CN101811067A - Novel CO2 cycloaddion ionic liquid catalyst and preparation method thereof - Google Patents
Novel CO2 cycloaddion ionic liquid catalyst and preparation method thereof Download PDFInfo
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- 229920000642 polymer Polymers 0.000 claims description 11
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2-(2-cyanopropan-2-yldiazenyl)-2-methylpropanenitrile Chemical compound N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 claims description 8
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 claims description 8
- QVRCRKLLQYOIKY-UHFFFAOYSA-M 1-methyl-3-prop-2-enylimidazol-1-ium;chloride Chemical compound [Cl-].C[N+]=1C=CN(CC=C)C=1 QVRCRKLLQYOIKY-UHFFFAOYSA-M 0.000 claims description 7
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Abstract
本发明提供了一种具有高选择性和高转化率的新型高效CO2环加成反应离子液体催化剂,由N-甲基咪唑与烯丙基氯以一定的摩尔比混合,加热至55~70℃,在氮气保护下反应8~12h,得氯化1-烯丙基-3-甲基咪唑离子液体;再由氯化1-烯丙基-3-甲基咪唑离子液体与丙烯酸共聚制得。本发明制备的离子液体催化剂具有较好的热稳定性,对于二氧化碳与环氧化合物反应生成五元环化合物有很高的选择性和转化率,而且其制备方法简单,成本低并且可以重复利用,适合大规模生产,在工业催化领域有着广泛的应用前景。The invention provides a novel high-efficiency CO2 cycloaddition reaction ionic liquid catalyst with high selectivity and high conversion rate, which is composed of N-methylimidazole and allyl chloride mixed in a certain molar ratio and heated to 55-70 ℃, under the protection of nitrogen, react for 8-12 hours to obtain 1-allyl-3-methylimidazolium chloride ionic liquid; then it is prepared by copolymerization of 1-allyl-3-methylimidazolium chloride ionic liquid and acrylic acid . The ionic liquid catalyst prepared by the present invention has good thermal stability, has high selectivity and conversion rate for the reaction of carbon dioxide and epoxy compounds to generate five-membered ring compounds, and its preparation method is simple, low in cost and can be reused. It is suitable for large-scale production and has broad application prospects in the field of industrial catalysis.
Description
技术领域technical field
本发明属于工业催化技术领域,涉及一种CO2环加成反应催化剂,尤其涉及一种具有高选择性和高转化率的新型高效CO2环加成反应催化剂。The invention belongs to the technical field of industrial catalysis, and relates to a CO2 cycloaddition reaction catalyst, in particular to a novel high-efficiency CO2 cycloaddition reaction catalyst with high selectivity and high conversion rate.
背景技术Background technique
随着世界各国工业化进程加快,人口不断增多,煤、石油及天然气等资源的需求越来越大,这些地球上储量有限而又不可再生的资源在大量被消耗着。而且还因燃烧排放而导致区域大气污染及“温室效应”。据统计,近100年以来,地表温度上升了0.6℃,相当于大气中CO2每增加10%,则地表温度上升0.43℃。根据有关资料中介绍,大气中CO2浓度每增加一倍,气温将增加2.8~5.2℃。气候变暖还将引起地球气候的很大变化,给人类生存构成严重威胁。因此,必须采取相应对策,减少CO2向大气的排放。除了对CO2的排放加以限制外,另一个有效措施就是对这些产生的CO2加以回收利用,将其转化为化学品、燃料,或其它有用的产品。其中CO2和环氧化合物经过催化偶联生成环碳酸酯的反应就是一种有效的办法。这是因为环碳酸酯是可以广泛的应用于聚合物合成的单体、极性非质子型溶剂、药物中间体以及其他的生物化学应用。而且CO2与环氧化合物直接偶联生成碳酸酯,没有其它的副产物产生,符合绿色化学与原子经济性等观点。With the acceleration of industrialization and the increasing population of countries all over the world, the demand for resources such as coal, oil and natural gas is increasing. These limited and non-renewable resources on the earth are being consumed in large quantities. Moreover, it also causes regional air pollution and "greenhouse effect" due to combustion emissions. According to statistics, in the past 100 years, the surface temperature has increased by 0.6°C, which means that for every 10% increase in CO 2 in the atmosphere, the surface temperature will rise by 0.43°C. According to relevant information, every time the concentration of CO 2 in the atmosphere doubles, the temperature will increase by 2.8-5.2°C. Climate warming will also cause great changes in the earth's climate, posing a serious threat to human existence. Therefore, corresponding countermeasures must be taken to reduce CO2 emissions to the atmosphere. In addition to limiting CO 2 emissions, another effective measure is to recycle the generated CO 2 and convert it into chemicals, fuels, or other useful products. Among them, the reaction of CO2 and epoxy compound to generate cyclocarbonate through catalytic coupling is an effective method. This is because cyclic carbonates are widely used as monomers for polymer synthesis, polar aprotic solvents, pharmaceutical intermediates, and other biochemical applications. Moreover, CO 2 is directly coupled with epoxy compounds to form carbonates, and no other by-products are produced, which is in line with the views of green chemistry and atom economy.
自1943年,Karl首次发现氢氧化钠负载于活性炭上能有效催化与环氧化合物环加成反应以来,到目前为止,人们相继开发出金属氧化物,碱金属的卤化物,离子液体等新型催化剂。作为与环氧化物的环加成反应催化剂,离子液体的环境友好特性使其相对于传统的季胺盐催化剂反应条件更温和,催化反应活性和产物选择性更高,同时反应不需要溶剂等优点,成为新型的反应催化剂。但是,离子液体作为催化剂催化反应完成之后,需要减压蒸馏使产物和离子液体分离,这样从能量消耗的角度考虑,不适合工业化生产。从实际应用的角度看,目前催化剂活性仍不能令人满意。因此,开发简单、易于分离、可工业化、高效的催化剂是当前研究的重中之重。Since Karl first discovered that sodium hydroxide supported on activated carbon can effectively catalyze the cycloaddition reaction with epoxy compounds in 1943, so far, people have successively developed new catalysts such as metal oxides, alkali metal halides, and ionic liquids. . As a catalyst for the cycloaddition reaction with epoxides, the environmental friendliness of ionic liquids makes the reaction conditions milder than traditional quaternary ammonium salt catalysts, the catalytic reaction activity and product selectivity are higher, and the reaction does not require solvents, etc. , as a new type of reaction catalyst. However, after the ionic liquid is used as a catalyst to catalyze the reaction, vacuum distillation is required to separate the product from the ionic liquid, which is not suitable for industrial production from the perspective of energy consumption. From the point of view of practical application, the catalyst activity is still not satisfactory. Therefore, the development of simple, easy-to-separate, industrializable, and highly efficient catalysts is the top priority of current research.
发明内容Contents of the invention
本发明的目的是提供一种具有高选择性和高转化率的新型高效CO2环加成反应离子液体催化剂。The object of the present invention is to provide a novel high-efficiency CO2 cycloaddition reaction ionic liquid catalyst with high selectivity and high conversion.
本发明的另一目的是提供一种该新型高效CO2环加成反应离子液体催化剂的制备方法。Another object of the present invention is to provide a preparation method of the novel high-efficiency CO cycloaddition reaction ionic liquid catalyst.
一、新型CO2环加成反应催化剂1. Novel CO2 cycloaddition reaction catalyst
本发明的新型CO2环加成反应离子液体催化剂,其结构式如下:Novel CO of the present invention cycloaddition reaction ionic liquid catalyst, its structural formula is as follows:
二、新型CO2环加成反应催化剂的制备2. Preparation of novel CO2 cycloaddition reaction catalysts
本发明新型CO2环加成反应催化剂的制备方法,包括以下工艺步骤:Novel CO of the present invention The preparation method of cycloaddition reaction catalyst comprises the following processing steps:
(1)氯化1-烯丙基-3-甲基咪唑离子液体的合成:将N-甲基咪唑和烯丙基氯以1∶1.10~1∶1.11的摩尔比混合,加热至55~70℃,在氮气保护下反应8~12h,得氯化1-烯丙基-3-甲基咪唑离子液体;(1) Synthesis of chlorinated 1-allyl-3-methylimidazolium ionic liquid: N-methylimidazole and allyl chloride are mixed in a molar ratio of 1:1.10 to 1:1.11 and heated to 55 to 70 °C, react for 8-12 hours under the protection of nitrogen to obtain 1-allyl-3-methylimidazolium chloride ionic liquid;
(2)离子液体催化剂的制备:将氯化1-烯丙基-3-甲基咪唑离子液体与丙烯酸以1∶5~1∶10的摩尔比混合,再向其中加入丙烯酸摩尔量2~5倍的N,N-二甲基甲酰胺和丙烯酸摩尔量1~2%的偶氮二异丁腈,在氮气保护下于60~70℃反应24~36h;然后用氯仿沉淀,过滤,干燥得浅黄色的目标聚合物。(2) Preparation of ionic liquid catalyst: mix 1-allyl-3-methylimidazolium chloride ionic liquid with acrylic acid at a molar ratio of 1:5 to 1:10, and then add 2 to 5 moles of acrylic acid to it. Double N,N-dimethylformamide and azobisisobutyronitrile with 1-2% molar weight of acrylic acid, react at 60-70°C for 24-36h under the protection of nitrogen; then precipitate with chloroform, filter and dry to obtain Light yellow target polymer.
其合成路线如下:Its synthetic route is as follows:
三、聚合物的表征3. Characterization of polymers
下面通过具体实验对本发明制备的聚合物(新型CO2环加成反应催化剂)用红外、热重、元素分析、光散射进行表征。The polymer (new CO 2 cycloaddition reaction catalyst) prepared by the present invention is characterized by infrared, thermogravimetric, elemental analysis, and light scattering through specific experiments below.
1、实验原料1. Experimental raw materials
烯丙基氯、氯仿均为分析纯,购买于国药集团化学试剂有限公司,未经处理直接使用。N,N-二甲基甲酰胺(DMF)、丙烯酸使用之前重蒸。偶氮二异丁腈为工业级。Allyl chloride and chloroform were of analytical grade, purchased from Sinopharm Chemical Reagent Co., Ltd., and used directly without treatment. N,N-Dimethylformamide (DMF), acrylic acid were redistilled before use. Azobisisobutyronitrile is technical grade.
2聚合物的表征2 Characterization of polymers
(1)红外光谱(1) Infrared Spectrum
样品用KBr压片后,用美国尼高尼公司产360型FT-IR光谱仪测试。After the samples were compressed with KBr, they were tested with a 360 FT-IR spectrometer produced by Nigoni Company, USA.
图1为催化剂的红外谱图。从图1可以看出,在1553cm-1的吸收峰为甲基咪唑上面C=N的谱峰,而在聚丙烯酸的标准谱峰在1553cm-1处没有C=N的谱峰,由此可以看出,我们成功的将丙烯酸和离子液体共聚到了一起。Fig. 1 is the infrared spectrogram of catalyst. As can be seen from Fig. 1, the absorption peak at 1553cm -1 is the spectrum peak of C=N above the methylimidazole, while the standard spectrum peak of polyacrylic acid does not have the spectrum peak of C=N at 1553cm -1 place, thus can It can be seen that we successfully copolymerized acrylic acid and ionic liquid together.
(2)热失重分析:(2) Thermogravimetric analysis:
热失重分析(TG-DTA)用TG-DTA 2000S测得,扫描范围30~500℃,升温速率10℃·min-1,氮气流速100mL·min-1。Thermogravimetric analysis (TG-DTA) was measured by TG-DTA 2000S, with a scanning range of 30-500°C, a heating rate of 10°C·min -1 , and a nitrogen flow rate of 100mL·min -1 .
图2为新型CO2环加成反应催化剂的热失重曲线。从图2中可以看出,在150℃之前,失重了1%,是由于聚合物吸水的原因。说明本发明制备的催化剂在150℃之前是稳定的,热失重分析表明,本发明制备的新型催化剂具有较好的热稳定性,可以成功地应用到CO2环加成反应。Figure 2 is the thermogravimetric curve of the novel CO2 cycloaddition reaction catalyst. It can be seen from Figure 2 that before 150°C, the weight loss of 1% is due to the water absorption of the polymer. It shows that the catalyst prepared by the present invention is stable before 150°C, and the thermogravimetric analysis shows that the novel catalyst prepared by the present invention has good thermal stability and can be successfully applied to the CO 2 cycloaddition reaction.
(3)元素分析(3) Elemental analysis
元素分析结果:N:3.80%,C:48.29%,H:5.67%,Cl:13.91%,O:28.33%。表明每一克聚合物上面负载3.9mmol离子液体。Elemental analysis results: N: 3.80%, C: 48.29%, H: 5.67%, Cl: 13.91%, O: 28.33%. It was shown that 3.9 mmol of ionic liquid was loaded on each gram of polymer.
(4)光散射分析(4) Light scattering analysis
采用用光散射仪器(型号Wyatt Technology DAWN EOS),以醋酸溶液作为流动相,测定其重均分子量。Using a light scattering instrument (model Wyatt Technology DAWN EOS), with acetic acid solution as the mobile phase, the weight average molecular weight was measured.
光散射分析结果:本发明制备的新型CO2环加成反应催化剂的重均分子量为Mw=2645,D=1.27。从D值可以知道,该聚合物的分散系数接近于1,表明聚合物分散度好。Light scattering analysis results: the weight average molecular weight of the novel CO 2 cycloaddition reaction catalyst prepared by the present invention is Mw =2645, D=1.27. It can be known from the D value that the dispersion coefficient of the polymer is close to 1, indicating that the dispersion of the polymer is good.
四、催化剂在CO2环加成反应的应用4. Application of Catalysts in CO2 Cycloaddition Reaction
下面通过具体实验说明本发明的新型催化剂对二氧化碳与环氧化合物反应生成五元环化合物的催化效果。The following specific experiments illustrate the catalytic effect of the new catalyst of the present invention on the reaction of carbon dioxide and epoxy compounds to form five-membered ring compounds.
试验方法:在50mL的不锈钢高压反应釜中加入10ml的环氧氯丙烷,磁子,0.1g本发明制备的催化剂,置换空气后,先升温至设定温度,再通二氧化碳调节压力,在搅拌下进行反应一定时间。反应结束后,先用冰盐浴冷却,再放气,得到的混合物过滤,得到相应的环碳酸酯。Test method: Add 10ml of epichlorohydrin, magneton, and 0.1g of the catalyst prepared by the present invention into a 50mL stainless steel high-pressure reaction kettle. After replacing the air, first heat up to the set temperature, and then pass carbon dioxide to adjust the pressure. to react for a certain period of time. After the reaction was completed, it was cooled with an ice-salt bath, and then deflated, and the obtained mixture was filtered to obtain the corresponding cyclocarbonate.
反应式如下:The reaction formula is as follows:
本发明催化剂在CO2环加成反应中转化率和选择性随反应时间、温度的变化曲线见图3、图4。从图3、图4可知,随着温度的升高,转化率先增大,到120℃达到最大转化率:90%,选择性为99%。随着时间的延长,转化率先增大后减小,当反应时间为2h时,转化率达到最大值:90%,选择性为99%。上述实验证明,本发明制备的催化剂是CO2环加成反应的催化剂,对于二氧化碳与环氧化合物反应生成五元环化合物有很高的选择性和转化率,并且可以重复利用。The curves of the conversion rate and selectivity of the catalyst of the present invention in the CO2 cycloaddition reaction with reaction time and temperature are shown in Fig. 3 and Fig. 4 . It can be seen from Figure 3 and Figure 4 that as the temperature increases, the conversion increases first, and reaches the maximum conversion rate of 90% at 120°C, with a selectivity of 99%. With the prolongation of time, the conversion first increased and then decreased. When the reaction time was 2h, the conversion reached the maximum value: 90%, and the selectivity was 99%. The above experiments prove that the catalyst prepared by the present invention is a catalyst for the CO2 cycloaddition reaction, has high selectivity and conversion rate for the reaction of carbon dioxide and epoxy compounds to form five-membered ring compounds, and can be reused.
通过大量的研究发现:环氧化合物与CO2环加成反应在该催化剂存在的条件下,在1.25Mpa,温度为115℃,反应时间为1h时效果最佳。Through a lot of research, it is found that the cycloaddition reaction between epoxy compound and CO 2 has the best effect under the condition of the presence of the catalyst, at 1.25Mpa, the temperature is 115°C, and the reaction time is 1h.
本发明与现有技术相比具有以下优点:Compared with the prior art, the present invention has the following advantages:
1、本发明制备的催化剂具有较好的热稳定性,与环氧化合物反应生成五元环化合物有很高的选择性和转化率。1. The catalyst prepared by the present invention has good thermal stability, and reacts with epoxy compounds to form five-membered ring compounds with high selectivity and conversion rate.
2、本发明高效催化剂的制备方法简单,成本低,并且可以重复利用,适合大规模生产,在工业催化领域有着广泛的应用前景。2. The preparation method of the high-efficiency catalyst of the present invention is simple, low in cost, reusable, suitable for large-scale production, and has broad application prospects in the field of industrial catalysis.
附图说明Description of drawings
图1为本发明CO2环加成反应催化剂的红外谱图Fig. 1 is the infrared spectrogram of CO of the present invention Cycloaddition reaction catalyst
图2为本发明CO2环加成反应催化剂的热失重曲线Fig. 2 is the thermogravity curve of CO cycloaddition reaction catalyst of the present invention
图3为本发明催化剂在CO2环加成反应中转化率和选择性随反应时间的变化曲线Fig. 3 is the change curve of conversion rate and selectivity with reaction time in CO cycloaddition reaction of catalyst of the present invention
图4为本发明催化剂在CO2环加成反应中转化率和选择性随反应温度的变化曲线Fig. 4 is the change curve of conversion rate and selectivity with reaction temperature in CO cycloaddition reaction of catalyst of the present invention
具体实施方式Detailed ways
实施例1、新型CO2环加成反应催化剂的制备
1、氯化1-烯丙基-3-甲基咪唑离子液体的合成:将N-甲基咪唑和烯丙基氯按1∶1.11的摩尔比混合,加热至55℃,在氮气保护下反应8h,得氯化1-烯丙基-3-甲基咪唑离子液体,产率:78%。1. Synthesis of chlorinated 1-allyl-3-methylimidazolium ionic liquid: mix N-methylimidazole and allyl chloride at a molar ratio of 1:1.11, heat to 55°C, and react under nitrogen protection 8h, 1-allyl-3-methylimidazolium chloride ionic liquid was obtained, yield: 78%.
2、氯化1-烯丙基-3-甲基咪唑离子液体与丙烯酸共聚制备离子液体:将氯化1-烯丙基-3-甲基咪唑离子液体与丙烯酸按1∶8的摩尔比混合,再加入丙烯酸摩尔量2倍的N,N-二甲基甲酰胺(DMF)和丙烯酸摩尔量1%的偶氮二异丁腈,于70℃、氮气保护下反应24h,然后用氯仿沉淀,过滤,得到浅黄色的聚合物,真空干燥箱100℃干燥24h即得。产率:51%。2. Preparation of ionic liquid by copolymerization of 1-allyl-3-methylimidazolium chloride ionic liquid and acrylic acid: mixing 1-allyl-3-methylimidazolium chloride ionic liquid with acrylic acid in a molar ratio of 1:8 , then add N,N-dimethylformamide (DMF) with 2 times the molar weight of acrylic acid and azobisisobutyronitrile with 1% molar weight of acrylic acid, react at 70°C for 24h under the protection of nitrogen, and then precipitate with chloroform, Filter to obtain a light yellow polymer, and dry it in a vacuum oven at 100°C for 24 hours. Yield: 51%.
实施例2、催化CO2环加成反应
在50mL的不锈钢高压反应釜中加入10ml的环氧氯丙烷,磁子,0.1g本发明的催化剂,置换空气后,先升温150℃,再通二氧化碳,调节反应釜的压力至1.25Mpa,搅拌,反应1h时。反应结束后,先用冰盐浴冷却,再放气,得到的混合物过滤,得到相应的环碳酸酯。转化率为92%。Add 10ml of epichlorohydrin, magneton, and 0.1g of the catalyst of the present invention into a 50mL stainless steel autoclave. After replacing the air, first raise the temperature to 150° C., then pass carbon dioxide, adjust the pressure of the reactor to 1.25Mpa, and stir. When reacting for 1h. After the reaction was completed, it was cooled with an ice-salt bath, and then deflated, and the obtained mixture was filtered to obtain the corresponding cyclocarbonate. The conversion rate was 92%.
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US9260405B2 (en) | 2013-10-24 | 2016-02-16 | Industrial Technology Research Institute | Cayalyst system and manufacturing method of cyclic carbonate by the same |
CN107626308A (en) * | 2017-08-30 | 2018-01-26 | 江南大学 | One kind is used for CO2The hydrotalcite carried with doped Au catalyst and preparation method of cycloaddition reaction and bisphenol synthesis F |
CN114733550A (en) * | 2022-04-29 | 2022-07-12 | 四川鸿鹏新材料有限公司 | Production process of ethylene carbonate and catalyst for production |
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CN101037431A (en) * | 2006-03-16 | 2007-09-19 | 中国科学院兰州化学物理研究所 | Method for synthesizing cricoid carbonate by addition reaction of carbon dioxide and epoxy compound ring |
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US9260405B2 (en) | 2013-10-24 | 2016-02-16 | Industrial Technology Research Institute | Cayalyst system and manufacturing method of cyclic carbonate by the same |
CN107626308A (en) * | 2017-08-30 | 2018-01-26 | 江南大学 | One kind is used for CO2The hydrotalcite carried with doped Au catalyst and preparation method of cycloaddition reaction and bisphenol synthesis F |
CN107626308B (en) * | 2017-08-30 | 2020-08-04 | 江南大学 | For CO2Hydrotalcite loaded gold-doped catalyst for cycloaddition reaction and bisphenol F synthesis and preparation method thereof |
CN114733550A (en) * | 2022-04-29 | 2022-07-12 | 四川鸿鹏新材料有限公司 | Production process of ethylene carbonate and catalyst for production |
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