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CN1322710A - Prepn of triphenylamine derivative - Google Patents

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CN1322710A
CN1322710A CN 01112714 CN01112714A CN1322710A CN 1322710 A CN1322710 A CN 1322710A CN 01112714 CN01112714 CN 01112714 CN 01112714 A CN01112714 A CN 01112714A CN 1322710 A CN1322710 A CN 1322710A
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薛敏钊
黄德音
刘燕刚
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Shanghai Jiao Tong University
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Abstract

The prepn of triphenylamine derivative includes the first step of synthesizing arene iodide with diazo salt or other compound as material and the second step of condensating different aromatic amine compound and arene iodide. Potassium iodide solution produced during the reaction may be recovered for reuse and reduction of potassium iodide. In addition, mixed crown ether as phase transfer catalyst is adopted during the condensation of the second step, and this raises the activity of catalyst while reducing consumption and exhaust of the toxic catalyst.

Description

三苯胺衍生物的制备方法The preparation method of triphenylamine derivative

本发明涉及一种三苯胺衍生物的制备方法,可以高效、低消耗地制备新型的光电功能材料的重要中间体一三苯胺衍生物。The invention relates to a preparation method of triphenylamine derivatives, which can efficiently and low-consumption prepare triphenylamine derivatives, an important intermediate of novel photoelectric functional materials.

含三苯胺结构的化合物是制备新型的光电材料诸如静电复印、激光打印机的电荷传输材料,电致发光材料等的重要的原材料。一般采用乌尔曼(Ullmann)反应制备,随采用的合成起始原料的不同,合成的三苯胺的收率有较大的差别。合成原料之一的卤代芳烃如果采用碘代芳烃,所得的三苯胺衍生物的收率最好。同时,由于乌尔曼反应需要高温条件,一般的季铵盐类相转移催化剂不能满足要求,而使用聚乙二醇类相转移催化剂的反应收率相对较低,因此,只有冠醚类催化剂可以使用。Compounds containing triphenylamine structure are important raw materials for the preparation of new optoelectronic materials such as electrostatic copying, charge transport materials for laser printers, and electroluminescent materials. Generally adopt Ullmann (Ullmann) reaction to prepare, with the difference of synthetic starting material adopted, the yield of the synthetic triphenylamine has bigger difference. If one of the halogenated aromatic hydrocarbons of synthetic raw materials adopts iodo aromatic hydrocarbons, the yield of the obtained triphenylamine derivatives is the best. At the same time, because the Ullmann reaction requires high temperature conditions, general quaternary ammonium salt phase transfer catalysts cannot meet the requirements, and the reaction yield of polyethylene glycol phase transfer catalysts is relatively low. Therefore, only crown ether catalysts can use.

采用不同的芳胺类化合物和不同的卤代芳烃以及不同相转移催化剂制备三苯胺衍生物的方法在文献中(Gauthier S.等,Synthesis 4:383-385(1987)和Sutaka K.等J.Org.Chem.54:1476-79(1989))已有涉及。综合文献中述及的制备方法,以采用碘代芳烃为反应原料之一和18-冠-6醚为相转移催化剂的效果为最好。但不足之处在于:1.碘代芳烃相对较难制备,原料不容易获得,常常需要在制备三苯胺衍生物之前先期制备。而且制备三苯胺衍生物的反应中产生的碘化钾会作为废物丢弃。整个工艺过程的综合消耗较高。2.用18-冠-6醚作为相转移催化剂虽然稳定性和催化效果都较好,但价格较高,使综合消耗大,更重要的是它的毒性较大,反应之后的废水排放会造成环境污染。其它的制备方法如菊池千幸等在中国专利(公开号1130174)中述及的采用环己酮衍生物为反应物的方法存在着原料不容易得到等不足。The method for preparing triphenylamine derivatives using different arylamine compounds and different halogenated aromatics and different phase transfer catalysts is in the literature (Gauthier S. et al., Synthesis 4:383-385 (1987) and Sutaka K. et al. J. Org.Chem.54:1476-79 (1989)) has been involved. Based on the preparation methods mentioned in the literature, the effect of using iodoarene as one of the reaction raw materials and 18-crown-6 ether as a phase transfer catalyst is the best. But the disadvantages are: 1. Iodoarenes are relatively difficult to prepare, and the raw materials are not easy to obtain, and often need to be prepared in advance before the preparation of triphenylamine derivatives. Moreover, the potassium iodide produced in the reaction to prepare triphenylamine derivatives is discarded as waste. The comprehensive consumption of the whole process is relatively high. 2. Although 18-crown-6 ether is used as a phase transfer catalyst, although the stability and catalytic effect are good, the price is relatively high, so that the overall consumption is large, and more importantly, its toxicity is relatively large, and the discharge of waste water after the reaction will cause environmental pollution . Other preparation methods, such as the method of adopting cyclohexanone derivatives as reactants described in Chinese patent (publication number 1130174) by Chiyuki Kikuchi et al., have the disadvantages that the raw materials are not easy to obtain.

本发明的目的是开发一种合成三苯胺衍生物的新工艺,从重氮盐类化合物出发,采用通用的方法,第一步用碘化钾溶液和重氮盐反应制备碘代的芳烃,第二步选用不同的芳胺类化合物和碘代芳烃进行缩合反应,制备三苯胺衍生物,缩合反应产生的碘化钾溶液可以回收循环利用,使整个工艺过程中的碘化钾消耗较少。在第二步缩合反应中使用混合的冠醚类相转移催化剂,既使合成三苯胺衍生物的反应收率较高,又使毒性较大的18-冠-6醚的排放较少。实现高效、低消耗地制备三苯胺衍生物的目的。The purpose of this invention is to develop a new process for the synthesis of triphenylamine derivatives. Starting from diazonium salt compounds, a general method is adopted. The first step uses potassium iodide solution and diazonium salt to react to prepare iodo aromatics, and the second step selects Different arylamine compounds and iodoaromatics undergo condensation reactions to prepare triphenylamine derivatives, and the potassium iodide solution produced by the condensation reaction can be recovered and recycled, so that the consumption of potassium iodide in the whole process is less. Using a mixed crown ether phase transfer catalyst in the second-step condensation reaction not only makes the reaction yield of the synthesis of triphenylamine derivatives higher, but also reduces the emission of the more toxic 18-crown-6 ether. The purpose of preparing triphenylamine derivatives with high efficiency and low consumption is realized.

本发明的制备方法包括:第一步采用通用的制备重氮盐的方法来制备不同结构的重氮盐类化合物,用碘化钾和重氮盐反应制备碘代芳烃,第二步采用复合冠醚催化剂制备三苯胺衍生物以及碘化钾的循环再利用等步骤。The preparation method of the present invention comprises: the first step adopts the general method for preparing diazonium salts to prepare diazonium salt compounds of different structures, reacts potassium iodide and diazonium salts to prepare iodoaromatic hydrocarbons, and the second step uses a compound crown ether catalyst Preparation of triphenylamine derivatives and recycling of potassium iodide and other steps.

重氮盐的制备采用通用的方法,根据制备的三苯胺衍生物结构的不同,选用不同的芳胺作为起始原料,合成反应方程式如下: The preparation of diazonium salt adopts general method, and according to the difference of the triphenylamine derivative structure of preparation, selects different aromatic amines as starting raw material, and synthetic reaction equation is as follows:

这里的R1可以是取代在苯环的对位、间位的甲基、甲氧基等基团;酸H+可以是盐酸或硫酸。具体的反应条件采用通用的方法控制原料的配比和反应温度。Here R1 can be substituted in the para-position of the benzene ring, meta-methyl, methoxy and other groups; the acid H + can be hydrochloric acid or sulfuric acid. Concrete reaction conditions adopt general method to control the proportioning of raw materials and reaction temperature.

碘代芳烃的制备是采用通用的方法,用碘化钾的饱和溶液与上述步骤中制备的重氮盐反应,根据制备的碘代芳烃的结构的不同采用不同的方法纯化反应产物,可以采用水汽蒸馏、减压蒸馏、结晶等方法。这里所用的碘化钾溶液在第一次制备时要用市售的固体配制,在以后的制备过程中可以采用缩合反应之后回收的含冠醚以及铜离子的溶液,用回收的碘化钾溶液不影响碘代反应的收率。The preparation of iodoarenes is to adopt general method, reacts with the diazonium salt prepared in the above-mentioned steps with the saturated solution of potassium iodide, adopts different methods to purify reaction product according to the difference of the structure of the iodoarenes of preparation, can adopt steam distillation, Vacuum distillation, crystallization and other methods. The potassium iodide solution used here should be prepared with commercially available solids when preparing for the first time. In the subsequent preparation process, the solution containing crown ether and copper ions recovered after the condensation reaction can be used. The potassium iodide solution of recovery does not affect the iodine The yield of the reaction.

在制备了碘代芳烃之后,选用不同的芳胺和碘代芳烃反应可以制备不同结构的三苯胺衍生物,制备三苯胺衍生物的反应式如下:

Figure A0111271400042
After preparing iodoarenes, different arylamines and iodoarenes can be used to react to prepare triphenylamine derivatives of different structures. The reaction formula for preparing triphenylamine derivatives is as follows:
Figure A0111271400042

这里的R1同上,R2可以是氢、苯环的对位或间位取代的甲基、甲氧基等,R3可以是氢、苯基、对甲苯基等。Here R1 is the same as above, R2 can be hydrogen, para- or meta-substituted methyl, methoxy, etc. of the benzene ring, and R3 can be hydrogen, phenyl, p-tolyl, etc.

由于反应需要较高的温度(200℃左右),因此,反应所需的溶剂的选择性有限,只能选用高温惰性的溶剂,如硝基苯、邻二氯苯等。加温到溶剂的沸点温度并保持回流可以满足反应所需的高温条件,而且这两种溶剂可以在反应结束后用水蒸气蒸馏的方法除去。溶剂经提纯、干燥后可以循环使用。同样的原因,本反应的相转移催化剂选用高温稳定的冠醚类催化剂。除此之外,反应体系中还需要加入活化铜粉催化剂和无水碳酸钾作为碱性试剂。Because the reaction requires a higher temperature (about 200°C), the selectivity of the solvent required for the reaction is limited, and only high-temperature inert solvents, such as nitrobenzene and o-dichlorobenzene, can be used. Heating to the boiling point of the solvent and maintaining reflux can meet the high temperature conditions required for the reaction, and these two solvents can be removed by steam distillation after the reaction. The solvent can be recycled after being purified and dried. For the same reason, the phase transfer catalyst of this reaction is a high temperature stable crown ether catalyst. In addition, the reaction system also needs to add activated copper powder catalyst and anhydrous potassium carbonate as alkaline reagents.

反应所采用的相转移催化剂为复合的冠醚类催化剂。由于18-冠-6醚在水中的溶解度较大,价格较高,毒性较大,因而,反应的消耗较大,排放对水体的污染较为严重。本发明选用二苯并18-冠-6和18-冠-6复配制成复合催化剂,减少了18-冠-6的用量,同时,由于二苯并18-冠-6在苯类溶剂中的溶解性较18-冠-6好,而水中的溶解性较差,不但有效地提高了复合催化剂的催化活性,而且降低了消耗和排放物中18-冠-6的含量。具体复配的成分为二苯并18-冠-6和18-冠-6按摩尔比为3∶1的比例配制。催化剂在催化反应中的使用量为1-5%(wt)。二苯并18-冠-6和18-冠-6的结构分别为:

Figure A0111271400051
The phase transfer catalyst used in the reaction is a composite crown ether catalyst. Because 18-crown-6 ether has high solubility in water, high price and high toxicity, the consumption of reaction is large, and the pollution of water body is relatively serious when discharged. The present invention selects dibenzo-18-crown-6 and 18-crown-6 to be compounded into composite catalyst, reduces the consumption of 18-crown-6, simultaneously, because dibenzo-18-crown-6 in benzene solvent The solubility is better than that of 18-crown-6, but the solubility in water is poor, which not only effectively improves the catalytic activity of the composite catalyst, but also reduces the content of 18-crown-6 in consumption and emissions. The specific compounded components are prepared by dibenzo-18-crown-6 and 18-crown-6 in a molar ratio of 3:1. The usage amount of the catalyst in the catalytic reaction is 1-5% (wt). The structures of dibenzo 18-crown-6 and 18-crown-6 are respectively:
Figure A0111271400051

制备三苯胺反应结束后,回收的水溶液经原子吸收光谱分析证明碘离子的回收率一般在80%左右。回收的溶液经放置沉降4天后过滤,铜离子在溶液中的含量经分析为30-60ppm,铜离子及其它的杂质的存在不足以影响碘化反应。回收的KI溶液可以用于制备碘代芳烃。After the reaction of preparing triphenylamine is finished, the recovered aqueous solution is analyzed by atomic absorption spectrum to prove that the recovery rate of iodide ion is generally about 80%. The recovered solution was left to settle for 4 days and then filtered. The content of copper ions in the solution was analyzed to be 30-60 ppm. The presence of copper ions and other impurities was not enough to affect the iodination reaction. The recovered KI solution can be used to prepare iodoarenes.

采用上述的技术路线,不但使制备三苯胺衍生物的收率较高(基本在75%以上)而且使整个工艺过程中的碘化钾消耗较少、有毒的冠醚类催化剂的排放较少。By adopting the above-mentioned technical route, not only the yield of preparing triphenylamine derivatives is higher (substantially more than 75%), but also the consumption of potassium iodide in the whole process is less, and the emission of toxic crown ether catalysts is less.

下面的实施例是对本发明的进一步说明,而不是限定本发明的范围。The following examples are to further illustrate the present invention, but not to limit the scope of the present invention.

实施例1:Example 1:

对甲苯胺54克放于1000ml的圆底烧瓶中,搅拌下加入20%的稀盐酸100ml,加热搅拌至固体全部溶解后,将此溶液冷至5℃以下。保持温度5℃以下加入事先配好的亚硝酸钠溶液,搅拌至溶液用KI淀粉试纸检验变蓝,停止加入亚硝酸钠溶液,继续搅拌10分钟,制得的透明溶液为重氮盐的水溶液。Put 54 grams of p-toluidine in a 1000ml round bottom flask, add 100ml of 20% dilute hydrochloric acid under stirring, heat and stir until all the solids are dissolved, then cool the solution to below 5°C. Keep the temperature below 5°C and add the pre-prepared sodium nitrite solution, stir until the solution turns blue with KI starch test paper, stop adding the sodium nitrite solution, continue stirring for 10 minutes, the obtained transparent solution is an aqueous solution of diazonium salt.

将75克KI溶解于尽量少的水中制成KI溶液,保持0-5℃的温度下,将KI溶液加入到上述制备的重氮盐溶液中,并不断搅拌。缓缓升温至60-70℃,保温3-4小时后,将溶液冷却至室温,分离出水后,得到棕黑色的粗产品。用NaOH溶液洗涤得到的固体至黄色,进一步的提纯需要将固体转移至蒸馏烧瓶中,进行水蒸气蒸馏。最后得到的纯品为淡黄色的蜡状固体,产率86%。Dissolve 75 grams of KI in as little water as possible to make a KI solution, keep the temperature of 0-5°C, add the KI solution to the diazonium salt solution prepared above, and keep stirring. Slowly raise the temperature to 60-70°C, keep the temperature for 3-4 hours, then cool the solution to room temperature, and separate the water to obtain a brown-black crude product. The resulting solid was washed with NaOH solution until yellow, further purification required transferring the solid to a distillation flask for steam distillation. The finally obtained pure product is light yellow waxy solid with a yield of 86%.

在一个装有机械搅拌装置、分水装置和气体导入装置的500ml三口烧瓶中,分别加入85克二苯胺,120克对碘甲苯,70克碳酸钾,0.5克活化铜粉,0.6克复合相转移催化剂和240ml的硝基苯。从气体导入口通氮气至液面下,保持氮气的流速在每小时0.01-0.03立方米。开动机械搅拌,缓慢升温至回流温度(约200℃),回流10-16小时后停止通入氮气。搅拌下将反应液冷却至室温,将反应烧瓶改为水蒸气蒸馏烧瓶进行水蒸气蒸馏,蒸出的溶剂硝基苯回收利用。蒸馏完毕分出蒸馏烧瓶中的水相和油相,含有大量KI的水相转移到烧杯中放置沉降。油相用甲苯溶解,过滤除去不溶解的铜粉等固体杂质。甲苯溶液经干燥后进行蒸馏,待甲苯蒸馏完毕,改为减压蒸馏装置,在5-10毫米汞柱的压力下蒸馏,收集180-200℃的馏分。得到的产品4-甲基三苯胺为淡黄色的固体,收率76%。In a 500ml three-neck flask equipped with a mechanical stirring device, a water separator and a gas introduction device, add 85 grams of diphenylamine, 120 grams of p-iodotoluene, 70 grams of potassium carbonate, 0.5 grams of activated copper powder, and 0.6 grams of composite phase transfer Catalyst and 240ml of nitrobenzene. Pass nitrogen gas from the gas inlet to the liquid surface, and keep the nitrogen flow rate at 0.01-0.03 cubic meters per hour. Start the mechanical stirring, slowly raise the temperature to the reflux temperature (about 200° C.), and stop feeding nitrogen gas after reflux for 10-16 hours. Cool the reaction liquid to room temperature under stirring, change the reaction flask into a steam distillation flask for steam distillation, and recycle the evaporated solvent nitrobenzene. After the distillation, the water phase and the oil phase in the distillation flask were separated, and the water phase containing a large amount of KI was transferred to a beaker for sedimentation. The oil phase is dissolved with toluene, and solid impurities such as insoluble copper powder are removed by filtration. Distill the toluene solution after drying. After the toluene distillation is complete, change to a vacuum distillation device, distill at a pressure of 5-10 mm Hg, and collect fractions at 180-200 ° C. The obtained product 4-methyltriphenylamine is a pale yellow solid with a yield of 76%.

上述含有KI的水溶液放置沉降4天后,过滤除去容器底部的沉淀,定容后进行原子吸收光谱测试。经测试溶液中碘的含量,计算得到回收的KI为65克;铜离子的含量为43ppm。该KI溶液经补充溶解少量的KI固体后,可用于制备碘代芳烃的反应。After the above-mentioned aqueous solution containing KI was left to settle for 4 days, the precipitate at the bottom of the container was removed by filtration, and the atomic absorption spectrum test was performed after constant volume. After testing the content of iodine in the solution, the calculated KI recovered was 65 grams; the content of copper ions was 43 ppm. The KI solution can be used for the reaction of preparing iodoarene after supplementing and dissolving a small amount of KI solid.

实施例2Example 2

用对甲苯胺制备重氮盐的各原料配比及具体的工艺过程与上述实施例1相同,碘代反应中所用的KI溶液是由上述实施例中制备三苯胺反应回收的KI溶液150ml(含KI65克)补加10克KI固体制成的。碘代反应的工艺及产物的提纯方法同实施例1,干燥后的对碘甲苯收率为84%。Prepare each raw material ratio of diazonium salt with p-toluidine and concrete technological process are identical with above-mentioned embodiment 1, the KI solution used in the iodination reaction is to prepare the KI solution 150ml that triphenylamine reaction reclaims in above-mentioned embodiment (containing KI65g) made by adding 10g of KI solid. The technique of iodination reaction and the purification method of product are the same as in Example 1, and the p-iodotoluene yield after drying is 84%.

在一个装有机械搅拌装置、分水装置和气体导入装置的1000ml三口烧瓶中,分别加入47克苯胺,220克对碘甲苯,140克碳酸钾,0.5克活化铜粉,0.6克复合相转移催化剂和400ml的邻二氯苯。从气体导入口通氮气至液面下,保持氮气的流速在每小时0.01-0.03立方米。开动机械搅拌,在保证反应液不至溢出的情况下,使搅拌的速度尽可能大。缓慢升温至回流温度(约180℃),回流10-16小时后停止通入氮气。搅拌下将反应液冷却至室温,将反应烧瓶改为水蒸气蒸馏烧瓶进行水蒸气蒸馏,蒸出的邻二氯苯溶剂回收利用。蒸馏完毕分出蒸馏烧瓶中的水相和油相,含有大量KI的水相转移到烧杯中放置沉降。油相用甲苯溶解,过滤除去不溶解的铜粉等固体杂质。甲苯溶液经干燥后进行蒸馏,待甲苯蒸馏完毕,改为减压蒸馏装置,在5-10毫米汞柱的压力下蒸馏,收集200-220℃的馏分。得到的产品4,4’-二甲基三苯胺为黄色的固体,收率70%。In a 1000ml three-necked flask equipped with a mechanical stirring device, a water separator and a gas introduction device, add 47 grams of aniline, 220 grams of p-iodotoluene, 140 grams of potassium carbonate, 0.5 grams of activated copper powder, and 0.6 grams of composite phase transfer catalyst and 400ml of o-dichlorobenzene. Pass nitrogen gas from the gas inlet to the liquid surface, and keep the nitrogen flow rate at 0.01-0.03 cubic meters per hour. Start the mechanical stirring, and make the stirring speed as high as possible while ensuring that the reaction solution does not overflow. Slowly raise the temperature to reflux temperature (about 180° C.), and stop feeding nitrogen gas after reflux for 10-16 hours. Cool the reaction liquid to room temperature under stirring, change the reaction flask into a steam distillation flask for steam distillation, and recycle the o-dichlorobenzene solvent evaporated. After the distillation, the water phase and the oil phase in the distillation flask were separated, and the water phase containing a large amount of KI was transferred to a beaker for sedimentation. The oil phase is dissolved with toluene, and solid impurities such as insoluble copper powder are removed by filtration. Distill the toluene solution after drying. After the toluene distillation is complete, change to a vacuum distillation device, distill at a pressure of 5-10 mm Hg, and collect fractions at 200-220°C. The obtained product 4,4'-dimethyltriphenylamine is a yellow solid with a yield of 70%.

含有KI的水溶液放置沉降4天后,过滤除去容器底部的沉淀,定容后进行原子吸收光谱测试。经测试溶液中碘的含量,计算得到回收的KI为128克;铜离子的含量为51ppm。该KI溶液经补充溶解少量的KI固体后,同样可用于制备碘代芳烃的反应。After the aqueous solution containing KI was left to settle for 4 days, the precipitate at the bottom of the container was removed by filtration, and atomic absorption spectrometry was performed after constant volume. After testing the content of iodine in the solution, the calculated KI recovered was 128 grams; the content of copper ions was 51 ppm. The KI solution can also be used for the reaction of preparing iodoarenes after supplementing and dissolving a small amount of KI solid.

实施例3Example 3

61克对氨基苯甲醚放于1000ml的圆底烧瓶中,搅拌下加入20%的稀盐酸130ml,加热搅拌至固体全部溶解后,将此溶液冷至0℃左右。保持温度0℃左右加入事先配好的亚硝酸钠溶液,搅拌至溶液用KI淀粉试纸检验变蓝,停止加入亚硝酸钠溶液,继续搅拌10分钟,制得的透明溶液为重氮盐的水溶液。Put 61 grams of p-aminoanisole in a 1000ml round bottom flask, add 130ml of 20% dilute hydrochloric acid under stirring, heat and stir until all the solids are dissolved, then cool the solution to about 0°C. Keep the temperature around 0°C and add the pre-prepared sodium nitrite solution, stir until the solution turns blue with KI starch test paper, stop adding the sodium nitrite solution, and continue stirring for 10 minutes, the obtained transparent solution is an aqueous solution of diazonium salt.

制备对碘苯甲醚可以采用实施例1的工艺条件用新配制的KI溶液,也可以采用实施例2中制备对碘甲苯的方法采用回收的KI溶液,制备的原料配比和反应条件控制同实施例1。两种方法制备的对碘苯甲醚的物理性质及反应收率没有差别。Prepare p-iodoanisole and can adopt the process condition of embodiment 1 to use the newly prepared KI solution, also can adopt the KI solution that the method for preparing p-iodotoluene in embodiment 2 adopts reclaiming, the raw material proportioning of preparation and reaction condition control are the same Example 1. There is no difference in the physical properties and reaction yields of p-iodoanisole prepared by the two methods.

在一个装有机械搅拌装置、分水装置和气体导入装置的500ml三口烧瓶中,分别加入85克二苯胺,70克对碘甲苯,80克碳酸钾,0.5克活化铜粉,0.6克复合相转移催化剂和250ml的硝基苯。从气体导入口通氮气至液面下,保持氮气的流速在每小时0.01-0.03立方米。开动机械搅拌,缓慢升温至回流温度(约200℃),回流10小时后停止通入氮气。搅拌下将反应液冷却至室温,将反应烧瓶改为水蒸气蒸馏烧瓶进行水蒸气蒸馏,蒸出的溶剂硝基苯回收利用。蒸馏完毕分出蒸馏烧瓶中的水相和油相,含有大量KI的水相转移到烧杯中放置沉降。油相用甲苯溶解,过滤除去不溶解的铜粉等固体杂质。甲苯溶液经干燥后进行蒸馏,待甲苯蒸馏完毕,产品用95%的乙醇重结晶二次,得到的纯品4-甲氧基三苯胺为淡黄色的固体,收率68%。In a 500ml three-neck flask equipped with a mechanical stirring device, a water separator and a gas introduction device, add 85 grams of diphenylamine, 70 grams of p-iodotoluene, 80 grams of potassium carbonate, 0.5 grams of activated copper powder, and 0.6 grams of composite phase transfer Catalyst and 250ml of nitrobenzene. Pass nitrogen gas from the gas inlet to the liquid surface, and keep the nitrogen flow rate at 0.01-0.03 cubic meters per hour. Start the mechanical stirring, slowly raise the temperature to the reflux temperature (about 200° C.), and stop feeding nitrogen after reflux for 10 hours. Cool the reaction liquid to room temperature under stirring, change the reaction flask into a steam distillation flask for steam distillation, and recycle the evaporated solvent nitrobenzene. After the distillation, the water phase and the oil phase in the distillation flask were separated, and the water phase containing a large amount of KI was transferred to a beaker for sedimentation. The oil phase is dissolved with toluene, and solid impurities such as insoluble copper powder are removed by filtration. The toluene solution was dried and then distilled. After the toluene was distilled, the product was recrystallized twice with 95% ethanol to obtain pure 4-methoxytriphenylamine as a light yellow solid with a yield of 68%.

含KI的水溶液的处理方法同实施例1,经原子吸收光谱检测得KI的含量为63克,铜离子的含量为48ppm。该KI溶液同样可用于碘代芳烃的制备。The treatment method of the aqueous solution containing KI is the same as in Example 1, and the content of KI detected by atomic absorption spectroscopy is 63 grams, and the content of copper ions is 48 ppm. This KI solution can also be used for the preparation of iodoarenes.

Claims (3)

1.一种三苯胺衍生物的制备方法,其特征在于第一步采用重氮盐类化合物为原料合成碘代芳烃,第二步是用不同芳胺化合物和碘代芳烃进行缩合反应。1. A method for preparing triphenylamine derivatives is characterized in that in the first step, diazonium salt compounds are used as raw materials to synthesize iodoaromatics, and in the second step, condensation reactions are carried out with different aromatic amine compounds and iodoaromatics. 2.根据权利要求1所述的三苯胺衍生物的制备方法,其特征在第二步缩合反应中产生的碘化钾溶液可以回收循环使用。2. The preparation method of triphenylamine derivative according to claim 1 is characterized in that the potassium iodide solution produced in the second step condensation reaction can reclaim and recycle. 3.根据权利要求1所述的三苯胺衍生物的制备方法,其特征在第二步反应中使用二苯并18-冠-6和18-冠-6的复合相转移催化剂,其中二苯并18-冠-6和18-冠-6的摩尔比为3∶1,复合催化剂的使用量为1-5%(wt)。3. The preparation method of triphenylamine derivative according to claim 1 is characterized in that in the second step reaction, the composite phase transfer catalyst of dibenzo-18-crown-6 and 18-crown-6 is used, wherein dibenzo-18- The molar ratio of crown-6 and 18-crown-6 is 3:1, and the usage amount of the composite catalyst is 1-5% (wt).
CN 01112714 2001-04-26 2001-04-26 Prepn of triphenylamine derivative Pending CN1322710A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100355710C (en) * 2005-12-15 2007-12-19 上海交通大学 Method for preparing aryl iodo substance
CN102643203A (en) * 2005-01-05 2012-08-22 出光兴产株式会社 Aromatic amine derivative and organic electroluminescent element using same
CN105793233A (en) * 2013-10-04 2016-07-20 日产化学工业株式会社 Aniline derivatives and uses thereof
CN107428676A (en) * 2015-02-24 2017-12-01 日产化学工业株式会社 Anil and its utilization

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102643203A (en) * 2005-01-05 2012-08-22 出光兴产株式会社 Aromatic amine derivative and organic electroluminescent element using same
CN100355710C (en) * 2005-12-15 2007-12-19 上海交通大学 Method for preparing aryl iodo substance
CN105793233A (en) * 2013-10-04 2016-07-20 日产化学工业株式会社 Aniline derivatives and uses thereof
CN105793233B (en) * 2013-10-04 2019-03-08 日产化学工业株式会社 Aniline derivatives and their utilization
CN107428676A (en) * 2015-02-24 2017-12-01 日产化学工业株式会社 Anil and its utilization

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