JPH01197476A - Production of aromatic polycarboxylic acid anhydride - Google Patents
Production of aromatic polycarboxylic acid anhydrideInfo
- Publication number
- JPH01197476A JPH01197476A JP2008588A JP2008588A JPH01197476A JP H01197476 A JPH01197476 A JP H01197476A JP 2008588 A JP2008588 A JP 2008588A JP 2008588 A JP2008588 A JP 2008588A JP H01197476 A JPH01197476 A JP H01197476A
- Authority
- JP
- Japan
- Prior art keywords
- acid
- wet crystals
- raw material
- diphenyl sulfone
- tetracarboxylic acid
- 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 6
- 150000008065 acid anhydrides Chemical class 0.000 title description 10
- 125000003118 aryl group Chemical group 0.000 title description 5
- 239000013078 crystal Substances 0.000 claims abstract description 16
- GTDPSWPPOUPBNX-UHFFFAOYSA-N ac1mqpva Chemical compound CC12C(=O)OC(=O)C1(C)C1(C)C2(C)C(=O)OC1=O GTDPSWPPOUPBNX-UHFFFAOYSA-N 0.000 claims description 4
- 239000002994 raw material Substances 0.000 abstract description 6
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 abstract description 3
- 239000003795 chemical substances by application Substances 0.000 abstract description 3
- 229910017604 nitric acid Inorganic materials 0.000 abstract description 3
- 239000004642 Polyimide Substances 0.000 abstract description 2
- CMMUKUYEPRGBFB-UHFFFAOYSA-L dichromic acid Chemical compound O[Cr](=O)(=O)O[Cr](O)(=O)=O CMMUKUYEPRGBFB-UHFFFAOYSA-L 0.000 abstract description 2
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 abstract description 2
- 229920001721 polyimide Polymers 0.000 abstract description 2
- 235000010290 biphenyl Nutrition 0.000 abstract 3
- 239000004305 biphenyl Substances 0.000 abstract 3
- 125000006267 biphenyl group Chemical group 0.000 abstract 3
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N phenylbenzene Natural products C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 abstract 3
- 150000001875 compounds Chemical class 0.000 abstract 2
- 230000001590 oxidative effect Effects 0.000 abstract 2
- 238000006467 substitution reaction Methods 0.000 abstract 2
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- 238000010438 heat treatment Methods 0.000 description 10
- WFDIJRYMOXRFFG-UHFFFAOYSA-N Acetic anhydride Chemical compound CC(=O)OC(C)=O WFDIJRYMOXRFFG-UHFFFAOYSA-N 0.000 description 9
- 239000002904 solvent Substances 0.000 description 9
- 230000018044 dehydration Effects 0.000 description 7
- 238000006297 dehydration reaction Methods 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- ZHBXLZQQVCDGPA-UHFFFAOYSA-N 5-[(1,3-dioxo-2-benzofuran-5-yl)sulfonyl]-2-benzofuran-1,3-dione Chemical compound C1=C2C(=O)OC(=O)C2=CC(S(=O)(=O)C=2C=C3C(=O)OC(C3=CC=2)=O)=C1 ZHBXLZQQVCDGPA-UHFFFAOYSA-N 0.000 description 6
- 238000002844 melting Methods 0.000 description 6
- 230000008018 melting Effects 0.000 description 6
- 239000002253 acid Substances 0.000 description 4
- 150000008064 anhydrides Chemical class 0.000 description 4
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 3
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 238000009835 boiling Methods 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- CPELXLSAUQHCOX-UHFFFAOYSA-N Hydrogen bromide Chemical compound Br CPELXLSAUQHCOX-UHFFFAOYSA-N 0.000 description 2
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 2
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 2
- 238000001816 cooling Methods 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
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 description 1
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 150000001735 carboxylic acids Chemical class 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- BZRRQSJJPUGBAA-UHFFFAOYSA-L cobalt(ii) bromide Chemical compound Br[Co]Br BZRRQSJJPUGBAA-UHFFFAOYSA-L 0.000 description 1
- 238000004040 coloring Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- SBZXBUIDTXKZTM-UHFFFAOYSA-N diglyme Chemical compound COCCOCCOC SBZXBUIDTXKZTM-UHFFFAOYSA-N 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 229910000042 hydrogen bromide Inorganic materials 0.000 description 1
- 229940071125 manganese acetate Drugs 0.000 description 1
- UOGMEBQRZBEZQT-UHFFFAOYSA-L manganese(2+);diacetate Chemical compound [Mn+2].CC([O-])=O.CC([O-])=O UOGMEBQRZBEZQT-UHFFFAOYSA-L 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000001953 recrystallisation Methods 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
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
- AGGKEGLBGGJEBZ-UHFFFAOYSA-N tetramethylenedisulfotetramine Chemical compound C1N(S2(=O)=O)CN3S(=O)(=O)N1CN2C3 AGGKEGLBGGJEBZ-UHFFFAOYSA-N 0.000 description 1
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、芳香族ポリカルボン酸無水物、更に詳しくは
、ポリイミド、ポリアミド、ポリエステル等の原料とし
て有用な芳香族ポリカルボン酸無水物であるジフェニル
スルホン−3,3=、4゜4−一テトラカルボン酸二無
水物の製造方法に関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to an aromatic polycarboxylic anhydride, more specifically, an aromatic polycarboxylic anhydride useful as a raw material for polyimide, polyamide, polyester, etc. The present invention relates to a method for producing diphenylsulfone-3,3=,4°4-1-tetracarboxylic dianhydride.
[従来の技術]
従来、芳香族ポリカルボン酸無水物の製造方法としでは
、無水酢酸を用いて無水化する方法、融解して脱水する
方法、ジフェニルエーテル等の溶媒中で脱水する湿式熱
脱水法等が知られている。[Prior Art] Conventionally, methods for producing aromatic polycarboxylic acid anhydrides include anhydration using acetic anhydride, melting and dehydration, and wet thermal dehydration in a solvent such as diphenyl ether. It has been known.
しかしながら、これらの方法は、いずれも夫々問題点を
有してあり、満足し得るものではない。However, all of these methods have their own problems and are not satisfactory.
即ら、無水酢酸を用いる方法では得られた酸無水物中に
は酢酸が残存し、斯かる酸無水物を原料として各種の誘
導体を製造した場合には、当該残存している酢酸が悪影
響を及ぼす傾向にある。又、一般に、芳香族ポリカルボ
ン酸の融点は高く、融解脱水して得られる酸無水物が着
色するため、別途、精製工程を必要とする。更に、湿式
熱脱水法(米国特許第3,106.568)では、22
0°C以上の高温を要し、かつ用いる高沸点溶媒を酸無
水物から除去することが困難であるため、生成物をベン
ゼン等の低沸点溶媒により洗浄する必要がある等工程が
煩雑どなる。That is, in the method using acetic anhydride, acetic acid remains in the obtained acid anhydride, and when various derivatives are manufactured using such acid anhydride as a raw material, the remaining acetic acid may have an adverse effect. It tends to affect Furthermore, aromatic polycarboxylic acids generally have a high melting point, and the acid anhydride obtained by melting and dehydration is colored, requiring a separate purification step. Furthermore, in the wet thermal dehydration method (U.S. Pat. No. 3,106.568), 22
Since a high temperature of 0° C. or higher is required and it is difficult to remove the high boiling point solvent used from the acid anhydride, the process becomes complicated, such as the need to wash the product with a low boiling point solvent such as benzene.
[発明が解決しようとする課題] 本発明者らは、ジフェニルスルホン−3,3”。[Problem to be solved by the invention] We used diphenylsulfone-3,3''.
4.4−−テトラカルボン酸く以下rDsTcJと略称
する。)を無水化して、ジフェニルスルホン−3,3′
,4,4−−テトラカルボン酸二無水物(以下rDSD
AJと略称する。)を製造するに際し、高価な無水酢酸
等の脱水剤を用いることなく経済的で、生成物の着色が
少なく、工業的に有利な製造方法を開発すべく鋭意検討
の結果、DSTCは他のポリカルボン酸と異な、す、特
に無水化するための特殊な工程を必要とせず、単に当該
含水湿結晶を比較的低温で加熱脱水することにより無水
化し得ることを見い出した。4.4--Tetracarboxylic acid is hereinafter abbreviated as rDsTcJ. ) to anhydride to give diphenylsulfone-3,3'
,4,4-tetracarboxylic dianhydride (rDSD)
It will be abbreviated as AJ. ).As a result of intensive research to develop an industrially advantageous manufacturing method that is economical, does not require the use of expensive dehydrating agents such as acetic anhydride, and has little coloring of the product, DSTC It has been found that unlike carboxylic acids, it is possible to anhydride the hydrous wet crystals by simply heating and dehydrating them at a relatively low temperature without requiring any special process for anhydration.
本発明は、斯かる知見に基づいてなされたものであって
、新規で工業的に有用なりSDAの製造方法を提供する
ことを目的とする。The present invention was made based on this knowledge, and an object of the present invention is to provide a novel and industrially useful method for producing SDA.
[課題を解決するための手段]
本発明に係るDSDAの製造方法は、DSTCの含水湿
結晶を加熱脱水することを特徴とする。[Means for Solving the Problems] The method for producing DSDA according to the present invention is characterized by heating and dehydrating hydrated wet crystals of DSTC.
本発明に係るDSTCは、例えば、対応するメチル置換
体を硝酸酸化又は重クロム酸酸化あるいは接触空気酸化
することにより得られる。The DSTC according to the present invention can be obtained, for example, by subjecting the corresponding methyl substituted product to nitric acid oxidation, dichromic acid oxidation, or catalytic air oxidation.
このDSTCは、含水湿結晶の形態で用いられることか
必要であって、具体的には、水を含む反応系から得られ
たものはそのままで、又、水を含まない系から得られた
ものは水を含む溶媒で再結晶した後に原料として用いら
れる。This DSTC must be used in the form of water-containing wet crystals, and specifically, those obtained from a reaction system containing water can be used as is, and those obtained from a reaction system that does not contain water can be used directly. is used as a raw material after being recrystallized in a water-containing solvent.
斯かる再結晶溶媒は、所定の効果を奏する限りその種類
並びに当該溶媒の含水率は特に限定されない。適当な溶
媒としては、酢酸、ギ酸、メタノール、イソプロパツー
ル、アセトン、メチルエチルケトン、テトラヒドロフラ
ン、ジオキサン、ジグライム等の水と相溶する溶媒が例
示される。The type of such recrystallization solvent and the water content of the solvent are not particularly limited as long as the desired effect is achieved. Suitable solvents include water-compatible solvents such as acetic acid, formic acid, methanol, isopropanol, acetone, methyl ethyl ketone, tetrahydrofuran, dioxane, and diglyme.
湿結晶中の含水率は、湿式換算で5〜80重量%程度が
好ましく、特に10〜60重徂%程度が推奨される。こ
れより少ないと所定の無水化が進行し難く、一方、多い
場合には脱水に長時間を要し、工業的に不利となる傾向
におる。The water content in the wet crystals is preferably about 5 to 80% by weight in wet terms, particularly about 10 to 60% by weight. If the amount is less than this, it will be difficult to achieve the desired level of dehydration, while if it is more than this, it will take a long time for dehydration, which tends to be industrially disadvantageous.
加熱温度としては、好ましくは110〜250°C程度
、特に150〜230’C程度が推奨される。The heating temperature is preferably about 110 to 250°C, particularly about 150 to 230'C.
この温度より低いと脱水速度が遅く経済的に不利であり
、これより高いと生成物が着色する傾向におる。If the temperature is lower than this, the dehydration rate is slow and it is economically disadvantageous; if the temperature is higher than this, the product tends to be colored.
加熱下における圧力条件としては、常圧下又は減圧下で
あることが好ましく、特に減圧下においては加熱時間を
短縮することができるため推奨される。The pressure conditions during heating are preferably normal pressure or reduced pressure, and reduced pressure is particularly recommended because the heating time can be shortened.
加熱時間は、DSTCの含水率により適宜選択し得るも
のの、通常、1〜20時間程間抜おる。Although the heating time can be appropriately selected depending on the water content of DSTC, it is usually about 1 to 20 hours.
加熱は、DSTCを静置した状態で行なってもよいし、
かきまぜながら又は流動させながら行なってもよい。Heating may be performed with the DSTC standing still, or
It may be carried out while stirring or flowing.
[実施例] 以下に実施例を掲げ、本発明の詳細な説明する。[Example] The present invention will be described in detail below with reference to Examples.
実施例1
3.3−.4,4−−テトラメチルジフェニルスルホン
137g(0,5モル〉を、臭化コバルトを20ミリモ
ル、酢酸マンガン5ミリモル及び臭化水素20ミリモル
を夫々含有する11の酢酸溶液に加え、空気圧50に3
/ctA下、180℃で1時間反応した。冷却後、析出
したDSTCの結晶を濾別し、水から再結晶した。40
重量%の水を含有する湿結晶1009をステンレス製の
皿に入れ、1〜2 mm Hgの減圧下、180’Cで
3時間加熱脱水して54.0gのDSDAを得た。この
ものの無水酸量は99.7%、融点は287°C(文献
値286〜287°C)であった。Example 1 3.3-. 137 g (0.5 mol) of 4,4-tetramethyldiphenylsulfone were added to an acetic acid solution containing 20 mmol of cobalt bromide, 5 mmol of manganese acetate, and 20 mmol of hydrogen bromide, respectively, at an air pressure of 50 ml.
/ctA at 180°C for 1 hour. After cooling, the precipitated DSTC crystals were filtered off and recrystallized from water. 40
Wet crystal 1009 containing % by weight of water was placed in a stainless steel dish and dehydrated by heating at 180'C for 3 hours under reduced pressure of 1 to 2 mm Hg to obtain 54.0 g of DSDA. The acid anhydride content of this product was 99.7%, and the melting point was 287°C (literature value 286-287°C).
ここで、上記の無水酸量(%)は、DSDAの理論仝酸
価に対する、[2×(生成物の仝酸価−生成物の土酸価
)]の百分率を算出して求めた。Here, the above acid anhydride amount (%) was determined by calculating the percentage of [2×(hydric acid value of product - earth acid value of product)] with respect to the theoretical acid value of DSDA.
実施例2
実施例1で得たDSTAの湿結晶100gを1〜2Ir
unHgの減圧下、200℃で1時間加熱脱水して53
.89のDSDAを得た。このものの無水酸量は99.
8%、融点は287℃であった。Example 2 100 g of wet crystals of DSTA obtained in Example 1 were mixed with 1 to 2 Ir.
Dehydrated by heating at 200°C for 1 hour under reduced pressure of unHg.
.. A DSDA of 89 was obtained. The amount of acid anhydride in this product is 99.
8%, and the melting point was 287°C.
実施例3
3.3−.4.4”−テトラメチルジフェニルスルホン
137g(0,5モル)に60%硝酸を525g加え、
加圧下、200 ’Cで6時間反応した。冷却後、析出
したDSTCの結晶を濾別し、その1多、よく水で洗浄
した。得られた結晶は、水を50重倒%含んでいた。こ
の湿結晶1009を1〜2IwnHQの減圧下、180
’Cで4時間加熱脱水して44.59のDSDAを得た
。このものの無水Mfflは99.5%、融点は287
℃であった。Example 3 3.3-. 4. Add 525 g of 60% nitric acid to 137 g (0.5 mol) of 4”-tetramethyldiphenylsulfone,
The reaction was carried out under pressure at 200'C for 6 hours. After cooling, the precipitated DSTC crystals were filtered off and washed thoroughly with water. The obtained crystals contained 50% water by weight. This wet crystal 1009 was heated to 180 mL under reduced pressure of 1 to 2 IwnHQ.
The mixture was dehydrated by heating at 100°C for 4 hours to obtain a DSDA of 44.59. This product has an anhydrous Mffl of 99.5% and a melting point of 287.
It was ℃.
比較例1
実施例1で得たDSTCの湿結晶100gを常圧下、1
00℃で6時間乾燥し、含水率2重量%のDSTCを6
”l得た。このものを1〜2 mm Hqの減圧下、1
80’Cで3時間加熱した。得られたものの無水酸量は
2.5%であった。Comparative Example 1 100 g of wet crystals of DSTC obtained in Example 1 were mixed under normal pressure for 1
After drying at 00°C for 6 hours, DSTC with a moisture content of 2% by weight was
"l" was obtained.
Heated at 80'C for 3 hours. The amount of acid anhydride in the obtained product was 2.5%.
[発明の効果]
本発明に係る方法により、高価な脱水剤や高沸点の溶剤
を用いることなく、容易に、かつ安価にDSDAを得る
ことができる。[Effects of the Invention] According to the method of the present invention, DSDA can be obtained easily and inexpensively without using expensive dehydrating agents or high-boiling point solvents.
特許出願人 新日本理化株式会社Patent applicant: Shin Nihon Rika Co., Ltd.
Claims (1)
カルボン酸二無水物を製造するに際し、ジフェニルスル
ホン−3,3′,4,4′−テトラカルボン酸の含水湿
結晶を加熱脱水することを特徴とするジフェニルスルホ
ン−3,3′,4,4′−テトラカルボン酸二無水物の
製造方法。1. When producing diphenylsulfone-3,3',4,4'-tetracarboxylic dianhydride, the hydrous wet crystals of diphenylsulfone-3,3',4,4'-tetracarboxylic acid are heated and dehydrated. A method for producing diphenylsulfone-3,3',4,4'-tetracarboxylic dianhydride, characterized in that:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2008588A JPH01197476A (en) | 1988-01-30 | 1988-01-30 | Production of aromatic polycarboxylic acid anhydride |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2008588A JPH01197476A (en) | 1988-01-30 | 1988-01-30 | Production of aromatic polycarboxylic acid anhydride |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01197476A true JPH01197476A (en) | 1989-08-09 |
JPH059434B2 JPH059434B2 (en) | 1993-02-04 |
Family
ID=12017267
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2008588A Granted JPH01197476A (en) | 1988-01-30 | 1988-01-30 | Production of aromatic polycarboxylic acid anhydride |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01197476A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5047560A (en) * | 1989-10-06 | 1991-09-10 | Hitachi, Ltd. | Process for producing highly pure 3,3',4,4'-biphenyltetracarboxylic acid or dianhydride thereof |
JP2005132772A (en) * | 2003-10-30 | 2005-05-26 | New Japan Chem Co Ltd | Method for producing diphenylsulfonetetracarboxylic acid dianhydride |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP6171160B2 (en) | 2015-07-10 | 2017-08-02 | 株式会社アクトメント | Nail corrector |
-
1988
- 1988-01-30 JP JP2008588A patent/JPH01197476A/en active Granted
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5047560A (en) * | 1989-10-06 | 1991-09-10 | Hitachi, Ltd. | Process for producing highly pure 3,3',4,4'-biphenyltetracarboxylic acid or dianhydride thereof |
JP2005132772A (en) * | 2003-10-30 | 2005-05-26 | New Japan Chem Co Ltd | Method for producing diphenylsulfonetetracarboxylic acid dianhydride |
JP4622233B2 (en) * | 2003-10-30 | 2011-02-02 | 新日本理化株式会社 | Method for producing diphenylsulfonetetracarboxylic dianhydride |
Also Published As
Publication number | Publication date |
---|---|
JPH059434B2 (en) | 1993-02-04 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JPS61293949A (en) | Optical resolution of alpha-isopropyl-p-chlorophenylacetic acid | |
JPS582222B2 (en) | Production method of aromatic polycarboxylic acid | |
JPH01165544A (en) | Partially fluorinated carboxylic acid and its derivative, its production and use | |
JPH01197476A (en) | Production of aromatic polycarboxylic acid anhydride | |
JP3747493B2 (en) | Process for producing alicyclic polycarboxylic acid and acid anhydride thereof | |
JPH031313B2 (en) | ||
JP2509704B2 (en) | Method for producing high-purity 5,5 '-[2,2,2-trifluoro-1- (trifluoromethyl) -ethylidene] bis-1,3-isobenzofurandione | |
JP4048689B2 (en) | Method for producing 3,3 ', 4,4'-biphenyltetracarboxylic dianhydride | |
JP3608354B2 (en) | Dicyclohexyl-2,3,3 ', 4'-tetracarboxylic acid compound | |
JPH0610158B2 (en) | Method for producing 3-fluorobenzoic acids | |
JPH0696570B2 (en) | Method for producing biphenyltetracarboxylic dianhydride | |
JPH03215455A (en) | Production of aromatic bisanilines | |
JPS5914015B2 (en) | Method for producing 3,3',4,4'-biphenyltetracarboxylic acid salt | |
SU648096A3 (en) | Method of obtaining n-(6-acyloxybenzothiazol-2-yl)-n,-phenyl or substituted phenylurea of formula 1 | |
JPH06211744A (en) | Production of high-purity dimethyl 4,4'-biphenyldicarboxylate | |
JPH02149539A (en) | Alicyclic tetracarboxylic acid and derivative thereof | |
JPH0337551B2 (en) | ||
JP4386153B2 (en) | Crystallization method of acid dianhydride | |
JPS6019903B2 (en) | Maleimide and its manufacturing method | |
JP2000281682A (en) | Alicyclic tetracarboxylic dianhydride and its production | |
JP2611289B2 (en) | Method for producing polyamic acid or polyamic acid ester | |
JPH04264050A (en) | Method for purifying 2,6-naphthalenedicarboxylic acid | |
JPS6183158A (en) | Preparation of n,n'-m-phenylenebismaleimide | |
JPS5822112B2 (en) | Method for producing N-(hydroxyphenyl)maleimides | |
JPS61151183A (en) | Production of 1,2,3,4-butanetetracarboxylic acid dianhydride |