JPS6348244A - Production of substituted phenylpyruvic acid - Google Patents
Production of substituted phenylpyruvic acidInfo
- Publication number
- JPS6348244A JPS6348244A JP61189831A JP18983186A JPS6348244A JP S6348244 A JPS6348244 A JP S6348244A JP 61189831 A JP61189831 A JP 61189831A JP 18983186 A JP18983186 A JP 18983186A JP S6348244 A JPS6348244 A JP S6348244A
- Authority
- JP
- Japan
- Prior art keywords
- acid
- water
- substituted
- solvent
- chloride
- 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
- 238000004519 manufacturing process Methods 0.000 title claims description 11
- BTNMPGBKDVTSJY-UHFFFAOYSA-N keto-phenylpyruvic acid Chemical class OC(=O)C(=O)CC1=CC=CC=C1 BTNMPGBKDVTSJY-UHFFFAOYSA-N 0.000 title abstract 4
- 239000001903 2-oxo-3-phenylpropanoic acid Substances 0.000 title abstract 2
- DEDGUGJNLNLJSR-UHFFFAOYSA-N alpha-hydroxycinnamic acid Natural products OC(=O)C(O)=CC1=CC=CC=C1 DEDGUGJNLNLJSR-UHFFFAOYSA-N 0.000 title abstract 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 26
- 229910017052 cobalt Inorganic materials 0.000 claims abstract description 20
- 239000010941 cobalt Substances 0.000 claims abstract description 20
- -1 cobalt carbonyl compound Chemical class 0.000 claims abstract description 20
- 239000003054 catalyst Substances 0.000 claims abstract description 18
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims abstract description 17
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 16
- 229910002091 carbon monoxide Inorganic materials 0.000 claims abstract description 16
- 239000002904 solvent Substances 0.000 claims abstract description 15
- UIHCLUNTQKBZGK-UHFFFAOYSA-N Methyl isobutyl ketone Natural products CCC(C)C(C)=O UIHCLUNTQKBZGK-UHFFFAOYSA-N 0.000 claims abstract description 12
- NTIZESTWPVYFNL-UHFFFAOYSA-N Methyl isobutyl ketone Chemical compound CC(C)CC(C)=O NTIZESTWPVYFNL-UHFFFAOYSA-N 0.000 claims abstract description 11
- 229940073608 benzyl chloride Drugs 0.000 claims abstract description 11
- MQIKJSYMMJWAMP-UHFFFAOYSA-N dicobalt octacarbonyl Chemical group [Co+2].[Co+2].[O+]#[C-].[O+]#[C-].[O+]#[C-].[O+]#[C-].[O+]#[C-].[O+]#[C-].[O+]#[C-].[O+]#[C-] MQIKJSYMMJWAMP-UHFFFAOYSA-N 0.000 claims abstract description 11
- 150000005524 benzylchlorides Chemical class 0.000 claims abstract description 10
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims abstract description 10
- 239000000920 calcium hydroxide Substances 0.000 claims abstract description 10
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims abstract description 10
- 150000001342 alkaline earth metals Chemical class 0.000 claims abstract description 9
- KWOLFJPFCHCOCG-UHFFFAOYSA-N Acetophenone Chemical compound CC(=O)C1=CC=CC=C1 KWOLFJPFCHCOCG-UHFFFAOYSA-N 0.000 claims abstract description 7
- 150000002576 ketones Chemical class 0.000 claims abstract description 4
- KRIOVPPHQSLHCZ-UHFFFAOYSA-N phenyl propionaldehyde Natural products CCC(=O)C1=CC=CC=C1 KRIOVPPHQSLHCZ-UHFFFAOYSA-N 0.000 claims abstract description 3
- 239000002253 acid Substances 0.000 claims description 31
- 238000006243 chemical reaction Methods 0.000 claims description 28
- 238000000034 method Methods 0.000 abstract description 4
- 239000003814 drug Substances 0.000 abstract description 2
- 230000000694 effects Effects 0.000 abstract description 2
- IZXWCDITFDNEBY-UHFFFAOYSA-N 1-(chloromethyl)-4-fluorobenzene Chemical compound FC1=CC=C(CCl)C=C1 IZXWCDITFDNEBY-UHFFFAOYSA-N 0.000 abstract 1
- UTTDJAPJOSBBIO-UHFFFAOYSA-N 3-(4-fluorophenyl)-2-oxopropanoic acid Chemical compound OC(=O)C(=O)CC1=CC=C(F)C=C1 UTTDJAPJOSBBIO-UHFFFAOYSA-N 0.000 abstract 1
- 150000001875 compounds Chemical class 0.000 abstract 1
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 33
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 15
- WLJVXDMOQOGPHL-UHFFFAOYSA-N benzyl-alpha-carboxylic acid Natural products OC(=O)CC1=CC=CC=C1 WLJVXDMOQOGPHL-UHFFFAOYSA-N 0.000 description 11
- 239000010410 layer Substances 0.000 description 10
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 7
- 239000007787 solid Substances 0.000 description 6
- 239000000243 solution Substances 0.000 description 6
- 239000002585 base Substances 0.000 description 5
- 239000006227 byproduct Substances 0.000 description 5
- WLJVXDMOQOGPHL-PPJXEINESA-N 2-phenylacetic acid Chemical class O[14C](=O)CC1=CC=CC=C1 WLJVXDMOQOGPHL-PPJXEINESA-N 0.000 description 4
- 239000007864 aqueous solution Substances 0.000 description 4
- 239000000706 filtrate Substances 0.000 description 4
- 229910052500 inorganic mineral Inorganic materials 0.000 description 4
- 239000011707 mineral Substances 0.000 description 4
- 229960003424 phenylacetic acid Drugs 0.000 description 4
- 239000003279 phenylacetic acid Substances 0.000 description 4
- 239000003021 water soluble solvent Substances 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 230000002378 acidificating effect Effects 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- 239000003960 organic solvent Substances 0.000 description 3
- CYAKWEQUWJAHLW-UHFFFAOYSA-N 1-(chloromethyl)-4-propan-2-ylbenzene Chemical compound CC(C)C1=CC=C(CCl)C=C1 CYAKWEQUWJAHLW-UHFFFAOYSA-N 0.000 description 2
- HXVNBWAKAOHACI-UHFFFAOYSA-N 2,4-dimethyl-3-pentanone Chemical compound CC(C)C(=O)C(C)C HXVNBWAKAOHACI-UHFFFAOYSA-N 0.000 description 2
- SYBYTAAJFKOIEJ-UHFFFAOYSA-N 3-Methylbutan-2-one Chemical compound CC(C)C(C)=O SYBYTAAJFKOIEJ-UHFFFAOYSA-N 0.000 description 2
- 229910021503 Cobalt(II) hydroxide Inorganic materials 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 description 2
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 125000001931 aliphatic group Chemical group 0.000 description 2
- 229910052783 alkali metal Inorganic materials 0.000 description 2
- 229910001860 alkaline earth metal hydroxide Inorganic materials 0.000 description 2
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 2
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 2
- ASKVAEGIVYSGNY-UHFFFAOYSA-L cobalt(ii) hydroxide Chemical compound [OH-].[OH-].[Co+2] ASKVAEGIVYSGNY-UHFFFAOYSA-L 0.000 description 2
- BGTOWKSIORTVQH-UHFFFAOYSA-N cyclopentanone Chemical compound O=C1CCCC1 BGTOWKSIORTVQH-UHFFFAOYSA-N 0.000 description 2
- USIUVYZYUHIAEV-UHFFFAOYSA-N diphenyl ether Chemical compound C=1C=CC=CC=1OC1=CC=CC=C1 USIUVYZYUHIAEV-UHFFFAOYSA-N 0.000 description 2
- 239000012044 organic layer Substances 0.000 description 2
- 229910052938 sodium sulfate Inorganic materials 0.000 description 2
- 235000011152 sodium sulphate Nutrition 0.000 description 2
- ABJGYUSFOIMJPT-UHFFFAOYSA-N 1-(chloromethyl)-2-propan-2-ylbenzene Chemical compound CC(C)C1=CC=CC=C1CCl ABJGYUSFOIMJPT-UHFFFAOYSA-N 0.000 description 1
- LZBOHNCMCCSTJX-UHFFFAOYSA-N 1-(chloromethyl)-3-methylbenzene Chemical compound CC1=CC=CC(CCl)=C1 LZBOHNCMCCSTJX-UHFFFAOYSA-N 0.000 description 1
- OCFXNUNCMJFLML-UHFFFAOYSA-N 1-(chloromethyl)-3-propan-2-ylbenzene Chemical compound CC(C)C1=CC=CC(CCl)=C1 OCFXNUNCMJFLML-UHFFFAOYSA-N 0.000 description 1
- MOHYOXXOKFQHDC-UHFFFAOYSA-N 1-(chloromethyl)-4-methoxybenzene Chemical compound COC1=CC=C(CCl)C=C1 MOHYOXXOKFQHDC-UHFFFAOYSA-N 0.000 description 1
- DMHZDOTYAVHSEH-UHFFFAOYSA-N 1-(chloromethyl)-4-methylbenzene Chemical compound CC1=CC=C(CCl)C=C1 DMHZDOTYAVHSEH-UHFFFAOYSA-N 0.000 description 1
- HLQZCRVEEQKNMS-UHFFFAOYSA-N 1-(chloromethyl)-4-phenylbenzene Chemical compound C1=CC(CCl)=CC=C1C1=CC=CC=C1 HLQZCRVEEQKNMS-UHFFFAOYSA-N 0.000 description 1
- ZFZDHCZLDOAJCA-UHFFFAOYSA-N 1-butyl-4-(chloromethyl)benzene Chemical compound CCCCC1=CC=C(CCl)C=C1 ZFZDHCZLDOAJCA-UHFFFAOYSA-N 0.000 description 1
- MWBXCWLRASBZFB-UHFFFAOYSA-N 2-(2,4-dimethylphenyl)acetic acid Chemical compound CC1=CC=C(CC(O)=O)C(C)=C1 MWBXCWLRASBZFB-UHFFFAOYSA-N 0.000 description 1
- OTTPBKINJOYJGW-UHFFFAOYSA-N 2-(3,4-dimethylphenyl)acetic acid Chemical compound CC1=CC=C(CC(O)=O)C=C1C OTTPBKINJOYJGW-UHFFFAOYSA-N 0.000 description 1
- RERBQXVRXYCGLT-UHFFFAOYSA-N 2-(4-propan-2-ylphenyl)acetic acid Chemical compound CC(C)C1=CC=C(CC(O)=O)C=C1 RERBQXVRXYCGLT-UHFFFAOYSA-N 0.000 description 1
- PTTPXKJBFFKCEK-UHFFFAOYSA-N 2-Methyl-4-heptanone Chemical compound CC(C)CC(=O)CC(C)C PTTPXKJBFFKCEK-UHFFFAOYSA-N 0.000 description 1
- NGNBDVOYPDDBFK-UHFFFAOYSA-N 2-[2,4-di(pentan-2-yl)phenoxy]acetyl chloride Chemical compound CCCC(C)C1=CC=C(OCC(Cl)=O)C(C(C)CCC)=C1 NGNBDVOYPDDBFK-UHFFFAOYSA-N 0.000 description 1
- UBQRAAXAHIKWRI-UHFFFAOYSA-N 4-(chloromethyl)-1,2-dimethylbenzene Chemical compound CC1=CC=C(CCl)C=C1C UBQRAAXAHIKWRI-UHFFFAOYSA-N 0.000 description 1
- OEBIVOHKFYSBPE-UHFFFAOYSA-N 4-Benzyloxybenzyl alcohol Chemical compound C1=CC(CO)=CC=C1OCC1=CC=CC=C1 OEBIVOHKFYSBPE-UHFFFAOYSA-N 0.000 description 1
- CDPKJZJVTHSESZ-UHFFFAOYSA-N 4-chlorophenylacetic acid Chemical compound OC(=O)CC1=CC=C(Cl)C=C1 CDPKJZJVTHSESZ-UHFFFAOYSA-N 0.000 description 1
- JRLTTZUODKEYDH-UHFFFAOYSA-N 8-methylquinoline Chemical group C1=CN=C2C(C)=CC=CC2=C1 JRLTTZUODKEYDH-UHFFFAOYSA-N 0.000 description 1
- ZAFNJMIOTHYJRJ-UHFFFAOYSA-N Diisopropyl ether Chemical compound CC(C)OC(C)C ZAFNJMIOTHYJRJ-UHFFFAOYSA-N 0.000 description 1
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 description 1
- 238000010306 acid treatment Methods 0.000 description 1
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 description 1
- 229910001854 alkali hydroxide Inorganic materials 0.000 description 1
- 150000008044 alkali metal hydroxides Chemical class 0.000 description 1
- 229910000287 alkaline earth metal oxide Inorganic materials 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 150000008365 aromatic ketones Chemical class 0.000 description 1
- 150000008378 aryl ethers Chemical class 0.000 description 1
- KCXMKQUNVWSEMD-UHFFFAOYSA-N benzyl chloride Chemical compound ClCC1=CC=CC=C1 KCXMKQUNVWSEMD-UHFFFAOYSA-N 0.000 description 1
- 125000001797 benzyl group Chemical group [H]C1=C([H])C([H])=C(C([H])=C1[H])C([H])([H])* 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 150000001728 carbonyl compounds Chemical class 0.000 description 1
- 239000007810 chemical reaction solvent Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- GPGMRSSBVJNWRA-UHFFFAOYSA-N hydrochloride hydrofluoride Chemical compound F.Cl GPGMRSSBVJNWRA-UHFFFAOYSA-N 0.000 description 1
- 230000033444 hydroxylation Effects 0.000 description 1
- 238000005805 hydroxylation reaction Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000012046 mixed solvent Substances 0.000 description 1
- WSGCRAOTEDLMFQ-UHFFFAOYSA-N nonan-5-one Chemical compound CCCCC(=O)CCCC WSGCRAOTEDLMFQ-UHFFFAOYSA-N 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- COLNVLDHVKWLRT-UHFFFAOYSA-N phenylalanine Natural products OC(=O)C(N)CC1=CC=CC=C1 COLNVLDHVKWLRT-UHFFFAOYSA-N 0.000 description 1
- 150000002993 phenylalanine derivatives Chemical class 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance 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
- 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】
(イ)産業上の利用分野
本発明は、コバルトカルボニル化合物触媒の存在下、置
換ベンジルクロライドと一酸化炭素及びアルカリ土類金
属塩基とを反応させる際に、溶媒として水と水に難溶性
の溶媒を存在させ反応させることを特徴とする置換フェ
ニルビルピン酸の製造法に関するものである。Detailed Description of the Invention (a) Industrial Application Field The present invention provides a method for reacting substituted benzyl chloride with carbon monoxide and an alkaline earth metal base in the presence of a cobalt carbonyl compound catalyst using water as a solvent. The present invention relates to a method for producing substituted phenylbilpic acid, which is characterized in that the reaction is carried out in the presence of a poorly soluble solvent in water.
置換フェニルビルピン酸は、例えば置換フェニルアラニ
ンとして医薬品等として利用される物質である。Substituted phenylbilpic acid is a substance used, for example, as a substituted phenylalanine as a medicine.
(ロ)従来の技術
置換ベンジルクロライドと一酸化炭素との反応による置
換フェニルビルピン酸4の製造法は公知であり、例えば
特公昭56−.18587号公報等が挙げられる。(b) Prior art The method for producing substituted phenylbilpic acid 4 by reacting substituted benzyl chloride with carbon monoxide is known, for example, as described in Japanese Patent Publication No. 56-1983. 18587 and the like.
特公昭56−18587号公報では、触媒として金属カ
ルボニル化合物、特にコバルトカルボニル化合物を使用
して、アルカリ土類金属塩基の存在下、置換ベンジルク
ロライドと一酸化炭素とを水/アルコール混合溶媒中で
反応させ置換フェニルビルピン酸を製造する方法が提案
されている。In Japanese Patent Publication No. 56-18587, a substituted benzyl chloride and carbon monoxide are reacted in a water/alcohol mixed solvent in the presence of an alkaline earth metal base using a metal carbonyl compound, particularly a cobalt carbonyl compound, as a catalyst. A method for producing substituted phenylbilpic acid has been proposed.
(ハ)発明が解決しようとする問題点
しかし、上述の特公昭56−18587号公報をはじめ
とする既存の置換フェニルビルピン酸の製造法では、置
換フェニルビルピン酸は反応中に固体として析出する置
換フェニルビルピン酸のアルカリ金属塩又はアルカリ土
類金属塩を濾過後酸処理することにより簡単に得ること
ができるが、副生置換フェニノに酢酸のアルカリ金属塩
又はアルカリ土類金属塩とコバルトカルボニル触媒が反
応濾液中に、溶解しており、これら副生置換フェニル酢
酸アルカリ金属塩又はアルカリ土類金属塩とコバルトカ
ルボニル触媒の相互分離並びにコバルトカルボニル触媒
の再生には煩雑な工程を必要とする。(c) Problems to be solved by the invention However, in existing methods for producing substituted phenylbilpic acid, including the above-mentioned Japanese Patent Publication No. 56-18587, substituted phenylbilpic acid precipitates as a solid during the reaction. The alkali metal salt or alkaline earth metal salt of substituted phenylbirupic acid can be easily obtained by acid treatment after filtration. The carbonyl catalyst is dissolved in the reaction filtrate, and complicated steps are required to separate the by-product substituted phenylacetic acid alkali metal salt or alkaline earth metal salt from the cobalt carbonyl catalyst and to regenerate the cobalt carbonyl catalyst. .
又、コバルトカルボニル触媒の再生は、反応濾液より水
/アルコール溶媒等を除去し、鉱酸で処理して副生置換
フェニル酢酸を回収後、生成したコバルトの鉱酸塩を、
例えば水酸化アルカリ等で処理して水酸化コバルトとし
た後、更に水酸化コバルトを高温、高圧の水性ガスと反
応させてコバルトカルボニル化合物とするモ(7)であ
る。In addition, to regenerate the cobalt carbonyl catalyst, water/alcohol solvent etc. are removed from the reaction filtrate, treated with mineral acid to recover the by-product substituted phenylacetic acid, and then the produced cobalt mineral acid salt is
For example, after processing with an alkali hydroxide or the like to form cobalt hydroxide, the cobalt hydroxide is further reacted with high-temperature, high-pressure water gas to form a cobalt carbonyl compound (7).
又、特公昭56−18587号公報の方法は、5〜20
0バールの圧力下で反応が行われ、置換フェニルビルピ
ン酸を実用的な収率で得るためには40バ一ル以上の圧
力が必要で常圧下では好ましい収率で置換フェニルビル
ピン酸を得ることができない。In addition, the method disclosed in Japanese Patent Publication No. 56-18587 uses 5 to 20
The reaction is carried out under a pressure of 0 bar; a pressure of 40 bar or more is required to obtain substituted phenylbilpic acid in a practical yield; under normal pressure, substituted phenylbilpic acid can be produced in a preferred yield. can't get it.
本発明者らは、これらの欠点を改良すべく鋭意努力検討
した結果本発明を完成したものである。The present inventors have completed the present invention as a result of their earnest efforts and studies to improve these drawbacks.
(ニ)問題点を解決するための手段
本発明は、コバルトカルボニル化合物触媒の存在下、置
換ベンジルクコライドと一酸化炭素及びアルカリ土類金
属塩基とを反応させる際に、溶媒として水と水に難溶性
の溶媒を存在させ反応させることを特徴とする置換フェ
ニルビルピン酸の製造法に関するものである。(d) Means for Solving the Problems The present invention uses water as a solvent when reacting a substituted benzyl cocolide with carbon monoxide and an alkaline earth metal base in the presence of a cobalt carbonyl compound catalyst. The present invention relates to a method for producing substituted phenylbilpic acid characterized by carrying out the reaction in the presence of a poorly soluble solvent.
本発明の置換ベンジルクロライドとしては、〇−弗化ペ
ンジルクロライド、m−弗化ペンジルクロライド、p−
弗化ペンジルクロライド、0−メチルベンジルクロライ
ド、m−メチルベンジルクロライド、p−メチルベンジ
ルクロライド、o −イソプロピルベンジルクロライド
、m−イソプロピルベンジルクロライド、p−イソプロ
ピルベンシルクロライド、〇−塩化ペンジルクロライド
、m−塩化ペンジルクロライド、p−塩化ペンジルクロ
ライド、2.4−ジメチルベンジルクロライド、3.4
−ジメチルベンジルクロライド、3゜5−ジメチルベン
ジルクロライド、0−メトキシヘシルクロライド、m−
メトキシへジルクロライド、p−メトキシベンジルクロ
ライド、0−ペンジロキシベジルクロライド、m−ペン
ジロキシベジルクロライド、p−ベンジロキシベンジル
クロライド、m、p−メチレンジオキシジベンジルクロ
ライド、p−フェニルベンジルクロライド、p−1−ブ
チルベンジルクロライド等が挙げられる。The substituted benzyl chloride of the present invention includes 〇-fluoropenzyl chloride, m-fluoropenzyl chloride, p-fluoropenzyl chloride,
Fluorinated penzyl chloride, 0-methylbenzyl chloride, m-methylbenzyl chloride, p-methylbenzyl chloride, o-isopropylbenzyl chloride, m-isopropylbenzyl chloride, p-isopropylbenzyl chloride, 〇-penzyl chloride, m-penzyl chloride, p-penzyl chloride, 2.4-dimethylbenzyl chloride, 3.4
-dimethylbenzyl chloride, 3゜5-dimethylbenzyl chloride, 0-methoxyhexyl chloride, m-
Methoxyhedyl chloride, p-methoxybenzyl chloride, 0-penzyloxybenzyl chloride, m-penzyloxybenzyl chloride, p-benzyloxybenzyl chloride, m, p-methylenedioxydibenzyl chloride, p-phenylbenzyl chloride , p-1-butylbenzyl chloride and the like.
本発明における水に難溶性の溶媒としては、ベンゼン、
トルエン等の芳香族炭化水素類、ヘキサン、ヘプタン等
の脂肪族炭化水素類、ジエチルエーテル、ジイソプロピ
ルエーテル、ジフェニルエーテル等の脂肪族及び芳香族
エーテル類、メチルイソブチルケトン、アセトフェノン
、ジイソプロピルケトン、メチルイソプロピルケトン、
ジブチルケトン、ジイソブチルケトン、シクロペンタノ
ン等の脂肪族及び芳香族ケトン類が選ばれ、特にメチル
イソブチルケトン、アセトフェノン等のケトン類が好ま
しい。Examples of the slightly water-soluble solvent in the present invention include benzene,
Aromatic hydrocarbons such as toluene, aliphatic hydrocarbons such as hexane and heptane, aliphatic and aromatic ethers such as diethyl ether, diisopropyl ether, diphenyl ether, methyl isobutyl ketone, acetophenone, diisopropyl ketone, methyl isopropyl ketone,
Aliphatic and aromatic ketones such as dibutyl ketone, diisobutyl ketone, and cyclopentanone are selected, and ketones such as methyl isobutyl ketone and acetophenone are particularly preferred.
反応溶媒中の置換ベンジルクロライドの濃度は特に制限
はないが、水に難溶性の溶媒に対して一般に1〜50重
景%重量される。The concentration of the substituted benzyl chloride in the reaction solvent is not particularly limited, but it is generally 1 to 50% by weight based on the slightly water-soluble solvent.
水の量は、一般に水に難溶性の溶媒に対し10〜200
重景%使用重量る。The amount of water is generally 10 to 200% of the solvent that is poorly soluble in water.
Heavy view% use weight.
本発明で使用されるアルカリ土類金属塩基は、一般にア
ルカリ土類金属水酸化物、アルカリ土類金属酸化物及び
アルカリ土類金属炭酸塩から選ばれるが、特にアルカリ
土類金属水酸化物が使用され、なかでも水酸化カルシウ
ムが好ましい。The alkaline earth metal base used in the present invention is generally selected from alkaline earth metal hydroxides, alkaline earth metal oxides and alkaline earth metal carbonates, but in particular alkaline earth metal hydroxides are used. Among them, calcium hydroxide is preferred.
アルカリ土類金属塩基の使用量は、一般に置換ベンジル
クロライド1モル当たり少なくとも1モル使用するする
必要があり、置換ベンジルクロライド1モル当たり少な
(とも1.0〜2.5モルの使用が好ましい。The amount of the alkaline earth metal base used generally needs to be at least 1 mol per mol of substituted benzyl chloride, and is preferably small (1.0 to 2.5 mol per mol of substituted benzyl chloride).
触媒としては、コバルトカルボニル化合物、特にジコバ
ルトオクタカルボニルが好ましい。As the catalyst, cobalt carbonyl compounds, especially dicobalt octacarbonyl, are preferred.
触媒は、コバルトカルボニル化合物/塩化ベンジル(モ
ル比)として一般に1/1〜1/1000の範囲で使用
されるが、1/30〜j/200の範囲が特に好ましい
。The cobalt carbonyl compound/benzyl chloride (mole ratio) of the catalyst is generally used in a range of 1/1 to 1/1000, but a range of 1/30 to j/200 is particularly preferred.
一酸化炭素は、高純度である必要はなく水性ガス等も使
用できる。一酸化炭素圧力は、一般に常圧〜200に+
r/caの範囲が採用される。Carbon monoxide does not need to be of high purity, and water gas or the like can also be used. Carbon monoxide pressure generally ranges from normal pressure to 200+
A range of r/ca is adopted.
反応温度は、20〜150℃が好ましくは40〜100
°Cが良い。The reaction temperature is preferably 20 to 150°C, preferably 40 to 100°C.
°C is good.
一般に、反応は一酸化炭素の吸収が停止するまで行い、
反応溶液は目的物である置換フェニルビルピン酸、副生
物である置換フェニル酢酸及びコバルトカルボニル触媒
を回収する為に次のように処理される。Generally, the reaction is carried out until absorption of carbon monoxide stops;
The reaction solution is treated as follows in order to recover the target product, substituted phenylbilpic acid, by-products, substituted phenylacetic acid, and cobalt carbonyl catalyst.
即ち、反応溶液を濾過することにより、反応中に固体と
して析出した置換フェニルビルピン酸のアルカリ土類金
属塩よりなる固体部分、置換フェニル酢酸のアルカリ土
類金属塩を含有する水層部分及びコバルトカルボニル触
媒を含有する水に難溶性の溶媒層部分に分離することが
できる。That is, by filtering the reaction solution, a solid portion consisting of the alkaline earth metal salt of substituted phenylbilpic acid precipitated as a solid during the reaction, an aqueous layer portion containing the alkaline earth metal salt of substituted phenylacetic acid, and cobalt. It can be separated into a slightly water-soluble solvent layer containing a carbonyl catalyst.
続いて、濾過操作により分取された置換フェニルビルピ
ン酸のアルカリ土類金属塩は、鉱酸水溶液、例えば希塩
酸水溶液で酸性とし、得られた水溶液を適当な有機溶媒
、例えばジエチルエーテル等で抽出後、有機溶媒を除去
することにより置換フェニルビルピン酸を得ることがで
きる。 同様に、置換フェニル酢酸のアルカリ土類金属
塩を含有する水層部分は、鉱酸水溶液、例えば希塩酸水
溶液で酸性とし、得られた水溶液を適当な有機溶媒、例
えばジエチルエーテル等で抽出後、有機溶媒を除去する
ことにより副生置換フェニル酢酸を回収することができ
る。Subsequently, the alkaline earth metal salt of substituted phenylbilpic acid separated by filtration is made acidic with an aqueous mineral acid solution, for example, a dilute aqueous hydrochloric acid solution, and the resulting aqueous solution is extracted with a suitable organic solvent, such as diethyl ether. Thereafter, substituted phenylbilpic acid can be obtained by removing the organic solvent. Similarly, the aqueous layer portion containing the alkaline earth metal salt of substituted phenylacetic acid is made acidic with a mineral acid aqueous solution, for example, dilute hydrochloric acid aqueous solution, and the resulting aqueous solution is extracted with a suitable organic solvent, such as diethyl ether. By-product substituted phenylacetic acid can be recovered by removing the solvent.
又、コバルトカルボニル触媒を含有する水に難溶性の溶
媒層部分は何等処理を行うことなくそのまま反応系にリ
サイクルし、再使用することができる。Further, the portion of the solvent layer containing the cobalt carbonyl catalyst that is sparingly soluble in water can be recycled to the reaction system as it is without any treatment and can be reused.
(ホ)発明の効果
本発明によれば、置換フェニルビルピン酸牧率が高(、
副生置換フェニル酢酸のアルカリ土類金属塩とコバルト
カルボニル触媒の相互分離が容易で且つコバルトカルボ
ニル触媒はそのまま反応系にリサイクルして再使用する
ことかできる。(e) Effects of the invention According to the present invention, the substituted phenylbilpine acid oxidation rate is high (,
The alkaline earth metal salt of the by-product substituted phenylacetic acid and the cobalt carbonyl catalyst can be easily separated from each other, and the cobalt carbonyl catalyst can be recycled to the reaction system as it is for reuse.
従って、経済的に置換フェニルビルピン酸を製造するこ
とが可能となった。Therefore, it has become possible to economically produce substituted phenylbilpic acid.
以下に本発明を実施例を挙げて詳細に説明するが、本発
明はこれらに限定されるものではない。The present invention will be described in detail below with reference to Examples, but the present invention is not limited thereto.
(へ)実施例
実施例1
500m#のステンレス製オートクレーブに、メチルイ
ソブチルケトン100mA、水50m1、水酸化カルシ
ウム9.3 g (0,126モル)、p−弗化ペンジ
ルクロライド8.8 g (0,OEi 1モル)、及
びジコバルトオクタカルボニル1.2g(0,0035
モル)を仕込んだ。(F) Examples Example 1 In a 500 m# stainless steel autoclave, 100 mA of methyl isobutyl ketone, 50 ml of water, 9.3 g (0,126 mol) of calcium hydroxide, and 8.8 g of p-penzyl fluoride chloride ( 0.0, OEi 1 mole), and dicobalt octacarbonyl 1.2 g (0.0035
Mol) was prepared.
オートクレーブ内を一酸化炭素で洗浄し、一酸化炭素加
圧下で攪拌しなから昇温後、一酸化炭素圧力1kg/c
れ温度50℃で一酸化炭素の吸収が停止するまで10時
間反応を行った。Clean the inside of the autoclave with carbon monoxide, raise the temperature without stirring under carbon monoxide pressure, and then reduce the carbon monoxide pressure to 1 kg/c.
The reaction was carried out at a temperature of 50° C. for 10 hours until absorption of carbon monoxide stopped.
反応後、反応混合物は一酸化炭素圧力を利用してオート
クレーブから加圧濾過器を介して固体と有機層及び水層
に分離した。After the reaction, the reaction mixture was separated from the autoclave into a solid, an organic layer, and an aqueous layer through a pressure filter using carbon monoxide pressure.
得られた固体を500mfのフラスコに移し、10%塩
酸水溶液270mj!とジエチルエーテル150mj!
を加え固体が完全に溶解するまで攪拌した。ジエチルエ
ーテル層を分離後、水層を更にジエチルエーテル100
mj2で2回抽出した。これらジエチルエーテル層を併
せ、水洗後硫酸ナトリウムで乾燥した。乾燥後ジエチル
エーテルを留去するとp−弗化フェニルビルピン酸8゜
1gが得られ、収率は73.0%であった。The obtained solid was transferred to a 500 mf flask, and 270 mj! of 10% aqueous hydrochloric acid solution was added. and diethyl ether 150mj!
was added and stirred until the solid was completely dissolved. After separating the diethyl ether layer, the aqueous layer was further diluted with 100% diethyl ether.
Extracted twice with mj2. These diethyl ether layers were combined, washed with water, and then dried over sodium sulfate. After drying, diethyl ether was distilled off to obtain 8.1 g of p-fluorinated phenylbilpic acid, with a yield of 73.0%.
反応濾液の水層は、10%塩酸水溶液70mj!で酸性
としジエチルエーテル100m7!で3回抽出した。こ
れらジエチルエーテル層を併せ、硫酸ナトリウムで乾燥
後、ジエチルエーテルを留去するとp−弗化フェニル酢
酸が1.0g得られ、収率は10.7%であった。The aqueous layer of the reaction filtrate was treated with 70mj of 10% aqueous hydrochloric acid solution! Make it acidic and diethyl ether 100m7! Extracted three times. These diethyl ether layers were combined, dried over sodium sulfate, and then the diethyl ether was distilled off to obtain 1.0 g of p-fluorinated phenylacetic acid, with a yield of 10.7%.
反応濾液の有機層には、コバルトカルボニル触媒が存在
した。A cobalt carbonyl catalyst was present in the organic layer of the reaction filtrate.
実施例2
水に難溶性の溶媒としてアセトフェノンを使用した他は
、実施例1と同様に反応及び処理を行った。p−弗化フ
ェニルビルピン酸の収率は72.0%、p−弗化フェニ
ル酢酸の収率は10.5%であった。Example 2 The reaction and treatment were carried out in the same manner as in Example 1, except that acetophenone was used as a poorly water-soluble solvent. The yield of p-fluorinated phenylbilpic acid was 72.0%, and the yield of p-fluorinated phenylacetic acid was 10.5%.
実施例3
常圧下一酸化炭素を吹込みながら、反応温度を50℃、
反応時間を20時間とした他は、実施例1と同様に反応
及び処理を行った。p−弗化フェニルビルピン酸の収率
は71.5%、p−弗化フェニル酢酸の収率は9.2%
であった。Example 3 While blowing carbon monoxide under normal pressure, the reaction temperature was set at 50°C.
The reaction and treatment were carried out in the same manner as in Example 1, except that the reaction time was 20 hours. The yield of p-fluorinated phenylbilpic acid was 71.5%, and the yield of p-fluorinated phenylacetic acid was 9.2%.
Met.
実施例4
メチルイソブチルケトン100m#、水50m11水酸
化カルシウム9.3 g (0,126モル)、〇−弗
化ペンジルクロライド8.8 g (0,061モル)
、及びジコバルトオクタカルボニル1.2g(0,00
35モル)を仕込み、実施例1と同様に反応及び処理を
行った。〇−弗化フェニルビルピン酸の収率は68.0
%、〇−弗化フェニル酢酸の収率は5.9%であった。Example 4 100 m# of methyl isobutyl ketone, 50 m of water, 9.3 g (0,126 mol) of calcium hydroxide, 8.8 g (0,061 mol) of 〇-fluorinated penzyl chloride
, and dicobalt octacarbonyl 1.2 g (0,00
35 mol), and the reaction and treatment were carried out in the same manner as in Example 1. 〇-Yield of fluorinated phenylvirpic acid is 68.0
%, the yield of 0-fluorinated phenylacetic acid was 5.9%.
実施例5
メチルイソブチルケトン100m4.水50m1、水酸
化カルシウム9.3g(0,126モル)、m−弗化ペ
ンジルクロライド8.8 g (0,061モル)、及
びジコバルトオクタカルボニル1.2g(0,0035
モル)を仕込み、実施例1と同様に反応及び処理を行っ
た。m−弗化フェニルビルピン酸の収率は71.4%、
m−弗化フェニル酢酸の収率は3.5%であった。Example 5 Methyl isobutyl ketone 100m4. 50 ml of water, 9.3 g (0,126 mol) of calcium hydroxide, 8.8 g (0,061 mol) of m-penzyl fluoride, and 1.2 g (0,0035 mol) of dicobalt octacarbonyl.
mol), and the reaction and treatment were carried out in the same manner as in Example 1. The yield of m-fluorinated phenylbilpic acid was 71.4%,
The yield of m-fluorinated phenylacetic acid was 3.5%.
実施例6
メチルイソブチルケトン100nl、水50m1、水酸
化力)Li’、i”)L9.3 g (0,126モル
)、p−塩化ペンジルクロライド9.8 g (0,0
61モル)、及びジコバルトオクタカルボニル1.2g
(0,OO35モル)を仕込み、実施例1と同様に反応
及び処理を行った。p−塩化フェニルビルピン酸の収率
は77.4%、p−塩化フェニル酢酸の牧酸の収率は2
.4%であった。Example 6 100 nl of methyl isobutyl ketone, 50 ml of water, hydroxylation power)Li',i'')L9.3 g (0,126 mol), p-penzyl chloride 9.8 g (0,0
61 mol), and 1.2 g of dicobalt octacarbonyl
(0,0035 mol) was charged, and the reaction and treatment were carried out in the same manner as in Example 1. The yield of p-chlorinated phenylvirupic acid is 77.4%, and the yield of p-chlorinated phenylbilpic acid is 2.
.. It was 4%.
実施例7
メチルイソブチルケトン100mI!、水50mp1水
酸化カルシウム9’、3 g (0,126モル)、p
−塩化ペンジルクロライド9.8 g (0’、061
モル)、及びジコバルトオクタカルボニル1.2g(0
,0035モル)を仕込み、実施例1と同様に反応及び
処理を行った。p−塩化フェニルビルピン酸の収率は7
7.4%、p−塩化フェニル酢酸の収率は10.3%で
あった。Example 7 Methyl isobutyl ketone 100mI! , water 50 mp1 calcium hydroxide 9', 3 g (0,126 mol), p
-penzyl chloride 9.8 g (0', 061
mole), and dicobalt octacarbonyl 1.2 g (0
,0035 mol), and the reaction and treatment were carried out in the same manner as in Example 1. The yield of p-phenylvirpic acid chloride is 7
The yield of p-chlorophenylacetic acid was 10.3%.
実施例8
メチルイソブチルケトン100mji!、水50m11
水酸化カルシウム9.3g(0,126モル)、2.4
−ジメチルベンジルクロライ)’9.4 g (0゜0
61モル)、及びジコバルトオクタカルボニル1.2
g (0,0035モル)を仕込み、実施例1と同様に
反応及び処理を行った。2,4−ジメチルフェニルビル
ピン酸の収率は81.0%、2.4−ジメチルフェニル
酢酸の収率は1.7%であった。Example 8 Methyl isobutyl ketone 100mji! , water 50m11
Calcium hydroxide 9.3g (0,126 mol), 2.4
-dimethylbenzylchloride)'9.4 g (0°0
61 mol), and dicobalt octacarbonyl 1.2
g (0,0035 mol) was charged, and the reaction and treatment were carried out in the same manner as in Example 1. The yield of 2,4-dimethylphenylbilpic acid was 81.0%, and the yield of 2,4-dimethylphenylacetic acid was 1.7%.
実施例9
メチルイソブチルケトン100mβ、水50m1、水酸
化カルシウム9.3g(0,126モル)、3.4−ジ
メチルベンジルクロライド9.4g(0゜061モル)
、及びジコバルトオクタカルボニル1.2 g (0,
0035モル)を仕込み、実施例1と同様に反応及び処
理を行った。3,4−ジメチルフェニルビルピン酸の収
率は73.5%、3,4−ジメチルフェニル酢酸の収率
は2.0%であった。Example 9 Methyl isobutyl ketone 100 mβ, water 50 ml, calcium hydroxide 9.3 g (0,126 mol), 3,4-dimethylbenzyl chloride 9.4 g (0°061 mol)
, and dicobalt octacarbonyl 1.2 g (0,
0035 mol), and the reaction and treatment were carried out in the same manner as in Example 1. The yield of 3,4-dimethylphenylbilpic acid was 73.5%, and the yield of 3,4-dimethylphenylacetic acid was 2.0%.
実施例10
メチルイソブチルケトン100m#、水50川l、水酸
化カルシウム9.3g(0,126モル)、p−イソプ
ロピルベンジルクロライド10.3g(0,061モル
)、及びジコバルトオクタカルボニル1.2 g (0
,0035モル)を仕込み、実施例1と同様に反応及び
処理を行った。p−イソプロピルフェニルビルピン酸の
収率は72.1%、p−イソプロビルフェニル酢酸の収
率は6.8%であった。Example 10 100 m# of methyl isobutyl ketone, 50 liters of water, 9.3 g (0,126 mol) of calcium hydroxide, 10.3 g (0,061 mol) of p-isopropylbenzyl chloride, and 1.2 g (0,061 mol) of dicobalt octacarbonyl. g (0
,0035 mol), and the reaction and treatment were carried out in the same manner as in Example 1. The yield of p-isopropylphenylbilpic acid was 72.1%, and the yield of p-isopropylphenylacetic acid was 6.8%.
Claims (1)
ジルクロライドと一酸化炭素及びアルカリ土類金属塩基
とを反応させる際に、溶媒として水と水に難溶性の溶媒
を存在させ反応させることを特徴とする置換フェニルビ
ルピン酸の製造法。 2、水に難溶性の溶媒がケトンであることを特徴とする
特許請求の範囲第1項の製造法。 3、ケトンがメチルイソブチルケトン又はアセトフェノ
ンであることを特徴とする特許請求の範囲第1項の製造
法。 4、アルカリ土類金属塩基が水酸化カルシウムであるこ
とを特徴とする特許請求の範囲第1項の製造法。 5、コバルトカルボニル化合物がジコバルトオクタカル
ボニルであることを特徴とする特許請求の範囲第1項の
製造法。 6、一酸化炭素圧力が常圧〜100kg/cm^2であ
ることを特徴とする特許請求の範囲第1項の製造法。[Claims] 1. When reacting substituted benzyl chloride with carbon monoxide and an alkaline earth metal base in the presence of a cobalt carbonyl compound catalyst, the reaction is performed in the presence of water as a solvent and a solvent that is sparingly soluble in water. A method for producing substituted phenylbilpic acid, characterized by: 2. The manufacturing method according to claim 1, wherein the solvent that is poorly soluble in water is a ketone. 3. The manufacturing method according to claim 1, wherein the ketone is methyl isobutyl ketone or acetophenone. 4. The production method according to claim 1, wherein the alkaline earth metal base is calcium hydroxide. 5. The manufacturing method according to claim 1, wherein the cobalt carbonyl compound is dicobalt octacarbonyl. 6. The manufacturing method according to claim 1, wherein the carbon monoxide pressure is normal pressure to 100 kg/cm^2.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61189831A JPS6348244A (en) | 1986-08-13 | 1986-08-13 | Production of substituted phenylpyruvic acid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61189831A JPS6348244A (en) | 1986-08-13 | 1986-08-13 | Production of substituted phenylpyruvic acid |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6348244A true JPS6348244A (en) | 1988-02-29 |
JPH0533938B2 JPH0533938B2 (en) | 1993-05-20 |
Family
ID=16247939
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61189831A Granted JPS6348244A (en) | 1986-08-13 | 1986-08-13 | Production of substituted phenylpyruvic acid |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6348244A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2003014057A1 (en) * | 2001-08-08 | 2003-02-20 | Tanabe Seiyaku Co., Ltd. | Processes for producing halogenophenylpyruvic acid and optically active halogenophenylalanine |
-
1986
- 1986-08-13 JP JP61189831A patent/JPS6348244A/en active Granted
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2003014057A1 (en) * | 2001-08-08 | 2003-02-20 | Tanabe Seiyaku Co., Ltd. | Processes for producing halogenophenylpyruvic acid and optically active halogenophenylalanine |
Also Published As
Publication number | Publication date |
---|---|
JPH0533938B2 (en) | 1993-05-20 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US6686482B2 (en) | Process for preparing piperonal | |
JPH0256331B2 (en) | ||
JPH0747125B2 (en) | Method for producing acetic acid derivative | |
JPS6348244A (en) | Production of substituted phenylpyruvic acid | |
JPS62158239A (en) | Recovery of catalyst for production of phenylpyruvic acid | |
JPH1072396A (en) | Production of 1-(3-trifluoromethyl)phenyl-2-propanone | |
JPS5865241A (en) | Carbonylation of secondary benzylhalide | |
JPH07300316A (en) | Method for recovery of cobalt and tungsten from reaction solution and method for reuse of them | |
JPS62158240A (en) | Production of phenylpyruvic acid | |
EP0195530B1 (en) | Process for the preparation of phenyl pyruvic acid | |
JPH0680030B2 (en) | Method for recovering phenylpyruvic acid production catalyst | |
JPS58144337A (en) | Selective removal of catechol from 2-methallyloxyphenol | |
JPH0680029B2 (en) | Method for producing phenylpyruvic acid | |
JPH0899971A (en) | Purification of piperonal | |
JPS62108842A (en) | Production of malonic acid diester | |
JPH07330755A (en) | Production of piperonal | |
JP2968104B2 (en) | Method for producing aminocarboxylate | |
JPH05213926A (en) | Production of 2-furancarboxylic acid | |
JP3208458B2 (en) | Method for producing 1,4-dihydroxy-2-naphthoic acid | |
JPS59157039A (en) | Production of xylylene glycol | |
JPH0578307A (en) | Process for producing dialkyl, dicycloalkyl or diaryl disulfide | |
JPH05194313A (en) | Production of 2,6-dihydroxybenzoic acid | |
JPH03228830A (en) | Method for recoverying cobalt compound | |
JP2004256466A (en) | Method for producing 2,3,4,5-tetrafluorobenzoic acid | |
JPH01226850A (en) | Production of alkali metal salt of ether carboxylic acid |