[go: up one dir, main page]

CN115974756A - A kind of purification method of melatonin and its crystallization mother liquor - Google Patents

A kind of purification method of melatonin and its crystallization mother liquor Download PDF

Info

Publication number
CN115974756A
CN115974756A CN202310012510.XA CN202310012510A CN115974756A CN 115974756 A CN115974756 A CN 115974756A CN 202310012510 A CN202310012510 A CN 202310012510A CN 115974756 A CN115974756 A CN 115974756A
Authority
CN
China
Prior art keywords
melatonin
mother liquor
crystallization mother
purifying
crystallization
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN202310012510.XA
Other languages
Chinese (zh)
Other versions
CN115974756B (en
Inventor
邱语康
罗华东
李安冰
罗奕火
肖艳梅
黄成裕
陈建明
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shaanxi Jianhe Biotechnology Co ltd
Fujian Kehong Biological Engineering Co ltd
Original Assignee
Shaanxi Jianhe Biotechnology Co ltd
Fujian Kehong Biological Engineering Co ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shaanxi Jianhe Biotechnology Co ltd, Fujian Kehong Biological Engineering Co ltd filed Critical Shaanxi Jianhe Biotechnology Co ltd
Priority to CN202310012510.XA priority Critical patent/CN115974756B/en
Publication of CN115974756A publication Critical patent/CN115974756A/en
Application granted granted Critical
Publication of CN115974756B publication Critical patent/CN115974756B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Indole Compounds (AREA)

Abstract

本发明公开了一种褪黑素及其结晶母液的提纯方法,通过乙醇提纯过程中加入除氧水、全程充氮保护,极大地提高了褪黑素的纯度和回收率;并且,结晶母液通过碱解将褪黑素及其自缩合杂质还原成合成前体5‑甲氧基色胺,合成前体进行酰化得到与褪黑素粗品纯度相当的母液物料产品,不仅能够有效提高母液中褪黑素的回收率和总提纯收率,而且降低了最终母液的处理量,减轻了三废处理压力,有利于增大产品的竞争力。

Figure 202310012510

The invention discloses a method for purifying melatonin and its crystallization mother liquor. The purity and recovery rate of melatonin are greatly improved by adding deoxygenated water and full nitrogen protection during the ethanol purification process; and the crystallization mother liquor is passed through Alkaline hydrolysis reduces melatonin and its self-condensed impurities to the synthetic precursor 5-methoxytryptamine, and the synthetic precursor is acylated to obtain a mother liquor material product with a purity equivalent to that of the crude melatonin, which can not only effectively improve the melatonin in the mother liquor The recovery rate and total purification yield of the element are improved, and the treatment volume of the final mother liquor is reduced, the pressure of the three wastes treatment is reduced, and it is beneficial to increase the competitiveness of the product.

Figure 202310012510

Description

一种褪黑素及其结晶母液的提纯方法A kind of purification method of melatonin and its crystallization mother liquor

技术领域technical field

本发明涉及化工分离技术领域,尤其涉及一种褪黑素及其结晶母液的提纯方法。The invention relates to the technical field of chemical separation, in particular to a method for purifying melatonin and its crystallization mother liquor.

背景技术Background technique

褪黑素又称松果体素、褪黑激素,具有强大的神经内分泌免疫调节活性和清除自由基抗氧化能力,是迄今为止发现最强的内源性自由基清除剂;在防止病变、调节昼夜节律、推迟老化方面具有显著作用,同时,褪黑素对中枢神经系统、免疫系统、心血管系统具有明显的调节作用。Melatonin, also known as pineal gland and melatonin, has strong neuroendocrine immune regulation activity and free radical scavenging antioxidant capacity, and is the strongest endogenous free radical scavenger found so far; Circadian rhythm and delaying aging have significant effects. At the same time, melatonin has obvious regulatory effects on the central nervous system, immune system, and cardiovascular system.

褪黑素具有多种的化学合成方法,较优良的路线最终是以5-甲氧基色胺为原料,经过酰化反应得到褪黑素粗品,褪黑素粗品经过重结晶后而得到精品褪黑素。目前,工业生产中褪黑素的结晶方法主要以乙醇为溶剂进行结晶,而结晶的过程必然产生母液。现有技术对于褪黑素的提纯处理,大多采用乙醇作为溶剂,但提纯收率较低。为此,也有采用乙醇水溶液,如使用浓度为15~20%的乙醇水溶液对褪黑素粗品进行提纯,提纯收率为90~93%,产品纯度可以达到99.5%以上,但是保留时间为12.398分钟出峰的杂质含量为0.13%,超过了USP≤0.1%的要求,不符合USP43标准;且使用浓度过低的乙醇水溶液,针对后续母液处理量大,处理能耗高。又如,采用动物的松果体来提取结晶母液中的褪黑素,但原料动物的松果体来源是最大的问题。Melatonin has a variety of chemical synthesis methods, and the better route is finally to use 5-methoxytryptamine as raw material to obtain crude melatonin through acylation reaction, and the crude melatonin is recrystallized to obtain fine melatonin white. At present, the crystallization method of melatonin in industrial production mainly uses ethanol as a solvent for crystallization, and the crystallization process will inevitably produce mother liquor. For the purification treatment of melatonin in the prior art, ethanol is mostly used as a solvent, but the purification yield is low. For this reason, there is also the use of ethanol aqueous solution, such as the use of 15-20% ethanol aqueous solution to purify the crude melatonin, the purification yield is 90-93%, and the product purity can reach more than 99.5%, but the retention time is 12.398 minutes The impurity content of the peak is 0.13%, which exceeds the requirement of USP ≤ 0.1%, and does not meet the USP43 standard; and the use of ethanol aqueous solution with too low concentration will cause a large amount of subsequent mother liquor treatment and high energy consumption. As another example, the pineal gland of animals is used to extract melatonin in the crystallization mother liquor, but the source of the pineal gland of the raw material animal is the biggest problem.

此外,现有褪黑素提纯技术中所采用的乙醇溶剂,由于褪黑素在乙醇中的溶解度比较大,且褪黑素乙醇母液在浓缩过程中会发生分解,产生一种无法通过乙醇提纯的自缩合杂质,造成单杂>0.1%(USP43标准:单杂≤0.1%),未达到USP标准。因此,如何提取溶解在乙醇母液中的褪黑素,将是提高褪黑素提纯技术总收率的关键所在。同时,如何去除褪黑素乙醇母液浓缩中产生的自缩合杂质,以提高从母液中提取褪黑素的纯度,将有利于增大产品的竞争力。In addition, the ethanol solvent used in the existing melatonin purification technology, due to the relatively high solubility of melatonin in ethanol, and the ethanol mother liquor of melatonin will decompose during the concentration process, resulting in a melatonin that cannot be purified by ethanol Self-condensation impurities, resulting in simple impurities > 0.1% (USP43 standard: simple impurities ≤ 0.1%), which did not reach the USP standard. Therefore, how to extract the melatonin dissolved in the ethanol mother liquor will be the key to improving the total yield of the melatonin purification technology. At the same time, how to remove the self-condensation impurities produced in the concentration of melatonin ethanol mother liquor will help increase the competitiveness of the product to improve the purity of melatonin extracted from the mother liquor.

发明内容Contents of the invention

本发明的目的在于克服现有技术的不足,提供一种褪黑素及其结晶母液的提纯方法,以解决目前褪黑素乙醇提纯过程收率偏低、结晶母液中褪黑素残留较大,且母液处理过程造成褪黑素自缩合带来的杂质等问题。The purpose of the present invention is to overcome the deficiencies in the prior art, to provide a method for purifying melatonin and its crystallization mother liquor, to solve the low yield of melatonin ethanol purification process, the relatively large residual melatonin in the crystallization mother liquor, Moreover, the mother liquor treatment process causes problems such as impurities caused by the self-condensation of melatonin.

本发明的目的通过以下技术方案予以实现:The purpose of the present invention is achieved through the following technical solutions:

本发明提供的一种褪黑素及其结晶母液的提纯方法,包括以下步骤:A method for purifying melatonin and its crystallization mother liquor provided by the invention comprises the following steps:

(1)褪黑素粗品提纯(1) Purification of crude melatonin

(1-1)将褪黑素粗品与浓度为30~95%的乙醇水溶液,按照质量比褪黑素粗品∶乙醇水溶液=1∶1~5进行混合而得到溶解液,其中乙醇水溶液中所用水为除氧水;优选地,乙醇水溶液浓度为40~60%,按照质量比褪黑素粗品∶乙醇水溶液=1∶2~3;(1-1) The crude melatonin is mixed with the aqueous ethanol solution with a concentration of 30-95% according to the mass ratio of crude melatonin: aqueous ethanol=1:1-5 to obtain a solution, wherein the aqueous ethanol uses water It is deoxygenated water; preferably, the concentration of ethanol aqueous solution is 40-60%, according to the mass ratio of melatonin crude product: ethanol aqueous solution=1: 2-3;

(1-2)在所述溶解液中加入用量为褪黑素粗品1~3wt%的活性炭,以氮气置换体系空气,升温至50~75℃溶解脱色后得到的脱色液,经过滤分离活性炭而得到褪黑素过滤液;(1-2) Add active carbon with an amount of 1 to 3 wt% of crude melatonin to the dissolving liquid, replace the air in the system with nitrogen, heat up to 50 to 75° C. to dissolve the decolorized solution obtained after decolorization, and separate the active carbon by filtration to obtain Obtain melatonin filtrate;

(1-3)所述褪黑素过滤液以10℃/h的速率降温至-10~10℃后继续结晶4~8h得到的结晶液,经离心分离后得到褪黑素精品湿料和褪黑素结晶母液;所述褪黑素精品湿料经真空烘干后得到褪黑素精品;优选地,降温至0~5℃;(1-3) The melatonin filtrate is cooled to -10-10°C at a rate of 10°C/h, and then the crystallization liquid obtained by continuing to crystallize for 4-8 hours is centrifuged to obtain melatonin fine-quality wet material and melatonin Melatonin crystallization mother liquor; the melatonin refined product wet material is vacuum-dried to obtain the melatonin refined product; preferably, the temperature is lowered to 0-5°C;

(2)褪黑素结晶母液处理(2) Melatonin crystallization mother liquor treatment

(2-1)将所述褪黑素结晶母液与碱性催化剂混合,控制体系pH值为10~14,在60~80℃温度下回流2~8h得到碱解液;(2-1) Mix the melatonin crystallization mother liquor with an alkaline catalyst, control the pH value of the system to 10-14, and reflux at a temperature of 60-80° C. for 2-8 hours to obtain an alkaline hydrolysis solution;

(2-2)将所述碱解液真空浓缩析出固体馏分,加入酸调节至pH值为1~4,优选地,pH值为1~2,搅拌至固体完全溶解后得到酸化液;(2-2) Concentrating the alkali hydrolysis solution in vacuum to separate solid fractions, adding acid to adjust the pH value to 1-4, preferably, the pH value is 1-2, and stirring until the solid is completely dissolved to obtain an acidified solution;

(2-3)在所述酸化液中加入用量为酸化液0.1~0.3wt%的活性炭进行脱色得到的脱色液,经分离活性炭而得到过滤液;(2-3) adding activated carbon in an amount of 0.1 to 0.3 wt% of the acidified solution to the acidified solution to decolorize the obtained decolorized solution, and separating the activated carbon to obtain a filtrate;

(2-4)在所述过滤液中加入碱调节pH值为10~14,优选地,pH值为12~13,离心分离后得到褪黑素前体5-甲氧基色胺,经酰化后得到纯度>99.5%的母液物料;所述母液物料循环加入褪黑素粗品中进行提纯。(2-4) Add alkali to the filtrate to adjust the pH value to 10-14, preferably, the pH value is 12-13, obtain the melatonin precursor 5-methoxytryptamine after centrifugation, and acylate Afterwards, a mother liquor material with a purity of >99.5% is obtained; the mother liquor material is recycled and added to crude melatonin for purification.

进一步地,本发明所述步骤(2-1)中碱性催化剂为氢氧化钠、氢氧化钾、甲醇钠、叔丁醇钠、三乙胺;优选地,体系pH值为12~13,回流温度为70~75℃,回流时间为4~5h;Further, the basic catalyst in the step (2-1) of the present invention is sodium hydroxide, potassium hydroxide, sodium methoxide, sodium tert-butoxide, triethylamine; preferably, the pH value of the system is 12-13, and the reflux The temperature is 70~75℃, and the reflux time is 4~5h;

上述方案中,本发明所述步骤(1-1)褪黑素粗品的纯度为99.50%以上。所述步骤(1-3)褪黑素精品的纯度为99.70%以上、单杂0.05%以下,收率为88%以上。所述步骤(2-4)母液物料的纯度为99.50%以上。In the above scheme, the purity of the crude melatonin in step (1-1) of the present invention is above 99.50%. The purity of the refined melatonin in the step (1-3) is more than 99.70%, less than 0.05% of simple impurities, and the yield is more than 88%. The purity of the mother liquor material in the step (2-4) is above 99.50%.

本发明具有以下有益效果:The present invention has the following beneficial effects:

(1)在褪黑素的提纯过程中,现有技术多采用乙醇作为溶剂,褪黑素在乙醇中的溶解度较大,最高可达20%左右,因此提纯收率较低。本发明通过在提纯过程中加入除氧水,全程氮气保护,由于褪黑素在水中微溶,可降低褪黑素在乙醇中的溶解度,从而降低褪黑素在结晶母液中的含量,有助于大大提高褪黑素提纯技术中的回收率;同时,通过降低提纯体系中的氧含量,减小了提纯过程中产生的自缩合杂质,有助于提高褪黑素精品的纯度,使得褪黑素精品的纯度均达到99.7%以上,单杂<0.1%。(1) In the purification process of melatonin, ethanol is mostly used as a solvent in the prior art, and the solubility of melatonin in ethanol is relatively large, up to about 20%, so the purification yield is low. In the present invention, by adding deoxygenated water in the purification process and nitrogen protection throughout the whole process, since melatonin is slightly soluble in water, the solubility of melatonin in ethanol can be reduced, thereby reducing the content of melatonin in the crystallization mother liquor, which helps It is used to greatly improve the recovery rate of melatonin purification technology; at the same time, by reducing the oxygen content in the purification system, it reduces the self-condensation impurities generated during the purification process, which helps to improve the purity of melatonin products and makes melatonin The purity of the prime products is above 99.7%, and the purity of simple and impurity is less than 0.1%.

(2)本发明通过碱解还原的方式,将褪黑素结晶母液中的褪黑素及其自缩合杂质还原成褪黑素合成前体5-甲氧基色胺,合成前体经过酸化、碱中等二次提纯,最后进行酰化得到与褪黑素粗品纯度相当的母液物料,母液物料纯度可达99.5%以上,提高了母液中褪黑素的回收率,总提纯收率可达95%以上,并降低了母液处理量,减轻三废处理压力。(2) The present invention reduces melatonin and its self-condensed impurities in the melatonin crystallization mother liquor to melatonin synthesis precursor 5-methoxytryptamine by means of alkaline hydrolysis reduction, and the synthesis precursor is acidified, alkali Medium secondary purification, and finally carry out acylation to obtain the mother liquor material with the same purity as the crude melatonin. The purity of the mother liquor material can reach more than 99.5%, which improves the recovery rate of melatonin in the mother liquor, and the total purification yield can reach more than 95%. , and reduced the amount of mother liquor treatment, reducing the pressure on the treatment of three wastes.

附图说明Description of drawings

下面将结合实施例和附图对本发明作进一步的详细描述:The present invention will be described in further detail below in conjunction with embodiment and accompanying drawing:

图1是本发明实施例的处理工艺流程图;Fig. 1 is the processing flow chart of the embodiment of the present invention;

图2是本发明实施例一的褪黑素精品纯度检测图谱;Fig. 2 is the melatonin high-quality goods purity detection collection of illustrative plates of the embodiment of the present invention;

图3是本发明实施例一的褪黑素结晶母液处理后所得母液物料纯度检测图谱;Fig. 3 is the detection spectrum of the material purity of the mother liquor obtained after the treatment of the melatonin crystallization mother liquor of Embodiment 1 of the present invention;

图4是褪黑素结晶母液按照现有技术(浓缩、结晶、重结晶)得到的母液物料纯度检测图谱。Fig. 4 is the detection spectrum of the material purity of the mother liquor obtained by the prior art (concentration, crystallization, recrystallization) of the melatonin crystallization mother liquor.

具体实施方式Detailed ways

实施例一:Embodiment one:

本实施例一种褪黑素及其结晶母液的提纯方法,如图1所示,其步骤如下:A kind of purification method of melatonin and crystallization mother liquor thereof of the present embodiment, as shown in Figure 1, its steps are as follows:

(1)褪黑素粗品提纯(1) Purification of crude melatonin

(1-1)将纯度为99.63%的褪黑素粗品300g,与浓度为40%的乙醇水溶液900g进行混合而得到溶解液,其中乙醇水溶液中所用水为除氧水;(1-1) 300 g of crude melatonin with a purity of 99.63% was mixed with 900 g of a 40% aqueous ethanol solution to obtain a solution, wherein the water used in the aqueous ethanol solution was deoxygenated water;

(1-2)在上述溶解液中加入5g活性炭,以氮气置换体系空气,升温至70℃溶解脱色30min后得到的脱色液,经过滤分离活性炭而得到褪黑素过滤液;(1-2) Add 5 g of activated carbon to the above solution, replace the air in the system with nitrogen, heat up to 70° C. to dissolve the decolorized solution obtained after 30 minutes of decolorization, and separate the activated carbon by filtration to obtain the melatonin filtrate;

(1-3)上述褪黑素过滤液以10℃/h的速率降温至5℃后继续结晶4h得到的结晶液,经离心分离后得到褪黑素精品湿料280g和褪黑素结晶母液913g;褪黑素精品湿料经真空烘干后得到纯度为99.87%、单杂0.04%(见图2)的褪黑素精品273g,收率为91.0%;(1-3) The above-mentioned melatonin filtrate was cooled to 5°C at a rate of 10°C/h, and then the crystallization liquid obtained by continuing to crystallize for 4 hours was centrifuged to obtain 280g of melatonin high-quality wet material and 913g of melatonin crystallization mother liquor The melatonin high-quality goods wet material obtains the melatonin high-quality goods 273g that purity is 99.87%, single impurity 0.04% (seeing Fig. 2) after vacuum drying, and yield is 91.0%;

(2)褪黑素结晶母液处理(2) Melatonin crystallization mother liquor treatment

(2-1)将上述褪黑素结晶母液与甲醇钠混合,控制体系pH值为12,在70℃温度下回流4h得到碱解液;(2-1) Mix the above-mentioned melatonin crystallization mother liquor with sodium methoxide, control the pH value of the system to 12, and reflux at a temperature of 70°C for 4 hours to obtain an alkaline solution;

(2-2)将上述碱解液真空浓缩得到固体馏分411g,加入酸调节至pH值为2,搅拌20min至固体完全溶解后得到酸化液;(2-2) Vacuum-concentrate the alkaline solution to obtain 411 g of solid fraction, add acid to adjust the pH value to 2, stir for 20 minutes until the solid is completely dissolved, and then obtain the acidified solution;

(2-3)在上述酸化液中加入0.5g活性炭进行脱色得到的脱色液,经分离活性炭而得到过滤液;(2-3) adding 0.5 g of activated carbon to the above-mentioned acidified solution to decolorize the decolorized solution obtained, and obtain the filtrate through separation of the activated carbon;

(2-4)在上述过滤液中加入碱调节pH值为12,离心分离后得到褪黑素前体5-甲氧基色胺18g,经酰化后得到纯度为99.57%的母液物料18.7g,该母液物料循环加入褪黑素粗品中进行提纯。(2-4) Add alkali to the above-mentioned filtrate to adjust the pH to 12, obtain 18 g of melatonin precursor 5-methoxytryptamine after centrifugation, and obtain 18.7 g of mother liquor material with a purity of 99.57% after acylation, The mother liquor material is recycled and added to the crude melatonin for purification.

实施例二:Embodiment two:

本实施例一种褪黑素及其结晶母液的提纯方法,如图1所示,其步骤如下:A kind of purification method of melatonin and crystallization mother liquor thereof of the present embodiment, as shown in Figure 1, its steps are as follows:

(1)褪黑素粗品提纯(1) Purification of crude melatonin

(1-1)将纯度为99.58%的褪黑素粗品300g,与浓度为50%的乙醇水溶液720g进行混合而得到溶解液,其中乙醇水溶液中所用水为除氧水;(1-1) 300 g of crude melatonin with a purity of 99.58% was mixed with 720 g of a 50% aqueous ethanol solution to obtain a solution, wherein the water used in the aqueous ethanol solution was deoxygenated water;

(1-2)在上述溶解液中加入5g活性炭,以氮气置换体系空气,升温至65℃溶解脱色30min后得到的脱色液,经过滤分离活性炭而得到褪黑素过滤液;(1-2) Add 5 g of activated carbon to the above solution, replace the air in the system with nitrogen, heat up to 65° C. to dissolve the decolorized solution obtained after decolorization for 30 minutes, and separate the activated carbon by filtration to obtain the melatonin filtrate;

(1-3)上述褪黑素过滤液以10℃/h的速率降温至0℃后继续结晶5h得到的结晶液,经离心分离后得到褪黑素精品湿料272g和褪黑素结晶母液729g;褪黑素精品湿料经真空烘干后得到纯度为99.81%、单杂0.03%的褪黑素精品268g,收率为89.3%;(1-3) The above-mentioned melatonin filtrate was cooled to 0°C at a rate of 10°C/h, and then the crystallization liquid obtained by continuing to crystallize for 5 hours was centrifuged to obtain 272g of melatonin high-quality wet material and 729g of melatonin crystallization mother liquor 268g of melatonin fine-quality product with a purity of 99.81% and 0.03% of simple impurities were obtained after vacuum drying the wet material of melatonin fine-quality product, and the yield was 89.3%;

(2)褪黑素结晶母液处理(2) Melatonin crystallization mother liquor treatment

(2-1)将上述褪黑素结晶母液与叔丁醇钠混合,控制体系pH值为13,在75℃温度下回流4h得到碱解液;(2-1) Mix the above-mentioned melatonin crystallization mother liquor with sodium tert-butoxide, control the pH value of the system to 13, and reflux at a temperature of 75° C. for 4 hours to obtain an alkaline solution;

(2-2)将上述碱解液真空浓缩得到固体馏分380g,加入酸调节至pH值为1,搅拌20min至固体完全溶解后得到酸化液;(2-2) Vacuum-concentrate the alkaline solution to obtain 380 g of solid fraction, add acid to adjust the pH value to 1, stir for 20 minutes until the solid is completely dissolved, and then obtain the acidified solution;

(2-3)在上述酸化液中加入0.5g活性炭进行脱色得到的脱色液,经分离活性炭而得到过滤液;(2-3) adding 0.5 g of activated carbon to the above-mentioned acidified solution to decolorize the decolorized solution obtained, and obtain the filtrate through separation of the activated carbon;

(2-4)在上述过滤液中加入碱调节pH值为13,离心分离后得到褪黑素前体5-甲氧基色胺21.8g,经酰化后得到纯度为99.62%的母液物料22.5g,该母液物料循环加入褪黑素粗品中进行提纯。(2-4) Add alkali to the above filtrate to adjust the pH value to 13, obtain 21.8 g of melatonin precursor 5-methoxytryptamine after centrifugation, and obtain 22.5 g of mother liquor material with a purity of 99.62% after acylation , the mother liquor material is recycled into the crude melatonin for purification.

实施例三:Embodiment three:

本实施例一种褪黑素及其结晶母液的提纯方法,如图1所示,其步骤如下:A kind of purification method of melatonin and crystallization mother liquor thereof of the present embodiment, as shown in Figure 1, its steps are as follows:

(1)褪黑素粗品提纯(1) Purification of crude melatonin

(1-1)将纯度为99.60%的褪黑素粗品300g,与浓度为60%的乙醇水溶液600g进行混合而得到溶解液,其中乙醇水溶液中所用水为除氧水;(1-1) 300 g of crude melatonin with a purity of 99.60% was mixed with 600 g of an aqueous ethanol solution with a concentration of 60% to obtain a solution, wherein the water used in the aqueous ethanol solution was deoxygenated water;

(1-2)在上述溶解液中加入5g活性炭,以氮气置换体系空气,升温至60℃溶解脱色30min后得到的脱色液,经过滤分离活性炭而得到褪黑素过滤液;(1-2) Add 5 g of activated carbon to the above solution, replace the air in the system with nitrogen, heat up to 60° C. to dissolve the decolorized solution obtained after decolorization for 30 minutes, and separate the activated carbon by filtration to obtain the melatonin filtrate;

(1-3)上述褪黑素过滤液以10℃/h的速率降温至-5℃后继续结晶8h得到的结晶液,经离心分离后得到褪黑素精品湿料265g和褪黑素结晶母液611g;褪黑素精品湿料经真空烘干后得到纯度为99.83%、单杂0.03%的褪黑素精品266g,收率为88.6%;(1-3) The above-mentioned melatonin filtrate was cooled to -5°C at a rate of 10°C/h, and then the crystallization liquid obtained by continuing to crystallize for 8 hours was centrifuged to obtain 265g of melatonin high-quality wet material and melatonin crystallization mother liquor 611g; the high-quality melatonin wet material obtained after vacuum drying has a purity of 99.83%, 0.03% pure melatonin 266g, and a yield of 88.6%;

(2)褪黑素结晶母液处理(2) Melatonin crystallization mother liquor treatment

(2-1)将上述褪黑素结晶母液与氢氧化钾混合,控制体系pH值为14,在75℃温度下回流6h得到碱解液;(2-1) Mix the above-mentioned melatonin crystallization mother liquor with potassium hydroxide, control the pH value of the system to 14, and reflux for 6 hours at a temperature of 75° C. to obtain an alkaline solution;

(2-2)将上述碱解液真空浓缩得到固体馏分375g,加入酸调节至pH值为1,搅拌20min至固体完全溶解后得到酸化液;(2-2) Vacuum-concentrate the alkaline hydrolysis solution to obtain 375 g of solid fraction, add acid to adjust the pH value to 1, stir for 20 minutes until the solid is completely dissolved, and obtain an acidified solution;

(2-3)在上述酸化液中加入0.5g活性炭进行脱色得到的脱色液,经分离活性炭而得到过滤液;(2-3) adding 0.5 g of activated carbon to the above-mentioned acidified solution to decolorize the decolorized solution obtained, and obtain the filtrate through separation of the activated carbon;

(2-4)在上述过滤液中加入碱调节pH值为14,离心分离后得到褪黑素前体5-甲氧基色胺23.0g,经酰化后得到纯度为99.67%的母液物料24.1g,该母液物料循环加入褪黑素粗品中进行提纯。(2-4) Add alkali to the above filtrate to adjust the pH value to 14, obtain 23.0 g of melatonin precursor 5-methoxytryptamine after centrifugation, and obtain 24.1 g of mother liquor material with a purity of 99.67% after acylation , the mother liquor material is recycled into the crude melatonin for purification.

本发明基于美国药典USP43中关于褪黑素纯度与杂质的检测方法进行检测,本发明的褪黑素结晶母液提纯工艺产品品质优于现有技术常规提纯工艺(见图3和图4)。The present invention detects based on the detection method of melatonin purity and impurities in the United States Pharmacopoeia USP43, and the product quality of the purification process of the melatonin crystallization mother liquor of the present invention is superior to the conventional purification process of the prior art (see Figure 3 and Figure 4).

Claims (10)

1. A method for purifying melatonin and a crystallization mother liquor thereof is characterized by comprising the following steps:
(1) Purification of crude melatonin
(1-1) mixing the melatonin crude product with an ethanol water solution with the concentration of 30-95% according to the mass ratio of the melatonin crude product to the ethanol water solution = 1: 1-5 to obtain a dissolved solution, wherein the water used in the ethanol water solution is deoxygenated water;
(1-2) adding activated carbon with the amount of 1-3 wt% of the melatonin crude product into the dissolved solution, replacing system air with nitrogen, heating to 50-75 ℃, dissolving and decolorizing to obtain decolorized solution, and filtering and separating the activated carbon to obtain melatonin filtrate;
(1-3) cooling the melatonin filtrate to-10 ℃ at the speed of 10 ℃/h, then continuously crystallizing for 4-8 h to obtain a crystallization liquid, and performing centrifugal separation to obtain a melatonin refined wet material and a melatonin crystallization mother liquor; vacuum drying the melatonin refined wet material to obtain melatonin refined product;
(2) Melatonin crystallization mother liquor treatment
(2-1) mixing the melatonin crystallization mother liquor with an alkaline catalyst, controlling the pH value of the system to be 10-14, and refluxing at the temperature of 60-80 ℃ for 2-8 h to obtain alkaline hydrolysis liquid;
(2-2) concentrating the alkaline hydrolysis liquid in vacuum to separate out solid fraction, adding acid to adjust the pH value to 1-4, and stirring until the solid is completely dissolved to obtain acidified liquid;
(2-3) adding activated carbon with the use amount of 0.1-0.3 wt% of the acidified liquid into the acidified liquid for decolorization to obtain decolorized liquid, and separating the activated carbon to obtain filtrate;
(2-4) adding alkali into the filtrate to adjust the pH value to 10-14, performing centrifugal separation to obtain melatonin precursor 5-methoxytryptamine, and performing acylation to obtain a mother liquor material with the purity of more than 99.5%; and circularly adding the mother liquor material into the melatonin crude product for purification.
2. The method of purifying melatonin and the crystallization mother liquor thereof as claimed in claim 1, wherein: in the step (1-1), the concentration of the ethanol water solution is 40-60%, and the mass ratio of the melatonin crude product to the ethanol water solution is = 1: 2-3.
3. The method of purifying melatonin and the crystallization mother liquor thereof as claimed in claim 1, wherein: the crystallization temperature in the step (1-3) is 0-5 ℃.
4. The method of purifying melatonin and the crystallization mother liquor thereof as claimed in claim 1, wherein: and (3) in the step (2-1), the basic catalyst is sodium hydroxide, potassium hydroxide, sodium methoxide, sodium tert-butoxide or triethylamine.
5. The method of purifying melatonin and crystallization mother liquor thereof as claimed in claim 1 or 4, wherein: the pH value of the system in the step (2-1) is 12-13, the reflux temperature is 70-75 ℃, and the reflux time is 4-5 h.
6. The method of purifying melatonin and the crystallization mother liquor thereof as claimed in claim 1, wherein: the pH value in the step (2-2) is 1-2.
7. The method of purifying melatonin and the crystallization mother liquor thereof as claimed in claim 1, wherein: the pH value in the step (2-4) is 12-13.
8. The method of purifying melatonin and the crystallization mother liquor thereof as claimed in claim 1, wherein: the purity of the melatonin crude product in the step (1-1) is more than 99.50%.
9. The method of purifying melatonin and the crystallization mother liquor thereof as claimed in claim 1, wherein: the purity of the refined melatonin in the step (1-3) is more than 99.70%, the purity of the refined melatonin is less than 0.05%, and the yield is more than 88.0%.
10. The method of purifying melatonin and the crystallization mother liquor thereof as claimed in claim 1, wherein: the purity of the mother liquor material in the step (2-4) is more than 99.50%.
CN202310012510.XA 2023-01-05 2023-01-05 Melatonin and purification method of crystallization mother liquor thereof Active CN115974756B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202310012510.XA CN115974756B (en) 2023-01-05 2023-01-05 Melatonin and purification method of crystallization mother liquor thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202310012510.XA CN115974756B (en) 2023-01-05 2023-01-05 Melatonin and purification method of crystallization mother liquor thereof

Publications (2)

Publication Number Publication Date
CN115974756A true CN115974756A (en) 2023-04-18
CN115974756B CN115974756B (en) 2025-01-10

Family

ID=85972157

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202310012510.XA Active CN115974756B (en) 2023-01-05 2023-01-05 Melatonin and purification method of crystallization mother liquor thereof

Country Status (1)

Country Link
CN (1) CN115974756B (en)

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4772726A (en) * 1983-07-01 1988-09-20 Nestec S. A. Preparation of melatonine and mexamine
CN104496882A (en) * 2014-11-29 2015-04-08 湖北金赛药业有限公司 Synthesis method of melatonin
CN112920104A (en) * 2021-01-25 2021-06-08 福建科宏生物工程股份有限公司 Preparation method for green synthesis of N-acetyl-5-methoxytryptamine
CN113072479A (en) * 2021-03-26 2021-07-06 罗田县新普生药业有限公司 Method for extracting melatonin from melatonin crystallization mother liquor
CN113214133A (en) * 2021-05-08 2021-08-06 保定保利瑞合生物科技有限公司 Synthesis method of melatonin
CN114195696A (en) * 2021-12-27 2022-03-18 杭州易合生物医药科技有限公司 Preparation method of melatonin
CN114685345A (en) * 2022-05-23 2022-07-01 南京桦冠生物技术有限公司 Refining and decoloring method of melatonin

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4772726A (en) * 1983-07-01 1988-09-20 Nestec S. A. Preparation of melatonine and mexamine
CN104496882A (en) * 2014-11-29 2015-04-08 湖北金赛药业有限公司 Synthesis method of melatonin
CN112920104A (en) * 2021-01-25 2021-06-08 福建科宏生物工程股份有限公司 Preparation method for green synthesis of N-acetyl-5-methoxytryptamine
CN113072479A (en) * 2021-03-26 2021-07-06 罗田县新普生药业有限公司 Method for extracting melatonin from melatonin crystallization mother liquor
CN113214133A (en) * 2021-05-08 2021-08-06 保定保利瑞合生物科技有限公司 Synthesis method of melatonin
CN114195696A (en) * 2021-12-27 2022-03-18 杭州易合生物医药科技有限公司 Preparation method of melatonin
CN114685345A (en) * 2022-05-23 2022-07-01 南京桦冠生物技术有限公司 Refining and decoloring method of melatonin

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
C. PRABHAKAR等: "Process Research and Development of Melatonin", ORGANIC PROCESS RESEARCH & DEVELOPMENT, vol. 3, no. 3, 1 April 1999 (1999-04-01), pages 155 - 160, XP002582702, DOI: 10.1021/OP9800820 *
MASANORI SOMEI等: "SYNTHESES OF MELATONIN AND ITS DERIVATIVES", HETEROCYCLES, vol. 53, no. 8, 31 December 2000 (2000-12-31), pages 1725 - 1736 *

Also Published As

Publication number Publication date
CN115974756B (en) 2025-01-10

Similar Documents

Publication Publication Date Title
CN116496159A (en) Preparation method of ethyl 6,8-dichloro octoate
WO2023066026A1 (en) Method for purifying ethylene carbonate by means of dynamic crystallization
EP4215538A1 (en) Method for purifying sucralose
CN111087326A (en) Method for refining guanidine nitrate
CN107304186B (en) Refining method of olaparib
CN115974756A (en) A kind of purification method of melatonin and its crystallization mother liquor
CN109851568B (en) Method for purifying prothioconazole
CN114716335A (en) Process for preparing N-acetyl-L-tyrosine
CN115636772B (en) Preparation method of high-purity creatine monohydrate
CN111362860A (en) Method for extracting tryptophan from fermentation liquor
CN101284775B (en) Process for reclaiming 2-keto-L-gulonate by salting out method
CN103664848B (en) A kind of extracting method of mycophenolic acid
CN106554273B (en) Method for purifying long-chain dicarboxylic acid in fermentation liquor
CN103254102B (en) A kind of method of purifying acrylamide alkyl sulfonic acid
CN114014835A (en) Glycolide purification process
CN112979450B (en) Preparation method of ammonium azelate hydrogen
CN114736118B (en) Method for separating 3-methoxy-4-hydroxy mandelic acid and preparing high-purity product thereof
CN104326901B (en) Method for recycling and mechanically using L- (+) -tartaric acid in D-ethyl ester production
CN112724012B (en) Method for refining long-chain dibasic acid
CN115626882B (en) Purification method of creatine monohydrate
CN104557651A (en) Method for extracting astaxanthin from haematococcus pluvialis by double-aqueous-phase coupled wall breaking technology
CN112661719B (en) Clean preparation process of aminothiazoly loximate
CN112979451B (en) Preparation method of ammonium azelate hydrogen
US2982616A (en) Method of producing calcium-free crystalline cyanamide
CN112661727B (en) Purification method of 7- (2, 2-trichloroethyl oxycarbonyl) taxol

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant