TW201221521A - An improved process for preparation of trialkyl phosphites - Google Patents

An improved process for preparation of trialkyl phosphites Download PDF

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TW201221521A
TW201221521A TW100134551A TW100134551A TW201221521A TW 201221521 A TW201221521 A TW 201221521A TW 100134551 A TW100134551 A TW 100134551A TW 100134551 A TW100134551 A TW 100134551A TW 201221521 A TW201221521 A TW 201221521A
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formula
phosphite
temperature
alcohol
hours
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TW100134551A
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Chinese (zh)
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Jaidev Rajnikant Shroff
Vikram Rajnikant Shroff
Birja Shanker
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United Phosphorus Ltd
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F9/00Compounds containing elements of Groups 5 or 15 of the Periodic System
    • C07F9/02Phosphorus compounds
    • C07F9/06Phosphorus compounds without P—C bonds
    • C07F9/08Esters of oxyacids of phosphorus
    • C07F9/141Esters of phosphorous acids
    • C07F9/142Esters of phosphorous acids with hydroxyalkyl compounds without further substituents on alkyl

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Biochemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • Molecular Biology (AREA)

Abstract

According to an aspect of the invention, there is provided an improved process for the preparation of trialkyl phosphite of Formula I: said process comprising reacting trialkyl phosphite of Formula II with alkanol of formula III R<SP>1</SP>-OH III such that R<SP>1</SP> represents an alkyl moiety having 8 to 16 carbon atoms and R represents an alkyl moiety having 1 to 3 carbon atoms. Also disclosed is the compound of formula I that is substantially free of a phenolic impurity.

Description

201221521 六、發明說明: 【發明所屬之技術領域】 [0001] 本發明關於用於製備三烷基亞磷酸鹽的改良方法,以及 關於從其製造的三炫基亞構酸鹽。 【先前技術】 [0002] 於本技術領域中報導了三烷基亞磷酸鹽的各種用途被報 導,例如其作為用於合成樹脂、潤滑劑的添加物、消泡 劑、用於製造各種化學製品之中間產物等等之安定劑的 用途。 已發展許多方法用於製備三烷基亞磷酸鹽。例如,亞磷 酸三乙醋是藉由在氯化氫受體(例如氛或胺)的存在下 三氣化磷與乙醇的反應而製備。然而,當藉由此技術製 備亞磷酸三乙酯時,各種問題被關聯。例如,該反應是 高度放熱的,因此必須使用昂貴的冷卻裝置以控制該反 應溫度。所形成的該產物不是以純形式獲得,因此非經 濟上可行的冗長程序被使用以得到純的產物。 更近來’三烷基亞磷酸鹽已在鹼性催化劑的存在下三芳 基亞磷酸鹽(比如三苯基亞磷酸鹽)與烷基醇的轉酯化 作用而製備。然而,當將此技術應用至低級烷基醇(例 如乙醇)時,不容易從其他反應產物獲得該三烷基亞碼 酸鹽(例如亞磷酸三乙酯)的分離。該產物需要藉由乏 味以及昂責的程序而從該反應混合物分離。 此外’已發現由此方法製備的三烷基亞磷酸鹽總是包括 0. 1 %至0. 3%或更多的酚醛雜質,由於其固有的秦性,該 紛搭雜質對於其意欲的用途是不想要的。本技術領域中 有導致二烷基亞磷酸鹽的製備大體上沒有酚醛雜質之方 100134551^單編號A〇101 帛4頁/共29頁 1013064654-0 201221521 法的需要。顧語「大體上沒有」在本文中意欲意指三 烧基亞雜敗全沒有贿雜質或包含少於1QQ _的紛 搭雜質。此祕雜質源自該三芳基亞填酸鹽起始材的芳 基部分體,且是非常不想要的。因此,本技術領域内清 楚地有大體上沒有祕雜質之三烧基以及用於 製備其之方法的需要。 美國專利編號3636145揭露了藉由牽涉亞磷酸三曱酯以及 烯醇之轉酯化作用反應而用於製備三烯基亞磷酸鹽方法 的製備。根據所主張的方法,此揭露發明的必要元素是 該方法中鹼性催化劑的存在以及非共沸溶劑的存在。 美國專利編號3184496揭露了製備以及回收亞填酸三甲酯 的方法以及亞磷酸三甲酯衍生物的製備。該方法也揭露 了該反應中鹼性催化劑的用途。 上述所Φξ:及的方法要不就是牽涉冗長以及乏味的工作程 序以得到純的產物,要不就是使用催化劑以及溶劑,因 此使得這些方法不經濟且較不環保。 因此本技術領域中有需要發展環保、有效率且經濟的方 法’用於製造三烷基亞磷酸鹽而不使用任何溶劑及/或鹼 性催化劑以以高產率以及純度而獲得該產物。 發明目的 此發明的一個目的是提供用於製備三烷基亞磷酸鹽化合 物的改良方法。 本發明的另一個目的是提供以高產率以及墙含量利用百 分比而製備三烷基亞磷酸鹽的改良方法。 本發明的另一個目的是提供製備三烷基亞磷酸鹽的改良 方法’該改良方法是環保的。 1013064654-0 10013455产單編號AOm 第5頁/共29頁 201221521 本發明再另—個目岐提供用_備三絲越酸鹽的 改良方法’該改良方法是經濟上可行且較不耗時的。 本發明再另—個目的是提供導致製備大體上沒有祕雜 質之三烷基亞磷酸鹽的改良方法。 本發明㈣-個目岐提供讀上沒搞_ f或包含 少於100 ppm酚醛雜質的三烷基亞磷酸鹽。 從下述細節的描述,此發明的這些以及其他目的將變得 顯而易見。 【發明内容】 [0003]根據本發明的-方面,有提供了用於製備分子式 基亞磷酸鹽的改良方法: 工201221521 VI. Description of the Invention: [Technical Field of the Invention] [0001] The present invention relates to an improved method for producing a trialkyl phosphite, and to a tristeamidate produced therefrom. [Prior Art] [0002] Various uses of trialkyl phosphites have been reported in the art, for example, as additives for synthetic resins, lubricants, defoamers, and for the manufacture of various chemicals. The use of stabilizers such as intermediates and the like. A number of methods have been developed for the preparation of trialkyl phosphites. For example, triethyl phosphite is prepared by the reaction of tri-phosphorus phosphorus with ethanol in the presence of a hydrogen chloride acceptor such as an amine or an amine. However, when triethyl phosphite is prepared by this technique, various problems are associated. For example, the reaction is highly exothermic and therefore expensive cooling equipment must be used to control the reaction temperature. The product formed is not obtained in pure form, so a lengthy procedure that is not economically feasible is used to obtain a pure product. More recently, trialkyl phosphites have been prepared by transesterification of triaryl phosphites such as triphenyl phosphite with alkyl alcohols in the presence of a basic catalyst. However, when this technique is applied to a lower alkyl alcohol (e.g., ethanol), it is not easy to obtain separation of the trialkyl methacrylate (e.g., triethyl phosphite) from other reaction products. The product needs to be separated from the reaction mixture by a tedious and cumbersome procedure. In addition, it has been found that the trialkyl phosphite prepared by this method always includes 0.1% to 0.3% or more of phenolic impurities, and due to its inherent Qin nature, the use of the mixed impurities for its intended use. It is not wanted. There is a need in the art to produce a dialkyl phosphite that is substantially free of phenolic impurities. 100134551^Single number A〇101 帛4 pages/total 29 pages 1013064654-0 201221521 The need for the method. Gu Yu "substantially no" in this article is intended to mean that there is no bribe impurity or contains more than 1QQ _ impurities. This secret impurity is derived from the aryl moiety of the triaryl sulphate starting material and is highly undesirable. Accordingly, it is clear in the art that there is a need for a trialkyl group which is substantially free of secret impurities and a method for preparing the same. U.S. Patent No. 3,636,145 discloses the preparation of a process for the preparation of a triallyl phosphite by a transesterification reaction involving tridecyl phosphite and an enol. According to the claimed process, an essential element of the disclosed invention is the presence of a basic catalyst and the presence of a non-azeotropic solvent in the process. U.S. Patent No. 3,184,496 discloses the preparation and recovery of trimethyl linoleate and the preparation of trimethyl phosphite derivatives. This method also discloses the use of a basic catalyst in the reaction. The above method of Φξ: and is involved in lengthy and tedious work processes to obtain pure products, or the use of catalysts and solvents, thus making these methods uneconomical and less environmentally friendly. There is therefore a need in the art to develop an environmentally friendly, efficient and economical process for the manufacture of trialkyl phosphites without the use of any solvents and/or basic catalysts to obtain the product in high yields and purity. OBJECT OF THE INVENTION One object of the present invention is to provide an improved process for the preparation of trialkyl phosphite compounds. Another object of the present invention is to provide an improved process for the preparation of trialkyl phosphites in high yields and wall fractions using a percentage. Another object of the present invention is to provide an improved process for the preparation of trialkyl phosphites. The improved process is environmentally friendly. 1013064654-0 10013455 Production Order No. AOm Page 5 of 29 201221521 Another aspect of the present invention provides an improved method for preparing trisperate. The improved method is economically feasible and less time consuming. . Still another object of the present invention is to provide an improved process which results in the preparation of trialkyl phosphites which are substantially free of impurities. The present invention (4) - a catalogue provides a trialkyl phosphite which is read without _f or contains less than 100 ppm of phenolic impurities. These and other objects of the invention will become apparent from the following detailed description. SUMMARY OF THE INVENTION [0003] According to an aspect of the invention, there is provided an improved method for preparing a molecular formula phosphite:

R ο.R ο.

R bR b

-〇——R 式 子 分 將 含 包 法 方 述 所-〇——R-type sub-segment will contain the method of inclusion

R 鹽 酸 磷 亞 基 烷 三 之R salt phosphorus subunit alkane

R Io/ \o——R P 與分子式111之烷醇 rLoH 醇 腿廳产單編號A0101 * 6頁/共29頁 III201221521 反應,使得Rl代表具有8至16個碳原子的烷基部分體, 以及R代表具有1至3個碳原子的烷基部分體。 在另一方面中,有提供了分子式丨之三烷基亞磷酸鹽化合 物: οR Io / \o - RP and the alkanol rLoH of the formula 111 are produced by the reaction number No. A0101 * 6 pages / 29 pages III201221521, such that Rl represents an alkyl moiety having 8 to 16 carbon atoms, and R Represents an alkyl moiety having from 1 to 3 carbon atoms. In another aspect, there is provided a trialkyl phosphite compound of the formula:

R ο/ \olhR I P I1 \o R 其使得rI代表具有8至16個碳原子的烷基部分體,其中 所述分子式I之化合物大體上沒有酚醛雜質。 【實施方式】 [0004] 本發明藉由如上所描述地將分子式II之三烷基亞磷酸鹽 與分子式III之烷醇反應而提供了製備分子式I之三烷基 亞磷酸鹽的改良方法,其中R1代表具有(^-(:1(:碳原子的 烷基部分體,以及R代表具有\-(:3碳原子的烷基部分體 〇 該反應以下述示意圖的形式表示。不希望被理論限制, 一般相信該反應可能經由該中間產物單烷基亞磷酸鹽以 及二烷基亞磷酸鹽而繼續進行,以產生分子式I之該三炫 基亞磷酸鹽化合物。 用於製備分子式I之三烷基亞磷酸鹽的反應路徑 10013455^^^ A〇101 第7頁/共29頁 1〇13〇64654-〇 201221521 3 -OH 烷醇 分子式 三烷基亞磷醆金 (OR) 3P _分子式〗1 _ 喑段1R ο / \olhR I P I1 \o R such that rI represents an alkyl moiety having 8 to 16 carbon atoms, wherein the compound of formula I is substantially free of phenolic impurities. [Embodiment] The present invention provides an improved process for the preparation of a trialkyl phosphite of formula I by reacting a trialkyl phosphite of formula II with an alkanol of formula III as described above, wherein R1 represents an alkyl moiety having (^-(:1(: carbon atom), and R represents an alkyl moiety having \-(:3 carbon atoms). The reaction is represented in the following schematic form. It is not desired to be limited by theory. It is generally believed that the reaction may continue via the intermediate monoalkyl phosphite and dialkyl phosphite to produce the tripent phosphite compound of formula I. Reaction pathway of phosphite 10013455^^^ A〇101 Page 7 of 29 1〇13〇64654-〇201221521 3 -OH Alkanol molecular formula Trialkylphosphonium ruthenium (OR) 3P _ Molecular Formula 1 _ Section 1

0—R0-R

0—P0-P

R 單烷基亞磷酸鹽 中間產物IR monoalkyl phosphite intermediate I

R 〇-'R \ / 0—P 0I, R 二炫基㈣酸金 中間產物HR 〇-'R \ / 0—P 0I, R dihistyl (tetra) acid gold intermediate H

0一R0-R

0—P0-P

R 三烷基δ磷酸S △ » C - 210 C 喑段11R trialkyl δ phosphoric acid S △ » C - 210 C 喑 segment 11

3R——ΟΗ IV3R - ΟΗ IV

0—R 0—Ρ 三烷基亞磷酸鹽 分子式1 根據一方面,本發明關於藉由如上所描述地將分子式π 之三烷基亞磷酸鹽與分子式ΠΙ之烷醇反應而製備分子式 I之二院基亞填酸鹽的改良方法,其中該反應在不存在催 化劑及/或溶劑下進行。 在—個具體實施例中,本發明的改良方法包含在缺少催 化劑下或缺少溶劑下或缺少催化剤與溶劑下將該分子式 Π之三烷基亞磷酸鹽與該烷醇|^_〇Η反應。 在-個具體實劇巾,分子幻之三统基亞磷_# r 刀體選自範圍為c8-c16,較佳為c9-c15以及更佳為 C10~Ci3的碳鍵。 在-個具體實施例中’分子式m之麟選自具有碳鍵範 圍為C8'c16,較佳為c9-c15以及更佳為(:10-〇13的烷醇。 第8頁/共29頁 單編號A0101 1013064654-0 201221521 在進一步的具體實施例中’分子式II之三烷基亞磷酸鹽 中的R基團選自具有 Ci-C3碳原子的烷基部分體,以及R最 佳為甲基。 根據一個具體實施例,分子式II之三烷基亞磷酸鹽在溫 度範圍在75°c-180°C之間下被加至該分子式III之烷醇 中。 在再另一個具體實施例中,分子式II之三烷基亞磷酸鹽 被加至該分子式III之烷醇,並攪拌〇. 5-7小時。 在進一步的具體實施例中,該分子式ΙΠ之烷醇關於該分 子式II之三烷基亞磷酸鹽是在5 :卜3 : 1的莫耳比中,該 比例較佳為4 : 1。 在另一個具體實施例中’在加入三烷基亞磷酸鹽之後, 將該反應物料加熱至180°C-220°C之間的溫度。該反應 物料被維持在此溫度達允許該反應完全的預定時間期間 在一個具體實施例中,該反應物料被維持在大約18〇。 C-220X的溫度之間,以及維持在此溫度達大約2-4小時 的期間。已發現將該反應物料維持在提升的溫度導致該 標的產物產率的增加。 在一個具體實施例中,前述該反應物料被維持2-4小時之 前述提升的溫度至少在該反應期間所產生之分子式丨7之 醇類副產物R—0H的沸點之上。已發現維持該反應物料的 溫度在至少該醇類副產物的沸點之上導致從該反應系統 同時移除該副產物,其已發現會增加分子式〗之該標的產 物的產率。 1013064654-0 10013455产單编號Α〇101 帛9頁/共29頁 201221521 因此’在此具體實施例巾,在該反應綱,所產生的該 分子式_綱產倾-斷觀應I驗同時移除。該 醇類副產物較健由冷凝ϋ藉由魏冷杨藉由在較低X 溫度冷凝它而回收,而不讓該醇類離開該系統。這是在 操作該反射額外的優勢,其使該方法成本有效且對環 境安全。 因此,在此具體實關巾,本發贿供了肖於製備分子 式I之三烷基亞磷酸鹽的改良方法: &lt; 0-R1 〇一Ρ \ 〇 所述方法包含: (a)藉纟在75H8CTC之間的溫度將分子式π的化合 物加至該騎子朗之三絲0-R 0 —Ρ Trialkyl phosphite Formula 1 According to one aspect, the present invention relates to the preparation of the formula I by reacting a trialkyl phosphite of the formula π with an alkanol of the formula oxime as described above. An improved process for the anhydride acidate wherein the reaction is carried out in the absence of a catalyst and/or solvent. In a specific embodiment, the improved process of the present invention comprises reacting the trialkyl phosphite of the formula with the alkyl alcohol in the absence or absence of a solvent or in the absence of a catalytic hydrazine and a solvent. . In a specific real scarf, the molecular illusion of the genus phosphazone _# r is selected from carbon bonds in the range of c8-c16, preferably c9-c15 and more preferably C10~Ci3. In a specific embodiment, the 'molecular formula m' is selected from the group consisting of alkanols having a carbon bond range of C8'c16, preferably c9-c15 and more preferably (10-〇13). Page 8 of 29 Single No. A0101 1013064654-0 201221521 In a further embodiment, the R group in the trialkyl phosphite of the formula II is selected from the group consisting of an alkyl moiety having a Ci-C3 carbon atom, and R is preferably a methyl group. According to a specific embodiment, the trialkyl phosphite of formula II is added to the alkanol of formula III at a temperature ranging from 75 ° C to 180 ° C. In yet another embodiment, The trialkyl phosphite of the formula II is added to the alkanol of the formula III and stirred for 5-7 hours. In a further embodiment, the alkylalkanol of the formula is related to the trialkyl group of the formula II The phosphite is in a molar ratio of 5:3:1, preferably in a ratio of 4: 1. In another embodiment, after the addition of the trialkyl phosphite, the reaction mass is heated to a temperature between 180 ° C and 220 ° C. The reaction mass is maintained at this temperature to allow the reaction to be complete. In a specific embodiment, the reaction mass is maintained between about 18 Torr. between C-220X and maintained at this temperature for a period of about 2-4 hours. It has been found that the reaction mass is maintained at The elevated temperature results in an increase in the yield of the target product. In one embodiment, the foregoing reaction mass is maintained for a period of 2-4 hours of the elevated temperature of at least the alcoholic by-product of the formula 丨7 produced during the reaction. Above the boiling point of R-0H, it has been found that maintaining the temperature of the reaction mass above at least the boiling point of the alcohol by-product results in simultaneous removal of the by-product from the reaction system, which has been found to increase the product of the formula The yield of 1013064654-0 10013455, the production number Α〇101 帛9 pages/total 29 pages 201221521 Therefore, the specific embodiment of the towel, in the reaction class, the molecular formula produced _ Simultaneous removal of the alcohol. The alcohol by-product is more robust by condensation and is cooled by condensing it at a lower X temperature without allowing the alcohol to leave the system. Excellent The method makes the method cost-effective and environmentally safe. Therefore, in this specific case, the bribe is provided by an improved method for preparing the trialkyl phosphite of formula I: &lt; 0-R1 〇一Ρ \ 〇 The method comprises: (a) adding a compound of formula π to the rider's third wire by means of a temperature between 75H8CTC

Ro—/p、o—R I\o R 與分子式III的燒醇rl〇h反應,以使得Rl代表 具有8至16個碳原子眺基部分體,以及狄表具有㈤ 100134551*^ A〇101 第10頁/共29頁 1013064654-0 201221521 個碳原子的烷基部分體; (b) 維持該反應物料在至少具有1至3個碳原子之烷醇 的沸點溫度之上達預定時間期間而同步地移除在該反應 期間產生的該分子式IV醇類副產物R—〇H ;以及 (c) 藉由過濾而回收該分子式I的標的化合物; 其中該改良包含在缺少催化劑或缺少溶劑或缺少 催化劑以及溶劑下將該分子式Π之三烷基亞磷酸鹽與該 烷醇反應。 在一個具體實施例中’在上述步驟(b)完成之後,在鈍氣 〇 下冷卻該反應物料。該較佳的鈍氣是氮。將該冷卻的反 應物料在80-100DC下經歷真空,以移除任何該醇類副產 物的殘餘物。 在一個具體實施例中,該反應物料再次在1-2麵真空下 被加熱至ig〇_2Q[|DC達足夠的時間期間,以移除任何剩餘 微量的醇類。 在一個具體實施例中’該反應在其後被冷卻,較佳冷卻 〇 至大約40°c的溫度,以及藉由過濾回收該標的化合物。 因此,在另一個具體實施例中’本發明提供了用於製備 分子式I之三烷基亞磷酸鹽的改良方法: Ό—R1 0——p \ 〇 I,Ro—/p, o—RI\o R is reacted with the alcoholic alcohol rl〇h of the formula III such that R1 represents a thiol moiety having 8 to 16 carbon atoms, and the digraph has (5) 100134551*^ A〇101 10 pages/total 29 pages 1013064654-0 201221521 alkyl moiety of carbon atom; (b) maintaining the reaction mass synchronously shifting over the boiling temperature of the alkanol having at least 1 to 3 carbon atoms for a predetermined period of time Except for the alcoholic by-product R-〇H of the formula IV produced during the reaction; and (c) recovering the target compound of the formula I by filtration; wherein the improvement is contained in the absence of a catalyst or lack of a solvent or lack of a catalyst and a solvent The trialkyl phosphite of the formula is reacted with the alkanol. In a specific embodiment, after completion of step (b) above, the reaction mass is cooled under a blunt gas. The preferred inert gas is nitrogen. The cooled reaction mass was subjected to a vacuum at 80-100 DC to remove any residue of the alcohol by-product. In one embodiment, the reaction mass is again heated to ig 〇 2Q [|DC for a sufficient period of time under 1-2 vacuum to remove any remaining traces of alcohol. In a specific embodiment, the reaction is thereafter cooled, preferably cooled to a temperature of about 40 ° C, and the target compound is recovered by filtration. Thus, in another embodiment, the invention provides an improved process for the preparation of a trialkyl phosphite of formula I: Ό-R1 0 - p \ 〇 I,

R 第11頁/共29頁 10013455产·單編號 A0101 201221521 所述方法包含: (a) 藉由將分子式II的化合物在 75eC&quot;18(TC之間的溫 度下’在至少0.5小時的期間緩慢地加至該分子式in的 垸醇RLOH中,以及在將該分子式II的化合物加至所述 燒醇完成之後,將分子式II之三烧基亞填酸鹽 〇—pR Page 11 of 29 10013455 Production · Single Number A0101 201221521 The method comprises: (a) by slowly bringing the compound of formula II at a temperature between 75 ° C &quot; 18 (TC) for at least 0.5 hours Addition to the sterol RLOH of the formula in, and after the addition of the compound of the formula II to the aniolate, the tribasic acid ylide of the formula II

〇——R 與分子式III的烷醇 F^-OH反應’以使得p 1代表 具有8至16個碳原子烷基部分體,以及R代表具有1至3個 碳原子的烷基部分體, (b) 維持該反應物料在至少具有1至3個碳原子之烷醇 的沸點上溫度達預定時間期間而同步地移除在該反應期 間產生的該醇類副產物R—0H ; (c) 隨選地,在鈍氣下冷卻該反應產物; (d) 在1-2腿真空壓力下將該冷卻的反應產物加熱至 19D_2GD0C達足夠的時間期間;以及 (e) 將該反應產物冷卻至大約 400C的溫度,以及藉由 過渡回收該分子式I的化合物; 其中該改良包含在缺少催化劑或缺少溶劑或缺少 催化劑以及溶劑下將該分子式II之三烷基亞碟酸鹽與該 烧醇反應。 10013455^^'^^ A0101 第12頁/共29頁 1013064654-0 201221521 在進一步的具體實施例中,在大約75。〇180。(:的提升溫 度下將該分子式II之三烷基亞磷酸鹽被加至該分子式ΠΙ 之燒醇中’隨選地維持在相同溫度達〇_6小時,然後將該 反應溫度提升至大約195°C-21(TC ’並在相同溫度下授 拌大約2-4小時’以於高產率以及純度而得到所想要的分 子式I之三烷基亞磷酸鹽。 在再另一個具體實施例中’在3-7小時中’在17〇。〇180 C下將亞填酸三甲酯加至該燒醇中,接著在丨95。(;-21〇。 C擾摔大約2-4小時。 在一個具體實施例中,藉由本技術領域中已知的方法分 離該產物。 在一個具體實施例中,以多於85%產率獲得該分子式I之 三烷基亞磷酸鹽。 在此說明書中所描述的該方法是完全沒有溶劑以及沒有 催化劑的,其使該方法是環保的。已令人驚訝地發現, 相較於使用催化劑及/或溶劑的傳統方法,在缺少溶劑及 /或催化劑下,該分子式I的標的化合物以令人驚訝的較 高產率形成。因此,已令人驚訝地發現,在缺少催化劑 及/或溶剤下,源自起始三烷基亞磷酸鹽之初始磷含量的 利用百分比被最大化。 因此,本發_方法完全齡了具有絲部分體之起始 反應物的使用《本發明人已發現消除具有芳基部分體的 起始材料導致形成大體上沒有酚醛雜質的三炫基亞填酸 鹽化合物。 因此,在此方面,本發明提供了分子式丨的三烷基亞磷酸 鹽化合物: 束單編號A0101 10013455广 第13頁/共29頁 1013064654-0 201221521〇-R is reacted with an alkanol F^-OH of formula III such that p 1 represents an alkyl moiety having 8 to 16 carbon atoms, and R represents an alkyl moiety having 1 to 3 carbon atoms, b) maintaining the temperature of the reaction mass at a boiling point of the alkanol having at least 1 to 3 carbon atoms for a predetermined period of time while synchronously removing the alcohol by-product R-0H produced during the reaction; (c) Optionally, cooling the reaction product under blunt gas; (d) heating the cooled reaction product to 19D_2GD0C under a vacuum pressure of 1-2 legs for a sufficient period of time; and (e) cooling the reaction product to about 400C The temperature, and the recovery of the compound of formula I; wherein the modification comprises reacting the trialkyl sulfite of formula II with the animate in the absence or absence of a solvent or a lack of a catalyst and a solvent. 10013455^^'^^ A0101 Page 12 of 29 1013064654-0 201221521 In a further embodiment, at approximately 75. 〇180. (The trialkyl phosphite of formula II is added to the oleanol of the formula ' at the elevated temperature of '', optionally maintained at the same temperature for 〇6 hours, and then the reaction temperature is raised to about 195 °C-21 (TC 'and at about the same temperature for about 2-4 hours' to obtain the desired trialkyl phosphite of formula I in high yield and purity. In yet another embodiment 'In 3-7 hours' at 17 〇. Trimethyl sulphate was added to the alcohol at 〇180 C, followed by 丨95. (;-21 〇 C disturbed for about 2-4 hours. In a particular embodiment, the product is isolated by methods known in the art. In a particular embodiment, the trialkyl phosphite of formula I is obtained in more than 85% yield. The process described is completely solvent free and catalyst free, which makes the process environmentally friendly. It has been surprisingly found that in the absence of solvents and/or catalysts compared to conventional processes using catalysts and/or solvents , the target compound of formula I is surprisingly higher yield Thus, it has been surprisingly found that in the absence of catalyst and/or lysing, the percentage of utilization of the initial phosphorus content derived from the starting trialkyl phosphite is maximized. Therefore, the present method is completely old. Use of the starting reactant having a silk moiety "The inventors have found that the elimination of a starting material having an aryl moiety results in the formation of a trisyl sub-salt compound which is substantially free of phenolic impurities. Thus, in this regard, The present invention provides a trialkyl phosphite compound of the formula :: bundle number A0101 10013455 wide page 13 / total 29 page 1013064654-0 201221521

1- R ί 1 I ο/ \OIR p I \o R ,、使得Ri代表具有8至16個碳原子的淀基部分體其中 舰分子式I的化合物大體上沒有_雜質。 該用語「大體上沒有」在本文中意欲意指三燒基亞猶 鹽完全沒有祕雜質,或包含少於1〇〇 _的盼搭雜質。 該用語「祕雜質」意指可從驗衍生及/或包括經基被取 代成苯環或比該起始三芳基亞碟酸鹽化合物更高度取代 之盼酸化合物的所有化合物。 本發明的具體實施例在下表中解釋。 下述範例被呈現以更完整地定義本發明,而沒有被其限 制的任何意圖。除非另外具體說明,所有的百分比以及 比例為重量百分比與重量比例。 範例1 在曱醇納的存在下製備亞碟酸三異癸酯。 在乾淨的乾反應燒瓶中,在n2氣下加入316卿的異癸醇 並授拌5分鐘。然後加入〇. 45 gm的甲醇鈉並攪拌。然後 將該溫度提升至75。0然後在〇.5小時中將63卿的亞磷 酸三甲酯加至異癸醇中,同時維持該溫度。然後將該反 應溫度提升至195-20ITC,並將該反應物料在相同溫度 下攪拌2小時。在該方法期間,作為副產物而產生的甲醇 10013455产单編號A0101 第I4頁/共29頁 1013064654-0 201221521 被同時移除。將該反應物料在 N2氣下冷卻至8〇-l〇〇°C, 同時施加真空以回收該異癸醇。然後在卜2 nun真空下將 該反應物料維持在190-200°C,以移除微量的異癸醇。 然後在N2下允許該溫度來到4〇°C,並在過濾之後回收該 產物。 該產物的產率:82.47% 酚醛含量:NIL 範例2 不使用曱醇鈉而製備亞磷酸三異癸酯。 在乾淨的乾反應燒瓶中,在 N2氣下加入316 gra的異癸醇 並攪拌5分鐘》然後將該溫度提升至75°C。然後在0. 5小 時中將63 gm的亞磷酸三甲酯加至異癸醇令,同時維持該 溫度。然後將該反應溫度提升至195-20(TC,並將該反 應物料在相同溫度下擾拌2小時。在該方法期間,作為副 產物而產生的曱醇被同時移除。將該反應物料在 叫氣下 冷卻至80-100°C ’同時施加真空以回收該異癸醇 '然後 Ο 在1-2 ram真空下將該反應物料維持在190-20(TC,以移 除微量的異癸醇。然後在 |S|2下允許該溫度來到40。0,並 在過濾之後回收該產物。 該產物的產率:93.82% 酚醛含量:NIL 範例3 亞磷酸三異癸酯的製備: 在乾淨的乾反應器中’在 1\|2氣下加入2743 Kg的異癸醇 1013064654-0 並授拌5分鐘。然後將該溫度提升至95°C。然後在將溫度 10013455产單編號AOm 第15頁/共29頁 201221521 維持在95-98°C之間的方式將後將542 Kg的亞填酸三甲 醋加至異癸醇中(總加入時間5小時)。然後將該反應溫 度提升至19{TC-20(TC,並將該反應物料在相同溫度下 挽拌2小時。在該方法期間,作為副產物而產生的曱醇藉 由冷凝作用而被同時移除以及回收。將該反應物料在 ^ 氣下冷卻至80-l〇(rc ’同時施加真空以回收該微量的醇 類。然後在1-2 mm真訂賴反應物料轉在⑽―2〇〇。 C,以移除最後微量的異癸醇。然後在咏下允許該溫度來 到40 C,並在過濾之後回收該產物。 該產物的產率:92% 在25°C的比重:〇.88〜〇 9阳 在25°C的折射率:145〜丨46ι〇 酚醛含量:NIL 也使用上述範例1-3中所於m 田迷的方法進行下述範例 表1 1〇〇13455产單編號 A0101 [0005]1-R ί 1 I ο / \OIR p I \o R , such that Ri represents a aryl moiety having 8 to 16 carbon atoms wherein the compound of formula I is substantially free of _impurities. The phrase "substantially absent" is intended herein to mean that the tricarboyl sulphate is completely free of secret impurities or contains less than 1 〇〇 _ of the desired impurities. The term "secret impurity" means all compounds which may be derived from the test and/or include an acid-substituting compound which is substituted with a benzene ring or more highly substituted than the starting triaryl sulfonate compound. Specific embodiments of the invention are explained in the table below. The following examples are presented to more fully define the invention without any intent. All percentages and ratios are by weight to weight ratio unless otherwise specifically stated. Example 1 Preparation of triisodecyl oxalate in the presence of sodium sterol. In a clean dry reaction flask, 316 g of isodecyl alcohol was added under n2 gas and allowed to mix for 5 minutes. Then add 45 gm of sodium methoxide and stir. The temperature was then raised to 75. 0 and then 63 qing of trimethyl phosphite was added to isodecyl alcohol while maintaining the temperature. The reaction temperature was then raised to 195-20 ITC and the reaction mass was stirred at the same temperature for 2 hours. During the process, methanol 10013455 produced as a by-product number A0101, page I4, page 29, 1013064654-0, 201221521 was simultaneously removed. The reaction mass was cooled to 8 〇 - 10 ° C under N 2 gas while a vacuum was applied to recover the isodecyl alcohol. The reaction mass was then maintained at 190-200 ° C under vacuum to remove traces of isodecyl alcohol. This temperature was then allowed to reach 4 ° C under N2 and the product was recovered after filtration. Yield of the product: 82.47% Phenolic content: NIL Example 2 Triisodecyl phosphite was prepared without using sodium decoxide. In a clean dry reaction flask, 316 gra of isodecyl alcohol was added under N2 gas and stirred for 5 minutes" and then the temperature was raised to 75 °C. Then, 63 gm of trimethyl phosphite was added to isodecyl alcohol in 0.5 hour while maintaining the temperature. The reaction temperature was then raised to 195-20 (TC) and the reaction mass was scrambled for 2 hours at the same temperature. During this process, the sterol produced as a by-product was removed simultaneously. Cool down to 80-100 ° C ' while applying vacuum to recover the isodecyl alcohol' and then maintain the reaction mass at 190-20 (TC) under 1-2 ram vacuum to remove traces of isodecyl alcohol. The temperature was then allowed to reach 40. 0 under |S|2 and the product was recovered after filtration. Yield of the product: 93.82% Phenolic content: NIL Example 3 Preparation of triisodecyl phosphite: in a clean In the dry reactor, add 2743 Kg of isodecyl alcohol 1013064654-0 under 1⁄2 gas and mix for 5 minutes. Then raise the temperature to 95 ° C. Then the temperature is 10013455. Page / Total 29 pages 201221521 Maintained at a temperature between 95-98 ° C, then add 542 Kg of sub-acid trimethyl vinegar to isodecyl alcohol (total addition time 5 hours). Then raise the reaction temperature to 19 {TC-20 (TC, and the reaction material was mixed at the same temperature for 2 hours. During the method, as The sterol produced by the product is simultaneously removed and recovered by condensation. The reaction mass is cooled to 80-l 〇 (rc ' while applying a vacuum to recover the trace amount of alcohol. Then at 1- The 2 mm true reaction material was transferred to (10) - 2 Torr C to remove the last trace of isodecyl alcohol. The temperature was then allowed to come to 40 C under the helium and the product was recovered after filtration. Yield: 92% Specific gravity at 25 ° C: 〇.88~〇9 阳 Refractive index at 25 ° C: 145 ~ 丨 46 〇 phenolic content: NIL Also used in the above examples 1-3 Method for the following example Table 1 1〇〇13455 Production Order No. A0101 [0005]

第16頁/共29頁 反應條 回收的 產率gm 件 烷醇 (%) 在5小時 1,1 —--- 曱醇-90 ---—_ 474 中在 gm ; (94.42) 95-100 異癸醇 °C下加 -179 入TMP ; gm 在 195-207 頁 --- 1013064654-0 201221521Page 16 of 29 Reactive Columns Recovered Yield gm of Alkanol (%) in 5 hours 1,1 —---sterol-90 --- — _ 474 in gm ; (94.42) 95-100 Isodecyl alcohol °C plus -179 into TMP; gm at 195-207 pages --- 1013064654-0 201221521

°C攪拌2 小時。 2 TMP ; 異癸醇 在70-80 甲醇-90 471 125 ;632 〇c加入 gm ; (93.82) TMP ;攪 異癸醇 拌0. 5小 -179 時;在 gm 195-207 °C攪拌2 小時。 3 TMP ; 異癸醇 在70-80 甲醇-82 472 125 ;632 。(:加入 gm ; (94) TMP ;攪 異癸醇 拌9. 5小 -181 時;在 gm 195-207 °C攪拌2 小時。 4 TMP ; 異十三 在 甲醇-95 583 125 烧醇; 80-140 gm ; (92. 83) 800 X加入 異十三 TMP,攪 烧醇 拌3小時 -237 45分鐘 gm ;在 195-200 第17頁/共29頁 1013064654-0 100134551^單編號 A〇101 201221521 ! 丨°C攪拌2Stir at °C for 2 hours. 2 TMP; isodecyl alcohol in 70-80 methanol-90 471 125; 632 〇c added to gm; (93.82) TMP; isopropanol mixed 0. 5 small -179 hours; stirred at gm 195-207 °C for 2 hours . 3 TMP; isodecyl alcohol in 70-80 methanol - 82 472 125 ; 632 . (: Add gm; (94) TMP; stir isopropanol to mix 9.5 min -181; stir at gm 195-207 °C for 2 hours. 4 TMP; isotritate in methanol-95 583 125 ani alcohol; -140 gm ; (92. 83) 800 X added isotritium TMP, stir-fry alcohol for 3 hours -237 45 minutes gm; at 195-200 page 17 / 29 pages 1013064654-0 100134551^ single number A〇101 201221521 ! 丨 °C mixing 2

I ____I 小時。 TMP :本文中所指的是亞磷酸三甲^ 美國專利編號3636145揭露了以高產率、高純度並以極快 反應速率以及藉由牽涉亞磷酸三曱酯以及烷醇之轉酯化 作用的大量製造之合適方法而製備三烷基亞磷酸鹽的方 法。該所述反應實質在鹼性催化劑的存在下以及在非共 沸溶劑的存在下執行。令人驚訝的是,本發明的發明人 已發現該最終產物的產率在催化劑及/或溶劑會下降。 序號 TMP (gm ) 異癸醇 (gm) 甲醇鈉 (gm) -___—— 反應條 件 產率 (°/〇) ------ 1 63 316 0.45 在70-80 °C加入 TMP ;在 195-200 °C攪拌2 小時。 85.25 I i _____--— 2 63 316 在70-80 °C加入 TMP ;在 195-200 °C攪拌2 小時。 93.82 3 63 316 0.45 在70-80 °C加入 _ __一-— 82.47 _____一—------------ 10013455产單編號 A〇m 第 18 頁 / 共 29 頁 1013064654-0 201221521I ____I hours. TMP: referred to herein as trimethyl phosphite. US Pat. No. 3,636,145 discloses mass production in high yield, high purity and very fast reaction rate and by transesterification involving tridecyl phosphite and alkanol. A method of preparing a trialkyl phosphite by a suitable method. The reaction is substantially carried out in the presence of a basic catalyst and in the presence of a non-azeotropic solvent. Surprisingly, the inventors of the present invention have found that the yield of the final product decreases in the catalyst and/or solvent. No. TMP (gm) Isodecyl alcohol (gm) Sodium methoxide (gm) -___ - Reaction conditions Yield (°/〇) ------ 1 63 316 0.45 Add TMP at 70-80 °C; Stir at -200 °C for 2 hours. 85.25 I i _____--— 2 63 316 Add TMP at 70-80 °C; stir at 195-200 °C for 2 hours. 93.82 3 63 316 0.45 Add at 70-80 °C _ __一 - 82.47 _____一 —------------ 10013455 Order No. A〇m Page 18 of 29 1013064654 -0 201221521

~~一-- TMP ;在 85-90° C攪拌9 小時; 在 195-200 °C攪拌2 小時。 4 63 316 —— — 在70-80 。(:加入 TMP;在 85-90° C攪拌9 小時; 在 195-200 °C攪拌2 小時。 94 從表2得到證據顯示’當在缺少驗性催化劑下進行該反應 時’獲得了該產物的較高產率。甚至在缺少該非共彿溶 劑下,該反應產率是更高的。 餘.你丨4-14 下表顯示了 具有碳鏈範Μ 之分子式IU炫醇 以及使用分子式II之三烷基亞磷酸鹽進行的實驗,該分 子式III烷醇以及分子式11之三烷基亞磷酸鹽選自具有 100134551^^^ A〇101 第19頁/共29頁 1013064654-0 201221521 -c3碳原子的燒基部分體。在大約75&lt;ϊ(:_ιι(Γ{^提升溫 度下將该二烷基亞磷酸鹽加至該烷醇中,然後將該反應 溫度提升至大約195X-2HTC,並在相同溫度下攪拌大 約2-4小時’以得到想要的三烷基亞磷酸鹽。以多於850/〇 的產率獲得各自的三烷基亞麟酸鹽。觀察到當使用像是 Cm的較高級醇類時,該反應不以想要的速率以及想要的 產率繼續進行。 A1 範 例 編 m 所使用原始 材料的量 CTMP/TEP /TIPP) 力α入溫度 C TMP/T EP/TIPP )階段1 TIVIP/TE P/TIPP 加入時間 (階段 1) 憐第溫 度 階段2 回收烷酵 Λ 最終產物 Ά %產率 102 gm 217 gm 86.45 4 TMP=62gm 異癸醇 -316gm 都在室溫 下混合 〇分鐘- 在19〇 z〇〇°c 卞2小 時 — 5 99 gm 182 gm 86.95 TMP=62gm 辛酵 ^eigm 95-1050C 4小時 15分鏟 在18U 下2小 時 77 gm 192 gm 91.72 6 , TMP—e2gm 辛醇 =261gm 98-101 4小時 2〇3&quot;C 下2小 時 ___ — 聚合質置 Ύ TMP=s31gm 十八酵 =271 gm 95-100°C 3小時 40分鐘 Z6〇〇C 卞3小 時 — 聚合質Λ 8 TMP=23gm 十八醇 s=200gm 95-1000C 3小時 30分鎳 -\&amp;Cb 22&amp;^C 下2小 時 63 gm 104 gm 87.33 9 TMP=22gm 1-十四酵 =161gm 95-1030C 3小時 2〇2&quot;C 下2小 時 l〇〇m55产單編號A0101 第20頁/共29貢 1013064654-0 201221521 [0006] Ο [0007]~~1 - TMP; stirred at 85-90 ° C for 9 hours; stirred at 195-200 ° C for 2 hours. 4 63 316 —— — at 70-80. (: Add TMP; stir at 85-90 ° C for 9 hours; stir at 195-200 ° C for 2 hours. 94 Obtain evidence from Table 2 that 'when the reaction is carried out in the absence of an inert catalyst', the product is obtained. Higher yield. Even in the absence of the non-co-solvent, the yield of the reaction is higher. I. 丨 4-14 The following table shows the molecular formula IU sterol with carbon chain enthalpy and the use of the trioxane of formula II. The experiment conducted by the phosphite, the alkyl alcohol of the formula III and the trialkyl phosphite of the formula 11 are selected from the group consisting of 100134551^^^^〇 101 page 19/29 pages 1013064654-0 201221521 -c3 carbon atoms a base moiety. The dialkyl phosphite is added to the alkanol at about 75 ϊ(:_ιι(Γ{^ elevated temperature, and then the reaction temperature is raised to about 195X-2HTC, and at the same temperature Stir for about 2-4 hours to give the desired trialkyl phosphite. The respective trialkyl linoleate was obtained in more than 850/〇 yield. Observed when using a higher grade like Cm In the case of alcohols, the reaction does not proceed at the desired rate and the desired yield. M The amount of raw material used is CTMP/TEP /TIPP) Force α into temperature C TMP/T EP/TIPP ) Stage 1 TIVIP/TE P/TIPP Addition time (stage 1) Pity temperature stage 2 Recovery of alkaloids Final Product Ά % yield 102 gm 217 gm 86.45 4 TMP = 62 gm Isodecyl alcohol - 316 gm were mixed at room temperature for 〇 min - at 19 〇 z 〇〇 ° c 卞 2 hours - 5 99 gm 182 gm 86.95 TMP = 62 gm xin Yeast ^eigm 95-1050C 4 hours 15 minutes shovel at 18U 2 hours 77 gm 192 gm 91.72 6 , TMP-e2gm octanol = 261gm 98-101 4 hours 2 〇 3 &quot; C 2 hours ___ — Polymerization TMP=s31gm Eighteen yeast=271 gm 95-100°C 3 hours 40 minutes Z6〇〇C 卞3 hours—polymerization Λ 8 TMP=23gm octadecyl alcohol s=200gm 95-1000C 3 hours 30 minutes nickel-\&amp ;Cb 22&^C 2 hours 63 gm 104 gm 87.33 9 TMP=22gm 1-fourteen yeast=161gm 95-1030C 3 hours 2〇2&quot;C 2 hours l〇〇m55 order number A0101 Page 20/ Total 29 tribute 1013064654-0 201221521 [0006] Ο [0007]

10 TMP=22gm 1-十四醇 = 161gm 94-101 °C 4小時 在 190-200°C 下2小 時 62 gm 103 gm 87.49 11 TMP-21gm [十六烷醇 = 168 gm 95-100^0 3小時 在 190-2O0°C 下2小 時 58 gm 114 gm 89.12 12 TMP=21gm Ί-十六烷醇 = 168 gm 95-1000C 4小時 在 190-202。。 下2小 時 57 gm 115 gm 90.08 13 TEP=84gm 異癸醇 =316gm 95-1000C 4小時 30分鐘 在 190-202eC 下2小 時 92 gm 240 gm 95.61 14 TIPP=84gm 異癸醇 =250gm 95-1 QO°C 4小時 15分鐘 在 191-2000C 下2小 時 92 gm 170 gm 89.26 ΤΜΡ :本文中所指的是亞磷酸三曱酯 ΤΕΡ :本文中所指的是亞磷酸三乙酯 ΤΙΡΡ :本文中所指的是亞磷酸三異丙酯 酚含量 上述所有製備的所有樣本針對它們的純度而被分析。發 現酸值(mgKOH/gm)在0. 0072-0. 041變化。該樣本的 比重從0. 8866變化至0. 8905。令人驚訝的是,發現在所 有該製備樣本中的酚含量是NIL。 前述參考是針對具有已知均等物的組成,然後這種均等 物如同個別提及而在本文中併入。因此,將領略的是, 可對上述描述的方面以及本發明具體實施例做出改變, 而不悖離本文中所教導的原理。在考慮如同所討論以及 描繪之特定形式的原理之後,本發明的額外優勢對於本 領域的技術人員將變得顯而易。因此,將了解的是,本 發明不限於所描述或描繪的特定具體實施例,但意欲涵 1013064654-0 蓋在本發明範圍内的替代或修飾。 1(){)134551^單編號 A0101 第 21 頁 / 共 29 頁 201221521 【圖式簡單說明】 [0008] 【主要元件符號說明】 [0009] 100134551^^ A〇101 第22頁/共29頁 1013064654-010 TMP=22gm 1-tetradecyl alcohol = 161gm 94-101 °C 4 hours at 190-200 ° C for 2 hours 62 gm 103 gm 87.49 11 TMP-21gm [ cetyl alcohol = 168 gm 95-100^0 3 Hour at 190-2O0 °C for 2 hours 58 gm 114 gm 89.12 12 TMP = 21 gm Ί-cetyl alcohol = 168 gm 95-1000 C 4 hours at 190-202. . 2 hours 57 gm 115 gm 90.08 13 TEP=84gm isodecyl alcohol = 316gm 95-1000C 4 hours 30 minutes at 190-202eC 2 hours 92 gm 240 gm 95.61 14 TIPP=84gm isodecyl alcohol = 250gm 95-1 QO° C 4 hours 15 minutes at 191-2000C 2 hours 92 gm 170 gm 89.26 ΤΜΡ: referred to herein as tridecyl phosphite ΤΕΡ: referred to herein as triethyl phosphite ΤΙΡΡ: as referred to herein Is the triisopropyl phosphite phenol content All of the samples prepared above were analyzed for their purity. 041变化。 The acid value (mgKOH / gm) was changed at 0. 0072-0. The weight of the sample changed from 0. 8866 to 0. 8905. Surprisingly, the phenol content found in all of the prepared samples was NIL. The foregoing references are directed to compositions having known equivalents, and such equivalents are incorporated herein by reference. Therefore, it will be apparent that changes may be made to the above described aspects and embodiments of the invention without departing from the principles of the teachings herein. The additional advantages of the present invention will become apparent to those skilled in the art after considering the principles of the particular form discussed and illustrated. Therefore, it is understood that the invention is not limited to the specific embodiment shown or described, but is intended to be a substitute or modification within the scope of the invention. 1(){) 134551^Single number A0101 Page 21 of 29201221521 [Simplified illustration] [0008] [Explanation of main component symbols] [0009] 100134551^^ A〇101 Page 22 of 29 1013064654 -0

Claims (1)

201221521 七、申請專利範圍: 1 . 一種用於製備分子式I之三烷基亞磷酸鹽的改良方法: 1- R 〇 0-¾ I P - 1 \o R 所述方法包含將分子式11之三烷基亞磷酸鹽 R ο/ \o——R-P \o R 與分子式III之烷醇f-OH反應,以使得R1代表具 有8至16個碳原子的一烷基部分體,以及R代表具有1至3 個碳原子的一烷基部分體。 2 .如申請專利範圍第1項所述的方法,其中在缺少一催化劑 或缺少一溶劑或缺少一催化劑以及一溶劑下,將分子式11 之該三烷基亞磷酸鹽與該烷醇rLoh反應。 3 .如申請專利範圍第1項所述的方法,其中在75°C-180°C 之間的一溫度範圍將分子式II之該三烷基亞磷酸鹽加至所 述炫《醇。 4 .如申請專利範圍第3項所述的方法,其中在0.5-7小時的 一時期期間將所述烷基亞磷酸鹽加至分子式ΙΠ之該烷醇 10013455!^單編號删1 第23頁/共29頁 1013064654-0 201221521 5 ·如申請專利範圍第1—4項所述的方法,其中所述烧基亞碟 酸鹽以及所述烷醇以1 : 3至1 : 5的一莫耳比例被添加。 6 ·如申請專利範圍第丨項所述的方法,其中分子式ΙΠ之該 烧醇選自包含異癸醇、異十三院醇、辛醇、十四醇以及十 六烷醇的群組。 7 .如申請專利範圍第1項所述的方法,其中分子式II之該三 烧基亞磷酸鹽選自包含亞磷酸三乙酯、亞磷酸三甲酯以及 亞鱗酸三異丙醋的群組。 8. 如申請專利範圍第1項所述的方法,更包含藉由冷凝作用 回收該反應的分子式IV之醇類副產物R-0H的步驟。 9. 一種用於製備分子式I之三烷基亞磷酸鹽的改良方法: Rv 〇一¥ \ 〇 R1 所述方法包含: (a) 藉由在75。0180。0之間的一溫度下將分子式Π的 該化合物加至烷醇 ri_〇h,將分子式II之三烷基亞磷酸鹽 R\ 0—R 0—P \ 〇 I R 1013064654-0 1〇0丨3455产單蝙號 A0101 1丨 第24頁/共29頁 201221521 與刀子式1u的該烧醇rl〇h反應,以使得R1代 表具有8至16個碳原子的一烷基部分體,以及R代表具有1 至3個碳原子的一烷基部分體; ⑹將該反應物料至少維持在具有i至3個碳原子的一 烧醇的/弗點之上的-溫度達一預定時間期間而同步地移除 該反應的期間產生的該醇類副產物卜〇H;以及 (c)藉由過渡回收分子式!的該標的化合物。 10 .如巾請專利細第9項所述財法,其中在缺少—催化劑 或缺少一溶劑或缺少一催化劑以及一溶劑下將分子式〖!之 該三烧基亞填酸鹽與該燒醇反應β 11 .如申請專利範圍第9項所述的方法,其中在該醇類副產物 之該沸點之上的所述溫度是從18〇χ至約220Χ。 12 .如申請專利範圍第9項所述的方法,其中所述預定時間期 間是從大約2小時至大約4小時。 13 .如申請專利範圍第9項所述的方法,包含在使其受到步驟 (b)之前,在一鈍氣中冷卻在步驟(a)的最後獲得之該反 應物料。 14. 一種用於製備分子式I之三烷基亞磷酸鹽的改良方法: &lt; 0-R1 0 - P: 〇 100134551^單編號删1 第25頁/共29頁 1013064654-0 201221521 所述方法包含: (a) 藉由在75。〇180。〇之間的一溫度下,在至少0. 5小 ^的一 _朗將分子式Π的化合物缓慢地加至該烧醇 RLOH中’以及在完成將分子式丨丨的該化合物加至所述貌 醇之後,將分子式II之三烷基亞磷酸鹽201221521 VII. Patent Application Range: 1. An improved method for preparing a trialkyl phosphite of formula I: 1-R 〇0-3⁄4 IP - 1 \o R The method comprises a trialkyl group of formula 11 The phosphite R ο / \o - RP \o R is reacted with the alkanol f-OH of the formula III such that R1 represents an alkyl moiety having 8 to 16 carbon atoms, and R represents 1 to 3 a monoalkyl moiety of one carbon atom. 2. The method of claim 1, wherein the trialkyl phosphite of formula 11 is reacted with the alkanol rLoh in the absence of a catalyst or lack of a solvent or lack of a catalyst and a solvent. 3. The method of claim 1, wherein the trialkyl phosphite of the formula II is added to the damolol at a temperature ranging from 75 °C to 180 °C. 4. The method of claim 3, wherein the alkyl phosphite is added to the molecular formula of the alkanol 10013455 during a period of 0.5-7 hours! The method of claim 1, wherein the alkyl sulfonate and the alkanol are in a molar ratio of 1:3 to 1:5. Added. 6. The method of claim 2, wherein the alcoholic alcohol of the formula is selected from the group consisting of isodecyl alcohol, isotrienol, octanol, tetradecanol, and cetyl alcohol. 7. The method of claim 1, wherein the trialkyl phosphite of formula II is selected from the group consisting of triethyl phosphite, trimethyl phosphite, and triisopropyl sulphate. . 8. The method of claim 1, further comprising the step of recovering the alcohol by-product R-0H of the formula IV by condensation. 9. An improved process for the preparation of a trialkyl phosphite of formula I: Rv 〇 \ \ 1 R1 The method comprises: (a) by formulating a temperature at a temperature between 77.000.8 The compound of hydrazine is added to the alkanol ri_〇h, and the trialkyl phosphite of formula II R\0-R 0-P \ 〇IR 1013064654-0 1〇0丨3455 is produced as a single bat number A0101 1丨24 pages/total 29 pages 201221521 The calcined alcohol rl〇h of the knife formula 1u is reacted such that R1 represents a monoalkyl moiety having 8 to 16 carbon atoms, and R represents a one having 1 to 3 carbon atoms. An alkyl moiety; (6) the reaction material is maintained at a temperature above at least one of the ani alcohols having from i to 3 carbon atoms for a predetermined period of time while the reaction is removed synchronously An alcohol by-product, DiH; and (c) the target compound by a molecular recovery formula. 10. For example, please refer to the financial method described in Item 9 of the patent, in which the formula is in the absence of a catalyst or lack of a solvent or a catalyst and a solvent. The method of claim 9, wherein the temperature above the boiling point of the alcohol by-product is from 18 〇χ. To about 220 baht. 12. The method of claim 9, wherein the predetermined time period is from about 2 hours to about 4 hours. 13. The method of claim 9, comprising cooling the reaction material obtained at the end of step (a) in an inert gas before subjecting it to step (b). 14. An improved process for the preparation of a trialkyl phosphite of formula I: &lt; 0-R1 0 - P: 〇100134551^ singly numbered 1 Page 25 of 29 1013064654-0 201221521 The method comprises : (a) by at 75. 〇180. At a temperature between 〇, a compound of the formula 缓慢 is slowly added to the allylic alcohol RLOH at a temperature of at least 0.5 mM, and the compound of the formula 丨丨 is added to the phenol Thereafter, the trialkyl phosphite of formula II 〇一-p οIR 與分子式III的烷醇 R1-0H反應,以使得 R1代表 具有8至16個碳原子的一烷基部分體,以及R代表具有1至 3個碳原子的一烷基部分體; (b) 將該反應物料至少維持在具有1至3個碳原子的一 烷醇的沸點之上的一溫度達一預定時間期間而同步地移除 在該反應的期間產生的該醇類副產物R—〇H ; (c) 隨選地,在一鈍氣下冷卻該反應產物; (d) 在卜2 mm真空下將該冷卻的反應產物加熱至 190-2G00C達一足夠的時間期間;以及 (e) 將該反應產物冷卻至大約 400C的一溫度以及藉由 過濾回收分子式I的該化合物。 15 .如申請專利範圍第14項所述的方法,其中分子式π之該 三烷基亞磷酸鹽在大約0. 5小時至大約6小時的一時期期 10013455^^^^ A〇101 第26頁/共29頁 1013064654-0 201221521 間,在大約75°C-18(TC的一提升溫度下被加至分子式 ΠΙ之該烷醇中。 16 . 17 · 18 . (\ 19 . Ο 20 . 21 . 22 . 如申請專利範圍第14項所述的方法,其中在缺少一催化劑 或缺少一溶劑或缺少一催化劑以及一溶劑下將分子式Η之 該三垸基亞磷酸鹽與該烷醇反應。 如申请專利範圍第14項所述的方法’其中在具有1至3個 碳原子之一烷醇的沸點之上的所述溫度是從大約195。 C-210°C 。 如申請專利範圍第14項所述的方法,其中該反應物料被維 持在所述溫度達大約2至大約4小時。 一種分子式I之三烷基亞磷酸鹽:〇-p οIR is reacted with an alkanol R1-0H of formula III such that R1 represents an alkyl moiety having 8 to 16 carbon atoms, and R represents an alkyl moiety having 1 to 3 carbon atoms (b) simultaneously maintaining the reaction mass for at least a temperature above the boiling point of the monoalkanol having 1 to 3 carbon atoms for a predetermined period of time to synchronously remove the alcohol pair produced during the reaction Product R—〇H; (c) optionally cooling the reaction product under an inert gas; (d) heating the cooled reaction product to 190-2 G00C under a vacuum of 2 mm for a sufficient period of time; And (e) cooling the reaction product to a temperature of about 400 C and recovering the compound of formula I by filtration. 15. The method of claim 14, wherein the trialkyl phosphite having a molecular formula of π is in a period of from about 0.5 hours to about 6 hours. 10013455^^^^ A〇101 Page 26/ A total of 29 pages 1013064654-0 201221521, is added to the alkanol of the formula 大约 at a temperature of about 75 ° C-18. 16 . 17 · 18 . (\ 19 . Ο 20 . 21 . 22 The method of claim 14, wherein the trimethyl phosphite of the formula is reacted with the alkanol in the absence of a catalyst or lack of a solvent or a catalyst and a solvent. The method of claim 14 wherein the temperature above the boiling point of the alkanol having one of 1 to 3 carbon atoms is from about 195 C to 210 ° C. As described in claim 14 The method wherein the reaction mass is maintained at the temperature for from about 2 to about 4 hours. A trialkyl phosphite of formula I: 其使得R 1代表具有8至16個碳原子的一烷基部分 體,其中分子式I的化合物大體上沒有一酚醛雜質。 如申請專利範圍第18項所述的分子式I之三烷基亞磷酸鹽 ,其中分子式I的該化合物完全沒有一酚醛雜質。 如申請專利範圍第19項所述的分子式1之三烷基亞磷酸鹽 ,其中該分子式I的該化合物包含比一酚醛雜質的lOOppm 更少者。 一種用於製備分子式I之三烷基亞磷酸鹽的改良方法’該 10013455^·單編號 A0101 第27頁/共29賓 1013064654-0 201221521 分子式i之三烷基亞磷酸鹽大體上如同本文中參照該範例 所描述:It allows R 1 to represent a monoalkyl moiety having 8 to 16 carbon atoms, wherein the compound of formula I is substantially free of a phenolic impurity. The trialkyl phosphite of the formula I according to claim 18, wherein the compound of the formula I is completely free of a phenolic impurity. The trialkyl phosphite of the formula 1 according to claim 19, wherein the compound of the formula I contains less than 100 ppm of a phenolic impurity. An improved process for the preparation of trialkyl phosphites of formula I. 10013455^.Single number A0101 Page 27/29 guest 1013064654-0 201221521 The trialkyl phosphite of formula i is substantially as herein described The example describes: °-Px 〇 1001345#單編號 A〇101 第28頁/共29頁 1013064654-0°-Px 〇 1001345#单单 A〇101 Page 28 of 29 1013064654-0
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