JPS6347717B2 - - Google Patents
Info
- Publication number
- JPS6347717B2 JPS6347717B2 JP6964680A JP6964680A JPS6347717B2 JP S6347717 B2 JPS6347717 B2 JP S6347717B2 JP 6964680 A JP6964680 A JP 6964680A JP 6964680 A JP6964680 A JP 6964680A JP S6347717 B2 JPS6347717 B2 JP S6347717B2
- Authority
- JP
- Japan
- Prior art keywords
- reaction
- alkyl
- formula
- phosphorus oxychloride
- thiophosphoric 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.)
- Expired
Links
- XHXFXVLFKHQFAL-UHFFFAOYSA-N phosphoryl trichloride Chemical compound ClP(Cl)(Cl)=O XHXFXVLFKHQFAL-UHFFFAOYSA-N 0.000 claims description 31
- -1 thiophosphoric acid triester Chemical class 0.000 claims description 12
- 125000000217 alkyl group Chemical group 0.000 claims description 11
- 125000003118 aryl group Chemical group 0.000 claims description 11
- RYYWUUFWQRZTIU-UHFFFAOYSA-N Thiophosphoric acid Chemical compound OP(O)(S)=O RYYWUUFWQRZTIU-UHFFFAOYSA-N 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 125000004432 carbon atom Chemical group C* 0.000 claims description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims 1
- 229910052799 carbon Inorganic materials 0.000 claims 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 description 38
- 239000000460 chlorine Substances 0.000 description 15
- 239000002994 raw material Substances 0.000 description 13
- 239000000047 product Substances 0.000 description 11
- 238000000034 method Methods 0.000 description 7
- UHZYTMXLRWXGPK-UHFFFAOYSA-N phosphorus pentachloride Chemical compound ClP(Cl)(Cl)(Cl)Cl UHZYTMXLRWXGPK-UHFFFAOYSA-N 0.000 description 7
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 6
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 6
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 239000007810 chemical reaction solvent Substances 0.000 description 4
- 238000004817 gas chromatography Methods 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 3
- 239000012295 chemical reaction liquid Substances 0.000 description 3
- 238000004821 distillation Methods 0.000 description 3
- 150000002148 esters Chemical class 0.000 description 3
- 238000010813 internal standard method Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 150000005691 triesters Chemical class 0.000 description 3
- NGNBDVOYPDDBFK-UHFFFAOYSA-N 2-[2,4-di(pentan-2-yl)phenoxy]acetyl chloride Chemical compound CCCC(C)C1=CC=C(OCC(Cl)=O)C(C(C)CCC)=C1 NGNBDVOYPDDBFK-UHFFFAOYSA-N 0.000 description 2
- 238000006418 Brown reaction Methods 0.000 description 2
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 2
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- DQTRYXANLKJLPK-UHFFFAOYSA-N chlorophosphonous acid Chemical compound OP(O)Cl DQTRYXANLKJLPK-UHFFFAOYSA-N 0.000 description 2
- 238000000921 elemental analysis Methods 0.000 description 2
- 238000001819 mass spectrum Methods 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 2
- 150000002903 organophosphorus compounds Chemical class 0.000 description 2
- 125000004430 oxygen atom Chemical group O* 0.000 description 2
- RMVRSNDYEFQCLF-UHFFFAOYSA-N phenyl mercaptan Natural products SC1=CC=CC=C1 RMVRSNDYEFQCLF-UHFFFAOYSA-N 0.000 description 2
- RLOWWWKZYUNIDI-UHFFFAOYSA-N phosphinic chloride Chemical compound ClP=O RLOWWWKZYUNIDI-UHFFFAOYSA-N 0.000 description 2
- OJMIONKXNSYLSR-UHFFFAOYSA-N phosphorous acid Chemical compound OP(O)O OJMIONKXNSYLSR-UHFFFAOYSA-N 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- 238000007086 side reaction Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- FWMUJAIKEJWSSY-UHFFFAOYSA-N sulfur dichloride Chemical compound ClSCl FWMUJAIKEJWSSY-UHFFFAOYSA-N 0.000 description 2
- 238000005292 vacuum distillation Methods 0.000 description 2
- HMANYETUONUMIX-UHFFFAOYSA-N CCC[S+]=P(O)(O)O Chemical compound CCC[S+]=P(O)(O)O HMANYETUONUMIX-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- 125000003545 alkoxy group Chemical group 0.000 description 1
- 150000001350 alkyl halides Chemical class 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 125000004429 atom Chemical group 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 150000001805 chlorine compounds Chemical class 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 125000004093 cyano group Chemical group *C#N 0.000 description 1
- ALVPFGSHPUPROW-UHFFFAOYSA-N dipropyl disulfide Chemical compound CCCSSCCC ALVPFGSHPUPROW-UHFFFAOYSA-N 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 125000005843 halogen group Chemical group 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 125000000449 nitro group Chemical group [O-][N+](*)=O 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 150000003014 phosphoric acid esters Chemical class 0.000 description 1
- FAIAAWCVCHQXDN-UHFFFAOYSA-N phosphorus trichloride Chemical compound ClP(Cl)Cl FAIAAWCVCHQXDN-UHFFFAOYSA-N 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000010517 secondary reaction Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000013076 target substance Substances 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Description
本発明はO―アルキルS―アルキル(又はアリ
ール)チオリン酸クロライドの製造方法に関し、
その目的とするところは有機リン農薬の中間体と
して重要なO―アルキルS―アルキル(又はアリ
ール)チオリン酸クロライドの高純度のものを収
率良く製造する方法を提供することにある。
従来、五価のリン酸エステルの塩素化にオキシ
塩化リンを用いた例として下記の反応が知られて
いる〔ジー・エム・コゾラポフおよびエル・メイ
ヤー著「オルガノホスフオラスコンパウンドー」
第6巻第304頁(G.M.Kosolapoff and L.
Maier:Organic Phosphorus Compounds,
1973,Vol.6,p.304)〕:
(RO)3P(O)+P(O)Cl3
→(RO)2P(O)Cl+(RO)P(O)Cl2
(式中Rはアルキル基またはアリール基を示
す)
しかしながらこの反応はRが低級アルキル基ま
たは特定のアリール基の場合にはやや進行する
が、収率が低く工業的でない。しかも上記文献に
はトリアルキルチオリン酸エステルの反応につい
ては言及されておらず全く不明である。
また本発明と同一の目的物を得る方法として、
ジアルキルクロルホスフアイトとスルフエニルク
ロライドとを反応させる方法:
(RO)2PCl+R′SCl
→(RO)(R′S)P(O)Cl+RCl
(式中Rはアルキル基、R′はアリール基を示
す)
あるいはS―アリールチオリン酸エステルと五
塩化リンとを反応させる方法(特開昭48―103551
号公報):
(RO)2(R′S)P(O)+PCl5
→(RO)(R′S)P(O)Cl+POCl3+RCl
(式中Rはアルキル基、R′はアリール基を示
す)
が知られている。しかしながら前者の方法は原料
となるジアルキルクロルホスフアイトの収率が低
いうえにその中にはトリアルキルホスフアイトお
よびアルキルジクロルホスフアイト等の不純物が
存在し、得られる目的物が低純度であるという欠
点がある。また後者の方法は原料がS―アリール
チオ燐酸エステルのみに限定されるばかりか、反
応が激しく不純物が多量生成することが避けられ
ない。これは五塩化リンがS―アリールチオ燐酸
エステルから酸素原子の引き抜きをするために、
一度生成した(RO)(R′S)P(O)Clにさらに
作用しR′SP(O)Cl2等を生ずるためであろう。
また吸湿性、発煙性固体である五塩化リンの取扱
いが厄介で操業上問題がある。
上記の欠点に鑑み本発明者等はO―アルキルS
―アルキル(又はアリール)チオリン酸クロライ
ドの製造方法につき種々検討した結果、チオリン
酸トリエステルとオキシ塩化リンとを反応させる
ことにより、穏やかな反応で極めて高収率かつ高
純度で目的物質を製造し得ることを見出し本発明
を完成した。
すなわち本発明は一般式(RO)2(R′S)P(O)
〔式中Rは炭素数1〜8のアルキル基を示し、
R′は炭素数1〜8のアルキル基または
The present invention relates to a method for producing O-alkyl S-alkyl (or aryl) thiophosphoric acid chloride,
The objective is to provide a method for producing highly pure O-alkyl S-alkyl (or aryl) thiophosphoric acid chloride in good yield, which is important as an intermediate for organophosphorus pesticides. Conventionally, the following reaction is known as an example of using phosphorus oxychloride to chlorinate a pentavalent phosphoric acid ester [G.M. Kozolapov and L. Mayer, "Organophosphorus Compound"]
Volume 6, page 304 (GMKosolapoff and L.
Maier: Organic Phosphorus Compounds,
1973, Vol. 6, p. 304)]: (RO) 3 P(O) + P(O)Cl 3 → (RO) 2 P(O)Cl + (RO)P(O)Cl 2 (In the formula, R is (represents an alkyl group or an aryl group) However, this reaction proceeds somewhat when R is a lower alkyl group or a specific aryl group, but the yield is low and it is not industrially practical. Moreover, the above-mentioned document does not mention the reaction of trialkylthiophosphoric acid ester and is completely unclear. In addition, as a method for obtaining the same object as the present invention,
Method for reacting dialkyl chlorophosphite and sulfenyl chloride: (RO) 2 PCl + R′SCl
→(RO)(R'S)P(O)Cl+RCl (in the formula, R represents an alkyl group and R' represents an aryl group) or a method of reacting S-arylthiophosphate and phosphorus pentachloride (JP-A-Sho 48―103551
No. Publication): (RO) 2 (R′S)P(O)+PCl 5 → (RO)(R′S)P(O)Cl+POCl 3 +RCl (In the formula, R represents an alkyl group and R′ represents an aryl group. ) It has been known. However, the former method has a low yield of dialkyl chlorophosphite as a raw material and contains impurities such as trialkyl phosphite and alkyl dichlorophosphite, resulting in the obtained target product being of low purity. There are drawbacks. Furthermore, in the latter method, not only the raw material is limited to only S-arylthiophosphate ester, but also the reaction is intense and it is inevitable that a large amount of impurities will be produced. This is because phosphorus pentachloride abstracts oxygen atoms from S-arylthiophosphate ester.
This is probably because the once generated (RO)(R'S)P(O)Cl is further acted upon to produce R'SP(O)Cl 2 and the like.
Additionally, phosphorus pentachloride, which is a hygroscopic and fuming solid, is difficult to handle, which poses operational problems. In view of the above drawbacks, the present inventors have proposed that O-alkyl S
-As a result of various studies on the production method of alkyl (or aryl) thiophosphoric acid chloride, we found that the target substance can be produced in extremely high yield and purity through a mild reaction by reacting thiophosphoric acid triester and phosphorus oxychloride. The present invention was completed based on the discovery that the present invention can be obtained. That is, the present invention has the general formula (RO) 2 (R′S)P(O)
[In the formula, R represents an alkyl group having 1 to 8 carbon atoms,
R' is an alkyl group having 1 to 8 carbon atoms or
【式】(Xは水素原子、ハロゲン原
子、低級アルキル基、シアノ基又はニトロ基を示
し、nは1〜5の整数を示す)で示されるフエニ
ル基を示す〕で表わされるチオリン酸トリエステ
ルとオキシ塩化リンとを反応させることを特徴と
する一般式(RO)(R′S)P(O)Cl(式中R及び
R′は上記意義を有する)で表わされるO―アル
キルS―アルキル(又はアリール)チオリン酸ク
ロライドの製造方法である。
これを反応式で表わせば下記のとおりである。
(RO)2(R′S)P(O)+P(O)Cl3
→(RO)(R′S)P(O)Cl+ROP(O)Cl2
(式中RおよびR′は上記意義を有する)
ここで原料として用いられる一般式(RO)2
(R′S)P(O)〔式中RおよびR′は上記意義を示
す〕で表わされるチオリン酸トリエステルはアル
キル(又はアリール)スルフエニルクロライドと
トリアルキルホスフアイトの反応:R′SCl+
(RO)3P→(RO)2(R′S)P(O)+RCl〔式中R及
びR′は上記意義を示す〕でも得られるし、ジア
ルキルチオリン酸塩とハロゲン化アルキルとの反
応またはジアルキルリン酸クロライドとチオフエ
ノール系化合物との反応により得ることもでき
る。
本発明はかかるチオリン酸トリエステルとオキ
シ塩化リンとを反応溶剤の存在または不存在下に
反応させる。反応溶剤としては原料、目的生成物
と反応しないものであればいずれも使用可能であ
り例えばベンゼン、トルエン、キシレン、n―ペ
ンタン、n―ヘキサン、石油、エーテル、リグロ
イン、ケロシン、ジクロメタン、クロロホルム、
四塩化炭素等が挙げられる。なお反応溶剤を使用
しなくても本反応を遂行することは可能であり、
その場合にはチオリン酸トリエステルに対してや
や過剰のオキシ塩化リンを用いることが好まし
く、さらには三塩化リン中にチオリン酸トリエス
テルを溶解しその中へ酸素又は空気を吹込みつつ
反応させることも差支えない。
チオリン酸トリエステルに対するオキ塩化リン
の反応割合については最少限化学量論量を要する
ことは当然であるが、通常前者1モルに対して後
者5モル好ましくは3モルも使用すれば充分であ
る。1モル以下では反応達成が充分でなく5モル
以上の使用は反応容器の増大、過剰オキシ塩化リ
ンの回収、精製等操作が煩雑となる割に効果がな
い。
又反応温度については原料、目的物、反応溶剤
の有無等により一様ではないが一般的には常温な
いし150℃程度であり、原料、目的物の熱分解を
避ける意味で50〜100℃が好適である。圧力につ
いては減圧、加圧を問わない。
反応時間については上記緒条件により定まる
が、通常15分〜20時間好ましくは1時間〜15時間
も反応させれば充分である。本発明の反応によれ
ば、既述したS―アリールチオリン酸エステルと
五塩化リンとの反応の如く激しくなく副反応も少
く、原料の種類、反応条件の如何に拘わらず穏や
かにしかも定量的に目的物を得ることができる。
それはS―アリールチオ燐酸エステルと五塩化リ
ンとの反応が酸素原子の引き抜き反応という激し
い反応機構からなるのに対し、本発明に係るオキ
シ塩化リンの作用は、チオリン酸トリエステル中
のアルコキシ基と塩素原子の穏やかな交換反応を
呈るからである。またた目的物とオキシ塩化リン
の二次反応は起り難く、原料の反応割合を厳密に
制御しなくとも副反応の起る余地が少い。さらに
五塩化リンが発煙性で刺激臭の潮解性固体であり
操作上取扱い難い欠点を有するのに対し本発明の
オキシ塩化リンは液体であるので工業上極めて取
扱い易い。
かくして本発明によれば穏やかな反応で高純度
の目的物を高収率で得ることが可能となり、その
産業上の利用価値は大なるものがある。
以下実施例にて本発明をさらに具体的に説明す
る。
実施例 1〜8
撹拌器、温度計、還流冷却器を取付けた四ツ口
フラスコにO.O.S―トリメチルチオリン酸エステ
ル(CH3O)2P(O)SCH315.61g(0.1M相当)を
採り、オキシ塩化リンPOCl315.33g(0.1M相当)
を添加し、油浴により反応温度を60℃に保ち、ガ
スクロマトグラフにより原料であるO.O.S―トリ
メチルチオリン酸エステルの残存量を追跡しなが
ら反応を行つた。約2時間後原料が完全に消失し
反応が完結し、茶褐色の反応液30.92gが得られ
た。この反応液をガスクロマトグラフ内部標準法
で分析した結果、目的物であるO.S―ジメチルチ
オリン酸クロライド(CH3O)(CH3S)P(O)
Clの含有量が51.0重量%であつた。
次に、この反応液を真空蒸留により分離精製す
ると無色透明の液体15.23gが得られた。bp.54〜
6℃/0.4mmHg蒸留収率94.9重量%。これをマ
ススペクトルと元素分析により確認した。[Formula] (X represents a hydrogen atom, a halogen atom, a lower alkyl group, a cyano group, or a nitro group; General formula (RO)(R'S)P(O)Cl (in the formula, R and
This is a method for producing O-alkyl S-alkyl (or aryl) thiophosphoric acid chloride represented by (R' has the above meaning). This can be expressed as a reaction formula as follows. (RO) 2 (R′S)P(O)+P(O)Cl 3 →(RO)(R′S)P(O)Cl+ROP(O)Cl 2 (In the formula, R and R′ have the above meanings. ) The general formula (RO) used here as a raw material is 2
The thiophosphoric acid triester represented by (R'S)P(O) [in the formula, R and R' have the above meanings] is the reaction of alkyl (or aryl) sulfenyl chloride and trialkyl phosphite: R'SCl+
(RO) 3 P→(RO) 2 (R′S)P(O)+RCl [in the formula, R and R′ have the above meanings] can also be obtained, or by reaction between a dialkylthiophosphate and an alkyl halide or It can also be obtained by reacting a dialkyl phosphoric acid chloride with a thiophenol compound. In the present invention, such a thiophosphoric acid triester and phosphorus oxychloride are reacted in the presence or absence of a reaction solvent. Any reaction solvent can be used as long as it does not react with the raw materials or the desired product, such as benzene, toluene, xylene, n-pentane, n-hexane, petroleum, ether, ligroin, kerosene, dichloromethane, chloroform,
Examples include carbon tetrachloride. Note that it is possible to carry out this reaction without using a reaction solvent.
In that case, it is preferable to use a slight excess of phosphorus oxychloride relative to the thiophosphoric triester, and furthermore, the thiophosphoric triester is dissolved in phosphorus trichloride and the reaction is carried out while blowing oxygen or air into it. There is no problem. It goes without saying that the reaction ratio of phosphorus oxychloride to thiophosphoric acid triester requires a minimum stoichiometric amount, but it is usually sufficient to use 5 moles, preferably 3 moles of the latter per 1 mole of the former. If the amount is less than 1 mole, the reaction will not be achieved sufficiently, and if the amount is more than 5 moles, the number of reaction vessels will increase, and operations such as recovery and purification of excess phosphorus oxychloride will become complicated, but are not effective. The reaction temperature varies depending on the raw materials, the target product, the presence or absence of a reaction solvent, etc., but is generally room temperature to about 150°C, and 50 to 100°C is preferable in order to avoid thermal decomposition of the raw materials and target products. It is. Regarding the pressure, it does not matter whether it is reduced pressure or increased pressure. The reaction time is determined by the above conditions, but it is usually sufficient to react for 15 minutes to 20 hours, preferably 1 hour to 15 hours. According to the reaction of the present invention, it is not as violent as the reaction between S-arylthiophosphate and phosphorus pentachloride mentioned above, and there are few side reactions, and it is carried out gently and quantitatively regardless of the type of raw materials or reaction conditions. You can get what you want.
This is because the reaction between S-arylthiophosphate and phosphorus pentachloride involves a violent reaction mechanism called an oxygen atom abstraction reaction, whereas the action of phosphorus oxychloride according to the present invention is based on the reaction between the alkoxy group in the thiophosphoric acid triester and the chlorine This is because it exhibits a mild exchange reaction of atoms. Further, secondary reactions between the target product and phosphorus oxychloride are difficult to occur, and there is little room for side reactions to occur even if the reaction ratio of the raw materials is not strictly controlled. Further, while phosphorus pentachloride is a deliquescent solid that emits smoke and has a pungent odor and is difficult to handle in terms of operation, the phosphorus oxychloride of the present invention is a liquid and therefore extremely easy to handle industrially. Thus, according to the present invention, it is possible to obtain a highly purified target product in high yield through a mild reaction, and its industrial utility value is great. The present invention will be explained in more detail below with reference to Examples. Examples 1 to 8 15.61 g (equivalent to 0.1 M) of OOS-trimethylthiophosphate (CH 3 O) 2 P(O) SCH 3 was placed in a four-necked flask equipped with a stirrer, a thermometer, and a reflux condenser. Phosphorus oxychloride POCl 3 15.33g (equivalent to 0.1M)
was added, the reaction temperature was maintained at 60° C. using an oil bath, and the reaction was carried out while monitoring the remaining amount of the raw material OOS-trimethylthiophosphate using a gas chromatograph. After about 2 hours, the raw materials completely disappeared and the reaction was completed, yielding 30.92 g of a brown reaction liquid. As a result of analyzing this reaction solution by gas chromatography internal standard method, the target product OS-dimethylthiophosphoric acid chloride (CH 3 O) (CH 3 S) P(O)
The Cl content was 51.0% by weight. Next, this reaction solution was separated and purified by vacuum distillation to obtain 15.23 g of a colorless and transparent liquid. bp.54~
6°C/0.4mmHg distillation yield 94.9% by weight. This was confirmed by mass spectra and elemental analysis.
【表】
以下同様の方法によつて各種チオリン酸トリエ
ステルを用いて相当するO―アルキルS―アルキ
ル(又はアリール)チオリン酸クロライドを製造
し第1表の結果を得た。[Table] Corresponding O-alkyl S-alkyl (or aryl) thiophosphoric acid chlorides were produced using various thiophosphoric triesters by the same method, and the results shown in Table 1 were obtained.
【表】【table】
【表】
* 上段:理論値 下段:実測値
実施例 9〜11
実施例1と同様の四ツ口フラスコにO,O,S
―トリオクチルチオリン酸エステル
(C8H17O)2P(O)SC8H1745.07g(0.1M相当)を
採り、オキシ塩化リン30.66g(0.20M相当)を
添加し、油浴により反応温度を80℃に保ち、ガス
クロマトグラフにより、原料であるO,O,S―
トリオクチルチオリン酸エステルの残存量を追跡
しながら反応を行つた。14時間後原料が完全に消
失し反応液75.60gが得られた。この反応液をガ
スクロマトグラフ内部標準法で分析した結果、目
的物であるO,S―ジオクチルチオリン酸クロラ
イド(C8H17O)(C8H17S)P(O)Clの含量が
44.0重量%であり、収率は93.2重量%であつた。
この反応液より過剰のオキシ塩化リンと副生物
の(C8H17O)P(O)Cl2を減圧、回収し、残分
34.27gを得た。
これをマススペクトルと元素分析により確認し
た。[Table] * Upper row: Theoretical values Lower row: Actual measured values Examples 9 to 11 O, O, and S were added to the same four-necked flask as in Example 1.
-Take 45.07g (equivalent to 0.1M ) of trioctylthiophosphate (C8H17O)2P(O)SC8H17 , add 30.66g (equivalent to 0.20M) of phosphorus oxychloride, and react in an oil bath. While keeping the temperature at 80℃, the raw materials O, O, S-
The reaction was carried out while monitoring the remaining amount of trioctylthiophosphate. After 14 hours, the raw materials completely disappeared and 75.60 g of reaction liquid was obtained. As a result of analyzing this reaction solution by gas chromatography internal standard method, the content of the target product O,S- dioctylthiophosphoric acid chloride ( C8H17O )( C8H17S )P(O ) Cl was found to be
The yield was 93.2% by weight. Excess phosphorus oxychloride and by-product (C 8 H 17 O)P(O)Cl 2 are recovered from this reaction solution under reduced pressure, and the residue is
34.27g was obtained. This was confirmed by mass spectra and elemental analysis.
【表】
以下同様の方法によつてチオリン酸トリエステ
ルを変えて相当するO―アルキルS―アリールチ
オリン酸クロライドを製造し第2表の結果を得
た。
実施例 12
撹拌器、温度計、還流冷却器を取付けた四ツ口
フラスコにO,O―ジエチル―S―n―プロピル
チオリン酸エステル21.22g、トルエン40c.c.およ
びオキシ塩化リン16.86gを加え、油浴により反
応温度を80℃に保ち撹拌した。15時間後に反応は
完結し、薄茶色の反応液71.82gを得た。この反
応液をガスクロマトグラフ内部標準法で分析した
結果、目的物であるO―エチル―S―n―プロピ
ルチオリン酸クロライドの含有量は28.0重量%で
あり収率は99.2重量%であつた。
真空蒸留によりこの反応液から無色透明液
19.40gを得た。蒸留収率95.7重量%。[Table] Corresponding O-alkyl S-arylthiophosphoric acid chlorides were produced by changing the thiophosphoric acid triester by the same method, and the results shown in Table 2 were obtained. Example 12 21.22 g of O,O-diethyl-Sn-propylthiophosphate, 40 c.c. of toluene, and 16.86 g of phosphorus oxychloride were added to a four-necked flask equipped with a stirrer, thermometer, and reflux condenser. The reaction temperature was maintained at 80°C using an oil bath and the mixture was stirred. The reaction was completed after 15 hours, and 71.82 g of a light brown reaction liquid was obtained. Analysis of this reaction solution by gas chromatography internal standard method revealed that the content of the target product, O-ethyl-Sn-propylthiophosphoric acid chloride, was 28.0% by weight, and the yield was 99.2% by weight. A colorless transparent liquid is obtained from this reaction solution by vacuum distillation.
Obtained 19.40g. Distillation yield 95.7% by weight.
【表】
比較例
撹拌器、温度計およびコンデンサを付けた四ツ
口フラスコにO,O―ジエチル―S―n―プロピ
ルチオリン酸エステル21.22g(0.1モル)と四塩
化炭素60c.c.を加え溶解させる。
三角フラスコに五塩化リン20.82gを秤量し、
密栓する。この中から少量ずつをスパチユラで反
応フラスコに加える。
加え終つてから室温で1時間撹拌し、さらに50
℃で2時間反応させる。
反応液から四塩化炭素とオキシ塩化リンを蒸留
により除去する。このものをガスクロマトグラフ
によつて分析すると、不純物としてn―プロピル
―ジスルフイド、S―n―プロピルチオリン酸ジ
クロライドおよび原料のO,O―ジエチル―S―
n―プロピルチオリン酸エステルその他数ピーク
の不純物を含み目的物O―エチル―S―n―プロ
ピルチオリン酸クロライドの純度は62.2重量%で
あつた。[Table] Comparative example 21.22 g (0.1 mol) of O,O-diethyl-Sn-propylthiophosphate and 60 c.c. of carbon tetrachloride were added to a four-necked flask equipped with a stirrer, thermometer, and condenser. Dissolve. Weigh 20.82g of phosphorus pentachloride into an Erlenmeyer flask,
Seal tightly. Add a small amount of this to the reaction flask using a spatula. After the addition was complete, stir at room temperature for 1 hour, and then stir for another 50 minutes.
Incubate at ℃ for 2 hours. Carbon tetrachloride and phosphorus oxychloride are removed from the reaction solution by distillation. When this product was analyzed by gas chromatography, impurities were found to be n-propyl-disulfide, S-n-propylthiophosphoric acid dichloride, and the raw material O,O-diethyl-S-
The purity of the target product, O-ethyl-Sn-propylthiophosphoric acid chloride, was 62.2% by weight, including n-propylthiophosphoric acid ester and several other peaks of impurities.
【表】【table】
【表】
* 上段:理論値 下段:実測値
[Table] * Upper row: Theoretical value Lower row: Actual value
Claims (1)
素数1〜8のアルキル基を示し、R′は炭素数1
〜8のアルキル基又は【式】(Xは水 素原子、ハロゲン原子、低級アルキル基、シアノ
基又はニトロ基を示し、nは1〜5の整数を示
す)で示されるフエニル基を示す〕で表わされる
チオリン酸トリエステルとオキシ塩化リンとを反
応させることを特徴とする一般式(RO)(R′S)
P(O)Cl(式中R及びR′は上記意義を有する)
で表わされるO―アルキルS―アルキル(又はア
リール)チオリン酸クロライドの製造方法。[Claims] 1 General formula, (RO) 2 (R'S)P(O) [In the formula, R represents an alkyl group having 1 to 8 carbon atoms, and R' has 1 carbon number.
~8 alkyl group or a phenyl group represented by the formula General formula (RO) (R′S) characterized by reacting thiophosphoric acid triester and phosphorus oxychloride
P(O)Cl (in the formula, R and R' have the above meanings)
A method for producing O-alkyl S-alkyl (or aryl) thiophosphoric acid chloride represented by
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6964680A JPS56166197A (en) | 1980-05-27 | 1980-05-27 | O-alkyl s-alkyl or -aryl thiophosphoric chloride |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6964680A JPS56166197A (en) | 1980-05-27 | 1980-05-27 | O-alkyl s-alkyl or -aryl thiophosphoric chloride |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS56166197A JPS56166197A (en) | 1981-12-21 |
JPS6347717B2 true JPS6347717B2 (en) | 1988-09-26 |
Family
ID=13408811
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6964680A Granted JPS56166197A (en) | 1980-05-27 | 1980-05-27 | O-alkyl s-alkyl or -aryl thiophosphoric chloride |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS56166197A (en) |
-
1980
- 1980-05-27 JP JP6964680A patent/JPS56166197A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS56166197A (en) | 1981-12-21 |
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