WO2011113228A1 - A process for preparing guaiacol glycidyl - Google Patents

A process for preparing guaiacol glycidyl Download PDF

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WO2011113228A1
WO2011113228A1 PCT/CN2010/073337 CN2010073337W WO2011113228A1 WO 2011113228 A1 WO2011113228 A1 WO 2011113228A1 CN 2010073337 W CN2010073337 W CN 2010073337W WO 2011113228 A1 WO2011113228 A1 WO 2011113228A1
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guaiacol
glycidyl ether
crude
lower alcohol
guaiacol glycidyl
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PCT/CN2010/073337
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French (fr)
Chinese (zh)
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王磊
王鹏
甘立新
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浙江华海药业股份有限公司
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Publication of WO2011113228A1 publication Critical patent/WO2011113228A1/en

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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D301/00Preparation of oxiranes
    • C07D301/27Condensation of epihalohydrins or halohydrins with compounds containing active hydrogen atoms
    • C07D301/28Condensation of epihalohydrins or halohydrins with compounds containing active hydrogen atoms by reaction with hydroxyl radicals
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D303/00Compounds containing three-membered rings having one oxygen atom as the only ring hetero atom
    • C07D303/02Compounds containing oxirane rings
    • C07D303/12Compounds containing oxirane rings with hydrocarbon radicals, substituted by singly or doubly bound oxygen atoms
    • C07D303/18Compounds containing oxirane rings with hydrocarbon radicals, substituted by singly or doubly bound oxygen atoms by etherified hydroxyl radicals
    • C07D303/20Ethers with hydroxy compounds containing no oxirane rings
    • C07D303/24Ethers with hydroxy compounds containing no oxirane rings with polyhydroxy compounds

Definitions

  • the present invention relates to a process for the preparation of a compound, and in particular to a process for the preparation of guaiacol condensed glycerol ether. Background technique
  • Guaiacol glycidyl ether is widely used as an intermediate of ranolazine and motoprol, and its structural formula is as shown in formula (I):
  • This product is mainly formed by the condensation of guaiacol and epichlorohydrin in the presence of a base.
  • the reaction formula is as follows:
  • Patent GB2216520 discloses a preparation method for preparing epichlorohydrin, in which, after the reaction of epichlorohydrin and guaiacol is completed, it is diluted with dichlorosilane, and then extracted and distilled to obtain a crude product, which is then high. The crude product was fractionated under vacuum to obtain a finished product.
  • a large amount of dichloromethane is consumed, which has a great influence on the environment, and it is necessary to decompose at a high temperature in the purification process. Distillation, so the equipment is demanding.
  • Patent WO2008047388 describes that in the reaction process, terpene is used as a solvent, and epichlorohydrin and guaiacol are reacted. After the reaction is completed, it is extracted with terpene and then washed with water, and then distilled at 130 to 150 ° C and 3 bar. product. This method also involves a large amount of solvent, and since the product density is larger than water, it is easy to emulsify in the extraction process using benzene as a solvent. The purification method is also not mentioned in the patent, and the purity of the obtained product is only about 96%.
  • the object of the present invention is to provide a preparation method of a product having high purity, which is advantageous for industrialization and low cost guaiacol glycidyl ether.
  • the present invention provides a method for preparing guaiacol glycidyl ether, which comprises:
  • the guaiacol and epichlorohydrin are subjected to a condensation reaction under the action of an aqueous solution of an inorganic base and a phase transfer catalyst;
  • the crude guaiacol glycidic acid obtained by the condensation reaction was recrystallized from a lower alcohol to obtain a guaiacol glycidyl ether.
  • the method has the advantages of high yield, good quality, convenient operation and low requirement on equipment, and is a method for preparing high-purity guaiacol glycidyl ether which is very suitable for industrial production. detailed description
  • the guaiacol and epichlorohydrin are subjected to a condensation reaction under the action of an aqueous solution of an inorganic base and a phase transfer catalyst;
  • the crude guaiacol glycidic acid obtained by the condensation reaction is recrystallized from a lower alcohol to obtain guaiacol glycidyl ether.
  • the raw material needs to be added with a base during the reaction, and in order to control the residue of the alkali in the product, the selected base should be The product is well separated.
  • the unreacted raw materials and the impurities formed during the reaction should be well separated from the product.
  • the first choice should be to select cheap materials.
  • the input on the production equipment should be well controlled. The process should be easy to operate. The unreacted raw materials should be recycled. The solvent should not be used as much as possible. .
  • the use of the alkali used in the reaction of the present invention has obvious advantages in the above three aspects: First, the use of inorganic bases in the reaction, the use of two-phase reaction, can effectively control the alkali substances Residue in the product; Secondly, since the two raw materials and the main impurities formed during the reaction are liquid at room temperature, and the product is solid at room temperature, the use of crystallization is advantageous for the separation of the product and the inorganic base. It has a very good effect on improving the purity of the product. Further, one of the raw materials used in the reaction of the present invention is epichlorohydrin, and after the excess epoxy is added to the solvent after the reaction, the solvent can be directly recovered and applied, which has little environmental pollution and is costly.
  • the preparation method of guaiacol glycidyl ether according to the present invention is preferably carried out as follows:
  • the amount of epichlorohydrin may be selected from 1 to 8 equivalents, preferably from 2 to 5 equivalents, to guaiacol.
  • the inorganic base sodium carbonate, potassium carbonate, sodium hydroxide, potassium hydroxide or the like can be selected, and sodium hydroxide and potassium hydroxide are preferred.
  • the aqueous solution concentration of the base may be selected from 10% by weight to 50% by weight.
  • the phase transfer catalyst can be selected from tetrabutylammonium bromide, benzyltriethylammonium chloride, tetrabutyl One or more of ammonium hydrogen sulfate and tetrabutylammonium chloride.
  • the reaction temperature is preferably from 20 ° C to 80 ° C, more preferably from 30 to 60 ° C.
  • the reaction time is preferably from 1 to 10 hours, more preferably from 2 to 5 hours.
  • the organic solvent may be selected from the group consisting of alcohols, esters and ethers, of which lower alcohols are preferred. More preferred are C1 to C4 lower alcohol solvents such as decyl alcohol, ethanol, n-propanol, isopropanol and butanol.
  • the amount of the solvent to be crystallized is 1 to 10 ml/g (crude xylanol glycidic acid crude), and preferably 2 to 5 ml/g (crude xylanol glycidic acid crude).
  • the crystallization can be naturally stirred and crystallized or crystallized to induce crystallization. In order to control the crystallization rate to ensure the purity of the product, it is preferred to add seed crystals to induce crystallization.
  • Example 4 The crude product of 30 g of guaiacol glycidol obtained in Example 1 was added to 90 ml of decyl alcohol, heated to 40 ° C, and stirred until the solution was dissolved. Filtration, the filtrate was slowly cooled to 14 ° C, seeded After stirring at 14 to 16 ° C for 2 hours, the temperature was slowly reduced to 0 to 5 ° C and stirred for 1 hour, filtered, and the filter cake was vacuum dried at 25 ° C for 12 hours to obtain 24 g of a white solid, yield 80%. Purity: 99.6% (determined by GC).
  • Example 4 Preparation of high purity guaiacol glycidyl ether

Abstract

Disclosed is a process for preparing guaiacol glycidyl ether, which comprising the following steps: guaiacol and epichlorohydrin are reacted in the presence of an inorganic alkali aqueous solution and a phase transfer catalyst; thereafter, the crude guaiacol glycidyl ether is obtained by distilling under reduced pressure; the crude guaiacol glycidyl ether is recrystallizated by lower alcohol to obtain guaiacol glycidyl ether with a purity over 99.5%. According to the present process, the yield is high, the operation is easy and the demand to the equipment is low. Therefore, the process is suitable for industrial process.

Description

一种制备愈创木酚缩水甘油醚的方法  Method for preparing guaiacol phenol glycidyl ether
本申请要求于 2010 年 3 月 19 日提交中国专利局、 申请号为 201010144102.2, 发明名称为 "一种制备高纯度愈创木酚缩水甘油醚的方 法"的中国专利申请的优先权, 其全部内容通过引用结合在本申请中。 技术领域 This application claims priority to Chinese Patent Application No. 201010144102.2, entitled "A Method for Preparing High Purity Guaiacol Glycidyl Ether", filed on March 19, 2010, the entire contents of which is incorporated herein by reference. This is incorporated herein by reference. Technical field
本发明涉及化合物的制备方法, 具体涉及一种制备愈创木酚缩水甘 油醚的方法。 背景技术  The present invention relates to a process for the preparation of a compound, and in particular to a process for the preparation of guaiacol condensed glycerol ether. Background technique
愈创木酚缩水甘油醚作为雷诺嗪及莫普洛尔的中间体被广泛应用 , 其结构式如式( I )所示:  Guaiacol glycidyl ether is widely used as an intermediate of ranolazine and motoprol, and its structural formula is as shown in formula (I):
Figure imgf000002_0001
Figure imgf000002_0001
该产品主要是通过愈创木酚和环氧氯丙烷在碱的存在下缩合而成, 反 应式如下:  This product is mainly formed by the condensation of guaiacol and epichlorohydrin in the presence of a base. The reaction formula is as follows:
Figure imgf000002_0002
Figure imgf000002_0002
实际反应中是经过两步反应; 环氧氯丙烷先开环和愈创木酚缩合, 然 后再在碱的作用下脱去一个氯化氢形成环氧环。  In the actual reaction, a two-step reaction is carried out; epichlorohydrin is first opened and guaiacol is condensed, and then a hydrogen chloride is removed by the action of a base to form an epoxy ring.
专利 GB2216520公开了一种制备环氧氯丙烷的制备方法,在该方法中, 环氧氯丙烷和愈创木酚反应完毕后先用二氯曱烷稀释, 再提取、 蒸馏得 到粗品, 然后在高真空下分馏粗品得到成品。 在上述方法中, 需要消耗 大量二氯曱烷, 对环境影响很大, 而且提纯过程中需要在高温下减压分 馏, 因此对设备要求苛刻。 Patent GB2216520 discloses a preparation method for preparing epichlorohydrin, in which, after the reaction of epichlorohydrin and guaiacol is completed, it is diluted with dichlorosilane, and then extracted and distilled to obtain a crude product, which is then high. The crude product was fractionated under vacuum to obtain a finished product. In the above method, a large amount of dichloromethane is consumed, which has a great influence on the environment, and it is necessary to decompose at a high temperature in the purification process. Distillation, so the equipment is demanding.
专利 WO2008047388中描述, 反应过程中采用曱苯作为溶剂, 环氧氯 丙烷和愈创木酚反应, 反应完毕后用曱苯提取再用水洗涤, 然后在 130 ~ 150°C、 3bar的条件下蒸馏得到产物。 这个方法中同样涉及溶剂量大的问 题, 而且由于产物密度比水大, 用曱苯做溶剂在提取的过程中容易乳化。 该专利中也没有提到纯化方法, 得到的产品纯度只有 96%左右。  Patent WO2008047388 describes that in the reaction process, terpene is used as a solvent, and epichlorohydrin and guaiacol are reacted. After the reaction is completed, it is extracted with terpene and then washed with water, and then distilled at 130 to 150 ° C and 3 bar. product. This method also involves a large amount of solvent, and since the product density is larger than water, it is easy to emulsify in the extraction process using benzene as a solvent. The purification method is also not mentioned in the patent, and the purity of the obtained product is only about 96%.
目前公开的其它文献中除了高温下减压蒸馏外都没有提到其他的精 制方法。 而且高温下产物易发生聚合, 采用这种方法, 产物的纯度艮难 提高, 而且收率也比较低。 发明内容  Other refining methods have not been mentioned in other documents currently disclosed except for vacuum distillation under high temperature. Moreover, the product tends to be polymerized at a high temperature. With this method, the purity of the product is difficult to increase, and the yield is relatively low. Summary of the invention
本发明的目的在于提供一种产品纯度高、 有利于工业化、 低成本愈创 木酚缩水甘油醚的制备方法。  The object of the present invention is to provide a preparation method of a product having high purity, which is advantageous for industrialization and low cost guaiacol glycidyl ether.
为了解决以上技术问题, 本发明提供一种愈创木酚缩水甘油醚的制备 方法, 包括:  In order to solve the above technical problems, the present invention provides a method for preparing guaiacol glycidyl ether, which comprises:
将愈创木酚和环氧氯丙烷在无机碱的水溶液和相转移催化剂的作用 下进行缩合反应;  The guaiacol and epichlorohydrin are subjected to a condensation reaction under the action of an aqueous solution of an inorganic base and a phase transfer catalyst;
将缩合反应得到的愈创木酚缩水甘油酸粗品用低级醇重结晶得到愈 创木酚缩水甘油醚。  The crude guaiacol glycidic acid obtained by the condensation reaction was recrystallized from a lower alcohol to obtain a guaiacol glycidyl ether.
本方法收率高, 质量好, 操作方便, 对设备要求低, 是一种非常适 合工业化生产的制备高纯度愈创木酚缩水甘油醚的方法。 具体实施方式  The method has the advantages of high yield, good quality, convenient operation and low requirement on equipment, and is a method for preparing high-purity guaiacol glycidyl ether which is very suitable for industrial production. detailed description
以下实施方案可以有助于理解本发明, 但本发明的保护范围不限于 此。  The following embodiments may be helpful in understanding the present invention, but the scope of protection of the present invention is not limited thereto.
本发明提供的一个愈创木酚缩水甘油醚的制备方法的实施方案, 包 括:  An embodiment of a method for preparing a guaiacol glycidyl ether provided by the present invention comprises:
将愈创木酚和环氧氯丙烷在无机碱的水溶液和相转移催化剂的作用 下进行缩合反应; 将缩合反应得到的愈创木酚缩水甘油酸粗品用低级醇重结晶得到愈 创木酚缩水甘油醚。 The guaiacol and epichlorohydrin are subjected to a condensation reaction under the action of an aqueous solution of an inorganic base and a phase transfer catalyst; The crude guaiacol glycidic acid obtained by the condensation reaction is recrystallized from a lower alcohol to obtain guaiacol glycidyl ether.
按照本发明, 为了得到高纯度的产品, 该产品的合成过程中有几个关 键点: (1)原料在反应过程中需要加入碱, 为了控制碱在产品中的残留, 选用的碱应该要和产物很好的分离。 (2)反应完毕后, 未反应完毕的原料 以及反应过程中形成的杂质应该要和产品很好的分离。 (3 ) 为了控制产 品的成本, 首先应该尽量选取廉价的物料, 其次在生产设备上的投入应 该要得到很好的控制, 工艺应该方便操作, 未反应完的原料要能回收, 溶剂尽量不要使用。  According to the present invention, in order to obtain a high-purity product, there are several key points in the synthesis process of the product: (1) The raw material needs to be added with a base during the reaction, and in order to control the residue of the alkali in the product, the selected base should be The product is well separated. (2) After the reaction is completed, the unreacted raw materials and the impurities formed during the reaction should be well separated from the product. (3) In order to control the cost of the product, the first choice should be to select cheap materials. Secondly, the input on the production equipment should be well controlled. The process should be easy to operate. The unreacted raw materials should be recycled. The solvent should not be used as much as possible. .
综合以上三个关键点, 本发明反应中用到的碱选用无机碱类在以上三 个方面有比较明显的优势: 首先, 反应中使用无机碱类, 使用两相反应, 可以有效控制碱类物质在产品中的残留; 其次, 由于两个原料以及反应 过程中形成的主要杂质在室温下都是液体, 而产物在室温下为固体, 因 此采用结晶的方式有利于产品和无机碱的分离, 这样对提高产品的纯度 有非常好的效果。 此外, 本发明在反应中使用的原料之一为环氧氯丙烷, 过量的环氧在反应完毕进入溶剂后, 该溶剂可以直接回收套用, 对环境 污染小, 成本也氐。  Based on the above three key points, the use of the alkali used in the reaction of the present invention has obvious advantages in the above three aspects: First, the use of inorganic bases in the reaction, the use of two-phase reaction, can effectively control the alkali substances Residue in the product; Secondly, since the two raw materials and the main impurities formed during the reaction are liquid at room temperature, and the product is solid at room temperature, the use of crystallization is advantageous for the separation of the product and the inorganic base. It has a very good effect on improving the purity of the product. Further, one of the raw materials used in the reaction of the present invention is epichlorohydrin, and after the excess epoxy is added to the solvent after the reaction, the solvent can be directly recovered and applied, which has little environmental pollution and is costly.
按照本发明, 本发明中涉及的愈创木酚缩水甘油醚制备方法优选按如 下步骤进行:  According to the present invention, the preparation method of guaiacol glycidyl ether according to the present invention is preferably carried out as follows:
( 1 )将愈创木酚溶解于过量的环氧氯丙烷中, 然后在无机碱的水溶 液和相转移催化剂的作用下进行缩合反应, 反应结束后, 分去水层, 通 过减压蒸馏回收过量的环氧氯丙烷,继续浓缩收集 148〜153 °C/1.33KPa的 馏分得到愈创木酚缩水甘油醚粗品。  (1) Dissolving guaiacol in an excess amount of epichlorohydrin, and then performing a condensation reaction under the action of an aqueous solution of an inorganic base and a phase transfer catalyst. After the reaction is completed, the aqueous layer is separated, and excess is recovered by distillation under reduced pressure. The epichlorohydrin was continuously concentrated and collected into a fraction of 148-153 ° C / 1.33 KPa to obtain a crude guaiacol glycidyl ether.
( 2 )将步骤 ( 1 )得到的粗品用有机溶剂重结晶得到高纯度的愈创木 酚缩水甘油醚。  (2) The crude product obtained in the step (1) is recrystallized from an organic solvent to obtain a high-purity guaiacol glycidyl ether.
在步骤(1 )中, 环氧氯丙烷的量可以选择为愈创木酚的 1 ~ 8个当量, 优选为 2 ~ 5个当量。 无机碱可以选择碳酸钠、 碳酸钾、 氢氧化钠、 氢氧 化钾等, 优选氢氧化钠和氢氧化钾。 碱的水溶液浓度可以选择 10wt% - 50wt%。 相转移催化剂可以选择四丁基溴化铵、 苄基三乙基氯化铵、 四丁 基硫酸氢铵、 四丁基氯化铵中的一种或多种。 反应温度优选为 20°C ~ 80 °C , 更优选为 30 ~ 60°C。 反应时间优选为 1 ~ 10小时, 更优选为 2 ~ 5 小时。 In the step (1), the amount of epichlorohydrin may be selected from 1 to 8 equivalents, preferably from 2 to 5 equivalents, to guaiacol. As the inorganic base, sodium carbonate, potassium carbonate, sodium hydroxide, potassium hydroxide or the like can be selected, and sodium hydroxide and potassium hydroxide are preferred. The aqueous solution concentration of the base may be selected from 10% by weight to 50% by weight. The phase transfer catalyst can be selected from tetrabutylammonium bromide, benzyltriethylammonium chloride, tetrabutyl One or more of ammonium hydrogen sulfate and tetrabutylammonium chloride. The reaction temperature is preferably from 20 ° C to 80 ° C, more preferably from 30 to 60 ° C. The reaction time is preferably from 1 to 10 hours, more preferably from 2 to 5 hours.
在步骤(2 ) 中, 所述有机溶剂类可以选择醇类、 酯类和醚类, 其中 优选低级醇类。更为优选的是曱醇、乙醇、正丙醇、异丙醇、丁醇等 C1〜C4 低级醇类溶剂。 结晶的溶剂量为 1 ~ 10ml/g (愈创木酚缩水甘油酸粗品), 其中优选 2 ~ 5ml/g (愈创木酚缩水甘油酸粗品)。结晶可以自然搅拌析晶也 可以加晶种诱导析晶, 为了控制结晶速度保证产品的纯度, 优选加晶种 诱导析晶。  In the step (2), the organic solvent may be selected from the group consisting of alcohols, esters and ethers, of which lower alcohols are preferred. More preferred are C1 to C4 lower alcohol solvents such as decyl alcohol, ethanol, n-propanol, isopropanol and butanol. The amount of the solvent to be crystallized is 1 to 10 ml/g (crude xylanol glycidic acid crude), and preferably 2 to 5 ml/g (crude xylanol glycidic acid crude). The crystallization can be naturally stirred and crystallized or crystallized to induce crystallization. In order to control the crystallization rate to ensure the purity of the product, it is preferred to add seed crystals to induce crystallization.
以下结合具体实施例说明本发明的技术方案, 但本发明的保护范围 并不局限于以下实施例。  The technical solutions of the present invention will be described below with reference to specific embodiments, but the scope of protection of the present invention is not limited to the following embodiments.
实施例 1: 制备愈创木酚缩水甘油醚粗品 Example 1: Preparation of crude guaiacol glycidyl ether
愈创木酚 44.4g投入 250ml反应瓶中, 然后加入环氧氯丙烷 99.8g, 四丁基溴化铵 1.16g, 搅拌。 滴加 25%的氢氧化钠溶液 64g, 滴毕, 控制 温度 50〜55°C反应 2小时。 反应完毕后, 用水洗涤一次, 然后分层, 有机 相减压回收过量的环氧氯丙烷。 回收完毕后, 升温继续蒸馏, 收集 148〜153 °C/1.33KPa的馏分得无色透明液体 45.1g, 收率 70%, 纯度: 98% ( GC测定) 实施例 2: 制备高纯度愈创木酚缩水甘油醚  44.4 g of guaiacol was placed in a 250 ml reaction flask, and then 99.8 g of epichlorohydrin and 1.16 g of tetrabutylammonium bromide were added and stirred. 64 g of a 25% sodium hydroxide solution was added dropwise, and the reaction was carried out at a temperature of 50 to 55 ° C for 2 hours. After completion of the reaction, it was washed once with water, then layered, and the organic phase was used to recover excess epichlorohydrin under reduced pressure. After the recovery was completed, the temperature was further distilled, and a fraction of 148 to 153 ° C / 1.33 KPa was collected to obtain a colorless transparent liquid of 45.1 g, yield 70%, purity: 98% (GC measurement) Example 2: Preparation of high purity guaiac wood Phenol glycidyl ether
取实施例 1制得的 30g愈创木酚缩水甘油酸粗品加入 90ml乙醇中, 加热至 40°C , 搅拌至溶液溶清。 过滤, 滤液緩慢降温至 20°C , 加入晶种, 保持温度在 18〜20°C下搅拌析晶 2小时, 然后将温度緩慢降至 0〜5°C搅拌 1小时, 过滤。 滤饼 25°C真空干燥 12小时得白色固体 25.5g, 收率 85%, 纯度: 99.8% ( GC测定)。 实施例 3: 制备高纯度愈创木酚缩水甘油醚  The crude product of 30 g of guaiacol glycidol obtained in Example 1 was added to 90 ml of ethanol, heated to 40 ° C, and stirred until the solution was dissolved. Filtration, the filtrate was slowly cooled to 20 ° C, seed crystals were added, and the temperature was maintained at 18 to 20 ° C for 2 hours with stirring, and then the temperature was slowly lowered to 0 to 5 ° C and stirred for 1 hour, and filtered. The filter cake was dried under vacuum at 25 ° C for 12 hours to give a white solid (25.5 g, yield: 85%, purity: 99.8% (GC). Example 3: Preparation of high purity guaiacol glycidyl ether
取实施例 1制得的 30g愈创木酚缩水甘油酸粗品加入 90ml曱醇中, 加热至 40°C , 搅拌至溶液溶清。 过滤, 滤液緩慢降温至 14°C , 加入晶种 后于 14〜16°C下搅拌析晶 2小时,然后将温度緩慢降至 0〜5°C搅拌 1小时, 过滤,滤饼 25°C真空干燥 12小时得白色固体 24g,收率 80%,纯度: 99.6% ( GC测定)。 实施例 4: 制备高纯度愈创木酚缩水甘油醚 The crude product of 30 g of guaiacol glycidol obtained in Example 1 was added to 90 ml of decyl alcohol, heated to 40 ° C, and stirred until the solution was dissolved. Filtration, the filtrate was slowly cooled to 14 ° C, seeded After stirring at 14 to 16 ° C for 2 hours, the temperature was slowly reduced to 0 to 5 ° C and stirred for 1 hour, filtered, and the filter cake was vacuum dried at 25 ° C for 12 hours to obtain 24 g of a white solid, yield 80%. Purity: 99.6% (determined by GC). Example 4: Preparation of high purity guaiacol glycidyl ether
取实施例 1制得的 30g愈创木酚缩水甘油酸粗品加入 120ml异丙醇 中, 加热至 50°C , 搅拌至溶液溶清。 过滤, 滤液緩慢降温至 20°C , 加入 晶种后于 15 ~ 20°C下搅拌析晶 2小时,然后将温度緩慢降至 0〜5°C搅拌 1 小时, 过滤,滤饼 25°C真空干燥 12小时得白色固体 26.4g, 收率 88%, 纯 度: 99.5% ( GC测定)。 实施例 5: 制备高纯度愈创木酚缩水甘油醚  The crude product of 30 g of guaiacol glycidol obtained in Example 1 was added to 120 ml of isopropyl alcohol, heated to 50 ° C, and stirred until the solution was dissolved. Filtration, the filtrate was slowly cooled to 20 ° C, seeded and stirred at 15 ~ 20 ° C for 2 hours, then slowly reduced to 0 ~ 5 ° C for 1 hour, filtered, filter cake 25 ° C vacuum Drying for 12 hours gave a white solid 26.4 g, yield 88%, purity: 99.5% (GC). Example 5: Preparation of high purity guaiacol glycidyl ether
取实施例 1制得的 30g愈创木酚缩水甘油酸粗品加入 120ml正丙醇中, 加热至 50°C , 搅拌至溶液溶清。 过滤, 滤液緩慢降温至 20°C , 加入晶种 后于 15 ~ 20°C下搅拌析晶 2小时, 然后将温度緩慢降至 0〜5 °C搅拌 1小时, 过滤,滤饼 25°C真空干燥 12小时得白色固体 26.1g, 收率 87%, 纯度: 99.7% ( GC测定)。  The crude product of 30 g of guaiacol glycidol obtained in Example 1 was added to 120 ml of n-propanol, heated to 50 ° C, and stirred until the solution was dissolved. Filtration, the filtrate was slowly cooled to 20 ° C, seeded and stirred at 15 ~ 20 ° C for 2 hours, then slowly reduced to 0 ~ 5 ° C for 1 hour, filtered, filter cake 25 ° C vacuum After drying for 12 hours, 26.1 g of a white solid was obtained, yield 87%, purity: 99.7% (GC).
通过以上实施例可以看出, 本发明制备的愈创木酚的方法收率高, 质量好。  It can be seen from the above examples that the method of the guaiacol prepared by the invention has high yield and good quality.

Claims

权 利 要 求 Rights request
1、 一种制备愈创木酚缩水甘油醚的方法, 包括:  A method for preparing guaiacol glycidyl ether, comprising:
将愈创木酚和环氧氯丙烷在无机碱的水溶液和相转移催化剂的条件 下进行缩合反应,  The guaiacol and epichlorohydrin are subjected to a condensation reaction under the conditions of an aqueous solution of an inorganic base and a phase transfer catalyst.
将所述缩合反应得到的愈创木酚缩水甘油醚粗品用低级醇重结晶得 到愈创木酚缩水甘油醚。  The crude guaiacol glycidyl ether obtained by the condensation reaction was recrystallized from a lower alcohol to obtain guaiacol glycidyl ether.
2、 如权利要求 1所述的方法, 其特征在于, 所述无机碱的水溶液为 为氢氧化钠水溶液、 氢氧化钾水溶液或碳酸钠水溶液。  The method according to claim 1, wherein the aqueous solution of the inorganic base is an aqueous sodium hydroxide solution, an aqueous potassium hydroxide solution or an aqueous sodium carbonate solution.
3、 根据权利要求 2所述的方法, 其特征在于, 所述无机碱的水溶液 为氢氧化钠水溶液或者氢氧化钾水溶液。  The method according to claim 2, wherein the aqueous solution of the inorganic base is an aqueous sodium hydroxide solution or an aqueous potassium hydroxide solution.
4、 如权利要求 2所述的方法, 其特征在于, 所述无机碱的水溶液的 浓度为 10wt% ~ 50wt%o 4. The method as claimed in claim 2, wherein the concentration of the inorganic alkali aqueous solution is 10wt% ~ 50wt% o
5、 如权利要求 1所述的方法, 其特征在于, 所述相转移催化剂为四 丁基溴化铵、 苄基三乙基氯化铵、 四丁基硫酸氢铵、 四丁基氯化铵中的 一种或多种。  5. The method according to claim 1, wherein the phase transfer catalyst is tetrabutylammonium bromide, benzyltriethylammonium chloride, tetrabutylammonium hydrogen sulfate, tetrabutylammonium chloride. One or more of them.
6、 如权利要求 1所述的方法, 其特征在于, 所述低级醇为曱醇、 乙 醇、 正丙醇、 异丙醇或丁醇中的一种或多种。  6. The method according to claim 1, wherein the lower alcohol is one or more of decyl alcohol, ethanol, n-propanol, isopropanol or butanol.
7、 如权利要求 6所述的方法, 其特征在于, 将所述愈创木酚缩水甘 油粗品用低级醇重结晶时低级醇的用量为按照每克愈创木酚缩水甘油醚 粗品计为 lml ~ 10ml。  7. The method according to claim 6, wherein the crude guaiacol glycidol is recrystallized from a lower alcohol, and the lower alcohol is used in an amount of 1 ml per gram of guaiacol glycidyl ether. ~ 10ml.
8、 根据权利要求 7所述的方法, 其特征在于, 将所述将所述愈创木 酚缩水甘油粗品用低级醇重结晶时低级醇的用量为按照每克愈创木酚缩 水甘油醚粗品计为 2ml ~ 5ml。  8. The method according to claim 7, wherein the amount of the lower alcohol in the crude guaiacol glycidol is recrystallized from the lower alcohol is in accordance with the crude product of guaiacol glycidyl ether per gram. Calculated as 2ml ~ 5ml.
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