首页> 外国专利> Preparation of 2-ethyl-3-methyl-1,4-diazine, useful as aroma, e.g. in food, involves reacting pentan-2,3-dione and ethan-1,2-diamine in aliphatic diol or triol containing alkaline salt, and catalytic dehydrogenation

Preparation of 2-ethyl-3-methyl-1,4-diazine, useful as aroma, e.g. in food, involves reacting pentan-2,3-dione and ethan-1,2-diamine in aliphatic diol or triol containing alkaline salt, and catalytic dehydrogenation

机译:用作香气的2-乙基-3-甲基-1,4-二嗪的制备,例如在食品中,涉及使戊二酮2,3-二酮和乙二胺1,2-二胺在含有碱性盐的脂肪族二醇或三醇中反应,并进行催化脱氢

摘要

In the preparation of 2-ethyl-3-methyl-1,4-diazine (I) by reacting pentan-2,3-dione and ethan-1,2-diamine in organic solvent (III) and catalytic dehydrogenation, (III) is a 3-5C aliphatic diol or triol containing an alkaline salt. The reaction mixture can be dripped directly into a solution of alkali hydroxide and (supported) sub-group 8 catalyst in (III) at 70-180 deg C. The product is separated by steam distillation. Preparation of 2-ethyl-3-methyl-1,4-diazine (I) involves (1) reacting pentan-2,3-dione (II) and ethan-1,2-diamine in (0.1-2):1 molar ratio in an organic solvent (III) at -30 to 60 deg C and (2) catalytic dehydrogenation of the resultant dihydropyrazine. The novel features are that (a) (III) is a 3-5 carbon (C) aliphatic diol or triol containing 0.001-5 wt.% alkaline salt with respect to (II); (b) the reaction mixture can be dripped directly into a solution of alkali hydroxide (IV) and a (supported) catalytic sub-group 8 element in (III) at 70-180 deg C; (c) the amount of (IV) is 0.2-3 molar equivalents with respect to (II) and the amount of catalyst 0.001-0.5 wt.% with respect to the amount of reaction mixture in stage (1); and (d) the product is separated by steam distillation.
机译:在有机溶剂(III)中使戊烷2,3-二酮和乙1,2-二胺反应并催化脱氢制备2-乙基-3-甲基-1,4-二嗪(I)是含有碱性盐的3-5C脂族二醇或三醇。可将反应混合物在70-180℃下直接滴入碱金属氢氧化物和(负载的)第8族第(III)催化剂的溶液中,温度为70-180℃。通过蒸汽蒸馏分离产物。 2-乙基-3-甲基-1,4-二嗪的制备(I)涉及(1)在(0.1-2):1摩尔的条件下使戊烷2,3-二酮(II)和乙烷1,2-二胺反应在-30℃至60℃下在有机溶剂(III)中的比例为(2)和所得二氢吡嗪的催化脱氢。新颖的特征是:(a)(III)是相对于(II)含有0.001-5重量%碱性盐的3-5碳(C)脂族二醇或三醇; (b)可将反应混合物在70-180℃下直接滴入碱金属氢氧化物(IV)和(III)中(负载的)催化第8族催化元素的溶液中; (c)(IV)的量相对于(II)为0.2-3摩尔当量,催化剂的量相对于步骤(1)中反应混合物的量为0.001-0.5wt。%; (d)通过蒸汽蒸馏分离产物。

著录项

  • 公开/公告号DE10022361C1

    专利类型

  • 公开/公告日2001-05-23

    原文格式PDF

  • 申请/专利权人 HAARMANN & REIMER GMBH;

    申请/专利号DE20001022361

  • 发明设计人 LAMBRECHT STEFAN;

    申请日2000-05-08

  • 分类号C07D241/12;

  • 国家 DE

  • 入库时间 2022-08-22 01:09:48

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