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CN100457268C - Catalyst of acetylacetone metal supported and carried by ion liquid, and preparation method - Google Patents

Catalyst of acetylacetone metal supported and carried by ion liquid, and preparation method Download PDF

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CN100457268C
CN100457268C CNB2006100533266A CN200610053326A CN100457268C CN 100457268 C CN100457268 C CN 100457268C CN B2006100533266 A CNB2006100533266 A CN B2006100533266A CN 200610053326 A CN200610053326 A CN 200610053326A CN 100457268 C CN100457268 C CN 100457268C
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acetylacetone
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pentanedione
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李浩然
胡兴邦
王从敏
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Zhejiang University ZJU
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Abstract

An ionic liquid carried acetylacetone-metal catalyst able to be easily recovered from reaction system by water washing is prepare through reaction between substituted acetylacetone and imidazole at -20-150 deg.C to obtain ionic liquid carried acetylacetone, and the complex reaction between said ionic liquid carried acetylacetone and transition metal at 0-100 deg.C.

Description

离子液体支载的乙酰丙酮金属的催化剂及制备方法 Catalyst and preparation method of metal acetylacetonate supported by ionic liquid

技术领域 technical field

本发明涉及一类离子液体支载的乙酰丙酮金属的催化剂及制备方法。The invention relates to a catalyst and a preparation method of a metal acetylacetonate supported by an ionic liquid.

背景技术 Background technique

众所周知,乙酰丙酮金属类试剂在氧化反应(US4970347,US4046813,CN1425642)、开环聚合反应、接枝聚合反应(CN1470534,CN1405192,CN1405192,CN1422876,CN1263520,CN1470535,CN1572809)等反应过程中是一种优良的催化剂。但在这些反应中使用乙酰丙酮金属类催化剂也有其固有的缺点,以氧化反应为例(US4970347,US4046813),由于乙酰丙酮金属类催化剂在有机相中具有较好的溶解性,能很好的溶解于反应体系,给后处理过程及催化剂的回收带来了困难:通过水洗萃取的方法,由于乙酰丙酮金属类催化剂在水中溶解性较差,很难对其进行回收;通过精馏的方法,由于反应过程中产生的副产物(尤其是一些聚合的副产物)在精馏中往往残留在角料中,这部分副产物和乙酰丙酮金属类催化剂混杂在一起,要从其中提取乙酰丙酮金属类催化剂也是相当困难的,同时乙酰丙酮金属类催化剂在高温精馏过程中还容易被破坏。As everyone knows, acetylacetone metal reagent is an excellent reaction process in oxidation reaction (US4970347, US4046813, CN1425642), ring-opening polymerization reaction, graft polymerization reaction (CN1470534, CN1405192, CN1405192, CN1422876, CN1263520, CN1470535, CN1572809) etc. catalyst. However, the use of acetylacetonate metal catalysts in these reactions also has its inherent disadvantages. Taking oxidation reactions as an example (US4970347, US4046813), because acetylacetone metal catalysts have good solubility in the organic phase, they can be well dissolved Due to the reaction system, it brings difficulties to the aftertreatment process and the recovery of the catalyst: by the method of water washing and extraction, it is difficult to recover it due to the poor solubility of metal acetylacetone catalysts in water; by the method of rectification, due to The by-products (especially some polymerization by-products) produced during the reaction often remain in the scrap during rectification. This part of the by-products is mixed with the metal acetylacetonate catalyst, and the metal acetylacetonate catalyst should be extracted from it It is also quite difficult, and the metal acetylacetone catalyst is also easily destroyed in the high-temperature rectification process.

发明内容 Contents of the invention

本发明的目的是提供一类离子液体支载的乙酰丙酮金属的催化剂及制备方法,这类催化剂在反应后可以简单的通过水洗的方法从反应体系中回收回来。The object of the present invention is to provide a catalyst and a preparation method of metal acetylacetonate supported by a class of ionic liquid. This catalyst can be simply recovered from the reaction system by washing with water after the reaction.

本发明涉及的离子液体支载的乙酰丙酮金属催化剂简写式为:[ace-Cnmim][X]-M,其中ace表示乙酰丙酮的种类,mim表示咪唑的种类,X表示阴离子的种类,M表示金属离子,具有如下的通式:The abbreviated formula of the acetylacetone metal catalyst supported by the ionic liquid involved in the present invention is: [ace-Cnmim][X]-M, wherein ace represents the type of acetylacetone, mim represents the type of imidazole, X represents the type of anion, and M represents Metal ions have the general formula:

Figure C20061005332600041
Figure C20061005332600041

其中n=1~6;M1为三价过渡金属Fe3+,Cr3+,V3+,M2为二价过渡金属Ti2+,Mn2+,Fe2+,Co2+,Ni2+,Cu2+;R1,R2,R3为H、具有通式CmH2m+1(m=1~6)或CmH2m(m=1~6)的直链烃或支链烃、苯基或取代的苯基;X为BF4 -,PF6 -,SbF6 -,H2PO4 -,F-,Cl-,Br-,HSO4 -,NO3 -阴离子。Where n=1~6; M1 is trivalent transition metal Fe 3+ , Cr 3+ , V 3+ , M2 is bivalent transition metal Ti 2+ , Mn 2+ , Fe 2+ , Co 2+ , Ni 2+ , Cu 2+ ; R1, R2, R3 are H, straight-chain or branched-chain hydrocarbons with the general formula C m H 2m+1 (m=1~6) or C m H 2m (m=1~6), Phenyl or substituted phenyl; X is BF 4 - , PF 6 - , SbF 6 - , H 2 PO 4 - , F - , Cl - , Br - , HSO 4 - , NO 3 - anion.

本发明所涉及的离子液体支载的乙酰丙酮金属催化剂具体的可通过如下两步反应制备:1)以取代乙酰丙酮类物质与咪唑类物质在合适的有机溶剂中反应得离子液体支载的乙酰丙酮,反应式如下:The metal acetylacetonate catalyst supported by the ionic liquid involved in the present invention can specifically be prepared by the following two-step reaction: 1) react the acetylacetonate supported by the ionic liquid with an imidazole in a suitable organic solvent to obtain the acetylacetonate supported by the ionic liquid Acetone, the reaction formula is as follows:

Figure C20061005332600051
Figure C20061005332600051

2)离子液体支载的乙酰丙酮与过渡金属盐在合适的有机溶剂中反应,络合生成离子液体支载的乙酰丙酮金属催化剂。2) The acetylacetone supported by the ionic liquid reacts with the transition metal salt in a suitable organic solvent to form a complexed acetylacetone metal catalyst supported by the ionic liquid.

本发明反应使用的有机溶剂可以是丙酮、丁酮、戊酮、四氢呋喃、乙醚、异丙醚、1~6个碳链的一元醇中的一种或一种以上。The organic solvent used in the reaction of the present invention may be one or more of acetone, methyl ethyl ketone, pentanone, tetrahydrofuran, ether, isopropyl ether, and monohydric alcohols with 1 to 6 carbon chains.

适合于本发明的第一步反应的温度在-20℃~150℃间,并优选在0℃~100℃间;适合于第二步反应的温度在-20℃~100℃间,并优选在0℃~80℃间。The temperature suitable for the first step reaction of the present invention is between -20°C and 150°C, and preferably between 0°C and 100°C; the temperature suitable for the second step reaction is between -20°C and 100°C, and preferably between Between 0°C and 80°C.

在第一步反应中,取代乙酰丙酮类物质与咪唑类物质的摩尔比在0.1~10之间,并优选在0.5~5之间;在第二步反应中,离子液体支载的乙酰丙酮与过渡金属盐的摩尔比在0.1~10之间,并优选在1~5之间。In the first step reaction, the molar ratio of substituted acetylacetones and imidazoles is between 0.1~10, and preferably between 0.5~5; in the second step reaction, the acetylacetone supported by ionic liquid and The molar ratio of the transition metal salt is between 0.1-10, and preferably between 1-5.

本发明不同于先前发明之处在于:通过该方法制得的乙酰丙酮金属催化剂在可溶于常规有机溶剂的同时在水中具有较好的溶解度,而且在水中的溶解度往往大于在有机溶剂中的溶解度。从而使得在反应过程中离子液体支载的乙酰丙酮金属催化剂可以很好的溶解于反应体系,而在反应结束后通过简单的水洗的方法便可以从反应体系中除去催化剂,然后在减压下蒸除水分,达到回收催化剂的目的。The present invention is different from previous inventions in that: the metal acetylacetonate catalyst prepared by the method has good solubility in water while being soluble in conventional organic solvents, and the solubility in water is often greater than the solubility in organic solvents . Thereby making the acetylacetonate metal catalyst supported by the ionic liquid in the reaction process can be well dissolved in the reaction system, and the catalyst can be removed from the reaction system by simple water washing after the reaction, and then evaporated under reduced pressure In addition to moisture, to achieve the purpose of catalyst recovery.

以下的实施例将对本发明进行更为全面的描述。The following examples will more fully describe the present invention.

具体实施方式 Detailed ways

实施例1Example 1

在250ml的三颈烧瓶中加入16.4g(0.2mol)甲基咪唑、150ml丙酮,搅拌并降温至0℃,在2小时内缓慢滴加33.5g(0.25mol)氯代乙酰丙酮,滴完后升温至室温继续搅拌8小时。减压蒸馏至恒重,得氯甲基咪唑乙酰丙酮39.3g(产率:91.0%)。Add 16.4g (0.2mol) of methylimidazole and 150ml of acetone into a 250ml three-necked flask, stir and cool down to 0°C, slowly add 33.5g (0.25mol) of chloroacetylacetone dropwise within 2 hours, and then raise the temperature Stirring was continued to room temperature for 8 hours. Distill under reduced pressure to constant weight to obtain 39.3 g of chloromethylimidazole acetylacetone (yield: 91.0%).

实施例2Example 2

在250ml的三颈烧瓶中加入10.8g(0.04mol)六水合三氯化铁和100ml乙醇中,在100ml的恒压滴液漏斗中将26.0g(0.12mol)实施例1所得氯甲基咪唑乙酰丙酮溶于80ml乙醇,搅拌下升温至40℃,在2小时内缓慢滴加氯甲基咪唑乙酰丙酮的乙醇溶液,滴完后继续保温搅拌5小时。减压蒸馏至恒重,得氯甲基咪唑乙酰丙酮铁(III)27.9g(产率:99.2%)。In a 250ml three-necked flask, add 10.8g (0.04mol) ferric chloride hexahydrate and 100ml ethanol, in a constant pressure dropping funnel of 100ml, 26.0g (0.12mol) chloromethylimidazole acetylene obtained in Example 1 Dissolve acetone in 80ml of ethanol, raise the temperature to 40°C with stirring, slowly add the ethanol solution of chloromethylimidazole acetylacetone dropwise within 2 hours, and continue to keep warm and stir for 5 hours after the drop is completed. Distill under reduced pressure to constant weight to obtain 27.9 g of chloromethylimidazolium acetylacetonate iron (III) (yield: 99.2%).

实施例3Example 3

在500ml的三颈烧瓶中加入16.4g(0.2mol)甲基咪唑、150ml甲醇,搅拌并降温至0℃,在2小时内缓慢滴加33.5g(0.25mol)氯代乙酰丙酮,滴完后升温至室温继续搅拌8小时。Add 16.4g (0.2mol) of methylimidazole and 150ml of methanol into a 500ml three-necked flask, stir and cool down to 0°C, slowly add 33.5g (0.25mol) of chloroacetylacetone dropwise within 2 hours, and then raise the temperature Stirring was continued to room temperature for 8 hours.

在250ml的恒压滴液漏斗中加入18.1g(0.067mol)六水合三氯化铁和150ml甲醇的混合溶液。将三颈烧瓶中的溶液搅拌下升温至40℃,在2小时内缓慢滴加三氯化铁的甲醇溶液,滴完后继续保温搅拌5小时。减压蒸馏至恒重,得氯甲基咪唑乙酰丙酮铁(III)46.2g(产率:98.1%)。In the constant pressure dropping funnel of 250ml, add the mixed solution of 18.1g (0.067mol) iron trichloride hexahydrate and 150ml methanol. The solution in the three-necked flask was heated up to 40°C with stirring, and the methanol solution of ferric chloride was slowly added dropwise within 2 hours, and continued to keep stirring for 5 hours after the drop was completed. Distill under reduced pressure to constant weight to obtain 46.2 g of chloromethylimidazolium acetylacetonate iron (III) (yield: 98.1%).

实施例4-14Example 4-14

类似于实施例3,分别采用不同的取代乙酰丙酮类物质、咪唑类物质、有机溶剂、过渡金属盐,反应结束后得如下结果:Similar to Example 3, different substituted acetylacetone substances, imidazole substances, organic solvents, and transition metal salts were used respectively, and the following results were obtained after the reaction:

  实施例 Example   取代乙酰丙酮(mol) Substituted acetylacetone (mol)   咪唑(mol) Imidazole (mol)   有机溶剂(ml) Organic solvent (ml)   过渡金属盐(mol) Transition metal salt (mol)   催化剂产率 Catalyst yield   4 4   氯代乙酰丙酮0.20 Chloroacetylacetone 0.20   咪唑0.22 Imidazole 0.22   甲醇300 Methanol 300   FeCl<sub>3</sub> 0.067 FeCl<sub>3</sub> 0.067   92.3% 92.3%   5 5   溴代乙酰丙酮0.20 Bromoacetylacetone 0.20   甲基咪唑0.25 Methylimidazole 0.25   甲醇300 Methanol 300   FeCl<sub>3</sub> 0.067 FeCl<sub>3</sub> 0.067   93.8% 93.8%   6 6   溴代乙酰丙酮0.20 Bromoacetylacetone 0.20   咪唑0.22 Imidazole 0.22   甲醇300 Methanol 300   FeCl<sub>3</sub> 0.067 FeCl<sub>3</sub> 0.067   90.1% 90.1%   7 7   氯代乙酰丙酮0.20 Chloroacetylacetone 0.20   丁基咪唑0.25 Butylimidazole 0.25   丙酮400 Acetone 400   CuCl<sub>2</sub> 0.10 CuCl<sub>2</sub> 0.10   98.7% 98.7%   8 8   氯代乙酰丙酮0.20 Chloroacetylacetone 0.20   咪唑0.22 Imidazole 0.22   丙酮400 Acetone 400   CuCl<sub>2</sub> 0.10 CuCl<sub>2</sub> 0.10   94.9% 94.9%

  9 9   溴代乙酰丙酮0.20 Bromoacetylacetone 0.20   丁基咪唑0.25 Butylimidazole 0.25   丙酮400 Acetone 400   CuCl<sub>2</sub> 0.10 CuCl<sub>2</sub> 0.10   95.3% 95.3%   10 10   溴代乙酰丙酮0.20 Bromoacetylacetone 0.20   甲基咪唑0.25 Methylimidazole 0.25   丙酮400 Acetone 400   CuCl<sub>2</sub> 0.10 CuCl<sub>2</sub> 0.10   91.2% 91.2%   11 11   3-氯乙基-乙酰丙酮0.20 3-Chloroethyl-acetylacetone 0.20   甲基咪唑0.25 Methylimidazole 0.25   甲醇300 Methanol 300   FeCl<sub>3</sub> 0.067 FeCl<sub>3</sub> 0.067   95.8% 95.8%   12 12   3-溴丙基-乙酰丙酮0.20 3-Bromopropyl-acetylacetone 0.20   丁基咪唑0.25 Butylimidazole 0.25   丙酮400 Acetone 400   CuCl<sub>2</sub> 0.10 CuCl<sub>2</sub> 0.10   93.5% 93.5%   13 13   3-氯乙基-乙酰丙酮0.20 3-Chloroethyl-acetylacetone 0.20   咪唑0.22 Imidazole 0.22   丙酮400 Acetone 400   CuCl<sub>2</sub> 0.10 CuCl<sub>2</sub> 0.10   92.1% 92.1%   14 14   3-溴丙基-乙酰丙酮0.20 3-Bromopropyl-acetylacetone 0.20   甲基咪唑0.25 Methylimidazole 0.25   甲醇300 Methanol 300   FeCl<sub>3</sub> 0.067 FeCl<sub>3</sub> 0.067   90.0% 90.0%

Claims (5)

1, a kind of ion liquid supported cetylacetone metallic catalyst, structural formula is as follows:
Figure C2006100533260002C1
N=1~6 wherein; M1 is the trivalent transition-metal Fe 3+, Cr 3+, V 3+M2 is divalent transition metal Ti 2+, Mn 2+, Fe 2+, Co 2+, Ni 2+, Cu 2+R 1, R 2, R 3Independently be H or have general formula C respectively mH 2m+1Straight-chain hydrocarbons or branched-chain hydrocarbons, m=1 in the formula~6; X -Be F -, Cl -, Br -Anion.
2, the described ion liquid supported cetylacetone metallic Preparation of catalysts method of claim 1 the steps include:
1) will replace levulinic ketone material and imidazoles material, the mixed in molar ratio by 0.1~10 in appropriate organic solvent, is reacted under-20 ℃~150 ℃ temperature, gets ion liquid supported acetylacetone,2,4-pentanedione, and reaction equation is as follows:
Figure C2006100533260002C2
N=1~6 wherein; R 1, R 2, R 3Independently be H or have general formula C respectively mH 2m+1Straight-chain hydrocarbons or branched-chain hydrocarbons, m=1 in the formula~6; X is F, Cl, Br; X -Be F -, Cl -, Br -Anion;
2) with above-mentioned ion liquid supported acetylacetone,2,4-pentanedione and transition metal salt, the mol ratio by 0.5~5 in appropriate organic solvent, is reacted under 0 ℃~100 ℃ temperature, and complexing generates ion liquid supported cetylacetone metallic catalyst.
3, method according to claim 2 is characterized in that replacing levulinic ketone material and imidazoles material mol ratio is 0.5~5, and the ion liquid supported acetylacetone,2,4-pentanedione and the mol ratio of transition metal salt are 1~5.
4, method according to claim 2, the reaction temperature that it is characterized in that obtaining ion liquid supported acetylacetone,2,4-pentanedione is 0 ℃~100 ℃, it is 0 ℃~80 ℃ that complexing generates ion liquid supported cetylacetone metallic catalyst reaction temperatures.
5, method according to claim 2 is characterized in that appropriate organic solvent is more than one in the monohydric alcohol of acetone, butanone, pentanone, oxolane, ether, isopropyl ether, 1~6 carbochain.
CNB2006100533266A 2006-09-08 2006-09-08 Catalyst of acetylacetone metal supported and carried by ion liquid, and preparation method Expired - Fee Related CN100457268C (en)

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Air oxidation of ethylbenzene catalysed bybis(acetylacetonate) nickel(Ⅱ) and1-n-butyl-3-methylimidazolium hexafluorophosphate. Ramon Alcantara, et al.Applied Catalysis A: General,Vol.218. 2001 *
Selective Hydrogenation of 1,3-butadiene by TransitionMetalCompounds Immobilized in 1-Butyl-3-methyl ImidazoliumRoomTemperature Ionic Liquids. Crestina S. Consorti, et al.J. Braz. Chem. Soc.,Vol.14 No.3. 2003
Selective Hydrogenation of 1,3-butadiene by TransitionMetalCompounds Immobilized in 1-Butyl-3-methyl ImidazoliumRoomTemperature Ionic Liquids. Crestina S. Consorti, et al.J. Braz. Chem. Soc.,Vol.14 No.3. 2003 *

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