TW219932B - - Google Patents
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- TW219932B TW219932B TW81101621A TW81101621A TW219932B TW 219932 B TW219932 B TW 219932B TW 81101621 A TW81101621 A TW 81101621A TW 81101621 A TW81101621 A TW 81101621A TW 219932 B TW219932 B TW 219932B
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219982 五、發明説明(1) 發明之背景 (1)發明之領域 本發明係有關一種光學活性H-(D-Ct -烷基-/3 -氫硫基丙 醛基)-L -脯胺酸之製法。 (2 )相關技術之説明 業已發現如下式(I V )所代表之N - D - ct -甲基-/3 -氫硫基 丙鰹基)-L - g南胺菡(俗名:卡普脫普利(C a p t 〇 p r ί丨)):219982 V. Description of the invention (1) Background of the invention (1) Field of the invention The present invention relates to an optically active H- (D-Ct-alkyl- / 3-hydrothiothiopropionaldehyde) -L-proline acid The system of law. (2) Description of the related art The N-D-ct-methyl- / 3-hydrothiopropyl propanyl group represented by the following formula (IV) has been found-L-g namamine (common name: captopril Profit (C apt 〇pr ί 丨)):
CH 3CH 3
HS-CH2-CH-CONHS-CH2-CH-CON
COOH (IV) 閱 in 背 而 之 意 事 項 堝 寫 本 η 裝 經濟部屮央標準局只工消代合作杜印製 由於對升壓素轉化鸯具有強力抑制作用,以及基於此種_ 之抑制作用,故具有顯著降血壓功效,因此,用作降血壓 劑極為有效(生物化學,1 6 , 5 4 8 7 ( 1 9 7 ?))。 至於此種Ν - ( D - ct -烷基-/3 -氫硫基丙韹基)-L -脯胺酸之 製法,己知令光學活性D - ct -烷基-/3 -藥基硫代丙酸鹵化 物作起始物料,與L -腩胺酸於有機溶劑或水介質内反應, 分雞所得N - ( D - ex -垸基-/?-證基硫!'t丙證基)-L -脯胺酸, 及隨後,將如此所分離的化合物進行脱韹S化反應,锫此 ,如所期望地,獲得N - ( D - <α -烷基-/3 -氫硫基丙舔基COOH (IV) Read in Contrary to the meaning of the manuscript η Installed by the Ministry of Economic Affairs, the Bureau of Standards, and only cooperated with the Consumer Council to produce Du Yin. Due to the strong inhibitory effect on the conversion of vasopressin, and based on this inhibitory effect, Therefore, it has a significant blood pressure lowering effect, so it is extremely effective as a blood pressure lowering agent (Biochemistry, 16, 5 4 8 7 (1 9 7?)). As for the preparation method of this N- (D-ct-alkyl- / 3-hydrothiothiopropyl) -L-proline acid, it is known that the optically active D-ct-alkyl- / 3-drug based sulfur Propionic acid halide as a starting material, react with L-amidoamine in an organic solvent or aqueous medium to separate N-(D-ex -alkyl-/?-Certified sulfur! 'T propylene group ) -L-proline, and subsequently, the compound thus separated is subjected to a desulfurization reaction, and then, as desired, N- (D- < α-alkyl- / 3-hydrogen sulfide is obtained Kiblick
L 脯胺酸。於有機溶剤内進行之反《曾報告於日本待許公開 菜第4 0 6 7 6 / 1 9 8 0號;而於水介質内之反惠則報告於日本持 許公開案第1 8 9 8 5 / 1 9 8 1號。 然而,作為起始物料之酸鹵化物對水不安定。除非如本 本紙5k尺度逡用中困8家榣準(CNS)T 4規格(210X297公龙) 81. 4. 10,000¾ (H) 玎 線 3 219932 經¥部屮央標準局员工消坨合作.吐_印¾ 五、發明説明(2) 發明般,對酸鹵化物與L -脯胺酸間之反應(醛胺化反應)待 別小心進行,否則會出現酸鹵化物之水解,結果生成D - ct -烷基- /3-醛基硫代丙酸之副産物,此乃酸鹵化物之水解 産物。因此,通常使用對酸鹵化物呈惰性之有機溶劑,例 如鹵化烴及四氫呋喃作醯胺化反應之反應介質。雖然使用 此等有機溶劑,可防止酸鹵化物之水解,但出現一種問題 ,L -脯胺酸於此等有機溶劑内之溶解度極低。因此,無可 避免地,必須藉著以固體形式懸浮L -脯胺酸進行證胺it反 應及犧牲反慝效率,或者遵循繁瑣的反應過程:先將L-脯 胺酸轉成於此有機溶劑内可溶的酯類後才進行反應。 於前述韹胺化反應中,需要脫酸化用之縮合劑,俥清除 由謖鹵化物所産生的鹵化氫。然而,當使用有機溶劑作反 應介質時,不允許使用便宜經濟的鹼屬氫氧化物,例如氣 氧化鈉因此,無可避免地,必須使用昂貴的有機胺類, 例如Η , Ν -二甲基苯胺,因為有機胺類可溶於有機溶劑。此 種有機胺必須從反應産物謅胺中分離及回收。但有機按之 分離及回收比鹼金屬氫氣化物更困難,結果導致未反應的 有機按容易混合於産物内蠻成雜質等問題。 當於水介質内進行時,酸鹵化物與L -腩胺St間之史高頓 鲍曼(S c h 〇 t t e η - B a u m a η η .)反應不會出現如同於有機溶劑内 進行反慼之問題,但會出現酸鹵化物水解的新問題。於曰 本持許公開案第1 8 9 5 8 / 1 9 8 1號持別說明的方法中,酸鹵化 物溶解於有機溶劑,例如四氬呋喃内,而所生成之溶液加 入L -脯胺遨之水溶液俾避免水解反應。 (請先閲請背而之注意事項孙填寫本页) 裝· 訂· 線· 本紙尺度逍用中a困家標準(CNS) T4規格(210x297公放) 81. 4. 10,000¾ (![) 4 219932 A 6 I? 6 經试部中央榀準局3工消疗合作社印製 五、發明説明(3 ) 然而,此種方法使用有機溶劑,因此,需要進行複雜的 後處理,俥從所得反應産物之水溶液中分離出有機溶劑。 此外,各種副産物,例如酸鹵化物之水解産物,及經由史 高頓鲍曼反應産物進行進一步反應所生成之反應産物,通常 、 容易出現於史高頓鮑曼反應中。帶有醯基之史高頓鲍曼反 應産物進行脱醯基化反應,侔獲得如本發明之帶有氫硫基 之终産物時,除非此等副産物事先被去除,否則由於終産 物具有水溶性,故終産物之纯化將變得困難。因此,没有 任何解決之辦法,除非遵照下列各步驟進行:史高頓鲍曼 産物一旦被純化及分雞後,即進行脱鏢基化反應,且將如 此所得之脱醯基化産物纯化。 發明之概述 本發明有一目的偽提供一種Μ高産率製備L -脯胺酸衍生 物之方法,該方法包括於水介質内進行酸鹵化物與L -脯胺 酸之史高頓鲍曼反應之同時,抑制酸鹵化物之水解,藉此進 行脱醯基化反應,而無需由反應混合物中分離史高頓鮑曼 反應産物。 有鑑於此,本發明人對可能影響酸鹵化物與L -脯胺酸藉 史高頓鮑曼反應生成醯胺化産物之産率的反應參數,以及 對D - ct -烷基-/3 -醯基硫代丙酸及Ν -醯基-L -脯胺酸等副産 物進行徹底研究。結果,發現使用脱酸化用之縮合劑將反 應混合物之P Η控制於預定水平,可無需使用有機溶劑,即 可避免薛鹵化物之水解,同時允許醯胺化反應迅速進行; 此外,頭著抑制易於極高Ρ Η下出現的副産物,例如Ν -醯基 (請先閲讀背而之注意事項再填寫木頁) 裝· 訂_ 線- 本紙張尺度遑用中a®家標準(CNS)T4規格(210x297公龙) 81. 4. 10,000^(11) 5 219932 Λ 6 _Π_6_ 五、發明説明(4) -L -脯胺酸的生成,因而,可以高産率獲得醛胺化産物。 也發現以前述方式獲得之醛胺化産物可直接進行脫酸·基化 反應,而無需預先由反應混合物中分離及純化,因此,可 以高純度及以高産率獲得N - ( D - α -烷基-/3 -氫硫基丙鏗基 s )-L -脯胺酸,結果完成本發明。 因此本發明提供一種製備式(I )所代表之L -脯胺酸衍生 物:L proline. The countermeasures carried out in the organic solvent "reported to be published in Japan No. 4 0 6 7 6/1 9 8 0; while the countermeasures in aqueous media were reported in the Japanese Open Publication No. 1 8 9 8 5/1 9 8 No. 1. However, the acid halide as the starting material is unstable to water. Unless the 5k scale of this book is used in the middle of the 8 standard (CNS) T 4 specifications (210X297 male dragon) 81. 4. 10,000¾ (H) 玎 线 3 219932 cooperation by the employees of the Central Standards Bureau of Japan. Spit_print ¾ V. Description of the invention (2) As invented, the reaction between the acid halide and L-proline (aldimination) should be carried out carefully, otherwise the hydrolysis of the acid halide will occur, resulting in D -By-product of ct-alkyl- / 3-aldehyde thiopropionic acid, which is a hydrolysate of acid halide. Therefore, organic solvents that are inert to acid halides, such as halogenated hydrocarbons and tetrahydrofuran, are generally used as the reaction medium for the amidation reaction. Although the use of these organic solvents can prevent the hydrolysis of acid halides, there is a problem that the solubility of L-proline in these organic solvents is extremely low. Therefore, it is inevitable that the L-proline acid must be suspended in a solid form to perform the amine it reaction and sacrifice the reaction efficiency, or follow the cumbersome reaction process: first convert L-proline acid to this organic solvent Only after the soluble esters are reacted. In the aforementioned amination reaction, a condensing agent for deacidification is required to remove the hydrogen halide generated from the halide. However, when using organic solvents as the reaction medium, it is not allowed to use cheap and economic alkali hydroxides, such as sodium gas oxide. Therefore, it is inevitable to use expensive organic amines, such as Η, Ν-dimethyl Aniline, because organic amines are soluble in organic solvents. This organic amine must be separated and recovered from the reaction product, cetylamine. However, the separation and recovery of organic compounds are more difficult than that of alkali metal hydride. As a result, unreacted organic compounds are easily mixed into the product and become impurities. When carried out in an aqueous medium, the Scotch Bowen (S ch tte η-B auma η η.) Reaction between the acid halide and L-hexylamine St does not appear as if it is carried out in an organic solvent. Problem, but there will be new problems of acid halide hydrolysis. In the method described separately in No. 1 8 9 5 8/1 9 8 No. 1 of Yu Yueben, the acid halide is dissolved in an organic solvent, such as tetrahydrofuran, and the resulting solution is added with L-proline Aqueous solutions to avoid hydrolysis reactions. (Please read the notes beforehand, Sun fills in this page) Packing · Ordering · Thread · The standard of this paper is easy to use in a sleepy home standard (CNS) T4 specification (210x297 public) 81. 4. 10,000¾ (! [) 4 219932 A 6 I? 6 Printed by the Central Bureau of Tests of the Ministry of Examination and Testing 3 The Cooperative Society of Medical Treatment 5. V. Description of the invention (3) However, this method uses organic solvents, therefore, complex post-processing is required to obtain the reaction The organic solvent is separated from the aqueous solution of the product. In addition, various by-products, such as the acid halide hydrolysate, and the reaction product formed by the further reaction of the Scottish Bowman reaction product, usually appear easily in the Scottish Bowman reaction. When the Gordon Baumann reaction product with an acyl group is subjected to a deacylation reaction to obtain the final product with a hydrosulfide group according to the present invention, unless these by-products are removed in advance, the final product is water-soluble Therefore, purification of the final product will become difficult. Therefore, there is no solution unless the following steps are followed: Once the Scotten Bowman product has been purified and separated, the de-arylation reaction is carried out, and the de-acylation product thus obtained is purified. SUMMARY OF THE INVENTION An object of the present invention is to provide a method for preparing L-proline acid derivatives with high yield of M, the method comprising performing a Scotten Bowman reaction of an acid halide and L-proline acid in an aqueous medium At the same time, the hydrolysis of the acid halide is inhibited, thereby performing the deacylation reaction without separating the Scottish Bowman reaction product from the reaction mixture. In view of this, the present inventors have determined the reaction parameters that may affect the yield of the acid halide and L-proline by the Scotton Bowman reaction to the amidation product, as well as the D-ct-alkyl- / 3- Acetyl thiopropionic acid and N-acyl-L-proline and other by-products were thoroughly studied. As a result, it was found that the use of a deacidification condensing agent to control the pH of the reaction mixture to a predetermined level can avoid the hydrolysis of the Xue halide without using an organic solvent, while allowing the amidation reaction to proceed quickly; It is easy to produce by-products under extremely high Η, such as Ν- 醯 基 (please read the precautions before filling in the wooden page) Binding · Binding-Line-This paper standard is not in accordance with the a® family standard (CNS) T4 specifications (210x297 male dragon) 81. 4. 10,000 ^ (11) 5 219932 Λ 6 _Π_6_ V. Description of the invention (4) The formation of -L-proline acid, therefore, the aldination product can be obtained in high yield. It has also been found that the aldination products obtained in the foregoing manner can be directly subjected to deacidification and debasing reactions without prior separation and purification from the reaction mixture. Therefore, N-(D-α-can be obtained in high purity and with high yield Alkyl- / 3-hydrothiothiopropenyl s) -L-proline acid, as a result, the present invention was completed. Therefore, the present invention provides a preparation of the L-proline derivative represented by formula (I):
(請先閲讀背而之注意事項洱堝寫木頁) 裝· 經3部屮央標準局Α工消作合作杜印¾ [式中R2代表低级垸基],該方法包括令如式(I )所代表之 D - cr -;垸基-德基硫代(7¾ S3 ®化物: R2 T r1s-ch2-ch-cox (工) [式中R:代表韹基,X代表鹵甭子及R2具有如前述之定義: 與L -脯胺酸反應。所述方法包活將::-« -烷基-/?-茜基硫 代丙酸鹵化物(I )加入含L -脯胺謖及脫渡ib用之縮合劑之 水介質内,令D-α -烷基-/3 -鏟基硫代丙酸鹵化物與L -捕 胺酸反癍,同時將反應溫度維持於1 2 Ό以下及將p Η維持於 1 0 . 5 - 1 1 . 5之範圍内,藉此獲得式(H )所代表之化合物: 訂_ 線_ 本紙张尺度遑用中8困家標準(CNS) T4規格(210x297公龙) δ 81. 4. 10,000^(11) 219982 Λ β 15 6 經沭部屮央捣準局貝工消坨合作社印利4 五、發明説明(5 ) r2 RiS-ch2-(!h-con^) (II) COOH [式中1^及1?2具有如前述之定義];及然後,令化合物(Π) 於強鹼條件下進行脱酿基化反應,而未由反應混合物中分 離化合物(3 )。 (衣據本發明之方法,D-cx -烷基_/3 -醯基硫代丙酸及N-醯基-L -脯胺酸副産物之生成可於醯胺化反應中受抑制, 因此可以高纯度及高産率獲得N-(D-a -烷基-/3 -醯基硫代 丙醯基)-L -脯胺酸。又復,如依本發明之方法,經由令前 述産物進行脫醯基化反應,可抑制D - ct -烷基-/3 -氫硫基 丙酸及N -醯基-L-脯胺酸等副産物之生成,因而可以高純 度及高産率獲得Η - ( D - <α -烷基-/3 -氫硫基丙黯基)-L -脯胺 酸。 較佳具證例之細節說明 於式(I)及(I)中,^所代表之醯基之例,包含C2_7烷 醯基,如乙醯基及丙醯基;及芳醯基,例如無取代或由一 或一以上低级烷基,如甲基,乙基,正-丙基,異-丙基, 正-丁基及三级丁基,或鹵原子(氟,氯,溴或碘原子), 所取代之苯甲鏗基。於式(I ) , ( I )及(S )中r2所代表之 低级烷基之例,包含直鏈或分支_ (:卜7烷基,例如甲基, 乙基,丙基及異丙基。式(I)中,X所代表之鹵原子之例 ,包含氛,溴或碘原子。 (請先閲請背而之注意事項再填寫本頁) 裝. 訂 線· 本紙張尺度遑用中國國家標準(CNS)<P4規格(210x297公;Ϊ) 7 81. 4. 10,000^(1!) 219932 Λ β Η 6 經濟部屮央楞準局ex工消作合作杜印3i(Please read the notes on the back of Erguo to write wooden pages first). Installed by 3 Department of Standards Bureau of Ayang, and cooperated with Du Yin ¾ [where R2 stands for low-grade embankment], the method includes the order (I ) Represented by D-cr-; emulsyl-deyl thio (7¾ S3 ® compound: R2 T r1s-ch2-ch-cox (technical) [where R: stands for chrysanthemum, X stands for halogen and R2 It has the above definition: react with L-proline. The method includes:-«-alkyl-/?-Alkyl thiopropionic acid halide (I) added to L-proline-containing radon and In the aqueous medium of the condensing agent used for the removal of ib, the D-α-alkyl- / 3-shodothiopropionic acid halide and the L-amino acid are reversed, while maintaining the reaction temperature below 1 2 Ό And maintaining p Η within the range of 10.5-11.5, thereby obtaining the compound represented by the formula (H): _ _ line _ the paper standard is used in the 8-sleeper standard (CNS) T4 specifications (210x297 male dragon) δ 81. 4. 10,000 ^ (11) 219982 Λ β 15 6 By the Ministry of Economic Affairs of the Ministry of Economic Affairs, Beigong Xiaotuo Cooperative Society, India 4 V. Description of the invention (5) r2 RiS-ch2- (! h-con ^) (II) COOH [where 1 ^ and 1? 2 have the definition as described above]; and then, make The compound (Π) is defermented under strong alkali conditions without separating the compound (3) from the reaction mixture. (D-cx -alkyl_ / 3 -acylthio according to the method of the present invention The formation of by-products of propionic acid and N-acyl-L-proline can be suppressed in the amidation reaction, so N- (Da -alkyl- / 3 -acylthio can be obtained in high purity and high yield Propionyl) -L-proline. Again, according to the method of the present invention, by subjecting the aforementioned product to deacylation, D-ct-alkyl- / 3-hydrothiothiopropionic acid and The formation of by-products such as N-acyl-L-proline, so that H- (D- < α-alkyl- / 3-hydrothiothiopropionyl) -L-pro Aminic acid. The details of the preferred certified examples are shown in formulas (I) and (I). Examples of acetyl groups represented by ^ include C2_7 alkyl acetyl groups, such as acetyl and propyl groups; and aryl acetyl groups , For example, unsubstituted or composed of one or more lower alkyl groups such as methyl, ethyl, n-propyl, iso-propyl, n-butyl and tertiary butyl, or halogen atoms (fluorine, chlorine, bromine Or iodine atom), the substituted benzylidene group. In formula (I ), (I) and (S) in the example of lower alkyl represented by r2, including linear or branched _ (: Bu 7 alkyl, such as methyl, ethyl, propyl and isopropyl. Formula (I ), The examples of halogen atoms represented by X include atmosphere, bromine or iodine atoms. (Please read the notes before filling in and then fill out this page) Binding. Thread · This paper standard uses the Chinese National Standard (CNS ) < P4 specification (210x297 g; Ϊ) 7 81. 4. 10,000 ^ (1!) 219932 Λ β Η 6 Ministry of Economic Affairs, Pyongyang Bureau of Industry and Commerce cooperation Du Yin 3i
五、發明説明(6) 用於實行本發明之酸鹵化物(I )之製法,例如,可經由 使用鹵化劑,例如亞磺醯氛,三氛化磷或三溴化磷,藉業 界已知之方法處理對應之羧酸(係經由日本待許公開案第 222798/1989號掲示之方法而得)而獲得。 、 至於可用於實施本發明之水介質,可使用具有PH10. 5-1 1 . 5之水溶液,3 脱酸化用之縮合劑之較佳範例,包含可溶於水介質之鹼 性化合物,例如鹼金屬氫氣化物,例如氫氧化鈉及氫氣化 鉀。脱酸化用之縮合劑也可用作水介質之P Η控制劑。 於實施本發明時,酸鹵化物與L -脯胺酸間之反應偽經由 將酸鹵化物加入含L -脯胺酸之水介質内,較好於攪拌下加 入。反應中,反應混合物之P Hi%維持於1 0 . 5 - 11 . 5之範圍 内。使用鹼金屬氫氧化物作脱酸化用之縮合劑,俥清除由 酸鹵化物所放出的鹵化氫,同時也用於控制反應混合物之 p Η。將L -脯胺酸之水溶液加入酸鹵化物内並不宜,歸咎於 酸鹵化物於水溶液内之停留時間過長,因而出現酸鹵化物 之水解。 隨箸反窸混合物之Ρ Η變成低於1 0 . 5 ,換言之,趨近酸性 側時,酸鹵化物變成對水解更敏感。Ρ Η愈接近ρ Η 7 ,則生 成愈多D - a -烷基-/3 -鏢基硫代丙酸副産物,亦即水解産 物。因此,pH低於10. 5並不宜。另一方面,隨著反應混合 物之P Η升高至超過1 1 . 5而趨近於1 4 ,則生成愈多N -鏟基-L -脯胺酸。因此Ρ Η高於1 1 . 5 &不宜。於較高ρ Η時,Ν -醯基-L -脯胺酸副産物之産量較大,可能偽歸因於所産生的Η - ( D (請先間讀背而之注意事項#塡寫本頁) 裝. 線, 本紙张足度遑用中國B家標準(CNS)肀4規格(210x297公址) 81. 4. 10,000¾ (II) 8 2ί9982 A fi n 6 經濟部中央榀準而β工消作合作杜印ft'14 五、發明説明(7) -α -烷基-/3 -醯基硫代丙ϋ基)-L -脯胺酸與反應混合物内 所含的L-脯胺酸反應之故。 需要於12f以下,較好1010或以下,且更好81或以下 之溫度進行醯胺化反應。溫度高於1 2 13導致N -醯基、-L -脯 胺酸副産物之産量增高,因此並不宜。如此,較好於反應 進行時,將反應混合物雒持於0Τ或以上之溫度,俥避免 反應混合物不期望的凍結。 對反應時間並無待殊限制,但反應時間較好為0 . 5 - 8小 時,以1 - 5小時為更佳。 就經濟上而言,有利地L -脯胺酸之進料量為0 . 9 - 1 . 1莫 耳/莫耳之酸鹵化物。雖然對所饋進的L -脯胺酸水溶液之 濃度並無待殊限制,但由反應溫度之控制的觀點看來,較 好以1 - 5 0 w 15C,更宜2 - 3 0 w t S;之濃度進料。 經由酸鹵化物與L -脯胺酸反應所生成的烷基-/3 -醯基硫代丙鏗基)-L -脯胺酸,於以業界已知方式進行 分離及純化後,可進行脫鏗基化反應。然而,於本發明之 方法中,醯胺化反應所得反應混合物中之副産物含量極低 ,因此,醯胺化産物可於同一反應器内進行脱鏜基化反應 ,同時將反愿混合物維持於鹼性條件下,而無需於醯胺化 反應大體完成後分離醯胺化産物。 如文所用之”醯胺化反應大體完成後”之表示法,代表以 進料為基準,所饋進的酸鹵化物及L -脯胺酸之至少一者之 數量降至5%或以下之狀態。 雖然對脱趦基化反應溫度範圍並無特殊限制,只要反應 (請先閲請背而之注意亊項朴塡寫本頁) 裝- 線- 本紙尺度边用中a國家楳準(CNS)甲4規格(210x297公:¢) 81. 4. 10,000¾ (H) 9 .年 Β2.5. Description of the invention (6) The method for preparing the acid halide (I) of the present invention, for example, through the use of a halogenating agent, such as sulfenamide, phosphorus tribromide or phosphorus tribromide, known by the industry It is obtained by processing the corresponding carboxylic acid (obtained by the method shown in Japanese Patent Publication No. 222798/1989). As for the aqueous medium that can be used in the practice of the present invention, an aqueous solution having a pH of 10.5-11.5 can be used, and a preferred example of a condensation agent for deacidification includes alkaline compounds soluble in an aqueous medium, such as alkali Metal hydroxides, such as sodium hydroxide and potassium hydroxide. The condensing agent used for deacidification can also be used as a pH control agent for aqueous media. In the practice of the present invention, the reaction between the acid halide and L-proline is carried out by adding the acid halide to the aqueous medium containing L-proline, preferably under stirring. During the reaction, the P Hi% of the reaction mixture was maintained in the range of 10.5-11.5. The alkali metal hydroxide is used as a condensation agent for deacidification to remove the hydrogen halide emitted from the acid halide, and it is also used to control the pH of the reaction mixture. It is not appropriate to add the aqueous solution of L-proline to the acid halide, because the residence time of the acid halide in the aqueous solution is too long, and therefore hydrolysis of the acid halide occurs. The pH value of the mixture with the lanthanum becomes lower than 10.5. In other words, when approaching the acidic side, the acid halide becomes more sensitive to hydrolysis. The closer ΡΗ is to ρΗ7, the more D-a-alkyl- / 3-dartylthiopropionic acid by-product, that is, the hydrolysis product, is generated. Therefore, a pH lower than 10.5 is not suitable. On the other hand, as the pH of the reaction mixture rises above 1 1.5 and approaches 14, the more N-scaproyl-L-proline is produced. Therefore, P Η is higher than 1 1.5 & unsuitable. At higher ρ Η, the yield of by-products of N-acyl-L-proline is larger, which may be pseudo-attributed to the produced Η-(D (please read back and note beforehand # 塡 写 此 页) Install. Line, this paper is fully equipped with Chinese B standard (CNS) 4 specifications (210x297 public address) 81. 4. 10,000¾ (II) 8 2ί9982 A fi n 6 Central Ministry of Economic Affairs and β work consumption Cooperation Du Yin ft'14 V. Description of the invention (7) -α-alkyl- / 3-acylthiopropyl (propyl) -L-proline acid reacts with L-proline acid contained in the reaction mixture Reason. It is necessary to perform the amidation reaction at a temperature of 12f or less, preferably 1010 or less, and more preferably 81 or less. A temperature higher than 1 2 13 leads to an increase in the production of by-products of N-acyl and -L-proline, which is not suitable. In this way, it is preferable to keep the reaction mixture at a temperature of 0 T or above while the reaction is proceeding, so as to avoid undesired freezing of the reaction mixture. There is no special limitation on the reaction time, but the reaction time is preferably 0.5-8 hours, more preferably 1-5 hours. Economically, the feed amount of L-proline is advantageously 0.9-1.1 moles / mole acid halide. Although there is no particular limitation on the concentration of the L-proline acid aqueous solution fed, from the viewpoint of controlling the reaction temperature, it is preferably 1-5 0 w 15C, more preferably 2-3 0 wt S; Concentration feed. Alkyl- / 3-acylthiothiopropylbenzyl) -L-proline acid produced by the reaction of acid halide and L-proline acid can be removed after separation and purification in a manner known in the industry Rhenylation reaction. However, in the method of the present invention, the content of by-products in the reaction mixture obtained by the amidation reaction is extremely low. Therefore, the amidation product can be subjected to the deboration reaction in the same reactor, while maintaining the undesired mixture in the alkali Under aerobic conditions, it is not necessary to separate the amidation product after the amidation reaction is substantially complete. As used herein, the expression "after the amidation reaction is substantially completed" means that the amount of at least one of the acid halide and L-proline acid fed to the feed is reduced to 5% or less status. Although there is no special limit to the temperature range of the decyclization reaction, as long as the reaction (please read first, please pay attention to this item, please write this page). Install-Line-Use this standard as a national standard (CNS) A 4 specifications (210x297 g: ¢) 81. 4. 10,000¾ (H) 9 .year Β2.
經濟部中央標準局W工消費合作社印製 2199S2 A6 _;_B6__ 五、發明説明(8 ) 愾於鹼性條件下進行即可.但欲縮短反應時間,較好將反 應S度升至超過151.較好升至20¾或以上。待別更好於 40¾至50t:間之溫度及10.5至11.5間之pH下進行反應。若 反應混合物維持於PH12或以上之強_條件下,脱酵基化反 應甚至可於更低溫下進行.然而,就經濟上而言,此等較 低溫度並不利,因為於醒基化反應後,欲從反應混合物中 抽取分離L -脯胺酸衍生物將需要大量礦酸。另一方面,pH 低於10.5會導致出現較多副産物的問題。因此,pH在前述 範圍以外並不宜。 脱趦基化反應所需反應時間通常傜於1 0分鐘至1 0小時之 範圍内,以0.5-4小時為較佳。此外,較好於惰性氣體, 例如氡氣,氣氣及氬氣氛圍下,較好於氣流下,進行脱趦 基化反應。 於反應完成後.ϋ加入無機酸,如鹽酸將反應混合物調 整為酸性。然後,所生成之N-(D-cr-烷基- /3-氫硫基丙匿 基)-L -脯胺酸使用有機溶劑,如二氛甲烷及乙酸乙酯抽取 ,及於減饜下乾燥或再結晶,-藉此可分離及獲得檫的産物。 後文中將利用以下各例更詳細說明本發明之細節。但需 謹記本發明並非僅限於或僅受下列各例所囿限。 實施例1 於9 0 m儿蒸蹓水中加入5 . 8 s L -脯胺酸。所得溶液ϋ加入 2Ν氫氣化銷水溶液諝整為pHll。所得水溶液藉冰-水浴冷 卻至5T:〜0C。將反應混合物之溫度維持於5C〜0t:,以 1小時時間逐滴加入9 . 0 g D - α -甲基-召-乙醯基硫代丙 (請先閲讀背面之注意事項再填寫本頁) —裝- •V-0 . 本纸張尺度適用中國國家懔苹(CNS)甲丨規格(210 X 297公贷)jq 降正賓 82. 5. 20,000 涇濟部中央標準局員工消疗合作钍印?代 告本丨 Λ6 .、..... !_Β6__ 五、發明説明(9 ) 酵氛。逐滴添加完成後,反應混合物又反應2小時。逐滴 添加開始之時,反應開始進行而ρ Η開始下降。因此,反應 期間由Ρ Η控制泵浦添加2 Ν氫氣化鈉水溶液,俾便將反應混 合物之pH經常維持於11。 反窿混合物内大體不再測得任何D-α -甲基-/3 -乙醯基 硫代丙醛氣後,反應混合物於氮氣流下以溫水浴加熱至50 它。隨箸反應混合物之溫度之升高.其pH再度開始下降。 «著經由pH控制泵浦添加5N氫氣化納水溶液將溶液之pH維 持於1 1 ,脱匿基化反匾又進行2小時。脱醯基化反應完成 後,利用高效液相層析分析反應混合物内之反應産物之莫 耳産率。结果不於表1。 以等莫耳量使用D-ct -甲基-/3 -苯甲醯基硫代丙S氛置 換D-α-甲基-点-乙酵基硫代丙酵氛,也可同樣成功地進 行酵胺化及脱酵基化反應,結果導致以高純度及以高産率 生成對應的L-脯胺酸衍生物。 比較例1 - 4 反匾係以類似例1之方式進行,但S胺化反應中之-Ρ Η經 常維持於7 . 6 (比較例1中氫氣化納水溶液俱以碩酸氫納水 溶液置換),10.0(比較例2), 12.0(比較例3),或至少13 (比較例4 )。 各反醮混合物内之反應産物之莫耳産率偽薙高效液相 層析分析之。結果也示於表1。 ------------------------裝------,玎------^ (請先閲讀背面之注意事項再塡寫本頁) 本紙張尺度適用中aa家序準(CNS)平.!规丨各(210 X 297公义),、 A _ 禮 82. 5. 20,000 11 吹正買 ^19932 五、發明説明(10) m_1 實施例1 比 較 例 1 2 3 4 反應混合 物之pH 11.0 7.6 10.0 12.0 ^ 13 産物 (%) 1 95.1 38.7 79.8 85.1 4 0.4 2 3.3 6 1.3 20.2 3.7 22.2 3 1.6 0 0 11.2 37.4 (請先閱請背而之注意事項再塥寫本頁) 表1及後文中之表2及表3中,産物1,産物2及産物3分別 代表N-(D-a -甲基-/3 -氫硫基丙鏗基)-L-脯胺酸,D-a -甲基-/9 -氫硫基丙酸,及N -醯基-L -脯胺酸。 實施例2及3 反應偽以類似例1之方式進行,但P Η變成1 0 . 5 (例2 )或 11.5(例3)。各反應混合物内之莫耳産率傺以高效液相層 析分析之。結果示於表2。 表 實施例2 實施例3 反應混 合 10.5 11.5 物之pH ; 産物 1 90.0 92.0 : (X) 2 9.8 2.0 3 0.2 1 6·0 由實施例1-3及比較例1-4之結果可見,高純度N-(D-d -烷基-/3 -氫硫基丙鏗基)-L -脯胺酸可以高産率獲得,其製 裝- 線. 經濟部屮央榀準局只工消赀合作杜印#,'|4 g C rv 平 國 圉 T W Λ _ * 公 y y 12 81. 4. 10,000¾ (H) Λ 6 Π 6 五、發明説明(11) 法偽經由進行醯胺化反應,同時將反應混合物之pH維持於 本發明界定之範圍内,及然後,令所得反應産物就此於鹼 性條件下進行脱醯基化反應。 實施例4及比較例5及6 以類似例1之方式進行反應,但醯胺化之溫度改變。結 果示於表3。 (請先間讀背而之注意事項再填筠本頁) 裝· 訂_ 線· 表 3 實施例4 比較例 5 6 反應溫 度 10 15 20 (°c ) 産物 1 9 0.2 83.8 78.7 m 2 7 . 8 6 . 2 8 . 6 3 3.0 ί 10.0 12.7 經濟部屮央梂準局A工消费合作杜印製 5 ί 明 典 Τ W Λ Λ 人 i 公 81. 4. 10,000?*: (|[) 13 五、發明説明(11a) 比較例7 於 持 保 終 始 Η Ρ 之 時 應 反 化 胺0 了 除 例 施 實 與 均 外 之 生 産 應 反 由 ο 應 反 施 實 JiW 樣 同 硫0 乙 I θ· I 基 甲 物 純 不 % 為 2 % 8 8 為I 率 産 耳 莫 其 酸 胺 浦- f基 -L甲 \—/ -基 α 酵D-丙有 酸 丙 基 硫0 乙 含 物 合 混 應 反 於 由 該 使 酸 鹽 用 油 Ν 得if 獲 獲 以而 除 晶 餾結 劑再 溶酯 將乙 0 酸 之醋 取由 萃質 烷物 甲狀 化油 氣該 由以 後後 化然 酸 0 物質 合物 混' 狀 基 Ν 醯之 丙離 砍單 醯所 乙入 基Ηίι 甲ao % 基 7011 為丙 率硫 産醯 離乙 單- Ο I 酸基 胺甲 - α 脯 於 持 保 Η Ρ 之 物 合0 應 反 將 以 酸 胺 脯 下 流 氣 氮 在 溫 之 物 合 混 應 反 著 隨 ο V 0 5 至 熱 加 物 合 混 應 反 將 浴 水 溫0 WU 力 添 泵 制化 控醯 Ρ 脱 0 行 〇 進 降時 下同 始 , 開 1 度於 再持 ΡΗ保 其ΡΗ ,之 升液 上溶 度將 時 小 以完 ΟΗ化 ^ 0 Ν-脱 (請先閲讀背面之注意事項再填寫木S) 裝· 訂_Printed 2199S2 A6 _; _B6__ by the WBC Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs 5. Description of the invention (8) It can be carried out under alkaline conditions. But to shorten the reaction time, it is better to increase the reaction S degree to more than 151. It is better to rise to 20¾ or above. It is better to carry out the reaction at a temperature between 40¾ and 50t: and a pH between 10.5 and 11.5. If the reaction mixture is maintained at a strong pH of 12 or above, the dezymation reaction can be carried out even at lower temperatures. However, economically, these lower temperatures are not beneficial because after the wake-up reaction To extract L-proline derivatives from the reaction mixture will require a large amount of mineral acid. On the other hand, a pH lower than 10.5 will cause problems with more by-products. Therefore, the pH is not suitable outside the aforementioned range. The reaction time required for the decyclization reaction is usually in the range of 10 minutes to 10 hours, preferably 0.5-4 hours. In addition, it is preferably carried out under an inert gas, such as radon, gas and argon atmosphere, and preferably under a gas flow, to carry out the debasing reaction. After the reaction is complete, add mineral acid, such as hydrochloric acid, to adjust the reaction mixture to be acidic. Then, the generated N- (D-cr-alkyl- / 3-hydrothiopropylpropionyl) -L-proline acid is extracted with an organic solvent, such as dichloromethane and ethyl acetate, and reduced. Dry or recrystallize-by which the Sassafras product can be isolated and obtained. The details of the present invention will be explained in more detail in the following examples. However, it should be borne in mind that the present invention is not limited to or only limited by the following examples. Example 1 9.8 s L-proline was added to 90 m of distilled water. The resulting solution was added to 2N hydrogenated aqueous solution to adjust the pH to 11. The resulting aqueous solution was cooled by ice-water bath to 5T: ~ 0C. Maintain the temperature of the reaction mixture at 5C ~ 0t :, add 1 .0 g D-α-methyl-zhao-acetothiothiopropionate dropwise over 1 hour (please read the notes on the back before filling this page ) —Installed-• V-0. This paper scale is applicable to China National Apple (CNS) A 丨 specifications (210 X 297 public loan) jq Jiang Zhengbin 82. 5. 20,000 Jingji Ministry of Central Bureau of Standards and Staff Respiratory Cooperation Th seal? Announcement 丨 Λ6 ......! _Β6__ V. Description of the invention (9) Fermentation atmosphere. After the dropwise addition was completed, the reaction mixture was reacted for another 2 hours. At the beginning of the dropwise addition, the reaction started to proceed and ρΗ began to decrease. Therefore, during the reaction, 2 NH sodium hydroxide aqueous solution was added to the pump by pH control, so that the pH of the reaction mixture was always maintained at 11. After no more D-α-methyl- / 3-acetyl thiopropionaldehyde gas was detected in the anti-mixture, the reaction mixture was heated to 50 ° C in a warm water bath under a nitrogen flow. As the temperature of the reaction mixture rises, its pH begins to decrease again. «The pH of the solution was maintained at 1 1 by adding a 5N hydrogenated sodium aqueous solution via a pH-controlled pump, and the debasing anti-plaque was carried out for another 2 hours. After the deacylation reaction was completed, the molar yield of the reaction product in the reaction mixture was analyzed by high performance liquid chromatography.结果 不 于 表 1。 The results are not in Table 1. Using D-ct-methyl- / 3-benzylthiopropion S atmosphere in equal molar amounts to replace D-α-methyl-dot-acetoxythiopropionase atmosphere can also be carried out with similar success The enzymatic amination and deamination reaction results in the formation of the corresponding L-proline derivative with high purity and high yield. Comparative Examples 1-4 The anti-plaque was carried out in a similar manner as in Example 1, but the -P Η in the S amination reaction was always maintained at 7.6 (in Comparative Example 1, the hydrogenated sodium aqueous solution was replaced with sodium hydrogen peroxide solution) , 10.0 (Comparative Example 2), 12.0 (Comparative Example 3), or at least 13 (Comparative Example 4). The molar yield of the reaction products in each mixture was analyzed by pseudo-hydrazide high performance liquid chromatography. The results are also shown in Table 1. ------------------------ Installed ------, 玎 ------ ^ (Please read the precautions on the back first, then 塡Write this page) This paper scale is applicable to the CNA Standard. !! Regulations (210 X 297 justice), A _ Li 82. 5. 20,000 11 Blowing to buy ^ 19932 V. Description of the invention (10) m_1 Example 1 Comparative example 1 2 3 4 pH of the reaction mixture 11.0 7.6 10.0 12.0 ^ 13 Product (%) 1 95.1 38.7 79.8 85.1 4 0.4 2 3.3 6 1.3 20.2 3.7 22.2 3 1.6 0 0 11.2 37.4 (please read the precautions before writing this page) Table 1 and the following table 2 and Table 3, product 1, product 2 and product 3 respectively represent N- (Da-methyl- / 3-hydrothiopropylpropenyl) -L-proline, Da-methyl- / 9-hydrogen Thiopropionic acid, and N-acyl-L-proline. In Examples 2 and 3, the reaction was carried out in a similar manner as in Example 1, but P Η became 10.5 (Example 2) or 11.5 (Example 3). The molar yield in each reaction mixture was analyzed by high-performance liquid chromatography. The results are shown in Table 2. Table Example 2 Example 3 The pH of the reaction mixture 10.5 11.5; product 1 90.0 92.0: (X) 2 9.8 2.0 3 0.2 1 6 · 0 As can be seen from the results of Examples 1-3 and Comparative Examples 1-4, high purity N- (Dd-Alkyl- / 3-Hydroxythiopropylpropylenyl) -L-proline acid can be obtained in high yields, and its manufacture and assembly-line. #, '| 4 g C rv Pingguo TW Λ _ * Gongyy 12 81. 4. 10,000¾ (H) Λ 6 Π 6 V. Description of the invention (11) The method of carrying out the amidation reaction through pseudo-acidification and simultaneously reacting The pH of the mixture is maintained within the range defined by the present invention, and then, the resulting reaction product is subjected to deacylation under alkaline conditions. Example 4 and Comparative Examples 5 and 6 were reacted in a manner similar to Example 1, but the temperature of amidation was changed. The results are shown in Table 3. (Please read back the precautions before filling in this page) Binding · Order_ Line · Table 3 Example 4 Comparative Example 5 6 Reaction Temperature 10 15 20 (° c) Product 1 9 0.2 83.8 78.7 m 2 7. 8 6. 2 8. 6 3 3.0 ί 10.0 12.7 The Ministry of Economic Affairs, Central Bureau of Industry and Commerce, A Industrial and Consumer Cooperation Du Printing 5 ί Ming Dian T W Λ Λ Reni Gong 81. 4. 10,000? *: (| [) 13 Five Description of the invention (11a) Comparative Example 7 At the end of the warranty period, the amine should be reacted. The production of amine should be reversed except for the example and the application. The reaction should be implemented. JiW The same sulfur 0 乙 I θ · I The purity of the base compound is not 2% 2 8 8 is the rate of production of arginine motilate-f-yl-L alpha-/-yl alpha-fermentation D-propionate propyl sulfide After the acid salt oil N is obtained, if the crystal is removed, the solvent is re-dissolved, the acetic acid vinegar is taken from the extracted alkylate, the formazan oil and gas, and then the acid is removed. Mixed with the base Ν 醯 之 三 銯 漯 单 醯 冯 入入基基 Ηίι A ao% base 7011 for the rate of sulfur production of acetylenic acid mono- Ο I acid amine A-α preserved in the insurance The mixture of Η Ρ 0 should be mixed with the mixture of nitrogen and acid under the temperature of the acid amine, and the temperature of the mixture should be reversed with V 0 5 to the mixture of hot additives. The temperature of the bath water should be 0 WU. Acetate P off 0 and go on and off at the same time. Open 1 degree and then hold the pH to keep its pH. The solubility of the liquid will be lowered to the end to complete 〇Η 化 ^ 0 Ν- take off (please read the notes on the back Then fill in the wood S) Pack · Order _
之¾. 中67 液為 溶率 應産 反該 析 , 分是 術果 析結 層其 體 。 液率 速産 高耳 0 莫 -總 後之 成 J 列 普 脫 普 卡 低 當 相 線_ 經濟部中央標準局貝工消費合作社印製 本紙張尺度遑用中國a家標準(CNS)甲4規格(210x297公*) 13a 睜正齊No. ¾. The 67 fluid is the dissolution rate and should be reversed, which is the fruit of the fruit. Liquid rate rapid production high ears 0 Mo-the total success of the J Leptopka low phase line _ Printed by the Central Standards Bureau of the Ministry of Economic Affairs Beigong Consumer Cooperative Paper standard using the Chinese a standard (CNS) A4 specifications (210x297g *) 13a
Claims (1)
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
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JP26372090A JPH04145065A (en) | 1990-10-03 | 1990-10-03 | Production of l-proline derivative |
JP28840690 | 1990-10-29 | ||
JP3069916A JP2896818B2 (en) | 1991-04-02 | 1991-04-02 | Method for producing L-proline derivative |
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TW219932B true TW219932B (en) | 1994-02-01 |
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TW81101621A TW219932B (en) | 1990-10-03 | 1992-03-03 |
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