CN105348107A - Preparation method of p-nitrobenzaldehyde - Google Patents
Preparation method of p-nitrobenzaldehyde Download PDFInfo
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Abstract
本发明公开了一种对硝基苯甲醛的制备方法。以对硝基甲苯为原料,以偶氮双烷基腈催化溴素溴化对硝基甲苯生成对硝基溴苄和溴化氢,碳酸盐水溶液催化对硝基溴苄水解为对硝基苯甲醇,氢氧化钠催化双氧水氧化对硝基苯甲醇生成目标产物对硝基苯甲醛。本发明应用偶氮双烷基腈固体催化剂替代过氧化碳酸酯液相催化剂,催化溴化反应,提高工业制备反应操作安全性;使用卤代芳烃为溶剂介质,避免了卤代烷烃溶剂介质的使用,避免了低沸点挥发性有机溶剂的污染;应用双氧水氧化方法,提高了工业制备反应的清洁性,降低了环境污染。本发明提高了产品得率,产率较目前工业传统方法提高约3%,总收率达到76%,产品纯度99%以上。
The invention discloses a method for preparing p-nitrobenzaldehyde. With p-nitrotoluene as a raw material, azobisalkylnitrile is used to catalyze bromine to bromine p-nitrotoluene to generate p-nitrobenzyl bromide and hydrogen bromide, carbonate aqueous solution is used to catalyze the hydrolysis of p-nitrobenzyl bromide to p-nitrobenzyl alcohol, and sodium hydroxide is used to catalyze hydrogen peroxide to oxidize p-nitrobenzyl alcohol to generate the target product p-nitrobenzaldehyde. The invention uses azobisalkylnitrile solid catalyst to replace peroxycarbonate liquid phase catalyst to catalyze bromination reaction, thereby improving the safety of industrial preparation reaction operation; using halogenated aromatic hydrocarbons as solvent medium avoids the use of halogenated alkane solvent medium and avoids the pollution of low-boiling volatile organic solvents; using hydrogen peroxide oxidation method improves the cleanliness of industrial preparation reaction and reduces environmental pollution. The invention improves the product yield, and the yield is about 3% higher than that of the current traditional industrial method, the total yield reaches 76%, and the product purity is above 99%.
Description
技术领域technical field
本发明涉及一种已知化合物的制备方法,确切地说是一种对硝基苯甲醛的工业清洁制备方法。The present invention relates to a kind of preparation method of known compound, is exactly a kind of industrial clean preparation method of p-nitrobenzaldehyde.
背景技术Background technique
对硝基苯甲醛为一种淡黄色结晶性粉末,熔点105-107℃,微溶于水,溶于醇、芳烃、卤代烃、羧酸酯等有机溶剂,具有升华、光敏感、随水蒸汽挥发特性。分子式为C7H5NO3,相对分子质量151.1。其结构式为:p-Nitrobenzaldehyde is a light yellow crystalline powder with a melting point of 105-107°C. It is slightly soluble in water and soluble in organic solvents such as alcohols, aromatics, halogenated hydrocarbons, and carboxylates. Vapor volatility properties. The molecular formula is C 7 H 5 NO 3 , and the relative molecular mass is 151.1. Its structural formula is:
对硝基苯甲醛用作合成医药、染料、农药等精细有机功能材料的重要中间体,用途非常广泛,能够通过发生多种化学反应,如氧化、还原、加成、缩合等方法衍生出许多重要的功能化学品。在用作合成农药、医药、染料、感光材料和液晶材料等的重要中间体领域,如制备对硝基苯-2-丁烯酮、对氨基苯甲醛、对乙酰氨基苯甲醛、甲氧苄胺嘧啶、氨苯硫脲、对硫脲、乙酰氨苯烟腙、氯霉素等。另外,对硝基苯甲醛的下游产品也有很多新用途,如具有高倍频效应的有机非线性光学材料对硝基苯甲醛苯腙等。p-Nitrobenzaldehyde is used as an important intermediate in the synthesis of fine organic functional materials such as medicines, dyes, and pesticides. It has a wide range of uses and can derive many important functional chemicals. In the field of important intermediates used in the synthesis of pesticides, medicines, dyes, photosensitive materials and liquid crystal materials, such as the preparation of p-nitrobenzene-2-butenone, p-aminobenzaldehyde, p-acetamidobenzaldehyde, and trimethoprim Pyrimidine, thiocarbazone, p-thiourea, acetaminophen, chloramphenicol, etc. In addition, the downstream products of p-nitrobenzaldehyde also have many new uses, such as p-nitrobenzaldehyde phenylhydrazone, an organic nonlinear optical material with high frequency doubling effect.
对硝基苯甲醛制备有多种方法。以对硝基甲苯为原料,在乙酸酐介质中,用氧化铬、重铬酸盐、或高锰酸钾为氧化剂,氧化侧链合成对硝基苯甲醛。此方法反应选择性差,形成副产物对硝基苯甲酸,产率低,而且产生大量的难处理的含重金属盐的酸性废水,环境污染严重。而以甲苯为原料,经过氯化产生苄基氯、再经硝化产生硝基苄基氯、进一步水解和氧化得到目标产物。此方法需要应用氯气,苄基氯具有催泪作用;第二步硝化反应应用硝酸与五氧化二铌固体超强酸的混合物作为硝化剂,尽管较传统的硝酸硫酸混酸体系提高对位硝化选择性,但依然形成邻硝基氯苄、间硝基氯苄、对硝基氯苄三种异构体,分离困难,同样具有强烈的催泪作用,金属氧化物难以再生利用。余远斌等以对硝基甲苯为原料,采用金属卟啉类仿生催化剂,空气氧化剂,在甲醇-碱性介质中,合成了对硝基苯甲醛。但合成反应选择性差,收率很低,形成较多的副产物,压力工艺条件,成本高。There are many ways to prepare p-nitrobenzaldehyde. Using p-nitrotoluene as raw material, chromium oxide, dichromate, or potassium permanganate is used as oxidizing agent in acetic anhydride medium to oxidize the side chain to synthesize p-nitrobenzaldehyde. The reaction selectivity of this method is poor, the by-product p-nitrobenzoic acid is formed, the yield is low, and a large amount of refractory acid waste water containing heavy metal salts is produced, causing serious environmental pollution. Using toluene as raw material, chlorination produces benzyl chloride, then nitration produces nitrobenzyl chloride, further hydrolysis and oxidation to obtain the target product. This method requires the application of chlorine, and benzyl chloride has a lacrimal effect; the second step of nitration reaction uses a mixture of nitric acid and niobium pentoxide solid superacid as a nitrating agent, although the para-nitration selectivity is improved compared with the traditional nitric acid sulfuric acid mixed acid system, but Three isomers of o-nitrobenzyl chloride, m-nitrobenzyl chloride and p-nitrobenzyl chloride are still formed, which are difficult to separate, and also have a strong lachrymatory effect, and metal oxides are difficult to recycle. Yu Yuanbin and others synthesized p-nitrobenzaldehyde in methanol-alkaline medium by using p-nitrotoluene as raw material, using metalloporphyrin biomimetic catalysts, and air oxidant. However, the selectivity of the synthesis reaction is poor, the yield is very low, more by-products are formed, the process conditions are under pressure, and the cost is high.
Kaneda等发现,载有Ru(Ⅲ)的羟基磷灰石可以催化多种醇类的氧化,且催化活性和选择性都很好。刘长春等将这一方法应用于对硝基苯甲醛的合成,用RuHAP作催化剂,常压下氧气氧化对硝基苯甲醇制备对硝基苯甲醛,此方法能够明显改善对硝基苯甲醛合成的选择性和提高产品收率,但催化剂价格昂贵,难以回收再生利用。彭新华等以对硝基甲苯为原料,通过与溴素反应形成对硝基溴苄,再经碳酸钠催化水解形成对硝基苯甲醇,进一步经金属有机配合物催化氧气氧化合成对硝基苯甲醛,尽管显著改善了反应选择性,提高了产率,但溴化反应工序的有机过氧化物液体催化剂,其工业应用热稳定性差;第三步氧化反应工序所使用的金属有机配合物催化剂难以再生,而且氧气氧化是气液相反应体系,需要在一定压力条件下进行反应,因此,造成生产成本和工业操作等方便不具有明显优势。Kaneda et al. found that Ru(III)-loaded hydroxyapatite can catalyze the oxidation of various alcohols with good catalytic activity and selectivity. Liu Changchun and others applied this method to the synthesis of p-nitrobenzaldehyde, using RuHAP as a catalyst, oxygen oxidation of p-nitrobenzyl alcohol under normal pressure to prepare p-nitrobenzaldehyde, this method can significantly improve the synthesis of p-nitrobenzaldehyde Selectivity and increase product yield, but the catalyst is expensive and difficult to recycle and reuse. Peng Xinhua et al. used p-nitrotoluene as a raw material, reacted with bromine to form p-nitrobenzyl bromide, then catalyzed hydrolysis by sodium carbonate to form p-nitrobenzyl alcohol, and further synthesized p-nitrobenzene by oxygen oxidation catalyzed by metal-organic complexes. Formaldehyde, although significantly improved reaction selectivity, has improved productive rate, but the organic peroxide liquid catalyst of bromination reaction procedure, its thermal stability of industrial application is poor; The used metal organic complex catalyst of the 3rd step oxidation reaction procedure is difficult Regeneration, and oxygen oxidation is a gas-liquid phase reaction system, which needs to be reacted under certain pressure conditions. Therefore, there are no obvious advantages in terms of production cost and convenience in industrial operation.
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、选择性好、收率高,并宜于工业化低成本、安全操作制备对硝基甲苯醛的清洁方法,满足环境经济双重发展要求。The purpose of the present invention is to provide a clean method for preparing p-nitrotolualdehyde with mild reaction conditions, good selectivity and high yield, which is suitable for industrialization with low cost and safe operation, and meets the dual development requirements of environment and economy.
本发明的技术方案是:一种对硝基苯甲醛的制备方法,包括如下步骤:Technical scheme of the present invention is: a kind of preparation method of p-nitrobenzaldehyde comprises the steps:
(1)溴化反应(1) bromination reaction
于反应器中加入对硝基甲苯、溶剂卤代芳烃、催化剂偶氮双烷基腈,不断搅拌下控制温度40-50℃滴加溴素,溴素的使用剂量为理论量的0.5-0.6倍,滴完后加热回流反应至溴素颜色褪去,然后加入双氧水回流反应不少于2h,得到对硝基苄基溴反应液;Add p-nitrotoluene, solvent halogenated aromatic hydrocarbon, and catalyst azobisalkylnitrile into the reactor, and add bromine dropwise under constant stirring at a controlled temperature of 40-50°C. The dosage of bromine is 0.5-0.6 times the theoretical amount After dripping, heat and reflux to react until the color of bromine fades, then add hydrogen peroxide and reflux for no less than 2 hours to obtain a p-nitrobenzyl bromide reaction solution;
(2)水解反应(2) Hydrolysis reaction
在第一步的反应液中加入碳酸盐水溶液,加热回流水解反应,生成对硝基苯甲醇目标产物和溴化钠副产物,液液分离有机相和水相,得到对硝基苯甲醇有机相;Add carbonate aqueous solution to the reaction liquid of the first step, heat and reflux hydrolysis reaction, generate p-nitrobenzyl alcohol target product and sodium bromide by-product, liquid-liquid separation organic phase and aqueous phase, obtain p-nitrobenzyl alcohol organic Mutually;
(3)氧化反应(3) oxidation reaction
于对硝基苯甲醇有机相中,加入氢氧化钠,不断搅拌下于温度25-35℃滴加双氧水,加热回流反应,生成最终产物对硝基苯甲醛。Sodium hydroxide is added to the organic phase of p-nitrobenzyl alcohol, hydrogen peroxide is added dropwise at a temperature of 25-35° C. under continuous stirring, and the reaction is heated under reflux to generate the final product p-nitrobenzaldehyde.
步骤(1)中所述的偶氮双烷基腈选自偶氮二异丁腈、偶氮二异戊腈、偶氮二异庚腈或偶氮二异辛腈中任意一种,优选偶氮二异戊腈;所述催化剂的用量为对硝基甲苯质量的1%-20%;所述的卤代芳烃选自氯苯,邻二氯苯或溴苯。The azobisalkylnitrile described in step (1) is selected from any one of azobisisobutyronitrile, azobisisovaleronitrile, azobisisoheptanonitrile or azobisisooctanonitrile, preferably azobisisobutyronitrile Nitrogen diisovaleronitrile; the dosage of the catalyst is 1%-20% of the mass of p-nitrotoluene; the halogenated aromatic hydrocarbon is selected from chlorobenzene, o-dichlorobenzene or bromobenzene.
步骤(2)中所述的碳酸盐为碳酸钾或碳酸钠,优选碳酸钾,碳酸盐的用量为对硝基甲苯质量的5%-100%;回流反应时间为20-30h。The carbonate described in the step (2) is potassium carbonate or sodium carbonate, preferably potassium carbonate, and the consumption of the carbonate is 5%-100% of the mass of p-nitrotoluene; the reflux reaction time is 20-30h.
步骤(3)中所述的双氧水质量百分比浓度为10%-50%,优选20%-35%;氢氧化钠的用量为对硝基甲苯质量的10%-20%。The hydrogen peroxide mass percentage concentration described in step (3) is 10%-50%, preferably 20%-35%; the consumption of sodium hydroxide is 10%-20% of p-nitrotoluene mass.
本发明的合成路线如下:The synthetic route of the present invention is as follows:
以对硝基甲苯为原料,以偶氮双烷基腈催化溴素溴化对硝基甲苯生成对硝基溴苄和溴化氢(溴化氢被双氧水氧化成单质溴后进入反应体系循环利用),碳酸盐水溶液催化对硝基溴苄水解为对硝基苯甲醇,氢氧化钠催化双氧水氧化对硝基苯甲醇生成目标产物对硝基苯甲醛。Using p-nitrotoluene as raw material, azobisalkylnitrile catalyzes bromine bromination of p-nitrotoluene to generate p-nitrobenzyl bromide and hydrogen bromide (hydrogen bromide is oxidized by hydrogen peroxide into elemental bromine and enters the reaction system for recycling ), the carbonate aqueous solution catalyzes the hydrolysis of p-nitrobenzyl bromide to p-nitrobenzyl alcohol, and the sodium hydroxide catalyzes the oxidation of p-nitrobenzyl alcohol with hydrogen peroxide to generate the target product p-nitrobenzaldehyde.
本方法与传统工艺相比有着显著的优点,主要特点有:(1)本方法应用双氧水氧化方法,较其他无机重金属盐和无机矿物酸氧化方法,提高了工业制备反应的清洁性,降低了环境污染。(2)本方法应用双氧水氧化方法,实现常压液相制备反应,较空气(氧气)氧化方法的气液相的加压反应,反应条件温和,提高工业制备操作安全性,节能。(3)本方法提高了产品得率,产率较目前工业传统方法提高约3%,本方法总收率达到76%,产品纯度99%以上。(4)本方法应用无机固体碱氢氧化钠催化氧化反应,不使用金属有机配合物催化剂,提高反应稳定性,大大降低了工业制备成本。(5)本方法应用偶氮双烷基腈固体催化剂替代过氧化碳酸酯液相催化剂,催化溴化反应,提高工业制备反应操作安全性。(6)本方法使用卤代芳烃为溶剂介质,避免了卤代烷烃溶剂介质的使用,避免了低沸点挥发性有机溶剂的污染。(7)本方法能在常压下进行反应,反应条件温和,工业制备操作简便。(8)本方法减少了有机物副产物生成和无机盐(酸)废水排放量。(9)本方法能根据市场需求,制备分离出高纯度中间化合物对硝基苯甲醇。Compared with the traditional process, this method has significant advantages. The main features are: (1) This method uses hydrogen peroxide oxidation method, which improves the cleanliness of industrial preparation reactions and reduces environmental pollution compared with other inorganic heavy metal salts and inorganic mineral acid oxidation methods. pollute. (2) This method uses the hydrogen peroxide oxidation method to realize the normal pressure liquid phase preparation reaction, which is milder than the gas-liquid phase pressurized reaction of the air (oxygen) oxidation method, which improves the safety of industrial preparation operations and saves energy. (3) The method improves the product yield, which is about 3% higher than the current industrial traditional method. The total yield of the method reaches 76%, and the product purity is more than 99%. (4) The method uses the inorganic solid alkali sodium hydroxide to catalyze the oxidation reaction, does not use metal-organic complex catalysts, improves the reaction stability, and greatly reduces the industrial preparation cost. (5) In this method, the azobisalkylnitrile solid catalyst is used to replace the peroxycarbonate liquid phase catalyst to catalyze the bromination reaction and improve the safety of the industrial preparation reaction operation. (6) The method uses halogenated aromatic hydrocarbon as solvent medium, avoids the use of halogenated alkane solvent medium, and avoids the pollution of low boiling point volatile organic solvent. (7) The method can be reacted under normal pressure, the reaction conditions are mild, and the industrial preparation is easy to operate. (8) The method reduces the generation of organic by-products and the discharge of inorganic salt (acid) wastewater. (9) The method can prepare and isolate high-purity intermediate compound p-nitrobenzyl alcohol according to market demand.
附图说明Description of drawings
图1为本发明工艺流程图。Fig. 1 is process flow chart of the present invention.
具体实施方式detailed description
下面结合附图1对新方法作进一步详细技术说明。Below in conjunction with accompanying drawing 1, the new method is described in further detail.
结合附图1,本发明包括三个单元反应工序,即溴化、水解、氧化反应。在第一溴化反应工序阶段,应用偶氮双烷基腈催化溴素与对硝基甲苯反应,形成的溴化氢副产物被双氧水氧化成单质溴后进入反应体系循环利用,这样不但降低了溴的消耗和减少了废物排放量,同时可以降低生产成本。该工序应用卤代芳烃替代卤代烷烃,避免挥发性有机溶剂的使用。在第二水解反应工序阶段,将第一工序阶段的反应混合物直接进入第二反应工序阶段,降低了环境污染,节能减排,简化工艺过程中的分离操作,易于工程化实施,除生成了对硝基苯甲醇外,还有少量的对硝基苯甲醛最终产物,此阶段的对硝基苯甲醇可以作为产品分离提取出来,且纯度非常高。在第三氧化反应工序阶段,双氧水是一种廉价环境友好型氧化剂,采用氢氧化钠催化双氧水氧化对硝基苯甲醇,高选择性生成对硝基苯甲醛,常压反应,条件温和,操作简单,不使用金属有机配合物,大大降低了原材料成本。新方法较传统工业方法提高3%产率,减少了有机物副产物生成,避免了过渡金属盐等对环境的影响,具有环境经济双重特性。With reference to accompanying drawing 1, the present invention comprises three unit reaction processes, i.e. bromination, hydrolysis, oxidation reaction. In the first bromination reaction process stage, azobisalkylnitrile is used to catalyze the reaction of bromine and p-nitrotoluene, and the hydrogen bromide by-product formed is oxidized by hydrogen peroxide into elemental bromine and then enters the reaction system for recycling, which not only reduces the Bromine consumption and waste reduction can reduce production costs. In this process, halogenated aromatic hydrocarbons are used instead of halogenated alkanes to avoid the use of volatile organic solvents. In the second hydrolysis reaction process stage, the reaction mixture of the first process stage directly enters the second reaction process stage, which reduces environmental pollution, saves energy and reduces emissions, simplifies the separation operation in the process, and is easy to implement engineering. In addition to nitrobenzyl alcohol, there is also a small amount of p-nitrobenzaldehyde final product. The p-nitrobenzyl alcohol at this stage can be isolated and extracted as a product, and its purity is very high. In the third oxidation reaction process stage, hydrogen peroxide is a cheap and environment-friendly oxidant. Sodium hydroxide is used to catalyze hydrogen peroxide to oxidize p-nitrobenzyl alcohol to generate p-nitrobenzaldehyde with high selectivity. The reaction is under normal pressure, the conditions are mild, and the operation is simple. , without the use of metal-organic complexes, greatly reducing the cost of raw materials. Compared with the traditional industrial method, the new method increases the yield by 3%, reduces the generation of organic by-products, avoids the impact of transition metal salts on the environment, and has dual characteristics of environment and economy.
下面以具体的实施例来详细说明本方法采用三个单元反应工序制备对硝基苯甲醛,但不代表限制本发明范围内容。The method uses three unit reaction processes to prepare p-nitrobenzaldehyde in detail below with specific examples, but it does not represent limiting the scope of the present invention.
实施例1Example 1
在反应器中,加入80g氯苯,13.7g对硝基甲苯、2.7g偶氮二异戊腈,在50℃下,在30min内缓慢滴加9.6g溴素,滴加完毕后,搅拌加热回流反应至溴素颜色褪去。在30min内缓慢滴加7.0g27.5%的双氧水,搅拌回流反应3h。在此反应液中加入68.5g20%的碳酸钾水溶液,搅拌回流反应30h,蒸馏回收氯苯后,冷却静置分离水相和含有对硝基苯甲醇有机相。将有机相转入反应器中,加入2.7g氢氧化钠,搅拌控制温度25℃在30min内滴加48.7g35%双氧水,加热回流反应26h。反应完成后冷却至室温,静置分离出有机相,洗涤后浓缩有机溶剂,经乙醇精制得11.5g对硝基苯甲醛,GC纯度99.1%,收率76.2%。In the reactor, add 80g chlorobenzene, 13.7g p-nitrotoluene, 2.7g azobisisovaleronitrile, slowly add 9.6g bromine dropwise within 30min at 50°C, after the dropwise addition, stir and heat to reflux React until the bromine color fades. Slowly add 7.0 g of 27.5% hydrogen peroxide dropwise within 30 min, and stir and reflux for 3 h. Add 68.5g of 20% potassium carbonate aqueous solution to the reaction solution, stir and reflux for 30h, recover chlorobenzene by distillation, cool and stand to separate the water phase and the organic phase containing p-nitrobenzyl alcohol. Transfer the organic phase into the reactor, add 2.7g of sodium hydroxide, stir and control the temperature at 25°C, add 48.7g of 35% hydrogen peroxide dropwise within 30min, and heat to reflux for 26h. After the reaction was completed, it was cooled to room temperature, and the organic phase was separated by standing. After washing, the organic solvent was concentrated, and 11.5 g of p-nitrobenzaldehyde was obtained by refining with ethanol. The GC purity was 99.1%, and the yield was 76.2%.
实施例2Example 2
在反应器中,加入80g氯苯,13.7g对硝基甲苯、1.2g偶氮二异庚腈,,在45℃下,在30min内缓慢滴加9.0g溴,滴加完毕后,搅拌加热回流反应至溴素颜色褪去。在30min内缓慢滴加7.0g27.5%的双氧水,搅拌回流反应2h。在此反应液中加入41.5g30%的碳酸钾水溶液,搅拌回流反应21h,蒸馏回收氯苯后,冷却静置分离水相和含有对硝基苯甲醇有机相。将有机相转入反应器中,加入1.5g氢氧化钠,搅拌控制温度30℃在30min内滴加62.0g27.5%的双氧水,加热回流反应26h。反应完成后冷却至室温,静置分离出有机相,洗涤后浓缩有机溶剂,经乙醇精制得11.3g对硝基苯甲醛,GC纯度99.0%,收率74.8%。In the reactor, add 80g of chlorobenzene, 13.7g of p-nitrotoluene, and 1.2g of azobisisoheptanonitrile, and slowly add 9.0g of bromine dropwise within 30min at 45°C. After the dropwise addition, stir and heat to reflux React until the bromine color fades. Slowly add 7.0 g of 27.5% hydrogen peroxide dropwise within 30 min, and stir and reflux for 2 h. Add 41.5 g of 30% potassium carbonate aqueous solution to the reaction solution, stir and reflux for 21 h, recover chlorobenzene by distillation, and cool and stand to separate the water phase and the organic phase containing p-nitrobenzyl alcohol. Transfer the organic phase into the reactor, add 1.5g of sodium hydroxide, stir and control the temperature at 30°C, add 62.0g of 27.5% hydrogen peroxide dropwise within 30min, and heat to reflux for 26h. After the reaction was completed, cool to room temperature, stand to separate the organic phase, concentrate the organic solvent after washing, and refine with ethanol to obtain 11.3 g of p-nitrobenzaldehyde, with a GC purity of 99.0% and a yield of 74.8%.
实施例3Example 3
在反应器中,加入80g邻二氯苯,13.7g对硝基甲苯、1.2g偶氮二异辛腈,在45℃下,在30min内缓慢滴加9.0g溴,滴加完毕后,搅拌加热回流反应至溴素颜色褪去。在30min内缓慢滴加7.0g27.5%的双氧水,搅拌回流反应2h。在此反应液中加入41.5g30%的碳酸钾水溶液,搅拌回流反应23h,蒸馏回收邻二氯苯后,冷却静置分离水相和含有对硝基苯甲醇有机相。将有机相转入反应器中,加入1.5g氢氧化钠,搅拌控制温度30℃在30min内滴加34.1g50%的双氧水,加热回流反应26h。反应完成后冷却至室温,静置分离出有机相,洗涤后浓缩有机溶剂,经乙醇精制得10.8g对硝基苯甲醛,GC纯度99.3%,收率71.5%。In the reactor, add 80g of o-dichlorobenzene, 13.7g of p-nitrotoluene, and 1.2g of azobisisooctanonitrile, and slowly add 9.0g of bromine dropwise within 30min at 45°C. After the dropwise addition, stir and heat The reaction was refluxed until the color of bromine faded. Slowly add 7.0 g of 27.5% hydrogen peroxide dropwise within 30 min, and stir and reflux for 2 h. Add 41.5 g of 30% potassium carbonate aqueous solution to the reaction solution, stir and reflux for 23 hours, recover o-dichlorobenzene by distillation, and cool and stand to separate the water phase and the organic phase containing p-nitrobenzyl alcohol. Transfer the organic phase into the reactor, add 1.5g of sodium hydroxide, stir and control the temperature at 30°C, add 34.1g of 50% hydrogen peroxide dropwise within 30min, and heat to reflux for 26h. After the reaction was completed, cool to room temperature, stand to separate the organic phase, concentrate the organic solvent after washing, and refine with ethanol to obtain 10.8 g of p-nitrobenzaldehyde, with a GC purity of 99.3% and a yield of 71.5%.
实施例4Example 4
在反应器中,加入80g氯苯,13.7g对硝基甲苯、1.5g偶氮二异戊腈,在45℃下,在30min内缓慢滴加9.0g溴,滴加完毕后,搅拌加热回流反应至溴素颜色褪去。在30min内缓慢滴加7.0g27.5%的双氧水,搅拌回流反应2h。在此反应液中加入50.0g25%的碳酸钾水溶液,搅拌回流反应23h,蒸馏回收65g氯苯后,冷却静置分离水相和含有对硝基苯甲醇有机相。将有机相转入反应器中,2.0g氢氧化钠,搅拌控制温度30℃在30min内滴加37.0g27.5%的双氧水,加热回流反应26h。反应完成后冷却至室温,静置分离出有机相,经亚硫酸氢钠反应提取精制得11.4g对硝基苯甲醛,GC纯度99.5%,收率75.5%。In the reactor, add 80g of chlorobenzene, 13.7g of p-nitrotoluene, and 1.5g of azobisisovaleronitrile, and slowly add 9.0g of bromine dropwise within 30min at 45°C. After the dropwise addition, stir and heat to reflux for reaction until the bromine color fades. Slowly add 7.0 g of 27.5% hydrogen peroxide dropwise within 30 min, and stir and reflux for 2 h. Add 50.0 g of 25% potassium carbonate aqueous solution to the reaction solution, stir and reflux for 23 hours, recover 65 g of chlorobenzene by distillation, and cool and stand to separate the water phase and the organic phase containing p-nitrobenzyl alcohol. Transfer the organic phase into the reactor, add 2.0 g of sodium hydroxide, stir and control the temperature at 30° C., add 37.0 g of 27.5% hydrogen peroxide dropwise within 30 min, and heat to reflux for 26 h. After the reaction was completed, it was cooled to room temperature, allowed to stand to separate the organic phase, and purified by reaction and extraction with sodium bisulfite to obtain 11.4 g of p-nitrobenzaldehyde with a GC purity of 99.5% and a yield of 75.5%.
实施例5Example 5
在反应器中,加入80g氯苯,13.7g对硝基甲苯、1.5g偶氮二异戊腈,在45℃下,在30min内缓慢滴加9.0g溴,滴加完毕后,搅拌加热回流反应至溴素颜色褪去。在30min内缓慢滴加7.0g27.5%的双氧水,搅拌回流反应2h。在此反应液中加入50.0g25%的碳酸钾水溶液,搅拌回流反应24h,蒸馏回收氯苯后,冷却静置分离水相和含有对硝基苯甲醇有机相。将有机相转入反应器中,加入2.0g氢氧化钠,搅拌控制温度30℃在30min内滴加68.7g20%的双氧水,加热回流反应25h。反应完成后冷却至室温,分离出有机相,经水蒸汽蒸馏精制得11.0g对硝基苯甲醛,GC纯度99.9%,收率72.8%。In the reactor, add 80g of chlorobenzene, 13.7g of p-nitrotoluene, and 1.5g of azobisisovaleronitrile, and slowly add 9.0g of bromine dropwise within 30min at 45°C. After the dropwise addition, stir and heat to reflux for reaction until the bromine color fades. Slowly add 7.0 g of 27.5% hydrogen peroxide dropwise within 30 min, and stir and reflux for 2 h. Add 50.0 g of 25% potassium carbonate aqueous solution to the reaction solution, stir and reflux for 24 hours, recover chlorobenzene by distillation, and cool and stand to separate the water phase and the organic phase containing p-nitrobenzyl alcohol. Transfer the organic phase into a reactor, add 2.0 g of sodium hydroxide, stir to control the temperature at 30° C., add 68.7 g of 20% hydrogen peroxide dropwise within 30 min, and heat to reflux for 25 h. After the reaction was completed, it was cooled to room temperature, the organic phase was separated, and purified by steam distillation to obtain 11.0 g of p-nitrobenzaldehyde with a GC purity of 99.9% and a yield of 72.8%.
实施例6Example 6
在反应器中,加入80g氯苯,13.7g对硝基甲苯、1.5g偶氮二异戊腈,在45℃下,在30min内缓慢滴加9.0g溴,滴加完毕后,搅拌加热回流反应至溴素颜色褪去。在30min内缓慢滴加7.0g27.5%的双氧水,搅拌回流反应2h。在此反应液中加入50.0g25%的碳酸钾水溶液,搅拌回流反应24h,蒸馏回收氯苯后,冷却静置分离水相和含有对硝基苯甲醇有机相。将有机相转入反应器中,加入10.0g20%氢氧化钠水溶液,搅拌控制温度30℃在30min内滴加49.0g35%的双氧水,加热回流反应26h。反应完成后冷却至室温,分离出有机相,经乙醇精制得11.1g对硝基苯甲醛,GC纯度99.3%,收率73.5%。In the reactor, add 80g of chlorobenzene, 13.7g of p-nitrotoluene, and 1.5g of azobisisovaleronitrile, and slowly add 9.0g of bromine dropwise within 30min at 45°C. After the dropwise addition, stir and heat to reflux for reaction until the bromine color fades. Slowly add 7.0 g of 27.5% hydrogen peroxide dropwise within 30 min, and stir and reflux for 2 h. Add 50.0 g of 25% potassium carbonate aqueous solution to the reaction solution, stir and reflux for 24 hours, recover chlorobenzene by distillation, and cool and stand to separate the water phase and the organic phase containing p-nitrobenzyl alcohol. Transfer the organic phase into the reactor, add 10.0g of 20% sodium hydroxide aqueous solution, stir and control the temperature at 30°C, add 49.0g of 35% hydrogen peroxide dropwise within 30min, and heat to reflux for 26h. After the reaction was completed, it was cooled to room temperature, the organic phase was separated, and purified with ethanol to obtain 11.1 g of p-nitrobenzaldehyde with a GC purity of 99.3% and a yield of 73.5%.
实施例7Example 7
在反应器中,加入80g溴苯,13.7g对硝基甲苯、0.1g偶氮二异丁腈,在40℃下,在30min内缓慢滴加8.0g溴素,滴加完毕后,搅拌加热回流反应至溴素颜色褪去。在30min内缓慢滴加7.0g27.5%的双氧水,搅拌回流反应2h。在此反应液中加入3.4g20%的碳酸钠水溶液,搅拌回流反应20h,蒸馏回收溴苯后,冷却静置分离水相和含有对硝基苯甲醇有机相。将有机相转入反应器中,加入1.5g氢氧化钠,搅拌控制温度35℃在30min内滴加170.5g10%双氧水,加热回流反应26h。反应完成后冷却至室温,静置分离出有机相,洗涤后浓缩有机溶剂,经乙醇精制得8.2g对硝基苯甲醛,GC纯度99.1%,收率54.2%。In the reactor, add 80g of bromobenzene, 13.7g of p-nitrotoluene, 0.1g of azobisisobutyronitrile, and slowly add 8.0g of bromine dropwise within 30min at 40°C. After the dropwise addition, stir and heat to reflux React until the bromine color fades. Slowly add 7.0 g of 27.5% hydrogen peroxide dropwise within 30 min, and stir and reflux for 2 h. Add 3.4g of 20% sodium carbonate aqueous solution to the reaction solution, stir and reflux for 20 hours, recover bromobenzene by distillation, cool and stand to separate the water phase and the organic phase containing p-nitrobenzyl alcohol. Transfer the organic phase into the reactor, add 1.5g of sodium hydroxide, stir to control the temperature at 35°C, add 170.5g of 10% hydrogen peroxide dropwise within 30min, and heat to reflux for 26h. After the reaction was completed, it was cooled to room temperature, and the organic phase was separated by standing. After washing, the organic solvent was concentrated, and 8.2 g of p-nitrobenzaldehyde was obtained by refining with ethanol. The GC purity was 99.1%, and the yield was 54.2%.
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CN111662180A (en) * | 2020-07-17 | 2020-09-15 | 山东卓俊实业有限公司 | Preparation method of p-nitrobenzaldehyde |
CN114230468A (en) * | 2021-08-02 | 2022-03-25 | 南京偌赛医药科技有限公司 | Method for catalytic synthesis of nitrobenzaldehyde |
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