JP2006022029A - Method for obtaining aromatic dihydroxy compound from waste aromatic polycarbonate - Google Patents
Method for obtaining aromatic dihydroxy compound from waste aromatic polycarbonate Download PDFInfo
- Publication number
- JP2006022029A JP2006022029A JP2004200620A JP2004200620A JP2006022029A JP 2006022029 A JP2006022029 A JP 2006022029A JP 2004200620 A JP2004200620 A JP 2004200620A JP 2004200620 A JP2004200620 A JP 2004200620A JP 2006022029 A JP2006022029 A JP 2006022029A
- Authority
- JP
- Japan
- Prior art keywords
- dihydroxy compound
- aromatic
- organic solvent
- aromatic dihydroxy
- waste
- 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.)
- Granted
Links
- 125000003118 aryl group Chemical group 0.000 title claims abstract description 141
- 150000001875 compounds Chemical class 0.000 title claims abstract description 114
- 238000000034 method Methods 0.000 title claims abstract description 70
- 239000004417 polycarbonate Substances 0.000 title claims abstract description 69
- 229920000515 polycarbonate Polymers 0.000 title claims abstract description 63
- 239000002699 waste material Substances 0.000 title claims abstract description 32
- 239000003960 organic solvent Substances 0.000 claims abstract description 59
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 49
- 238000000354 decomposition reaction Methods 0.000 claims abstract description 37
- 238000005406 washing Methods 0.000 claims abstract description 28
- 239000007864 aqueous solution Substances 0.000 claims abstract description 27
- 239000000243 solution Substances 0.000 claims abstract description 26
- 229910000000 metal hydroxide Inorganic materials 0.000 claims abstract description 23
- 150000004692 metal hydroxides Chemical class 0.000 claims abstract description 23
- 238000006243 chemical reaction Methods 0.000 claims abstract description 16
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 claims abstract description 15
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000002253 acid Substances 0.000 claims abstract description 10
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 claims description 58
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 21
- 238000004519 manufacturing process Methods 0.000 claims description 20
- 239000002904 solvent Substances 0.000 claims description 19
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 claims description 10
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 10
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 9
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 6
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 6
- 125000004432 carbon atom Chemical group C* 0.000 claims description 6
- SCYULBFZEHDVBN-UHFFFAOYSA-N 1,1-Dichloroethane Chemical compound CC(Cl)Cl SCYULBFZEHDVBN-UHFFFAOYSA-N 0.000 claims description 5
- 238000005809 transesterification reaction Methods 0.000 claims description 4
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 3
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 3
- 239000011260 aqueous acid Substances 0.000 claims description 3
- 229910017604 nitric acid Inorganic materials 0.000 claims description 3
- 238000004821 distillation Methods 0.000 abstract description 8
- 150000002148 esters Chemical class 0.000 abstract 1
- IISBACLAFKSPIT-UHFFFAOYSA-N bisphenol A Chemical compound C=1C=C(O)C=CC=1C(C)(C)C1=CC=C(O)C=C1 IISBACLAFKSPIT-UHFFFAOYSA-N 0.000 description 45
- 239000007787 solid Substances 0.000 description 21
- 239000012071 phase Substances 0.000 description 18
- 239000004431 polycarbonate resin Substances 0.000 description 17
- 229920005668 polycarbonate resin Polymers 0.000 description 16
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 15
- 238000003756 stirring Methods 0.000 description 14
- 238000001914 filtration Methods 0.000 description 11
- 239000000463 material Substances 0.000 description 11
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- 239000007788 liquid Substances 0.000 description 10
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- 230000007423 decrease Effects 0.000 description 8
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- 239000003054 catalyst Substances 0.000 description 7
- 239000012535 impurity Substances 0.000 description 7
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 7
- 150000003839 salts Chemical class 0.000 description 7
- 229910001415 sodium ion Inorganic materials 0.000 description 7
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 description 6
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 6
- FKNQFGJONOIPTF-UHFFFAOYSA-N Sodium cation Chemical compound [Na+] FKNQFGJONOIPTF-UHFFFAOYSA-N 0.000 description 6
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 description 6
- 239000008346 aqueous phase Substances 0.000 description 6
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N dimethylmethane Natural products CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 6
- 238000011084 recovery Methods 0.000 description 6
- 230000003078 antioxidant effect Effects 0.000 description 5
- -1 diaryl carbonate Chemical compound 0.000 description 5
- 229910052751 metal Inorganic materials 0.000 description 5
- 239000002184 metal Substances 0.000 description 5
- 238000002156 mixing Methods 0.000 description 5
- 230000003287 optical effect Effects 0.000 description 5
- 239000001294 propane Substances 0.000 description 5
- 239000002994 raw material Substances 0.000 description 5
- 229920005989 resin Polymers 0.000 description 5
- 239000011347 resin Substances 0.000 description 5
- QPFMBZIOSGYJDE-UHFFFAOYSA-N 1,1,2,2-tetrachloroethane Chemical compound ClC(Cl)C(Cl)Cl QPFMBZIOSGYJDE-UHFFFAOYSA-N 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 239000003963 antioxidant agent Substances 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 4
- 238000001035 drying Methods 0.000 description 4
- ZXEKIIBDNHEJCQ-UHFFFAOYSA-N isobutanol Chemical compound CC(C)CO ZXEKIIBDNHEJCQ-UHFFFAOYSA-N 0.000 description 4
- 239000011541 reaction mixture Substances 0.000 description 4
- HXDOZKJGKXYMEW-UHFFFAOYSA-N 4-ethylphenol Chemical compound CCC1=CC=C(O)C=C1 HXDOZKJGKXYMEW-UHFFFAOYSA-N 0.000 description 3
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 3
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 3
- DKGAVHZHDRPRBM-UHFFFAOYSA-N Tert-Butanol Chemical compound CC(C)(C)O DKGAVHZHDRPRBM-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- BTANRVKWQNVYAZ-UHFFFAOYSA-N butan-2-ol Chemical compound CCC(C)O BTANRVKWQNVYAZ-UHFFFAOYSA-N 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- IEJIGPNLZYLLBP-UHFFFAOYSA-N dimethyl carbonate Chemical compound COC(=O)OC IEJIGPNLZYLLBP-UHFFFAOYSA-N 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000008187 granular material Substances 0.000 description 3
- 230000007935 neutral effect Effects 0.000 description 3
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 3
- 238000010992 reflux Methods 0.000 description 3
- 239000002002 slurry Substances 0.000 description 3
- 239000011734 sodium Substances 0.000 description 3
- 150000003512 tertiary amines Chemical class 0.000 description 3
- UOCLXMDMGBRAIB-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl UOCLXMDMGBRAIB-UHFFFAOYSA-N 0.000 description 2
- WSLDOOZREJYCGB-UHFFFAOYSA-N 1,2-Dichloroethane Chemical group ClCCCl WSLDOOZREJYCGB-UHFFFAOYSA-N 0.000 description 2
- JWAZRIHNYRIHIV-UHFFFAOYSA-N 2-naphthol Chemical compound C1=CC=CC2=CC(O)=CC=C21 JWAZRIHNYRIHIV-UHFFFAOYSA-N 0.000 description 2
- YQUQWHNMBPIWGK-UHFFFAOYSA-N 4-isopropylphenol Chemical compound CC(C)C1=CC=C(O)C=C1 YQUQWHNMBPIWGK-UHFFFAOYSA-N 0.000 description 2
- QHPQWRBYOIRBIT-UHFFFAOYSA-N 4-tert-butylphenol Chemical compound CC(C)(C)C1=CC=C(O)C=C1 QHPQWRBYOIRBIT-UHFFFAOYSA-N 0.000 description 2
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- QIGBRXMKCJKVMJ-UHFFFAOYSA-N Hydroquinone Chemical compound OC1=CC=C(O)C=C1 QIGBRXMKCJKVMJ-UHFFFAOYSA-N 0.000 description 2
- 238000012695 Interfacial polymerization Methods 0.000 description 2
- 239000004677 Nylon Substances 0.000 description 2
- YGYAWVDWMABLBF-UHFFFAOYSA-N Phosgene Chemical compound ClC(Cl)=O YGYAWVDWMABLBF-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 230000002411 adverse Effects 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- PXKLMJQFEQBVLD-UHFFFAOYSA-N bisphenol F Chemical compound C1=CC(O)=CC=C1CC1=CC=C(O)C=C1 PXKLMJQFEQBVLD-UHFFFAOYSA-N 0.000 description 2
- 238000011088 calibration curve Methods 0.000 description 2
- 230000001186 cumulative effect Effects 0.000 description 2
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000011261 inert gas Substances 0.000 description 2
- 238000001746 injection moulding Methods 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 229920001778 nylon Polymers 0.000 description 2
- QWVGKYWNOKOFNN-UHFFFAOYSA-N o-cresol Chemical compound CC1=CC=CC=C1O QWVGKYWNOKOFNN-UHFFFAOYSA-N 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- IWDCLRJOBJJRNH-UHFFFAOYSA-N p-cresol Chemical compound CC1=CC=C(O)C=C1 IWDCLRJOBJJRNH-UHFFFAOYSA-N 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
- 229920000139 polyethylene terephthalate Polymers 0.000 description 2
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- 230000002035 prolonged effect Effects 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- GHMLBKRAJCXXBS-UHFFFAOYSA-N resorcinol Chemical compound OC1=CC=CC(O)=C1 GHMLBKRAJCXXBS-UHFFFAOYSA-N 0.000 description 2
- 230000000717 retained effect Effects 0.000 description 2
- JVBXVOWTABLYPX-UHFFFAOYSA-L sodium dithionite Chemical compound [Na+].[Na+].[O-]S(=O)S([O-])=O JVBXVOWTABLYPX-UHFFFAOYSA-L 0.000 description 2
- GEHJYWRUCIMESM-UHFFFAOYSA-L sodium sulfite Chemical compound [Na+].[Na+].[O-]S([O-])=O GEHJYWRUCIMESM-UHFFFAOYSA-L 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000000758 substrate Substances 0.000 description 2
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 description 1
- 238000005160 1H NMR spectroscopy Methods 0.000 description 1
- FMUYQRFTLHAARI-UHFFFAOYSA-N 2,4-bis(2-phenylpropan-2-yl)phenol Chemical compound C=1C=C(O)C(C(C)(C)C=2C=CC=CC=2)=CC=1C(C)(C)C1=CC=CC=C1 FMUYQRFTLHAARI-UHFFFAOYSA-N 0.000 description 1
- KUFFULVDNCHOFZ-UHFFFAOYSA-N 2,4-xylenol Chemical compound CC1=CC=C(O)C(C)=C1 KUFFULVDNCHOFZ-UHFFFAOYSA-N 0.000 description 1
- ISPYQTSUDJAMAB-UHFFFAOYSA-N 2-chlorophenol Chemical compound OC1=CC=CC=C1Cl ISPYQTSUDJAMAB-UHFFFAOYSA-N 0.000 description 1
- HORNXRXVQWOLPJ-UHFFFAOYSA-N 3-chlorophenol Chemical compound OC1=CC=CC(Cl)=C1 HORNXRXVQWOLPJ-UHFFFAOYSA-N 0.000 description 1
- RXNYJUSEXLAVNQ-UHFFFAOYSA-N 4,4'-Dihydroxybenzophenone Chemical compound C1=CC(O)=CC=C1C(=O)C1=CC=C(O)C=C1 RXNYJUSEXLAVNQ-UHFFFAOYSA-N 0.000 description 1
- VPWNQTHUCYMVMZ-UHFFFAOYSA-N 4,4'-sulfonyldiphenol Chemical compound C1=CC(O)=CC=C1S(=O)(=O)C1=CC=C(O)C=C1 VPWNQTHUCYMVMZ-UHFFFAOYSA-N 0.000 description 1
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- UJCYBTZHUJWCMB-UHFFFAOYSA-N 4-[1-(4-hydroxyphenyl)-4-propan-2-ylcyclohexyl]phenol Chemical compound C1CC(C(C)C)CCC1(C=1C=CC(O)=CC=1)C1=CC=C(O)C=C1 UJCYBTZHUJWCMB-UHFFFAOYSA-N 0.000 description 1
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- VCCBEIPGXKNHFW-UHFFFAOYSA-N biphenyl-4,4'-diol Chemical group C1=CC(O)=CC=C1C1=CC=C(O)C=C1 VCCBEIPGXKNHFW-UHFFFAOYSA-N 0.000 description 1
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- GRWZHXKQBITJKP-UHFFFAOYSA-L dithionite(2-) Chemical compound [O-]S(=O)S([O-])=O GRWZHXKQBITJKP-UHFFFAOYSA-L 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000010408 film Substances 0.000 description 1
- 238000004128 high performance liquid chromatography Methods 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 229940035429 isobutyl alcohol Drugs 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Natural products C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 239000012452 mother liquor Substances 0.000 description 1
- PCILLCXFKWDRMK-UHFFFAOYSA-N naphthalene-1,4-diol Chemical compound C1=CC=C2C(O)=CC=C(O)C2=C1 PCILLCXFKWDRMK-UHFFFAOYSA-N 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- NIHNNTQXNPWCJQ-UHFFFAOYSA-N o-biphenylenemethane Natural products C1=CC=C2CC3=CC=CC=C3C2=C1 NIHNNTQXNPWCJQ-UHFFFAOYSA-N 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- QBDSZLJBMIMQRS-UHFFFAOYSA-N p-Cumylphenol Chemical compound C=1C=C(O)C=CC=1C(C)(C)C1=CC=CC=C1 QBDSZLJBMIMQRS-UHFFFAOYSA-N 0.000 description 1
- NKTOLZVEWDHZMU-UHFFFAOYSA-N p-cumyl phenol Natural products CC1=CC=C(C)C(O)=C1 NKTOLZVEWDHZMU-UHFFFAOYSA-N 0.000 description 1
- NWVVVBRKAWDGAB-UHFFFAOYSA-N p-methoxyphenol Chemical compound COC1=CC=C(O)C=C1 NWVVVBRKAWDGAB-UHFFFAOYSA-N 0.000 description 1
- NFHFRUOZVGFOOS-UHFFFAOYSA-N palladium;triphenylphosphane Chemical compound [Pd].C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1.C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1.C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1.C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1 NFHFRUOZVGFOOS-UHFFFAOYSA-N 0.000 description 1
- SVHOVVJFOWGYJO-UHFFFAOYSA-N pentabromophenol Chemical compound OC1=C(Br)C(Br)=C(Br)C(Br)=C1Br SVHOVVJFOWGYJO-UHFFFAOYSA-N 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 150000002989 phenols Chemical class 0.000 description 1
- 239000005020 polyethylene terephthalate Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000007873 sieving Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 235000010267 sodium hydrogen sulphite Nutrition 0.000 description 1
- 235000010265 sodium sulphite Nutrition 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 150000003462 sulfoxides Chemical class 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- AJHKJOCIGPIJFZ-UHFFFAOYSA-N tris(2,6-ditert-butylphenyl) phosphite Chemical compound CC(C)(C)C1=CC=CC(C(C)(C)C)=C1OP(OC=1C(=CC=CC=1C(C)(C)C)C(C)(C)C)OC1=C(C(C)(C)C)C=CC=C1C(C)(C)C AJHKJOCIGPIJFZ-UHFFFAOYSA-N 0.000 description 1
- 229910021642 ultra pure water Inorganic materials 0.000 description 1
- 239000012498 ultrapure water Substances 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Abstract
Description
本発明は、芳香族ポリカーボネートを炭素数１〜４のアルコール、有機溶媒および金属水酸化物の存在下に分解し、得られた固体の芳香族ジヒドロキシ化合物を洗浄し高純度の芳香族ジヒドロキシ化合物を得る方法に関する。また、得られた高純度の芳香族ジヒドロキシ化合物をポリカーボネートの製造工程に使用する芳香族ポリカーボネートの製造方法に関する。 In the present invention, an aromatic polycarbonate is decomposed in the presence of an alcohol having 1 to 4 carbon atoms, an organic solvent and a metal hydroxide, and the resulting solid aromatic dihydroxy compound is washed to obtain a high-purity aromatic dihydroxy compound. On how to get. Moreover, it is related with the manufacturing method of the aromatic polycarbonate which uses the obtained high purity aromatic dihydroxy compound for the manufacturing process of a polycarbonate.
芳香族ポリカーボネート（以下、ＰＣと略すことがある）は、優れた機械的性質、電気的性質、耐熱性、耐寒性、透明性等を有しており、レンズ、コンパクトディスク等の光ディスク、建築材料、自動車部品、ＯＡ機器のシャーシー、カメラボディー等様々な用途に利用されている材料であり、その需要は年々増加している。ＰＣの需要の増加に伴い、廃棄されるＰＣ製品の多くは焼却若しくは地中に埋める等の方法で処理される。これは、ＰＣの需要の増加から石油資源の枯渇を加速させるだけでなく、地球環境の悪化を促進する。そこで、廃棄されたプラスチックを再利用（リサイクル）することが重要になってきた。 Aromatic polycarbonate (hereinafter sometimes abbreviated as PC) has excellent mechanical properties, electrical properties, heat resistance, cold resistance, transparency, etc., optical disks such as lenses and compact disks, and building materials. These materials are used in various applications such as automobile parts, OA equipment chassis and camera bodies, and the demand for these materials is increasing year by year. Along with the increase in demand for PCs, many of the PC products to be discarded are processed by methods such as incineration or filling in the ground. This not only accelerates the depletion of petroleum resources due to the increasing demand for PC, but also promotes the deterioration of the global environment. Therefore, it has become important to reuse (recycle) discarded plastic.
廃プラスチックをリサイクルする方法は、（１）廃プラスチックを熱エネルギーとして回収するサーマルリサイクル、（２）廃プラスチックを製品にある割合で混合し、加工して製品とするマテリアルリサイクル、（３）廃プラスチックを化学的に分解してプラスチックの原材料にまで戻して、プラスチック製造に再使用するケミカルリサイクルがある。しかし、サーマルリサイクルは、プラスチックを焼却して熱を取りだすので、二酸化炭素と水が生成し、本質的には地球環境を破壊し、資源を減少させていることになる。マテリアルリサイクルは、資源の消費に関しては、一番環境の負荷が少なく、環境的に望ましいが、混合できる製品が限定されていたり、製品に混入できる割合が少なく、リサイクルできる量が限られる。ケミカルリサイクルは、プラスチックを原材料まで分解するので、そのまま製造に利用することが可能であり、産業上有用なリサイクル方法である。 The methods for recycling waste plastics are as follows: (1) Thermal recycling in which waste plastic is recovered as thermal energy, (2) Material recycling in which waste plastic is mixed and processed in a certain proportion to the product, and (3) Waste plastic There is chemical recycling in which the material is chemically decomposed back to the raw material of the plastic and reused for plastic manufacturing. However, because thermal recycling incinerates plastic to extract heat, carbon dioxide and water are generated, essentially destroying the global environment and reducing resources. Material recycling has the least environmental impact and is environmentally desirable in terms of resource consumption, but the products that can be mixed are limited, the proportion that can be mixed into the products is small, and the amount that can be recycled is limited. Since chemical recycling decomposes plastics into raw materials, it can be used for manufacturing as it is, and is an industrially useful recycling method.
ＰＣをケミカルリサイクルする方法として、例えば特許文献１には、アルカリ触媒の存在下、ＰＣをフェノールで分解し、芳香族ジヒドロキシ化合物と炭酸ジアリールを回収する方法が示されている。また特許文献２にはトルエン、キシレン、ベンゼンまたはジオキサン溶剤中で、少量のアルカリを触媒として、エステル交換反応を行い、炭酸ジアルキルと芳香族ジヒドロキシ化合物を得る方法が示されている。特許文献３には、ＰＣを塩化アルキル、エーテル類または芳香族炭化水素系溶媒等の溶媒と触媒としての３級アミンの存在下、低級アルコールとエステル交換させて芳香族ジヒドロキシ化合物と炭酸ジアルキルを得る方法が提案されている。 As a method for chemically recycling PC, for example, Patent Document 1 discloses a method in which PC is decomposed with phenol in the presence of an alkali catalyst to recover an aromatic dihydroxy compound and a diaryl carbonate. Patent Document 2 discloses a method for obtaining a dialkyl carbonate and an aromatic dihydroxy compound by performing a transesterification reaction in a toluene, xylene, benzene or dioxane solvent using a small amount of alkali as a catalyst. In Patent Document 3, PC is transesterified with a lower alcohol in the presence of a solvent such as an alkyl chloride, an ether or an aromatic hydrocarbon solvent and a tertiary amine as a catalyst to obtain an aromatic dihydroxy compound and a dialkyl carbonate. A method has been proposed.
しかしながら、特許文献１の方法は溶媒と分解生成物との分離回収工程が煩雑である。特許文献２の方法は反応終了後、水中に反応混合物を投入し、芳香族ジヒドロキシ化合物を晶出させるか、分解混合物の数倍の量の溶媒を投入して、芳香族ジヒドロキシ化合物を析出させ、水洗する方法であり、この方法は使用したアルコールおよび溶剤の回収が非常に煩雑である。また、使用した溶剤を固体芳香族ジヒドロキシ化合物から除去するのが困難である。特許文献３の方法は、触媒としての３級アミンが、有機溶媒より多量用いられており、エバポレータなどで減圧除去を試みても、３級アミン、炭酸ジアルキルおよび芳香族ジヒドロキシ化合物をそれぞれ分離するのが非常に困難である。さらに、得られた芳香族ジヒドロキシ化合物中に末端停止剤が含有しており、末端停止剤の分離も必要である。実際、ポリカーボネートを製造する際、反応初期段階に末端停止剤が混入していると分子量調節が困難になるという不都合がある。 However, in the method of Patent Document 1, the separation and recovery step of the solvent and the decomposition product is complicated. In the method of Patent Document 2, after completion of the reaction, the reaction mixture is introduced into water to crystallize the aromatic dihydroxy compound, or a solvent several times the amount of the decomposition mixture is introduced to precipitate the aromatic dihydroxy compound, This is a method of washing with water, and in this method, the recovery of the used alcohol and solvent is very complicated. It is also difficult to remove the solvent used from the solid aromatic dihydroxy compound. In the method of Patent Document 3, a tertiary amine as a catalyst is used in a larger amount than an organic solvent, and even if an attempt is made to remove under reduced pressure with an evaporator or the like, the tertiary amine, dialkyl carbonate and aromatic dihydroxy compound are separated. Is very difficult. Furthermore, a terminal terminator is contained in the obtained aromatic dihydroxy compound, and it is necessary to separate the terminal terminator. In fact, when manufacturing polycarbonate, there is an inconvenience that it is difficult to adjust the molecular weight if a terminal terminator is mixed in the initial stage of the reaction.
本発明の目的は、廃芳香族ポリカーボネート（例えば不要となったＣＤ、ＣＤ−ＲＯＭ、ＤＶＤ等の芳香族ポリカーボネート製品）を安価で大量に処理し、高純度の芳香族ジヒドロキシ化合物を得る方法を提供することにある。 An object of the present invention is to provide a method for obtaining a high-purity aromatic dihydroxy compound by treating a large amount of waste aromatic polycarbonate (for example, aromatic polycarbonate products such as CDs, CD-ROMs, and DVDs that are no longer needed) at low cost. There is to do.
本発明の他の目的は、得られた芳香族ジヒドロキシ化合物を用いてＣＤ等に使用できる高品質の芳香族ポリカーボネートを製造する方法を提供することにある。 Another object of the present invention is to provide a method for producing a high-quality aromatic polycarbonate that can be used for CD or the like using the obtained aromatic dihydroxy compound.
本発明者は、これらの問題を解決するために鋭意検討した結果、廃芳香族ポリカーボネートをアルコールと塩素化化合物有機溶媒および金属水酸化物を用いた穏和な条件で、分解反応を進行させ、芳香族ジヒドロキシ化合物の有機溶媒溶液を得、さらに蒸留操作を行い有機溶媒およびジアルキルカーボネートと芳香族ジヒドロキシ化合物とを分離して芳香族ジヒドロキシ化合物を得、この芳香族ジヒドロキシ化合物を塩素化化合物有機溶媒と水で洗浄処理することにより高品質の芳香族ジヒドロキシ化合物が得られること、さらに該芳香族ジヒドロキシ化合物を用いて製造された芳香族ポリカーボネートの品質は市販のジヒドロキシ化合物を用いて製造した芳香族ポリカーボネートの品質と遜色ないことを見出し、本発明を完成した。 As a result of diligent investigations to solve these problems, the present inventor has promoted a decomposition reaction of waste aromatic polycarbonate under mild conditions using an alcohol, a chlorinated compound organic solvent, and a metal hydroxide, An organic solvent solution of an aromatic dihydroxy compound is obtained, and further an distillation operation is performed to separate the organic solvent and dialkyl carbonate from the aromatic dihydroxy compound to obtain an aromatic dihydroxy compound. The aromatic dihydroxy compound is chlorinated with the organic solvent and water. A high-quality aromatic dihydroxy compound can be obtained by washing with, and the quality of the aromatic polycarbonate produced using the aromatic dihydroxy compound is the quality of the aromatic polycarbonate produced using a commercially available dihydroxy compound. The present invention has been completed.
すなわち、本発明によれば、
１．（Ａ）廃芳香族ポリカーボネートを炭素数１〜４のアルコール、塩素化化合物有機溶媒および金属水酸化物の存在下、エステル交換反応により分解反応せしめる工程（ａ工程）、（Ｂ）分解反応後の反応液に酸水溶液を加え、有機溶媒相と水溶液相とを分液し、有機溶媒相を回収する工程（ｂ工程）、（Ｃ）この有機溶媒相から蒸留により有機溶媒およびジアルキルカーボネートと芳香族ジヒドロキシ化合物とを分離して芳香族ジヒドロキシ化合物を得る工程（ｃ工程）および（Ｄ）得られた芳香族ジヒドロキシ化合物を塩素化化合物有機溶媒及び／又は水で洗浄する工程（ｄ工程）からなる廃芳香族ポリカーボネートから芳香族ジヒドロキシ化合物を得る方法。
That is, according to the present invention,
1. (A) a step of decomposing a waste aromatic polycarbonate by transesterification in the presence of an alcohol having 1 to 4 carbon atoms, a chlorinated compound organic solvent and a metal hydroxide (step a), (B) after the decomposition reaction An acid aqueous solution is added to the reaction solution, and the organic solvent phase and the aqueous solution phase are separated, and the organic solvent phase is recovered (step b). (C) The organic solvent, dialkyl carbonate and aromatic are distilled from the organic solvent phase. Waste consisting of the step of obtaining an aromatic dihydroxy compound by separating the dihydroxy compound (step c) and the step (D) of washing the obtained aromatic dihydroxy compound with a chlorinated compound organic solvent and / or water (step d) A method for obtaining an aromatic dihydroxy compound from an aromatic polycarbonate.
２．前記ａ工程において使用する金属水酸化物が水酸化ナトリウムおよび／または水酸化カリウムである前項１記載の廃芳香族ポリカーボネートから芳香族ジヒドロキシ化合物を得る方法。 2. 2. The method for obtaining an aromatic dihydroxy compound from the waste aromatic polycarbonate according to item 1, wherein the metal hydroxide used in the step a is sodium hydroxide and / or potassium hydroxide.
３．前記ｂ工程において使用する酸水溶液が塩酸、硫酸、硝酸またはリン酸の水溶液である前項１記載の廃芳香族ポリカーボネートから芳香族ジヒドロキシ化合物を得る方法。 3. The method for obtaining an aromatic dihydroxy compound from the waste aromatic polycarbonate according to item 1, wherein the acid aqueous solution used in the step b is an aqueous solution of hydrochloric acid, sulfuric acid, nitric acid or phosphoric acid.
４．前記ａ工程およびｄ工程において使用する塩素化化合物有機溶媒がジクロロメタン、ジクロロエタンおよびクロロホルムからなる群より選ばれる少なくとも１種の溶媒である前項１記載の廃芳香族ポリカーボネートから芳香族ジヒドロキシ化合物を得る方法。 4). The method for obtaining an aromatic dihydroxy compound from the waste aromatic polycarbonate according to item 1, wherein the chlorinated compound organic solvent used in the steps a and d is at least one solvent selected from the group consisting of dichloromethane, dichloroethane and chloroform.
５．前記ｄ工程において、芳香族ジヒドロキシ化合物の洗浄に用いる水の電気伝導度が５０μＳ／ｃｍ以下である前項１記載の廃芳香族ポリカーボネートから芳香族ジヒドロキシ化合物を得る方法。 5. 2. The method for obtaining an aromatic dihydroxy compound from the waste aromatic polycarbonate according to item 1, wherein the electric conductivity of water used for washing the aromatic dihydroxy compound in the step d is 50 μS / cm or less.
６．前記ｄ工程において、洗浄方法がバッチ式であり、芳香族ジヒドロキシ化合物の洗浄を塩素化化合物有機溶媒と水と交互に行う前項１記載の廃芳香族ポリカーボネートから芳香族ジヒドロキシ化合物を得る方法。 6). The method of obtaining an aromatic dihydroxy compound from the waste aromatic polycarbonate according to the preceding item 1, wherein, in the step d, the cleaning method is a batch type, and the aromatic dihydroxy compound is washed alternately with a chlorinated compound organic solvent and water.
７．前項１〜６のいずれか１項に記載の方法により得られた芳香族ジヒドロキシ化合物を芳香族ポリカーボネートの製造工程に用いる芳香族ポリカーボネートの製造方法。
が提供される。
7). The manufacturing method of an aromatic polycarbonate which uses the aromatic dihydroxy compound obtained by the method of any one of the preceding clauses 1-6 for the manufacturing process of an aromatic polycarbonate.
Is provided.
以下、本発明を詳細に説明する。
本発明において、使用される廃芳香族ポリカーボネートは、界面重合法や溶融重合法等公知の方法で製造されたものでよく、分子量は粘度平均分子量で１０００〜１０００００のものが好ましい。廃芳香族ポリカーボネートの形状はパウダー、ペレット、シート、フィルム、成形品等特に限定されない。例えば、ＣＤ、ＣＤ−Ｒ、ＤＶＤ等の光ディスクにおいて、廃棄されたものや成形不良のものなど不要になった廃光ディスクをそのままあるいは印刷膜や金属膜を剥離し除去したものを分解に使用することができる。また、分解に用いられる廃芳香族ポリカーボネートとして、ポリカーボネート製造途中に目標とする分子量に到達せず、パウダーあるいはペレット化されなかったポリカーボネートの溶液から溶媒を除去し、乾燥した固形物でもよい。ここで、ポリカーボネート樹脂の粘度平均分子量（Ｍ）は塩化メチレン１００ｍｌにポリカーボネート樹脂０．７ｇを２０℃で溶解した溶液から求めた比粘度（ηｓｐ）を次式に挿入して求めたものである。
ηｓｐ／ｃ＝［η］＋０．４５×［η］２ｃ（但し［η］は極限粘度）
［η］＝１．２３×１０−４Ｍ０．８３
ｃ＝０．７
Hereinafter, the present invention will be described in detail.
In the present invention, the waste aromatic polycarbonate to be used may be one produced by a known method such as an interfacial polymerization method or a melt polymerization method, and the molecular weight is preferably a viscosity average molecular weight of 1000 to 100,000. The shape of the waste aromatic polycarbonate is not particularly limited, such as powder, pellets, sheets, films, and molded products. For example, optical discs such as CDs, CD-Rs, DVDs, etc., which are no longer used, such as discarded ones or defective ones, are used as they are, or ones that have been removed by removing the printed film or metal film are used for disassembly. Can do. Further, the waste aromatic polycarbonate used for decomposition may be a solid obtained by removing the solvent from the solution of the polycarbonate that has not reached the target molecular weight during the production of the polycarbonate, and has not been pelletized or pelletized. Here, the viscosity average molecular weight (M) of the polycarbonate resin is obtained by inserting the specific viscosity (η sp ) obtained from a solution obtained by dissolving 0.7 g of the polycarbonate resin in 100 ml of methylene chloride at 20 ° C. into the following equation. .
η sp /c=[η]+0.45×[η] 2 c (where [η] is the intrinsic viscosity)
[Η] = 1.23 × 10 −4 M 0.83
c = 0.7
該ポリカーボネートは、ハイドロキノン、レゾルシノール、４，４′−ジヒドロキシジフェニル、１，４−ジヒドロキシナフタレン、ビス（４−ヒドロキシフェニル）メタン、ビス｛（４−ヒドロキシ−３，５−ジメチル）フェニル｝メタン、１，１−ビス（４−ヒドロキシフェニル）エタン、１，１−ビス（４−ヒドロキシフェニル）−１−フェニルエタン、２，２−ビス（４−ヒドロキシフェニル）プロパン（通称ビスフェノールＡ）、２，２−ビス｛（４−ヒドロキシ−３−メチル）フェニル｝プロパン、２，２−ビス｛（４−ヒドロキシ−３，５−ジメチル）フェニル｝プロパン、２，２−ビス｛（３，５−ジブロモ−４−ヒドロキシ）フェニル｝プロパン、２，２−ビス｛（３−イソプロピル−４−ヒドロキシ）フェニル｝プロパン、２，２−ビス｛（４−ヒドロキシ−３−フェニル）フェニル｝プロパン、２，２−ビス（４−ヒドロキシフェニル）ブタン、２，２−ビス（４−ヒドロキシフェニル）−３−メチルブタン、２，２−ビス（４−ヒドロキシフェニル）−３，３−ジメチルブタン、２，４−ビス（４−ヒドロキシフェニル）−２−メチルブタン、２，２−ビス（４−ヒドロキシフェニル）ペンタン、２，２−ビス（４−ヒドロキシフェニル）−４−メチルペンタン、１，１−ビス（４−ヒドロキシフェニル）シクロヘキサン、１，１−ビス（４−ヒドロキシフェニル）−４−イソプロピルシクロヘキサン、１，１−ビス（４−ヒドロキシフェニル）−３，３，５−トリメチルシクロヘキサン、９，９−ビス（４−ヒドロキシフェニル）フルオレン、９，９−ビス｛（４−ヒドロキシ−３−メチル）フェニル｝フルオレン、α，α′−ビス（４−ヒドロキシフェニル）−ｏ−ジイソプロピルベンゼン、α，α′−ビス（４−ヒドロキシフェニル）−ｍ−ジイソプロピルベンゼン、α，α′−ビス（４−ヒドロキシフェニル）−ｐ−ジイソプロピルベンゼン、１，３−ビス（４−ヒドロキシフェニル）−５，７−ジメチルアダマンタン、４，４′−ジヒドロキシジフェニルスルホン、４，４′−ジヒドロキシジフェニルスルホキシド、４，４′−ジヒドロキシジフェニルスルフィド、４，４′−ジヒドロキシジフェニルケトン、４，４′−ジヒドロキシジフェニルエーテルおよび４，４′−ジヒドロキシジフェニルエステル等のジヒドロキシ化合物の単独または２種以上の混合物から製造されたものである。 The polycarbonate includes hydroquinone, resorcinol, 4,4′-dihydroxydiphenyl, 1,4-dihydroxynaphthalene, bis (4-hydroxyphenyl) methane, bis {(4-hydroxy-3,5-dimethyl) phenyl} methane, , 1-bis (4-hydroxyphenyl) ethane, 1,1-bis (4-hydroxyphenyl) -1-phenylethane, 2,2-bis (4-hydroxyphenyl) propane (commonly called bisphenol A), 2,2 -Bis {(4-hydroxy-3-methyl) phenyl} propane, 2,2-bis {(4-hydroxy-3,5-dimethyl) phenyl} propane, 2,2-bis {(3,5-dibromo- 4-hydroxy) phenyl} propane, 2,2-bis {(3-isopropyl-4-hydroxy) phenyl} propa 2,2-bis {(4-hydroxy-3-phenyl) phenyl} propane, 2,2-bis (4-hydroxyphenyl) butane, 2,2-bis (4-hydroxyphenyl) -3-methylbutane, , 2-bis (4-hydroxyphenyl) -3,3-dimethylbutane, 2,4-bis (4-hydroxyphenyl) -2-methylbutane, 2,2-bis (4-hydroxyphenyl) pentane, 2,2 -Bis (4-hydroxyphenyl) -4-methylpentane, 1,1-bis (4-hydroxyphenyl) cyclohexane, 1,1-bis (4-hydroxyphenyl) -4-isopropylcyclohexane, 1,1-bis ( 4-hydroxyphenyl) -3,3,5-trimethylcyclohexane, 9,9-bis (4-hydroxyphenyl) fluorene, 9,9- {(4-hydroxy-3-methyl) phenyl} fluorene, α, α'-bis (4-hydroxyphenyl) -o-diisopropylbenzene, α, α'-bis (4-hydroxyphenyl) -m-diisopropylbenzene , Α, α'-bis (4-hydroxyphenyl) -p-diisopropylbenzene, 1,3-bis (4-hydroxyphenyl) -5,7-dimethyladamantane, 4,4'-dihydroxydiphenylsulfone, 4,4 Single or two or more of dihydroxy compounds such as' -dihydroxydiphenyl sulfoxide, 4,4'-dihydroxydiphenyl sulfide, 4,4'-dihydroxydiphenyl ketone, 4,4'-dihydroxydiphenyl ether and 4,4'-dihydroxydiphenyl ester Made from a mixture of
また、末端停止剤（分子量調節剤）としては、１価のフェノール化合物が好ましく用いられ、フェノール、ｐ−クレゾール、ｐ−エチルフェノール、ｐ−イソプロピルフェノール、ｐ−ｔｅｒｔ−ブチルフェノール、ｐ−クミルフェノール、ｐ−シクロヘキシルフェノール、ｐ−オクチルフェノール、ｐ−ノニルフェノール、２，４−キシレノール、ｐ−メトキシフェノール、ｐ−ヘキシルオキシフェノール、ｐ−デシルオキシフェノール、ｏ−クロロフェノール、ｍ−クロロフェノール、ｐ−クロロフェノール、ｐ−ブロモフェノール、ペンタブロモフェノール、ペンタクロロフェノール、ｐ−フェニルフェノール、ｐ−イソプロペニルフェノール、２，４−ジ（１’−メチル−１’−フェニルエチル）フェノール、β−ナフトール、α−ナフトール、ｐ−（２’，４’，４’−トリメチルクロマニル）フェノール、２−（４’−メトキシフェニル）−２−（４’’−ヒドロキシフェニル）プロパン等のフェノール類等の単独または２種以上の混合物が用いられる。 Moreover, as a terminal stopper (molecular weight regulator), a monovalent phenol compound is preferably used, and phenol, p-cresol, p-ethylphenol, p-isopropylphenol, p-tert-butylphenol, p-cumylphenol. , P-cyclohexylphenol, p-octylphenol, p-nonylphenol, 2,4-xylenol, p-methoxyphenol, p-hexyloxyphenol, p-decyloxyphenol, o-chlorophenol, m-chlorophenol, p-chloro Phenol, p-bromophenol, pentabromophenol, pentachlorophenol, p-phenylphenol, p-isopropenylphenol, 2,4-di (1′-methyl-1′-phenylethyl) phenol, β-naphthol, α -NA Phthol, phenols such as p- (2 ′, 4 ′, 4′-trimethylchromanyl) phenol, 2- (4′-methoxyphenyl) -2- (4 ″ -hydroxyphenyl) propane, etc. alone or 2 A mixture of seeds or more is used.
（ａ工程について）
本発明において、まず、（Ａ）廃芳香族ポリカーボネートを炭素数１〜４のアルコール、塩素化化合物有機溶媒および金属水酸化物の存在下、エステル交換反応により分解反応せしめる工程（ａ工程）が行われる。
(About step a)
In the present invention, first, (A) a step (a step) in which waste aromatic polycarbonate is decomposed by transesterification in the presence of an alcohol having 1 to 4 carbon atoms, a chlorinated compound organic solvent, and a metal hydroxide is performed. Is called.
ａ工程では、アルコールと塩素化化合物有機溶媒と金属水酸化物の存在下で芳香族ポリカーボネートの分解（解重合反応）が行われる。塩素化化合物有機溶媒と金属水酸化物を使用すると分解反応が低温で進み易く好ましい。 In step a, the aromatic polycarbonate is decomposed (depolymerization reaction) in the presence of an alcohol, a chlorinated compound organic solvent, and a metal hydroxide. It is preferable to use a chlorinated compound organic solvent and a metal hydroxide because the decomposition reaction easily proceeds at a low temperature.
芳香族ポリカーボネートの分解に使用される炭素数１〜４のアルコールとしては、メタノール、エタノール、１−プロパノール、２−プロパノール（イソプロピルアルコール）、１−ブタノール、２−ブタノール、２−メチル−１−プロパノール（イソブチルアルコール）、１，１−ジメチル−１−エタノール（ｔ−ブチルアルコール）が挙げられる。特にメタノールが好ましい。炭素数５以上のアルコールでは、分解反応が遅く、精製、分離工程において、分離が難しくなるので好ましくない。 Examples of the alcohol having 1 to 4 carbon atoms used for the decomposition of the aromatic polycarbonate include methanol, ethanol, 1-propanol, 2-propanol (isopropyl alcohol), 1-butanol, 2-butanol, and 2-methyl-1-propanol. (Isobutyl alcohol) and 1,1-dimethyl-1-ethanol (t-butyl alcohol). Methanol is particularly preferable. Alcohols having 5 or more carbon atoms are not preferable because the decomposition reaction is slow and separation is difficult in the purification and separation steps.
アルコールの使用量は、芳香族ポリカーボネートのカーボネート結合１モルに対して、好ましくは２．４〜７モルであり、さらに好ましくは３〜７モルである。モル比が７モルより多いと芳香族ジヒドロキシ化合物の回収率が悪化し、さらに未反応アルコールの分離、回収に多大なコストがかかることがある。また、モル比が２．４モルより小さいと分解反応速度が遅いか、またはポリカーボネート樹脂が完全に分解されずにカーボネートオリゴマーが残存し易く、芳香族ジヒドロキシ化合物の回収率が低下することがある。 The amount of the alcohol used is preferably 2.4 to 7 mol, more preferably 3 to 7 mol, per 1 mol of the carbonate bond of the aromatic polycarbonate. When the molar ratio is more than 7 moles, the recovery rate of the aromatic dihydroxy compound is deteriorated, and further, the separation and recovery of the unreacted alcohol may be costly. On the other hand, when the molar ratio is less than 2.4 mol, the decomposition reaction rate is slow, or the polycarbonate resin is not completely decomposed and the carbonate oligomer tends to remain, and the recovery rate of the aromatic dihydroxy compound may decrease.
本発明において使用される分解触媒は金属水酸化物である。金属水酸化物の非存在下では分解反応は進行しない。金属水酸化物としては水酸化ナトリウムおよび／または水酸化カリウムが好ましく使用できる。特に水酸化ナトリウムが好ましい。 The cracking catalyst used in the present invention is a metal hydroxide. The decomposition reaction does not proceed in the absence of metal hydroxide. As the metal hydroxide, sodium hydroxide and / or potassium hydroxide can be preferably used. Sodium hydroxide is particularly preferable.
金属水酸化物の使用量は、ポリカーボネートのカーボネート結合１モルに対して０．００２〜０．４モルが好ましい。金属水酸化物の使用量が０．００２モルより少ないと分解反応速度は大きく低下する。０．４モルより多いと経済的に不利となり、また炭酸ジアルキルの分解が起こり易くなる。 The amount of the metal hydroxide used is preferably 0.002 to 0.4 mol with respect to 1 mol of the carbonate bond of the polycarbonate. When the amount of metal hydroxide used is less than 0.002 mol, the decomposition reaction rate is greatly reduced. When the amount is more than 0.4 mol, it is economically disadvantageous, and the decomposition of the dialkyl carbonate tends to occur.
通常、芳香族ポリカーボネートの製造で用いる金属水酸化物は固形、または水溶液の状態で購入、使用される。反応系内に水が多量に存在すると、触媒と生成した芳香族ジヒドロキシ化合物が反応して塩になり析出し、触媒が消費されてしまい、分解反応が非常に遅くなる。また、回収可能な炭酸ジアルキルの収率が低下する。特に、金属水酸化物の水溶液を使用する場合、反応系内に水分が多くなり易い。反応系内の水を除去する方法としては、塩素化化合物有機溶媒と金属水酸化物水溶液を混合、共沸してデカンタで分離する方法、混合液を脱水剤（吸着剤）に通す方法等いくつかの方法が挙げられるが、どの方法で除去しても差し支えない。分解反応を行う前（分解反応初期）の系内（すなわち分解反応処理される溶液中）の水分量は２．５重量％以下が好ましく、１重量％以下がより好ましく、０．５重量％以下がさらに好ましく、特に０．３重量％以下が好ましい。 Usually, the metal hydroxide used in the production of the aromatic polycarbonate is purchased and used in the form of a solid or an aqueous solution. When a large amount of water is present in the reaction system, the catalyst and the generated aromatic dihydroxy compound react to form a salt, which is consumed, and the decomposition reaction becomes very slow. In addition, the yield of recoverable dialkyl carbonate decreases. In particular, when an aqueous solution of metal hydroxide is used, water tends to increase in the reaction system. There are several methods for removing water from the reaction system, such as mixing chlorinated compound organic solvent and metal hydroxide aqueous solution, azeotropically separating them with a decanter, and passing the mixture through a dehydrating agent (adsorbent). However, it can be removed by any method. The amount of water in the system (that is, in the solution subjected to the decomposition reaction) before the decomposition reaction (that is, in the solution subjected to the decomposition reaction) is preferably 2.5% by weight or less, more preferably 1% by weight or less, and 0.5% by weight or less. Is more preferable, and 0.3% by weight or less is particularly preferable.
本発明において使用される有機溶媒は塩素化化合物有機溶媒であり、具体的にはジクロロメタン、クロロホルム、ジクロロエタン、トリクロロエタン、テトラクロロエタン、ジクロロエチレン等が挙げられ、ジクロロメタン、ジクロロエタンおよびクロロホルムからなる群より選ばれる少なくとも１種の溶媒が好適であり、特にジクロロメタンが好適である。これらの溶媒は、ポリカーボネートの良溶媒で、実際にポリカーボネートの製造工程において反応溶媒として用いられており、分解、分離後の芳香族ジヒドロキシ化合物にこれらの溶媒が残留していても、ポリカーボネート製造に悪影響を及ぼさない利点がある。 The organic solvent used in the present invention is a chlorinated compound organic solvent, and specifically includes dichloromethane, chloroform, dichloroethane, trichloroethane, tetrachloroethane, dichloroethylene, etc., and at least selected from the group consisting of dichloromethane, dichloroethane and chloroform One solvent is preferred, especially dichloromethane. These solvents are good solvents for polycarbonate, and are actually used as reaction solvents in the polycarbonate production process. Even if these solvents remain in the aromatic dihydroxy compound after decomposition and separation, they adversely affect polycarbonate production. There is an advantage that does not affect.
本発明において、塩素化化合物有機溶媒の使用量は、ポリカーボネート樹脂１００重量部に対し４０重量部〜１０００重量部の範囲が好ましい。溶媒量が４０重量部より少ないと、初期の混合がうまくいかず、さらにポリカーボネート樹脂が充分膨潤または溶解せず、分解反応終了までの時間が長くなることがある。また１０００重量部より多いと、反応系内のカーボネート結合濃度、触媒濃度が低くなり、分解反応速度が低下し、分解反応時間が長くなり、また溶媒の回収コストが高くなることがある。なお、光ディスク等の成形品はあらかじめ０．１〜２ｃｍ程度の大きさに粉砕し、この粉砕物を溶解すると溶解時間が短縮されるため好ましい。 In this invention, the usage-amount of a chlorinated compound organic solvent has the preferable range of 40 weight part-1000 weight part with respect to 100 weight part of polycarbonate resin. If the amount of the solvent is less than 40 parts by weight, the initial mixing may not be successful, the polycarbonate resin may not be sufficiently swollen or dissolved, and the time until the decomposition reaction may be prolonged. On the other hand, when the amount is more than 1000 parts by weight, the carbonate bond concentration and the catalyst concentration in the reaction system become low, the decomposition reaction rate decreases, the decomposition reaction time becomes long, and the solvent recovery cost may increase. In addition, it is preferable that a molded product such as an optical disk is pulverized to a size of about 0.1 to 2 cm in advance and the pulverized material is dissolved, because the dissolution time is shortened.
分解反応において、廃ポリカーボネートをあらかじめ塩素化化合物有機溶媒に溶解しておいてもよいし、全てを溶解させずに分解反応を行なう反応器に投入してもよい。反応器とは別に溶解槽を使用し、該有機溶媒にポリカーボネート樹脂を溶解させた場合、該有機溶媒に溶解しない不純物、例えば成型品中に含まれる添加剤、金属膜、コーティング剤、充填剤等をろ過し、除去することが可能である。除去しないで分解反応を行った場合、これらの不純物も分解され、芳香族ジヒドロキシ化合物に混入し、不純物分解物が混ざったままポリカーボネート製造工程に使用すると、製品のポリカーボネート樹脂の品質に悪影響を及ぼす可能性があるので、あらかじめ不溶物を除去することが好ましい。 In the decomposition reaction, the waste polycarbonate may be dissolved in advance in a chlorinated compound organic solvent, or may be charged into a reactor that performs the decomposition reaction without dissolving all of the polycarbonate. When a dissolution tank is used separately from the reactor and the polycarbonate resin is dissolved in the organic solvent, impurities that do not dissolve in the organic solvent, such as additives, metal films, coating agents, fillers, etc. contained in the molded product Can be filtered off. If the decomposition reaction is performed without removing these impurities, these impurities are also decomposed, mixed into the aromatic dihydroxy compound, and if used in the polycarbonate manufacturing process with the impurity decomposition products mixed, it may adversely affect the quality of the product polycarbonate resin. Therefore, it is preferable to remove insoluble matters in advance.
本発明において、分解反応を行う温度は３０℃〜９０℃が好ましい。３０℃未満の場合は分解反応時間が長くなり、処理効率が著しく劣ることがある。また、９０℃を越えると、加熱のエネルギーが多く必要となり、さらに分解処理中に溶液の色が褐色に着色し易く、品質の良い芳香族ジヒドロキシ化合物が得られなくなることがある。 In the present invention, the temperature at which the decomposition reaction is performed is preferably 30 ° C to 90 ° C. When it is less than 30 ° C., the decomposition reaction time becomes long, and the processing efficiency may be remarkably inferior. If the temperature exceeds 90 ° C., a large amount of heating energy is required, and the color of the solution tends to turn brown during the decomposition treatment, and a high-quality aromatic dihydroxy compound may not be obtained.
分解反応中に生成した芳香族ジヒドロキシ化合物は、塩基性条件下では酸化されやすいので、反応溶液中に酸化防止剤を添加することが好ましい。また、工程内の酸素濃度を不活性ガスにより、低減しておくことも有効である。 Since the aromatic dihydroxy compound produced during the decomposition reaction is easily oxidized under basic conditions, it is preferable to add an antioxidant to the reaction solution. It is also effective to reduce the oxygen concentration in the process with an inert gas.
酸化防止剤として、重亜硫酸ナトリウム（Ｎａ２Ｓ２Ｏ５）、亜硫酸ナトリウム（Ｎａ２ＳＯ３）、ハイドロサルファイトナトリウム（Ｎａ２Ｓ２Ｏ４）等が挙げられる。これらを１種または２種以上混合して用いても差し支えない。酸化防止剤の使用量は芳香族ポリカーボネート１００重量部に対し、０．０５〜４．０重量部が好ましい。０．０５〜４．０重量部の範囲であると酸化防止効果があり、また、コスト的に有利で、分解反応速度が低下せず好ましい。
不活性ガスの種類として、窒素、アルゴン等が挙げられる。窒素がコスト的に有利であり好ましい。
Examples of the antioxidant include sodium bisulfite (Na 2 S 2 O 5 ), sodium sulfite (Na 2 SO 3 ), and sodium hydrosulfite (Na 2 S 2 O 4 ). These may be used alone or in combination of two or more. As for the usage-amount of antioxidant, 0.05-4.0 weight part is preferable with respect to 100 weight part of aromatic polycarbonate. If it is in the range of 0.05 to 4.0 parts by weight, it has an antioxidant effect, is advantageous in terms of cost, and is preferable because the decomposition reaction rate does not decrease.
Nitrogen, argon etc. are mentioned as a kind of inert gas. Nitrogen is preferred because of its cost advantage.
（ｂ工程について）
ａ工程の分解反応後、（Ｂ）分解反応後の反応液に酸水溶液を加え、有機溶媒相と水溶液相とを分液し、有機溶媒相を回収する工程（ｂ工程）を行なう。
分解反応後の反応液に酸水溶液を加え中和することにより、芳香族ジヒドロキシ化合物は塩素化化合物有機溶媒相に溶解する。酸水溶液としては塩酸、硫酸、硝酸またはリン酸等の無機酸の水溶液が好ましく用いられる。加える酸水溶液の量は、水溶液相が中性〜酸性になるような量が必要であり、中性のｐＨ６〜８の範囲になるような量が特に好ましい。酸を加えずに水を加えると炭酸ジアルキルの加水分解が起こり、さらに芳香族ジヒドロキシ化合物が金属水酸化物と反応して塩になり、それぞれ収率が低下することとなる。また、反応混合物のまま溶媒を除去すると、芳香族ジヒドロキシ化合物が金属水酸化物と反応して塩になり、着色成分が発生する。このため、着色成分を除去する工程が必要になり、不利な方法となる。
(About step b)
After the decomposition reaction of step a, (B) a step (step b) of adding an acid aqueous solution to the reaction solution after the decomposition reaction, separating the organic solvent phase and the aqueous solution phase, and recovering the organic solvent phase.
The aromatic dihydroxy compound is dissolved in the organic solvent phase of the chlorinated compound by neutralizing the reaction solution after the decomposition reaction by adding an aqueous acid solution. As the acid aqueous solution, an aqueous solution of an inorganic acid such as hydrochloric acid, sulfuric acid, nitric acid or phosphoric acid is preferably used. The amount of the acid aqueous solution to be added needs to be such that the aqueous solution phase is neutral to acidic, and is particularly preferably such that the pH is in the neutral pH range of 6 to 8. When water is added without adding an acid, hydrolysis of the dialkyl carbonate occurs, and the aromatic dihydroxy compound reacts with the metal hydroxide to form a salt, and the yield decreases. Further, when the solvent is removed in the reaction mixture, the aromatic dihydroxy compound reacts with the metal hydroxide to form a salt, and a colored component is generated. For this reason, the process of removing a coloring component is needed and it becomes a disadvantageous method.
分解反応後の反応液に酸水溶液を加えると、有機溶媒相と水溶液相との２つの相に分離し、有機溶媒相と水溶液相をデカンター等の液液分離器で分離して有機溶媒相を回収する。液液分離器において分離が不十分であると、有機溶媒相に粒状に浮遊している水が次の工程に混入し、製品に影響を及ぼすので、有機溶媒相をさらに純水と接触させ、可能な限り除去することが好ましい。この方法は、洗浄塔による接触、撹拌機、液液分離器による分離、遠心分離機など、公知の方法が使用できる。 When an aqueous acid solution is added to the reaction solution after the decomposition reaction, it is separated into two phases, an organic solvent phase and an aqueous solution phase, and the organic solvent phase and the aqueous solution phase are separated by a liquid-liquid separator such as a decanter, and the organic solvent phase is separated. to recover. If separation is insufficient in the liquid-liquid separator, water suspended in a granular form in the organic solvent phase is mixed in the next step, affecting the product, so the organic solvent phase is further brought into contact with pure water, It is preferable to remove as much as possible. As this method, a known method such as contact with a washing tower, separation with a stirrer, liquid-liquid separator, or centrifugal separator can be used.
（ｃ工程について）
ｂ工程で回収された有機溶媒相から蒸留により有機溶媒およびジアルキルカーボネートと芳香族ジヒドロキシ化合物とを分離して芳香族ジヒドロキシ化合物を得る工程（ｃ工程）が行われる。
(About step c)
A step (step c) of separating the organic solvent, dialkyl carbonate and aromatic dihydroxy compound by distillation from the organic solvent phase recovered in step b to obtain an aromatic dihydroxy compound is performed.
蒸留操作は減圧または常圧で行われ、その方法はバッチ式でも連続式でもよいが、芳香族ジヒドロキシ化合物を析出させるためにはバッチ式の方が好ましい。蒸留は有機溶媒および生成するジアルキルカーボネートが留去できる温度、圧力条件が必要とされるが、芳香族ジヒドロキシ化合物の熱分解を抑えるため、蒸留温度（蒸留槽ボトム温度）は１００℃以下とすることが好ましい。 The distillation operation is carried out under reduced pressure or atmospheric pressure, and the method may be either batch type or continuous type, but batch type is preferred for precipitation of the aromatic dihydroxy compound. Distillation requires temperature and pressure conditions at which the organic solvent and the dialkyl carbonate to be produced can be distilled off, but in order to suppress thermal decomposition of the aromatic dihydroxy compound, the distillation temperature (distillation tank bottom temperature) should be 100 ° C or lower. Is preferred.
（ｄ工程について）
ｃ工程の蒸留操作により分離して得られた芳香族ジヒドロキシ化合物は微量のジアルキルカーボネート、末端停止剤、ポリカーボネート由来の炭酸塩および金属水酸化物と酸水溶液が反応して生成した中性塩等の不純物を含んでいる。これらの不純物を除去するために、次いで（Ｄ）得られた芳香族ジヒドロキシ化合物を塩素化化合物有機溶媒及び／又は水で洗浄する工程（ｄ工程）が行われる。
(About step d)
The aromatic dihydroxy compound obtained by separation by the distillation operation in step c includes a trace amount of a dialkyl carbonate, a terminal terminator, a carbonate derived from polycarbonate, and a neutral salt produced by reacting a metal hydroxide with an acid aqueous solution. Contains impurities. In order to remove these impurities, (D) a step (step d) of washing the obtained aromatic dihydroxy compound with a chlorinated compound organic solvent and / or water is then performed.
塩素化化合物有機溶媒としては、２５℃における芳香族ジヒドロキシ化合物の溶解度が２０ｇ／Ｌ以下で、２５℃における芳香族モノヒドロキシ化合物（末端停止剤）の溶解度が５０ｇ／Ｌ以上である溶媒が好ましく、具体的にはジクロロメタン、クロロホルム、ジクロロエタン、トリクロロエタン、テトラクロロエタン、ジクロロエチレン等が好ましく、ジクロロメタン（塩化メチレン）が特に好ましく用いられる。水は５０μＳ／ｃｍ以下の電気伝導度の純水を用いることが好ましい。 As the chlorinated compound organic solvent, a solvent in which the solubility of the aromatic dihydroxy compound at 25 ° C. is 20 g / L or less and the solubility of the aromatic monohydroxy compound (terminal stopper) at 25 ° C. is 50 g / L or more is preferable. Specifically, dichloromethane, chloroform, dichloroethane, trichloroethane, tetrachloroethane, dichloroethylene and the like are preferable, and dichloromethane (methylene chloride) is particularly preferably used. It is preferable to use pure water having an electric conductivity of 50 μS / cm or less.
また、洗浄される芳香族ジヒドロキシ化合物は、その平均粒径（重量平均粒子径）が好ましくは１００〜１０００μｍ、より好ましくは１００〜８００μｍ、特に好ましくは２００〜６００μｍである。前記範囲の平均粒径の芳香族ジヒドロキシ化合物を使用すると効率良く洗浄できるため好ましい。 The aromatic dihydroxy compound to be washed preferably has an average particle size (weight average particle size) of 100 to 1000 μm, more preferably 100 to 800 μm, and particularly preferably 200 to 600 μm. Use of an aromatic dihydroxy compound having an average particle diameter in the above range is preferable because it can be efficiently washed.
洗浄の方法は、固体の芳香族ジヒドロキシ化合物を攪拌槽に移し、有機溶媒と水を同時または別々に投入し、攪拌、ろ過する方法、遠心分離機内で有機溶媒と水を同時または交互に振りかけそのまま遠心分離で脱液する方法等が挙げられる。特に、バッチ式で有機溶媒と水を交互に使用して洗浄する方法が好ましく、それぞれ２回以上洗浄する方法が好ましい。 The washing method is a method in which a solid aromatic dihydroxy compound is transferred to a stirring tank, and an organic solvent and water are added simultaneously or separately, followed by stirring and filtering. The organic solvent and water are sprinkled simultaneously or alternately in a centrifuge. Examples include a method of removing liquid by centrifugation. In particular, a cleaning method using an organic solvent and water alternately in batch mode is preferable, and a method of cleaning twice or more is preferable.
上記ろ過により洗浄する方法において、使用するろ過器は好ましくは目開き１〜１００μｍ、より好ましくは目開き１０〜５０μｍのフィルターを備えている。目開きが１μｍを下回ると濾過時間が長くなり生産効率が落ちることがあり、１００μｍを超えると芳香族ジヒドロキシ化合物の粉体が母液と共に流出し易くなり、歩留まり低下ひいてはコストアップとなることがある。フィルターの材質はＰＥＴ、ナイロン、セルロース等の樹脂製、もしくはセラミック、ステンレス等の金属製のものが好ましく用いられる。また、芳香族ジヒドロキシ化合物の濾過時の差圧を好ましくは０．０１ＭＰａ以上、より好ましくは０．０５ＭＰａ以上与えることが望ましい。差圧の上限は特に限定されないが１ＭＰａ以下で十分な効果を有する。 In the method of washing by filtration, the filter used is preferably provided with a filter having an opening of 1 to 100 μm, more preferably an opening of 10 to 50 μm. If the mesh opening is less than 1 μm, the filtration time may be prolonged and the production efficiency may be lowered. If the mesh opening exceeds 100 μm, the aromatic dihydroxy compound powder tends to flow out together with the mother liquor, resulting in a decrease in yield and an increase in cost. The filter material is preferably made of a resin such as PET, nylon, or cellulose, or a metal such as ceramic or stainless steel. Further, it is desirable that the differential pressure during filtration of the aromatic dihydroxy compound is preferably 0.01 MPa or more, more preferably 0.05 MPa or more. The upper limit of the differential pressure is not particularly limited, but a sufficient effect is obtained at 1 MPa or less.
上記遠心分離機により洗浄する方法において、好ましくは遠心力１００〜１０００Ｇ、より好ましくは遠心力２００〜７００Ｇの条件により洗浄液は除去される。遠心力が１００Ｇを下回ると十分な洗浄効果が得られないことがあり、芳香族ジヒドロキシ化合物中に水溶性塩が残存し易くなる。１０００Ｇを越えると水溶性塩の残存量は減少するが、動力が過大になりコストアップにつながり経済的に不利となることがある。また、遠心分離機の金属製脱水部（バスケット部）の孔径は１〜５０ｍｍが好ましく、５〜２０ｍｍが特に好ましい。また金属製脱水部に取り付ける濾過フィルターの材質は綿やＰＥＴ、ナイロン製等の樹脂製が好ましく、濾過フィルターの孔径が好ましくは１０〜１０００μｍであり、より好ましくは１０〜５００μｍ、さらに好ましくは１０〜３００μｍである。 In the method of washing with the centrifuge, the washing liquid is preferably removed under conditions of a centrifugal force of 100 to 1000 G, more preferably a centrifugal force of 200 to 700 G. When the centrifugal force is less than 100 G, a sufficient cleaning effect may not be obtained, and the water-soluble salt tends to remain in the aromatic dihydroxy compound. If it exceeds 1000 G, the remaining amount of water-soluble salt will decrease, but the power will become excessive, leading to an increase in cost, which may be economically disadvantageous. Moreover, 1-50 mm is preferable and, as for the hole diameter of the metal dehydration part (basket part) of a centrifuge, 5-20 mm is especially preferable. The material of the filtration filter attached to the metal dehydration part is preferably made of resin such as cotton, PET, nylon, etc., and the pore size of the filtration filter is preferably 10 to 1000 μm, more preferably 10 to 500 μm, and still more preferably 10 to 10 μm. 300 μm.
遠心分離機を使用する方法とろ過器を使用する方法とを比べると、遠心分離機の場合は装置が濾過器に比べ小さくなること、得られるケークの含水率が低くなり洗浄回数が少なくても高純度の芳香族ジヒドロキシ化合物が得られる利点がある。 Comparing the method of using a centrifuge with the method of using a filter, in the case of a centrifuge, the device is smaller than the filter, and the moisture content of the resulting cake is low and the number of washings is small. There is an advantage that a highly pure aromatic dihydroxy compound can be obtained.
また、洗浄後に得られる固形の芳香族ジヒドロキシ化合物の含液率は５〜３５％になるように濾過条件を設定することが好ましい。含液率を５％未満に下げる為には過大な濾過分離器が必要になり、３５％を越えると水溶性塩等の不純物を多く含むため、洗浄、濾過のサイクルを繰り返すことが必要になり、芳香族ジヒドロキシ化合物の収率低下につながることがある。 Moreover, it is preferable to set filtration conditions so that the liquid content of the solid aromatic dihydroxy compound obtained after washing may be 5 to 35%. To reduce the liquid content to less than 5%, an excessive filtration separator is required. When it exceeds 35%, it contains a large amount of impurities such as water-soluble salts. Therefore, it is necessary to repeat the washing and filtration cycle. , This may lead to a decrease in the yield of the aromatic dihydroxy compound.
有機溶媒で洗浄する場合、一度の洗浄時間は１分〜６０分の範囲が好ましく、洗浄温度は５〜４０℃の範囲が好ましい。一度の洗浄に使用する有機溶媒の量は、芳香族ジヒドロキシ化合物１００重量部に対して好ましくは５０〜１０００重量部、より好ましくは１００〜５００重量部である。 When washing with an organic solvent, the washing time for one time is preferably in the range of 1 minute to 60 minutes, and the washing temperature is preferably in the range of 5 to 40 ° C. The amount of the organic solvent used for one-time washing is preferably 50 to 1000 parts by weight, more preferably 100 to 500 parts by weight with respect to 100 parts by weight of the aromatic dihydroxy compound.
水で洗浄する場合、一度の洗浄時間は１〜６０分の範囲が好ましく、洗浄温度は５〜８０℃の範囲が好ましい。一度の洗浄に使用する水の量は、芳香族ジヒドロキシ化合物１００重量部に対して好ましくは５０〜１０００重量部、より好ましくは１００〜５００重量部である。 When washing with water, the time for one washing is preferably in the range of 1 to 60 minutes, and the washing temperature is preferably in the range of 5 to 80 ° C. The amount of water used for one-time washing is preferably 50 to 1000 parts by weight, more preferably 100 to 500 parts by weight with respect to 100 parts by weight of the aromatic dihydroxy compound.
洗浄後の芳香族ジヒドロキシ化合物は、高品質で芳香族ジヒドロキシ化合物の純度が好ましくは９９．５％以上となる。また、ナトリウムイオン含有量は好ましくは１０ｐｐｍ以下となる。この芳香族ジヒドロキシ化合物を用いて製造された芳香族ポリカーボネートの品質は市販の芳香族ジヒドロキシ化合物を用いて製造した芳香族ポリカーボネートの品質と遜色ないものとなる。 The aromatic dihydroxy compound after washing has a high quality and the purity of the aromatic dihydroxy compound is preferably 99.5% or more. The sodium ion content is preferably 10 ppm or less. The quality of an aromatic polycarbonate produced using this aromatic dihydroxy compound is comparable to that of an aromatic polycarbonate produced using a commercially available aromatic dihydroxy compound.
本発明の方法で得られた固形の芳香族ジヒドロキシ化合物は、芳香族ポリカーボネートの製造工程に原料として再使用することができる。再使用する方法としては、溶融重合法ではそのまま使用することができ、また、界面重合法では金属水酸化物水溶液に所望の濃度で溶解し、芳香族ポリカーボネートの製造に使用することが可能である。その際、芳香族ジヒドロキシ化合物を金属水酸化物水溶液に溶解した溶液を加熱し、残存する有機溶媒を揮発したものを使用することも好ましい。 The solid aromatic dihydroxy compound obtained by the method of the present invention can be reused as a raw material in the production process of an aromatic polycarbonate. As a re-use method, it can be used as it is in the melt polymerization method, and in the interfacial polymerization method, it can be dissolved in a metal hydroxide aqueous solution at a desired concentration and used for the production of an aromatic polycarbonate. . At that time, it is also preferable to use a solution obtained by heating a solution obtained by dissolving an aromatic dihydroxy compound in a metal hydroxide aqueous solution and volatilizing the remaining organic solvent.
また、本発明の方法で回収した芳香族ジヒドロキシ化合物と市販の芳香族ジヒドロキシ化合物とを一緒に芳香族ポリカーボネートの製造に使用しても構わない。回収した芳香族ジヒドロキシ化合物と市販の芳香族ジヒドロキシ化合物を混合する方法は、固体同士、固体と液体、液体同士を混合する方法のどの方法であってもよい。 Moreover, you may use the aromatic dihydroxy compound collect | recovered with the method of this invention, and a commercially available aromatic dihydroxy compound together for manufacture of an aromatic polycarbonate. The method for mixing the recovered aromatic dihydroxy compound and the commercially available aromatic dihydroxy compound may be any method of solids, solids and liquids, or liquids.
本発明の方法で回収した芳香族ジヒドロキシ化合物を原料として用いて得られるポリカーボネート樹脂は、色相および熱安定性に優れることから、例えば光磁気ディスク、各種追記型ディスク、デジタルオーディオディスク（いわゆるコンパクトディスク）、光学式ビデオディスク（いわゆるレーザディスク）、デジタル・バーサイル・ディスク（ＤＶＤ）等の光学ディスク基板用の材料として、あるいはシリコンウエハー等の精密機材収納容器の材料として好適に使用でき、殊に光学ディスク基板用の材料として好適に採用される。 Since the polycarbonate resin obtained by using the aromatic dihydroxy compound recovered by the method of the present invention as a raw material is excellent in hue and thermal stability, for example, a magneto-optical disc, various write-once discs, a digital audio disc (so-called compact disc) It can be suitably used as a material for an optical disk substrate such as an optical video disk (so-called laser disk) or a digital versatile disk (DVD), or as a material for a precision equipment container such as a silicon wafer. It is suitably employed as a substrate material.
本発明によれば、廃ポリカーボネート樹脂を分解し、洗浄して得られた高品質の芳香族ジヒドロキシ化合物は芳香族ポリカーボネート製造の原材料として再利用できる。本発明の奏する工業的効果は格別である。 According to the present invention, a high-quality aromatic dihydroxy compound obtained by decomposing and washing waste polycarbonate resin can be reused as a raw material for producing an aromatic polycarbonate. The industrial effect produced by the present invention is exceptional.
以下に実施例を挙げて本発明を更に説明するが、本発明はこれに限定されるものではない。特に断り書きのない場合、部は重量部を表す。なお、評価は次に示す方法で行った。 EXAMPLES The present invention will be further described below with reference to examples, but the present invention is not limited thereto. Unless indicated otherwise, parts represent parts by weight. The evaluation was performed by the following method.
（１）色相（ｂ値）
ポリカーボネート樹脂ペレットを射出成形機（日本製鋼所（株）製：日鋼アンカー Ｖ−１７−６５型）を用い、シリンダー温度３４０℃で、厚さ２ｍｍの５０ｍｍ角板を成形した。その成形板を色差計（日本電色（株）製）を用いてｂ値を測定した。
(1) Hue (b value)
Using a polycarbonate resin pellet, a 50 mm square plate having a thickness of 2 mm was molded at a cylinder temperature of 340 ° C. using an injection molding machine (manufactured by Nippon Steel Works, Ltd .: Nikko Anchor V-17-65 type). The molded plate was measured for b value using a color difference meter (manufactured by Nippon Denshoku Co., Ltd.).
（２）熱安定性（△Ｅ）
ポリカーボネート樹脂ペレットを射出成形機（日本製鋼所（株）製：日鋼アンカー Ｖ−１７−６５型）を用い、シリンダー温度３４０℃で１０分間滞留させたものとさせないものの試験片（厚さ２ｍｍの５０ｍｍ角板）をそれぞれ作成し、その色相の変化（△Ｅ）を測定した。色相の変化は、色差計（日本電色（株）製）でそれぞれのＬ、ａ、ｂ値を測定し、下記式を用いて算出した。
ΔＥ＝［（Ｌ′−Ｌ）２＋（ａ′−ａ）２＋（ｂ′−ｂ）２］１／２
（Ｌ、ａ、ｂは滞留させないもの、Ｌ′、ａ′、ｂ′は１０分間滞留させたもの）
(2) Thermal stability (△ E)
Test pieces (thickness 2 mm) of polycarbonate resin pellets that were not allowed to stay for 10 minutes at a cylinder temperature of 340 ° C. using an injection molding machine (manufactured by Nippon Steel Co., Ltd .: Nikko Anchor V-17-65 type) 50 mm square plate) was prepared, and the change in hue (ΔE) was measured. The change in hue was calculated using the following formula after measuring the L, a, and b values with a color difference meter (manufactured by Nippon Denshoku Co., Ltd.).
ΔE = [(L′−L) 2 + (a′−a) 2 + (b′−b) 2 ] 1/2
(L, a, b are not retained, L ′, a ′, b ′ are retained for 10 minutes)
（３）ビスフェノールＡの純度（有機物中のビスフェノールＡ純度）
Ｗａｔｅｒｓ社製高速液体クロマトグラフィを用い、サンプル（有機物）０．２ｇに内部標準としてｏ−クレゾールを添加したアセトニトリル１ｍＬを加え、溶解し、アセトニトリル／０．２％酢酸水溶液を展開溶媒としてクロマトグラフを得、あらかじめ作成した検量線により、ビスフェノールＡの純度を求めた。
(3) Purity of bisphenol A (bisphenol A purity in organic matter)
Using Waters high performance liquid chromatography, 0.2 mL of sample (organic matter) was added with 1 mL of acetonitrile with o-cresol added as an internal standard, dissolved, and a chromatograph was obtained using acetonitrile / 0.2% acetic acid aqueous solution as a developing solvent. The purity of bisphenol A was determined using a calibration curve prepared in advance.
（４）ビスフェノールＡのナトリウムイオン含有量
ビスフェノールＡ１ｇに超純水１０ｍＬを加えて２４時間静置し、イオン成分を抽出した。この液をイオンクロマトグラフを得、あらかじめ作成した検量線によりナトリウムイオンの量を求めた。
(4) Sodium ion content of bisphenol A 10 mL of ultrapure water was added to 1 g of bisphenol A and allowed to stand for 24 hours to extract ionic components. An ion chromatograph was obtained from this solution, and the amount of sodium ions was determined using a calibration curve prepared in advance.
（５）ビスフェノールＡの平均粒径
ビスフェノールＡを２．０ｍｍ、１．０ｍｍ、０．７１ｍｍ、０．４２５ｍｍ、０．３ｍｍ、０．１８ｍｍ、０．０７５ｍｍの目開きを持つ篩を使用して、篩い分けた後、重量を基準とした累積粒度分布グラフを作成し、累積重量が５０％になるところの粒径を求め、これを平均粒径とした。
(5) Average particle diameter of bisphenol A Using a sieve having openings of bisphenol A of 2.0 mm, 1.0 mm, 0.71 mm, 0.425 mm, 0.3 mm, 0.18 mm, 0.075 mm, After sieving, a cumulative particle size distribution graph based on weight was created, and the particle size at which the cumulative weight reached 50% was determined, and this was taken as the average particle size.
（６）水分量
Ｍｅｔｒｏｈｍ社製カールフィッシャー水分測定器を用い、サンプル２ｇを投入して測定した。
(6) Moisture content Using a Karl Fischer moisture meter manufactured by Metrohm, a sample 2 g was charged and measured.
［実施例１］
温度計、撹拌機及び還流冷却器、水浴付き反応器に、固体の水酸化ナトリウム４部（芳香族ポリカーボネートのカーボネート結合に対し、２０モル％）、メタノール８０部（芳香族ポリカーボネートのカーボネート結合１モルに対し、５モル）を投入し、２５℃で攪拌して溶解した。次に、酸化防止剤としてハイドロサルファイトナトリウム２部、塩化メチレン２００部、ＣＤ−Ｒの金属部分を剥離し、粉砕した樹脂（主成分ビスフェノールＡポリカーボネート樹脂、粘度平均分子量１５２００）１２７部を投入し、２５℃で攪拌を継続した。投入直後は樹脂が団子状態になっていたが、内部の温度が上昇するにつれて固形分が溶解し、攪拌１０分後に完全に溶解した。ここで、系内の濃度を測定するため溶液の一部をサンプリングして水分量を測定したところ、０．０５重量％であった。その後、内温を４０℃にするため、水浴を調節した。樹脂投入から４時間後、反応混合物中のポリカーボネート樹脂オリゴマーを１Ｈ−ＮＭＲで分析したところ、完全に消失しており、メタノール／ジメチルカーボネートのピーク面積比が１．５であり理論量のジメチルカーボネートが生成していることを確認できたので、０．５ｍｏｌ／Ｌ塩酸水溶液２０２部投入し、分解反応を停止させた。
[Example 1]
In a reactor equipped with a thermometer, a stirrer and a reflux condenser and a water bath, 4 parts of solid sodium hydroxide (20 mol% with respect to the carbonate bond of the aromatic polycarbonate), 80 parts of methanol (1 mol of the carbonate bond of the aromatic polycarbonate) 5 mol) was added and dissolved by stirring at 25 ° C. Next, 2 parts of hydrosulfite sodium as an antioxidant, 200 parts of methylene chloride, and 127 parts of a pulverized resin (principal component bisphenol A polycarbonate resin, viscosity average molecular weight 15200) are added. Stirring was continued at 25 ° C. Immediately after the addition, the resin was in a dumpling state, but as the internal temperature increased, the solid content was dissolved and completely dissolved after 10 minutes of stirring. Here, in order to measure the concentration in the system, a part of the solution was sampled and the water content was measured, and it was 0.05% by weight. Thereafter, the water bath was adjusted to bring the internal temperature to 40 ° C. Four hours after the addition of the resin, the polycarbonate resin oligomer in the reaction mixture was analyzed by 1 H-NMR. As a result, it completely disappeared, the methanol / dimethyl carbonate peak area ratio was 1.5, and the theoretical amount of dimethyl carbonate. As a result, it was confirmed that the decomposition reaction was stopped by adding 202 parts of 0.5 mol / L hydrochloric acid aqueous solution.
分液ロートに反応混合物を移し、有機相３８２部と水相２３３部に分離した。デカンターにより分液し有機相を回収した。この有機相を絶対濾過精度２０μｍのフィルターで濾過した後、４０℃の水浴を設けたエバポレータにより減圧して、塩化メチレン、メタノール、ジメチルカーボネートを除去し固形分１３３部を得た。 The reaction mixture was transferred to a separatory funnel and separated into 382 parts of an organic phase and 233 parts of an aqueous phase. The organic phase was recovered by liquid separation using a decanter. This organic phase was filtered through a filter having an absolute filtration accuracy of 20 μm, and then the pressure was reduced by an evaporator provided with a 40 ° C. water bath to remove methylene chloride, methanol, and dimethyl carbonate to obtain 133 parts of a solid content.
この固形分に塩化メチレン２００部を加えスラリーとした後、このスラリーをＰＥＴ製の孔径５０μｍのろ過フィルターを取り付けた遠心分離機（タナベウィルテック（株）製遠心分離機ＣＴ−２０−２０型）により３００Ｇの遠心力で濾過し、遠心分離機内で運転しながら、温度２０℃の塩化メチレン７０部、温度２０℃の電気伝導度が１０μＳ／ｃｍの純水７０部、前記塩化メチレン７０部、前記純水７０部をそれぞれ５分間かけてこの順番で固体に振りかけ、リンス洗浄を行った。固体を遠心分離機内から掻き出し、乾燥後重量を測定したところ１０７部であった。この固体の平均粒径は５００μｍであった。ビスフェノールＡ純度を測定したところ９９．８％であり、ナトリウムイオン含有量は８ｐｐｍであった。 After adding 200 parts of methylene chloride to this solid to make a slurry, this slurry was centrifuged with a filter made of PET having a pore size of 50 μm (centrifuge CT-20-20 manufactured by Tanabe Wiltech Co., Ltd.). While filtering in a centrifugal force of 300 G and operating in a centrifuge, 70 parts of methylene chloride at a temperature of 20 ° C., 70 parts of pure water having an electrical conductivity of 10 μS / cm at a temperature of 20 ° C., 70 parts of the methylene chloride, 70 parts of pure water was sprinkled on the solid in this order over 5 minutes, respectively, and rinsed. The solid was scraped out of the centrifuge and the weight after drying was 107 parts. The average particle size of this solid was 500 μm. When the purity of bisphenol A was measured, it was 99.8% and the sodium ion content was 8 ppm.
［実施例２］
実施例１において、電気伝導度が１０μＳ／ｃｍの純水を使用する代わりに電気伝導度が８０μｓ／ｃｍの水を使用してリンス洗浄を行なった。固体を掻き出し、乾燥後重量を測定したところ１０７部であった。ビスフェノールＡ純度を測定したところ９８．９％であり、ナトリウムイオン含有量は１０ｐｐｍであった。
[Example 2]
In Example 1, instead of using pure water having an electric conductivity of 10 μS / cm, rinsing was performed using water having an electric conductivity of 80 μs / cm. The solid was scraped out and the weight measured after drying was 107 parts. When the purity of bisphenol A was measured, it was 98.9% and the sodium ion content was 10 ppm.
［実施例３］
実施例１において得られたスラリーを５０μｍのフィルターを設けたろ過器を使用し０．０８Ｍｐａの差圧でろ過した。温度２０℃の塩化メチレン７０部を５分間かけてろ過器に入れ前記ろ過器で０．０８Ｍｐａの差圧でろ過し、温度２０℃の電気伝導度が１０μＳ／ｃｍの純水７０部を５分間かけてろ過器に入れ前記ろ過器で０．０８Ｍｐａの差圧でろ過し、前記塩化メチレン７０部を５分間かけてろ過器に入れ前記ろ過器で０．０８Ｍｐａの差圧でろ過し、前記純水４５部を５分間かけてろ過器に入れ前記ろ過器で０．０８Ｍｐａの差圧でろ過して固体のビスフェノールＡを得た。この固体の平均粒径は６００μｍであった。ビスフェノールＡ純度を測定したところ９９．７％であり、ナトリウムイオン含有量は８ｐｐｍであった。
[Example 3]
The slurry obtained in Example 1 was filtered at a differential pressure of 0.08 Mpa using a filter provided with a 50 μm filter. 70 parts of methylene chloride at a temperature of 20 ° C. are put in a filter over 5 minutes and filtered with a differential pressure of 0.08 Mpa with the filter, and 70 parts of pure water at a temperature of 20 ° C. and an electric conductivity of 10 μS / cm for 5 minutes. The filter is filtered with a pressure difference of 0.08 Mpa through the filter, 70 parts of methylene chloride is put into the filter over 5 minutes, and the filter is filtered with a pressure difference of 0.08 Mpa. 45 parts of water was placed in a filter over 5 minutes, and filtered with a differential pressure of 0.08 Mpa with the filter to obtain solid bisphenol A. The average particle size of this solid was 600 μm. When the purity of bisphenol A was measured, it was 99.7% and the sodium ion content was 8 ppm.
［比較例１］
実施例１において遠心分離機でろ過した後、リンス洗浄せずに固体を掻き出し、乾燥後重量を測定したところ１２４部であった。ビスフェノールＡ純度を測定したところ９８．２％であり、ナトリウムイオン含有量は１．３％であった。
[Comparative Example 1]
In Example 1, after filtering with a centrifuge, the solid was scraped out without rinsing, and the weight after drying was 124 parts. When the purity of bisphenol A was measured, it was 98.2% and the sodium ion content was 1.3%.
［実施例４］ ポリカーボネート樹脂の製造
（Ａ）温度計、撹拌機、還流冷却器、循環器付き反応器に、イオン交換水６５０部、２５％水酸化ナトリウム水溶液２５２部を仕込み、これに実施例１で得られたビスフェノールＡ１７０部、塩化メチレン１３部およびハイドロサルファイト０．３４部を加え、循環しながら温度を３０℃に保持し４０分間で溶解し、ビスフェノールＡ水溶液を調合した。
[Example 4] Production of polycarbonate resin (A) A thermometer, a stirrer, a reflux condenser, and a reactor with a circulator were charged with 650 parts of ion-exchanged water and 252 parts of a 25% aqueous sodium hydroxide solution. 170 parts of bisphenol A obtained in 1 above, 13 parts of methylene chloride and 0.34 part of hydrosulfite were added, and the temperature was maintained at 30 ° C. while circulating and dissolved in 40 minutes to prepare a bisphenol A aqueous solution.
（Ｂ）温度計、撹拌機及び還流冷却器付き反応器に、（Ａ）で調合したビスフェノールＡ水溶液３６７部を仕込み、塩化メチレン１８１部を加え、撹拌下１５〜２５℃でホスゲン２８．３部を４０分要して吹込んだ。ホスゲン吹き込み終了後、４８％水酸化ナトリウム水溶液７．２部および固体のｐ−ターシャリーブチルフェノール１．５５部を加え、乳化せしめた後、１０分後にトリエチルアミン０．０６部を加え、さらに２８〜３３℃で１時間撹拌して反応を終了した。反応終了後生成物に塩化メチレン４００部を加え混合した後、攪拌を停止し、水相と有機相を分離して、ポリカーボネート樹脂濃度１４．５重量％有機溶媒溶液を得た。（この操作を、反応機２機を用いて繰り返し行った。）
この有機溶媒溶液に水１５０部を加えて攪拌混合した後、攪拌を停止し、水相と有機相を分離した。この有機相にｐＨ３の塩酸水２００部を加え、攪拌混合しトリエチルアミン等を抽出した後、攪拌を停止し、水相と有機相を分離した。次いでさらに分離した有機相にイオン交換水２００部を加え攪拌混合した後、攪拌を停止し、水相と有機相を分離した。この操作を水相の導電率がイオン交換水と殆ど同じになるまで（４回）繰返した。得られた精製ポリカーボネート樹脂溶液をＳＵＳ３０４製の濾過精度１μｍフィルターで濾過した。
(B) A thermometer, a stirrer, and a reactor equipped with a reflux condenser were charged with 367 parts of the bisphenol A aqueous solution prepared in (A), 181 parts of methylene chloride was added, and 28.3 parts of phosgene at 15 to 25 ° C. with stirring. It took 40 minutes to blow. After completion of the phosgene blowing, 7.2 parts of a 48% aqueous sodium hydroxide solution and 1.55 parts of solid p-tertiary butylphenol were added and emulsified. After 10 minutes, 0.06 part of triethylamine was added, and further 28 to 33 The reaction was terminated by stirring for 1 hour at ° C. After completion of the reaction, 400 parts of methylene chloride was added to the product and mixed, and then stirring was stopped, and the aqueous phase and the organic phase were separated to obtain an organic solvent solution having a polycarbonate resin concentration of 14.5% by weight. (This operation was repeated using two reactors.)
After adding 150 parts of water to this organic solvent solution and stirring and mixing, stirring was stopped and the aqueous phase and the organic phase were separated. To this organic phase, 200 parts of aqueous hydrochloric acid having a pH of 3 was added and mixed by stirring to extract triethylamine and the like. Then, stirring was stopped and the aqueous phase and the organic phase were separated. Subsequently, 200 parts of ion-exchanged water was added to the separated organic phase, and the mixture was stirred and mixed. Then, stirring was stopped and the aqueous phase and the organic phase were separated. This operation was repeated (four times) until the conductivity of the aqueous phase was almost the same as that of ion-exchanged water. The obtained purified polycarbonate resin solution was filtered with a 1 μm filter made of SUS304.
次に、該有機溶媒溶液を軸受け部に異物取出口を有する隔離室を設けた内壁の材質がＳＵＳ３１６Ｌ製の１０００Ｌニーダーにイオン交換水１００Ｌを投入し、水温４２℃にて塩化メチレンを蒸発させて粉粒体とし、該粉粒体と水の混合物を水温９５℃にコントロールされた攪拌機付熱水処理槽を有した熱水処理工程の熱水処理槽に投入し、粉粒体２５部、水７５部の混合比で３０分間攪拌機混合した。この粉粒体と水の混合物を遠心分離機で分離して塩化メチレン０．５重量％、水４５重量％の含有粉粒体を得た。次に、この粉粒体を１４０℃にコントロールされているＳＵＳ３１６Ｌ製伝導受熱式溝型２軸攪拌連続乾燥機に５０ｋｇ／ｈ（ポリカーボネート樹脂換算）で連続供給して、平均乾燥時間３時間の条件で乾燥して粉粒体を得た。 Next, 100 L of ion-exchanged water is introduced into a 1000 L kneader made of SUS316L, and the methylene chloride is evaporated at a water temperature of 42 ° C. The powder and the mixture of the powder and water were put into a hot water treatment tank of a hot water treatment process having a hot water treatment tank with a stirrer controlled at a water temperature of 95 ° C., and 25 parts of powder and water The mixture was stirred for 30 minutes at a mixing ratio of 75 parts. This mixture of powder and water was separated by a centrifugal separator to obtain a powder containing 0.5% by weight of methylene chloride and 45% by weight of water. Next, this granular material is continuously supplied at 50 kg / h (in terms of polycarbonate resin) to a SUS316L conductive heat receiving groove type biaxial stirring continuous dryer controlled at 140 ° C., and the condition of an average drying time of 3 hours. And dried to obtain a granular material.
この粉粒体にトリス（２，６−ジ−ｔｅｒｔ−ブチルフェニル）ホスファイトを０．０１０重量％、４，４’−ビフェニレンジホスホスフィン酸テトラキス（２，４−ジ−ｔｅｒｔ−ブチルフェニル）を０．０１０重量％、ステアリン酸モノグリセリドを０．０８０重量％加え混合した。次に、かかる粉粒体をベント式二軸押出機［東芝機械（株）製ＴＥＭ−５０Ｂ］によりシリンダー温度２８０℃、乾式真空ポンプを用いてベント吸引圧７００Ｐａで吸引脱気しながら溶融混練押出し、ペレットを得た。得られたペレットを成形して、色相と熱安定性を評価し、その結果を表１に示した。 Tris (2,6-di-tert-butylphenyl) phosphite is 0.010 wt%, 4,4′-biphenylenediphosphosphinic acid tetrakis (2,4-di-tert-butylphenyl) to the powder. 0.010 wt% and stearic acid monoglyceride 0.080 wt% were added and mixed. Next, this powder and granule are melt kneaded and extruded by a vent type twin screw extruder [TEM-50B manufactured by TOSHIBA MACHINE CO., LTD.] With a cylinder temperature of 280 ° C. and a suction vacuum of 700 Pa using a dry vacuum pump. A pellet was obtained. The obtained pellets were molded and evaluated for hue and thermal stability. The results are shown in Table 1.
［実施例５］
実施例４において、（Ａ）で使用するビスフェノールＡとして実施例２で得られたビスフェノールＡを使用する以外は、実施例４と同様な操作をして、ペレットを得た。得られたペレットを成形して、色相と熱安定性を評価し、その結果を表１に示した。
[Example 5]
In Example 4, pellets were obtained in the same manner as in Example 4 except that bisphenol A obtained in Example 2 was used as bisphenol A used in (A). The obtained pellets were molded and evaluated for hue and thermal stability. The results are shown in Table 1.
［実施例６］
実施例４において、（Ａ）で使用するビスフェノールＡとして実施例３で得られたビスフェノールＡを使用する以外は、実施例４と同様な操作をして、ペレットを得た。得られたペレットを成形して、色相と熱安定性を評価し、その結果を表１に示した。
[Example 6]
In Example 4, pellets were obtained in the same manner as in Example 4 except that bisphenol A obtained in Example 3 was used as bisphenol A used in (A). The obtained pellets were molded and evaluated for hue and thermal stability. The results are shown in Table 1.
［比較例２］
実施例４において、（Ａ）で使用するビスフェノールＡとして比較例１で得られたビスフェノールＡを使用する以外は、実施例４と同様な操作をして、ペレットを得た。得られたペレットを成形して、色相と熱安定性を評価し、その結果を表１に示した。
[Comparative Example 2]
In Example 4, pellets were obtained in the same manner as in Example 4 except that bisphenol A obtained in Comparative Example 1 was used as bisphenol A used in (A). The obtained pellets were molded and evaluated for hue and thermal stability. The results are shown in Table 1.
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| WO2022113847A1 (en) | 2020-11-27 | 2022-06-02 | 三菱ケミカル株式会社 | Polycarbonate resin decomposition method, bisphenol production method, dialkyl carbonate production method, alkyl aryl carbonate production method, diaryl carbonate production method, recycled polycarbonate resin production method, epoxy resin production method, and epoxy resin cured product production method |
| KR20230112112A (en) | 2020-11-27 | 2023-07-26 | 미쯔비시 케미컬 주식회사 | Polycarbonate resin decomposition method, bisphenol production method, dialkyl carbonate production method, alkylaryl carbonate production method, diaryl carbonate production method, regenerated polycarbonate resin production method, epoxy resin production method, and epoxy resin cured product production method |
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