JP6390079B2 - Process for producing branched polyarylene sulfide resin - Google Patents
Process for producing branched polyarylene sulfide resin Download PDFInfo
- Publication number
- JP6390079B2 JP6390079B2 JP2013173416A JP2013173416A JP6390079B2 JP 6390079 B2 JP6390079 B2 JP 6390079B2 JP 2013173416 A JP2013173416 A JP 2013173416A JP 2013173416 A JP2013173416 A JP 2013173416A JP 6390079 B2 JP6390079 B2 JP 6390079B2
- Authority
- JP
- Japan
- Prior art keywords
- sulfide
- compound
- polyarylene sulfide
- mass
- oligoarylene
- 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.)
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- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 title claims description 162
- 229920005989 resin Polymers 0.000 title claims description 87
- 239000011347 resin Substances 0.000 title claims description 87
- 229920000412 polyarylene Polymers 0.000 title claims description 70
- 238000000034 method Methods 0.000 title claims description 36
- 230000008569 process Effects 0.000 title claims description 7
- 150000001875 compounds Chemical class 0.000 claims description 87
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 74
- 239000000203 mixture Substances 0.000 claims description 49
- 238000006116 polymerization reaction Methods 0.000 claims description 42
- 238000004519 manufacturing process Methods 0.000 claims description 40
- -1 arylene sulfide (2) Chemical compound 0.000 claims description 35
- 239000002798 polar solvent Substances 0.000 claims description 34
- 239000011541 reaction mixture Substances 0.000 claims description 31
- 239000012298 atmosphere Substances 0.000 claims description 24
- 150000008045 alkali metal halides Chemical class 0.000 claims description 23
- 238000005406 washing Methods 0.000 claims description 23
- 238000000926 separation method Methods 0.000 claims description 20
- 229910052783 alkali metal Chemical group 0.000 claims description 19
- 239000007788 liquid Substances 0.000 claims description 19
- 239000000155 melt Substances 0.000 claims description 19
- 230000001590 oxidative effect Effects 0.000 claims description 19
- 229910052977 alkali metal sulfide Inorganic materials 0.000 claims description 14
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims description 14
- 229910001508 alkali metal halide Inorganic materials 0.000 claims description 12
- 125000005843 halogen group Chemical group 0.000 claims description 11
- 125000004432 carbon atom Chemical group C* 0.000 claims description 10
- 150000008044 alkali metal hydroxides Chemical class 0.000 claims description 9
- 125000004122 cyclic group Chemical group 0.000 claims description 7
- 150000001340 alkali metals Chemical group 0.000 claims description 6
- 125000000217 alkyl group Chemical group 0.000 claims description 6
- 125000002947 alkylene group Chemical group 0.000 claims description 4
- 125000000113 cyclohexyl group Chemical group [H]C1([H])C([H])([H])C([H])([H])C([H])(*)C([H])([H])C1([H])[H] 0.000 claims description 4
- 239000000539 dimer Substances 0.000 claims description 2
- 239000003495 polar organic solvent Substances 0.000 claims description 2
- 239000013638 trimer Substances 0.000 claims description 2
- 238000011010 flushing procedure Methods 0.000 claims 1
- 125000000843 phenylene group Chemical group C1(=C(C=CC=C1)*)* 0.000 claims 1
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 description 46
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 38
- 239000002904 solvent Substances 0.000 description 38
- 239000004734 Polyphenylene sulfide Substances 0.000 description 29
- 229920000069 polyphenylene sulfide Polymers 0.000 description 29
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 24
- 239000000706 filtrate Substances 0.000 description 19
- 238000002844 melting Methods 0.000 description 19
- 230000008018 melting Effects 0.000 description 19
- 238000001914 filtration Methods 0.000 description 18
- 238000003756 stirring Methods 0.000 description 17
- 239000007864 aqueous solution Substances 0.000 description 16
- 238000011282 treatment Methods 0.000 description 16
- 230000009257 reactivity Effects 0.000 description 15
- 239000000843 powder Substances 0.000 description 14
- 239000007787 solid Substances 0.000 description 14
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 12
- 238000006243 chemical reaction Methods 0.000 description 12
- 238000010438 heat treatment Methods 0.000 description 12
- 239000012071 phase Substances 0.000 description 12
- 239000002002 slurry Substances 0.000 description 11
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 10
- JBKVHLHDHHXQEQ-UHFFFAOYSA-N epsilon-caprolactam Chemical compound O=C1CCCCCN1 JBKVHLHDHHXQEQ-UHFFFAOYSA-N 0.000 description 10
- 239000001257 hydrogen Substances 0.000 description 10
- 229910052739 hydrogen Inorganic materials 0.000 description 10
- OCJBOOLMMGQPQU-UHFFFAOYSA-N 1,4-dichlorobenzene Chemical compound ClC1=CC=C(Cl)C=C1 OCJBOOLMMGQPQU-UHFFFAOYSA-N 0.000 description 9
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 9
- 239000006227 byproduct Substances 0.000 description 9
- 239000007795 chemical reaction product Substances 0.000 description 9
- 238000000605 extraction Methods 0.000 description 9
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 8
- 125000003277 amino group Chemical group 0.000 description 8
- 239000008346 aqueous phase Substances 0.000 description 8
- 238000001816 cooling Methods 0.000 description 8
- 239000007789 gas Substances 0.000 description 8
- 230000004580 weight loss Effects 0.000 description 8
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 7
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 7
- 239000000047 product Substances 0.000 description 7
- 239000002994 raw material Substances 0.000 description 7
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 6
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 description 6
- 125000004181 carboxyalkyl group Chemical group 0.000 description 6
- 238000001035 drying Methods 0.000 description 6
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 5
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 5
- 239000002253 acid Substances 0.000 description 5
- 125000003118 aryl group Chemical group 0.000 description 5
- 239000004202 carbamide Substances 0.000 description 5
- 125000000524 functional group Chemical group 0.000 description 5
- GNOIPBMMFNIUFM-UHFFFAOYSA-N hexamethylphosphoric triamide Chemical compound CN(C)P(=O)(N(C)C)N(C)C GNOIPBMMFNIUFM-UHFFFAOYSA-N 0.000 description 5
- 239000006166 lysate Substances 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 238000005259 measurement Methods 0.000 description 5
- OKKJLVBELUTLKV-UHFFFAOYSA-N methanol Natural products OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 5
- 239000003960 organic solvent Substances 0.000 description 5
- AVQQQNCBBIEMEU-UHFFFAOYSA-N 1,1,3,3-tetramethylurea Chemical compound CN(C)C(=O)N(C)C AVQQQNCBBIEMEU-UHFFFAOYSA-N 0.000 description 4
- DLFVBJFMPXGRIB-UHFFFAOYSA-N Acetamide Chemical compound CC(N)=O DLFVBJFMPXGRIB-UHFFFAOYSA-N 0.000 description 4
- ZHNUHDYFZUAESO-UHFFFAOYSA-N Formamide Chemical compound NC=O ZHNUHDYFZUAESO-UHFFFAOYSA-N 0.000 description 4
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 description 4
- ZWXPDGCFMMFNRW-UHFFFAOYSA-N N-methylcaprolactam Chemical compound CN1CCCCCC1=O ZWXPDGCFMMFNRW-UHFFFAOYSA-N 0.000 description 4
- ATHHXGZTWNVVOU-UHFFFAOYSA-N N-methylformamide Chemical compound CNC=O ATHHXGZTWNVVOU-UHFFFAOYSA-N 0.000 description 4
- 150000001408 amides Chemical class 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 4
- MVPPADPHJFYWMZ-UHFFFAOYSA-N chlorobenzene Chemical compound ClC1=CC=CC=C1 MVPPADPHJFYWMZ-UHFFFAOYSA-N 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 238000004128 high performance liquid chromatography Methods 0.000 description 4
- 238000001746 injection moulding Methods 0.000 description 4
- 150000003951 lactams Chemical class 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 238000000465 moulding Methods 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 229920000642 polymer Polymers 0.000 description 4
- 238000000746 purification Methods 0.000 description 4
- HNJBEVLQSNELDL-UHFFFAOYSA-N pyrrolidin-2-one Chemical compound O=C1CCCN1 HNJBEVLQSNELDL-UHFFFAOYSA-N 0.000 description 4
- 229910052979 sodium sulfide Inorganic materials 0.000 description 4
- GRVFOGOEDUUMBP-UHFFFAOYSA-N sodium sulfide (anhydrous) Chemical compound [Na+].[Na+].[S-2] GRVFOGOEDUUMBP-UHFFFAOYSA-N 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- 229920002725 thermoplastic elastomer Polymers 0.000 description 4
- PBKONEOXTCPAFI-UHFFFAOYSA-N 1,2,4-trichlorobenzene Chemical compound ClC1=CC=C(Cl)C(Cl)=C1 PBKONEOXTCPAFI-UHFFFAOYSA-N 0.000 description 3
- CYSGHNMQYZDMIA-UHFFFAOYSA-N 1,3-Dimethyl-2-imidazolidinon Chemical compound CN1CCN(C)C1=O CYSGHNMQYZDMIA-UHFFFAOYSA-N 0.000 description 3
- 241001244373 Carex spissa Species 0.000 description 3
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 3
- 239000004593 Epoxy Substances 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- 239000004609 Impact Modifier Substances 0.000 description 3
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical compound [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 description 3
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- 239000006087 Silane Coupling Agent Substances 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 239000002585 base Substances 0.000 description 3
- JFDZBHWFFUWGJE-UHFFFAOYSA-N benzonitrile Chemical compound N#CC1=CC=CC=C1 JFDZBHWFFUWGJE-UHFFFAOYSA-N 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- GVEPBJHOBDJJJI-UHFFFAOYSA-N fluoranthene Chemical compound C1=CC(C2=CC=CC=C22)=C3C2=CC=CC3=C1 GVEPBJHOBDJJJI-UHFFFAOYSA-N 0.000 description 3
- 239000002440 industrial waste Substances 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- 239000011734 sodium Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- HQJQYILBCQPYBI-UHFFFAOYSA-N 1-bromo-4-(4-bromophenyl)benzene Chemical group C1=CC(Br)=CC=C1C1=CC=C(Br)C=C1 HQJQYILBCQPYBI-UHFFFAOYSA-N 0.000 description 2
- NQMUGNMMFTYOHK-UHFFFAOYSA-N 1-methoxynaphthalene Chemical compound C1=CC=C2C(OC)=CC=CC2=C1 NQMUGNMMFTYOHK-UHFFFAOYSA-N 0.000 description 2
- WXNZTHHGJRFXKQ-UHFFFAOYSA-N 4-chlorophenol Chemical compound OC1=CC=C(Cl)C=C1 WXNZTHHGJRFXKQ-UHFFFAOYSA-N 0.000 description 2
- KWOLFJPFCHCOCG-UHFFFAOYSA-N Acetophenone Chemical compound CC(=O)C1=CC=CC=C1 KWOLFJPFCHCOCG-UHFFFAOYSA-N 0.000 description 2
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- RGSFGYAAUTVSQA-UHFFFAOYSA-N Cyclopentane Chemical compound C1CCCC1 RGSFGYAAUTVSQA-UHFFFAOYSA-N 0.000 description 2
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 description 2
- AFBPFSWMIHJQDM-UHFFFAOYSA-N N-methylaniline Chemical compound CNC1=CC=CC=C1 AFBPFSWMIHJQDM-UHFFFAOYSA-N 0.000 description 2
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- MWPLVEDNUUSJAV-UHFFFAOYSA-N anthracene Chemical compound C1=CC=CC2=CC3=CC=CC=C3C=C21 MWPLVEDNUUSJAV-UHFFFAOYSA-N 0.000 description 2
- 150000001491 aromatic compounds Chemical class 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- LLEMOWNGBBNAJR-UHFFFAOYSA-N biphenyl-2-ol Chemical compound OC1=CC=CC=C1C1=CC=CC=C1 LLEMOWNGBBNAJR-UHFFFAOYSA-N 0.000 description 2
- YXVFYQXJAXKLAK-UHFFFAOYSA-N biphenyl-4-ol Chemical compound C1=CC(O)=CC=C1C1=CC=CC=C1 YXVFYQXJAXKLAK-UHFFFAOYSA-N 0.000 description 2
- DIKBFYAXUHHXCS-UHFFFAOYSA-N bromoform Chemical compound BrC(Br)Br DIKBFYAXUHHXCS-UHFFFAOYSA-N 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 2
- 238000000748 compression moulding Methods 0.000 description 2
- 239000007822 coupling agent Substances 0.000 description 2
- IYYZUPMFVPLQIF-UHFFFAOYSA-N dibenzothiophene Chemical compound C1=CC=C2C3=CC=CC=C3SC2=C1 IYYZUPMFVPLQIF-UHFFFAOYSA-N 0.000 description 2
- 229910001873 dinitrogen Inorganic materials 0.000 description 2
- USIUVYZYUHIAEV-UHFFFAOYSA-N diphenyl ether Chemical compound C=1C=CC=CC=1OC1=CC=CC=C1 USIUVYZYUHIAEV-UHFFFAOYSA-N 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 229920001971 elastomer Polymers 0.000 description 2
- 239000000806 elastomer Substances 0.000 description 2
- 150000002170 ethers Chemical class 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 150000002367 halogens Chemical group 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- 239000011261 inert gas Substances 0.000 description 2
- 238000005342 ion exchange Methods 0.000 description 2
- 239000008204 material by function Substances 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- IZUPBVBPLAPZRR-UHFFFAOYSA-N pentachlorophenol Chemical compound OC1=C(Cl)C(Cl)=C(Cl)C(Cl)=C1Cl IZUPBVBPLAPZRR-UHFFFAOYSA-N 0.000 description 2
- YNPNZTXNASCQKK-UHFFFAOYSA-N phenanthrene Chemical compound C1=CC=C2C3=CC=CC=C3C=CC2=C1 YNPNZTXNASCQKK-UHFFFAOYSA-N 0.000 description 2
- LYXOWKPVTCPORE-UHFFFAOYSA-N phenyl-(4-phenylphenyl)methanone Chemical group C=1C=C(C=2C=CC=CC=2)C=CC=1C(=O)C1=CC=CC=C1 LYXOWKPVTCPORE-UHFFFAOYSA-N 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- BBEAQIROQSPTKN-UHFFFAOYSA-N pyrene Chemical compound C1=CC=C2C=CC3=CC=CC4=CC=C1C2=C43 BBEAQIROQSPTKN-UHFFFAOYSA-N 0.000 description 2
- 239000011342 resin composition Substances 0.000 description 2
- 238000007151 ring opening polymerisation reaction Methods 0.000 description 2
- 239000012265 solid product Substances 0.000 description 2
- HXJUTPCZVOIRIF-UHFFFAOYSA-N sulfolane Chemical class O=S1(=O)CCCC1 HXJUTPCZVOIRIF-UHFFFAOYSA-N 0.000 description 2
- 229920003002 synthetic resin Polymers 0.000 description 2
- 239000000057 synthetic resin Substances 0.000 description 2
- 125000003396 thiol group Chemical group [H]S* 0.000 description 2
- BZWGZQNUCNUCES-UHFFFAOYSA-N (2,3-dibromophenyl)-phenylmethanone Chemical compound BrC1=CC=CC(C(=O)C=2C=CC=CC=2)=C1Br BZWGZQNUCNUCES-UHFFFAOYSA-N 0.000 description 1
- RLUFBDIRFJGKLY-UHFFFAOYSA-N (2,3-dichlorophenyl)-phenylmethanone Chemical compound ClC1=CC=CC(C(=O)C=2C=CC=CC=2)=C1Cl RLUFBDIRFJGKLY-UHFFFAOYSA-N 0.000 description 1
- KGANAERDZBAECK-UHFFFAOYSA-N (3-phenoxyphenyl)methanol Chemical compound OCC1=CC=CC(OC=2C=CC=CC=2)=C1 KGANAERDZBAECK-UHFFFAOYSA-N 0.000 description 1
- UOCLXMDMGBRAIB-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl UOCLXMDMGBRAIB-UHFFFAOYSA-N 0.000 description 1
- DBNWBEGCONIRGQ-UHFFFAOYSA-N 1,1-diphenylpropan-2-one Chemical compound C=1C=CC=CC=1C(C(=O)C)C1=CC=CC=C1 DBNWBEGCONIRGQ-UHFFFAOYSA-N 0.000 description 1
- GBDZXPJXOMHESU-UHFFFAOYSA-N 1,2,3,4-tetrachlorobenzene Chemical compound ClC1=CC=C(Cl)C(Cl)=C1Cl GBDZXPJXOMHESU-UHFFFAOYSA-N 0.000 description 1
- GMVJKSNPLYBFSO-UHFFFAOYSA-N 1,2,3-tribromobenzene Chemical compound BrC1=CC=CC(Br)=C1Br GMVJKSNPLYBFSO-UHFFFAOYSA-N 0.000 description 1
- RELMFMZEBKVZJC-UHFFFAOYSA-N 1,2,3-trichlorobenzene Chemical compound ClC1=CC=CC(Cl)=C1Cl RELMFMZEBKVZJC-UHFFFAOYSA-N 0.000 description 1
- RIWAPWDHHMWTRA-UHFFFAOYSA-N 1,2,3-triiodobenzene Chemical compound IC1=CC=CC(I)=C1I RIWAPWDHHMWTRA-UHFFFAOYSA-N 0.000 description 1
- WSLDOOZREJYCGB-UHFFFAOYSA-N 1,2-Dichloroethane Chemical compound ClCCCl WSLDOOZREJYCGB-UHFFFAOYSA-N 0.000 description 1
- YDCWAFIIYQBOFT-UHFFFAOYSA-N 1,2-dibromo-3,4-diphenylbenzene Chemical compound C=1C=CC=CC=1C1=C(Br)C(Br)=CC=C1C1=CC=CC=C1 YDCWAFIIYQBOFT-UHFFFAOYSA-N 0.000 description 1
- JTYRXXKXOULVAP-UHFFFAOYSA-N 1,2-dibromo-3-phenoxybenzene Chemical compound BrC1=CC=CC(OC=2C=CC=CC=2)=C1Br JTYRXXKXOULVAP-UHFFFAOYSA-N 0.000 description 1
- WQONPSCCEXUXTQ-UHFFFAOYSA-N 1,2-dibromobenzene Chemical compound BrC1=CC=CC=C1Br WQONPSCCEXUXTQ-UHFFFAOYSA-N 0.000 description 1
- QGZAUMUFTXCDBD-UHFFFAOYSA-N 1,2-dibromonaphthalene Chemical compound C1=CC=CC2=C(Br)C(Br)=CC=C21 QGZAUMUFTXCDBD-UHFFFAOYSA-N 0.000 description 1
- GSOXNLLPTMSRCO-UHFFFAOYSA-N 1,2-dichloro-3,4-diphenylbenzene Chemical compound C=1C=CC=CC=1C1=C(Cl)C(Cl)=CC=C1C1=CC=CC=C1 GSOXNLLPTMSRCO-UHFFFAOYSA-N 0.000 description 1
- VSKSUBSGORDMQX-UHFFFAOYSA-N 1,2-dichloro-3-phenoxybenzene Chemical compound ClC1=CC=CC(OC=2C=CC=CC=2)=C1Cl VSKSUBSGORDMQX-UHFFFAOYSA-N 0.000 description 1
- WFLOTYSKFUPZQB-UHFFFAOYSA-N 1,2-difluoroethene Chemical group FC=CF WFLOTYSKFUPZQB-UHFFFAOYSA-N 0.000 description 1
- BBOLNFYSRZVALD-UHFFFAOYSA-N 1,2-diiodobenzene Chemical compound IC1=CC=CC=C1I BBOLNFYSRZVALD-UHFFFAOYSA-N 0.000 description 1
- XKEFYDZQGKAQCN-UHFFFAOYSA-N 1,3,5-trichlorobenzene Chemical compound ClC1=CC(Cl)=CC(Cl)=C1 XKEFYDZQGKAQCN-UHFFFAOYSA-N 0.000 description 1
- DMEDNTFWIHCBRK-UHFFFAOYSA-N 1,3-dichloro-2-methylbenzene Chemical compound CC1=C(Cl)C=CC=C1Cl DMEDNTFWIHCBRK-UHFFFAOYSA-N 0.000 description 1
- RYMMNSVHOKXTNN-UHFFFAOYSA-N 1,3-dichloro-5-methyl-benzene Natural products CC1=CC(Cl)=CC(Cl)=C1 RYMMNSVHOKXTNN-UHFFFAOYSA-N 0.000 description 1
- ZPQOPVIELGIULI-UHFFFAOYSA-N 1,3-dichlorobenzene Chemical compound ClC1=CC=CC(Cl)=C1 ZPQOPVIELGIULI-UHFFFAOYSA-N 0.000 description 1
- JTNRGGLCSLZOOQ-UHFFFAOYSA-N 1,3-diphenoxybenzene Chemical compound C=1C=CC(OC=2C=CC=CC=2)=CC=1OC1=CC=CC=C1 JTNRGGLCSLZOOQ-UHFFFAOYSA-N 0.000 description 1
- RLTTZFDRZKJVKJ-UHFFFAOYSA-N 1,4,6-trichloronaphthalene Chemical compound ClC1=CC=C(Cl)C2=CC(Cl)=CC=C21 RLTTZFDRZKJVKJ-UHFFFAOYSA-N 0.000 description 1
- RZKKOBGFCAHLCZ-UHFFFAOYSA-N 1,4-dichloro-2-nitrobenzene Chemical compound [O-][N+](=O)C1=CC(Cl)=CC=C1Cl RZKKOBGFCAHLCZ-UHFFFAOYSA-N 0.000 description 1
- VRBLNWVVFVBNRK-UHFFFAOYSA-N 1,6-diphenylhexane-1,6-dione Chemical compound C=1C=CC=CC=1C(=O)CCCCC(=O)C1=CC=CC=C1 VRBLNWVVFVBNRK-UHFFFAOYSA-N 0.000 description 1
- DLKQHBOKULLWDQ-UHFFFAOYSA-N 1-bromonaphthalene Chemical compound C1=CC=C2C(Br)=CC=CC2=C1 DLKQHBOKULLWDQ-UHFFFAOYSA-N 0.000 description 1
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Landscapes
- Polymers With Sulfur, Phosphorus Or Metals In The Main Chain (AREA)
Description
ポリアリーレンスルフィド樹脂の製造時の精製工程で排出されるオリゴアリーレンスルフィドを回収して再利用する、分岐型ポリアリーレンスルフィド樹脂の製造方法に関する。 The present invention relates to a method for producing a branched polyarylene sulfide resin, in which oligoarylene sulfide discharged in a purification step during the production of the polyarylene sulfide resin is recovered and reused.
ポリフェニレンスルフィド樹脂に代表されるポリアリーレンスルフィド樹脂は、耐熱性、耐薬品性等に優れ、電気電子部品、自動車部品、給湯機部品、繊維、フィルム用途等に幅広く利用されている。特に、リチウムイオン電池用パッキンやガスケット部材といった用途では、近年、特に高分子量PAS樹脂が、靭性および成形性に優れることから広く用いられている。 Polyarylene sulfide resins represented by polyphenylene sulfide resins are excellent in heat resistance and chemical resistance, and are widely used in electrical and electronic parts, automobile parts, water heater parts, fibers, films and the like. Particularly in applications such as packing for lithium ion batteries and gasket members, in recent years, high molecular weight PAS resins have been widely used because of their excellent toughness and moldability.
PPSの工業的な重合方法は、N−メチル−2−ピロリドン(NMP)溶媒中で硫化ナトリウムなどのアルカリ金属硫化物とp−ジクロロベンゼンなどのポリハロ芳香族化合物とを反応させる方法が一般的であるが、PAS重合反応段階において副生物として、オリゴアリーレンスルフィドが約2〜5%程度生成することが知られている(非特許文献1参照、特に第388頁右下欄参照。)。 As an industrial polymerization method of PPS, a method of reacting an alkali metal sulfide such as sodium sulfide and a polyhaloaromatic compound such as p-dichlorobenzene in an N-methyl-2-pyrrolidone (NMP) solvent is generally used. However, it is known that about 2 to 5% of oligoarylene sulfide is produced as a by-product in the PAS polymerization reaction stage (see Non-Patent Document 1, especially page 388, lower right column).
このオリゴアリーレンスルフィドは、ポリアリーレンスルフィド樹脂の結晶化速度を低下させ、射出成形時の成形サイクルを遅延させる原因となり、また、溶融時発生ガス量が増え、射出成形時のヤニが増加する等の原因にもなるため、PAS重合の後処理工程で精製され除去されている。 This oligoarylene sulfide reduces the crystallization rate of polyarylene sulfide resin, causes a delay in the molding cycle during injection molding, increases the amount of gas generated during melting, increases the amount of resin during injection molding, etc. Since it also causes, it is purified and removed in the post-treatment step of PAS polymerization.
しかしながら、当該オリゴアリーレンスルフィドの精製除去は、収量低下を招き、その分余計に原料が必要となり、製造コストを圧迫する要因となっており、さらに、産業廃棄物量の増加をもたらし、工業規模では年間数百トン(オリゴアリーレンスルフィド生成量が5%の場合、1万トン生産で産廃は500トン)もの産廃処理問題が発生する原因となっていた。 However, the purification and removal of the oligoarylene sulfide leads to a decrease in yield, which requires additional raw materials, which is a factor that presses down on manufacturing costs, and further increases the amount of industrial waste. Several hundred tons (when the amount of oligoarylene sulfide produced is 5%, production of 10,000 tons and industrial waste of 500 tons) caused industrial waste disposal problems.
そこでオリゴアリーレンスルフィド中に含まれる繰り返し単位n=4〜13量体の環状オリゴアリーレンスルフィドに着目し、該環状オリゴアリーレンスルフィドを、モノマー原料として開環重合し、高分子量直鎖状化合物を合成する方法などをはじめとして、環状物であることを活用した高機能材料や機能材料への応用展開の可能性に注目が集まっている(特許文献1、2)。 Therefore, paying attention to the cyclic oligoarylene sulfide having a repeating unit n = 4 to 13-mer contained in the oligoarylene sulfide, the cyclic oligoarylene sulfide is subjected to ring-opening polymerization as a monomer raw material to synthesize a high molecular weight linear compound. Attention has been focused on the possibility of application development to high-functional materials and functional materials that utilize ring-shaped materials, including methods (Patent Documents 1 and 2).
しかしながら、PAS重合の副生物には前記環状オリゴアリーレンスルフィドの他に下記構造式(1) However, the by-product of the PAS polymerization includes the following structural formula (1) in addition to the cyclic oligoarylene sulfide.
そこで本発明が解決しようとする課題は、ポリアリーレンスルフィド樹脂の重合工程で副生物として精製除去されたオリゴアリーレンスルフィドを用いて、エポキシシランカップリング剤や官能基含有熱可塑性エラストマーなどの耐衝撃性改質剤との反応性に優れる高分子量の分岐型アリーレンスルフィド樹脂を製造する方法を提供する。 Therefore, the problem to be solved by the present invention is to use an oligoarylene sulfide purified and removed as a by-product in the polymerization process of the polyarylene sulfide resin, and to provide an impact resistance such as an epoxy silane coupling agent or a functional group-containing thermoplastic elastomer. Provided is a method for producing a high molecular weight branched arylene sulfide resin having excellent reactivity with a modifier.
本願発明者らは種々の検討を行った結果、ポリアリーレンスルフィド樹脂の重合工程で精製除去された副生物を100℃以上かつpH6以上の水と接触させる方法により、オリゴアリーレンスルフィドと前記カルボキシアルキルアミノ基含有化合物(1)とを効率よく分離し、回収した高濃度でオリゴアリーレンスルフィドを含有する組成物を得、この組成物を酸化性雰囲気下で加熱して、高重合度体へ溶融重合することで高分子量の分岐型ポリアリーレンスルフィド樹脂を製造できることを見出し、本発明を解決するに至った。 As a result of various investigations, the inventors of the present invention have found that by-products purified and removed in the polymerization process of the polyarylene sulfide resin are brought into contact with water at 100 ° C. or higher and pH 6 or higher, the oligoarylene sulfide and the carboxyalkylamino are obtained. The group-containing compound (1) is efficiently separated and a recovered composition containing oligoarylene sulfide at a high concentration is obtained, and this composition is heated in an oxidizing atmosphere to melt polymerize to a high degree of polymerization. As a result, it was found that a branched polyarylene sulfide resin having a high molecular weight can be produced, and the present invention has been solved.
すなわち、本発明は、下記構造式(1)で表される化合物(1)0.01〜20質量部とオリゴアリーレンスルフィド(2)99.99〜80質量部とを、酸化性雰囲気下で溶融重合することを特徴とする分岐型ポリアリーレンスルフィド樹脂の製造方法に関する。 That is, the present invention melts 0.01 to 20 parts by mass of the compound (1) represented by the following structural formula (1) and 99.99 to 80 parts by mass of the oligoarylene sulfide (2) in an oxidizing atmosphere. The present invention relates to a method for producing a branched polyarylene sulfide resin characterized by polymerization.
本発明によりポリアリーレンスルフィド樹脂の重合工程で副生物として精製除去されたオリゴアリーレンスルフィドを用いて、エポキシシランカップリング剤や官能基含有熱可塑性エラストマーなどの耐衝撃性改質剤との反応性に優れる高分子量の分岐型ポリアリーレンスルフィド樹脂を製造する方法を提供できる。 Using the oligoarylene sulfide purified and removed as a by-product in the polymerization process of the polyarylene sulfide resin according to the present invention, the reactivity with an impact modifier such as an epoxysilane coupling agent or a functional group-containing thermoplastic elastomer is improved. A method for producing an excellent high molecular weight branched polyarylene sulfide resin can be provided.
本発明の分岐型ポリアリーレンスルフィド樹脂の製造方法は、下記構造式(1)で表される化合物(1)0.01〜20質量部とオリゴアリーレンスルフィド(2)99.99〜80質量部とを、酸化性雰囲気下で溶融重合することを特徴とする。 The method for producing the branched polyarylene sulfide resin of the present invention comprises 0.01 to 20 parts by mass of the compound (1) represented by the following structural formula (1) and 99.99 to 80 parts by mass of the oligoarylene sulfide (2). Is characterized by melt polymerization in an oxidizing atmosphere.
以下、詳述する。
本発明で用いる、下記構造式(1)で表される化合物(1)とオリゴアリーレンスルフィド(2)は、例えば下記の工程(1)〜工程(3)により製造することができる。
Details will be described below.
The compound (1) represented by the following structural formula (1) and the oligoarylene sulfide (2) used in the present invention can be produced by, for example, the following steps (1) to (3).
・工程(1)
有機極性溶媒中で、ポリハロ芳香族化合物と、(i)アルカリ金属硫化物とを、または、(ii)アルカリ金属水硫化物及びアルカリ金属水酸化物とを反応させて、下記構造式(1)で表される化合物(1)、オリゴアリーレンスルフィド(2)、有機極性溶媒(3)、ポリアリーレンスルフィド(4)及びアルカリ金属ハロゲン化物(5)を含む粗反応混合物を得たのち、該粗反応混合物を有機極性溶媒(6)で洗浄して、ポリアリーレンスルフィド(4)及びアルカリ金属ハロゲン化物(5)を分離除去して、前記化合物(1)、オリゴアリーレンスルフィド(2)および有機極性溶媒(3)を含む反応混合物(a1)を得る工程(1)を有する。
・ Process (1)
In an organic polar solvent, a polyhaloaromatic compound and (i) an alkali metal sulfide or (ii) an alkali metal hydrosulfide and an alkali metal hydroxide are reacted to form the following structural formula (1): After obtaining a crude reaction mixture containing the compound (1), oligoarylene sulfide (2), organic polar solvent (3), polyarylene sulfide (4) and alkali metal halide (5) represented by The mixture is washed with an organic polar solvent (6) to separate and remove the polyarylene sulfide (4) and the alkali metal halide (5), and the compound (1), the oligoarylene sulfide (2) and the organic polar solvent ( A step (1) of obtaining a reaction mixture (a1) comprising 3).
まず始めに、工程(1)は、有機極性溶媒中で、少なくともポリハロ芳香族化合物とアルカリ金属硫化物とを反応させて、前記構造式(1)で表される化合物(1)、オリゴアリーレンスルフィド(2)、有機極性溶媒(3)、ポリアリーレンスルフィド(4)及びアルカリ金属ハロゲン化物(5)を含む粗反応混合物を製造するか、または、有機極性溶媒中で、少なくともポリハロ芳香族化合物とアルカリ金属水硫化物及びアルカリ金属水酸化物とを反応させて下記構造式(1)で表される化合物(1)、オリゴアリーレンスルフィド(2)、有機極性溶媒(3)、ポリアリーレンスルフィド(4)及びアルカリ金属ハロゲン化物(5)を含む粗反応混合物を製造する方法を工程(1a)として有する。 First, in step (1), at least a polyhaloaromatic compound and an alkali metal sulfide are reacted in an organic polar solvent to obtain a compound (1) represented by the structural formula (1), an oligoarylene sulfide. (2) preparing a crude reaction mixture comprising an organic polar solvent (3), a polyarylene sulfide (4) and an alkali metal halide (5), or at least a polyhaloaromatic compound and an alkali in an organic polar solvent A compound (1) represented by the following structural formula (1) by reacting a metal hydrosulfide and an alkali metal hydroxide, an oligoarylene sulfide (2), an organic polar solvent (3), a polyarylene sulfide (4) And a method for producing a crude reaction mixture containing an alkali metal halide (5) is included as step (1a).
本発明で用いられるポリハロ芳香族化合物は、例えば、芳香族環に直接結合した2個以上のハロゲン原子を有するハロゲン化芳香族化合物であり、具体的には、p−ジクロルベンゼン、o−ジクロルベンゼン、m−ジクロルベンゼン、トリクロルベンゼン、テトラクロルベンゼン、ジブロムベンゼン、ジヨードベンゼン、トリブロムベンゼン、ジブロムナフタレン、トリヨードベンゼン、ジクロルジフェニルベンゼン、ジブロムジフェニルベンゼン、ジクロルベンゾフェノン、ジブロムベンゾフェノン、ジクロルジフェニルエーテル、ジブロムジフェニルエーテル、ジクロルジフェニルスルフィド、ジブロムジフェニルスルフィド、ジクロルビフェニル、ジブロムビフェニル等のジハロ芳香族化合物及びこれらの混合物が挙げられ、これらの化合物をブロック共重合してもよい。これらの中でも好ましいのはジハロゲン化ベンゼン類であり、特に好ましいのはp−ジクロルベンゼンを80モル%以上含むものである。 The polyhaloaromatic compound used in the present invention is, for example, a halogenated aromatic compound having two or more halogen atoms directly bonded to an aromatic ring, and specifically includes p-dichlorobenzene, o-dioxy. Chlorobenzene, m-dichlorobenzene, trichlorobenzene, tetrachlorobenzene, dibromobenzene, diiodobenzene, tribromobenzene, dibromonaphthalene, triiodobenzene, dichlorodiphenylbenzene, dibromodiphenylbenzene, dichlorobenzophenone, And dihaloaromatic compounds such as dibromobenzophenone, dichlorodiphenyl ether, dibromodiphenyl ether, dichlorodiphenyl sulfide, dibromodiphenyl sulfide, dichlorobiphenyl, dibromobiphenyl, and mixtures thereof. The compound may be block copolymerized. Of these, dihalogenated benzenes are preferred, and those containing p-dichlorobenzene of 80 mol% or more are particularly preferred.
また、枝分かれ構造とすることによってポリアリーレンスルフィド樹脂の粘度増大を図る目的で、1分子中に3個以上のハロゲン置換基を有するポリハロ芳香族化合物を分岐剤として所望に応じて用いてもよい。このようなポリハロ芳香族化合物としては、例えば、1,2,4−トリクロルベンゼン、1,3,5−トリクロルベンゼン、1,4,6−トリクロルナフタレン等が挙げられる。 Further, for the purpose of increasing the viscosity of the polyarylene sulfide resin by using a branched structure, a polyhaloaromatic compound having 3 or more halogen substituents in one molecule may be used as a branching agent as desired. Examples of such polyhaloaromatic compounds include 1,2,4-trichlorobenzene, 1,3,5-trichlorobenzene, 1,4,6-trichloronaphthalene, and the like.
更に、アミノ基、チオール基、ヒドロキシル基等の活性水素を持つ官能基を有するポリハロ芳香族化合物を挙げることが出来、具体的には、2,6−ジクロルアニリン、2,5−ジクロルアニリン、2,4−ジクロルアニリン、2,3−ジクロルアニリン等のジハロアニリン類;2,3,4−トリクロルアニリン、2,3,5−トリクロルアニリン、2,4,6−トリクロルアニリン、3,4,5−トリクロルアニリン等のトリハロアニリン類;2,2’−ジアミノ−4,4’−ジクロルジフェニルエーテル、2,4’−ジアミノ−2’,4−ジクロルジフェニルエーテル等のジハロアミノジフェニルエーテル類およびこれらの混合物においてアミノ基がチオール基やヒドロキシル基に置き換えられた化合物などが例示される。また、これらの活性水素含有ポリハロ芳香族化合物中の芳香族環を形成する炭素原子に結合した水素原子が他の不活性基、例えばアルキル基などの炭化水素基に置換している活性水素含有ポリハロ芳香族化合物も使用出来る。これらの各種活性水素含有ポリハロ芳香族化合物の中でも、好ましいのは活性水素含有ジハロ芳香族化合物であり、特に好ましいのはジクロルアニリンである。 Furthermore, polyhaloaromatic compounds having a functional group having active hydrogen such as amino group, thiol group, hydroxyl group can be mentioned. Specifically, 2,6-dichloroaniline, 2,5-dichloroaniline 2,4-dichloroaniline, 2,3-dichloroaniline and other dihaloanilines; 2,3,4-trichloroaniline, 2,3,5-trichloroaniline, 2,4,6-trichloroaniline, 3, Trihaloanilines such as 4,5-trichloroaniline; dihaloaminodiphenyl ethers such as 2,2′-diamino-4,4′-dichlorodiphenyl ether and 2,4′-diamino-2 ′, 4-dichlorodiphenyl ether Examples thereof include compounds in which the amino group is replaced by a thiol group or a hydroxyl group in a mixture thereof. In addition, active hydrogen-containing polyhalo compounds in which the hydrogen atom bonded to the carbon atom forming the aromatic ring in these active hydrogen-containing polyhaloaromatic compounds is substituted with another inert group, for example, a hydrocarbon group such as an alkyl group. Aromatic compounds can also be used. Among these various active hydrogen-containing polyhaloaromatic compounds, an active hydrogen-containing dihaloaromatic compound is preferable, and dichloroaniline is particularly preferable.
ニトロ基を有するポリハロ芳香族化合物としては、例えば、2,4−ジニトロクロルベンゼン、2,5−ジクロルニトロベンゼン等のモノまたはジハロニトロベンゼン類;2−ニトロ−4,4’−ジクロルジフェニルエーテル等のジハロニトロジフェニルエーテル類;3,3’−ジニトロ−4,4’−ジクロルジフェニルスルホン等のジハロニトロジフェニルスルホン類;2,5−ジクロル−3−ニトロピリジン、2−クロル−3,5−ジニトロピリジン等のモノまたはジハロニトロピリジン類;あるいは各種ジハロニトロナフタレン類などが挙げられる。 Examples of the polyhaloaromatic compound having a nitro group include mono- or dihalonitrobenzenes such as 2,4-dinitrochlorobenzene and 2,5-dichloronitrobenzene; 2-nitro-4,4′-dichlorodiphenyl ether Dihalonitrodiphenyl ethers; dihalonitrodiphenyl sulfones such as 3,3′-dinitro-4,4′-dichlorodiphenyl sulfone; 2,5-dichloro-3-nitropyridine, 2-chloro-3,5 -Mono or dihalonitropyridines such as dinitropyridine; or various dihalonitronaphthalenes.
本発明で用いられるアルカリ金属硫化物としては、硫化リチウム、硫化ナトリウム、硫化ルビジウム、硫化セシウム及びこれらの混合物が含まれる。かかるアルカリ金属硫化物は、水和物あるいは水性混合物あるいは無水物として使用することができる。また、アルカリ金属硫化物はアルカリ金属水硫化物とアルカリ金属水酸化物との反応によっても導くことができる。 Examples of the alkali metal sulfide used in the present invention include lithium sulfide, sodium sulfide, rubidium sulfide, cesium sulfide, and mixtures thereof. Such alkali metal sulfides can be used as hydrates, aqueous mixtures or anhydrides. The alkali metal sulfide can also be derived from the reaction between an alkali metal hydrosulfide and an alkali metal hydroxide.
尚、通常、アルカリ金属硫化物中に微量存在するアルカリ金属水硫化物、チオ硫酸アルカリ金属と反応させるために、少量のアルカリ金属水酸化物を加えても差し支えない。 Normally, a small amount of alkali metal hydroxide may be added to react with alkali metal hydrosulfide or alkali metal thiosulfate present in a trace amount in the alkali metal sulfide.
本発明で用いられる有機極性溶媒としては、ホルムアミド、アセトアミド、N−メチルホルムアミド、N,N−ジメチルアセトアミド、テトラメチル尿素、N−メチル−2−ピロリドン、2−ピロリドン、N−メチル−ε−カプロラクタム、ε−カプロラクタム、ヘキサメチルホスホルアミド、N−ジメチルプロピレン尿素、1,3−ジメチル−2−イミダゾリジノン酸などのアミド、尿素及びラクタム類;スルホラン、ジメチルスルホラン等のスルホラン類;ベンゾニトリル等のニトリル類;メチルフェニルケトン等のケトン類及びこれらの混合物を挙げることができ、これらの中でもN−メチル−2−ピロリドン、2−ピロリドン、N−メチル−ε−カプロラクタム、ε−カプロラクタム、ヘキサメチルホスホルアミド、N−ジメチルプロピレン尿素、1,3−ジメチル−2−イミダゾリジノン酸の脂肪族系環状構造を有するアミドが好ましい。 Examples of the organic polar solvent used in the present invention include formamide, acetamide, N-methylformamide, N, N-dimethylacetamide, tetramethylurea, N-methyl-2-pyrrolidone, 2-pyrrolidone, and N-methyl-ε-caprolactam. , Ε-caprolactam, hexamethylphosphoramide, N-dimethylpropyleneurea, amides such as 1,3-dimethyl-2-imidazolidinone, urea and lactams; sulfolanes such as sulfolane and dimethylsulfolane; benzonitrile and the like Nitriles; ketones such as methyl phenyl ketone and mixtures thereof, among which N-methyl-2-pyrrolidone, 2-pyrrolidone, N-methyl-ε-caprolactam, ε-caprolactam, hexamethyl Phosphoramide, N-dimethylpro Ren urea, 1,3-dimethyl-2-amide having an aliphatic cyclic structure imidazolidinone acid.
ポリアリーレンスルフィド樹脂の重合反応は、これらの有機極性溶媒の存在下、いわゆるスルフィド化剤と呼ばれる上記のアルカリ金属硫化物またはアルカリ金属水硫化物及びアルカリ金属水酸化物と、ポリハロ芳香族化合物とを反応させる。重合条件は一般に、温度200〜330℃の範囲であり、圧力は重合溶媒及び重合モノマーであるポリハロ芳香族化合物を実質的に液層に保持するような範囲であるべきであり、一般には0.1〜20MPaの範囲、好ましくは0.1〜2MPaの範囲より選択される。 In the presence of these organic polar solvents, the polymerization reaction of the polyarylene sulfide resin is carried out by combining the above-mentioned alkali metal sulfide or alkali metal hydrosulfide and alkali metal hydroxide called a sulfidizing agent with a polyhaloaromatic compound. React. The polymerization conditions are generally in the range of 200 to 330 ° C., and the pressure should be in such a range that the polymerization solvent and the polymerization monomer polyhaloaromatic compound are substantially retained in the liquid layer. It is selected from the range of 1-20 MPa, preferably from the range of 0.1-2 MPa.
本発明で用いるポリアリーレンスルフィド樹脂の製造方法の具体的態様の一つとして、1)例えば、ポリハロ芳香族化合物の存在下、アルカリ金属硫化物、又は、含水アルカリ金属水硫化物及びアルカリ金属水酸化物と、脂肪族環状構造を有するアミド、尿素またはラクタムとを、脱水させながら反応させて固形のアルカリ金属硫化物を含むスラリーを製造する工程、該スラリーを製造した後、更にNMPなどの極性有機溶媒を加え、水を留去して脱水を行う工程、次いで、脱水工程を経て得られたスラリー中で、ポリハロ芳香族化合物と、アルカリ金属水硫化物と、前記脂肪族環状構造を有するアミド、尿素またはラクタムの加水分解物のアルカリ金属塩とを、NMPなどの極性有機溶媒1モルに対して反応系内に現存する水分量が0.02モル以下で反応させて重合を行う工程を必須の製造工程として有するポリアリーレンスルフィド樹脂の製造方法が挙げられる。 As one of the specific embodiments of the method for producing the polyarylene sulfide resin used in the present invention, 1) For example, an alkali metal sulfide or a hydrous alkali metal hydrosulfide and an alkali metal hydroxide in the presence of a polyhaloaromatic compound. And a amide, urea or lactam having an aliphatic cyclic structure to react while dehydrating to produce a slurry containing solid alkali metal sulfide, and after producing the slurry, polar organic such as NMP A step of adding a solvent, distilling off water and then dehydrating, and then in a slurry obtained through the dehydration step, a polyhaloaromatic compound, an alkali metal hydrosulfide, and an amide having the above aliphatic cyclic structure, The amount of water existing in the reaction system with respect to 1 mol of a polar organic solvent such as NMP is 0.0% of the alkali metal salt of urea or lactam hydrolyzate. Method for producing a polyarylene sulfide resins having a step of performing polymerization by reacting a molar below as essential production steps.
アミド基含有環状炭化水素化合物の存在下、アルカリ金属硫化物又はアルカリ金属水硫化物と芳香族ポリハロゲン化合物とを重合させるその他の具体的方法としては、
2)アルカリ金属カルボン酸塩またはハロゲン化リチウム等の重合助剤を使用する方法、
3)芳香族ポリハロゲン化合物等の架橋剤を使用する方法、
4)少量の水の存在下に重合反応を行い次いで水を追加してさらに重合する方法、
5)アルカリ金属硫化物と芳香族ジハロゲン化合物との反応中に、反応釜の気相部分を冷却して反応釜内の気相の一部を凝縮させ液相に還流させる方法、等が挙げられる。
これらの中でも特に、副生成物の生成が少なく、かつ、直鎖状で高分子量を有するポリアリーレンスルフィド樹脂が容易に低コストで得られる点から前記1)の方法が好ましい。
Other specific methods for polymerizing an alkali metal sulfide or alkali metal hydrosulfide and an aromatic polyhalogen compound in the presence of an amide group-containing cyclic hydrocarbon compound include:
2) A method of using a polymerization aid such as an alkali metal carboxylate or lithium halide,
3) A method using a crosslinking agent such as an aromatic polyhalogen compound,
4) A method in which a polymerization reaction is carried out in the presence of a small amount of water, followed by addition of water and further polymerization.
5) During the reaction between the alkali metal sulfide and the aromatic dihalogen compound, a method of cooling the gas phase part of the reaction vessel to condense a part of the gas phase in the reaction vessel and refluxing it to the liquid phase, etc. .
Among these, the method 1) is preferred because it produces little by-products and can easily obtain a linear and high molecular weight polyarylene sulfide resin at low cost.
本発明においては、オリゴアリーレンスルフィドと、ポリハロ芳香族化合物とアルカリ金属硫化物とを反応させてカルボキシアルキルアミノ基含有化合物(1)、オリゴアリーレンスルフィド(2)、有機極性溶媒(3)、ポリアリーレンスルフィド(4)及びアルカリ金属ハロゲン化物(5)を含む粗反応混合物を得るか、または、オリゴアリーレンスルフィドとポリハロ芳香族化合物とアルカリ金属水硫化物及びアルカリ金属水酸化物とを反応させてカルボキシアルキルアミノ基含有化合物(1)、オリゴアリーレンスルフィド(2)、有機極性溶媒(3)、ポリアリーレンスルフィド(4)及びアルカリ金属ハロゲン化物(5)を含む粗反応混合物を得る形態も包含する。 In the present invention, an oligoarylene sulfide, a polyhaloaromatic compound and an alkali metal sulfide are reacted to produce a carboxyalkylamino group-containing compound (1), an oligoarylene sulfide (2), an organic polar solvent (3), a polyarylene. A crude reaction mixture containing sulfide (4) and alkali metal halide (5) is obtained, or oligoarylene sulfide, polyhaloaromatic compound, alkali metal hydrosulfide and alkali metal hydroxide are reacted to produce carboxyalkyl The form which obtains the crude reaction mixture containing the amino group-containing compound (1), oligoarylene sulfide (2), organic polar solvent (3), polyarylene sulfide (4) and alkali metal halide (5) is also included.
なお、ポリアリーレンスルフィド樹脂の製造時に、ポリアリーレンスルフィド樹脂の製造原料として、例えば、有機極性溶媒がN−メチル−2−ピロリドン、ポリハロ芳香族化合物がp−ジクロロベンゼンである場合には前記カルボキシアルキルアミノ基含有化合物として、下記一般式(1’) In the production of the polyarylene sulfide resin, as a raw material for producing the polyarylene sulfide resin, for example, when the organic polar solvent is N-methyl-2-pyrrolidone and the polyhaloaromatic compound is p-dichlorobenzene, the carboxyalkyl As an amino group-containing compound, the following general formula (1 ′)
続いて、工程(1)は、工程(1a)で得られた上記粗反応混合物を有機極性溶媒(6)で洗浄して、ポリアリーレンスルフィド(4)及びアルカリ金属ハロゲン化物(5)を分離除去して、カルボキシアルキルアミノ基含有化合物(1)、オリゴアリーレンスルフィド(2)、有機極性溶媒(3)および(6)を含む反応混合物(a1)を製造する方法を工程(1b)として有する。 Subsequently, in the step (1), the crude reaction mixture obtained in the step (1a) is washed with an organic polar solvent (6) to separate and remove the polyarylene sulfide (4) and the alkali metal halide (5). And it has as a process (1b) the method of manufacturing the reaction mixture (a1) containing a carboxyalkylamino group containing compound (1), an oligoarylene sulfide (2), an organic polar solvent (3), and (6).
上記粗反応混合物からポリアリーレンスルフィド(4)及びアルカリ金属ハロゲン化物(5)を分離除去して、カルボキシアルキルアミノ基含有化合物(1)、オリゴアリーレンスルフィド(2)および有機極性溶媒(3)を含む反応混合物(a1)を得る方法に特に制限は無く、例えば必要に応じて有機極性溶媒(3)の一部もしくは大部分を蒸留等の固液分離操作により除去した後に、得られたスラリーに有機極性溶媒(6)を混和し、10〜200℃、好ましくは50〜150℃、より好ましくは80〜130℃の範囲で接触させることにより、ポリアリーレンスルフィド(4)及びアルカリ金属ハロゲン化物(5)を含む固形成分を簡易な濾過操作で分離し、カルボキシアルキルアミノ基含有化合物(1)、オリゴアリーレンスルフィド(2)および有機極性溶媒(3および6)を含む反応混合物(a1)を濾液成分として得ることができる。 The polyarylene sulfide (4) and the alkali metal halide (5) are separated and removed from the crude reaction mixture, and contain a carboxyalkylamino group-containing compound (1), an oligoarylene sulfide (2), and an organic polar solvent (3). There is no restriction | limiting in particular in the method of obtaining reaction mixture (a1), for example, after removing a part or most part of organic polar solvent (3) by solid-liquid separation operations, such as distillation, as needed, it is organic in the obtained slurry. The polyarylene sulfide (4) and the alkali metal halide (5) are mixed by mixing the polar solvent (6) and bringing them into contact with each other in the range of 10 to 200 ° C, preferably 50 to 150 ° C, more preferably 80 to 130 ° C. The solid component containing is separated by a simple filtration operation, the carboxyalkylamino group-containing compound (1), oligo arylsulfur Can be obtained de (2) and an organic polar solvent (3 and 6) the reaction mixture containing the (a1) as the filtrate component.
この様な有機極性溶媒(6)としては、オリゴアリーレンスルフィド(2)の溶解を行う環境においてオリゴアリーレンスルフィド(2)は溶解するがポリアリーレンスルフィド樹脂(4)は溶解しにくい溶剤が好ましく、ポリアリーレンスルフィド樹脂(4)は溶解しない溶剤がより好ましい。前記スラリーと有機極性溶剤(6)とを接触させる際の圧力は常圧もしくは加圧いずれでも良いが、0.1〜0.5〔MPa〕の範囲の加圧下で行うことが好ましい。用いる有機極性溶剤(6)としてはポリアリーレンスルフィド樹脂(4)の分解や架橋など好ましくない副反応を実質的に引き起こさないものが好ましく、例えばペンタン、ヘキサン、ヘプタン、オクタン、シクロヘキサン、シクロペンタン、ベンゼン、トルエン、キシレン等の炭化水素系溶媒、クロロホルム、ブロモホルム、塩化メチレン、1,2−ジクロロエタン、1,1,1−トリクロロエタン、クロロベンゼン、2,6−ジクロロトルエン等のハロゲン系溶媒、ジエチルエーテル、テトラヒドロフラン、ジイソプロピルエーテル等のエーテル系溶媒、ホルムアミド、アセトアミド、N−メチルホルムアミド、N,N−ジメチルホルムアミド、N,N−ジメチルアセトアミド、テトラメチル尿素、N−メチル−2−ピロリドン、2−ピロリドン、N−メチル−ε−カプロラクタム、ε−カプロラクタム、ヘキサメチルホスホルアミド、N−ジメチルプロピレン尿素、1,3−ジメチル−2−イミダゾリジノン酸などのアミド、尿素及びラクタム類、ジメチルスルホキシド、トリメチルリン酸、N,N−ジメチルイミダゾリジノン、メチルエチルケトンなどの極性溶媒を例示できる。 Such an organic polar solvent (6) is preferably a solvent in which the oligoarylene sulfide (2) is dissolved but the polyarylene sulfide resin (4) is difficult to dissolve in an environment where the oligoarylene sulfide (2) is dissolved. The arylene sulfide resin (4) is more preferably a solvent that does not dissolve. Although the pressure at the time of making the said slurry and organic polar solvent (6) contact may be either normal pressure or pressurization, it is preferable to carry out under the pressurization of the range of 0.1-0.5 [MPa]. As the organic polar solvent (6) to be used, those which do not substantially cause undesirable side reactions such as decomposition and crosslinking of the polyarylene sulfide resin (4) are preferable. For example, pentane, hexane, heptane, octane, cyclohexane, cyclopentane, benzene , Hydrocarbon solvents such as toluene and xylene, halogen solvents such as chloroform, bromoform, methylene chloride, 1,2-dichloroethane, 1,1,1-trichloroethane, chlorobenzene and 2,6-dichlorotoluene, diethyl ether, tetrahydrofuran Ether solvents such as diisopropyl ether, formamide, acetamide, N-methylformamide, N, N-dimethylformamide, N, N-dimethylacetamide, tetramethylurea, N-methyl-2-pyrrolidone, 2-pi Amides such as lidone, N-methyl-ε-caprolactam, ε-caprolactam, hexamethylphosphoramide, N-dimethylpropyleneurea, 1,3-dimethyl-2-imidazolidinone, urea and lactams, dimethyl sulfoxide, Examples include polar solvents such as trimethyl phosphoric acid, N, N-dimethylimidazolidinone, and methyl ethyl ketone.
前記スラリーと有機極性溶剤(6)とを接触させる際の雰囲気に特に制限はないが、接触させる際の温度や時間などの条件によってポリアリーレンスルフィド樹脂(4)や有機極性溶媒(6)が酸化劣化するような場合には、非酸化性雰囲気下で行うことが望ましい。 Although there is no restriction | limiting in particular in the atmosphere at the time of making the said slurry and organic polar solvent (6) contact, Polyarylene sulfide resin (4) and organic polar solvent (6) are oxidized according to conditions, such as temperature and time at the time of making contact. When it deteriorates, it is desirable to carry out in a non-oxidizing atmosphere.
・工程(2)
工程(2)は、工程(1)に続いて、前記反応混合物(a1)から前記有機極性溶媒を固液分離して、オリゴアリーレンスルフィド(2)およびカルボキシアルキルアミノ基含有化合物(1)を含む反応混合物(a2)を得る工程である。
前記濾液成分として得られた反応混合物(a1)から有機極性溶媒(3)および(6)を除去する方法は、たとえば溶媒を蒸発させて溶媒回収し、同時に固形物も回収する、いわゆるフラッシュ法や、膜を利用した溶剤の除去を例示できる。有機極性溶剤を除去する際、固形物(不揮発分)の割合が20〜100〔質量%〕、好ましくは20〜99.99〔質量%〕、さらに好ましくは30〜90〔質量%〕の範囲となるよう溶剤を除去することが望ましい。加熱による溶剤の除去を行う際の温度は用いる溶剤の特性に依存するため一意的には限定できないが、通常、20〜150℃、好ましくは40〜120℃の範囲が選択できる。また、溶剤の除去を行う圧力は常圧以下が好ましく、これにより溶剤の除去をより低温で行うことが可能になる。
・ Process (2)
In the step (2), following the step (1), the organic polar solvent is separated from the reaction mixture (a1) by solid-liquid separation, and the oligoarylene sulfide (2) and the carboxyalkylamino group-containing compound (1) are contained. In this step, a reaction mixture (a2) is obtained.
The method for removing the organic polar solvents (3) and (6) from the reaction mixture (a1) obtained as the filtrate component is, for example, a so-called flash method in which the solvent is recovered by evaporating the solvent and simultaneously recovering the solid matter. The removal of the solvent using a film can be exemplified. When removing the organic polar solvent, the ratio of the solid (non-volatile content) is 20 to 100 [mass%], preferably 20 to 99.99 [mass%], more preferably 30 to 90 [mass%]. It is desirable to remove the solvent. Although the temperature at which the solvent is removed by heating depends on the characteristics of the solvent used, it cannot be limited uniquely. However, the temperature can usually be selected from 20 to 150 ° C, preferably from 40 to 120 ° C. In addition, the pressure for removing the solvent is preferably normal pressure or lower, which makes it possible to remove the solvent at a lower temperature.
・工程(3)
工程(3)は、工程(2)に続いて、該反応混合物(a2)を100℃超かつpH6以上で、水と接触させることにより、カルボキシアルキルアミノ基含有化合物(1)とオリゴアリーレンスルフィド(2)とを分離する工程である。
・ Process (3)
Step (3), following step (2), the reaction mixture (a2) at 100 ° C. ultra and pH6 above, by contacting with water, carboxyalkyl amino group-containing compound (1) and oligo arylene sulfide (2) is a step of separating.
前記該反応混合物(a2)は、必要に応じて前処理として20〜100℃の範囲の条件下で水洗処理した後に、100℃越かつpH6以上で、水と接触させる。
前記必要に応じて行う水洗処理は、例えば反応混合物(a2)に水を加えて撹拌した後にろ過装置を用いてろ過する方法、前記したろ過によって得られた水分を含有するろ過残渣(以下「含水ケーキ」と略記する。)に再度水を加えてスラリーとした後にろ過する方法、または前記含水ケーキがろ過器に保持された状態で再度水を加えろ過する方法等が挙げられる。
The reaction mixture (a2), after washing with water under the conditions of the range of 20 to 100 ° C. as the pre-treatment if necessary, at 100 ° C. Katsu Yue pH6 above, is contacted with water.
The washing treatment performed as required, for example, a method of filtering using the filtration device after stirring water was added to the reaction mixture (a2), the filter residue (hereinafter containing water obtained by filtration above " Abbreviated as “water-containing cake”), and a method of adding water again to form a slurry and then filtering, or a method of adding water again and filtering while the water-containing cake is held in a filter.
前記必要に応じて行う水洗処理の際に加える水の量は、最終的に得られるオリゴアリーレンスルフィド(2)の理論収量に対して2倍〜10倍の範囲にあることが洗浄効率の点から好ましく、上記の量の水を2〜10回、好ましくは2〜4回に分割して水洗に供することが好ましい。前記水洗処理時の水の温度は50〜90℃の範囲であることが、やはり洗浄効率が良好となる点から好ましく、なかでも70〜90℃の範囲であることが特に好ましい。 From the viewpoint of washing efficiency, the amount of water added in the washing treatment performed as necessary is in the range of 2 to 10 times the theoretical yield of the finally obtained oligoarylene sulfide (2). Preferably, the above amount of water is divided into 2 to 10 times, preferably 2 to 4 times, and then subjected to water washing. The temperature of the water during the water washing treatment is preferably in the range of 50 to 90 ° C. from the viewpoint of good washing efficiency, and particularly preferably in the range of 70 to 90 ° C.
必要に応じて行う水洗処理はバッチ処理として複数回行うことができる。複数回行う際には、例えば、50〜90℃で洗浄を行う。複数回繰り返し水洗浄する場合、前記温度条件は同一でも異なっていても良い。 The water washing process performed as needed can be performed a plurality of times as a batch process. When performing several times, it wash | cleans at 50-90 degreeC, for example. When the water washing is repeated a plurality of times, the temperature condition may be the same or different.
カルボキシアルキルアミノ基含有化合物(1)とオリゴアリーレンスルフィドを含む反応混合物(a2)は、必要に応じて水洗処理を行った後、加圧条件下、100℃超かつpH6以上で、水と接触させる。 Carboxyalkyl amino group-containing compound (1) and the reaction mixture containing the oligo arylene sulfide (a2) is, after the water washing treatment if necessary, under pressure, at 100 ° C. ultra and pH6 or more, in contact with water Let
加圧条件としては、0.02〜0.1〔MPa〕の範囲、さらに、優れた所定の精製効果を発揮しつつ、前記化合物(1)の水への溶解を促進させるために、0.02〜0.1〔MPa〕で行うことが好ましい。加圧する雰囲気としては、安全性の面から窒素ガス、アルゴンガス、ネオンガス等の不活性ガスとの混合ガスを用いても良いが、経済性の面から、空気を用いることが最も好ましい。 The pressurizing condition is in the range of 0.02 to 0.1 [MPa], and in order to promote the dissolution of the compound (1) in water while exhibiting an excellent predetermined purification effect, the pressure is set to 0. It is preferable to carry out at 02-0.1 [MPa]. As an atmosphere to be pressurized, a mixed gas with an inert gas such as nitrogen gas, argon gas, or neon gas may be used from the viewpoint of safety, but air is most preferable from the viewpoint of economy.
加圧条件下でカルボキシアルキルアミノ基含有化合物(1)とオリゴアリーレンスルフィドと水を接触させる際の温度は、カルボキシアルキルアミノ基含有化合物(1)の水への溶解度がより顕著となりカルボキシアルキルアミノ基含有化合物(1)とオリゴアリーレンスルフィドの分離がより効率的に行えることから、100℃超、好ましくは120℃以上、より好ましくは140℃以上である。また、この際の温度の上限は特に限定されないが、200℃以下、より好ましくは180℃以下である。 The temperature at which the carboxyalkylamino group-containing compound (1), oligoarylene sulfide and water are brought into contact with each other under pressure is such that the solubility of the carboxyalkylamino group-containing compound (1) in water becomes more pronounced. Since separation of contained compound (1) and oligoarylene sulfide can be performed more efficiently, it is over 100 ° C, preferably 120 ° C or higher, more preferably 140 ° C or higher. Moreover, the upper limit of the temperature in this case is not particularly limited, but is 200 ° C. or lower, more preferably 180 ° C. or lower.
加圧条件下でカルボキシアルキルアミノ基含有化合物(1)とオリゴアリーレンスルフィドと水を接触させる際、酸や塩基を添加してpHを6以上、好ましくは6.5〜11.5の範囲に調整をすることによって、前記化合物(1)の水への溶解度等を制御することが好ましい。
特に、100℃超の熱水洗の際に塩基を添加して熱水洗後のpHを9.5〜11.5にすると、カルボキシアルキルアミノ基含有化合物(1)の酸性型末端(H型末端)が塩基性型末端(Na型末端)に変換されるためカルボキシアルキルアミノ基含有化合物(1)の水への溶解度がさらに高められるため好ましい。
When the carboxyalkylamino group-containing compound (1), oligoarylene sulfide and water are brought into contact with each other under pressure, acid or base is added to adjust the pH to 6 or more, preferably 6.5 to 11.5. It is preferable to control the solubility of the compound (1) in water and the like.
In particular, when a base is added at the time of hot water washing above 100 ° C. and the pH after hot water washing is adjusted to 9.5 to 11.5, the acidic type terminal (H type terminal) of the carboxyalkylamino group-containing compound (1) Is converted to a basic type terminal (Na type terminal), so that the solubility of the carboxyalkylamino group-containing compound (1) in water is further increased, which is preferable.
ここで用いられる酸は、例えば、塩酸、硫酸、炭酸、酢酸等が挙げられ、これらの中でも炭酸や酢酸が好ましい。また用いられる塩基性化合物は水酸化リチウム、水酸化ナトリウム、水酸化カリウム等のアルカリ金属水酸化物、または炭酸ナトリウム、炭酸アンモニウム、リン酸ナトリウム等が挙げられ、これらの中でも水酸化ナトリウムが好ましい。pHの測定方法は、例えば、スラリーに対して酸を添加する場合には該スラリーを濾過した濾液のpHを測定する方法が挙げられる。 Examples of the acid used here include hydrochloric acid, sulfuric acid, carbonic acid, and acetic acid. Among these, carbonic acid and acetic acid are preferable. Examples of the basic compound used include alkali metal hydroxides such as lithium hydroxide, sodium hydroxide, and potassium hydroxide, or sodium carbonate, ammonium carbonate, sodium phosphate, and the like. Among these, sodium hydroxide is preferable. Examples of the pH measurement method include a method of measuring the pH of a filtrate obtained by filtering the slurry when an acid is added to the slurry.
また加圧条件下でカルボキシアルキルアミノ基含有化合物(1)とオリゴアリーレンスルフィド(2)と水を接触させる際に用いる水の量についても、水分子が液体として存在する量であれば特に制限は無い。加圧条件下、密閉系内の水の圧力が、その温度での飽和蒸気圧に達していれば、水が液体として存在するが、本発明においては、カルボキシアルキルアミノ基含有化合物(1)が効率的に水に溶解できるためには、カルボキシアルキルアミノ基含有化合物(1)100質量部に対して、100〜1000質量部の範囲が好ましく、さらに100〜1000質量部の範囲がより好ましく、200〜800質量部の範囲がさらに好ましい。 Further, the amount of water used when the carboxyalkylamino group-containing compound (1), the oligoarylene sulfide (2) and water are brought into contact with each other under pressure is not particularly limited as long as water molecules are present as a liquid. No. If the pressure of the water in the closed system reaches the saturated vapor pressure at that temperature under the pressurized condition, the water exists as a liquid. In the present invention, the carboxyalkylamino group-containing compound (1) In order to efficiently dissolve in water, the range of 100 to 1000 parts by mass, more preferably the range of 100 to 1000 parts by mass, is more preferable with respect to 100 parts by mass of the carboxyalkylamino group-containing compound (1). A range of ˜800 parts by mass is more preferable.
本発明においては、加圧条件下でカルボキシアルキルアミノ基含有化合物(1)とオリゴアリーレンスルフィドと水との接触は連続的に行っても良いし、バッチ式に行ってもいずれでも良い。
本発明においては、加圧条件下で前記カルボキシアルキルアミノ基含有化合物(1)とオリゴアリーレンスルフィド(2)と水とを接触させる際に用いる容器は、前記化合物(1)を液層に溶解可能な密閉型あるいは密閉可能な混合機能を有す容器であり、本発明の目的を達成可能なものであるなら何れのものでもよいが、容器内部に撹拌翼を有し、且つ、底部に濾過用フィルターが配設された密閉型あるいは密閉可能な混合機能を有す容器などが挙げられる。
In the present invention, the contact of the carboxyalkylamino group-containing compound (1), the oligoarylene sulfide and the water under pressure may be performed continuously or in a batch manner.
In the present invention, the container used when the carboxyalkylamino group-containing compound (1), oligoarylene sulfide (2) and water are brought into contact under pressure can dissolve the compound (1) in the liquid layer. The container has a mixing function that can be sealed or can be sealed, and may be any container that can achieve the object of the present invention, but has a stirring blade inside the container and is used for filtration at the bottom. Examples thereof include a sealed type provided with a filter or a container having a mixing function capable of being sealed.
前記カルボキシアルキルアミノ基含有化合物(1)とオリゴアリーレンスルフィド(2)を含む反応混合物(a2)は、必要に応じて水洗処理を行った後、加圧条件下、100℃超かつpH6以上で、水と接触させ、その後、室温まで冷却した後、必要に応じて濾過し、イオン交換水を加えて20〜90℃の範囲で再度濾過して、液層として塩基性型末端(Na型末端)に変換された前記カルボキシアルキルアミノ基含有化合物(1)を分離して、固形分としてオリゴアリーレンスルフィド(2)を回収する。しかしながら、このようにして反応混合物(a2)から固液分離して得られた固形分はオリゴアリーレンスルフィド(2)を高濃度に含む他、分離せずにカルボキシアルキルアミノ基含有化合物(1)が残留する為、カルボキシアルキルアミノ基含有化合物(1)0.01〜20質量%とオリゴアリーレンスルフィド99.99〜80質量%とを含む組成物(α)となるまで、上記固液分離操作を1回または複数回行うことが好ましい。組成物(α)中のカルボキシアルキルアミノ基含有化合物(1)が20質量%を超える範囲であると、ポリアリーレンスルフィド樹脂の原料の一部として用いた場合に、ポリアリーレンスルフィド樹脂の溶融重合時の阻害要因となり、一方、0.01質量%未満にするためには、過剰な固液分離が必要となり生産性を低下させる原因となる。
In the carboxyalkyl amino group-containing compound (1) and oligo arylene sulfide (2) the reaction mixture containing (a2), after performing the water washing treatment if necessary, under pressure, 100 ° C. ultra and pH6 more After contacting with water and then cooling to room temperature, it is filtered if necessary, and ion-exchanged water is added and filtered again in the range of 20 to 90 ° C. to form a basic type terminal (Na type terminal) as a liquid layer. The carboxyalkylamino group-containing compound (1) converted to) is separated, and the oligoarylene sulfide (2) is recovered as a solid content. However, the reaction mixture in this way solids obtained by solid-liquid separation from (a2) other containing oligo arylene sulfide (2) in a high concentration, without separation carboxyalkyl amino group-containing compound (1) Therefore, the solid-liquid separation operation is performed until the composition (α) containing 0.01 to 20% by mass of the carboxyalkylamino group-containing compound (1) and 99.99 to 80% by mass of the oligoarylene sulfide is obtained. It is preferable to carry out once or a plurality of times. When the carboxyalkylamino group-containing compound (1) in the composition (α) is in a range exceeding 20% by mass, when used as part of the raw material of the polyarylene sulfide resin, the polyarylene sulfide resin is melt polymerized. On the other hand, in order to make it less than 0.01% by mass, excessive solid-liquid separation is required, which causes a decrease in productivity.
回収して得られたオリゴアリーレンスルフィド(2)を高濃度で含有する組成物(α)は、そのまま乾燥して粉末を得ても良いし、更に数回の水洗処理した後、固液分離し、乾燥を行って粉末として得ても良い。100℃超の熱水洗後に行う水洗処理に用いる水量は特に制限は無いが、オリゴアリーレンスルフィド(2)の理論収量に対して2〜10倍の範囲である。また乾燥は実質的に水が蒸発する温度に加熱して行う。乾燥は真空下で行っても良いし、空気中あるいは窒素のような不活性雰囲気下で行っても良い。 The recovered composition (α) containing the oligoarylene sulfide (2) at a high concentration may be dried as it is to obtain a powder, and further subjected to several water washing treatments, followed by solid-liquid separation. It may be dried to obtain a powder. Although there is no restriction | limiting in particular in the amount of water used for the water-washing process performed after hot water washing over 100 degreeC, It is the range of 2-10 times with respect to the theoretical yield of oligoarylene sulfide (2). Drying is performed by heating to a temperature at which water substantially evaporates. Drying may be performed under vacuum, or may be performed in air or in an inert atmosphere such as nitrogen.
なお、オリゴアリーレンスルフィド(2)中には、下記構造式(2) In the oligoarylene sulfide (2), the following structural formula (2)
PASの製造方法
本発明は、上記工程(1)〜(3)を経ることによって、構造式(1)で表される化合物(1)0.01〜20質量部とオリゴアリーレンスルフィド(2)99.99〜80質量部とを含む組成物(α)として得られたものを原料として用い、酸化性雰囲気下で溶融重合することにより、分岐型ポリアリーレンスルフィド樹脂を製造することができるが、それぞれ別々に製造した前記化合物(1)とオリゴアリーレンスルフィド(2)とを、前記化合物(1)0.01〜20質量部とオリゴアリーレンスルフィド(2)99.99〜80質量部となるよう配合して、酸化性雰囲気下で溶融重合することもできる。
Production method of PAS The present invention undergoes steps (1) to (3) described above, whereby 0.01 to 20 parts by mass of compound (1) represented by structural formula (1) and oligoarylene sulfide (2) 99. A branched polyarylene sulfide resin can be produced by melt polymerization in an oxidizing atmosphere using a material (α) containing .99 to 80 parts by mass as a raw material. The compound (1) and oligoarylene sulfide (2) produced separately are blended so as to be 0.01 to 20 parts by mass of the compound (1) and 99.99 to 80 parts by mass of the oligoarylene sulfide (2). In addition, melt polymerization can be performed in an oxidizing atmosphere.
本発明において溶融重合は押出機等を用いてオリゴアリーレンスルフィドの融点以上で、オリゴアリーレンスルフィドを溶融した状態で行ってもよいが、オリゴアリーレンスルフィドの熱劣化の可能性が高まるため、融点プラス100℃以下で行うことが好ましい。ただし、ここでの融点とは、示差走査熱量計(パーキンエルマー製DSC装置 Pyris Diamond)を用いてJIS K 7121に準拠して測定したものをさす。 In the present invention, the melt polymerization may be carried out in a state where the oligoarylene sulfide is melted at a temperature equal to or higher than the melting point of the oligoarylene sulfide using an extruder or the like. It is preferable to carry out at a temperature of ℃ or less. However, melting | fusing point here refers to what was measured based on JISK7121 using the differential scanning calorimeter (DSC apparatus Pyris Diamond made from Perkin Elmer).
本発明において溶融重合は、分岐度を高め、かつ高重合度体を得ることができる観点から酸化性雰囲気下で行う。なお、本発明において酸化性雰囲気とは、気相の酸素濃度が5体積%以上、かつ30体積%以下の範囲、好ましくは10体積%以上かつ、25体積%以下の範囲を指し、大気中で行うことが生産性の点から最も好ましい。 In the present invention, melt polymerization is performed in an oxidizing atmosphere from the viewpoint of increasing the degree of branching and obtaining a high degree of polymerization. In the present invention, the oxidizing atmosphere refers to a range where the oxygen concentration in the gas phase is 5% by volume or more and 30% by volume or less, preferably 10% by volume or more and 25% by volume or less. It is most preferable from the viewpoint of productivity.
また、本発明において溶融重合は、溶媒を実質的に含まない条件下で行うことが好ましい。溶媒を実質的に含まない条件であるとは、化合物(1)とオリゴアリーレンスルフィド(2)の合計100質量部に対して、溶媒が10質量部以下、好ましくは5質量部以下、さらに好ましくは1質量部以下から、0質量部以上、好ましくは0.01質量部以上、さらに好ましくは0.1質量部以上の範囲であることを意味する。 In the present invention, the melt polymerization is preferably performed under a condition that does not substantially contain a solvent. The condition that substantially does not contain a solvent means that the solvent is 10 parts by mass or less, preferably 5 parts by mass or less, more preferably 100 parts by mass relative to the total of 100 parts by mass of the compound (1) and the oligoarylene sulfide (2). It means that it is in the range of 1 part by mass or more, 0 part by mass or more, preferably 0.01 part by mass or more, and more preferably 0.1 part by mass or more.
また、本発明において溶融重合の原料として前記構造式(1)で表される化合物(1)0.01〜20質量部とオリゴアリーレンスルフィド(2)99.99〜80質量部に加え、さらに、該化合物(1)とオリゴアリーレンスルフィド(2)の合計100質量部に対し、50質量部以下、好ましくは0〜50質量部、より好ましくは0〜10質量部の範囲でポリアリーレンスルフィド樹脂(β)を含む条件下で加熱処理を行うことができる。 In addition, in addition to 0.01 to 20 parts by mass of the compound (1) represented by the structural formula (1) and 99.99 to 80 parts by mass of the oligoarylene sulfide (2) as a raw material for melt polymerization in the present invention, Polyarylene sulfide resin (β) in the range of 50 parts by mass or less, preferably 0 to 50 parts by mass, more preferably 0 to 10 parts by mass with respect to a total of 100 parts by mass of the compound (1) and oligoarylene sulfide (2). ).
ここで、ポリアリーレンスルフィド樹脂(β)としては、本発明の効果を損なうものでなければ特に制限されるものではなく、例えば前記工程(1b)で分離除去した、ポリアリーレンスルフィド(4)及びアルカリ金属ハロゲン化物(5)を回収し、さらに水と接触させてアルカリ金属ハロゲン化物(5)を濾別するなどの公知の精製工程を施して得られたものを用いることができる。 Here, the polyarylene sulfide resin (β) is not particularly limited as long as it does not impair the effects of the present invention. For example, the polyarylene sulfide (4) and the alkali separated and removed in the step (1b) are used. The metal halide (5) can be recovered, and a product obtained by subjecting to a known purification step such as contact with water and filtration of the alkali metal halide (5) can be used.
溶融重合により得られた本発明の分岐型ポリアリーレンスルフィド樹脂を含む反応生成物は、そのまま直接、溶融混練機に投入する等の方法により樹脂組成物を製造することもできるが、当該反応生成物に当該反応生成物が溶解する溶媒を加えて溶解物を調製し、当該溶解物の状態で反応装置から反応生成物を取り出すことが、生産性に優れるだけでなく、さらに反応性も良好となるため好ましい。当該反応生成物が溶解する溶媒の添加は、溶融重合後に行うことが好ましいが、溶融重合の反応後期に行ってもよく、また、上記のとおり溶融混合物(反応生成物)を冷却して固体状態の混合物を得た後、加圧下、減圧下、又は非酸化性雰囲気の大気圧下で、混合物を加熱して重合反応を更に進行させた後であってもよい。当該溶解物を調製する工程は、非酸化性雰囲気下で行ってもよい。また、加熱溶解の温度としては、前記反応生成物が溶解する溶媒の融点以上の範囲であればよく、好ましくは200〜350℃の範囲、より好ましくは210〜250℃の範囲であり、加圧下で行うことが好ましい。 The reaction product containing the branched polyarylene sulfide resin of the present invention obtained by melt polymerization can be directly produced in a melt kneader or the like to produce a resin composition. It is not only excellent in productivity but also good in reactivity to prepare a lysate by adding a solvent in which the reaction product is dissolved in and removing the reaction product from the reaction apparatus in the state of the lysate. Therefore, it is preferable. The addition of the solvent in which the reaction product is dissolved is preferably performed after the melt polymerization, but it may be performed in the later stage of the reaction of the melt polymerization, or as described above, the molten mixture (reaction product) is cooled and solid state After obtaining the mixture, the polymerization reaction may be further advanced by heating the mixture under pressure, reduced pressure, or atmospheric pressure in a non-oxidizing atmosphere. The step of preparing the lysate may be performed in a non-oxidizing atmosphere. Further, the temperature for heating and dissolving may be in the range of the melting point or higher of the solvent in which the reaction product dissolves, preferably in the range of 200 to 350 ° C, more preferably in the range of 210 to 250 ° C, under pressure. It is preferable to carry out with.
前記溶解物を調製するために用いる、前記反応生成物が溶解する溶媒の配合割合は、ポリアリーレンスルフィド樹脂を含む反応生成物100質量部に対して、好ましくは90〜1000質量部、より好ましくは200〜400質量部の範囲である。 The blending ratio of the solvent in which the reaction product is used for preparing the dissolved product is preferably 90 to 1000 parts by mass, more preferably 100 parts by mass with respect to 100 parts by mass of the reaction product containing the polyarylene sulfide resin. It is the range of 200-400 mass parts.
反応生成物が溶解する溶媒としては、例えば、フィリップス法等の溶液重合において重合反応溶媒として用いられる溶媒を用いることができる。好ましい溶媒の例としては、N−メチル−2−ピロリドン(以下、NMPと略記)、N−シクロヘキシル−2−ピロリドン、2−ピロリドン、1,3−ジメチル−2−イミダゾリジノン酸、ε−カプロラクタム、N−メチル−ε−カプロラクタム等の脂肪族環状アミド化合物、ヘキサメチルリン酸トリアミド(HMPA)、テトラメチル尿素(TMU)、ジメチルホルムアミド(DMF)、及びジメチルアセトアミド(DMA)等のアミド化合物、ポリエチレングリコールジアルキルエーテル(重合度は2000以下で、炭素数1〜20のアルキル基を有するもの)等のエーテル化ポリエチレングリコール化合物、並びに、テトラメチレンスルホキシド、及びジメチルスルホキシド(DMSO)等のスルホキシド化合物が挙げられる。その他の使用可能な溶媒の例として、ベンゾフェノン、ジフェニルエーテル、ジフェニルスルフィド、4,4’−ジブロモビフェニル、1−フェニルナフタレン、2,5−ジフェニル−1,3,4−オキサジアゾール、2,5−ジフェニルオキサゾール、トリフェニルメタノール、N,N−ジフェニルホルムアミド、ベンジル、アントラセン、4−ベンゾイルビフェニル、ジベンゾイルメタン、2−ビフェニルカルボン酸、ジベンゾチオフェン、ペンタクロロフエノール、1−ベンジル−2−ピロリジオン、9−フルオレノン、2−ベンゾイルナフタレン、1−ブロモナフタレン、1,3−ジフェノキシベンゼン、フルオレン、1−フェニル−2−ピロリジノン、1−メトキシナフタレン、1−エトキシナフタレン、1,3−ジフェニルアセトン、1,4−ジベンゾイルプタン、フェナントレン、4−ベンゾイルビフェニル、1,1−ジフェニルアセトン、o,o’−ビフェノール、2,6−ジフェニルフェノール、トリフェニレン、2−フェニルフェノール、チアントレン、3−フェノキシベンジルアルコール、4−フェニルフェノール、9,10−ジクロロアントラセン、トリフェニルメタン、4,4’−ジメトキシベンゾフェノン、9,10−ジフェニルアントラセン、フルオランテン、ジフェニルフタレート、ジフェニルカルボネート、2,6−ジメトキシナフタレン、2,7−ジメトキシナフタレン、4−ブロモジフェニルエーテル、ピレン、9,9’−ビ−フルオレン、4,4’−イソプロピルリデン−ジフェノール、イプシロン−カプロラクタム、N−シクロヘキシル−2−ピロリドン、ジフェニルイソフタレート及びジフェニルーターフタレート及び1−クロロナフタレンからなる群から選ばれる1種以上の溶媒が挙げられる。 As a solvent in which the reaction product dissolves, for example, a solvent used as a polymerization reaction solvent in solution polymerization such as a Philips method can be used. Examples of preferred solvents include N-methyl-2-pyrrolidone (hereinafter abbreviated as NMP), N-cyclohexyl-2-pyrrolidone, 2-pyrrolidone, 1,3-dimethyl-2-imidazolidinone, and ε-caprolactam. , Aliphatic cyclic amide compounds such as N-methyl-ε-caprolactam, amide compounds such as hexamethylphosphoric triamide (HMPA), tetramethylurea (TMU), dimethylformamide (DMF), and dimethylacetamide (DMA), polyethylene Examples include etherified polyethylene glycol compounds such as glycol dialkyl ether (having a degree of polymerization of 2000 or less and an alkyl group having 1 to 20 carbon atoms), and sulfoxide compounds such as tetramethylene sulfoxide and dimethyl sulfoxide (DMSO). . Examples of other usable solvents include benzophenone, diphenyl ether, diphenyl sulfide, 4,4′-dibromobiphenyl, 1-phenylnaphthalene, 2,5-diphenyl-1,3,4-oxadiazole, 2,5- Diphenyloxazole, triphenylmethanol, N, N-diphenylformamide, benzyl, anthracene, 4-benzoylbiphenyl, dibenzoylmethane, 2-biphenylcarboxylic acid, dibenzothiophene, pentachlorophenol, 1-benzyl-2-pyrrolidione, 9- Fluorenone, 2-benzoylnaphthalene, 1-bromonaphthalene, 1,3-diphenoxybenzene, fluorene, 1-phenyl-2-pyrrolidinone, 1-methoxynaphthalene, 1-ethoxynaphthalene, 1,3-diphenylacetate 1,4-dibenzoylbutane, phenanthrene, 4-benzoylbiphenyl, 1,1-diphenylacetone, o, o'-biphenol, 2,6-diphenylphenol, triphenylene, 2-phenylphenol, thianthrene, 3-phenoxy Benzyl alcohol, 4-phenylphenol, 9,10-dichloroanthracene, triphenylmethane, 4,4′-dimethoxybenzophenone, 9,10-diphenylanthracene, fluoranthene, diphenylphthalate, diphenyl carbonate, 2,6-dimethoxynaphthalene, 2,7-dimethoxynaphthalene, 4-bromodiphenyl ether, pyrene, 9,9'-bifluorene, 4,4'-isopropylidene-diphenol, epsilon-caprolactam, N-cyclohexyl- Examples thereof include one or more solvents selected from the group consisting of 2-pyrrolidone, diphenylisophthalate, diphenyl-terephthalate and 1-chloronaphthalene.
反応装置から取り出された当該溶解物は、後処理を行った後、他の成分と溶融混練して樹脂組成物を調製することが、反応性がより良好となるため好ましい。溶解物の後処理の方法としては、特に制限されるものではないが、例えば、以下の方法が挙げられる。
処理(1)当該溶解物を、そのまま、又は酸若しくは塩基を加えた後、減圧下又は常圧化で溶媒を留去し、次いで溶媒留去後の固形物を水、当該溶解物に用いた溶媒(又は低分子ポリマーに対して同等の溶解度を有する有機溶媒)、アセトン、メチルエチルケトン、及びアルコール類などから選ばれる溶媒で1回又は2回以上洗浄し、更に中和、水洗、濾過及び乾燥する方法。
処理(2)当該溶解物に水、アセトン、メチルエチルケトン、アルコール、エーテル、ハロゲン化炭化水素、芳香族炭化水素、及び脂肪族炭化水素などの溶媒(当該溶解物の溶媒に可溶であり、且つ少なくともポリアリーレンスルフィド樹脂に対しては貧溶媒である溶媒)を沈降剤として添加して、ポリアリーレンスルフィド樹脂及び無機塩等を含む固体状生成物を沈降させ、固体状生成物を濾別、洗浄及び乾燥する方法。
処理(3)当該溶解物に、当該溶解物に用いた溶媒(又は低分子ポリマーに対して同等の溶解度を有する有機溶媒)を加えて撹拌した後、濾過して低分子量重合体を除いた後、水、アセトン、メチルエチルケトン、及びアルコールなどから選ばれる溶媒で1回又は2回以上洗浄し、その後中和、水洗、濾過及び乾燥をする方法。
The melted product taken out from the reaction apparatus is preferably subjected to post-treatment and then melt-kneaded with other components to prepare a resin composition because the reactivity becomes better. The method for post-treatment of the lysate is not particularly limited, and examples thereof include the following methods.
Treatment (1) The solution is used as it is, or after adding an acid or a base, the solvent is distilled off under reduced pressure or normal pressure, and then the solid after the solvent is distilled off is used for water and the solution. Wash once or twice with a solvent (or an organic solvent having an equivalent solubility in a low molecular weight polymer), acetone, methyl ethyl ketone, and alcohols, then neutralize, wash with water, filter and dry. Method.
Treatment (2) Solvent such as water, acetone, methyl ethyl ketone, alcohol, ether, halogenated hydrocarbon, aromatic hydrocarbon, and aliphatic hydrocarbon (soluble in the solvent of the lysate, and at least (A solvent which is a poor solvent for polyarylene sulfide resin) is added as a precipitating agent to precipitate a solid product containing polyarylene sulfide resin and inorganic salt, and the solid product is filtered, washed and How to dry.
Treatment (3) After adding the solvent (or an organic solvent having an equivalent solubility with respect to the low molecular weight polymer) used in the dissolved material to the dissolved material and stirring, and then filtering to remove the low molecular weight polymer , Washing with a solvent selected from water, acetone, methyl ethyl ketone, alcohol and the like once or twice, followed by neutralization, washing with water, filtration and drying.
なお、上記処理(1)〜(3)に例示したような後処理方法において、ポリアリーレンスルフィド樹脂の乾燥は真空中で行なってもよいし、空気中又は窒素のような不活性ガス雰囲気中で行なってもよい。酸素濃度が5〜30体積%の範囲の酸化性雰囲気中又は減圧条件下で熱処理を行い、分岐型ポリアリーレンスルフィド樹脂を、さらに酸化架橋させることもできる。 In the post-treatment methods exemplified in the above treatments (1) to (3), the polyarylene sulfide resin may be dried in a vacuum, or in an inert gas atmosphere such as air or nitrogen. You may do it. The branched polyarylene sulfide resin can be further oxidized and crosslinked by performing a heat treatment in an oxidizing atmosphere having an oxygen concentration in the range of 5 to 30% by volume or under reduced pressure.
・ポリアリーレンスルフィド樹脂
本発明の製造方法により得られたポリアリーレンスルフィド樹脂は300℃で測定した溶融粘度(V6)が20〜5,000〔Pa・s〕の範囲のものとなる。ただし、300℃で測定した溶融粘度(V6)とは、フローテスターを用いて、温度300℃、荷重1.96MPa、オリフィス長とオリフィス径との、前者/後者の比が10/1であるオリフィスを使用して6分間保持した後の溶融粘度を表す。
-Polyarylene sulfide resin The polyarylene sulfide resin obtained by the production method of the present invention has a melt viscosity (V6) measured at 300 ° C in the range of 20 to 5,000 [Pa · s]. However, melt viscosity (V6) measured at 300 ° C. is an orifice having a temperature / 300 ° C., a load of 1.96 MPa, an orifice length and an orifice diameter of 10/1 using a flow tester. Represents the melt viscosity after holding for 6 minutes.
本発明の製造方法により得られたポリアリーレンスルフィド樹脂は、その非ニュートン指数が1.26〜2.50の範囲であり、好ましくは1.30〜2.20の範囲であり、さらに好ましくは1.50〜2.0の範囲である。このような分岐型ポリアリーレンスルフィド樹脂は機械的物性、流動性、耐磨耗性に優れる。ただし、非ニュートン指数(N値)は、キャピログラフを用いて300℃、オリフィス長(L)とオリフィス径(D)の比、L/D=40の条件下で、剪断速度及び剪断応力を測定し、下記式を用いて算出した値である。 The polyarylene sulfide resin obtained by the production method of the present invention has a non-Newtonian index in the range of 1.26 to 2.50, preferably in the range of 1.30 to 2.20, more preferably 1 The range is from 50 to 2.0. Such a branched polyarylene sulfide resin is excellent in mechanical properties, fluidity, and abrasion resistance. However, the non-Newtonian index (N value) is measured by measuring the shear rate and shear stress using a capillograph at 300 ° C, the ratio of the orifice length (L) to the orifice diameter (D), and L / D = 40. These are values calculated using the following formula.
さらに、本発明の製造方法により得られた分岐型ポリアリーレンスルフィド樹脂は質量平均分子量で15,000〜1,500,000の範囲、好ましくは30,000〜750,000の範囲、より好ましくは60,000〜150,000の範囲である。 Furthermore, the branched polyarylene sulfide resin obtained by the production method of the present invention has a mass average molecular weight in the range of 15,000 to 1,500,000, preferably in the range of 30,000 to 750,000, more preferably 60. , 150,000 to 150,000.
本発明の製造方法により得られた分岐型ポリアリーレンスルフィド樹脂の分子量分布の広がり、すなわち質量平均分子量と数平均分子量の比(質量平均分子量/数平均分子量)で2.5以上、好ましくは3.0以上の範囲である。 The molecular weight distribution of the branched polyarylene sulfide resin obtained by the production method of the present invention is broadened, that is, the ratio of the mass average molecular weight to the number average molecular weight (mass average molecular weight / number average molecular weight) is 2.5 or more, preferably 3. It is a range of 0 or more.
本発明の製造方法により得られた分岐型ポリアリーレンスルフィド樹脂は、カルボキシアルキルアミノ基含有化合物(1)を低減した、高濃度のオリゴアリーレンスルフィドを含有する組成物を原料として使用していることから、溶融成形加工時の発生ガス成分を抑制し臭気改善と金型汚れを防止することができる。 The branched polyarylene sulfide resin obtained by the production method of the present invention uses, as a raw material, a composition containing a high concentration of oligoarylene sulfide, in which the carboxyalkylamino group-containing compound (1) is reduced. In addition, it is possible to suppress the gas component generated during the melt molding process and to improve the odor and prevent mold contamination.
本発明の製造方法により得られた分岐型ポリアリーレンスルフィド樹脂は、従来のポリアリーレンスルフィド樹脂と同様に、本発明の目的を逸脱しない範囲で、離型剤、着色剤、耐熱安定剤、紫外線安定剤、発泡剤、防錆剤、難燃剤、滑剤、カップリング剤、充填材など公知慣用の添加剤を含有せしめることができる。更に、同様に下記のごとき合成樹脂及びエラストマーを混合して使用することもできる。これら合成樹脂としては、ポリエステル、ポリアミド、ポリイミド、ポリエーテルイミド、ポリカーボネート、ポリフェニレンエーテル、ポリスルフォン、ポリエーテルスルフォン、ポリエーテルエーテルケトン、ポリエーテルケトン、ポリアリーレン、ポリエチレン、ポリプロピレン、ポリ四弗化エチレン、ポリ二弗化エチレン、ポリスチレン、ABS樹脂、エポキシ樹脂、シリコーン樹脂、フェノール樹脂、ウレタン樹脂、液晶ポリマー等が挙げられ、エラストマーとしては、ポリオレフィン系ゴム、弗素ゴム、シリコーンゴム等が挙げられる。 The branched polyarylene sulfide resin obtained by the production method of the present invention is similar to the conventional polyarylene sulfide resin in that it does not depart from the object of the present invention. Known and commonly used additives such as an agent, a foaming agent, a rust preventive agent, a flame retardant, a lubricant, a coupling agent, and a filler can be contained. Furthermore, the following synthetic resins and elastomers can also be mixed and used. These synthetic resins include polyester, polyamide, polyimide, polyetherimide, polycarbonate, polyphenylene ether, polysulfone, polyethersulfone, polyetheretherketone, polyetherketone, polyarylene, polyethylene, polypropylene, polytetrafluoroethylene, Examples thereof include poly (difluoroethylene), polystyrene, ABS resin, epoxy resin, silicone resin, phenol resin, urethane resin, and liquid crystal polymer. Examples of the elastomer include polyolefin rubber, fluorine rubber, and silicone rubber.
また、本発明の製造方法により得られた分岐型ポリアリーレンスルフィド樹脂は、エポキシシランカップリング剤や官能基含有熱可塑性エラストマーなどの耐衝撃性改質剤との反応性に優れ、従来のポリアリーレンスルフィド樹脂と同様に、そのまま射出成形、押出成形、圧縮成形、ブロー成形のごとき各種溶融加工法により、耐熱性、成形加工性、寸法安定性等に優れた成形物にすることができ、例えば、コネクタ・プリント基板・封止成形品などの電気・電子部品、ランプリフレクター・各種電装部品などの自動車部品、各種建築物や航空機・自動車などの内装用材料、あるいはOA機器部品・カメラ部品・時計部品などの精密部品等の射出成形・圧縮成形品、あるいは繊維・フィルム・シート・パイプなどの押出成形・引抜成形品等として幅広く利用可能である。 Further, the branched polyarylene sulfide resin obtained by the production method of the present invention is excellent in reactivity with an impact modifier such as an epoxy silane coupling agent or a functional group-containing thermoplastic elastomer, and is a conventional polyarylene. Like the sulfide resin, it can be made into a molded product excellent in heat resistance, molding processability, dimensional stability, etc. by various melt processing methods such as injection molding, extrusion molding, compression molding and blow molding. Electrical / electronic parts such as connectors / printed boards / encapsulated molded parts, automotive parts such as lamp reflectors / electrical parts, interior materials for various buildings, aircraft / automobiles, OA equipment parts / camera parts / watch parts Injection molding and compression molding products such as precision parts, etc., or extrusion molding and pultrusion molding products such as fibers, films, sheets, and pipes It is a wide range of possible use this in.
以下に実施例を挙げて本発明を具体的に説明する。これら例は例示的なものであって限定的なものではない。 The present invention will be specifically described below with reference to examples. These examples are illustrative and not limiting.
(CP−MABAの定量方法)
CP−MABA量はHPLCで液中のCP−MABA濃度を測定し、算出した。
サンプル調製:有機溶媒中にCP-MABAが含まれる場合は、溶媒をエバポレータで溶媒を留去したたのち、残渣にHPLCの移動相を加え溶解して測定サンプルを調製した。水溶液中にCP−MABAが含まれる場合は、そのまま移動相を加えて調製した。
測定サンプルのHPLC測定を行い、下記の方法で作製した標準サンプルと同じ保持時間のピーク面積と検量線とから液中の濃度を求め、算出した。
(CP-MABA quantification method)
The amount of CP-MABA was calculated by measuring the concentration of CP-MABA in the liquid by HPLC.
Sample preparation: When CP-MABA was contained in an organic solvent, the solvent was distilled off with an evaporator, and then a HPLC mobile phase was added to the residue and dissolved to prepare a measurement sample. When CP-MABA was contained in the aqueous solution, it was prepared by adding the mobile phase as it was.
The measurement sample was subjected to HPLC measurement, and the concentration in the liquid was determined and calculated from the peak area and calibration curve of the same retention time as the standard sample prepared by the following method.
(標準物質:CP−MABAの合成)
48%NaOH水溶液83.4g(1.0モル)とN‐メチル‐2‐ピロリドン297.4g(3.0モル)を、撹拌機付き耐圧容器に仕込み、230℃で3時間撹拌した。この撹拌が終了した後、温度230℃のままバルブを開き、放圧し、N‐メチル‐2‐ピロリドンの蒸気圧程度である230℃において0.1MPaまで圧力を低下させ、水を留去した。その後、再び密閉し200℃程度まで温度を低下させた。
(Synthesis of standard substance: CP-MABA)
83.4 g (1.0 mol) of 48% NaOH aqueous solution and 297.4 g (3.0 mol) of N-methyl-2-pyrrolidone were charged in a pressure vessel equipped with a stirrer and stirred at 230 ° C. for 3 hours. After the stirring was completed, the valve was opened with the temperature kept at 230 ° C., the pressure was released, and the pressure was reduced to 0.1 MPa at 230 ° C., which is about the vapor pressure of N-methyl-2-pyrrolidone, and water was distilled off. Then, it sealed again and the temperature was reduced to about 200 degreeC.
p−ジクロロベンゼン147.0g(1.0モル)を60℃以上の温度条件下で加熱溶解して反応混合物中に投入し、250℃まで昇温後4時間撹拌した。この撹拌が終了した後、室温まで冷却した。p−ジクロロベンゼンの反応率は31モル%であった。冷却後、内容物を取り出し、水を加えて撹拌後、未反応のp−ジクロロベンゼンが不溶物となって残ったものをろ過によって取り除いた。 147.0 g (1.0 mol) of p-dichlorobenzene was heated and dissolved under a temperature condition of 60 ° C. or higher, charged into the reaction mixture, heated to 250 ° C., and stirred for 4 hours. After completion of this stirring, the mixture was cooled to room temperature. The reaction rate of p-dichlorobenzene was 31 mol%. After cooling, the contents were taken out, water was added, and the mixture was stirred. Unreacted p-dichlorobenzene remained as an insoluble matter and was removed by filtration.
次いで、ろ液である水溶液に塩酸を加えて該水溶液のpHを4に調整した。このとき水溶液中に褐色オイル状のCP−MABA(水素型)が生じた。そこにクロロホルムを加えて褐色オイル状物質を抽出した。このときの水相には、N‐メチル‐2‐ピロリドン及びその開環物である4−メチルアミノ酪酸(以下「MABA」と略記する。)が含まれるため水相は廃棄した。クロロホルム相は水洗を2回繰り返した。 Next, hydrochloric acid was added to the aqueous solution as the filtrate to adjust the pH of the aqueous solution to 4. At this time, brown oily CP-MABA (hydrogen type) was formed in the aqueous solution. Chloroform was added thereto to extract a brown oily substance. Since the aqueous phase at this time contained N-methyl-2-pyrrolidone and its ring-opened product, 4-methylaminobutyric acid (hereinafter abbreviated as “MABA”), the aqueous phase was discarded. The chloroform phase was washed twice with water.
クロロホルム相に水を加えてスラリー化した状態で48%NaOH水溶液を加え、該スラリーのpHを13に調整した。このときCP−MABAはナトリウム塩となって水相に移り、クロロホルム相には副生成物であるp−クロロ−N−メチルアニリン及びN−メチルアニリンが溶解しているためクロロホルム相は廃棄した。水相はクロロホルム洗浄を2回繰り返した。 In a state where water was added to the chloroform phase to form a slurry, a 48% NaOH aqueous solution was added to adjust the pH of the slurry to 13. At this time, CP-MABA was converted to a sodium salt and moved to the aqueous phase, and the chloroform phase was discarded because p-chloro-N-methylaniline and N-methylaniline as by-products were dissolved in the chloroform phase. The aqueous phase was washed twice with chloroform.
水溶液に希塩酸を加えて該水溶液のpHを1以下に調整した。このときCP−MABAは塩酸塩となって水溶液中にとどまるので、水溶液にクロロホルムを加えて、副生成物であるp−クロロフェノールを抽出した。p−クロロフェノールが溶解したクロロホルム相は廃棄した。 Dilute hydrochloric acid was added to the aqueous solution to adjust the pH of the aqueous solution to 1 or less. At this time, CP-MABA became hydrochloride and remained in the aqueous solution, so chloroform was added to the aqueous solution to extract p-chlorophenol as a by-product. The chloroform phase in which p-chlorophenol was dissolved was discarded.
残った水溶液に48%NaOH水溶液を加え、該水溶液のpHを4に調整した。これにより、CP−MABAの塩酸塩が中和され、褐色オイル状のCP−MABA(水素型)が水溶液から析出した。CP−MABA(水素型)をクロロホルムで抽出し、クロロホルムを減圧除去することによってCP−MABA(水素型)を得た。 A 48% aqueous NaOH solution was added to the remaining aqueous solution to adjust the pH of the aqueous solution to 4. As a result, the hydrochloride of CP-MABA was neutralized, and brown oily CP-MABA (hydrogen type) was precipitated from the aqueous solution. CP-MABA (hydrogen type) was extracted with chloroform, and chloroform was removed under reduced pressure to obtain CP-MABA (hydrogen type).
(加熱時重量減少率測定)
リガク製示差熱天秤TG8120を用い、サンプル10mgを秤量し、50℃から400℃まで20℃/minで昇温し、100℃時点のサンプル重量を基準に320℃時点のサンプル重量減少量を測定し、重量減少率を算出した。
(Measurement of weight loss during heating)
Using a Rigaku differential thermal balance TG8120, weigh 10 mg of sample, raise the temperature from 50 ° C. to 400 ° C. at 20 ° C./min, and measure the decrease in sample weight at 320 ° C. based on the sample weight at 100 ° C. The weight loss rate was calculated.
(融点測定)
パーキンエルマー製DSC装置を用い、50℃から350℃まで20℃/minで昇温し、ポリマーが溶融した時に現れる吸熱ピークのピーク温度(Tm)を測定した。
(Melting point measurement)
Using a Perkin Elmer DSC apparatus, the temperature was raised from 50 ° C. to 350 ° C. at 20 ° C./min, and the endothermic peak temperature (Tm) that appeared when the polymer melted was measured.
(溶融粘度(V6))
フローテスター(島津製作所製高化式フローテスター「CFT−500D型」)を用い
て、温度300℃、荷重1.96MPa、オリフィス長とオリフィス径との、前者/後者
の比が10/1であるオリフィスを使用して6分間保持後の溶融粘度(Pa・s)を測定
した。
(非ニュートン指数測定法)
非ニュートン指数(N値)は、キャピログラフを用いて300℃、オリフィス長(L)とオリフィス径(D)の比、L/D=40の条件下で、剪断速度及び剪断応力を測定し、下記式を用いて算出した。
SR=K・SSN
ただし、SRは剪断速度(秒−1)、SSは剪断応力(ダイン/cm2)、Kは定数を示す。N値は1に近いほどPPS樹脂は線状に近い構造であり、N値が高いほど分岐が進んだ構造であることを示す。
(Melt viscosity (V6))
Using a flow tester (Shimadzu Corporation Koka-type flow tester “CFT-500D type”), the temperature / 300 ° C., the load 1.96 MPa, the orifice length / orifice diameter ratio is 10/1. The melt viscosity (Pa · s) after holding for 6 minutes was measured using an orifice.
(Non-Newton index measurement method)
The non-Newtonian index (N value) was measured by measuring the shear rate and the shear stress using a capillograph at 300 ° C., the ratio of the orifice length (L) to the orifice diameter (D), and L / D = 40. Calculated using the formula.
SR = K · SS N
However, SR represents a shear rate (second −1), SS represents a shear stress (dyne / cm 2), and K represents a constant. The closer the N value is to 1, the closer the PPS resin is to a linear structure, and the higher the N value is, the more branched the structure is.
(反応性評価方法)
PPS樹脂を小型粉砕機で粉砕した後、日本工業規格Z8801の目開き0.5mmの試験用篩いを用いて篩った。篩いを通過したPPS樹脂100質量部に対し、3−グリシドキシプロピルトリメトキシシラン0.5質量部を配合し、均一に混合した後に溶融粘度V6を測定した。添加後の溶融粘度V6/添加前の溶融粘度V6の比から粘度上昇度を倍率として算出した。粘度上昇度が大きいほど反応性が高く、優れていることを示す。
(Reactivity evaluation method)
The PPS resin was pulverized with a small pulverizer and then sieved using a test sieve of Japanese Industrial Standard Z8801 with an aperture of 0.5 mm. With respect to 100 parts by mass of the PPS resin that passed through the sieve, 0.5 part by mass of 3-glycidoxypropyltrimethoxysilane was blended and mixed uniformly, and then the melt viscosity V6 was measured. The degree of increase in viscosity was calculated as a magnification from the ratio of melt viscosity V6 after addition / melt viscosity V6 before addition. The higher the degree of increase in viscosity, the higher the reactivity and the better.
〔製造例1〕
(オリゴフェニレンスルフィドを含むポリフェニレンスルフィド樹脂の製造)
圧力計、温度計、コンデンサ−を連結した撹拌翼付き1リットルオートクレーブに、フレーク状硫化ソーダ(60.3重量%Na2S)129.42gと、N‐メチル‐2‐ピロリドン(NMP)300.0gを仕込んだ。窒素気流下攪拌しながら209℃まで昇温して、水30.96gを留出させた(残存する水分量は硫化ソーダ1モル当り1.13モル)。その後、オートクレーブを密閉して180℃まで冷却し、パラジクロロベンゼン(p−DCB)147.90g及びNMP120.0gを仕込んだ。液温150℃で窒素ガスを用いてゲージ圧で0.1MPaに加圧して昇温を開始した。液温260℃で3時間攪拌しつつ反応を進め、オートクレーブ上部を散水することにより冷却した。次に降温させると共にオートクレーブ上部の冷却を止めた。オートクレーブ上部を冷却中、液温が下がらないように一定に保持した。反応中の最高圧力は、0.85MPaであった。反応後、冷却し、温度170℃の時点でシュウ酸・2水和物1.89g(0.015モル)をNMP0.663kgに含む溶液を加圧注入し、30分間撹拌後、冷却した。
[Production Example 1]
(Production of polyphenylene sulfide resin containing oligophenylene sulfide)
In a 1 liter autoclave with a stirring blade connected with a pressure gauge, a thermometer, and a condenser, 129.42 g of flaked sodium sulfide (60.3% by weight Na 2 S) and N-methyl-2-pyrrolidone (NMP) 300. 0 g was charged. While stirring in a nitrogen stream, the temperature was raised to 209 ° C. to distill 30.96 g of water (the amount of water remaining was 1.13 mol per mol of sodium sulfide). Thereafter, the autoclave was sealed and cooled to 180 ° C., and 147.90 g of paradichlorobenzene (p-DCB) and 120.0 g of NMP were charged. The temperature was raised by pressurizing to 0.1 MPa with a gauge pressure using nitrogen gas at a liquid temperature of 150 ° C. The reaction was allowed to proceed with stirring at a liquid temperature of 260 ° C. for 3 hours, and the upper part of the autoclave was sprinkled to cool it. Next, the temperature was lowered and cooling of the upper part of the autoclave was stopped. The upper part of the autoclave was kept constant during cooling to prevent the liquid temperature from dropping. The maximum pressure during the reaction was 0.85 MPa. After the reaction, the mixture was cooled, and at a temperature of 170 ° C., a solution containing 1.89 g (0.015 mol) of oxalic acid dihydrate in 0.663 kg of NMP was injected under pressure, stirred for 30 minutes, and then cooled.
得られた反応スラリー全量を120℃でろ過し、NMP320gを加えケーキ洗浄ろ過した。NMPろ液量は536gであった。得られた含NMPケーキ全量に70℃のイオン交換水1Lを加えて10分間攪拌した後にろ過し、ろ過後のケーキに70℃のイオン交換水1Lを加えケーキ洗浄を行った。得られた含水ケーキにイオン交換水1Lを加えて10分間攪拌した後にろ過し、ろ過後のケーキに70℃のイオン交換水1Lを加えケーキ洗浄を行った。この操作をもう一度繰り返した後、120℃で4時間乾燥し、溶融粘度(V6)63Pa・s、収量96.9gのPPS樹脂を得た。 The total amount of the obtained reaction slurry was filtered at 120 ° C., 320 g of NMP was added, and the cake was washed and filtered. The amount of NMP filtrate was 536 g. 1 L of 70 ° C. ion-exchanged water was added to the total amount of the NMP-containing cake thus obtained and stirred for 10 minutes, followed by filtration. The cake was washed by adding 1 L of 70 ° C. ion-exchanged water to the cake after filtration. 1 L of ion-exchanged water was added to the obtained water-containing cake and stirred for 10 minutes, followed by filtration. The cake after filtration was added with 1 L of ion-exchanged water at 70 ° C. This operation was repeated once, followed by drying at 120 ° C. for 4 hours to obtain a PPS resin having a melt viscosity (V6) of 63 Pa · s and a yield of 96.9 g.
(オリゴフェニレンスルフィドとCP−MABAを含む反応混合物の回収)
上記NMPろ液536gを1Lナスフラスコに仕込み、ロータリーエバポレーターを用いて、減圧下150℃でNMPを蒸留により除去し、茶色の固形状残渣18.35gを得た。この残渣を150℃真空乾燥機で1時間乾燥した後の重量は7.52g(オリゴフェニレンスルフィド5.09gとNa型CP−MABA2.4320gを含む)で、固形状残渣の不揮発分は41.0wt%であった。ただし、オリゴフェニレンスルフィドとCP−MABAの定量は以下の方法で行った。
(オリゴフェニレンスルフィドとCP−MABAの定量方法)
NMPろ液から回収したオリゴフェニレンスルフィドとCP−MABAを含む反応混合物にクロロホルムとイオン交換水と48%NaOH水溶液を加え、水相をpH13に調整した。オリゴフェニレンスルフィドを抽出したクロロホルム相からクロロホルムを減圧留去することでオリゴフェニレンスルフィドを得た。抽出残渣を150℃真空乾燥機で1時間乾燥した後の重量を秤量することによりオリゴフェニレンスルフィド量を求めた。水相をHPLCで定量することによりCP−MABA量を求めた。
(Recovery of reaction mixture containing oligophenylene sulfide and CP-MABA)
536 g of the NMP filtrate was charged into a 1 L eggplant flask, and NMP was removed by distillation at 150 ° C. under reduced pressure using a rotary evaporator to obtain 18.35 g of a brown solid residue. The weight of this residue after drying for 1 hour in a 150 ° C. vacuum dryer is 7.52 g (including 5.09 g of oligophenylene sulfide and 2.4320 g of Na-type CP-MABA), and the non-volatile content of the solid residue is 41.0 wt. %Met. However, oligophenylene sulfide and CP-MABA were quantified by the following method.
(Quantitative method of oligophenylene sulfide and CP-MABA)
Chloroform, ion-exchanged water, and 48% NaOH aqueous solution were added to the reaction mixture containing oligophenylene sulfide and CP-MABA recovered from the NMP filtrate to adjust the aqueous phase to pH13. From the chloroform phase from which oligophenylene sulfide was extracted, chloroform was distilled off under reduced pressure to obtain oligophenylene sulfide. The amount of oligophenylene sulfide was calculated | required by weighing the weight after drying an extraction residue with a 150 degreeC vacuum dryer for 1 hour. The amount of CP-MABA was determined by quantifying the aqueous phase with HPLC.
〔参考例1〕
(CP−MABAの分離)
製造例1で得られた固形状残渣18.35gとイオン交換水100gを0.5リッターオートクレーブに仕込み、48%NaOH水溶液を添加してpHを10.6に調整し、180℃で60分間撹拌を行った。室温まで冷却した後、ろ過し、ろ過後のケーキに70℃のイオン交換水100gを加えケーキ洗浄を行った。ろ液のpHは10.0で、ろ液中のNa型CP−MABA量は2.4315gで、抽出率は99.98%であった。ケーキ洗浄後のケーキを60℃真空乾燥機で1時間乾燥した後、オリゴフェニレンスルフィド5.09gと、CP−MABA0.0005gを含んだ乳白色の粉末状混合物(A−1)を得た。粉末状混合物(A−1)の融点はTm204℃であった。
[Reference Example 1]
(Separation of CP-MABA)
18.35 g of the solid residue obtained in Production Example 1 and 100 g of ion-exchanged water were charged into a 0.5 liter autoclave, pH was adjusted to 10.6 by adding a 48% NaOH aqueous solution, and the mixture was stirred at 180 ° C. for 60 minutes. Went. After cooling to room temperature, the mixture was filtered, and 100 g of ion exchange water at 70 ° C. was added to the cake after filtration to wash the cake. The pH of the filtrate was 10.0, the amount of Na-type CP-MABA in the filtrate was 2.4315 g, and the extraction rate was 99.98%. The cake after washing the cake was dried with a vacuum dryer at 60 ° C. for 1 hour, and then a milky white powder mixture (A-1) containing 5.09 g of oligophenylene sulfide and 0.0005 g of CP-MABA was obtained. The melting point of the powdery mixture (A-1) was Tm204 ° C.
〔実施例1〕
(酸化性雰囲気下、溶融重合による分岐型PPS樹脂の製造)
上記粉末状混合物(A−1)を3.0g秤量し、テフロン(登録商標)製のシートに挟み、大気雰囲気下の320℃熱風乾燥機で1時間、加熱溶融して、ポリマー化した。室温まで冷却し、分岐型PPS樹脂を得た。得られた分岐型PPS樹脂の融点Tm(℃)、溶融粘度V6(Pa・s)、非ニュートン指数、加熱時重量減少率(%)、反応性(倍率)を表1に示した。
[Example 1]
(Production of branched PPS resin by melt polymerization under oxidizing atmosphere)
3.0 g of the powdery mixture (A-1) was weighed, sandwiched between Teflon (registered trademark) sheets, and heated and melted in a 320 ° C. hot air dryer in an air atmosphere for 1 hour to polymerize. After cooling to room temperature, a branched PPS resin was obtained. Table 1 shows the melting point Tm (° C.), the melt viscosity V6 (Pa · s), the non-Newtonian index, the weight loss rate during heating (%), and the reactivity (magnification) of the obtained branched PPS resin.
〔参考例2〕
(CP−MABAの分離)
「180℃で60分間撹拌」を「170℃で60分間撹拌」としたこと以外は参考例1と同じ操作を行った。ろ液のpHは10.0で、ろ液中のNa型CP−MABA量は2.4223gで、抽出率は99.6%であった。オリゴフェニレンスルフィド5.09gと、CP−MABA0.0097gを含んだ乳白色の粉末状混合物(A−2)を得た。粉末状混合物(A−2)の融点はTm204℃であった。
[Reference Example 2]
(Separation of CP-MABA)
The same operation as in Reference Example 1 was performed except that “stirring at 180 ° C. for 60 minutes” was changed to “stirring at 170 ° C. for 60 minutes”. The pH of the filtrate was 10.0, the amount of Na-type CP-MABA in the filtrate was 2.4223 g, and the extraction rate was 99.6%. A milky white powdery mixture (A-2) containing 5.09 g of oligophenylene sulfide and 0.0097 g of CP-MABA was obtained. The melting point of the powdery mixture (A-2) was Tm204 ° C.
〔実施例2〕
(酸化性雰囲気下、溶融重合による分岐型PPS樹脂の製造)
粉末状混合物(A−1)の代わりに上記粉末状混合物(A−2)を使用した以外は実施例1と同じ操作を行い、分岐型PPS樹脂を得た。得られた分岐型PPS樹脂の融点Tm(℃)、溶融粘度V6(Pa・s)、非ニュートン指数、加熱時重量減少率(%)、反応性(倍率)を表1に示した。
[Example 2]
(Production of branched PPS resin by melt polymerization under oxidizing atmosphere)
A branched PPS resin was obtained in the same manner as in Example 1, except that the powder mixture (A-2) was used instead of the powder mixture (A-1). Table 1 shows the melting point Tm (° C.), the melt viscosity V6 (Pa · s), the non-Newtonian index, the weight loss rate during heating (%), and the reactivity (magnification) of the obtained branched PPS resin.
〔参考例3〕
(CP−MABAの分離)
「180℃で60分間撹拌」を「150℃で10分間撹拌」としたこと以外は参考例1と同じ操作を行った。ろ液のpHは10.0で、ろ液中のNa型CP−MABA量は2.3348gで、抽出率は96%であった。オリゴフェニレンスルフィド5.09gと、CP−MABA0.0972gを含んだ乳白色の粉末状混合物(A−3)を得た。粉末状混合物(A−3)の融点はTm204℃であった。
[Reference Example 3]
(Separation of CP-MABA)
The same operation as in Reference Example 1 was performed except that “stirring at 180 ° C. for 60 minutes” was changed to “stirring at 150 ° C. for 10 minutes”. The pH of the filtrate was 10.0, the amount of Na-type CP-MABA in the filtrate was 2.3348 g, and the extraction rate was 96%. A milky white powdery mixture (A-3) containing 5.09 g of oligophenylene sulfide and 0.0972 g of CP-MABA was obtained. The melting point of the powdery mixture (A-3) was Tm204 ° C.
〔実施例3〕
(酸化性雰囲気下、溶融重合による分岐型PPS樹脂の製造)
粉末状混合物(A−1)の代わりに上記粉末状混合物(A−3)を使用した以外は実施例1と同じ操作を行い、分岐型PPS樹脂を得た。得られた分岐型PPS樹脂の融点Tm(℃)、溶融粘度V6(Pa・s)、非ニュートン指数、加熱時重量減少率(%)、反応性(倍率)を表1に示した。
Example 3
(Production of branched PPS resin by melt polymerization under oxidizing atmosphere)
A branched PPS resin was obtained in the same manner as in Example 1 except that the powder mixture (A-3) was used instead of the powder mixture (A-1). Table 1 shows the melting point Tm (° C.), the melt viscosity V6 (Pa · s), the non-Newtonian index, the weight loss rate during heating (%), and the reactivity (magnification) of the obtained branched PPS resin.
〔参考例4〕
(CP−MABAの分離)
「180℃で60分間撹拌」を「120℃で10分間撹拌」としたこと以外は参考例1と同じ操作を行った。ろ液のpHは10.0で、ろ液中のNa型CP−MABA量は1.8727gで、抽出率は77%であった。オリゴフェニレンスルフィド5.09gと、CP−MABA0.5593gを含んだ乳白色の粉末状混合物(A−4)を得た。粉末状混合物(A−4)の融点はTm196℃であった。
[Reference Example 4]
(Separation of CP-MABA)
The same operation as in Reference Example 1 was performed except that “stirring at 180 ° C. for 60 minutes” was changed to “stirring at 120 ° C. for 10 minutes”. The pH of the filtrate was 10.0, the amount of Na-type CP-MABA in the filtrate was 1.8727 g, and the extraction rate was 77%. A milky white powdery mixture (A-4) containing 5.09 g of oligophenylene sulfide and 0.5593 g of CP-MABA was obtained. The melting point of the powdery mixture (A-4) was Tm196 ° C.
〔実施例4〕
(酸化性雰囲気下、溶融重合による分岐型PPS樹脂の製造)
粉末状混合物(A−1)の代わりに上記粉末状混合物(A−4)を使用した以外は実施例1と同じ操作を行い、分岐型PPS樹脂を得た。得られた分岐型PPS樹脂の融点Tm(℃)、溶融粘度V6(Pa・s)、非ニュートン指数、加熱時重量減少率(%)、反応性(倍率)を表1に示した。
Example 4
(Production of branched PPS resin by melt polymerization under oxidizing atmosphere)
A branched PPS resin was obtained in the same manner as in Example 1 except that the powder mixture (A-4) was used instead of the powder mixture (A-1). Table 1 shows the melting point Tm (° C.), the melt viscosity V6 (Pa · s), the non-Newtonian index, the weight loss rate during heating (%), and the reactivity (magnification) of the obtained branched PPS resin.
〔参考例5〕
(CP−MABAの分離)
「180℃で60分間撹拌」を「100℃で10分間撹拌」としたこと以外は参考例1と同じ操作を行った。ろ液のpHは10.0で、ろ液中のNa型CP−MABA量は1.4325gで、抽出率は58.9%であった。オリゴフェニレンスルフィド5.09gと、CP−MABA0.9995gを含んだ乳白色の粉末状混合物(A−5)を得た。粉末状混合物(A−5)の融点はTm184℃であった。
[Reference Example 5]
(Separation of CP-MABA)
The same operation as in Reference Example 1 was performed except that “stirring at 180 ° C. for 60 minutes” was changed to “stirring at 100 ° C. for 10 minutes”. The pH of the filtrate was 10.0, the amount of Na-type CP-MABA in the filtrate was 1.4325 g, and the extraction rate was 58.9%. A milky white powdery mixture (A-5) containing 5.09 g of oligophenylene sulfide and 0.9995 g of CP-MABA was obtained. The melting point of the powdery mixture (A-5) was Tm184 ° C.
〔実施例5〕
(酸化性雰囲気下、溶融重合による分岐型PPS樹脂の製造)
粉末状混合物(A−1)の代わりに上記粉末状混合物(A−5)を使用した以外は実施例1と同じ操作を行い、分岐型PPS樹脂を得た。得られた分岐型PPS樹脂の融点Tm(℃)、溶融粘度V6(Pa・s)、非ニュートン指数、加熱時重量減少率(%)、反応性(倍率)を表1に示した。
Example 5
(Production of branched PPS resin by melt polymerization under oxidizing atmosphere)
A branched PPS resin was obtained in the same manner as in Example 1, except that the powder mixture (A-5) was used instead of the powder mixture (A-1). Table 1 shows the melting point Tm (° C.), the melt viscosity V6 (Pa · s), the non-Newtonian index, the weight loss rate during heating (%), and the reactivity (magnification) of the obtained branched PPS resin.
〔比較参考例1〕
(CP−MABAの分離)
製造例1で得られた固形状残渣18.35gとイオン交換水100gを0.5リッターオートクレーブに仕込み、pHを調整せず、70℃で10分間撹拌を行った。室温まで冷却した後、ろ過し、ろ過後のケーキに70℃のイオン交換水100gを加えケーキ洗浄を行った。ろ液のpHは3.2で、ろ液中のNa型CP−MABA量は0.5107gで、抽出率は21%であった。ケーキ洗浄後のケーキを60℃真空乾燥機で1時間乾燥した後、オリゴフェニレンスルフィド5.09gと、CP−MABA1.9213gを含んだ茶色の粉末状混合物(A−6)を得た。粉末状混合物(A−6)の融点は明確なピークを示さなかった。
[Comparative Reference Example 1]
(Separation of CP-MABA)
18.35 g of the solid residue obtained in Production Example 1 and 100 g of ion-exchanged water were charged into a 0.5 liter autoclave, and the mixture was stirred at 70 ° C. for 10 minutes without adjusting the pH. After cooling to room temperature, the mixture was filtered, and 100 g of ion exchange water at 70 ° C. was added to the cake after filtration to wash the cake. The pH of the filtrate was 3.2, the amount of Na-type CP-MABA in the filtrate was 0.5107 g, and the extraction rate was 21%. The cake after cake washing was dried with a vacuum dryer at 60 ° C. for 1 hour, and then a brown powdery mixture (A-6) containing 5.09 g of oligophenylene sulfide and 1.9213 g of CP-MABA was obtained. The melting point of the powdery mixture (A-6) did not show a clear peak.
〔比較例1〕
(酸化性雰囲気下、溶融重合によるPPS樹脂の製造)
粉末状混合物(A−1)の代わりに上記粉末状混合物(A−6)を使用した以外は実施例1と同じ操作を行い、PPS樹脂を得た。得られたPPS樹脂の融点Tm(℃)、溶融粘度V6(Pa・s)、非ニュートン指数、加熱時重量減少率(%)、反応性(倍率)を表1に示した。
[Comparative Example 1]
(Production of PPS resin by melt polymerization under oxidizing atmosphere)
A PPS resin was obtained in the same manner as in Example 1 except that the powdery mixture (A-6) was used instead of the powdery mixture (A-1). Table 1 shows the melting point Tm (° C.), melt viscosity V6 (Pa · s), non-Newton's index, weight reduction rate (%) and reactivity (magnification) of the obtained PPS resin.
〔比較参考例2〕
(CP−MABAの分離)
製造例1で得られた固形状残渣18.35gにクロロホルム100gとイオン交換水100gを加え、48%NaOH水溶液を加えて水相をpH13に調整した。オリゴフェニレンスルフィドを抽出したクロロホルム相からクロロホルムを減圧留去した後、固形状残渣に再度クロロホルム10gを加え、室温で溶解した。これをメタノール100gに撹拌しながらゆっくりと滴下し、沈殿物をろ過した。得られたケーキを60℃真空乾燥機で1時間乾燥した後、白色粉末状のオリゴフェニレンスルフィド5.09g(A−7)得た。水相のNa型CP−MABA量は2.4320gで、抽出率は100%であった。粉末状混合物(A−7)の融点はTm204℃であった。
[Comparative Reference Example 2]
(Separation of CP-MABA)
To 18.35 g of the solid residue obtained in Production Example 1, 100 g of chloroform and 100 g of ion-exchanged water were added, and a 48% NaOH aqueous solution was added to adjust the aqueous phase to pH 13. Chloroform was distilled off under reduced pressure from the chloroform phase from which oligophenylene sulfide was extracted, and 10 g of chloroform was again added to the solid residue and dissolved at room temperature. This was slowly added dropwise to 100 g of methanol while stirring, and the precipitate was filtered. The obtained cake was dried in a vacuum dryer at 60 ° C. for 1 hour to obtain 5.09 g (A-7) of a white powder of oligophenylene sulfide. The amount of Na-type CP-MABA in the aqueous phase was 2.4320 g, and the extraction rate was 100%. The melting point of the powdery mixture (A-7) was Tm204 ° C.
〔比較例2〕
(酸化性雰囲気下、溶融重合による分岐型PPS樹脂の製造)
粉末状混合物(A−1)の代わりに上記粉末状混合物(A−7)を使用した以外は実施例1と同じ操作を行い、分岐型PPS樹脂を得た。得られた分岐型PPS樹脂の融点Tm(℃)、溶融粘度V6(Pa・s)、非ニュートン指数、加熱時重量減少率(%)、反応性(倍率)を表1に示した。
[Comparative Example 2]
(Production of branched PPS resin by melt polymerization under oxidizing atmosphere)
A branched PPS resin was obtained in the same manner as in Example 1, except that the powder mixture (A-7) was used instead of the powder mixture (A-1). Table 1 shows the melting point Tm (° C.), the melt viscosity V6 (Pa · s), the non-Newtonian index, the weight loss rate during heating (%), and the reactivity (magnification) of the obtained branched PPS resin.
Claims (6)
前記化合物(1)とオリゴアリーレンスルフィド(2)に加え、さらに該化合物(1)とオリゴアリーレンスルフィド(2)の合計100質量部に対して、50質量部以下の割合でポリアリーレンスルフィド樹脂を含む条件下で溶融重合すること、
前記化合物(1)とオリゴアリーレンスルフィド(2)は、ポリアリーレンスルフィド樹脂の重合工程で精製除去された反応混合物を100℃以上かつpH6以上の水と接触させて得られたものであること、
かつ、前記オリゴアリーレンスルフィド(2)が、下記構造式(2)
を特徴とする分岐型ポリアリーレンスルフィド樹脂の製造方法。
In addition to the compound (1) and the oligoarylene sulfide (2), the polyarylene sulfide resin is further contained at a ratio of 50 parts by mass or less with respect to 100 parts by mass in total of the compound (1) and the oligoarylene sulfide (2). Melt polymerization under conditions,
Before hear compound (1) and oligo arylene sulfide (2) are those obtained polyarylene sulfide reaction mixture was purified removed in the polymerization step of the resin is contacted with 100 ° C. or more and pH6 more water about,
And the said oligo arylene sulfide (2) is following Structural formula (2)
A process for producing a branched polyarylene sulfide resin characterized by
有機極性溶媒中で、ポリハロ芳香族化合物と、(i)アルカリ金属硫化物とを、または、(ii)アルカリ金属水硫化物及びアルカリ金属水酸化物とを反応させて、前記構造式(1)で表される化合物(1)、オリゴアリーレンスルフィド(2)、有機極性溶媒(3)、ポリアリーレンスルフィド(4)及びアルカリ金属ハロゲン化物(5)を含む粗反応混合物を得たのち、該粗反応混合物を有機極性溶媒(6)で洗浄して、ポリアリーレンスルフィド(4)及びアルカリ金属ハロゲン化物(5)を分離除去して、前記化合物(1)、オリゴアリーレンスルフィド(2)および有機極性溶媒(3)を含む反応混合物(a1)を得る工程(1)、
前記反応混合物(a1)から前記有機極性溶媒を固液分離して、前記化合物(1)およびオリゴアリーレンスルフィド(2)を含む反応混合物(a2)を得る工程(2)、
反応混合物(a2)を100℃超かつpH6以上で、水と接触させることにより、前記構造式(1)で表される化合物(1)とオリゴアリーレンスルフィド(2)とを分離する工程(3)、
分離したオリゴアリーレンスルフィド(2)を回収する工程(4)によって得られたものである請求項1〜3の何れか一項記載の分岐型ポリアリーレンスルフィド樹脂の製造方法。 Before hear compound (1) and oligo arylene sulfide (2)
In an organic polar solvent, the structural formula (1) is obtained by reacting a polyhaloaromatic compound with (i) an alkali metal sulfide or (ii) an alkali metal hydrosulfide and an alkali metal hydroxide. After obtaining a crude reaction mixture containing the compound (1), oligoarylene sulfide (2), organic polar solvent (3), polyarylene sulfide (4) and alkali metal halide (5) represented by The mixture is washed with an organic polar solvent (6) to separate and remove the polyarylene sulfide (4) and the alkali metal halide (5), and the compound (1), the oligoarylene sulfide (2) and the organic polar solvent ( A step (1) of obtaining a reaction mixture (a1) comprising 3),
(2) a step of solid-liquid separation of the organic polar solvent from the reaction mixture (a1) to obtain a reaction mixture (a2) containing the compound (1) and oligoarylene sulfide (2);
A step (3) of separating the compound (1) represented by the structural formula (1) and the oligoarylene sulfide (2) by contacting the reaction mixture (a2) with water at a temperature higher than 100 ° C. and pH 6 or higher. ,
The method for producing a branched polyarylene sulfide resin according to any one of claims 1 to 3, which is obtained by the step (4) of recovering the separated oligoarylene sulfide (2).
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