JPH03200741A - Production of hydroxynaphthalenecarboxylic acids - Google Patents

Production of hydroxynaphthalenecarboxylic acids

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Publication number
JPH03200741A
JPH03200741A JP33820289A JP33820289A JPH03200741A JP H03200741 A JPH03200741 A JP H03200741A JP 33820289 A JP33820289 A JP 33820289A JP 33820289 A JP33820289 A JP 33820289A JP H03200741 A JPH03200741 A JP H03200741A
Authority
JP
Japan
Prior art keywords
hydroxynaphthalene
carboxylic acid
naphthol
salt
carbon dioxide
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
Application number
JP33820289A
Other languages
Japanese (ja)
Inventor
Takehisa Nakanishi
中西 武久
Toshisumi Miura
三浦 俊澄
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP33820289A priority Critical patent/JPH03200741A/en
Publication of JPH03200741A publication Critical patent/JPH03200741A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To obtain 2-hydroxynaphthalene-3-carboxylic acid and 2- hydroxynaphthalene-6-carboxylic acid under a mild condition in high selectivity by reacting alkali metallic salt of 2-naphthol with carbon dioxide in a specific organic phoshine oxide as a solvent. CONSTITUTION:An alkali metallic salt of 2-naphthol is reacted with carbon dioxide in a solvent of one or more organic phoshine oxides shown by the formula (R1 to R3 are 1-8C alkyl, phenyl and preferably R1=R2=R3) preferably at 100-220 deg.C to give 2-hydroxynaphthalene-3-carboxylic acid and 2- hydroxynaphthalene-6-carboxylic acid useful as a dye intermediate or a wholly aromatic polyester-based raw material in high selectively, economically and advantageously in the same manner whether the alkali metallic salt of the raw material is sodium salt or potassium salt.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、ナフタレンヒドロキシカルボン酸の製造法に
関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing naphthalene hydroxycarboxylic acid.

〔従来の技術〕[Conventional technology]

従来、ナフトール類の二酸化炭素によるカルボキシル化
方法としては、2−ナフトールのナトリウム塩の無水物
の固体と二酸化炭素を130℃で反応させることにより
2−ヒドロキシナフタレン−1−カルボン酸く以下、2
.1−11N^と略記する〉が得られ230〜240℃
で反応させることにより2.ヒドロキシナフタレン−3
−カルボン酸(以下、2.3−11NAと略記する)が
得られる。また、カリウム塩の無水物の固体と二酸化炭
素を200℃で反応させることにより2−ヒドロキシナ
フタレン−6−カルボン酸(以下、2.6−11N^と
略記する)が60χの選択率で得られる。このことは、
堀口 博「実験有機合成論」上巻543頁に記載されて
いる。また、非プロトン性極性溶媒として、ジメチルス
ルホキシド、ジメチルフォルムアミド、ピリジン、ジオ
キサン、ニトロベンゼンを用いる方法(日本化学会誌、
1989(7) 1164頁)が山口等により検討され
ている、彼らは、無水のカリウム塩を用い80℃で2.
1−11N^を収率46〜77!で得ている。
Conventionally, as a method for carboxylating naphthols with carbon dioxide, 2-hydroxynaphthalene-1-carboxylic acid, 2-hydroxynaphthalene-1-carboxylic acid, etc.
.. 1-11N^ was obtained at 230-240°C.
By reacting with 2. Hydroxynaphthalene-3
-carboxylic acid (hereinafter abbreviated as 2.3-11NA) is obtained. In addition, 2-hydroxynaphthalene-6-carboxylic acid (hereinafter abbreviated as 2.6-11N^) can be obtained with a selectivity of 60χ by reacting a solid potassium salt anhydride with carbon dioxide at 200°C. . This means that
It is described in Hiroshi Horiguchi's "Experimental Organic Synthesis" Volume 1, page 543. In addition, a method using dimethyl sulfoxide, dimethyl formamide, pyridine, dioxane, or nitrobenzene as an aprotic polar solvent (Journal of the Chemical Society of Japan,
1989 (7) p. 1164) was reviewed by Yamaguchi et al., who used anhydrous potassium salt at 80°C for 2.
Yield 46-77 for 1-11N^! I am getting it from

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

しかし、上述した従来の方法では、無水のカリラム塩の
固体との反応では反応温度が高く、且つ反応が15時間
以上かかるという問題があり、また、極1生溶媒を用い
る反応では有用性の高い2.3−11NAまたは2.6
−11NAの選択性は102以下である。
However, in the conventional method described above, there are problems in that the reaction temperature is high and the reaction takes more than 15 hours when reacting anhydrous kalirum salt with a solid. 2.3-11NA or 2.6
-11NA has a selectivity of 102 or less.

c問題点を解決するための手段〕 本発明は、前記課題を解決するため鋭意明文を行った結
果、有機フメスフィンオキン1′溶媒中で2−ナフト−
ルのナトリウム塩またはカリ1シム塩を二酸化炭素と反
応さ・吐るごとに上り2,311N^及び2、G−11
N八を、より温和な条件で高選択率で得られることを見
出し、本発明を完成さlたものである。ずなわら、本発
明は、下記−・船人(1)で表される41機フォスフィ
ンオ二トシドの一神またも、L二捕以上の71L合物を
溶媒として、2−ナフト−ルのアルカリ金属塩と二酸化
炭素との反応を行うことを1、!酸とする2−ヒドロキ
シナフタレン−3−カルボン酸及び2−ヒドロキシナフ
タレン−6−カルボン酸の製造法である。
Means for Solving Problems c] As a result of extensive efforts to solve the above-mentioned problems, the present invention has been achieved by producing 2-naphtho-2-naphtho-
2,311 N^ and 2, G-11 of sodium salt or potassium salt reacts with carbon dioxide.
The present invention was completed by discovering that N8 can be obtained with high selectivity under milder conditions. In addition, the present invention is directed to the use of an alkali of 2-naphthol using a 71L compound having two or more L compounds as a solvent. 1, to perform a reaction between a metal salt and carbon dioxide! This is a method for producing 2-hydroxynaphthalene-3-carboxylic acid and 2-hydroxynaphthalene-6-carboxylic acid as acids.

(R,、R1,及びR1は炭素数4〜8のアル・1−ル
丞、またはフェニル基を示す)。
(R, , R1, and R1 each represent an alkyl group having 4 to 8 carbon atoms or a phenyl group).

本発明に用いる有機フォスフインオキシ1′と【上(R
0R5及びR1は炭素数4〜Bのアルキル凸、またはフ
ェニル基を示し、互いに同一・でも異なっていてもよい
)で表される。
Organic phosphineoxy 1' used in the present invention and [upper (R
0R5 and R1 represent a convex alkyl group having 4 to B carbon atoms or a phenyl group, and may be the same or different from each other.

具体的には、トリー〇−プチルフAスフィンオートシト
、トリセカンダリ−ブチルフォスフインオキシド、トリ
ーn−ヘキシルフォスフインオキシド、トリーn−オク
チルフォスフインオキシド、トリフェニルフォスフイン
オキシド等が挙げられる。
Specific examples include tri0-butylphosphine oxide, tri-butylphosphine oxide, tri-n-hexylphosphine oxide, tri-n-octylphosphine oxide, triphenylphosphine oxide, and the like.

好ましくは、−船人(1)において、R,、)?、、及
びR,が互いに同一である炭素数4〜8のトリアルキル
フォスフインオキシド、あるいはトリフェニルフォスフ
インオキシドである。
Preferably, in -Sailor (1), R,, )? , , and R are the same as each other, a trialkylphosphine oxide having 4 to 8 carbon atoms, or a triphenylphosphine oxide.

これら有機フォスフインオキシドは反応に際し、溶媒と
して単独であるいは二種以上の混合物とし°C用いるこ
とが出来る。
These organic phosphine oxides can be used as a solvent alone or in a mixture of two or more at °C during the reaction.

また、2−ナフトールのアルカリ金属塩は、アルカリ金
属塩がカリウムであっても、ナトリウムであっ°ζも高
い選択率で2.3−11NA 、 2.(i−11N^
を与える。
In addition, even if the alkali metal salt of 2-naphthol is potassium or sodium, it has a high selectivity of 2.3-11NA. (i-11N^
give.

使用する2−ナフトールのアルカリ金属塩は種々の方法
で得ることができる0例えば、2−ナフトールに当量の
水酸化アルカリ金属水溶液を加え、蒸発乾固した後、真
空下に実質的に無水物を生成する方法、更に好ましくは
、有81溶媒に2−ナフI−−ルを溶解し、水酸化アル
カリ金属水溶液により中和した後、有機溶媒を留去する
ことにより適切な−)°トリウム塩が得られる。
The alkali metal salt of 2-naphthol used can be obtained in various ways.For example, an equivalent amount of aqueous alkali metal hydroxide solution is added to 2-naphthol, evaporated to dryness, and then the substantially anhydrous salt is prepared under vacuum. More preferably, a suitable -)° thorium salt is produced by dissolving 2-naph I-- in a solvent, neutralizing it with an aqueous alkali metal hydroxide solution, and then distilling off the organic solvent. can get.

2〜ナフトールのアルカリ金属塩は前記有機フォスフイ
ンオキシドに高濃度で溶解するため、カル、1ξキンル
化が迅速に進むものと考えられる。
Since the alkali metal salt of 2 to naphthol is dissolved in the organic phosphine oxide at a high concentration, it is thought that the quinlation of cal and 1ξ proceeds rapidly.

好ましい反応温度は、100〜220°Cである。反応
温度が100°Cより低いと、アルカリ金属塩の転化率
が低下し、220’Cを越えると不純物の副4Iが署し
くなる。
The preferred reaction temperature is 100-220°C. When the reaction temperature is lower than 100°C, the conversion rate of the alkali metal salt decreases, and when it exceeds 220°C, the impurity sub-4I becomes significant.

反応時間は特に阻止されないが、一般に反1.61−r
間を延ばずことによっ゛(転化率を、;fiめることが
できる0反応時間は、原料、溶媒の種類、反応温度によ
り変わるが、例えば、反応温度+50 ’C′r:4:
112時間以内に反応は完結する。
The reaction time is not particularly limited, but generally anti-1.61-r
The conversion rate can be reduced by not prolonging the reaction time. The reaction time varies depending on the raw materials, the type of solvent, and the reaction temperature, but for example, reaction temperature + 50'C'r: 4:
The reaction is complete within 112 hours.

二酸化炭素の量は本反応が起こるのに必要な化学量論量
以上供給すれば良い。
The amount of carbon dioxide may be supplied in a stoichiometric amount or more necessary for this reaction to occur.

反応方法としては、原料のアルカリ金属塩を反応溶媒に
溶解して二酸化炭素を化学M論量吸収させてから昇温し
てカルボキシル化反応を生起させても良いし、原料溶液
を所定の反応温度に加熱した状態で二酸化炭素を吹き込
みながら反応を行っても良い。
As a reaction method, the alkali metal salt of the raw material may be dissolved in a reaction solvent to absorb a stoichiometric amount of carbon dioxide, and then the temperature may be raised to cause the carboxylation reaction, or the raw material solution may be heated to a predetermined reaction temperature. The reaction may be carried out while blowing carbon dioxide in a heated state.

反応は減圧下、常圧下、加圧下いずれでも実施でき、例
えば、二酸化炭素の加圧下で行う場合には、反応時間を
短縮することができる。この場合の二酸化炭素圧力は1
〜20kg/cdゲージ程度で充分である。叉、本反応
は、回分てもi!l!続でも行うことができる。
The reaction can be carried out under reduced pressure, normal pressure, or increased pressure. For example, when carried out under increased pressure of carbon dioxide, the reaction time can be shortened. In this case, the carbon dioxide pressure is 1
~20 kg/cd gauge is sufficient. For this reaction, even if it's a batch, it's i! l! It can also be done continuously.

〔実施例) 以下、本発明を実施例により更に具体的に説明する、な
お、原料および生成物は液体クロマトグラフ(充填剤ニ
ジリカゲル−〇4、溶離液ニアセトニトリル−水)によ
り分析した。
[Example] Hereinafter, the present invention will be described in more detail with reference to Examples. The raw materials and products were analyzed by liquid chromatography (filling material Nijirica gel-04, eluent Niacetonitrile-water).

実施例1 2−ナフトール29.8g(0,206+wol)に水
酸化ナトリウム8.7gを加え脱水し、実質上無水の原
料固体を得た。このようにして得られた無水のす1・1
Jウム塩を原料とし、撹拌機、二酸化炭素吹き込み管、
還流冷却器を備えた300dガラス製四っに1フラスコ
に入れ、溶媒として予めモレキュラシープで乾燥した無
水のトリブチルフォスフインオキシド(以下、TIIP
Oと略記する。 ) 180gを加え、攪拌下75°C
で溶解し、均一な液を得た0次いで常圧下75°Cに保
った状態で二酸化炭素を吹き込み充分吸収さセた後、同
様に二酸化炭素を吹き込みながら反応器の内温を180
°Cまで昇温し、3時間反応を行った。内温を80°C
まで冷却した後、反応マスに水200idを加えよく振
盪し、静置して水層とTOPO層とに分液後、それぞれ
を液体クロマトグラフにより分析した。
Example 1 8.7 g of sodium hydroxide was added to 29.8 g (0,206+wol) of 2-naphthol and dehydrated to obtain a substantially anhydrous raw material solid. Anhydrous 1.1 obtained in this way
Jum salt is used as raw material, stirrer, carbon dioxide blowing pipe,
Anhydrous tributylphosphine oxide (hereinafter referred to as TIIP), which had been previously dried with molecular sheep, was added as a solvent to a 300D glass quarter flask equipped with a reflux condenser.
It is abbreviated as O. ) Add 180g and stir at 75°C.
After dissolving and obtaining a homogeneous liquid, carbon dioxide was blown into the reactor while maintaining the temperature at 75°C under normal pressure to ensure sufficient absorption.
The temperature was raised to °C and the reaction was carried out for 3 hours. Internal temperature 80°C
After cooling, 200 id of water was added to the reaction mass, shaken well, allowed to stand, and separated into an aqueous layer and a TOPO layer, each of which was analyzed by liquid chromatography.

2−ナフトール転化率21%、2.3−11NA選択率
44%、2.[1−11NA選沢率50%を得た。その
他2.1−11N八が少量見出された。
2-naphthol conversion rate 21%, 2.3-11NA selectivity 44%, 2. [1-11NA selection rate of 50% was obtained. In addition, a small amount of 2.1-11N8 was found.

実施例2 原料塩を2−ナフトールナトリウム塩に代え°C実hN
例1と同J″Qな方法により得られた2−)・ソト−ル
カリウl、塩を用い、反応時間を1時間とした他は実施
例Iと同様に行った0分析の結果、2−ナフトール転化
率33%、2.311NA選択率34%、2.(i I
IN八選へ率63%であった。
Example 2 Raw material salt was replaced with 2-naphthol sodium salt °C actual hN
As a result of 0 analysis carried out in the same manner as in Example I, except that 2-).sotol potassium l obtained by the same method as in Example 1 and salt was used and the reaction time was 1 hour, 2- Naphthol conversion rate 33%, 2.311NA selectivity 34%, 2.(i I
The rate of passing the IN8 selection was 63%.

実施例3 溶媒をTIIIIOに代えトリオクチルツメスフィンオ
キシド(以下、TOPOと略記する。)を用い、反JI
L>時間を6時間とした他は実施例1と同様に11った
Example 3 Using trioctyltumesphine oxide (hereinafter abbreviated as TOPO) in place of TIIIO as a solvent,
Example 11 was carried out in the same manner as in Example 1 except that L>time was set to 6 hours.

分JJF c7) 結果、2− す71・−ル転化率1
4%、2.3−11NA選沢率62%、2.6−11N
A選択率29%であった。
min JJF c7) Result, 2-su71·-le conversion rate 1
4%, 2.3-11NA selection rate 62%, 2.6-11N
The A selection rate was 29%.

実施例4 反応温度を150°Cに変えた他は実施例1と同様に行
った0分析の結果、2−ナフトール転化率13%、2.
3−11NA選択率38%、2.(i−11NA !ベ
キ25%であった。その(1112,1−11N八が少
量見出された。
Example 4 A zero analysis conducted in the same manner as in Example 1 except that the reaction temperature was changed to 150°C revealed that the 2-naphthol conversion rate was 13%, 2.
3-11NA selectivity 38%, 2. (i-11NA! power was 25%. A small amount of (1112, 1-11N8) was found.

実施例5 実施例1で得られた無水のすトリウJ、Jムと乾燥した
Tl1l’0180gを内容積300rIrffiの5
O5−31(iL製のオートクレーブに入れ、180℃
に加熱した後、二酸化炭素を吹き込み、全圧をlokg
/eIiゲージに保らながら3時間反応を行った。内温
を80°Cまで冷却した後、反応マスに水200sff
iを加え振盪した後静置して、水層とTOPO層とに分
離した。 TIIPOWJには未反応の2−ナフトール
、2−ナフトールナトリウム塩及び少量の2.3−11
N^ナトリウム塩、2.6−11N^ナトリウム塩が含
まれていた。水層には各種のIIN^すトリウム塩が抽
出された0分析の結果、2−ナフトール転化率37%、
2.3−11NA選択率43%、2.(i−11NA選
択率48%であった。
Example 5 180 g of the anhydrous Sutriu J, Jmu and dried Tl1l' obtained in Example 1 were placed in a
O5-31 (Put in iL autoclave, 180℃
After heating to , blow in carbon dioxide and reduce the total pressure to
The reaction was carried out for 3 hours while maintaining the /eIi gauge. After cooling the internal temperature to 80°C, add 200sff of water to the reaction mass.
After adding i and shaking, the mixture was allowed to stand to separate into an aqueous layer and a TOPO layer. TIIPOWJ contains unreacted 2-naphthol, 2-naphthol sodium salt and a small amount of 2.3-11.
It contained N^sodium salt, 2.6-11N^sodium salt. Various IIN^thorium salts were extracted from the aqueous layer.As a result of analysis, the conversion rate of 2-naphthol was 37%,
2.3-11NA selectivity 43%, 2. (The i-11NA selectivity was 48%.

実施例6 溶媒をT 11110に代え1リフエニルフA・スフィ
ンオ・トシド(以下T 11110と略記する。)を用
い、反15時間を8特問とした他は実施例1と同様に行
った。
Example 6 The same procedure as in Example 1 was carried out, except that the solvent was replaced with T 11110 and 1 rifenylph A. sphinotoside (hereinafter abbreviated as T 11110) was used, and 8 special questions were used for 15 hours.

分析の結果、2−ナフトール転化率9%、2.3−11
NA選択率59%、2.6−11NA選沢率27%であ
った。
As a result of analysis, 2-naphthol conversion rate was 9%, 2.3-11
The NA selection rate was 59%, and the 2.6-11NA selection rate was 27%.

〔発明の効果〕〔Effect of the invention〕

本発明の方法によれば、染料中間体あるい(よ全芳香族
系ポリエステル系原料として有用なヒドロキシナフタレ
ンカルボン酸は、有機フォスフインオキシド溶媒中で反
応を行うことにより、原料に用いる2−ナフトールのア
ルカリ金属塩がす1リウム塩でもカリウム塩と同様に高
選択率で得ることができ、経済的に有利であり産業に利
するところ極めて大である。
According to the method of the present invention, hydroxynaphthalenecarboxylic acid, which is useful as a dye intermediate or a fully aromatic polyester raw material, can be obtained by reacting it in an organic phosphine oxide solvent. The monolium salt of the alkali metal salt can be obtained with high selectivity in the same way as the potassium salt, which is economically advantageous and extremely beneficial to industry.

Claims (1)

【特許請求の範囲】 下記一般式(1)で表される有機フォスフィンオキシド
の一種または二種以上の混合物を溶媒として、2−ナフ
トールのアルカリ金属塩と二酸化炭素との反応を行うこ
とを特徴とする2−ヒドロキシナフタレン−3−カルボ
ン酸及び2−ヒドロキシナフタレン−6−カルボン酸の
製造法。 一般式▲数式、化学式、表等があります▼(1) (R_1、R_2、及びR_3は炭素数4〜8のアルキ
ル基、またはフェニル基を示す)。
[Claims] The method is characterized by carrying out a reaction between an alkali metal salt of 2-naphthol and carbon dioxide using one or a mixture of two or more organic phosphine oxides represented by the following general formula (1) as a solvent. A method for producing 2-hydroxynaphthalene-3-carboxylic acid and 2-hydroxynaphthalene-6-carboxylic acid. General formula ▲ Numerical formula, chemical formula, table, etc. ▼ (1) (R_1, R_2, and R_3 represent an alkyl group having 4 to 8 carbon atoms or a phenyl group).
JP33820289A 1989-12-28 1989-12-28 Production of hydroxynaphthalenecarboxylic acids Pending JPH03200741A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33820289A JPH03200741A (en) 1989-12-28 1989-12-28 Production of hydroxynaphthalenecarboxylic acids

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33820289A JPH03200741A (en) 1989-12-28 1989-12-28 Production of hydroxynaphthalenecarboxylic acids

Publications (1)

Publication Number Publication Date
JPH03200741A true JPH03200741A (en) 1991-09-02

Family

ID=18315890

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33820289A Pending JPH03200741A (en) 1989-12-28 1989-12-28 Production of hydroxynaphthalenecarboxylic acids

Country Status (1)

Country Link
JP (1) JPH03200741A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007269717A (en) * 2006-03-31 2007-10-18 Ueno Technology:Kk Method for producing 2-hydroxynaphthalene-3,6-dicarboxylic acid

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007269717A (en) * 2006-03-31 2007-10-18 Ueno Technology:Kk Method for producing 2-hydroxynaphthalene-3,6-dicarboxylic acid

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