WO2006012791A1 - Composition containing active prourokinase, its freeze-drying process and lyophilized preparation - Google Patents

Composition containing active prourokinase, its freeze-drying process and lyophilized preparation Download PDF

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Publication number
WO2006012791A1
WO2006012791A1 PCT/CN2005/001149 CN2005001149W WO2006012791A1 WO 2006012791 A1 WO2006012791 A1 WO 2006012791A1 CN 2005001149 W CN2005001149 W CN 2005001149W WO 2006012791 A1 WO2006012791 A1 WO 2006012791A1
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pro
prourokinase
composition
freeze
activity
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PCT/CN2005/001149
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French (fr)
Chinese (zh)
Inventor
Yan Jiang
Tieqiang Hu
Chengzu Xiao
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Shanghai Tasly Pharmaceutical Co., Ltd.
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Publication of WO2006012791A1 publication Critical patent/WO2006012791A1/en

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    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K38/00Medicinal preparations containing peptides
    • A61K38/16Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof
    • A61K38/43Enzymes; Proenzymes; Derivatives thereof
    • A61K38/46Hydrolases (3)
    • A61K38/48Hydrolases (3) acting on peptide bonds (3.4)
    • A61K38/49Urokinase; Tissue plasminogen activator
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/14Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles
    • A61K9/19Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles lyophilised, i.e. freeze-dried, solutions or dispersions
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61PSPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P7/00Drugs for disorders of the blood or the extracellular fluid
    • A61P7/02Antithrombotic agents; Anticoagulants; Platelet aggregation inhibitors
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61PSPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P9/00Drugs for disorders of the cardiovascular system
    • A61P9/10Drugs for disorders of the cardiovascular system for treating ischaemic or atherosclerotic diseases, e.g. antianginal drugs, coronary vasodilators, drugs for myocardial infarction, retinopathy, cerebrovascula insufficiency, renal arteriosclerosis

Definitions

  • the present invention relates to the field of medicine, and in particular to a pharmaceutical composition containing active prourokinase, a lyophilization method thereof, and a lyophilized preparation.
  • BACKGROUND OF THE INVENTION Cardiovascular diseases caused by blood clots are a serious threat to human health, and there is an urgent need for a drug having a good thrombolytic effect and a small side effect.
  • Pro-ukogenase specifically activates plasminogen on the surface of the thrombus, which specifically dissolves the thrombus, while not destroying the fibrinolytic system.
  • Pro-uk also has the advantages of small dosage, safe use, good thrombolytic effect, low recombination rate, no allergic reaction, etc. It is a safe and non-toxic, ideal biological thrombolytic preparation with Broad market pre-study
  • Pro-uk Due to the low content of Pro-uk in natural materials, it is difficult to prepare in large quantities. Since the 1980s, genetic engineering technology has been used to produce recombinant Pro-uk, which is currently in E. coli (Homes WE, et al. Cloning and expression of the gene for pro-urokinase in Escherichia coli. Biotechnology, 1985; 3:923; Winkler ME, et al. Purification and characterization of recombinant single-chain
  • Urokinase produced in Escherichea coli. Biochemistry, 1986; 25:4041) mammalian cells such as mouse IC9 cells, CHO cells, Namalwa cells (Nolli ML, et al. Production and charaterisation of human recombinant single chain
  • the Pro-uk preparation is extremely unstable and is easily cleaved by various proteases into urokinase (UK). At the same time, it is automatically decomposed even in the liquid state even after cryopreservation (Yu Fang et al., Stability observation of recombinant semi-finished recombinant urokinase, Proceedings of the Academy of Military Medical Sciences, 2000, 24 (1): 70); In addition, due to laboratory measurements, clinical use, and daily transportation and storage requirements, it is often necessary to use a dry method to stabilize its activity to prevent degradation. Summary of the invention
  • the inventors of the present invention have obtained a composition containing active prourokinase by long-term research, and the present invention is compared with the existing prourokinase preparation.
  • the composition can be stably stored for a long time.
  • Another aspect of the invention provides a method of preparing the prourokinase composition.
  • compositions of the present invention contain appropriate amounts of Pro-uk, excipients, and buffer solutions and salts.
  • the excipient may be a saccharide and/or a polyhydric alcohol, and one or more selected from the group consisting of sucrose, trehalose, mannitol, lactose, glucose, sorbitol, maltose, etc., wherein mannitol is preferred because mannitol Freezing products are superior to other forms in appearance and lyophilization time, and mannitol has been used in clinical practice for many years, and the price is also cheaper. Therefore, the choice of mannitol can shorten the freeze-drying time of the product and increase the freezing. Dry efficiency, reduce costs.
  • the preferred range of mannitol content is 6% to 12% (weight/volume ratio), and most preferably 6% (weight/volume ratio) from the economical point of view;
  • the buffer may be phosphate buffer and/or Tris-HCl, Wherein the content of the phosphate buffer is preferably in the range of 8 to 25 mmol/L, and the content of the Tris-HCl is preferably in the range of 0.005 to 0.015 mol/L; in the composition, the salt thereof may be sodium chloride, chlorinated
  • the preferred range of sodium content is from 0.03 to 0.20 mol/L; Pro-uk can be any possible concentration, but for ease of lyophilization and medical use, a preferred concentration range is from 1.5 to 5.5 mg/ml.
  • the protective agent can be added if lyophilized to give better results
  • the protective agent may be a protein, preferably albumin, the albumin content is preferably in the range of the composition is 5-7.5% 0 ⁇ 1 (weight/volume ratio)
  • Pro-uk in the above pharmaceutical composition can be prepared according to the prior art method, but is not limited to these methods; the solution can be prepared according to the general solution preparation method, but in order to prevent degradation of Pro-uk, it is best Formulated at low temperatures, the action should be mild during formulation.
  • the invention also provides a freeze-drying method for a solution containing a composition of active Pro-uk, the method comprising the steps of: placing the packaged Pro-uk product in a pre-cooling to -35 ° C to - 45 ° C Dry machine, pre-freeze for 2-4h, then start vacuuming, first temperature rise to -25 °C ⁇ - 30 °C, when the water in the bottle is basically sublimated, the second temperature is raised, and the temperature rises to 25 T: ⁇ At 35 °C, after standing for 0.5h ⁇ 1.5h, the lyophilization can be ended.
  • freeze drying is one of the best methods for clinical and laboratory preservation of protein products.
  • the active Pro-uk-containing pharmaceutical composition of the present invention was freeze-dried by the above method to obtain a frozen Pro-uk preparation.
  • the lyophilized preparation has a good appearance, and has no change in storage for 3 years under storage conditions of -20 ° C and 4 ° C; the long-term stability of the lyophilized preparation under different conditions is observed by an accelerated storage test, and the storage life is performed.
  • the results are as follows: Pro-uk lyophilized preparation can be stored for 173 days at 37 ° C, 2.78 years at 25 ° C, 70.8 years at 4 ° C, and stored at 0 ° C for 1 18 cases with Pro-uk activity loss of 50%.
  • Pro-uk lyophilized preparation can be stored for 20 days at 37 °C, stored for 100 days at 25 °C, stored for 7.6 years at 4 °C, and stored for 1 year at 0 °C, which is sufficient for Pro-uk laboratory. And the need for clinical storage.
  • Figure 1 Pro-uk activity degradation rate curve.
  • Embodiment 1 Preparation of prourokinase
  • Detroit 562 cells were induced by myristyl ester (PMA), total RNA was extracted, and a cDNA library was constructed. A positive clone containing a urokinase gene fragment was obtained by screening, and a human prourokinase full-length cDNA gene was obtained.
  • the gene recombination technique operates to place two transcription units expressing the prourokinase and the dihydrofolate reductase gene in the same vector, which are respectively controlled by metallothionein (MT) and the SV40 early promoter.
  • MT metallothionein
  • pMTSV-du plasmid DNA 20-40 ⁇ g of pMTSV-du plasmid DNA was transfected into CHO-dhfr-cells by phospho-facial coprecipitation, first screened with HAT selection medium, and replaced with l-3xl (T 8 M MTX selective culture after 10 days). The dhfr and MTX dual screening were performed, and the positive transformed cells expressing prourokinase activity were subjected to multiple subcloning and MTX pressure amplification genes, induced by zinc ions, and finally a cell line capable of efficiently expressing prourokinase was screened.
  • the engineered cell strain expressing prourokinase was cultured at a high density using a microcarrier (Cytopore) perfusion culture technique and a low serum medium to obtain a prourokinase-containing material.
  • a microcarrier Cytopore
  • Purified prourokinase is obtained by a four-step method, namely CM cation chromatography, MPG adsorption chromatography, Sephacryl S-200 gel filtration and p-aminobenzidine chromatography.
  • Purified Pro-uk pure product 2mg/ml, mannitol to 6% (weight/volume ratio), albumin to 3%. (weight/volume ratio), concentration of p-acid buffer to 10mmol/L, sodium chloride concentration to 0.05mol/L, dispense into 1 ml ampoules, and freeze-dried to -40 °C beforehand.
  • Machine pre-freezing for 3h, then start vacuuming, first temperature rise to -30 °C, when the water in the bottle is basically sublimated, the second temperature is raised, the temperature is raised to 30 ⁇ , and after stabilization for 1 h, the lyophilization is completed. .
  • Purified Pro-uk pure product 4mg/ml, add mannitol to 6% (weight/volume ratio), Albumin to 3%. (weight/volume ratio), phosphate buffer concentration to 10mmol/L, sodium chloride concentration to 0.10mol/L, dispense into 1 ml ampoules, and put into freeze dryer with pre-cooling to -40 °C , pre-freezing for 3h, then start vacuuming, for the first time to warm up to -30 ° C, when the water in the bottle is basically sublimated, the second temperature is raised, the temperature is raised to 30 ° C, and after stabilization for 1 h, the freezing can be ended. dry.
  • Purified Pro-uk pure product 5mg/ml, mannitol to 10% (weight/volume ratio), albumin to 7%. (weight/volume ratio), phosphate buffer concentration to 20mmol/L, sodium chloride concentration to 0.20mol/L, dispensed into 1 ml ampoules, and placed in a lyophilizer pre-cooled to -40 °C , pre-freezing for 4h, then start vacuuming, for the first time to warm up to -30 ° C, when the water in the bottle is basically sublimated, the second temperature is raised, the temperature is raised to 35 ° C, and after stabilization for 1 h, the freezing can be ended. dry.
  • 3 : ⁇ + + good appearance, low loss of activity; + good appearance; no effect of forming the buffer type, buffer concentration and sodium chloride concentration on the shape of Pro-uk lyophilized preparation
  • the human albumin is completely dissolved and placed in a vial, 1 ml per bottle, and placed in a freeze-drying box for freeze-drying. After drying, the product is taken out for visual inspection, and it can be seen that the phosphate buffer (PB) is contained.
  • PB phosphate buffer
  • the Pro-uk preparation of Tris-HCl has a loose appearance and good morphology (see Table 2). After adding water, the solution dissolves quickly and completely, and the transparency is good, and the original trait is immediately restored.
  • N 4 : + + Appearance is good; + Appearance is good; One is not formed. Stability of Pm-uk lyophilized preparation is observed. Purified Pro-uk pure 2 mg/ml, and mannitol is added to 6 % (weight/volume ratio), albumin to 3%. (weight/volume ratio), the phosphate buffer concentration was 10 mmol/L, the sodium chloride concentration was 0.05 mol/L, and the mixture was dispensed into a 1 ml ampoule and lyophilized as in Example 2.
  • Pro-uk lyophilized preparations are stored at -20 ° C, 4 ° C, 25 ° C and 37 ° C, and regularly (January, March, June, September, December, December) The stability of the activity was observed. It can be seen that the activity is unchanged at -20 and 4, and the activity is decreased by 37% and 81% at 25 °C and 37 °C, respectively (see Table 3).
  • Accelerated storage test of Pro-uk lyophilized product was purified and purified Pro-uk pure 2 mg/ml, mannitol to 6% (weight/volume ratio), albumin to 3%. (weight/volume ratio), phosphate buffer concentration to 10 mmol/L, sodium chloride concentration to 0.05 mol/L, dispensed into a 1 ml ampoule, and lyophilized as in Example 2. Plus The multi-point isothermal stability test (MIS) reported by Greiff et al. (Griff D, et al, An accelerated storage test for predicting the stability of suspension of measles virus dried by sublimation in vacuo.
  • MIS multi-point isothermal stability test
  • the data processing is roughly the same as that described by Greiff et al.
  • the logarithm of the Pro-uk titer measured at different temperatures after storage and the logarithm of the storage time and the corresponding Pro-uk activity.
  • the degradation logarithm was input into the computer, and the Pro-uk activity degradation rate (K1) was determined to be -0.068, -0.161 and -0.443, respectively.
  • the degradation rate curve is shown in Fig. 1. From this curve, the degradation rates of Pro-uk lyophilized preparations at 37° (:, 25 V, 4 ° ⁇ , and 0 ° C were -0.00608, -0.00169, -0.00016, and -0.00011, respectively.
  • Pro-uk's storage life estimation curve was plotted against the time required for Pro-uk activity to degrade 10% or 50% corresponding to each K1 value, and the degradation rate of Pro-uk lyophilized preparation activity was based on the above two curves.
  • Estimation of shelf life Calculated according to the MIS test, the Pro-uk lyophilized preparations were stored at 60 ° C, 70 ° C and 80 ° C, and the time required for loss of activity was 50%, 6.27d, 1.92d and 0.48.
  • the time required for loss of activity of 10% is 0.8d, 0.2d and 0.04d, and thus the storage life curve of Pro-uk can be plotted (Fig. 2). This curve can estimate the loss of Pro-uk activity by 50%.
  • the frozen preparation can be stored for 173 days at 37 °C, 2.78 years at 25 °C, 70.8 years at 4 °C, and 118 years at 0 °C. Also, according to this method, it can be inferred that when the activity loss is 10%, The Pro-uk lyophilized preparation can be stored at 37 ° C for 20 days, stored at 25 ° C for 100 days, stored at 4 ° C for 7.6 years, and stored at 0 ° C for 11 years.

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Abstract

The present invention discloses a pharmaceutical composition containing active prourokinase, its freeze-drying process and lyophilized preparation.

Description

含活性尿激酶原的组合物、 其冻干方法及冻干制剂 技术领域 本发明涉及医药领域, 具体涉及一种含有活性尿激酶原的药物组合 物、 其冻干方法及冻干制剂。 背景技术 由血栓引起的心血管系统疾病严重威胁着人类健康,临床上急需一种 溶栓效果好、 副作用小的药物。 尿激酶原 (Pro-uk) 可专一地激活血栓 表面的纤溶酶原, 进而特异性地溶解血栓, 与此同时不会破坏纤溶系统, 全身出血的副作用小; 经过临床前的动物实验和临床试验验证, Pro-uk 还具有使用剂量小、 使用安全、 溶栓效果好、 再栓率低、 无过敏反应等 优点, 是一种安全无毒的、 理想的生物类溶栓制剂, 具有广阔的市场前 學  TECHNICAL FIELD The present invention relates to the field of medicine, and in particular to a pharmaceutical composition containing active prourokinase, a lyophilization method thereof, and a lyophilized preparation. BACKGROUND OF THE INVENTION Cardiovascular diseases caused by blood clots are a serious threat to human health, and there is an urgent need for a drug having a good thrombolytic effect and a small side effect. Pro-ukogenase (Pro-uk) specifically activates plasminogen on the surface of the thrombus, which specifically dissolves the thrombus, while not destroying the fibrinolytic system. The side effects of systemic bleeding are small; preclinical animal experiments And clinical trials verify that Pro-uk also has the advantages of small dosage, safe use, good thrombolytic effect, low recombination rate, no allergic reaction, etc. It is a safe and non-toxic, ideal biological thrombolytic preparation with Broad market pre-study
由于天然材料中 Pro-uk含量甚微, 难以大量制备, 人们从二十世纪八 十年代开始就开始采用基因工程技术来生产重组 Pro-uk, 目前, 已经在 大肠杆菌 ( Homes WE, et al. Cloning and expression of the gene for pro-urokinase in Escherichia coli. Biotechnology, 1985; 3 :923; Winkler ME, et al. Purification and characterization of recombinant single-chain  Due to the low content of Pro-uk in natural materials, it is difficult to prepare in large quantities. Since the 1980s, genetic engineering technology has been used to produce recombinant Pro-uk, which is currently in E. coli (Homes WE, et al. Cloning and expression of the gene for pro-urokinase in Escherichia coli. Biotechnology, 1985; 3:923; Winkler ME, et al. Purification and characterization of recombinant single-chain
urokinase produced in Escherichea coli. Biochemistry, 1986; 25 :4041 ) 、 哺 乳动物细胞如小鼠 IC9细胞、 CHO细胞、 Namalwa细胞 ( Nolli ML, et al. Production and charaterisation of human recombinant single chain Urokinase produced in Escherichea coli. Biochemistry, 1986; 25:4041), mammalian cells such as mouse IC9 cells, CHO cells, Namalwa cells (Nolli ML, et al. Production and charaterisation of human recombinant single chain
urokinase-type plasminogen activator from mouse cells. Fibnrinolysis, 1989 3 : 101; Nelles L, et al. Characterization of recombinant human single chain urokinase-type plasminogen activator mutants produced by site-specific mutagenesis of Lysine. J Biol Chem, 1987; 262:5682; 李风知等. 人尿激酶 原全长 cDNA在中国仓鼠卵巢细胞中的稳定表达. 生物工程学报, 1991 ; 7 : 1 14; Satoh M, et al. Stable production of recombinant pro-urokinase by human lymphoblastoid Namalwa KJM- 1 cells: Host-cell dependency of the espressed-protein stability. Cytotechnology, 1993; 13 :79; Satoh M, et al. Efficient expression of pro-urokinase by human lymphoblastoid Namalwa KJM- 1 cells using Moloney retroviral promoter. Cytotechnology, 1996; Urobinase-type plasminogen activator from mouse cells. Fibnrinolysis, 1989 3 : 101; Nelles L, et al. Characterization of recombinant human single chain urokinase-type plasminogen activator mutants produced by site-specific mutagenesis of Lysine. J Biol Chem, 1987; :5682; Li Fengzhi et al. Stable expression of human prourokinase full-length cDNA in Chinese hamster ovary cells. Chinese Journal of Biotechnology, 1991; 7 : 1 14; Satoh M, et al. Stable production of recombinant pro-urokinase by human lymphoblastoid Namalwa KJM-1 cells: Host-cell dependency of the espressed-protein stability. Cytotechnology, 1993; 13:79; Satoh M, et al. Efficient expression of pro-urokinase by human lymphoblastoid Namalwa KJM-1 cells using Moloney retroviral promoter. Cytotechnology, 1996;
18: 167 ) 和昆虫细胞 (徐杨等. 人尿激酶原 cDNA在昆虫杆状病毒真核表 达系统中的高效表达. 生物化学杂志, 1993; 6:709 )、骨髓瘤细胞(Weaver WD, et al. New recombinant glycosylated prourokinase for treatment of patients with acute myocardial infarction. J Am Coll Cardiol, 1994; 18: 167) and insect cells (Xu Yang et al. High expression of human prourokinase cDNA in the eukaryotic expression system of insect baculovirus. J. Biol. Chem., 1993; 6:709), myeloma cells (Weaver WD, et Al. New recombinant glycosylated prourokinase for treatment of patients with acute myocardial infarction. J Am Coll Cardiol, 1994;
24: 1242 ) 等中都获得了很高的表达并进行了纯化。 24: 1242) Both were highly expressed and purified.
Pro-uk制剂极不稳定, 容易被多种蛋白酶切割成尿激酶 (UK) , 同时, 在液体状态下, 即使低温保存也会自动分解 (于芳等, 重组尿激酶原半 成品的稳定性观察, 军事医学科学院院刊, 2000, 24 ( 1 ) : 70 ) ; 另夕卜, 由于实验室测定、 临床使用以及日常运输和贮存的需要, 通常需要采用 干燥的方法稳定其活'性防止降解。 发明内容  The Pro-uk preparation is extremely unstable and is easily cleaved by various proteases into urokinase (UK). At the same time, it is automatically decomposed even in the liquid state even after cryopreservation (Yu Fang et al., Stability observation of recombinant semi-finished recombinant urokinase, Proceedings of the Academy of Military Medical Sciences, 2000, 24 (1): 70); In addition, due to laboratory measurements, clinical use, and daily transportation and storage requirements, it is often necessary to use a dry method to stabilize its activity to prevent degradation. Summary of the invention
为了解决现有技术中尿激酶原制剂不稳定的问题,本发明的发明人通过 长期研究, 获得了一种含有活性尿激酶原的组合物, 与现有的尿激酶原制剂 相比, 本发明的组合物可以长期稳定保存。  In order to solve the problem of instability of the prourokinase preparation in the prior art, the inventors of the present invention have obtained a composition containing active prourokinase by long-term research, and the present invention is compared with the existing prourokinase preparation. The composition can be stably stored for a long time.
本发明另一方面提供了该尿激酶原组合物的制备方法。  Another aspect of the invention provides a method of preparing the prourokinase composition.
本发明药物组合物含有适量的 Pro-uk、 赋形剂和缓冲溶液和盐类。 其中, 赋形剂可为糖类和 /或多元醇, 可选择蔗糖、海藻糖、甘露醇、 乳糖、 葡萄糖、 山梨醇、 麦芽糖等中的一种或多种, 其中优选甘露醇, 因为甘露醇冻千的产品无论从外观形态还是冻干时间都优于其它赋形 齐 ij, 而且甘露醇已在临床使用多年, 价格也较便宜, 因此, 选择甘露醇 可以缩短产品的冻干时间, 提高冻干效率, 降低成本。 甘露醇含量的优 选范围为 6%- 12% (重量 /体积比) , 从经济角度考虑, 最优选 6% (重量 /体积比) ; 缓冲液可以为磷酸盐缓冲液和 /或 Tris-HCl, 其中磷酸盐缓冲 液的含量的优选范围为 8-25mmol/L, Tris-HCl 含量的优选范围为 0.005-0.015mol/L; 在该组合物中, 其中的盐类可以为氯化钠, 氯化钠含 量的优选范围为 0.03-0.20mol/L ; Pro-uk可以为任何可能的浓度, 但为了 冻干和医疗上使用的方便, 优选浓度范围为 1.5-5.5mg/ml。  The pharmaceutical compositions of the present invention contain appropriate amounts of Pro-uk, excipients, and buffer solutions and salts. Wherein, the excipient may be a saccharide and/or a polyhydric alcohol, and one or more selected from the group consisting of sucrose, trehalose, mannitol, lactose, glucose, sorbitol, maltose, etc., wherein mannitol is preferred because mannitol Freezing products are superior to other forms in appearance and lyophilization time, and mannitol has been used in clinical practice for many years, and the price is also cheaper. Therefore, the choice of mannitol can shorten the freeze-drying time of the product and increase the freezing. Dry efficiency, reduce costs. The preferred range of mannitol content is 6% to 12% (weight/volume ratio), and most preferably 6% (weight/volume ratio) from the economical point of view; the buffer may be phosphate buffer and/or Tris-HCl, Wherein the content of the phosphate buffer is preferably in the range of 8 to 25 mmol/L, and the content of the Tris-HCl is preferably in the range of 0.005 to 0.015 mol/L; in the composition, the salt thereof may be sodium chloride, chlorinated The preferred range of sodium content is from 0.03 to 0.20 mol/L; Pro-uk can be any possible concentration, but for ease of lyophilization and medical use, a preferred concentration range is from 1.5 to 5.5 mg/ml.
另外, 在上述组合物中, 如果添加保护剂则可得到更好的冻干效果, 保护剂可为蛋白质, 优选白蛋白, 白蛋白在组合物中含量的优选范围为 1 ·5-7.5%0 (重量 /体积比) 需要说明的是上述药物组合物中的 Pro-uk 可按现有技术的方法制 备, 但并不限于这些方法; 溶液可按一般溶液的配制方法配制, 但为防 止 Pro-uk的降解, 最好在低温下配制, 配制时动作应温和。 In the above composition, the protective agent can be added if lyophilized to give better results, the protective agent may be a protein, preferably albumin, the albumin content is preferably in the range of the composition is 5-7.5% 0 · 1 (weight/volume ratio) It should be noted that Pro-uk in the above pharmaceutical composition can be prepared according to the prior art method, but is not limited to these methods; the solution can be prepared according to the general solution preparation method, but in order to prevent degradation of Pro-uk, it is best Formulated at low temperatures, the action should be mild during formulation.
本发明还提供了含活性 Pro-uk的组合物溶液的冷冻干燥方法, 该方 法包括以下步骤: 将分装好的 Pro-uk产品放入预先降温至 -35 °C〜- 45 °C 的冻干机, 预冻 2-4h, 然后开始抽真空, 进行首次升温至 -25 °C〜- 30°C, 当瓶内水分基本升华后进行第二次升温, 使其温度上升至 25 T:〜 35 °C, 稳定后保持 0.5h〜1.5h, 即可结束冻干。  The invention also provides a freeze-drying method for a solution containing a composition of active Pro-uk, the method comprising the steps of: placing the packaged Pro-uk product in a pre-cooling to -35 ° C to - 45 ° C Dry machine, pre-freeze for 2-4h, then start vacuuming, first temperature rise to -25 °C ~ - 30 °C, when the water in the bottle is basically sublimated, the second temperature is raised, and the temperature rises to 25 T:~ At 35 °C, after standing for 0.5h~1.5h, the lyophilization can be ended.
生物制品干燥的方法很多, 但多数可使蛋白质变性。 而冷冻干燥技 术利用冷冻的溶液在低温低压条件下, 从冻结状态不经过液态直接升华 除去水分完成干燥。 冷冻千燥技术可以很好地保持药物原有的理化性质 和生理活性, 且有效成分损失极少。 此外, 冻干制剂特有的疏松多孔结 构, 可以使药物易于重新复水而恢复活性, 而且冻干制剂含水量低, 易 于长期保存。 因此, 冷冻干燥是临床和实验室保存蛋白产品的最佳方法 之一。  There are many methods for drying biological products, but most of them can denature proteins. The freeze-drying technique uses a frozen solution to remove dryness from a frozen state without direct liquid sublimation under low temperature and low pressure conditions. Freezing and drying technology can maintain the original physical and chemical properties and physiological activity of the drug, and the loss of active ingredients is minimal. In addition, the loose porous structure unique to the lyophilized preparation can make the drug easy to rehydrate and restore activity, and the lyophilized preparation has low water content and is easy to store for a long time. Therefore, freeze drying is one of the best methods for clinical and laboratory preservation of protein products.
本发明的含活性 Pro-uk的药物组合物采用以上方法冻干后, 获得了 活性 Pro-uk的冻千制剂。 该冻干制剂外观良好, 在 -20°C和 4°C贮存条件 下, 保存 3年活性无变化; 通过加速贮存试验对冻干制剂在不同条件下 的长期稳定性进行观察, 对贮存寿命进行了估算, 结果如下: Pro-uk活 性损失 50 %的情况下 Pro-uk冻干制剂在 37°C可存放 173d, 25 °C存放 2.78 年, 4°C存放 70.8年, 0°C存放 1 18年; 活性损失 10 %时, Pro-uk冻干制 剂在 37°C可存放 20d, 25 °C存放 100d, 4°C存放 7.6年, 0°C存放 1 1年, 足以满足 Pro-uk实验室和临床贮存的需要。 附图说明  The active Pro-uk-containing pharmaceutical composition of the present invention was freeze-dried by the above method to obtain a frozen Pro-uk preparation. The lyophilized preparation has a good appearance, and has no change in storage for 3 years under storage conditions of -20 ° C and 4 ° C; the long-term stability of the lyophilized preparation under different conditions is observed by an accelerated storage test, and the storage life is performed. Estimated, the results are as follows: Pro-uk lyophilized preparation can be stored for 173 days at 37 ° C, 2.78 years at 25 ° C, 70.8 years at 4 ° C, and stored at 0 ° C for 1 18 cases with Pro-uk activity loss of 50%. Year: When the activity loss is 10%, Pro-uk lyophilized preparation can be stored for 20 days at 37 °C, stored for 100 days at 25 °C, stored for 7.6 years at 4 °C, and stored for 1 year at 0 °C, which is sufficient for Pro-uk laboratory. And the need for clinical storage. DRAWINGS
附图 1 : Pro-uk活性降解速度曲线。  Figure 1 : Pro-uk activity degradation rate curve.
附图 2 : Pro-uk的贮存寿命曲线。 具体实施方式  Figure 2: Storage life curve of Pro-uk. detailed description
以下是实施本发明的具体实施方案的例证。 实施例仅用于说明发明 的目的, 并非意在以任何方式限制本发明的范围。  The following are examples of specific embodiments for carrying out the invention. The examples are for illustrative purposes only and are not intended to limit the scope of the invention in any way.
实施例一 尿激酶原的制备 Embodiment 1 Preparation of prourokinase
(参见中国专利: 重组人糖基化尿激酶原的制备方法, 公告号 (See Chinese patent: Preparation method of recombinant human glycosylated prourokinase, bulletin number
CN1062016C, 公告日: 2001年 2月 14曰) CN1062016C, Announcement Date: February 2001, 14曰)
( 1 ) 尿激酶原基因的克隆和表达载体的构建  (1) Cloning of prourokinase gene and construction of expression vector
采用肉豆寇酯 (PMA)诱导 Detroit 562细胞, 提取细胞总 RNA, 构建 cDNA 文库, 通过筛选获得了含有编码尿激酶基因片段的阳性克隆株, 得到人尿激酶原全长 cDNA基因, 通过多步基因重组技术操作, 将表达 尿激酶原和二氢叶酸还原酶基因的两个转录单位置于同一载体, 分别受 金属硫蛋白 (MT) 和 SV40早期启动子控制。  Detroit 562 cells were induced by myristyl ester (PMA), total RNA was extracted, and a cDNA library was constructed. A positive clone containing a urokinase gene fragment was obtained by screening, and a human prourokinase full-length cDNA gene was obtained. The gene recombination technique operates to place two transcription units expressing the prourokinase and the dihydrofolate reductase gene in the same vector, which are respectively controlled by metallothionein (MT) and the SV40 early promoter.
( 2 ) 转染和筛选高效表达的 CHO工程细胞  ( 2 ) Transfection and screening of highly expressed CHO engineered cells
将 20-40 μ g pMTSV-du 质粒 DNA 通过磷酸麪'共沉淀法转染 CHO-dhfr—细胞, 先用 HAT选择培养基筛选, 10天后换成含 l-3xl(T8M MTX的选择培养基进行 dhfr和 MTX双重筛选, 并对表达有尿激酶原活 性的阳性转化细胞经多次亚克隆和 MTX 加压扩增基因, 锌离子诱导, 最终筛选到能高效表达尿激酶原的细胞株。 20-40 μg of pMTSV-du plasmid DNA was transfected into CHO-dhfr-cells by phospho-facial coprecipitation, first screened with HAT selection medium, and replaced with l-3xl (T 8 M MTX selective culture after 10 days). The dhfr and MTX dual screening were performed, and the positive transformed cells expressing prourokinase activity were subjected to multiple subcloning and MTX pressure amplification genes, induced by zinc ions, and finally a cell line capable of efficiently expressing prourokinase was screened.
( 3 ) CHO工程细胞的培养和放大  (3) CHO engineering cell culture and amplification
采用微载体 (Cytopore) 灌流培养技术和低血清培养基高密度培养表 达尿激酶原的工程细胞株, 得到含尿激酶原的原料。  The engineered cell strain expressing prourokinase was cultured at a high density using a microcarrier (Cytopore) perfusion culture technique and a low serum medium to obtain a prourokinase-containing material.
( 4 ) 重组人尿激酶原的纯化  (4) Purification of recombinant human prourokinase
采用四步法, 即 CM阳离子层析、 MPG吸附层析、 Sephacryl S-200 凝胶过滤和对氨基苯甲脒层析, 即可得到纯品尿激酶原。  Purified prourokinase is obtained by a four-step method, namely CM cation chromatography, MPG adsorption chromatography, Sephacryl S-200 gel filtration and p-aminobenzidine chromatography.
实施例二  Embodiment 2
Pro-uk组合物的真空冷冻干燥  Vacuum freeze drying of Pro-uk composition
经分离纯化后的 Pro-uk纯品 2mg/ml,加甘露醇至 6% (重量 /体积比), 白蛋白至 3%。 (重量 /体积比) , 憐酸盐缓冲液浓度至 10mmol/L, 氯化钠 浓度至 0.05mol/L, 分装到 1 ml的安瓿瓶中, 放入预先降温至 -40°C的冻 干机, 预冻 3h, 然后开始抽真空, 进行首次升温至 -30°C, 当瓶内水分基 本升华后进行第二次升温, 使其温度上升至 30Ό , 稳定后保持 lh, 即可 结束冻干。  Purified Pro-uk pure product 2mg/ml, mannitol to 6% (weight/volume ratio), albumin to 3%. (weight/volume ratio), concentration of p-acid buffer to 10mmol/L, sodium chloride concentration to 0.05mol/L, dispense into 1 ml ampoules, and freeze-dried to -40 °C beforehand. Machine, pre-freezing for 3h, then start vacuuming, first temperature rise to -30 °C, when the water in the bottle is basically sublimated, the second temperature is raised, the temperature is raised to 30 Ό, and after stabilization for 1 h, the lyophilization is completed. .
实施例三  Embodiment 3
Pro-uk组合物的真空冷冻干燥  Vacuum freeze drying of Pro-uk composition
经分离纯化后的 Pro-uk纯品 4mg/ml,加甘露醇至 6%(重量 /体积比), 白蛋白至 3%。 (重量 /体积比) , 磷酸盐缓冲液浓度至 10mmol/L, 氯化钠 浓度至 0.10mol/L, 分装到 l ml的安瓿瓶中, 放入预先降温至 -40°C的冻 干机, 预冻 3h, 然后开始抽真空, 进行首次升温至 -30°C, 当瓶内水分基 本升华后进行第二次升温, 使其温度上升至 30°C, 稳定后保持 lh, 即可 结束冻干。 Purified Pro-uk pure product 4mg/ml, add mannitol to 6% (weight/volume ratio), Albumin to 3%. (weight/volume ratio), phosphate buffer concentration to 10mmol/L, sodium chloride concentration to 0.10mol/L, dispense into 1 ml ampoules, and put into freeze dryer with pre-cooling to -40 °C , pre-freezing for 3h, then start vacuuming, for the first time to warm up to -30 ° C, when the water in the bottle is basically sublimated, the second temperature is raised, the temperature is raised to 30 ° C, and after stabilization for 1 h, the freezing can be ended. dry.
实施例四  Embodiment 4
Pro-uk组合物的真空冷冻干燥  Vacuum freeze drying of Pro-uk composition
经分离纯化后的 Pro-uk纯品 5mg/ml, 加甘露醇至 10% (重量 /体积 比) , 白蛋白至 7%。 (重量 /体积比) , 磷酸盐缓冲液浓度至 20mmol/L, 氯化钠浓度至 0.20mol/L, 分装到 l ml的安瓿瓶中, 放入预先降温至 -40 °C的冻干机, 预冻 4h, 然后开始抽真空, 进行首次升温至 -30°C, 当瓶内 水分基本升华后进行第二次升温,使其温度上升至 35 °C,稳定后保持 lh, 即可结束冻干。  Purified Pro-uk pure product 5mg/ml, mannitol to 10% (weight/volume ratio), albumin to 7%. (weight/volume ratio), phosphate buffer concentration to 20mmol/L, sodium chloride concentration to 0.20mol/L, dispensed into 1 ml ampoules, and placed in a lyophilizer pre-cooled to -40 °C , pre-freezing for 4h, then start vacuuming, for the first time to warm up to -30 ° C, when the water in the bottle is basically sublimated, the second temperature is raised, the temperature is raised to 35 ° C, and after stabilization for 1 h, the freezing can be ended. dry.
实施例五  Embodiment 5
Pro-uk组合物的真空冷冻干燥  Vacuum freeze drying of Pro-uk composition
经分离纯化后的 Pro-uk纯品 2mg/ml,加甘露醇至 6%(重量 /体积比), 白蛋白至 3%。 (重量 /体积比) , 磷酸盐缓冲液浓度至 20mmol/L, 氯化钠 浓度至 0.20mol/L, 分装到 lml的安瓿瓶中, 放入预先降温至 -40°C的冻 干机, 预冻 3h, 然后开始抽真空, 进行首次升温至 -30°C, 当瓶内水分基 本升华后进行第二次升温, 使其温度上升至 30°C, 稳定后保持 lh, 即可 结束冻干。  Purified Pro-uk pure 2 mg/ml, mannitol to 6% (weight/volume ratio), albumin to 3%. (weight/volume ratio), phosphate buffer concentration to 20mmol/L, sodium chloride concentration to 0.20mol/L, dispensed into 1ml ampoules, and placed in a lyophilizer pre-cooled to -40 °C, Pre-freezing for 3h, then start vacuuming, for the first time to warm up to -30 °C, after the water in the bottle is basically sublimated, the second temperature is raised, the temperature is raised to 30 ° C, and after stabilization for 1 h, the freeze-drying is completed. .
实施例六  Embodiment 6
Pro-uk组合物的真空冷冻干燥  Vacuum freeze drying of Pro-uk composition
经分离纯化后的 Pro-uk纯品 2mg/ml,加甘露醇至 6%(重量 /体积比), 白蛋白至 3%。 (重量 /体积比) , Tris-HCl缓冲液浓度至 0.10mol/L, 氯化 钠浓度至 0.05mol/L, 分装到 lml的安瓿瓶中, 放入预先降温至- 40°C的 冻干机, 预冻 3h, 然后开始抽真空, 进行首次升温至 -30°C, 当瓶内水分 基本升华后进行第二次升温, 使其温度上升至 30°C, 稳定后保持 lh, 即 可结束冻干。  Purified Pro-uk pure 2 mg/ml, mannitol to 6% (weight/volume ratio), albumin to 3%. (weight/volume ratio), Tris-HCl buffer concentration to 0.10mol/L, sodium chloride concentration to 0.05mol/L, dispense into 1ml ampoules, and freeze-dried to -40 °C beforehand. Machine, pre-freezing for 3h, then start vacuuming, first temperature rise to -30 °C, when the water in the bottle is basically sublimated, the second temperature is raised, the temperature is raised to 30 °C, and it is kept for 1h after stabilization, then it can be finished. Freeze dried.
实施例七  Example 7
不同浓度赋形剂和保护剂对 Pro- uk冻千制剂形态及活性的影响 经分离纯化后的 Pro-uk纯品 2mg/ml, 加磷酸盐缓冲液浓度至 10mmol/L, 氯化钠浓度至 0.05mol/L, 并加不同浓度赋形剂和保护剂以评 价它们对 pro-uk冻干制剂形态及活性的影响。 Pro-uk的活性测定采用改良 的琼脂糖一纤维蛋白溶解圈法 (参见 Xiao C, Huang Z, Lin F, et al. High density cultivation of genetically-engineered CHO cell line with microcarrier culture system. Chin Med Sci J, 1994, 9(2): 71-74 )。 以下未具 体说明, 则活性测定均采用同样方法。 表一: 不同浓度赋形剂和保护剂对 pro-uk冻干制剂形态及活性的影响 类型 赋形剂和保护剂的含量 (%) 保护率 Effects of different concentrations of excipients and protective agents on the morphology and activity of Pro-uk frozen preparations. Purified Pro-uk pure 2mg/ml, plus phosphate buffer concentration to 10 mmol/L, sodium chloride concentration to 0.05 mol/L, and different concentrations of excipients and protectants were added to evaluate their effects on the morphology and activity of the pro-uk lyophilized formulation. The activity of Pro-uk was determined using a modified agarose-fibrinolytic method (see Xiao C, Huang Z, Lin F, et al. High density cultivation of genetically-engineered CHO cell line with microcarrier culture system. Chin Med Sci J , 1994, 9(2): 71-74). Unless otherwise specified below, the same method was employed for the activity measurement. Table 1: Effect of different concentrations of excipients and protective agents on the morphology and activity of pro-uk lyophilized preparations Types of excipients and protective agents (%) Protection ratio
1 2 3 -1 5 6 7 8 9 ( % ) 甘露醇 一 一 + + + + 33 乳糖 一 ― ― + + + + + 28 1 2 3 -1 5 6 7 8 9 ( % ) Mannitol One + One + + 33 Lactose One ― ++ + + + + + 28
3 %。白蛋白 +甘露醇 ― 一 + + + + 80 3 %. Albumin + mannitol - one + + + + 80
+ + + +  + + + +
Ν=3 : · + +外观形态好, 活性损失小; +外观形态好; 一不成形 实施例八 缓冲液类型、 缓冲液浓度及氯化钠的浓度对 Pro-uk冻干制剂外形的 影响 含有不同的缓冲液和氯化钠浓度的 Pro-uk产品, 加入 7%的甘露醇、 5%。的人血白蛋白使其完全溶解后装入小瓶, 每瓶 l ml, 放入冻干箱内进 行冷冻干燥, 待干燥完毕后, 取出产品进行外观检查, 可以看出含有磷 酸缓冲液(PB )、 Tris-HCl的 Pro-uk制剂外观疏松,形态良好(见表二), 加水后溶解迅速而完全、 透明度好, 立即恢复原来的性状。 Ν=3 : · + + good appearance, low loss of activity; + good appearance; no effect of forming the buffer type, buffer concentration and sodium chloride concentration on the shape of Pro-uk lyophilized preparation For Pro-uk products with different buffer and sodium chloride concentrations, add 7% mannitol, 5%. The human albumin is completely dissolved and placed in a vial, 1 ml per bottle, and placed in a freeze-drying box for freeze-drying. After drying, the product is taken out for visual inspection, and it can be seen that the phosphate buffer (PB) is contained. The Pro-uk preparation of Tris-HCl has a loose appearance and good morphology (see Table 2). After adding water, the solution dissolves quickly and completely, and the transparency is good, and the original trait is immediately restored.
表二: 不同缓冲液浓度对 pro-uk冻千产品外观形态的影响 缓冲液类型 氯化钠 (mol/L ) Table 2: Effect of different buffer concentrations on the appearance of pro-uk frozen product. Buffer type Sodium chloride (mol/L)
0.50 0 0 025 O20 0Λ 5 0J 0 0 Λ5 l OmM PB + ― + + +■ + + + + +0.50 0 0 025 O20 0Λ 5 0J 0 0 Λ5 l OmM PB + ― + + +■ + + + + +
20mM PB + + ― ― + + + + + +20mM PB + + ― ― + + + + + +
9.2mM NaAc ― ― ― ― ― ― ―9.2mM NaAc ― ― ― ― ― ―
5mM NaAc ― 一 ― ― ― ― 一5mM NaAc ― 一― ― ― ―
0.01 M Tris-HCl + + + + + + 0.01 M Tris-HCl + + + + + +
N=4 : + +外观形态良好; +外观形态好; 一不成形 实施例九 Pm-uk冻干制剂的稳定性观察 经分离纯化后的 Pro-uk纯品 2mg/ml,加甘露醇至 6%(重量 /体积比), 白蛋白至 3%。(重量 /体积比) , 磷酸盐缓冲液浓度至 10mmol/L, 氯化钠 浓度至 0.05mol/L, 分装到 1 ml 的安瓿瓶中, 按实施例二的方法冻干。 pro-uk冻干制剂放入 -20°C、 4°C、 25 °C和 37°C下保存, 并定期 (1月、 3 月、 6月、 9月、 12月、 15月) 对其活性的稳定性进行观察。 可见在 -20 和4 下保存, 其活性无变化; 而在 25 °C和 37°C下保存, 其活性分别 下降 37%和 81% (见表三) 。  N=4 : + + Appearance is good; + Appearance is good; One is not formed. Stability of Pm-uk lyophilized preparation is observed. Purified Pro-uk pure 2 mg/ml, and mannitol is added to 6 % (weight/volume ratio), albumin to 3%. (weight/volume ratio), the phosphate buffer concentration was 10 mmol/L, the sodium chloride concentration was 0.05 mol/L, and the mixture was dispensed into a 1 ml ampoule and lyophilized as in Example 2. Pro-uk lyophilized preparations are stored at -20 ° C, 4 ° C, 25 ° C and 37 ° C, and regularly (January, March, June, September, December, December) The stability of the activity was observed. It can be seen that the activity is unchanged at -20 and 4, and the activity is decreased by 37% and 81% at 25 °C and 37 °C, respectively (see Table 3).
表三: Pro-uk保存在 -20°C、 4°C、 25 °C和 37°C时的活性 (IU/ml) 时间 (月) -20 °C 4°C 25 °C 37°C Table 3: Pro-uk activity at -20 ° C, 4 ° C, 25 ° C and 37 ° C (IU/ml) Time (month) -20 °C 4 °C 25 °C 37 °C
1 26704 27627 27627 267041 26704 27627 27627 26704
3 25630 25632 21471 206693 25630 25632 21471 20669
6 23000 21200 1 8023 125006 23000 21200 1 8023 12500
9 27253 26786 21429 150009 27253 26786 21429 15000
12 25522 26055 18593 667812 25522 26055 18593 6678
1 5 25070 25000 1 7500 5000
Figure imgf000008_0001
1 5 25070 25000 1 7500 5000
Figure imgf000008_0001
Pro-uk冻干产品的加速贮存试验 经分离纯化后的 Pro-uk纯品 2mg/ml, 加甘露醇至 6% (重量 /体积比) , 白蛋白至 3%。 (重量 /体积比) , 磷酸盐缓冲液浓度至 10mmol/L, 氯化钠 浓度至 0.05mol/L, 分装到 1ml的安瓿瓶中, 按实施例二的方法冻干。 加 速试验采用 Greiff等 ( Griff D, et al, An accelerated storage test for predicting the stability of suspension of measles virus dried by sublimation in vacuo. J Immunol, 1965; 94: 395 ) 报道的多点等温稳定性试验 (MIS), 将冻千后的 Pro-uk小瓶分别置于 60°C (20瓶)、 70 °C (12瓶)、 80 °C (5瓶) 的水浴中, 每间隔 24h从 3种不同温度水浴中取一瓶, 测 Pro-uk的活性(表 五) 。 Accelerated storage test of Pro-uk lyophilized product was purified and purified Pro-uk pure 2 mg/ml, mannitol to 6% (weight/volume ratio), albumin to 3%. (weight/volume ratio), phosphate buffer concentration to 10 mmol/L, sodium chloride concentration to 0.05 mol/L, dispensed into a 1 ml ampoule, and lyophilized as in Example 2. Plus The multi-point isothermal stability test (MIS) reported by Greiff et al. (Griff D, et al, An accelerated storage test for predicting the stability of suspension of measles virus dried by sublimation in vacuo. J Immunol, 1965; 94: 395) ), the Pro-uk vials after freezing are placed in a water bath of 60 ° C (20 bottles), 70 ° C (12 bottles), 80 ° C (5 bottles), and water baths from 3 different temperatures at intervals of 24 hours. Take a bottle and measure the activity of Pro-uk (Table 5).
表五: MIS试验尿激酶原测定结果  Table 5: MIS test results of prourokinase determination
60 °C 70 °C 80 °C 60 °C 70 °C 80 °C
时间 活性 时间 . 活性 时间 活性 Time active time . activity time activity
(d) LogIU/ml (d) LogIU/ml (d) LogIU/ml(d) LogIU/ml (d) LogIU/ml (d) LogIU/ml
0 5.1 03 0 5.1 03 0 5.1030 5.1 03 0 5.1 03 0 5.103
1 5.048 1 5.005 1 4.5571 5.048 1 5.005 1 4.557
2 5.022 2 4.862 2 3.902 5.022 2 4.862 2 3.90
3 4.954 3 4.752 3 3.533 4.954 3 4.752 3 3.53
4 4.935 4 4.580 4 3.244 4.935 4 4.580 4 3.24
5 4.927 5 4.291 5 2.885 4.927 5 4.291 5 2.88
6 4.883 6 4.229 6 4.883 6 4.229
7 4.81 8 7 4.015  7 4.81 8 7 4.015
8 4.699 8 3.799  8 4.699 8 3.799
9 4.622 9 3.398  9 4.622 9 3.398
10 4.589 10 3.286  10 4.589 10 3.286
1 1 4.426 1 1 3.081  1 1 4.426 1 1 3.081
12 4.380 12 2.970  12 4.380 12 2.970
13 4.3 19  13 4.3 19
14 4.163  14 4.163
1 5 4.097  1 5 4.097
16 4.000  16 4.000
17 3.999  17 3.999
21 3.875  21 3.875
28 3.476  28 3.476
3 1 3.327 数据处理与 Greiff等介绍的方法大致相同,将不同温度贮存后测得的 Pro-uk效价的对数与各效价相对应的时间、 贮存时间的对数与各相对应 的 Pro-uk 活性降解的对数分别输入计算机, 即可求出不同贮存时间时 Pro-uk活性降解速度 (K1) 分别为 -0.068、 -0.161和 -0.443, 其降解速度 曲线如附图 1。 通过该曲线可计算出 Pro-uk冻干制剂在 37° (:、 25 V、 4 °〇和 0°C时的降解速度分别为 -0.00608、 -0.00169、 -0.00016和 -0.00011。 据降解速度 K1和各 K1值相对应的 Pro-uk活性降解 10%或 50%所需的 时间,绘制 Pro-uk的贮存寿命估算曲线,依据上述两条曲线即可对 Pro-uk 冻干制剂活性的降解速度和贮存寿命进行估算: 依据 MIS 试验计算出 Pro-uk冻干制剂在 60°C、 70°C和 80°C贮存时, 其活性损失 50%时所需 时间为 6.27d、 1.92d和 0.48山 活性损失 10%时所需时间为 0.8d、 0.2d 和 0.04d, 并由此可绘制出 Pro-uk的贮存寿命曲线(附图 2)。 由此曲线可 估算出 Pro-uk活性损失 50%的情况下 Pro-uk冻千制剂在 37Ό可存放 173d; 25°C存放 2.78年, 4°C存放 70.8年, 0°C存放 118年。 同样根据此 方法也可推测出活性损失 10%时, Pro-uk冻干制剂在 37°C可存放 20d, 25°C存放 100d, 4°C存放 7.6年, 0°C存放 11年。 3 1 3.327 The data processing is roughly the same as that described by Greiff et al. The logarithm of the Pro-uk titer measured at different temperatures after storage and the logarithm of the storage time and the corresponding Pro-uk activity. The degradation logarithm was input into the computer, and the Pro-uk activity degradation rate (K1) was determined to be -0.068, -0.161 and -0.443, respectively. The degradation rate curve is shown in Fig. 1. From this curve, the degradation rates of Pro-uk lyophilized preparations at 37° (:, 25 V, 4 ° 〇, and 0 ° C were -0.00608, -0.00169, -0.00016, and -0.00011, respectively. According to the degradation rate K1 Pro-uk's storage life estimation curve was plotted against the time required for Pro-uk activity to degrade 10% or 50% corresponding to each K1 value, and the degradation rate of Pro-uk lyophilized preparation activity was based on the above two curves. Estimation of shelf life: Calculated according to the MIS test, the Pro-uk lyophilized preparations were stored at 60 ° C, 70 ° C and 80 ° C, and the time required for loss of activity was 50%, 6.27d, 1.92d and 0.48. The time required for loss of activity of 10% is 0.8d, 0.2d and 0.04d, and thus the storage life curve of Pro-uk can be plotted (Fig. 2). This curve can estimate the loss of Pro-uk activity by 50%. In the case of Pro-uk, the frozen preparation can be stored for 173 days at 37 °C, 2.78 years at 25 °C, 70.8 years at 4 °C, and 118 years at 0 °C. Also, according to this method, it can be inferred that when the activity loss is 10%, The Pro-uk lyophilized preparation can be stored at 37 ° C for 20 days, stored at 25 ° C for 100 days, stored at 4 ° C for 7.6 years, and stored at 0 ° C for 11 years.

Claims

权利要求 Rights request
1. 一种尿激酶原组合物, 含有适量的尿激酶原、 赋形剂、 缓冲溶液和盐 类。 A prourokinase composition comprising an appropriate amount of prourokinase, an excipient, a buffer solution and a salt.
2. 权利要求 1所述的组合物, 其中还包括保护剂。 2. The composition of claim 1 further comprising a protective agent.
3. 权利要求 1或 2所述的组合物, 其中尿激酶原含量为 1.5-5.5mg/ml。 3. The composition of claim 1 or 2, wherein the prourokinase content is from 1.5 to 5.5 mg/ml.
4. 权利要求 2 所述的组合物, 其中所说的保护剂是浓度为 1.5%。-7.5%。 4. The composition of claim 2 wherein said protective agent is at a concentration of 1.5%. -7.5%.
(重量 /体积比) 的白蛋白。  (weight/volume ratio) of albumin.
5. 权利要求 1或 2所述的组合物, 其中的赋形剂是糖类和 /或多元醇。  5. The composition of claim 1 or 2 wherein the excipient is a saccharide and/or a polyol.
6. 权利要求 6所述的组合物, 其中的糖类和 /或多元醇选自甘露醇、 蔗 糖、 海藻糖、 甘露醇、 乳糖、 葡萄糖、 山梨醇、 麦芽糖中的一种或几 禾中。 6. The composition of claim 6 wherein the saccharide and/or polyol is selected from the group consisting of mannitol, sucrose, trehalose, mannitol, lactose, glucose, sorbitol, maltose.
7. 权利要求 1 或 2 所述的组合物, 其中的缓冲溶液是憐酸盐缓冲液或 Tris-HCl缓冲液。  7. The composition of claim 1 or 2 wherein the buffer solution is a diacid buffer or a Tris-HCl buffer.
8. 权利要求 1或 2所述的组合物, 其中的盐类是浓度为 0.03-0.20mol/L 的氯化钠。 The composition according to claim 1 or 2, wherein the salt is sodium chloride having a concentration of 0.03 to 0.20 mol/L.
9. 权利要求 1至 8中任意组合物的冷冻干燥方法,该方法包括以下步骤: i ) 取权利要求 1至 8的任意组合物, 放入预先降温至 -35 °C〜- 45 9. A method of freeze-drying any of claims 1 to 8, the method comprising the steps of: i) taking any of the compositions of claims 1 to 8 and pre-cooling to -35 ° C to - 45
°C的冻干机, 预冻 2-4h; °C lyophilizer, pre-freezing 2-4h;
ii ) 然后开始抽真空, 升温至 -25 °C〜- 35 °C ;  Ii) Then start vacuuming and heat up to -25 °C ~ - 35 °C;
iii ) 当容器内水分基本升华后进行第二次升温,使其温度上升至 -25 °C〜-35 °C, 稳定后保持 0.5h〜1.5h。  Iii) When the water in the container is substantially sublimated, the temperature is raised for the second time, and the temperature is raised to -25 °C to -35 °C, and is maintained for 0.5h~1.5h after stabilization.
1 0.由权利要求 9的方法制备得到的尿激酶原冻千制剂。  10. A prourokinase procalculin prepared by the method of claim 9.
PCT/CN2005/001149 2004-08-06 2005-07-28 Composition containing active prourokinase, its freeze-drying process and lyophilized preparation WO2006012791A1 (en)

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