JPH05339208A - Production of pyruvic ester - Google Patents
Production of pyruvic esterInfo
- Publication number
- JPH05339208A JPH05339208A JP4168490A JP16849092A JPH05339208A JP H05339208 A JPH05339208 A JP H05339208A JP 4168490 A JP4168490 A JP 4168490A JP 16849092 A JP16849092 A JP 16849092A JP H05339208 A JPH05339208 A JP H05339208A
- Authority
- JP
- Japan
- Prior art keywords
- ester
- bromine
- chlorine
- catalyst
- pref
- 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
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
【0001】[0001]
【産業上の利用分野】本発明はピルビン酸エステルの製
造法に関する。さらに詳しくは、各種化学薬品の合成原
料および半導体製造時の溶媒等として使用されるピルビ
ン酸エステルを乳酸エステルの酸化により製造する方法
に関する。FIELD OF THE INVENTION The present invention relates to a method for producing pyruvic acid ester. More specifically, it relates to a method for producing pyruvic acid ester, which is used as a raw material for synthesizing various chemicals and as a solvent in semiconductor production, by oxidizing lactate ester.
【0002】ピルビン酸は生体内物質代謝経路における
重要な中間体であり、そのエステルとともに各種生理活
性物質を合成する際の原料として有用である。また、近
年ピルビン酸エステルは半導体製造の際等の溶剤として
も用いられている。[0002] Pyruvate is an important intermediate in the metabolic pathway of substances in vivo, and is useful as a raw material when synthesizing various physiologically active substances together with its ester. Further, in recent years, pyruvic acid ester has been used as a solvent for semiconductor production.
【0003】[0003]
【従来の技術およびその課題】従来、ピルビン酸は、シ
アン化ナトリウムと塩化アセチルとの反応により得られ
るシアン化アセチルを加水分解する方法、あるいは酒石
酸を硫酸水素カリウムの存在下に乾留する方法によって
製造されている。しかしながら、シアン化アセチルを経
由する方法は多量の副生成物を生じ収率が低く、また酒
石酸を原料とする方法は原料が高価であり、収率も低い
などの欠点を有している。BACKGROUND OF THE INVENTION Conventionally, pyruvic acid is produced by a method of hydrolyzing acetyl cyanide obtained by the reaction of sodium cyanide and acetyl chloride, or a method of dry-distilling tartaric acid in the presence of potassium hydrogen sulfate. Has been done. However, the method via acetyl cyanide has drawbacks that a large amount of by-products are produced and the yield is low, and the method using tartaric acid as a raw material is expensive and the yield is low.
【0004】そこで、安価でかつ工業的に有利に入手で
きる乳酸あるいは乳酸エステルを原料に用い、これを酸
化的に脱水素してピルビン酸あるいはピルビン酸エステ
ルを製造する方法が注目されている。Therefore, a method of producing pyruvic acid or a pyruvic acid ester by using lactic acid or a lactic acid ester that is inexpensive and industrially advantageous as a raw material and oxidatively dehydrogenating the lactic acid or lactic acid ester has been drawing attention.
【0005】乳酸(エステル)を原料とし、ピルビン酸
(エステル)を製造する方法としては、例えば、(1)
乳酸脱水素酵素または乳酸脱水素酵素を持つ微生物を用
いて乳酸を脱水素する方法、(2)過マンガン酸カリウ
ム等の酸化剤により酸化する方法、(3)白金、パラジ
ウム等の貴金属触媒(特開昭54-138514 号公報,特公昭
38-3662 号公報,特公昭61-16263号公報)、あるいは金
属酸化物触媒(特公昭56-19854号公報,特開昭54-21982
号公報,特公昭64-11011号公報)を用いる接触酸化方
法、および(4)過酸化水素水を用いる液相酸化方法
(特開平1-242554号公報)等が提案されている。As a method for producing pyruvic acid (ester) from lactic acid (ester) as a raw material, for example, (1)
A method for dehydrogenating lactic acid using lactate dehydrogenase or a microorganism having lactate dehydrogenase, (2) a method for oxidizing with an oxidizing agent such as potassium permanganate, (3) a precious metal catalyst such as platinum or palladium (special Japanese Laid-Open Publication No. 54-138514, Japanese Patent Publication
38-3662, JP 61-16263), or metal oxide catalyst (JP 56-19854, JP 54-21982).
Japanese Patent Publication No. 64-11011), and (4) Liquid phase oxidation method using hydrogen peroxide solution (Japanese Patent Laid-Open No. 1-242554).
【0006】しかし、(1)の微生物を用いる方法は、
副生するα−ケトグルタル酸の分離が困難なこと、また
高BOD廃水が多量に生じることなどの欠点がある。
(2)の過マンガン酸カリウム等の酸化剤を用いる方法
は、酸化剤が高価であり、また収率が50%程度と低い
という欠点を有する。(3)の接触酸化法は、触媒が高
価であること、触媒の寿命が短いこと、転化率が十分で
なく、そのため沸点の近い乳酸エステルとピルビン酸エ
ステルとの分離操作が面倒であるなどの欠点を有する。
(4)の過酸化水素水を用いる方法は、過酸化水素水が
高価であり、工業的製造方法としてはコスト面で問題が
ある。However, the method using the microorganism of (1) is
There are drawbacks such as difficulty in separating α-ketoglutaric acid produced as a by-product and generation of a large amount of high BOD wastewater.
The method (2) using an oxidizing agent such as potassium permanganate has the drawbacks that the oxidizing agent is expensive and the yield is low at about 50%. In the catalytic oxidation method of (3), the catalyst is expensive, the life of the catalyst is short, the conversion rate is not sufficient, and therefore the separation operation of lactate ester and pyruvate ester having close boiling points is troublesome. It has drawbacks.
The method of using hydrogen peroxide solution of (4) has a problem in terms of cost as an industrial manufacturing method because hydrogen peroxide solution is expensive.
【0007】以上の如く、乳酸(エステル)を原料とす
る従来のピルビン酸(エステル)の製造方法は工業的製
造方法としては、必ずしも満足できるものではない。従
って、本発明の目的は、乳酸エステルからピルビン酸エ
ステルを工業的に有利に製造する方法を提供することに
ある。As described above, the conventional method for producing pyruvic acid (ester) using lactic acid (ester) as a raw material is not always satisfactory as an industrial production method. Therefore, an object of the present invention is to provide a method for industrially producing pyruvic acid ester from lactate ester in an industrially advantageous manner.
【0008】[0008]
【課題を解決するための手段】本発明者らは上記に鑑
み、酸化剤として塩素あるいは塩素系化合物を用いる方
法につき鋭意検討を重ねた結果、触媒として臭素または
臭素化合物を用い、光照射の下で反応を行なうとピルビ
ン酸エステルが選択性よく高収率で得られることを見出
し、本発明に到達したものである。In view of the above, the inventors of the present invention have made extensive studies as to a method of using chlorine or a chlorine-based compound as an oxidant. As a result, bromine or a bromine compound is used as a catalyst and is irradiated with light. It was found that the pyruvic acid ester can be obtained with high selectivity in a high yield when the reaction is carried out in accordance with the present invention, and has arrived at the present invention.
【0009】すなわち、本発明は臭素または臭素化合物
の存在下、光を照射しながら乳酸エステルを塩素または
次亜塩素酸塩により酸化することを特徴とするピルビン
酸エステルの製造法を提供したものである。なお、従来
塩素または臭素を用いて2級アルコールの酸化する方法
は知られているが、α−ヒドロキシカルボン酸を塩素ま
たは臭素により酸化して、α−ケトカルボン酸を製造す
る方法は報告されていない。That is, the present invention provides a method for producing a pyruvate ester, which comprises oxidizing a lactate ester with chlorine or hypochlorite in the presence of bromine or a bromine compound while irradiating light. is there. Although a method of oxidizing a secondary alcohol using chlorine or bromine is conventionally known, a method of producing an α-ketocarboxylic acid by oxidizing an α-hydroxycarboxylic acid with chlorine or bromine has not been reported. ..
【0010】以下、本発明のピルビン酸エステルの製造
法を詳細に説明する。乳酸エステル 本発明の製造方法において、原料として用いる乳酸エス
テルは下記一般式The method for producing the pyruvic acid ester of the present invention will be described in detail below. Lactate ester In the production method of the present invention, the lactate ester used as a raw material has the following general formula:
【化1】CH3 CH(OH)COOR で示される。ここでRは炭素数1〜6のアルキル基、具
体的には、メチル基、エチル基、プロピル基、ブチル
基、ペンチル基、ヘキシル基、およびそれらの異性体基
を表わす。これら本発明方法の原料となる乳酸エステル
は、市販のものを使用しても良いし、公知の方法によっ
て合成したものを用いても良い。Embedded image CH 3 CH (OH) COOR. Here, R represents an alkyl group having 1 to 6 carbon atoms, specifically, a methyl group, an ethyl group, a propyl group, a butyl group, a pentyl group, a hexyl group, and an isomer group thereof. As the lactic acid ester which is a raw material for the method of the present invention, a commercially available one may be used, or one synthesized by a known method may be used.
【0011】触媒 本発明の方法で用いる触媒としては、反応溶液中で臭素
イオンを生ずるものであれば良い。具体例としては、臭
素、臭化水素、臭化ナトリウム、臭化カリウム、臭化カ
ルシウム、臭化マグネシウム等が挙げられる。これらの
触媒は乳酸エステルに対し 0.5〜30モル%、好ましく
は2〜15モル%使用する。0.5 モル%以下では塩素に
よる酸化が十分起こらず、また30モル%を越えると、
例えば、ピルビン酸エステルの臭素化物等の副生が増大
する恐れがある。 Catalyst The catalyst used in the method of the present invention may be any catalyst that produces bromine ions in the reaction solution. Specific examples include bromine, hydrogen bromide, sodium bromide, potassium bromide, calcium bromide, magnesium bromide and the like. These catalysts are used in an amount of 0.5 to 30 mol%, preferably 2 to 15 mol% based on the lactate ester. If it is less than 0.5 mol%, oxidation by chlorine does not occur sufficiently, and if it exceeds 30 mol%,
For example, there is a possibility that by-products such as a bromide of pyruvate ester will increase.
【0012】酸化剤 本発明の方法では酸化剤として、塩素あるいは次亜塩素
酸塩を使用する。次亜塩素酸塩としては次亜塩素酸ナト
リウム、次亜塩素酸カリウム等を用いることができる。
酸化剤の使用量は乳酸エステルに対し 0.9〜1.5 当量、
好ましくは1当量用いる。なお、触媒に臭素を用いる場
合には、臭素も酸化剤として作用するので、塩素と臭素
の合計量が上記の範囲であればよい。 Oxidizing Agent In the method of the present invention, chlorine or hypochlorite is used as an oxidizing agent. As the hypochlorite, sodium hypochlorite, potassium hypochlorite or the like can be used.
The amount of oxidant used is 0.9 to 1.5 equivalents to lactate,
Preferably 1 equivalent is used. When bromine is used as the catalyst, bromine also acts as an oxidizing agent, so the total amount of chlorine and bromine may be within the above range.
【0013】溶媒 本発明の方法では、原料の乳酸および生成するピルビン
酸の溶媒として、これら試薬に対して不活性な有機溶剤
を使用する。このような有機溶剤としては、例えば塩化
メチレン、クロロホルム、1,1,1−トリクロロエタ
ン等のハロゲン化炭化水素が好ましく用いられる。ま
た、有機溶剤と共に酸化剤の塩素あるいは次亜塩素酸塩
を溶解する水を同時に使用し、水−有機溶剤の不均一2
相系で、十分な撹拌の下で反応を行なう。 Solvent In the method of the present invention, an organic solvent inert to these reagents is used as a solvent for the raw material lactic acid and the produced pyruvic acid. As such an organic solvent, halogenated hydrocarbons such as methylene chloride, chloroform, and 1,1,1-trichloroethane are preferably used. Also, water that dissolves chlorine as an oxidant or hypochlorite is used together with an organic solvent, so that water-organic solvent is not uniform.
The reaction is carried out in a phase system with sufficient stirring.
【0014】反応条件 乳酸エステルおよび触媒を前記水と水不溶性溶媒の2相
系混合溶媒中に溶解する。ここで水不溶性溶媒中の原料
乳酸エステルの濃度を1〜30重量%程度に設定し、光
を照射しながら反応液温度を−5〜50℃、好ましくは
0〜20℃として酸化剤を添加(導入)する。反応によ
り熱が発生するので、酸化剤の添加は徐々に行なうとと
もに反応媒質の温度を前記範囲に保持するため適宜冷却
する必要がある。 Reaction conditions The lactate ester and the catalyst are dissolved in a two-phase mixed solvent of water and a water-insoluble solvent. Here, the concentration of the raw material lactate ester in the water-insoluble solvent is set to about 1 to 30% by weight, and the reaction solution temperature is adjusted to -5 to 50 ° C, preferably 0 to 20 ° C while irradiating light, and an oxidizer is added ( Introduce. Since heat is generated by the reaction, it is necessary to add the oxidizing agent gradually and to cool the reaction medium appropriately in order to keep the temperature in the above range.
【0015】本発明の方法で、反応時に照射する光は、
可視光、近赤外光、近紫外光等、300〜800nmの
波長の光であり、650nm以上の波長の光が好まし
い。酸化剤として塩素ガスを用いる場合は、塩素ガスを
反応液下部にバブリングさせる。反応終了後は、溶媒中
に残存している過剰な塩素を窒素等の不活性ガスを導入
して除去する。また、酸化剤として次亜塩素酸塩を用い
る場合は、濃塩酸等の強酸を用い反応溶液を酸性域、好
ましくはpHを4以下に保持しながら反応を行なう。In the method of the present invention, the light irradiated during the reaction is
Light having a wavelength of 300 to 800 nm, such as visible light, near infrared light, and near ultraviolet light, and light having a wavelength of 650 nm or more is preferable. When chlorine gas is used as the oxidant, chlorine gas is bubbled under the reaction solution. After completion of the reaction, excess chlorine remaining in the solvent is removed by introducing an inert gas such as nitrogen. When hypochlorite is used as the oxidant, a strong acid such as concentrated hydrochloric acid is used to carry out the reaction while maintaining the reaction solution in an acidic region, preferably pH 4 or less.
【0016】反応の進行は、クロマトグラフィーなどに
より追跡し、乳酸エステルの消失を確認したところで終
了させればよい。一般に反応時間は1〜10時間であ
る。反応後は炭酸水素ナトリウムおよび亜硫酸ナトリウ
ムの水溶液で処理した後、有機層を分液し、減圧蒸留等
により精製単離することにより目的のピルビン酸エステ
ルを高純度で得ることができる。The progress of the reaction may be traced by chromatography or the like and terminated when the disappearance of the lactate ester is confirmed. Generally, the reaction time is 1 to 10 hours. After the reaction, the target pyruvate ester can be obtained in high purity by treating with an aqueous solution of sodium hydrogen carbonate and sodium sulfite, separating the organic layer, and purifying and isolating by distillation under reduced pressure.
【0017】[0017]
【実施例】以下、本発明の実施例および比較例を挙げて
説明するが、本発明は下記の例により限定されるもので
ない。EXAMPLES The present invention will be described below with reference to examples and comparative examples, but the present invention is not limited to the following examples.
【0018】実施例1 20Wの蛍光灯2本の光が照射されたドラフト内に、撹
拌機、塩素導入管、温度計および冷却機を取り付けた3
00ml三口フラスコをセットする。ジクロロメタン2
70g、乳酸エチル 41.6 g(353ミリモル)、臭素
2.8g( 17.5 ミリモル)、水45gを加え撹拌する。
外部より冷却を行ない、フラスコ内の温度を5℃とした
後撹拌下に導入管から塩素を吹き込むと数分後発熱が始
まり内温が上昇するが、冷却により10〜15℃に調節
しながら45分かけて塩素 25.7 gを加えた後、窒素ガ
スを吹き込んで過剰の塩素を追い出す。 Example 1 A stirrer, a chlorine introduction tube, a thermometer and a cooler were installed in a draft irradiated with two lights of a 20 W fluorescent lamp.
Set up a 00 ml three neck flask. Dichloromethane 2
70 g, ethyl lactate 41.6 g (353 mmol), bromine
Add 2.8 g (17.5 mmol) and 45 g of water and stir.
After cooling from the outside and adjusting the temperature in the flask to 5 ° C, chlorine is blown into the flask from the inlet tube under stirring to generate heat after a few minutes and the internal temperature rises. After adding 25.7 g of chlorine over a period of time, blow excess nitrogen by blowing nitrogen gas.
【0019】有機層をガスクロマトグラフィーで分析し
たところ、ピルビン酸エチル収率は85%で、残存乳酸
エチルは0.2 %であった。有機層を分液し、炭酸水素ナ
トリウム5gと亜硫酸ナトリウム3gを水100gに溶
かした液を加え30分撹拌する。静置後50gの水で洗
浄した後、溶媒を留去し、減圧蒸留することによって、
32.2 g(278ミリモル,収率 78.8 %)のピルビン
酸エチルを得た。When the organic layer was analyzed by gas chromatography, the yield of ethyl pyruvate was 85% and the residual ethyl lactate was 0.2%. The organic layer is separated, a solution obtained by dissolving 5 g of sodium hydrogen carbonate and 3 g of sodium sulfite in 100 g of water is added, and the mixture is stirred for 30 minutes. After standing still and washing with 50 g of water, the solvent was distilled off, and the residue was distilled under reduced pressure.
32.2 g (278 mmol, yield 78.8%) of ethyl pyruvate was obtained.
【0020】実施例2 1リットル四口フラスコに、滴下ロート、温度計、pH
計、冷却機および撹拌機を取り付け、乳酸エチル50g
(424ミリモル)、ジクロロメタン338g、および
臭化ナトリウム1.7 g(17ミリモル)を水30gに溶
解した液を加え、7℃まで冷却する。この温度を維持し
ながら、撹拌下で35%塩酸 9.5gを加える。直径20
mmのハロゲン光照射装置により反応液面に光をスポッ
ト照射しながら、 12.4 %の次亜塩素酸ナトリウム水溶
液 254.6gをpH=1以下に保って、3時間かけて滴下
する。滴下終了後、30分熟成した後実施例1と同様の
操作を行ない、ピルビン酸エチル 39.8 g(343ミリ
モル, 81.0 %)を得た。 Example 2 A 1-liter four-necked flask was charged with a dropping funnel, thermometer, and pH.
Equipped with meter, cooler and stirrer, ethyl lactate 50g
(424 mmol), dichloromethane 338 g, and a solution prepared by dissolving 1.7 g (17 mmol) of sodium bromide in 30 g of water are added, and the mixture is cooled to 7 ° C. While maintaining this temperature, 9.5 g of 35% hydrochloric acid is added with stirring. Diameter 20
254.6 g of a 12.4% sodium hypochlorite aqueous solution was added dropwise over 3 hours while spot-irradiating the reaction liquid surface with a halogen light irradiation device of mm. After completion of dropping, the mixture was aged for 30 minutes and then the same operation as in Example 1 was carried out to obtain 39.8 g (343 mmol, 81.0%) of ethyl pyruvate.
【0021】実施例3 臭化ナトリウムの代わりに、臭素 1.35 g(8.5 ミリモ
ル)を加えて実施例2と同様に反応を行ない、同様の操
作を行なってピルビン酸エチル 40.4 g(348ミリモ
ル,収率 82.2 %)を得た。 Example 3 In place of sodium bromide, 1.35 g (8.5 mmol) of bromine was added and the reaction was carried out in the same manner as in Example 2. The same operation was carried out to obtain 40.4 g of ethyl pyruvate (348 mmol, yield). 82.2%).
【0022】実施例4 乳酸エチルの代わりに乳酸メチル44g(424ミリモ
ル)を用いた他は実施例2と同様の操作を行なうことに
よって、ピルビン酸メチル 30.3 g(297ミリモル,
収率 70.0 %)を得た。 Example 4 By repeating the same procedure as in Example 2 except that 44 g (424 mmol) of methyl lactate was used instead of ethyl lactate, 30.3 g (297 mmol, methyl pyruvate) of methyl pyruvate was obtained.
Yield 70.0%) was obtained.
【0023】実施例5 乳酸エチル 1182 g(10モル)、ジクロロメタン6リ
ットルおよび臭素32g( 0.2モル)を20リットルの
ガラス反応装置にしこみ、7℃に冷却する。水500g
と35%塩酸225gを加え、300Wの白熱電球を反
応器に照射しながら、 13.2 %の次亜塩素酸ナトリウム
5531 g( 29.8 モル)を10〜15℃で加える。反応
後、実施例1と同様の操作を行ない、ピルビン酸エチル
947g(8.2 モル,収率 82.0 %)を得た。 Example 5 1182 g (10 mol) of ethyl lactate, 6 liters of dichloromethane and 32 g (0.2 mol) of bromine were charged into a 20 liter glass reactor and cooled to 7 ° C. 500g of water
And 225 g of 35% hydrochloric acid are added, and while irradiating the reactor with an incandescent lamp of 300 W, 13.2% sodium hypochlorite is added.
5531 g (29.8 mol) are added at 10-15 ° C. After the reaction, the same operation as in Example 1 was performed to obtain 947 g (8.2 mol, yield 82.0%) of ethyl pyruvate.
【0024】[0024]
【発明の効果】臭素または臭素化合物の存在下、光を照
射しながら塩素または次亜塩素酸塩により乳酸エステル
を酸化する本発明の方法によれば、各種生理活性物質合
成の原料および半導体製造の際の溶剤等として有用なピ
ルビン酸エステルを高純度、高収率で製造することがで
きる。INDUSTRIAL APPLICABILITY According to the method of the present invention in which lactic acid ester is oxidized by chlorine or hypochlorite while irradiating with light in the presence of bromine or a bromine compound, the method of synthesizing various physiologically active substances and semiconductor production can be achieved. A pyruvic acid ester useful as a solvent or the like can be produced with high purity and high yield.
Claims (1)
射しながら乳酸エステルを塩素または次亜塩素酸塩によ
り酸化することを特徴とするピルビン酸エステルの製造
法。1. A method for producing a pyruvate ester, which comprises oxidizing a lactate ester with chlorine or hypochlorite while irradiating light in the presence of bromine or a bromine compound.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4168490A JPH05339208A (en) | 1992-06-03 | 1992-06-03 | Production of pyruvic ester |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4168490A JPH05339208A (en) | 1992-06-03 | 1992-06-03 | Production of pyruvic ester |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH05339208A true JPH05339208A (en) | 1993-12-21 |
Family
ID=15869059
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4168490A Pending JPH05339208A (en) | 1992-06-03 | 1992-06-03 | Production of pyruvic ester |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH05339208A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006151853A (en) * | 2004-11-26 | 2006-06-15 | Nagoya Industrial Science Research Inst | Method for producing carbonyl compound and method for producing aromatic carboxylic acid |
JP2008044908A (en) * | 2006-08-18 | 2008-02-28 | Nagoya Industrial Science Research Inst | Method for producing carbonyl compound |
-
1992
- 1992-06-03 JP JP4168490A patent/JPH05339208A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006151853A (en) * | 2004-11-26 | 2006-06-15 | Nagoya Industrial Science Research Inst | Method for producing carbonyl compound and method for producing aromatic carboxylic acid |
JP4670078B2 (en) * | 2004-11-26 | 2011-04-13 | 財団法人名古屋産業科学研究所 | Method for producing carbonyl compound and method for producing aromatic carboxylic acid |
JP2008044908A (en) * | 2006-08-18 | 2008-02-28 | Nagoya Industrial Science Research Inst | Method for producing carbonyl compound |
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