TW391959B - Purification of sterically hindered 4-aminopiperidines - Google Patents

Purification of sterically hindered 4-aminopiperidines Download PDF

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TW391959B
TW391959B TW86107408A TW86107408A TW391959B TW 391959 B TW391959 B TW 391959B TW 86107408 A TW86107408 A TW 86107408A TW 86107408 A TW86107408 A TW 86107408A TW 391959 B TW391959 B TW 391959B
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distillation
hexahydropyridine
crude
added
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TW86107408A
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Chinese (zh)
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Manfred Julius
Harald Rust
Alfred Krause
Hardo Siegel
Wolfgang Siegel
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Basf Ag
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87.12. Θ 2彳多正 年月曰 補充 五、發明説明( 第861074〇8號專利申_案 中文説明書修正頁(87年& 本發明係關於純化式I粗六氫吡啶之方法87.12. Θ 2 彳 年 月 曰 曰 五 Supplementary V. Description of the invention (patent application No. 861074〇8 Chinese Version Correction Page (87 & The present invention is a method for purifying crude hexahydropyridine of formula I)

其R1至R4爲Cj-CV烷基,或者|^與尺2及/或以與^^〜起形 成2至5個碳之CH2-鏈。 式I之立體障礙六氫吡啶係經廣泛地應用,尤其係於合成 聚合物的UV安定劑之製備中作爲中間物。因此,相當重 要的是,六氫吡啶I本身儘可能具有極小之著色性,並且 即使含有微量副產物亦能長期保有此性質。 立體障礙之4 -胺六氫峨啶其工業製備係自丙酮或丙酮衍 .生物開始’化合物I可在氨水與氳存在下,於單.一階段的 催化性閉環反應中,自化合物 ! ---ο裝-- (請先聞讀背面之注意事項再填窝本頁) 、11Its R1 to R4 are Cj-CV alkyl groups, or | ^ and chi 2 and / or CH2- chains of 2 to 5 carbons are formed from ^^ ~. The sterically hindered hexahydropyridine of formula I is widely used, especially as an intermediate in the preparation of UV stabilizers for synthetic polymers. Therefore, it is quite important that the hexahydropyridine I itself has as little coloring property as possible, and that this property can be retained for a long period of time even if a trace by-product is contained. Stereotropic 4-amine hexahydroeridine is produced industrially from acetone or acetone. The biological start 'Compound I can be in a single stage in the presence of ammonia and tritium. In a one-stage catalytic ring-closure reaction, from compounds!- -ο 装-(Please read the precautions on the back before filling in this page), 11

經濟部中央標準局員工消費合作社印製 製得(DE 2 4 1 2 75〇)。或於單一或二階段的氨氫化反應中 ,自三丙酮胺Π於例如催化作用下製得,Printed by the Consumer Cooperatives of the Central Bureau of Standards of the Ministry of Economic Affairs (DE 2 4 1 2 75). Or in a single or two-stage hydrogenation reaction, prepared from triacetone amine, for example, under catalysis,

.11' -4 本紙張尺度適用中國國家標準(CMS ) A4規格(210X297公釐).11 '-4 This paper size applies to China National Standard (CMS) A4 specification (210X297 mm)

87.12. Θ 2彳多正 年月曰 補充 五、發明説明( 第861074〇8號專利申_案 中文説明書修正頁(87年& 本發明係關於純化式I粗六氫吡啶之方法87.12. Θ 2 彳 年 月 曰 曰 五 Supplementary V. Description of the invention (patent application No. 861074〇8 Chinese Version Correction Page (87 & The present invention is a method for purifying crude hexahydropyridine of formula I)

其R1至R4爲Cj-CV烷基,或者|^與尺2及/或以與^^〜起形 成2至5個碳之CH2-鏈。 式I之立體障礙六氫吡啶係經廣泛地應用,尤其係於合成 聚合物的UV安定劑之製備中作爲中間物。因此,相當重 要的是,六氫吡啶I本身儘可能具有極小之著色性,並且 即使含有微量副產物亦能長期保有此性質。 立體障礙之4 -胺六氫峨啶其工業製備係自丙酮或丙酮衍 .生物開始’化合物I可在氨水與氳存在下,於單.一階段的 催化性閉環反應中,自化合物 ! ---ο裝-- (請先聞讀背面之注意事項再填窝本頁) 、11Its R1 to R4 are Cj-CV alkyl groups, or | ^ and chi 2 and / or CH2- chains of 2 to 5 carbons are formed from ^^ ~. The sterically hindered hexahydropyridine of formula I is widely used, especially as an intermediate in the preparation of UV stabilizers for synthetic polymers. Therefore, it is quite important that the hexahydropyridine I itself has as little coloring property as possible, and that this property can be retained for a long period of time even if a trace by-product is contained. Stereotropic 4-amine hexahydroeridine is produced industrially from acetone or acetone. The biological start 'Compound I can be in a single stage in the presence of ammonia and tritium. In a one-stage catalytic ring-closure reaction, from compounds!- -ο 装-(Please read the precautions on the back before filling in this page), 11

經濟部中央標準局員工消費合作社印製 製得(DE 2 4 1 2 75〇)。或於單一或二階段的氨氫化反應中 ,自三丙酮胺Π於例如催化作用下製得,Printed by the Consumer Cooperatives of the Central Bureau of Standards of the Ministry of Economic Affairs (DE 2 4 1 2 75). Or in a single or two-stage hydrogenation reaction, prepared from triacetone amine, for example, under catalysis,

.11' -4 本紙張尺度適用中國國家標準(CMS ) A4規格(210X297公釐) 第 86107408 號專利^"——一一 中文説明書修正頁(^年以月)··, 士 \7 年月θ M t 1 M w ,'%七7 . ^ π , . 2 、.....-..................J . 1 補充 (見於例如 DE2040975, DE2349962, DE2621870, EP33529, EP42119, EP303279, EP410970, EP611137, EP623585 與 DE42〗0311)。此等工業上製備之立體障礙扣胺六氫吡啶 一般使用蒸顧純化。 然而,使用習知技術製備之六氫吡啶j,通常仍含有具干 擾夏的著色物質,或者,此等物質會於短時間後形成。 爲克服等狀態,已知例如在EP477 593中,經由添加 金屬硼^氣化物、並在特定條件下及水存在下進行蒸餾,可 改善粗產物N-烷基二烷醇胺之顏色問題。然而,N_烷基二 烷醇胺與本發明之立體障礙4_胺六氫吡啶係完全不同種類 I 物質。進一步從 Spec Chem 4⑺,Μ,, US3,159,276, 1153,207,790,與1^3,222,3 1 0 中已知,於蒸餾 之d或之後,經由添加硼氫化鈉於乙醇胺、伸乙胺或芳胺 中,以改良產物顏色係屬可行。然此文件亦未提及六氫吡 啶ί,更未提及特定的蒸餾技術。 相反的,高純度立體障礙之心胺六氫吡啶之形成方法, 係經由極爲不同的途徑。 經濟部中央標準局員工消費合作社印製 kDD2 6 6 799中已知,將六氫吡啶丨在丙酮/水之溶液中與 二氧化後反應,之後分離其沈澱物並以丙酮沖洗,接著進 行熱分解,並以蒸餾純化產物。su丨8 i i 527描述立體障 嶮I 4_胺六氫吡啶丨之另一純化技術··將受污染的粗產物溶 於非質子溶劑中並與乙二醇反應,蒸餾反應產物並經數個 步骤以純化。上述兩項技術皆極耗費力氣及成本。 因此,本發明之目的在於提供一種具成本效益之方法, -5 - 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 第 86107408 號專利^"——一一 中文説明書修正頁(^年以月)··, 士 \7 年月θ M t 1 M w ,'%七7 . ^ π , . 2 、.....-..................J . 1 補充 (見於例如 DE2040975, DE2349962, DE2621870, EP33529, EP42119, EP303279, EP410970, EP611137, EP623585 與 DE42〗0311)。此等工業上製備之立體障礙扣胺六氫吡啶 一般使用蒸顧純化。 然而,使用習知技術製備之六氫吡啶j,通常仍含有具干 擾夏的著色物質,或者,此等物質會於短時間後形成。 爲克服等狀態,已知例如在EP477 593中,經由添加 金屬硼^氣化物、並在特定條件下及水存在下進行蒸餾,可 改善粗產物N-烷基二烷醇胺之顏色問題。然而,N_烷基二 烷醇胺與本發明之立體障礙4_胺六氫吡啶係完全不同種類 I 物質。進一步從 Spec Chem 4⑺,Μ,, US3,159,276, 1153,207,790,與1^3,222,3 1 0 中已知,於蒸餾 之d或之後,經由添加硼氫化鈉於乙醇胺、伸乙胺或芳胺 中,以改良產物顏色係屬可行。然此文件亦未提及六氫吡 啶ί,更未提及特定的蒸餾技術。 相反的,高純度立體障礙之心胺六氫吡啶之形成方法, 係經由極爲不同的途徑。 經濟部中央標準局員工消費合作社印製 kDD2 6 6 799中已知,將六氫吡啶丨在丙酮/水之溶液中與 二氧化後反應,之後分離其沈澱物並以丙酮沖洗,接著進 行熱分解,並以蒸餾純化產物。su丨8 i i 527描述立體障 嶮I 4_胺六氫吡啶丨之另一純化技術··將受污染的粗產物溶 於非質子溶劑中並與乙二醇反應,蒸餾反應產物並經數個 步骤以純化。上述兩項技術皆極耗費力氣及成本。 因此,本發明之目的在於提供一種具成本效益之方法, -5 - 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 第861〇74〇8號專剝:未請案, 中文説明書修正頁(87年12月) 11-1111- 11.1 , — 一.11 '-4 This paper size is applicable to Chinese National Standard (CMS) A4 specification (210X297 mm) Patent No. 86107408 ^ " —— One-to-One Chinese Manual Correction Page (^ year to month) ·, taxi \ 7 Year and month θ M t 1 M w, '% 七 7. ^ Π,. 2, .....-........ J. 1 Supplement (see in For example, DE2040975, DE2349962, DE2621870, EP33529, EP42119, EP303279, EP410970, EP611137, EP623585 and DE42 (0311). These industrially prepared sterically hindered amine hexahydropyridines are generally purified by distillation. However, the hexahydropyridine j prepared by the conventional technique usually still contains a disturbing coloring substance, or these substances may be formed after a short time. In order to overcome such conditions, it is known that, for example, in EP477 593, the color problem of the crude product N-alkyldialkanolamine can be improved by adding metal boron gaseous distillation and performing distillation under specific conditions and in the presence of water. However, the N-alkyl dialkanolamine is completely different from the sterically hindered 4-amine hexahydropyridine of the present invention in the class I substance. It is further known from Spec Chem 4 (M), US, US 3,159,276, 1153,207,790, and 1 ^ 3,222,3 1 0. After d or after distillation, sodium borohydride is added to ethanolamine, ethyleneamine or arylamine. It is feasible to improve the product color. However, this document does not mention hexahydropyridine, let alone specific distillation techniques. In contrast, the formation of high-purity steric heart amine hexahydropyridine takes a very different route. It is known in the printing of kDD2 6 6 799 by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs that hexahydropyridine 丨 is reacted with dioxidation in an acetone / water solution, after which the precipitate is separated and washed with acetone, followed by thermal decomposition The product was purified by distillation. su 丨 8 ii 527 describes another purification technique of steric hindrance I 4_amine hexahydropyridine 丨 · The contaminated crude product is dissolved in an aprotic solvent and reacted with ethylene glycol, the reaction product is distilled and subjected to several Steps for purification. Both of these technologies are extremely laborious and costly. Therefore, the purpose of the present invention is to provide a cost-effective method. -5-This paper size is applicable to the Chinese National Standard (CNS) A4 specification (210X297 mm) Patent No. 86107408 ^ " —— One-to-one Chinese specification amendment Page (^ year by month) ..., taxi \ 7 year month θ M t 1 M w, '% 七 7. ^ Π,. 2, .....-........... ....... J. 1 supplements (see for example DE2040975, DE2349962, DE2621870, EP33529, EP42119, EP303279, EP410970, EP611137, EP623585 and DE42) 0311). These industrially prepared sterically hindered amine hexahydropyridines are generally purified by distillation. However, the hexahydropyridine j prepared by the conventional technique usually still contains a disturbing coloring substance, or these substances may be formed after a short time. In order to overcome such conditions, it is known that, for example, in EP477 593, the color problem of the crude product N-alkyldialkanolamine can be improved by adding metal boron gaseous distillation and performing distillation under specific conditions and in the presence of water. However, the N-alkyl dialkanolamine is completely different from the sterically hindered 4-amine hexahydropyridine of the present invention in the class I substance. It is further known from Spec Chem 4 (M), US, US 3,159,276, 1153,207,790, and 1 ^ 3,222,3 1 0. After d or after distillation, sodium borohydride is added to ethanolamine, ethyleneamine or arylamine. It is feasible to improve the product color. However, this document does not mention hexahydropyridine, let alone specific distillation techniques. In contrast, the formation of high-purity steric heart amine hexahydropyridine takes a very different route. It is known in the printing of kDD2 6 6 799 by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs that hexahydropyridine 丨 is reacted with dioxidation in an acetone / water solution, after which the precipitate is separated and washed with acetone, followed by thermal decomposition The product was purified by distillation. su 丨 8 ii 527 describes another purification technique of steric hindrance I 4_amine hexahydropyridine 丨 · The contaminated crude product is dissolved in an aprotic solvent and reacted with ethylene glycol, the reaction product is distilled and subjected to several Steps for purification. Both of these technologies are extremely laborious and costly. Therefore, the object of the present invention is to provide a cost-effective method. -5-This paper size applies Chinese National Standard (CNS) A4 specification (210X297mm) No. 86107048: Stripped: Unclaimed, Chinese Manual revision page (December 87) 11-1111- 11.1, — 1

五、發明説明( 經由本發明之方法可製得高純度、顏色穩定的立體障礙之 4:胺六氫^卜即,產物可長期保持低程度著色性與低含 量副產物,諸如穩定輔劑。 ° 我們已發現此目的係經由上述方法而達成,丨包括,於 第一步驟中,經由蒸餾將高沸點物質以及,若存在,水,' 自粗六氫❹中奋除;第二步驟中,添加爲第—步驟產物 重量之0.01-5%的還原劑;及第三步驟中,經由蒸餘分離 六氫P比淀。 本發明其他特徵詳明於申請專利範圍附屬項中。 亙體障礙之4-胺六氫吡啶丨中,…上^與^係較佳分別 爲(^-(:3烷基,尤其是乙基或甲基,例如甲基。 經濟部中央標準局員工消費合作社印製 返原劑一般係使用標準狀態下爲固體之物質,較優之化 合物爲MXH4_mYra,其M爲鹼金屬,NR4,其中各個尺係相 同或不同之Ci-C:4烷基,或i當量之鹼土金屬或1當量之鋅 較佳爲驗益屬,尤其.是朝或卸,例如爲鈉時,X是銘或 尤/、疋朋.Y疋CN或較佳爲氫,及瓜爲}或〇或尤其是〇。實 例I—爲硼氫化鈉,已發現(RaO)2TiBH4或(Ra〇)3TiBH4, 其中Ra爲C! -C4-烷基者,係.適用於本發明中。 本新穎方法可於大氣或較佳於減壓下,尤其是1〇_2〇〇毫 巴’例如從2〇_100毫巴,經由連續或批次進行。 f1*非另外指出,否則本發明中所界定之沸點或沸點範圍 係相關於壓力4〇毫巴下測定者,其係關於每一例中4_胺_ 2,2,6,6,-六氫吡啶之純化。對於其他扣胺六氫吡啶丨,技藝 人士可經由簡單實驗導出適當的條件。 —6 - 本紙張尺度適财酬家辟(CNS)〜驗(⑽心祕 第861〇74〇8號專剝:未請案, 中文説明書修正頁(87年12月) 11-1111- 11.1 , — 一V. Description of the invention (The method of the present invention can be used to prepare a high-purity, color-stable steric obstacle 4: amine hexahydrogen. That is, the product can maintain low-level colorability and low content of by-products such as stable auxiliary agents for a long time. ° We have found that this is achieved by the method described above, which includes, in the first step, the high boiling point substance and, if present, water, are removed from the crude hexahydropyrene through distillation; in the second step, The reducing agent is added in an amount of 0.01-5% of the weight of the product in the first step; and in the third step, the hexahydro P ratio is separated by distillation. Other features of the present invention are detailed in the appendix to the scope of the patent application. Carcass barrier 4 In the amine hexahydropyridine, the above ^ and ^ are preferably (^-(: 3 alkyl, especially ethyl or methyl, such as methyl. Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs.) The original agent is generally a solid material in the standard state. The preferred compound is MXH4_mYra, where M is an alkali metal, and NR4, in which each size is the same or different Ci-C: 4 alkyl, or i-equivalent alkaline earth metal. Or 1 equivalent of zinc is preferred In particular, it is oriented or unloaded, for example, when it is sodium, X is Ming or especially, Y.CN or preferably hydrogen, and melamine is} or 〇 or especially 〇. Example I-is sodium borohydride, It has been found that (RaO) 2TiBH4 or (Ra〇) 3TiBH4, where Ra is C! -C4-alkyl, is suitable for use in the present invention. The novel method can be used in the atmosphere or preferably under reduced pressure, especially 1 〇_2〇〇mbar ', for example, from 20-100 mbar, continuous or batch. F1 * Unless otherwise specified, otherwise the boiling point or boiling point range defined in the present invention is related to a pressure of 40 mbar The tester is about the purification of 4-amine_2,2,6,6, -hexahydropyridine in each case. For other amines hexahydropyridine, the skilled person can derive appropriate conditions through simple experiments. —6 -This paper is suitable for home finances (CNS) ~ inspection (Xin Xin Mi No. 86107074): Unclaimed, Chinese manual amendment page (December 87) 11-1111- 11.1, — One

五、發明説明( 經由本發明之方法可製得高純度、顏色穩定的立體障礙之 4:胺六氫^卜即,產物可長期保持低程度著色性與低含 量副產物,諸如穩定輔劑。 ° 我們已發現此目的係經由上述方法而達成,丨包括,於 第一步驟中,經由蒸餾將高沸點物質以及,若存在,水,' 自粗六氫❹中奋除;第二步驟中,添加爲第—步驟產物 重量之0.01-5%的還原劑;及第三步驟中,經由蒸餘分離 六氫P比淀。 本發明其他特徵詳明於申請專利範圍附屬項中。 亙體障礙之4-胺六氫吡啶丨中,…上^與^係較佳分別 爲(^-(:3烷基,尤其是乙基或甲基,例如甲基。 經濟部中央標準局員工消費合作社印製 返原劑一般係使用標準狀態下爲固體之物質,較優之化 合物爲MXH4_mYra,其M爲鹼金屬,NR4,其中各個尺係相 同或不同之Ci-C:4烷基,或i當量之鹼土金屬或1當量之鋅 較佳爲驗益屬,尤其.是朝或卸,例如爲鈉時,X是銘或 尤/、疋朋.Y疋CN或較佳爲氫,及瓜爲}或〇或尤其是〇。實 例I—爲硼氫化鈉,已發現(RaO)2TiBH4或(Ra〇)3TiBH4, 其中Ra爲C! -C4-烷基者,係.適用於本發明中。 本新穎方法可於大氣或較佳於減壓下,尤其是1〇_2〇〇毫 巴’例如從2〇_100毫巴,經由連續或批次進行。 f1*非另外指出,否則本發明中所界定之沸點或沸點範圍 係相關於壓力4〇毫巴下測定者,其係關於每一例中4_胺_ 2,2,6,6,-六氫吡啶之純化。對於其他扣胺六氫吡啶丨,技藝 人士可經由簡單實驗導出適當的條件。 —6 - 本紙張尺度適财酬家辟(CNS)〜驗(⑽心祕 第801〇74〇8號專收今V. Description of the invention (The method of the present invention can be used to prepare a high-purity, color-stable steric obstacle 4: amine hexahydrogen. That is, the product can maintain low-level colorability and low content of by-products such as stable auxiliary agents for a long time. ° We have found that this is achieved by the method described above, which includes, in the first step, the high boiling point substance and, if present, water, are removed from the crude hexahydropyrene through distillation; in the second step, The reducing agent is added in an amount of 0.01-5% of the weight of the product in the first step; and in the third step, the hexahydro P ratio is separated by distillation. Other features of the present invention are detailed in the appendix to the scope of the patent application. Carcass barrier 4 In the amine hexahydropyridine, the above ^ and ^ are preferably (^-(: 3 alkyl, especially ethyl or methyl, such as methyl. Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs.) The original agent is generally a solid material in the standard state. The preferred compound is MXH4_mYra, where M is an alkali metal, and NR4, in which each size is the same or different Ci-C: 4 alkyl, or i-equivalent alkaline earth metal. Or 1 equivalent of zinc is preferred In particular, it is oriented or unloaded, for example, when it is sodium, X is Ming or especially, Y.CN or preferably hydrogen, and melamine is} or 〇 or especially 〇. Example I-is sodium borohydride, It has been found that (RaO) 2TiBH4 or (Ra〇) 3TiBH4, where Ra is C! -C4-alkyl, is suitable for use in the present invention. The novel method can be used in the atmosphere or preferably under reduced pressure, especially 1 〇_2〇〇mbar ', for example, from 20-100 mbar, continuous or batch. F1 * Unless otherwise specified, otherwise the boiling point or boiling point range defined in the present invention is related to a pressure of 40 mbar The tester is about the purification of 4-amine_2,2,6,6, -hexahydropyridine in each case. For other amines hexahydropyridine, the skilled person can derive appropriate conditions through simple experiments. —6 -This paper is suitable for home finance (CNS) ~ Experience (Jin Xin Mi No. 80107074)

五、發明説明( 經濟部中央標準局員工消費合作社印製 一般所指之鬲沸點物質,係彼等於壓力4 〇毫巴下,具有 南於所欲產物沸點至少3 5以上之沸點者。在4 _胺_ 2,2,6,6-四甲基六氫吡啶中,高沸點物質係經由蒸餾去除 ,例如,在1 4 0 °C及4 0毫巴之下。 第一步驟中,粗產物係經由蒸餾而將高沸點物質完全去 除,以及,於本發明之特別具體實例中,係爲將水去除。 一般係經由(a)精餾,其中高沸點物質係以液相移除,而水 係以單一步驟由精餾塔頂端去除,或者藉由在適當裝置 中,如拭葉蒸餾器’落膜蒸餾器或連接濃縮器的攪拌容器 ’經由蒸餾將粗產物自高沸點物質中餾出,接著蒸餾以移 除水。水的分離是不重要的,且可在例如1 0 0毫巴,4 0 - 5 0 °C或在適當的不同壓力下而進行。爲分離高沸點物質,蒸 餾之液相通常加熱至1 4 0 °C (4 0毫巴下)。較佳的結果係獲得 存在少量高沸點物質之六氫吡啶I。一般而言,六氫吡啶Ϊ 中含有低於其重量之0.1 %的高沸點成分仍可接受,然而, 較佳爲高沸點成分的含量係低於六氩吡啶重量之0.0 1 %。 水含量是不重要的且通常調整至六氫吡啶重量之1 °/。_以下 0 接著,於第二步驟中添加還原劑,一般添加重量計爲 〇 . 〇 1 -2 %的量即可得到具有所欲性質之無色產物’較佳係 使用其以重量之0 · 0 1 -1 %,尤其是0 . 〇卜0 · 5 %。添加方法並 不重要;還原劑通常可以粉末或溶液形式添加於寐'館的液 相中。 於添加還原劑後,產物係經由蒸顧而純化’通常以習知 本紙張尺度適用中國國家標準(CNS ) A4規格(21〇χ297公釐) 請 先 閱 讀 背 ft 之 注 意 事 項V. Description of the invention (Generally referred to as “boiling point substances” printed by employees' consumer cooperatives of the Central Bureau of Standards of the Ministry of Economic Affairs, those who have a boiling point of at least 35 above the desired product at a pressure of 40 mbar. _Amine_ In 2,2,6,6-tetramethylhexahydropyridine, high-boiling substances are removed by distillation, for example, at 140 ° C and 40 mbar. In the first step, the crude product High boiling point substances are completely removed by distillation, and, in a particular embodiment of the present invention, water is removed. Generally, (a) rectification is performed in which high boiling point substances are removed in the liquid phase and water It is removed from the top of the rectification column in a single step, or the crude product is distilled off from the high-boiling point substance by distillation in a suitable device, such as a leaf wiper 'falling film still or stirred vessel connected to a concentrator', Distillation is then performed to remove the water. The separation of the water is not important and can be carried out at, for example, 100 mbar, 40-50 ° C or under suitable different pressures. To separate high-boiling substances, distill The liquid phase is usually heated to 140 ° C (under 40 mbar). Better As a result, hexahydropyridine I with a small amount of high-boiling substances is obtained. In general, hexahydropyridine hydrazone containing less than 0.1% by weight of high-boiling components is still acceptable, however, the content of high-boiling components is preferred It is less than 0.01% by weight of hexaargyridine. The water content is not important and is usually adjusted to 1 ° / of the weight of hexahydropyridine. _ Following 0 Next, in the second step, a reducing agent is added, and the weight is generally added as 〇. 〇1-2% of the amount can be obtained with the desired properties of colorless products' preferably to use 0. 0 1 -1% by weight, especially 0. 〇0 0. 5%. Add the method and It is not important; the reducing agent can usually be added to the liquid phase of the 馆 'kan in the form of powder or solution. After adding the reducing agent, the product is purified by steaming.' Usually the Chinese paper standard (CNS) A4 is applicable to this paper standard. Specifications (21〇χ297mm) Please read the precautions for back ft first

费 褽 .1% 第801〇74〇8號專收今Fee 褽 .1% Special Collection No. 80107074

五、發明説明( 經濟部中央標準局員工消費合作社印製 一般所指之鬲沸點物質,係彼等於壓力4 〇毫巴下,具有 南於所欲產物沸點至少3 5以上之沸點者。在4 _胺_ 2,2,6,6-四甲基六氫吡啶中,高沸點物質係經由蒸餾去除 ,例如,在1 4 0 °C及4 0毫巴之下。 第一步驟中,粗產物係經由蒸餾而將高沸點物質完全去 除,以及,於本發明之特別具體實例中,係爲將水去除。 一般係經由(a)精餾,其中高沸點物質係以液相移除,而水 係以單一步驟由精餾塔頂端去除,或者藉由在適當裝置 中,如拭葉蒸餾器’落膜蒸餾器或連接濃縮器的攪拌容器 ’經由蒸餾將粗產物自高沸點物質中餾出,接著蒸餾以移 除水。水的分離是不重要的,且可在例如1 0 0毫巴,4 0 - 5 0 °C或在適當的不同壓力下而進行。爲分離高沸點物質,蒸 餾之液相通常加熱至1 4 0 °C (4 0毫巴下)。較佳的結果係獲得 存在少量高沸點物質之六氫吡啶I。一般而言,六氫吡啶Ϊ 中含有低於其重量之0.1 %的高沸點成分仍可接受,然而, 較佳爲高沸點成分的含量係低於六氩吡啶重量之0.0 1 %。 水含量是不重要的且通常調整至六氫吡啶重量之1 °/。_以下 0 接著,於第二步驟中添加還原劑,一般添加重量計爲 〇 . 〇 1 -2 %的量即可得到具有所欲性質之無色產物’較佳係 使用其以重量之0 · 0 1 -1 %,尤其是0 . 〇卜0 · 5 %。添加方法並 不重要;還原劑通常可以粉末或溶液形式添加於寐'館的液 相中。 於添加還原劑後,產物係經由蒸顧而純化’通常以習知 本紙張尺度適用中國國家標準(CNS ) A4規格(21〇χ297公釐) 請 先 閱 讀 背 ft 之 注 意 事 項V. Description of the invention (Generally referred to as “boiling point substances” printed by employees' consumer cooperatives of the Central Bureau of Standards of the Ministry of Economic Affairs, those who have a boiling point of at least 35 above the desired product at a pressure of 40 mbar. _Amine_ In 2,2,6,6-tetramethylhexahydropyridine, high-boiling substances are removed by distillation, for example, at 140 ° C and 40 mbar. In the first step, the crude product High boiling point substances are completely removed by distillation, and, in a particular embodiment of the present invention, water is removed. Generally, (a) rectification is performed in which high boiling point substances are removed in the liquid phase and water It is removed from the top of the rectification column in a single step, or the crude product is distilled off from the high-boiling point substance by distillation in a suitable device, such as a leaf wiper 'falling film still or stirred vessel connected to a concentrator', Distillation is then performed to remove the water. The separation of the water is not important and can be carried out at, for example, 100 mbar, 40-50 ° C or under suitable different pressures. To separate high-boiling substances, distill The liquid phase is usually heated to 140 ° C (under 40 mbar). Better As a result, hexahydropyridine I with a small amount of high-boiling substances is obtained. In general, hexahydropyridine hydrazone containing less than 0.1% by weight of high-boiling components is still acceptable, however, the content of high-boiling components is preferred It is less than 0.01% by weight of hexaargyridine. The water content is not important and is usually adjusted to 1 ° / of the weight of hexahydropyridine. _ Following 0 Next, in the second step, a reducing agent is added, and the weight is generally added as 〇. 〇1-2% of the amount can be obtained with the desired properties of colorless products' preferably to use 0. 0 1 -1% by weight, especially 0. 〇0 0. 5%. Add the method and It is not important; the reducing agent can usually be added to the liquid phase of the 馆 'kan in the form of powder or solution. After adding the reducing agent, the product is purified by steaming.' Usually the Chinese paper standard (CNS) A4 is applicable to this paper standard. Specifications (21〇χ297mm) Please read the precautions for back ft first

费 褽 .1% 細59 第86107408號專利 中文説明書修正頁Fee 褽 .1% Fine 59 Patent No. 86107408 Revised Chinese Manual

五、發明説明 4.9 %中及高沸點物質 係在MO°C及4〇毫巴下,使用拭葉蒸發器(2〇0平方公分蒸 發器表面積,4〇Orpm)蒸餾。進料速率爲500克/小時(預熱 至100°C),液相溫度l〇6°C,塔頂溫度爲89。(:,蒸餾出256〇 克(92.3%)。蒸餾後成分如下: 8 7.2 %三丙酮二胺 9.9 % 水 1 · 5 %低沸點物質 1.4%中及高沸點物質 經濟部中央標準局員工消費合作社印製 粗TAD產物係經由2.4公尺Sulzer_CY充填之管柱(約η 理論層板’寬度43毫米)、於壓力1〇〇毫巴下、以5:1之比 例迴流,而與高沸點物質分離。當塔頂溫度43_44°C時, 首先蒸餾出2 5 6克水。蒸餾時,添加〇丨。/。硼氫化鈉於液 相中’並於4 〇毫巴連績精餾。塔頂溫度8 9。〇時,分離餾 出物含8 5 _ 9 % TAD( 1 1 1克),進—步分餾於塔頂溫度99。〇 時’分離餾出物含有9S 4%TAD(24〇克)。在塔頂溫度99-i〇2°C時,精餾的主要餾出物含有純度99 8 〇/〇(GC) 1 786克 T AD,蒸館產率爲7 7 %。 A) 純TAD顏色穩定至少超過5週(APhA顏色數値&lt;5 0) ’結果列於下表。 B) 經由此技術而得之TAD樣品係於添加1 1 0 ppm硼氫化 納下儲存,經此添加,TAD產物確實無色至少5週,此外 ’其顏色穩定,測得ΑΡΗA顏色數値&lt; 1 5。 樣品(A)與(B)儲存於室溫相同狀沉下。 本紙張尺度適用中國國^1^7^-2;&gt;&lt;297公 五、發明説明(5 的精鶴塔完成,如層板塔或填充塔,較佳爲後者 不同的迴流比操作,其係杈藝人 ⑨ ^ ..ai, ^ , 士了使用間要的預先實驗 而4速獻h已證實適用以脱去'產物量之遊流比係^ 至1〇:1,尤其係自3:1至7:1。產物4_胺_2,2,6,6_四^基六氬 吡啶係於101。。及在40毫巴下沸騰,如同技藝人士可輕易 察知的(例如,J TP〇lvm ς^,· Ώ ^ .. • r〇lym. bC1·,Part A-1,1〇⑴),(1972) 3295-310)。因此,一般可於96_1〇3^(4〇毫巴下)獲得。 對於得之本身爲無色之產物,可添加少量還原劑而增加 儲藏時之穩定性,還原劑通常係爲上述之物質,一般係添 加以重量計爲產物之0_001_0.02〇/〇。一般而言,最多2〇〇 ppm的還原劑量係爲足夠。在特殊情況中,丨〇〇_,5〇或 lOppm即已足夠。 此新穎方法係以簡單及成本效益的方式,提供純的立體 障礙之4 -胺六氫吡啶I,其確實無色,且於儲存期間 '於 含有極低含量如穩定劑的副產物時,仍可同時保持顏色之 穩定。 實例 經濟部中央標準局員工消費合作社印製 立體障礙之4-胺六氫吡啶I之顏色測定係經由DIN-JSO 627 1測定APHA顏色數値。 , 實例1 粗4-胺-2.;2,6,6-四曱六氫吡啶含有下列成分 83.6%三丙酮二胺(TAD) 10.0% 水 1·5%低沸點物質 本纸張尺度適用中國國家標準(CNS ) Α4规格(210X297公釐) J91959 第861〇74〇8號專利史請襄 中文説明書修正頁 ---— 丨---- 五、發明説明( 請 先 閲 讀 背 之 注 意 事 項 再, 43耄米)、於壓力100毫巴下、以5:1之比例迴流精餾。於 壓力100毫巴下,43-44。(:時蒸餾出349克主要含有水之起 始德出物’。接著添加3.0克(以重量計爲〇 ·丨〇/。)硼氫化鈉 於含有低於0 · 1 %水之蒸餾液相中,並繼續精餾。待起始餾 出物222克之TAD具有純度99.0 %,之後,可於壓力4〇毫巴 下’塔頂溫度9:TC時獲得主要餾出物,其含有2丨丨g克、純 度爲99.7 %以及水含量&lt;〇〗%之TAD,蒸餾產率2丨丨6克(82 %)。 於氮氣下黑暗中儲存兩天,所得之純TAD產物變爲黃色 (APHA顏色數値&gt;100)。 比較實例2 訂 4208克粗TAD組合物 85.6%三丙酮二胺(TAD) 9.0% 水 約0.7 %低沸點物質 4.7 %中及高沸點物質 經濟部中央標準局員工消費合作社印製 於100至4〇毫巴壓力下,經由2·4公尺Sulzer-CY充填之管柱 (約2 2理論層板,寬度4 3毫米),以5 :1之比例迴流精館。接 著在磨力1〇〇爱巴下及於43_44〇時,自起始館出物中分離 水,於壓力4〇毫巴下,塔頂溫度97-1 03°C時,得到主要館 出物,其含有TAD含量&gt;99.6 % (GC)之純TAD餾出物,蒸飽 產率:3022 克(84%)。 純餾出物(GC測出T AD含量99 ·7 % )儲存於無硼氫化鋼, 與儲存於添加硼氫化鈉中,如例1,並測定之,其結果如 -11 - 本纸張尺度適用中國國家標準(CNS ) Α4規格(2丨0X297公釐) 細59 第86107408號專利 中文説明書修正頁V. Description of the invention 4.9% medium and high boiling point materials are distilled at MO ° C and 40 mbar using a wiper evaporator (200 cm2 evaporator surface area, 400 rpm). The feed rate was 500 g / h (preheated to 100 ° C), the liquid phase temperature was 106 ° C, and the top temperature was 89. (:, 2560 grams (92.3%) are distilled off. The components after distillation are as follows: 8 7.2% triacetone diamine 9.9% water 1.5% low-boiling substances 1.4% medium and high-boiling substances Employees' Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs The printed crude TAD product is separated from high-boiling substances through a 2.4-meter Sulzer_CY-filled column (approximately η theoretical plate 'width of 43 mm) at a pressure of 100 mbar and reflux at a ratio of 5: 1 When the temperature at the top of the column is 43-44 ° C, 256 g of water is distilled off first. During the distillation, 〇 丨 sodium borohydride in the liquid phase is added and the continuous distillation is performed at 40 mbar. The temperature at the top of the column At 8 o'clock, the separated distillate contained 8 5-9% TAD (11 1 g), and further fractionated at the top temperature of 99.0 o'clock. The separated distillate contained 9S 4% TAD (24.0 g). ). At the top temperature of 99-102 ° C, the main distillate of the rectification contained a purity of 99 8 0 / (GC) 1 786 g T AD, and the yield of the steamhouse was 77%. A) Pure The TAD color was stable for at least 5 weeks (APhA color number 値 <50). The results are shown in the table below. B) The TAD sample obtained by this technology is stored under the addition of 110 ppm sodium borohydride. After this addition, the TAD product is indeed colorless for at least 5 weeks. In addition, its color is stable. 5. Samples (A) and (B) were stored at room temperature and sunk. This paper scale is applicable to China ^ 1 ^ 7 ^ -2; &gt; &lt; 297. V. Description of the invention (5's completed crane tower, such as a slab tower or a packed tower, preferably the latter with a different reflux ratio operation, The artiste ⑨ ^ ..ai, ^, has applied the pre-experiment and the 4 speed h has been proven to be suitable for removing the product flow ratio ^ to 10: 1, especially from 3 : 1 to 7: 1. The product 4_amine_2,2,6,6_tetratylhexahydropyridine is at 101 ... and boils at 40 mbar, as can be easily detected by the skilled person (for example, J TP〇lvm ς ^, Ώ ^ ^ .. • rlym. BC1 ·, Part A-1, 10⑴), (1972) 3295-310). Therefore, it is generally available at 96-103 (under 40 mbar). For products that are colorless in nature, a small amount of reducing agent can be added to increase the stability during storage. The reducing agent is usually the above-mentioned substance, and it is generally added to 0_001_0.02 // by weight of the product. In general, a reducing dose of up to 200 ppm is sufficient. In special cases, 〇〇〇_, 50 or 10 ppm is sufficient. This novel method provides a simple and cost-effective way to provide pure sterically hindered 4-amine hexahydropyridine I, which is indeed colorless and can be used during storage 'with very low levels of by-products such as stabilizers. At the same time keep the color stable. Example Printed by the Consumers' Cooperative of the Central Bureau of Standards of the Ministry of Economics. The color determination of 4-aminehexahydropyridine I for steric disorders is determined by DIN-JSO 627 1 for the APHA color number. Example 1 Crude 4-amine-2.; 2,6,6-tetrahydropyridine contains the following ingredients: 83.6% triacetone diamine (TAD) 10.0% water 1.5% low boiling point substance This paper applies to China National Standard (CNS) Α4 Specification (210X297 mm) J91959 No. 861〇74〇8 Patent History, please revise page of Chinese specification ------- 丨 ---- V. Description of invention (Please read the precautions in the back first (43 耄 m), reflux distillation at a pressure of 100 mbar at a ratio of 5: 1. 43-44 at 100 mbar. (: 349 grams of the original German extract mainly containing water was distilled off at that time. Next, 3.0 grams (by weight 〇 · 丨 〇 /.) Of sodium borohydride was added in a distillation liquid phase containing less than 0.1% water. After the TAD of 222 g of the initial distillate has a purity of 99.0%, the main distillate can be obtained at a pressure of 40 mbar at the top temperature of the column 9: TC, which contains 2 丨 丨g of TAD with a purity of 99.7% and a water content of &lt; 〇%, a distillation yield of 2 丨 6 g (82%). Stored in nitrogen in the dark for two days, the resulting pure TAD product turned yellow (APHA Color number 値> 100). Comparative Example 2 Order 4208 g of crude TAD composition 85.6% triacetone diamine (TAD) 9.0% water 0.7% low boiling point substance 4.7% medium and high boiling point substance consumption by the Central Standards Bureau of the Ministry of Economic Affairs Cooperatives are printed at a pressure of 100 to 40 mbar through a 2.4-meter Sulzer-CY-filled column (approximately 22 theoretical laminates, with a width of 43 mm) and returned to the fine hall at a ratio of 5: 1. Then under the grinding force of 100 bar and at 43-44 o'clock, water was separated from the output of the starting hall, under the pressure of 40 mbar, the temperature of the top of the tower was 97-1 03 ° C. At that time, the main library output was obtained, which contained a pure TAD distillate with a TAD content &gt; 99.6% (GC). The steam-saturated yield: 3022 g (84%). Pure distillate (GC measured T AD content 99 · 7%) stored in borohydride-free steel, and stored in sodium borohydride, as in Example 1, and measured, the results are shown as -11-This paper size applies Chinese National Standard (CNS) Α4 specification (2 丨0X297 mm) Fine 59 Chinese Patent No. 86107408 Revised Page

五、發明説明 4.9 %中及高沸點物質 係在MO°C及4〇毫巴下,使用拭葉蒸發器(2〇0平方公分蒸 發器表面積,4〇Orpm)蒸餾。進料速率爲500克/小時(預熱 至100°C),液相溫度l〇6°C,塔頂溫度爲89。(:,蒸餾出256〇 克(92.3%)。蒸餾後成分如下: 8 7.2 %三丙酮二胺 9.9 % 水 1 · 5 %低沸點物質 1.4%中及高沸點物質 經濟部中央標準局員工消費合作社印製 粗TAD產物係經由2.4公尺Sulzer_CY充填之管柱(約η 理論層板’寬度43毫米)、於壓力1〇〇毫巴下、以5:1之比 例迴流,而與高沸點物質分離。當塔頂溫度43_44°C時, 首先蒸餾出2 5 6克水。蒸餾時,添加〇丨。/。硼氫化鈉於液 相中’並於4 〇毫巴連績精餾。塔頂溫度8 9。〇時,分離餾 出物含8 5 _ 9 % TAD( 1 1 1克),進—步分餾於塔頂溫度99。〇 時’分離餾出物含有9S 4%TAD(24〇克)。在塔頂溫度99-i〇2°C時,精餾的主要餾出物含有純度99 8 〇/〇(GC) 1 786克 T AD,蒸館產率爲7 7 %。 A) 純TAD顏色穩定至少超過5週(APhA顏色數値&lt;5 0) ’結果列於下表。 B) 經由此技術而得之TAD樣品係於添加1 1 0 ppm硼氫化 納下儲存,經此添加,TAD產物確實無色至少5週,此外 ’其顏色穩定,測得ΑΡΗA顏色數値&lt; 1 5。 樣品(A)與(B)儲存於室溫相同狀沉下。 本紙張尺度適用中國國^1^7^-2;&gt;&lt;297公 391959 五、發明説明(7 ) 儲存天數 顏色數値(未稀釋產物) (A) 未加NaBH4 (B)添加 1 1 Oppm NaBH4 13 43 5 14 37 6 16 37 5 18 38 4 19 40 3 20 38 .7 21 41 11 22 36 8 25 48 13 32 36 3 39 43 4 比較性實例1 經濟部中央標準局員工消費合作社印製 2987克粗TAD其成分爲 8 7.2 %三丙酮二胺 : 8.7% 水 約Μ %低沸點物質 4.0%中及高沸點物質 使用2.4公尺Sulzer-CY充填之管柱(約22理論層板,寬度V. Description of the invention 4.9% medium and high boiling point materials are distilled at MO ° C and 40 mbar using a wiper evaporator (200 cm2 evaporator surface area, 400 rpm). The feed rate was 500 g / h (preheated to 100 ° C), the liquid phase temperature was 106 ° C, and the top temperature was 89. (:, 2560 grams (92.3%) are distilled off. The components after distillation are as follows: 8 7.2% triacetone diamine 9.9% water 1.5% low-boiling substances 1.4% medium and high-boiling substances Employees' Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs The printed crude TAD product is separated from high-boiling substances through a 2.4-meter Sulzer_CY-filled column (approximately η theoretical plate 'width of 43 mm) at a pressure of 100 mbar and reflux at a ratio of 5: 1. When the temperature at the top of the column is 43-44 ° C, 256 g of water is distilled off first. During the distillation, 〇 丨 sodium borohydride in the liquid phase is added and the continuous distillation is performed at 40 mbar. The temperature at the top of the column At 8 o'clock, the separated distillate contained 8 5-9% TAD (11 1 g), and further fractionated at the top temperature of 99.0 o'clock. The separated distillate contained 9S 4% TAD (24.0 g). ). At the top temperature of 99-102 ° C, the main distillate of the rectification contained a purity of 99 8 0 / (GC) 1 786 g T AD, and the yield of the steamhouse was 77%. A) Pure The TAD color was stable for at least 5 weeks (APhA color number 値 <50). The results are shown in the table below. B) The TAD sample obtained by this technology is stored under the addition of 110 ppm sodium borohydride. After this addition, the TAD product is indeed colorless for at least 5 weeks. In addition, its color is stable. 5. Samples (A) and (B) were stored at room temperature and sunk. This paper size is applicable to China ^ 1 ^ 7 ^ -2; &gt; &lt; 297 public 391959 V. Description of the invention (7) Number of days of storage 値 Color (undiluted product) (A) Without NaBH4 (B) Added 1 1 Oppm NaBH4 13 43 5 14 37 6 16 37 5 18 38 4 19 40 3 20 38 .7 21 41 11 22 36 8 25 48 13 32 36 3 39 43 4 Comparative example 1 Printed by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 2987 grams of crude TAD contains 8 7.2% triacetone diamine: 8.7% water, about Μ%, low boiling point materials, 4.0% medium and high boiling point materials. Use a 2.4 m Sulzer-CY packed column (about 22 theoretical laminates, width

T A 1/ J i τ * y Z X υ ζ J91959 第861〇74〇8號專利史請襄 中文説明書修正頁 ---— 丨---- 五、發明説明( 請 先 閲 讀 背 之 注 意 事 項 再, 43耄米)、於壓力100毫巴下、以5:1之比例迴流精餾。於 壓力100毫巴下,43-44。(:時蒸餾出349克主要含有水之起 始德出物’。接著添加3.0克(以重量計爲〇 ·丨〇/。)硼氫化鈉 於含有低於0 · 1 %水之蒸餾液相中,並繼續精餾。待起始餾 出物222克之TAD具有純度99.0 %,之後,可於壓力4〇毫巴 下’塔頂溫度9:TC時獲得主要餾出物,其含有2丨丨g克、純 度爲99.7 %以及水含量&lt;〇〗%之TAD,蒸餾產率2丨丨6克(82 %)。 於氮氣下黑暗中儲存兩天,所得之純TAD產物變爲黃色 (APHA顏色數値&gt;100)。 比較實例2 訂 4208克粗TAD組合物 85.6%三丙酮二胺(TAD) 9.0% 水 約0.7 %低沸點物質 4.7 %中及高沸點物質 經濟部中央標準局員工消費合作社印製 於100至4〇毫巴壓力下,經由2·4公尺Sulzer-CY充填之管柱 (約2 2理論層板,寬度4 3毫米),以5 :1之比例迴流精館。接 著在磨力1〇〇爱巴下及於43_44〇時,自起始館出物中分離 水,於壓力4〇毫巴下,塔頂溫度97-1 03°C時,得到主要館 出物,其含有TAD含量&gt;99.6 % (GC)之純TAD餾出物,蒸飽 產率:3022 克(84%)。 純餾出物(GC測出T AD含量99 ·7 % )儲存於無硼氫化鋼, 與儲存於添加硼氫化鈉中,如例1,並測定之,其結果如 -11 - 本纸張尺度適用中國國家標準(CNS ) Α4規格(2丨0X297公釐)TA 1 / J i τ * y ZX υ ζ J91959 Patent History No. 861〇74〇8 please revise the Chinese instruction manual ------- 丨 ---- V. Description of the invention (Please read the precautions of the back first , 43 耄 m), reflux distillation at a pressure of 100 mbar at a ratio of 5: 1. 43-44 at 100 mbar. (: 349 grams of the original German extract mainly containing water was distilled off at that time. Next, 3.0 grams (by weight 〇 · 丨 〇 /.) Of sodium borohydride was added in a distillation liquid phase containing less than 0.1% water. After the TAD of 222 g of the initial distillate has a purity of 99.0%, the main distillate can be obtained at a pressure of 40 mbar at the top temperature of the column 9: TC, which contains 2 丨 丨g of TAD with a purity of 99.7% and a water content of &lt; 〇%, a distillation yield of 2 丨 6 g (82%). Stored in nitrogen in the dark for two days, the resulting pure TAD product turned yellow (APHA Color number 値> 100). Comparative Example 2 Order 4208 g of crude TAD composition 85.6% triacetone diamine (TAD) 9.0% water 0.7% low boiling point substance 4.7% medium and high boiling point substance consumption by the Central Standards Bureau of the Ministry of Economic Affairs Cooperatives are printed at a pressure of 100 to 40 mbar through a 2.4-meter Sulzer-CY-filled column (approximately 22 theoretical laminates, with a width of 43 mm) and returned to the fine hall at a ratio of 5: 1. Then under the grinding force of 100 bar and at 43-44 o'clock, water was separated from the output of the starting hall, under the pressure of 40 mbar, the temperature of the top of the tower was 97-1 03 ° C. At that time, the main library output was obtained, which contained a pure TAD distillate with a TAD content &gt; 99.6% (GC). The steam-saturated yield: 3022 g (84%). Pure distillate (GC measured T AD content 99 · 7%) stored in borohydride-free steel, and stored in sodium borohydride, as in Example 1, and measured, the results are shown as -11-This paper size applies Chinese National Standard (CNS) Α4 specification (2 丨0X297 mm)

Sil.859 A7 -—-- B7 五、發明説明(9 ) ' 下表♦· |-- 顏色數値(未稀釋產物) :(根據DIN-ISO 6271) 儲存天數 未加NaBH4 • ——* 1OOOppm 1OOppm 1 238 207 225 3 297 16 61 4 ~ 1 289 12 35 5 2 87 -----— -—. -— 10 27 6 286 9 32 10 ----- 299 5 73 11 297 4 172 42 309 3 255 請 先。 閱 讀 背 ίτ 之 注 意 事 項 再 f 玎 即使添加大量還原劑(0 . 1。/。=丨0 0 0ppm )改善顏色移定度 ’但也會增加不希望的副產物之比率。 經濟部中央標準局員工消費合作社印製 尺 張 紙 本Sil.859 A7 ----- B7 V. Description of the invention (9) 'The following table ♦ · |-Color number 未 (undiluted product): (according to DIN-ISO 6271) Storage days without adding NaBH4 • —— * 1000 ppm 1OOppm 1 238 207 225 3 297 16 61 4 ~ 1 289 12 35 5 2 87 -----— -—. -— 10 27 6 286 9 32 10 ----- 299 5 73 11 297 4 172 42 309 3 255 please. After reading the note of ίτ, note that f 再 Even if a large amount of reducing agent (0.1./. = 丨 0 0 0 ppm) is added to improve the color shift degree, it will increase the ratio of undesired by-products. Printed by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs on paper

Ns C /IV一準 標一家 I國. 一國 |中 用 .itNs C / IV is a standard bid for a country I. A country | China.it

釐 公 7 9 · 2 XCm 7 9 2 x

Claims (1)

0^1^59 第86107408號專利申請案 中文申請專利範圍修正本⑽年12月) A8 B8 C8 D8 申請專利範圍 L 本 1:純化式I粗六氫P比0 ^ 1 ^ 59 Patent Application No. 86107408 Chinese Patent Application Range Amendment (December of the following year) A8 B8 C8 D8 Patent Application Range L this 1: Purified formula I crude hexahydrogen P ratio 經濟部中央標準局員工消費合作社印製 其R至R—爲Ci-C^-燒基,.或者ri 〃形成2至5個碳之、CH2_鏈―,其包含,第一步驟,經由蒸 館將一高一滞—點〜物質一以—及’若存在,水,自粗六氫吡啶中 一去除;第二步驟,添加爲第一步驟產物重量之0.0 1-5% 心逐原淨1 ;及,第三步驟,利用蒸餾分離六氫峨啶; 其中遝原劑爲式MXH4-mYm之化合物,其趾爲藍金屬, NR*,其中各個似系相同或不同之烷基,或j當量 t鹼土-金屬或1當量之鋅,χ爲硼或鋁,γ爲氫或CM, 及m爲0或1。 2.根據申請專利範園一第.4項之方法,其中rI,R2,汉3及尺4爲 α-α3·烷基—_。 3 .根據—申請.專利範圍第i項之方法,其中添加六氫1?比咬重 I &lt; 0.0 (H - 0.0 2 %的還原劑.於第三步驟中經蒸館分離之 六氫峨啶I中。 [與R2與/或R3與R4—起 (請先閲讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 0^1^59 第86107408號專利申請案 中文申請專利範圍修正本⑽年12月) A8 B8 C8 D8 申請專利範圍 L 本 1:純化式I粗六氫P比The Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs prints its R to R—Ci-C ^ -base, or riri to form a 2 to 5 carbon CH2 chain—which includes, the first step, by steaming The museum will remove one high and one lag-point ~ substance one-and 'if present, water is removed from the crude hexahydropyridine; in the second step, it is added as 0.0 1-5% of the weight of the product in the first step. 1; and, the third step, the separation of hexahydroeridine by distillation; wherein the rhenium agent is a compound of the formula MXH4-mYm, the toe of which is a blue metal, NR *, each of which may be the same or different alkyl group, or j Equivalent t alkaline earth-metal or 1 equivalent of zinc, χ is boron or aluminum, γ is hydrogen or CM, and m is 0 or 1. 2. The method according to item 4. of the patent application, in which rI, R2, Han 3 and Chi 4 are α-α3 · alkyl-. 3. According to—Application. The method of item i of the patent scope, in which hexahydro 1? Specific bite weight I &lt; 0.0 (H-0.0 2% of reducing agent) is added. In pyridine I. [From R2 and / or R3 and R4— (Please read the notes on the back before filling in this page) This paper size applies to China National Standard (CNS) A4 (210X297 mm) 0 ^ 1 ^ 59 No. 86107408 Patent Application Chinese Patent Application Range Amendment (December of the following year) A8 B8 C8 D8 Patent Application Range L Version 1: Purified Formula I crude hexahydrogen P ratio 經濟部中央標準局員工消費合作社印製 其R至R—爲Ci-C^-燒基,.或者ri 〃形成2至5個碳之、CH2_鏈―,其包含,第一步驟,經由蒸 館將一高一滞—點〜物質一以—及’若存在,水,自粗六氫吡啶中 一去除;第二步驟,添加爲第一步驟產物重量之0.0 1-5% 心逐原淨1 ;及,第三步驟,利用蒸餾分離六氫峨啶; 其中遝原劑爲式MXH4-mYm之化合物,其趾爲藍金屬, NR*,其中各個似系相同或不同之烷基,或j當量 t鹼土-金屬或1當量之鋅,χ爲硼或鋁,γ爲氫或CM, 及m爲0或1。 2.根據申請專利範園一第.4項之方法,其中rI,R2,汉3及尺4爲 α-α3·烷基—_。 3 .根據—申請.專利範圍第i項之方法,其中添加六氫1?比咬重 I &lt; 0.0 (H - 0.0 2 %的還原劑.於第三步驟中經蒸館分離之 六氫峨啶I中。 [與R2與/或R3與R4—起 (請先閲讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐)The Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs prints its R to R—Ci-C ^ -base, or riri to form a 2 to 5 carbon CH2 chain—which includes, the first step, by steaming The museum will remove one high and one lag-point ~ substance one-and 'if present, water is removed from the crude hexahydropyridine; in the second step, it is added as 0.0 1-5% of the weight of the product in the first step. 1; and, the third step, the separation of hexahydroeridine by distillation; wherein the rhenium agent is a compound of the formula MXH4-mYm, the toe of which is a blue metal, NR *, each of which may be the same or different alkyl group, or j Equivalent t alkaline earth-metal or 1 equivalent of zinc, χ is boron or aluminum, γ is hydrogen or CM, and m is 0 or 1. 2. The method according to item 4. of the patent application, in which rI, R2, Han 3 and Chi 4 are α-α3 · alkyl-. 3. According to—Application. The method of item i of the patent scope, in which hexahydro 1? Specific bite weight I &lt; 0.0 (H-0.0 2% of reducing agent) is added. In pyridine I. [From R2 and / or R3 and R4— (Please read the notes on the back before filling in this page) This paper size is applicable to China National Standard (CNS) A4 specification (210X297 mm)
TW86107408A 1997-05-30 1997-05-30 Purification of sterically hindered 4-aminopiperidines TW391959B (en)

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