CN112028793A - Method for preparing nitrile by bismuth complex catalytic amide dehydration - Google Patents

Method for preparing nitrile by bismuth complex catalytic amide dehydration Download PDF

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CN112028793A
CN112028793A CN202010822370.9A CN202010822370A CN112028793A CN 112028793 A CN112028793 A CN 112028793A CN 202010822370 A CN202010822370 A CN 202010822370A CN 112028793 A CN112028793 A CN 112028793A
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bismuth
amide
nitrile
dehydration
complex
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陈新志
阮诗想
阮建成
周少东
钱超
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Zhejiang University ZJU
Institute of Zhejiang University Quzhou
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Abstract

The invention discloses a method for preparing nitrile by catalyzing amide dehydration with a bismuth complex, which comprises the following steps: reacting bismuth salt and a ligand in a solvent at room temperature to obtain a solution containing a bismuth complex; adding amide into the solution containing the bismuth complex, and reacting for 6-18 h at room temperature and normal pressure to realize amide dehydration to generate nitrile, wherein the bismuth complex is used as a catalyst; and separating the obtained reaction liquid to obtain a crude product of the nitrile corresponding to the amide. The method has the advantages of mild reaction conditions, high reaction selectivity, wide substrate applicability, simple post-treatment and energy consumption reduction.

Description

铋配合物催化酰胺脱水制备腈的方法Method for preparing nitrile by bismuth complex-catalyzed amide dehydration

技术领域technical field

本发明涉及一种由酰胺制备腈的方法。The present invention relates to a method for preparing nitriles from amides.

背景技术Background technique

腈是重要的化工原料和合成中间体,广泛用于制造药物、合成纤维和塑料例如,己二腈是制备尼纶66的原料。丙烯腈则是生产聚丙烯腈的单体,它与其他单体共聚合,可用于生产合成橡胶和工程塑料。苯甲腈主要用作苯代三聚氰胺等高级涂料的中间体,也是合成农药、脂肪族胺、苯甲酸的中间体,并可作为腈基橡胶、树脂、聚合物和涂料等的溶剂。苯乙腈用来生产医药、农药的中间体苯乙酸、苯乙胺、二苯乙腈、β-苯乙醇、苯乙醛、α-氯代苯乙酸乙酯等,用于制造辛硫磷、稻丰散、青霉素、苯巴比妥等。邻甲基苯甲腈可用于合成农用杀菌剂醚菌酯、灭锈胺、氟酰胺等。异丙基苯甲腈可以合成异丙基苯胺。邻氯苯甲腈主要用于合成染料中间体2-氰基-4-硝基苯胺,医药工业用于合成抗疟疾药物硝喹等。邻苯二甲腈可用于合成酞菁颜料和染料、酞磺胺药物、二甲苯二异氰酸酯塑料、高热阻聚酰胺纤维以及脱硫催化剂等。Nitrile is an important chemical raw material and synthetic intermediate, which is widely used in the manufacture of medicines, synthetic fibers and plastics. For example, adiponitrile is the raw material for the preparation of nylon 66. Acrylonitrile is a monomer for the production of polyacrylonitrile, which is copolymerized with other monomers and can be used to produce synthetic rubber and engineering plastics. Benzonitrile is mainly used as an intermediate for advanced coatings such as benzo-substituted melamine, as well as an intermediate for the synthesis of pesticides, aliphatic amines, and benzoic acid, and as a solvent for nitrile-based rubber, resins, polymers, and coatings. Phenylacetonitrile is used to produce intermediates of medicine and pesticides such as phenylacetic acid, phenylethylamine, diphenylacetonitrile, β-phenylethyl alcohol, phenylacetaldehyde, α-chlorophenylacetate, etc. powder, penicillin, phenobarbital, etc. o-Toluonitrile can be used to synthesize agricultural fungicides pyraclostrobin, rust amine, fluorinamide, etc. Isopropyl benzonitrile can synthesize isopropyl aniline. o-Chlorobenzonitrile is mainly used in the synthesis of dye intermediates 2-cyano-4-nitroaniline, and in the pharmaceutical industry for the synthesis of antimalarial drugs such as nitroquine. Phthalonitrile can be used to synthesize phthalocyanine pigments and dyes, phthalosulfonamide drugs, xylene diisocyanate plastics, high thermal resistance polyamide fibers and desulfurization catalysts.

目前,腈的合成方法主要包括烷烃、烯烃、醛醇和胺类底物的氧化腈化,采用氰基源为反应试剂对烷烃、卤代烷烃、烯烃类底物的直接氰化以及酰胺、羧酸(酯)和醛肟底物的脱水腈化。在这些方法中,由酰胺脱水制备相应腈的方法具有反应试剂低毒、反应副产物为水、反应选择性高等优势,具有较高的环境与经济效益。At present, the synthesis methods of nitriles mainly include the oxidative nitrification of alkanes, alkenes, aldols and amine substrates, the direct cyanation of alkanes, halogenated alkanes, and alkene substrates by using cyano sources as reagents, and the direct cyanation of amides, carboxylic acids ( esters) and dehydration nitrification of aldoxime substrates. Among these methods, the method for preparing the corresponding nitrile by amide dehydration has the advantages of low toxicity of the reaction reagent, water by-product of the reaction, high reaction selectivity, and high environmental and economic benefits.

酰胺脱水制备腈的传统方法是采用化学计量的酸性试剂(如P4O10、POCl3、SOCl2、TiCl4等)以及碱性试剂(如NaBH4)作为脱水剂促进酰胺脱水,这些方法会产生大量酸性或碱性副产物,腐蚀设备且环保压力较大;在此基础上,学者们开发了一系列新型催化剂,包括氢化硅烷脱水体系、高温催化体系、钯催化脱水腈化体系等,其中,各种过渡金属或氮宾催化活化氢硅化物的Si-H键,形成亲电子的硅氢物种,这些反应中间体可促进伯酰胺脱水生成腈,但是在反应过程中伴随生成氢气和甲硅烷基醚,增大分离难度;在没有脱水剂的情况下,酰胺脱水生成腈需要较高的反应温度(>160℃),Campbell等(Campbell J,McdougaldG,Mcnab H,et al.Synthesis,2007,20:3179-3184)报道了在快速真空热解条件下,脱水剂3A二氧化硅和三氧化钨催化酰胺和肟的脱水性能,该反应不产生其它副产物,但是反应温度较高(300℃以上),只适合热稳定的酰胺。Sueoka等(Sueoka S,Mitsudome T,MizugakiT,et al.Chem Commun,2010,46:8243-8245)报道了一种在水滑石上负载单体氧化钒的材料可以用于酰胺脱水的非均相催化剂,酰胺在负载量为20mol%的催化作用下,在均三甲苯中回流反应脱水成腈,该体系反应温度较高(>160℃),能耗较高且增加腈与溶剂的分离难度。The traditional method of amide dehydration to prepare nitrile is to use stoichiometric acid reagents (such as P 4 O 10 , POCl 3 , SOCl 2 , TiCl 4 , etc.) and basic reagents (such as NaBH 4 ) as dehydrating agents to promote amide dehydration. A large number of acidic or basic by-products are produced, which corrode equipment and put a lot of pressure on environmental protection; on this basis, scholars have developed a series of new catalysts, including hydrosilane dehydration system, high temperature catalytic system, palladium catalytic dehydration nitrification system, etc., among which , various transition metals or nitrenes catalyze the activation of Si-H bonds of hydrosilicides to form electrophilic silicon-hydrogen species, these reaction intermediates can promote the dehydration of primary amides to form nitriles, but are accompanied by the formation of hydrogen and monosilane during the reaction. base ether, which increases the difficulty of separation; in the absence of a dehydrating agent, the dehydration of amides to nitrile requires higher reaction temperatures (>160 °C), Campbell et al. (Campbell J, McdougaldG, Mcnab H, et al.Synthesis, 2007, 20:3179-3184) reported the dehydration performance of dehydrating agent 3A silicon dioxide and tungsten trioxide catalyzing amide and oxime under the condition of rapid vacuum pyrolysis, the reaction does not produce other by-products, but the reaction temperature is relatively high (300 ℃). above), only for thermally stable amides. Sueoka et al. (Sueoka S, Mitsudome T, Mizugaki T, et al. Chem Commun, 2010, 46: 8243-8245) reported a heterogeneous catalyst for amide dehydration based on hydrotalcite-supported monomeric vanadium oxide , the amide is dehydrated into nitrile by reflux reaction in mesitylene under the catalysis of 20mol% loading. The reaction temperature of this system is high (>160°C), the energy consumption is high and the separation difficulty of nitrile and solvent is increased.

上述在无脱水剂存在下的酰胺脱水反应假设改成在常规的室温下进行,会导致反应无法有效进行。The above-mentioned amide dehydration reaction in the absence of a dehydrating agent is assumed to be carried out at a conventional room temperature, which will result in the ineffective reaction.

发明内容SUMMARY OF THE INVENTION

本发明要解决的技术问题是提供一种温和条件下的铋配合物催化酰胺脱水制备腈的方法。The technical problem to be solved by the present invention is to provide a method for preparing nitrile by catalytic amide dehydration of bismuth complex under mild conditions.

为了解决上述技术问题,本发明提供一种铋配合物催化酰胺脱水制备腈的方法,包括以下步骤:In order to solve the above-mentioned technical problems, the present invention provides a method for preparing nitrile by bismuth complex catalyzed amide dehydration, comprising the following steps:

1)、铋盐(三价铋盐)与配体在溶剂中于室温下反应(2±0.5)小时,得含有铋配合物的溶液;1), bismuth salt (trivalent bismuth salt) and ligand react (2 ± 0.5) hours at room temperature in solvent to obtain a solution containing bismuth complex;

所述铋盐:配体=1:1~5的摩尔比;The bismuth salt: ligand=1:1~5 molar ratio;

2)、向步骤1)所得的含有铋配合物的溶液中加入酰胺,于室温、常压下反应6~18h,从而实现酰胺脱水生成腈,铋配合物作为催化剂;2), adding an amide to the solution containing the bismuth complex obtained in step 1), and reacting at room temperature and normal pressure for 6 to 18 hours, thereby realizing the dehydration of the amide to generate nitrile, and the bismuth complex is used as a catalyst;

所述酰胺:步骤1)中的铋盐=5~25:1的摩尔比;The amide: the bismuth salt in step 1)=5~25:1 mol ratio;

3)、步骤2)所得的反应液经分离,得到酰胺所对应的腈的粗品。3) The reaction solution obtained in step 2) is separated to obtain the crude product of the nitrile corresponding to the amide.

作为本发明的铋配合物催化酰胺脱水制备腈的方法的改进:The improvement of the method for preparing nitrile as bismuth complex catalyzed amide dehydration of the present invention:

步骤3)分离过程中所得的溶剂、催化剂和未反应的酰胺进行循环反应。Step 3) The solvent, catalyst and unreacted amide obtained in the separation process are subjected to cyclic reaction.

作为本发明的铋配合物催化酰胺脱水制备腈的方法的进一步改进:As the further improvement of the method for preparing nitrile by catalyzing amide dehydration of bismuth complex of the present invention:

铋盐为醋酸铋(优选)、三氟化铋、三氯化铋、三溴化铋、硝酸铋(优选)、硫酸铋、磷酸铋、硼酸铋中的至少一种;The bismuth salt is at least one of bismuth acetate (preferred), bismuth trifluoride, bismuth trichloride, bismuth tribromide, bismuth nitrate (preferred), bismuth sulfate, bismuth phosphate, and bismuth borate;

配体为二乙胺、三乙胺、乙二胺、乙醇胺、二乙醇胺、三乙醇胺、吡啶、2,2'-联吡啶、1,10-邻二氮杂菲、三苯基膦、三环己基膦、1,1'-联二萘酚中的至少一种。Ligands are diethylamine, triethylamine, ethylenediamine, ethanolamine, diethanolamine, triethanolamine, pyridine, 2,2'-bipyridine, 1,10-o-phenanthroline, triphenylphosphine, tricyclic At least one of hexylphosphine and 1,1'-binaphthol.

作为本发明的铋配合物催化酰胺脱水制备腈的方法的进一步改进:As the further improvement of the method for preparing nitrile by catalyzing amide dehydration of bismuth complex of the present invention:

所述步骤2)中的酰胺为R-(CONH2)X,R为C6-20芳基、C1-20直链或支链烷基、C1-20直链或支链烯基、C1-20直链或支链炔基、C3-20环烷基、C3-20烯基、C3-20氮杂环基、C3-20氧杂环基、C3-20硫杂环基;X为1或2;The amide in the step 2) is R-(CONH 2 ) X , and R is C 6-20 aryl, C 1-20 straight or branched alkyl, C 1-20 straight or branched alkenyl, C 1-20 straight or branched chain alkynyl, C 3-20 cycloalkyl, C 3-20 alkenyl, C 3-20 azacyclyl, C 3-20 oxacyclyl , C 3-20 sulfur Heterocyclyl; X is 1 or 2;

基团R中可含有至少一个(一个或多个)的卤素、羟基、羧基、羰基、氨基、硝基、巯基等基团。The group R may contain at least one (one or more) halogen, hydroxyl, carboxyl, carbonyl, amino, nitro, mercapto and other groups.

作为示例,所述酰胺为以下任一:苯甲酰胺、2-甲基苯甲酰胺、3-甲基苯甲酰胺、2,3-二甲基苯甲酰胺、2-硝基-4羧基苯甲酰胺、4-叔丁基苯甲酰胺、4-甲氧基苯甲酰胺、2-氟苯甲酰胺、2-氯苯甲酰胺、2-溴苯甲酰胺、4-羟基苯甲酰胺、3-甲氧基苯甲酰胺、4-硝基苯甲酰胺、2-氨基苯甲酰胺、2-噻吩甲酰胺、对苯二甲酰胺、苯乙酰胺、萘-1-甲酰胺、喹啉-6-甲酰胺、4-吡啶甲酰胺、2,5-呋喃二甲酰胺、丁酰胺、异丁酰胺、己酰胺、琥珀酰胺、己二酰胺、十二酰胺、十八酰胺、环己甲酰胺。By way of example, the amide is any of the following: benzamide, 2-methylbenzamide, 3-methylbenzamide, 2,3-dimethylbenzamide, 2-nitro-4-carboxybenzene Formamide, 4-tert-butylbenzamide, 4-methoxybenzamide, 2-fluorobenzamide, 2-chlorobenzamide, 2-bromobenzamide, 4-hydroxybenzamide, 3 -Methoxybenzamide, 4-nitrobenzamide, 2-aminobenzamide, 2-thiophenecarboxamide, terephthalamide, phenylacetamide, naphthalene-1-carboxamide, quinoline-6 - Formamide, 4-pyridinecarboxamide, 2,5-furandicarboxamide, butanamide, isobutyramide, caproamide, succinamide, adipamide, dodecamide, octadecylamide, cyclohexylcarboxamide.

作为本发明的铋配合物催化酰胺脱水制备腈的方法的进一步改进:As the further improvement of the method for preparing nitrile by catalyzing amide dehydration of bismuth complex of the present invention:

步骤1)中的溶剂为甲醇、乙醇、乙二醇、异丙醇、四氢呋喃、乙腈、乙酸乙酯、环己烷、二氯甲烷、1,2-二氯乙烷、甲苯中的至少一种。The solvent in step 1) is at least one of methanol, ethanol, ethylene glycol, isopropanol, tetrahydrofuran, acetonitrile, ethyl acetate, cyclohexane, dichloromethane, 1,2-dichloroethane and toluene .

作为本发明的铋配合物催化酰胺脱水制备腈的方法的进一步改进,步骤3)中的分离为:步骤2)所得的反应液减压精馏,馏出液分别为溶剂、水、腈的粗品;釜底液中含有催化剂和未反应的酰胺。As a further improvement of the method for preparing nitrile by catalytic amide dehydration of bismuth complex of the present invention, the separation in step 3) is as follows: the reaction solution obtained in step 2) is rectified under reduced pressure, and the distillate is respectively the crude product of solvent, water and nitrile ; The bottom liquid contains catalyst and unreacted amide.

腈的粗品可通过常规的精馏方式进行进一步提纯,从而得到腈的纯品。The crude nitrile can be further purified by conventional rectification to obtain the pure nitrile.

在本发明中,1mol酰胺一般配用0.5~1L溶剂;室温是指15~35℃。In the present invention, 1 mol of amide is generally matched with 0.5 to 1 L of solvent; room temperature refers to 15 to 35°C.

本发明步骤2)的酰胺转化率不低于95.0%。步骤3)中,反应液经分离后得到纯度≥95.0%的腈(腈的粗品),而后经过进一步的提纯,得到纯度≥99.5%的腈。The amide conversion rate of step 2) of the present invention is not less than 95.0%. In step 3), the reaction solution is separated to obtain nitrile (crude product of nitrile) with a purity of ≥95.0%, and further purification to obtain a nitrile with a purity of ≥99.5%.

与现有技术相比,本发明具有如下技术优势:Compared with the prior art, the present invention has the following technical advantages:

(1)催化剂制备简单、在铋配合物催化下,由酰胺制备相应的腈,无需使用脱水剂,副产物只有水,减少三废排放;(1) The preparation of the catalyst is simple. Under the catalysis of the bismuth complex, the corresponding nitrile is prepared from the amide without using a dehydrating agent, and the by-product is only water, which reduces the discharge of three wastes;

(2)在均相催化体系中反应,反应效率高;(2) The reaction is carried out in a homogeneous catalytic system, and the reaction efficiency is high;

(3)在温和条件下反应,反应选择性高,底物适用性广,后处理简单,降低能耗。(3) The reaction is carried out under mild conditions, the reaction selectivity is high, the substrate applicability is wide, the post-processing is simple, and the energy consumption is reduced.

具体实施方式Detailed ways

下面根据具体实施例对本发明的技术方案做进一步说明。本发明的保护范围不限于以下实施例,列举这些实例仅出于示例性目的而不以任何方式限制本发明。The technical solutions of the present invention will be further described below according to specific embodiments. The protection scope of the present invention is not limited to the following examples, which are listed for illustrative purposes only and do not limit the present invention in any way.

实施例1-1、一种铋配合物催化苯甲酰胺高效脱水制备苯甲腈的方法,依次进行以下步骤:Embodiment 1-1, a kind of bismuth complex catalyzed the method for the efficient dehydration of benzamide to prepare benzonitrile, carry out the following steps successively:

(1)、在反应容器中,先将3mol三乙胺溶于10L的甲醇中,得含有三乙胺的甲醇溶液;(1), in reaction vessel, first 3mol triethylamine is dissolved in the methanol of 10L, must contain the methanol solution of triethylamine;

再将1mol的醋酸铋溶于上述含有三乙胺的甲醇溶液中,室温下搅拌2h,得到含铋配合物的溶液;铋配合物作为催化剂;Then 1 mol of bismuth acetate was dissolved in the methanol solution containing triethylamine, and stirred at room temperature for 2 h to obtain a solution containing bismuth complex; the bismuth complex was used as a catalyst;

(2)将15mol的苯甲酰胺加入至上述反应器,在常压、室温下搅拌反应12h;得反应后物料(反应液)。(2) 15mol of benzamide was added to the above-mentioned reactor, and the reaction was stirred at normal pressure and room temperature for 12 hours; the reacted material (reaction solution) was obtained.

(3)步骤(2)所得的反应后物料经GC分析,原料(苯甲酰胺)转化率为98.8%,选择性为99.8%;(3) The material after the reaction of step (2) gained is analyzed by GC, and the conversion rate of the raw material (benzamide) is 98.8%, and the selectivity is 99.8%;

将上述反应后物料按照如下条件进行分离:进行减压(2.0kPa~5.0kPa)精馏,馏出液依次得到甲醇、水、苯甲腈粗品(约80~100℃的馏分),釜底液为催化剂、未反应的苯甲酰胺等的混合物。苯甲腈粗品纯度为95.0%。The materials after the above-mentioned reaction are separated according to the following conditions: carry out rectification under reduced pressure (2.0kPa~5.0kPa), and the distillate successively obtains methanol, water, and benzonitrile crude products (fractions of about 80~100° C.), and the bottom liquid It is a mixture of catalyst, unreacted benzamide, etc. The purity of crude benzonitrile was 95.0%.

所述苯甲腈粗品通过常规的精馏进行进一步提纯,得到苯甲腈产品。苯甲腈产品纯度大于99.5%,收率96.5%。苯甲腈收率的计算公式为:The benzonitrile crude product is further purified by conventional rectification to obtain the benzonitrile product. The purity of the benzonitrile product is more than 99.5%, and the yield is 96.5%. The formula for calculating the yield of benzonitrile is:

Figure BDA0002634963180000041
Figure BDA0002634963180000041

其中,Y——产物收率;Wherein, Y---product yield;

M1——苯甲腈实际产量;M 1 - the actual output of benzonitrile;

M2——苯甲腈理论产量。M 2 ——the theoretical yield of benzonitrile.

实施例1-2、催化剂循环套用:Embodiment 1-2, the catalyst circulation is applied mechanically:

首次循环套用:在实施例1反应后分离所得的釜底液、甲醇中补充加入苯甲酰胺和甲醇,直至加入的苯甲酰胺以及釜底液中含有的苯甲酰胺的总量为15mol,且甲醇的总量为10L(即,同实施例1-1的用量),其余等同于实施例1-1。反应时间为12h时,苯甲酰胺转化率为98.6%,反应选择性为99.8%,产品收率为96.3%,产品纯度为99.0%。The first cycle is applied mechanically: after the reaction of Example 1, the addition of benzamide and methyl alcohol is added in the bottom liquid, methanol of the separated gained, until the total amount of the benzamide contained in the benzamide added and the bottom liquid is 15mol, and The total amount of methanol is 10L (that is, the same as the amount used in Example 1-1), and the rest are the same as in Example 1-1. When the reaction time is 12h, the conversion rate of benzamide is 98.6%, the reaction selectivity is 99.8%, the product yield is 96.3%, and the product purity is 99.0%.

说明:一般需要事先检测釜底液中苯甲酰胺的含量。Note: Generally, it is necessary to detect the content of benzamide in the bottom liquid of the kettle in advance.

重复上述循环套用,到第八次时,苯甲酰胺转化率为95.2%,反应选择性为99.0%,产品收率为92.0%,产品纯度为98.0%。此时,反应体系中有较多杂质,降低产品纯度,不再循环套用。By repeating the above cycle, at the eighth time, the benzamide conversion rate was 95.2%, the reaction selectivity was 99.0%, the product yield was 92.0%, and the product purity was 98.0%. At this time, there are many impurities in the reaction system, which reduces the product purity and is no longer recycled.

实施例2~5、改变催化剂中配体与醋酸铋的摩尔比,醋酸铋的用量保持不变;其他操作等同于实施例1-1,得到实施例2~5,工艺参数及反应结果参见表1。Embodiment 2~5, change the molar ratio of ligand and bismuth acetate in the catalyst, the consumption of bismuth acetate remains unchanged; other operations are equivalent to embodiment 1-1, obtain embodiment 2~5, process parameter and reaction result refer to table 1.

表1Table 1

实施例Example 配体与醋酸铋的摩尔比Molar ratio of ligand to bismuth acetate 原料转化率(%)Raw material conversion rate (%) 反应选择性(%)Reaction selectivity (%) 产品收率(%)Product yield (%) 22 1:11:1 95.195.1 99.899.8 92.592.5 33 2:12:1 97.897.8 99.899.8 95.295.2 44 4:14:1 99.399.3 99.899.8 97.097.0 55 5:15:1 99.599.5 99.899.8 97.197.1

实施例6~12、改变铋盐种类,铋盐的用量保持不变,仍然为1mol,其他操作等同于实施例1-1,得到实施例6~12,工艺参数及反应结果参见表2。Examples 6-12, changing the type of bismuth salt, the consumption of bismuth salt remains unchanged, still 1mol, other operations are equivalent to embodiment 1-1, obtain embodiment 6-12, process parameter and reaction result refer to Table 2.

表2Table 2

实施例Example 铋盐种类Types of Bismuth Salts 原料转化率(%)Raw material conversion rate (%) 反应选择性(%)Reaction selectivity (%) 产品收率(%)Product yield (%) 66 硫酸铋Bismuth sulfate 96.596.5 99.899.8 94.894.8 77 三氟化铋Bismuth trifluoride 97.197.1 99.899.8 95.095.0 88 三氯化铋Bismuth trichloride 97.597.5 99.899.8 95.395.3 99 三溴化铋Bismuth tribromide 97.297.2 99.899.8 95.895.8 1010 硝酸铋Bismuth nitrate 98.398.3 99.899.8 96.196.1 1111 磷酸铋Bismuth Phosphate 97.897.8 99.899.8 95.295.2 1212 硼酸铋Bismuth borate 98.698.6 99.899.8 96.396.3

实施例13~22、改变配体种类,配体的用量保持不变,仍然为3mol,其他操作等同于实施例1-1,得到实施例13~22,工艺参数及反应结果参见表3。In Examples 13-22, the types of ligands were changed, and the amount of the ligand remained unchanged at 3 mol. Other operations were equivalent to those of Example 1-1, and Examples 13-22 were obtained.

表3table 3

实施例Example 配体种类Ligand species 原料转化率(%)Raw material conversion rate (%) 反应选择性(%)Reaction selectivity (%) 产品收率(%)Product yield (%) 1313 二乙胺Diethylamine 98.598.5 99.899.8 95.895.8 1414 乙二胺Ethylenediamine 98.198.1 99.899.8 95.495.4 1515 二乙醇胺Diethanolamine 98.898.8 99.899.8 96.396.3 1616 三乙醇胺Triethanolamine 99.299.2 99.899.8 96.896.8 1717 吡啶Pyridine 98.398.3 99.899.8 95.195.1 1818 2,2'-联吡啶2,2'-bipyridine 98.898.8 99.899.8 96.296.2 1919 1,10-邻二氮杂菲1,10-phenanthroline 98.698.6 99.899.8 96.196.1 2020 三苯基膦Triphenylphosphine 98.998.9 99.899.8 96.596.5 21twenty one 三环己基膦tricyclohexylphosphine 98.298.2 99.899.8 95.795.7 22twenty two 1,1'-联二萘酚1,1'-Binaphthol 98.598.5 99.899.8 96.096.0

实施例23~50、改变酰胺种类,酰胺的用量保持不变,仍然为15mol,其他操作等同于实施例1-1,得到实施例23~50,工艺参数及反应结果参见表4。In Examples 23-50, the types of amides were changed, and the amount of amides remained unchanged at 15 mol. Other operations were identical to those in Example 1-1, and Examples 23-50 were obtained. See Table 4 for process parameters and reaction results.

表4Table 4

Figure BDA0002634963180000051
Figure BDA0002634963180000051

Figure BDA0002634963180000061
Figure BDA0002634963180000061

Figure BDA0002634963180000071
Figure BDA0002634963180000071

实施例51~54、改变酰胺与醋酸铋的摩尔比,醋酸铋的用量保持不变,仍然为1mol,其他操作等同于实施例1-1,得到实施例51~54,工艺参数及反应结果参见表5。Embodiment 51~54, change the molar ratio of amide and bismuth acetate, the consumption of bismuth acetate remains unchanged, still is 1mol, other operations are equivalent to embodiment 1-1, obtain embodiment 51~54, process parameter and reaction result refer to table 5.

表5table 5

实施例Example 酰胺与醋酸铋的摩尔比Molar ratio of amide to bismuth acetate 原料转化率(%)Raw material conversion rate (%) 反应选择性(%)Reaction selectivity (%) 产品收率(%)Product yield (%) 5151 5:15:1 99.199.1 99.899.8 97.097.0 5252 10:110:1 99.099.0 99.899.8 96.896.8 5353 20:120:1 97.597.5 99.899.8 95.095.0 5454 25:125:1 95.595.5 99.899.8 93.193.1

实施例55~63、改变溶剂种类,体积用量保持不变;其他操作等同于实施例1-1,得到实施例55~63,工艺参数及反应结果参见表6。In Examples 55 to 63, the type of solvent was changed, and the volume and dosage remained unchanged; other operations were identical to those of Example 1-1, and Examples 55 to 63 were obtained. See Table 6 for process parameters and reaction results.

表6Table 6

实施例Example 溶剂种类Type of solvent 原料转化率(%)Raw material conversion rate (%) 反应选择性(%)Reaction selectivity (%) 产品收率(%)Product yield (%) 5555 乙醇Ethanol 98.598.5 99.899.8 95.895.8 5656 乙二醇Ethylene Glycol 98.798.7 99.899.8 96.296.2 5757 异丙醇isopropyl alcohol 98.498.4 99.899.8 95.795.7 5858 四氢呋喃tetrahydrofuran 98.598.5 99.899.8 95.995.9 5959 乙腈Acetonitrile 97.897.8 99.899.8 95.095.0 6060 环己烷Cyclohexane 95.595.5 99.899.8 92.792.7 6161 二氯甲烷Dichloromethane 97.897.8 99.899.8 95.395.3 6262 1,2-二氯乙烷1,2-Dichloroethane 96.496.4 99.899.8 93.893.8 6363 甲苯Toluene 98.298.2 99.899.8 95.095.0

实施例64~69、改变步骤2)的反应时间,其他操作同实施例1-1,得到实施例64~69,工艺参数及反应结果参见表7。In Examples 64 to 69, the reaction time of step 2) was changed, and other operations were the same as those in Example 1-1 to obtain Examples 64 to 69. The process parameters and reaction results are shown in Table 7.

表7Table 7

Figure BDA0002634963180000072
Figure BDA0002634963180000072

Figure BDA0002634963180000081
Figure BDA0002634963180000081

对比例1、反应体系中只加入醋酸铋,不加入配体;Comparative example 1, only add bismuth acetate in the reaction system, do not add ligand;

即,具体为:(1)、在反应容器中,加入1mol的醋酸铋和10L的甲醇;而后立即进行后续步骤;That is, be specifically: (1), in reaction vessel, add the bismuth acetate of 1mol and the methanol of 10L; Then immediately carry out subsequent steps;

后续步骤同实施例1-1。The subsequent steps are the same as in Example 1-1.

苯甲酰胺转化率仅为35.5%,苯甲腈收率仅为31.8%。The conversion of benzamide was only 35.5%, and the yield of benzonitrile was only 31.8%.

对比例2、取消步骤(1)的的室温下搅拌2h,Comparative example 2, cancel the stirring at room temperature of step (1) for 2h,

即,具体为:(1)、在反应容器中,加入3mol三乙胺、1mol的醋酸铋和10L的甲醇;而后立即进行后续步骤;That is, be specifically: (1), in reaction vessel, add the methanol of 3mol triethylamine, 1mol of bismuth acetate and 10L; Then immediately carry out subsequent steps;

后续步骤同实施例1-1。The subsequent steps are the same as in Example 1-1.

苯甲酰胺转化率仅为75.2%,苯甲腈收率仅为70.5%。The conversion of benzamide was only 75.2%, and the yield of benzonitrile was only 70.5%.

最后,还需要注意的是,以上列举的仅是本发明的若干个具体实施例。显然,本发明不限于以上实施例,还可以有许多变形。本领域的普通技术人员能从本发明公开的内容直接导出或联想到的所有变形,均应认为是本发明的保护范围。Finally, it should also be noted that the above enumeration is only a few specific embodiments of the present invention. Obviously, the present invention is not limited to the above embodiments, and many modifications are possible. All deformations that those of ordinary skill in the art can directly derive or associate from the disclosure of the present invention shall be considered as the protection scope of the present invention.

Claims (6)

1.铋配合物催化酰胺脱水制备腈的方法,其特征在于包括以下步骤:1. the method for preparing nitrile by bismuth complex catalyzed amide dehydration is characterized in that comprising the following steps: 1)、铋盐与配体在溶剂中于室温下反应(2±0.5)小时,得含有铋配合物的溶液;1), bismuth salt and ligand react at room temperature in solvent for (2 ± 0.5) hours to obtain a solution containing bismuth complex; 所述铋盐:配体=1:1~5的摩尔比;The bismuth salt: ligand=1:1~5 molar ratio; 2)、向步骤1)所得的含有铋配合物的溶液中加入酰胺,于室温、常压下反应6~18h,从而实现酰胺脱水生成腈,所述铋配合物作为催化剂;2), adding an amide to the solution containing the bismuth complex obtained in step 1), and reacting at room temperature and normal pressure for 6-18 hours, thereby realizing dehydration of the amide to generate nitrile, and the bismuth complex is used as a catalyst; 所述酰胺:步骤1)中的铋盐=5~25:1的摩尔比;The amide: the bismuth salt in step 1)=5~25:1 mol ratio; 3)、步骤2)所得的反应液经分离,得到酰胺所对应的腈的粗品。3) The reaction solution obtained in step 2) is separated to obtain the crude product of the nitrile corresponding to the amide. 2.根据权利要求1所述的铋配合物催化酰胺脱水制备腈的方法,其特征在于:2. the method for preparing nitrile by bismuth complex catalytic amide dehydration according to claim 1, is characterized in that: 步骤3)分离过程中所得的溶剂、催化剂和未反应的酰胺进行循环反应。Step 3) The solvent, catalyst and unreacted amide obtained in the separation process are subjected to cyclic reaction. 3.根据权利要求1或2所述的铋配合物催化酰胺脱水制备腈的方法,其特征在于所述步骤1)中:3. bismuth complex catalyzed amide dehydration according to claim 1 and 2 prepares the method for nitrile, it is characterized in that in described step 1): 铋盐为醋酸铋、三氟化铋、三氯化铋、三溴化铋、硝酸铋、硫酸铋、磷酸铋、硼酸铋中的至少一种;The bismuth salt is at least one of bismuth acetate, bismuth trifluoride, bismuth trichloride, bismuth tribromide, bismuth nitrate, bismuth sulfate, bismuth phosphate, and bismuth borate; 配体为二乙胺、三乙胺、乙二胺、乙醇胺、二乙醇胺、三乙醇胺、吡啶、2,2'-联吡啶、1,10-邻二氮杂菲、三苯基膦、三环己基膦、1,1'-联二萘酚中的至少一种。Ligands are diethylamine, triethylamine, ethylenediamine, ethanolamine, diethanolamine, triethanolamine, pyridine, 2,2'-bipyridine, 1,10-o-phenanthroline, triphenylphosphine, tricyclic At least one of hexylphosphine and 1,1'-binaphthol. 4.根据权利要求3所述的铋配合物催化酰胺脱水制备腈的方法,其特征在于:4. the method for preparing nitrile by bismuth complex catalytic amide dehydration according to claim 3, is characterized in that: 所述步骤2)中的酰胺为R-(CONH2)X,R为C6-20芳基、C1-20直链或支链烷基、C1-20直链或支链烯基、C1-20直链或支链炔基、C3-20环烷基、C3-20烯基、C3-20氮杂环基、C3-20氧杂环基、C3-20硫杂环基;X为1或2;The amide in the step 2) is R-(CONH 2 ) X , and R is C 6-20 aryl, C 1-20 straight or branched alkyl, C 1-20 straight or branched alkenyl, C 1-20 straight or branched chain alkynyl, C 3-20 cycloalkyl, C 3-20 alkenyl, C 3-20 azacyclyl, C 3-20 oxacyclyl , C 3-20 sulfur Heterocyclyl; X is 1 or 2; 基团R中含有至少一个的卤素、羟基、羧基、羰基、氨基、硝基、巯基。The group R contains at least one halogen, hydroxyl, carboxyl, carbonyl, amino, nitro and mercapto. 5.根据权利要求1~4任一所述的铋配合物催化酰胺脱水制备腈的方法,其特征在于:5. the method for preparing nitrile by bismuth complex catalyzed amide dehydration according to any one of claims 1 to 4, is characterized in that: 所述步骤1)中的溶剂为甲醇、乙醇、乙二醇、异丙醇、四氢呋喃、乙腈、乙酸乙酯、环己烷、二氯甲烷、1,2-二氯乙烷、甲苯中的至少一种。The solvent in the step 1) is at least one of methanol, ethanol, ethylene glycol, isopropanol, tetrahydrofuran, acetonitrile, ethyl acetate, cyclohexane, dichloromethane, 1,2-dichloroethane and toluene. A sort of. 6.根据权利要求1~5所述的铋配合物催化酰胺脱水制备腈的方法,其特征在于所述步骤3)中的分离为:步骤2)所得的反应液减压精馏,馏出液分别为溶剂、水、腈的粗品;釜底液中含有催化剂和未反应的酰胺。6. the method for preparing nitrile by bismuth complex catalytic amide dehydration according to claim 1~5, it is characterized in that the separation in described step 3) is: step 2) the reaction solution obtained by vacuum distillation, distillate They are the crude products of solvent, water and nitrile respectively; the bottom liquid contains catalyst and unreacted amide.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112961079A (en) * 2021-03-04 2021-06-15 浙江工业大学 Method for dehydrating primary amide into nitriles by cobalt catalysis

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE851330A (en) * 1976-02-19 1977-08-11 Unibra Sa PROCESS FOR PREPARING NITRILS FROM AMIDS
BE864289R (en) * 1978-02-24 1978-08-24 Unibra Sa PROCESS FOR PREPARING NITRILS FROM AMIDS
CN102267915A (en) * 2011-06-16 2011-12-07 浙江大学 Method for reducing aromatic nitriles
CN112010777A (en) * 2020-08-20 2020-12-01 浙江大学衢州研究院 Method for continuously preparing nitrile from amide in pipeline reactor
CN112028726A (en) * 2020-08-18 2020-12-04 浙江大学衢州研究院 Method for continuously preparing nitrile from amide

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE851330A (en) * 1976-02-19 1977-08-11 Unibra Sa PROCESS FOR PREPARING NITRILS FROM AMIDS
BE864289R (en) * 1978-02-24 1978-08-24 Unibra Sa PROCESS FOR PREPARING NITRILS FROM AMIDS
CN102267915A (en) * 2011-06-16 2011-12-07 浙江大学 Method for reducing aromatic nitriles
CN112028726A (en) * 2020-08-18 2020-12-04 浙江大学衢州研究院 Method for continuously preparing nitrile from amide
CN112010777A (en) * 2020-08-20 2020-12-01 浙江大学衢州研究院 Method for continuously preparing nitrile from amide in pipeline reactor

Non-Patent Citations (5)

* Cited by examiner, † Cited by third party
Title
ELUMALAI GOPI ET AL.: "Triphenylbismuth dichloride-mediated conversion of thioamides to nitriles", 《EUROPEAN JOURNAL OF ORGANIC CHEMISTRY》 *
EMMANUEL CALLENS ET AL.: "Synthesis of amides using the Ritter reaction with bismuth triflate catalysis", 《TETRAHEDRON LETTERS》 *
LAKHINATH SAIKIA ET AL.: "A rapid, convenient, solventless green approach for the synthesis of oximes using grindstone chemistry", 《ORGANIC AND MEDICINAL CHEMISTRY LETTERS》 *
MASAHARU UENO ET AL.: "Environmentally Benign Ritter Reaction Using Bismuth Salts as a Catalyst", 《EUROPEAN JOURNAL OF ORGANIC CHEMISTRY》 *
YING-SHUAN E. LEE ET AL.: "Discovery of 4-Aryl-N-arylcarbonyl-2-aminothiazoles as Hec1/Nek2 Inhibitors. Part I: Optimization of in Vitro Potencies and Pharmacokinetic Properties", 《J. MED. CHEM.》 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112961079A (en) * 2021-03-04 2021-06-15 浙江工业大学 Method for dehydrating primary amide into nitriles by cobalt catalysis

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