CN1629149A - A kind of phase transfer catalyzed method for synthesizing α, β-epoxy ketone compound - Google Patents
A kind of phase transfer catalyzed method for synthesizing α, β-epoxy ketone compound Download PDFInfo
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Abstract
本发明涉及α,β-环氧基酮化合物的合成,具体地说是一种相转移催化合成α,β-环氧基酮化合物的方法,在相转移催化剂存在下,以三氯异氰尿酸(TCCA)为氧化剂,碱金属氢氧化物为碱性调节剂,α,β-不饱和酮为原料,在纯有机溶剂、有机溶剂-水、或水中进行反应;反应式如上式其中:取代基R1、R2可为烷基基团或者芳基基团;当R1和/或R2为芳基取代基时,其可带一个或多个给电子和/或吸电子基团;反应完成后按常规方法分离即得产品。本发明操作简便,条件温和,原料易得,选择性高,产率好,可以根据原料溶解性质选择反应溶剂。
The present invention relates to the synthesis of α, β-epoxy ketone compounds, specifically a method for synthesizing α, β-epoxy ketone compounds by phase transfer catalysis, in the presence of a phase transfer catalyst, trichloroisocyanuric acid (TCCA) is the oxidizing agent, the alkali metal hydroxide is the basic modifier, and the α, β-unsaturated ketone is the raw material, which is reacted in pure organic solvent, organic solvent-water, or water; the reaction formula is as above: substituent R 1 and R 2 can be alkyl groups or aryl groups; when R 1 and/or R 2 are aryl substituents, they can have one or more electron-donating and/or electron-withdrawing groups; the reaction After completion, the product is obtained by separating according to conventional methods. The invention has the advantages of simple and convenient operation, mild conditions, readily available raw materials, high selectivity and good yield, and the reaction solvent can be selected according to the dissolution properties of raw materials.
Description
技术领域technical field
本发明涉及α,β-环氧基酮化合物的合成,具体地说是一种相转移催化合成α,β-环氧基酮化合物的方法。The invention relates to the synthesis of α, β-epoxy ketone compounds, in particular to a method for synthesizing α, β-epoxy ketone compounds by phase transfer catalysis.
背景技术Background technique
α,β-环氧基酮化合物是有机合成中用途最广的一类中间体,羰基和环氧丙烷基团都可以进行功能化【文献:Tetrahedron:Asymmetry,2001,12,2359-2383等】。其中羰基功能化包括还原成α,β-环氧基醇,还原胺化反应,拜耳-维利格反应,梅尔魏因-庞多夫-韦莱反应等。而环氧丙烷基团受含硫、氧、卤素等亲核试剂进攻开环可以进行合成种类繁多的化合物。α, β-epoxy ketone compounds are the most widely used intermediates in organic synthesis, and both carbonyl and propylene oxide groups can be functionalized [Document: Tetrahedron: Asymmetry, 2001, 12, 2359-2383, etc.] . The carbonyl functionalization includes reduction to α, β-epoxy alcohol, reductive amination reaction, Bayer-Villiger reaction, Melwein-Pondorf-Weilay reaction, etc. And the ring-opening of the propylene oxide group by nucleophilic reagents such as sulfur, oxygen, and halogen can be used to synthesize a wide variety of compounds.
α,β-环氧基酮结构砌块可以用于合成生物活性化合物,如白三烯受体拮抗剂SK&F104353【文献:J.Org.Chem.1993,58,6247-6254等】,地尔硫卓和紫杉醇Taxol支链【文献:J.Chem.Soc.,Perkin Trans.11997,3501-3507等】,半乳糖醛酸类衍生物【文献:J.Chem.Soc.,Perkin Trans.1 2001,149-153.等】,蛋白激酶C激动剂【文献:Tetrahedron Lett.2000,41,9569-9574等】。α, β-epoxy ketone building blocks can be used to synthesize bioactive compounds, such as leukotriene receptor antagonist SK&F104353 [Document: J.Org.Chem.1993, 58, 6247-6254, etc.], diltiazem and paclitaxel Taxol branched [document: J.Chem.Soc., Perkin Trans.11997, 3501-3507, etc.], galacturonic acid derivatives [document: J.Chem.Soc., Perkin Trans.1 2001, 149-153 etc.], protein kinase C agonist [Document: Tetrahedron Lett.2000, 41, 9569-9574, etc.].
目前常规合成α,β-环氧基酮化合物的方法包括α,β-不饱和酮环氧化反应,α卤代酮与醛之间的达因反应【文献:Tetrahedron Lett.1998,39,2145-2148,Tetrahedron 1999,55,6375-6386等】。α,β-不饱和酮环氧化反应是合成α,β-环氧基酮的最直接的方法。常用于α,β-不饱和酮环氧化反应的氧化剂有双氧水【文献:Tetrahedron Lett.1998,39,7563-7566等】,次氯酸钠【文献:Tetrahedron Lett.1998,39,1599-1602,等】,叔丁基过氧化氢【文献:J.Am.Chem.Soc.1997,119,2329-2330等】等,氧气【文献:Angew.Chem.,Int.Ed.Engl.1996,35,1725-1728等】。虽然这些氧化剂能成功地用于α,β-不饱和酮环氧化反应,但双氧水、次氯酸钠、次氯酸钾和叔丁基过氧化氢等氧化剂普遍存在稳定性差,易分解等缺点,而氧气作氧源,需要使用化学计量的二乙基锌助剂。At present, the conventional methods for synthesizing α, β-epoxy ketone compounds include α, β-unsaturated ketone epoxidation reaction, dyne reaction between α-halogenated ketones and aldehydes [Document: Tetrahedron Lett.1998, 39, 2145 -2148, Tetrahedron 1999, 55, 6375-6386, etc.]. The epoxidation of α, β-unsaturated ketones is the most direct method for the synthesis of α, β-epoxy ketones. Oxidants commonly used in the epoxidation of α, β-unsaturated ketones include hydrogen peroxide [document: Tetrahedron Lett.1998, 39, 7563-7566, etc.], sodium hypochlorite [document: Tetrahedron Lett. , tert-butyl hydroperoxide [document: J.Am.Chem.Soc.1997, 119, 2329-2330, etc.], etc., oxygen [document: Angew.Chem., Int.Ed.Engl.1996, 35, 1725- 1728 etc]. Although these oxidizing agents can be successfully used in the epoxidation reaction of α, β-unsaturated ketones, the oxidizing agents such as hydrogen peroxide, sodium hypochlorite, potassium hypochlorite and tert-butyl hydroperoxide generally have the disadvantages of poor stability and easy decomposition, while oxygen acts as oxygen source, a stoichiometric amount of diethylzinc promoter is required.
发明内容Contents of the invention
本发明的目的在于提供一种反应条件温和、成本低的相转移催化α,β-不饱和酮环氧化反应合成α,β-环氧基酮化合物。The object of the present invention is to provide a phase transfer catalyzed α, β-unsaturated ketone epoxidation reaction to synthesize α, β-epoxy ketone compound with mild reaction conditions and low cost.
为实现上述目的,本发明采用的技术方案为:在相转移催化剂存在下,以α,β-不饱和酮为原料,三氯异氰尿酸为氧化剂,碱金属氢氧化物无机碱作添加剂,在纯有机溶剂,有机溶剂-水,或水中进行反应;反应式如下:In order to achieve the above object, the technical scheme adopted in the present invention is: in the presence of a phase transfer catalyst, using α, β-unsaturated ketones as raw materials, trichloroisocyanuric acid as an oxidizing agent, and alkali metal hydroxide inorganic bases as additives. Pure organic solvent, organic solvent-water, or react in water; the reaction formula is as follows:
其中:取代基R1可为一种烷基基团或者芳基基团;取代基R2可为一种烷基基团或者芳基基团;芳基取代基R1和/或R2可带一个或多个给电子和/或吸电子基团;芳基取代基R1和/或R2的一个或多个给电子和/或吸电子基团可位于芳环的不同取代位置;氧化剂的用量一般以所含有效氯含量等于或大于其与原料的化学计量比即可,通常三氯异氰尿酸的用量为原料的50~500%mol,碱金属氢氧化物的用量也是如此,通常为原料的200~1000%mol;催化剂通常为季铵盐或季膦盐或聚乙二醇或它们的混合物,它们的用量可为原料的0.1~20%mol;溶剂以将原料完全溶解即可,原料与溶剂的摩尔比通常为:1∶1至1∶50;反应通常在0.5~72小时即可完成;反应温度以在反应体系的凝固点以上即可,通常在-50~30℃之间;有机溶剂为一种或多种极性或非极性惰性溶剂或极性溶剂和非极性溶剂的混合物,其中极性溶剂常为甲苯、二甲苯、四氢呋喃、N,N’-二甲基甲酰胺(DMF)、二甲基亚砜(DMSO)、二氯甲烷、氯仿或水等,非极性溶剂常为己烷或苯等,混合溶剂例如:甲苯/水,二甲苯/水,二氯甲烷/水,三氯甲烷/水。产物分离可采用萃取或重结晶或柱层析或简单过滤等分离方法。Wherein: substituent R 1 can be a kind of alkyl group or aryl group; Substituent R 2 can be a kind of alkyl group or aryl group; Aryl substituent R 1 and/or R 2 can be With one or more electron-donating and/or electron-withdrawing groups; one or more electron-donating and/or electron-withdrawing groups of the aryl substituents R1 and/or R2 can be located at different substitution positions on the aromatic ring; oxidizing agent Generally, the amount of available chlorine is equal to or greater than the stoichiometric ratio of the raw material. Usually, the amount of trichloroisocyanuric acid is 50-500% mol of the raw material, and the same is true for the amount of alkali metal hydroxide. Usually It is 200-1000% mol of the raw material; the catalyst is usually a quaternary ammonium salt or a quaternary phosphonium salt or polyethylene glycol or their mixture, and their dosage can be 0.1-20% mol of the raw material; the solvent can completely dissolve the raw material , the molar ratio of raw material to solvent is usually: 1:1 to 1:50; the reaction can be completed usually within 0.5 to 72 hours; the reaction temperature should be above the freezing point of the reaction system, usually between -50 and 30°C ; The organic solvent is a mixture of one or more polar or non-polar inert solvents or polar solvents and non-polar solvents, wherein the polar solvents are often toluene, xylene, tetrahydrofuran, N, N'-dimethyl Formamide (DMF), dimethyl sulfoxide (DMSO), dichloromethane, chloroform or water, etc., non-polar solvents are usually hexane or benzene, mixed solvents such as: toluene/water, xylene/water, di Chloromethane/water, Chloroform/water. Products can be separated by extraction or recrystallization or column chromatography or simple filtration and other separation methods.
本发明有如下优点:The present invention has following advantage:
1.固体氧化剂三氯异氰尿酸性质稳定,价廉易得,是一种广泛使用的泳池消毒剂;同其它氧化剂,如次氯酸钠水溶液,次氯酸钙固体,双氧水等相比,具有稳定性高、运输贮藏方便、使用安全可靠,氧化能力强,选择性好等优点;在相转移催化剂和碱性调节剂作用下对α,β-不饱和酮表现出良好的环氧化能力。1. The solid oxidant trichloroisocyanuric acid is stable in nature, cheap and easy to get, and is a widely used disinfectant for swimming pools; compared with other oxidants, such as sodium hypochlorite aqueous solution, calcium hypochlorite solid, hydrogen peroxide, etc., it has high stability , convenient transportation and storage, safe and reliable use, strong oxidation ability, good selectivity, etc.; under the action of phase transfer catalyst and alkaline regulator, it shows good epoxidation ability for α, β-unsaturated ketones.
2.反应条件温和。在相转移催化剂存在下,在极性、非极性有机溶剂,有机溶剂/水,或纯水介质下可将α,β-不饱和酮转化成α,β-环氧基酮化合物。可以根据反应物(原料)溶解性质选择反应介质(溶剂)反应;这是其它氧化剂难以比拟的优点。2. The reaction conditions are mild. In the presence of a phase transfer catalyst, the α, β-unsaturated ketone can be converted into α, β-epoxy ketone compound in polar, non-polar organic solvent, organic solvent/water, or pure water medium. The reaction medium (solvent) can be selected according to the dissolution properties of the reactants (raw materials); this is an incomparable advantage of other oxidants.
3.反应选择性和转化率高。本发明在给定条件下,α,β-不饱和酮能以高产率,甚至定量转化成α,β-环氧基酮化合物,没有副产物,选择性高,产率好。3. The reaction selectivity and conversion rate are high. In the present invention, under given conditions, α, β-unsaturated ketones can be converted into α, β-epoxy ketone compounds with high yield, even quantitatively, without by-products, high selectivity and good yield.
4.操作简便,反应产物易于分离。可通过萃取、重结晶、柱层析或简单过滤等分离方法加以纯化;有机溶剂可以回收利用。4. The operation is simple and the reaction products are easy to separate. It can be purified by separation methods such as extraction, recrystallization, column chromatography or simple filtration; the organic solvent can be recycled.
总之,本发明具有操作简便,条件温和,原料易得,选择性高,产率好,可以根据原料溶解性质选择反应溶剂等优点。In a word, the present invention has the advantages of simple operation, mild conditions, readily available raw materials, high selectivity, good yield, and the ability to select a reaction solvent according to the dissolution properties of raw materials.
具体实施方式Detailed ways
下面通过实施例详述本发明;但本发明并不限于下述的实施例。The present invention is described in detail below through examples; but the present invention is not limited to the following examples.
实施例1 固液两相相转移催化合成反式-2,3-环氧-1,3-二苯基丙-1-酮Example 1 Synthesis of trans-2,3-epoxy-1,3-diphenylpropan-1-one by solid-liquid two-phase phase transfer catalysis
在100ml圆底烧瓶中,加入查尔酮(2.08g,10mmol),四丁基溴化铵(322mg,1mmol)及30ml甲苯,冷却至10℃,加入固体三氯异氰尿酸(2.32g,10mmol),加入固体KOH(3.36,60mmol)。滴加完毕后10℃下继续搅拌4小时,TLC检测反应终点。升温至室温,往反应液中加入15ml乙醚,过滤,滤液用水洗涤,无水MgSO4干燥。蒸馏除去溶剂,柱色谱分离(硅胶,洗脱液为石油醚/乙酸乙酯:50/1),蒸馏除去溶剂,得到白色晶体,收率为92%。In a 100ml round bottom flask, add chalcone (2.08g, 10mmol), tetrabutylammonium bromide (322mg, 1mmol) and 30ml toluene, cool to 10°C, add solid trichloroisocyanuric acid (2.32g, 10mmol ), solid KOH (3.36, 60 mmol) was added. After the dropwise addition was completed, stirring was continued at 10° C. for 4 hours, and the end point of the reaction was detected by TLC. Warm up to room temperature, add 15ml of diethyl ether to the reaction solution, filter, wash the filtrate with water, and dry over anhydrous MgSO 4 . The solvent was distilled off, separated by column chromatography (silica gel, eluent: petroleum ether/ethyl acetate: 50/1), and the solvent was distilled off to obtain white crystals with a yield of 92%.
实施例2 固液两相相转移催化合成反式-2,3-环氧-1,3-二苯基丙-1-酮Example 2 Synthesis of trans-2,3-epoxy-1,3-diphenylpropan-1-one by solid-liquid two-phase phase transfer catalysis
将不同相转移催化剂存在下的实施例以表格形式总结如下:(反应条件和步骤同实施例1)The embodiment under the existence of different phase transfer catalysts is summarized as follows in tabular form: (reaction condition and step are with embodiment 1)
Table 1.不同相转移催化剂及用量对环氧化反应的影响Table 1. Effects of different phase transfer catalysts and dosage on epoxidation reaction
序号 催化剂 催化剂用量[%] 碱 反应时间[小时] 收率[%]No. Catalyst Catalyst dosage [%] Alkali Reaction time [hours] Yield [%]
1 PEG-4600 10 KOH 24 371 PEG-4600 10 KOH 24 37
2 PEG-400 10 KOH 24 712 PEG-400 10 KOH 24 71
3 TBPB 10 KOH 24 713 TBPB 10 KOH 24 71
4 TBPC 10 KOH 24 484 TBPC 10 KOH 24 48
5 CTMAB 10 KOH 24 705 CTMAB 10 KOH 24 70
6 TBABS 10 KOH 3 916 TBABS 10 KOH 3 91
7 TBAB 10 KOH 4 927 TBAB 10 KOH 4 92
8 TBAB 5 KOH 4 918 TBAB 5 5 KOH 4 91
9 TBAB 1 KOH 24 429 TBAB 1 1 KOH 24 42
10 TBAB 0.1 KOH 48 4010 TBAB 0.1 KOH 48 40
催化剂:catalyst:
PEG-4600:聚乙二醇-4600(polyethylene glycol-4600),PEG-4600: polyethylene glycol-4600 (polyethylene glycol-4600),
PEG-400:聚乙二醇-400(polyethylene glycol-400),PEG-400: polyethylene glycol-400 (polyethylene glycol-400),
TBPB:四丁基溴化膦(tetrabutyl phosphonium bromide),TBPB: Tetrabutyl phosphonium bromide,
TBPC:四丁基氯化膦(tetrabutyl phosphonium chloride),TBPC: tetrabutyl phosphonium chloride,
CTMAB:十六烷基三甲基溴化铵(Cetyl trimethyl ammonium bromide),CTMAB: Cetyl trimethyl ammonium bromide,
TBABS:四丁基硫酸氢铵(tetrabutyl ammonium bisulfate),TBABS: tetrabutyl ammonium bisulfate (tetrabutyl ammonium bisulfate),
TBAB:四丁基溴化铵(tetrabutyl ammonium bromide)。TBAB: tetrabutyl ammonium bromide.
实施例3 固液两相相转移催化合成反式-2,3-环氧-1,3-二苯基丙-1-酮Example 3 Synthesis of trans-2,3-epoxy-1,3-diphenylpropan-1-one by solid-liquid two-phase phase transfer catalysis
将不同反应溶剂、碱的种类和用量、温度条件下的实施例以表格形式总结如下:(反应条件和步骤同实施例1)The embodiment under different reaction solvent, the kind and consumption of alkali, temperature condition is summarized as follows in tabular form: (reaction condition and step are with embodiment 1)
Table 2.反应溶剂、碱的种类和用量、TCCA用量、温度对环氧化反应的影Table 2. Effect of reaction solvent, type and amount of base, TCCA amount, temperature on epoxidation reaction
响 ring
序号 溶剂 碱/[%] TCCA[%] 温度 反应时间 收率No. Solvent Alkali/[%] TCCA[%] Temperature Reaction Time Yield
[℃] [小时] [%][℃] [hour] [%]
11 二氯甲烷 KOH/600 100 0 24 7311 dichloromethane KOH/600 100 0 24 73
12 二甲苯 KOH/500 90 0 5 7812 xylene KOH/500 90 0 5 78
13 甲苯 KOH/600 100 0 4 9113 Toluene KOH/600 100 0 4 91
14 甲苯 KOH/200 50 0 24 6314 Toluene KOH/200 50 0 24 63
15 甲苯 LiOH/600 90 0 24 3815 Toluene LiOH/600 90 0 24 38
16 甲苯 NaOH/600 90 0 24 5316 Toluene NaOH/600 90 0 24 53
17 甲苯 CsOH/600 90 0 24 4517 Toluene CsOH/600 90 0 24 45
18 甲苯 KOH/600 67 20 24 6718 Toluene KOH/600 67 20 24 67
19 甲苯 KOH/500 100 10 4 9219 Toluene KOH/500 100 10 4 92
20 甲苯 KOH/600 100 10 4 9120 Toluene KOH/600 100 10 4 91
21 甲苯 KOH/200 100 -10 8 7321 Toluene KOH/200 100 -10 8 73
22 甲苯 KOH/600 100 -10 6 8722 Toluene KOH/600 100 -10 6 87
23 甲苯 KOH/600 100 -20 8 8523 Toluene KOH/600 100 -20 8 85
实施例4 固液两相相转移催化合成反式取代-2,3-环氧-1,3-二苯基丙-1-酮Example 4 Synthesis of trans-substituted-2,3-epoxy-1,3-diphenylpropan-1-one by solid-liquid two-phase phase transfer catalysis
将不同反应底物的实施例以表格形式总结如下:(反应条件和步骤同实施例1)The embodiment of different reaction substrates is summarized as follows in tabular form: (reaction condition and step are with embodiment 1)
Table 3.TBAB催化环氧化反应 Table 3.TBAB Catalyzed Epoxidation Reaction
序号 α,β-不饱和 反应时间 收率No. α, β-Unsaturated Reaction Time Yield
羰基化合物 [小时] [%]Carbonyls [hours] [%]
R1 R2 R 1 R 2
24 C6H5 C6H5 4 8824 C 6 H 5 C 6 H 5 4 88
25 C6H5 4-CH3OC6H4 4 8525 C 6 H 5 4-CH 3 OC 6 H 4 4 85
26 4-ClC6H4 4-FC6H4 3 9426 4-ClC 6 H 4 4-FC 6 H 4 3 94
27 C6H5 4-FC6H4 5 8127 C 6 H 5 4-FC 6 H 4 5 81
28 4-NO2C6H4 C6H5 4 7728 4-NO 2 C 6 H 4 C 6 H 5 4 77
29 C6H5 4-ClC6H4 4 9129 C 6 H 5 4-ClC 6 H 4 4 91
30 4-ClC6H4 C6H5 4 9330 4-ClC 6 H 4 C 6 H 5 4 93
31 2-ClC6H4 C6H5 4 9331 2-ClC 6 H 4 C 6 H 5 4 93
32 4-ClC6H4 4-ClC6H4 2 8032 4-ClC 6 H 4 4-ClC 6 H 4 2 80
33 4-ClC6H4 4-CH3OC6H4 3 7233 4-ClC 6 H 4 4-CH 3 OC 6 H 4 3 72
34 3-ClC6H5 4-PhC6H4 4 8834 3-ClC 6 H 5 4-PhC 6 H 4 4 88
35 3-ClC6H5 4-CF3C6H4 4 9135 3-ClC 6 H 5 4-CF 3 C 6 H 4 4 91
36 4-ClC6H5 4-MeC6H4 4 9336 4-ClC 6 H 5 4-MeC 6 H 4 4 93
37 3-ClC6H4 3-MeC6H4 4 8937 3-ClC 6 H 4 3-MeC 6 H 4 4 89
38 4-CH3OC6H4 C6H5 5 038 4-CH 3 OC 6 H 4 C 6 H 5 5 0
39 2-CH3OC6H4 C6H5 5 039 2-CH 3 OC 6 H 4 C 6 H 5 5 0
实施例5 固液两相相转移催化合成反式-2,3-环氧-3-苯基-1-(4-甲氧基苯基)-丙-1-酮Example 5 Synthesis of trans-2,3-epoxy-3-phenyl-1-(4-methoxyphenyl)-propan-1-one by solid-liquid two-phase phase transfer catalysis
在100ml圆底烧瓶中,加入四丁基溴化铵(322mg,1mmol),30ml甲苯,冷却至10℃,加入固体三氯异氰尿酸(2.32g,10mmol),加入固体KOH(3.36,60mmol),搅拌15分钟。加入反式3-苯基-1-(4-甲氧基苯基)-丙烯酮(2.38g,10mmol),继续搅拌5小时,TLC检测反应终点。升温至室温,往反应液中加入15ml乙醚,过滤,滤液用水洗涤,无水MgSO4干燥。蒸馏除去溶剂,柱色谱分离(硅胶,洗脱液为石油醚/乙酸乙酯:50/1),得到白色晶体,收率为79%。In a 100ml round bottom flask, add tetrabutylammonium bromide (322mg, 1mmol), 30ml toluene, cool to 10°C, add solid trichloroisocyanuric acid (2.32g, 10mmol), add solid KOH (3.36, 60mmol) , and stir for 15 minutes. Trans 3-phenyl-1-(4-methoxyphenyl)-propenone (2.38 g, 10 mmol) was added, stirring was continued for 5 hours, and the end of the reaction was detected by TLC. Warm up to room temperature, add 15ml of diethyl ether to the reaction solution, filter, wash the filtrate with water, and dry over anhydrous MgSO 4 . The solvent was distilled off and separated by column chromatography (silica gel, eluent: petroleum ether/ethyl acetate: 50/1) to obtain white crystals with a yield of 79%.
实施例6 固液两相相转移催化合成反式-2,3-环氧-3-苯基-1-(2-甲氧基苯基)-丙-1-酮Example 6 Synthesis of trans-2,3-epoxy-3-phenyl-1-(2-methoxyphenyl)-propan-1-one by solid-liquid two-phase phase transfer catalysis
反式3-苯基-1-(2-甲氧基苯基)-丙烯酮(2.38g,10mmol),实验方法和步骤同实施例5,收率为76%。Trans 3-phenyl-1-(2-methoxyphenyl)-propenone (2.38 g, 10 mmol), the experimental method and steps are the same as in Example 5, and the yield is 76%.
实施例7 液液两相相转移催化合成反式-2,3-环氧-1,3-二苯基丙-1-酮Example 7 Synthesis of trans-2,3-epoxy-1,3-diphenylpropan-1-one by liquid-liquid two-phase phase transfer catalysis
在100ml圆底烧瓶中,加入查尔酮(2.08g,10mmol),四丁基溴化铵(322mg,1mmol)及30ml甲苯,冷却至0℃,加入固体三氯异氰尿酸(2.32g,10mmol),滴加50% KOH水溶液(6.68g,60mmol)。滴加完毕后0℃下继续搅拌9小时,TLC检测反应终点。升温至室温,往反应液中加入15ml水,两相分离,有机相用无水MgSO4干燥。蒸馏除去溶剂,得到淡黄色固体,正己烷重结晶,得到白色晶体,收率为75%。In a 100ml round bottom flask, add chalcone (2.08g, 10mmol), tetrabutylammonium bromide (322mg, 1mmol) and 30ml toluene, cool to 0°C, add solid trichloroisocyanuric acid (2.32g, 10mmol ), and 50% KOH aqueous solution (6.68 g, 60 mmol) was added dropwise. After the dropwise addition was completed, the mixture was stirred at 0° C. for 9 hours, and the end point of the reaction was detected by TLC. The temperature was raised to room temperature, 15ml of water was added to the reaction solution, the two phases were separated, and the organic phase was dried with anhydrous MgSO 4 . The solvent was distilled off to obtain a light yellow solid, which was recrystallized from n-hexane to obtain white crystals with a yield of 75%.
实施例8 无有机溶剂相转移催化合成反式-2,3-环氧-1,3-二苯基丙-1-酮Example 8 Synthesis of trans-2,3-epoxy-1,3-diphenylpropan-1-one by phase transfer catalysis without organic solvent
20℃下,在100ml圆底烧瓶中,加入十六烷基三甲基溴化铵(0.18g,0.5mmol),50ml水,固体三氯异氰尿酸(2.32g,10mmol),滴加50% KOH水溶液(6.68g,60mmol)。加入查尔酮(2.08g,10mmol),继续搅拌24小时,TLC检测反应终点。往反应液中加入30ml乙醚,两相分离,有机相用无水MgSO4干燥。蒸馏除去溶剂,得到淡黄色固体,正己烷重结晶,得到白色晶体,收率为98%。At 20°C, in a 100ml round bottom flask, add cetyltrimethylammonium bromide (0.18g, 0.5mmol), 50ml of water, solid trichloroisocyanuric acid (2.32g, 10mmol), add dropwise 50% Aqueous KOH (6.68 g, 60 mmol). Chalcone (2.08 g, 10 mmol) was added, stirring was continued for 24 hours, and the end of the reaction was detected by TLC. Add 30ml of diethyl ether to the reaction solution, separate the two phases, and dry the organic phase with anhydrous MgSO 4 . The solvent was distilled off to obtain a light yellow solid, which was recrystallized from n-hexane to obtain white crystals with a yield of 98%.
实施例9 无有机溶剂相转移催化合成反式取代-2,3-环氧-1,3-二苯基丙-1-酮Example 9 Synthesis of trans-substituted-2,3-epoxy-1,3-diphenylpropan-1-one by phase transfer catalysis without organic solvent
将不同反应底物的实施例以表格形式总结如下:(反应条件和步骤同实施例8)The embodiment of different reaction substrates is summarized as follows in tabular form: (reaction condition and step are with embodiment 8)
Table 4.CTMAB催化环氧化反应 Table 4. CTMAB Catalyzed Epoxidation Reaction
序 α,β-不饱和 反应时 收率Sequence α, β-unsaturation Reaction time Yield
号 羰基化合物 间 [%]No. Carbonyl Compounds Between [%]
[小时] [Hour]
R1 R2 R 1 R 2
40 C6H5 4-CH3OC6H4 24 8640 C 6 H 5 4-CH 3 OC 6 H 4 24 86
41 4-ClC6H4 4-FC6H4 24 9441 4-ClC 6 H 4 4-FC 6 H 4 24 94
42 C6H5 4-FC6H4 24 9542 C 6 H 5 4-FC 6 H 4 24 95
43 4-NO2C6H4 C6H5 24 8643 4-NO 2 C 6 H 4 C 6 H 5 24 86
44 C6H5 4-ClC6H4 24 9044 C 6 H 5 4-ClC 6 H 4 24 90
45 4-ClC6H4 C6H5 24 9645 4-ClC 6 H 4 C 6 H 5 24 96
46 2-ClC6H4 C6H5 24 9546 2-ClC 6 H 4 C 6 H 5 24 95
47 4-ClC6H4 4-ClC6H4 24 9347 4-ClC 6 H 4 4-ClC 6 H 4 24 93
48 4-ClC6H4 4-CH3OC6H4 24 8948 4-ClC 6 H 4 4-CH 3 OC 6 H 4 24 89
49 4-CH3OC6H4 C6H4 24 9049 4-CH 3 OC 6 H 4 C 6 H 4 24 90
50 4-CH3OC6H4 4-ClC6H4 24 8750 4-CH 3 OC 6 H 4 4-ClC 6 H 4 24 87
51 2-CH3OC6H4 C6H4 24 8651 2-CH 3 OC 6 H 4 C 6 H 4 24 86
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| CN119569565A (en) * | 2024-11-08 | 2025-03-07 | 杭州云上新材有限公司 | Method for synthesizing 2, 5-dihydroxyterephthalic acid |
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| CN115819377A (en) * | 2022-11-24 | 2023-03-21 | 北京恒加润科技有限公司 | Preparation method and application of perfluoro-2,3-epoxy-2-methylpentane |
| CN115819377B (en) * | 2022-11-24 | 2024-03-01 | 北京恒加润科技有限公司 | Preparation method and application of perfluoro-2, 3-epoxy-2-methylpentane |
| CN119569565A (en) * | 2024-11-08 | 2025-03-07 | 杭州云上新材有限公司 | Method for synthesizing 2, 5-dihydroxyterephthalic acid |
| CN119569565B (en) * | 2024-11-08 | 2025-10-21 | 杭州云上新材有限公司 | A method for synthesizing 2,5-dihydroxyterephthalic acid |
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