JPH0224868B2 - - Google Patents
Info
- Publication number
- JPH0224868B2 JPH0224868B2 JP21909787A JP21909787A JPH0224868B2 JP H0224868 B2 JPH0224868 B2 JP H0224868B2 JP 21909787 A JP21909787 A JP 21909787A JP 21909787 A JP21909787 A JP 21909787A JP H0224868 B2 JPH0224868 B2 JP H0224868B2
- Authority
- JP
- Japan
- Prior art keywords
- parts
- polymer
- carbon black
- group
- groups
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 229920000642 polymer Polymers 0.000 claims description 64
- 239000006229 carbon black Substances 0.000 claims description 45
- 229920000578 graft copolymer Polymers 0.000 claims description 34
- 238000006243 chemical reaction Methods 0.000 claims description 21
- 125000003504 2-oxazolinyl group Chemical group O1C(=NCC1)* 0.000 claims description 14
- 238000004519 manufacturing process Methods 0.000 claims description 12
- 238000003756 stirring Methods 0.000 claims description 10
- 125000004069 aziridinyl group Chemical group 0.000 claims description 8
- 238000002156 mixing Methods 0.000 claims description 7
- 239000000178 monomer Substances 0.000 description 23
- 238000000034 method Methods 0.000 description 21
- 239000000203 mixture Substances 0.000 description 16
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 12
- 239000000126 substance Substances 0.000 description 12
- 239000000243 solution Substances 0.000 description 10
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 9
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 9
- 150000001875 compounds Chemical class 0.000 description 9
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical group OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 9
- 238000006116 polymerization reaction Methods 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 229920002554 vinyl polymer Polymers 0.000 description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 5
- 239000002202 Polyethylene glycol Substances 0.000 description 5
- 238000007664 blowing Methods 0.000 description 5
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 5
- 229910001873 dinitrogen Inorganic materials 0.000 description 5
- 238000005259 measurement Methods 0.000 description 5
- 229920001223 polyethylene glycol Polymers 0.000 description 5
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 4
- FQPSGWSUVKBHSU-UHFFFAOYSA-N methacrylamide Chemical compound CC(=C)C(N)=O FQPSGWSUVKBHSU-UHFFFAOYSA-N 0.000 description 4
- 239000003960 organic solvent Substances 0.000 description 4
- 229920000728 polyester Polymers 0.000 description 4
- 239000004793 Polystyrene Substances 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 239000006185 dispersion Substances 0.000 description 3
- 125000000524 functional group Chemical group 0.000 description 3
- 229920000570 polyether Polymers 0.000 description 3
- 229920002223 polystyrene Polymers 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- 239000000725 suspension Substances 0.000 description 3
- 125000000391 vinyl group Chemical class [H]C([*])=C([H])[H] 0.000 description 3
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2-(2-cyanopropan-2-yldiazenyl)-2-methylpropanenitrile Chemical compound N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 description 2
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 2
- LPIQIQPLUVLISR-UHFFFAOYSA-N 2-prop-1-en-2-yl-4,5-dihydro-1,3-oxazole Chemical compound CC(=C)C1=NCCO1 LPIQIQPLUVLISR-UHFFFAOYSA-N 0.000 description 2
- JLBJTVDPSNHSKJ-UHFFFAOYSA-N 4-Methylstyrene Chemical compound CC1=CC=C(C=C)C=C1 JLBJTVDPSNHSKJ-UHFFFAOYSA-N 0.000 description 2
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 description 2
- 239000004342 Benzoyl peroxide Substances 0.000 description 2
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical compound C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-N 0.000 description 2
- SOGAXMICEFXMKE-UHFFFAOYSA-N Butylmethacrylate Chemical compound CCCCOC(=O)C(C)=C SOGAXMICEFXMKE-UHFFFAOYSA-N 0.000 description 2
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 2
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 2
- BAPJBEWLBFYGME-UHFFFAOYSA-N Methyl acrylate Chemical compound COC(=O)C=C BAPJBEWLBFYGME-UHFFFAOYSA-N 0.000 description 2
- NTIZESTWPVYFNL-UHFFFAOYSA-N Methyl isobutyl ketone Chemical compound CC(C)CC(C)=O NTIZESTWPVYFNL-UHFFFAOYSA-N 0.000 description 2
- UIHCLUNTQKBZGK-UHFFFAOYSA-N Methyl isobutyl ketone Natural products CCC(C)C(C)=O UIHCLUNTQKBZGK-UHFFFAOYSA-N 0.000 description 2
- WHNWPMSKXPGLAX-UHFFFAOYSA-N N-Vinyl-2-pyrrolidone Chemical compound C=CN1CCCC1=O WHNWPMSKXPGLAX-UHFFFAOYSA-N 0.000 description 2
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 2
- 239000004721 Polyphenylene oxide Substances 0.000 description 2
- 125000003277 amino group Chemical group 0.000 description 2
- ROOXNKNUYICQNP-UHFFFAOYSA-N ammonium persulfate Chemical compound [NH4+].[NH4+].[O-]S(=O)(=O)OOS([O-])(=O)=O ROOXNKNUYICQNP-UHFFFAOYSA-N 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 235000019400 benzoyl peroxide Nutrition 0.000 description 2
- CQEYYJKEWSMYFG-UHFFFAOYSA-N butyl acrylate Chemical compound CCCCOC(=O)C=C CQEYYJKEWSMYFG-UHFFFAOYSA-N 0.000 description 2
- 239000003086 colorant Substances 0.000 description 2
- 239000008367 deionised water Substances 0.000 description 2
- 229910021641 deionized water Inorganic materials 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229920001971 elastomer Polymers 0.000 description 2
- 125000003700 epoxy group Chemical group 0.000 description 2
- 229920001519 homopolymer Polymers 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- 239000000976 ink Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000012778 molding material Substances 0.000 description 2
- 238000010137 moulding (plastic) Methods 0.000 description 2
- BSCJIBOZTKGXQP-UHFFFAOYSA-N n-(2-hydroxyethyl)-2-methylprop-2-enamide Chemical compound CC(=C)C(=O)NCCO BSCJIBOZTKGXQP-UHFFFAOYSA-N 0.000 description 2
- 229920000620 organic polymer Polymers 0.000 description 2
- 239000003973 paint Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 230000000379 polymerizing effect Effects 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- CWERGRDVMFNCDR-UHFFFAOYSA-N thioglycolic acid Chemical compound OC(=O)CS CWERGRDVMFNCDR-UHFFFAOYSA-N 0.000 description 2
- YVLJEXBGMVDKBR-UHFFFAOYSA-N 1,10-dichloro-7-methyldec-1-ene Chemical compound ClCCCC(C)CCCCC=CCl YVLJEXBGMVDKBR-UHFFFAOYSA-N 0.000 description 1
- BOVQCIDBZXNFEJ-UHFFFAOYSA-N 1-chloro-3-ethenylbenzene Chemical compound ClC1=CC=CC(C=C)=C1 BOVQCIDBZXNFEJ-UHFFFAOYSA-N 0.000 description 1
- KTZVZZJJVJQZHV-UHFFFAOYSA-N 1-chloro-4-ethenylbenzene Chemical compound ClC1=CC=C(C=C)C=C1 KTZVZZJJVJQZHV-UHFFFAOYSA-N 0.000 description 1
- NVZWEEGUWXZOKI-UHFFFAOYSA-N 1-ethenyl-2-methylbenzene Chemical compound CC1=CC=CC=C1C=C NVZWEEGUWXZOKI-UHFFFAOYSA-N 0.000 description 1
- JZHGRUMIRATHIU-UHFFFAOYSA-N 1-ethenyl-3-methylbenzene Chemical compound CC1=CC=CC(C=C)=C1 JZHGRUMIRATHIU-UHFFFAOYSA-N 0.000 description 1
- QEDJMOONZLUIMC-UHFFFAOYSA-N 1-tert-butyl-4-ethenylbenzene Chemical compound CC(C)(C)C1=CC=C(C=C)C=C1 QEDJMOONZLUIMC-UHFFFAOYSA-N 0.000 description 1
- SUUSNDZEWZWPSK-UHFFFAOYSA-N 2-(aziridin-1-yl)-4,5-dihydro-1,3-oxazole Chemical compound C1CN1C1=NCCO1 SUUSNDZEWZWPSK-UHFFFAOYSA-N 0.000 description 1
- XEZCCHVCBAZAQD-UHFFFAOYSA-N 2-(aziridin-1-yl)ethyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCCN1CC1 XEZCCHVCBAZAQD-UHFFFAOYSA-N 0.000 description 1
- GOXQRTZXKQZDDN-UHFFFAOYSA-N 2-Ethylhexyl acrylate Chemical compound CCCCC(CC)COC(=O)C=C GOXQRTZXKQZDDN-UHFFFAOYSA-N 0.000 description 1
- CCJAYIGMMRQRAO-UHFFFAOYSA-N 2-[4-[(2-hydroxyphenyl)methylideneamino]butyliminomethyl]phenol Chemical compound OC1=CC=CC=C1C=NCCCCN=CC1=CC=CC=C1O CCJAYIGMMRQRAO-UHFFFAOYSA-N 0.000 description 1
- ISRGONDNXBCDBM-UHFFFAOYSA-N 2-chlorostyrene Chemical compound ClC1=CC=CC=C1C=C ISRGONDNXBCDBM-UHFFFAOYSA-N 0.000 description 1
- LFKGHGICJZFGIS-UHFFFAOYSA-N 2-cyclohexyl-n-hydroxyprop-2-enamide Chemical compound ONC(=O)C(=C)C1CCCCC1 LFKGHGICJZFGIS-UHFFFAOYSA-N 0.000 description 1
- BQBSIHIZDSHADD-UHFFFAOYSA-N 2-ethenyl-4,5-dihydro-1,3-oxazole Chemical compound C=CC1=NCCO1 BQBSIHIZDSHADD-UHFFFAOYSA-N 0.000 description 1
- NVADAERBBAQCLW-UHFFFAOYSA-N 2-ethenyl-4-ethyl-4,5-dihydro-1,3-oxazole Chemical compound CCC1COC(C=C)=N1 NVADAERBBAQCLW-UHFFFAOYSA-N 0.000 description 1
- PBYIFPWEHGSUEY-UHFFFAOYSA-N 2-ethenyl-4-methyl-4,5-dihydro-1,3-oxazole Chemical compound CC1COC(C=C)=N1 PBYIFPWEHGSUEY-UHFFFAOYSA-N 0.000 description 1
- HFRTWUSGUFBWTL-UHFFFAOYSA-N 2-ethenyl-5-ethyl-4,5-dihydro-1,3-oxazole Chemical compound CCC1CN=C(C=C)O1 HFRTWUSGUFBWTL-UHFFFAOYSA-N 0.000 description 1
- HMEVYZZCEGUONQ-UHFFFAOYSA-N 2-ethenyl-5-methyl-4,5-dihydro-1,3-oxazole Chemical compound CC1CN=C(C=C)O1 HMEVYZZCEGUONQ-UHFFFAOYSA-N 0.000 description 1
- WDQMWEYDKDCEHT-UHFFFAOYSA-N 2-ethylhexyl 2-methylprop-2-enoate Chemical compound CCCCC(CC)COC(=O)C(C)=C WDQMWEYDKDCEHT-UHFFFAOYSA-N 0.000 description 1
- CTHJQRHPNQEPAB-UHFFFAOYSA-N 2-methoxyethenylbenzene Chemical compound COC=CC1=CC=CC=C1 CTHJQRHPNQEPAB-UHFFFAOYSA-N 0.000 description 1
- RUMACXVDVNRZJZ-UHFFFAOYSA-N 2-methylpropyl 2-methylprop-2-enoate Chemical compound CC(C)COC(=O)C(C)=C RUMACXVDVNRZJZ-UHFFFAOYSA-N 0.000 description 1
- CFVWNXQPGQOHRJ-UHFFFAOYSA-N 2-methylpropyl prop-2-enoate Chemical compound CC(C)COC(=O)C=C CFVWNXQPGQOHRJ-UHFFFAOYSA-N 0.000 description 1
- WYYZXZICJOSDSB-UHFFFAOYSA-N 4,5-dimethyl-2-prop-1-en-2-yl-4,5-dihydro-1,3-oxazole Chemical compound CC1OC(C(C)=C)=NC1C WYYZXZICJOSDSB-UHFFFAOYSA-N 0.000 description 1
- PTTDUFDXZBSJTM-UHFFFAOYSA-N 4-ethyl-2-prop-1-en-2-yl-4,5-dihydro-1,3-oxazole Chemical compound CCC1COC(C(C)=C)=N1 PTTDUFDXZBSJTM-UHFFFAOYSA-N 0.000 description 1
- NNBLOUMFYMUBHQ-UHFFFAOYSA-N 4-ethyl-n-hydroxy-2-methylideneoctanamide Chemical compound CCCCC(CC)CC(=C)C(=O)NO NNBLOUMFYMUBHQ-UHFFFAOYSA-N 0.000 description 1
- MBLQIMSKMPEILU-UHFFFAOYSA-N 4-methyl-2-prop-1-en-2-yl-4,5-dihydro-1,3-oxazole Chemical compound CC1COC(C(C)=C)=N1 MBLQIMSKMPEILU-UHFFFAOYSA-N 0.000 description 1
- IRHWINGBSHBXAD-UHFFFAOYSA-N 5-ethyl-2-prop-1-en-2-yl-4,5-dihydro-1,3-oxazole Chemical compound CCC1CN=C(C(C)=C)O1 IRHWINGBSHBXAD-UHFFFAOYSA-N 0.000 description 1
- OEIDKVHIXLGFQK-UHFFFAOYSA-N 5-methyl-2-prop-1-en-2-yl-4,5-dihydro-1,3-oxazole Chemical compound CC1CN=C(C(C)=C)O1 OEIDKVHIXLGFQK-UHFFFAOYSA-N 0.000 description 1
- JTHZUSWLNCPZLX-UHFFFAOYSA-N 6-fluoro-3-methyl-2h-indazole Chemical compound FC1=CC=C2C(C)=NNC2=C1 JTHZUSWLNCPZLX-UHFFFAOYSA-N 0.000 description 1
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 1
- JIGUQPWFLRLWPJ-UHFFFAOYSA-N Ethyl acrylate Chemical compound CCOC(=O)C=C JIGUQPWFLRLWPJ-UHFFFAOYSA-N 0.000 description 1
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 1
- 239000004372 Polyvinyl alcohol Substances 0.000 description 1
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- XYLMUPLGERFSHI-UHFFFAOYSA-N alpha-Methylstyrene Chemical compound CC(=C)C1=CC=CC=C1 XYLMUPLGERFSHI-UHFFFAOYSA-N 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 229910001870 ammonium persulfate Inorganic materials 0.000 description 1
- 238000012662 bulk polymerization Methods 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000004040 coloring Methods 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- GMSCBRSQMRDRCD-UHFFFAOYSA-N dodecyl 2-methylprop-2-enoate Chemical compound CCCCCCCCCCCCOC(=O)C(C)=C GMSCBRSQMRDRCD-UHFFFAOYSA-N 0.000 description 1
- 239000000806 elastomer Substances 0.000 description 1
- 238000007720 emulsion polymerization reaction Methods 0.000 description 1
- SUPCQIBBMFXVTL-UHFFFAOYSA-N ethyl 2-methylprop-2-enoate Chemical compound CCOC(=O)C(C)=C SUPCQIBBMFXVTL-UHFFFAOYSA-N 0.000 description 1
- 238000010528 free radical solution polymerization reaction Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- IQPQWNKOIGAROB-UHFFFAOYSA-N isocyanate group Chemical group [N-]=C=O IQPQWNKOIGAROB-UHFFFAOYSA-N 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- PBOSTUDLECTMNL-UHFFFAOYSA-N lauryl acrylate Chemical compound CCCCCCCCCCCCOC(=O)C=C PBOSTUDLECTMNL-UHFFFAOYSA-N 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 125000000956 methoxy group Chemical group [H]C([H])([H])O* 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003607 modifier Substances 0.000 description 1
- UUORTJUPDJJXST-UHFFFAOYSA-N n-(2-hydroxyethyl)prop-2-enamide Chemical compound OCCNC(=O)C=C UUORTJUPDJJXST-UHFFFAOYSA-N 0.000 description 1
- TVDRFWWLJYRVMV-UHFFFAOYSA-N n-(4-hydroxybutyl)-2-methylprop-2-enamide Chemical compound CC(=C)C(=O)NCCCCO TVDRFWWLJYRVMV-UHFFFAOYSA-N 0.000 description 1
- YBWQZBVPWXXJKQ-UHFFFAOYSA-N n-(4-hydroxybutyl)prop-2-enamide Chemical compound OCCCCNC(=O)C=C YBWQZBVPWXXJKQ-UHFFFAOYSA-N 0.000 description 1
- DNTMQTKDNSEIFO-UHFFFAOYSA-N n-(hydroxymethyl)-2-methylprop-2-enamide Chemical compound CC(=C)C(=O)NCO DNTMQTKDNSEIFO-UHFFFAOYSA-N 0.000 description 1
- YOWXYQUBAKXMRO-UHFFFAOYSA-N n-hydroxy-4-methyl-2-methylidenepentanamide Chemical compound CC(C)CC(=C)C(=O)NO YOWXYQUBAKXMRO-UHFFFAOYSA-N 0.000 description 1
- HMZGPNHSPWNGEP-UHFFFAOYSA-N octadecyl 2-methylprop-2-enoate Chemical compound CCCCCCCCCCCCCCCCCCOC(=O)C(C)=C HMZGPNHSPWNGEP-UHFFFAOYSA-N 0.000 description 1
- 125000002347 octyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- HDBWAWNLGGMZRQ-UHFFFAOYSA-N p-Vinylbiphenyl Chemical compound C1=CC(C=C)=CC=C1C1=CC=CC=C1 HDBWAWNLGGMZRQ-UHFFFAOYSA-N 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- PNJWIWWMYCMZRO-UHFFFAOYSA-N pent‐4‐en‐2‐one Natural products CC(=O)CC=C PNJWIWWMYCMZRO-UHFFFAOYSA-N 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 238000012643 polycondensation polymerization Methods 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000012673 precipitation polymerization Methods 0.000 description 1
- NHARPDSAXCBDDR-UHFFFAOYSA-N propyl 2-methylprop-2-enoate Chemical compound CCCOC(=O)C(C)=C NHARPDSAXCBDDR-UHFFFAOYSA-N 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000010526 radical polymerization reaction Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 239000012744 reinforcing agent Substances 0.000 description 1
- 239000012763 reinforcing filler Substances 0.000 description 1
- 238000001226 reprecipitation Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 238000010558 suspension polymerization method Methods 0.000 description 1
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
- Polymerisation Methods In General (AREA)
- Graft Or Block Polymers (AREA)
- Pigments, Carbon Blacks, Or Wood Stains (AREA)
Description
(産業上の利用分野)
本発明は新規のカーボンブラツクグラフトポリ
マー及びその製造方法に関する。更に詳しくは、
カーボンブラツク(以下CBという。)に特定の反
応性基を有する重合体が反応してなり、インキ、
複写機用トナー、塗料、プラスチツク成形材料等
の着色剤、或いは各種高分子の改質等として有用
な新規のカーボンブラツクグラフトポリマー及び
その製造方法に関する。
(従来の技術)
CBは着色性、導電性、耐侯性、耐薬品性等に
優れる為、例えばプラスチツクやエラストマーの
補強剤、充填剤等種々の目的で巾広く使用されて
いる。しかし、CBは、その形状が粉状又は粒状
の為、単独で使用されることが少なく、通常、ゴ
ムや樹脂等の固状の基材又は水や溶剤等の液体に
均一に分散されてその特性を発揮する。
しかし、CBは粒子間の凝集力に比べて他の物
質、例えば有機高分子、水及び有機溶剤等との親
和力が弱い為、通常の混合又は分散条件では、均
一に混合又は分散することが極めて困難であつ
た。
この問題を解決する為に、CB表面を各種の界
面活性剤や樹脂で被覆して、固状又は液状の基材
との親和性を高めることにより、CBの分散性を
改良する検討が数多くなされている。
中でも、重合性単量体をCB共存中で重合させ
ることにより得られるカーボンブラツクグラフト
ポリマーは、重合性単量体の種類を適当に選択す
ることにより、親水性及び/又は親油性を適宜、
変えることができる為、近年注目を浴びている。
このカーボンブラツクグラフトポリマーを製造
する方法としては、例えば特公昭42−22047号、
特公昭44−3826号、特公昭45−17248号、特公昭
46−26970号により開示されているが、これらの
方法で得られるカーボンブラツクグラフトポリマ
ーの収率は数%〜10数%と低く、大半はビニル系
ホモポリマーの形で存在し、CBの表面処理効率
の極めて悪いものであつた。この為、他の物質と
の親和性は期待した程には改良されず、混合又は
分散条件によつて分散状態が異なる場合が多々あ
つた。
(発明が解決しようとする問題)
本発明者等は、このような現状に鑑み鋭意検討
を行つた結果、特定の反応性基を分子内に有する
重合体がCBの表面官能基と極めて効率良く反応
し、得られたカーボンブラツクグラフトポリマー
は各種の物質への分散性が著しく優れていると共
に、該反応時の条件を特定することにより分散性
が一段と高められたカーボンブラツクグラフトポ
リマーが簡便に得られる事を見出し本発明を完成
するに至つた。
(問題点を解決する為の手段)
本発明はCBに100重量部に対し、分子内にアジ
リジン基、オキサゾリン基及びN−ヒドロキシア
ルキルアミド基よりなる群から選ばれる1種又は
2種以上の反応性基を有する重合体(以下、反応
性基を有する重合体(A)という。)が1〜3000重量
部の割合で反応してなることを特徴とするカーボ
ンブラツクグラフトポリマー及びCBと反応性基
を有する重合体(A)を常温〜350℃の反応温度条件
下で撹拌混合することを特徴とするカーボンブラ
ツクグラフトポリマーの製造方法に係わるもので
ある。
本発明における反応性基を有する重合体(A)はア
ジリジン基、オキサゾリン基、及びN−ヒドロキ
シアルキルアミド基から選ばれる1種又は2種以
上の反応性基を分子内に有するビニル系重合体、
ポリエステル、ポリエーテル等である。CBの表
面に存在する官能基と反応しうる基としては必ず
しもこれら反応性基のみに限られるものではない
が、これら反応性基以外の基を有する重合体を用
いる場合は使用できるCBの種類に制限を受けた
り、反応に先立つてCBを予め処理しておく工程
を必要とする。CBとの反応に際し、前記反応性
基を有する重合体(A)を用いる意義は、使用する
CBの種類や状態に関わらず、温和な反応条件に
おいてもCBと重合体(A)とが非常に高いグラフト
効率で反応し、各種物質への分散性に著しく優れ
たカーボンブラツクグラフトポリマーが得られる
ところにある。
反応性基を有する重合体(A)を得る方法としては
例えば、
前記の反応性基を分子内に有する重合性単量
体(a)(以下、単量体(a)という。)を必要により
その他の重合性単量体(b)(以下、単量体(b)とい
う。)と重合する方法、
前記の反応性基を分子内に有する化合物(c)を
該化合物(c)(以下、化合物(c)という。)と反応
しうる基を有する重合体(d)(以下、重合体(d)と
いう。)に反応させて前記反応性基を該重合体
(d)に導入する方法、
等を挙げることができ、これらの方法をその使用
目的に応じて適宜採用することができる。
の方法において使用できる単量体(a)として
は、例えば
等で表わされるアジリジン基含有重合性単量体;
2−ビニル−2−オキサゾリン、2−ビニル−4
−メチル−2−オキサゾリン、2−ビニル−5−
メチル−2−オキサゾリン、2−ビニル−4−エ
チル−2−オキサゾリン、2−ビニル−5−エチ
ル−2−オキサゾリン、2−イソプロペニル−2
−オキサゾリン、2−イソプロペニル−4−メチ
ル−2−オキサゾリン、2−イソプロペニル−5
−メチル−2−オキサゾリン、2−イソプロペニ
ル−4−エチル−2−オキサゾリン、2−イソプ
ロペニル−5−エチル−2−オキサゾリン、2−
イソプロペニル−4,5−ジメチル−2−オキサ
ゾリンなどのオキサゾリン基含有重合性単量体
類;N−ヒドロキシメチルアクリルアミド、N−
ヒドロキシエチルアクリルアミド、N−ヒドロキ
シブチルアクリルアミド、N−ヒドロキシイソブ
チルアクリルアミド、N−ヒドロキシ−2−エチ
ルヘキシルアクリルアミド、N−ヒドロキシシク
ロヘキシルアクリルアミド、N−ヒドロキシメチ
ルメタクリルアミド、N−ヒドロキシエチルメタ
クリルアミド、N−ヒドロキシブチルメタクリル
アミド、N−ヒドロキシイソブチルメタクリルア
ミド、N−ヒドロキシ−2−エチルヘキシルメタ
クリルアミド、N−ヒドロキシシクロヘキシルメ
タクリルアミドなどのN−ヒドロキシアルキルア
ミド基含有重合性単量体等を挙げることができこ
れらの群から選ばれる1種又は2種以上を使用す
ることができる。
の方法において必要により使用できる単量体
(b)としては、単量体(a)と共重合しうるものであれ
は特に制限されず、例えばスチレン、o−メチル
スチレン、m−メチルスチレン、p−メチルスチ
レン、α−メチルスチレン、p−メトキシスチレ
ン、p−tert−ブチルスチレン、p−フエニルス
チレン、o−クロルスチレン、m−クロルスチレ
ン、p−クロルスチレン等のスチレン系モノマ
ー;アクリル酸、アクリル酸メチル、アクリル酸
エチル、アクリル酸n−ブチル、アクリル酸イソ
ブチル、アクリル酸ドデシル、アクリル酸ステア
リル、アクリル酸2−エチルヘキシル、メタクリ
ル酸、メタクリル酸メチル、メタクリル酸エチ
ル、メタクリル酸プロピル、メタクリル酸n−ブ
チル、メタクリル酸イソブチル、メタクリル酸n
−オクチル、メタクリル酸ドデシル、メタクリル
酸2−エチルヘキシル、メタクリル酸ステアリル
等のアクリル酸あるいはメタクリル酸系モノマ
ー;エチレン、プロピレン、ブチレン、塩化ビニ
ル、酢酸ビニル、アクリロニトリル、アクリルア
ミド、メタクリルアミド、N−ビニルピロリドン
等が挙げられ、これらの1種又は2種以上を用い
ることができる。
の方法により反応性基を有する重合体(A)を得
るには、単量体(a)を必要により用いる単量体(b)と
従来公知の重合方法、例えば塊状重合法、懸濁重
合法、乳化重合法、沈澱重合法、溶液重合法等に
よつて重合すればよい。
の方法において使用できる化合物(c)として
は、例えば
(2‐1 ) 前記反応性基の1種を分子内に2個以
上有する化合物
(2‐2 ) 前記反応性基の2種以上を分子内に有
する化合物
(2‐3 ) 前記反応性基の1種以上と前記反応性
基以外の基とを分子内に有する化合物
等を挙げる事ができる。但し、(2−3)項に記
載の前記反応性基以外の基とはアジリジン基、オ
キサゾリン基及びN−ヒドロキシアルキルアミド
基以外のものであつて、かつ後述の重合体(d)に含
まれる基と反応しうるものであり、例えばイソシ
アネート基、エポキシ基、アミノ基、カルボキシ
ル基、ヒドロキシル基、ビニル基等がこれに該当
するものである。
の方法における重合体(d)とは、前記(2−
1)〜(2−3)項に記載した化合物(c)と反応し
うる基を有するビニル系重合体、ポリエステル、
ポリエーテル等である。化合物(c)と反応しうる基
としては、例えばヒドロキシル基、カルボキシル
基、アミノ基、エポキシ基等を挙げることがで
き、これらの基を有する重合体(d)はラジカル重
合、縮重合等の公知の重合手順で容易に得ること
ができる。
の方法により反応性基を有する重合体(A)を得
るには、化合物(c)と重合体(d)とを前記反応性基の
少なくとも1個が未反応で残存する条件を選択し
て反応すればよい。
本発明において、反応性基を有する重合体(A)は
カーボンブラツクグラフトポリマーに付与すべき
性質、例えば親水性、親油性又はその他の親和性
等に応じて適宜選択され、例えば親水性を付与す
べき場合にはアクリル酸を主成分とするビニル系
重合体やポリエーテル等が、又親油性を付与すべ
き場合にはスチレンを主成分とするビニル系重合
体やポリエステル等が好適に用いられる。反応性
基を有する重合体(A)の分子量については特に制限
されないが、CBに対する顕著な処理効果やCBと
の反応時の作業性の面で平均分子量が200〜
1000000の範囲とするのが好ましく、より好まし
くは300〜100000の範囲である。
本発明のカーボンブラツクグラフトポリマー
は、CBに反応性基を有する重合体(A)が反応して
なり、該重合体(A)がCBに極めて高い効率でグラ
フト結合したものである。その反応は種々の方法
によることができる。例えば、前記したやの
方法により得られた反応性基を有する重合体(A)を
CBに反応する方法によつてもよく、CBの存在下
にやの方法を実施して反応性基を有する重合
体(A)を得る工程と該重合体(A)とCBとの反応の工
程を一つにまとめてもよい。但し、高いグラフト
効率でカーボンブラツクグラフトポリマーを得る
には前者の方法によるのが好ましい。
反応に際し、反応性基を有する重合体(A)の使用
量はCB100重量部に対し1〜3000重量部の割合と
する。
本発明は、更に各種物質への分散性が一段と高
められたカーボンブラツクグラフトポリマーを簡
便に得るための製造方法も提供するものである。
この様な製造方法はCBと反応性基を有する重合
体(A)とを常温〜350℃の温度条件下に撹拌混合し
て反応することにより達成される。本発明の製造
方法によれば、原料に用いた二次凝集状態にある
CBが撹拌混合して反応する際に効率良く解砕さ
れて微細且つ均一な粒子径となりしかも反応の効
率も向上するので、得られたカーボンブラツクグ
ラフトポリマーは特性が一段と高められたもので
ある。反応時の温度条件が350℃を越える場合は
ポリマー成分が変質するので好ましくない。
本発明の製造方法において、CBと反応性基を
有する重合体(A)との反応は、これら二成分だけを
反応する方法であつてもよく、又反応性基を有す
る重合体(A)に該当しないポリマー成分、重合性単
量体、有機溶剤、水等他の物質の混在下での反応
であつてもよい。本発明の製造方法の実施態様を
具体的に示す一例としては、例えばCB100重量部
に対し、反応性基を有する重合体(A)1重量部〜
3000重量部、好ましくは5重量部〜1000重量部、
反応性基を有しないポリマー0重量部〜1000重量
部、重合性単量体0重量部〜200重量部及び有機
溶剤0重量部〜1000重量部を配合してなる混合物
を、常温〜350℃、好ましくは50℃〜250℃の温度
条件下に撹拌混合して本発明のカーボンブラツク
グラフトポリマーを得る。
(発明の効果)
本発明のカーボンブラツクグラフトポリマー
は、CBに反応性基を有する重合体(A)が反応して
なり、該重合体(A)中の反応性基がCBの表面官能
基と高い反応性を有するために、該重合体(A)成分
が高い効率でCB表面にグラフト化されたもので
ある。そして、本発明において規定された反応性
基を有するものであれば重合体(A)の組成、種類等
は任意に選択することができるために、目的に応
じて種種の特性をCBに付与することが可能であ
る。そして、こうして得られるカーボンブラツク
グラフトポリマーは、種々の物質との親和性が改
良されており、例えば有機高分子、水、有機溶剤
等の物質への分散性が著しく優れているために、
インキ、複写機用トナー、塗料、プラスチツク成
形材料等の着色剤や各種高分子の改質剤等に好適
に使用できる。また、本発明の製造方法によれ
ば、分散性を始めとする前記特徴が一段と高めら
れたカーボンブラツクグラフトポリマーがCBに
反応性基を有する重合体(A)を加熱下に単に撹拌混
合するだけという簡便な操作で製造できる。した
がつて、本発明のカーボンブラツクグラフトポリ
マーの製造方法は、産業上極めて有用なものであ
る。
(実施例)
以下、実施例により本発明を詳細に説明する
が、本発明は以下の実施例によつて限定されるも
のではない。尚、例中の部は重量部を、%は重量
%をそれぞれ示す。
実施例 1
撹拌機、不活性ガス導入管、還流冷却管及び温
度計を備えたフラスコにポリビニルアルコール
0.2部を溶解した脱イオン水400部を仕込んだ。そ
こへ予め調整しておいたスチレン196部およびイ
ソプロペニルオキサゾリン4部からなる重合性単
量体にベンゾイルパーオキサイド16部を溶解した
混合物を仕込み、高速で撹拌した均一な懸濁液と
した。次いで窒素ガスを吹き込みながら80℃に加
熱し、この温度で5時間撹拌を続けて重合反応を
行つた後冷却して重合体懸濁液を得た。この重合
体懸濁液をロ過、洗浄した後乾燥して反応性基と
してオキサゾリン基を有する重合体を得た。この
重合体の分子量はGPC測定によりMn=5800であ
つた。
反応性基としてオキサゾリン基を有する重合体
40部とカーボンブラツクMA−600(三菱化成工業
(株)製)20部とをラボプラストミル(東洋精機(株)
製)を用いて160℃、100rpmの条件下に混練して
反応した後冷却、粉砕してカーボンブラツクグラ
フトポリマー(1)を得た。
実施例 2
実施例1で用いたのと同じフラスコにトルエン
200部及びメチルイソブチルケトン200部を仕込
み、窒素ガスを吹き込みながら80℃に加熱した。
そこへ予め用意しておいたスチレン190部及び2
−(1−アジリジニル)エチルメタクリレート10
部からなる重合性単量体にベンゾイルパーオキサ
イド4部を溶解した混合物を2時間に亘つて滴下
ロートより滴下し、更に5時間撹拌を続けて重合
反応を行つた後冷却して重合体溶液を得た。この
重合体溶液100部にメタノール2000部を加えて再
沈した後乾燥して反応性基としてアジリジン基を
有する重合体を得た。この重合体の分子量は
GPC測定によりMn=3000であつた。
反応性基としてアジリジン基を有する重合体20
部及び反応性基を有しないポリスチレンであるス
タイロン−666(旭化成工業(株)製,Mn=4000)20
部とカーボンブラツクMA−600を20部とを実施
例1と同様に反応した後冷却、粉砕してカーボン
ブラツクグラフトポリマー(2)を得た。
実施例 3
実施例1で用いたのと同じフラスコにシクロヘ
キサン460部、レオドールSP−S10(花王(株)製)2
部を仕込み窒素ガスを吹き込みながら75℃まで昇
温した。そこへ予め用意しておいたアクリルアマ
イド60部、N−ビニルピロリドン15.2部、N−ヒ
ドロキシエチルメタクリルアミド1.6部からなる
重合性単量体に脱イオン水140部、過硫酸アンモ
ニウム2部を加えた混合物を1.5時間に亘つて滴
下ロートより滴下し、更に0.5時間撹拌を続けて
重合反応を行つた。冷却後シクロヘキサンを除去
し、ポリマーを80〜100℃で減圧下に乾燥し、反
応性基としてN−ヒドロキシアルキルアミド基を
有する重合体を得た。この重合体の分子量は
GPC測定によりMn=12000であつた。
反応性基としてN−ヒドロキシアルキルアミド
基を有する重合体45部とカーボンブラツクMA−
100R(三菱化成工業(株)製)15部とを実施例1と同
様に反応した後冷却、粉砕してカーボンブラツク
グラフトポリマー(3)を得た。
実施例 4
実施例2で用いたのと同じフラスコにトルエン
217部を仕込み、窒素ガスを吹き込みながら90℃
に加熱した。そこへ予め用意しておいたスチレン
480部及びアクリル酸n−ブチル20部からなる重
合性単量体にチオグリコール酸5.44部、アゾビス
イソブチロニトリル1.32部とを溶解した混合物を
2時間にわたつて滴下ロートより滴下し、更に5
時間撹拌を続けて重合反応を行つた。この重合体
の分子量はGPC測定によりMn=9500であつた。
次いで、この反応生成物(末端にカルボキシル
基を有するプレポリマーを含む溶液)185.1部に
2−p−フエニレン−ビス−2−オキサゾリン
2.95部を加え80℃で2時間反応して、末端に反応
性基としてオキサゾリン基を有する重合体の溶液
(不揮発分70%)を得た。
末端にオキサゾリン基を有する重合体の溶液
(不揮発分70%)57.1部とカーボンブラツクMA
−100R20部をラボプラストミルを用いて160℃、
100rpmの条件下に混練して、反応及び脱溶剤し
た後、冷却粉砕してカーボンブラツクグラフトポ
リマー(4)を得た。
実施例 5
撹拌機、温度計、エチレンオキサイド供給装置
を備えたオートクレーブ中にメタノール32部、水
酸化ナトリウム0.35部を仕込み、温度を110℃ま
で昇温させ、撹拌を行いつつ圧力を5〜8Kg/cm2
に維持しながらエチレンオキサイド88部を滴下
し、30分間熟成を行つた後、さらに反応温度を
150℃に昇温しエチレンオキサイド352部を5時間
にわたつて滴下し、その後1時間熟成して片末端
メトキシ化エチレンオキサイド10モル付加物を得
た。この片末端メトキシ化エチレンオキサイド10
モル付加物47.2部と水酸化ナトリウム0.62部を上
記と同様のオートクレーブに仕込み、温度を150
℃まで昇温し、エチレンオキサイド616部を5時
間にわたつて滴下し、その後1時間熟成して重合
を完結させて片末端メトキシ化ポリエチレングリ
コールを合成した。
上で用いたのと同じオートクレーブに蒸留水
400部、上記反応により得た片末端メトキシ化ポ
リエチレングリコール100部、白金/パラジウム
系触媒10部を仕込み、温度90〜95℃に保ち、圧力
が10Kg/cm2を維持するように圧縮空気を随時追加
しながら30時間撹拌を続け反応させ、酸価8.4の
片末端がメトキシ基、他方の末端がカルボキシル
基で変性されたポリエチレングリコールの水溶液
を得た。この重合体の分子量はGPC測定により
Mn=6600であつた。この変性されたポリエチレ
ングリコールの水溶液の溶媒をジエチレングリコ
ールに置換し、不揮発分33.3%に調整した。こう
して得た片末端カルボキシル変性ポリエチレング
リコールのジエチレングリコール溶液300部を実
施例1で用いたのと同じフラスコに仕込み50℃ま
で昇温した後、滴下漏斗より1.70部の2−(1−
アジリジニル)−2−オキサゾリンを30分にわた
つて滴下した。5時間反応させた後冷却し、片末
端に反応性基としてオキサゾリン基を有する重合
体を含む溶液(不揮発分33.7%)を得た。
反応性基としてオキサゾリン基を有する重合体
を含む溶液90部とカーボンブラツク#45(三菱化
成工業(株)製)30部とを実施例1で示すフラスコに
移し、100℃で5時間反応させ、カーボンブラツ
クグラフトポリマー(5)のジエチレングリコール溶
液を得た。
実施例 6
実施例2で用いたのと同じフラスコに末端カル
ボキシル基含有線状飽和ポリエステルアロプラツ
ツOB−63(日本触媒化学工業(株)製、分子量Mn=
6000、不揮発分50%)200部、2−p−フエニレ
ン−ビス−2−オキサゾリン3.60部を加え、110
℃で2時間反応して、末端に反応性基としてオキ
サゾリン基を有する重合体の溶液(不揮発分50
%)を得た。末端にオキサゾリン基を有する重合
体の溶液(不揮発分50%)80.0部とカーボンブラ
ツクMA−100R20部とを実施例4と同様の条件
下で混練反応し、カーボンブラツクグラフトポリ
マー(6)を得た。
比較例 1
実施例1で用いたものと同様のフラスコにスチ
レンを48部及びカーボンブラツクMA−600を12
部仕込み窒素ガスを吹き込みながら、140℃に加
熱し、この温度で5時間撹拌を続けて重合反応を
行つた後冷却した。反応後、生成物にトルエン
300部を加え、メタノール7000部に再沈し、比較
用カーボンブラツクグラフトポリマー(1)を得た。
この比較用カーボンブラツクグラフトポリマー(1)
の組成はCB成分100部に対しポリスチレン成分が
250部の割合であつた。
比較例 2
実施例2で用いた反応性基を有しないポリスチ
レン45部とカーボンブラツクMA−600を15部と
を実施例1と同様に混練した後冷却、粉砕して
CB成分と重合体成分とが実質的に結合していな
い比較用カーボンブラツクグラフトポリマー(2)を
得た。
実施例 7
実施例1〜6および比較例1〜2で得たカーボ
ンブラツクグラフトポリマー(1)〜(6)および比較用
カーボンブラツクグラフトポリマー(1)〜(2)を用い
て、トルエンおよび水に対する分散性を試験し
た。その結果は第1表に示した通りであつた。
(Industrial Application Field) The present invention relates to a novel carbon black graft polymer and a method for producing the same. For more details,
Carbon black (hereinafter referred to as CB) is reacted with a polymer having a specific reactive group, resulting in ink,
The present invention relates to a new carbon black graft polymer useful as a coloring agent for copying machine toners, paints, plastic molding materials, etc., or as a modification of various polymers, and a method for producing the same. (Prior Art) CB has excellent coloring properties, electrical conductivity, weather resistance, chemical resistance, etc., and is therefore widely used for various purposes such as reinforcing agents and fillers for plastics and elastomers. However, since CB is in the form of powder or granules, it is rarely used alone; it is usually dispersed uniformly in a solid base material such as rubber or resin, or in a liquid such as water or a solvent. Demonstrate characteristics. However, CB has a weak affinity with other substances such as organic polymers, water, and organic solvents compared to the cohesive force between particles, so it is extremely difficult to mix or disperse uniformly under normal mixing or dispersion conditions. It was difficult. To solve this problem, many studies have been conducted to improve the dispersibility of CB by coating the CB surface with various surfactants and resins to increase its affinity with solid or liquid substrates. ing. Among them, carbon black graft polymers obtained by polymerizing polymerizable monomers in the coexistence of CB can be modified to have hydrophilicity and/or lipophilicity by appropriately selecting the type of polymerizable monomers.
It has attracted attention in recent years because it can be changed. As a method for producing this carbon black graft polymer, for example, Japanese Patent Publication No. 42-22047,
Special Publication No. 44-3826, Special Publication No. 17248, Special Publication No. 45-17248, Special Publication No. 17248, Special Publication No.
No. 46-26970, however, the yield of carbon black graft polymer obtained by these methods is low, ranging from several percent to several tens of percent, and the majority exists in the form of a vinyl homopolymer, and the carbon black graft polymer obtained by these methods is in the form of a vinyl homopolymer. It was extremely inefficient. For this reason, the affinity with other substances was not improved as much as expected, and the state of dispersion often differed depending on the mixing or dispersion conditions. (Problem to be Solved by the Invention) The present inventors have conducted extensive studies in view of the current situation, and have found that a polymer having a specific reactive group in its molecule can interact with the surface functional groups of CB extremely efficiently. The carbon black graft polymer obtained by the reaction has excellent dispersibility in various substances, and by specifying the conditions during the reaction, a carbon black graft polymer with even higher dispersibility can be easily obtained. The present invention was completed based on the discovery that this can be done. (Means for Solving the Problems) The present invention involves reacting one or more types selected from the group consisting of an aziridine group, an oxazoline group, and an N-hydroxyalkylamide group in the molecule with respect to 100 parts by weight of CB. A carbon black graft polymer characterized in that it is formed by reacting a polymer having a reactive group (hereinafter referred to as a polymer having a reactive group (A)) in a proportion of 1 to 3,000 parts by weight, and CB and a reactive group. The present invention relates to a method for producing a carbon black graft polymer, which comprises stirring and mixing a polymer (A) having the following properties at a reaction temperature of room temperature to 350°C. The polymer (A) having a reactive group in the present invention is a vinyl polymer having in its molecule one or more reactive groups selected from an aziridine group, an oxazoline group, and an N-hydroxyalkylamide group;
These include polyester and polyether. Groups that can react with the functional groups present on the surface of CB are not necessarily limited to these reactive groups, but when using a polymer having groups other than these reactive groups, the type of CB that can be used It is subject to limitations and requires a step to pre-treat CB prior to the reaction. The significance of using the polymer (A) having the above-mentioned reactive group in the reaction with CB is that
Regardless of the type and state of CB, CB and polymer (A) react with extremely high grafting efficiency even under mild reaction conditions, yielding carbon black grafted polymers with outstanding dispersibility in various substances. It's there. As a method for obtaining the polymer (A) having a reactive group, for example, if necessary, the polymerizable monomer (a) having the above-mentioned reactive group in the molecule (hereinafter referred to as monomer (a)) is used. A method of polymerizing the compound (c) with another polymerizable monomer (b) (hereinafter referred to as monomer (b)); The reactive group is reacted with a polymer (d) (hereinafter referred to as polymer (d)) having a group capable of reacting with the compound (c).
(d), etc., and these methods can be adopted as appropriate depending on the purpose of use. Examples of the monomer (a) that can be used in the method include: An aziridine group-containing polymerizable monomer represented by;
2-vinyl-2-oxazoline, 2-vinyl-4
-Methyl-2-oxazoline, 2-vinyl-5-
Methyl-2-oxazoline, 2-vinyl-4-ethyl-2-oxazoline, 2-vinyl-5-ethyl-2-oxazoline, 2-isopropenyl-2
-oxazoline, 2-isopropenyl-4-methyl-2-oxazoline, 2-isopropenyl-5
-Methyl-2-oxazoline, 2-isopropenyl-4-ethyl-2-oxazoline, 2-isopropenyl-5-ethyl-2-oxazoline, 2-
Oxazoline group-containing polymerizable monomers such as isopropenyl-4,5-dimethyl-2-oxazoline; N-hydroxymethylacrylamide, N-
Hydroxyethyl acrylamide, N-hydroxybutylacrylamide, N-hydroxyisobutylacrylamide, N-hydroxy-2-ethylhexylacrylamide, N-hydroxycyclohexylacrylamide, N-hydroxymethylmethacrylamide, N-hydroxyethylmethacrylamide, N-hydroxybutylmethacrylamide N-hydroxyalkylamide group-containing polymerizable monomers such as amide, N-hydroxyisobutyl methacrylamide, N-hydroxy-2-ethylhexyl methacrylamide, N-hydroxycyclohexyl methacrylamide, etc., and selected from these groups. One type or two or more types can be used. Monomers that can be used as necessary in the method of
(b) is not particularly limited as long as it can be copolymerized with monomer (a), such as styrene, o-methylstyrene, m-methylstyrene, p-methylstyrene, α-methylstyrene, p-methylstyrene, - Styrenic monomers such as methoxystyrene, p-tert-butylstyrene, p-phenylstyrene, o-chlorostyrene, m-chlorostyrene, p-chlorostyrene; acrylic acid, methyl acrylate, ethyl acrylate, acrylic acid n-butyl, isobutyl acrylate, dodecyl acrylate, stearyl acrylate, 2-ethylhexyl acrylate, methacrylic acid, methyl methacrylate, ethyl methacrylate, propyl methacrylate, n-butyl methacrylate, isobutyl methacrylate, n-methacrylate
- Acrylic acid or methacrylic acid monomers such as octyl, dodecyl methacrylate, 2-ethylhexyl methacrylate, stearyl methacrylate; ethylene, propylene, butylene, vinyl chloride, vinyl acetate, acrylonitrile, acrylamide, methacrylamide, N-vinylpyrrolidone, etc. are mentioned, and one or more of these can be used. In order to obtain a polymer (A) having a reactive group by the method described above, monomer (a) is combined with monomer (b) using the monomer (b) if necessary, and a conventionally known polymerization method, such as bulk polymerization method or suspension polymerization method. The polymerization may be carried out by emulsion polymerization, precipitation polymerization, solution polymerization, or the like. Compounds (c) that can be used in the method include, for example, (2-1) a compound having two or more of the above-mentioned reactive groups in the molecule (2-2) a compound having two or more of the above-mentioned reactive groups in the molecule; (2-3) Compounds having one or more of the above-mentioned reactive groups and a group other than the above-mentioned reactive groups in the molecule can be mentioned. However, the groups other than the reactive groups described in item (2-3) are groups other than aziridine groups, oxazoline groups, and N-hydroxyalkylamide groups, and are included in the polymer (d) described below. Examples of such groups include isocyanate groups, epoxy groups, amino groups, carboxyl groups, hydroxyl groups, and vinyl groups. The polymer (d) in the method of (2-
A vinyl polymer, polyester, having a group capable of reacting with the compound (c) described in items 1) to (2-3),
Polyether etc. Examples of groups that can react with compound (c) include hydroxyl groups, carboxyl groups, amino groups, and epoxy groups, and polymers (d) having these groups can be prepared by known methods such as radical polymerization and condensation polymerization. It can be easily obtained by the following polymerization procedure. In order to obtain a polymer (A) having a reactive group by the method described above, compound (c) and polymer (d) are reacted under conditions such that at least one of the reactive groups remains unreacted. do it. In the present invention, the polymer (A) having a reactive group is appropriately selected depending on the properties to be imparted to the carbon black graft polymer, such as hydrophilicity, lipophilicity, or other affinity. When it is necessary to impart oleophilicity, vinyl polymers or polyethers containing acrylic acid as a main component are preferably used, and when lipophilic properties are to be imparted, vinyl polymers or polyesters containing styrene as a main component are preferably used. There is no particular restriction on the molecular weight of the polymer (A) having a reactive group, but the average molecular weight is preferably 200 to 200 in terms of remarkable treatment effects on CB and workability during reaction with CB.
The range is preferably 1,000,000, more preferably 300 to 100,000. The carbon black graft polymer of the present invention is obtained by reacting a polymer (A) having a reactive group with CB, and the polymer (A) is graft-bonded to CB with extremely high efficiency. The reaction can be carried out in various ways. For example, if the polymer (A) having a reactive group obtained by the above-mentioned method is
A method of reacting with CB may be used, and a step of obtaining a polymer (A) having a reactive group by carrying out a method of reacting with CB in the presence of CB, and a step of reacting the polymer (A) with CB. may be combined into one. However, the former method is preferred in order to obtain a carbon black graft polymer with high grafting efficiency. In the reaction, the amount of the polymer (A) having a reactive group used is 1 to 3000 parts by weight per 100 parts by weight of CB. The present invention also provides a manufacturing method for easily obtaining a carbon black graft polymer with further improved dispersibility in various substances.
Such a production method is achieved by stirring and mixing CB and the polymer (A) having a reactive group at a temperature of room temperature to 350°C to react. According to the production method of the present invention, in the secondary agglomerated state used as the raw material,
When the CB is stirred and mixed and reacted, it is efficiently crushed and becomes fine and uniform in particle size, and the efficiency of the reaction is also improved, so the properties of the obtained carbon black graft polymer are further improved. If the temperature condition during the reaction exceeds 350°C, the quality of the polymer component will deteriorate, which is not preferable. In the production method of the present invention, the reaction between CB and the polymer (A) having a reactive group may be a method in which only these two components are reacted, or the reaction between the CB and the polymer (A) having a reactive group may be a method in which only these two components are reacted. The reaction may be carried out in the presence of other substances such as polymer components, polymerizable monomers, organic solvents, and water that are not applicable. As a specific example of the embodiment of the production method of the present invention, for example, 1 part by weight of the polymer (A) having a reactive group to 100 parts by weight of CB.
3000 parts by weight, preferably 5 parts by weight to 1000 parts by weight,
A mixture of 0 to 1000 parts by weight of a polymer having no reactive group, 0 to 200 parts by weight of a polymerizable monomer, and 0 to 1000 parts by weight of an organic solvent is heated at room temperature to 350°C. The carbon black graft polymer of the present invention is obtained by stirring and mixing preferably at a temperature of 50°C to 250°C. (Effect of the invention) The carbon black graft polymer of the present invention is obtained by reacting a polymer (A) having a reactive group with CB, and the reactive group in the polymer (A) interacts with the surface functional group of CB. Due to its high reactivity, the polymer (A) component is grafted onto the CB surface with high efficiency. Since the composition, type, etc. of the polymer (A) can be arbitrarily selected as long as it has the reactive groups defined in the present invention, various properties can be imparted to CB depending on the purpose. Is possible. The carbon black graft polymer obtained in this way has improved affinity with various substances, and has extremely excellent dispersibility in substances such as organic polymers, water, and organic solvents.
It can be suitably used as a coloring agent for inks, copying machine toners, paints, plastic molding materials, etc., and as a modifier for various polymers. Furthermore, according to the production method of the present invention, the carbon black graft polymer, which has further improved characteristics such as dispersibility, can be obtained by simply stirring and mixing the polymer (A) having a reactive group on CB with heating. It can be manufactured with a simple operation. Therefore, the method for producing a carbon black graft polymer of the present invention is extremely useful industrially. (Examples) Hereinafter, the present invention will be explained in detail with reference to Examples, but the present invention is not limited to the following Examples. In addition, parts in the examples indicate parts by weight, and % indicates weight %, respectively. Example 1 Polyvinyl alcohol was added to a flask equipped with a stirrer, an inert gas inlet tube, a reflux condenser, and a thermometer.
400 parts of deionized water dissolved in 0.2 parts was charged. A mixture of 16 parts of benzoyl peroxide dissolved in a polymerizable monomer consisting of 196 parts of styrene and 4 parts of isopropenyloxazoline prepared in advance was added thereto, and stirred at high speed to form a uniform suspension. Next, the mixture was heated to 80° C. while blowing nitrogen gas, and stirred at this temperature for 5 hours to carry out a polymerization reaction, and then cooled to obtain a polymer suspension. This polymer suspension was filtered, washed, and dried to obtain a polymer having an oxazoline group as a reactive group. The molecular weight of this polymer was Mn=5800 by GPC measurement. Polymers with oxazoline groups as reactive groups
40 parts and Carbon Black MA-600 (Mitsubishi Chemical Industries)
Co., Ltd.) 20 parts and Laboplasto Mill (Toyo Seiki Co., Ltd.)
After reaction, the mixture was kneaded and reacted at 160° C. and 100 rpm using a commercially available product (manufactured by Alumni Co., Ltd.), followed by cooling and pulverization to obtain carbon black graft polymer (1). Example 2 Toluene was added to the same flask used in Example 1.
200 parts of methyl isobutyl ketone and 200 parts of methyl isobutyl ketone were charged, and the mixture was heated to 80°C while blowing nitrogen gas.
There, 190 parts of styrene prepared in advance and 2
-(1-aziridinyl)ethyl methacrylate 10
A mixture of 4 parts of benzoyl peroxide dissolved in a polymerizable monomer consisting of Obtained. 2000 parts of methanol was added to 100 parts of this polymer solution, reprecipitated, and then dried to obtain a polymer having an aziridine group as a reactive group. The molecular weight of this polymer is
Mn was found to be 3000 by GPC measurement. Polymer 20 with an aziridine group as a reactive group
Styron-666 (manufactured by Asahi Kasei Corporation, Mn = 4000), which is a polystyrene having no moieties or reactive groups, 20
and 20 parts of Carbon Black MA-600 were reacted in the same manner as in Example 1, then cooled and pulverized to obtain Carbon Black graft polymer (2). Example 3 Into the same flask as used in Example 1, 460 parts of cyclohexane and 2 parts of Rheodol SP-S10 (manufactured by Kao Corporation) were added.
The temperature was raised to 75°C while blowing nitrogen gas. A mixture of 140 parts of deionized water and 2 parts of ammonium persulfate was added to the previously prepared polymerizable monomers consisting of 60 parts of acrylamide, 15.2 parts of N-vinylpyrrolidone, and 1.6 parts of N-hydroxyethylmethacrylamide. was added dropwise from the dropping funnel over 1.5 hours, and stirring was continued for an additional 0.5 hours to carry out a polymerization reaction. After cooling, cyclohexane was removed, and the polymer was dried under reduced pressure at 80 to 100°C to obtain a polymer having N-hydroxyalkylamide groups as reactive groups. The molecular weight of this polymer is
Mn=12000 was determined by GPC measurement. 45 parts of a polymer having an N-hydroxyalkylamide group as a reactive group and carbon black MA-
15 parts of 100R (manufactured by Mitsubishi Chemical Industries, Ltd.) was reacted in the same manner as in Example 1, then cooled and pulverized to obtain a carbon black graft polymer (3). Example 4 Toluene was added to the same flask used in Example 2.
Pour 217 parts and heat to 90℃ while blowing nitrogen gas.
heated to. Styrene prepared in advance
A mixture of 5.44 parts of thioglycolic acid and 1.32 parts of azobisisobutyronitrile dissolved in a polymerizable monomer consisting of 480 parts of n-butyl acrylate and 20 parts of n-butyl acrylate was added dropwise from a dropping funnel over 2 hours, and then 5
The polymerization reaction was carried out by continuing stirring for a certain period of time. The molecular weight of this polymer was Mn=9500 by GPC measurement. Next, 2-p-phenylene-bis-2-oxazoline was added to 185.1 parts of this reaction product (a solution containing a prepolymer having a carboxyl group at the end).
2.95 parts were added and reacted at 80°C for 2 hours to obtain a solution (non-volatile content: 70%) of a polymer having an oxazoline group as a terminal reactive group. 57.1 parts of a solution of a polymer having an oxazoline group at the end (70% non-volatile content) and Carbon Black MA
20 parts of −100R was heated at 160°C using a laboplasto mill.
After kneading at 100 rpm to perform reaction and solvent removal, the mixture was cooled and pulverized to obtain a carbon black graft polymer (4). Example 5 32 parts of methanol and 0.35 parts of sodium hydroxide were placed in an autoclave equipped with a stirrer, a thermometer, and an ethylene oxide supply device, the temperature was raised to 110°C, and the pressure was increased to 5 to 8 kg/kg while stirring. cm2
88 parts of ethylene oxide was added dropwise while maintaining the temperature, and after aging for 30 minutes, the reaction temperature was further increased.
The temperature was raised to 150°C, 352 parts of ethylene oxide was added dropwise over 5 hours, and the mixture was aged for 1 hour to obtain a 10 mole adduct of ethylene oxide with methoxylated one end. This one-end methoxylated ethylene oxide 10
47.2 parts of molar adduct and 0.62 parts of sodium hydroxide were placed in the same autoclave as above, and the temperature was raised to 150
The temperature was raised to .degree. C., 616 parts of ethylene oxide was added dropwise over 5 hours, and the mixture was aged for 1 hour to complete the polymerization to synthesize polyethylene glycol having one end methoxylated. Distilled water in the same autoclave used above.
400 parts, 100 parts of one-end methoxylated polyethylene glycol obtained by the above reaction, and 10 parts of platinum/palladium catalyst were charged, and the temperature was maintained at 90 to 95°C, and compressed air was supplied as needed to maintain the pressure at 10 kg/ cm2. The reaction was continued for 30 hours while stirring, and an aqueous solution of polyethylene glycol having an acid value of 8.4 and modified with a methoxy group at one end and a carboxyl group at the other end was obtained. The molecular weight of this polymer was determined by GPC measurement.
Mn=6600. The solvent of this aqueous solution of modified polyethylene glycol was replaced with diethylene glycol, and the nonvolatile content was adjusted to 33.3%. 300 parts of the diethylene glycol solution of the one-end carboxyl-modified polyethylene glycol thus obtained was charged into the same flask used in Example 1, heated to 50°C, and then 1.70 parts of 2-(1-
aziridinyl)-2-oxazoline was added dropwise over 30 minutes. After reacting for 5 hours, the mixture was cooled to obtain a solution (non-volatile content: 33.7%) containing a polymer having an oxazoline group as a reactive group at one end. 90 parts of a solution containing a polymer having an oxazoline group as a reactive group and 30 parts of Carbon Black #45 (manufactured by Mitsubishi Chemical Industries, Ltd.) were transferred to the flask shown in Example 1, and reacted at 100°C for 5 hours. A diethylene glycol solution of carbon black graft polymer (5) was obtained. Example 6 Into the same flask as used in Example 2, a terminal carboxyl group-containing linear saturated polyester alloplatz OB-63 (manufactured by Nippon Shokubai Kagaku Kogyo Co., Ltd., molecular weight Mn =
6000, non-volatile content 50%) 200 parts, 2-p-phenylene-bis-2-oxazoline 3.60 parts were added, 110
℃ for 2 hours to form a solution of a polymer having an oxazoline group as a terminal reactive group (non-volatile content: 50
%) was obtained. 80.0 parts of a solution of a polymer having an oxazoline group at the end (nonvolatile content 50%) and 20 parts of Carbon Black MA-100R were kneaded and reacted under the same conditions as in Example 4 to obtain a carbon black graft polymer (6). . Comparative Example 1 In a flask similar to that used in Example 1, 48 parts of styrene and 12 parts of carbon black MA-600 were added.
The mixture was heated to 140° C. while blowing nitrogen gas into the mixture, and stirring was continued at this temperature for 5 hours to carry out a polymerization reaction, followed by cooling. After the reaction, toluene is added to the product.
300 parts were added thereto, and reprecipitation was carried out in 7000 parts of methanol to obtain carbon black graft polymer (1) for comparison.
Carbon black graft polymer for comparison (1)
The composition is 100 parts of CB component and polystyrene component.
The proportion was 250 copies. Comparative Example 2 45 parts of the polystyrene without reactive groups used in Example 2 and 15 parts of carbon black MA-600 were kneaded in the same manner as in Example 1, then cooled and pulverized.
A comparative carbon black graft polymer (2) in which the CB component and the polymer component were not substantially bonded was obtained. Example 7 Using the carbon black graft polymers (1) to (6) obtained in Examples 1 to 6 and Comparative Examples 1 to 2 and the comparative carbon black graft polymers (1) to (2), Dispersibility was tested. The results were as shown in Table 1.
【表】【table】
Claims (1)
にアジリジン基、オキサゾリン基及びN−ヒドロ
キシアルキルアミド基よりなる群から選ばれる1
種又は2種以上の反応性基を有する重合体が1〜
3000重量部の割合で反応してなることを特徴とす
るカーボンブラツクグラフトポリマー。 2 カーボンブラツク100重量部に対し、分子内
にアジリジン基、オキサゾリン基及びN−ヒドロ
キシアルキルアミド基よりなる群から選ばれる1
種又は2種以上の反応性基を有する重合体を1〜
3000重量部の割合で常温〜350℃の温度条件下で
撹拌混合して反応することを特徴とするカーボン
ブラツクグラフトポリマーの製造方法。[Scope of Claims] 1. 1 selected from the group consisting of aziridine group, oxazoline group and N-hydroxyalkylamide group in the molecule based on 100 parts by weight of carbon black.
The species or polymers having two or more reactive groups are 1-
A carbon black graft polymer characterized by being formed by reacting at a ratio of 3000 parts by weight. 2 Based on 100 parts by weight of carbon black, 1 selected from the group consisting of aziridine group, oxazoline group and N-hydroxyalkylamide group in the molecule.
1 to 1 polymer having a species or two or more reactive groups
1. A method for producing a carbon black graft polymer, characterized in that the reaction is carried out by stirring and mixing 3000 parts by weight at a temperature of room temperature to 350°C.
Priority Applications (7)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62219097A JPS63270767A (en) | 1986-12-17 | 1987-09-03 | Carbon black graft polymer and production of the same |
| US07/134,319 US4880857A (en) | 1986-12-17 | 1987-12-16 | Carbon black-graft polymer, method for production thereof, and use thereof |
| CA000554540A CA1285083C (en) | 1986-12-17 | 1987-12-16 | Carbon black-graft polymer, method for production thereof, and use thereof |
| EP87311145A EP0272127A3 (en) | 1986-12-17 | 1987-12-17 | Carbon black-graft polymer, its production and use |
| KR1019870014435A KR940007357B1 (en) | 1986-12-17 | 1987-12-17 | Carbon black-graft polymer, its production and use |
| US07/373,234 US4940749A (en) | 1986-12-17 | 1989-06-29 | Carbon black-graft polymer, method for production thereof, and use thereof |
| US07/533,780 US4994520A (en) | 1986-12-17 | 1990-06-06 | Carbon black-graft polymer, method for production thereof, and use thereof |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61-298985 | 1986-12-17 | ||
| JP29898586 | 1986-12-17 | ||
| JP62219097A JPS63270767A (en) | 1986-12-17 | 1987-09-03 | Carbon black graft polymer and production of the same |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63270767A JPS63270767A (en) | 1988-11-08 |
| JPH0224868B2 true JPH0224868B2 (en) | 1990-05-30 |
Family
ID=26522920
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62219097A Granted JPS63270767A (en) | 1986-12-17 | 1987-09-03 | Carbon black graft polymer and production of the same |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS63270767A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1997000295A1 (en) | 1995-06-14 | 1997-01-03 | Nippon Shokubai Co., Ltd. | Carbon black graft polymer, process for the production of the polymer and use thereof |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3338507B2 (en) * | 1993-04-14 | 2002-10-28 | 株式会社日本触媒 | Method for producing carbon black graft polymer composition |
| JP2761188B2 (en) | 1994-05-27 | 1998-06-04 | 株式会社日本触媒 | Emulsion polymerization inhibitor and suspension polymerization method using the same |
| JP3435371B2 (en) * | 1998-09-14 | 2003-08-11 | 株式会社日本触媒 | Carbon black graft polymer and its use |
| JP2006160801A (en) * | 2004-12-03 | 2006-06-22 | Japan Polypropylene Corp | Conductive polypropylene resin composition |
-
1987
- 1987-09-03 JP JP62219097A patent/JPS63270767A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1997000295A1 (en) | 1995-06-14 | 1997-01-03 | Nippon Shokubai Co., Ltd. | Carbon black graft polymer, process for the production of the polymer and use thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63270767A (en) | 1988-11-08 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Shea et al. | Synthesis and characterization of highly crosslinked poly (acrylamides) and poly (methacrylamides). A new class of macroporous polyamides | |
| GB2090602A (en) | Polymer composition | |
| JPH0778089B2 (en) | Method of manufacturing composite material | |
| EP1847560A1 (en) | Process for producing spherical polymer powder and spherical powder comprising (meth)acrylic block copolymer | |
| CN107501486A (en) | A kind of nano silicon of surface grafting polyisoprene, preparation method and applications | |
| JPS5853003B2 (en) | Shinkijiyugoutairiyuushinoseizohou | |
| JPS61502390A (en) | Production of crosslinked styrene polymer foam | |
| JPH0224868B2 (en) | ||
| JPH0627269B2 (en) | Method for producing carbon black graft polymer | |
| JP2532521B2 (en) | Method for producing surface-treated inorganic filler | |
| JP2725031B2 (en) | Method for producing crosslinked polymer fine particles | |
| JP2954432B2 (en) | Polymers, surface modifiers for inorganic materials, and modified products thereof | |
| JP2000169632A (en) | Carbon black-rubber composite and its production | |
| JPH1160987A (en) | Hydrophobic fine particle dispersant and hydrophobic fine particle dispersant obtained by using the same | |
| JP3338507B2 (en) | Method for producing carbon black graft polymer composition | |
| JPH01138271A (en) | Production of surface-treated organic pigment | |
| JPH10120935A (en) | Electrical resistance-adjusting material | |
| CN119976820B (en) | A method for preparing and applying modified graphene oxide | |
| JPH04220465A (en) | Production of surface-treated organic pigment | |
| CA1285083C (en) | Carbon black-graft polymer, method for production thereof, and use thereof | |
| JPH0742421B2 (en) | Method for producing surface-treated carbon black | |
| JPH09118754A (en) | Masterbatch of fine inorganic powder | |
| JPS6261633A (en) | Preparation of polymer coated capsule | |
| JPH023826B2 (en) | ||
| CN117264094A (en) | A comb copolymer that improves the dispersion of alumina polishing liquid and its preparation method |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |