JPS5912653B2 - Method for producing 1,4-dihydroxy-2-naphthoic acid - Google Patents
Method for producing 1,4-dihydroxy-2-naphthoic acidInfo
- Publication number
- JPS5912653B2 JPS5912653B2 JP1081481A JP1081481A JPS5912653B2 JP S5912653 B2 JPS5912653 B2 JP S5912653B2 JP 1081481 A JP1081481 A JP 1081481A JP 1081481 A JP1081481 A JP 1081481A JP S5912653 B2 JPS5912653 B2 JP S5912653B2
- Authority
- JP
- Japan
- Prior art keywords
- reaction
- dihydroxynaphthalene
- dihydroxy
- naphthoic acid
- potassium carbonate
- 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
- VOJUXHHACRXLTD-UHFFFAOYSA-N 1,4-dihydroxy-2-naphthoic acid Chemical compound C1=CC=CC2=C(O)C(C(=O)O)=CC(O)=C21 VOJUXHHACRXLTD-UHFFFAOYSA-N 0.000 title claims description 30
- 238000004519 manufacturing process Methods 0.000 title claims description 6
- 238000006243 chemical reaction Methods 0.000 claims description 39
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims description 38
- PCILLCXFKWDRMK-UHFFFAOYSA-N naphthalene-1,4-diol Chemical compound C1=CC=C2C(O)=CC=C(O)C2=C1 PCILLCXFKWDRMK-UHFFFAOYSA-N 0.000 claims description 26
- 239000007789 gas Substances 0.000 claims description 21
- 229910000027 potassium carbonate Inorganic materials 0.000 claims description 19
- 239000002994 raw material Substances 0.000 claims description 16
- 238000003756 stirring Methods 0.000 claims description 15
- 238000000034 method Methods 0.000 claims description 9
- 238000006473 carboxylation reaction Methods 0.000 claims description 6
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims description 2
- 229910001882 dioxygen Inorganic materials 0.000 claims description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 claims 1
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 36
- 239000001569 carbon dioxide Substances 0.000 description 18
- 229910002092 carbon dioxide Inorganic materials 0.000 description 18
- 239000002904 solvent Substances 0.000 description 15
- 239000000243 solution Substances 0.000 description 8
- -1 alkali metal salt Chemical class 0.000 description 7
- 230000035484 reaction time Effects 0.000 description 6
- NTIZESTWPVYFNL-UHFFFAOYSA-N Methyl isobutyl ketone Chemical compound CC(C)CC(C)=O NTIZESTWPVYFNL-UHFFFAOYSA-N 0.000 description 5
- UIHCLUNTQKBZGK-UHFFFAOYSA-N Methyl isobutyl ketone Natural products CCC(C)C(C)=O UIHCLUNTQKBZGK-UHFFFAOYSA-N 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- XAEFZNCEHLXOMS-UHFFFAOYSA-M potassium benzoate Chemical compound [K+].[O-]C(=O)C1=CC=CC=C1 XAEFZNCEHLXOMS-UHFFFAOYSA-M 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 4
- AMQJEAYHLZJPGS-UHFFFAOYSA-N N-Pentanol Chemical compound CCCCCO AMQJEAYHLZJPGS-UHFFFAOYSA-N 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 239000013078 crystal Substances 0.000 description 4
- 239000013067 intermediate product Substances 0.000 description 4
- PGMYKACGEOXYJE-UHFFFAOYSA-N pentyl acetate Chemical compound CCCCCOC(C)=O PGMYKACGEOXYJE-UHFFFAOYSA-N 0.000 description 4
- 229920000642 polymer Polymers 0.000 description 4
- 238000007086 side reaction Methods 0.000 description 4
- 229910052708 sodium Inorganic materials 0.000 description 4
- 239000011734 sodium Substances 0.000 description 4
- 239000000725 suspension Substances 0.000 description 4
- LNETULKMXZVUST-UHFFFAOYSA-N 1-naphthoic acid Chemical compound C1=CC=C2C(C(=O)O)=CC=CC2=C1 LNETULKMXZVUST-UHFFFAOYSA-N 0.000 description 3
- PTTPXKJBFFKCEK-UHFFFAOYSA-N 2-Methyl-4-heptanone Chemical compound CC(C)CC(=O)CC(C)C PTTPXKJBFFKCEK-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 229910052783 alkali metal Inorganic materials 0.000 description 3
- 239000006227 byproduct Substances 0.000 description 3
- 239000007795 chemical reaction product Substances 0.000 description 3
- GJRQTCIYDGXPES-UHFFFAOYSA-N iso-butyl acetate Natural products CC(C)COC(C)=O GJRQTCIYDGXPES-UHFFFAOYSA-N 0.000 description 3
- FGKJLKRYENPLQH-UHFFFAOYSA-M isocaproate Chemical compound CC(C)CCC([O-])=O FGKJLKRYENPLQH-UHFFFAOYSA-M 0.000 description 3
- OQAGVSWESNCJJT-UHFFFAOYSA-N isovaleric acid methyl ester Natural products COC(=O)CC(C)C OQAGVSWESNCJJT-UHFFFAOYSA-N 0.000 description 3
- 238000010926 purge Methods 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- BBMCTIGTTCKYKF-UHFFFAOYSA-N 1-heptanol Chemical compound CCCCCCCO BBMCTIGTTCKYKF-UHFFFAOYSA-N 0.000 description 2
- QQZOPKMRPOGIEB-UHFFFAOYSA-N 2-Oxohexane Chemical compound CCCCC(C)=O QQZOPKMRPOGIEB-UHFFFAOYSA-N 0.000 description 2
- YIWUKEYIRIRTPP-UHFFFAOYSA-N 2-ethylhexan-1-ol Chemical compound CCCCC(CC)CO YIWUKEYIRIRTPP-UHFFFAOYSA-N 0.000 description 2
- MSXVEPNJUHWQHW-UHFFFAOYSA-N 2-methylbutan-2-ol Chemical group CCC(C)(C)O MSXVEPNJUHWQHW-UHFFFAOYSA-N 0.000 description 2
- HCFAJYNVAYBARA-UHFFFAOYSA-N 4-heptanone Chemical compound CCCC(=O)CCC HCFAJYNVAYBARA-UHFFFAOYSA-N 0.000 description 2
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Natural products CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 2
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- KWOLFJPFCHCOCG-UHFFFAOYSA-N Acetophenone Chemical compound CC(=O)C1=CC=CC=C1 KWOLFJPFCHCOCG-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- RZKSECIXORKHQS-UHFFFAOYSA-N Heptan-3-ol Chemical compound CCCCC(O)CC RZKSECIXORKHQS-UHFFFAOYSA-N 0.000 description 2
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 2
- 238000003916 acid precipitation Methods 0.000 description 2
- 230000001476 alcoholic effect Effects 0.000 description 2
- 150000001298 alcohols Chemical class 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- DKPFZGUDAPQIHT-UHFFFAOYSA-N butyl acetate Chemical compound CCCCOC(C)=O DKPFZGUDAPQIHT-UHFFFAOYSA-N 0.000 description 2
- HPXRVTGHNJAIIH-UHFFFAOYSA-N cyclohexanol Chemical compound OC1CCCCC1 HPXRVTGHNJAIIH-UHFFFAOYSA-N 0.000 description 2
- JHIVVAPYMSGYDF-UHFFFAOYSA-N cyclohexanone Chemical compound O=C1CCCCC1 JHIVVAPYMSGYDF-UHFFFAOYSA-N 0.000 description 2
- MWKFXSUHUHTGQN-UHFFFAOYSA-N decan-1-ol Chemical compound CCCCCCCCCCO MWKFXSUHUHTGQN-UHFFFAOYSA-N 0.000 description 2
- FKRCODPIKNYEAC-UHFFFAOYSA-N ethyl propionate Chemical compound CCOC(=O)CC FKRCODPIKNYEAC-UHFFFAOYSA-N 0.000 description 2
- CATSNJVOTSVZJV-UHFFFAOYSA-N heptan-2-one Chemical compound CCCCCC(C)=O CATSNJVOTSVZJV-UHFFFAOYSA-N 0.000 description 2
- NGAZZOYFWWSOGK-UHFFFAOYSA-N heptan-3-one Chemical compound CCCCC(=O)CC NGAZZOYFWWSOGK-UHFFFAOYSA-N 0.000 description 2
- ZSIAUFGUXNUGDI-UHFFFAOYSA-N hexan-1-ol Chemical compound CCCCCCO ZSIAUFGUXNUGDI-UHFFFAOYSA-N 0.000 description 2
- QNVRIHYSUZMSGM-UHFFFAOYSA-N hexan-2-ol Chemical compound CCCCC(C)O QNVRIHYSUZMSGM-UHFFFAOYSA-N 0.000 description 2
- RXTNIJMLAQNTEG-UHFFFAOYSA-N hexan-2-yl acetate Chemical compound CCCCC(C)OC(C)=O RXTNIJMLAQNTEG-UHFFFAOYSA-N 0.000 description 2
- RWSOTUBLDIXVET-UHFFFAOYSA-M hydrosulfide Chemical compound [SH-] RWSOTUBLDIXVET-UHFFFAOYSA-M 0.000 description 2
- MLFHJEHSLIIPHL-UHFFFAOYSA-N isoamyl acetate Chemical compound CC(C)CCOC(C)=O MLFHJEHSLIIPHL-UHFFFAOYSA-N 0.000 description 2
- XAOGXQMKWQFZEM-UHFFFAOYSA-N isoamyl propanoate Chemical compound CCC(=O)OCCC(C)C XAOGXQMKWQFZEM-UHFFFAOYSA-N 0.000 description 2
- ZXEKIIBDNHEJCQ-UHFFFAOYSA-N isobutanol Chemical compound CC(C)CO ZXEKIIBDNHEJCQ-UHFFFAOYSA-N 0.000 description 2
- 150000002576 ketones Chemical class 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- ZWRUINPWMLAQRD-UHFFFAOYSA-N nonan-1-ol Chemical compound CCCCCCCCCO ZWRUINPWMLAQRD-UHFFFAOYSA-N 0.000 description 2
- SJWFXCIHNDVPSH-UHFFFAOYSA-N octan-2-ol Chemical compound CCCCCCC(C)O SJWFXCIHNDVPSH-UHFFFAOYSA-N 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- XNLICIUVMPYHGG-UHFFFAOYSA-N pentan-2-one Chemical compound CCCC(C)=O XNLICIUVMPYHGG-UHFFFAOYSA-N 0.000 description 2
- AQIXEPGDORPWBJ-UHFFFAOYSA-N pentan-3-ol Chemical group CCC(O)CC AQIXEPGDORPWBJ-UHFFFAOYSA-N 0.000 description 2
- FDPIMTJIUBPUKL-UHFFFAOYSA-N pentan-3-one Chemical compound CCC(=O)CC FDPIMTJIUBPUKL-UHFFFAOYSA-N 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000003746 solid phase reaction Methods 0.000 description 2
- 150000005846 sugar alcohols Polymers 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- FUPIVZHYVSCYLX-UHFFFAOYSA-N 1,4-dihydronaphthalene Chemical compound C1=CC=C2CC=CCC2=C1 FUPIVZHYVSCYLX-UHFFFAOYSA-N 0.000 description 1
- GDXHBFHOEYVPED-UHFFFAOYSA-N 1-(2-butoxyethoxy)butane Chemical compound CCCCOCCOCCCC GDXHBFHOEYVPED-UHFFFAOYSA-N 0.000 description 1
- SJJCQDRGABAVBB-UHFFFAOYSA-N 1-hydroxy-2-naphthoic acid Chemical compound C1=CC=CC2=C(O)C(C(=O)O)=CC=C21 SJJCQDRGABAVBB-UHFFFAOYSA-N 0.000 description 1
- VXQBJTKSVGFQOL-UHFFFAOYSA-N 2-(2-butoxyethoxy)ethyl acetate Chemical compound CCCCOCCOCCOC(C)=O VXQBJTKSVGFQOL-UHFFFAOYSA-N 0.000 description 1
- HQLKZWRSOHTERR-UHFFFAOYSA-N 2-Ethylbutyl acetate Chemical compound CCC(CC)COC(C)=O HQLKZWRSOHTERR-UHFFFAOYSA-N 0.000 description 1
- AVMSWPWPYJVYKY-UHFFFAOYSA-N 2-Methylpropyl formate Chemical compound CC(C)COC=O AVMSWPWPYJVYKY-UHFFFAOYSA-N 0.000 description 1
- JTXMVXSTHSMVQF-UHFFFAOYSA-N 2-acetyloxyethyl acetate Chemical compound CC(=O)OCCOC(C)=O JTXMVXSTHSMVQF-UHFFFAOYSA-N 0.000 description 1
- POAOYUHQDCAZBD-UHFFFAOYSA-N 2-butoxyethanol Chemical compound CCCCOCCO POAOYUHQDCAZBD-UHFFFAOYSA-N 0.000 description 1
- NQBXSWAWVZHKBZ-UHFFFAOYSA-N 2-butoxyethyl acetate Chemical compound CCCCOCCOC(C)=O NQBXSWAWVZHKBZ-UHFFFAOYSA-N 0.000 description 1
- SVONRAPFKPVNKG-UHFFFAOYSA-N 2-ethoxyethyl acetate Chemical compound CCOCCOC(C)=O SVONRAPFKPVNKG-UHFFFAOYSA-N 0.000 description 1
- TZYRSLHNPKPEFV-UHFFFAOYSA-N 2-ethyl-1-butanol Chemical compound CCC(CC)CO TZYRSLHNPKPEFV-UHFFFAOYSA-N 0.000 description 1
- WOYWLLHHWAMFCB-UHFFFAOYSA-N 2-ethylhexyl acetate Chemical compound CCCCC(CC)COC(C)=O WOYWLLHHWAMFCB-UHFFFAOYSA-N 0.000 description 1
- UOBYKYZJUGYBDK-UHFFFAOYSA-N 2-naphthoic acid Chemical compound C1=CC=CC2=CC(C(=O)O)=CC=C21 UOBYKYZJUGYBDK-UHFFFAOYSA-N 0.000 description 1
- ZPVFWPFBNIEHGJ-UHFFFAOYSA-N 2-octanone Chemical compound CCCCCCC(C)=O ZPVFWPFBNIEHGJ-UHFFFAOYSA-N 0.000 description 1
- VGVHNLRUAMRIEW-UHFFFAOYSA-N 4-methylcyclohexan-1-one Chemical compound CC1CCC(=O)CC1 VGVHNLRUAMRIEW-UHFFFAOYSA-N 0.000 description 1
- CPIVYSAVIPTCCX-UHFFFAOYSA-N 4-methylpentan-2-yl acetate Chemical compound CC(C)CC(C)OC(C)=O CPIVYSAVIPTCCX-UHFFFAOYSA-N 0.000 description 1
- YYLLIJHXUHJATK-UHFFFAOYSA-N Cyclohexyl acetate Chemical compound CC(=O)OC1CCCCC1 YYLLIJHXUHJATK-UHFFFAOYSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 238000007065 Kolbe-Schmitt synthesis reaction Methods 0.000 description 1
- DIQMPQMYFZXDAX-UHFFFAOYSA-N Pentyl formate Chemical compound CCCCCOC=O DIQMPQMYFZXDAX-UHFFFAOYSA-N 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 1
- 238000006085 Schmidt reaction Methods 0.000 description 1
- IPTNXMGXEGQYSY-UHFFFAOYSA-N acetic acid;1-methoxybutan-1-ol Chemical compound CC(O)=O.CCCC(O)OC IPTNXMGXEGQYSY-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- BTMVHUNTONAYDX-UHFFFAOYSA-N butyl propionate Chemical compound CCCCOC(=O)CC BTMVHUNTONAYDX-UHFFFAOYSA-N 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 150000007942 carboxylates Chemical class 0.000 description 1
- 230000021523 carboxylation Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 229940117955 isoamyl acetate Drugs 0.000 description 1
- JMMWKPVZQRWMSS-UHFFFAOYSA-N isopropanol acetate Natural products CC(C)OC(C)=O JMMWKPVZQRWMSS-UHFFFAOYSA-N 0.000 description 1
- 229940011051 isopropyl acetate Drugs 0.000 description 1
- GWYFCOCPABKNJV-UHFFFAOYSA-N isovaleric acid Chemical compound CC(C)CC(O)=O GWYFCOCPABKNJV-UHFFFAOYSA-N 0.000 description 1
- 238000004811 liquid chromatography Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- NMJJFJNHVMGPGM-UHFFFAOYSA-N n-butylmethanoate Natural products CCCCOC=O NMJJFJNHVMGPGM-UHFFFAOYSA-N 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- WSGCRAOTEDLMFQ-UHFFFAOYSA-N nonan-5-one Chemical compound CCCCC(=O)CCCC WSGCRAOTEDLMFQ-UHFFFAOYSA-N 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 150000002989 phenols Chemical class 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 229920000052 poly(p-xylylene) Polymers 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 159000000001 potassium salts Chemical class 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 239000012429 reaction media Substances 0.000 description 1
- DCKVNWZUADLDEH-UHFFFAOYSA-N sec-butyl acetate Chemical compound CCC(C)OC(C)=O DCKVNWZUADLDEH-UHFFFAOYSA-N 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
【発明の詳細な説明】
本発明は、1・4−ジヒドロオキシー2−ナフトエ酸の
製造方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing 1,4-dihydroxy-2-naphthoic acid.
詳しく述べると、本発明は、1・4−ジヒドロオキシナ
フタリンを原料として有機媒体中で粉末状無水の炭酸カ
リウムと炭酸ガスとにより直接力ルボキシル化すること
により、1・4−ジヒドロオキシー2−ナフトエ酸を効
率よく製造する方法に関するものである。Specifically, the present invention uses 1,4-dihydroxynaphthalene as a raw material and directly carboxylates it with anhydrous powdered potassium carbonate and carbon dioxide gas in an organic medium to produce 1,4-dihydroxy-2-naphthalene. This invention relates to a method for efficiently producing acid.
本発明が目的とする1・4−ジヒドロオキシー2−ナフ
トエ酸は、染料、顔料および感光材料と10して有用な
ものであるにもかかわらず、工業的に有利な製造方法は
いまだ開発されていない。Although 1,4-dihydroxy-2-naphthoic acid, which is the object of the present invention, is useful as a dye, pigment, and photosensitive material, an industrially advantageous manufacturing method has not yet been developed. do not have.
1・4−ジヒドロオキシナフタリンから1・4−ジヒド
ロオキシー2−ナフトエ酸を合成する試みはたとえば、
Russig、、J、prakt−Chem−152区
旦、30(1900)によると、1 ・4−ジヒドロオ
キシナフタリンをアルコール溶媒中アルコール性苛性ナ
トリウム又はカリウムにより1・4−ジヒドロオキシナ
フタリンのナトリウム又はカリウム塩を合成し水素気流
中乾燥し次いで1・204−ジヒドロオキシナフタリン
のナトリウム又はカリウム塩の結晶を炭酸ガス加圧下1
70℃で20〜30時間反応させて希塩酸で酸析せしめ
1・4−ジヒドロオキシー 2−ナフトエ酸を合成した
という報告がある。Attempts to synthesize 1,4-dihydroxy-2-naphthoic acid from 1,4-dihydroxynaphthalene include, for example,
According to Russig, J. Prakt-Chem-152, 30 (1900), the sodium or potassium salt of 1,4-dihydroxynaphthalene is prepared with alcoholic sodium or potassium in an alcoholic solvent. was synthesized and dried in a hydrogen stream, and then crystals of sodium or potassium salt of 1,204-dihydroxynaphthalene were heated under pressure of carbon dioxide gas.
There is a report that 1,4-dihydroxy-2-naphthoic acid was synthesized by reacting at 70°C for 20 to 30 hours and acid precipitation with dilute hydrochloric acid.
しかし本発明者等の知見では25反応中間物である1・
4−ジヒドロオキシナフタリンのアルカリ金属塩は空気
の存在下で極めて不安定であり空気すなわち分子状酸素
と接触することにより容易に酸化され構造不明のメール
状物質に変化してしまい1・4−ジヒドロオキシナフメ
30 リンのアルカリ金属塩の結晶を安定に取り出すこ
とは極めて困難で実用的には不可能であること、さらに
1・4−ジヒドロオキシナフタリンのアルカリ金属塩と
炭酸ガスとの反応は気一固相反応であり気一固相反応は
高温では熱的に不均一になり35やすく、気一固相の接
触効率が悪いことから反応速度も著るしくおそくならざ
るをえないことが欠点となる。そのため副反応によるメ
ール状重合物が多量に副生したり未反応物が多く残存す
ることから1・4−ジヒドロオキシ−2−ナフトエ酸の
収率が悪く分離、精製も困難となる。従つて工業的にこ
の反応を実施する上で種々の難点を克服せねばならない
ことがわかつた。このように1・4−ジヒドロオキシナ
フタリンからの1・4−ジヒドロオキシ−2−ナフトエ
酸の合成は困難が伴なう故に従来から考えられている別
の方法としてフタル酸エステルとコハク酸エステルから
合成する方法が知られている(J.Anl.Chem.
SOc64798(1942))。However, according to the knowledge of the present inventors, 1.
The alkali metal salt of 4-dihydroxynaphthalene is extremely unstable in the presence of air, and when it comes into contact with air, that is, molecular oxygen, it is easily oxidized and turns into a mail-like substance of unknown structure, resulting in 1,4-dihydro Oxynaphme 30 It is extremely difficult and practically impossible to stably extract the crystals of the alkali metal salt of phosphorus, and furthermore, the reaction between the alkali metal salt of 1,4-dihydroxynaphthalene and carbon dioxide gas is difficult. The disadvantage of a gas-solid phase reaction is that it tends to become thermally non-uniform at high temperatures, and because the contact efficiency of the gas-solid phase is poor, the reaction rate must be extremely slow. Become. As a result, a large amount of mail-like polymers are produced due to side reactions and a large amount of unreacted substances remain, resulting in a poor yield of 1,4-dihydroxy-2-naphthoic acid and difficulty in separation and purification. Therefore, it has been found that various difficulties must be overcome in carrying out this reaction industrially. Since the synthesis of 1,4-dihydroxy-2-naphthoic acid from 1,4-dihydroxynaphthalene is difficult, an alternative method that has been considered in the past is to synthesize 1,4-dihydroxy-2-naphthoic acid from phthalate ester and succinate ester. A method of synthesis is known (J. Anl. Chem.
SOc64798 (1942)).
しかしこの方法とても収率が悪くしかも工程が多く繁雑
であることから工業的に有利な製造方法とは云えない。
本発明は、1・4−ジヒドロオキシナフタリンの直接カ
ルボキシル化反応により、1・4−ジヒドロオキシ−2
−ナフトエ酸を工業的に有利に製造することを目的とす
るもので1・4−ジヒドロオキシナフタリンを溶解性の
ある有機媒体に溶解せしめ粉末状無水の炭酸カリウムを
懸濁分散させながら加圧、撹拌下反応温度130〜20
0℃にて炭酸ガスによりカルボキシル化させることを特
徴とする。However, this method has a very poor yield and is complicated due to the large number of steps, so it cannot be said to be an industrially advantageous production method.
The present invention provides 1,4-dihydroxynaphthalene by direct carboxylation reaction of 1,4-dihydroxynaphthalene.
- The purpose is to produce naphthoic acid industrially advantageously, by dissolving 1,4-dihydroxynaphthalene in a soluble organic medium and applying pressure while suspending and dispersing powdered anhydrous potassium carbonate. Reaction temperature under stirring: 130-20
It is characterized by carboxylation with carbon dioxide gas at 0°C.
一般にフエノール類を水酸化ナトリウム又は水酸化カリ
ウム水溶液を用いてナトリウム塩又はカリウム塩とし次
いで脱水後炭酸ガスによりカルボキシル化させることは
コルベシュミット反応として良く知られている。本発明
では2個の水酸基を有する1・4−ジヒドロオキシナフ
タリンに対して溶解性のある媒体中で粉末状無水の炭酸
カリウムを懸濁分散させながら炭酸ガスにより同一反応
系で1段で2の位置を選択的にカルボキシル化し高収率
で1・4−ジヒドロオキシ−2−ナフトエ酸を製造する
方法が提供される。Generally, the process of converting phenols into sodium or potassium salts using an aqueous sodium hydroxide or potassium hydroxide solution, dehydrating them, and then carboxylating them with carbon dioxide gas is well known as the Kolbe-Schmidt reaction. In the present invention, 1,4-dihydroxynaphthalene, which has two hydroxyl groups, is dissolved in a medium in which powdered anhydrous potassium carbonate is suspended and dispersed, and carbon dioxide gas is used to react with 1,4-dihydrooxynaphthalene in the same reaction system in one step. A method for producing 1,4-dihydroxy-2-naphthoic acid in high yield by selectively carboxylating a position is provided.
本発明は具体的には以下に記すように実施される。The present invention is specifically implemented as described below.
本発明に用いるアルカリ源としては粉末状無水の炭酸カ
リウムが用いられ、原料1・4−ジヒドロオキシナフノ
リンに対し1.゛5モル倍以上、好ましくは2.0〜2
.5モル倍量メ:用いられる。炭酸カリウムの添加量が
1.5モル倍以下になると1・4−ジヒドロオキシ−2
−ナフトエ酸の収率が悪く未反応物が増加すると共に副
反応による構造不明のタール状重合物が増加する。粉末
状無水の炭酸カリウムは工業用グレードのものが用いら
れるが、反応速度を速めるためには微粒子状のものが好
ましく、粒子径は通常200ミクロン以下、好ましくは
100ミクロン以下のものが用いられる。Powdered anhydrous potassium carbonate is used as the alkali source used in the present invention, and 1.゛5 times or more by mole, preferably 2.0 to 2
.. 5 molar amount: Used. When the amount of potassium carbonate added is 1.5 times the mole or less, 1,4-dihydroxy-2
- The yield of naphthoic acid is poor, the amount of unreacted substances increases, and the amount of tar-like polymers of unknown structure due to side reactions increases. The powdered anhydrous potassium carbonate used is of industrial grade, but in order to speed up the reaction rate, it is preferably in the form of fine particles, and the particle size is usually 200 microns or less, preferably 100 microns or less.
本発明は1・4−ジヒドロオキシナフタリンに対し溶解
性のある媒体中で懸濁状態で反応を遂行させる。In the present invention, the reaction is carried out in a suspension state in a medium in which 1,4-dihydroxynaphthalene is soluble.
気一固相反応では粉体の伝熱速度がおそい。In the gas-solid phase reaction, the heat transfer rate of the powder is slow.
そのため除熱が困難で熱的に不均になつたり、炭酸ガス
との接触効率が悪いと云つたことから反応時間が長くな
り、反応温度も高くせざるを得ない。その結果、高温に
不安定な原料1・4−ジヒドロオキシナフタリンや中間
生成物の1・4−ジヒドロオキシナフタリンのカリウム
塩が高温で長時間保持されるため反応そのものでの収率
が悪くなり、しかも副反応による重合物の増加、あるい
は未反応物の増加により1・4−ジヒドロオキシ−2−
ナフトエ酸の分離、精製が困難となる。したがつて本発
明は媒体中で反応させる方が有利である。本発明に用い
る媒体としては、原料及び反応生成物に対して溶解性の
ある有機溶媒が用いられる。さらに溶解性のある有機溶
媒を用いる利点としては、1・4−ジヒドロオキシナフ
タリンと炭酸カリウムとの反応が固体一固体の懸濁状態
での反応に較べ1・4−ジヒドロオキシナフタリンを溶
媒に溶解した溶液中で粉末状無水の炭酸カリウムを懸濁
させながら反応を行ない、反応速度が著るしく増大しよ
り低温での反応が可能となり副生成物が減少し高収率で
1・4−ジヒドロオキシ−2−ナフトエ酸が得られるこ
ともあげられる。原料1・4−ジヒドロオキシナフタリ
ン及び反応生成物に対して溶解性のある溶媒としては、
ケトン類、エステル類及び炭素数4以上のアルコール、
多価アルコールとその誘導体から選ばれる。As a result, it is difficult to remove heat, resulting in thermal imbalance, and the contact efficiency with carbon dioxide gas is poor, resulting in a long reaction time and a high reaction temperature. As a result, the raw material 1,4-dihydroxynaphthalene and the intermediate product potassium salt of 1,4-dihydroxynaphthalene, which are unstable at high temperatures, are kept at high temperatures for a long time, resulting in poor yields in the reaction itself. Moreover, due to an increase in polymerized products due to side reactions or an increase in unreacted products, 1,4-dihydroxy-2-
Separation and purification of naphthoic acid becomes difficult. Therefore, in the present invention, it is advantageous to carry out the reaction in a medium. The medium used in the present invention is an organic solvent that is soluble in the raw materials and reaction products. Furthermore, the advantage of using a soluble organic solvent is that the reaction between 1,4-dihydroxynaphthalene and potassium carbonate is better when 1,4-dihydroxynaphthalene is dissolved in the solvent than when the reaction is in a solid-solid suspension state. The reaction is carried out while suspending powdered anhydrous potassium carbonate in the solution, which significantly increases the reaction rate, allows the reaction to be carried out at lower temperatures, reduces by-products, and produces 1,4-dihydrocarbonate in high yield. It is also possible to obtain oxy-2-naphthoic acid. Solvents that are soluble for the raw material 1,4-dihydroxynaphthalene and the reaction product include:
Ketones, esters, and alcohols with 4 or more carbon atoms,
Selected from polyhydric alcohols and their derivatives.
これらの溶媒は1・4−ジヒドロナフタリンに対して溶
解性があるのみならず、反応生成物である1・4−ジヒ
ドロオキシ−2−ナフトエ酸に対しても溶解性があり、
しかも副生成物である重合物に対する溶解性が小さいこ
とから分離、精製工程においても好都合なものである。
具体的には次のような媒体が例示される。These solvents are not only soluble in 1,4-dihydronaphthalene, but also in 1,4-dihydroxy-2-naphthoic acid, which is a reaction product.
Moreover, it is convenient in separation and purification steps because it has low solubility in polymerized by-products.
Specifically, the following media are exemplified.
ケトン類
メチルn−プロピルケトン、メチルn−ブチルケトン、
メチルイソブチルケトン、メチルn−アミルケトン、メ
チルn−ヘキシルケトン、ジエチルケトン、エチルn−
ブチルケトン、ジn−プロピルケトン、ジイソブチルケ
トン、アセトン油、タンチルオキシド、シクロヘキサノ
ン、メチルシクロヘキサノン、アセトフエノン、エステ
ル類
ギ酸n−ブチル、ギ酸イソブチル、ギ酸アミル、酢酸n
−プロピル、酢酸イソプロピル、酢酸nブチル、酢酸イ
ソブチル、酢酸第2ブチル、酢酸n−アミル、酢酸イソ
アミル、酢酸メチルイソアミル、酢酸メトキシブチル、
酢酸第2ヘキシル、酢酸2エチルブチル、酢酸2エチル
ヘキシル、酢酸シクロヘキシル、酢酸ペンチル、プロピ
オン酸エチル、プロピオン酸n−ブチル、プロピオン酸
イソアミルC4以上のアルコール類
n−ブタノール、イソブタノール、n−アミルアルコー
ル、インアミルアルコール、メチルアミルアルコール、
n−ヘプタノール、シクロヘキサノール、第二アミルア
ルコール、3−ペンタノール、第三アミルアルコール、
フーデル油、n−ヘキサノール、2エチルブタノール、
2ヘプ汐ノール、3ヘプタノール、n−オクノノール、
2オクタノール、2エチルヘキサノール、ノナノール、
n−デカノール、シクロヘキサノール多価アルコールと
その誘導体
エチレングリコールジブチルエーテル、エチレングリコ
ールモノブチルエーテルアセテート、エチレングリコー
ルジアセテート、ジエチレングリコールモノブチルエー
テルアセテート、エチルセロソルブアセテート、エチレ
ングリコールモノブチルエーテル以上のような媒体があ
げられるが原料1・4ジヒドロオキシナフタリンと媒体
の比は、1・4〜ジヒドロオキシナフタリンの溶解度に
関係するが必ずしも完全な溶液状にする必要はなく、大
部分溶解した状態で反応に供してもよい。Ketones methyl n-propyl ketone, methyl n-butyl ketone,
Methyl isobutyl ketone, methyl n-amyl ketone, methyl n-hexyl ketone, diethyl ketone, ethyl n-
Butyl ketone, di-n-propyl ketone, diisobutyl ketone, acetone oil, tantyl oxide, cyclohexanone, methylcyclohexanone, acetophenone, esters n-butyl formate, isobutyl formate, amyl formate, acetic acid n
-propyl, isopropyl acetate, n-butyl acetate, isobutyl acetate, sec-butyl acetate, n-amyl acetate, isoamyl acetate, methylisoamyl acetate, methoxybutyl acetate,
2-hexyl acetate, 2-ethylbutyl acetate, 2-ethylhexyl acetate, cyclohexyl acetate, pentyl acetate, ethyl propionate, n-butyl propionate, isoamyl propionate C4 or higher alcohols n-butanol, isobutanol, n-amyl alcohol, in amyl alcohol, methyl amyl alcohol,
n-heptanol, cyclohexanol, secondary amyl alcohol, 3-pentanol, tertiary amyl alcohol,
Fudel oil, n-hexanol, 2-ethylbutanol,
2-hepshionol, 3-heptanol, n-oknonol,
2 octanol, 2 ethylhexanol, nonanol,
Examples include n-decanol, cyclohexanol polyhydric alcohol and its derivatives ethylene glycol dibutyl ether, ethylene glycol monobutyl ether acetate, ethylene glycol diacetate, diethylene glycol monobutyl ether acetate, ethyl cellosolve acetate, and ethylene glycol monobutyl ether. The ratio of the raw material 1.4 dihydrooxynaphthalene to the medium is related to the solubility of 1.4 to dihydrooxynaphthalene, but it is not necessarily necessary to form a complete solution, and the reaction may be carried out in a mostly dissolved state.
通常1・4−ジヒドロオキシナフメリン:媒体は1:1
〜15重量倍の範囲が実質的である。又原料1・4−ジ
ヒドロオキシナフタリンと粉末状炭酸カリウム、及び炭
酸ガスとの接触効率を良好にするためには攪拌速度、攪
拌機の構造も、懸濁物を微粒化分散させ反応速度を増大
させる意味で重要である。一般にコルベシユミツト反応
は原料系への水分フの混入は反応を阻害すると言われて
いるが、本発明においてはカルボキシル化反応が阻害さ
れるのみならず、原料及び中間生成物が強アルカリ性に
おいて極めて不安定であるため強アルカリ性にならない
ように原料及び媒体混合物中の水分を0.5%以下、好
ましくは0.3%以下にすることにより重合物等の副反
応が抑制される。Usually 1,4-dihydroxynaphmelin: vehicle is 1:1
A range of 15 to 15 times by weight is substantial. In addition, in order to improve the contact efficiency between the raw material 1,4-dihydroxynaphthalene, powdered potassium carbonate, and carbon dioxide gas, the stirring speed and the structure of the stirrer should be adjusted to atomize and disperse the suspended matter and increase the reaction rate. important in meaning. It is generally said that the Kolbeschmitt reaction is inhibited by the introduction of water into the raw material system, but in the present invention, not only is the carboxylation reaction inhibited, but the raw materials and intermediate products are extremely unstable in strong alkalinity. Therefore, by controlling the water content in the raw material and medium mixture to 0.5% or less, preferably 0.3% or less so as not to become strongly alkaline, side reactions of polymers, etc. are suppressed.
かくして媒体1・4−ジヒドロオキシナフタリン及び粉
末状炭酸カリウムが反応器に仕込まれカルボキシル化反
応に供されるが、原料媒体懸濁物及び反応器空間部に存
在する空気を完全に置換するため攪拌下炭酸ガスを吹き
込みパージする操作をし空気を置換排除する。Thus, the medium 1,4-dihydroxynaphthalene and powdered potassium carbonate are charged into the reactor and subjected to the carboxylation reaction, but stirring is required to completely replace the raw material medium suspension and the air present in the reactor space. Perform a purge operation by blowing in carbon dioxide gas to replace and eliminate air.
次に炭酸ガス加圧下で昇温する。この操作は酸素の存在
下で不安定な1・4−ジヒドロオキシナフタリン及び中
間生成物である1・4−ジヒドロオキシナフタリンのカ
リウム塩、1・4−ジ.ヒドロオキシ−2−ナフトエ酸
のカリウム塩の重合などによる変質を防止するために極
めて重要である。反応圧力は20kg/Cd以上、好ま
しくは30kg/CrA以上必要であり、炭酸ガス加圧
下で反応させる。Next, the temperature is raised under pressure of carbon dioxide gas. This operation involves the use of 1,4-dihydroxynaphthalene, which is unstable in the presence of oxygen, and the intermediate product, the potassium salt of 1,4-dihydroxynaphthalene, 1,4-dihydrooxynaphthalene. This is extremely important in order to prevent deterioration due to polymerization of potassium salt of hydroxy-2-naphthoic acid. The reaction pressure is required to be 20 kg/Cd or more, preferably 30 kg/CrA or more, and the reaction is carried out under carbon dioxide gas pressure.
反応温度は130℃〜200℃、好ましくは140〜1
80℃である。The reaction temperature is 130°C to 200°C, preferably 140 to 1
The temperature is 80°C.
反応温度は低いとカルボキシル化反応は進まず、逆に2
00℃を越えると原料及び中間生成物の重合反応が進み
汐−ル状黒色重合物、緑色重合物が副生してくる。反応
時間は2時間以上、好ましくは4〜8時間である。If the reaction temperature is low, the carboxylation reaction will not proceed; on the contrary, 2
When the temperature exceeds 00 DEG C., the polymerization reaction of the raw materials and intermediate products progresses, and a slug-like black polymer and a green polymer are produced as by-products. The reaction time is 2 hours or more, preferably 4 to 8 hours.
次に本発明方法を実施例により説明する。Next, the method of the present invention will be explained using examples.
実施例 1
1・4−ジヒドロオキシナフタリン80y1粉末状無水
の炭酸カリウム平均粒径100ミクロンのもの138y
1媒体としてメチルイソブチルケトン400m1を内容
積11の攪拌式オートクレーブに仕込み攪拌混合して原
料懸濁物を調製した。Example 1 1,4-dihydroxynaphthalene 80y1 Powdered anhydrous potassium carbonate with an average particle size of 100 microns 138y
A raw material suspension was prepared by charging 400 ml of methyl isobutyl ketone as a medium into a stirring autoclave having an internal volume of 11 and stirring and mixing.
この原料及び媒体中の水分は0.2%であつた。次に炭
酸ガスを圧入攪拌しながら圧力15k9/CrAでオー
トクレーブ内ガスをパージした。パージ後再び同様の操
作をし、オートクレーブ内空気を完全に置換した後炭酸
ガスを圧入しながら昇温速度3℃/分で150℃まで昇
温し、ついで攪拌速度600rpm、炭酸ガス流通下圧
力50kg/Cdに保持しながら6時間反応させた。反
応後冷却解圧し1%ハイドロサルファイド水溶液200
m1をオートクレーブ内に入れ30分間攪拌後内容物を
窒素置換された容器に取出し攪拌下1:1硫酸水溶液を
加え酸性とし、溶媒としてメチルイソブチルケトン70
0m1を加え1・4ジヒドロオキシ−2−ナフトエ酸を
溶解した。The moisture content in this raw material and medium was 0.2%. Next, the gas inside the autoclave was purged at a pressure of 15k9/CrA while carbon dioxide gas was injected and stirred. After purging, perform the same operation again to completely replace the air in the autoclave, and then raise the temperature to 150°C at a rate of 3°C/min while injecting carbon dioxide gas, then stir at 600 rpm and under a pressure of 50 kg under carbon dioxide gas flow. /Cd and allowed to react for 6 hours. After the reaction, cool and depressurize and add 1% hydrosulfide aqueous solution 200ml.
After stirring for 30 minutes in an autoclave, the contents were taken out into a container purged with nitrogen, and while stirring, a 1:1 aqueous sulfuric acid solution was added to make it acidic, and methyl isobutyl ketone 70% was used as a solvent.
0 ml was added to dissolve 1,4 dihydroxy-2-naphthoic acid.
次にこの溶液を沢過し、沢液を溶媒層と水層に分液し、
溶媒層を活性炭で脱色し、溶媒を蒸発させたところ1・
4−ジヒドロオキシ−2−ナフトエ酸の結晶(純度94
.2%)103.7fを得た。収率は95.3モル%で
あり、未反応1・4−ジヒドロオキシナフタリンは液体
クロマトグラフ分析により1.4%であつた。以上の結
果を第1表に示す。実施例 2〜31・4−ジヒドロオ
キシナフノリン807に対して粉末状無水の炭酸カリウ
ム平均粒径100ミクロンのものをそれぞれ1727及
び1037とした以外は実施例1と同じ条件で反応を行
なつた結果、炭酸カリウム103Vの場合すなわち1・
4−ジヒドロオキシナフタリンと炭酸カリウムのモル比
1:1.5とすると未反応率が増加した。Next, filter this solution, separate the solution into a solvent layer and an aqueous layer,
After decolorizing the solvent layer with activated carbon and evaporating the solvent, 1.
Crystals of 4-dihydroxy-2-naphthoic acid (purity 94
.. 2%) 103.7f was obtained. The yield was 95.3 mol%, and unreacted 1,4-dihydroxynaphthalene was found to be 1.4% by liquid chromatography analysis. The above results are shown in Table 1. Examples 2 to 3 The reaction was carried out under the same conditions as in Example 1, except that powdered anhydrous potassium carbonate with an average particle size of 100 microns was used as 1727 and 1037, respectively, for 1,4-dihydroxynaphnoline 807. As a result, in the case of potassium carbonate 103V, that is, 1.
When the molar ratio of 4-dihydroxynaphthalene and potassium carbonate was set to 1:1.5, the unreacted rate increased.
結果を第1表に示す。実施例 4
1・4−ジヒドロオキシナフタリン80V、粉末状無水
の炭酸カリウム平均粒径100ミクロンのもの1387
、媒体としてメチルインブチルケトン200m1を用い
た。The results are shown in Table 1. Example 4 1,4-dihydroxynaphthalene 80V, powdered anhydrous potassium carbonate 1387 with an average particle size of 100 microns
, 200 ml of methyl in butyl ketone was used as the medium.
また反応終了後使用する溶媒としてメチルイソブチルケ
トン900m1を加え1・4−ジヒドロオキシ−2−ナ
フトエ酸を溶解した以外は実施例1と同じ条件で反応を
行なつた。結果を第1表に示す。実施例 5
反応圧力を351<9/CWiとした以外は実施例1と
同じ条件で行なつた。The reaction was carried out under the same conditions as in Example 1, except that 900 ml of methyl isobutyl ketone was added as a solvent after the reaction was completed to dissolve 1,4-dihydroxy-2-naphthoic acid. The results are shown in Table 1. Example 5 The reaction was carried out under the same conditions as in Example 1 except that the reaction pressure was 351<9/CWi.
結果を第1表に示す。実施例 6反応温度を140℃、
反応時間を8時間とした以外は実施例1と同じ条件で反
応を行なつた。The results are shown in Table 1. Example 6 Reaction temperature was 140°C.
The reaction was carried out under the same conditions as in Example 1 except that the reaction time was 8 hours.
結果を第1表に示す。実施例 7
反応温度170℃、反応時間を5時間とした以外は実施
例1と同じ条件で反応を行なつた。The results are shown in Table 1. Example 7 A reaction was carried out under the same conditions as in Example 1 except that the reaction temperature was 170°C and the reaction time was 5 hours.
結果を第1表に示す。実施例 8〜10
反応媒体としてそれぞれジイソブチルケトン、フイソア
ミルアルコール、酢酸イソブチルを用いた以外は実施例
1と同じ条件で反応を行なつた。The results are shown in Table 1. Examples 8 to 10 Reactions were carried out under the same conditions as in Example 1 except that diisobutyl ketone, physoamyl alcohol, and isobutyl acetate were used as reaction media, respectively.
但し、ジイソブチルケトン、酢酸イソブチルを媒体とし
て用いた場合には、酸析後の1・4−ジヒドロオキシ−
2−ナフトエ酸の溶媒量を各々18001800m1用
いた。結果を第1表に示す。比較例 1(無溶媒下の反
応)
1・4−ジヒドロオキシナフタリン207、粉末状無水
の炭酸カリウム平均粒径100ミクロンのもの60Vを
内容積11の攪拌式オートクレーブに仕込み攪拌混合し
て原料懸濁物を調製した。However, when diisobutyl ketone or isobutyl acetate is used as a medium, 1,4-dihydroxy-
The amount of solvent for 2-naphthoic acid was 1,800 and 1,800 ml, respectively. The results are shown in Table 1. Comparative Example 1 (Reaction without solvent) 1,4-dihydroxynaphthalene 207, powdered anhydrous potassium carbonate with an average particle diameter of 100 microns, 60 V, was charged into a stirring autoclave with an internal volume of 11, and the raw materials were suspended by stirring and mixing. I prepared something.
この原料及び媒体中の水分は0.2%であつた。次に炭
酸ガスを圧入攪拌しながら圧力151<g/Cdでオー
トクレーブ内ガスをパージしたパージ後再び同様の操作
をし、オートクレーブ内空気を完全に置換した後、炭酸
ガスを圧入しながら昇温速度3℃/分で175℃まで昇
温し、攪拌速度600rpm炭酸ガス流通下圧力50k
g/Cdに保持しながら7時間反応させた。反応後、冷
却解圧し1%ハイドロサルファイド水溶液200miを
オートクレーブ内に入れ30分間攪拌後内容物を窒素置
換された容器に取出し、攪拌下1:1硫酸水溶液を加え
酸析した。The moisture content in this raw material and medium was 0.2%. Next, the gas inside the autoclave was purged at a pressure of 151<g/Cd while stirring and injecting carbon dioxide gas. After purging, the same operation was performed again to completely replace the air inside the autoclave, and the temperature increase rate was increased while injecting carbon dioxide gas. The temperature was raised to 175°C at a rate of 3°C/min, stirring speed was 600 rpm, and the pressure was 50 k under carbon dioxide gas flow.
The reaction was carried out for 7 hours while maintaining g/Cd. After the reaction, the autoclave was cooled and depressurized, and 200 ml of a 1% aqueous hydrosulfide solution was put into the autoclave. After stirring for 30 minutes, the contents were taken out into a nitrogen-purged container, and while stirring, a 1:1 aqueous sulfuric acid solution was added thereto for acid precipitation.
次に析出した1・4−ジヒドロオキシ−2−ナフトエ酸
に溶媒としてメチルイソブチルケトン300耐を加え溶
解し、この溶液を沢過し、沢液を溶媒層と水層に分液し
、溶媒層を活性炭で脱色し溶媒を蒸発させ析出した結晶
を沢過、乾燥し純度65.2%の粗1・4−ジヒドロオ
キシ−2−ナフトエ酸20.1Vを得た。収率は51.
2モル%であり、1・4−ジヒドロオキシナフタリンの
未反応率は24.4%であつた。以上の結果を第1表に
示す。比較例 2粉末状炭酸カリウム40f7、圧力4
5kg/Cd、反応時間を12時間とした以外は比較例
1と同じ条件で行つた。Next, methyl isobutyl ketone 300 resistant was added as a solvent to the precipitated 1,4-dihydroxy-2-naphthoic acid and dissolved, this solution was filtered, the slurry was separated into a solvent layer and an aqueous layer, and the solvent layer was decolorized with activated carbon, the solvent was evaporated, and the precipitated crystals were filtered and dried to obtain 20.1 V of crude 1,4-dihydroxy-2-naphthoic acid with a purity of 65.2%. Yield is 51.
2 mol %, and the unreacted rate of 1,4-dihydroxynaphthalene was 24.4%. The above results are shown in Table 1. Comparative Example 2 Powdered potassium carbonate 40f7, pressure 4
The reaction was carried out under the same conditions as Comparative Example 1 except that the reaction time was 5 kg/Cd and the reaction time was 12 hours.
結果を第1.表に示す。比較例 3
オートクレーブ内の空気を炭酸ガスで置換せずに反応し
た以外は実施例1と同じ条件で行なつた。Results first. Shown in the table. Comparative Example 3 The reaction was carried out under the same conditions as in Example 1, except that the reaction was carried out without replacing the air in the autoclave with carbon dioxide gas.
Claims (1)
解性のある有機媒体中に溶解し、これに炭酸カリウムを
懸濁せしめ加圧、攪拌下130〜200℃の温度にて炭
酸ガスによりカルボキシル化反応せしめることを特徴と
する1・4−ジヒドロオキシ−2−ナフトエ酸の製造方
法。 2 1・4−ジヒドロオキシナフタリンと炭酸カリウム
のモル比を1:1.5以上で反応を行なうことを特徴と
する特許請求の範囲第1項記載の方法。 3 原料及び媒体中の水分が0.5重量パーセント以下
であることを特徴とする特許請求の範囲第1項記載の方
法。 4 実質的に分子状酸素の不存在下で行なうことを特徴
とする特許請求の範囲第1項記載の方法。[Scope of Claims] 1. 1,4-Dihydroxynaphthalene is dissolved in an organic medium that is soluble therein, potassium carbonate is suspended in this, and carbonic acid is added under pressure and stirring at a temperature of 130 to 200°C. A method for producing 1,4-dihydroxy-2-naphthoic acid, which comprises carrying out a carboxylation reaction using a gas. 2. The method according to claim 1, wherein the reaction is carried out at a molar ratio of 1,4-dihydroxynaphthalene and potassium carbonate of 1:1.5 or more. 3. The method according to claim 1, wherein the moisture content in the raw materials and medium is 0.5% by weight or less. 4. The method according to claim 1, which is carried out substantially in the absence of molecular oxygen.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1081481A JPS5912653B2 (en) | 1981-01-29 | 1981-01-29 | Method for producing 1,4-dihydroxy-2-naphthoic acid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1081481A JPS5912653B2 (en) | 1981-01-29 | 1981-01-29 | Method for producing 1,4-dihydroxy-2-naphthoic acid |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57126443A JPS57126443A (en) | 1982-08-06 |
| JPS5912653B2 true JPS5912653B2 (en) | 1984-03-24 |
Family
ID=11760809
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1081481A Expired JPS5912653B2 (en) | 1981-01-29 | 1981-01-29 | Method for producing 1,4-dihydroxy-2-naphthoic acid |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5912653B2 (en) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59141537A (en) * | 1983-02-01 | 1984-08-14 | Kawasaki Kasei Chem Ltd | Method for producing 1,4-dihydroxy-2-naphthoic acid |
| JPS59186942A (en) * | 1983-04-07 | 1984-10-23 | Kawasaki Kasei Chem Ltd | Method for purifying crude 1,4-dihydroxy-2-naphthoic acid or its salt |
| JPS60104037A (en) * | 1983-11-10 | 1985-06-08 | Kawasaki Kasei Chem Ltd | Method for producing 1,4-dihydroxy-2-naphthoic acid |
| JP3208458B2 (en) * | 1992-01-17 | 2001-09-10 | 住友化学工業株式会社 | Method for producing 1,4-dihydroxy-2-naphthoic acid |
| DE4316933A1 (en) * | 1993-05-21 | 1994-11-24 | Hoechst Ag | Process for the preparation of aromatic hydroxycarboxylic acids |
| DE4316937A1 (en) * | 1993-05-21 | 1994-12-01 | Hoechst Ag | Process for the preparation of aromatic hydroxycarboxylic acids |
| JP5380683B2 (en) * | 2008-01-22 | 2014-01-08 | 学校法人千葉工業大学 | Process for producing aromatic hydroxycarboxylic acid |
-
1981
- 1981-01-29 JP JP1081481A patent/JPS5912653B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57126443A (en) | 1982-08-06 |
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