WO2022257519A1 - Process for preparing hydroxytyrosol - Google Patents

Process for preparing hydroxytyrosol Download PDF

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WO2022257519A1
WO2022257519A1 PCT/CN2022/080320 CN2022080320W WO2022257519A1 WO 2022257519 A1 WO2022257519 A1 WO 2022257519A1 CN 2022080320 W CN2022080320 W CN 2022080320W WO 2022257519 A1 WO2022257519 A1 WO 2022257519A1
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acid
catalyst
hydroxytyrosol
preparing
reaction
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PCT/CN2022/080320
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French (fr)
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刘小红
王凡
王康
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南京斯贝源医药科技有限公司
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C37/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring
    • C07C37/01Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring by replacing functional groups bound to a six-membered aromatic ring by hydroxy groups, e.g. by hydrolysis
    • C07C37/055Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring by replacing functional groups bound to a six-membered aromatic ring by hydroxy groups, e.g. by hydrolysis the substituted group being bound to oxygen, e.g. ether group
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D317/00Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms
    • C07D317/08Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms having the hetero atoms in positions 1 and 3
    • C07D317/44Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms having the hetero atoms in positions 1 and 3 ortho- or peri-condensed with carbocyclic rings or ring systems
    • C07D317/46Heterocyclic compounds containing five-membered rings having two oxygen atoms as the only ring hetero atoms having the hetero atoms in positions 1 and 3 ortho- or peri-condensed with carbocyclic rings or ring systems condensed with one six-membered ring
    • C07D317/48Methylenedioxybenzenes or hydrogenated methylenedioxybenzenes, unsubstituted on the hetero ring
    • C07D317/50Methylenedioxybenzenes or hydrogenated methylenedioxybenzenes, unsubstituted on the hetero ring with only hydrogen atoms, hydrocarbon or substituted hydrocarbon radicals, directly attached to atoms of the carbocyclic ring
    • C07D317/54Radicals substituted by oxygen atoms

Definitions

  • the invention belongs to the field of organic synthesis, and in particular relates to a process for preparing hydroxytyrosol.
  • Hydroxytyrosol is a natural polyphenol compound with strong antioxidant activity, mainly in the form of esters in olive fruits and leaves.
  • Hydroxytyrosol has a variety of biological and pharmacological activities, the main functions are: (1) prevent cancer, promote late cancer recovery and improve the effect of chemotherapy; (2) prevent and treat cardiovascular and cerebrovascular diseases, the effect is better than similar drugs; (3) Improve the function of the endocrine system, promote metabolism, and promote wound healing; (4) Eliminate free radicals in the body, prevent brain failure, and delay aging; (5) Enhance skin elasticity and moisture, wrinkle and anti-aging.
  • the details are as follows.
  • A the synthesis technique of hydroxytyrosol
  • This route uses eugenol as the starting material to prepare hydroxytyrosol.
  • the reaction process needs to be carried out at -78°C, the reaction conditions are harsh, and the reaction process also requires reagents such as sodium borohydride with a high price.
  • This route uses methyl 3,4-dihydroxyphenylacetate as the starting material, and the starting material is expensive, while using relatively expensive reagents such as sodium borohydride, and the process cost is relatively high.
  • the specific route is as follows:
  • This route uses 3,4-dimethoxyphenylacetic acid as the starting material, and the starting material is expensive, and simultaneously uses relatively expensive reagents such as dibutyl aluminum hydride, and the process cost is relatively high.
  • the route uses 3,4-dimethoxyphenylacetic acid as the starting material to prepare hydroxytyrosol through esterification, reduction, and demethylation reactions.
  • Genotoxic reagents such as methyl sulfate and boron trifluoride are used in the reaction process. and other highly toxic reagents.
  • the price of starting materials is high, reagents such as aluminum triiodide and sodium borohydride are expensive, and the overall process cost is relatively high.
  • the applicant has searched and sorted out the synthetic method of the key intermediate piperonyl alcohol of hydroxytyrosol, which mainly contains the following: route 1, the method [5-7] for preparing piperonyl alcohol by bromopipercycline; route 2, by safrole Method for preparing pepper ethanol [8-10] ; route 3, method for preparing pepper ethanol from pepper acetic acid [11-13] .
  • route 1 the method [5-7] for preparing piperonyl alcohol by bromopipercycline
  • route 2 by safrole Method for preparing pepper ethanol [8-10]
  • route 3 method for preparing pepper ethanol from pepper acetic acid [11-13] .
  • the specific content is as follows:
  • route 1 metal magnesium is used in the reaction process, the cost is high, anhydrous and oxygen-free conditions are required, and the operating conditions are harsh.
  • the raw material of safrole in route 2 is expensive, requires -78°C, and the reaction conditions are harsh.
  • route 3 reagents and raw materials with higher prices such as lithium hydride and pepper alcohol are used.
  • route 1 uses boron tribromide, which is a highly toxic reagent and has a high price.
  • Use expensive metal sodium in route 2 and the high temperature of 170 °C is needed in the reaction process.
  • the present invention proposes a process for preparing hydroxytyrosol, the process is mainly divided into two steps, in step 1, the Friedel-Crafts alkylation reaction of piperonyl ring and ethylene oxide directly prepares piperonyl alcohol, The process route is short, the raw materials are easy to obtain, ethylene oxide belongs to a large chemical product, the cost is low, and the yield is high; in step 2, pepper ethanol is hydrolyzed under the action of a solid acid catalyst to prepare hydroxytyrosol, and the purity is higher than 98%. To avoid highly toxic reagents, and to complete at close to room temperature.
  • the process for preparing hydroxytyrosol in the present invention combines two-step reactions, and has the characteristics of low cost, mild reaction conditions, simple aftertreatment, safety and environmental protection, and the like.
  • reaction route is as follows:
  • a kind of technique for preparing hydroxytyrosol of the present invention comprises the following steps:
  • Step 1 the preparation of 5-hydroxymethylbenzo-1,3-dioxolane (piperethanol): add piperonyl, catalyst, and then add ethylene oxide to react in the reaction flask, and the reaction temperature is -20 ⁇ 10°C, the reaction time is 0.5-1h, quenched after the reaction is completed, pickled, washed with water, concentrated and distilled to obtain peppery alcohol;
  • Step 2 the preparation of 3,4-dihydroxyphenylethanol (hydroxytyrosol): add protonic acid, the pepper alcohol obtained in step 1, a catalyst, and react at 20-60°C under nitrogen protection for 5-36h in the reaction flask, adjust The pH was adjusted to 10, washed with DCM, the pH of the aqueous layer was adjusted to 1-2, extracted with methyl tert-butyl ether, dried, decolorized, and concentrated to obtain hydroxytyrosol.
  • the catalyst is a Lewis acid
  • the Lewis acid is selected from one of AlBr 3 , AlCl 3 , FeCl 3 , SbCl 5 , SnCl 4 , BF 3 , TiCl 4 , and ZnCl 2 A combination of one or more; preferably AlCl 3 , FeCl 3 , more preferably AlCl 3 .
  • the reaction conditions are mild.
  • the reaction temperature is -15°C to -5°C, preferably -10°C to -5°C.
  • the molar ratio of piperonyl ring to catalyst is 5-10:1, preferably 5-8:1, more preferably 8:1;
  • the mol ratio of the catalyst to ethylene oxide was 1:1-5, preferably Preferably it is 1:3-3.5; when the feed ratio of ethylene oxide to catalyst is less than 3.0, the yield will decrease obviously, and when the feed (molar) ratio is 3.0-3.5, the yield will be relatively high.
  • the molar ratio of piperonyl ring, catalyst, and ethylene oxide is 5-10:1:1-5, more preferably 8:1:3-3.5.
  • ethylene oxide is added by slowly feeding ethylene oxide gas under rapid stirring.
  • the quenching reagent is 2M HCl.
  • the protonic acid is selected from any one or more of hydrofluoric acid, hydrochloric acid, hydrobromic acid, hydroiodic acid, sulfuric acid, phosphoric acid, and nitric acid.
  • the protonic acid is hydrochloric acid.
  • the catalyst is a solid strong acid or a solid superacid, selected from HND-32 solid superacid catalyst, HND-34 solid superacid catalyst, Amberlyst15 solid strong acid catalyst, HNF-5W perfluorosulfonic acid resin , NKC-9 catalytic resin any one or more.
  • the combination of protonic acid and catalyst is hydrochloric acid/Amberlyst15 solid strong acid catalyst, hydrochloric acid/HND-32 solid super acid catalyst.
  • the mass ratio of pepper to ethanol to catalyst 1: 0.001-0.02, preferably 0.002-0.01.
  • the mass ratio of pepper to ethanol and the catalyst is 1:0.01.
  • HND-32 solid superacid when used as catalyst, the mass ratio of pepper alcohol and HND-32 solid superacid catalyst is 1:0.002.
  • the reaction temperature is 20-60°C, preferably 20-30°C.
  • the invention provides a process for preparing hydroxytyrosol.
  • piperonyl cyclocycline is used as a starting material, and ethylene oxide is reacted with Friedel-Crafts alkylation to prepare pepper ethanol, and the pepper ethanol is hydrolyzed to prepare hydroxy tyrosol.
  • the process has the characteristics of low cost and high yield:
  • step 1 of the present invention reaction type, reaction substrate, catalyst are studied, and the yield of intermediate pepper ethanol is promoted to 60-70% by about 20%, and simultaneously this process raw material is easy to get, cheap, The cost is lower, and the operation process is simple, safe and environmentally friendly;
  • step 2 of the present invention the combination of protonic acid and fixed strong acid/solid superacid is used to prepare hydroxytyrosol with a purity of more than 98% and a yield of more than 85%;
  • Fig. 1 is the 1 H-NMR of hydroxytyrosol obtained in Example 8 of the present invention.
  • Embodiment 1 the preparation of 5-hydroxymethylbenzo-1,3-dioxolane (piperethanol)
  • Embodiment 2 Preparation of 5-hydroxymethylbenzo-1,3-dioxolane (piperethanol)
  • Embodiment 3 Preparation of 5-hydroxymethylbenzo-1,3-dioxolane (piperethanol)
  • Embodiment 4 Preparation of 5-hydroxymethylbenzo-1,3-dioxolane (piperethanol)
  • Embodiment 5 Preparation of 5-hydroxymethylbenzo-1,3-dioxolane (piperethanol)
  • Embodiment 6 Preparation of 5-hydroxymethylbenzo-1,3-dioxolane (piperethanol)
  • Embodiment 7 Preparation of 5-hydroxymethylbenzo-1,3-dioxolane (piperethanol)
  • Example 1 Using the feed ratio and operation of Example 1, when the Lewis acid is selected as BF 3 and ZnCl 2 , there is no product; when TiCl 4 is selected, the yield is 4.1%.
  • Adjusting the feed ratio of ethylene oxide and catalyst can find that the yield when feed ratio is 3.5 is significantly better than that of 3.0; choosing different catalysts also has a great influence on the yield of pepper ethanol, and aluminum trichloride is better than trichloride Iron, superior to other Lewis acids.
  • Embodiment 8 Preparation of 3,4-dihydroxyphenylethanol (hydroxytyrosol)
  • Embodiment 9 Preparation of 3,4-dihydroxyphenethyl alcohol (hydroxytyrosol)
  • reaction solution was adjusted to pH 10 with 3ml NaOH solution in an ice-water bath, washed twice with 180ml DCM, the aqueous layer was adjusted to pH 1-2 with 3M HCl solution, extracted 5 times with 350ml methyl tert-butyl ether, and combined with methyl tert-butyl ether , dried over anhydrous sodium sulfate, decolorized with 5% activated carbon, concentrated by rotary evaporation to obtain an orange-yellow oil, and dried in vacuo to obtain 11.9 g. Yield 25.6%, HPLC purity: 98.686%.

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  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)

Abstract

Disclosed in the present invention is a process for preparing hydroxytyrosol. According to the process, 1,3-benzodioxole as a starting material is firstly subjected to a Friedel-Crafts alkylation reaction together with ethylene oxide to prepare piperonyl alcohol, and the piperonyl alcohol is then subjected to a catalytic hydrolysis reaction to prepare hydroxytyrosol. The process for preparing hydroxytyrosol disclosed in the present invention has the characteristics of easily-available and low-price raw materials, a simple operation process, safety, environmental protection, etc.

Description

一种制备羟基酪醇的工艺A kind of technique for preparing hydroxytyrosol 技术领域technical field
本发明属于有机合成领域,具体涉及一种制备羟基酪醇的工艺。The invention belongs to the field of organic synthesis, and in particular relates to a process for preparing hydroxytyrosol.
背景技术Background technique
羟基酪醇是一种天然多酚类化合物,具有很强的抗氧化活性,主要以酯类的形式存在于橄榄的果实和枝叶中。Hydroxytyrosol is a natural polyphenol compound with strong antioxidant activity, mainly in the form of esters in olive fruits and leaves.
羟基酪醇具有多种生物和药理活性,主要作用有:(1)预防癌症,促进癌症后期恢复和提高化疗效果;(2)预防与治疗心脑血管疾病,效果优于同类药品;(3)提高内分泌系统功能,促进新陈代谢,促进伤口愈合;(4)消除体内自由基,防止脑衰,延缓衰老;(5)增强皮肤弹性和润泽,除皱抗衰老。Hydroxytyrosol has a variety of biological and pharmacological activities, the main functions are: (1) prevent cancer, promote late cancer recovery and improve the effect of chemotherapy; (2) prevent and treat cardiovascular and cerebrovascular diseases, the effect is better than similar drugs; (3) Improve the function of the endocrine system, promote metabolism, and promote wound healing; (4) Eliminate free radicals in the body, prevent brain failure, and delay aging; (5) Enhance skin elasticity and moisture, wrinkle and anti-aging.
资料调研显示,国内橄榄种植面积较小,2018年全国橄榄油产量4.5万吨,仅占全球总产量的1.5%,依靠提取获得羟基酪醇成本较高,产量较小。国内羟基酪醇的主要来源于化学合成,研究以化学合成法制备羟基酪醇具有现实意义。Data research shows that domestic olive planting area is relatively small. In 2018, the national olive oil output was 45,000 tons, accounting for only 1.5% of the global total output. The cost of obtaining hydroxytyrosol by extraction is relatively high, and the output is relatively small. The main source of hydroxytyrosol in China is chemical synthesis, and it is of practical significance to study the preparation of hydroxytyrosol by chemical synthesis.
申请人调研了羟基酪醇合成的工艺资料(A),关键中间体胡椒乙醇合成的工艺资料(B)以及由胡椒乙醇制备羟基酪醇的工艺资料(C),具体介绍如下。A、羟基酪醇的合成工艺The applicant investigated the process data (A) for the synthesis of hydroxytyrosol, the process data (B) for the synthesis of the key intermediate pepper ethanol, and the process data (C) for the preparation of hydroxytyrosol from pepper ethanol. The details are as follows. A, the synthesis technique of hydroxytyrosol
申请人调研了羟基酪醇的主要合成工艺,主要有四种,分别收录于CN103038203B [1]、CN103420804B [2]、CN104030894B [3]、CN106866384B [4]详细内容如下: The applicant investigated the main synthesis processes of hydroxytyrosol. There are mainly four types, which are respectively included in CN103038203B [1] , CN103420804B [2] , CN104030894B [3] , and CN106866384B [4]. The details are as follows:
广东南沙龙沙有限公司 [1]于2010年提出了一种以丁子香酚制备羟基酪醇的工艺,具体内容如下: Guangdong Nansha Lonza Co., Ltd. [1] proposed a process for preparing hydroxytyrosol with eugenol in 2010. The details are as follows:
Figure PCTCN2022080320-appb-000001
Figure PCTCN2022080320-appb-000001
该路线以丁子香酚为起始原料制备羟基酪醇,反应过程需要在-78℃进行,反应条件苛刻,同时反应过程还需要价格较高的硼氢化钠等试剂。This route uses eugenol as the starting material to prepare hydroxytyrosol. The reaction process needs to be carried out at -78°C, the reaction conditions are harsh, and the reaction process also requires reagents such as sodium borohydride with a high price.
凌霄 [2]等人于2013年公布了一种以3,4-二羟基苯乙酸甲酯为原料制备羟基酪醇的工艺,具体路线如下: Ling Xiao [2] and others announced a process for preparing hydroxytyrosol from 3,4-dihydroxyphenylacetic acid methyl ester in 2013. The specific route is as follows:
Figure PCTCN2022080320-appb-000002
Figure PCTCN2022080320-appb-000002
该路线以3,4-二羟基苯乙酸甲酯为起始物料,起始物料价格昂贵同时使用了硼氢化钠等价格较高的试剂,工艺成本较高。This route uses methyl 3,4-dihydroxyphenylacetate as the starting material, and the starting material is expensive, while using relatively expensive reagents such as sodium borohydride, and the process cost is relatively high.
德国瓦克化学股份公司 [3]于2014年公布了3,4-二甲氧基苯乙酸甲酯为原料制备羟基酪醇的工艺,具体路线如下: Wacker Chemie AG [3] announced in 2014 a process for preparing hydroxytyrosol from methyl 3,4-dimethoxyphenylacetate. The specific route is as follows:
Figure PCTCN2022080320-appb-000003
Figure PCTCN2022080320-appb-000003
该路线以3,4-二甲氧基苯乙酸为起始物料,起始物料价格昂贵同时使用了二丁基氢化铝等价格较高的试剂,工艺成本较高。This route uses 3,4-dimethoxyphenylacetic acid as the starting material, and the starting material is expensive, and simultaneously uses relatively expensive reagents such as dibutyl aluminum hydride, and the process cost is relatively high.
陕西嘉禾药业有限公司 [4]于2016年公布了一种由3,4-二甲氧基苯乙酸制备制备羟基酪醇的工艺,具体路线如下: Shaanxi Jiahe Pharmaceutical Co., Ltd. [4] announced a process for preparing hydroxytyrosol from 3,4-dimethoxyphenylacetic acid in 2016. The specific route is as follows:
Figure PCTCN2022080320-appb-000004
Figure PCTCN2022080320-appb-000004
该路线以3,4-二甲氧基苯乙酸为起始物料,经酯化,还原,脱甲基反应制备羟基酪醇,反应过程中使用了硫酸甲酯等基因毒性试剂,三氟化硼等剧毒试剂。起始物料价格较高,三碘化铝、硼氢化钠等试剂价格昂贵,整体工艺成本较高。B、关键中间体胡椒乙醇制备工艺The route uses 3,4-dimethoxyphenylacetic acid as the starting material to prepare hydroxytyrosol through esterification, reduction, and demethylation reactions. Genotoxic reagents such as methyl sulfate and boron trifluoride are used in the reaction process. and other highly toxic reagents. The price of starting materials is high, reagents such as aluminum triiodide and sodium borohydride are expensive, and the overall process cost is relatively high. B. Preparation process of key intermediate pepper ethanol
申请人就羟基酪醇的关键中间体胡椒乙醇的合成方法进行了检索整理,主要有以下几种:路线1、由溴代胡椒环制备胡椒乙醇的方法 [5-7];路线2、由黄樟素制备胡椒乙醇的方法 [8-10];路线3、胡椒乙酸制备胡椒乙醇的方法 [11-13]。具体内容如下: The applicant has searched and sorted out the synthetic method of the key intermediate piperonyl alcohol of hydroxytyrosol, which mainly contains the following: route 1, the method [5-7] for preparing piperonyl alcohol by bromopipercycline; route 2, by safrole Method for preparing pepper ethanol [8-10] ; route 3, method for preparing pepper ethanol from pepper acetic acid [11-13] . The specific content is as follows:
Figure PCTCN2022080320-appb-000005
Figure PCTCN2022080320-appb-000005
路线1中反应过程使用了金属镁,成本较高,需要无水无氧条件,操作条件苛刻。路线2中黄樟素原料价格昂贵,需要-78℃,反应条件苛刻。路线3中使用氢化锂、胡椒乙醇等价格较高的试剂与原料。In route 1, metal magnesium is used in the reaction process, the cost is high, anhydrous and oxygen-free conditions are required, and the operating conditions are harsh. The raw material of safrole in route 2 is expensive, requires -78°C, and the reaction conditions are harsh. In route 3, reagents and raw materials with higher prices such as lithium hydride and pepper alcohol are used.
C、由胡椒乙醇制备羟基酪醇工艺C, the preparation process of hydroxytyrosol by pepper ethanol
申请人就胡椒乙醇水解制备羟基酪醇的合成工艺进行了检索整理主要有以下几种:路线1、三溴化硼法 [14,15];路线2、金属钠法 [16]The applicant searched and sorted out the synthetic process of preparing hydroxytyrosol by the hydrolysis of pepper ethanol. There are mainly the following types: route 1, boron tribromide method [14,15] ; route 2, metal sodium method [16] .
Figure PCTCN2022080320-appb-000006
Figure PCTCN2022080320-appb-000006
文献报道胡椒乙醇水解制备羟基酪醇的工艺中,路线1采用了三溴化硼,三溴化硼属于剧毒试剂,价格较高。路线2中使用价格昂贵的金属钠,反应过程需要170℃的高温。It is reported in the literature that in the process of preparing hydroxytyrosol by ethanol hydrolysis of pepper, route 1 uses boron tribromide, which is a highly toxic reagent and has a high price. Use expensive metal sodium in route 2, and the high temperature of 170 ℃ is needed in the reaction process.
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发明内容Contents of the invention
针对以上合成工艺中的诸多问题,本发明提出了一种制备羟基酪醇的工艺,该工艺主要分为两步,步骤1中胡椒环与环氧乙烷发生傅克烷基化反应直接制备胡椒乙醇,工艺路线短,原料易得,环氧乙烷属于大化工产品,成本低,收率高;步骤2中胡椒乙醇在固体酸催化剂作用下,水解制备羟基酪醇,纯度高于98%,该步骤中避免了剧毒试剂,且在接近室温的条件下完成。本发明制备羟基酪醇的工艺,综合两步反应,具有成本低,反应条件温和,后处理简单,安全环保等特点。Aiming at many problems in the above synthesis process, the present invention proposes a process for preparing hydroxytyrosol, the process is mainly divided into two steps, in step 1, the Friedel-Crafts alkylation reaction of piperonyl ring and ethylene oxide directly prepares piperonyl alcohol, The process route is short, the raw materials are easy to obtain, ethylene oxide belongs to a large chemical product, the cost is low, and the yield is high; in step 2, pepper ethanol is hydrolyzed under the action of a solid acid catalyst to prepare hydroxytyrosol, and the purity is higher than 98%. To avoid highly toxic reagents, and to complete at close to room temperature. The process for preparing hydroxytyrosol in the present invention combines two-step reactions, and has the characteristics of low cost, mild reaction conditions, simple aftertreatment, safety and environmental protection, and the like.
本发明解决其技术问题采用的技术方案是:The technical scheme that the present invention solves its technical problem adopts is:
本发明的一种制备羟基酪醇的工艺,反应路线如下:A kind of technique of preparing hydroxytyrosol of the present invention, reaction route is as follows:
Figure PCTCN2022080320-appb-000007
Figure PCTCN2022080320-appb-000007
具体的,本发明一种制备羟基酪醇的工艺,包括如下步骤:Concretely, a kind of technique for preparing hydroxytyrosol of the present invention comprises the following steps:
步骤1,5-羟甲基苯并-1,3-二恶环戊烷(胡椒乙醇)的制备:向反应瓶中加入胡椒环,催化剂,再加入环氧乙烷反应,反应温度为-20~10℃,反应时间0.5-1h,反应结束后猝灭,经酸洗,水洗,浓缩,蒸馏,得到胡椒乙醇; Step 1, the preparation of 5-hydroxymethylbenzo-1,3-dioxolane (piperethanol): add piperonyl, catalyst, and then add ethylene oxide to react in the reaction flask, and the reaction temperature is -20 ~10°C, the reaction time is 0.5-1h, quenched after the reaction is completed, pickled, washed with water, concentrated and distilled to obtain peppery alcohol;
步骤2,3,4-二羟基苯乙醇(羟基酪醇)的制备:向反应瓶中加入质子酸、步骤1所得的胡椒乙醇、催化剂、氮气保护下20~60℃,反应5-36h,调节pH至10,DCM洗涤,水层调节pH至1-2,甲基叔丁基醚萃取,干燥,脱色,浓缩得羟基酪醇。 Step 2, the preparation of 3,4-dihydroxyphenylethanol (hydroxytyrosol): add protonic acid, the pepper alcohol obtained in step 1, a catalyst, and react at 20-60°C under nitrogen protection for 5-36h in the reaction flask, adjust The pH was adjusted to 10, washed with DCM, the pH of the aqueous layer was adjusted to 1-2, extracted with methyl tert-butyl ether, dried, decolorized, and concentrated to obtain hydroxytyrosol.
作为本申请的优选技术方案,所述步骤1中,催化剂为路易斯酸,所述路易斯酸选自AlBr 3、AlCl 3、FeCl 3、SbCl 5、SnCl 4,BF 3、TiCl 4、ZnCl 2中一种或多种的组合;优选为AlCl 3、FeCl 3,更优选为AlCl 3。采用卤化物作为催化剂,反应条件温和。 As a preferred technical solution of the present application, in the step 1, the catalyst is a Lewis acid, and the Lewis acid is selected from one of AlBr 3 , AlCl 3 , FeCl 3 , SbCl 5 , SnCl 4 , BF 3 , TiCl 4 , and ZnCl 2 A combination of one or more; preferably AlCl 3 , FeCl 3 , more preferably AlCl 3 . Using halides as catalysts, the reaction conditions are mild.
作为本申请的优选技术方案,所述步骤1中,反应温度为-15℃~-5℃,优选为-10℃~-5℃。As a preferred technical solution of the present application, in the step 1, the reaction temperature is -15°C to -5°C, preferably -10°C to -5°C.
作为本申请的优选技术方案,所述步骤1中,胡椒环与催化剂的摩尔比为5-10:1,优选为5-8:1,更优选为8:1;胡椒环既作为反应试剂又作为反应溶 剂,当胡椒环与催化剂投料(摩尔)比小于5时,反应过程中反应液变得粘稠不利于搅拌;所述催化剂与环氧乙烷的摩尔比为1:1-5,更优选为1:3-3.5;当环氧乙烷与催化剂投料比小于3.0时,收率明显降低,投料(摩尔)比3.0~3.5时,收率相对较高。As a preferred technical solution of the present application, in the step 1, the molar ratio of piperonyl ring to catalyst is 5-10:1, preferably 5-8:1, more preferably 8:1; As a reaction solvent, when the piperonyl ring and the catalyst feed (mol) ratio were less than 5, the reaction solution became viscous and unfavorable for stirring during the reaction; the mol ratio of the catalyst to ethylene oxide was 1:1-5, preferably Preferably it is 1:3-3.5; when the feed ratio of ethylene oxide to catalyst is less than 3.0, the yield will decrease obviously, and when the feed (molar) ratio is 3.0-3.5, the yield will be relatively high.
作为本申请的优选技术方案,所述步骤1中,胡椒环、催化剂、环氧乙烷的摩尔比为5-10:1:1-5,更优选为8:1:3-3.5。As a preferred technical solution of the present application, in the step 1, the molar ratio of piperonyl ring, catalyst, and ethylene oxide is 5-10:1:1-5, more preferably 8:1:3-3.5.
作为本申请的优选技术方案,所述步骤1中,环氧乙烷通过在快速搅拌下缓慢通入环氧乙烷气体的方式加入。As a preferred technical solution of the present application, in the step 1, ethylene oxide is added by slowly feeding ethylene oxide gas under rapid stirring.
作为本申请的优选技术方案,所述步骤1中,猝灭试剂为2M HCl。As the preferred technical scheme of the present application, in the step 1, the quenching reagent is 2M HCl.
作为本申请的优选技术方案,所述步骤2中,质子酸选自氢氟酸、盐酸、氢溴酸、氢碘酸、硫酸、磷酸、硝酸中的任一种或多种。As a preferred technical solution of the present application, in the step 2, the protonic acid is selected from any one or more of hydrofluoric acid, hydrochloric acid, hydrobromic acid, hydroiodic acid, sulfuric acid, phosphoric acid, and nitric acid.
优选的,所述质子酸为盐酸。Preferably, the protonic acid is hydrochloric acid.
作为本申请的优选技术方案,所述催化剂为固体强酸或固体超强酸,选自HND-32固体超强酸催化剂、HND-34固体超强酸催化剂、Amberlyst15固体强酸催化剂、HNF-5W全氟磺酸树脂、NKC-9催化树脂任一种或多种。As a preferred technical solution of the present application, the catalyst is a solid strong acid or a solid superacid, selected from HND-32 solid superacid catalyst, HND-34 solid superacid catalyst, Amberlyst15 solid strong acid catalyst, HNF-5W perfluorosulfonic acid resin , NKC-9 catalytic resin any one or more.
优选的,质子酸与催化剂的组合为盐酸/Amberlyst15固体强酸催化剂、盐酸/HND-32固体超强酸催化剂。Preferably, the combination of protonic acid and catalyst is hydrochloric acid/Amberlyst15 solid strong acid catalyst, hydrochloric acid/HND-32 solid super acid catalyst.
作为本申请的优选技术方案,所述步骤2中,胡椒乙醇、催化剂质量比=1:0.001-0.02,优选为0.002-0.01。As a preferred technical solution of the present application, in the step 2, the mass ratio of pepper to ethanol to catalyst = 1: 0.001-0.02, preferably 0.002-0.01.
其中,当以Amberlyst15固体强酸催化剂为催化剂时,胡椒乙醇、催化剂质量比为1:0.01。Among them, when the Amberlyst15 solid strong acid catalyst is used as the catalyst, the mass ratio of pepper to ethanol and the catalyst is 1:0.01.
其中,当以HND-32固体超强酸为催化剂时,胡椒乙醇、HND-32固体超强酸催化剂质量比为1:0.002。Among them, when HND-32 solid superacid is used as catalyst, the mass ratio of pepper alcohol and HND-32 solid superacid catalyst is 1:0.002.
作为本申请的优选技术方案,所述步骤2中,所述反应温度为20-60℃,优选20-30℃。As a preferred technical solution of the present application, in the step 2, the reaction temperature is 20-60°C, preferably 20-30°C.
有益效果Beneficial effect
本发明提供的一种制备羟基酪醇的工艺,该工艺以胡椒环为起始物料,与环氧乙烷经傅克烷基化反应制备胡椒乙醇,胡椒乙醇经水解制备羟基酪醇。该工艺具有成本低,收率高等特点:The invention provides a process for preparing hydroxytyrosol. In the process, piperonyl cyclocycline is used as a starting material, and ethylene oxide is reacted with Friedel-Crafts alkylation to prepare pepper ethanol, and the pepper ethanol is hydrolyzed to prepare hydroxy tyrosol. The process has the characteristics of low cost and high yield:
(1)本发明步骤1中,对反应类型、反应底物、催化剂进行研究,将中间体胡椒乙醇的收率由20%左右提升至60-70%,同时该工艺原料易得、价格低廉,成本更低,且操作过程简单,安全环保;(1) In step 1 of the present invention, reaction type, reaction substrate, catalyst are studied, and the yield of intermediate pepper ethanol is promoted to 60-70% by about 20%, and simultaneously this process raw material is easy to get, cheap, The cost is lower, and the operation process is simple, safe and environmentally friendly;
(2)本发明步骤2中,将质子酸和固定强酸/固体超强酸组合使用,制备羟基酪醇,纯度在98%以上,收率在85%以上;(2) In step 2 of the present invention, the combination of protonic acid and fixed strong acid/solid superacid is used to prepare hydroxytyrosol with a purity of more than 98% and a yield of more than 85%;
(3)避免使用溴化硼等剧毒试剂,成本低,反应条件温和且更加安全环保。(3) Avoid using highly toxic reagents such as boron bromide, low cost, mild reaction conditions and safer and more environmentally friendly.
附图说明Description of drawings
图1是本发明实施例8所得羟基酪醇的 1H-NMR。 Fig. 1 is the 1 H-NMR of hydroxytyrosol obtained in Example 8 of the present invention.
具体实施方式Detailed ways
以下结合数个较佳实施案例对本发明技术方案坐进一步非限制性的说明。所用试剂或者仪器设备未注明生产厂商的,均视为可以通过市场购买的常规产品。The technical solution of the present invention will be further described in a non-limiting manner in conjunction with several preferred implementation examples below. The reagents or instruments used are not indicated by the manufacturer, and they are all regarded as conventional products that can be purchased through the market.
实施例1:5-羟甲基苯并-1,3-二恶环戊烷(胡椒乙醇)的制备Embodiment 1: the preparation of 5-hydroxymethylbenzo-1,3-dioxolane (piperethanol)
室温下,向四颈瓶中加入880.5g(7.21mol,8eq)胡椒环,120.0g(0.901mol,1.0eq)三氯化铝,降温至-10℃至-5℃。以气体形式通入139.0g(3.155mol,3.5eq)环氧乙烷,加入完毕继续反应1h。反应液加入1L二氯甲烷,1.5L 2M盐酸溶液室温搅拌30min,分液,DCM有机层分别以1M盐酸溶液洗涤2次,水洗3次,无水硫酸钠干燥,过滤。滤液减压蒸馏收胡椒环,收集115-120℃馏分,得胡椒乙醇:102.0g,收率:68.1%,HPLC纯度:98.305%。At room temperature, 880.5g (7.21mol, 8eq) of piperonylcycline and 120.0g (0.901mol, 1.0eq) of aluminum trichloride were added to the four-neck flask, and the temperature was lowered to -10°C to -5°C. 139.0 g (3.155 mol, 3.5 eq) of ethylene oxide was introduced in the form of gas, and the reaction was continued for 1 h after the addition was complete. Add 1L of dichloromethane and 1.5L of 2M hydrochloric acid solution to the reaction solution, stir at room temperature for 30 minutes, separate the layers, and wash the DCM organic layer twice with 1M hydrochloric acid solution and three times with water, dry over anhydrous sodium sulfate, and filter. The filtrate was distilled under reduced pressure to collect the piperonine, and the fraction at 115-120°C was collected to obtain 102.0 g of pepper ethanol, yield: 68.1%, and HPLC purity: 98.305%.
实施例2:5-羟甲基苯并-1,3-二恶环戊烷(胡椒乙醇)的制备Embodiment 2: Preparation of 5-hydroxymethylbenzo-1,3-dioxolane (piperethanol)
室温下,向四颈瓶中加入733.8g(6.009mol,8eq)胡椒环,100.0g(0.751mol,1.0eq)三氯化铝,降温至-10℃至-5℃。以气体形式通入99.3g(2.253mol,3.0eq)环氧乙烷,加入完毕继续反应1h。反应液加入800ml二氯甲烷,1.2L 2M盐酸溶液室温搅拌30min,分液,DCM有机层分别以1M盐酸溶液洗涤2次,水洗3次,无水硫酸钠干燥,过滤。滤液减压蒸馏收胡椒环,收集115-120℃馏分,得胡椒乙醇:73.2g,收率:58.7%,HPLC纯度:97.565%。At room temperature, 733.8g (6.009mol, 8eq) of piperonylcycline and 100.0g (0.751mol, 1.0eq) of aluminum trichloride were added to the four-neck flask, and the temperature was lowered to -10°C to -5°C. 99.3g (2.253mol, 3.0eq) of ethylene oxide was introduced in the form of gas, and the reaction was continued for 1h after the addition was complete. Add 800ml of dichloromethane to the reaction solution, stir 1.2L of 2M hydrochloric acid solution at room temperature for 30min, separate the layers, wash the DCM organic layer twice with 1M hydrochloric acid solution, wash three times with water, dry over anhydrous sodium sulfate, and filter. The filtrate was distilled under reduced pressure to collect the peppercycline, and the fraction at 115-120°C was collected to obtain 73.2 g of pepper ethanol, yield: 58.7%, and HPLC purity: 97.565%.
实施例3:5-羟甲基苯并-1,3-二恶环戊烷(胡椒乙醇)的制备Embodiment 3: Preparation of 5-hydroxymethylbenzo-1,3-dioxolane (piperethanol)
室温下,向四颈瓶中加入542.1g(4.439mol,8eq)胡椒环,90.0g(0.555mol,1.0eq)三氯化铁,降温至-10℃至-5℃。以气体形式通入85.5g(1.942mol,3.5eq)环氧乙烷,加入完毕继续反应1h。反应液加入800ml二氯甲烷,1.2L 2M盐酸溶 液室温搅拌30min,分液,DCM有机层分别以1M盐酸溶液洗涤2次,水洗3次,无水硫酸钠干燥,过滤。滤液减压蒸馏收胡椒环,收集115-120℃馏分,得胡椒乙醇:19.0g,收率:20.6%,HPLC纯度:98.119%。At room temperature, 542.1g (4.439mol, 8eq) of piperonylcycline and 90.0g (0.555mol, 1.0eq) of ferric trichloride were added to the four-necked flask, and the temperature was lowered to -10°C to -5°C. 85.5g (1.942mol, 3.5eq) of ethylene oxide was introduced in the form of gas, and the reaction was continued for 1h after the addition. Add 800ml of dichloromethane to the reaction solution, stir 1.2L 2M hydrochloric acid solution at room temperature for 30min, separate the layers, wash the DCM organic layer twice with 1M hydrochloric acid solution, wash three times with water, dry over anhydrous sodium sulfate, and filter. The filtrate was distilled under reduced pressure to collect the peppercycline, and the fraction at 115-120°C was collected to obtain pepper alcohol: 19.0 g, yield: 20.6%, HPLC purity: 98.119%.
实施例4:5-羟甲基苯并-1,3-二恶环戊烷(胡椒乙醇)的制备Embodiment 4: Preparation of 5-hydroxymethylbenzo-1,3-dioxolane (piperethanol)
室温下,向四颈瓶中加入481.8g(3.946mol,8eq)胡椒环,80.0g(0.493mol,1.0eq)三氯化铁,降温至-10℃至-5℃。以气体形式通入65.2g(1.480mol,3.0eq)环氧乙烷,加入完毕继续反应1h。反应液加入600ml二氯甲烷,1.0L 2M盐酸溶液室温搅拌30min,分液,DCM有机层分别以1M盐酸溶液洗涤2次,水洗3次,无水硫酸钠干燥,过滤。滤液减压蒸馏收胡椒环,收集115-120℃馏分,得胡椒乙醇:14.8g,收率:18.1%,HPLC纯度:98.645%。At room temperature, 481.8g (3.946mol, 8eq) of piperonylcycline and 80.0g (0.493mol, 1.0eq) of ferric trichloride were added to the four-neck flask, and the temperature was lowered to -10°C to -5°C. 65.2g (1.480mol, 3.0eq) of ethylene oxide was introduced in the form of gas, and the reaction was continued for 1h after the addition was complete. Add 600ml of dichloromethane to the reaction solution, stir 1.0L of 2M hydrochloric acid solution at room temperature for 30min, separate the layers, wash the DCM organic layer twice with 1M hydrochloric acid solution, wash three times with water, dry over anhydrous sodium sulfate, and filter. The filtrate was distilled under reduced pressure to collect the peppercycline, and the fraction at 115-120°C was collected to obtain 14.8 g of pepper ethanol, yield: 18.1%, and HPLC purity: 98.645%.
实施例5:5-羟甲基苯并-1,3-二恶环戊烷(胡椒乙醇)的制备Embodiment 5: Preparation of 5-hydroxymethylbenzo-1,3-dioxolane (piperethanol)
室温下,向四颈瓶中加入183.4g(1.502mol,4eq)胡椒环,50.0g(0.376mol,1.0eq)三氯化铝,降温至-10℃至-5℃。以气体形式通入57.9g(1.314mol,3.5eq)环氧乙烷,加入完毕继续反应1h。反应液加入0.5L二氯甲烷,0.75L 2M盐酸溶液室温搅拌30min,分液,DCM有机层分别以1M盐酸溶液洗涤2次,水洗3次,无水硫酸钠干燥,过滤。滤液减压蒸馏收胡椒环,收集115-120℃馏分,得胡椒乙醇:27.2g,收率:43.6%,HPLC纯度:98.155%。At room temperature, 183.4g (1.502mol, 4eq) of piperonylcycline and 50.0g (0.376mol, 1.0eq) of aluminum trichloride were added to the four-neck flask, and the temperature was lowered to -10°C to -5°C. 57.9g (1.314mol, 3.5eq) of ethylene oxide was introduced in the form of gas, and the reaction was continued for 1h after the addition was complete. Add 0.5L dichloromethane and 0.75L 2M hydrochloric acid solution to the reaction solution, stir at room temperature for 30 minutes, separate the layers, wash the DCM organic layer twice with 1M hydrochloric acid solution, wash three times with water, dry over anhydrous sodium sulfate, and filter. The filtrate was distilled under reduced pressure to collect the peppercycline, and the fraction at 115-120°C was collected to obtain 27.2 g of pepper ethanol, yield: 43.6%, and HPLC purity: 98.155%.
实施例6:5-羟甲基苯并-1,3-二恶环戊烷(胡椒乙醇)的制备Embodiment 6: Preparation of 5-hydroxymethylbenzo-1,3-dioxolane (piperethanol)
室温下,向四颈瓶中加入336.9g(3.004mol,8eq)胡椒环,50.0g(0.376mol,1.0eq)三氯化铝,降温至-10℃至-5℃。以气体形式通入33.1g(0.751mol,2.0eq)环氧乙烷,加入完毕继续反应1h。反应液加入0.5L二氯甲烷,0.75L 2M盐酸溶液室温搅拌30min,分液,DCM有机层分别以1M盐酸溶液洗涤2次,水洗3次,无水硫酸钠干燥,过滤。滤液减压蒸馏收胡椒环,收集115-120℃馏分,得胡椒乙醇:24.5g,收率:39.3%,HPLC纯度:98.359%。At room temperature, 336.9g (3.004mol, 8eq) of piperonylcycline and 50.0g (0.376mol, 1.0eq) of aluminum trichloride were added to the four-neck flask, and the temperature was lowered to -10°C to -5°C. 33.1g (0.751mol, 2.0eq) of ethylene oxide was introduced in the form of gas, and the reaction was continued for 1h after the addition was completed. Add 0.5L dichloromethane and 0.75L 2M hydrochloric acid solution to the reaction solution, stir at room temperature for 30 minutes, separate the layers, wash the DCM organic layer twice with 1M hydrochloric acid solution, wash three times with water, dry over anhydrous sodium sulfate, and filter. The filtrate was distilled under reduced pressure to collect the peppercycline, and the fraction at 115-120°C was collected to obtain 24.5 g of pepper ethanol, yield: 39.3%, and HPLC purity: 98.359%.
实施例7:5-羟甲基苯并-1,3-二恶环戊烷(胡椒乙醇)的制备Embodiment 7: Preparation of 5-hydroxymethylbenzo-1,3-dioxolane (piperethanol)
采用实施例1投料比与操作,当选用路易斯酸为BF 3、ZnCl 2时,无产物;当选用TiCl 4时,收率为4.1%。 Using the feed ratio and operation of Example 1, when the Lewis acid is selected as BF 3 and ZnCl 2 , there is no product; when TiCl 4 is selected, the yield is 4.1%.
调整环氧乙烷与催化剂的投料比可以发现,投料比3.5时的收率显著优于3.0时;选择不同的催化剂对胡椒乙醇收率的影响也很大,三氯化铝优于三氯化铁, 优于其他路易斯酸。Adjusting the feed ratio of ethylene oxide and catalyst can find that the yield when feed ratio is 3.5 is significantly better than that of 3.0; choosing different catalysts also has a great influence on the yield of pepper ethanol, and aluminum trichloride is better than trichloride Iron, superior to other Lewis acids.
实施例8:3,4-二羟基苯乙醇(羟基酪醇)的制备Embodiment 8: Preparation of 3,4-dihydroxyphenylethanol (hydroxytyrosol)
室温下向四口瓶中加入55.0g(0.331mol,1.0eq)胡椒乙醇,134.2g(1.324mol,4.0eq)36%盐酸,Amberlyst15固体强酸催化剂0.55g,氮气保护下20-30℃反应36h。反应结束,过滤,滤液以3ml NaOH溶液在冰水浴下调节pH至10,以150ml DCM洗涤2次,水层以3M HCl溶液调节pH至1-2,300ml甲基叔丁基醚萃取5次,合并甲基叔丁基醚,无水硫酸钠干燥,5%活性炭脱色,旋转蒸发浓缩得橙黄色油状物,真空干燥得43.4g。收率85.1%,HPLC纯度:98.858%。Add 55.0g (0.331mol, 1.0eq) pepper ethanol, 134.2g (1.324mol, 4.0eq) 36% hydrochloric acid, 0.55g Amberlyst15 solid strong acid catalyst to the four-necked flask at room temperature, and react at 20-30°C for 36h under nitrogen protection. The reaction is completed, filtered, and the filtrate is adjusted to pH 10 with 3ml NaOH solution in an ice-water bath, washed twice with 150ml DCM, the aqueous layer is adjusted to pH 1-2 with 3M HCl solution, extracted 5 times with 300ml methyl tert-butyl ether, The methyl tert-butyl ether was combined, dried over anhydrous sodium sulfate, decolorized with 5% activated carbon, concentrated by rotary evaporation to obtain an orange-yellow oil, and dried in vacuo to obtain 43.4 g. Yield: 85.1%, HPLC purity: 98.858%.
1H NMR(DMSO-D6)δ,ppm:8.060(s,1H),6.875-6.846(m,1H),6.725-6.710(m,1H),5.989(s,2H),2.976-2.946(m,2H),2.848-2.818(m,2H). 1 H NMR(DMSO-D6)δ,ppm:8.060(s,1H),6.875-6.846(m,1H),6.725-6.710(m,1H),5.989(s,2H),2.976-2.946(m, 2H),2.848-2.818(m,2H).
实施例9:3,4-二羟基苯乙醇(羟基酪醇)的制备Embodiment 9: Preparation of 3,4-dihydroxyphenethyl alcohol (hydroxytyrosol)
室温下向四口瓶中加入80.0g(0.481mol,1.0eq)胡椒乙醇,195.2g(1.926mol,4.0eq)36%盐酸,HND-32固体超强酸催化剂0.16g,氮气保护下20-30℃反应28h。反应结束,过滤,滤液以3ml NaOH溶液在冰水浴下调节pH至10,以150ml DCM洗涤2次,水层以3M HCl溶液调节pH至1-2,300ml甲基叔丁基醚萃取5次,合并甲基叔丁基醚,无水硫酸钠干燥,5%活性炭脱色,旋转蒸发浓缩得橙黄色油状物,真空干燥得64.8g。收率87.3%,HPLC纯度:98.566%。Add 80.0g (0.481mol, 1.0eq) pepper ethanol, 195.2g (1.926mol, 4.0eq) 36% hydrochloric acid, 0.16g HND-32 solid superacid catalyst to the four-necked flask at room temperature, under nitrogen protection at 20-30°C Reaction 28h. The reaction is completed, filtered, and the filtrate is adjusted to pH 10 with 3ml NaOH solution in an ice-water bath, washed twice with 150ml DCM, the aqueous layer is adjusted to pH 1-2 with 3M HCl solution, extracted 5 times with 300ml methyl tert-butyl ether, The methyl tert-butyl ether was combined, dried over anhydrous sodium sulfate, decolorized with 5% activated carbon, concentrated by rotary evaporation to obtain an orange-yellow oil, and dried in vacuo to obtain 64.8 g. Yield: 87.3%, HPLC purity: 98.566%.
对比例1:3,4-二羟基苯乙醇(羟基酪醇)的制备Comparative Example 1: Preparation of 3,4-dihydroxyphenylethanol (hydroxytyrosol)
室温下向四口瓶中加入60.0g(0.361mol,1.0eq)胡椒乙醇,182.6g(1.083mol,3.0eq)48%氢溴酸,氮气保护下升温至20-30℃,反应12h,TLC监控原料消失,反应结束。反应液以3mlNaOH溶液在冰水浴下调节pH至10,以200mlDCM洗涤2次,水层以3MHCl溶液调节pH至1-2,400ml甲基叔丁基醚萃取5次,合并甲基叔丁基醚,无水硫酸钠干燥,5%活性炭脱色,旋转蒸发浓缩得橙黄色油状物,真空干燥得6.5g,收率11.6%,HPLC纯度:98.232%。Add 60.0g (0.361mol, 1.0eq) of pepper alcohol and 182.6g (1.083mol, 3.0eq) of 48% hydrobromic acid to the four-neck flask at room temperature, raise the temperature to 20-30°C under the protection of nitrogen, react for 12 hours, and monitor by TLC The starting material disappeared, and the reaction ended. Adjust the pH of the reaction solution to 10 with 3ml NaOH solution in an ice-water bath, wash twice with 200ml DCM, adjust the pH of the aqueous layer to 1-2 with 3M HCl solution, extract 5 times with 400ml methyl tert-butyl ether, and combine methyl tert-butyl ether , dried over anhydrous sodium sulfate, decolorized with 5% activated carbon, concentrated by rotary evaporation to obtain an orange-yellow oil, dried in vacuo to obtain 6.5 g, yield 11.6%, HPLC purity: 98.232%.
对比例2:3,4-二羟基苯乙醇(羟基酪醇)的制备Comparative Example 2: Preparation of 3,4-dihydroxyphenylethanol (hydroxytyrosol)
室温下向四口瓶中加入50.0g(0.301mol,1.0eq)胡椒乙醇,122.0g(1.204mol,4.0eq)36%盐酸,氮气保护下升温至50-60℃,反应6h,反应TLC监控原料消失时,反应结束。反应液以3mlNaOH溶液在冰水浴下调节pH至10,以180mlDCM洗涤2次,水层以3MHCl溶液调节pH至1-2,350ml甲基叔丁基醚萃取5次, 合并甲基叔丁基醚,无水硫酸钠干燥,5%活性炭脱色,旋转蒸发浓缩得橙黄色油状物,真空干燥得11.9g。收率25.6%,HPLC纯度:98.686%。Add 50.0g (0.301mol, 1.0eq) pepper ethanol, 122.0g (1.204mol, 4.0eq) 36% hydrochloric acid to the four-neck flask at room temperature, raise the temperature to 50-60°C under nitrogen protection, react for 6h, and monitor the raw materials by reaction TLC When it disappears, the reaction ends. The reaction solution was adjusted to pH 10 with 3ml NaOH solution in an ice-water bath, washed twice with 180ml DCM, the aqueous layer was adjusted to pH 1-2 with 3M HCl solution, extracted 5 times with 350ml methyl tert-butyl ether, and combined with methyl tert-butyl ether , dried over anhydrous sodium sulfate, decolorized with 5% activated carbon, concentrated by rotary evaporation to obtain an orange-yellow oil, and dried in vacuo to obtain 11.9 g. Yield 25.6%, HPLC purity: 98.686%.
本发明的保护内容不局限于以上实施例。在不背离发明构思的精神和范围下,本领域技术人员能够想到的变化和优点都被包括在本发明中,并且以所附的权利要求为保护范围。The protection content of the present invention is not limited to the above embodiments. Without departing from the spirit and scope of the inventive concept, changes and advantages that can be conceived by those skilled in the art are all included in the present invention, and the appended claims are the protection scope.

Claims (10)

  1. 一种制备羟基酪醇的工艺,其特征在于,包括如下步骤:A kind of technique for preparing hydroxytyrosol, is characterized in that, comprises the steps:
    步骤1,胡椒乙醇的制备:向反应瓶中加入胡椒环、催化剂,再通入环氧乙烷气体反应,反应温度为-20~10℃,反应时间0.5-1h,反应结束后猝灭,再经酸洗、水洗、浓缩、蒸馏,得到关键中间体胡椒乙醇;Step 1, the preparation of pepper ethanol: add piperonyl ring and catalyst to the reaction bottle, and then feed ethylene oxide gas to react. The reaction temperature is -20-10°C, and the reaction time is 0.5-1h. After acid washing, water washing, concentration and distillation, the key intermediate pepper ethanol is obtained;
    步骤2,羟基酪醇的制备:向反应瓶中加入质子酸、步骤1所得的胡椒乙醇、催化剂、氮气保护下20~60℃,反应5-36h;反应结束后调节pH至10±0.5,DCM洗涤,水层调节pH至1-2,再以甲基叔丁基醚萃取,干燥,脱色,浓缩得羟基酪醇。Step 2, preparation of hydroxytyrosol: add protonic acid, pepper alcohol obtained in step 1, catalyst, nitrogen protection at 20-60°C to the reaction flask, and react for 5-36 hours; after the reaction, adjust the pH to 10±0.5, DCM Wash and adjust the pH of the aqueous layer to 1-2, then extract with methyl tert-butyl ether, dry, decolorize, and concentrate to obtain hydroxytyrosol.
  2. 根据权利要求1所述的制备羟基酪醇的工艺,其特征在于,步骤1中,所述催化剂为路易斯酸,选自AlBr 3、AlCl 3、FeCl 3、SbCl 5、SnCl 4,BF 3、TiCl 4、ZnCl 2中一种或多种的组合,优选为AlCl 3、FeCl 3,更优选为AlCl 3The process for preparing hydroxytyrosol according to claim 1, wherein in step 1, the catalyst is a Lewis acid selected from AlBr 3 , AlCl 3 , FeCl 3 , SbCl 5 , SnCl 4 , BF 3 , TiCl 4. A combination of one or more of ZnCl 2 , preferably AlCl 3 , FeCl 3 , more preferably AlCl 3 .
  3. 根据权利要求1或2所述的制备羟基酪醇的工艺,其特征在于,步骤1中,所述反应温度为-10~-5℃。The process for preparing hydroxytyrosol according to claim 1 or 2, characterized in that, in step 1, the reaction temperature is -10 to -5°C.
  4. 根据权利要求1所述的制备羟基酪醇的工艺,其特征在于,步骤1中,胡椒环与催化剂的摩尔比为5~10:1,优选为5~8:1。The process for preparing hydroxytyrosol according to claim 1, characterized in that, in step 1, the molar ratio of piperonyl ring to catalyst is 5-10:1, preferably 5-8:1.
  5. 根据权利要求1或4所述的制备羟基酪醇的工艺,其特征在于,步骤1中,所述催化剂与环氧乙烷的摩尔比为1:1~5,优选为1:3~3.5。The process for preparing hydroxytyrosol according to claim 1 or 4, characterized in that, in step 1, the molar ratio of the catalyst to ethylene oxide is 1:1-5, preferably 1:3-3.5.
  6. 根据权利要求1所述的制备羟基酪醇的工艺,其特征在于,步骤2中,所述质子酸选自氢氟酸、盐酸、氢溴酸、氢碘酸、硫酸、磷酸、硝酸中的任一种或多种。The process for preparing hydroxytyrosol according to claim 1, wherein in step 2, the protonic acid is selected from any of hydrofluoric acid, hydrochloric acid, hydrobromic acid, hydroiodic acid, sulfuric acid, phosphoric acid, and nitric acid. one or more.
  7. 根据权利要求6所述的制备羟基酪醇的工艺,其特征在于,所述质子酸为盐酸。The process for preparing hydroxytyrosol according to claim 6, wherein the protonic acid is hydrochloric acid.
  8. 根据权利要求1所述的制备羟基酪醇的工艺,其特征在于,步骤2中,所述催化剂为固体强酸或固体超强酸,选自HND-32固体超强酸催化剂、HND-34固体超强酸催化剂、Amberlyst15固体强酸催化剂、HNF-5W全氟磺酸树脂、NKC-9催化树脂任一种或多种。The process for preparing hydroxytyrosol according to claim 1, wherein in step 2, the catalyst is a solid strong acid or a solid superacid, selected from HND-32 solid superacid catalyst, HND-34 solid superacid catalyst , Amberlyst15 solid strong acid catalyst, HNF-5W perfluorosulfonic acid resin, NKC-9 catalytic resin any one or more.
  9. 根据权利要求8所述的制备羟基酪醇的工艺,其特征在于,所述催化剂为HND-32固体超强酸催化剂或Amberlyst15固体强酸催化剂。The process for preparing hydroxytyrosol according to claim 8, wherein the catalyst is HND-32 solid superacid catalyst or Amberlyst15 solid strong acid catalyst.
  10. 根据权利要求1所述的制备羟基酪醇的工艺,其特征在于,质子酸与催化剂的组合为盐酸/Amberlyst15固体强酸催化剂,或盐酸/HND-32固体超强酸催化剂。The process for preparing hydroxytyrosol according to claim 1, wherein the combination of protonic acid and catalyst is hydrochloric acid/Amberlyst15 solid strong acid catalyst, or hydrochloric acid/HND-32 solid superacid catalyst.
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