WO2020077927A1 - Post-processing method for gonadotropin-releasing hormone antagonist - Google Patents

Post-processing method for gonadotropin-releasing hormone antagonist Download PDF

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WO2020077927A1
WO2020077927A1 PCT/CN2019/075757 CN2019075757W WO2020077927A1 WO 2020077927 A1 WO2020077927 A1 WO 2020077927A1 CN 2019075757 W CN2019075757 W CN 2019075757W WO 2020077927 A1 WO2020077927 A1 WO 2020077927A1
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nanofiltration
acetic acid
solution
sample
drying
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PCT/CN2019/075757
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French (fr)
Chinese (zh)
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付玉清
张利香
李世东
舒遂智
王宏欣
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深圳市健元医药科技有限公司
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/027Nanofiltration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02Reverse osmosis; Hyperfiltration ; Nanofiltration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D65/00Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
    • B01D65/02Membrane cleaning or sterilisation ; Membrane regeneration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D7/00Sublimation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/40Mixing liquids with liquids; Emulsifying
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/40Mixing liquids with liquids; Emulsifying
    • B01F23/405Methods of mixing liquids with liquids
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07KPEPTIDES
    • C07K1/00General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
    • C07K1/14Extraction; Separation; Purification
    • C07K1/34Extraction; Separation; Purification by filtration, ultrafiltration or reverse osmosis
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B5/00Drying solid materials or objects by processes not involving the application of heat
    • F26B5/04Drying solid materials or objects by processes not involving the application of heat by evaporation or sublimation of moisture under reduced pressure, e.g. in a vacuum
    • F26B5/06Drying solid materials or objects by processes not involving the application of heat by evaporation or sublimation of moisture under reduced pressure, e.g. in a vacuum the process involving freezing

Definitions

  • the invention relates to a post-treatment method of GnRH antagonist. It belongs to the field of biomedical technology.
  • Gonadotropin-releasing hormone (GnRH) antagonists are synthetic gonadotropin-releasing hormone analogs that inhibit the proliferation and metastasis of prostate cancer by inhibiting testosterone.
  • GnRH antagonists mainly include abarelix, cetrorelix, Nal-Glu, ganirelix and degarelix.
  • the post-processing method involved in the present invention mainly refers to the concentration method and lyophilization process of the purified sample solution.
  • the post-processing method is a very important link in the process of preparing the GnRH antagonist API and directly affects the quality of the active ingredient of the drug.
  • the patent CN102428097 uses the method of column concentration + vacuum rotary evaporation to condense the sample of Digarek after purification, and then freeze-dry.
  • the patent CN201380028448 proposes three concentration methods, which are through vacuum rotary evaporation. Through column concentration or lyophilization to achieve the purpose of concentrating the sample after purification, and finally using lyophilization to obtain qualified pharmaceutical active ingredients.
  • the present invention creatively uses nanofiltration technology to concentrate the sample after purification of the GnRH antagonist, while adding an appropriate amount of acetic acid during the nanofiltration process to prevent the sample from undergoing self-polymerization reaction, thereby achieving the purpose of concentration, and according to freeze-drying It is required to nanofilter the sample to the required concentration.
  • organic solvents such as ethanol and acetonitrile is not involved in the nanofiltration process. The cost is lower, the yield is higher, the sample is more stable, and it is more suitable for large-scale industrial production.
  • the object of the present invention is to provide a method for concentrating samples after purification of GnRH antagonists using nanofiltration technology, so as to overcome the above-mentioned deficiencies in the prior art.
  • the post-processing method of the GnRH antagonist provided by the present invention includes the following steps:
  • the nanofiltration membrane in step (1) above is characterized by a pore size of 1-20 nm and a molecular weight cut-off of 200-1000 Daltons.
  • the temperature of the sample solution in the above step (2) is: 0 ° C to 35 ° C.
  • the acetic acid content of the sample solution in the above step (2) is: 0% -50%.
  • the sample concentration in the above step (3) is: 5 g / L to 75 g / L.
  • the thickness of the solution in the above step (4) is: 0.5-2.5 cm.
  • the pre-freezing temperature in the above step (4) is: -65 ° C to -25 ° C.
  • the above step (5) is characterized in that the sublimation drying temperature is -15 ° C to 15 ° C, and the sublimation drying time is 10h to 35h.
  • the above step (6) is characterized in that the analytical drying temperature is 15 ° C to 40 ° C, and the analytical drying time is 5h to 30h.
  • the above step (7) is characterized by controlling the ambient temperature to 15 ° C to 35 ° C and the ambient humidity to be 0% to 60%.
  • the nanofiltration membrane is selected from polyamide nanofiltration membrane, polyethersulfone nanofiltration membrane, cellulose acetate nanofiltration membrane, polyvinyl alcohol nanofiltration membrane, and polypiperazine nanofiltration membrane.
  • the GnRH antagonist is selected from the group consisting of degarelix, cetrorelix, ganirelix, abarelix, and Nal-Glu. .
  • the present invention has the following beneficial effects:
  • the nanofiltration process used in this patent has shorter concentration time, higher efficiency and higher productivity.
  • the relatively low concentration temperature makes the sample more stable and more suitable for large-scale industrial production;
  • the nanofiltration process used in this patent avoids the use of organic solvents such as acetonitrile, the steps are simpler, the cost is lower, the yield can reach more than 93%, and the sample concentration that can be achieved after concentration is higher .
  • the addition of acetic acid during the nanofiltration process can effectively prevent the sample from undergoing self-polymerization and make the sample more stable.
  • the nanofiltration process combined with the subsequent freeze-drying process can not only obtain samples with controllable moisture, acetic acid and optical density, but also have lower cost, more stable samples, and are more suitable for large-scale industrial production.
  • the nanofiltration membrane material is polyamide nanofiltration membrane, prepare nanofiltration;
  • the nano filtrate is discharged, the nano filter is washed with a 35% acetic acid aqueous solution, the nano filtrate and the cleaning solution are mixed, and then diluted with a 35% acetic acid aqueous solution, the diluted sample concentration is 15g / L, and the acetic acid content is 35 %, Nanofiltration time 4h;
  • Sublimation drying sublimation drying temperature is -10 °C, sublimation drying time is 15h;
  • the nanofiltrate is discharged, and the nanofiltration machine is washed with 10% acetic acid aqueous solution, the nanofiltrate and the cleaning solution are mixed, and then diluted with a 10% acetic acid aqueous solution. %
  • Sublimation drying sublimation drying temperature is 0 °C, sublimation drying time is 15h;
  • the nanofiltration membrane material is polyamide nanofiltration membrane, prepare nanofiltration;
  • the volume of the ganerlix sample solution is 30 L, and 3.3 L of acetic acid is added to make the acetic acid content in the sample solution 10%, and nanofiltration is started.
  • the volume of the sample solution is nanofiltration to 15L, add 3L of acetic acid to control the content of acetic acid in the sample solution to 25%, and then continue the nanofiltration;
  • Nanofiltration is discharged after 6.5h of nanofiltration, the nanofiltration machine is washed with 25% acetic acid aqueous solution, the nanofiltrate and the cleaning solution are mixed, and then diluted with 25% acetic acid aqueous solution, the sample concentration after dilution is 26g / L, and the acetic acid content is 25%.
  • Sublimation drying sublimation drying temperature is -5 °C, sublimation drying time is 20h;
  • the nanofiltration membrane material is polyamide nanofiltration membrane, prepare nanofiltration;
  • the nano filtrate is discharged.
  • the nano filter is washed with 15% acetic acid aqueous solution, the nano filtrate and the cleaning solution are mixed, and then diluted with a 15% acetic acid aqueous solution. %
  • Sublimation drying sublimation drying temperature is -20 °C, sublimation drying time is 15h;
  • the nanofiltrate is discharged after 7h of nanofiltration, the nanofiltration machine is washed with 30% acetic acid aqueous solution, the nanofiltrate and the cleaning solution are mixed, the sample concentration after mixing is 30g / L, and the acetic acid content is 30%;
  • Sublimation drying sublimation drying temperature is -5 °C, sublimation drying time is 20h;
  • sample analysis is as follows, including 7.1% moisture, 8.6% acetic acid, 0.02 optical density, and 97.19% concentrated yield.
  • the nanofiltrate is discharged, the nanofiltration machine is washed with a 40% acetic acid aqueous solution, and the nanofiltrate and the cleaning solution are mixed. After mixing, the sample concentration is 40 g / L and the acetic acid content is 40%;
  • Sublimation drying sublimation drying temperature is -13 °C, sublimation drying time is 35h;
  • the samples were analyzed as follows. Among them, the water content was 12.6%, acetic acid 16.3%, optical density 0.02, and concentrated yield 95.33%.
  • the nanofiltrate is discharged, and the nanofiltration machine is washed with 10% acetic acid aqueous solution, the nanofiltrate and the cleaning solution are mixed, and then diluted with a 10% acetic acid aqueous solution. %
  • Sublimation drying sublimation drying temperature is -5 °C, sublimation drying time is 15h;
  • the nanofiltration membrane material is polyamide nanofiltration membrane, prepare nanofiltration;
  • the nano filtrate is discharged.
  • the nano filter is washed with 15% acetic acid aqueous solution, the nano filtrate and the cleaning solution are mixed, and then diluted with a 15% acetic acid aqueous solution.
  • the sample concentration after dilution is 10g / L and the acetic acid content is 15 %
  • Sublimation drying sublimation drying temperature is -15 °C, sublimation drying time is 20h;
  • the nanofiltration membrane material is polyamide nanofiltration membrane, prepare nanofiltration;
  • the nano filtrate is discharged, the nano filter is washed with a 35% acetic acid aqueous solution, the nano filtrate and the cleaning solution are mixed, and then diluted with a 35% acetic acid aqueous solution, the diluted sample concentration is 15g / L, and the acetic acid content is 35 %, Nanofiltration time 4h;
  • Sublimation drying sublimation drying temperature is -20 °C, sublimation drying time is 25h;
  • Nanofiltration is discharged after 7.5h of nanofiltration, the nanofiltration machine is washed with 30% acetic acid aqueous solution, and the nanofiltrate and the cleaning solution are mixed. After mixing, the sample concentration is 30g / L and the acetic acid content is 30%;
  • Sublimation drying sublimation drying temperature is -15 °C, sublimation drying time is 25h;
  • Vacuum concentration temperature 35 °C
  • the acetic acid concentration in the sample solution is 24%;
  • the concentration of Digaric sample before lyophilization is 18g / L;
  • the sample is subjected to a freeze-drying step, in which the thickness of the freeze-dried solution is 0.75 cm, the sublimation temperature is -5 ° C, and the analytical drying temperature is 25 ° C.
  • the concentrated yield was 93.5%.
  • the sample was detected by the above method, in which the water content was 8.5%, acetic acid 10.5%, and optical density 0.12.
  • the BUCHI rotary evaporator is preferred.
  • concentration the sample is depolymerized by adding appropriate amount of acetic acid, and then filtered and lyophilized under the following conditions:
  • Vacuum concentration temperature 28 °C
  • the acetic acid concentration in the sample solution is 12%;
  • the concentration of Abarek sample before lyophilization is 35g / L;
  • the sample is subjected to a lyophilization step, in which the thickness of the lyophilized solution is 0.75 cm, the sublimation temperature is -15 ° C, and the analytical drying temperature is 27 ° C.
  • the concentrated yield was 92.9%, of which moisture was 7.5%, acetic acid was 8.7%, and optical density was 0.10.
  • the yield can reach more than 93% and the concentration time of the nanofiltration process is shorter compared with the vacuum rotary evaporation concentration and the column concentration + vacuum rotary evaporation concentration process. Higher efficiency and productivity.
  • the nanofiltration process used in this patent avoids the use of organic solvents such as acetonitrile, the steps are simpler and the cost is lower.
  • the nanofiltration process combined with the subsequent freeze-drying process can not only obtain samples with controllable moisture, acetic acid and optical density, the samples are more stable and more suitable for large-scale industrial production.

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Abstract

A post-processing method for a GnRH antagonist, comprising the following steps: (1) preparing before nanofiltration, installing a nanofiltration membrane, using purified water to clean a nanofiltration machine, and preparing nanofiltration; (2) starting nanofiltration, controlling the temperature of a sample solution, and adding acetic acid during the nanofiltration process to control the acetic acid content of the sample solution; (3) ending nanofiltration, discharging the nanofiltered solution, and diluting the nanofiltered solution using an acetic acid aqueous solution to control the concentration of the sample; (4) upper freeze-drying, pouring the nanofiltered and concentrated solution into a freeze-drying dish to control the thickness of the solution, and then pre-freezing to control the pre-freezing temperature; (5) sublimation drying; (6) desorption drying; (7) lower freeze-drying, and subpackaging and putting the sample into storage.

Description

一种促性腺激素释放激素拮抗剂的后处理方法Post-processing method of gonadotropin-releasing hormone antagonist 技术领域Technical field
本发明涉及一种GnRH拮抗剂的后处理方法。属于生物医药技术领域。The invention relates to a post-treatment method of GnRH antagonist. It belongs to the field of biomedical technology.
背景技术Background technique
促性腺激素释放激素(GnRH)拮抗剂是人工合成的促性腺激素释放激素类似物,通过抑制睾丸素来抑制前列腺癌增生和转移。GnRH拮抗剂主要包括阿巴瑞克、西曲瑞克、Nal-Glu、加尼瑞克和地加瑞克等。本发明涉及到的后处理方法主要是指纯化后样品溶液的浓缩方法和冻干工艺,后处理方法是制备GnRH拮抗剂原料药过程中非常重要的环节,会直接影响药物活性成分的质量。Gonadotropin-releasing hormone (GnRH) antagonists are synthetic gonadotropin-releasing hormone analogs that inhibit the proliferation and metastasis of prostate cancer by inhibiting testosterone. GnRH antagonists mainly include abarelix, cetrorelix, Nal-Glu, ganirelix and degarelix. The post-processing method involved in the present invention mainly refers to the concentration method and lyophilization process of the purified sample solution. The post-processing method is a very important link in the process of preparing the GnRH antagonist API and directly affects the quality of the active ingredient of the drug.
现有技术中,专利CN102428097是利用过柱浓缩+真空旋蒸的方式对地加瑞克纯化后样品进行浓缩,然后冻干,专利CN201380028448则提出了三种浓缩方式,分别是通过真空旋蒸,过柱浓缩或者冻干来达到纯化后样品浓缩的目的,最后利用冻干得到合格的药物活性成分。In the prior art, the patent CN102428097 uses the method of column concentration + vacuum rotary evaporation to condense the sample of Digarek after purification, and then freeze-dry. The patent CN201380028448 proposes three concentration methods, which are through vacuum rotary evaporation. Through column concentration or lyophilization to achieve the purpose of concentrating the sample after purification, and finally using lyophilization to obtain qualified pharmaceutical active ingredients.
专利CN201380028448中虽然提到了三种浓缩方式,但是在利用真空旋蒸对样品进行浓缩时,浓缩速度较慢,效率低,浓缩时间长,旋蒸温度相对较高可能会引起样品的降解,因此并不适合大规模工业化生产;采用冻干的方式来对样品进行浓缩,不仅耗时,而且对冻干机的性能有很高的要求,同样不适合工业化生产;过柱浓缩的方法虽然在一定程度上可以达到浓缩的目的,但是缺点也很明显,过柱浓缩过程中涉及到有机溶剂的使用,对人类健康和自然环境都会造成危害,而且过柱浓缩过程中样品必然存在一定的损失,同时废液的处理也直接增加了浓缩的成本。而专利CN102428097中提到的过柱浓缩+真空旋蒸的方式不仅步骤繁琐,还增加了有机溶剂的使用,浓缩成本更高。特别要注意的是,GnRH拮抗剂因粘度较大,上述几种后处理方法在使用过程中样品会发生自聚反应,合成中的自聚将引入新的杂质,影响药物纯度,增加患者风险,虽然合成中发生自聚后加入醋酸可以解聚,但是否能解聚完全,样品是否稳定也是需要重点考虑的问题。Although the patent CN201380028448 mentions three concentration methods, when using vacuum rotary evaporation to concentrate the sample, the concentration speed is slow, the efficiency is low, the concentration time is long, and the relatively high rotary evaporation temperature may cause the degradation of the sample. Not suitable for large-scale industrial production; the use of freeze-drying to concentrate samples is not only time-consuming, but also has high requirements for the performance of the freeze dryer, and is also not suitable for industrial production; although the method of column concentration is to a certain extent It can achieve the purpose of concentration, but the shortcomings are also obvious. The use of organic solvents in the process of column concentration will cause harm to human health and the natural environment, and there must be some loss of samples during the process of column concentration. The treatment of the liquid also directly increases the cost of concentration. The method of column concentration + vacuum rotary evaporation mentioned in the patent CN102428097 not only has complicated steps, but also increases the use of organic solvents, and the concentration cost is higher. In particular, due to the high viscosity of GnRH antagonists, samples of the above-mentioned post-treatment methods will undergo self-polymerization during use. The self-polymerization in the synthesis will introduce new impurities, affecting the purity of the drug and increasing the risk of patients. Although it can be depolymerized by adding acetic acid after self-polymerization in the synthesis, whether it can be completely depolymerized and whether the sample is stable is also an important issue to be considered.
结合上述问题,本发明创造性地利用纳滤技术对GnRH拮抗剂纯化后样品进行浓缩的同时,在纳滤过程中加入适量醋酸以防止样品发生自聚反应,从而达到浓缩的目的,并根据冻干要求将样品纳滤到需要的浓度。在纳滤过程中不涉及到乙醇和乙腈等有机溶剂的使用,成本更低,收率更高,样品更加稳定,更加适用于大规模工业化生产。Combining the above problems, the present invention creatively uses nanofiltration technology to concentrate the sample after purification of the GnRH antagonist, while adding an appropriate amount of acetic acid during the nanofiltration process to prevent the sample from undergoing self-polymerization reaction, thereby achieving the purpose of concentration, and according to freeze-drying It is required to nanofilter the sample to the required concentration. The use of organic solvents such as ethanol and acetonitrile is not involved in the nanofiltration process. The cost is lower, the yield is higher, the sample is more stable, and it is more suitable for large-scale industrial production.
发明内容Summary of the invention
本发明的目的是提供一种利用纳滤技术对GnRH拮抗剂纯化后样品进行浓缩的方法,以克服现有技术中上述提到的不足。The object of the present invention is to provide a method for concentrating samples after purification of GnRH antagonists using nanofiltration technology, so as to overcome the above-mentioned deficiencies in the prior art.
本发明提供的GnRH拮抗剂的后处理方法,包括以下步骤:The post-processing method of the GnRH antagonist provided by the present invention includes the following steps:
(1)纳滤前准备,安装纳滤膜,用纯化水清洗纳滤机,准备纳滤;(1) Prepare before nanofiltration, install nanofiltration membrane, wash the nanofiltration machine with purified water, prepare nanofiltration;
(2)开始纳滤,控制样品溶液温度,并在纳滤过程中加入适量醋酸,控制样品溶液醋酸含量;(2) Start nanofiltration, control the temperature of the sample solution, and add an appropriate amount of acetic acid during the nanofiltration process to control the acetic acid content of the sample solution;
(3)纳滤结束,排放出所有样品纳滤溶液,用醋酸水溶液对纳滤后溶液进行稀释,控制样品浓度;(3) At the end of nanofiltration, discharge all sample nanofiltration solutions, dilute the nanofiltration solution with acetic acid aqueous solution, and control the sample concentration;
(4)上冻干,将纳滤浓缩后样品溶液倒入冻干盘,控制溶液厚度,后进行预冻,控制预冻温度;(4) Upper lyophilization, pour the sample solution after nanofiltration concentration into the lyophilization tray, control the thickness of the solution, then pre-freeze, and control the pre-freezing temperature;
(5)升华干燥;(5) Sublimation and drying;
(6)解析干燥;(6) Parsing and drying;
(7)下冻干,将样品分装入库。(7) Lyophilize and load the sample into the library.
在一些实施方案中,上述步骤(1)中所述纳滤膜特征为:孔径1-20nm,截留分子量200~1000道尔顿。In some embodiments, the nanofiltration membrane in step (1) above is characterized by a pore size of 1-20 nm and a molecular weight cut-off of 200-1000 Daltons.
在一些实施方案中,上述步骤(2)中所述样品溶液温度为:0℃~35℃。In some embodiments, the temperature of the sample solution in the above step (2) is: 0 ° C to 35 ° C.
在一些实施方案中,上述步骤(2)中所述样品溶液醋酸含量为:0%~50%。In some embodiments, the acetic acid content of the sample solution in the above step (2) is: 0% -50%.
在一些实施方案中,上述步骤(3)中所述样品浓度为:5g/L~75g/L。In some embodiments, the sample concentration in the above step (3) is: 5 g / L to 75 g / L.
在一些实施方案中,上述步骤(4)中所述溶液厚度为:0.5~2.5cm。In some embodiments, the thickness of the solution in the above step (4) is: 0.5-2.5 cm.
在一些实施方案中,上述步骤(4)中所述预冻温度为:-65℃~-25℃。In some embodiments, the pre-freezing temperature in the above step (4) is: -65 ° C to -25 ° C.
在一些实施方案中,上述步骤(5),其特征为:升华干燥温度为-15℃~15℃,升华干燥时间为10h~35h。In some embodiments, the above step (5) is characterized in that the sublimation drying temperature is -15 ° C to 15 ° C, and the sublimation drying time is 10h to 35h.
在一些实施方案中,上述步骤(6),其特征为:解析干燥温度为15℃~40℃,解析干燥时间为5h~30h。In some embodiments, the above step (6) is characterized in that the analytical drying temperature is 15 ° C to 40 ° C, and the analytical drying time is 5h to 30h.
在一些实施方案中,上述步骤(7),其特征为:控制环境温度为15℃~35℃,环境湿度为0%~60%。In some embodiments, the above step (7) is characterized by controlling the ambient temperature to 15 ° C to 35 ° C and the ambient humidity to be 0% to 60%.
如前所述的方法中,纳滤膜选自聚酰胺纳滤膜、聚醚砜纳滤膜、醋酸纤维素纳滤膜、聚乙烯醇纳滤膜、聚哌嗪纳滤膜。In the method described above, the nanofiltration membrane is selected from polyamide nanofiltration membrane, polyethersulfone nanofiltration membrane, cellulose acetate nanofiltration membrane, polyvinyl alcohol nanofiltration membrane, and polypiperazine nanofiltration membrane.
如前所述的方法中,GnRH拮抗剂选自以下物质:地加瑞克、西曲瑞克、加尼瑞克、阿 巴瑞克、Nal-Glu。。In the method described above, the GnRH antagonist is selected from the group consisting of degarelix, cetrorelix, ganirelix, abarelix, and Nal-Glu. .
与现有技术相比,本发明有如下有益效果:Compared with the prior art, the present invention has the following beneficial effects:
与真空旋蒸浓缩相比,本专利所用纳滤工艺浓缩时间更短,效率和产能更高,相对较低的浓缩温度使样品更加稳定,更加适合于大规模工业化生产;而与过柱浓缩+真空旋蒸浓缩工艺相比,本专利所用纳滤工艺避免了乙腈等有机溶剂的使用,步骤更为简单,成本更低,收率可以达到93%以上,而且浓缩后可以达到的样品浓度更高。更重要的是纳滤过程中加入醋酸可以有效防止样品发生自聚反应,使样品更加稳定。与现有技术相比,纳滤工艺结合后续的冻干工艺不仅可以得到水分、醋酸和光密度可控的样品,而且成本更低,样品更加稳定,更加适用于大规模工业化生产。Compared with vacuum rotary evaporation concentration, the nanofiltration process used in this patent has shorter concentration time, higher efficiency and higher productivity. The relatively low concentration temperature makes the sample more stable and more suitable for large-scale industrial production; Compared with the vacuum rotary evaporation concentration process, the nanofiltration process used in this patent avoids the use of organic solvents such as acetonitrile, the steps are simpler, the cost is lower, the yield can reach more than 93%, and the sample concentration that can be achieved after concentration is higher . More importantly, the addition of acetic acid during the nanofiltration process can effectively prevent the sample from undergoing self-polymerization and make the sample more stable. Compared with the prior art, the nanofiltration process combined with the subsequent freeze-drying process can not only obtain samples with controllable moisture, acetic acid and optical density, but also have lower cost, more stable samples, and are more suitable for large-scale industrial production.
具体实施方式detailed description
下面结合具体实施例对本发明中技术方案的应用作进一步详细的说明,以便于本领域的技术人员进一步地理解本发明。实施例不应限定为对保护范围的限制。The application of the technical solution in the present invention will be further described in detail below in conjunction with specific embodiments, so that those skilled in the art can further understand the present invention. The embodiments should not be limited to the scope of protection.
实施例1Example 1
(1)纳滤前准备,用纯化水清洗纳滤机,纳滤膜材质为聚酰胺纳滤膜,准备纳滤;(1) Prepare before nanofiltration, wash the nanofiltration machine with purified water, the nanofiltration membrane material is polyamide nanofiltration membrane, prepare nanofiltration;
(2)取地加瑞克样品溶液20L,加入10.7L醋酸使样品溶液中醋酸含量为35%,开始纳滤;(2) Take 20L of Digaric sample solution, add 10.7L of acetic acid to make the acetic acid content in the sample solution 35%, and start nanofiltration;
(3)纳滤结束后排放出纳滤液,用35%醋酸水溶液清洗纳滤机,混合纳滤液和清洗液,然后用35%醋酸水溶液进行稀释,稀释后样品浓度为15g/L,醋酸含量为35%,纳滤时长4h;(3) After the nanofiltration is completed, the nano filtrate is discharged, the nano filter is washed with a 35% acetic acid aqueous solution, the nano filtrate and the cleaning solution are mixed, and then diluted with a 35% acetic acid aqueous solution, the diluted sample concentration is 15g / L, and the acetic acid content is 35 %, Nanofiltration time 4h;
(4)将稀释后样品倒入冻干盘,样品溶液厚度为0.65cm,然后进行预冻,预冻温度-35℃;(4) Pour the diluted sample into the lyophilization tray, the thickness of the sample solution is 0.65cm, and then pre-freeze, the pre-freezing temperature is -35 ℃;
(5)升华干燥,升华干燥温度为-10℃,升华干燥时间为15h;(5) Sublimation drying, sublimation drying temperature is -10 ℃, sublimation drying time is 15h;
(6)解析干燥,解析干燥温度20℃,解析干燥时间10h;(6) Analysis drying, analysis drying temperature 20 ℃, analysis drying time 10h;
(7)下冻干,分装入库,环境温度为15℃,环境湿度为60%。(7) Freeze-dried and stored separately in a warehouse with an ambient temperature of 15 ° C and an ambient humidity of 60%.
冻干后收集样品,其中水分6.6%,醋酸7.8%,光密度0.02,浓缩收率94.26%。Samples were collected after lyophilization, of which water content was 6.6%, acetic acid was 7.8%, optical density was 0.02, and concentrated yield was 94.26%.
实施例2Example 2
(1)纳滤前准备,用纯化水清洗纳滤机,纳滤膜材质为聚醚砜纳滤膜,准备纳滤;(1) Prepare before nanofiltration, wash the nanofiltration machine with purified water, the material of the nanofiltration membrane is polyethersulfone nanofiltration membrane, prepare nanofiltration;
(2)地加瑞克样品溶液30L,加入醋酸3.3L使样品溶液中醋酸含量为10%,开始纳滤;(2) 30L of degarelix sample solution, add 3.3L of acetic acid to make the acetic acid content in the sample solution 10%, and start nanofiltration;
(3)纳滤6h后排放出纳滤液,用10%醋酸水溶液清洗纳滤机,混合纳滤液和清洗液,然后用10%醋酸水溶液进行稀释,稀释后样品浓度为15g/L,醋酸含量为10%;(3) After 6 hours of nanofiltration, the nanofiltrate is discharged, and the nanofiltration machine is washed with 10% acetic acid aqueous solution, the nanofiltrate and the cleaning solution are mixed, and then diluted with a 10% acetic acid aqueous solution. %
(4)将稀释后样品倒入冻干盘,样品溶液厚度为0.65cm,然后进行预冻,预冻温度-35℃;(4) Pour the diluted sample into the lyophilization tray, the thickness of the sample solution is 0.65cm, and then pre-freeze, the pre-freezing temperature is -35 ℃;
(5)升华干燥,升华干燥温度为0℃,升华干燥时间为15h;(5) Sublimation drying, sublimation drying temperature is 0 ℃, sublimation drying time is 15h;
(6)解析干燥,解析干燥温度30℃,解析干燥时间10h;(6) Analysis drying, analysis drying temperature 30 ℃, analysis drying time 10h;
(7)下冻干,分装入库,环境温度为15℃,环境湿度为60%。(7) Freeze-dried and stored separately in a warehouse with an ambient temperature of 15 ° C and an ambient humidity of 60%.
冻干后收集样品,其中水分8.6%,醋酸8.8%,光密度0.02,浓缩收率94.56%。Samples were collected after lyophilization, of which water content was 8.6%, acetic acid was 8.8%, optical density was 0.02, and concentrated yield was 94.56%.
实施例3Example 3
(1)纳滤前准备,用纯化水清洗纳滤机,纳滤膜材质为聚酰胺纳滤膜,准备纳滤;(1) Prepare before nanofiltration, wash the nanofiltration machine with purified water, the nanofiltration membrane material is polyamide nanofiltration membrane, prepare nanofiltration;
(2)加尼瑞克样品溶液体积为30L,加入醋酸3.3L使样品溶液中醋酸含量为10%,开始纳滤。纳滤到样品溶液体积为15L时,加入3L醋酸控制样品溶液中醋酸含量为25%,然后继续纳滤;(2) The volume of the ganerlix sample solution is 30 L, and 3.3 L of acetic acid is added to make the acetic acid content in the sample solution 10%, and nanofiltration is started. When the volume of the sample solution is nanofiltration to 15L, add 3L of acetic acid to control the content of acetic acid in the sample solution to 25%, and then continue the nanofiltration;
(3)纳滤6.5h后排放出纳滤液,用25%醋酸水溶液清洗纳滤机,混合纳滤液和清洗液,然后用25%醋酸水溶液进行稀释,稀释后样品浓度为26g/L,醋酸含量为25%。(3) Nanofiltration is discharged after 6.5h of nanofiltration, the nanofiltration machine is washed with 25% acetic acid aqueous solution, the nanofiltrate and the cleaning solution are mixed, and then diluted with 25% acetic acid aqueous solution, the sample concentration after dilution is 26g / L, and the acetic acid content is 25%.
(4)将稀释后样品倒入冻干盘,样品溶液厚度为0.85cm,然后进行预冻,预冻温度-40℃;(4) Pour the diluted sample into the lyophilization tray, the thickness of the sample solution is 0.85cm, and then pre-freeze, the pre-freezing temperature is -40 ℃;
(5)升华干燥,升华干燥温度为-5℃,升华干燥时间为20h;(5) Sublimation drying, sublimation drying temperature is -5 ℃, sublimation drying time is 20h;
(6)解析干燥,解析干燥温度29℃,解析干燥时间10h;(6) Analysis drying, analysis drying temperature 29 ℃, analysis drying time 10h;
(7)下冻干,分装入库,环境温度为25℃,环境湿度为55%。(7) Freeze-dried and stored separately in a warehouse with an ambient temperature of 25 ° C and an ambient humidity of 55%.
冻干后收集样品,其中水分8.6%,醋酸8.3%,光密度0.02,浓缩收率93.58%。Samples were collected after freeze-drying, of which water content was 8.6%, acetic acid was 8.3%, optical density was 0.02, and concentrated yield was 93.58%.
实施例4Example 4
(1)纳滤前准备,用纯化水清洗纳滤机,纳滤膜材质为聚酰胺纳滤膜,准备纳滤;(1) Prepare before nanofiltration, wash the nanofiltration machine with purified water, the nanofiltration membrane material is polyamide nanofiltration membrane, prepare nanofiltration;
(2)取阿巴瑞克样品溶液30L,加入醋酸1.5L使样品溶液中醋酸含量为5%,开始纳滤,纳滤到样品溶液体积为15L时,加入醋酸1.8L使使样品溶液中醋酸含量为15%,继续纳滤;(2) Take 30L of Abarelix sample solution, add 1.5L of acetic acid to make the acetic acid content in the sample solution 5%, and start nanofiltration. When the volume of the sample solution is 15L, add 1.8L of acetic acid to make acetic acid in the sample solution The content is 15%, continue nanofiltration;
(3)纳滤7h后排放出纳滤液,用15%醋酸水溶液清洗纳滤机,混合纳滤液和清洗液,然后用15%醋酸水溶液进行稀释,稀释后样品浓度为10g/L,醋酸含量为15%;(3) After 7h of nanofiltration, the nano filtrate is discharged. The nano filter is washed with 15% acetic acid aqueous solution, the nano filtrate and the cleaning solution are mixed, and then diluted with a 15% acetic acid aqueous solution. %
(4)将稀释后样品倒入冻干盘,样品溶液厚度为0.85cm,然后进行预冻,预冻温度-35℃;(4) Pour the diluted sample into the lyophilization tray, the thickness of the sample solution is 0.85cm, and then pre-freeze, the pre-freezing temperature is -35 ℃;
(5)升华干燥,升华干燥温度为-20℃,升华干燥时间为15h;(5) Sublimation drying, sublimation drying temperature is -20 ℃, sublimation drying time is 15h;
(6)解析干燥,解析干燥温度25℃,解析干燥时间10h;(6) Analysis drying, analysis drying temperature 25 ℃, analysis drying time 10h;
(7)下冻干,分装入库,环境温度为15℃,环境湿度为39%。(7) Freeze-dried and stored separately in a warehouse with an ambient temperature of 15 ° C and an ambient humidity of 39%.
冻干后样品分析如下,其中水分7.6%,醋酸9.3%,光密度0.02,浓缩收率97.02%。After lyophilization, the samples were analyzed as follows, including moisture 7.6%, acetic acid 9.3%, optical density 0.02, and concentrated yield 97.02%.
实施例5Example 5
(1)纳滤前准备,用纯化水清洗纳滤机,纳滤膜材质为醋酸纤维素纳滤膜,准备纳滤;(1) Prepare before nanofiltration, wash the nanofiltration machine with purified water, the material of the nanofiltration membrane is cellulose acetate nanofiltration membrane, prepare nanofiltration;
(2)地加瑞克样品溶液30L,加入醋酸1.5L使样品溶液中醋酸含量为5%,开始纳滤,纳滤到样品溶液体积为15L时,加入醋酸1.8L使使样品溶液中醋酸含量为15%,继续纳滤, 纳滤到样品溶液体积为7.5L时,加入醋酸1.6L使使样品溶液中醋酸含量为30%,继续纳滤;(2) Digaric sample solution 30L, add 1.5L acetic acid to make the acetic acid content in the sample solution 5%, start nanofiltration, when nanofiltration is to the sample solution volume is 15L, add 1.8L acetic acid to make the acetic acid content in the sample solution 15%, continue the nanofiltration, when the nanofiltration reaches the sample solution volume of 7.5L, add 1.6L of acetic acid to make the acetic acid content in the sample solution 30%, continue the nanofiltration;
(3)纳滤7h后排放出纳滤液,用30%醋酸水溶液清洗纳滤机,混合纳滤液和清洗液,混合后样品浓度为30g/L,醋酸含量为30%;(3) The nanofiltrate is discharged after 7h of nanofiltration, the nanofiltration machine is washed with 30% acetic acid aqueous solution, the nanofiltrate and the cleaning solution are mixed, the sample concentration after mixing is 30g / L, and the acetic acid content is 30%;
(4)将稀释后样品倒入冻干盘,样品溶液厚度为1.0cm,然后进行预冻,预冻温度-45℃;(4) Pour the diluted sample into the lyophilization tray, the thickness of the sample solution is 1.0cm, and then pre-freeze, the pre-freezing temperature is -45 ℃;
(5)升华干燥,升华干燥温度为-5℃,升华干燥时间为20h;(5) Sublimation drying, sublimation drying temperature is -5 ℃, sublimation drying time is 20h;
(6)解析干燥,解析干燥温度27℃,解析干燥时间15h;(6) Analysis drying, analysis drying temperature 27 ℃, analysis drying time 15h;
(7)下冻干,分装入库,环境温度为23℃,环境湿度为44%。(7) Freeze-dried and stored separately in a warehouse with an ambient temperature of 23 ° C and an ambient humidity of 44%.
冻干后样品分析如下,其中水分7.1%,醋酸8.6%,光密度0.02,浓缩收率97.19%。After lyophilization, the sample analysis is as follows, including 7.1% moisture, 8.6% acetic acid, 0.02 optical density, and 97.19% concentrated yield.
实施例6Example 6
(1)纳滤前准备,用纯化水清洗纳滤机,纳滤膜材质为聚醚砜纳滤膜,准备纳滤;(1) Prepare before nanofiltration, wash the nanofiltration machine with purified water, the material of the nanofiltration membrane is polyethersulfone nanofiltration membrane, prepare nanofiltration;
(2)地加瑞克样品溶液30L,加入醋酸1.5L使样品溶液中醋酸含量为5%,开始纳滤。纳滤到样品溶液体积为15L时,加入醋酸1.8L使使样品溶液中醋酸含量为15%,继续纳滤;。纳滤到样品溶液体积为7.5L时,加入醋酸3.2L使使样品溶液中醋酸含量为40%,继续纳滤;(2) 30L of degarelix sample solution, add 1.5L of acetic acid to make the acetic acid content in the sample solution 5%, and start nanofiltration. When the volume of the sample solution is nanofiltration to 15L, add 1.8L of acetic acid to make the content of acetic acid in the sample solution 15%, and continue nanofiltration; When the volume of the sample solution is nanofiltration to 7.5L, add 3.2L of acetic acid to make the content of acetic acid in the sample solution 40%, and continue nanofiltration;
(3)纳滤结束后排放出纳滤液,用40%醋酸水溶液清洗纳滤机,混合纳滤液和清洗液,混合后样品浓度为40g/L,醋酸含量为40%;(3) After the nanofiltration is completed, the nanofiltrate is discharged, the nanofiltration machine is washed with a 40% acetic acid aqueous solution, and the nanofiltrate and the cleaning solution are mixed. After mixing, the sample concentration is 40 g / L and the acetic acid content is 40%;
(4)将稀释后样品倒入冻干盘,样品溶液厚度为1.8cm,然后进行预冻,预冻温度-60℃;(4) Pour the diluted sample into the lyophilization tray, the thickness of the sample solution is 1.8cm, and then pre-freeze, the pre-freezing temperature is -60 ℃;
(5)升华干燥,升华干燥温度为-13℃,升华干燥时间为35h;(5) Sublimation drying, sublimation drying temperature is -13 ℃, sublimation drying time is 35h;
(6)解析干燥,解析干燥温度35℃,解析干燥时间15h;(6) Analysis drying, analysis drying temperature 35 ℃, analysis drying time 15h;
(7)下冻干,分装入库,环境温度为35℃,环境湿度为35%。(7) Freeze-dried and stored separately in a warehouse with an ambient temperature of 35 ° C and an ambient humidity of 35%.
冻干后样品分析如下,其中水分12.6%,醋酸16.3%,光密度0.02,浓缩收率95.33%。After lyophilization, the samples were analyzed as follows. Among them, the water content was 12.6%, acetic acid 16.3%, optical density 0.02, and concentrated yield 95.33%.
实施例7Example 7
(1)纳滤前准备,将纯化后的加尼瑞克样品溶液中加入水,纳滤膜材质为聚乙烯醇纳滤膜,控制溶液中的乙腈含量为2%;(1) Preparation before nanofiltration, add water to the purified Ganirelix sample solution, the material of the nanofiltration membrane is a polyvinyl alcohol nanofiltration membrane, and the content of acetonitrile in the solution is controlled to 2%;
(2)加尼瑞克样品溶液40L,加入醋酸4.5L使样品溶液中醋酸含量为10%,开始纳滤;(2) 40L of Ganirelix sample solution, add 4.5L of acetic acid to make the acetic acid content in the sample solution 10%, and start nanofiltration;
(3)纳滤6h后排放出纳滤液,用10%醋酸水溶液清洗纳滤机,混合纳滤液和清洗液,然后用10%醋酸水溶液进行稀释,稀释后样品浓度为15g/L,醋酸含量为10%;(3) After 6 hours of nanofiltration, the nanofiltrate is discharged, and the nanofiltration machine is washed with 10% acetic acid aqueous solution, the nanofiltrate and the cleaning solution are mixed, and then diluted with a 10% acetic acid aqueous solution. %
(4)将稀释后样品倒入冻干盘,样品溶液厚度为1.25cm,然后进行预冻,预冻温度-40℃;(4) Pour the diluted sample into the lyophilization dish, the thickness of the sample solution is 1.25cm, and then pre-freeze, the pre-freezing temperature is -40 ℃;
(5)升华干燥,升华干燥温度为-5℃,升华干燥时间为15h;(5) Sublimation drying, sublimation drying temperature is -5 ℃, sublimation drying time is 15h;
(6)解析干燥,解析干燥温度28℃,解析干燥时间15h;(6) Analysis drying, analysis drying temperature 28 ℃, analysis drying time 15h;
(7)下冻干,分装入库,环境温度为26℃,环境湿度为51%。(7) Freeze-dried and stored separately in a warehouse with an ambient temperature of 26 ° C and an ambient humidity of 51%.
冻干后样品进行分析,其中水分7.7%,醋酸7.9%,光密度0.06,浓缩收率98.02%。After lyophilization, the samples were analyzed, including 7.7% moisture, 7.9% acetic acid, 0.06 optical density, and 98.02% concentrated yield.
实施例8Example 8
(1)纳滤前准备,用纯化水清洗纳滤机,纳滤膜材质为聚酰胺纳滤膜,准备纳滤;(1) Prepare before nanofiltration, wash the nanofiltration machine with purified water, the nanofiltration membrane material is polyamide nanofiltration membrane, prepare nanofiltration;
(2)加尼瑞克样品溶液30L,加入醋酸1.5L使样品溶液中醋酸含量为5%,开始纳滤,纳滤到样品溶液体积为15L时,加入醋酸1.8L使使样品溶液中醋酸含量为15%,继续纳滤;(2) 30L of Garnirec sample solution, adding 1.5L of acetic acid to make the acetic acid content in the sample solution 5%, start nanofiltration. When the volume of the sample solution is 15L, add 1.8L of acetic acid to make the acetic acid content in the sample solution 15%, continue nanofiltration;
(3)纳滤7h后排放出纳滤液,用15%醋酸水溶液清洗纳滤机,混合纳滤液和清洗液,然后用15%醋酸水溶液进行稀释,稀释后样品浓度为10g/L,醋酸含量为15%;(3) After 7h of nanofiltration, the nano filtrate is discharged. The nano filter is washed with 15% acetic acid aqueous solution, the nano filtrate and the cleaning solution are mixed, and then diluted with a 15% acetic acid aqueous solution. The sample concentration after dilution is 10g / L and the acetic acid content is 15 %
(4)将稀释后样品倒入冻干盘,样品溶液厚度为1.5cm,然后进行预冻,预冻温度-28℃;(4) Pour the diluted sample into the lyophilization tray, the thickness of the sample solution is 1.5cm, and then pre-freeze, the pre-freezing temperature is -28 ℃;
(5)升华干燥,升华干燥温度为-15℃,升华干燥时间为20h;(5) Sublimation drying, sublimation drying temperature is -15 ℃, sublimation drying time is 20h;
(6)解析干燥,解析干燥温度15℃,解析干燥时间12h;(6) Analysis drying, analysis drying temperature 15 ℃, analysis drying time 12h;
(7)下冻干,分装入库,环境温度为20℃,环境湿度为42%。(7) Freeze-dried and stored separately in a warehouse with an ambient temperature of 20 ° C and an ambient humidity of 42%.
冻干后收集样品,其中水分9.6%,醋酸7.3%,光密度0.09,浓缩收率94.39%。Samples were collected after lyophilization, of which water content was 9.6%, acetic acid was 7.3%, optical density was 0.09, and concentrated yield was 94.39%.
实施例9Example 9
(1)纳滤前准备,用纯化水清洗纳滤机,纳滤膜材质为聚酰胺纳滤膜,准备纳滤;(1) Prepare before nanofiltration, wash the nanofiltration machine with purified water, the nanofiltration membrane material is polyamide nanofiltration membrane, prepare nanofiltration;
(2)西曲瑞克样品溶液40L,加入21.5L醋酸使样品溶液中醋酸含量为35%,开始纳滤;(2) 40L of cetrorelix sample solution, add 21.5L of acetic acid to make the acetic acid content in the sample solution 35%, and start nanofiltration;
(3)纳滤结束后排放出纳滤液,用35%醋酸水溶液清洗纳滤机,混合纳滤液和清洗液,然后用35%醋酸水溶液进行稀释,稀释后样品浓度为15g/L,醋酸含量为35%,纳滤时长4h;(3) After the nanofiltration is completed, the nano filtrate is discharged, the nano filter is washed with a 35% acetic acid aqueous solution, the nano filtrate and the cleaning solution are mixed, and then diluted with a 35% acetic acid aqueous solution, the diluted sample concentration is 15g / L, and the acetic acid content is 35 %, Nanofiltration time 4h;
(4)将稀释后样品倒入冻干盘,样品溶液厚度为0.80cm,然后进行预冻,预冻温度-55℃;(4) Pour the diluted sample into the lyophilization tray, the thickness of the sample solution is 0.80cm, and then pre-freeze, the pre-freezing temperature is -55 ℃;
(5)升华干燥,升华干燥温度为-20℃,升华干燥时间为25h;(5) Sublimation drying, sublimation drying temperature is -20 ℃, sublimation drying time is 25h;
(6)解析干燥,解析干燥温度30℃,解析干燥时间20h;(6) Analysis drying, analysis drying temperature 30 ℃, analysis drying time 20h;
(7)下冻干,分装入库,环境温度为20℃,环境湿度为45%。(7) Freeze-dried and stored separately in a warehouse with an ambient temperature of 20 ° C and an ambient humidity of 45%.
冻干后收集样品,其中水分5.6%,醋酸10.8%,光密度0.12,浓缩收率95.89%。Samples were collected after freeze-drying, in which the water content was 5.6%, acetic acid 10.8%, optical density 0.12, and concentrated yield 95.89%.
实施例10Example 10
(1)纳滤前准备,用纯化水清洗纳滤机,纳滤膜材质为聚醚砜纳滤膜,准备纳滤;(1) Prepare before nanofiltration, wash the nanofiltration machine with purified water, the material of the nanofiltration membrane is polyethersulfone nanofiltration membrane, prepare nanofiltration;
(2)西曲瑞克样品溶液40L,加入醋酸2.1L使样品溶液中醋酸含量为5%,开始纳滤,纳滤到样品溶液体积为20L时,加入醋酸2.4L使样品溶液中醋酸含量为15%,继续纳滤,纳滤到样品溶液体积为10L时,加入醋酸2.2L使样品溶液中醋酸含量为30%,继续纳滤;(2) 40L of cetrorelix sample solution, add 2.1L of acetic acid to make the acetic acid content in the sample solution 5%, start nanofiltration. When the volume of the sample solution is 20L, add 2.4L of acetic acid to make the acetic acid content in the sample solution 15%, continue the nanofiltration. When the volume of the sample solution is 10L, add 2.2L of acetic acid to make the content of acetic acid in the sample solution 30%, and continue the nanofiltration;
(3)纳滤7.5h后排放出纳滤液,用30%醋酸水溶液清洗纳滤机,混合纳滤液和清洗液,混合后样品浓度为30g/L,醋酸含量为30%;(3) Nanofiltration is discharged after 7.5h of nanofiltration, the nanofiltration machine is washed with 30% acetic acid aqueous solution, and the nanofiltrate and the cleaning solution are mixed. After mixing, the sample concentration is 30g / L and the acetic acid content is 30%;
(4)将稀释后样品倒入冻干盘,样品溶液厚度为1.15cm,然后进行预冻,预冻温度-43℃;(4) Pour the diluted sample into the lyophilization dish, the thickness of the sample solution is 1.15cm, and then pre-freeze, the pre-freezing temperature is -43 ℃;
(5)升华干燥,升华干燥温度为-15℃,升华干燥时间为25h;(5) Sublimation drying, sublimation drying temperature is -15 ℃, sublimation drying time is 25h;
(6)解析干燥,解析干燥温度20℃,解析干燥时间10h;(6) Analysis drying, analysis drying temperature 20 ℃, analysis drying time 10h;
(7)下冻干,分装入库,环境温度为35℃,环境湿度为55%。(7) Freeze-dried and stored separately in a warehouse with an ambient temperature of 35 ° C and an ambient humidity of 55%.
冻干后收集样品,其中水分5.1%,醋酸6.6%,光密度0.06,浓缩收率94.19%。Samples were collected after lyophilization, in which the moisture was 5.1%, acetic acid was 6.6%, the optical density was 0.06, and the concentrated yield was 94.19%.
对比例1Comparative Example 1
取纯化后的地加瑞克样品溶液共16L,含地加瑞克48g,进行真空旋蒸浓缩,通过真空旋蒸除去样品溶液中的有机溶剂,该步骤优选BUCHI旋转蒸发仪,浓缩过程用时9h,浓缩后样品加入适量醋酸解聚,然后过滤上冻干,条件如下:Take a total of 16L of purified degarelix sample solution, containing 48 g of degarelix, perform vacuum rotary evaporation concentration, and remove the organic solvent in the sample solution by vacuum rotary evaporation. This step is preferably a BUCHI rotary evaporator. The concentration process takes 9h After concentration, the sample is depolymerized by adding appropriate amount of acetic acid, and then filtered and lyophilized under the following conditions:
a.真空浓缩温度:35℃;a. Vacuum concentration temperature: 35 ℃;
b.真空浓缩时间:11h;b. Vacuum concentration time: 11h;
c.样品溶液中醋酸浓度为24%;c. The acetic acid concentration in the sample solution is 24%;
d.冻干前地加瑞克样品浓度为18g/L;d. The concentration of Digaric sample before lyophilization is 18g / L;
浓缩后样品进行冻干步骤,其中冻干溶液厚度为0.75cm,升华温度-5℃,解析干燥温度25℃。浓缩收率93.5%,冻干后样品利用上述方法进行检测,其中水分8.5%,醋酸10.5%,光密度0.12。After concentration, the sample is subjected to a freeze-drying step, in which the thickness of the freeze-dried solution is 0.75 cm, the sublimation temperature is -5 ° C, and the analytical drying temperature is 25 ° C. The concentrated yield was 93.5%. After freeze-drying, the sample was detected by the above method, in which the water content was 8.5%, acetic acid 10.5%, and optical density 0.12.
对比例2Comparative Example 2
取纯化后的地加瑞克样品8.0L,加水稀释之后用于反相色谱柱,然后用15%的醋酸水溶液:乙腈=40:60的溶液洗脱地加瑞克样品,收集合格馏分,随后将馏分通过真空旋蒸的方式进行浓缩以除去里面的乙腈,过滤上冻干,其中冻干溶液厚度为0.75cm,升华温度-8℃,解析干燥温度23℃。冻干后样品利用实施例1中的方法进行检测,其中浓缩收率通过标定为85.25%,水分9.5%,醋酸12.5%,光密度0.06。Take 8.0L of purified degarelix sample, dilute with water and use it for reversed-phase chromatography column, then elute degarelix sample with 15% acetic acid aqueous solution: acetonitrile = 40:60 solution, collect qualified fractions, The fraction was concentrated by vacuum rotary evaporation to remove the acetonitrile inside, filtered and lyophilized. The thickness of the lyophilized solution was 0.75 cm, the sublimation temperature was -8 ° C, and the analytical drying temperature was 23 ° C. After lyophilization, the sample was tested by the method in Example 1, wherein the concentrated yield was calibrated to 85.25%, moisture 9.5%, acetic acid 12.5%, and optical density 0.06.
对比例3Comparative Example 3
纯化后的加尼瑞克样品4.0L,加水稀释之后用于反相色谱柱,然后用10%的醋酸水溶液:乙醇=50:50的溶液洗脱加尼瑞克样品,收集合格馏分,随后将馏分通过真空旋蒸的方式进行浓缩以除去里面的乙醇,过滤上冻干,其中冻干溶液厚度为0.55cm,升华温度-12℃,解析干燥温度20℃。冻干后样品利用实施例1中的方法进行检测,其中浓缩收率通过标定为81.82%,水分6.5%,醋酸7.5%,光密度0.18。Purified Ganarik sample 4.0L, diluted with water and used in reversed-phase chromatography column, and then eluted Ganarik sample with 10% acetic acid aqueous solution: ethanol = 50: 50 solution, collected qualified fractions, and then collected The fraction was concentrated by vacuum rotary evaporation to remove the ethanol inside, filtered and lyophilized. The thickness of the lyophilized solution was 0.55 cm, the sublimation temperature was -12 ° C, and the analytical drying temperature was 20 ° C. After lyophilization, the sample was tested using the method in Example 1, wherein the concentrated yield was 81.82%, moisture 6.5%, acetic acid 7.5%, and optical density 0.18.
对比例4Comparative Example 4
取纯化后的阿巴瑞克样品溶液共30L,含阿巴瑞克68g,进行真空旋蒸浓缩,通过真空旋蒸除去样品溶液中的有机溶剂,该步骤优选BUCHI旋转蒸发仪,浓缩过程用时15h,浓缩后 样品加入适量醋酸解聚,然后过滤上冻干,条件如下:Take 30L of purified abaric sample solution, containing 68g of abaric, and perform vacuum rotary evaporation to condense the organic solvent in the sample solution by vacuum rotary evaporation. In this step, the BUCHI rotary evaporator is preferred. After concentration, the sample is depolymerized by adding appropriate amount of acetic acid, and then filtered and lyophilized under the following conditions:
a.真空浓缩温度:28℃;a. Vacuum concentration temperature: 28 ℃;
b.真空浓缩时间:15h;b. Vacuum concentration time: 15h;
c.样品溶液中醋酸浓度为12%;c. The acetic acid concentration in the sample solution is 12%;
d.冻干前阿巴瑞克样品浓度为35g/L;d. The concentration of Abarek sample before lyophilization is 35g / L;
浓缩后样品进行冻干步骤,其中冻干溶液厚度为0.75cm,升华温度-15℃,解析干燥温度27℃。浓缩收率92.9%,其中水分7.5%,醋酸8.7%,光密度0.10。After concentration, the sample is subjected to a lyophilization step, in which the thickness of the lyophilized solution is 0.75 cm, the sublimation temperature is -15 ° C, and the analytical drying temperature is 27 ° C. The concentrated yield was 92.9%, of which moisture was 7.5%, acetic acid was 8.7%, and optical density was 0.10.
从实施例与对比例的浓缩收率及光密度结果可知,与真空旋蒸浓缩及过柱浓缩+真空旋蒸浓缩工艺相比,收率可以达到93%以上,纳滤工艺浓缩时间更短,效率和产能更高。与过柱浓缩+真空旋蒸浓缩工艺相比,本专利所用纳滤工艺避免了乙腈等有机溶剂的使用,步骤更为简单,成本更低。纳滤工艺结合后续的冻干工艺不仅可以得到水分、醋酸和光密度可控的样品,样品更加稳定,更加适用于大规模工业化生产。It can be seen from the concentration yield and optical density results of the examples and comparative examples that the yield can reach more than 93% and the concentration time of the nanofiltration process is shorter compared with the vacuum rotary evaporation concentration and the column concentration + vacuum rotary evaporation concentration process. Higher efficiency and productivity. Compared with the column concentration + vacuum rotary evaporation concentration process, the nanofiltration process used in this patent avoids the use of organic solvents such as acetonitrile, the steps are simpler and the cost is lower. The nanofiltration process combined with the subsequent freeze-drying process can not only obtain samples with controllable moisture, acetic acid and optical density, the samples are more stable and more suitable for large-scale industrial production.
以上所述仅是本发明的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明原理的前提下,还可以做出若干改进和润饰,这些改进和润饰也应视为本发明的保护范围。The above is only a preferred embodiment of the present invention. It should be pointed out that for those of ordinary skill in the art, without departing from the principles of the present invention, several improvements and retouches can be made. These improvements and retouches also It should be regarded as the protection scope of the present invention.

Claims (11)

  1. 一种GnRH拮抗剂的后处理方法,其特征在于包括以下步骤:A post-processing method for GnRH antagonists, characterized in that it includes the following steps:
    (1)纳滤前准备,安装纳滤膜,用纯化水清洗纳滤机,准备纳滤;(1) Prepare before nanofiltration, install nanofiltration membrane, wash the nanofiltration machine with purified water, prepare nanofiltration;
    (2)开始纳滤,控制样品溶液温度,并在纳滤过程中加入醋酸,控制样品溶液醋酸含量;(2) Start nanofiltration, control the temperature of the sample solution, and add acetic acid during the nanofiltration process to control the acetic acid content of the sample solution;
    (3)纳滤结束,排放纳滤溶液,用醋酸水溶液对纳滤后溶液进行稀释,控制样品浓度;(3) At the end of nanofiltration, discharge the nanofiltration solution, dilute the nanofiltration solution with acetic acid aqueous solution, and control the sample concentration;
    (4)上冻干,将纳滤浓缩后溶液倒入冻干盘,控制溶液厚度,后进行预冻,控制预冻温度;(4) Upper freeze-drying, pour the solution after nanofiltration concentration into the freeze-drying tray, control the thickness of the solution, then pre-freeze, and control the pre-freezing temperature;
    (5)升华干燥;(5) Sublimation and drying;
    (6)解析干燥;(6) Parsing and drying;
    (7)下冻干,将样品分装入库。(7) Lyophilize and load the sample into the library.
  2. 如权利要求1中步骤(2)的方法,其中所述样品溶液温度为:0℃~35℃。The method of step (2) according to claim 1, wherein the temperature of the sample solution is: 0 ° C to 35 ° C.
  3. 如权利要求1中步骤(2)的方法,其中所述样品溶液醋酸含量为:0%~50%。The method of step (2) according to claim 1, wherein the acetic acid content of the sample solution is: 0% to 50%.
  4. 如权利要求1中步骤(3)的方法,其中所述样品浓度为:5g/L~75g/L。The method of step (3) according to claim 1, wherein the sample concentration is: 5 g / L to 75 g / L.
  5. 如权利要求1中步骤(4)的方法,其中所述溶液厚度为:0.5~2.5cm。The method of step (4) according to claim 1, wherein the thickness of the solution is: 0.5 to 2.5 cm.
  6. 如权利要求1中步骤(4)的方法,其中所述预冻温度为:-65℃~-25℃。The method of step (4) according to claim 1, wherein the pre-freezing temperature is: -65 ° C to -25 ° C.
  7. 如权利要求1中步骤(5)的方法,其特征为:升华干燥温度为-15℃~15℃,升华干燥时间为10h~35h。The method of step (5) according to claim 1, wherein the sublimation drying temperature is -15 ° C to 15 ° C, and the sublimation drying time is 10h to 35h.
  8. 如权利要求1中步骤(6)的方法,其特征为:解析干燥温度为15℃~40℃,解析干燥时间为5h~30h。The method of step (6) according to claim 1, wherein the analytical drying temperature is 15 ° C to 40 ° C, and the analytical drying time is 5h to 30h.
  9. 如权利要求1中步骤(7)的方法,其特征为:控制环境温度为15℃~35℃,环境湿度为0%~60%。The method of step (7) according to claim 1, wherein the ambient temperature is controlled to be 15 ° C to 35 ° C, and the ambient humidity is 0% to 60%.
  10. 如上所述权利要求1中一种GnRH拮抗剂的后处理方法,其特征在于:纳滤所用纳滤膜选自聚酰胺纳滤膜、聚醚砜纳滤膜、醋酸纤维素纳滤膜、聚乙烯醇纳滤膜、聚哌嗪纳滤膜。A post-treatment method for GnRH antagonists as claimed in claim 1, characterized in that the nanofiltration membrane used for nanofiltration is selected from polyamide nanofiltration membrane, polyethersulfone nanofiltration membrane, cellulose acetate nanofiltration membrane, poly Vinyl alcohol nanofiltration membrane, polypiperazine nanofiltration membrane.
  11. 如上所述权利要求中任一项方法,其中所述GnRH拮抗剂选自以下物质:地加瑞克、西曲瑞克、加尼瑞克、阿巴瑞克、Nal-Glu。The method of any one of the preceding claims, wherein the GnRH antagonist is selected from the group consisting of degarelix, cetrorelix, ganirelix, abarelix, and Nal-Glu.
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