 | 2013-01-02 | 北京化工大学 | Novel method for preparing itaconic anhydride-styrene monomer alternating copolymer |
CN102250273B (en) * | 2011-06-02 | 2012-10-17 | 北京化工大学 | A kind of preparation method of styrene-maleic anhydride random copolymer |
CN103193932B (en) * | 2012-01-09 | 2015-09-16 | 上海飞凯光电材料股份有限公司 | The synthetic method of low molecular weight phenylethylene-maleic anhydride alternate copolymer |
CN103923247B (en) * | 2013-01-11 | 2017-11-24 | 上海飞凯光电材料股份有限公司 | A kind of production technology of styrene maleic anhydride copolymer |
CN105175598A (en) * | 2015-08-12 | 2015-12-23 | 莘县阳光包装材料有限公司 | Synthesis method of SMA resin with low molecular weight |
CN107337746B (en) * | 2016-11-16 | 2018-09-28 | 上海化工研究院有限公司 | Chain-transferring agent of epoxy group and the preparation method and application thereof is contained in a kind of end |
CN109575172B (en) * | 2018-12-11 | 2021-01-05 | 三明学院 | Low molecular weight styrene maleic anhydride copolymer and preparation method thereof |
CN111234081B (en) * | 2020-03-06 | 2022-12-20 | 长春工业大学 | A kind of low molecular weight narrow distribution styrene-maleic anhydride copolymer and preparation method thereof |
CN114426639A (en) * | 2020-10-15 | 2022-05-03 | 中国石油化工股份有限公司 | Alpha-olefin-maleic anhydride copolymer and preparation method and application thereof |
CN114437279B (en) * | 2020-10-16 | 2024-07-02 | 中国石油化工股份有限公司 | Maleic anhydride copolymer and preparation method and application thereof |
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