JPH0437839B2 - - Google Patents

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Publication number
JPH0437839B2
JPH0437839B2 JP59007050A JP705084A JPH0437839B2 JP H0437839 B2 JPH0437839 B2 JP H0437839B2 JP 59007050 A JP59007050 A JP 59007050A JP 705084 A JP705084 A JP 705084A JP H0437839 B2 JPH0437839 B2 JP H0437839B2
Authority
JP
Japan
Prior art keywords
reaction
thio
phosphorus
tris
alkali metal
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.)
Expired - Lifetime
Application number
JP59007050A
Other languages
Japanese (ja)
Other versions
JPS60152492A (en
Inventor
Iwahiro Ootsuka
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.)
AGC Inc
Original Assignee
Asahi Glass Co Ltd
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 Asahi Glass Co Ltd filed Critical Asahi Glass Co Ltd
Priority to JP705084A priority Critical patent/JPS60152492A/en
Publication of JPS60152492A publication Critical patent/JPS60152492A/en
Publication of JPH0437839B2 publication Critical patent/JPH0437839B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明は、フエノールのP位にニトロ基、アミ
ノ基、あるいはN−アシルアミノ基を有するP−
置換フエノールとオキシ塩化リンあるいはチオ塩
化リンとを反応させて対応するトリリン酸エステ
ルあるいはトリチオリン酸エステルを製造する方
法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides P-
The present invention relates to a method for producing a corresponding triphosphate or trithiophosphate by reacting a substituted phenol with phosphorus oxychloride or phosphorus thiochloride.

リン酸エステルあるいはトリチオリン酸エステ
ル(以下両者をまとめて(チオ)リン酸エステル
という)は合成樹脂原料、難燃剤、農薬あるいは
その中間体として有用な化合物である。特にトリ
ス(P−アミノフエニル)(チオ)リン酸エステ
ルはポリウレタン等の原料として有用なトリス
(P−イソシアネートフエニル)(チオ)リン酸エ
ステルの中間体として有用である。このトリス
(P−アミノフエニル)(チオ)リン酸エステルは
トリフエニル(チオ)リン酸エステルを合成しこ
れをニトロ化し、次いで還元して対応するアミン
にする方法やP−ニトロフエノールのナトリウム
塩を合成しこれを高温でオキシ塩化リンあるいは
チオ塩化リンと反応させて対応するニトロ化合物
を製造しこれを還元する方法で製造されるが、ま
たP−置換フエノールとオキシ塩化リンあるいは
チオ塩化リンをアルカリ存在下に直接反応させて
製造する方法も知られている。たとえば特公昭57
−25559号公報には (X:ニトロ基、アミノ基、あるいはN−アシル
アミノ基)で表わされるP−置換フエノールとオ
キシ塩化リンあるいはチオ塩化リンとをアルカリ
金属水酸化物あるいは炭酸塩、水、および低級脂
肪族ケトンの存在下に反応させて対応するトリス
(P−置換フエニル)(チオ)リン酸エステルを製
造する方法が記載されている。しかしながら、こ
の方法は水存在下の反応であるので原料や反応中
間体が加水分解を受け易く、収率を充分に高める
ことが困難であつた。即ち、オキシ塩化リンある
いはチオ塩化リン、および反応中間体であるモノ
あるいはジエステルはそれに含まれるリン原子に
結合した塩素原子が加水分解により脱離し易く、
トリエステルの収率が不充分となり易いものであ
つた。上記公報記載の発明ではこの加水分解を防
ぐためにアルカリの濃度を規定しているが、加水
分解を完全には抑制することはできないものであ
つた。
Phosphoric acid esters or trithiophosphoric acid esters (hereinafter both are collectively referred to as (thio)phosphoric acid esters) are useful compounds as raw materials for synthetic resins, flame retardants, agricultural chemicals, or intermediates thereof. In particular, tris(P-aminophenyl)(thio)phosphate is useful as an intermediate for tris(P-isocyanatephenyl)(thio)phosphate, which is useful as a raw material for polyurethane and the like. This tris(P-aminophenyl)(thio)phosphate ester can be obtained by synthesizing triphenyl(thio)phosphate, nitrating it, and then reducing it to the corresponding amine, or by synthesizing the sodium salt of P-nitrophenol. It is produced by reacting this with phosphorus oxychloride or phosphorus thiochloride at high temperature to produce the corresponding nitro compound, which is then reduced.Also, P-substituted phenol and phosphorus oxychloride or phosphorus thiochloride are reacted in the presence of an alkali. A method of manufacturing by directly reacting with is also known. For example, special public service in 1987
−25559 Publication P-substituted phenol represented by A method for producing the corresponding tris(P-substituted phenyl)(thio)phosphate ester is described below. However, since this method involves a reaction in the presence of water, the raw materials and reaction intermediates are susceptible to hydrolysis, making it difficult to sufficiently increase the yield. That is, in phosphorus oxychloride or phosphorus thiochloride, and the mono- or diester reaction intermediate, the chlorine atom bonded to the phosphorus atom contained therein is easily eliminated by hydrolysis.
The yield of triester was likely to be insufficient. In the invention described in the above-mentioned publication, the concentration of alkali is specified in order to prevent this hydrolysis, but the hydrolysis cannot be completely suppressed.

本発明者は加水分解に起因する収率の低下を防
ぐ方法を種々研究検討した結果、アルカリ金属炭
酸塩を共存させると実質的に無水の反応条件下で
高い収率でトリ(チオ)リン酸エステルを製造し
うることを見い出した。本発明はこれを要旨とす
るものであり、即ち、 式[] (X:ニトロ基、アミノ基、あるいはN−アシル
アミノ基) で表わされるP−置換フエノールとオキシ塩化リ
ンあるいはチオ塩化リンとを、アルカリ金属炭酸
塩および溶媒の存在下に実質的に無水の条件下で
反応させることを特徴とする下記式[]で表わ
されるリン酸エステルまたは(チオ)リン酸エス
テルの製造法、 (Y:酸素原子あるいはイオウ原子、X:上記式
[]のXに同じ) である。
As a result of various research studies on methods to prevent the decrease in yield caused by hydrolysis, the present inventor found that when an alkali metal carbonate is present, a high yield of tri(thio)phosphate can be obtained under substantially anhydrous reaction conditions. It was discovered that esters can be produced. This is the gist of the present invention, that is, the formula [] P-substituted phenol represented by (X: nitro group, amino group, or N-acylamino group) and phosphorus oxychloride or phosphorus thiochloride are added under substantially anhydrous conditions in the presence of an alkali metal carbonate and a solvent. A method for producing a phosphoric acid ester or (thio)phosphoric acid ester represented by the following formula [], which is characterized by reacting with (Y: oxygen atom or sulfur atom, X: same as X in the above formula []).

本発明においては反応系に実質的に水が存在し
ないため、前記加水分解に起因する問題は起らな
い。即ち前記公知例記載の発明の場合は勿論、た
とえ非水系溶媒を使用した場合でもアルカリ金属
水酸化物を使用するとP−置換フエノールのアル
カリ金属ナトリウム塩の生成により水が副生する
が、アルカリ金属炭酸塩の使用により水が副生す
ることはないと考えられる。本発明においては次
のような反応を経由して反応が進むと考えられる
がこの反応は充分に確認されるものではない。
In the present invention, since substantially no water is present in the reaction system, the above-mentioned problems caused by hydrolysis do not occur. That is, of course in the case of the invention described in the above-mentioned known examples, even when a non-aqueous solvent is used, when an alkali metal hydroxide is used, water is produced as a by-product due to the formation of an alkali metal sodium salt of P-substituted phenol. It is thought that water will not be produced as a by-product due to the use of carbonate. In the present invention, the reaction is thought to proceed via the following reaction, but this reaction has not been fully confirmed.

(M:アルカリ金属) M2CO3で表わされるアルカリ金属炭酸塩とし
ては炭酸リチウム、炭酸ナトリウム、炭酸カリウ
ムなどがあるが、特に炭酸ナトリウムと炭酸カリ
ウムが適当である。このアルカリ金属炭酸塩は実
質的に無水物が適当であり、結晶水を含む塩は好
ましくない。たとえば、炭酸ナトリウムの場合、
無水塩以外に十水塩、七水塩、一水塩などがある
が、無水塩(即ちソーダ灰)が適当である。
(M: Alkali metal) Examples of the alkali metal carbonate represented by M 2 CO 3 include lithium carbonate, sodium carbonate, and potassium carbonate, with sodium carbonate and potassium carbonate being particularly suitable. This alkali metal carbonate is suitably substantially anhydrous, and salts containing water of crystallization are not preferred. For example, for sodium carbonate,
In addition to anhydrous salts, there are decahydrate salts, heptahydrate salts, monohydrate salts, etc., but anhydrous salts (i.e., soda ash) are suitable.

本発明によれば、P−アミノフエノールとオキ
シ塩化リンあるいはチオ塩化リンとから一挙に合
成しうるので工業的に有利である。P−ニトロフ
エノールのアルカリ金属塩を一度製造する必要が
なくP−ニトロフエノールから直接トリス(P−
ニトロフエニル)(チオ)リン酸エステルを製造
でき、引き続きこれを還元してトリス(P−アミ
ノフエニル)(チオ)リン酸エステルを製造すれ
ば多くの場合上記の直接トリス(P−アミノフエ
ニル)(チオ)リン酸エステルを製造する方法よ
りも経済的に有利である。また、N−アシル−P
−アミノフエノールを原料としてトリス(4−ア
シルアミノフエニル)(チオ)リン酸エステルを
製造する方法は、上記P−アミノフエノールを原
料とする場合以上に高純度の化合物が得られ、次
いでこの(チオ)リン酸エステルを酸の存在下に
加水分解すれば容易に高純度のトリス(P−アミ
ノフエニル)(チオ)リン酸エステルとすること
ができる。いずれの場合も、対応する前記公知例
記載の発明の方法よりも高収率で純度の高い製品
が得られる。
According to the present invention, it is industrially advantageous because it can be synthesized all at once from P-aminophenol and phosphorus oxychloride or phosphorus thiochloride. There is no need to produce an alkali metal salt of P-nitrophenol, and tris(P-
Nitrophenyl)(thio)phosphate can be produced, which is subsequently reduced to produce tris(P-aminophenyl)(thio)phosphate in many cases. It is economically more advantageous than the method of producing acid esters. Also, N-acyl-P
The method for producing tris(4-acylaminophenyl)(thio)phosphate ester using -aminophenol as a raw material yields a compound with higher purity than when using the above-mentioned P-aminophenol as a raw material, and then this ( High purity tris(P-aminophenyl)(thio)phosphate can be easily obtained by hydrolyzing the thio)phosphate in the presence of an acid. In either case, a product with higher yield and purity can be obtained than the corresponding method of the invention described in the above-mentioned known example.

本発明の実施においては、通常溶媒の存在下に
前記式[]で表わされるP−置換フエノールに
アルカリ金属炭酸塩を加え、冷却しながらオキシ
塩化リンあるいはチオ塩化リンを滴下する方法が
とられる。溶媒としては反応に対し不活性な溶
媒、たとえばトルエン,キシレン,クロルベンゼ
ン,O−ジクロルベンゼン,アセトニトリル,ジ
エチレングリコールジメチルエーテル,イソプロ
ピルエーテル,ジオキサン,アセトン,メチルエ
チルケトン,クロロホルム,ジクロメタンなどを
挙げることができるが、特にエーテル系溶媒やケ
トン系溶媒が好ましい。溶媒の使用量は特に限定
されないが、上記P−置換フエノールに対して約
10〜20倍量程度が適当である。アルカリ金属炭酸
塩の使用量はP−置換フエノールに対して約当モ
ル以上、特に1〜1.5倍モルが好ましく、通常ほ
ぼ当モルかやや過剰に用いるのが適当である。P
−置換フエノールの使用量はオキシ塩化リンある
いはチオ塩化リンに対し約2.5〜10倍モルの範囲
で使用しうるが、通常は約3倍モルかやや過剰に
用いるのが適当である。反応温度は特に限定され
ないが約80℃以下が適当であり、特に約0〜40℃
が好ましい。反応時間は反応温度によつて変化す
るが、好適な反応温度で反応を行なつた場合約1
〜10時間が適当である。このようにして製造した
(チオ)リン酸エステルは、未反応P−置換フエ
ノール,モノあるいはジエステルを含むもので減
圧蒸留により溶媒を留去して濃縮し、次いで水に
排出し析出物を過した後、結晶物を希アルカリ
水溶液で洗浄して精製することが好ましい。これ
により上記未反応物や副生物はアルカリ塩となつ
て溶解除去される。
In carrying out the present invention, a method is usually used in which an alkali metal carbonate is added to the P-substituted phenol represented by the formula [] in the presence of a solvent, and phosphorus oxychloride or phosphorus thiochloride is added dropwise while cooling. Examples of the solvent include solvents inert to the reaction, such as toluene, xylene, chlorobenzene, O-dichlorobenzene, acetonitrile, diethylene glycol dimethyl ether, isopropyl ether, dioxane, acetone, methyl ethyl ketone, chloroform, dichloromethane, etc. Particularly preferred are ether solvents and ketone solvents. The amount of solvent to be used is not particularly limited, but approximately
Approximately 10 to 20 times the amount is appropriate. The amount of the alkali metal carbonate to be used is preferably about an equivalent mole or more, particularly 1 to 1.5 times the mole, relative to the P-substituted phenol, and it is usually appropriate to use about an equimolar amount or a slight excess. P
The amount of the -substituted phenol to be used may range from about 2.5 to 10 times the mole of phosphorus oxychloride or phosphorus thiochloride, but it is usually appropriate to use about 3 times the mole or slightly in excess. The reaction temperature is not particularly limited, but is suitably about 80°C or lower, especially about 0 to 40°C.
is preferred. The reaction time varies depending on the reaction temperature, but when the reaction is carried out at a suitable reaction temperature, the reaction time is about 1
~10 hours is appropriate. The (thio)phosphate ester produced in this manner contained unreacted P-substituted phenol, mono- or diester, and was concentrated by distilling off the solvent under reduced pressure, and then drained into water to filter out the precipitate. Afterwards, it is preferable to purify the crystalline material by washing it with a dilute aqueous alkaline solution. As a result, the unreacted substances and by-products become alkali salts and are dissolved and removed.

以下に本発明の方法を実施例によつて具体的に
説明するが本発明はこれら実施例のみに限定され
るものではない。
EXAMPLES The method of the present invention will be specifically explained below using Examples, but the present invention is not limited to these Examples.

実施例 1 撹拌機、温度計、コンデンサーおよび滴下ロー
ト付の300mlの4ツ口フラスコにアセトン120ml、
P−ニトロフエノール9.18g(0.066モル)、炭酸
カリウム9.12g(0.066モル)を装入し、激しく
撹拌しながらチオ塩化リン3.73g(0.022モル)
を滴下しながら加えた。この間、反応温度が5℃
以下となるように氷水で冷却し、さらに冷却を続
けながら5時間反応を続けた。
Example 1 120 ml of acetone was added to a 300 ml four-necked flask equipped with a stirrer, thermometer, condenser, and dropping funnel.
Charge 9.18 g (0.066 mol) of P-nitrophenol and 9.12 g (0.066 mol) of potassium carbonate, and add 3.73 g (0.022 mol) of phosphorus thiochloride while stirring vigorously.
was added dropwise. During this time, the reaction temperature was 5℃.
The reaction mixture was cooled with ice water as shown below, and the reaction was continued for 5 hours with continued cooling.

反応終了後減圧下でアセトンを留去して濃縮し
た後、0.2%の水酸化ナトリウム水溶液500mlの中
に注ぎ、析出させた。析出物を過水洗して60℃
で減圧乾燥することにより、トリス(P−ニトロ
フエニル)(チオ)リン酸エステル10.18g(P−
ニトロフエノールに対し収率97%)を淡黄色粉末
として得た。このものの融点は179℃であつた。
After the reaction was completed, the acetone was distilled off and concentrated under reduced pressure, and then poured into 500 ml of 0.2% aqueous sodium hydroxide solution to precipitate. Wash the precipitate with water and heat at 60℃
10.18 g of tris(P-nitrophenyl)(thio)phosphate ester (P-
(Yield 97% based on nitrophenol) was obtained as a pale yellow powder. The melting point of this product was 179°C.

比較例 実施例1で使用したと同じ反応容器にアセトン
200mlおよびP−ニトロフエノール13.91g(0.1
モル)を装入し、次にチオ塩化リン6.27g
(0.037モル)を加え直ちに滴下ロートより45%水
酸化ナトリウム水溶液9.60g(0.108モル)を激
しく撹拌しながら6分間で滴下した。この間、反
応温度を8℃以下となるように氷水で冷却し、さ
らに冷却を続けながら5時間反応を続けた。
Comparative Example Acetone was added to the same reaction vessel used in Example 1.
200 ml and P-nitrophenol 13.91 g (0.1
mol), then 6.27 g of phosphorus thiochloride
(0.037 mol), and immediately 9.60 g (0.108 mol) of a 45% aqueous sodium hydroxide solution was added dropwise from the dropping funnel over 6 minutes with vigorous stirring. During this time, the mixture was cooled with ice water so that the reaction temperature was 8° C. or less, and the reaction was continued for 5 hours with continued cooling.

反応終了後減圧下35℃で濃縮した後氷冷下30%
の水酸化ナトリウム水溶液をPH11となるまで滴下
しトリス(P−ニトロフエニル)(チオ)リン酸
エステルを沈殿させ、過水洗後60℃で減圧乾燥
した。その結果、融点179℃の淡黄色結晶を8.59
g(P−ニトロフエノールに対し収率54%)得
た。
After the reaction was completed, it was concentrated under reduced pressure at 35°C and then 30% under ice cooling.
An aqueous solution of sodium hydroxide was added dropwise until the pH reached 11 to precipitate tris(P-nitrophenyl)(thio)phosphate, which was washed with water and dried under reduced pressure at 60°C. As a result, pale yellow crystals with a melting point of 179℃ were obtained at 8.59℃.
g (yield 54% based on P-nitrophenol) was obtained.

実施例 2 チオ塩化リンの代りにオキシ塩化リン3.37g
(0.022モル)を用いる以外は実施例1と同様に操
作してトリス(P−ニトロフエニル)リン酸エス
テル9.94g(P−ニトロフエノールに対し収率97
%}を白色粉末で得た。このものの融点は156℃
であつた。
Example 2 3.37g of phosphorus oxychloride instead of phosphorus thiochloride
Tris(P-nitrophenyl) phosphate ester 9.94g (yield 97% based on P-nitrophenol)
%} was obtained as a white powder. The melting point of this substance is 156℃
It was hot.

実施例 3 P−ニトロフエノールの代りにP−アミノフエ
ノール7.22g(0.066モル)、またチオ塩化リンの
代りにオキシ塩化リン3.37g(0.022モル)を用
いる以外は実施例1と同様に操作してトリス(P
−アミノフエニル)リン酸エステルの白色結晶を
5.64g(P−アミノフエノールに対し収率69%)
得た。このものの融点は154℃であつた。
Example 3 The procedure was repeated in the same manner as in Example 1, except that 7.22 g (0.066 mol) of P-aminophenol was used instead of P-nitrophenol, and 3.37 g (0.022 mol) of phosphorus oxychloride was used instead of phosphorus thiochloride. Tris (P
-aminophenyl) phosphate ester white crystals
5.64g (yield 69% based on P-aminophenol)
Obtained. The melting point of this product was 154°C.

実施例 4 実施例1と同じ反応容器にN−アセチル−P−
アミノフエノール9.99g(0.066モル)、ジオキサ
ン120mlおよび炭酸ナトリウム7.0g(0.066モル)
を装入し、激しく撹拌しながらチオ塩化リン3.73
g(0.022モル)を滴下しながら加えた。この間、
反応温度は30℃以下になるように水で冷却し、滴
下終了後室温で5時間反応を続けた。
Example 4 In the same reaction vessel as in Example 1, N-acetyl-P-
Aminophenol 9.99g (0.066mol), dioxane 120ml and sodium carbonate 7.0g (0.066mol)
3.73 phosphorus thiochloride while stirring vigorously.
g (0.022 mol) was added dropwise. During this time,
The mixture was cooled with water so that the reaction temperature was 30°C or less, and after the dropwise addition was completed, the reaction was continued at room temperature for 5 hours.

反応終了後減圧下で濃縮した後、0.2%の水酸
化ナトリウム水溶液500mlの中に注ぎ析出させた。
析出物を過水洗して60℃で減圧乾燥することに
より、トリス(4−アセチルアミノフエニル)チ
オリン酸エステルの白色結晶を11.18g(N−ア
セチル−P−アミノフエノールに対し収率99%)
得た。このものの融点は196℃であつた。
After the reaction was completed, it was concentrated under reduced pressure and poured into 500 ml of 0.2% aqueous sodium hydroxide solution to precipitate.
By washing the precipitate with water and drying under reduced pressure at 60°C, 11.18 g of white crystals of tris(4-acetylaminophenyl)thiophosphoric acid ester (99% yield based on N-acetyl-P-aminophenol) was obtained.
Obtained. The melting point of this product was 196°C.

Claims (1)

【特許請求の範囲】 1 式[] (X:ニトロ基、アミノ基、あるいはN−アシル
アミノ基) で表わされるP−置換フエノールとオキシ塩化リ
ンあるいはチオ塩化リンとを、アルカリ金属炭酸
塩および溶媒の存在下に実質的に無水の条件下で
反応させることを特徴とする下記式[]で表わ
されるリン酸エステルまたはチオリン酸エステル
の製造法。 (Y:酸素原子あるいはイオウ原子、X:上記式
[]のXに同じ)
[Claims] 1 Formula [] P-substituted phenol represented by (X: nitro group, amino group, or N-acylamino group) and phosphorus oxychloride or phosphorus thiochloride are added under substantially anhydrous conditions in the presence of an alkali metal carbonate and a solvent. A method for producing a phosphoric acid ester or thiophosphoric acid ester represented by the following formula [], which comprises reacting with: (Y: oxygen atom or sulfur atom, X: same as X in the above formula [])
JP705084A 1984-01-20 1984-01-20 Preparation of phosphoric acid ester or thiophosphoric acid ester Granted JPS60152492A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP705084A JPS60152492A (en) 1984-01-20 1984-01-20 Preparation of phosphoric acid ester or thiophosphoric acid ester

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP705084A JPS60152492A (en) 1984-01-20 1984-01-20 Preparation of phosphoric acid ester or thiophosphoric acid ester

Publications (2)

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JPS60152492A JPS60152492A (en) 1985-08-10
JPH0437839B2 true JPH0437839B2 (en) 1992-06-22

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Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0768258B2 (en) * 1989-12-22 1995-07-26 大八化学工業株式会社 Method for producing tris (trihaloneopentyl) phosphate
CN101460511A (en) * 2006-06-09 2009-06-17 昭和高分子株式会社 Process for production of aminated phosphoric acid ester compound, flame-retardant resin, and flame-retardant resin composition

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53136510A (en) * 1977-04-27 1978-11-29 Nattermann A & Cie Production of high purity phosphatidil choline containing oil

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53136510A (en) * 1977-04-27 1978-11-29 Nattermann A & Cie Production of high purity phosphatidil choline containing oil

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JPS60152492A (en) 1985-08-10

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