[go: up one dir, main page]

CN116371467A - Preparation method and application of solid acid catalyst loaded with acidic ionic liquid - Google Patents

Preparation method and application of solid acid catalyst loaded with acidic ionic liquid Download PDF

Info

Publication number
CN116371467A
CN116371467A CN202310260062.5A CN202310260062A CN116371467A CN 116371467 A CN116371467 A CN 116371467A CN 202310260062 A CN202310260062 A CN 202310260062A CN 116371467 A CN116371467 A CN 116371467A
Authority
CN
China
Prior art keywords
ionic liquid
solid acid
acid catalyst
preparation
acidic ionic
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN202310260062.5A
Other languages
Chinese (zh)
Inventor
李忠涛
李涛
谢平
路文学
张志伟
钟天浩
邵毓霖
于英民
赵青山
杨晓娟
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Yankuang Coal Water Slurry Gasification And Coal Chemical Industry National Engineering Research Center Co ltd
China University of Petroleum East China
Original Assignee
Yankuang Coal Water Slurry Gasification And Coal Chemical Industry National Engineering Research Center Co ltd
China University of Petroleum East China
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Yankuang Coal Water Slurry Gasification And Coal Chemical Industry National Engineering Research Center Co ltd, China University of Petroleum East China filed Critical Yankuang Coal Water Slurry Gasification And Coal Chemical Industry National Engineering Research Center Co ltd
Priority to CN202310260062.5A priority Critical patent/CN116371467A/en
Publication of CN116371467A publication Critical patent/CN116371467A/en
Pending legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
    • B01J31/06Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing polymers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/02Sulfur, selenium or tellurium; Compounds thereof
    • B01J27/053Sulfates
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
    • B01J31/0277Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature
    • B01J31/0278Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature containing nitrogen as cationic centre
    • B01J31/0281Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature containing nitrogen as cationic centre the nitrogen being a ring member
    • B01J31/0282Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature containing nitrogen as cationic centre the nitrogen being a ring member of an aliphatic ring, e.g. morpholinium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
    • B01J31/0277Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature
    • B01J31/0278Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature containing nitrogen as cationic centre
    • B01J31/0285Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature containing nitrogen as cationic centre also containing elements or functional groups covered by B01J31/0201 - B01J31/0274
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00Preparation of carboxylic acid esters
    • C07C67/08Preparation of carboxylic acid esters by reacting carboxylic acids or symmetrical anhydrides with the hydroxy or O-metal group of organic compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2231/00Catalytic reactions performed with catalysts classified in B01J31/00
    • B01J2231/40Substitution reactions at carbon centres, e.g. C-C or C-X, i.e. carbon-hetero atom, cross-coupling, C-H activation or ring-opening reactions
    • B01J2231/49Esterification or transesterification
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/584Recycling of catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Catalysts (AREA)

Abstract

本发明公开了负载酸性离子液体的固体酸催化剂的制备方法及其应用,其将4‑羟基苯磺酸钠和甲醛混合,然后加入离子液体,在带有回流冷凝器的烧瓶中在回流条件下进行反应,反应结束后,冷却,加入水,回收沉淀,干燥、研磨、洗涤,得到负载离子液体的固体酸催化剂。使得催化剂稳定性和活性得到提升,并且经过简单的过滤就可以重复利用。

Figure 202310260062

The invention discloses a preparation method and an application thereof of a solid acid catalyst loaded with an acidic ionic liquid. It mixes sodium 4-hydroxybenzenesulfonate and formaldehyde, then adds the ionic liquid, and puts it in a flask with a reflux condenser under reflux conditions. The reaction is carried out, and after the reaction is completed, cooling is added, water is added, the precipitate is recovered, dried, ground and washed to obtain a solid acid catalyst loaded with ionic liquid. The stability and activity of the catalyst are improved, and it can be reused after simple filtration.

Figure 202310260062

Description

一种负载酸性离子液体的固体酸催化剂的制备方法及其应用Preparation method and application of a solid acid catalyst loaded with acidic ionic liquid

技术领域technical field

本发明属于催化剂制备技术领域,具体涉及一种负载酸性离子液体的固体酸催化剂的制备方法及其应用。The invention belongs to the technical field of catalyst preparation, and in particular relates to a preparation method and application of a solid acid catalyst loaded with acidic ionic liquid.

背景技术Background technique

酸醇的酯化反应力求使用最少量的均相酸性催化剂。学界在此方面的探索已取得一定的成果,但酯化反应仍然面临着使用更高效、简单、绿色催化剂的挑战。Esterification of acid alcohols strives to use the least amount of homogeneous acidic catalyst. The academic circles have achieved certain results in this aspect, but the esterification reaction still faces the challenge of using more efficient, simple and green catalysts.

近年来,在酯化反应中取代传统无机酸的新型绿色催化剂相继开发报道,其中引人注目的是酸性离子液体(IL)作为催化剂在酯化反应中的应用,随着反应的进行,酯产物能够和催化剂IL自动分层,推动平衡正向移动,酸性离子液体在催化酯化反应中已取得瞩目的成果,但催化剂以液态形式存在,要进行复杂的减压蒸馏才能回收,并且反应过程要求使用大量昂贵的离子液体,不符合最优经济原则。In recent years, new green catalysts that have replaced traditional inorganic acids in esterification reactions have been developed and reported one after another. Among them, the application of acidic ionic liquids (IL) as catalysts in esterification reactions has attracted attention. As the reaction progresses, the ester products It can automatically stratify with the catalyst IL and promote the positive shift of the equilibrium. The acidic ionic liquid has achieved remarkable results in the catalytic esterification reaction, but the catalyst exists in the form of a liquid, which can only be recovered by complex vacuum distillation, and the reaction process requires The use of large amounts of expensive ionic liquids is not in line with optimal economic principles.

发明内容Contents of the invention

本部分的目的在于概述本发明的实施例的一些方面以及简要介绍一些较佳实施例。在本部分以及本申请的说明书摘要和发明名称中可能会做些简化或省略以避免使本部分、说明书摘要和发明名称的目的模糊,而这种简化或省略不能用于限制本发明的范围。The purpose of this section is to outline some aspects of embodiments of the invention and briefly describe some preferred embodiments. Some simplifications or omissions may be made in this section, as well as in the abstract and titles of this application, to avoid obscuring the purpose of this section, abstract and titles, and such simplifications or omissions should not be used to limit the scope of the invention.

作为本发明其中一个方面,本发明提供一种负载酸性离子液体的固体酸催化剂的制备方法,其为:将交联聚乙烯基吡咯烷酮粉末放入甲苯中,加入1,3丙烷磺酸内酯。将混合物80℃加热回流条件下连续搅拌24小时。所得到的固体两性离子通过过滤回收,乙酸乙酯洗涤,然后真空干燥过夜,得到样品[PVPP-PS]。将制备的[PVPP-PS]在研钵中研磨分散到乙酸乙酯中,后加入硫酸搅拌24h,然后将混合物用乙醇过滤和洗涤三次,60℃真空干燥,得到最终产品[PVPP-PS]HSO4作为固体酸催化剂。As one aspect of the present invention, the present invention provides a preparation method of a solid acid catalyst loaded with an acidic ionic liquid, which comprises: putting crosslinked polyvinylpyrrolidone powder into toluene, and adding 1,3 propane sultone. The mixture was stirred continuously under reflux at 80°C for 24 hours. The resulting solid zwitterions were recovered by filtration, washed with ethyl acetate, and then vacuum dried overnight to obtain the sample [PVPP-PS]. Grind and disperse the prepared [PVPP-PS] into ethyl acetate in a mortar, add sulfuric acid and stir for 24 hours, then filter and wash the mixture three times with ethanol, and dry in vacuum at 60°C to obtain the final product [PVPP-PS]HSO 4 as a solid acid catalyst.

作为本发明所述的负载酸性离子液体的固体酸催化剂的制备方法,其特征在于:所述将交联聚乙烯基吡咯烷酮和1,3丙烷磺酸内酯混合,其中,交联聚乙烯基吡咯烷酮和1,3丙烷磺酸内酯的摩尔比为1:1。As the preparation method of the solid acid catalyst supporting acidic ionic liquid according to the present invention, it is characterized in that: the crosslinked polyvinylpyrrolidone and 1,3 propane sultone are mixed, wherein the crosslinked polyvinylpyrrolidone And the molar ratio of 1,3 propane sultone is 1:1.

作为本发明所述的负载酸性离子液体的固体酸催化剂的制备方法的一种优选方案:所述加入硫酸搅拌24h,其中,所述硫酸与样品[PVPP-PS]质量比为18:1。As a preferred solution of the preparation method of the acidic ionic liquid-loaded solid acid catalyst of the present invention: adding sulfuric acid and stirring for 24 hours, wherein the mass ratio of sulfuric acid to the sample [PVPP-PS] is 18:1.

作为本发明所述的负载酸性离子液体的固体酸催化剂的制备方法的一种优选方案:所述在回流条件下进行反应,其反应时间为24h。As a preferred solution of the preparation method of the acidic ionic liquid-loaded solid acid catalyst of the present invention: the reaction is carried out under reflux conditions, and the reaction time is 24 hours.

作为本发明所述的负载酸性离子液体的固体酸催化剂的制备方法的一种优选方案:所述洗涤,为用乙酸乙酯洗涤。As a preferred solution of the preparation method of the acidic ionic liquid-loaded solid acid catalyst of the present invention: the washing is washing with ethyl acetate.

作为本发明所述的负载酸性离子液体的固体酸催化剂的制备方法的一种优选方案:所述固体酸,其制备方法为:在氮气气氛下,将交联聚乙烯基吡咯烷酮粉末放入甲苯中,一段时间后,加入1,3丙烷磺酸内酯。将混合物加热到80℃,并在100mL的烧瓶中连续搅拌24小时。所得到的固体两性离子通过过滤回收,用乙酸乙酯洗涤,完全去除未反应的反应物,然后在60℃条件下真空干燥过夜,得到样品[PVPP-PS]。As a preferred version of the preparation method of the solid acid catalyst supporting acidic ionic liquid of the present invention: the solid acid, its preparation method is: under nitrogen atmosphere, put the cross-linked polyvinylpyrrolidone powder in toluene , After a while, add 1,3 propane sultone. The mixture was heated to 80 °C and stirred continuously for 24 hours in a 100 mL flask. The obtained solid zwitterions were recovered by filtration, washed with ethyl acetate to completely remove unreacted reactants, and then dried under vacuum at 60° C. overnight to obtain a sample [PVPP-PS].

作为本发明所述的负载酸性离子液体的固体酸催化剂的制备方法的一种优选方案:所述溶剂为乙酸乙酯。As a preferred solution of the preparation method of the acidic ionic liquid-loaded solid acid catalyst of the present invention: the solvent is ethyl acetate.

本发明的有益效果:本发明提供了一种负载

Figure BDA0004130931000000021
酸性离子液体H2SO4的固体酸催化剂及其制备方法。本发明制备的固体酸作为一种催化剂,可以催化乙酸和乙醇反应合成乙酸乙酯,具有较高的催化活性和稳定性。单独使用固体酸催化剂容易在反应中酸位点失活,从而造成反应活性下降,而负载/>
Figure BDA0004130931000000022
酸性离子液体的固体酸催化剂,固体酸包裹/>
Figure BDA0004130931000000023
酸性离子液体,使得催化剂稳定性和活性得到提升,负载/>
Figure BDA0004130931000000024
酸性离子液体后的催化剂催化性能比单纯的固体酸催化剂有着明显的提升,说明负载离子液体对提高催化性能有着促进作用。制备的催化剂其催化活性高,并且经过简单的过滤就可以重复利用。Beneficial effects of the present invention: the present invention provides a load
Figure BDA0004130931000000021
Solid acid catalyst of acidic ionic liquid H2SO4 and preparation method thereof. As a catalyst, the solid acid prepared by the invention can catalyze the reaction of acetic acid and ethanol to synthesize ethyl acetate, and has high catalytic activity and stability. Using a solid acid catalyst alone is easy to deactivate the acid site in the reaction, resulting in a decrease in reactivity, and the load/>
Figure BDA0004130931000000022
Solid acid catalyst of acidic ionic liquid, solid acid coating/>
Figure BDA0004130931000000023
Acidic ionic liquid, which improves the stability and activity of the catalyst, supports
Figure BDA0004130931000000024
The catalytic performance of the catalyst after the acidic ionic liquid is significantly improved compared with the pure solid acid catalyst, which shows that the supported ionic liquid can promote the improvement of the catalytic performance. The prepared catalyst has high catalytic activity and can be reused after simple filtration.

附图说明Description of drawings

为了更清楚地说明本发明实施例的技术方案,下面将对实施例描述中所需要使用的附图作简单地介绍。其中:In order to illustrate the technical solutions of the embodiments of the present invention more clearly, the following briefly introduces the drawings that need to be used in the description of the embodiments. in:

图1为实施例1制备的负载

Figure BDA0004130931000000025
酸性离子液体固体酸催化剂的红外谱图。Fig. 1 is the load that embodiment 1 prepares
Figure BDA0004130931000000025
Infrared spectrum of acidic ionic liquid solid acid catalyst.

图2为分别使用各实施例所制备的负载

Figure BDA0004130931000000026
酸性离子液体催化合成乙酸乙酯的结果,横坐标为时间,纵坐标为乙酸乙酯收率。Fig. 2 is the load prepared by using each embodiment respectively
Figure BDA0004130931000000026
The result of the acidic ionic liquid catalyzed synthesis of ethyl acetate, the abscissa is time, and the ordinate is the yield of ethyl acetate.

图3为实施例3制备的固体酸和负载

Figure BDA0004130931000000027
酸性离子液体后的固体酸催化剂的催化稳定性对比图。Fig. 3 is the solid acid and load prepared by embodiment 3
Figure BDA0004130931000000027
Comparison of catalytic stability of solid acid catalysts after acidic ionic liquids.

具体实施方式Detailed ways

为使本发明的上述目的、特征和优点能够更加明显易懂,下面结合具体实施例对本发明的具体实施方式做详细的说明。In order to make the above objects, features and advantages of the present invention more comprehensible, the specific implementation of the present invention will be described in detail below in conjunction with specific examples.

在下面的描述中阐述了很多具体细节以便于充分理解本发明,但是本发明还可以采用其他不同于在此描述的其它方式来实施,本领域技术人员可以在不违背本发明内涵的情况下做类似推广,因此本发明不受下面公开的具体实施例的限制。In the following description, a lot of specific details are set forth in order to fully understand the present invention, but the present invention can also be implemented in other ways different from those described here, and those skilled in the art can do it without departing from the meaning of the present invention. By analogy, the present invention is therefore not limited to the specific examples disclosed below.

实施例1:Example 1:

在100mL的烧瓶中,氮气气氛下交联聚乙烯基吡咯烷酮粉末(22.23g,单体摩尔量为0.2mol,购自阿拉丁,货号P101410)放入甲苯中,一段时间后,加入1,3丙烷磺酸内酯(6.8g,0.05mol),将混合物加热到80℃连续搅拌24小时。所得到的固体两性离子通过过滤回收,用乙酸乙酯洗涤,完全去除未反应的反应物,然后在60℃条件下真空干燥过夜得到交联聚乙烯基吡咯烷酮:1,3丙烷磺酸内酯的摩尔比为1:0.25的固体酸[PVPP-PS],将得到的[PVPP-PS]取1g在研钵中研磨均匀后,分散到乙酸乙酯溶液中,然后将将硫酸(5.0g,0.05mol)加入到溶液中,搅拌24h,完成后,将混合物用甲醇过滤和洗涤三次,然后在60℃的真空中除去水和甲醇,得到最终产品负载

Figure BDA0004130931000000031
酸性离子液体的固体酸催化剂[PVPP-PS]HSO4。In a 100mL flask, under a nitrogen atmosphere, cross-linked polyvinylpyrrolidone powder (22.23g, the molar weight of the monomer is 0.2mol, purchased from Aladdin, product number P101410) was placed in toluene, and after a period of time, 1,3 propane was added sultone (6.8 g, 0.05 mol), and the mixture was heated to 80° C. and stirred continuously for 24 hours. The resulting solid zwitterions were recovered by filtration, washed with ethyl acetate to completely remove unreacted reactants, and then dried under vacuum at 60°C overnight to obtain cross-linked polyvinylpyrrolidone: 1,3 propane sultone A solid acid [PVPP-PS] with a molar ratio of 1:0.25, 1 g of the obtained [PVPP-PS] was ground in a mortar, dispersed in ethyl acetate solution, and then sulfuric acid (5.0 g, 0.05 mol) was added to the solution and stirred for 24 h, upon completion, the mixture was filtered and washed three times with methanol, then the water and methanol were removed in vacuo at 60 °C to obtain the final product loaded
Figure BDA0004130931000000031
Solid acid catalyst of acidic ionic liquid [PVPP-PS]HSO 4 .

酯化反应(反应釜进行):采用不分水的回流蒸馏方式,加热装置采用无明火不接触热源的二甲基硅油油浴锅油浴加热,常温水冷凝,在装入磁力搅拌器,连接好冷凝管跟温度计的三口烧瓶中先加乙酸,并升温到80摄氏度加入催化剂,待达到80摄氏度,加入乙醇,开启磁力搅拌器,开始反应。实施例1-5及对照例1-5的酯化反应方法与本实施例相同。重复三次实验取平均值。Esterification reaction (conducted in a reaction kettle): the reflux distillation method without water separation is adopted, the heating device is heated by a dimethyl silicone oil bath oil bath without an open flame and no contact with the heat source, the water at room temperature is condensed, and the magnetic stirrer is installed, connected First add acetic acid to the three-necked flask with the condenser tube and thermometer, and then raise the temperature to 80 degrees Celsius to add the catalyst. When the temperature reaches 80 degrees Celsius, add ethanol, turn on the magnetic stirrer, and start the reaction. The esterification reaction methods of Examples 1-5 and Comparative Examples 1-5 are the same as in this example. The experiment was repeated three times to obtain the average value.

酯化产物分析:乙酸和乙醇的经典反应,主要产物是乙酸乙酯和水,因此,实验以检测反应物乙酸的减少量,以及检测乙酸乙酯的增加量来表征实验进行程度,并为后续计算提供数据支持。Esterification product analysis: in the classic reaction of acetic acid and ethanol, the main products are ethyl acetate and water. Therefore, the experiment uses the reduction of the reactant acetic acid and the increase of ethyl acetate to characterize the progress of the experiment, and to provide a basis for the follow-up Calculations provide data support.

本实验所用气相色谱为北分瑞利生产的GC-3420A,所用分离柱为毛细柱,柱参数为30m*0.32mm*0.50um,检测器为氢火焰离子化检测器,初始柱温为80摄氏度,进样器温度为220摄氏度,检测器温度为250摄氏度,升温程序是在80摄氏度保留2min,之后以30摄氏度每min的速率升至200摄氏度,待升至200摄氏度后保留5min。实验准备时,制备了比例为15:3:1的乙酸乙酯、乙醇、乙酸混合液体,取混合液体并进行气相色谱分析,标定各组分的出峰时间。反应一开始,用移液枪调节至250μL,迅速移取试样,将样品置于并迅速转移至色谱室,进行气相色谱分析测试其含量比例。反应过程中,每20min取一次样,并迅速转移至色谱室,进行气相色谱分析测试各组分含量比例。气相色谱分析时,反复润洗针管8次以上,取样时吸取0.6μL待测液体。从三口烧瓶取样到色谱分析注射入色谱仪中,控制总时长不超过1min,以控制测试准确性。以下实施例的酯化产物分析方法和检测方法除说明外均与本实施例相同。The gas chromatograph used in this experiment is GC-3420A produced by Beifen Rayleigh, the separation column used is a capillary column, the column parameters are 30m*0.32mm*0.50um, the detector is a hydrogen flame ionization detector, and the initial column temperature is 80 degrees Celsius , the temperature of the injector is 220 degrees Celsius, the temperature of the detector is 250 degrees Celsius, the temperature rise program is to keep at 80 degrees Celsius for 2 minutes, then rise to 200 degrees Celsius at a rate of 30 degrees Celsius per minute, and keep it for 5 minutes after rising to 200 degrees Celsius. During the preparation of the experiment, a mixed liquid of ethyl acetate, ethanol and acetic acid with a ratio of 15:3:1 was prepared, and the mixed liquid was taken and analyzed by gas chromatography, and the peak time of each component was calibrated. At the beginning of the reaction, use a pipette gun to adjust to 250 μL, quickly remove the sample, place the sample and quickly transfer it to the chromatographic chamber, and perform gas chromatographic analysis to test its content ratio. During the reaction process, a sample was taken every 20 minutes, and quickly transferred to the chromatographic chamber for gas chromatography analysis to test the content ratio of each component. During gas chromatographic analysis, rinse the needle tube more than 8 times repeatedly, and absorb 0.6 μL of the liquid to be tested when sampling. From the sampling of the three-necked flask to the chromatographic analysis and injection into the chromatograph, the total time should not exceed 1 minute to control the accuracy of the test. The esterification product analysis method and detection method of the following examples are all the same as the present example except for the description.

本实施例乙酸乙酯收率为64.2%±0.74%。The yield of ethyl acetate in this embodiment is 64.2%±0.74%.

实施例2:Example 2:

在100mL的烧瓶中,氮气气氛下交联聚乙烯基吡咯烷酮粉末(11.11g,单体摩尔量为0.1mol)放入甲苯中,一段时间后,加入1,3丙烷磺酸内酯(6.8g,0.05mol),将混合物加热到80℃连续搅拌24小时。所得到的固体两性离子通过过滤回收,用乙酸乙酯洗涤,完全去除未反应的反应物,然后在60℃条件下真空干燥过夜得摩尔比1:0.5的固体酸[PVPP-PS]。将制备的[PVPP-PS]取1g在研钵中研磨均匀后,然后将样品分散到乙酸乙酯溶液中,然后将将硫酸(5.0g,0.05mol)加入到溶液中,搅拌24h,完成后,将混合物用甲醇过滤和洗涤三次,然后在60℃的真空中除去水和甲醇,得到最终产品负载

Figure BDA0004130931000000041
酸性离子液体的固体酸催化剂[PVPP-PS]HSO4。In a 100mL flask, under a nitrogen atmosphere, cross-linked polyvinylpyrrolidone powder (11.11g, the molar weight of the monomer is 0.1mol) was put into toluene, and after a period of time, 1,3 propane sultone (6.8g, 0.05mol), the mixture was heated to 80°C and stirred continuously for 24 hours. The obtained solid zwitterions were recovered by filtration, washed with ethyl acetate to completely remove unreacted reactants, and then dried under vacuum at 60°C overnight to obtain a solid acid [PVPP-PS] with a molar ratio of 1:0.5. Take 1g of the prepared [PVPP-PS] and grind it evenly in a mortar, then disperse the sample into the ethyl acetate solution, then add sulfuric acid (5.0g, 0.05mol) into the solution, stir for 24h, after completion , the mixture was filtered and washed three times with methanol, then water and methanol were removed in vacuo at 60 °C to obtain the final product loading
Figure BDA0004130931000000041
Solid acid catalyst of acidic ionic liquid [PVPP-PS]HSO 4 .

本实施例乙酸乙酯收率为68.5%±1.3%。The yield of ethyl acetate in this embodiment is 68.5%±1.3%.

实施例3:Example 3:

在100mL的烧瓶中,氮气气氛下将交联聚乙烯基吡咯烷酮粉末(5.55g,单体摩尔量为0.05mol,购自阿拉丁,货号P101410)放入甲苯中,一段时间后,加入1,3丙烷磺酸内酯(6.8g,0.05mol),将混合物加热到80℃连续搅拌24小时。所得到的固体两性离子通过过滤回收,用乙酸乙酯洗涤,完全去除未反应的反应物,然后在60℃条件下真空干燥过夜得到交联聚乙烯基吡咯烷酮:1,3丙烷磺酸内酯的摩尔比为1:1的固体酸[PVPP-PS]。将制备的[PVPP-PS]取1g在研钵中研磨均匀后,然后将样品分散到乙酸乙酯溶液中,然后将将硫酸(5.0g,0.05mol)加入到溶液中,搅拌24h,完成后,将混合物用甲醇过滤和洗涤三次,然后在60℃的真空中除去水和甲醇,得到最终产品负载

Figure BDA0004130931000000051
酸性离子液体的固体酸催化剂[PVPP-PS]HSO4。In a 100mL flask, under a nitrogen atmosphere, put cross-linked polyvinylpyrrolidone powder (5.55g, the molar weight of the monomer is 0.05mol, purchased from Aladdin, product number P101410) into toluene, after a period of time, add 1,3 Propane sultone (6.8 g, 0.05 mol), the mixture was heated to 80° C. and stirred continuously for 24 hours. The resulting solid zwitterions were recovered by filtration, washed with ethyl acetate to completely remove unreacted reactants, and then dried under vacuum at 60°C overnight to obtain cross-linked polyvinylpyrrolidone: 1,3 propane sultone Solid acid [PVPP-PS] with a molar ratio of 1:1. Take 1g of the prepared [PVPP-PS] and grind it evenly in a mortar, then disperse the sample into the ethyl acetate solution, then add sulfuric acid (5.0g, 0.05mol) into the solution, stir for 24h, after completion , the mixture was filtered and washed three times with methanol, then water and methanol were removed in vacuo at 60 °C to obtain the final product loading
Figure BDA0004130931000000051
Solid acid catalyst of acidic ionic liquid [PVPP-PS]HSO 4 .

本实施例乙酸乙酯收率为82.3%±0.22%。The yield of ethyl acetate in this embodiment is 82.3%±0.22%.

酯化反应(反应釜进行):采用不分水的回流蒸馏方式,加热装置采用无明火不接触热源的二甲基硅油油浴锅油浴加热,常温水冷凝,在装入磁力搅拌器,连接好冷凝管跟温度计的三口烧瓶中先加乙酸,并升温到80摄氏度加入催化剂,待达到80摄氏度,加入乙醇,开启磁力搅拌器,开始反应。实施例1-5及对照例1-5的酯化反应方法与本实施例相同。重复三次实验取平均值。Esterification reaction (conducted in a reaction kettle): the reflux distillation method without water separation is adopted, the heating device is heated by a dimethyl silicone oil bath oil bath without an open flame and no contact with the heat source, the water at room temperature is condensed, and the magnetic stirrer is installed, connected First add acetic acid to the three-necked flask with the condenser tube and thermometer, and then raise the temperature to 80 degrees Celsius to add the catalyst. When the temperature reaches 80 degrees Celsius, add ethanol, turn on the magnetic stirrer, and start the reaction. The esterification reaction methods of Examples 1-5 and Comparative Examples 1-5 are the same as in this example. The experiment was repeated three times to obtain the average value.

酯化产物分析:乙酸和乙醇的经典反应,主要产物是乙酸乙酯和水,因此,实验以检测反应物乙酸的减少量,以及检测乙酸乙酯的增加量来表征实验进行程度,并为后续计算提供数据支持。Esterification product analysis: in the classic reaction of acetic acid and ethanol, the main products are ethyl acetate and water. Therefore, the experiment uses the reduction of the reactant acetic acid and the increase of ethyl acetate to characterize the progress of the experiment, and to provide a basis for the follow-up Calculations provide data support.

本实验所用气相色谱为北分瑞利生产的GC-3420A,所用分离柱为毛细柱,柱参数为30m*0.32mm*0.50um,检测器为氢火焰离子化检测器,初始柱温为80摄氏度,进样器温度为220摄氏度,检测器温度为250摄氏度,升温程序是在80摄氏度保留2min,之后以30摄氏度每min的速率升至200摄氏度,待升至200摄氏度后保留5min。实验准备时,制备了比例为15:3:1的乙酸乙酯、乙醇、乙酸混合液体,取混合液体并进行气相色谱分析,标定各组分的出峰时间。反应一开始,用移液枪调节至250μL,迅速移取试样,将样品置于并迅速转移至色谱室,进行气相色谱分析测试其含量比例。反应过程中,每20min取一次样,并迅速转移至色谱室,进行气相色谱分析测试各组分含量比例。气相色谱分析时,反复润洗针管8次以上,取样时吸取0.6μL待测液体。从三口烧瓶取样到色谱分析注射入色谱仪中,控制总时长不超过1min,以控制测试准确性。The gas chromatograph used in this experiment is GC-3420A produced by Beifen Rayleigh, the separation column used is a capillary column, the column parameters are 30m*0.32mm*0.50um, the detector is a hydrogen flame ionization detector, and the initial column temperature is 80 degrees Celsius , the temperature of the injector is 220 degrees Celsius, the temperature of the detector is 250 degrees Celsius, the temperature rise program is to keep at 80 degrees Celsius for 2 minutes, then rise to 200 degrees Celsius at a rate of 30 degrees Celsius per minute, and keep it for 5 minutes after rising to 200 degrees Celsius. During the preparation of the experiment, a mixed liquid of ethyl acetate, ethanol and acetic acid with a ratio of 15:3:1 was prepared, and the mixed liquid was taken and analyzed by gas chromatography, and the peak time of each component was calibrated. At the beginning of the reaction, use a pipette gun to adjust to 250 μL, quickly remove the sample, place the sample and quickly transfer it to the chromatographic chamber, and perform gas chromatographic analysis to test its content ratio. During the reaction process, a sample was taken every 20 minutes, and quickly transferred to the chromatographic chamber for gas chromatography analysis to test the content ratio of each component. During gas chromatographic analysis, rinse the needle tube more than 8 times repeatedly, and absorb 0.6 μL of the liquid to be tested when sampling. From the sampling of the three-necked flask to the chromatographic analysis and injection into the chromatograph, the total time should not exceed 1 minute to control the accuracy of the test.

实施例4:Example 4:

在100mL的烧瓶中,氮气气氛下交联聚乙烯基吡咯烷酮粉末(4.55g,单体摩尔量为0.041mol)放入甲苯中,一段时间后,加入1,3丙烷磺酸内酯(6.8g,0.05mol),将混合物加热到80℃连续搅拌24小时。所得到的固体两性离子通过过滤回收,用乙酸乙酯洗涤,完全去除未反应的反应物,然后在60℃条件下真空干燥过夜得摩尔比1:1.2的固体酸[PVPP-PS]。将制备的[PVPP-PS]取1g在研钵中研磨均匀后,然后将样品分散到乙酸乙酯溶液中,然后将将硫酸(5.0g,0.05mol)加入到溶液中,搅拌24h,完成后,将混合物用甲醇过滤和洗涤三次,然后在60℃的真空中除去水和甲醇,得到最终产品负载

Figure BDA0004130931000000061
酸性离子液体的固体酸催化剂[PVPP-PS]HSO4。In a 100mL flask, under a nitrogen atmosphere, cross-linked polyvinylpyrrolidone powder (4.55g, the molar weight of the monomer is 0.041mol) was put into toluene, and after a period of time, 1,3 propane sultone (6.8g, 0.05mol), the mixture was heated to 80°C and stirred continuously for 24 hours. The obtained solid zwitterions were recovered by filtration, washed with ethyl acetate to completely remove unreacted reactants, and then dried under vacuum at 60°C overnight to obtain a solid acid [PVPP-PS] with a molar ratio of 1:1.2. Take 1g of the prepared [PVPP-PS] and grind it evenly in a mortar, then disperse the sample into the ethyl acetate solution, then add sulfuric acid (5.0g, 0.05mol) into the solution, stir for 24h, after completion , the mixture was filtered and washed three times with methanol, then water and methanol were removed in vacuo at 60 °C to obtain the final product loading
Figure BDA0004130931000000061
Solid acid catalyst of acidic ionic liquid [PVPP-PS]HSO 4 .

本实施例乙酸乙酯收率为80.5%±0.61%。The yield of ethyl acetate in this embodiment is 80.5%±0.61%.

实施例5:Example 5:

在100mL的烧瓶中,氮气气氛下交联聚乙烯基吡咯烷酮粉末(3.7g,单体摩尔量为0.033mol)放入甲苯中,一段时间后,加入1,3丙烷磺酸内酯(6.8g,0.05mol),将混合物加热到80℃连续搅拌24小时。所得到的固体两性离子通过过滤回收,用乙酸乙酯洗涤,完全去除未反应的反应物,然后在60℃条件下真空干燥过夜得摩尔比1:1.5的固体酸[PVPP-PS]。将制备的[PVPP-PS]取1g在研钵中研磨均匀后,然后将样品分散到乙酸乙酯溶液中,然后将将硫酸(5.0g,0.05mol)加入到溶液中,搅拌24h,完成后,将混合物用甲醇过滤和洗涤三次,然后在60℃的真空中除去水和甲醇,得到最终产品负载

Figure BDA0004130931000000062
酸性离子液体的固体酸催化剂[PVPP-PS]HSO4。In a 100mL flask, under a nitrogen atmosphere, cross-linked polyvinylpyrrolidone powder (3.7g, the molar weight of the monomer is 0.033mol) was put into toluene, and after a period of time, 1,3 propane sultone (6.8g, 0.05mol), the mixture was heated to 80°C and stirred continuously for 24 hours. The obtained solid zwitterions were recovered by filtration, washed with ethyl acetate to completely remove unreacted reactants, and then dried under vacuum at 60°C overnight to obtain a solid acid [PVPP-PS] with a molar ratio of 1:1.5. Take 1g of the prepared [PVPP-PS] and grind it evenly in a mortar, then disperse the sample into the ethyl acetate solution, then add sulfuric acid (5.0g, 0.05mol) into the solution, stir for 24h, after completion , the mixture was filtered and washed three times with methanol, then water and methanol were removed in vacuo at 60 °C to obtain the final product loading
Figure BDA0004130931000000062
Solid acid catalyst of acidic ionic liquid [PVPP-PS]HSO 4 .

本实施例乙酸乙酯收率为72.4%±1.02%。The yield of ethyl acetate in this embodiment is 72.4%±1.02%.

实施例6:Embodiment 6:

将实施例3制备的交联聚乙烯基吡咯烷酮:1,3丙烷磺酸内酯的摩尔比为1:1的[PVPP-PS]取1g在研钵中研磨均匀后,分散到乙酸乙酯溶液中,然后将将硫酸(5.0g,0.05mol)加入到溶液中,搅拌24h,完成后,将混合物用甲醇过滤和洗涤三次,然后在60℃的真空中除去水和甲醇,得到最终产品负载

Figure BDA0004130931000000063
酸性离子液体的固体酸催化剂[PVPP-PS]HSO4。Take 1g of [PVPP-PS] prepared in Example 3 with a molar ratio of 1,3 propane sultone: 1:1 [PVPP-PS], grind it evenly in a mortar, and disperse it into ethyl acetate solution , then sulfuric acid (5.0 g, 0.05 mol) was added to the solution and stirred for 24 h. After completion, the mixture was filtered and washed three times with methanol, and then water and methanol were removed in vacuum at 60° C. to obtain the final product supported
Figure BDA0004130931000000063
Solid acid catalyst of acidic ionic liquid [PVPP-PS]HSO 4 .

酯化反应(精馏塔进行):将制备的负载离子液体的固体酸催化剂装填到填料精馏塔中,填满整个填料柱,在回流比为12:4,乙醇和乙酸的进料摩尔比为1.2:1,反应温度为85℃的条件下,反应2个小时,探究固体酸催化剂的催化效果。按实施例1方法计算乙酸乙酯收率。Esterification reaction (rectification tower): The prepared solid acid catalyst loaded with ionic liquid is packed into the packed rectification tower, and the whole packed column is filled. The feed molar ratio of ethanol and acetic acid is Under the conditions of 1.2:1, the reaction temperature is 85 ℃, the reaction is carried out for 2 hours, and the catalytic effect of the solid acid catalyst is explored. The ethyl acetate yield was calculated according to the method of Example 1.

本实施例乙酸乙酯收率为95.6%±0.37%。The yield of ethyl acetate in this embodiment is 95.6%±0.37%.

实施例7:Embodiment 7:

在100mL的烧瓶中,氮气气氛下将交联聚乙烯基吡咯烷酮粉末(5.55g,单体摩尔量为0.05mol,购自阿拉丁,货号P101410)放入甲苯中,一段时间后,加入1,3丙烷磺酸内酯(6.8g,0.05mol),将混合物加热到80℃连续搅拌24小时。所得到的固体两性离子通过过滤回收,用乙酸乙酯洗涤,完全去除未反应的反应物,然后在60℃条件下真空干燥过夜得到交联聚乙烯基吡咯烷酮:1,3丙烷磺酸内酯的摩尔比为1:1的固体酸[PVPP-PS]。In a 100mL flask, under a nitrogen atmosphere, put cross-linked polyvinylpyrrolidone powder (5.55g, the molar weight of the monomer is 0.05mol, purchased from Aladdin, product number P101410) into toluene, after a period of time, add 1,3 Propane sultone (6.8 g, 0.05 mol), the mixture was heated to 80° C. and stirred continuously for 24 hours. The resulting solid zwitterions were recovered by filtration, washed with ethyl acetate to completely remove unreacted reactants, and then dried under vacuum at 60°C overnight to obtain cross-linked polyvinylpyrrolidone: 1,3 propane sultone Solid acid [PVPP-PS] with a molar ratio of 1:1.

按实施例1方法酯化反应方法制备乙酸乙酯,计算乙酸乙酯收率。Ethyl acetate was prepared by the esterification reaction method of the method in Example 1, and the ethyl acetate yield was calculated.

本实施例乙酸乙酯收率为66.3%±0.91%。The yield of ethyl acetate in this embodiment is 66.3%±0.91%.

对照例1:Comparative example 1:

在100mL的烧瓶中,氮气气氛下2-甲基吡啶(4.65g,单体摩尔量为0.05mol)放入甲苯中,一段时间后,加入1,3丙烷磺酸内酯(6.8g,0.05mol),将混合物加热到80℃连续搅拌24小时。所得到的固体两性离子通过过滤回收,用乙酸乙酯洗涤,完全去除未反应的反应物,然后在60℃条件下真空干燥过夜得固体酸[CHNO-PS]催化剂。In a 100mL flask, 2-picoline (4.65g, monomer molar weight is 0.05mol) was put into toluene under nitrogen atmosphere, and after a period of time, 1,3 propane sultone (6.8g, 0.05mol ), the mixture was heated to 80°C and stirred continuously for 24 hours. The obtained solid zwitterions were recovered by filtration, washed with ethyl acetate to completely remove unreacted reactants, and then dried under vacuum at 60° C. overnight to obtain a solid acid [CHNO-PS] catalyst.

按实施例1方法酯化反应方法制备乙酸乙酯,计算乙酸乙酯收率。Ethyl acetate was prepared by the esterification reaction method of the method in Example 1, and the ethyl acetate yield was calculated.

本实施例乙酸乙酯收率为55.1%±0.46%。The yield of ethyl acetate in this embodiment is 55.1%±0.46%.

对照例2:Comparative example 2:

在100mL的烧瓶中,氮气气氛下咪唑(3.4g,单体摩尔量为0.05mol)放入甲苯中,一段时间后,加入1,3丙烷磺酸内酯(6.8g,0.05mol),将混合物加热到80℃连续搅拌24小时。所得到的固体两性离子通过过滤回收,用乙酸乙酯洗涤,完全去除未反应的反应物,然后在60℃条件下真空干燥过夜得固体酸[Bmim-PS]催化剂。In a 100mL flask, imidazole (3.4g, monomer molar weight: 0.05mol) was put into toluene under a nitrogen atmosphere, after a period of time, 1,3 propane sultone (6.8g, 0.05mol) was added, and the mixture Heating to 80°C continued stirring for 24 hours. The obtained solid zwitterions were recovered by filtration, washed with ethyl acetate to completely remove unreacted reactants, and then dried under vacuum at 60° C. overnight to obtain a solid acid [Bmim-PS] catalyst.

按实施例1方法酯化反应方法制备乙酸乙酯,计算乙酸乙酯收率。Ethyl acetate was prepared by the esterification reaction method of the method in Example 1, and the ethyl acetate yield was calculated.

本实施例乙酸乙酯收率为60.2%±0.83%。The yield of ethyl acetate in this embodiment is 60.2%±0.83%.

对照例3:Comparative example 3:

在100mL的烧瓶中,氮气气氛下间胺基苯磺酸(8.66g,单体摩尔量为0.05mol)放入甲苯中,一段时间后,加入1,3丙烷磺酸内酯(6.8g,0.05mol),将混合物加热到80℃连续搅拌24小时。所得到的固体两性离子通过过滤回收,用乙酸乙酯洗涤,完全去除未反应的反应物,然后在60℃条件下真空干燥过夜得固体酸[3-AMSA-PS]催化剂。In a 100mL flask, m-aminobenzenesulfonic acid (8.66g, monomer molar weight: 0.05mol) was put into toluene under a nitrogen atmosphere, and after a period of time, 1,3 propane sultone (6.8g, 0.05 mol), the mixture was heated to 80°C and stirred continuously for 24 hours. The obtained solid zwitterions were recovered by filtration, washed with ethyl acetate to completely remove unreacted reactants, and then dried under vacuum at 60° C. overnight to obtain a solid acid [3-AMSA-PS] catalyst.

按实施例1方法酯化反应方法制备乙酸乙酯,计算乙酸乙酯收率。Ethyl acetate was prepared by the esterification reaction method of the method in Example 1, and the ethyl acetate yield was calculated.

本实施例乙酸乙酯收率为50.5%±0.36%。The yield of ethyl acetate in this embodiment is 50.5%±0.36%.

对照例4:Comparative example 4:

将实施例3得到的1:1制备的[PVPP-PS]在研钵中研磨均匀后,取1g分散到乙酸乙酯溶液中,然后将将磷酸(4.9g,0.05mol)加入到溶液中,搅拌24h,完成后,将混合物用甲醇过滤和洗涤三次,然后在60℃的真空中除去水和甲醇,得到最终产品负载

Figure BDA0004130931000000082
酸性离子液体的固体酸催化剂[PVPP-PS]H2PO4。After the [PVPP-PS] prepared in a ratio of 1:1 obtained in Example 3 was uniformly ground in a mortar, 1 g was dispersed into an ethyl acetate solution, and then phosphoric acid (4.9 g, 0.05 mol) was added to the solution, Stirring for 24 h, upon completion, the mixture was filtered and washed three times with methanol, then the water and methanol were removed in vacuo at 60 °C to obtain the final product loading
Figure BDA0004130931000000082
Solid acid catalyst of acidic ionic liquid [PVPP-PS]H 2 PO 4 .

本实施例乙酸乙酯收率74.5%±0.51%。The ethyl acetate yield of this embodiment is 74.5% ± 0.51%.

对照例5:Comparative example 5:

将实施例3得到的1:1制备的[PVPP-PS]在研钵中研磨均匀后,取1g分散到乙酸乙酯溶液中,然后将将氟硼酸(4.39g,0.05mol)加入到溶液中,搅拌24h,完成后,将混合物用甲醇过滤和洗涤三次,然后在60℃的真空中除去水和甲醇,得到最终产品负载

Figure BDA0004130931000000081
酸性离子液体的固体酸催化剂[PVPP-PS]BF4。After grinding the [PVPP-PS] obtained in Example 3 at a ratio of 1:1 in a mortar, take 1 g and disperse it into the ethyl acetate solution, then add fluoroboric acid (4.39 g, 0.05 mol) into the solution , stirred for 24 h, upon completion, the mixture was filtered and washed three times with methanol, then water and methanol were removed in vacuo at 60 °C to obtain the final product loaded
Figure BDA0004130931000000081
Solid acid catalyst [PVPP-PS]BF 4 of acidic ionic liquid.

按实施例1方法酯化反应方法制备乙酸乙酯,计算乙酸乙酯收率。Ethyl acetate was prepared by the esterification reaction method of the method in Example 1, and the ethyl acetate yield was calculated.

本实施例乙酸乙酯收率为65.4%±0.24%。The yield of ethyl acetate in this embodiment is 65.4%±0.24%.

本发明提供了一种负载

Figure BDA0004130931000000083
酸性离子液体的固体酸催化剂及其制备方法。本发明制备的负载/>
Figure BDA0004130931000000084
酸性离子液体的固体酸催化剂作为一种催化剂,可以催化乙酸和乙醇反应合成乙酸乙酯,具有较高的催化活性和稳定性。单独使用离子液体的液体催化剂容易在反应中分解,从而造成反应活性下降,而负载离子液体的固体酸催化剂,固体酸包裹离子液体,使得催化剂稳定性和活性得到提升,负载离子液体后的催化剂催化性能比单纯的固体酸催化剂有着显著的提升(实验结果具有统计学差异)。制备的固体酸其催化活性高,并且经过简单的过滤就可以重复利用。The present invention provides a load
Figure BDA0004130931000000083
Solid acid catalyst of acidic ionic liquid and preparation method thereof. The load prepared by the present invention/>
Figure BDA0004130931000000084
The solid acid catalyst of the acidic ionic liquid, as a catalyst, can catalyze the reaction of acetic acid and ethanol to synthesize ethyl acetate, and has high catalytic activity and stability. The liquid catalyst using ionic liquid alone is easy to decompose in the reaction, resulting in a decrease in reactivity, while the solid acid catalyst loaded with ionic liquid, the solid acid wraps the ionic liquid, which improves the stability and activity of the catalyst, and the catalyst after loading the ionic liquid catalyzes Compared with the pure solid acid catalyst, the performance is significantly improved (the experimental results have statistical differences). The prepared solid acid has high catalytic activity and can be reused after simple filtration.

应说明的是,以上实施例仅用以说明本发明的技术方案而非限制,尽管参照较佳实施例对本发明进行了详细说明,本领域的普通技术人员应当理解,可以对本发明的技术方案进行修改或者等同替换,而不脱离本发明技术方案的精神和范围,其均应涵盖在本发明的权利要求范围当中。It should be noted that the above embodiments are only used to illustrate the technical solutions of the present invention without limitation, although the present invention has been described in detail with reference to the preferred embodiments, those of ordinary skill in the art should understand that the technical solutions of the present invention can be carried out Modifications or equivalent replacements without departing from the spirit and scope of the technical solution of the present invention shall be covered by the claims of the present invention.

Claims (9)

1.一种负载酸性离子液体的固体酸催化剂的制备方法,其特征在于:将交联聚乙烯基吡咯烷酮粉末放入甲苯中,加入1,3丙烷磺酸内酯得到混合物,将所述混合物在加热回流条件下搅拌反应,将所得到的两性固体离子过滤回收、洗涤,真空干燥过夜,得到固体[PVPP-PS]催化剂,将固体[PVPP-PS]催化剂在研钵中研磨分散到溶剂中,加入硫酸搅拌20~30h,过滤、洗涤,真空干燥,得到[PVPP-PS]HSO4固体酸催化剂。1. a kind of preparation method of the solid acid catalyst of load acidic ionic liquid, it is characterized in that: cross-linked polyvinylpyrrolidone powder is put into toluene, add 1,3 propane sultone obtains mixture, described mixture is in Stir the reaction under heating and reflux conditions, filter and recover the obtained amphoteric solid ions, wash, and vacuum dry overnight to obtain a solid [PVPP-PS] catalyst, and grind the solid [PVPP-PS] catalyst in a mortar and disperse it in the solvent, Add sulfuric acid and stir for 20-30 hours, filter, wash, and vacuum-dry to obtain [PVPP-PS]HSO 4 solid acid catalyst. 2.根据权利要求1所述的负载酸性离子液体的固体酸催化剂的制备方法,其特征在于:交联聚乙烯基吡咯烷酮与1,3丙烷磺酸内酯的摩尔比为1:1。2. The preparation method of the solid acid catalyst supporting acidic ionic liquid according to claim 1, characterized in that: the molar ratio of cross-linked polyvinylpyrrolidone to 1,3 propane sultone is 1:1. 3.根据权利要求1或2所述的负载酸性离子液体的固体酸催化剂的制备方法,其特征在于:所述加入硫酸,其中,硫酸与固体[PVPP-PS]催化剂的质量比为18:1。3. the preparation method of the solid acid catalyst of supporting acidic ionic liquid according to claim 1 or 2, is characterized in that: described adding sulfuric acid, wherein, the mass ratio of sulfuric acid and solid [PVPP-PS] catalyst is 18:1 . 4.根据权利要求1或2所述的负载酸性离子液体的固体酸催化剂的制备方法,其特征在于:所述在加热回流条件下搅拌反应,反应温度为80℃,反应时间为24h。4. The preparation method of the acidic ionic liquid-loaded solid acid catalyst according to claim 1 or 2, characterized in that: the stirring reaction is carried out under heating and reflux conditions, the reaction temperature is 80° C., and the reaction time is 24 hours. 5.根据权利要求1或2所述的负载酸性离子液体的固体酸催化剂的制备方法,其特征在于:所述将所得到的两性固体离子过滤回收、洗涤,为用乙酸乙酯洗涤。5. The preparation method of the solid acid catalyst loaded with acidic ionic liquid according to claim 1 or 2, characterized in that: the obtained amphoteric solid ions are recovered by filtration and washed by washing with ethyl acetate. 6.根据权利要求1或2所述的负载酸性离子液体的固体酸催化剂的制备方法,其特征在于:所述真空干燥过夜,是在60℃条件下真空干燥过夜。6 . The preparation method of the acidic ionic liquid-loaded solid acid catalyst according to claim 1 or 2, characterized in that: the vacuum drying overnight is vacuum drying at 60° C. overnight. 7.根据权利要求6所述的负载酸性离子液体的固体酸催化剂的制备方法,其特征在于:所述溶剂为乙酸乙酯。7. The preparation method of the solid acid catalyst supporting acidic ionic liquid according to claim 6, characterized in that: the solvent is ethyl acetate. 8.权利要求1所述制备方法得到的负载酸性离子液体的固体酸催化剂作为酯化反应催化剂的应用。8. the application of the solid acid catalyst of the loaded acidic ionic liquid obtained by the preparation method of claim 1 as an esterification catalyst. 9.根据权利要求8所述的应用,其特征在于:所述酯化反应,其反应底物为乙酸和乙醇。9. The application according to claim 8, characterized in that: in the esterification reaction, the reaction substrates are acetic acid and ethanol.
CN202310260062.5A 2023-03-17 2023-03-17 Preparation method and application of solid acid catalyst loaded with acidic ionic liquid Pending CN116371467A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202310260062.5A CN116371467A (en) 2023-03-17 2023-03-17 Preparation method and application of solid acid catalyst loaded with acidic ionic liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202310260062.5A CN116371467A (en) 2023-03-17 2023-03-17 Preparation method and application of solid acid catalyst loaded with acidic ionic liquid

Publications (1)

Publication Number Publication Date
CN116371467A true CN116371467A (en) 2023-07-04

Family

ID=86976092

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202310260062.5A Pending CN116371467A (en) 2023-03-17 2023-03-17 Preparation method and application of solid acid catalyst loaded with acidic ionic liquid

Country Status (1)

Country Link
CN (1) CN116371467A (en)

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1880303A (en) * 2005-06-17 2006-12-20 广东工业大学 substituted pyrrolidone synthesized ion liquid and its synthesis method
CN101024625A (en) * 2007-03-23 2007-08-29 广东工业大学 Ketopyrrolidine sulfurate in liquid and its prpearing method
CN101255111A (en) * 2008-03-25 2008-09-03 广东工业大学 A kind of method for ionic liquid catalyzed continuous esterification reaction rectification to synthesize ethyl acetate
CN103124586A (en) * 2010-07-22 2013-05-29 海内肯供应连锁公司 Method for regeneration of PVPP from the retentate of a membrane filter after clarification and stabilization of a yeast-fermented beverage
CN104084234A (en) * 2014-07-16 2014-10-08 沈阳工业大学 Crosslinked polyethylene pyrrolidone based catalyst and preparation method thereof
CN104492485A (en) * 2014-11-26 2015-04-08 绍兴文理学院 Acidic ionic liquid-coated polymeric core solid acid material catalyst and preparation method thereof
CN104525260A (en) * 2014-12-25 2015-04-22 江南大学 Polymeric solid acid catalyst for esterification reaction and preparation method thereof
CN107029784A (en) * 2017-04-25 2017-08-11 福州大学 A kind of Polymer-supported dual-core acidic ionic liquid catalyst and its preparation and application

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1880303A (en) * 2005-06-17 2006-12-20 广东工业大学 substituted pyrrolidone synthesized ion liquid and its synthesis method
CN101024625A (en) * 2007-03-23 2007-08-29 广东工业大学 Ketopyrrolidine sulfurate in liquid and its prpearing method
CN101255111A (en) * 2008-03-25 2008-09-03 广东工业大学 A kind of method for ionic liquid catalyzed continuous esterification reaction rectification to synthesize ethyl acetate
CN103124586A (en) * 2010-07-22 2013-05-29 海内肯供应连锁公司 Method for regeneration of PVPP from the retentate of a membrane filter after clarification and stabilization of a yeast-fermented beverage
CN104084234A (en) * 2014-07-16 2014-10-08 沈阳工业大学 Crosslinked polyethylene pyrrolidone based catalyst and preparation method thereof
CN104492485A (en) * 2014-11-26 2015-04-08 绍兴文理学院 Acidic ionic liquid-coated polymeric core solid acid material catalyst and preparation method thereof
CN104525260A (en) * 2014-12-25 2015-04-22 江南大学 Polymeric solid acid catalyst for esterification reaction and preparation method thereof
CN107029784A (en) * 2017-04-25 2017-08-11 福州大学 A kind of Polymer-supported dual-core acidic ionic liquid catalyst and its preparation and application

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
田程程: "交联聚乙烯吡咯烷酮负载型催化剂的性能研究", 中国优秀硕士学位论文全文数据库 工程科技Ⅰ辑, no. 2019, 15 January 2019 (2019-01-15), pages 11 - 22 *

Similar Documents

Publication Publication Date Title
Ren et al. Silver-exchanged heteropolyacid catalyst (Ag1H2PW): An efficient heterogeneous catalyst for the synthesis of 5-ethoxymethylfurfural from 5-hydroxymethylfurfural and fructose
CN102516128B (en) Synthetic technology of diphenylmethane dicarbamate by adopting Bronsted-Lewis acidic ionic liquid catalysis
CN101574667B (en) Solid acid catalyst, preparation thereof and application thereof in esterification reaction
CN104525260B (en) Polymeric solid acid catalyst for esterification reaction and preparation method thereof
CN108689838B (en) Method for preparing formic ether by catalyzing esterification of formic acid and olefin through swellable acidic polyion liquid
CN106732768A (en) A kind of immobilized ionic liquid catalyst for carbon dioxide cycloaddition reaction and preparation method thereof
CN106179453A (en) A kind of carried heteropoly acid catalyst of high stability and its preparation method and application
Liu et al. Facile synthesis of fructone from ethyl acetoacetate and ethylene glycol catalyzed by SO 3 H-functionalized Brønsted acidic ionic liquids
CN108579807B (en) Cross-linked polymerization acidic ionic liquid alkylation catalyst and preparation method thereof
CN110776418A (en) Method for preparing maleic acid ester by catalyzing maleic anhydride with ionic liquid
CN115106125B (en) Preparation method and application of a solid acid catalyst loaded with ionic liquid
CN107141208B (en) Preparation method of 1, 3-dihydroxyacetone
CN116371467A (en) Preparation method and application of solid acid catalyst loaded with acidic ionic liquid
CN110732347A (en) binuclear ionic liquid type heteropoly acid salt solid acid catalyst for synthesizing chalcone derivatives, preparation method and application
CN103406146B (en) Preparation method of immobilized alkaline ionic liquid catalyst
CN117654560B (en) Method for continuously preparing nitro compound by oxidizing amino
CN107903225A (en) A kind of method that 5 hydroxymethylfurfurals are prepared with glucose
CN105669413B (en) A kind of method for preparing 2-methyl-1,4-naphthoquinone by microwave irradiation
CN101973873B (en) Method for synthesizing carboxylic ester by microwave radiation catalysis
CN116574214A (en) A kind of polyionic liquid catalyst and its preparation method and application
CN106378189A (en) A catalyst used for synthesizing polyoxymethylene dimethyl ether, a preparing method thereof and applications of the catalyst
CN117777065A (en) A method for continuously synthesizing 2,2,5,5-tetramethyltetrahydrofuran
CN107382961B (en) Method for preparing 2-thiocarbonyl-2H-thiopyran derivative by chitosan catalysis one-pot method
CN106699504A (en) Preparation method of 2,2-bis(3,4-dimethylphenyl)hexafluoropropane
JP2024503958A (en) Method for producing α-halogenated acetophenone compound using ionic liquid [TEA] [TfOH]2 as a catalyst

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20230704