JPS63277645A - Esterification of aromatic compound - Google Patents
Esterification of aromatic compoundInfo
- Publication number
- JPS63277645A JPS63277645A JP62112614A JP11261487A JPS63277645A JP S63277645 A JPS63277645 A JP S63277645A JP 62112614 A JP62112614 A JP 62112614A JP 11261487 A JP11261487 A JP 11261487A JP S63277645 A JPS63277645 A JP S63277645A
- Authority
- JP
- Japan
- Prior art keywords
- acid
- reaction
- aromatic compound
- phenolic hydroxyl
- hydroxyl group
- 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.)
- Pending
Links
- 150000001491 aromatic compounds Chemical class 0.000 title claims abstract description 24
- 230000032050 esterification Effects 0.000 title description 4
- 238000005886 esterification reaction Methods 0.000 title description 4
- 238000006243 chemical reaction Methods 0.000 claims abstract description 36
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 claims abstract description 24
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims abstract description 21
- 150000007524 organic acids Chemical class 0.000 claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 12
- 239000003377 acid catalyst Substances 0.000 claims abstract description 7
- 238000000034 method Methods 0.000 claims description 22
- 238000000066 reactive distillation Methods 0.000 claims description 5
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 abstract description 27
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 abstract description 14
- 239000002253 acid Substances 0.000 abstract description 9
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 abstract description 8
- 238000004821 distillation Methods 0.000 abstract description 8
- 150000001875 compounds Chemical class 0.000 abstract description 7
- WPYMKLBDIGXBTP-UHFFFAOYSA-N benzoic acid Chemical compound OC(=O)C1=CC=CC=C1 WPYMKLBDIGXBTP-UHFFFAOYSA-N 0.000 abstract description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract description 4
- 235000019260 propionic acid Nutrition 0.000 abstract description 4
- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical compound O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 abstract description 4
- 239000002994 raw material Substances 0.000 abstract description 4
- 239000005711 Benzoic acid Substances 0.000 abstract description 3
- 235000010233 benzoic acid Nutrition 0.000 abstract description 3
- 239000003054 catalyst Substances 0.000 abstract description 3
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 abstract description 2
- 230000002378 acidificating effect Effects 0.000 abstract description 2
- 239000011261 inert gas Substances 0.000 abstract description 2
- 239000003456 ion exchange resin Substances 0.000 abstract description 2
- 229920003303 ion-exchange polymer Polymers 0.000 abstract description 2
- KYTZHLUVELPASH-UHFFFAOYSA-N naphthalene-1,2-dicarboxylic acid Chemical compound C1=CC=CC2=C(C(O)=O)C(C(=O)O)=CC=C21 KYTZHLUVELPASH-UHFFFAOYSA-N 0.000 abstract description 2
- 229910052757 nitrogen Inorganic materials 0.000 abstract description 2
- 229920000642 polymer Polymers 0.000 abstract description 2
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 abstract 1
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 15
- 150000002148 esters Chemical class 0.000 description 7
- 239000000203 mixture Substances 0.000 description 7
- -1 nitrile compound Chemical class 0.000 description 7
- 235000005985 organic acids Nutrition 0.000 description 7
- LFSHREXVLSTLFB-UHFFFAOYSA-N 1-cyanoethenyl acetate Chemical compound CC(=O)OC(=C)C#N LFSHREXVLSTLFB-UHFFFAOYSA-N 0.000 description 4
- KJCVRFUGPWSIIH-UHFFFAOYSA-N 1-naphthol Chemical compound C1=CC=C2C(O)=CC=CC2=C1 KJCVRFUGPWSIIH-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 150000008065 acid anhydrides Chemical class 0.000 description 3
- 125000003118 aryl group Chemical group 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- 150000001805 chlorine compounds Chemical class 0.000 description 3
- 230000035484 reaction time Effects 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 125000001424 substituent group Chemical group 0.000 description 3
- GXXXUZIRGXYDFP-UHFFFAOYSA-M 2-(4-methylphenyl)acetate Chemical compound CC1=CC=C(CC([O-])=O)C=C1 GXXXUZIRGXYDFP-UHFFFAOYSA-M 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
- FERIUCNNQQJTOY-UHFFFAOYSA-N Butyric acid Chemical compound CCCC(O)=O FERIUCNNQQJTOY-UHFFFAOYSA-N 0.000 description 2
- VZCYOOQTPOCHFL-OWOJBTEDSA-N Fumaric acid Chemical compound OC(=O)\C=C\C(O)=O VZCYOOQTPOCHFL-OWOJBTEDSA-N 0.000 description 2
- YLQBMQCUIZJEEH-UHFFFAOYSA-N Furan Chemical compound C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-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
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- AFVFQIVMOAPDHO-UHFFFAOYSA-N Methanesulfonic acid Chemical compound CS(O)(=O)=O AFVFQIVMOAPDHO-UHFFFAOYSA-N 0.000 description 2
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 description 2
- KAESVJOAVNADME-UHFFFAOYSA-N Pyrrole Chemical compound C=1C=CNC=1 KAESVJOAVNADME-UHFFFAOYSA-N 0.000 description 2
- YTPLMLYBLZKORZ-UHFFFAOYSA-N Thiophene Chemical compound C=1C=CSC=1 YTPLMLYBLZKORZ-UHFFFAOYSA-N 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 150000001298 alcohols Chemical class 0.000 description 2
- MWPLVEDNUUSJAV-UHFFFAOYSA-N anthracene Chemical compound C1=CC=CC2=CC3=CC=CC=C3C=C21 MWPLVEDNUUSJAV-UHFFFAOYSA-N 0.000 description 2
- LLEMOWNGBBNAJR-UHFFFAOYSA-N biphenyl-2-ol Chemical class OC1=CC=CC=C1C1=CC=CC=C1 LLEMOWNGBBNAJR-UHFFFAOYSA-N 0.000 description 2
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 2
- YCIMNLLNPGFGHC-UHFFFAOYSA-N catechol Chemical compound OC1=CC=CC=C1O YCIMNLLNPGFGHC-UHFFFAOYSA-N 0.000 description 2
- 239000004927 clay Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N diphenyl Chemical compound C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- FUZZWVXGSFPDMH-UHFFFAOYSA-N hexanoic acid Chemical compound CCCCCC(O)=O FUZZWVXGSFPDMH-UHFFFAOYSA-N 0.000 description 2
- LELOWRISYMNNSU-UHFFFAOYSA-N hydrogen cyanide Chemical compound N#C LELOWRISYMNNSU-UHFFFAOYSA-N 0.000 description 2
- RJNPPEUAJCEUPV-UHFFFAOYSA-N naphthalen-2-yl acetate Chemical compound C1=CC=CC2=CC(OC(=O)C)=CC=C21 RJNPPEUAJCEUPV-UHFFFAOYSA-N 0.000 description 2
- IWDCLRJOBJJRNH-UHFFFAOYSA-N p-cresol Chemical compound CC1=CC=C(O)C=C1 IWDCLRJOBJJRNH-UHFFFAOYSA-N 0.000 description 2
- YNPNZTXNASCQKK-UHFFFAOYSA-N phenanthrene Chemical compound C1=CC=C2C3=CC=CC=C3C=CC2=C1 YNPNZTXNASCQKK-UHFFFAOYSA-N 0.000 description 2
- JOXIMZWYDAKGHI-UHFFFAOYSA-N toluene-4-sulfonic acid Chemical compound CC1=CC=C(S(O)(=O)=O)C=C1 JOXIMZWYDAKGHI-UHFFFAOYSA-N 0.000 description 2
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 2
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 150000004786 2-naphthols Chemical class 0.000 description 1
- WXNZTHHGJRFXKQ-UHFFFAOYSA-N 4-chlorophenol Chemical compound OC1=CC=C(Cl)C=C1 WXNZTHHGJRFXKQ-UHFFFAOYSA-N 0.000 description 1
- GCNTZFIIOFTKIY-UHFFFAOYSA-N 4-hydroxypyridine Chemical compound OC1=CC=NC=C1 GCNTZFIIOFTKIY-UHFFFAOYSA-N 0.000 description 1
- 239000005725 8-Hydroxyquinoline Substances 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 1
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- IPBVNPXQWQGGJP-UHFFFAOYSA-N acetic acid phenyl ester Natural products CC(=O)OC1=CC=CC=C1 IPBVNPXQWQGGJP-UHFFFAOYSA-N 0.000 description 1
- PQLVXDKIJBQVDF-UHFFFAOYSA-N acetic acid;hydrate Chemical compound O.CC(O)=O PQLVXDKIJBQVDF-UHFFFAOYSA-N 0.000 description 1
- 239000003905 agrochemical Substances 0.000 description 1
- 125000002723 alicyclic group Chemical group 0.000 description 1
- 125000001931 aliphatic group Chemical group 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 125000003545 alkoxy group Chemical group 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000004305 biphenyl Substances 0.000 description 1
- 235000010290 biphenyl Nutrition 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 239000012320 chlorinating reagent Substances 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012374 esterification agent Substances 0.000 description 1
- FPIQZBQZKBKLEI-UHFFFAOYSA-N ethyl 1-[[2-chloroethyl(nitroso)carbamoyl]amino]cyclohexane-1-carboxylate Chemical compound ClCCN(N=O)C(=O)NC1(C(=O)OCC)CCCCC1 FPIQZBQZKBKLEI-UHFFFAOYSA-N 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000005194 fractionation Methods 0.000 description 1
- 239000001530 fumaric acid Substances 0.000 description 1
- 125000005843 halogen group Chemical group 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 description 1
- 239000011976 maleic acid Substances 0.000 description 1
- 229940098779 methanesulfonic acid Drugs 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 125000000449 nitro group Chemical group [O-][N+](*)=O 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- 125000000962 organic group Chemical group 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229960003540 oxyquinoline Drugs 0.000 description 1
- 229940090668 parachlorophenol Drugs 0.000 description 1
- 150000002989 phenols Chemical class 0.000 description 1
- FCJSHPDYVMKCHI-UHFFFAOYSA-N phenyl benzoate Chemical compound C=1C=CC=CC=1C(=O)OC1=CC=CC=C1 FCJSHPDYVMKCHI-UHFFFAOYSA-N 0.000 description 1
- 229940049953 phenylacetate Drugs 0.000 description 1
- WLJVXDMOQOGPHL-UHFFFAOYSA-N phenylacetic acid Chemical compound OC(=O)CC1=CC=CC=C1 WLJVXDMOQOGPHL-UHFFFAOYSA-N 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000011403 purification operation Methods 0.000 description 1
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 description 1
- MCJGNVYPOGVAJF-UHFFFAOYSA-N quinolin-8-ol Chemical compound C1=CN=C2C(O)=CC=CC2=C1 MCJGNVYPOGVAJF-UHFFFAOYSA-N 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 238000001953 recrystallisation Methods 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 150000003460 sulfonic acids Chemical class 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 229930192474 thiophene Natural products 0.000 description 1
- 238000005292 vacuum distillation Methods 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、フェノール性水酸基を有する芳香族化合物を
有機酸によりエステル化する方法に関する。DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a method for esterifying an aromatic compound having a phenolic hydroxyl group with an organic acid.
芳香族化合物のフェノール性水酸基のエステル化物は、
医薬、農薬、ポリマー原料の中間体として工業的に重要
な用途を持っている。Esterified products of phenolic hydroxyl groups of aromatic compounds are
It has important industrial uses as an intermediate for medicines, agricultural chemicals, and polymer raw materials.
(従来の技術)
有機酸によるアルコールのエステル化は容易に進行する
が、フェノール性水酸基のエステル化は反応が困難であ
り、有機酸の代わりに酸無水物または酸塩化物などを用
いて反応させる方法や、種々の触媒を用い有機酸と反応
させる方法が知られている。(Prior art) Esterification of alcohols with organic acids progresses easily, but esterification of phenolic hydroxyl groups is difficult, so the reaction is performed using acid anhydrides or acid chlorides instead of organic acids. Methods for reacting with organic acids using various catalysts are known.
例えば特公昭44−55号にはフェノール性水酸基を持
つ芳香族化合物のエステル化法として、酸またはアルカ
リの存在下、1−シアノビニルアセテートと反応させる
方法が記載されている。また特公昭55−10575号
にはカルボン酸をニトリル化合物の存在下で加熱する方
法、特開昭48−36131号にはカルボン酸と二)
IJル化合物からなる混合物を硫酸または芳香族スルホ
ン酸の存在下で加熱する方法、特開昭48−48433
号にはカルボン酸とニトリル化合物からなる混合物を銅
、亜鉛、鉄、コバルト、ニッケルからなる群より選ばれ
た化合物の存在下で加熱する方法が記載されている。更
に特開昭51−54525号には有機酸を活性白土の存
在下で反応させる方法が記載されている。For example, Japanese Patent Publication No. 44-55 describes a method for esterifying an aromatic compound having a phenolic hydroxyl group by reacting it with 1-cyanovinyl acetate in the presence of an acid or an alkali. Furthermore, Japanese Patent Publication No. 55-10575 describes a method of heating carboxylic acid in the presence of a nitrile compound;
Method of heating a mixture consisting of IJ compound in the presence of sulfuric acid or aromatic sulfonic acid, JP-A-48-48433
No. 1, No. 1, pp. 10-12, 1999 describes a method in which a mixture of a carboxylic acid and a nitrile compound is heated in the presence of a compound selected from the group consisting of copper, zinc, iron, cobalt, and nickel. Further, JP-A-51-54525 describes a method in which an organic acid is reacted in the presence of activated clay.
(発明が解決しようとする問題点)
有機酸から酸無水物または酸塩化物を製造するには、周
知の如く過酷な条件で反応を行うか、または腐食性の著
しく大きな塩素化剤を使用する必要がある。(Problems to be Solved by the Invention) In order to produce acid anhydrides or acid chlorides from organic acids, as is well known, the reaction must be carried out under harsh conditions or a highly corrosive chlorinating agent must be used. There is a need.
1−シアノビニルアセテートをエステル化剤とする方法
は、収率が良好であるが、1−シアノビニルアセテート
の合成原料が高価であると共に、青酸を使用することに
よる危険性が伴うなどの問題がある。The method using 1-cyanovinyl acetate as an esterification agent has a good yield, but there are problems such as the expensive raw materials for 1-cyanovinyl acetate synthesis and the danger of using hydrocyanic acid. be.
ニトリル化合物を使用する特公昭55−10575号、
特開昭48−36131号および特開昭48−4843
3号でのエステル類の収率は26〜64%と満足すべき
ものではなく、またニトリル化合物からのアミド化合物
の生成があるので精製操作が複雑である。活性白土の存
在下で反応させる特開昭51−54525号の方法もエ
ステル類の収率が低く、反応時間が長い。Japanese Patent Publication No. 55-10575 using a nitrile compound,
JP-A-48-36131 and JP-A-48-4843
The yield of esters in No. 3 was 26 to 64%, which is unsatisfactory, and the purification operation is complicated because an amide compound is produced from a nitrile compound. The method of JP-A-51-54525 in which the reaction is carried out in the presence of activated clay also has a low yield of esters and requires a long reaction time.
このように従来法は、高価なエステル化剤を使用するこ
とや第三物質を添加する場合はその分離操作等の複雑な
工程が加わり収率が低いことなどが問題点として挙げら
れる。As described above, problems with the conventional method include the use of an expensive esterifying agent and the addition of a third substance, which requires complicated steps such as separation operations, resulting in a low yield.
(問題点を解決するための手段)
発明者等は、以上の如き問題点を有する芳香族化合物の
フェノール性水酸基をエステル化する方法に関し鋭意検
討した結果、エステル化剤として有機酸を用い、酵触媒
の存在下、生成水を反応蒸留により除去しつつ反応させ
れば、短時間で驚くべき高収率が達成されることを見出
し本発明に至った。(Means for Solving the Problems) As a result of extensive research into methods for esterifying the phenolic hydroxyl groups of aromatic compounds that have the above-mentioned problems, the inventors have developed a method for esterifying the phenolic hydroxyl groups of aromatic compounds using an organic acid as an esterifying agent. The present inventors have discovered that surprisingly high yields can be achieved in a short period of time by allowing the reaction to occur in the presence of a catalyst while removing produced water by reactive distillation, leading to the present invention.
即ち本発明は、フェノール性水酸基を有する芳香族化合
物を有機酸によりエステル化するに際し、酸触媒の存在
下、反応蒸留により生成水を除去しつつ反応を行うこと
を特徴とする芳香族化合物のエステル化方法である。That is, the present invention provides an ester of an aromatic compound, which is characterized in that when an aromatic compound having a phenolic hydroxyl group is esterified with an organic acid, the reaction is carried out while removing produced water by reactive distillation in the presence of an acid catalyst. It is a method of conversion.
本発明のフェノール性水酸基を有する芳香族化合物とは
、水酸基により核置換された芳香族化合物である。この
芳香族化合物には、ベンゼン、ナフタリン、アントラセ
ンおよびフェナントレン、ビフェニルなどの芳香族炭化
水素およびその置換化合物ばかりでなく、一般に芳香族
基と称せられる性質を有するピリジン、チオフェン、ピ
ロールおよびフランなどを含めた広義の芳香族環化合物
およびその置換化合物を含む。この化合物の置換基は、
アルキル基、ハロゲン基、ニトロ基、アルコキシ基など
有機酸と反応しない置換基であり、これらの置換基の数
に制限がない。またフェノール性水酸基の数も特に制限
されない。The aromatic compound having a phenolic hydroxyl group of the present invention is an aromatic compound whose nucleus is substituted with a hydroxyl group. These aromatic compounds include not only aromatic hydrocarbons and their substituted compounds such as benzene, naphthalene, anthracene, phenanthrene, and biphenyl, but also pyridine, thiophene, pyrrole, and furan, which have properties that are generally referred to as aromatic groups. It includes aromatic ring compounds in a broad sense and their substituted compounds. The substituents of this compound are:
These are substituents that do not react with organic acids, such as alkyl groups, halogen groups, nitro groups, and alkoxy groups, and there is no limit to the number of these substituents. Further, the number of phenolic hydroxyl groups is not particularly limited either.
従って本発明において対象とされるフェノール性水酸基
を有する芳香族化合物としては、例えば、フェノール、
カテコール、ハイドロキノン、バラメトキシフェノール
、バラクレゾール、バラニトロフェノール、パラクロロ
フェノールなどのフェノール類、α−ナフトール、β−
ナフトールなどのナフトール類およびその置換誘導体、
バラフェニルフェノニルなどのフェニルフェノール類お
よびその置換誘導体、4−ヒドロキシピリジン、8−ヒ
ドロキシキノリンなどの含窒素異部核置換アルコールな
どが挙げられる。Therefore, the aromatic compounds having a phenolic hydroxyl group targeted in the present invention include, for example, phenol,
Phenols such as catechol, hydroquinone, varamethoxyphenol, valacresol, varanitrophenol, parachlorophenol, α-naphthol, β-
naphthols such as naphthol and substituted derivatives thereof;
Examples include phenylphenols such as phenylphenol and substituted derivatives thereof, and nitrogen-containing heteronuclear substituted alcohols such as 4-hydroxypyridine and 8-hydroxyquinoline.
本発明において用いられる有機酸は、炭素数2〜18個
の脂肪族、脂環族、芳香族のカルボン酸であり、例えば
、酢酸、プロピオン酸、酪酸、カプロン酸、アクリル酸
、メタクリル酸、アジピン酸、マレイン酸、フマル酸、
シクロヘキサンカルボン酸、安息香酸、トリル酸、ナフ
タリンジカルボン酸などが挙げられる。The organic acids used in the present invention are aliphatic, alicyclic, and aromatic carboxylic acids having 2 to 18 carbon atoms, such as acetic acid, propionic acid, butyric acid, caproic acid, acrylic acid, methacrylic acid, and adipine. acids, maleic acid, fumaric acid,
Examples include cyclohexanecarboxylic acid, benzoic acid, tolylic acid, and naphthalenedicarboxylic acid.
これらの有機酸の使用量は、フェノール性水酸基を持つ
芳香族化合物1モル当り10〜100モル、好ましくは
20〜50モルである。The amount of these organic acids used is 10 to 100 mol, preferably 20 to 50 mol, per mol of the aromatic compound having a phenolic hydroxyl group.
本発明の方法では、酸触媒が無いと反応が全く進行しな
い。酸触媒としては、硫酸、塩酸などの鉱酸、p−トル
エンスルホン酸、メタンスルホン酸などの有機スルホン
酸、および強酸性イオン交換樹脂、例えばアンバーライ
ト200Cやアンバーライ)IR−120B (いず
れも商品名、オルガノ側製)が挙げられる。特に硫酸が
有効である。In the method of the present invention, the reaction does not proceed at all in the absence of an acid catalyst. Examples of acid catalysts include mineral acids such as sulfuric acid and hydrochloric acid, organic sulfonic acids such as p-toluenesulfonic acid and methanesulfonic acid, and strong acidic ion exchange resins such as Amberlyte 200C and Amberlye IR-120B (both products). (namely, made by organo side). Sulfuric acid is particularly effective.
酸触媒の使用量は、フェノール性水酸基を持つ芳香族化
合物に対する重量比で、1〜30%、好ましくは5〜1
5%である。The amount of acid catalyst used is 1 to 30%, preferably 5 to 1% by weight relative to the aromatic compound having a phenolic hydroxyl group.
It is 5%.
反応温度は、フェノール性水酸基を持つ芳香族化合物の
種類によるが、一般には120〜300℃である。温度
が低過ぎれば反応速度が遅く、高過ぎれば副反応が併発
し易い。また装置の耐食性からも反応温度が制限される
。The reaction temperature depends on the type of aromatic compound having a phenolic hydroxyl group, but is generally 120 to 300°C. If the temperature is too low, the reaction rate is slow, and if the temperature is too high, side reactions are likely to occur. The reaction temperature is also limited by the corrosion resistance of the equipment.
反応時間は反応温度によって変化するが、上記温度範囲
では、通常1〜10時間の反応時間が必要である。圧力
は特に制限がなく、一般に常圧ないし加圧下で行う。The reaction time varies depending on the reaction temperature, but in the above temperature range, a reaction time of 1 to 10 hours is usually required. There is no particular restriction on the pressure, and the reaction is generally carried out under normal pressure or increased pressure.
生成水の除去方法は、10段ないしそれ以上の段数を有
する蒸留塔を使用した反応蒸留法が好ましい。生成水を
純粋に分離する方法もあるが、有機酸との混合物として
分離する方法や、溶媒としてベンゼン、トルエンなどの
水と共沸混合物を形成する第三物質を添加して共沸混合
物として蒸留塔で分離することもできる。The method for removing the produced water is preferably a reactive distillation method using a distillation column having 10 or more stages. There is a method of separating the produced water pure, but there is also a method of separating it as a mixture with an organic acid, or a method of distilling the azeotrope by adding a third substance that forms an azeotrope with water, such as benzene or toluene, as a solvent. It can also be separated in a column.
フェノール性水酸基を有する芳香族化合物のエステルは
、空気中の酸素によって酸化され、黄褐色に着色するこ
とがあるので、窒素などの不活性ガス雰囲気下で反応を
行うことが好ましい。Since the ester of an aromatic compound having a phenolic hydroxyl group may be oxidized by oxygen in the air and turn yellowish brown, it is preferable to carry out the reaction under an inert gas atmosphere such as nitrogen.
反応終了後の混合物からのエステルの分離・精製は、蒸
留、抽出あるいは再結晶などの一般的な方法により行わ
れる。After the reaction is completed, separation and purification of the ester from the mixture is carried out by common methods such as distillation, extraction, or recrystallization.
(効果)
有機酸とフェノール性水酸基を有する芳香族化合物のエ
ステル反応はその平衡が著しく出発系に偏っているため
に、一般のエステル化法では効率良く反応させることが
不可能とされていた。(Effects) In the ester reaction between an organic acid and an aromatic compound having a phenolic hydroxyl group, the equilibrium is extremely biased towards the starting system, so it has been considered impossible to carry out the reaction efficiently using general esterification methods.
本発明は、酸無水物、酸塩化物や1−シアノビニルアセ
テートなど従来法で使用される高価なエステル化剤を使
用せず、またニトリル化合物の如き第三物質の添加によ
る複雑な分離操作も不要である。The present invention does not use expensive esterifying agents such as acid anhydrides, acid chlorides, or 1-cyanovinyl acetate, and does not require complicated separation operations due to the addition of third substances such as nitrile compounds. Not necessary.
本発明は、以上の如き従来困難とされていた有機酸と多
くの種類のフェノール性水酸基を有する芳香族化合物の
エステル反応が、単純な操作により容易に高収率で得ら
れる方法を見出したものであり、その工業的意義が大き
い。The present invention has discovered a method that allows the ester reaction of an organic acid and an aromatic compound having many types of phenolic hydroxyl groups, which has been considered difficult in the past, to be easily obtained in high yield through simple operations. , and its industrial significance is great.
(実施例)
次に実施例により本発明を更に具体的に説明する。勿論
本発明はこれらの実施例により制限されるものでは無い
。(Example) Next, the present invention will be explained in more detail with reference to Examples. Of course, the present invention is not limited to these examples.
実施例1
撹拌機、温度計および15rnrnφX150mmのビ
グリュー型分留塔を有する内容積11のフラスコにフェ
ノール20g (0,213モル)、酢酸500g (
8,333モル)、硫酸1gを仕込み、昇温した。内部
温度が120℃となった時点で酢酸・水混合物がビグリ
ュー型分留塔頂部より留出し始めた。留出する酢酸・水
混合物が30g/hrになるような速度に調節し、6時
間反応を継続した。反応混合物を減圧蒸留して酢酸を回
収した後、13mm11gにおける沸点が83℃の留分
として無色透明のフェニルアセテートが28.2g得ら
れ、収率は97%であった。Example 1 20 g (0,213 mol) of phenol and 500 g (0,213 mol) of phenol and 500 g (
8,333 mol) and 1 g of sulfuric acid were charged, and the temperature was raised. When the internal temperature reached 120°C, an acetic acid/water mixture began to be distilled out from the top of the Vigreux type fractionation column. The reaction rate was adjusted so that the amount of the acetic acid/water mixture distilled out was 30 g/hr, and the reaction was continued for 6 hours. After recovering acetic acid by distilling the reaction mixture under reduced pressure, 28.2 g of clear colorless phenylacetate was obtained as a fraction with a boiling point of 83° C. in 11 g of 13 mm, and the yield was 97%.
実施例2
p−クレゾール24g (0,2モル)、酢酸600g
(10モル)、硫酸1,2gを内容積的11の内側を
テフロンコーティングした5O3−316製の塔を備え
た反応蒸留器でエステル化を行った。反応条件は、圧力
1、7kg/cm2G、温度154℃とし、蒸留塔頂部
より水含有酢酸を60〜70g/hrで抜き出し2時間
反応を行った。この反応液から未反応酢酸を回収した後
、減圧蒸留によりp−クレジルアセテートが31.1g
(0゜192モル)得られ、収率は96%であった。Example 2 24 g (0.2 mol) of p-cresol, 600 g of acetic acid
(10 moles) and 1.2 g of sulfuric acid were esterified in a reactive distillation vessel equipped with a column made of 5O3-316 whose inner volume was coated with Teflon. The reaction conditions were a pressure of 1.7 kg/cm 2 G and a temperature of 154° C., and water-containing acetic acid was extracted from the top of the distillation column at a rate of 60 to 70 g/hr, and the reaction was carried out for 2 hours. After recovering unreacted acetic acid from this reaction solution, 31.1 g of p-cresyl acetate was obtained by distillation under reduced pressure.
(0.192 mol) was obtained, and the yield was 96%.
実施例3
フェノール性水酸基を持つ芳香族化合物としてβ−ナフ
トール33.6g (0,2モル)を用い、実施例2と
同じ条件で4時間反応させた。反応液から未反応酢酸を
回収した後、減圧蒸留によりβ−ナフチルアセテート3
8゜9g (0,185モル)が得られ、収率は92.
6%であった。Example 3 Using 33.6 g (0.2 mol) of β-naphthol as an aromatic compound having a phenolic hydroxyl group, a reaction was carried out under the same conditions as in Example 2 for 4 hours. After recovering unreacted acetic acid from the reaction solution, β-naphthyl acetate 3 was obtained by distillation under reduced pressure.
8.9 g (0.185 mol) was obtained, yield 92.
It was 6%.
実施例4
有機酸としてプロピオン酸600g(8,11モル)を
用い、反応温度を173℃とした以外は実施例2と同じ
条件で2時間反応させた。反応液から未反応プロピオン
酸を回収した後、減圧蒸留によりP−タレジルプロピオ
ネート33.1gが得られ、収率は94%であった。Example 4 A reaction was carried out for 2 hours under the same conditions as in Example 2 except that 600 g (8.11 moles) of propionic acid was used as the organic acid and the reaction temperature was 173°C. After recovering unreacted propionic acid from the reaction solution, 33.1 g of P-talesylpropionate was obtained by vacuum distillation, with a yield of 94%.
実施例5
実施例2と同じ装置を用いて、フェノール18゜8g
(0,2モル)、安息香酸500g (4,1モル)、
ベンゼン200g、 p−)ルエンスルホン酸2.8g
を仕込み、圧力3kg/cm2G、反応温度140℃に
おいて、蒸留塔頂部からベンゼン・水共沸物を50〜6
0g/hrの速度で抜き出しながら3時間反応させた。Example 5 Using the same equipment as in Example 2, 18°8 g of phenol
(0.2 mol), 500 g of benzoic acid (4.1 mol),
200 g of benzene, 2.8 g of p-)luenesulfonic acid
At a pressure of 3 kg/cm2G and a reaction temperature of 140°C, a benzene/water azeotrope of 50 to 6
The reaction was carried out for 3 hours while withdrawing at a rate of 0 g/hr.
反応液よりベンゼンを回収した後、減圧蒸留により安息
香酸フェニル35.3g (0,178モル)が得られ
た。収率は89%であった。After recovering benzene from the reaction solution, 35.3 g (0,178 mol) of phenyl benzoate was obtained by distillation under reduced pressure. The yield was 89%.
比較例1
ビグリュー型分留塔の無いフラスコを用い、酢酸−水混
合液の抜き出しを行わない以外は、実施例1と全く同じ
条件で反応を行った。その結果、収率は17%であった
。Comparative Example 1 A reaction was carried out under exactly the same conditions as in Example 1, except that a flask without a Vigreux type fractionator was used and the acetic acid-water mixture was not extracted. As a result, the yield was 17%.
比較例2
実施例2において硫酸を添加しない以外は、実施例2と
全く同じ条件で反応を行った。その結果、p−クレジル
アセテートの生成は無かった。Comparative Example 2 A reaction was carried out under exactly the same conditions as in Example 2, except that sulfuric acid was not added. As a result, no p-cresyl acetate was produced.
Claims (1)
りエステル化するに際し、酸触媒の存在下、反応蒸留に
より生成水を除去しつつ反応を行うことを特徴とする芳
香族化合物のエステル化方法A method for esterifying an aromatic compound, which is characterized in that when an aromatic compound having a phenolic hydroxyl group is esterified with an organic acid, the reaction is carried out while removing produced water by reactive distillation in the presence of an acid catalyst.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62112614A JPS63277645A (en) | 1987-05-11 | 1987-05-11 | Esterification of aromatic compound |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62112614A JPS63277645A (en) | 1987-05-11 | 1987-05-11 | Esterification of aromatic compound |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS63277645A true JPS63277645A (en) | 1988-11-15 |
Family
ID=14591143
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62112614A Pending JPS63277645A (en) | 1987-05-11 | 1987-05-11 | Esterification of aromatic compound |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS63277645A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5808130A (en) * | 1996-06-27 | 1998-09-15 | Henkel Corporation | Esterification of phenols |
JP2007106749A (en) * | 2005-09-13 | 2007-04-26 | Osaka Organic Chem Ind Ltd | Method for producing hydroquinone mono(meth)acrylate |
WO2011043204A1 (en) * | 2009-10-06 | 2011-04-14 | 住友化学株式会社 | Method for producing diepoxy compound |
JP2012531452A (en) * | 2009-06-30 | 2012-12-10 | クラリアント・ファイナンス・(ビーブイアイ)・リミテッド | Process for the continuous production of esters of aliphatic carboxylic acids |
-
1987
- 1987-05-11 JP JP62112614A patent/JPS63277645A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5808130A (en) * | 1996-06-27 | 1998-09-15 | Henkel Corporation | Esterification of phenols |
JP2007106749A (en) * | 2005-09-13 | 2007-04-26 | Osaka Organic Chem Ind Ltd | Method for producing hydroquinone mono(meth)acrylate |
JP2012531452A (en) * | 2009-06-30 | 2012-12-10 | クラリアント・ファイナンス・(ビーブイアイ)・リミテッド | Process for the continuous production of esters of aliphatic carboxylic acids |
WO2011043204A1 (en) * | 2009-10-06 | 2011-04-14 | 住友化学株式会社 | Method for producing diepoxy compound |
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