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CN104313635A - Electrochemical catalytic synthesis method of alpha-carbonyl ketone compounds - Google Patents

Electrochemical catalytic synthesis method of alpha-carbonyl ketone compounds Download PDF

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CN104313635A
CN104313635A CN201410602128.5A CN201410602128A CN104313635A CN 104313635 A CN104313635 A CN 104313635A CN 201410602128 A CN201410602128 A CN 201410602128A CN 104313635 A CN104313635 A CN 104313635A
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catalyst
ketone compounds
diacetyl
carbonyl
bromide
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曾程初
李龙吉
肖环兰
田红玉
梁森
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Beijing University of Technology
Beijing Technology and Business University
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Beijing University of Technology
Beijing Technology and Business University
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Abstract

α-羰基酮类化合物的电化学催化合成方法,属于α-羰基酮类化合物制备技术领域。该方法是在单室电解池中,在一定的电解质溶液中,以α-羟基酮为原料,以卤化物为催化剂,在一定的温度和电流密度下恒电流电解,得到α-羰基酮类化合物。与合成该类化合物的现有其他电化学方法相比,本发明方法采用单室电解池,使用价格便宜的电极材料,用电化学方法再生氧化剂。本发明不需外加支持电解质,只使用催化量的卤化物为催化剂,成本大为降低,后处理简单,更便于工业化生产。An electrochemical catalytic synthesis method for α-carbonyl ketone compounds belongs to the technical field of preparation of α-carbonyl ketone compounds. The method is in a single-chamber electrolytic cell, in a certain electrolyte solution, using α-hydroxy ketones as raw materials, halides as catalysts, and constant current electrolysis at a certain temperature and current density to obtain α-carbonyl ketone compounds . Compared with other existing electrochemical methods for synthesizing such compounds, the method of the invention adopts a single-chamber electrolytic cell, uses cheap electrode materials, and regenerates the oxidant by electrochemical methods. The invention does not need to add supporting electrolyte, only uses catalytic amount of halide as the catalyst, greatly reduces the cost, is simple in post-treatment, and is more convenient for industrialized production.

Description

α-羰基酮类化合物的电化学催化合成方法Electrochemical catalytic synthesis method of α-carbonyl ketones

技术领域technical field

本发明涉及一种α-羰基酮类化合物的电化学催化合成方法,属于α-羰基酮类化合物制备技术领域。The invention relates to an electrochemical catalytic synthesis method of α-carbonyl ketone compounds, belonging to the technical field of preparation of α-carbonyl ketone compounds.

背景技术Background technique

α-羰基酮类化合物是重要的溶剂,反应中间体或化学试剂。此外,许多α-羰基酮类化合物也作为香料广泛使用。如3,4-己二酮具有黄油香味,丁二酮具有奶油香味,它们被广泛地用于奶油、奶酪、巧克力、糖果、胶冻及布丁的生产中,因此α-羰基酮类化合物的高效合成是人们关注的焦点。α-Carbonyl ketones are important solvents, reaction intermediates or chemical reagents. In addition, many α-carbonyl ketones are also widely used as fragrances. For example, 3,4-hexanedione has a buttery aroma, and diacetyl has a creamy aroma. They are widely used in the production of cream, cheese, chocolate, candy, jelly and pudding. Therefore, the efficient use of α-carbonyl ketones Synthesis is in the spotlight.

α-羟基酮的电化学氧化是合成该类化合物的途径之一。Torii(Inokuchi,T.;Matsumoto,S.;Torii,S.J.Org.Chem.1991,56,2416)等在溴化钠和N-氧代-2,2,6,6-四甲基哌啶铵组成的双催化剂的存在下,以碳酸钠缓冲溶液与二氯甲烷为溶剂,在单室电解池中恒电流电解制备了苯偶酰;王江梅等(王江梅,张银新,丁世玲,刘慧、陈凡立,蒋文强,辽宁化工,2011,40,451)在单室电解池中,以KI为催化剂,电解乙偶姻制备丁二酮,反应中需缓慢滴加双氧水还原KI。Nishiguchi(Maekawa,H.;Sguino,Y.;Nishiguchi,I.Chem.Lett.1994,1017)则在双室电解池中,以溴化钠为催化剂,氧化α-羟基酮合成了α-羰基酮。以上方法存在的主要问题有:The electrochemical oxidation of α-hydroxy ketones is one of the ways to synthesize these compounds. Torii (Inokuchi, T.; Matsumoto, S.; Torii, S.J.Org.Chem.1991,56,2416) etc. in sodium bromide and N-oxo-2,2,6,6-tetramethylpiperidinium In the presence of the double catalyst composed, benzil was prepared by constant current electrolysis in a single chamber electrolytic cell with sodium carbonate buffer solution and dichloromethane as solvent; Wang Jiangmei et al. (Wang Jiangmei, Zhang Yinxin, Ding Shiling, Liu Hui, Chen Fanli, Jiang Wenqiang , Liaoning Chemical Industry, 2011, 40, 451) In a single-chamber electrolytic cell, KI was used as a catalyst to electrolyze acetoin to prepare diacetyl, and hydrogen peroxide was slowly added dropwise to reduce KI during the reaction. Nishiguchi (Maekawa, H.; Sguino, Y.; Nishiguchi, I. Chem. Lett.1994, 1017) synthesized α-carbonyl ketone by oxidation of α-hydroxy ketone with sodium bromide as a catalyst in a double-chamber electrolytic cell . The main problems with the above methods are:

(1)Torii和王江梅虽然使用简单的单室电解池进行电解合成,但合成的α-羟基酮的种类有限,需要使用复杂的双催化剂体系或通过外加氧化剂来再生催化剂,这增加了反应成本和后处理的复杂程度。(1) Although Torii and Wang Jiangmei used a simple single-chamber electrolytic cell for electrolytic synthesis, the types of α-hydroxy ketones synthesized were limited, and it was necessary to use a complex dual-catalyst system or regenerate the catalyst by adding an oxidant, which increased the reaction cost and The complexity of post-processing.

(2)Nishiguchi发现,在单室电解池中该反应不能够有效进行,必须采用双室电解池,同时使用昂贵的金属铂作为电极材料。与单室电解池相比,双室电解池的使用增加了设备的成本,加大了能耗,操作也更复杂。(2) Nishiguchi found that the reaction cannot be carried out effectively in a single-chamber electrolytic cell, and a double-chamber electrolytic cell must be used, while using expensive metal platinum as an electrode material. Compared with the single-chamber electrolytic cell, the use of the double-chamber electrolytic cell increases the cost of the equipment, increases the energy consumption, and the operation is more complicated.

(3)反应液未能循环使用,造成了高浓度有机废液的大量排放。(3) The reaction solution cannot be recycled, resulting in a large discharge of high-concentration organic waste liquid.

目前,在单室电解池中,使用单一催化剂,催化剂可原位再生并且反应液可循环使用的α-羰基酮的制备方法尚未见国内外文献报道。At present, in a single-chamber electrolytic cell, a single catalyst is used, and the preparation method of α-carbonyl ketone, in which the catalyst can be regenerated in situ and the reaction solution can be recycled, has not been reported in the literature at home and abroad.

发明内容Contents of the invention

本发明的目的是提供一种操作简便、成本低且绿色环保的α-羰基酮类化合物的电化学催化合成方法。The object of the present invention is to provide an electrochemical catalytic synthesis method of α-carbonyl ketone compounds with simple operation, low cost and environmental protection.

本发明所提供的α-羰基酮类化合物的的电化学催化合成方法,其步骤是,在单室电解池中,在一定的电解质体系中,以式(II)表示的α-羟基酮为原料,以卤化物为催化剂,在一定的电流密度条件下恒电流电解,得到式(I)表示的α-羰基酮类化合物。The electrochemical catalytic synthesis method of α-carbonyl ketone compounds provided by the present invention comprises the following steps: in a single-chamber electrolytic cell, in a certain electrolyte system, the α-hydroxy ketone represented by formula (II) is used as a raw material , using halides as catalysts, and constant current electrolysis under certain current density conditions, to obtain α-carbonyl ketone compounds represented by formula (I).

其中式(I)与式(II)中R1、R2表示链长1-8个碳原子直链烷基、芳烃取代的直链烷基、苯基、取代苯、芳杂环等,R1、R2相同或不同。Among them, R 1 and R 2 in formula (I) and formula (II) represent straight-chain alkyl groups with a chain length of 1-8 carbon atoms, straight-chain alkyl groups substituted by aromatic hydrocarbons, phenyl groups, substituted benzenes, aromatic heterocycles, etc., and R 1. R 2 are the same or different.

上述的催化剂为碘化四丁基铵、碘化四乙基铵、碘化钠、碘化钾、溴化四丁基铵、溴化四乙基铵、溴化钠或溴化钾,优选溴化钠或溴化钾。Above-mentioned catalyst is tetrabutylammonium iodide, tetraethylammonium iodide, sodium iodide, potassium iodide, tetrabutylammonium bromide, tetraethylammonium bromide, sodium bromide or potassium bromide, preferably sodium bromide or potassium bromide.

上述催化剂的用量为α-羟基酮原料的5-50mol%,优选5-10mol%。The amount of the catalyst used is 5-50 mol%, preferably 5-10 mol%, of the α-hydroxy ketone raw material.

上述电解质体系为水或者水与二氯甲烷的两相混合溶液,优选水与二氯甲烷的两相混合溶液,进一步优选水与二氯甲烷的体积比为(1-2):1。The above electrolyte system is water or a two-phase mixed solution of water and dichloromethane, preferably a two-phase mixed solution of water and dichloromethane, and more preferably the volume ratio of water to dichloromethane is (1-2):1.

上述电解质体系的pH值在1-8之间,优选3-7。The pH value of the above electrolyte system is between 1-8, preferably 3-7.

上述电流密度为10-60mA/cm2,优选10-20mA/cm2The aforementioned current density is 10-60 mA/cm 2 , preferably 10-20 mA/cm 2 .

上述电解用的阳极为玻碳电极、石墨电极或铂电极,优选石墨电极。阴极优选铁。The above-mentioned anode for electrolysis is a glassy carbon electrode, a graphite electrode or a platinum electrode, preferably a graphite electrode. The cathode is preferably iron.

上述反应温度一般为0-室温,优选为室温。The above-mentioned reaction temperature is generally 0-room temperature, preferably room temperature.

本发明方法与现有其他方法相比,具有以下有益效果:Compared with other existing methods, the inventive method has the following beneficial effects:

(1)单室电解池代替双室电解池,避免了隔膜的使用带来设备成本的增加。同时降低了能耗,操作简单。(1) The single-chamber electrolytic cell replaces the double-chamber electrolytic cell, which avoids the increase of equipment cost caused by the use of the diaphragm. At the same time, the energy consumption is reduced and the operation is simple.

(2)用阳极再生催化剂,避免了双催化剂或再生用的外加氧化剂的加入,从而降低了反应成本和后处理的复杂程度,也减少了共氧化剂的大量使用而产生大量的还原废物。(2) Using the anode to regenerate the catalyst avoids the addition of double catalysts or additional oxidants for regeneration, thereby reducing the reaction cost and the complexity of post-treatment, and also reducing the use of co-oxidants to generate a large amount of reduction waste.

(3)反应液可以循环使用,减少环境污染。(3) The reaction solution can be recycled to reduce environmental pollution.

(4)本发明方法使用价格便宜的电极材料,反应条件温和,操作简单,易于工业化。(4) The method of the present invention uses cheap electrode materials, has mild reaction conditions, is simple to operate, and is easy to industrialize.

(5)产率高。(5) High yield.

具体实施方式Detailed ways

下面结合实施例对本发明做进一步说明,但本发明并不限于以下实施例。以下实施例中的每100mmol2-羟基-3-戊酮对应300mL电解质溶液。The present invention will be further described below in conjunction with the examples, but the present invention is not limited to the following examples. In the following examples, every 100 mmol of 2-hydroxy-3-pentanone corresponds to 300 mL of electrolyte solution.

实施例1:2,3-戊二酮的电催化合成Embodiment 1: the electrocatalytic synthesis of 2,3-pentanedione

在400mL的单室电解池中,将100mmol的2-羟基-3-戊酮溶于200mL的NaBr(10mmol)水溶液中,加入100mL二氯甲烷。在室温搅拌下,以石墨为阳极、铁片为阴极,在30mA/cm2恒定电流下电解。当电流效率达到59%时,停止电解,静止分层,常压除去下层有机相中的二氯甲烷,得到2,3戊二酮,产率:78%。In a 400 mL single-chamber electrolytic cell, 100 mmol of 2-hydroxy-3-pentanone was dissolved in 200 mL of NaBr (10 mmol) aqueous solution, and 100 mL of dichloromethane was added. Stirring at room temperature, with graphite as anode and iron sheet as cathode, electrolyze at a constant current of 30mA/ cm2 . When the current efficiency reaches 59%, the electrolysis is stopped, the stratification is static, and the dichloromethane in the lower organic phase is removed under normal pressure to obtain 2,3-pentanedione with a yield of 78%.

黄绿色液体;bp 110-112℃;1H NMR(400MHz,CDCl3):δ1.09(t,3H,J=7.6Hz),2.17(s,3H),2.44(q,2H,J=7.6Hz).Yellow-green liquid; bp 110-112°C; 1 H NMR (400MHz, CDCl 3 ): δ1.09(t, 3H, J=7.6Hz), 2.17(s, 3H), 2.44(q, 2H, J=7.6 Hz).

实施例2:2,3-戊二酮的电催化合成Example 2: Electrocatalytic synthesis of 2,3-pentanedione

同实施例1,以3-羟基-2-戊酮为原料,电催化合成2,3戊二酮,产率:76%。As in Example 1, 2,3-pentanedione was synthesized by electrocatalysis using 3-hydroxy-2-pentanone as a raw material, with a yield of 76%.

黄绿色液体;bp 110-112℃;1H NMR(400MHz,CDCl3):δ1.09(t,3H,J=7.6Hz),2.17(s,3H),2.44(q,2H,J=7.6Hz).Yellow-green liquid; bp 110-112°C; 1 H NMR (400MHz, CDCl 3 ): δ1.09(t, 3H, J=7.6Hz), 2.17(s, 3H), 2.44(q, 2H, J=7.6 Hz).

实施例3:3,4-己二酮的电催化合成Example 3: Electrocatalytic synthesis of 3,4-hexanedione

同实施例1,以丙偶姻为原料,电催化合成3,4-己二酮,产率:85%。As in Example 1, 3,4-hexanedione was electrocatalytically synthesized using propioin as a raw material, with a yield of 85%.

黄绿色液体;bp 131℃;1H NMR(400MHz,CDCl3):δ1.10(t,3H,J=7.6Hz),2.47(q,2H,J=7.6Hz).Yellow-green liquid; bp 131°C; 1 H NMR (400MHz, CDCl 3 ): δ1.10(t, 3H, J=7.6Hz), 2.47(q, 2H, J=7.6Hz).

实施例4:十二烷-6,7-二酮的电催化合成Example 4: Electrocatalytic synthesis of dodecane-6,7-dione

同实施例1,以己偶姻为原料,电催化合成十二烷-6,7-二酮,产率:89%。As in Example 1, dodecane-6,7-dione was electrocatalytically synthesized with axoin as a raw material, and the yield was 89%.

黄绿色液体;bp 110-113℃;1H NMR(400MHz):δ0.88(m,6H),1.22-1.32(m,8H),1.57(m,4H),2.72(t,J=7.6Hz,4H).Yellow-green liquid; bp 110-113°C; 1 H NMR (400MHz): δ0.88(m, 6H), 1.22-1.32(m, 8H), 1.57(m, 4H), 2.72(t, J=7.6Hz ,4H).

实施例5:苯偶酰的电催化合成Embodiment 5: the electrocatalytic synthesis of benzil

同实施例1,以苯偶姻为原料,电催化合成苯偶酰,产率:71%。Same as Example 1, using benzoin as raw material, electrocatalytically synthesized benzil, yield: 71%.

黄绿色固体;mp 94-95℃;1H NMR(400MHz,CDCl3):δ7.98(d,J=7.2Hz,4H),7.67-7.64(m,2H),7.53-7.50(m,4H).Yellow-green solid; mp 94-95°C; 1 H NMR (400MHz, CDCl 3 ): δ7.98(d, J=7.2Hz, 4H), 7.67-7.64(m, 2H), 7.53-7.50(m, 4H ).

实施例6:4-甲氧基苯偶酰的电催化合成Embodiment 6: the electrocatalytic synthesis of 4-methoxybenzil

同实施例1,以4-甲氧基苯偶姻为原料,电催化合成4-甲氧基苯偶酰,产率:77%。Same as Example 1, using 4-methoxybenzoin as raw material, electrocatalytically synthesized 4-methoxybenzil, yield: 77%.

黄绿色粉末;mp 132-134℃;1H NMR(400MHz,CDCl3):δ7.16(t,1H,J=7.2Hz,Ar-H),7.30(d,2H,J=8.8Hz,Ar-H),3.77(s,6H).Yellow-green powder; mp 132-134°C; 1 H NMR (400MHz, CDCl 3 ): δ7.16(t, 1H, J=7.2Hz, Ar-H), 7.30(d, 2H, J=8.8Hz, Ar -H),3.77(s,6H).

实施例7:4-氯苯偶酰的电催化合成Example 7: Electrocatalytic synthesis of 4-chlorobenzil

同实施例1,以4-氯苯偶姻为原料,电催化合成4-氯苯偶酰,产率:80%。.Same as Example 1, using 4-chlorobenzoin as raw material, electrocatalytically synthesized 4-chlorobenzil, yield: 80%. .

黄绿色粉末;mp 224-226℃;1H NMR(400MHz,CDCl3):δ7.00(d,4H,J=8.8Hz),7.48(d,4H,J=8.8Hz).Yellow-green powder; mp 224-226°C; 1 H NMR (400MHz, CDCl 3 ): δ7.00(d, 4H, J=8.8Hz), 7.48(d, 4H, J=8.8Hz).

实施例8:丁二酮的电催化合成Embodiment 8: the electrocatalytic synthesis of diacetyl

同实施例1,以乙偶姻为原料,体积比为1:1,产率:62%。Same as Example 1, using acetoin as the raw material, the volume ratio is 1:1, and the yield: 62%.

黄绿色液体;bp:88-90℃;1H NMR(400MHz,CDCl3):δ2.17(s,3H).Yellow-green liquid; bp: 88-90°C; 1 H NMR (400MHz, CDCl 3 ): δ2.17(s, 3H).

实施例9:丁二酮的电催化合成Embodiment 9: the electrocatalytic synthesis of diacetyl

同实施例8,催化剂为溴化钾,丁二酮的GC产率为53%。Same as Example 8, the catalyst is potassium bromide, and the GC yield of diacetyl is 53%.

实施例10:丁二酮的电催化合成Embodiment 10: the electrocatalytic synthesis of diacetyl

同实施例8,催化剂为碘化钠,丁二酮的GC产率为45%。Same as Example 8, the catalyst is sodium iodide, and the GC yield of diacetyl is 45%.

实施例11:丁二酮的电催化合成Example 11: Electrocatalytic synthesis of diacetyl

同实施例8,催化剂为碘化钾,丁二酮的GC产率为48%。Same as Example 8, the catalyst is potassium iodide, and the GC yield of diacetyl is 48%.

实施例12:丁二酮的电催化合成Example 12: Electrocatalytic synthesis of diacetyl

同实施例8,催化剂为溴化四丁基铵,丁二酮的GC产率为56%。Same as Example 8, the catalyst is tetrabutylammonium bromide, and the GC yield of diacetyl is 56%.

实施例13:丁二酮的电催化合成Example 13: Electrocatalytic synthesis of diacetyl

同实施例8,催化剂为溴化四乙基铵,丁二酮的GC产率为57%。Same as Example 8, the catalyst is tetraethylammonium bromide, and the GC yield of diacetyl is 57%.

实施例14:丁二酮的电催化合成Example 14: Electrocatalytic synthesis of diacetyl

同实施例8,电流密度为10mA/cm2,丁二酮的GC产率为45%。As in Example 8, the current density was 10 mA/cm 2 , and the GC yield of diacetyl was 45%.

实施例15:丁二酮的电催化合成Example 15: Electrocatalytic synthesis of diacetyl

同实施例8,电流密度为20mA/cm2,丁二酮的GC产率为61%。As in Example 8, the current density was 20 mA/cm 2 , and the GC yield of diacetyl was 61%.

实施例16:丁二酮的电催化合成Example 16: Electrocatalytic synthesis of diacetyl

同实施例8,电流密度为40mA/cm2,丁二酮的GC产率为58%。As in Example 8, the current density was 40 mA/cm 2 , and the GC yield of diacetyl was 58%.

实施例17:丁二酮的电催化合成Example 17: Electrocatalytic synthesis of diacetyl

同实施例8,电流密度为50mA/cm2,丁二酮的GC产率为55%。As in Example 8, the current density was 50 mA/cm 2 , and the GC yield of diacetyl was 55%.

实施例18:丁二酮的电催化合成Example 18: Electrocatalytic synthesis of diacetyl

同实施例8,电流密度为60mA/cm2,丁二酮的GC产率为32%。Same as Example 8, the current density was 60 mA/cm 2 , and the GC yield of diacetyl was 32%.

实施例19:丁二酮的电催化合成Embodiment 19: Electrocatalytic synthesis of diacetyl

同实施例8,NaBr(5mmol),丁二酮的GC产率为61%。Same as Example 8, NaBr (5mmol), the GC yield of diacetyl was 61%.

实施例20:丁二酮的电催化合成Example 20: Electrocatalytic synthesis of diacetyl

同实施例8,NaBr(20mmol),丁二酮的GC产率为55%。Same as Example 8, NaBr (20mmol), the GC yield of diacetyl was 55%.

实施例21:丁二酮的电催化合成Example 21: Electrocatalytic synthesis of diacetyl

同实施例8,NaBr(50mmol),丁二酮的GC产率为39%。Same as Example 8, NaBr (50mmol), the GC yield of diacetyl was 39%.

实施例22:丁二酮的电催化合成Example 22: Electrocatalytic synthesis of diacetyl

同实施例8,玻碳作为阳极,丁二酮的GC产率为55%。Same as Example 8, glassy carbon is used as the anode, and the GC yield of diacetyl is 55%.

实施例23:丁二酮的电催化合成Example 23: Electrocatalytic synthesis of diacetyl

同实施例8,铂作为阳极,丁二酮的GC产率为58%。Same as Example 8, platinum was used as the anode, and the GC yield of diacetyl was 58%.

Claims (10)

1.α-羰基酮类化合物的的电化学催化合成方法,其特征在于,步骤是,在单室电解池中,在一定的电解质体系中,以式(II)表示的α-羟基酮为原料,以卤化物为催化剂,在一定的电流密度条件下恒电流电解,得到式(I)表示的α-羰基酮类化合物;  1. The electrochemical catalytic synthesis method of α-carbonyl ketone compounds is characterized in that, the step is, in a single chamber electrolytic cell, in a certain electrolyte system, the α-hydroxy ketone represented by formula (II) is used as raw material , using halides as catalysts, constant current electrolysis under certain current density conditions, to obtain α-carbonyl ketone compounds represented by formula (I); 其中式(I)与式(II)中R1、R2表示链长1-8个碳原子直链烷基、芳烃取代的直链烷基、苯基、取代苯、芳杂环,R1、R2相同或不同;  In formula (I) and formula (II), R 1 and R 2 represent straight-chain alkyl groups with a chain length of 1-8 carbon atoms, straight-chain alkyl groups substituted by aromatic hydrocarbons, phenyl groups, substituted benzenes, aromatic heterocycles, and R 1 , R 2 are the same or different; 催化剂为碘化四丁基铵、碘化四乙基铵、碘化钠、碘化钾、溴化四丁基铵、溴化四乙基铵、溴化钠或溴化钾;电解质体系为水或者水与二氯甲烷的两相混合溶液。  The catalyst is tetrabutylammonium iodide, tetraethylammonium iodide, sodium iodide, potassium iodide, tetrabutylammonium bromide, tetraethylammonium bromide, sodium bromide or potassium bromide; the electrolyte system is water or water Two-phase mixed solution with dichloromethane. the 2.按照权利要求1的方法,其特征在于,催化剂为催化剂的用量为α-羟基酮原料的5-50mol%。  2. according to the method for claim 1, it is characterized in that, catalyst is that the consumption of catalyst is 5-50mol% of α-hydroxy ketone raw material. the 3.按照权利要求1的方法,其特征在于,催化剂的用量为α-羟基酮原料的5-10mol%。  3. The method according to claim 1, characterized in that the catalyst is used in an amount of 5-10 mol% of the alpha-hydroxy ketone starting material. the 4.按照权利要求1的方法,其特征在于,水与二氯甲烷的体积比为(1-2):1。  4. according to the method for claim 1, it is characterized in that, the volume ratio of water and methylene chloride is (1-2):1. the 5.按照权利要求1的方法,其特征在于,电解质体系的pH值在1-8之间。  5. The method according to claim 1, characterized in that the pH of the electrolyte system is between 1-8. the 6.按照权利要求5的方法,其特征在于,电解质体系的pH值在3-7。  6. The method according to claim 5, characterized in that the pH of the electrolyte system is between 3-7. the 7.按照权利要求1的方法,其特征在于,电流密度为10-60mA/cm2。  7. The method according to claim 1, characterized in that the current density is 10-60 mA/cm 2 . 8.按照权利要求7的方法,其特征在于,电流密度为10-20mA/cm2。  8. The method according to claim 7, characterized in that the current density is 10-20 mA/cm 2 . 9.按照权利要求1的方法,其特征在于,电解用的阳极为玻碳电极、石墨电极或铂电极。  9. according to the method for claim 1, it is characterized in that, the anode that electrolysis is used is glassy carbon electrode, graphite electrode or platinum electrode. the 10.按照权利要求1的方法,其特征在于,反应温度一般为0-室温。  10. The method according to claim 1, characterized in that the reaction temperature is generally 0-room temperature. the
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