Patent Application
20230070714
The following specification particularly describes the invention and the manner in which it is to be performed.
The present disclosure is related to polysaccharide - carrier protein conjugate vaccines manufacturing and evaluation of stability and quality of conjugate vaccines.
All publications herein are incorporated by reference to the same extent as if each individual publication or patent application was specifically and individually indicated to be incorporated by reference. The following description includes information that may be useful in understanding the present invention. It is not an admission that any of the information provided herein is prior art or relevant to the presently claimed invention, or that any publication specifically or implicitly referenced is prior art.
Vaccines based on capsular polysaccharides stimulate humoral immunity but fail to induce immunologic memory, and thus are ineffective in young infants. First generation vaccines were based on bacterial capsular polysaccharides; yet, most of these antigens are considered T-independent antigens, showing significant gaps in terms of immunogenicity, particularly with respect to the generation of the immune memory. The development of protein-polysaccharide conjugation technology in the 1980s allowed the availability of novel vaccines against Haemophilusinfluenzae type b (Hib), Streptococcuspneumoniae and different serogroup of Neisseriameningitidis that have demonstrated a very good safety and tolerability, together with the capability of eliciting a strong immunogenicity combined with the demonstration of the anamnestic antibody responses.
For a vaccine to be effective and induce long lasting immunity, induction of T cell memory is very important. Increased immunogenic response of an antigen can be achieved by converting the T-independent antigen to T-dependent antigen. The conjugation of polysaccharide to carrier protein renders the antigenic molecule to undergo the process of antigen presentation and enhance the polysaccharide immunogenicity by eliciting the T-cell dependent response. The proteins used for conjugation to polysaccharides include CRM197, tetanus toxoid, diphtheria toxoid, Neisseriameningitidis outer membrane complex, Haemophilusinfluenzae protein D, Pneumolysin, etc.
The meningococcal meningitis is caused by Neisseriameningitidis (meningococcal) which is an aerobic Gram-negative encapsulated bacterium. To date, more than 10 serotypes of meningococcal have been characterized by differences in the polysaccharide capsule. The polysaccharides from serotype A, C, Y, W, & X have been conjugated to various carrier proteins to prepare a polysaccharide-protein conjugate vaccine (Menactra®, Menveo®, Nimenrix®, MenQuadFi®), effective against infection by these serotypes.
Similarly, for Streptococcuspneumoniae, more than 90 distinct serotypes have been identified throughout the world (WHO); of which a small number of serotypes accounts for most diseases in infants. Pneumococcal conjugate vaccines containing poly-saccharide from 7+ serotypes i.e. Prevnar® & Synflorix® are already into market. The polysaccharides from S.pneumoniae serotype have been conjugated to various carrier proteins i.e. CRM197, Protein D, TT, DT, etc. to prepare a conjugate vaccine against these serotypes.
Synflorix®, a licensed 10 valent Pneumococcal polysaccharide conjugate vaccine comprises Ps conjugated to three different carrier proteins. Polysaccharide from serotype 1, 4, 5, 6B, 7F, 9V, 14 and 23F are conjugated to protein D (derived from non-type able Haemophilus influenzae) carrier protein; Polysaccharide from serotype 18C is conjugated to tetanus toxoid carrier protein; and polysaccharide from serotype 19F is conjugated to diphtheria toxoid carrier protein. A 11 valent Pneumococcal conjugate vaccine comprising Ps conjugated to at least two different carrier proteins has also been reported (Ref: Rose-Marie Olandera et al 2002; Booster response to the tetanus and diphtheria toxoid carriers of 11-valent pneumococcal conjugate vaccine in adults and toddlers; Vaccine 20; 336-341) wherein polysaccharide is selected from 1, 3, 4, 5, 6B, 7F, 9V, 14, 18C, 19F and 23F and carrier proteins are Diphtheria toxoid and tetanus toxoid. Further, Serum Institute of India’s Penumosil® is a licensed 10 valent Pneumococcal polysaccharide conjugate vaccine that comprises of polysaccharide from serotype 1, 5, 6A, 6B, 7F, 9V, 14 19A, 19F and 23F individually conjugated to CRM197.
Also, a pentavalent Meningococcal conjugate vaccine comprising of Ps conjugated to two different carrier proteins is being developed, wherein polysaccharide from serotype A and X are individually conjugated to tetanus toxoid and polysaccharide from serotype C, Y, W are individually conjugated to CRM197.
Polysaccharide-protein conjugates are relatively more stable compared to live attenuated bacterial vaccines but the polysaccharide (PS) chains of such conjugates tend to degrade by hydrolysis. The potency of these vaccines depends on effective conjugation of the saccharide to a protein carrier and preservation of the integrity of the conjugate molecule during shelf life. Thereby, factors adversely affecting conjugate stability may diminish vaccine potency by reducing the amount, accessibility, and solubility of the conjugated saccharide and carrier protein epitopes, limiting their protective efficacy. High temperature is known to cause physical instability, such as altered tertiary structure and protein aggregation, as well as chemical instability, such as dissociation of polysaccharides from the protein carrier, in this kind of vaccine. These changes can be assessed under thermal stress, the most widespread adverse condition used in the industry.
Polysaccharide protein conjugate vaccine composition are known to be associated with contaminants such as un-reacted polysaccharide (free polysaccharide), un-reacted carrier protein (free protein), low molecular weight conjugates, and other chemicals used for affecting conjugation such as linkers, coupling agents etc. are highly undesirable in a product which is intended for use as a vaccine.
Furthermore, studies under stress conditions may be useful in determining whether short-term accidental exposure to undesired conditions, such as improper transportation, may compromise product quality. Therefore, effective methods are essential for monitoring quality and detecting changes that may potentially affect the efficacy of these vaccines. Establishing stability indicators for conjugate vaccine molecules is a key step to ensure their quality. Physicochemical analysis methods are widely used in pre- and post-licensing quality control of these vaccines to ensure compliance with manufacturing specifications and Lot-to-lot (or batch-to-batch) product consistency. Understanding stability of the molecule helps in the selection of a proper formulation and package as well as providing proper storage conditions and shelf life, which is essential from regulatory/licensure perspective.
Thus, the Food and Drug Administration and International Conference on harmonization guidelines state the requirement of stability testing data to understand how the quality of a drug substance (i.e., bulk material) and drug product changes with time under the influence of various environmental factors. There is no single stability-indicating assay or parameter that provides the stability characteristics of a biotechnological/biological product. Consequently, a stability profile should be proposed ensuring detection of changes in product identity, purity, and potency.
Adequate stability studies form an essential part of the vaccine development studies, they should be designed to help in setting the shelf-life of the vaccines. WHO has developed further guidance on the stability studies of vaccines and general principles should be followed. Stability indicate separately all relevant details including changes in the proportion of free saccharide, molecular size distribution, pH, residual moisture and immunogenicity in accelerated degradation tests, and after storage for the maximum period claimed for the product at the recommended temperature.
The stability of intermediate products such as the purified polysaccharide and the bulk conjugate before mixing into the final bulk must be demonstrated. The stability of the vaccine in its final form, with final containers and at the recommended storage temperatures should be demonstrated to the satisfaction of the national regulatory authorities for at least three lots of final product manufactured from different independent bulk conjugates. In addition, a real-time stability study should be conducted on at least one final container lot produced per year. The saccharide component of conjugate vaccines may be subject to gradual hydrolysis at a rate which may vary depending upon the type of conjugate, the type of formulation or adjuvant, the types of excipient and conditions of storage. The hydrolysis may result in reduced molecular size of the saccharide component, a reduction in the amount of the saccharide bound to the carrier protein and/or in a reduced molecular size of the conjugate. The structural stability of the saccharide chains and of the protein carrier varies between different conjugate vaccines as found for group C meningococcal conjugate vaccines.
Tests should be conducted before licensing to determine the extent to which the stability of the product has been maintained throughout the proposed validity period. The free saccharide content as a percentage of the total saccharide should be determined. The vaccine should meet the recommendations for final product up to the expiry date. Molecular sizing of the final product and estimation of free saccharide may be carried out to ensure the integrity of the conjugate.
Free or unconjugated polysaccharides that are not bound to the carrier proteins also exist in a conjugate vaccine due to incomplete conjugation reaction. Since these free polysaccharides are identical to the polysaccharide only vaccines, they may act as contaminants by interfering with the immunological responses induced by polysaccharide-protein conjugates. Thus, it is difficult to achieve increased immunogenicity when the amount of free polysaccharide exceeds that of the conjugated polysaccharide. Therefore, the low level of free polysaccharide content is an important control to preserve vaccine immunogenicity.
Commonly used methods for free polysaccharide separation in conjugate vaccines, are ammonium sulphate/ethanol/CTAB/deoxycholate conjugate precipitation, capillary electrophoresis, ultrafiltration, reverse phase-solid phase extraction separation, ion exchange chromatography, hydrophobic interaction chromatography and affinity chromatography.
Suker et al. 2004 mentions that the development of control tests for MenC conjugate vaccines has in many respects been based on the recommendations for Hib conjugate vaccines and places emphasis on determining the integrity of the conjugate by physicochemical methods such as nuclear magnetic resonance (NMR) spectroscopy, size exclusion chromatography (SEC) and high performance anionic exchange chromatography with pulsed amperometric detection (HPAEC-PAD). Immunogenicity assays have been valuable in conjugate vaccine development but are not necessary for routine batch-release, where vaccine consistency has been demonstrated by other means.
Assays of molecular size by SEC can be sensitive to batch-to-batch changes, although the accuracy of molecular-weight values determined using protein or saccharide standards is poor. The addition of light-scattering detectors to the chromatographic system gives much more accurate molecular-mass values than the values obtained from the use of concentration detectors, such as UV or refractive index alone. The key control test for glycoconjugate vaccines is free saccharide determination, which is considered to be the critical assay to evaluate conjugate stability. First, the free saccharide is separated from conjugated saccharide, for example by ultrafiltration, interaction with hydrophobic beads, or detergent precipitation. The quantity of saccharide is then measured by HPAEC-PAD in both the separated free saccharide portion and the conjugate sample before separation, in order to determine the percentage of free saccharide in the original vaccine sample.
Final vaccine composition (Drug product) comprises antigens and excipient/stabilizer and preservative. During quality control assays, it is difficult to analyze antigens in presence of these components which may cause interference during analysis. In addition to the problems related to desorption or dissolution of adjuvant, high concentrations of salts or aluminum complexes may remain on chromatographic equipment and could potentially interfere with assay procedures relying on spectrophotometric measurement. This has driven refinements to the batch-release testing schedule such that molecular size is measured at the bulk conjugate rather than final-fill stage comprising multiple antigens of similar molecular weight that gets mixed up to make a formulation. This strategy is also used in the evaluation of multivalent pneumococcal conjugates vaccines and will be considered for meningococcal conjugate combinations (e.g., A/C or ACW-135Y). However, as formulations and combinations become more complex, it will be important for manufacturers to rule out that significant changes in immunogenicity and the physicochemical profile occur as a result of component interactions, formulation or filling.
According to Annex_2_WHO_TRS_962 - The molecular size of the saccharide-protein conjugate is an important parameter in establishing consistency of production and in studying stability during storage. The relative molecular size of the saccharide-protein conjugate should be determined for each bulk conjugate, using a gel matrix appropriate to the size of the conjugate. The method should be validated with an emphasis on specificity to distinguish the saccharide-protein conjugate from other components that may be present, e.g. unbound protein or free saccharide for monovalent glycoconjugate vaccine.
Typically, the size of the saccharide-protein conjugate may be examined by methods such as gel filtration on Sepharose CL-4B, or by HPSEC on an appropriate column. Since the saccharide to protein ratio is an average value, characterization of this ratio over the size distribution (e.g. by dual monitoring of the column eluent) can be used to provide further proof of manufacturing consistency.
Physicochemical methods to measure molecular size and amount of free saccharide are used as the main control tests and indicators of product conformity for monovalent polysaccharide protein conjugate vaccines. It is anticipated that monovalent polysaccharide protein conjugate vaccines will in future be replaced by multi-component products which will require more extensive testing to ensure that vaccine quality is not compromised.
K. Jumel et al. 2002 discloses Men C - CRM197 conjugate molecular mass determination by SEC-MALLS (Mol size determined by GPC, Avg Mol wt Men C conjugate 74.9 kDa ± 5 kDa). LEMERCINIER ET AL. 1997 discloses mol wt determination of Hib conjugate and Men CCRM197 conjugate by FPLC. M.M. Ho et al. 2001 discloses FPLC-SEC and SEC-MALLS/RI to determine size of Men C - CRM197 conjugate and molecular mass.
Multivalent polysaccharide vaccines contain many immunogenic components, each of which must be characterized separately. At present, no suitable assay for quality control of these multi-component mixtures is available wherein the final quality control technique is traceable to reliable analytical methods such as SEC-MALS.
Nimenrix EMEA (Procedure No. EMEA/H/C/002226) 2011 discloses molecular size distribution (MSD) for the commercial batches of MenACWY-TT at the 9 months, 18 months & acknowledges that free PS, MSD analysis, both are indicative of degradation and aggregation. It also mentions that integrity of the conjugates with respect to degradation, the MSD assay might be one of the more appropriate methods applied.
Aggregate formation or aggregate molecules are observed during manufacturing or during storage period of vaccine at various conditions. Aggregate molecules contribute to high molecular weight (HMW) and low molecular weight (LMW) molecules. Conjugated carrier proteins also appeared to form oligomers or ‘aggregates’ at elevated temperatures.
Polysaccharide-polysaccharide aggregates are also encountered. Free polysaccharide analysis method as the in-process and stability evaluation parameter mostly provides information about the free polysaccharide content in the vaccine sample and does not give information related to such aggregate formation/molecules present in the vaccine sample. Applicant has found that aforementioned aggregates have an adverse impact on both the stability and immunogenicity of polysaccharide-protein conjugate vaccine. There is an unmet need for monitoring conjugate vaccines across manufacturing and storage for profiling of such aggregates in addition to free polysaccharide measurement.
Some of the objects of the present disclosure, which at least one embodiment herein satisfies, are as follows:
Novel Multicomponent products (multivalent polysaccharide protein conjugate vaccines will require more extensive testing to ensure that vaccine quality is not compromised. In Multicomponent products (multivalent polysaccharide protein conjugate vaccines), free polysaccharide and free protein are individually/separately considered as stability indicating parameters for which individual tests are to be carried out. At present, no known method exists for measuring aggregation profile & molecular size distribution of conjugates in a multivalent drug product to support the lot to lot consistency and to an extent confirm the stability & integrity of the multivalent polysaccharide protein conjugate vaccine formulation (ACWYX comprising of N. meningitidis serogroup X in particular). Applicant has found a method comprising use of SEC-HPLC-MALS for profiling of conjugates based on molecular size and/or molar mass in a multivalent N. Meningitidis conjugate vaccine (ACWYX)drug product in terms of Average Molecular Weight/AMW, High Molecular Weight/HMW, Low Molecular Weight/LMW molecules showing correlation between Molecular Size Distribution (SEC-HPLC-MALS) and Stability which ultimately contributes to determining integrity, degradation and aggregation profile of multivalent drug product and its ingredients.
Particularly applicant has found that such molecular size distribution (measurement & profiling of a multivalent in terms of AMW, HMW, LMW) is an effective alternative method (in addition to free polysaccharide and free protein measurement) to assess stability of multivalent conjugate mix ACWYX (drug product). The novel assay for measuring aggregation profile & molecular size distribution of a multivalent drug product mix is done in the presence of two carrier proteins, free polysaccharides and excipient, without any interference of said components. Applicant’s assay utilizes set of three columns [Shodex 807/Shodex 806 + Shodex 806/Mixed Bead columns + TSK gel 6000/5000 PwxL + with guard column] in a series, using Phosphate buffer as mobile phase along with optimized flow rate, time, temperature and detectors [UV; RI; & MALS].
The present disclosure will now be described with the help of the accompanying drawing, in which:
Although the present disclosure may be susceptible to different embodiments, certain embodiments are shown in the drawing and following detailed discussion, with the understanding that the present disclosure can be considered an exemplification of the principles of the disclosure and is not intended to limit the scope of disclosure to that which is illustrated and disclosed in this description.
Embodiments are provided so as to thoroughly and fully convey the scope of the present disclosure to the person skilled in the art. Numerous details are set forth, relating to specific components, and processes, to provide a complete understanding of embodiments of the present disclosure. It will be apparent to the person skilled in the art that the details provided in the embodiments should not be construed to limit the scope of the present disclosure. In some embodiments, well-known composition, well-known processes, and well-known techniques are not described in detail.
The terminology used, in the present disclosure, is only for the purpose of explaining a particular embodiment and such terminology shall not be considered to limit the scope of the present disclosure. As used in the present disclosure, the forms “a,” “an,” and “the” may be intended to include the plural forms as well, unless the context clearly suggests otherwise.
The terms “comprises,” “comprising,” “including,” and “having,” are open ended transitional phrases and therefore specify the presence of stated features, integers, steps, operations, elements, modules, units and/or components, but do not forbid the presence or addition of one or more other features, integers, steps, operations, elements, components, and/or groups thereof. The particular order of steps disclosed in the process of the present disclosure is not to be construed as necessarily requiring their performance as described or illustrated. It is also to be understood that additional or alternative steps may be employed.
The terms first, second, third, etc., should not be construed to limit the scope of the present disclosure as the aforementioned terms may be only used to distinguish one element, component, region, layer or section from another component, region, layer or section. Terms such as first, second, third etc., when used herein do not imply a specific sequence or order unless clearly suggested by the present disclosure. The present disclosure provides an immunogenic composition and a process for preparing the same.
It is understood that each feature or embodiment, or combination, described herein is a nonlimiting, illustrative example of any of the aspects of the invention and, as such, is meant to be combinable with any other feature or embodiment, or combination, described herein. For example, where features are described with language such as “one embodiment”, “some embodiments”, “certain embodiments”, “further embodiment”, “specific exemplary embodiments”, and/or “another embodiment”, each of these types of embodiments is a nonlimiting example of a feature that is intended to be combined with any other feature, or combination of features, described herein without having to list every possible combination. Such features or combinations of features apply to any of the aspects of the invention.
As used herein the terms “Freeze-drying” or “lyophilize” or “lyophilisation” involves lyophilization and refers to the process by which a suspension is frozen, after which the water is removed by sublimation at low pressure.
An embodiment of the disclosure provides an evaluation of stability and quality of polysaccharide-carrier protein conjugate vaccine composition.
An embodiment of the present disclosure provides designing and development of an assay for determination of stability indicating parameter. In an aspect of the present embodiment, the disclosure provides determination of molecular size and/or weight in polysaccharide-carrier protein conjugate vaccine composition. In another aspect of the present embodiment disclosure provides to understand lot to lot consistency of vaccine composition by determining and analysing information on distribution of various molecules (conjugates) in terms of presence of high molecular weight (HMW) and low molecular weight (LMW) in the vaccine composition. In another aspect of the said embodiment, it is provided that molar mass distribution of the vaccine composition may provide an information on the confirmation of the molecules through its presentation as HMW, LMW, aggregates and the presentation of majority of molecules of particular molecular weight and its contribution in the vaccine sample. In another aspect of the present embodiment, the distribution pattern of the molecules present in a vaccine composition may help to elucidate the characteristics/attributes of different dose presentations and formulations. The present disclosure further provides elucidating characteristics/attributes in terms of molecular weight/molar mass and molecular size of the various liquid and lyophilized vaccine compositions.
An embodiment of the present disclosure, it is provided that the vaccine composition stored at various temperature ranges may be analyzed to study, analyze and correlate the molecular size distribution & molar mass distribution with stability and immunogenicity of the vaccine composition. It is further provided that the vaccine composition may be stored at temperaturebetween -80 to 55 Degree Celcius.
An embodiment of the present disclosure provides an assay for elucidation of characteristics/attributes in a vaccine composition including molecular size pattern, molecular size distribution pattern, average molecular weight (AMW), high molecular weight (HMW) and low molecular weight (LMW); and the majority molecules present in a vaccine composition.
It is understood that low molecular weight (LMW) are molecules/components having molecular weight in range between 200 & 2000; average molecular weight (AMW) are molecules/components having molecular weight in range between 2000 & 11000; high molecular weight (HMW) are molecules/components having molecular weight in range between 10000 & 50000 or 13000 & 50000.
An embodiment of the present disclosure provides an assay for elucidation of characteristics / attributes in a vaccine composition wherein the behaviour (characteristics / attributes) of individual conjugates in a multivalent polysaccharide-carrier protein conjugate (and/or multivalent drug product) is not possible. In an aspect of the said embodiment, it is further provided to provide information and to assess / elucidate lot to lot consistency and to generate characterization data to understand the process dynamics of stability indicating parameters in presence of excipient, including presence of molecular size pattern, molecular size distribution pattern, average molecular weight (AMW), high molecular weight (HMW) and low molecular weight (LMW); and the majority molecules present in a vaccine composition.
Size-exclusion chromatography (SEC) is a separation technique based on the molecular size of the components. Separation is achieved by the differential exclusion from the pores of the packing material of the sample molecules as they pass through a bed of porous particles. Size exclusion chromatography (SEC) is preferably used as one of HPLC separation modes, wherein column used is filled with material/resin containing pores of suitable sizes. When dissolved molecules of various sizes flow into the column, smaller dissolved molecules flow more slowly through the column because they penetrate deep into the pores, whereas large dissolved molecules flow quickly through the column because they do not enter the pores. Consequently, larger molecules elute from the column sooner and smaller molecules later, which effectively sorts the molecules by size. This is the separation principle of size exclusion chromatography.
In an embodiment of the present disclosure, vaccine composition is subjected to size-exclusion chromatography (SEC). Size-exclusion chromatography (SEC) used may be selected from gel permeation chromatography (GPC) and/or gel filtration chromatography (GFC). Gel permeation chromatography (GPC), uses a hydrophobic column packing material and a nonaqueous mobile phase (organic solvent) to measure the molecular weight distribution of synthetic polymers, whereas the gel filtration chromatography (GFC) uses a hydrophilic packing material and an aqueous mobile phase to separate, fractionate, or measure the molecular weight distribution of molecules soluble in water, such as polysaccharides and proteins. In an aspect of the said embodiment, it is provided that large molecular size molecules in a vaccine composition elutes out first from the column followed by small molecular size molecule (like unconjugated carrier protein); molecules are eluted out at different retention time on the basis of their size, molecular weight and shows clear separation which is captured and tracked by three different detectors i.e. UV, RI and MALS (Multi angle light scattering). In an aspect of the said embodiment, it is provided that selection of column, run conditions, method/program, mobile phase and chromatogram integration may be optimized.
In an embodiment of the present disclosure, it is provided to study, analyze and correlate the molecular size distribution and absolute molecular weights of the distributed components of a vaccine composition. In an aspect of the said embodiment, it is further provided to assess / elucidate and characterize the vaccine composition based on molecular size distribution with respect to absolute molecular weight and percent molar mass distribution.
In an embodiment of the present disclosure, it is provided to further study, analyze and correlate the molecular size distribution & molar mass distribution with immunogenicity of the vaccine composition. In an aspect of the said embodiment, it is provided to further study, analyze and correlate range (%) of average molecular weight (AMW) with stability, immunogenicity and potency/efficacy of the vaccine composition. In other aspect of the said embodiment, it is provided to further study, analyze and correlate range (%) of High molecular weight (HMW) and Low molecular weight (LMW) with stability, immunogenicity and potency/efficacy of the vaccine composition. In another aspect of the said embodiment, it is provided to further study, analyze and correlate ratio of average molecular weight (AMW), high molecular weight (HMW) and Low molecular weight (LMW) with stability, immunogenicity and potency/efficacy of the vaccine composition. In a further aspect of the present embodiment, it is further provided to study the interference of excipient in a vaccine composition during analysis of vaccine composition.
An embodiment of the present disclosure, it is provided to design and optimize a process for size exclusion chromatography (SEC) maintaining specificity and precision. It is understood that the SEC process requires optimization depending on the type of sample to be analyzed. It is understood that the SEC process should be optimized in a manner that there is no interference of the sample components with the column material/resin. It is further understood that the integrity of the sample should remain intact thereby facilitating further analysis of the sample. In other words, process designed should be non-interfering with the sample and should avoid harsh conditions (like high pH buffer, voltage, temperature) for analysis practically maintaining the integrity of molecules/components of sample as it is to provide true presentation of the components/conjugate behaviour in a vaccine composition.
In one of the aspects of the said embodiment, it is provided to use Gel Chromatography for separation of components/molecules present in a vaccine composition. It is understood that Gel chromatography used may be selected from gel filtration chromatography and gel permeation chromatography. Gel permeation chromatography (GPC), which uses a hydrophobic column packing material and a non-aqueous mobile phase (organic solvent) to measure the molecular weight distribution of synthetic polymers. The other is gel filtration chromatography (GFC), which uses a hydrophilic packing material and an aqueous mobile phase to separate, fractionate, or measure the molecular weight distribution of molecules soluble in water, such as polysaccharides and proteins. It is understood that in gel chromatography, large molecular size components/molecule in a vaccine elutes out first from the column followed by small molecular size molecule (Free protein i.e. TT). The molecules are eluted out at different retention time on the basis of their size, molecular weight and show clear separation which is captured and tracked by three different detectors i.e. UV, RI and MALS (Multi angle light scattering). It is further provided that the columns for gel chromatography may be selected on the basis of separation with defined exclusion limits which can resolve very high molecular weight molecules present in a vaccine composition. It is further provided that selection of column is based on consideration that no structural dependency of the molecule is interfering with the final outcome of the process, and lot-to-lot variations in vaccine composition are suitably catered. It is further provided that the process is independent of the inactive components/excipient present in a vaccine composition.
In a multivalent vaccine, the identity of sample remains no more individual from structural and analytical point of view and act as a single component, therefore the individual conjugate containing two carrier protein cannot be discriminated. The assay or method provides the behaviour of total molecules as a whole present in the sample when get mixed to support the lot to lot consistency and to an extent the stability of the mixed formulation or composition.
An embodiment of the present disclosure provides an assay or method for determining the stability of a polysaccharide-protein conjugate vaccine, said method comprising the following steps:
In an aspect of the said embodiment a pre-treatment step is carried out before step a).
In an aspect of the said embodiment the pre-treatment step comprises of reconstitution of polysaccharide-protein conjugate vaccine using a buffer.
In an aspect of the said embodiment the buffer used for reconstitution of polysaccharide-protein conjugate vaccine in pre-treatment step is selected from phosphate buffer saline, Tris, MES, HEPES, citrate and combinations thereof.
In an aspect of the said embodiment the buffer used for reconstitution of polysaccharide-protein conjugate vaccine in pre-treatment step is Tris buffer.
In an aspect of the said embodiment the set of three chromatography columns in series is connected with a guard column.
In an aspect of the said embodiment the arrangement of columns is guard column followed by first column, first column followed by second column and second column followed by third column.
In an aspect of the said embodiment it is provided that the resolution of samples in multivalent (mixed composition) which are likely to be of high molecular weight and obviously complex was important to obtain appropriate molar mass data which is possible by introducing the suitable column with high resolution or exclusion column capabilities.
In a preferred aspect of the said embodiment, considering the range of molar mass and molecular size of the components in a vaccine composition, it is provided to use a combination of 3 columns connected in a series to form a 90 cm long column along with a guard column to ensure that the complete range (HMW to LMW) of molecules are captured for analysis. In a preferred aspect, polymethacrylate based resin columns (Shodex 807, Shodex 806, Shodex mix bead columns SB806M), and polymethacrylate based resin (TSK gel 5000/6000 PwxL) along with guard column in series are provided to be used.
In the other aspect of the said embodiment connection of chromatography columns in the series is required to separate out the novel combination of five serogroups with two different carrier proteins. This strategy of connecting the multiple column is formulated considering and selecting the broad exclusion limit which support the separation of vaccine molecules. If columns are not connected in series and are used individually then it is not able to achieve the created dynamic exclusion limit, ultimately affecting the overall analysis or separation which is based on the variable size of molecules present in the vaccine sample. Guard column is not used for the separation purpose but is used to remove particulate contaminants from the sample if present and helps in prolonging the life of the main columns. The usage of guard column is the indication of good chromatographic practices.
In an aspect of the said embodiment the guard column comprises polymer-based packed column for e.g. polyhydroxymethacrylate, etc based material having particle size 9 - 14 µm.
In an aspect of the said embodiment the first and second chromatography columns comprises polyhydroxymethacrylate based material and third chromatography column is selected from hydroxylated polymethacrylate based material and hydrophilic vinyl polymer based material.
In an aspect of the said embodiment the particle size of first column is 34 - 36 µm, particle size of second column is 12 - 14 µm and particle size of third column is 9 - 14 µm.
In an aspect of the said embodiment the length of the set of three chromatography columns in series ranges from 85 - 95 cm.
In an aspect of the said embodiment the guard column and chromatography columns in series are connected using a connector.
In an aspect of the said embodiment the connector used for connecting guard column and chromatography columns in series is a ferrule.
In another aspect of the said embodiment, it is provided that the eluate is further subjected to analysis using detectors including but not limited to UV (280 nm), Refractive Index (RI), Multiangle light scattering (MALS) or a combination thereof. The detectors used may provide details related to concentration of proteins, presence of aggregates, concentration of polysaccharides and molecular weight, size and mass of the molecules present in a vaccine composition.
In an aspect of the said embodiment the detectors in step b) is selected from UV detector, refractive index (RI) detector and multiangle light scattering (MALS) detector and combinations thereof.
In an aspect of the said embodiment the UV detector was used to track the molecules present in the vaccine having the absorbance at 280 nm. The UV detector was used to track the protein molecules present in the vaccine having the absorbance at 280 nm.
In an aspect of the said embodiment the refractive index (RI) was used to measure the refractive index of the molecules present in the vaccine. The refractive index (RI) was used to measure the refractive index of the polysaccharides present in the vaccine.
In an aspect of the said embodiment the multiangle light scattering (MALS) detector was used to determine the molar mass and molecular weight of the molecules present in the vaccine.
In another aspect of the present embodiment, it is provided to use a mobile phase with non-interference with the components in a vaccine sample; preferably mobile phase used is Phosphate buffer with 200 mM NaCl. It is understood that other suitable buffers may be used as mobile phase.
In an aspect of the said embodiment the mobile phase is a buffer selected from phosphate buffer saline, Tris, MES, HEPES, citrate and combinations thereof.
In an aspect of the said embodiment the mobile phase does not interfere with the vaccine.
In an aspect of the said embodiment the buffer is phosphate buffer saline having 7.2 to 7.5, preferably pH 7.4.
In an aspect of the said embodiment the phosphate buffer saline comprises of sodium chloride in the range of 20 to 40 g, preferably 23.38 g.
In another aspect of the said embodiment, it is provided to use a flow rate lower than the usual ensuring the quality of the chromatography is good and the components in a vaccine composition should get sufficient time to interact with the stationary phase, preferably flow rate is set at 0.1 - 1 ml per minute.
In an aspect of the said embodiment wherein the high performance size exclusion chromatography (HPLC-SEC) in step a) comprises a flow rate ranging from 0.1 to 1 ml per minute, preferably 0.30 to 0.80 ml per minute.
In another aspect of the said embodiment, it is provided to set time parameter in the range of 50 - 300 minutes per injection thereby ensuring the complete separation and recovery of the components in a vaccine composition, and column temperature in the range of 20-40 Degree C thereby ensuring no exceptional temperature is set for analysis making the test procedure simple and temperature independent.
In an aspect of the said embodiment the high performance size exclusion chromatography (HPLC-SEC) in step a) comprises a column temperature ranging from 25° C. to 35° C.
In an aspect of the said embodiment the high performance size exclusion chromatography (HPLC-SEC) comprises a column temperature ranging from 25° C. to 35° C. to ensure that no exceptional temperature is set for analysis and the test procedure was made simple and temperature independent.
In an aspect of the said embodiment the high performance size exclusion chromatography (HPLC-SEC) in step a) comprises injection run time ranging from 50 - 160 min to ensure the complete separation and recovery of the sample.
In an aspect of the said embodiment the high performance size exclusion chromatography (HPLC-SEC) in step a) comprises injection run time ranging from 60 - 70 min.
In an embodiment of the present disclosure for lyophilized vaccine low molecular weight (LMW) are molecules/components having molecular weight in range between 200 & 2000; average molecular weight (AMW) are molecules/components having molecular weight in range between 2000 & 11000; high molecular weight (HMW) are molecules/components having molecular weight in range between 13000 & 19000.
In an embodiment of the present disclosure for liquid vaccine low molecular weight (LMW) are molecules/components having molecular weight in range between 200 & 1000; average molecular weight (AMW) are molecules/components having molecular weight in range between 1000 & 10000; high molecular weight (HMW) are molecules/components having molecular weight in range between 10000 & 19000.
In an embodiment of the present disclosure, optimized assay is provided to provide characteristics/attributes of each component (AMW, LMW, HMW) present in a vaccine composition wherein no other methods of analysis of components is feasible.
To arrive at the distribution cut the following mathematical calculation is considered
Where,
An elution volume (Ve) is where the peak is cut to get percent (%) molecular size distribution.
In an aspect of the present embodiment the high molecular weight is in the range from 13000 kDa to 19000 kDa, average molecular weight is in the range of 2000 kDa to 11000 kDa and low molecular weight is in the range of 200 kDa to 2000 kDa for lyophilized polysaccharide-protein conjugate vaccine.
In an aspect of the present embodiment the high molecular weight is in the range from 10000 Kda to 19000 Kda, average molecular weight is in the range of 1000 Kda to 10000 Kda and low molecular weight is in the range of 200 to 1000 Kda for liquid polysaccharide-protein conjugate vaccine.
An embodiment of the disclosure provides a polysaccharide-carrier protein conjugate vaccine composition.
In an aspect of the present embodiment vaccine composition may comprise of combination of different conjugates having multiple polysaccharides and carrier proteins.
An embodiment of present disclosure provides a polysaccharide-carrier protein conjugate vaccine composition/formulation suitable for the prevention and treatment of more than one disease state and meets the criterion for the stability and effective seroprotection for each of the said immunogenic components. It is further provided that the polysaccharide-carrier protein conjugate vaccine composition is a monovalent bulk polysaccharide-carrier protein conjugate or multivalent polysaccharide-carrier protein conjugate or a drug product comprising of polysaccharide-carrier protein conjugates. In one of the aspects, monovalent bulk polysaccharide-carrier protein conjugate is a component stored prior to formulation. In other aspect monovalent bulk polysaccharide-carrier protein conjugate vaccine is a drug product comprising of polysaccharide-carrier protein conjugate and the excipient and stabilizers. In other aspect multivalent polysaccharide-carrier protein conjugate is a mixture of one or more different types of polysaccharide-carrier protein conjugates and is free of excipient and stabilizers. In another aspect drug product of multivalent polysaccharide-carrier protein conjugate is a mixture of one or more different types of polysaccharide-carrier protein conjugates along with the excipient and stabilizers. In one of the aspects of the present embodiment, the polysaccharide-carrier protein conjugate vaccine composition may additionally comprise of antigen of viral origin, recombinant proteins, inactivated and/or attenuated bacteria.
An embodiment of the present disclosure provides a polysaccharide-carrier protein conjugate vaccine composition is a fully liquid vaccine composition and/or a lyophilized vaccine composition. As used herein the terms “Freeze-drying” or “lyophilize” or “lyophilization” involves lyophilization and refers to the process by which a suspension is frozen, after which the water is removed by sublimation at low pressure. As used herein, the term “sublimation” refers to a change in the physical properties of a composition, wherein the composition changes directly from a solid state to a gaseous state without becoming a liquid. In one of the aspect of said embodiment it is provided that said liquid or lyophilized vaccine composition may comprise of a stabilizer combination selected from a) 2 to 5% (w/v) Trehalose, 0.25 to 0.75% sodium citrate; b) 2 to 5% (w/v) Sucrose and 0.25 to 0.75% sodium citrate; c) 2 to 5% (w/v) Sucrose,2 to 5% (w/v) Lactose and 0.25 to 0.75% sodium citrate; d) 2 to 5% (w/v) Trehalose ,2 to 5% (w/v) Lactose and 0.25 to 0.75% sodium citrate; e) Sucrose, Potassium dihydrogen phosphate, Sodium dihydrogen phosphate monohydrate, Disodium phosphate dihydrate, sodium chloride, water for injections; f) sodium phosphate buffered isotonic sodium chloride solution; g) Sucrose, Trometamol, Sodium chloride, Water for injections; h) sodium chloride, sodium acetate; i) Sucrose and Mannitol. Another aspect of the said embodiment it is provided that said vaccine composition may further comprise a buffer selected from Tris and phosphate.
In one of the aspects of said embodiment it is provided that said liquid or lyophilized vaccine composition may comprise of one or more selected 2-phenoxyethanol, Benzethonium chloride (Phemerol), Phenol, m-cresol, Thiomersal, Formaldehyde, paraben esters (e.g. methyl-, ethyl-, propyl- or butyl- paraben), benzalkonium chloride, benzyl alcohol, chlorobutanol, p-chlor-m-cresol, or benzyl alcohol or a combination thereof. It is also understood that the preservatives may be used in case of multi-dose presentations of vaccine composition, whereas single dose vaccine formulations may be devoid of preservatives.
An embodiment of the present disclosure provides a polysaccharide-carrier protein conjugate vaccine composition, wherein the polysaccharide is an immunogenic component and is derived from a microorganism. In one of the aspect of the present embodiment, the polysaccharide is derived from a gram negative and/or gram positive microorganism. It is further provided that polysaccharide is one or more polysaccharide derived from the group comprising of but not limited to Helicobacterpylori, Chlamydiapneumoniae, Chlamydiatrachomatis,Ureaplasmaurealyticum,Mycoplasmapneumoniae,Staphylococcusspp.,Staphylococcusaureus,Streptococcusspp.,Streptococcuspyogenes,Streptococcusagalactiae,Streptococcuspneumoniae,Streptococcusviridans,Enterococcusfaecalis,Neisseriameningitidis,Neisseriagonorrhoeae,Bacillusanthracis,Salmonellaspp.,Salmonellatyphi,Salmonellaparatyphi,Salmonellatyphimurium,SalmonellaenteritidisVibriocholerae,Pasteurellapestis,Pseudomonasaeruginosa,Campylobacterspp.,Campylobacterjejuni,Clostridiumspp.,Clostridiumdifficile,Mycobacteriumspp.,Mycobacteriumtuberculosis,Treponemaspp.,Borreliaspp.,Borreliaburgdorferi,Leptospiraspp.,Hemophilusducreyi,Corynebacteriumdiphtheria,Bordetellapertussis,Bordetellaparapertussis,Bordetellabronchiseptica,Hemophilusinfluenzae,Escherichiacoli,Shigellaspp.,Ehrlichiaspp.,andRickettsiaspp. Polysaccharides of Streptococcuspneumoniae type 1 , 2, 3, 4, 5, 6A, 6B, 7F, 8, 9N, 9V, 10A, 11A, 12F, 14, 15B, 15C, 17F, 18A, 18B, 18C, 18F, 19F, 19A, 20, 22F, 23F, 35B, 38, 45 and 33F, Polysaccharides of Meningococcal serogroup A, B, C, D, W135, X, Y, Z, 29E, H. influenzae type b, etc.
In one of the aspects of the present embodiment, polysaccharide may be conjugated to one or more carrier protein selected from group comprising of but not limited to CRM197, diphtheria toxoid, Tetanus toxoid, Neisseriameningitidis outer membrane complex, fragment C of tetanus toxoid, pertussis toxoid, protein D of H.influenzae, E.coli LT, E.coli ST, exotoxin A from Pseudomonasaeruginosa, outer membrane complex c (OMPC), porins, transferrin binding proteins, pneumolysin, pneumococcal surface protein A (PspA), pneumococcal surface adhesin A (PsaA), PhtA, PhtB, PhtE, pneumococcal PhtD, pneumococcal surface proteins BVH-3 and BVH-11, M.catarrhalis uspA, protective antigen (PA) of Bacillusanthracis and detoxified edema factor (EF) and lethal factor (LF) of Bacillusanthracis, ovalbumin, keyhole limpet hemocyanin (KLH), C5a peptidase group A or group B Streptococcus, human serum albumin, bovine serum albumin (BSA), purified protein derivative of tuberculin (PPD), Cholera toxin subunit B, fHbp, Por A and Por B . It is further provided that the skilled person in the art, the vaccine may comprise of conjugate(s) wherein afore-mentioned polysaccharides are conjugated to afore-mentioned carrier proteins in any combination.
In another aspect of the present embodiment, polysaccharide-carrier protein conjugate vaccine composition comprises of a polysaccharide derived from Neisseriameningitidis. The said polysaccharide may be derived from Neisseriameningitidis serogroup A, C, W, Y and X, and further conjugated to carrier protein selected from CRM197 and/or Tetanus toxoid. N. meningitidis serotype X strains selected from M9601, M9592, M9591, 247X, M9554, M8210 and M2526, 5967 strain (ST 750), most preferably to “M8210”.
In preferred aspect of the said embodiment, the polysaccharide-carrier protein conjugate vaccine composition comprises of a polysaccharide derived from Neisseriameningitidis serogroup A conjugated to Tetanus toxoid; Neisseriameningitidis serogroup C conjugated to CRM197; Neisseriameningitidis serogroup W conjugated to CRM197; Neisseriameningitidis serogroup Y conjugated to CRM197; and/or Neisseriameningitidis serogroup X conjugated to Tetanus toxoid.
In another aspect of the said embodiment, Neisseriameningitidis vaccine composition (liquid/lyophilized) comprises of each conjugate having concentration of 5-15 microgram per millilitre, along with excipient including 10-100 milligram per millilitre of Sucrose, 1-10 milligram per millilitre of Sodium citrate dehydrate, and 0.1 - 2 milligram per millilitre of Tris. The vaccine composition may additionally comprise one or more of 10-50 milligram per millilitre of Mannitol, 1-20 milligram per millilitre of Sodium chloride and/or 0.1 - 20 milligram per millilitre of 2-Phenoxyethanol (as preservative). It is very well understood that the concentration of excipient may be designed in a way to obtain the desired osmolality of vaccine composition.
In another aspect of the present embodiment, polysaccharide-carrier protein conjugate vaccine composition comprises of a polysaccharide derived from StreptococcusPneumoniae.
The said polysaccharide may be derived from serogroup 1, 2, 3, 4, 5, 6A, 6B, 7F, 8, 9N, 9V, 10A, 11A, 12F, 14, 15B, 17F, 18C, 19F, 19A, 20, 22F, 23F, 35B, 38, 45 and 33F and further conjugated to one or more carrier protein selected from CRM197, Tetanus Toxoid, Diphtheria Toxoid, Protein D, Pneumolysin and/or PsaA.
In a preferred aspect of present embodiment, the polysaccharide - carrier protein conjugate vaccine composition comprises of a 10 or more StreptococcusPneumoniae polysaccharide conjugated to one or more carrier proteins selected from Diphtheria Toxoid, Tetanus toxoid and CRM197.
In another aspect of the present embodiment, polysaccharide-carrier protein conjugate vaccine composition comprises of a polysaccharide derived from SalmonellaSpp. The said salmonella spp includes one or more of S.typhi, Salmonellaenterica serovar Paratyphi (S.Paratyphi) A and B, Salmonellaenterica serovar Typhimurium (S.Typhimurium) and Salmonellaenterica serovar Enteritidis (S.Enteritidis). The said polysaccharides may be conjugated to one or more carrier proteins selected from the group comprising of Tetanus toxoid, CRM197 and/or Diphtheria toxoid.
In one of the embodiments of the present disclosure, the vaccine composition comprises of a polysaccharide-protein conjugates having maximum molecular size in the range of 10 -10000 kDa. The polysaccharide may be subjected to sizing before conjugation. In another aspect of the present embodiment, the polysaccharide is subjected to sizing using mechanical or chemical means before conjugation. The polysaccharide may be subjected to mechanical sizing methods including homogenization, sonication, microfluidization and high pressure cell disruption; and/or chemical sizing methods like use of sodium acetate, acids/low pH treatment or bases/high pH treatment.
In a preferred aspect of this embodiment, the vaccine composition is a pentavalent vaccine composition comprising of polysaccharides derived from Neisseriameningitidis serogroup A and X conjugated to Tetanus toxoid; and serogroup C, W, & Y conjugated to CRM197. The polysaccharide may be conjugated to a carrier protein using reductive amination, cyanylation, carbodiimide conjugation chemistry.
The composition may additionally comprise of excipients like Sucrose, Mannitol, Sodium citrate dehydrate, Tris, 2-phenoxyethanol as preservative. It is further provided that the total molar mass/ molecular weight would add value to help determining & maintaining the consistency of lot-to-lot manufacturing of vaccine composition.
The geographical source of the strains is as follows:
Neisseria meningitidis A
Neisseria meningitidis C
Neisseria meningitidis W
Neisseria meningitidis Y
Neisseria meningitidis X
In an embodiment of the present disclosure, optimized assay is provided to provide data with respect to molecular size distribution & molar mass distribution correlating individual/monovalent bulk conjugates and the multivalent vaccine composition (drug product).
In an embodiment of the present disclosure, it is provided to design a vaccine composition with a pattern of molecular size distribution & molar mass distribution of the vaccine composition.
In an aspect of the said embodiment, it is provided to design a vaccine composition with specified range (%) of average molecular weight (AMW) with stability, immunogenicity and potency/efficacy of the vaccine composition.
In other aspect of the said embodiment, it is provided to design a vaccine composition with specified pattern/range of High molecular weight (HMW) and Low molecular weight (LMW) with stability, immunogenicity and potency/efficacy of the vaccine composition.
In another aspect of the said embodiment, it is provided to design a vaccine composition with pattern/range of average molecular weight (AMW), high molecular weight (HMW) and Low molecular weight (LMW) with stability, immunogenicity and potency/efficacy of the vaccine composition.
In a further aspect of the present embodiment, it is further provided to design a vaccine composition without interference of excipient in a vaccine composition.
In another aspect of the said embodiment, the said vaccine composition is provided to be analyzed for determining characteristics/attributes of each component present in a vaccine composition using the assay provided in the present disclosure.
In an embodiment of the present invention, multivalent Neisseria meningitidis polysaccharide carrier protein conjugate vaccine composition is provided. It is further provided that said vaccine composition comprises of specified amount of Average molecular weight components with optimum immunogenicity, potency and stability. It is also provided that said vaccine composition comprises of specified amount of Low molecular weight and High molecular weight components with optimum immunogenicity, potency and stability. It is also provided that a vaccine composition having specified correlation between ratio of Average molecular weight; Low molecular weight and High molecular weight components provides optimum immunogenicity, potency and stability.
The present disclosure described herein above has several technical advantages including, but not limited to, the realization of:
The following examples are included to demonstrate preferred embodiments of the invention. It should be appreciated by those of skill in the art that the techniques disclosed in the examples which follow represent techniques discovered by the inventor to function well in the practice of the invention, and thus can be considered to constitute preferred modes for its practice. However, those of skilled in the art should, in light of the present disclosure, appreciate that many changes can be made in the specific embodiments which are disclosed and still obtain a like or similar result without departing from the spirit and scope of the invention.
Following lyophilized (Table 1) and liquid (Table 2) polysaccharide protein conjugate vaccine was considered and used further for analysis.
Since, the concept is the analysis of formulation containing multiple serogroups along with multiple carrier proteins i.e. a pentavalent (multivalent) mix, it would not be scientifically as well as analytically judicious to apply or use the single column method, which has limitation with respect to resolution or separation ability of molecules noting its exclusion limits. Therefore, the comparison between single column Vs multiple columns becomes not applicable in this case. Hence, the complete development was conducted on series of columns i.e. three columns in series to understand the behaviour of molecule from the starting phase to establish the methodical correlation with respect to changes, which may happen during the study.
Hence, since beginning accepting the complex nature of formulation and challenges which may appear with respect to structural change in the molecule over the period of time during stability studies the requirement of dynamic column separating range (exclusion limit i.e. separation capacity) was necessary and needed.
Further, due to non-availability of a single column, which can provide the envisaged wide range of separating capacity, a unique column set up was assembled by attaching three columns in a series. The wise selection of each individual column was considered which would have ability to separate out not only the monovalent but multivalent formulation samples including stability studies sample exposed at various temperatures when connected in series.
Step 1: MATERIAL & EQUIPMENT:
Step 2: CHEMICALS AND REAGENTS:
Step 3: Procedure:
Sample Preparation (Pre-treatment):
Vaccine vial was reconstituted in 0.5-1.0 mL of 10 mM Tris buffer. The 10 kDa Amicon ultra-15 centrifugal filter device was assembled, and 15 mL of Milli Q water was added. The filter device was centrifuged at 4400 g for 30 min as prewash. The Milli Q water was discarded, and reconstituted sample was added in sample reservoir. Volume was made up to 15 mL with 10 mm Tris buffer. The sample was centrifuged at 4400 g for 1 hr. ~100 µL of the sample was collected in microfuge tube and final volume was made to 500 µL. The sample was used for further analysis in HPLC.
Mobile Phase with concentration:
Phosphate buffer saline (PBS): 1800 mL MQW was taken in 2000 mL bottle. 2.87 g di-sodium hydrogen orthophosphate, 1.0 g of potassium dihydrogen orthophosphate and 23.38 g of sodium chloride were weighed and added. The bottle was kept on magnetic stirrer with the magnetic bead into it. The component was dissolved by stirring it on magnetic stirrer. The pH was adjusted with 50 % NaOH to pH 7.4. The final volume was made up to 2000 ml with MQW. The mobile phase was filtered using 0.1 µ filters and was stored at room temperature.
Table 3, 4 and 5 provide details with respect to process parameters, column details and HPLC make/Model
Sample injection:
A suitable mobile phase was used as mentioned above and the vaccine was reconstituted and run into the same mobile phase along with mobile phase blank. The Blank injection showed the non-interference of the mobile phase components in the analysis.
Calculation formula:
An elution volume (Ve) is where the peak is cut to get percent (%) molecular size distribution.
To characterize the sample, firstly the multiple i.e. 1D and 5D formulation samples were analyzed by the optimum method to get an information on the average molecular weight (AMW) of the lyophilized multivalent (pentavalent) mix. In the next stage, we analyzed the multivalent (pentavalent) liquid formulation to obtain the information on average molecular weight. Then a comparative analysis was run to understand the sample behaviour in Lyophilized Vs Liquid as shown in the Table 6.
The data presented below indicated that the AMW for lyophilized formulation is more as compare to liquid. Whereas the 1 dose formulation looks alike in Lyophilized and Liquid. This triggered to measure and characterizes the same sample on molecular weight scale/ruler.
Based on the AMW and distribution of the molecules with respect to molar mass, the following presentation cum information about the sample was obtained which gives an information about presence and percentage of HMW, AMW and LMW molecules (Table 7 and 8). The chromatogram obtained provides presence 100% molecules. Further the peak is split/cut to obtain HMW, Main peak and LMW which finally resulted into the percent contribution of molecules per split as provide in Tables 7 and 8.
Above both the tables (Table No. 7 and 8) provides information about the dominating population of molecules present in the mixed sample.
Since the standards are not required for the estimation of molecular size or weight, the linearity, range, becomes not applicable. In addition, as per the standard guidance, the only parameter becomes applicable in case of molecular size or estimation is precision (intraday and interday), is established and result mentioned confirms the accuracy of the test. The precision data shown in Tables 10 and 11 is presented below-
I. Stability studies of MenFive (Lyophilized) vaccine 1 Dose and 5 Dose at 25° C., 40° C., 60° C. of 1 month compared with initial 2-8° C.
Observations:
From Table 12 and
For LMW molecules: After one-month analysis,
- There are no major changes in the presence of LMW molecules at all temperature conditions 25° C., 40° C. and 60° C. as compared to the initial (2-8° C.) temperature condition.
For AMW molecules: After one-month analysis,
- There are no major changes in the presence of AMW molecules at all temperature conditions 25° C., 40° C. and 60° C. as compared to the initial (2-8° C.) temperature condition.
Conclusion:
Observations:
From Table 13 and
For LMW molecules: After one-month analysis,
There are no major changes in the presence of LMW molecules at all temperature conditions 25° C., 40° C. and 60° C. as compared to the initial (2-8° C.) temperature condition.
For AMW molecules: After one-month analysis,
There are no major changes in the presence of AMW molecules at all temperature conditions 25° C., 40° C. and 60° C. as compared to the initial (2-8° C.) temperature condition.
Conclusion:
II. Comparison between Lyophilized and Liquid vaccine of 1 Dose and 5 Dose at 2-8° C. (initial), 25° C., 40° C., 60° C. respectively:
Observations:
Table 14 focuses on the presentation of molecules in terms of molecular weight. From Table 14 and
For LMW molecules: After one-month analysis,
For AMW molecules: After one-month analysis,
For Lyophilized vaccine:
For Liquid vaccine:
Table 15 focuses on the presentation of molecules in terms of molecular weight. From Table 15 and
For LMW molecules: After one-month analysis,
For AMW molecules: After one-month analysis,
For Lyophilized vaccine:
For Liquid vaccine:
| Number | Date | Country | Kind |
|---|---|---|---|
| 202121040146 | Sep 2021 | IN | national |
