JPH01299245A - Production of squalic acid - Google Patents
Production of squalic acidInfo
- Publication number
- JPH01299245A JPH01299245A JP12629888A JP12629888A JPH01299245A JP H01299245 A JPH01299245 A JP H01299245A JP 12629888 A JP12629888 A JP 12629888A JP 12629888 A JP12629888 A JP 12629888A JP H01299245 A JPH01299245 A JP H01299245A
- Authority
- JP
- Japan
- Prior art keywords
- hydroxy
- cyclobutenedione
- bromine
- acid
- reaction
- 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
- 238000004519 manufacturing process Methods 0.000 title claims description 7
- 239000002253 acid Substances 0.000 title abstract description 9
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 claims abstract description 15
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 claims abstract description 15
- 229910052794 bromium Inorganic materials 0.000 claims abstract description 15
- KGPQKNJSZNXOPV-UHFFFAOYSA-N moniliformin Chemical class OC1=CC(=O)C1=O KGPQKNJSZNXOPV-UHFFFAOYSA-N 0.000 claims abstract description 11
- 239000007788 liquid Substances 0.000 claims abstract description 5
- 230000003301 hydrolyzing effect Effects 0.000 claims abstract description 3
- PWEBUXCTKOWPCW-UHFFFAOYSA-N squaric acid Chemical compound OC1=C(O)C(=O)C1=O PWEBUXCTKOWPCW-UHFFFAOYSA-N 0.000 claims description 13
- 150000003839 salts Chemical class 0.000 claims description 5
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 abstract description 14
- 238000000034 method Methods 0.000 abstract description 10
- 238000001914 filtration Methods 0.000 abstract description 6
- ZHSNCPHBWJGYMR-UHFFFAOYSA-N 3-bromo-4-hydroxycyclobut-3-ene-1,2-dione Chemical compound OC1=C(Br)C(=O)C1=O ZHSNCPHBWJGYMR-UHFFFAOYSA-N 0.000 abstract description 4
- 229910052783 alkali metal Inorganic materials 0.000 abstract description 3
- -1 alkali metal salt Chemical class 0.000 abstract description 2
- 239000003814 drug Substances 0.000 abstract description 2
- 150000008282 halocarbons Chemical class 0.000 abstract description 2
- 239000002585 base Substances 0.000 abstract 1
- 150000001875 compounds Chemical class 0.000 abstract 1
- CPELXLSAUQHCOX-UHFFFAOYSA-N Hydrogen bromide Chemical compound Br CPELXLSAUQHCOX-UHFFFAOYSA-N 0.000 description 18
- 238000006243 chemical reaction Methods 0.000 description 10
- 229910000042 hydrogen bromide Inorganic materials 0.000 description 9
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 6
- 238000006460 hydrolysis reaction Methods 0.000 description 5
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 4
- 150000007513 acids Chemical class 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 239000000543 intermediate Substances 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- WSLDOOZREJYCGB-UHFFFAOYSA-N 1,2-Dichloroethane Chemical compound ClCCCl WSLDOOZREJYCGB-UHFFFAOYSA-N 0.000 description 3
- 238000005893 bromination reaction Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000002244 precipitate Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- RWNKSTSCBHKHTB-UHFFFAOYSA-N Hexachloro-1,3-butadiene Chemical compound ClC(Cl)=C(Cl)C(Cl)=C(Cl)Cl RWNKSTSCBHKHTB-UHFFFAOYSA-N 0.000 description 2
- AFVFQIVMOAPDHO-UHFFFAOYSA-N Methanesulfonic acid Chemical compound CS(O)(=O)=O AFVFQIVMOAPDHO-UHFFFAOYSA-N 0.000 description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000004128 high performance liquid chromatography Methods 0.000 description 2
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 2
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 239000002904 solvent Substances 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
- SCYULBFZEHDVBN-UHFFFAOYSA-N 1,1-Dichloroethane Chemical compound CC(Cl)Cl SCYULBFZEHDVBN-UHFFFAOYSA-N 0.000 description 1
- BMYNFMYTOJXKLE-UHFFFAOYSA-N 3-azaniumyl-2-hydroxypropanoate Chemical compound NCC(O)C(O)=O BMYNFMYTOJXKLE-UHFFFAOYSA-N 0.000 description 1
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- 241000220317 Rosa Species 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 1
- 150000001342 alkaline earth metals Chemical class 0.000 description 1
- 229910002090 carbon oxide Inorganic materials 0.000 description 1
- 239000007806 chemical reaction intermediate Substances 0.000 description 1
- RGBVWCQARBEPPW-UHFFFAOYSA-N cyclobut-3-ene-1,2-dione Chemical compound O=C1C=CC1=O RGBVWCQARBEPPW-UHFFFAOYSA-N 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 150000002561 ketenes Chemical class 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229940098779 methanesulfonic acid Drugs 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 150000007530 organic bases Chemical class 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 159000000000 sodium salts Chemical class 0.000 description 1
- FERDNJVXTWPNSA-UHFFFAOYSA-M sodium;3,4-dioxocyclobuten-1-olate Chemical compound [Na+].[O-]C1=CC(=O)C1=O FERDNJVXTWPNSA-UHFFFAOYSA-M 0.000 description 1
- 238000011282 treatment Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、感レーザー色素や医薬品などの合成中間体と
して有用なスクアリン酸の製造方法に関する。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a method for producing squaric acid, which is useful as a synthetic intermediate for laser-sensitive dyes, pharmaceuticals, and the like.
従来の技術及び解決課題
スクアリン酸を製造する方法は、例えばヘキサクロロブ
タジェンを原料とする方法(米国特許4、104.30
8号など)、ケテン誘導体から製造する方法(JOC,
44,1208,(1979)ナト) 、−酸化炭素の
電解還元的4量化反応による製法(米国特許 3.83
3.489号)などが知られているが、合成中間体に爆
発危険性があること(米国特許4、104.308号)
、原料が高価、入手し難い、又は高圧の反応器を要する
などの欠点がある。Conventional techniques and problems to be solved A method for producing squaric acid is, for example, a method using hexachlorobutadiene as a raw material (U.S. Pat. No. 4,104.30).
No. 8), method of manufacturing from ketene derivatives (JOC,
44, 1208, (1979) Nat), -Production method by electroreductive tetramerization reaction of carbon oxide (US Patent 3.83)
3.489), but the synthetic intermediate has an explosion risk (U.S. Pat. No. 4, 104.308).
, the raw materials are expensive, difficult to obtain, or require a high-pressure reactor.
又、3−ヒドロキシ−3−シクロブテンジオンから下記
反応でスクアリン酸が製造できることが知られている〔
ヘルペチ力・キミ力・アクタ、。It is also known that squaric acid can be produced from 3-hydroxy-3-cyclobutenedione by the following reaction [
Herpechi Power, Kimi Power, Acta.
61、 (5)、 1784 (1978))。この
方法は中間体の4−ブロモ−3−ヒドロキシ−3−シク
ロブテンジオン単離時に臭化水素の白煙が生じること、
又、加水分解後のスクアリン酸の分離を濃塩酸中から行
うなど、工業的スケールでの取り扱いが非常に面倒であ
る。61, (5), 1784 (1978)). This method produces hydrogen bromide white smoke when isolating the intermediate 4-bromo-3-hydroxy-3-cyclobutenedione;
Furthermore, it is very troublesome to handle on an industrial scale, such as separating squaric acid from concentrated hydrochloric acid after hydrolysis.
収率73%
問題点を解決するための手段
3−ヒドロキシ−3−シクロブテンジオンからスクアリ
ン酸を製造する方法に関して検討を行った結果3−ヒド
ロキシ−3−シクロブテンジオンを臭素化するに際し、
−船釣に用いられる塩化メチレン、2塩化エチレンなど
の一10ゲン化炭化水素や、不活性な有機溶媒の代わり
に溶媒として水を使用できることが見出された。これに
より、反応中間体である4−ブロモ−3−ヒドロキシ−
3−シクロブテンジオンを単離することなく、反応液に
濃硫酸、塩化水素ガス、燐酸等の強酸類を添加して加水
分解反応に供する方法が完成された。Yield: 73% Means for solving the problem As a result of studying the method for producing squaric acid from 3-hydroxy-3-cyclobutenedione, when brominating 3-hydroxy-3-cyclobutenedione,
- It has been found that water can be used as a solvent in place of 110-generated hydrocarbons such as methylene chloride and ethylene dichloride used in boat fishing, and inert organic solvents. This allows the reaction intermediate 4-bromo-3-hydroxy-
A method has been completed in which strong acids such as concentrated sulfuric acid, hydrogen chloride gas, and phosphoric acid are added to the reaction solution to subject it to a hydrolysis reaction without isolating 3-cyclobutenedione.
本発明によれば、3−ヒドロキシ−3−シクロブテンジ
オンを水性液中臭素と反応させ、反応混合物を加水分解
処理してスクアリン酸を製造することができる。According to the present invention, squaric acid can be produced by reacting 3-hydroxy-3-cyclobutenedione with bromine in an aqueous liquid and hydrolyzing the reaction mixture.
臭素化反応に際して採用する水の量は、3−ヒドロキシ
−3−シクロブテンジオン又はその塩類に対して1〜5
0倍用いる。生産性や、攪拌効率の点から好ましくは2
〜10倍の量が用いられる。The amount of water employed in the bromination reaction is 1 to 5, based on 3-hydroxy-3-cyclobutenedione or its salt.
Use 0 times. Preferably 2 in terms of productivity and stirring efficiency.
~10 times the amount is used.
反応に使用する臭素の量は、3−ヒドロキシ−3−シク
ロブテンジオンに対し0.1〜2.0当量用いられるが
、原料を十分に消費し、過剰の臭素による副反応を抑え
るために、1.0〜1.2当量の範囲が好ましい。反応
は、0〜50℃、好ましくは、0〜30℃の温度で行わ
れる。The amount of bromine used in the reaction is 0.1 to 2.0 equivalents relative to 3-hydroxy-3-cyclobutenedione, but in order to consume enough raw materials and suppress side reactions caused by excess bromine, A range of 1.0 to 1.2 equivalents is preferred. The reaction is carried out at a temperature of 0-50<0>C, preferably 0-30<0>C.
臭素化反応に供する3−ヒドロキシ−3−シクロブテン
ジオンは遊離型、塩類いずれも用いられ、塩類としては
、アルカル金属又はアルカリ土類金属との塩や、各種有
機塩基との塩類が用いられるが、水溶媒に可溶で速やか
に反応が進行するK。3-Hydroxy-3-cyclobutenedione to be subjected to the bromination reaction can be used in either its free form or its salts, and salts with alkali metals or alkaline earth metals and salts with various organic bases are used. , K which is soluble in water solvent and the reaction proceeds rapidly.
Naなどとのアルカリ金属塩が好ましい。Alkali metal salts such as Na are preferred.
臭素化反応液は、強酸類を添加することにより、そのま
ま加水分解反応に供することができるが、過剰の臭素を
取り除く方が好ましい。30〜70℃で加熱、減圧する
ことにより臭素および、生成した臭化水素酸が除去され
る。The bromination reaction solution can be directly subjected to a hydrolysis reaction by adding a strong acid, but it is preferable to remove excess bromine. Bromine and generated hydrobromic acid are removed by heating at 30 to 70°C and reducing pressure.
加水分解反応には、強酸例えば、塩化水素、臭化水素、
硫酸、リン酸などの鉱酸類の他にパラトルエンスルホン
酸、メタンスルホン酸等が使用可能であるが、安価で取
り扱い容易な硫酸が最も好ましい。For hydrolysis reactions, strong acids such as hydrogen chloride, hydrogen bromide,
In addition to mineral acids such as sulfuric acid and phosphoric acid, p-toluenesulfonic acid and methanesulfonic acid can be used, but sulfuric acid is most preferred because it is inexpensive and easy to handle.
使用する強酸類濃度は10〜95%、使用する量は、4
−ブロモ−3−ヒドロキシ−3−シクロブテンジオンに
対して0,5〜50当量好ましくは濃度10〜70%の
ものを1〜30当量用いられる。反応は、70〜150
℃好ましくは70〜120℃で行われる。The concentration of strong acids used is 10 to 95%, and the amount used is 4
-Bromo-3-hydroxy-3-cyclobutenedione is used in an amount of 0.5 to 50 equivalents, preferably 1 to 30 equivalents at a concentration of 10 to 70%. The reaction is 70-150
It is preferably carried out at a temperature of 70 to 120°C.
得られたスクアリン酸は、加水分解反応系内で析出沈殿
するので、常法により濾取し、必要により精製して、高
純度スクアリン酸を得ることができる。The obtained squaric acid precipitates in the hydrolysis reaction system, so it can be collected by filtration by a conventional method and purified if necessary to obtain high-purity squaric acid.
作用および発明の効果
本発明により、4−ブロモ−3〜ヒドロキシ−3−シク
ロブテンジオンを単離をすることなくスクアリン酸の製
造が可能であり、工業的製法として、工程の簡略化作業
環境の改善に優れた効果を発揮する。又、前記中間体の
単離が不要なため、臭化水素の刺激臭が激しく劣悪な作
業環境になる濾過工程が不要となるうえ、工程も短縮し
、さらに臭素化溶媒に水を用いることにより、人体に有
害なハロゲン化炭化水素の使用を避けることができ、有
機溶剤を用いないので経済的にも有利である。Effects of the Invention According to the present invention, it is possible to produce squaric acid without isolating 4-bromo-3-hydroxy-3-cyclobutenedione, and as an industrial production method, it is possible to simplify the process and improve the work environment. Demonstrates excellent improvement effects. In addition, since isolation of the intermediate is not required, the filtration process, which produces a strong pungent odor of hydrogen bromide and creates a poor working environment, is not necessary, and the process is also shortened. This method is economically advantageous because it avoids the use of halogenated hydrocarbons, which are harmful to the human body, and does not use organic solvents.
実施例 以下、実施例により本発明を具体的に説明する。Example Hereinafter, the present invention will be specifically explained with reference to Examples.
実施例1゜
3−ヒドロキシ−3−シクロブテンジオン・ナトリウム
塩19.5g(0,163モル)、水117m1を50
0ffl14ツロフラスコに仕込み、N、下、攪拌しな
がら、温度15℃に保ち、滴下ローLより臭素27.3
g (0,171モル)を3時間で滴下した。この間、
温度を15〜20℃に保ち、臭素の滴下終了後、2時間
熟成した。反応終了後、減圧下、内温50℃にて軽く振
とうしながら3時間処理して、過剰の臭素および生成し
た臭化水素の一部を除去した。この液に、濃硫酸78g
(0,795モル)を加え、硫酸濃度4 Qwt%に調
製した後、90〜95℃、10時間加熱攪拌した後、3
0℃まで冷却し生成したスクアリン酸を十分に析出させ
た。析出物を濾取、アセトン洗浄、乾燥してスクアリン
酸17.5 gを得た。収率94.4%HPLC純度9
9.3wt%。本島は必要に応じて、更に高純度に再結
晶精製することができる。Example 1 19.5 g (0,163 mol) of 3-hydroxy-3-cyclobutenedione sodium salt and 117 ml of water were added to 50
Pour 0ffl into a 14-meter flask and add 27.3 bromine from dropping funnel L while stirring under N.
g (0,171 mol) was added dropwise over 3 hours. During this time,
The temperature was maintained at 15 to 20°C, and the mixture was aged for 2 hours after the dropwise addition of bromine was completed. After the reaction was completed, the mixture was treated under reduced pressure at an internal temperature of 50° C. with gentle shaking for 3 hours to remove excess bromine and a portion of the generated hydrogen bromide. Add 78g of concentrated sulfuric acid to this liquid.
(0,795 mol) was added to adjust the sulfuric acid concentration to 4 Qwt%, and then heated and stirred at 90 to 95°C for 10 hours.
The mixture was cooled to 0° C. to sufficiently precipitate the generated squaric acid. The precipitate was collected by filtration, washed with acetone, and dried to obtain 17.5 g of squaric acid. Yield 94.4% HPLC purity 9
9.3wt%. Honjima can be recrystallized to a higher purity if necessary.
実施例2〜4
実施例1において硫酸使用量を変える以外は全て同様の
処理を行い下表の結果を得た。Examples 2 to 4 The same treatments as in Example 1 were carried out except that the amount of sulfuric acid used was changed, and the results shown in the table below were obtained.
比較例1゜
3−ヒドロキシ−3−シフ・ロブテンジオン・ナトリウ
ム塩19.5g(0,163モル)1.2−ジクロルエ
タン200mlを500ml 4ツロフラスコに仕込み
、N、下、攪拌しながら、内温を50℃に保ち、臭素2
7.3g (0,171モル)を2時間で滴下した。こ
の間内温を15〜20℃に保った。Comparative Example 1 19.5 g (0,163 mol) of 3-hydroxy-3-Schiff robenedione sodium salt and 200 ml of 1,2-dichloroethane were placed in a 500 ml 4-tube flask, and the internal temperature was brought to 50°C while stirring under N. Keep at ℃, bromine 2
7.3 g (0,171 mol) was added dropwise over 2 hours. During this time, the internal temperature was maintained at 15 to 20°C.
更に同温度で2時間熟成した後、減圧下、内温50℃で
軽く還流しながら、残存臭素及び生成した臭化水素を除
去した後、20℃に冷却し、析出生成物を濾取し、1.
2ジクロルエタンで洗浄した。濾過中、臭化水素の白煙
が上がり、1.2ジクロルエタンで洗浄後も強い臭化水
素臭が残存した。After further aging at the same temperature for 2 hours, residual bromine and generated hydrogen bromide were removed under reduced pressure with slight reflux at an internal temperature of 50°C, and then cooled to 20°C and the precipitated product was collected by filtration. 1.
Washed with 2 dichloroethane. During filtration, white smoke of hydrogen bromide rose, and even after washing with 1.2 dichloroethane, a strong hydrogen bromide odor remained.
この濾取物を50 Qm1反応フラスコにいれ、5 Q
wt%硫酸234gを加え、90〜95℃。Put this filtered material into a 50 Qm1 reaction flask, and add 5 Qm
Add 234 g of wt% sulfuric acid and heat to 90-95°C.
10時間加熱攪拌した後、30℃まで冷却し析出生成物
を濾過、アセトン洗浄、乾燥して、スクアリン酸17.
3 gを得た。After heating and stirring for 10 hours, it was cooled to 30°C, and the precipitated product was filtered, washed with acetone, and dried to obtain squaric acid 17.
3 g was obtained.
収率93.4% HPLC純度99.1%比較例2゜
上記比較例101.2−ジクロルエタンの代わりにジク
ロルメタンを使用した以外は比較例1と同様に反応を行
い、常圧下、ジクロルメタンの沸点で臭素、臭化水素を
除去したが、生成物濾過時には、臭素、臭化水素臭が強
烈であった。Yield: 93.4% HPLC purity: 99.1% Comparative Example 2 Comparative Example 10 Above: The reaction was carried out in the same manner as Comparative Example 1 except that dichloromethane was used instead of 2-dichloroethane. Although bromine and hydrogen bromide were removed, there was a strong odor of bromine and hydrogen bromide when the product was filtered.
Claims (1)
と臭素とを水性液中で反応させ、生成した4−ブロモ−
3−ヒドロキシ−3−シクロブテンジオンを加水分解す
ることを特徴とするスクアリン酸の製造方法。4-bromo-produced by reacting 3-hydroxy-3-cyclobutenedione or its salts with bromine in an aqueous liquid
A method for producing squaric acid, which comprises hydrolyzing 3-hydroxy-3-cyclobutenedione.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12629888A JPH01299245A (en) | 1988-05-24 | 1988-05-24 | Production of squalic acid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12629888A JPH01299245A (en) | 1988-05-24 | 1988-05-24 | Production of squalic acid |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01299245A true JPH01299245A (en) | 1989-12-04 |
Family
ID=14931743
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP12629888A Pending JPH01299245A (en) | 1988-05-24 | 1988-05-24 | Production of squalic acid |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01299245A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5118861A (en) * | 1990-02-26 | 1992-06-02 | Lonza Ltd. | 3-hydroxy-2-cyclobuten-1-one salts, their production and use |
JP2006282542A (en) * | 2005-03-31 | 2006-10-19 | Fuji Photo Film Co Ltd | Manufacturing method of croconic acid or salt thereof |
-
1988
- 1988-05-24 JP JP12629888A patent/JPH01299245A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5118861A (en) * | 1990-02-26 | 1992-06-02 | Lonza Ltd. | 3-hydroxy-2-cyclobuten-1-one salts, their production and use |
JP2006282542A (en) * | 2005-03-31 | 2006-10-19 | Fuji Photo Film Co Ltd | Manufacturing method of croconic acid or salt thereof |
JP4531610B2 (en) * | 2005-03-31 | 2010-08-25 | 富士フイルム株式会社 | Method for producing croconic acid or a salt thereof |
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