CN116102436A - A new process for preparing serinol - Google Patents
A new process for preparing serinol Download PDFInfo
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- CN116102436A CN116102436A CN202211603827.2A CN202211603827A CN116102436A CN 116102436 A CN116102436 A CN 116102436A CN 202211603827 A CN202211603827 A CN 202211603827A CN 116102436 A CN116102436 A CN 116102436A
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
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- C07C213/00—Preparation of compounds containing amino and hydroxy, amino and etherified hydroxy or amino and esterified hydroxy groups bound to the same carbon skeleton
- C07C213/02—Preparation 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
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- C07C201/00—Preparation of esters of nitric or nitrous acid or of compounds containing nitro or nitroso groups bound to a carbon skeleton
- C07C201/06—Preparation of nitro compounds
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- C07C213/00—Preparation 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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Abstract
本发明涉及在催化氢化条件下,以2‑硝基‑1,3‑丙二醇钠盐为原料合成丝氨醇的新工艺。通过向反应中加入离子液体,减少了2‑硝基‑1,3‑丙二醇钠盐的分解,大大提高了丝氨醇的收率。该工艺不需要改变原有设备,几乎不产生副产物,更经济环保。The invention relates to a new process for synthesizing serinol by using 2-nitro-1,3-propanediol sodium salt as a raw material under catalytic hydrogenation conditions. By adding ionic liquid to the reaction, the decomposition of 2-nitro-1,3-propanediol sodium salt is reduced, and the yield of serinol is greatly improved. The process does not need to change the original equipment, produces almost no by-products, and is more economical and environmentally friendly.
Description
技术领域technical field
本发明属于医药化工领域,涉及一种在催化氢化反应中,提高丝胺醇收率的工艺。The invention belongs to the field of medicine and chemical industry, and relates to a technique for increasing the yield of serinol in a catalytic hydrogenation reaction.
背景技术Background technique
碘帕醇是放射科常用的一种非离子型水溶性造影剂,主要用于神经介入、冠状动脉造影、CT增强扫描及血管成像等。其主要优点是毒性作用低、过敏反应少、对肝肾功能影响不大,不容易产生对比剂肾病,因此碘帕醇市场需求量很大且逐年增加。碘帕醇的合成原料之一是丝氨醇,即2-氨基-1,3-丙二醇,降低丝氨醇的生产成本,将有助于降低碘帕醇的生产成本,因此开发经济环保的丝氨醇制备新工艺,具有重大的经济效益和社会效益。Iopamidol is a non-ionic water-soluble contrast agent commonly used in radiology department, mainly used in neurointervention, coronary angiography, enhanced CT scan and angiography. Its main advantages are low toxicity, less allergic reactions, little impact on liver and kidney functions, and less likely to cause contrast nephropathy. Therefore, the market demand for iopamidol is very large and is increasing year by year. One of the synthetic raw materials of iopamidol is serinol, i.e. 2-amino-1,3-propanediol, reducing the production cost of serinol will help to reduce the production cost of iopamidol, so the development of economical and environmentally friendly silk A new process for the preparation of amino alcohol has great economic and social benefits.
其中,碘帕醇的分子式为:Wherein, the molecular formula of iopamidol is:
其中,丝氨醇的分子式为:Wherein, the molecular formula of serinol is:
经检索发现(DE2742981、US4448999、US6509504、US4221740),一种制备丝氨醇的常用方法是:硝基甲烷与多聚甲醛在烧碱的作用下,生成2-硝基-1,3-丙二醇钠盐,后者经过催化氢化还原为丝氨醇,最后减压蒸馏即得。After searching, it was found (DE2742981, US4448999, US6509504, US4221740) that a common method for preparing serinol is: nitromethane and paraformaldehyde under the action of caustic soda to generate 2-nitro-1,3-propanediol sodium salt , the latter is reduced to serinol by catalytic hydrogenation, and finally obtained by distillation under reduced pressure.
该方法操作简单,所用原料价廉易得。然而,上述方法中,催化氢化2-硝基-1,3-丙二醇钠盐制备丝氨醇的收率不高且不稳定,主要原因是这一步反应产生了大量的副产物。为了提高丝氨醇的收率,必须继续开发能够减少副产物生成的新工艺。为了确定副产物产生的途径,首先利用核磁共振碳谱技术分析蒸馏釜中残留的大量高沸点物质的结构,并与推测物质标准谱图对比,确定为三羟甲基氨基甲烷,即2-氨基-2-羟甲基-1,3-丙二醇(图1)。根据该副产物的结构,推测其产生途径为:(1)2-硝基-1,3-丙二醇钠盐I分解为2-硝基乙醇钠盐II和甲醛(Russian chemical Bulletin,2009,58(10),2063-2069;2011,60(8),1703-1711);(2)甲醛与2-硝基-1,3-丙二醇钠盐I进一步发生加成反应生成三羟甲基硝基甲烷III;(3)三羟甲基硝基甲烷III在催化氢化条件下还原为副产物三羟甲基氨基甲烷IV,从而造成丝氨醇收率不高。由于2-硝基-1,3-丙二醇钠盐的分解程度不同,使得每批丝氨醇的收率不稳定。The method is simple to operate, and the raw materials used are cheap and easy to obtain. However, in the above method, the yield of serinol prepared by catalytic hydrogenation of 2-nitro-1,3-propanediol sodium salt is not high and unstable, mainly because a large amount of by-products are produced in this step reaction. In order to increase the yield of serinol, new processes that can reduce the formation of by-products must continue to be developed. In order to determine the way of by-products, first use carbon nuclear magnetic resonance spectroscopy to analyze the structure of a large number of high-boiling substances remaining in the still, and compare it with the standard spectrum of the presumed substance, and determine that it is trishydroxymethylaminomethane, that is, 2-amino -2-Hydroxymethyl-1,3-propanediol (Figure 1). According to the structure of this by-product, it is inferred that its production route is: (1) 2-nitro-1,3-propanediol sodium salt I is decomposed into 2-nitroethanol sodium salt II and formaldehyde (Russian chemical Bulletin, 2009,58( 10), 2063-2069; 2011, 60(8), 1703-1711); (2) Further addition reaction between formaldehyde and 2-nitro-1,3-propanediol sodium salt I to generate trimethylolnitromethane III; (3) Trimethylolnitromethane III is reduced to by-product trishydroxymethylaminomethane IV under catalytic hydrogenation conditions, resulting in a low yield of serinol. The yield of each batch of serinol was unstable due to the different degrees of decomposition of the sodium salt of 2-nitro-1,3-propanediol.
其中,所述三羟甲基氨基甲烷产生的反应式为:Wherein, the reaction formula that described trishydroxymethylaminomethane produces is:
发明内容Contents of the invention
本发明的目的在于提供一种不需要改变现有设备,更经济环保的丝氨醇制备新工艺。The purpose of the present invention is to provide a new process for preparing serinol which is more economical and environment-friendly without changing the existing equipment.
为实现上述目的,本发明采用的新工艺是向2-硝基-1,3-丙二醇钠盐的催化氢化反应中加入离子液体,降低2-硝基-1,3-丙二醇钠盐的分解率,从而在不改变现有设备情况下,大大提高丝氨醇的收率。本发明采取的技术方案具体如下。In order to achieve the above object, the new technology adopted in the present invention is to add ionic liquid to the catalytic hydrogenation reaction of 2-nitro-1,3-propanediol sodium salt to reduce the decomposition rate of 2-nitro-1,3-propanediol sodium salt , thus greatly increasing the yield of serinol without changing the existing equipment. The technical scheme adopted by the present invention is specifically as follows.
一种丝氨醇的制备方法,以甲醇为溶剂,烧碱作用下,硝基甲烷与多聚甲醛发生加成反应,所得加成产物加氢还原为丝氨醇,最后经过高真空蒸馏提纯,具体步骤如下:A preparation method of serinol, using methanol as a solvent, under the action of caustic soda, addition reaction of nitromethane and paraformaldehyde occurs, the obtained addition product is hydrogenated and reduced to serinol, and finally purified by high vacuum distillation, specifically Proceed as follows:
步骤1:制备2-硝基-1,3-丙二醇钠盐Step 1: Preparation of 2-nitro-1,3-propanediol sodium salt
向甲醇中,依次加入硝基甲烷、多聚甲醛、烧碱溶液,控制反应温度25℃-30℃,过滤得到2-硝基-1,3-丙二醇钠盐滤饼。Add nitromethane, paraformaldehyde, and caustic soda solution to methanol in sequence, control the reaction temperature at 25°C-30°C, and filter to obtain 2-nitro-1,3-propanediol sodium salt filter cake.
步骤2:制备丝氨醇Step 2: Prepare Serinol
向甲醇中,依次加入步骤1制得的2-硝基-1,3-丙二醇钠盐滤饼、氯化铵、离子液体和钯/碳,通入氢气,反应温度为15℃-20℃,反应时间48小时,过滤出催化剂,制得丝氨醇溶液。To methanol, sequentially add the 2-nitro-1,3-propanediol sodium salt filter cake, ammonium chloride, ionic liquid and palladium/carbon prepared in step 1, and pass in hydrogen, and the reaction temperature is 15°C-20°C, The reaction time was 48 hours, and the catalyst was filtered out to obtain a serinol solution.
其中,离子液体加入量为2-硝基-1,3-丙二醇钠盐滤饼质量的0.5%-10%,优选为3%-10%,更优选为6%。Wherein, the addition amount of the ionic liquid is 0.5%-10% of the mass of the 2-nitro-1,3-propanediol sodium salt filter cake, preferably 3%-10%, more preferably 6%.
步骤3:高真空蒸馏提纯Step 3: Purification by high vacuum distillation
将步骤2得到的丝氨醇甲醇溶液,在高真空状态下,先蒸除甲醇,再蒸出丝氨醇。The methanol solution of serinol obtained in
采用本发明所述催化氢化合成丝氨醇的技术,所得丝氨醇的产率高且稳定,不改变现有设备,降低了生产成本。By adopting the technology for synthesizing serinol by catalytic hydrogenation of the present invention, the yield of the obtained serinol is high and stable, the existing equipment is not changed, and the production cost is reduced.
四、具体实施方式4. Specific implementation
实施例1Example 1
步骤1:制备2-硝基-1,3-丙二醇钠盐Step 1: Preparation of 2-nitro-1,3-propanediol sodium salt
向三颈烧瓶中依次加入甲醇0.5L,硝基甲烷100g、多聚甲醛103g,开启搅拌,待完全解聚后,向反应瓶中滴加30%氢氧化钠溶液240g,控制滴加速度,使反应温度保持在25℃-30℃,滴加完毕,保温1小时,过滤甩干得到2-硝基-1,3-丙二醇钠盐253g。Add 0.5L of methanol, 100g of nitromethane, and 103g of paraformaldehyde in the three-necked flask successively, start stirring, and after complete depolymerization, add 240g of 30% sodium hydroxide solution dropwise in the reaction flask, control the rate of addition, and make the reaction The temperature was kept at 25°C-30°C. After the dropwise addition was completed, the mixture was kept for 1 hour, filtered and dried to obtain 253g of 2-nitro-1,3-propanediol sodium salt.
步骤2:催化还原制备丝氨醇Step 2: Preparation of Serinol by Catalytic Reduction
向反应釜中加入0.8L甲醇、2-硝基-1,3-丙二醇钠盐253g、氯化铵100g、离子液体15g和5%钯/碳12.6g,通入氢气,氢气压力为1MPa,15-20℃保温48小时,制得丝氨醇甲醇溶液。过滤出钯/碳,清洗后重复使用。Add 0.8L of methanol, 253g of 2-nitro-1,3-propanediol sodium salt, 100g of ammonium chloride, 15g of ionic liquid, and 12.6g of 5% palladium/carbon into the reaction kettle, and feed hydrogen with a pressure of 1MPa, 15 Incubate at -20°C for 48 hours to prepare a serinol methanol solution. The palladium/carbon was filtered off, washed and reused.
步骤3:高真空蒸馏提纯Step 3: Purification by high vacuum distillation
将步骤2中制备的丝氨醇甲醇溶液,常压回收甲醇,然后减压蒸馏,得到丝氨醇纯品138g,收率为92.6%。The methanol solution of serinol prepared in
实施例2Example 2
离子液体加入量改为2-硝基-1,3-丙二醇钠盐质量的0.5%,其余条件同实施例1,丝氨醇收率为79.8%。The amount of ionic liquid added was changed to 0.5% of the mass of 2-nitro-1,3-propanediol sodium salt, and other conditions were the same as in Example 1, and the yield of serinol was 79.8%.
实施例3Example 3
离子液体加入量改为2-硝基-1,3-丙二醇钠盐质量的3%,其余条件同实施例1,丝氨醇收率为85.8%。The amount of ionic liquid added was changed to 3% of the mass of 2-nitro-1,3-propanediol sodium salt, and other conditions were the same as in Example 1, and the yield of serinol was 85.8%.
实施例4Example 4
离子液体加入量改为2-硝基-1,3-丙二醇钠盐质量的10%,其余条件同实施例1,丝氨醇收率为87.2%。The amount of ionic liquid added was changed to 10% of the mass of 2-nitro-1,3-propanediol sodium salt, and other conditions were the same as in Example 1, and the yield of serinol was 87.2%.
需要说明的是,上述发明内容及具体实施方式意在证明本发明所提供技术方案的实际应用,不应解释为对本发明保护范围的限定。本领域技术人员在本发明的精神和原理内,当可作各种修改、等同替换、或改进。本发明的保护范围以所附权利要求书为准。It should be noted that the above summary of the invention and specific implementation methods are intended to demonstrate the practical application of the technical solution provided by the present invention, and should not be construed as limiting the protection scope of the present invention. Those skilled in the art may make various modifications, equivalent replacements, or improvements within the spirit and principles of the present invention. The protection scope of the present invention shall be determined by the appended claims.
附图说明:Description of drawings:
图1为副产物三羟甲基氨基甲烷的碳谱。Figure 1 is the carbon spectrum of the by-product trishydroxymethylaminomethane.
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Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4221740A (en) * | 1977-09-21 | 1980-09-09 | Schering Aktiengesellschaft | Process for the preparation of serinol (1,3-dihydroxy-2-aminopropane) |
| US4448999A (en) * | 1981-07-30 | 1984-05-15 | Dynamit Nobel Aktiengesellschaft | Process for the preparation of 2-aminopropanediol-1,3(serinol) |
| EP0436414A1 (en) * | 1990-01-03 | 1991-07-10 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Process for the preparation of 2-amino-1,3-propanediol and its salts |
| WO2000053567A1 (en) * | 1999-03-09 | 2000-09-14 | Sk Corporation | Method for the production of serinol |
| CN1948272A (en) * | 2006-10-31 | 2007-04-18 | 江苏省原子医学研究所 | Preparation method of serinol |
| CN101767017A (en) * | 2009-01-04 | 2010-07-07 | 中国科学院成都有机化学有限公司 | Preparation of carbon-supported palladium alloy hydrogenated catalyst and technical technology of palladium extraction and recovery |
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- 2022-12-13 CN CN202211603827.2A patent/CN116102436A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4221740A (en) * | 1977-09-21 | 1980-09-09 | Schering Aktiengesellschaft | Process for the preparation of serinol (1,3-dihydroxy-2-aminopropane) |
| US4448999A (en) * | 1981-07-30 | 1984-05-15 | Dynamit Nobel Aktiengesellschaft | Process for the preparation of 2-aminopropanediol-1,3(serinol) |
| EP0436414A1 (en) * | 1990-01-03 | 1991-07-10 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Process for the preparation of 2-amino-1,3-propanediol and its salts |
| WO2000053567A1 (en) * | 1999-03-09 | 2000-09-14 | Sk Corporation | Method for the production of serinol |
| CN1948272A (en) * | 2006-10-31 | 2007-04-18 | 江苏省原子医学研究所 | Preparation method of serinol |
| CN101767017A (en) * | 2009-01-04 | 2010-07-07 | 中国科学院成都有机化学有限公司 | Preparation of carbon-supported palladium alloy hydrogenated catalyst and technical technology of palladium extraction and recovery |
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