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CN117384050A - Preparation method of pharmaceutical grade benzethonium chloride - Google Patents

Preparation method of pharmaceutical grade benzethonium chloride Download PDF

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CN117384050A
CN117384050A CN202311323346.0A CN202311323346A CN117384050A CN 117384050 A CN117384050 A CN 117384050A CN 202311323346 A CN202311323346 A CN 202311323346A CN 117384050 A CN117384050 A CN 117384050A
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benzethonium chloride
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CN117384050B (en
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瞿军
高德华
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Yangzhou Prince Pharmaceutical Technology Co ltd
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    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C213/00Preparation of compounds containing amino and hydroxy, amino and etherified hydroxy or amino and esterified hydroxy groups bound to the same carbon skeleton
    • C07C213/02Preparation of compounds containing amino and hydroxy, amino and etherified hydroxy or amino and esterified hydroxy groups bound to the same carbon skeleton by reactions involving the formation of amino groups from compounds containing hydroxy groups or etherified or esterified hydroxy groups
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C213/00Preparation of compounds containing amino and hydroxy, amino and etherified hydroxy or amino and esterified hydroxy groups bound to the same carbon skeleton
    • C07C213/08Preparation of compounds containing amino and hydroxy, amino and etherified hydroxy or amino and esterified hydroxy groups bound to the same carbon skeleton by reactions not involving the formation of amino groups, hydroxy groups or etherified or esterified hydroxy groups
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C213/00Preparation of compounds containing amino and hydroxy, amino and etherified hydroxy or amino and esterified hydroxy groups bound to the same carbon skeleton
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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Abstract

The invention discloses a preparation method of medical grade benzethonium chloride, which adopts salt of aryl polyoxyalkyl chloride and dimethylamine to carry out C-N coupling reaction, and realizes amination reaction mildly at normal pressure by introducing palladium catalyst or catalyst of iodized salt and polyethylene glycol; removing harmful impurities after molecular distillation treatment to obtain a compound 3; then the compound 3 and benzyl chloride are subjected to quaternization reaction in a solvent, and a benzethonium chloride product meeting the standard of raw materials can be obtained. The invention improves the product quality in terms of purity, impurities, residual solvent, chromaticity and the like, controls the product index more strictly, leads the standards of domestic and foreign peers and customers, and is superior to the USP36 standard and the EP10.0 standard.

Description

一种医药级苄索氯铵的制备方法A kind of preparation method of pharmaceutical grade benzethonium chloride

技术领域Technical field

本发明涉及一种医药级苄索氯铵的制备方法,属于医药技术领域。The invention relates to a preparation method of pharmaceutical grade benzethonium chloride and belongs to the field of medical technology.

背景技术Background technique

苄索氯铵(Benzethonium chloride),又名为苄基二甲基[2-[2-[4-(1,1,3,3-四甲基丁基)苯氧基]乙氧基]乙基]氯化铵,CAS登录号为121-54-0。其为片状晶体,熔点为164-166℃,易溶于水形成泡沫状肥皂水样溶液,溶于乙醇、丙酮、氯仿。Benzethonium chloride, also known as benzyldimethyl[2-[2-[4-(1,1,3,3-tetramethylbutyl)phenoxy]ethoxy]ethyl [Basic] ammonium chloride, CAS registration number is 121-54-0. It is a flaky crystal with a melting point of 164-166°C. It is easily soluble in water to form a foamy soapy water-like solution, and is soluble in ethanol, acetone and chloroform.

苄索氯铵的化学结构式如下:The chemical structural formula of benzethonium chloride is as follows:

苄索氯铵作为杀菌抗菌剂在医药卫生领域也有重要的应用,比如作为滴眼液的抑菌组分或者作为注射液的抑菌成分在西方国家一直有广泛的应用。本品收载于FDA《非活性组分指南》(肌内注射制剂,静脉注射制剂,眼用制剂和耳用制剂)。Benzethonium chloride also has important applications in the field of medicine and health as a bactericidal and antibacterial agent. For example, it has been widely used in Western countries as an antibacterial component of eye drops or as an antibacterial component of injections. This product is included in the FDA "Inactive Ingredients Guide" (intramuscular injection preparations, intravenous injection preparations, ophthalmic preparations and otic preparations).

在肝素钠领域,本产品每年的需求就达到五百吨,主要用于提纯肝素钠,或者用于低分子肝素钠和依诺肝素的生产,作为依诺肝素的合成关键起始原料,预防深静脉血栓形成及肺栓塞,治疗已形成的静脉血栓,预防血液透析时体外循环中血栓的形成,治疗不稳定性心绞痛和非Q波心梗。苄索氯铵也可用作润湿剂、增溶剂和外用消毒剂,在化妆品如除臭剂中,苄索氯铵的浓度大于0.5%w/v的溶液也可用作抗菌剂。In the field of heparin sodium, the annual demand for this product reaches 500 tons. It is mainly used for purifying heparin sodium or for the production of low molecular weight heparin sodium and enoxaparin. As a key starting material for the synthesis of enoxaparin, it is used to prevent severe Venous thrombosis and pulmonary embolism, treatment of existing venous thrombosis, prevention of thrombus formation in extracorporeal circulation during hemodialysis, treatment of unstable angina and non-Q wave myocardial infarction. Benzethonium chloride can also be used as a wetting agent, solubilizer and external disinfectant. In cosmetics such as deodorants, solutions of benzethonium chloride with a concentration greater than 0.5% w/v can also be used as antibacterial agents.

现有技术中苄索氯铵的合成路线有如下几种:The synthesis routes of benzethonium chloride in the prior art include the following:

北京桑普生物化学有限公司在美国专利US2014187819(A1)中公开了如下技术方案:1)酚与二卤代多亚烷基醚在相转移催化剂作用下反应得到芳基多氧烷基卤化物;2)芳基多氧烷基卤化物与胺化试剂在相转移催化剂作用下反应得到芳基多氧烷基胺化物;3)芳基多氧烷基胺化物与烷化试剂反应得到芳基多氧烷基季铵类化合物。Beijing Sangpu Biochemical Co., Ltd. disclosed the following technical solution in U.S. Patent US2014187819 (A1): 1) phenol and dihalogenated polyalkylene ether react under the action of a phase transfer catalyst to obtain arylpolyoxyalkyl halide; 2) Aryl polyoxyalkyl halides react with amination reagents under the action of phase transfer catalysts to obtain aryl polyoxyalkyl amines; 3) Aryl polyoxyalkyl amines react with alkylating reagents to obtain aryl polyoxyalkyl halides. Oxyalkyl quaternary ammonium compounds.

该技术路线的反应方程式如下:The reaction equation of this technical route is as follows:

上述技术方案中使用大量的相转移催化剂苄基三乙基氯化铵,反应温度约160℃,同时反应压力达到约8-10公斤,对设备要求较为苛刻,不利于生产车间放大。In the above technical solution, a large amount of phase transfer catalyst benzyltriethylammonium chloride is used, the reaction temperature is about 160°C, and the reaction pressure reaches about 8-10 kg. The equipment requirements are relatively stringent and are not conducive to the expansion of the production workshop.

科莱恩制造(德国)有限公司在美国专利US2003114533(A1)中披露了芳基多氧烷基卤化物和二甲基苄胺的季铵化反应,尽管该发明声称简化了制备工艺,但实际应用中还要涉及所用原料芳基多氧烷基卤化物的制备,且产品季铵类物质的收集纯化操作过于复杂。由于芳基多氧烷基卤化物的卤素活性也很低,导致和苄基二甲胺的反应,存在高温反应时间长,反应设备的耐温和耐压问题。最重要的是高温反应导致产品品质较差,不是最佳的商业化生产路线。该技术路径的反应式如下:Clariant Manufacturing (Germany) Co., Ltd. disclosed the quaternization reaction of arylpolyoxyalkyl halides and dimethylbenzylamine in US patent US2003114533 (A1). Although the invention claims to simplify the preparation process, the actual application It also involves the preparation of the raw material arylpolyoxyalkyl halide, and the collection and purification operation of the product quaternary ammonium substances is too complicated. Since the halogen activity of arylpolyoxyalkyl halides is also very low, the reaction with benzyldimethylamine has problems such as high temperature and long reaction time, and the temperature and pressure resistance of the reaction equipment. The most important thing is that high-temperature reaction results in poor product quality and is not the best commercial production route. The reaction formula of this technical path is as follows:

中国专利CN113372227(A)和专利CN109651177(A)分别公开了一种苄索氯铵的制备方法,该方法通过对特辛基苯酚加入二氯乙烷进行一步反应,再混合二甲基乙醇胺进行二步反应,最后再加入氯化苄进行三步反应制得产物,其反应方程式如下:Chinese patent CN113372227(A) and patent CN109651177(A) respectively disclose a preparation method of benzethonium chloride, which involves adding dichloroethane to p-teroctylphenol for a one-step reaction, and then mixing dimethylethanolamine for a second step. A three-step reaction, and finally benzyl chloride is added to perform a three-step reaction to obtain the product. The reaction equation is as follows:

但是该制备方法中反应温度也相对较高,存在高温高压环境下的隐患。苄索氯铵为季铵类化合物,在药物制剂中作为抗菌剂,可用于注射、眼用制剂和耳用制剂的抗菌剂,所以苄索氯铵的合成尽量不涉及使用到已知可致癌且对人和环境有害的一类溶剂1,2-二氯乙烷,所以该路线不适合生产。However, the reaction temperature in this preparation method is also relatively high, and there are hidden dangers in high temperature and high pressure environments. Benzethonium chloride is a quaternary ammonium compound. It is used as an antibacterial agent in pharmaceutical preparations. It can be used as an antibacterial agent for injections, eye preparations and otic preparations. Therefore, the synthesis of benzethonium chloride should try not to involve the use of substances that are known to be carcinogenic and 1,2-dichloroethane is a type of solvent that is harmful to people and the environment, so this route is not suitable for production.

印度迪氏曼在其专利EP1892235(A)中公开了一种以4-叔辛基苯酚、氯乙醇和(β-氯乙基)二甲胺作为原料,通过三步进行合成,均为常压反应。其反应方程式如下:Indian Dismant disclosed in its patent EP1892235(A) a method using 4-tert-octylphenol, chloroethanol and (β-chloroethyl)dimethylamine as raw materials, which was synthesized in three steps, all under normal pressure. reaction. The reaction equation is as follows:

2-二甲氨基氯乙烷盐酸盐因其具有卤代烃的基因毒性警示结构,需要对该类杂质进行控制,影响苄索氯铵产品的使用安全性。氯乙醇是剧毒品,根据中国的相关法律法规和政策,此产品禁止生产、买卖、使用或持有。所以,该专利的方法不适合商业化生产。2-Dimethylaminoethyl chloride hydrochloride has a genotoxicity warning structure of a halogenated hydrocarbon. This type of impurity needs to be controlled, which affects the safety of benzethonium chloride products. Chlorohydrin is a highly toxic drug. According to relevant laws, regulations and policies of China, the production, sale, use or possession of this product is prohibited. Therefore, the patented method is not suitable for commercial production.

综上所述,目前的生产工艺需要高温和压力,这对生产安全有隐患,有必要对工艺进行改进,降低反应的苛刻条件,从而得到高品质的医药级苄索氯铵产品。To sum up, the current production process requires high temperature and pressure, which has hidden dangers for production safety. It is necessary to improve the process and reduce the harsh conditions of the reaction, so as to obtain high-quality pharmaceutical-grade benzethonium chloride products.

发明内容Contents of the invention

为克服上述技术问题,本发明提供了一种医药级苄索氯铵的制备方法,其反应过程如下:In order to overcome the above technical problems, the present invention provides a preparation method of pharmaceutical grade benzethonium chloride, and the reaction process is as follows:

S1:S1:

,式中,HX为盐酸、氢溴酸、硫酸或氢碘酸;, in the formula, HX is hydrochloric acid, hydrobromic acid, sulfuric acid or hydriodic acid;

S2:S2:

针对现有合成方法的缺点,下面详细说明本发明的创新技术方法的来源和理论依据。In view of the shortcomings of existing synthesis methods, the source and theoretical basis of the innovative technical method of the present invention will be described in detail below.

S1:S1:

目前国内外生产普遍采用美国专利US2014187819(A1)中的技术方案,芳基多氧烷基卤化物与胺化试剂在相转移催化剂作用下反应得到芳基多氧烷基胺化物,即使使用大量的相转移催化剂,专利使用的反应温度约160℃,同时反应压力达到约8-10公斤。At present, domestic and foreign production generally adopt the technical solution in US patent US2014187819 (A1). Arylpolyoxyalkyl halides react with amination reagents under the action of a phase transfer catalyst to obtain arylpolyoxyalkyl aminations. Even if a large amount of The patented phase transfer catalyst uses a reaction temperature of about 160°C and a reaction pressure of about 8-10 kg.

科莱恩制造(德国)公司在美国专利US2003114533(A1)采用芳基多氧烷基卤化物和二甲基苄胺的季铵化反应,反应温度采用120℃,反应压力约2公斤,该专利得到的产品季铵类物质的品质差,需要采用过于复杂的纯化操作,才能达到合格产品。Clariant Manufacturing (Germany) Company's U.S. patent US2003114533 (A1) uses a quaternization reaction of arylpolyoxyalkyl halides and dimethylbenzylamine. The reaction temperature is 120°C and the reaction pressure is about 2 kg. The patent was obtained The quality of the quaternary ammonium substances in the products is poor and requires overly complex purification operations to achieve qualified products.

由于芳基多氧烷基卤化物的氯原子的反应活性低,目前几乎所有的厂家都是使用二甲胺水溶液做胺化反应,导致目前的生产工艺需要高温和压力,这对生产安全有隐患,有必要对工艺进行改进,降低反应的苛刻条件,这是本发明需要解决的关键技术难题。Due to the low reactivity of the chlorine atoms of arylpolyoxyalkyl halides, almost all manufacturers currently use dimethylamine aqueous solutions for amination reactions. As a result, the current production process requires high temperature and pressure, which has hidden dangers for production safety. , it is necessary to improve the process and reduce the harsh conditions of the reaction, which is a key technical problem to be solved by the present invention.

从有机合成理论上,采用包含碘化钾、碘化钠和聚乙二醇的催化剂体系进行对氯置换的亲核取代反应,由碘离子置换氯离子,碘离子的离去能力远远大于氯离子,碘离子脱离后又能循环作用于剩余的反应系统,从而大大的提高了反应速度并降低了反应的温度。From the theory of organic synthesis, a catalyst system containing potassium iodide, sodium iodide and polyethylene glycol is used to carry out a nucleophilic substitution reaction of chlorine replacement. The chloride ion is replaced by iodide ion. The leaving ability of iodide ion is much greater than that of chloride ion. After the iodide ions are detached, they can be recycled to the remaining reaction system, thereby greatly increasing the reaction speed and lowering the reaction temperature.

另外,Buchwald-Hartwig偶联反应是一种重要的芳胺合成方法,该反应是在钯催化和碱存在下,胺与芳卤的交叉偶联反应,产生C-N键,生成胺的N-芳基化产物。In addition, the Buchwald-Hartwig coupling reaction is an important method for the synthesis of aromatic amines. This reaction is a cross-coupling reaction between amines and aromatic halides under palladium catalysis and the presence of a base, producing C-N bonds and generating the N-aryl group of the amine. chemical products.

本发明相应的采用芳基多氧烷基氯化物和二甲胺的盐进行C-N偶联反应,通过引入钯催化剂或者碘化盐和聚乙二醇的催化剂,可以常压温和的实现胺化反应,从而形成了本发明步骤1的制备方法。Correspondingly, the present invention uses the salt of aryl polyoxyalkyl chloride and dimethylamine to carry out C-N coupling reaction. By introducing a palladium catalyst or a catalyst of iodide salt and polyethylene glycol, the amination reaction can be realized mildly under normal pressure. , thereby forming the preparation method of step 1 of the present invention.

S2:S2:

由于苄索氯铵被应用于黏膜消毒、眼药水和粉类产品的防霉,必须极低刺激,其中有害杂质,例如:残留溶剂、氯化苄、和β,β’-二氯二乙醚等,现有技术中在产品中的残留量没有进行有效的控制,造成产品达不到医药级别的质量要求。Since benzethonium chloride is used for mucous membrane disinfection and anti-mold in eye drops and powder products, it must be extremely low-irritating and contains harmful impurities, such as residual solvents, benzyl chloride, and β, β'-dichlorodiethyl ether, etc. , in the existing technology, the residual amount in the product is not effectively controlled, causing the product to fail to meet pharmaceutical grade quality requirements.

根据人用药品注册技术要求国际协调会ICHQ3指导原则,大都数厂家的苄索氯铵质量规格都没有达到医药级别的要求。According to the ICHQ3 guidelines of the International Conference on Harmonization of Technical Requirements for Registration of Pharmaceuticals for Human Use, the quality specifications of benzethonium chloride from most manufacturers do not meet pharmaceutical grade requirements.

例如:国内某企业的产品指标如下,但是从原料药ICHQ3的指导原则要求,指标内缺少对有害杂质限度的控制标准。For example: The product indicators of a domestic company are as follows, but according to the guiding principles of API ICHQ3, the indicators lack control standards for harmful impurity limits.

目前所报道的对叔辛基苯氧基乙氧基乙基二甲胺纯化方法,是通过减压蒸馏的方法,但是在蒸馏过程中产品由于长时间的处于高温状态下,会导致产物的降解聚合,不仅降低了收率,还有可能使产品产生杂质造成产品不合格。The currently reported purification method for p-tert-octylphenoxyethoxyethyldimethylamine is through vacuum distillation. However, during the distillation process, the product will be degraded due to being at high temperature for a long time. Polymerization not only reduces the yield, but may also produce impurities in the product and cause the product to be unqualified.

本发明研究发现,将第一步制备得到的对叔辛基苯氧基乙氧基乙基二甲胺,经过分子蒸馏处理后,除去有害杂质,再和氯化苄在溶剂中低温下进行季铵化反应,从而形成了目前行业领先的步骤2的制备工艺。The research of the present invention has found that the p-tert-octylphenoxyethoxyethyldimethylamine prepared in the first step is subjected to molecular distillation treatment to remove harmful impurities, and then is quaternized with benzyl chloride in a solvent at medium and low temperatures. Ammonization reaction, thus forming the current industry-leading step 2 preparation process.

同时,本发明在借鉴国内外同行产品指标,依据ICHQ3的指导原则,制定了具有制造特色的苄索氯铵产品企业标准,优于美国药典USP36标准和欧洲药典EP10.0标准。At the same time, the present invention draws on the product indicators of domestic and foreign counterparts and formulates enterprise standards for benzethonium chloride products with manufacturing characteristics based on the guiding principles of ICHQ3, which are superior to the United States Pharmacopoeia USP36 standard and the European Pharmacopoeia EP10.0 standard.

有益结果为本发明从纯度、杂质和残留溶剂和色度等方面对产品质量做了提升,产品指标控制更加严格,领先国内外同行、客户的标准。The beneficial results are that the present invention improves product quality in terms of purity, impurities, residual solvents, and color, and controls product indicators more strictly, leading domestic and foreign counterparts and customer standards.

上述医药级苄索氯铵的制备方法包括如下步骤:The preparation method of the above-mentioned pharmaceutical grade benzethonium chloride includes the following steps:

S1-1:化合物3的制备S1-1: Preparation of compound 3

向反应釜内,氮气保护下加入对叔辛基苯氧基乙氧基乙基氯2、二甲基胺盐和催化剂,升温反应,保持2-5h,HPLC检测控制:控制对叔辛基苯氧基乙氧基乙基氯2的残留量≤3.0%时,反应结束;将反应物搅拌反应完成后,降温至35℃以下,加入乙酸乙酯,反应液静置分层,得有机层。Into the reaction kettle, add p-tert-octylphenoxyethoxyethyl chloride 2, dimethylamine salt and catalyst under nitrogen protection, heat up the reaction, keep for 2-5h, HPLC detection control: control p-tert-octylbenzene When the residual amount of oxyethoxyethyl chloride 2 is ≤3.0%, the reaction ends; after the reaction is stirred and the reaction is completed, the temperature is lowered to below 35°C, ethyl acetate is added, and the reaction solution is allowed to stand and separated to obtain an organic layer.

进一步地,所述步骤S1-1中的二甲基胺盐为二甲胺盐酸盐、二甲胺氢溴酸盐、二甲胺硫酸盐和二甲胺基氢碘酸盐,优选为二甲胺盐酸盐。Further, the dimethylamine salt in step S1-1 is dimethylamine hydrochloride, dimethylamine hydrobromide, dimethylamine sulfate and dimethylamino hydroiodide, preferably dimethylamine hydroiodide. Methylamine hydrochloride.

进一步地,所述步骤S1-1中的催化剂为包含氯化锂、溴化锂、溴化钾、溴化钠、溴化亚铜、碘化钠、碘化钾、碘化亚铜和钯催化剂中至少一种;优选为碘化钠和钯催化剂。Further, the catalyst in step S1-1 is a catalyst containing at least one of lithium chloride, lithium bromide, potassium bromide, sodium bromide, cuprous bromide, sodium iodide, potassium iodide, cuprous iodide and palladium catalyst ; Preferred are sodium iodide and palladium catalysts.

进一步地,所述钯催化剂为Pd(OAc)2,Pd2(dba)3,PdCl2(dppf),PdCl2(PPh3)2,PdCl2(PCy)2,PdCl2,PdCl2(CH3CN)2等;优选为PdCl2(dppf)。Further, the palladium catalyst is Pd(OAc) 2 , Pd2(dba) 3 , PdCl 2 (dppf), PdCl 2 (PPh3) 2 , PdCl 2 (PCy) 2 , PdCl 2 , PdCl 2 (CH 3 CN) 2 , etc.; preferably PdCl 2 (dppf).

S1-2:粗品提纯S1-2: Crude product purification

有机层使用油泵减压,蒸馏体系的真空度控制为0.01-1.0mbar,油浴温度为160-180℃,刮膜器转速为200-300转/分钟,连续进样,控制进样速度,通过分子蒸馏得到化合物3。The organic layer is decompressed using an oil pump. The vacuum degree of the distillation system is controlled to 0.01-1.0 mbar. The oil bath temperature is 160-180°C. The film scraper speed is 200-300 rpm. Continuous sampling is performed. Control the sampling speed. Molecular distillation gave compound 3.

进一步地,步骤S1-2中的蒸馏方式为减压蒸馏、高真空精馏、分子蒸馏;优选为分子蒸馏。Further, the distillation method in step S1-2 is vacuum distillation, high vacuum distillation, and molecular distillation; preferably, molecular distillation is used.

进一步地,所述步骤S1-2中的采用分子蒸馏时的绝对压力为0.005MPa-0.01MPa。Further, the absolute pressure when using molecular distillation in step S1-2 is 0.005MPa-0.01MPa.

S2-1:化合物1的制备S2-1: Preparation of compound 1

化合物3的投料前处理:向反应釜内,氮气保护下加入化合物3和溶剂,搅拌升温至30-50℃之间,加入活性炭进行脱色至工艺规定时间,通过孔径小于45微米的精密压滤器,压滤至S2-2步骤进行反应。Pre-treatment of compound 3: Add compound 3 and solvent into the reaction kettle under nitrogen protection, stir and raise the temperature to between 30-50°C, add activated carbon to decolorize for the time specified in the process, and pass through a precision filter press with a pore size less than 45 microns. Press filtration to step S2-2 for reaction.

进一步地,所述步骤S2-1中的溶剂为乙酸乙酯、乙酸异丙酯、乙腈、丙酮或甲基异丁酮;优选为乙酸乙酯。Further, the solvent in step S2-1 is ethyl acetate, isopropyl acetate, acetonitrile, acetone or methyl isobutyl ketone; preferably, it is ethyl acetate.

S2-2:化合物1的制备S2-2: Preparation of compound 1

向反应釜内,氮气保护下加入步骤S2-1处理后的化合物3溶液,然后通过精密过滤器抽入氯化苄,搅拌升温至40-60℃之间反应,保持反应至工艺规定时间,无需取样中控,结束反应。将反应液过滤,所得的固体加入乙酸乙酯搅拌洗涤,所得白色固体减压下烘干得到化合物1。Into the reaction kettle, add the compound 3 solution treated in step S2-1 under nitrogen protection, then pump benzyl chloride through a precision filter, stir and raise the temperature to 40-60°C for reaction, and maintain the reaction until the specified time of the process. No need Sampling is controlled and the reaction is completed. The reaction solution was filtered, and the obtained solid was stirred and washed with ethyl acetate. The obtained white solid was dried under reduced pressure to obtain compound 1.

进一步地,步骤S2-2中的反应温度为20-150℃;优选为40-60℃。Further, the reaction temperature in step S2-2 is 20-150°C; preferably 40-60°C.

本发明的有益效果:Beneficial effects of the present invention:

1.本发明相应的芳基多氧烷基氯化物和二甲胺的盐进行C-N偶联反应,通过引入钯催化剂或者碘化盐和聚乙二醇的催化剂,常压温和的实现胺化反应;再经过分子蒸馏处理后,除去有害杂质,得到对叔辛基苯氧基乙氧基乙基二甲胺;然后和氯化苄在溶剂中进行季铵化反应,可以得到符合原料药标准的苄索氯铵产品。1. The salts of the corresponding arylpolyoxyalkyl chlorides and dimethylamines of the present invention carry out C-N coupling reactions. By introducing palladium catalysts or catalysts of iodide salts and polyethylene glycol, the amination reaction can be achieved mildly under normal pressure. ; After molecular distillation treatment, harmful impurities are removed to obtain p-tert-octylphenoxyethoxyethyldimethylamine; and then quaternization reaction is performed with benzyl chloride in a solvent to obtain API that meets the API standards. Benzethonium Chloride Products.

2.本发明在参考借鉴国内外同行产品指标的基础,制定了相关的苄索氯铵产品企业标准,优于美国药典USP36标准和欧洲药典EP10.0标准。2. Based on the product indicators of domestic and foreign counterparts, the present invention formulated relevant enterprise standards for benzethonium chloride products, which are superior to the United States Pharmacopoeia USP36 standard and the European Pharmacopoeia EP10.0 standard.

附图说明Description of the drawings

图1是实施例1的S2化合物1的纯度检测的HPLC谱图。Figure 1 is an HPLC spectrum of purity detection of S2 compound 1 in Example 1.

具体实施方式Detailed ways

通过下述实施例子将有助于科研人员理解本发明的制备技术要点,但是不能限制本发明的内容。The following examples will help researchers understand the key points of the preparation technology of the present invention, but they cannot limit the content of the present invention.

实施例1Example 1

本实施例提供了一种医药级苄索氯铵的制备方法,包括如下步骤:This embodiment provides a preparation method of pharmaceutical grade benzethonium chloride, which includes the following steps:

S1:化合物3的合成S1: Synthesis of Compound 3

向反应釜内,氮气保护下加入48.0g对叔辛基苯氧基乙氧基乙基氯2、88.0g二甲胺盐酸盐和2.5g碘化钠和0.05g PdCl2(dppf),升温至70-80℃反应,保持5h,控制对叔辛基苯氧基乙氧基乙基氯2的残留量≤3.0%时,反应结束;将反应物搅拌反应完成后,降温至35℃以下,加入50.0g乙酸乙酯,反应液静置分层,得有机层;有机层使用油泵减压,蒸馏体系的真空度控制为0.01-1.0mbar,油浴温度160-180℃,刮膜器转速为200-300转/分钟,物料进样速度为5-10mL/min,分子蒸馏得到42.4g无色透明液体化合物3,收率为86.0%,GC纯度99.52%,未知杂质小于0.3%。Into the reaction kettle, add 48.0g p-tert-octylphenoxyethoxyethyl chloride 2, 88.0g dimethylamine hydrochloride, 2.5g sodium iodide and 0.05g PdCl2 (dppf) under nitrogen protection, and heat to React at 70-80°C for 5 hours. When the residual amount of p-tert-octylphenoxyethoxyethyl chloride 2 is controlled to be ≤3.0%, the reaction ends; after stirring the reactants and completing the reaction, cool down to below 35°C and add 50.0g ethyl acetate, the reaction solution is allowed to stand and stratified to obtain an organic layer; the organic layer is decompressed using an oil pump, the vacuum degree of the distillation system is controlled to 0.01-1.0mbar, the oil bath temperature is 160-180°C, and the rotation speed of the film scraper is 200 -300 rpm, the material injection speed is 5-10mL/min, and 42.4g of colorless transparent liquid compound 3 is obtained by molecular distillation, with a yield of 86.0%, a GC purity of 99.52%, and unknown impurities less than 0.3%.

S2:化合物1的合成S2: Synthesis of Compound 1

S2-1:将化合物3的投料前处理S2-1: Pre-treatment of compound 3

向反应釜内,氮气保护下加入300.0g对叔辛基苯氧基乙氧基乙基二甲胺3和900.0g乙酸乙酯,搅拌升温至30-50℃之间,加入20.0g针用767炭进行脱色吸附至工艺规定时间,通过孔径小于45微米的精密压滤器,压滤至S2-2步骤进行反应。Into the reaction kettle, add 300.0g p-tert-octylphenoxyethoxyethyldimethylamine 3 and 900.0g ethyl acetate under nitrogen protection, stir and raise the temperature to between 30-50°C, add 20.0g needle 767 The carbon is decolorized and adsorbed to the time specified in the process, passed through a precision filter press with a pore size less than 45 microns, and filtered to step S2-2 for reaction.

S2-2:向反应釜内,氮气保护下加入S2-1的对叔辛基苯氧基乙氧基乙基二甲胺3溶液,然后通过精密过滤器抽入121.0g氯化苄,搅拌升温至40-60℃之间反应。保持反应至工艺规定时间,无需取样中控,结束反应。将反应液降温至10-20℃过滤,所得的固体加入300.0g乙酸乙酯搅拌洗涤,所得固体在-0.098MPa、35℃条件下对滤饼进行真空干燥,然后将滤饼粉碎即为苄索氯铵产品。得到365.9g化合物1,收率为87.5%,HPLC纯度为99.9%(如图1所示),单个杂质都小于0.05%,经过全检,符合苄索氯铵的质量内控指标。S2-2: Add the p-tert-octylphenoxyethoxyethyldimethylamine 3 solution of S2-1 into the reaction kettle under nitrogen protection, then pump 121.0g of benzyl chloride through the precision filter, stir and raise the temperature React between 40-60℃. Keep the reaction until the time specified in the process, without the need for sampling and control, and end the reaction. Cool the reaction solution to 10-20°C and filter. Add 300.0g of ethyl acetate to the resulting solid, stir and wash. The resulting solid is vacuum dried at -0.098MPa and 35°C. The filter cake is then pulverized to obtain benzyl ethyl acetate. Ammonium Chloride Products. 365.9g of compound 1 was obtained, with a yield of 87.5% and an HPLC purity of 99.9% (as shown in Figure 1). Each impurity was less than 0.05%. After full inspection, it complied with the internal quality control indicators of benzethonium chloride.

在其他物质不变的基础上,改变不同的二甲胺酸盐,得下表一所列数据:On the basis of keeping other substances unchanged, changing different dimethylamine salts, the data listed in Table 1 below are obtained:

实验编号Experiment number 二甲胺酸盐dimethylamino acid salt S1产物收率(%)S1 product yield (%) S1步骤产物纯度(%)Product purity of step S1 (%) 11 二甲胺硫酸盐dimethylamine sulfate 83.583.5 97.897.8 22 二甲胺基氢碘酸盐dimethylaminohydriodate 84.284.2 98.298.2 33 二甲胺氢溴酸盐Dimethylamine hydrobromide 82.682.6 98.598.5

在其他物质不变的基础上,改变催化剂,得下表二所列数据:On the basis of keeping other substances unchanged, changing the catalyst, the data listed in Table 2 below are obtained:

步骤S1中产品提纯方法的选择:Selection of product purification method in step S1:

在其他物质不变的基础上,本发明人比较了不同的蒸馏方法,得下表三所列数据:On the basis that other substances remained unchanged, the inventor compared different distillation methods and obtained the data listed in Table 3 below:

实施例2Example 2

本实施例提供了一种医药级苄索氯铵的制备方法,包括如下步骤:This embodiment provides a preparation method of pharmaceutical grade benzethonium chloride, which includes the following steps:

S1:化合物3的合成S1: Synthesis of Compound 3

向反应釜内,氮气保护下加入240.0Kg对叔辛基苯氧基乙氧基乙基氯2、220Kg二甲胺盐酸盐和1.5Kg碘化钠和0.05Kg PdCl2(dppf),升温至70-80℃反应,保持5h,控制对叔辛基苯氧基乙氧基乙基氯2的残留量≤3.0%时,反应结束;将反应物搅拌反应完成后,降温至35℃以下,加入100.0Kg乙酸乙酯,反应液静置分层,得有机层;有机层使用油泵减压,蒸馏体系的真空度控制为0.01-1.0mbar,油浴温度160-180℃,刮膜器转速为200-300转/分钟,物料进样速度为50-60L/h,分子蒸馏得到213.5Kg无色透明液体化合物3,收率为86.37%,GC纯度98.62%,未知杂质小于0.3%。Into the reaction kettle, add 240.0Kg p-tert-octylphenoxyethoxyethyl chloride 2, 220Kg dimethylamine hydrochloride, 1.5Kg sodium iodide and 0.05Kg PdCl2 (dppf) under nitrogen protection, and heat to 70 React at -80°C for 5 hours. When the residual amount of p-tert-octylphenoxyethoxyethyl chloride 2 is controlled to be ≤3.0%, the reaction ends. After the reactants are stirred and the reaction is completed, cool down to below 35°C and add 100.0 Kg of ethyl acetate, the reaction solution is allowed to stand and stratified to obtain an organic layer; the organic layer is decompressed using an oil pump, the vacuum degree of the distillation system is controlled to 0.01-1.0mbar, the oil bath temperature is 160-180°C, and the film scraper speed is 200-200 300 rpm, material injection speed 50-60L/h, molecular distillation to obtain 213.5Kg colorless transparent liquid compound 3, yield 86.37%, GC purity 98.62%, unknown impurities less than 0.3%.

S2:化合物1的合成S2: Synthesis of Compound 1

S2-1:化合物3的脱色吸附处理S2-1: Decolorization and adsorption treatment of compound 3

向反应釜内,氮气保护下加入150Kg对叔辛基苯氧基乙氧基乙基二甲胺3和600.0Kg乙酸乙酯,搅拌升温至30-50℃之间,加入20.0Kg针用767型针剂活性炭进行脱色吸附至工艺规定时间,通过孔径小于45微米的精密压滤器,压滤至S2-2步骤进行反应。Into the reaction kettle, add 150Kg p-tert-octylphenoxyethoxyethyldimethylamine 3 and 600.0Kg ethyl acetate under nitrogen protection, stir and raise the temperature to between 30-50°C, add 20.0Kg needle type 767 The injection activated carbon is decolorized and adsorbed for the time specified in the process, passed through a precision filter press with a pore size less than 45 microns, and filtered to step S2-2 for reaction.

S2-2:向反应釜内,氮气保护下加入S2-1的对叔辛基苯氧基乙氧基乙基二甲胺3溶液,然后通过精密过滤器抽入121.0Kg氯化苄,搅拌升温至40-60℃之间反应。保持反应至工艺规定时间,无需取样中控,结束反应。将反应液降温至10-20℃过滤,所得的固体加入300.0Kg乙酸乙酯搅拌洗涤,所得固体在-0.098MPa、45℃条件下对滤饼进行真空干燥,然后将滤饼粉碎即为苄索氯铵产品。得到187.8Kg化合物1,收率为89.8%,HPLC纯度为99.9%,单个杂质都小于0.03%,经过全检,符合苄索氯铵的质量内控指标。S2-2: Add the p-tert-octylphenoxyethoxyethyldimethylamine 3 solution of S2-1 into the reaction kettle under nitrogen protection, then pump 121.0Kg of benzyl chloride through the precision filter, stir and raise the temperature React between 40-60℃. Keep the reaction until the time specified in the process, without the need for sampling and control, and end the reaction. Cool the reaction solution to 10-20°C and filter. Add 300.0Kg of ethyl acetate to the resulting solid, stir and wash. The resulting solid is vacuum dried at -0.098MPa and 45°C. The filter cake is then crushed to obtain benzyl ethyl acetate. Ammonium Chloride Products. 187.8Kg of compound 1 was obtained, with a yield of 89.8%, an HPLC purity of 99.9%, and individual impurities less than 0.03%. After full inspection, it complied with the internal quality control indicators of benzethonium chloride.

对比例1Comparative example 1

本对比例重复北京桑普生物化学有限公司的美国专利US2014187819(A1)的实施例1。This comparative example repeats Example 1 of US Patent US2014187819 (A1) of Beijing Samp Biochemical Co., Ltd.

在一个1L密闭反应釜中,加入144.6g对叔辛基苯氧基乙氧基乙基氯、11.4g苄基三乙基氯化铵、135.3g浓度33%二甲胺水溶液,密闭后升温至160℃,搅拌反应8h,经气相检测对叔辛基苯氧基乙氧基乙基氯的转化率为100%。反应结束,物料静置分离除去水相,收集有机相136.2g。In a 1L sealed reaction kettle, add 144.6g p-tert-octylphenoxyethoxyethyl chloride, 11.4g benzyltriethylammonium chloride, and 135.3g 33% dimethylamine aqueous solution, seal it and raise the temperature to The reaction was stirred for 8 hours at 160°C, and the conversion rate to tert-octylphenoxyethoxyethyl chloride was 100% through gas phase detection. At the end of the reaction, the material was allowed to stand and separated to remove the aqueous phase, and 136.2g of the organic phase was collected.

将上述得到的136.2g对叔辛基苯氧基乙氧基乙基二甲胺,加入1L的四口反应瓶中,依次加入100.2g甲基异丁基酮、126.6g苄基氯,升温至回流,反应2h,缓慢加入168.2g环己烷,降温结晶,收集固体156.3g,在-0.098MPa、35℃条件下对滤饼进行真空干燥,然后将滤饼粉碎即为苄索氯铵产品。最终得到142.6g淡黄色产品,两步总收率为68.9%,纯度为97.60%,产品熔点为156.5-157.7℃,产品未达到美国药典的指标。Add 136.2g of p-tert-octylphenoxyethoxyethyldimethylamine obtained above into a 1L four-neck reaction bottle, add 100.2g methyl isobutyl ketone and 126.6g benzyl chloride in sequence, and heat to Reflux, react for 2 hours, slowly add 168.2g of cyclohexane, cool down for crystallization, collect 156.3g of solid, vacuum dry the filter cake at -0.098MPa, 35°C, and then crush the filter cake to obtain the benzethonium chloride product. Finally, 142.6g of light yellow product was obtained, with a two-step total yield of 68.9% and a purity of 97.60%. The melting point of the product was 156.5-157.7°C. The product did not meet the indicators of the United States Pharmacopoeia.

上述数据证实,现有合成技术的收率和含量都非常低,未能达到药典的要求。The above data confirm that the yield and content of existing synthesis technology are very low and fail to meet the requirements of the pharmacopoeia.

本发明并不局限于上述实施例,在本发明公开的技术方案的基础上,本领域的技术人员根据所公开的技术内容,不需要创造性的劳动就可以对其中的一些技术特征作出一些替换和变形,这些替换和变形均在本发明的保护范围内。The present invention is not limited to the above embodiments. On the basis of the technical solutions disclosed in the present invention, those skilled in the art can make some substitutions and modifications to some of the technical features without any creative work based on the disclosed technical content. Modifications, these substitutions and modifications are within the protection scope of the present invention.

Claims (9)

1.一种医药级苄索氯铵的制备方法,其特征在于,反应式如下:1. A preparation method of pharmaceutical grade benzethonium chloride, characterized in that the reaction formula is as follows: S1:S1: S2:S2: 制备方法包括如下步骤:The preparation method includes the following steps: S1:化合物3的制备S1: Preparation of compound 3 向反应釜内,氮气保护下加入对叔辛基苯氧基乙氧基乙基氯2、二甲胺的盐和催化剂,升温反应;将反应物搅拌反应完成后,静置分层得到有机层,使用油泵减压,通过分子蒸馏得到化合物3;Into the reaction kettle, add p-tert-octylphenoxyethoxyethyl chloride 2, dimethylamine salt and catalyst under nitrogen protection, and heat up the reaction; after the reactants are stirred and the reaction is completed, leave to stand and separate to form an organic layer. , use an oil pump to reduce pressure, and obtain compound 3 through molecular distillation; S2:化合物1的制备S2: Preparation of Compound 1 向反应釜内,氮气保护下加入化合物3和溶剂,进行脱色吸附,通过精密压滤器,压滤至季铵盐反应釜;Add compound 3 and solvent into the reaction kettle under nitrogen protection, perform decolorization and adsorption, and filter through a precision filter press into the quaternary ammonium salt reaction kettle; 向季铵盐反应釜内,氮气保护下通过精密过滤器抽入氯化苄,搅拌升温反应。将反应物搅拌反应完成后,反应液过滤所得的固体加入乙酸乙酯搅拌洗涤,所得固体减压下烘干得到化合物1。Into the quaternary ammonium salt reaction kettle, pump benzyl chloride through a precision filter under nitrogen protection, stir and heat up for reaction. After the reactants are stirred and the reaction is completed, the solid obtained by filtering the reaction solution is added to ethyl acetate for stirring and washing, and the solid obtained is dried under reduced pressure to obtain compound 1. 2.根据权利要求1所述的一种医药级苄索氯铵的制备方法,其特征在于,具体包括:2. a kind of preparation method of pharmaceutical grade benzethonium chloride according to claim 1, is characterized in that, specifically comprises: S1-1:化合物3的制备S1-1: Preparation of compound 3 向反应釜内,氮气保护下加入对叔辛基苯氧基乙氧基乙基氯2、二甲胺的盐和催化剂,升温反应,保持2-5h,控制对叔辛基苯氧基乙氧基乙基氯2的残留量≤3.0%时,反应结束;将反应物搅拌反应完成后,降温至35℃以下,加入乙酸乙酯,反应液静置分层,得有机层;Into the reaction kettle, add p-tert-octylphenoxyethoxyethyl chloride 2, dimethylamine salt and catalyst under nitrogen protection, heat up the reaction, keep for 2-5h, and control p-tert-octylphenoxyethoxyethyl chloride 2, dimethylamine salt and catalyst When the residual amount of ethyl chloride 2 is ≤3.0%, the reaction ends; after the reaction is stirred and the reaction is completed, the temperature is lowered to below 35°C, ethyl acetate is added, and the reaction solution is allowed to stand for layering to obtain an organic layer; S1-2:粗品蒸馏提纯S1-2: Crude distillation and purification 有机层使用油泵减压,蒸馏体系的真空度控制为0.01-1.0mbar,油浴温度160-180℃,刮膜器转速为200-300转/分钟,连续进料进行分子蒸馏得到化合物3;The organic layer is decompressed using an oil pump. The vacuum degree of the distillation system is controlled to 0.01-1.0 mbar. The oil bath temperature is 160-180°C. The film scraper speed is 200-300 rpm. The feed is continuously fed for molecular distillation to obtain compound 3; S2-1:化合物1的制备S2-1: Preparation of compound 1 化合物3的投料前处理:向反应釜内,氮气保护下加入化合物3和溶剂,搅拌升温至30-50℃之间,加入活性炭进行脱色至工艺规定时间,通过孔径小于45微米的精密压滤器,压滤至S2-2步骤进行反应。Pre-treatment of compound 3: Add compound 3 and solvent into the reaction kettle under nitrogen protection, stir and raise the temperature to between 30-50°C, add activated carbon to decolorize for the time specified in the process, and pass through a precision filter press with a pore size less than 45 microns. Press filtration to step S2-2 for reaction. S2-2:化合物1的制备S2-2: Preparation of compound 1 向反应釜内,氮气保护下加入S2-1的对叔辛基苯氧基乙氧基乙基二甲胺3溶液,然后通过精密过滤器抽入氯化苄,搅拌升温进行反应。保持反应至工艺规定时间,无需取样中控,结束反应。将反应液过滤,所得的固体加入乙酸乙酯搅拌洗涤,所得固体减压下烘干得到化合物1。Into the reaction kettle, add S2-1's p-tert-octylphenoxyethoxyethyldimethylamine 3 solution under nitrogen protection, then pump benzyl chloride through a precision filter, stir and heat to react. Keep the reaction until the time specified in the process, no need to take samples for in-process control, and end the reaction. The reaction solution was filtered, and the obtained solid was added to ethyl acetate, stirred and washed, and the obtained solid was dried under reduced pressure to obtain compound 1. 3.根据权利要求2所述的一种医药级苄索氯铵的制备方法,其特征在于,所述步骤S1-1中的式中,二甲基胺盐为二甲胺盐酸盐、二甲胺氢溴酸盐、二甲胺硫酸盐、二甲胺氢碘酸盐,优选二甲胺盐酸盐。3. The preparation method of a kind of pharmaceutical grade benzethonium chloride according to claim 2, characterized in that, in the formula in step S1-1, the dimethylamine salt is dimethylamine hydrochloride, dimethylamine hydrochloride, Methylamine hydrobromide, dimethylamine sulfate, dimethylamine hydroiodide, preferably dimethylamine hydrochloride. 4.根据权利要求2所述的一种医药级苄索氯铵的制备方法,其特征在于,所述步骤S1-1中的催化剂为包含氯化锂、溴化锂、溴化钾、溴化钠、溴化亚铜、碘化钠、碘化钾、碘化亚铜和钯催化剂中至少一种,优选为碘化钠和钯催化剂。4. the preparation method of a kind of pharmaceutical grade benzethonium chloride according to claim 2, is characterized in that, the catalyst in described step S1-1 is to comprise lithium chloride, lithium bromide, potassium bromide, sodium bromide, At least one of cuprous bromide, sodium iodide, potassium iodide, cuprous iodide and palladium catalyst, preferably sodium iodide and palladium catalyst. 5.根据权利要求4所述的一种医药级苄索氯铵的制备方法,其特征在于,所述步骤S1-1用的钯催化剂包括Pd(OAc)2,Pd2(dba)3,PdCl2(dppf),PdCl2(PPh3)2,PdCl2(PCy)2,PdCl2和PdCl2(CH3CN)2,优选为PdCl2(dppf)。5. The preparation method of a kind of pharmaceutical grade benzethonium chloride according to claim 4, characterized in that the palladium catalyst used in step S1-1 includes Pd(OAc) 2 , Pd 2 (dba) 3 , PdCl 2 (dppf), PdCl 2 (PPh3) 2 , PdCl 2 (PCy) 2 , PdCl 2 and PdCl 2 (CH 3 CN) 2 , preferably PdCl 2 (dppf). 6.根据权利要求2所述的一种医药级苄索氯铵的制备方法,其特征在于,步骤S1-2中的蒸馏方式为减压蒸馏、高真空精馏或分子蒸馏,优选为分子蒸馏。6. The preparation method of a kind of pharmaceutical grade benzethonium chloride according to claim 2, characterized in that the distillation mode in step S1-2 is vacuum distillation, high vacuum distillation or molecular distillation, preferably molecular distillation . 7.根据权利要求6所述的一种医药级苄索氯铵的制备方法,其特征在于,分子蒸馏时的绝对压力为0.005MPa-0.01MPa。7. The preparation method of pharmaceutical grade benzethonium chloride according to claim 6, characterized in that the absolute pressure during molecular distillation is 0.005MPa-0.01MPa. 8.根据权利要求2所述的一种医药级苄索氯铵的制备方法,其特征在于,步骤S2-1中的溶剂为乙酸乙酯、乙酸异丙酯、乙腈、丙酮或甲基异丁酮,优选乙酸乙酯。8. The preparation method of a kind of pharmaceutical grade benzethonium chloride according to claim 2, characterized in that the solvent in step S2-1 is ethyl acetate, isopropyl acetate, acetonitrile, acetone or methyl isobutyl Ketone, preferably ethyl acetate. 9.根据权利要求8所述的一种医药级苄索氯铵的制备方法,其特征在于,步骤S2-2中的反应温度为20-150℃,优选为40-60℃。9. The preparation method of pharmaceutical grade benzethonium chloride according to claim 8, characterized in that the reaction temperature in step S2-2 is 20-150°C, preferably 40-60°C.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN118084685A (en) * 2024-01-25 2024-05-28 江苏斯德瑞克化工有限公司 Preparation method of continuous pipelining benzethonium chloride
CN120607448A (en) * 2025-08-11 2025-09-09 潍坊汇韬化工有限公司 A method for continuously producing benzethonium chloride

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20030114533A1 (en) * 2000-05-16 2003-06-19 Klaus Raab Method for producing arylpoly(oxalkyl)-benzyldimethyl-ammonium derivatives
CN102993031A (en) * 2011-09-19 2013-03-27 北京桑普生物化学技术有限公司 Preparation process of aromatic polyoxyalkyl quaternary ammonium compound
CN109651177A (en) * 2018-12-20 2019-04-19 江西省隆南药化有限公司 Preparation method of benzethonium chloride
CN113372227A (en) * 2021-06-29 2021-09-10 扬州虹光生物科技有限公司 Synthesis process of high-purity benzethonium chloride
CN114805096A (en) * 2022-05-16 2022-07-29 扬州虹光生物科技有限公司 Production and preparation process of benzethonium chloride

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20030114533A1 (en) * 2000-05-16 2003-06-19 Klaus Raab Method for producing arylpoly(oxalkyl)-benzyldimethyl-ammonium derivatives
CN102993031A (en) * 2011-09-19 2013-03-27 北京桑普生物化学技术有限公司 Preparation process of aromatic polyoxyalkyl quaternary ammonium compound
CN109651177A (en) * 2018-12-20 2019-04-19 江西省隆南药化有限公司 Preparation method of benzethonium chloride
CN113372227A (en) * 2021-06-29 2021-09-10 扬州虹光生物科技有限公司 Synthesis process of high-purity benzethonium chloride
CN114805096A (en) * 2022-05-16 2022-07-29 扬州虹光生物科技有限公司 Production and preparation process of benzethonium chloride

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
罗代暄主编: "《化学试剂与精细化学品合成基础 有机分册》", 31 May 1991, 高等教育出版社, pages: 90 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN118084685A (en) * 2024-01-25 2024-05-28 江苏斯德瑞克化工有限公司 Preparation method of continuous pipelining benzethonium chloride
CN120607448A (en) * 2025-08-11 2025-09-09 潍坊汇韬化工有限公司 A method for continuously producing benzethonium chloride

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