CN104324749B - A kind of alkaline ionic liquid catalyst of based on POSS of carbonate synthesis glyceride and preparation method thereof - Google Patents
A kind of alkaline ionic liquid catalyst of based on POSS of carbonate synthesis glyceride and preparation method thereof Download PDFInfo
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- 239000003054 catalyst Substances 0.000 title claims abstract description 38
- 238000002360 preparation method Methods 0.000 title claims abstract description 20
- 239000002608 ionic liquid Substances 0.000 title claims abstract description 14
- 230000015572 biosynthetic process Effects 0.000 title abstract description 3
- 238000003786 synthesis reaction Methods 0.000 title abstract description 3
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 title 1
- 125000005456 glyceride group Chemical group 0.000 title 1
- JFMGYULNQJPJCY-UHFFFAOYSA-N 4-(hydroxymethyl)-1,3-dioxolan-2-one Chemical compound OCC1COC(=O)O1 JFMGYULNQJPJCY-UHFFFAOYSA-N 0.000 claims abstract description 20
- 239000011830 basic ionic liquid Substances 0.000 claims abstract description 19
- 230000002194 synthesizing effect Effects 0.000 claims abstract description 10
- RAXXELZNTBOGNW-UHFFFAOYSA-N imidazole Natural products C1=CNC=N1 RAXXELZNTBOGNW-UHFFFAOYSA-N 0.000 claims description 33
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 23
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 18
- 238000006243 chemical reaction Methods 0.000 claims description 14
- 238000003756 stirring Methods 0.000 claims description 14
- 238000000034 method Methods 0.000 claims description 13
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims description 9
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 9
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 7
- MCTWTZJPVLRJOU-UHFFFAOYSA-N 1-methyl-1H-imidazole Chemical group CN1C=CN=C1 MCTWTZJPVLRJOU-UHFFFAOYSA-N 0.000 claims description 6
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 6
- 239000002243 precursor Substances 0.000 claims description 6
- 239000011949 solid catalyst Substances 0.000 claims description 6
- IEJIGPNLZYLLBP-UHFFFAOYSA-N dimethyl carbonate Chemical compound COC(=O)OC IEJIGPNLZYLLBP-UHFFFAOYSA-N 0.000 claims description 5
- 238000003760 magnetic stirring Methods 0.000 claims description 4
- 239000000376 reactant Substances 0.000 claims description 4
- 230000035484 reaction time Effects 0.000 claims description 4
- 239000002904 solvent Substances 0.000 claims description 4
- IWDFHWZHHOSSGR-UHFFFAOYSA-N 1-ethylimidazole Chemical compound CCN1C=CN=C1 IWDFHWZHHOSSGR-UHFFFAOYSA-N 0.000 claims description 3
- KSCAZPYHLGGNPZ-UHFFFAOYSA-N 3-chloropropyl(triethoxy)silane Chemical compound CCO[Si](OCC)(OCC)CCCCl KSCAZPYHLGGNPZ-UHFFFAOYSA-N 0.000 claims description 3
- 238000009833 condensation Methods 0.000 claims description 3
- 230000005494 condensation Effects 0.000 claims description 3
- 239000013078 crystal Substances 0.000 claims description 3
- WCRDXYSYPCEIAK-UHFFFAOYSA-N dibutylstannane Chemical compound CCCC[SnH2]CCCC WCRDXYSYPCEIAK-UHFFFAOYSA-N 0.000 claims description 3
- 239000002244 precipitate Substances 0.000 claims description 3
- 238000010992 reflux Methods 0.000 claims description 3
- 238000002390 rotary evaporation Methods 0.000 claims description 3
- 239000007787 solid Substances 0.000 claims description 3
- DHXVGJBLRPWPCS-UHFFFAOYSA-N Tetrahydropyran Chemical compound C1CCOCC1 DHXVGJBLRPWPCS-UHFFFAOYSA-N 0.000 claims description 2
- FUOZJYASZOSONT-UHFFFAOYSA-N 2-propan-2-yl-1h-imidazole Chemical class CC(C)C1=NC=CN1 FUOZJYASZOSONT-UHFFFAOYSA-N 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 238000012986 modification Methods 0.000 abstract description 2
- 230000004048 modification Effects 0.000 abstract description 2
- 230000003197 catalytic effect Effects 0.000 abstract 1
- 235000011187 glycerol Nutrition 0.000 description 7
- 239000003225 biodiesel Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- XLXCHZCQTCBUOX-UHFFFAOYSA-N 1-prop-2-enylimidazole Chemical compound C=CCN1C=CN=C1 XLXCHZCQTCBUOX-UHFFFAOYSA-N 0.000 description 2
- IPIORGCOGQZEHO-UHFFFAOYSA-N 1-propan-2-ylimidazole Chemical compound CC(C)N1C=CN=C1 IPIORGCOGQZEHO-UHFFFAOYSA-N 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- OSSNTDFYBPYIEC-UHFFFAOYSA-N 1-ethenylimidazole Chemical compound C=CN1C=CN=C1 OSSNTDFYBPYIEC-UHFFFAOYSA-N 0.000 description 1
- 229920005830 Polyurethane Foam Polymers 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
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Abstract
本发明公开了一种合成碳酸甘油酯的基于POSS(Polyhedral Oligomeric Silsesquioxanes,多面体低聚倍半硅氧烷)的碱性离子液体催化剂及其制备方法。催化剂载体是八氯丙基倍半硅氧烷POSS‑Cl,修饰组分是碱性离子液体。催化剂的制备方法为:首先合成POSS‑Cl,然后进行碱性离子液体的固载,对POSS进行修饰,制得基于POSS的碱性离子液体催化剂。本发明的优点在于,所制得的催化剂用于催化合成碳酸甘油酯体系,催化效率高,无溶剂,催化剂可循环使用,生产过程对环境友好。The invention discloses a basic ionic liquid catalyst based on POSS (Polyhedral Oligomeric Silsesquioxanes, polyhedral oligomeric silsesquioxanes) for synthesizing glycerol carbonate and a preparation method thereof. The catalyst carrier is octachloropropylsilsesquioxane POSS‑Cl, and the modification component is alkaline ionic liquid. The preparation method of the catalyst is as follows: first synthesizing POSS-Cl, and then carrying out immobilization of the basic ionic liquid, modifying the POSS, and obtaining the basic ionic liquid catalyst based on the POSS. The invention has the advantages that the prepared catalyst is used to catalyze the synthesis of glycerol carbonate system, has high catalytic efficiency, is solvent-free, can be recycled, and the production process is environmentally friendly.
Description
技术领域technical field
本发明涉及合成碳酸甘油酯的基于POSS的碱性离子液体催化剂的制备及应用,属于甘油应用的技术领域。The invention relates to the preparation and application of a POSS-based alkaline ionic liquid catalyst for synthesizing glycerol carbonate, and belongs to the technical field of glycerin application.
背景技术Background technique
全球对石油资源紧缺和环境保护日益重视,发展生物柴油合成成为全球新能源开发的热点。在生物柴油生产过程中会副产大量甘油,其有效利用制约着生物柴油生产的经济性。因此,以甘油为原料的化学品的研究和应用引起世界各国的广泛关注。The world is paying more and more attention to the shortage of petroleum resources and environmental protection, and the development of biodiesel synthesis has become a hot spot in the development of new energy sources in the world. In the process of biodiesel production, a large amount of glycerol will be produced by-product, and its effective utilization restricts the economical efficiency of biodiesel production. Therefore, the research and application of chemicals using glycerol as raw materials has attracted widespread attention from all over the world.
碳酸甘油酯作为一种绿色可再生的化学品,可以广泛的应用于聚氨酯泡沫塑料、涂料、洗涤剂、化妆品行业。同时碳酸甘油酯作为有机化工的重要的中间体,具有可燃性低、毒性小、沸点高、可生物降解等优势,具有很好的工业应用前景。As a green and renewable chemical, glycerol carbonate can be widely used in polyurethane foam, coatings, detergents, and cosmetics industries. At the same time, as an important intermediate of organic chemical industry, glycerol carbonate has the advantages of low flammability, low toxicity, high boiling point, biodegradability, etc., and has a good industrial application prospect.
碱性离子液体作为一种新型的环境友好溶剂和液体催化剂,近几年得到催化领域的广泛应用,具有高密度反应活性位和固体催化剂的不挥发性,其结构和活性位具有可调性,是真正意义上可设计的绿色催化剂。然而大多数离子液体反应之后难以与产物分离,制约其催化制备碳酸甘油酯的工业化进程。As a new type of environmentally friendly solvent and liquid catalyst, alkaline ionic liquid has been widely used in the field of catalysis in recent years. It has high-density reactive sites and non-volatility of solid catalysts. Its structure and active sites are adjustable. It is a truly designable green catalyst. However, most ionic liquids are difficult to separate from the product after the reaction, which restricts the industrialization process of its catalyzed preparation of glycerol carbonate.
采用新型的POSS作载体,碱性离子液体作修饰组分,制得的基于POSS的碱性离子液体催化剂既具有均相催化剂的高活性,又避免了非均相催化过程中的扩散限制,同时赋予了催化剂易分离特性,简化了操作流程,降低了操作成本,目前引起人们广泛关注。Using a new type of POSS as a carrier and a basic ionic liquid as a modification component, the prepared POSS-based basic ionic liquid catalyst not only has the high activity of a homogeneous catalyst, but also avoids the diffusion limitation in the heterogeneous catalysis process, and at the same time It endows the catalyst with the characteristics of easy separation, simplifies the operation process, and reduces the operation cost, which has attracted widespread attention at present.
为了解决上述问题,本发明提供一种合成碳酸甘油酯的基于POSS的碱性离子液体催化剂及其制备方法,符合绿色化学的要求,有着诱人的工业化前景。In order to solve the above problems, the present invention provides a POSS-based alkaline ionic liquid catalyst for synthesizing glycerol carbonate and a preparation method thereof, which meet the requirements of green chemistry and have attractive industrialization prospects.
发明内容Contents of the invention
本发明的目的在于提供了一种合成碳酸甘油酯的基于POSS的碱性离子液体催化剂及其制备方法。以该方法所制得的催化剂具有活性高和易分离特性。The object of the present invention is to provide a kind of basic ionic liquid catalyst based on POSS of synthesizing glycerol carbonate and preparation method thereof. The catalyst prepared by the method has the characteristics of high activity and easy separation.
本发明通过下述技术方案加以实现的,一种合成碳酸甘油酯的基于POSS的碱性离子液体催化剂,所述的是甘油和碳酸二甲酯合成碳酸甘油酯,合成碳酸甘油酯的基于POSS的碱性离子液体催化剂的制备方法,其特征在于包括以下过程,The present invention is realized by following technical scheme, a kind of alkaline ionic liquid catalyst based on POSS of synthesizing glycerol carbonate, described is glycerol and dimethyl carbonate synthesizing glycerol carbonate, synthesizing glycerol carbonate based on POSS The preparation method of alkaline ionic liquid catalyst is characterized in that comprising following process,
(1)POSS-Cl的制备:取甲醇100~200ml,浓盐酸5~15ml加入三口烧瓶中,并将3-氯丙基三乙氧基硅烷10~20g逐滴滴加到上述溶液中,机械搅拌30~50h后,将缩合催化剂0.1~0.2g二丁基锡烷添加到上述混合物,于40~60℃的油浴中反应30~50h降至室温,得到白色晶型沉淀八氯丙基倍半硅氧烷POSS-Cl;(1) Preparation of POSS-Cl: Take 100-200ml of methanol, 5-15ml of concentrated hydrochloric acid into a three-necked flask, and add 10-20g of 3-chloropropyltriethoxysilane dropwise into the above solution, mechanically After stirring for 30 to 50 hours, add 0.1 to 0.2 g of dibutylstannane as a condensation catalyst to the above mixture, react in an oil bath at 40 to 60°C for 30 to 50 hours and cool down to room temperature to obtain a white crystal precipitate of octachloropropyl silsesquisil Oxane POSS-Cl;
(2)碱性离子液体的固载:在三口圆底烧瓶中将0.1~0.3g POSS-Cl溶于20~30ml二甲基甲酰胺,并缓慢滴加0.08~0.1mol的N-烷基咪唑,磁力搅拌下升温至60~75℃,滴加完毕继续搅拌回流18~32h,减压抽滤,乙酸乙酯洗涤2~5次得白色固体,最后在60~90℃下真空干燥18~32h,得到前驱体,取0.8~2g KOH加入50ml单口圆底烧瓶中,并加入10~20ml二甲基甲酰胺,在常温下搅拌使其溶解,分批加入上述前驱体0.1~0.3g,在磁力搅拌下室温反应2~5h,再向瓶中加入4~8ml乙醚,继续在室温下反应18~32h,停止反应,旋蒸除去溶剂,得到固态催化剂基于POSS的咪唑碱性离子液体。(2) Immobilization of basic ionic liquid: Dissolve 0.1-0.3g POSS-Cl in 20-30ml dimethylformamide in a three-necked round-bottomed flask, and slowly add 0.08-0.1mol of N-alkylimidazole dropwise , heated up to 60-75°C under magnetic stirring, continued to stir and reflux for 18-32 hours after the dropwise addition, filtered under reduced pressure, washed 2-5 times with ethyl acetate to obtain a white solid, and finally dried in vacuum at 60-90°C for 18-32 hours , to obtain the precursor, take 0.8-2g KOH and put it into a 50ml single-necked round bottom flask, and add 10-20ml dimethylformamide, stir at room temperature to dissolve, add 0.1-0.3g of the above-mentioned precursor in batches, Stir and react at room temperature for 2 to 5 hours, then add 4 to 8 ml of ether into the bottle, continue to react at room temperature for 18 to 32 hours, stop the reaction, remove the solvent by rotary evaporation, and obtain an imidazole basic ionic liquid based on POSS as a solid catalyst.
上述N-烷基咪唑为N-甲基咪唑、N-乙基咪唑、N-异丙基咪唑、N-烯丙基咪唑或N-乙烯基咪唑的任何一种。The aforementioned N-alkylimidazole is any one of N-methylimidazole, N-ethylimidazole, N-isopropylimidazole, N-allylimidazole or N-vinylimidazole.
上述制得基于POSS的碱性离子液体催化剂用于合成碳酸甘油酯的工艺,其特征在于包括以下过程:The above-mentioned making based on POSS alkaline ionic liquid catalyst is used for the technique of synthetic glycerol carbonate, it is characterized in that comprising following process:
(1)将甘油和碳酸二甲酯按照摩尔比1∶5~1∶15加入反应器中,再加入质量为反应物总质量的1~10%的基于POSS的碱性离子液体催化剂,在反应温度为50~200℃,压力为1~3Mpa,搅拌速率为500~1200rpm条件下,反应时间为1~10h,得到含有碳酸甘油酯的混合物;(1) Glycerol and dimethyl carbonate are added in the reactor according to the molar ratio of 1: 5~1: 15, and then adding quality is the alkaline ionic liquid catalyst based on POSS of 1~10% of the total mass of reactant, in reaction The temperature is 50-200°C, the pressure is 1-3Mpa, the stirring rate is 500-1200rpm, and the reaction time is 1-10h to obtain a mixture containing glycerol carbonate;
(2)对步骤(1)混合物进行过滤,滤出的固体催化剂继续循环使用。(2) Filter the mixture in step (1), and continue to recycle the filtered solid catalyst.
本发明的优点在于,催化剂具有活性高和易分离特性,可望成为极具竞争力的清洁工艺路线。The advantage of the invention is that the catalyst has the characteristics of high activity and easy separation, and is expected to become a very competitive cleaning process route.
下面通过具体实施例来对本发明加以进一步说明,但不限制本发明。The present invention will be further described below through specific examples, but the present invention will not be limited.
具体实施方式detailed description
【实施例1】【Example 1】
POSS-Cl的制备:取甲醇150ml,浓盐酸10ml加入三口烧瓶中,并将3-氯丙基三乙氧基硅烷15g逐滴滴加到上述溶液中,机械搅拌32h后,将缩合催化剂0.12g二丁基锡烷添加到上述混合物,于50℃的油浴中反应36h降至室温得到白色晶型沉淀八氯丙基倍半硅氧烷POSS-Cl;Preparation of POSS-Cl: Add 150ml of methanol and 10ml of concentrated hydrochloric acid into a three-necked flask, and add 15g of 3-chloropropyltriethoxysilane dropwise into the above solution, after mechanical stirring for 32h, add 0.12g of condensation catalyst Dibutylstannane was added to the above mixture, reacted in an oil bath at 50°C for 36 hours and cooled to room temperature to obtain a white crystal precipitate of octachloropropylsilsesquioxane POSS-Cl;
碱性离子液体的固载:在三口圆底烧瓶中将0.15g的POSS-Cl溶于25ml二甲基甲酰胺,并缓慢滴加N-甲基咪唑0.08mol,磁力搅拌下升温至60℃,滴加完后,继续搅拌回流24h,减压抽滤,乙酸乙酯洗涤3次得白色固体,最后在65℃下真空干燥24h,得到前驱体。取1g的KOH加入50ml单口圆底烧瓶中,并加入15ml二甲基甲酰胺,在常温下搅拌使其溶解,分批加入0.2g前驱体,在磁力搅拌下室温反应3h,再向瓶中加入6ml乙醚,继续在室温下反应24h,停止反应,旋蒸除去溶剂,得到固态催化剂基于POSS的咪唑碱性离子液体。Immobilization of basic ionic liquid: Dissolve 0.15g of POSS-Cl in 25ml of dimethylformamide in a three-neck round bottom flask, slowly add 0.08mol of N-methylimidazole dropwise, and raise the temperature to 60°C under magnetic stirring. After the dropwise addition, continue to stir and reflux for 24 h, filter under reduced pressure, wash with ethyl acetate three times to obtain a white solid, and finally vacuum dry at 65° C. for 24 h to obtain a precursor. Take 1g of KOH and add it to a 50ml single-necked round bottom flask, and add 15ml of dimethylformamide, stir at room temperature to dissolve, add 0.2g of precursor in batches, react at room temperature for 3h under magnetic stirring, and then add 6ml of diethyl ether, continue to react at room temperature for 24h, stop the reaction, and remove the solvent by rotary evaporation to obtain a POSS-based imidazole basic ionic liquid as a solid catalyst.
【实施例2】[Example 2]
在催化剂的制备条件与实施例1完全相同的情况下,只将制备方法中的N-甲基咪唑改为N-乙基咪唑,得到基于POSS的咪唑碱性离子液体催化剂。Under the situation that the preparation conditions of the catalyst are exactly the same as in Example 1, only the N-methylimidazole in the preparation method is changed into N-ethylimidazole to obtain the imidazole basic ionic liquid catalyst based on POSS.
【实施例3】[Example 3]
在催化剂的制备条件与实施例1完全相同的情况下,只将制备方法中的N-甲基咪唑改为N-异丙基咪唑,得到基于POSS的咪唑碱性离子液体催化剂。Under the situation that the preparation conditions of the catalyst are exactly the same as in Example 1, only the N-methylimidazole in the preparation method is changed to N-isopropylimidazole to obtain the imidazole basic ionic liquid catalyst based on POSS.
【实施例4】【Example 4】
在催化剂的制备条件与实施例1完全相同的情况下,只将制备方法中的N-甲基咪唑改为N-烯丙基咪唑,得到基于POSS的咪唑碱性离子液体催化剂。Under the situation that the preparation conditions of the catalyst are exactly the same as in Example 1, only the N-methylimidazole in the preparation method is changed to N-allylimidazole to obtain the imidazole basic ionic liquid catalyst based on POSS.
【反应实施例5-8】【Reaction Example 5-8】
在1L反应釜中,加入反应物9.2g甘油及60.8g碳酸二甲酯,加入3.5g基于POSS的咪唑碱性离子液体催化剂,在反应温度为100℃,压力为2Mpa,搅拌速率为800rpm条件下,反应时间为6h。以碳酸甘油酯选择性和收率为指标,所得反应性能如表1所示。In a 1L reactor, add reactant 9.2g glycerol and 60.8g dimethyl carbonate, add 3.5g POSS-based imidazole basic ionic liquid catalyst, at a reaction temperature of 100°C, a pressure of 2Mpa, and a stirring rate of 800rpm , The reaction time is 6h. Taking glycerol carbonate selectivity and yield as indicators, the obtained reaction properties are shown in Table 1.
表1基于POSS的咪唑碱性离子液体催化剂合成碳酸甘油酯的反应结果Table 1 The reaction result of synthesizing glycerol carbonate based on the imidazole alkaline ionic liquid catalyst of POSS
【反应实施例9】[Reaction Example 9]
基于POSS的咪唑碱性离子液体催化剂的重复利用性能。Recycling performance of POSS-based imidazole basic ionic liquid catalysts.
在1L反应釜中,加入反应物9.2g甘油及60.8g碳酸二甲酯,加入3.5g基于POSS的咪唑碱性离子液体催化剂,在反应温度为100℃,压力为2Mpa,搅拌速率为800rpm条件下,反应时间为6h。反应后将催化剂过滤,90℃干燥4h,将该催化剂再循环使用,以碳酸甘油酯选择性和收率为指标,所得反应性能如表2所示。In a 1L reactor, add reactant 9.2g glycerol and 60.8g dimethyl carbonate, add 3.5g POSS-based imidazole basic ionic liquid catalyst, at a reaction temperature of 100°C, a pressure of 2Mpa, and a stirring rate of 800rpm , The reaction time is 6h. After the reaction, the catalyst was filtered, dried at 90° C. for 4 h, and the catalyst was recycled. Taking the selectivity and yield of glycerol carbonate as indicators, the obtained reaction performance is shown in Table 2.
表2基于POSS的咪唑碱性离子液体催化剂的重复利用性能Table 2 Recycling performance of POSS-based imidazole alkaline ionic liquid catalysts
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CN104927403B (en) * | 2015-06-18 | 2017-06-06 | 合肥工业大学 | A kind of preparation method of high perofmrnace lubricating oils additive |
CN109575292B (en) * | 2017-09-29 | 2021-05-11 | 中国石油化工股份有限公司 | Ion exchange resin and use thereof |
CN109574807B (en) * | 2017-09-29 | 2021-05-11 | 中国石油化工股份有限公司 | Method for preparing ethylene glycol by catalytic hydration of alkylene oxide |
CN109574794B (en) * | 2017-09-29 | 2021-05-11 | 中国石油化工股份有限公司 | Method for producing ethylene glycol by catalytic hydration of alkylene oxide |
CN109575295B (en) * | 2017-09-29 | 2021-05-11 | 中国石油化工股份有限公司 | Method for catalytic hydration of alkylene oxides |
CN109574793B (en) * | 2017-09-29 | 2021-05-28 | 中国石油化工股份有限公司 | Method for preparing glycol by hydrating alkylene oxide |
CN109517176A (en) * | 2018-12-11 | 2019-03-26 | 怀化学院 | Silsesquioxane ionic liquid and preparation method thereof |
CN110467730B (en) * | 2019-09-10 | 2021-06-01 | 哈尔滨工业大学 | Synthetic method of octachloropropyl POSS |
CN112619705B (en) * | 2019-09-24 | 2023-08-04 | 中国石油化工股份有限公司 | Alkylene oxide addition reaction catalyst and application thereof |
CN115490864B (en) * | 2022-09-29 | 2023-08-15 | 长兴化学(天津)有限公司 | POSS hybridized waterborne polyurethane emulsion and preparation method and application thereof |
CN117624616A (en) * | 2023-12-05 | 2024-03-01 | 青岛科技大学 | Cage polysilsesquioxane (POSS) supported multinuclear boron catalyst and its preparation method and application |
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CN103212445A (en) * | 2013-04-10 | 2013-07-24 | 江南大学 | Basic ionic liquid modified magnetic nanoparticle catalyst for synthesizing biodiesel and preparation method thereof |
CN103588808A (en) * | 2013-11-08 | 2014-02-19 | 复旦大学 | Polyhedral oligomeric silsesquioxane (POSS)-based solid ionic liquid, and preparation method and application thereof |
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CN103212445A (en) * | 2013-04-10 | 2013-07-24 | 江南大学 | Basic ionic liquid modified magnetic nanoparticle catalyst for synthesizing biodiesel and preparation method thereof |
CN103588808A (en) * | 2013-11-08 | 2014-02-19 | 复旦大学 | Polyhedral oligomeric silsesquioxane (POSS)-based solid ionic liquid, and preparation method and application thereof |
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