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CN116396163A - A kind of method of solid acid catalyst one-step catalytic synthesis (R)-3-hydroxybutyric acid oligomer - Google Patents

A kind of method of solid acid catalyst one-step catalytic synthesis (R)-3-hydroxybutyric acid oligomer Download PDF

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CN116396163A
CN116396163A CN202310321782.8A CN202310321782A CN116396163A CN 116396163 A CN116396163 A CN 116396163A CN 202310321782 A CN202310321782 A CN 202310321782A CN 116396163 A CN116396163 A CN 116396163A
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solid
acid catalyst
hydroxybutyric acid
hydroxybutyrate
solid acid
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CN116396163B (en
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康世民
徐勇军
黄子稚
王俊涛
吴堉
何伟鑫
庄石炫
侯秋凤
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Dongguan New Energy Research Institute
Dongguan University of Technology
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Dongguan University of Technology
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    • C07C67/00Preparation of carboxylic acid esters
    • C07C67/03Preparation of carboxylic acid esters by reacting an ester group with a hydroxy group
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Abstract

The invention belongs to the technical field of chiral chemical R-3-hydroxybutyrate utilization, and relates to a method for synthesizing (R) -3-hydroxybutyrate oligomer by one-step catalysis by using a solid acid catalyst. The method comprises the following steps: stirring (R) -3-hydroxybutyrate, a solid acid catalyst and ultrapure water in an open mode under the flowing air condition and hydrolyzing until insoluble substances begin to appear in the aqueous solution, carrying out solid-liquid separation after the reaction is finished, and carrying out vacuum drying on a liquid product to obtain a water-soluble (R) -3-hydroxybutyrate oligomer; and (3) filtering and separating the solid after cleaning to recycle the solid as a solid acid catalyst. The invention solves the technical problems of multiple process steps, complicated conditions and high energy consumption in the synthesis process of the (R) -3-hydroxybutyric acid oligomer in the prior art, and the catalyst can be reused in the reaction process, and has the advantages of simple process, convenient operation, environmental protection and industrial application value.

Description

一种固体酸催化剂一步催化合成(R)-3-羟基丁酸低聚物的 方法One-step catalytic synthesis of (R)-3-hydroxybutyric acid oligomers by a solid acid catalyst method

技术领域technical field

本发明属于手性化学品R-3-羟基丁酸酯利用技术领域,涉及一种固体酸催化剂一步催化合成(R)-3-羟基丁酸低聚物的方法。The invention belongs to the technical field of utilization of chiral chemical R-3-hydroxybutyrate, and relates to a method for one-step catalytic synthesis of (R)-3-hydroxybutyric acid oligomers by a solid acid catalyst.

背景技术Background technique

(R)-3-羟基丁酸是绿色可再生聚3-羟基丁酸(PHB)的结构单体,可以通过PHB酸催化水解而获得。(R)-3-羟基丁酸是人体内一种重要的酮体,其可以为大脑提供燃料和被骨骼肌和心肌使用。目前,(R)-3-羟基丁酸已经被研究用于运动员、军人等紧急进入极端生理状态的特殊人员使用。此外,(R)-3-羟基丁酸也被认为是一种有益健康的固体饮料(如生酮减肥药),具有广泛的市场。然而,(R)-3-羟基丁酸在直接应用过程中是具有一定的局限性的,主要是包括两个方面,一是(R)-3-羟基丁酸是一种有机酸,因此人体在摄取过程中所提供的β-羟基丁酸的量和浓度是有限的;二是(R)-3-羟基丁酸稳定性较差、不易保存,在常温储存条件下容易分解产物有害物质巴豆酸。为了解决酸度和稳定性等问题,一些公司开发了(R)-3-羟基丁酸盐类化合物产品(如成钠,镁,钙和钾盐)。这些(R)-3-羟基丁酸盐又引起了一些其它问题,如金属离子超负荷的潜在危险。此外,(R)-3-羟基丁酸及其盐在人体内的吸收代谢过快,在人体内很难长期保持较高的浓度,起效时间过短。(R)-3-Hydroxybutyric acid is the structural monomer of green renewable poly-3-hydroxybutyric acid (PHB), which can be obtained by acid-catalyzed hydrolysis of PHB. (R)-3-Hydroxybutyrate is an important ketone body in the body that fuels the brain and is used by skeletal and cardiac muscles. At present, (R)-3-hydroxybutyric acid has been researched and used by special personnel such as athletes and soldiers who enter extreme physiological states in an emergency. In addition, (R)-3-hydroxybutyric acid is also considered as a healthy solid drink (such as ketogenic diet pills), which has a wide market. However, (R)-3-hydroxybutyric acid has certain limitations in the direct application process, mainly including two aspects, one is (R)-3-hydroxybutyric acid is an organic acid, so the human body The amount and concentration of β-hydroxybutyric acid provided during the intake process is limited; the second is that (R)-3-hydroxybutyric acid has poor stability and is not easy to store, and it is easy to decompose the harmful substance croton under normal temperature storage conditions acid. In order to solve problems such as acidity and stability, some companies have developed (R)-3-hydroxybutyrate products (such as sodium, magnesium, calcium and potassium salts). These (R)-3-hydroxybutyrates raise some other problems, such as the potential danger of metal ion overload. In addition, the absorption and metabolism of (R)-3-hydroxybutyric acid and its salts in the human body is too fast, it is difficult to maintain a high concentration in the human body for a long time, and the onset time is too short.

专利CN110776425A和多个学术研究成果都公开了(R)-3-羟基丁酸低聚物既可以延长作用时间起到缓释的效果,又可以降低酸中毒和金属离子超负荷的风险。为此,(R)-3-羟基丁酸低聚物有潜力成为一种具有较高安全性、低副作用以及较长时间作用效果的优质酮体。专利CN110776425A同时公开了(R)-3-羟基丁酸低聚物的合成方法,以PHB醇解所得(R)-3-羟基丁酸酯为原料,(R)-3-羟基丁酸酯催化水解后得到(R)-3-羟基丁酸[优选碱催化(如氢氧化钠),该均相碱催化过程存在环境污染风险,且需要酸化、萃取、蒸馏等后处理操作],然后(R)-3-羟基丁酸在复杂条件[较高温度(100~150℃)、惰性气体保护、负压(0.001~0.05Mpa)条件]聚合得到(R)-3-羟基丁酸低聚物。该专利工艺过程涉及两步独立反应,工艺步骤多、条件繁缛且能耗高。与(R)-3-羟基丁酸低聚物类似,水溶性(R)-3-羟基丁酸聚合物理论上也可以克服(R)-3-羟基丁酸的酸度问题和不稳定性问题,以及克服(R)-3-羟基丁酸盐类化合物的高盐含量问题。因此,开发绿色新技术,通过简单反应工艺把(R)-3-羟基丁酸酯转化为水溶性R-3-羟基丁酸低聚物具有重要意义。Patent CN110776425A and several academic research results have disclosed that (R)-3-hydroxybutyric acid oligomer can not only prolong the action time to achieve the effect of sustained release, but also reduce the risk of acidosis and metal ion overload. For this reason, (R)-3-hydroxybutyric acid oligomer has the potential to become a high-quality ketone body with high safety, low side effects and long-term effect. Patent CN110776425A discloses the synthetic method of (R)-3-hydroxybutyric acid oligomer at the same time, with (R)-3-hydroxybutyrate obtained by PHB alcoholysis as raw material, (R)-3-hydroxybutyrate catalyzes After hydrolysis, obtain (R)-3-hydroxybutyric acid [preferred base catalysis (such as sodium hydroxide), the homogeneous base catalysis process has environmental pollution risks, and requires post-treatment operations such as acidification, extraction, distillation], and then (R )-3-hydroxybutyric acid is polymerized under complex conditions [higher temperature (100~150°C), inert gas protection, negative pressure (0.001~0.05Mpa) conditions] to obtain (R)-3-hydroxybutyric acid oligomers. The patented process involves two independent reactions, with many process steps, complicated conditions and high energy consumption. Similar to (R)-3-hydroxybutyric acid oligomers, water-soluble (R)-3-hydroxybutyric acid polymers can also theoretically overcome the acidity and instability problems of (R)-3-hydroxybutyric acid , and overcome the problem of high salt content of (R)-3-hydroxybutyrate compounds. Therefore, it is of great significance to develop a new green technology to convert (R)-3-hydroxybutyrate into water-soluble R-3-hydroxybutyrate oligomers through a simple reaction process.

发明内容Contents of the invention

针对现有技术中(R)-3-羟基丁酸聚合物合成过程中工艺步骤多、条件繁琐且能耗高的技术问题,本发明提出一种固体酸催化剂一步催化合成(R)-3-羟基丁酸低聚物的方法。在该反应过程中,催化剂可以重复利用,并且催化过程工艺简单、操作方便且绿色环保,具有工业化应用价值。Aiming at the technical problems of many process steps, complicated conditions and high energy consumption in the synthesis process of (R)-3-hydroxybutyric acid polymer in the prior art, the present invention proposes a solid acid catalyst to catalyze the synthesis of (R)-3- A method for hydroxybutyric acid oligomers. In the reaction process, the catalyst can be reused, and the catalytic process is simple, convenient to operate and environmentally friendly, and has industrial application value.

为了达到上述目的,本发明的技术方案是这样实现的:In order to achieve the above object, the technical solution of the present invention is achieved in that:

一种固体酸催化剂一步催化合成(R)-3-羟基丁酸低聚物的方法,将(R)-3-羟基丁酸酯、固体酸催化剂和超纯水加入到敞口瓶中,敞口瓶放置在流动空气条件中,以加快副产物甲醇和水的蒸发。打开机械搅拌,然后在65~100℃水解,直至水溶液中开始出现不溶物。把反应产物进行固液分离,回收得到固体酸催化剂和液体产物。把液体产物进行真空干燥,得到水溶性(R)-3-羟基丁酸低聚物。回收所得固体酸催化剂用超纯水清洗后抽滤分离重新使用。A kind of solid acid catalyst one-step catalytic synthesis method of (R)-3-hydroxybutyric acid oligomer, (R)-3-hydroxybutyrate, solid acid catalyst and ultrapure water are added in open bottle, open The mouth bottle is placed in flowing air conditions to accelerate the evaporation of by-product methanol and water. Turn on mechanical stirring, then hydrolyze at 65~100°C until insoluble matter begins to appear in the aqueous solution. The reaction product is subjected to solid-liquid separation, and a solid acid catalyst and a liquid product are recovered. The liquid product was vacuum-dried to obtain a water-soluble (R)-3-hydroxybutyric acid oligomer. The recovered solid acid catalyst was washed with ultrapure water, separated by suction filtration and reused.

本发明所用的(R)-3-羟基丁酸酯主要是(R)-3-羟基丁酸甲酯和(R)-3-羟基丁酸乙酯。The (R)-3-hydroxybutyrate used in the present invention is mainly (R)-3-hydroxybutyrate methyl and (R)-3-hydroxybutyrate ethyl.

本发明所用催化剂为在100℃以下水溶液中具有良好稳定性的强酸性固体颗粒催化剂,包括Amberlyst-36,Amberlyst-315,Nafion® NR50,HND-34固体超强酸催化剂等。The catalyst used in the present invention is a strongly acidic solid particle catalyst with good stability in aqueous solution below 100°C, including Amberlyst-36, Amberlyst-315, Nafion® NR50, HND-34 solid superacid catalyst, etc.

本发明所述(R)-3-羟基丁酸酯与固体酸催化剂的质量比为(1~2):1。The mass ratio of (R)-3-hydroxybutyrate in the present invention to the solid acid catalyst is (1~2):1.

本发明所述每1~2 g (R)-3-羟基丁酸酯需要加入2~20 mL超纯水。According to the present invention, 2-20 mL of ultrapure water needs to be added for every 1-2 g of (R)-3-hydroxybutyrate.

本发明所开发的固体酸催化剂一步催化合成(R)-3-羟基丁酸低聚物的方法,可以实现把(R)-3-羟基丁酸酯在敞口反应器中一步转化为水溶性(R)-3-羟基丁酸低聚物。在该反应器中,可能的原理涉及了两个水解平衡反应。一是(R)-3-羟基丁酸酯[(R)-3-羟基丁酸甲酯或(R)-3-羟基丁酸乙酯]在固体酸催化作用下水解生成(R)-3-羟基丁酸和醇(甲醇或乙醇),所生成的甲醇或乙醇在加热条件下通过蒸馏从而从反应器中移除,从而促进(R)-3-羟基丁酸酯的水解和(R)-3-羟基丁酸的生成。二是所生成的(R)-3-羟基丁酸又在固体酸催化作用下发生分子间(一分子(R)-3-羟基丁酸的羟基和另一分子(R)-3-羟基丁酸的羧基)的催化酯化反应,最终生成(R)-3-羟基丁酸低聚物。随着反应的进行,溶剂水通过蒸馏从而从反应器中移除,进一步促进(R)-3-羟基丁酸低聚物的生成。当有不溶物开始出现时,立即停止反应,以避免生成水不溶高聚合物,降低原料(R)-3-羟基丁酸酯的利用效率。The solid acid catalyst developed by the present invention catalyzes the method for synthesizing (R)-3-hydroxybutyric acid oligomers in one step, which can realize the one-step conversion of (R)-3-hydroxybutyrate into water-soluble (R)-3-Hydroxybutyric acid oligomer. In this reactor, a possible mechanism involves two hydrolytic equilibrium reactions. One is (R)-3-hydroxybutyrate [(R)-3-hydroxybutyrate methyl ester or (R)-3-hydroxybutyrate ethyl ester] is hydrolyzed under solid acid catalysis to generate (R)-3 -Hydroxybutyric acid and alcohol (methanol or ethanol), the resulting methanol or ethanol is removed from the reactor by distillation under heated conditions, thereby promoting the hydrolysis of (R)-3-hydroxybutyrate and (R) - Generation of 3-hydroxybutyric acid. The second is that the generated (R)-3-hydroxybutyric acid undergoes intermolecular (the hydroxyl group of one molecule (R)-3-hydroxybutyric acid and the other molecule (R)-3-hydroxybutyric acid) under the catalysis of solid acid. The catalyzed esterification reaction of the carboxyl group of the acid) finally generates (R)-3-hydroxybutyric acid oligomers. As the reaction progressed, solvent water was removed from the reactor by distillation, further promoting the formation of (R)-3-hydroxybutyric acid oligomers. When insoluble matter begins to appear, stop reaction immediately, in order to avoid generating water-insoluble high polymer, reduce the utilization efficiency of raw material (R)-3-hydroxybutyrate.

为此,促成本发明技术良好效果的关键因素有三个:For this reason, the key factor that promotes the good effect of the technology of the present invention has three:

(1)是反应过程中反应器不是密闭的,水解生成的醇以及反应溶剂水可以通过蒸发移除,从而促进了(R)-3-羟基丁酸酯水解生成(R)-3-羟基丁酸、以及(R)-3-羟基丁酸进一步发生低聚反应生成(R)-3-羟基丁酸低聚物。(1) The reactor is not airtight during the reaction, and the alcohol generated by hydrolysis and the reaction solvent water can be removed by evaporation, thereby promoting the hydrolysis of (R)-3-hydroxybutyrate to generate (R)-3-hydroxybutyrate Acid and (R)-3-hydroxybutyric acid further oligomerize to generate (R)-3-hydroxybutyric acid oligomers.

(2)是该反应过程中采用了颗粒状固体酸催化剂,该固体酸催化剂不会因反应过程中溶剂水的蒸发减少而使其催化性能发生太大变化,且颗粒状固体酸催化剂在反应结束后很容易和产物分离,大大简化了(R)-3-羟基丁酸低聚物产物的后处理工艺以及实现催化剂的重复利用;此外,强酸性固体酸催化剂有利于降低(R)-3-羟基丁酸聚合反应温度,实现了在温和温度下生成(R)-3-羟基丁酸低聚物,从而有利于降低能耗以及避免了(R)-3-羟基丁酸可能的高温氧化,为此在反应过程中无需通入惰性气体保护。(2) The granular solid acid catalyst is used in the reaction process, and the catalytic performance of the solid acid catalyst will not change too much due to the reduction of solvent water evaporation during the reaction process, and the granular solid acid catalyst will not change much after the reaction ends. Afterwards, it is easy to separate from the product, which greatly simplifies the post-treatment process of (R)-3-hydroxybutyric acid oligomer product and realizes the reuse of the catalyst; in addition, the strong acidic solid acid catalyst is conducive to reducing the (R)-3- The polymerization reaction temperature of hydroxybutyric acid realizes the generation of (R)-3-hydroxybutyric acid oligomers at a mild temperature, which is beneficial to reduce energy consumption and avoid possible high-temperature oxidation of (R)-3-hydroxybutyric acid. For this reason, no inert gas protection is required during the reaction.

(3)控制反应时间,当水溶液中开始出现不溶物时,立即停止反应,以保障反应所得的聚合物属于水溶性的。(3) Control the reaction time. When insoluble matter begins to appear in the aqueous solution, stop the reaction immediately to ensure that the polymer obtained from the reaction is water-soluble.

本发明具有以下有益效果:The present invention has the following beneficial effects:

本发明提供了一种固体酸催化剂一步催化合成(R)-3-羟基丁酸低聚物的方法。该过程采用简单的带敞口反应装置,反应温度温和(65~100℃),无需惰性气体保护条件;所得聚合物具有水溶性,有利于产品应用于制备水剂产品(如作为固体饮料);采用了固体酸催化剂,促进了反应的进行且容易回收和重复利用。很明显,本发明技术工艺简单、操作方便、能耗低,且整个过程绿色环保,具有广阔的工业化应用前景。The invention provides a method for one-step catalytic synthesis of (R)-3-hydroxybutyric acid oligomers by a solid acid catalyst. The process adopts a simple reaction device with an open door, the reaction temperature is mild (65~100°C), and no inert gas protection conditions are required; the obtained polymer is water-soluble, which is conducive to the application of the product in the preparation of water-based products (such as solid beverages); The solid acid catalyst is adopted, which promotes the reaction and is easy to recycle and reuse. Obviously, the technical process of the present invention is simple, convenient to operate, low in energy consumption, and the whole process is green and environment-friendly, and has broad industrial application prospects.

附图说明Description of drawings

为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the technical solutions in the embodiments of the present invention or the prior art, the following will briefly introduce the drawings that need to be used in the description of the embodiments or the prior art. Obviously, the accompanying drawings in the following description are only These are some embodiments of the present invention. Those skilled in the art can also obtain other drawings based on these drawings without creative work.

图1为本发明实施例1过程步骤示意图。Fig. 1 is a schematic diagram of process steps in Embodiment 1 of the present invention.

图2为本发明实施例1所得白色固体实物图。Fig. 2 is the actual picture of the white solid obtained in Example 1 of the present invention.

图3为本发明实施例1所得白色固体质谱分析。Fig. 3 is the mass spectrum analysis of the white solid obtained in Example 1 of the present invention.

图4为本发明实施例1中白色固体醇解产物GC-MS分析图。Fig. 4 is a GC-MS analysis diagram of the white solid alcoholysis product in Example 1 of the present invention.

具体实施方式Detailed ways

下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有付出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The following will clearly and completely describe the technical solutions in the embodiments of the present invention with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only some, not all, embodiments of the present invention. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the protection scope of the present invention.

实施例1Example 1

本实施例为一种固体酸催化合成水溶性(R)-3-羟基丁酸低聚物的方法,步骤如下(示意图见图1):This example is a solid acid-catalyzed method for synthesizing water-soluble (R)-3-hydroxybutyric acid oligomers. The steps are as follows (see Figure 1 for the schematic diagram):

(1)取20g R-3-羟基丁酸甲酯,10g Nafion®NR50固体酸催化剂和100mL水加入到250mL带有机械搅拌的敞口烧杯中。敞口烧杯放置在通风柜中,且通风柜处于抽风状态以加快挥发反应过程中产生的甲醇和水蒸气。打开机械搅拌300rpm,并把敞口烧杯加热到75℃,然后在该温度下反应直至有不溶物开始出现,立即停止反应。在该反应过程中,R-3-羟基丁酸甲酯在Nafion®NR50固体酸催化剂催化作用下水解生成R-3-羟基丁酸和甲醇,所生成的甲醇(沸点64.7℃)在加热条件(反应温度75℃)下首先被蒸发移除,从而加快R-3-羟基丁酸甲酯水解生成R-3-羟基丁酸。在通风柜抽风状态下,敞口烧杯中的水也逐渐蒸发,形成高浓度的R-3-羟基丁酸,从而促进R-3-羟基丁酸在固体酸催化剂催化作用下聚合生成R-3-羟基丁酸低聚物。(1) Take 20g of methyl R-3-hydroxybutyrate, 10g of Nafion®NR50 solid acid catalyst and 100mL of water into a 250mL open beaker with mechanical stirring. The open beaker was placed in a fume hood, and the fume hood was in a draft state to speed up the methanol and water vapor generated during the volatilization reaction. Turn on the mechanical stirring at 300rpm, and heat the open beaker to 75°C, then react at this temperature until insoluble matter begins to appear, and stop the reaction immediately. During the reaction process, methyl R-3-hydroxybutyrate is hydrolyzed under the catalysis of Nafion®NR50 solid acid catalyst to generate R-3-hydroxybutyric acid and methanol, and the generated methanol (boiling point 64.7°C) is heated under ( At the reaction temperature of 75°C), it is first evaporated and removed, thereby accelerating the hydrolysis of R-3-hydroxybutyric acid methyl ester to generate R-3-hydroxybutyric acid. Under the exhaust state of the fume hood, the water in the open beaker also gradually evaporates to form a high concentration of R-3-hydroxybutyric acid, thereby promoting the polymerization of R-3-hydroxybutyric acid under the catalysis of a solid acid catalyst to form R-3 -Hydroxybutyric acid oligomers.

(2)把步骤(1)所得产物通过固液分离回收,得到Nafion®NR50固体酸催化剂和液体产物,其中Nafion®NR50固体酸催化剂通过水洗后可重复使用。把液体产物放入真空干燥箱,在50℃进行干燥,得到白色固体(见图2)。该白色固体易溶于水,是一种水溶性聚合物;同时也说明该固体聚合度不高(因为高聚合度的聚-3-羟基丁酸酯不溶于水)。把该白色固体溶解于乙醇中做质谱分析,发现了分子离子峰为258(见图3),该分子离子峰恰好是3个R-3-羟基丁酸(分子量104)发生分子间两两脱水(总共脱掉3个水,水分子量为18)聚合的数值(104*3-18*3=258),进一步验证了该白色固体为(R)-3-羟基丁酸低聚物。取0.5g该白色固体和5mL 2%硫酸甲醇溶液放入消解管中进行醇解反应(100℃反应1h),经GC-MS分析(见图4),主要产物为R-3-羟基丁酸甲酯,说明该固体又可以重新水解为R-3-羟基丁酸甲酯,进一步证明了该固体产物为水溶性R-3-羟基丁酸低聚物。(2) The product obtained in step (1) is recovered by solid-liquid separation to obtain Nafion®NR50 solid acid catalyst and liquid product, wherein Nafion®NR50 solid acid catalyst can be reused after being washed with water. The liquid product was put into a vacuum drying oven and dried at 50°C to obtain a white solid (see Figure 2). The white solid is easily soluble in water and is a water-soluble polymer; it also indicates that the degree of polymerization of the solid is not high (because poly-3-hydroxybutyrate with a high degree of polymerization is insoluble in water). The white solid was dissolved in ethanol for mass spectrometry analysis, and the molecular ion peak was found to be 258 (see Figure 3), which happened to be the intermolecular dehydration of three R-3-hydroxybutyric acid (molecular weight 104) (A total of 3 waters were removed, and the molecular weight of water was 18) The value of polymerization (104*3-18*3=258) further verified that the white solid was (R)-3-hydroxybutyric acid oligomer. Take 0.5g of the white solid and 5mL of 2% methanolic sulfuric acid solution into a digestion tube for alcoholysis reaction (reaction at 100°C for 1h). After GC-MS analysis (see Figure 4), the main product is R-3-hydroxybutyric acid methyl ester, indicating that the solid can be re-hydrolyzed into R-3-hydroxybutyrate methyl ester, further proving that the solid product is a water-soluble R-3-hydroxybutyrate oligomer.

实施例2Example 2

本实施例为一种固体酸催化合成水溶性(R)-3-羟基丁酸低聚物的方法,步骤如下:This embodiment is a method for solid acid catalyzed synthesis of water-soluble (R)-3-hydroxybutyric acid oligomers, the steps are as follows:

取50g R-3-羟基丁酸甲酯,25g Amberlyst-36固体酸催化剂和100mL水加入到250mL带有机械搅拌的敞口烧杯中。敞口烧杯放置在通风柜中,且通风柜处于抽风状态以加快挥发反应过程中产生的甲醇和水蒸气。打开机械搅拌300rpm,并把敞口烧杯加热到65℃,然后在该温度下反应直至有不溶物开始出现,立即停止反应。把所得产物通过固液分离回收得到 Amberlyst-36固体酸催化剂和液体产物,其中Amberlyst-36固体酸催化剂通过水洗后可重复使用。把液体产物放入真空干燥箱在50℃进行干燥,得到水溶性R-3-羟基丁酸低聚物。Take 50g of methyl R-3-hydroxybutyrate, 25g of Amberlyst-36 solid acid catalyst and 100mL of water into a 250mL open beaker with mechanical stirring. The open beaker was placed in a fume hood, and the fume hood was in a draft state to speed up the methanol and water vapor generated during the volatilization reaction. Turn on the mechanical stirring at 300rpm, and heat the open beaker to 65°C, then react at this temperature until insoluble matter begins to appear, and stop the reaction immediately. The resulting product is recovered through solid-liquid separation to obtain Amberlyst-36 solid acid catalyst and liquid product, wherein the Amberlyst-36 solid acid catalyst can be reused after being washed with water. Put the liquid product into a vacuum drying oven to dry at 50° C. to obtain a water-soluble R-3-hydroxybutyric acid oligomer.

实施例3Example 3

本实施例为一种固体酸催化合成水溶性(R)-3-羟基丁酸低聚物的方法,步骤如下:This embodiment is a method for solid acid catalyzed synthesis of water-soluble (R)-3-hydroxybutyric acid oligomers, the steps are as follows:

取10g R-3-羟基丁酸甲酯,5g Nafion®NR50固体酸催化剂和100mL水加入到250mL带有机械搅拌的敞口烧杯中。敞口烧杯放置在通风柜中,且通风柜处于抽风状态以加快反应过程中产生的甲醇和水蒸气。打开机械搅拌300rpm,并把敞口烧杯加热到100℃,然后在该温度下反应直至有不溶物开始出现,立即停止反应。把所得产物通过固液分离回收得到Nafion®NR50固体酸催化剂和液体产物,其中Nafion®NR50固体酸催化剂通过水洗后可重复使用。把液体产物放入真空干燥箱在50℃进行干燥,得到水溶性R-3-羟基丁酸低聚物。Take 10g of methyl R-3-hydroxybutyrate, 5g of Nafion®NR50 solid acid catalyst and 100mL of water into a 250mL open beaker with mechanical stirring. The open beaker was placed in a fume hood, and the fume hood was in a draft state to accelerate the methanol and water vapor generated during the reaction. Turn on the mechanical stirring at 300rpm, and heat the open beaker to 100°C, then react at this temperature until insoluble matter begins to appear, and stop the reaction immediately. The obtained product is recovered by solid-liquid separation to obtain Nafion®NR50 solid acid catalyst and liquid product, wherein Nafion®NR50 solid acid catalyst can be reused after being washed with water. Put the liquid product into a vacuum drying oven to dry at 50° C. to obtain a water-soluble R-3-hydroxybutyric acid oligomer.

实施例4Example 4

本实施例为一种固体酸催化合成水溶性(R)-3-羟基丁酸低聚物的方法,步骤如下:This embodiment is a method for solid acid catalyzed synthesis of water-soluble (R)-3-hydroxybutyric acid oligomers, the steps are as follows:

取50g R-3-羟基丁酸甲酯,25g Amberlyst-15固体酸催化剂和100mL水加入到250mL带有机械搅拌的敞口烧杯中。敞口烧杯放置在通风柜中,且通风柜处于抽风状态以加快挥发反应过程中产生的甲醇和水蒸气。打开机械搅拌300rpm,并把敞口烧杯加热到80℃,然后在该温度下反应直至有不溶物开始出现,立即停止反应。把所得产物通过固液分离回收得到 Amberlyst-36固体酸催化剂和液体产物,其中Amberlyst-36固体酸催化剂通过水洗后可重复使用。把液体产物放入真空干燥箱进行干燥,得到水溶性R-3-羟基丁酸低聚物。Take 50g of methyl R-3-hydroxybutyrate, 25g of Amberlyst-15 solid acid catalyst and 100mL of water and add it to a 250mL open beaker with mechanical stirring. The open beaker was placed in a fume hood, and the fume hood was in a draft state to speed up the methanol and water vapor generated during the volatilization reaction. Turn on the mechanical stirring at 300rpm, and heat the open beaker to 80°C, then react at this temperature until insoluble matter begins to appear, and stop the reaction immediately. The resulting product is recovered through solid-liquid separation to obtain Amberlyst-36 solid acid catalyst and liquid product, wherein the Amberlyst-36 solid acid catalyst can be reused after being washed with water. The liquid product is put into a vacuum drying oven for drying to obtain a water-soluble R-3-hydroxybutyric acid oligomer.

实施例5Example 5

本实施例为一种固体酸催化合成水溶性(R)-3-羟基丁酸低聚物的方法,步骤如下:This embodiment is a method for solid acid catalyzed synthesis of water-soluble (R)-3-hydroxybutyric acid oligomers, the steps are as follows:

取50g R-3-羟基丁酸甲酯,50g HND-34固体超强酸催化剂和100mL水加入到250mL带有机械搅拌的敞口烧杯中。敞口烧杯放置在通风柜中,且通风柜处于抽风状态以加快挥发反应过程中产生的甲醇和水蒸气。打开机械搅拌300rpm,并把敞口烧杯加热到90℃,然后在该温度下反应直至有不溶物开始出现,立即停止反应。把所得产物通过固液分离回收得到 HND-34固体超强酸催化剂和液体产物,其中HND-34固体超强酸催化剂通过水洗后可重复使用。把液体产物,放入真空干燥箱进行干燥,得到水溶性R-3-羟基丁酸低聚物。Take 50g R-3-hydroxybutyrate methyl ester, 50g HND-34 solid superacid catalyst and 100mL water and join in a 250mL open beaker with mechanical stirring. The open beaker was placed in a fume hood, and the fume hood was in a draft state to speed up the methanol and water vapor generated during the volatilization reaction. Turn on the mechanical stirring at 300rpm, and heat the open beaker to 90°C, then react at this temperature until insoluble matter begins to appear, and stop the reaction immediately. The resulting product is recovered by solid-liquid separation to obtain HND-34 solid superacid catalyst and liquid product, wherein the HND-34 solid superacid catalyst can be reused after being washed with water. The liquid product is put into a vacuum drying oven for drying to obtain a water-soluble R-3-hydroxybutyric acid oligomer.

以上所述仅为本发明的较佳实施例而已,并不用以限制本发明,凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。The above descriptions are only preferred embodiments of the present invention, and are not intended to limit the present invention. Any modifications, equivalent replacements, improvements, etc. made within the spirit and principles of the present invention shall be included in the scope of the present invention. within the scope of protection.

Claims (7)

1.一种固体酸催化剂一步催化合成(R)-3-羟基丁酸低聚物的方法,其特征在于:在流动空气条件下,将(R)-3-羟基丁酸酯、固体酸催化剂和超纯水敞口搅拌并水解,直至水溶液中开始出现不溶物,反应结束后进行固液分离,将液体产物干燥,得到水溶性(R)-3-羟基丁酸低聚物;将固体清洗后抽滤分离作为固体酸催化剂回收利用。1. a method for solid acid catalyst one-step catalytic synthesis of (R)-3-hydroxybutyric acid oligomers, characterized in that: under flowing air conditions, (R)-3-hydroxybutyrate, solid acid catalyst Stir openly with ultrapure water and hydrolyze until insoluble matter begins to appear in the aqueous solution. After the reaction, separate the solid from the liquid and dry the liquid product to obtain water-soluble (R)-3-hydroxybutyric acid oligomers; wash the solid After that, it is separated by suction filtration and recycled as a solid acid catalyst. 2.根据权利要求1所述的固体酸催化剂一步催化合成(R)-3-羟基丁酸低聚物的方法,其特征在于:所述(R)-3-羟基丁酸酯包括(R)-3-羟基丁酸甲酯或(R)-3-羟基丁酸乙酯。2. the method for one-step catalytic synthesis of (R)-3-hydroxybutyric acid oligomer by solid acid catalyst according to claim 1, is characterized in that: described (R)-3-hydroxybutyrate comprises (R) -methyl 3-hydroxybutyrate or ethyl (R)-3-hydroxybutyrate. 3.根据权利要求1所述的固体酸催化剂一步催化合成(R)-3-羟基丁酸低聚物的方法,其特征在于:所述固体酸催化剂为在100℃以下水溶液中具有良好稳定性的强酸性固体颗粒催化剂。3. the method for one-step catalytic synthesis of (R)-3-hydroxybutyric acid oligomers by the solid acid catalyst according to claim 1, characterized in that: the solid acid catalyst has good stability in an aqueous solution below 100°C strongly acidic solid particle catalyst. 4. 根据权利要求3所述的固体酸催化剂一步催化合成(R)-3-羟基丁酸低聚物的方法,其特征在于:所述固体酸催化剂包括Amberlyst-36、Amberlyst-15、Nafion® NR50或HND-34固体超强酸催化剂中的任意一种。4. the method for one-step catalytic synthesis of solid acid catalyst according to claim 3 (R)-3-hydroxybutyric acid oligomer, is characterized in that: described solid acid catalyst comprises Amberlyst-36, Amberlyst-15, Nafion® Any one of NR50 or HND-34 solid superacid catalyst. 5.根据权利要求1-4任一项所述的固体酸催化剂一步催化合成(R)-3-羟基丁酸低聚物的方法,其特征在于:所述(R)-3-羟基丁酸酯与固体酸催化剂的质量比为(1~2):1。5. the method for one-step catalytic synthesis of (R)-3-hydroxybutyric acid oligomers according to the solid acid catalyst described in any one of claims 1-4, is characterized in that: described (R)-3-hydroxybutyric acid The mass ratio of ester to solid acid catalyst is (1~2):1. 6. 根据权利要求5所述的固体酸催化剂一步催化合成(R)-3-羟基丁酸低聚物的方法,其特征在于:所述每1~2 g (R)-3-羟基丁酸酯需要加入2~20 mL超纯水。6. the method for solid acid catalyst one-step catalytic synthesis (R)-3-hydroxybutyric acid oligomer according to claim 5, is characterized in that: described every 1~2 g (R)-3-hydroxybutyric acid Esters need to add 2~20 mL ultrapure water. 7.根据权利要求1-4或6任一项所述的固体酸催化剂一步催化合成(R)-3-羟基丁酸低聚物的方法,其特征在于:所述水解的温度为65~100℃。7. according to the method for one-step catalytic synthesis of (R)-3-hydroxybutyric acid oligomers of the solid acid catalyst described in any one of claim 1-4 or 6, it is characterized in that: the temperature of described hydrolysis is 65~100 ℃.
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CN110776425A (en) * 2019-10-23 2020-02-11 清华大学 A kind of preparation method of (R)-3-hydroxybutyric acid and oligomer thereof

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4365088A (en) * 1980-07-03 1982-12-21 Solvay & Cie Process for the manufacture of β-hydroxybutyric acid and its oligocondensates
EP0823448A1 (en) * 1996-02-23 1998-02-11 Kyowa Hakko Kogyo Co., Ltd. Process for the preparation of polyhydroxycarboxylic acid
JPH10204156A (en) * 1997-01-17 1998-08-04 Kyowa Yuka Kk Method for producing polyhydroxycarboxylic acid
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