Patent Application
20230192832
The sequence listing associated with this application is provided in txt format and is hereby incorporated by reference in its entirety into the specification. The name of the text file containing the sequence listing is FPCH22160216US.sequence listing.txt; the file is 6 KB; was created on Aug. 16, 2022, and is being submitted via EFS-Web with the filing of the specification.
The present invention belongs to the technical field of biomedicine, and in particular relates to a pharmaceutical formulation comprising bevacizumab.
Highly specific, effective and safe protein (antibody) drugs, especially therapeutic antibody drugs, have become a global hotspot for drug development. Bevacizumab (Chinese trade name: ; English trade name: Avastin®) is developed by Roche, and is first approved for marketing by the US FDA in 2004 for widely used in the treatment of a variety of malignant tumors, such as metastatic colorectal cancer, non-small cell lung cancer, renal cell cancer, ovarian cancer, cervical cancer and glioblastoma. Bevacizumab is a humanized monoclonal IgG1 antibody, and can specifically bind to the vascular endothelial growth factor, thus blocking its binding to receptors (Flt-1 and KDR) on the surface of endothelial cells, avoiding a series of subsequent cascade reactions, inhibiting the neogenesis of abnormal blood vessels, thereby preventing the growth and spread of tumors, and finally achieving the purpose of eliminating tumors. Furthermore, bevacizumab has a strong specificity, and usually does not interfere with other targets while blocking the VEGF pathway. Since bevacizumab can destroy abnormal blood vessels and normalize mature blood vessels, it is usually used for combined chemotherapy, that is, used together with other drugs against tumor tissues. In such therapies, bevacizumab can effectively assist and consolidate the therapeutic effect of other drugs (Presta L G, Chen H, O\'Connor S J, Chisholm V, Meng Y G, Krummen L, et al. Cancer Res 1997; 57:4593-9).
In the study of monoclonal antibody drugs, the study of pharmaceutical formulations plays an important role. IgG1 monoclonal antibodies are mainly used as liquid formulations for injection, and the protein in the liquid formulations is apt to form aggregates or particles, which will affect the stability. Maintaining the good physical, chemical and biological stability of monoclonal antibody liquid formulations during the storage has become an issue that cannot be ignored. There is an urgent need for the development of stable protein formulations which can meet the requirements of the pharmaceutical industry.
It is an objective of the present invention to provide a pharmaceutical formulation comprising bevacizumab.
According to the present invention, the buffer system is examined with bevacizumab (HLX04 protein) as the subject of the study by means of screening and formula optimization; and the effects of different ion strengths, pH, stabilizer type, types and content of the surfactant, etc. in the buffer system on the protein stability are examined under high-temperature acceleration condition by designing a single-factor experiment. The proportion range of the content of each component in the formulation is experimentally determined.
According to the present invention, the detection items involved in the evaluation of the stability of the protein in the formulation under high-temperature acceleration condition include: appearance, protein concentration (A280), osmolality, purity (SEC-HPLC, CEX-HPLC, and CE-SDS), average particle size of the protein, PdI (DLS), and the number of sub-visible particles (FlowCam).
A preferred pharmaceutical formulation of the present invention includes: bevacizumab, a buffer, a stabilizer, and a surfactant, wherein the bevacizumab is a recombinant humanized monoclonal antibody with a content of preferably 10-100 mg/mL, preferably 10-80 mg/mL, or 10-50 mg/mL, and more preferably 10 mg/mL, 25 mg/mL, 50 mg/mL, and 80 mg/mL.
Preferably, the buffer of the present invention includes: one of a histidine-histidine hydrochloride system, an acetic acid-sodium acetate system, and a histidine hydrochloride-sodium acetate system; more preferably, the buffer is an acetic acid-sodium acetate buffer system, or a histidine hydrochloride-sodium acetate buffer system; and most preferably, the buffer is a histidine hydrochloride-sodium acetate buffer system.
The pH of the pharmaceutical formulation is preferably 5.0-5.6, and preferably 5.3.
In the buffer system, the histidine-histidine hydrochloride buffer, acetic acid-sodium acetate buffer, and histidine hydrochloride-sodium acetate buffer are preferably at a concentration of 10-30 mM, wherein the histidine hydrochloride-sodium acetate buffer is preferably at a concentration of 10 mM.
The formulation of the present invention also comprises a stabilizer for maintaining the stability of the protein drug and maintaining the function of the protein drug without being affected by changes in the conditions (such as changes in freezing, lyophilization, or other preparation conditions). The stabilizer is preferably selected from: one or more of sucrose, trehalose, mannitol, sorbitol or glycine; and the stabilizer is preferably sucrose, trehalose, and sorbitol, and more preferably is sucrose and sorbitol. The content of the stabilizer is preferably: 20-100 mg/mL; more preferably: 25-50 mg/mL; and preferably: 45 mg/mL.
The surfactant is a conventional surfactant in the art, and preferably, a nonionic surfactant. An example of the surfactant herein is preferably polysorbate, and more preferably, Tween 80. The content of the surfactant is preferably 0.1-0.5 mg/mL, and preferably 0.2 mg/mL.
The dosage forms of the pharmaceutical formulation are conventional dosage forms in the art, preferably including a liquid formulation or lyophilized formulation for injection. The liquid formulation for injection preferably includes a formulation for subcutaneous injection, a formulation for intravenous injection, a formulation for intraperitoneal administration, a formulation for intramuscular injection, a formulation for intravenous/subcutaneous injection or a formulation for intravitreal injection. The liquid formulation for injection preferably includes a formulation of aqueous solution for injection and a formulation for prefilled syringe injection, preferably the formulation of aqueous solution for injection, and the formulation of aqueous solution for injection can be used for intravenous injection or intravitreal injection.
A preferred formulation of bevacizumab is determined on the basis of the single-factor study results and the composition thereof is as follows: 25 mg/mL of bevacizumab, 10 mM of histidine hydrochloride-sodium acetate (pH 5.3), 45 mg/mL of sorbitol, and 0.2 mg/mL of Tween 80. According to the above-mentioned proportion, a finished product is prepared and the stability of the formulation formula of the present invention is verified by means of accelerated stability study and repeated freezing and thawing stability study. The formulations of the present application are compared with different formulations in stability tests. It can be seen according to the analysis of the results regarding molecular isomers, charge isomers and sub-visible particles in high-temperature acceleration tests that the stability of bevacizumab in the formulation of the present invention is significantly better than that of other formulations.
wherein (A) illustrates the Tagg temperatures at week 0, (B) illustrates the KD values at week 0; (C) illustrates the average particle sizes and polydispersity indexes (PDI) of the HLX04 protein in the buffer systems at week 0 and after standing at 40° C. for 4 weeks; (D) illustrates the Pk 1 Area percentage of the HLX04 protein in the buffer system at week 0 and after standing at 40° C. for 4 weeks; (E) change trend of the content of SEC aggregates at 40° C.; and (F) change trend of the content of CEX main peaks at 40° C.
wherein (A) is a diagram indicating thermodynamic stability comparison, (B) shows change trend of the average particle size of the protein at 40° C.; (C) shows change trend of the content of SEC aggregates at 40° C.; (D) shows change trend of the content of CEX main peaks at 40° C.; and (E) shows change trend of the number of sub-visible particles (by FlowCam) at 40° C.
wherein (A) is a diagram indicating thermodynamic stability comparison, (B) shows change trend of the average particle size of the protein at 40° C.; (C) shows change trend of the content of SEC aggregates at 40° C.; (D) shows change trend of the content of CEX main peaks at 40° C.; and (E) shows change trend of the number of sub-visible particles (by FlowCam) at 40° C.
wherein figure (A) shows a diagram indicating thermodynamic stability comparison, (B) shows change trend of the average hydrodynamic size and PdI at 40° C. measured by DLS; (C) shows change trend of the content of SEC aggregates at 40° C.; (D) shows change trend of the content of CEX main peaks at 40° C.; and (E) shows change trend of the number of sub-visible particles (by FlowCam) at 40° C.
The following examples are intended to provide those of ordinary skill in the art with a complete disclosure and description regarding how to implement and use the present invention, and are not intended to limit the scope of the invention, nor are they intended to mean that the experiments below are all the experiments implemented and the only experiments that can be implemented.
The chemical reagents used in the examples are all commercially available analytical reagents, and the recombinant monoclonal antibody can be a monoclonal antibody prepared according to any known method. The following exemplary antibody preparation method is provided by Shanghai Henlius Biotechnology Co., Ltd., and the exemplary method does not limit the present invention.
The antibody protein used in this study is HLX04 (bevacizumab), and the antibody is prepared according to the conventional method in the prior art, wherein the light and heavy chain sequences thereof are as follows:
The appearance is detected by visual inspection. The sample bottle is wiped clean and placed in SC-4000A clarity tester (Huanghai Medicine & Drug Testing Instruments, Shanghai) in a dark room, the illumination intensity is adjusted to 1000-1500 Lux, the sample is placed at the edge (25 cm) of the light blocking plate, and the color, clarity, visible particles, etc. are visually inspected against a black ground and a white background, respectively while holding the neck of the sample penicillin bottle.
The absorbance of the sample at the wavelength of 280 nm is measured and the protein concentration is calculated by using a Trinean Dropsense 16 protein concentration meter. The extinction coefficient is 1.60 mL*mg−1*cm−1.
1.3. pH
The sample (25 μL) is taken and the pH thereof is determined by using a Mettler Toledo multifunctional parameter meter, which is calibrated with three standard solutions (the pH being 4.01, 7.00 and 9.21, respectively), so that the electrode slope is in the range of 95%-105%.
The determination is carried out according to General Rule 0632 “Determination of Osmolality”, Pharmacopoeia of the People's Republic of China (2015 Edition) by using an Advanced Osmo PRO osmometer. The sample (20 μL) and two 290 mOsmol/kg of osmolality standards are taken, and the osmolality values of the sample and the standards are determined by using the cryoscopic method.
The viscosity of the sample is measured by using the BROOKFIELD DV2T viscometer. The external water bath kettle is switched on, the temperature is set at 25° C., 0.5 mL of the sample is suctioned up and dropwise added into the center of the sample cup, the rotor speed is set so that the measurement torque falls within 40%-60%, and the viscosity of the sample is determined.
The particle size and particle size distribution of the sample are determined by using the DynaPro PlateReader-III high-throughput dynamic and static light scattering instrument. In a clean bench, the sample (25 μL) is taken and added to the microwells of a 384-well plate, and after the addition is completed, the plate is covered with a film. The film-covered 384-well plate is placed into a refrigerated centrifuge and centrifuged to remove the bubbles in the microwells of the sample. The specific parameter settings of the instrument are shown in Table 1.
The aggregation temperature of the sample is determined by using the DynaPro PlateReader-III high-throughput dynamic and static light scattering instrument. In a clean bench, the sample (25 μL) is taken and added to the microwells of a 384-well plate, and after the addition is completed, the plate is covered with a film. The film-covered 384-well plate is placed into a refrigerated centrifuge and centrifuged to remove the bubbles in the microwells of the sample. The specific parameter settings of the instrument are shown in Table 2.
The thermodynamic parameters Tm onset, Tm1 and Tm2 values related to the protein conformation are determined by using the TA Nano DSC differential scanning calorimeter. The protein sample is diluted to a concentration of 1 mg/mL with a placebo, and the diluted protein sample and the corresponding placebo are respectively placed in a 96-well sample plate, and after degassing treatment, placed under a pressure condition of 300±50 Kpa. The pre-equilibration time is set as 600 s, the temperature range is set as 25° C.-100° C., and the scanning rate is set as 1° C./min. The DSC curves of the protein sample and placebo are collected, respectively, with three times of scanning for the placebo and one scanning for the protein sample. The Two State Scaled model is selected for data fitting.
The SEC-HPLC detection is carried out by using the Agilent 1260 high-performance liquid chromatography with a TOSOH TSKgel G3000 chromatographic column (7.8 mm×300 mm, 5 μm). The column temperature is room temperature (without controlling the temperature), the temperature of the sample tray is 2° C.-8° C., the mobile phase consists of 100 mM of sodium dihydrogen phosphate and 0.5% of sodium chloride, the pH is 6.8, and isocratic elution is carried out. The elution time is 30 min, and the flow rate is 0.5 mL/min. The detection wavelength is 280 nm, the concentration of the sample is diluted to 1 mg/mL, and the injection volume is 50 μL.
The CEX-HPLC detection is carried out by using the Agilent 1260 high-performance liquid chromatography with a Thermo ProPac™WCX-10 chromatographic column (4 mm×250 mm, 10 μm). The column temperature is 35° C., the sample tray temperature is 2° C.-8° C., the mobile phase A consists of 50 mM of phosphate buffer (the pH being 6.10), the mobile phase B (the pH being 6.10) consists of 50 mM of phosphate buffer and 300 mM of sodium chloride, and gradient elution is carried out. The elution gradient can be seen in Table 3, and the flow rate is 1.0 mL/min. The detection wavelength is 280 nm, the concentration of the sample is diluted to 1 mg/mL, and the injection volume is 50 μL.
The determination is carried out according to General Rule 3127 “Determination of Molecular Size Heterogeneities in Monoclonal Antibodies (CE-SDS method)”, Pharmacopoeia of the People's Republic of China (2015 Edition). Detection is carried out using non-reducing and reducing CE-SDS. The Beckman Coulter PA800 plus capillary electrophoresis apparatus and an uncoated capillary with a total length of 67 cm and an inner diameter of 50 μm are used. Injection: 5 KV, 20.0 s; separation: 15 KV, 35.0 min, and detection is carried out at the wavelength of 220 nm by using a PDA detector; and calculation is carried out by the area normalization method.
The morphology and number of sub-visible particles in the sample are determined by using the FlowCam 8100 particle analytical detector. The specific parameter settings of the instrument are shown in Table 4.
For the study of buffer system/pH, two rounds of experiments are carried out, and the type and pH range of the buffer system are screened by designing a single-factor experiment.
In this study, the HLX04 protein stock solution (batch number: AS201801) in which Tween 20 has been removed by using cation chromatography is subjected to ultrafiltration and medium exchange, and then the protein concentration is adjusted to prepare an alternative formulation with a final protein concentration of about 25.0 mg/mL (Table 5). In a biosafety cabinet, the sample is filtered by using a 0.22 μtm disposable sterile filter and then 1 mL of the protein solution is aseptically sub-packaged into 2 mL penicillin vials. The vials are capped with 13 mm rubber stoppers, and 13 mm aluminum-plastic composite caps are used to seal the stoppers. The sub-packaged samples are placed in a constant temperature and humidity chamber at 40° C. for storage, and are sampled and detected according to the design requirements in Table 6.
At week 0, the Tagg temperature is relatively higher (
After standing at 40° C. for 4 weeks, the results of protein concentrations and pH show no significant difference (Table 7). The SEC results show that the contents of the main peaks of the proteins in each buffer system all show a downward trend (
The results of the buffer system/pH screening study-I show that in the histidine-histidine hydrochloride, acetic acid-sodium acetate and citrate-sodium citrate buffer systems, the lower is the pH, the higher is the content of the SEC main peak; and with regard to the proteins in the formulations without stabilizers and surfactants, after being placed at 40° C. examination conditions for 1 week, there are particles visible to the naked eye in each of the formulations. Therefore, in this round of experiment, the buffer system screening is further performed in the formulation with sucrose and Tween 80 at a low pH of 5.0.
In this study, the HLX04 protein (batch number: AS201901-PT) is subjected to ultrafiltration and medium exchange, then auxiliary materials are added, and the protein concentration is adjusted to prepare an alternative formulation with a final protein concentration of about 25.0 mg/mL (Table 8). In a biosafety cabinet, the sample is filtered by using a 0.22 μm disposable sterile filter and then 1 mL of the protein solution is aseptically sub-packaged into 2 mL penicillin vials. The vials are capped with 13 mm rubber stoppers, and 13 mm aluminum-plastic composite caps are used to seal the stoppers. The sub-packaged samples are placed in a constant temperature and humidity chamber at 40° C. for storage, and are sampled and detected according to the design requirements in Table 9.
At week 0, there is no significant difference in the basic physicochemical detection results of the proteins in each buffer system (Table 10), and the formulations are ranked from superiority to inferiority according to the Tagg aggregation temperatures are A50≈HA50>H50>C50 (
After standing at 40° C. for 4 weeks, there is no significant difference in the basic physicochemical detection results (Table 10). The SEC results show that the contents of the main peaks of the proteins in each buffer system all show a downward trend, and the formulations are ranked from superiority to inferiority as A50≈H50≈HA50>C50 (
The results of this round of study show that the protein shows better conformational and colloidal stability in the acetic acid-sodium acetate and histidine hydrochloride-sodium acetate buffer systems. The results regarding charge isomers of the protein in the histidine-histidine hydrochloride buffer system are better, and after comprehensive consideration, histidine hydrochloride-sodium acetate is selected as the buffer system of the protein.
In this study, the HLX04 protein (batch number: AS201901-PT) is subjected to ultrafiltration and medium exchange, then auxiliary materials are added, and the protein concentration is adjusted to prepare an alternative formulation with a final protein concentration of about 25.0 mg/mL (Table 11). In a biosafety cabinet, the sample is filtered by using a 0.22 μm disposable sterile filter and then 1 mL of the protein solution is aseptically sub-packaged into 2 mL penicillin vials. The vials are capped with 13 mm rubber stoppers, and 13 mm aluminum-plastic composite caps are used to seal the stoppers. The sub-packaged samples are placed in a constant temperature and humidity chamber at 40° C. for storage, and are sampled and detected according to the design requirements in Table 12.
At week 0, the formulations are ranked from superiority to inferiority according to the Tagg aggregation temperatures (
After standing at 40° C. for 4 weeks, there is no significant difference in the basic physicochemical detection results (Table 13). The SEC results show that the contents of the main peaks of the proteins in each buffer system all show a downward trend (
The results of this round of study show that the protein shows better conformational and colloidal stability in 10 mM of histidine hydrochloride-sodium acetate buffer system. The content of the SEC main peak shows a slower downward trend. There are few FlowCam sub-visible particles.
In this study, the HLX04 protein (batch number: AS201901-PT) is subjected to ultrafiltration and medium exchange, then auxiliary materials are added, and the protein concentration is adjusted to prepare an alternative formulation with a final protein concentration of about 25.0 mg/mL (Table 14). In a biosafety cabinet, the sample is filtered by using a 0.22 μm disposable sterile filter and then 1 mL of the protein solution is aseptically sub-packaged into 2 mL penicillin vials. The vials are capped with 13 mm rubber stoppers, and 13 mm aluminum-plastic composite caps are used to seal the stoppers. The sub-packaged samples are placed in a constant temperature and humidity chamber at 40° C. for storage, and are sampled and detected according to the design requirements in Table 15.
The proteins are stored in 10 mM of histidine hydrochloride-sodium acetate system for 4 weeks, and there is no significant difference in the physicochemical properties of the proteins in the buffers in the pH range of 5.0-5.6 (Table 16,
In this study, the HLX04 protein (batch number: AS201901-PT) is subjected to ultrafiltration and medium exchange, then auxiliary materials are added, and the protein concentration is adjusted to prepare an alternative formulation with a final protein concentration of about 25.0 mg/mL (Table 17). In a biosafety cabinet, the sample is filtered by using a 0.22 μm disposable sterile filter and then 1 mL of the protein solution is aseptically sub-packaged into 2 mL penicillin vials. The vials are capped with 13 mm rubber stoppers, and 13 mm aluminum-plastic composite caps are used to seal the stoppers. The sub-packaged samples are examined and detected according to the design requirements in Table 18.
At week 0, the stabilizers are ranked from superiority to inferiority according to the Tagg temperatures of the proteins in the formulations containing various stabilizers as sucrose>trehalose>sorbitol≈mannitol>glycine; and the stabilizers are ranked from superiority to inferiority according to the Tm onset as glycine>mannitol≈sucrose≈trehalose≈sorbitol (
After standing at 40° C. for 4 weeks, the SEC results show that the contents of the main peaks of the proteins in the formulations containing various stabilizers all show a downward trend, and the samples containing glycine show a significantly faster downward trend (
After 10 rounds of repeated freezing and thawing cycles, the SEC results show that there is no change in the contents of the main peaks of the proteins in the formulations containing sucrose, trehalose and sorbitol compared with those at week 0, and the contents of the main peaks in the formulations containing mannitol or glycine show a significantly faster downward trend (
The results of this round of study show that under the conditions of standing at the high temperature of 40° C. and repeated freezing and thawing, in the formulation containing a stabilizer sucrose or sorbitol in 10 mM of histidine hydrochloride-sodium acetate buffer system (pH 5.3), the protein shows better stability.
In this round of study, three factors, namely stabilizer type, stabilizer content and Tween 80 content, are selected using the JMP 15 software, 10 experimental groups (Table 20) are designed by using the Box-Behnken response surface method, and the concentrations of the stabilizer and surfactant are determined by means of accelerated conditions such as freezing and thawing, shaking, illumination and high temperature (Table 21).
In this study, the HLX04 protein (batch number: AS201901-PT) is subjected to ultrafiltration and medium exchange, then auxiliary materials are added, and the protein concentration is adjusted to prepare an alternative formulation with a final protein concentration of about 25.0 mg/mL (Table 20). In a biosafety cabinet, the sample is filtered by using a 0.22 μm disposable sterile filter and then 1 mL of the protein solution is aseptically sub-packaged into 2 mL penicillin vials. The vials are capped with 13 mm rubber stoppers, and 13 mm aluminum-plastic composite caps are used to seal the stoppers. The sub-packaged samples are examined and detected according to the design requirements in Table 21.
The detection data is imported into the JMP 15 software, and each factor (dependent variable) is subjected to multiple linear regression and binomial equation fitting by using the least square method to obtain a statistically significant (P value<0.1) model (Table 22) with corrected coefficients of determination (R2) of greater than 0.95, indicating that the model and the actual condition are well fitted, the equation has good accuracy and reliability in terms of the response values, and the regression model can be used instead of real test points for the analysis and prediction of the experimental results.
Utilizing the JMP 15 software, the optimum formulation is predicted by using a maximized desirability model according to the analysis results in Table 22. When sorbitol is selected as the stabilizer, the desirability for the formulation is relatively higher; when the content of sorbitol is 4.5%, the desirability for the formulation is the highest; and as the content of polysorbate 80 increases, the desirability for the formulation shows a downward trend, and when the content of polysorbate 80 is in the range of 0.01%-0.03%, the desirability for the formulation is relatively higher and the midpoint of 0.02% is selected (see
According to the buffer system/pH screening study, ionic strength screening study, surfactant type screening study, stabilizer type screening study, and stabilizer and surfactant screening study, the composition of the final formulation is as follows: 10 mM of histidine hydrochloride-sodium acetate buffer system (pH 5.3), with 45 mg/mL of sorbitol and 0.2 mg/mL of Tween 80.
In this study, the HLX04 protein (batch number: AS201901-PT) is subjected to ultrafiltration and medium exchange, then auxiliary materials are added, and the protein concentration is adjusted to prepare an alternative formulation with a final protein concentration of about 25.0 mg/mL (Table 23). In a biosafety cabinet, the sample is filtered by using a 0.22 μm disposable sterile filter and then 1 mL of the protein solution is aseptically sub-packaged into 2 mL penicillin vials. The vials are capped with 13 mm rubber stoppers, and 13 mm aluminum-plastic composite caps are used to seal the stoppers. The sub-packaged samples are placed in a constant temperature and humidity chamber at 40° C. for storage, and are sampled and detected according to the design requirements in Table 24.
At week 0, the proteins in the 3 formulations are all colorless and slightly opalescent liquids with no obvious visible particles. The formulations are ranked from superiority to inferiority according to the Tagg aggregation temperatures as HA53>PB62>C50 (
After standing at 40° C. for 4 weeks, the protein stability can be maintained to a certain degree in the 3 formulations, and there is no significant change in the basic physicochemical detections of the proteins (Table 25). The SEC results show that the contents of the main peaks of the proteins in each formulation all show a downward trend (
According to the results regarding molecular isomers, charge isomers and sub-visible particles in high-temperature acceleration tests, the stability of bevacizumab in the formulation of the present application is significantly better than that of bevacizumab in the existing formulation (PB62) and other similar formulations.
After the formulation screening study, it is determined that the formulation of the HLX04 formulation is as follows: 10 mM of histidine hydrochloride-sodium acetate, 45 mg/mL of sorbitol and 0.2 mg/mL of Tween 80, pH 5.3. In this round of study, under the acceleration condition of the high temperature of 40° C., the stability differences between the samples of the HLX04 formulation in the concentration range of 10-80 mg/mL and Avastin® are compared. The HLX04 PT protein (batch number: AS201901-PT) is subjected to ultrafiltration and medium exchange, then auxiliary materials are added, and the protein concentration is adjusted to prepare various alternative formulations (Table 26). In a biosafety cabinet, the sample is filtered by using a 0.22 μm disposable sterile filter and then 0.5 mL of the protein solution is aseptically sub-packaged into 2 mL penicillin vials. The vials are capped with 13 mm rubber stoppers, and 13 mm aluminum-plastic composite caps are used to seal the stoppers. The sub-packaged samples and original drug (batch number: H0154B14, code: Avastin) are placed in a constant temperature and humidity chamber at 40° C. for storage, and are sampled and detected according to the design requirements in Table 27.
In this round of study, by means of high-temperature (40° C.) acceleration tests, the stability differences between the samples of the HLX04 formulation in the concentration range of 10-80 mg/mL and Avastin® are compared. The results of the study (Table 28) show that at week 0, the aggregate contents of the samples of the HLX04 formulation in the concentration range of 10-80 mg/mL are 2.0%-2.7%, which are less than the aggregate content (3.6%) of Avastin. After standing at 40° C. for 4 weeks, the aggregation rate (
In summary, compared with the original drug Avastin (60 mg/mL), the HLX04 formulation in the concentration range of 10-80 mg/mL has better stability.
| Number | Date | Country | Kind |
|---|---|---|---|
| 202010143839.6 | Mar 2020 | CN | national |
This is a national stage application of International Application No. PCT/CN2021/078395, filed on Mar. 1, 2021, which claims priority to CN 202010143839.6, filed on Mar. 4, 2020, all of which are incorporated herein by reference.
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/CN2021/078395 | 3/1/2021 | WO |
