The present patent application claims the benefit of priority from European patent application No. 11002145.8, filed on Mar. 15, 2011, the entire content of which is incorporated herein by reference.
The present invention relates to a pharmaceutical preparation and an aqueous formulation comprising an immunoglobulin or a protein conjugate comprising an immunoglobulin conjugated to a carrier protein. The pharmaceutical formulation may be for parenteral administration such as subcutaneous administration for the treatment of B-cell non-Hodgkin lymphoma. The invention further relates to a set of at least two different protein conjugate preparations.
Anti-idiotype antibodies and vaccines are a promising tool for the treatment of various cancers such as B-cell lymphoma, see López-Diaz de Cerio et al., Oncogene 26 (2007) 3594-3602; Levy, J. Clinical Oncology 17(11s) (1999) 7-13; J Natl Cancer Inst 98 (2006) 1292-1301. A blood cancer for which successful treatment has been demonstrated in clinical experiments is non-Hodgkin lymphoma (herein: NHL). Tumor therapy by anti-idiotype antibodies or vaccines requires patient-specific antibodies or vaccines, respectively, which represents a major challenge for large-scale application to many patients, since sufficient amounts of antibody or vaccine have to be produced for each patient separately within a reasonable time and at reasonable costs. Several technologies for the production of human immunoglobulins are known such as the concomitant production of heavy and light chains of immunoglobulin G in plants (WO2006/079546; Giritch et al., Proc. Natl. Acad. Sci. USA 2006 103 (40) 14701-14706; McCormick et al., Proc. Natl. Acad. Sci. USA 96 (1999) 703-708; Osterroth et al., Journal of Immunological Methods 229 (1999) 141-153). The technical challenges for cloning of relevant complementarity determining regions (CDRs) from autopsy-derived RNA and expression of heavy and light chains of immunoglobulins is also feasible. Due to the enormous costs for providing patient-specific immunoglobulins, automation of as many production steps as possible is imperative.
A problem inherent to the production of patient-specific medicaments is that the physical properties of individual immunoglobulins vary due to the differences in their variable regions. These differences affect the solubility and stability of the immunoglobulin preparations. It has been observed that immunoglobulins differing in their variable region have a high variability in terms of solubility of the antibodies in typical buffers used for extracting the immunoglobulins from cells as well as buffers used for downstream processing. In order to be able to provide predetermined dosages of the immunoglobulin to the medical personnel for administration to patients, immunoglobulin preparations must fulfil certain minimum stability requirements. However, it is not possible in a standardized manufacturing procedure to search for optimal conditions for each individual immunoglobulin. Thus, conditions must be found that allow achieving sufficiently stable immunoglobulin preparations over a wide range of immunoglobulins differing in their variable region.
It is therefore an object of the present invention to provide a pharmaceutical formulation of immunoglobulins, notably of IgG, and of their conjugates with suitable carrier proteins that provides high stability and solubility of the immunoglobulins and their conjugates. It is also an object to provide a method of treatment of B-cell lymphoma by anti-idiotype vaccines using the formulation of the present invention.
The present invention provides a pharmaceutical preparation comprising a protein conjugate comprising an immunoglobulin (such as immunoglobulin G) conjugated to a carrier protein, and histidine as a buffering agent.
The present invention further provides an aqueous pharmaceutical formulation comprising a protein conjugate comprising an immunoglobulin (such as immunoglobulin G) conjugated to a carrier protein, and histidine as a buffering agent.
Further, the present invention provides a formulation for use in a therapeutic method such as for the treatment of non-Hodgkin lymphoma. The present invention provides a formulation for use in a method for the treatment of B-cell lymphoma, notably follicular B-cell non-Hodgkin lymphoma.
The present invention further provides a set of at least two different protein conjugate preparations, each protein conjugate preparation comprising histidine as a buffering agent and a protein conjugate comprising one or more immunoglobulin moieties conjugated to a carrier protein; wherein the immunoglobulin moieties of each protein conjugate preparation have identical complementarity determining regions (CDRs); and wherein different protein conjugate preparations differ in that the immunoglobulin moieties of the protein conjugates have different CDRs. In one embodiment, the immunoglobulin moieties of each protein conjugate preparation have identical variable regions, and different protein conjugate preparations differ in that the immunoglobulin moieties of the protein conjugates have different variable regions.
Also provided is a method of treating a patient suffering from B-cell non-Hodgkin lymphoma (notably follicular B-cell lymphoma), comprising administering to the patient an aqueous pharmaceutical formulation, said formulation comprising a protein conjugate comprising an immunoglobulin conjugated to a carrier protein, and histidine as a buffering agent; wherein the complementarity determining regions of the immunoglobulin conjugated to the carrier protein elicits an immune response in the patient against the non-Hodgkin lymphoma B-cells.
In an important embodiment, the immunoglobulins used in the invention are plant-expressed immunoglobulins, such as plant-expressed IgGs. A preferred plant for expressing are Nicotiana plants such as Nicotiana benthamiana or Nicotiana tabacum.
Immunoglobulins and protein conjugates comprising immunoglobulins can vary considerably in their solubility and stability in solution due to differences in their variable region, notably in the complementary determining regions (CDR) of the immunoglobulins. It has now surprisingly been found by the inventors that aqueous formulations containing histidine as a buffering agent can stabilise a wide range of immunoglobulins and protein conjugates comprising immunoglobulins and a carrier protein. Using histidine as a buffering agent thus allows high throughput generation of different immunoglobulins and protein conjugates of sufficient stability without the need to search for suitable additives or buffers for immunoglobulins or protein conjugates of problematic stability. Further, use of histidine buffer, optionally in combination with suitable surfactants as described below, provides sufficient stability against shaking or shear stress as occurs during sterile filtration, storage, shipment or filtering of formulations before administration to patients. Thus, the invention provides an important contribution for making individualised medicine using immunoglobulins or protein conjugates thereof commercially viable.
The immunoglobulin used in the invention may be an immunoglobulin A, M or G. Immunoglobulins A and G are preferred and immunoglobulin G is most preferred. Immunoglobulin G refers to immunoglobulin G molecules of the subclasses such as IgG1, IgG2, IgG3 or IgG4. Preferably, the immunoglobulin G of the present invention is of the subclass IgG1 or IgG3, more preferably IgG1.
Examples of immunoglobulins (Igs) to be used in the present invention are tumor-derived idiotypic immunoglobulins from non-Hodgkin lymphoma patients. For example, immunoglobulins G (IgGs) can be used for this purpose. Tumor-specific antibodies from non-Hodgkin lymphoma patients contain a collection of epitopes present in the variable region of the clonal immunoglobulin which can be used as a target for active immunotherapy. The tumor-specific immunoglobulins from individual B cell lymphomas can be identified and isolated using “rescue hybridization” or molecular cloning techniques (Levy and Dilley, PNAS, 75 (1978) 2411-2415; Hawkins et al., Blood, 83 (1994), 3279-3288), yielding patient-specific (idiotypic) immunoglobulin which can be used as a tumor antigen for vaccination. Immunoglobulins can also be recombinantly expressed in host cells. A suitable process of expressing immunoglobulins, including patient-specific idiotypic immunoglobulins, is expression in plants or plant cells as described in WO 2006/079546 and Giritch et al., Proc. Natl. Acad. Sci. USA 2006 103 (40) 14701-14706.
When used for vaccination such as in the treatment of non-Hodgkin lymphoma (NHL), the immunoglobulins are preferably administered together with suitable adjuvants for increasing immune response. Established adjuvants can be used for this purpose such as hGM-CSF (human granulocyte-macrophage colony stimulating factor). Another possibility preferred herein is conjugation of the immunoglobulins to a highly immunogenic carrier protein for enhancing the immunogenicity. It is also possible to combine various adjuvants. For example, a protein conjugate having the immunoglobulin conjugated to a carrier protein can be administered together with an adjuvant such as hGM-CSF.
Carrier proteins to which immunoglobulins can be conjugated are known to the skilled person. Examples are diphtheria toxin, tetanus toxin, human serum albumin (HSA), bovine serum albumin (BSA), or hemocyanin such as keyhole limpet hemocyanin (KLH) or subunits thereof. In one embodiment, BSA, hemocyanin (such as KLH) or subunits of hemocyanin are used as the carrier protein. In a preferred embodiment, hemocyanin (such as KLH) or a subunit thereof is used as carrier proteins. KLH is commercially available e.g. from biosyn GmbH (see below).
Hemocyanins are generally isolated from mollusks such as the giant keyhole limpet. Hemocyanins are oligomeric proteins i.e. have multiple subunits. The hemocyanin subunits associate to form the multi-subunit oligomers. Native KLH is a cylindrical copper containing blue protein with a molecular mass ranging from 8 to 32 MDa. The most prevalent oligomeric forms are didecamers with a molecular mass of 8 MDa and multidecamers with a molecular mass of 12-32 MDa. The didecamer has 20 subunits and occurs in two different forms named KLH1 and KLH2. The amino acid sequences of KLH1 and KLH2 are given in the annex as SEQ ID NO: 1 and SEQ ID NO:2, respectively. Instead of native KLH, subunits of KLH can be used as carrier protein in the present invention. Subunits of KLH are also referred to as immunocyanin. A commercially available immunocyanin is VACMUNE® from biosyn.
Herein, “protein conjugate” means a protein comprising one or more immunoglobulin molecules that are covalently bound to a carrier protein. Thus, a protein conjugate molecule comprises a carrier protein and one or more immunoglobulin moieties. The “carrier protein” may be an oligomer, as described above for hemocyanin. It is possible that the immunoglobulin moieties are bound to the carrier protein via linkers. If more than one immunoglobulin molecule is bound to a carrier protein, the immunoglobulin moieties generally have the same CDRs or the same variable regions. In one embodiment, the immunoglobulin moieties are identical.
Methods for conjugating proteins are known to the skilled person and are widely used for conjugating haptens to carrier proteins in processes of antibody generation, and suitable kits are commercially available. As an example for the conjugation reaction, the reaction of an immunoglobulin (such as an IgG) and the carrier protein using the bifunctional linker glutaraldehyde may be used.
In the conjugation reaction, the Ig (such as IgG) molecule and the carrier protein can be employed in different ratios depending on whether multiple immunoglobulin molecules are to be bound to a carrier protein. Accordingly, the molar ratio of Ig to carrier protein subunit may be from about 4:1 to about 1:1, preferably the molar ratio is from about 2:1 to 1:1. In terms of mass ratio, the mass ratio of Ig to carrier protein may be from about 1.5 to 0.4, preferably from about 0.75 to 0.4.
A commercial kit for conjugating proteins to KLH as a carrier protein and that has been used in the examples of this invention for conjugating idiotypic IgG molecules to a carrier protein is VACMUNE® (biosyn GmbH, Fellbach, Germany). In this system, proteins are conjugated to 400 kDa subunits of hemocyanin in water, using 0.1% glutaraldehyde as the conjugating reagent with the molar ratio of IgG to the 400 kDa KLH subunits of about 2.5:1 in the conjugation reaction. The resulting protein conjugate was further purified and can be formulated into the formulation of the present invention by introducing the reaction product in the desired buffer.
The preparations of the invention contain histidine as the buffering agent and the immunoglobulin or the protein conjugate comprising the immunoglobulin. The preparations of the invention may be aqueous liquid preparations or solid preparations. The solid preparations may be prepared from the aqueous liquid preparation by freeze-drying (lyophilisation). The lyophilised solid preparation may be reconstituted to form a liquid aqueous preparation by adding water or an aqueous solvent. An example of the aqueous liquid preparation is the aqueous pharmaceutical formulation of the invention that may, in addition to the immunoglobulin or the protein conjugate, histidine and water, further contain pharmaceutical excipients such as an isotonizing agent, a preservative or others (see further below).
In the aqueous formulation of the invention, the protein conjugate may be present in a concentration of from about 0.1 to about 10 mg/ml, preferably in an amount of from about 0.5 to about 5 mg/ml and more preferably of about 0.7 to 2.5 mg/ml.
The histidine concentration in the aqueous formulation or the aqueous liquid preparations may be 5 mM to 100 mM histidine, preferably 10 mM to 50 mM, more in one embodiment 20 mM to 30 mM histidine. Regarding the pH of the aqueous formulation or the aqueous liquid preparations, a pH which is close to the physiological pH of humans should be chosen when used for administration to patients. The pH may be between 7.0 and 7.8. In one embodiment it is between 7.2 and 7.6 and more preferably 7.3 to 7.5. The pH may be set as commonly known by adding an acid to an aqueous histidine solution. Examples of the acid are inorganic acids such as hydrochloric acid and sulfuric acid, or organic acids such as citric acid, lactic acid, tartaric acid and other physiologically acceptable acids.
The aqueous formulation or the aqueous liquid preparation of the present invention may optionally further contain a nonionic surfactant. Examples of surfactants are known to the skilled person e.g. from McCutcheon's Emulsifiers and Detergents, 1986 North American Edition, McCutcheon Division Publishing Co., Glen Rock, N.J. For medical applications such as for the formulation of the invention, pharmaceutically acceptable nonionic surfactants can be used as known by the skilled person. Combinations of nonionic surfactants can also be used in the present invention.
Among nonionic surfactants, polysorbate surfactants are particularly preferable. Polysorbate surfactants are understood herein to comprise polyoxyethylene sorbitan fatty acid esters, such as polysorbate 80 (poly(oxyethylene)sorbitan monooleate, also known as Tween-80), polysorbate 60 (poly(oxyethylene)sorbitan monostearate, also known as Tween-60), polysorbate 40 (poly(oxyethylene)sorbitan monopalmitate, also known as Tween-40), polysorbate 20 (poly(oxyethylene)sorbitan monolaurate, also known as Tween-20), polysorbate 85 (poly(oxyethylene)sorbitan trioleate, also known as Tween-85) and polysorbate 65 (poly(oxyethylene)sorbitan tristearate, also known as Tween-65). Of these, polysorbate 20 and polysorbate 80 are preferred, with polysorbate 80 being particularly preferred.
Other nonionic surfactants usable in the invention are poly(propylenoxide) and block copolymers of poly(propylenoxide) and poly(ethylenoxide) such as Synperonic® F-68, Pluronic® F68, Lutrol® F68 or Poloxamer 188.
Further additives to the formulations of the invention that may be used instead of the nonionic surfactants are cyclodextrins, such as HP-β-CD, that may be used for protein stabilisation and can be used for parenteral administration of drugs.
The non-ionic surfactant may be present in the aqueous formulation or the aqueous liquid preparation in a concentration of from about 0.001% to about 2% (w/v), preferably from about 0.01% to about 0.5% (w/v). In a preferred embodiment, the surfactant is present in a concentration of about 0.1% (w/v), in an alternative preferred embodiment in a concentration of about 0.01% (w/v).
The formulation or the liquid preparation of the present invention may comprise an isotonization agent. For the parenteral administration of a pharmaceutical formulation, it is desirable to adjust the tonicity of the formulation to the fluids of the human body. The isotonization agents to be used in the formulation of the present invention will be apparent to a person skilled in the art. However, sugar alcohols, polyvinyl pyrrolidone and disaccharides are explicitly mentioned. Of these, mannitol and disaccharides are preferred with disaccharides being more preferred. Particularly preferred disaccharides comprise trehalose and sucrose. In a preferred embodiment of the formulation of the present invention, trehalose is used as isotonization agent.
The pharmaceutical formulation of the invention may further contain one or more additional pharmaceutically acceptable excipients such as buffers, anti-oxidants, bacteriostatic agents, diluents, carriers, surfactants, salts, preserving, stabilizing, wetting or solubilizing agents, and/or excipients for regulating the osmolarity.
In one embodiment of the formulation of the present invention, the formulation comprises histidine as a buffering agent in an amount of from 10 mM to 50 mM and polysorbate 20 or polysorbate 80 in an amount of from about 0.01% to about 0.1% (w/v), and an isotonization agent. In another embodiment, the formulation comprises histidine as a buffering agent in an amount of from 10 mM to 50 mM and polysorbate 20 or polysorbate 80 in an amount of from about 0.01% to about 0.1% (w/v), an isotonization agent, and a protein conjugate comprising an immunoglobulin G conjugated to a carrier protein (e.g. KLH or a subunit thereof) in a concentration of from 0.1 to 10 mg/ml, the formulation having a pH of from 7.3 to 7.5.
Generally, a pharmaceutical formulation herein means a formulation which is suitable for administration to patients, notably of human patients. The pharmaceutical formulation may be administered to the patient by way of parenteral administration, preferably by subcutaneous or intramuscular administration, more preferably by way of subcutaneous administration.
The invention has its full potential when a set of at least two different protein conjugate preparations are to be prepared, such as for the production of multiple B-cell lymphoma vaccines for two or more patients. Use of a histidine buffer as described herein then allows to obtain two or more conjugate preparations, each having a high likelihood of having sufficient stability and solubility. Each of the multiple protein conjugate preparations comprises histidine as a buffering agent and a protein conjugate comprising one or more immunoglobulin moieties conjugated to a carrier protein. The immunoglobulin moieties of each element of said set of protein conjugate preparation have identical complementarity determining regions (CDRs) or identical variable regions. Different protein conjugate preparations of said set differ in that the immunoglobulin moieties of the protein conjugates have different CDRs and thus different variable regions.
A method of preparing a plurality of at least two different protein conjugate preparations as defined above may comprise the following steps:
The invention also provides a pharmaceutical preparation comprising an immunoglobulin and histidine as a buffering agent, and an aqueous pharmaceutical formulation comprising an immunoglobulin (such as immunoglobulin G) and histidine as a buffering agent.
Also provided is a set of at least two different immunoglobulin preparations, each immunoglobulin preparation comprising histidine as a buffering agent and an immunoglobulin; wherein the immunoglobulin molecules of each immunoglobulin preparation have identical CDRs; and wherein different immunoglobulin preparations differ in that the immunoglobulins of different preparations have different CDRs.
In the following, preparation of idiotypic antibodies for vaccination against NHL and expression in plants will be described. Cloning methods that can be used for cloning and expression of variable regions of Igs are described in WO 2010/040531 that is incorporated herein by reference. Notably, cloning of variable Ig regions is described in detail in Example 2 and with reference to FIG. 2 in WO 2010/040531. Simultaneous expression of heavy and light chains in plants can be done as described in WO2006/079546 or Giritch et al., Proc. Natl. Acad. Sci. USA 2006, 103 (40) 14701-14706.
When the tumor sequence of the idiotypic antibody has been determined unequivocally (e.g. after cloning as described in Example 2 of WO 2010/040531), specific primers are designed to amplify the variable regions of the heavy and light chains for subsequent cloning in viral expression vectors of the pICOT (T for TMV) and pICOP (P for PVX) series. The variable region-specific primers (cf.
Two T4 clones (
All amplified variable regions can be cloned in TMV and PVX expression vectors with a rice alpha-amylase signal peptide referred to as “ats” in the figures (an alternative thereto is barley amylase signal peptide). The cloning vectors for the heavy and light chains are TMV (qualified vector designation: pICOT series) and PVX (qualified vector designation: pICOP series) based vectors. Both contain two BsaI restriction sites located between a plant signal peptide and a plant codon-optimized immunoglobulin constant domain. The variable region of heavy and light chain can both be cloned in TMV and PVX vector, as both combinations (heavy chain in TMV and light chain in PVX, and heavy chain in PVX and light chain in TMV) will be tested for expression. The optimal combination of vectors is chosen for production.
PCR products which should correspond to 300-400 bp in size are analyzed by agarose gel electrophoresis and column-purified prior to cloning in viral vectors. The PCR fragment is flanked by recognition sites for the class IIs restriction enzyme BsaI. This restriction enzyme is used because the sequence of the 4-nucleotide 5′ overhang obtained after digestion can be chosen to be any sequence of choice (the enzyme cuts outside of its recognition site). Therefore, the same enzyme can be used to digest both ends of the PCR product while producing overhangs that are different and therefore incompatible, but compatible with the target vector. Moreover, the recognition sites are eliminated after cloning, resulting in seamless junctions. See Engler et al. PLoS ONE, 2008; 3(11): e3647 for details on cloning methods using type IIs restriction enzymes.
The cloning vectors for the heavy and light chains are TMV (pICOT series) and PVX (pICOP series) based vectors. TMV stands for tobacco mosaic virus. PVX stands for potato virus X. Both types of cloning vectors contain two BsaI restriction sites located between a rice alpha-amylase signal peptide and a plant codon-optimized immunoglobulin constant domain, which can be, for example, IgG1, IgK, or IgL, resulting in a total of six different vectors. The cloning vectors also contain a lacZ-alpha gene for blue-white selection to facilitate screening of recombinant clones and a kanamycin-resistance cassette. The variable region of the heavy chain will be cloned in pICOT-RH and pICOP-RH, and the variable region of the light chain in either pICOT-RK and pICOP-RK if it belongs to a kappa chain, or in pICOT-RL and pICOP-RL if it belongs to a lambda chain. For an overview see
For cloning, vector and PCR product are digested with BsaI and ligated in a single reaction in a DNA thermocycler. The cloning reaction is transformed in chemo-competent E. coli DH10B and plated on LB agar medium containing X-gal and kanamycin and incubated overnight at 37° C. At least one clone per construct with correct sequence (alpha-amylase apoplast targeting signal, variable and constant region) is prepared for long-term storage as glycerol stock and the corresponding plasmid DNA can be transformed in Agrobacterium tumefaciens.
Transformation of Viral Expression Vectors into Agrobacterium tumefaciens
Plasmid DNA of all four viral expression vectors verified by sequencing is electroporated into Agrobacterium strain ICF 320, and the transformation plated on selective medium containing kanamycin (viral vector resistance marker), rifampicin (ICF 320 resistance marker) and X-gal (blue/white selection based on IacZ on the Ti plasmid of ICF 320). For an overview see
Antibody Expression Test by Agro-Infiltration of Single N. benthamiana Plants and SDS-PAGE Analysis
To determine which vector combination (heavy chain in TMV or PVX and light chain in the complementary vector) provides the highest expression level, both combinations are infiltrated manually using a syringe without a needle on individual Nicotiana benthamiana plants (see
Overnight cultures of all constructs are diluted in infiltration buffer to a final OD600=0.002 and the appropriate strains are mixed in one tube. The mixture is infiltrated in the lower side of upper leaves of different N. benthamiana plants. Plants are incubated in the greenhouse for about seven days, and infiltrated leaf areas harvested from different plants for each combination (approximately 100 mg fresh weight each). Proteins are extracted and the crude extract is analyzed using SDS-PAGE and Coomassie staining. The combination of vectors which results in the highest expression level is chosen, and the selected Agrobacterium strains used for upstream processing.
Igs expressed in plants can be isolated and purified according to generally known methods. For example, standard Protein A-based purification methods using commercial antibody purification kits can be used. Another method for Ig purification is described in WO2007/031339 using plant viral particles having bound affinity proteins such as protein A or derivatives displayed on the surface of the plant viral particles.
0.5 mg/ml keyhole limpet hemocyanine (VACMUNE® liquid IEX from biosyn) and 0.5 mg/ml IgG antibody in PBS buffer pH 7.4 are mixed and cross-linked by adding 0.1% (v/v) glutardialdehyde. The mixture is incubated at 25° C. for 120 minutes. Then, the cross-linking reaction is quenched by adding 1% (v/v) 1 M aqueous glycine solution and incubating for 30 minutes. The protein conjugate solution is then frozen in liquid nitrogen until further use.
Conjugates T038 and T096 were rebuffered into the buffers shown below. The final conjugate concentration was 1 mg/ml. The obtained solutions were analysed by the Thermofluor method and by Micro DSC (differential scanning calorimetry) as well as by shaking and by applying shear forces. The following buffers were tested:
The conjugates were provided in PBS buffer after conjugation of the IgG antibodies to KLH (see Example 1. Size-exclusion chromatography (SEC) was performed on an ÄKTA™ Explorer (GE) system to yield the conjugate in the buffers listed above and indicated in the tables below.
The Thermofluor method was performed using a 750 Fast Real Time PCR System (Applied Biosystems). The formulations were added to a fluorescent dye in a 96 well-plate and were analyzed in the PCR System. The temperature was increased from 20° C. to 90° C. The melting points of proteins were determined by fluorescence detection.
Micro DSC was measured using a VP-DSC (GE Healthcare). The temperature was moved from 20° C. to 105° C. and the melting point of the protein was determined with the calorimeter.
The shear stress was generated by shaking on shaker (IKA, HS 260 control) into a climate chamber (MMM, FrioCell 200). The Critical Quality Parameter (aggregation) was decided after 1 h at 300 rpm and 20° C.
The stability of the solutions after the stress test was checked by noting the visual appearance. Further, dynamic light scattering (DLS) was performed using a Horiba LB550 (Retsch® Technology). The hydrodynamic diameter dH (median) as determined by DLS are given in the tables.
The concentration cNHL was measured by using a Nanodrop 2000 (Thermo Scientific). The NHL vaccines were calibrated at a wavelength of 280 nm.
The results are shown in the following Table 1. “Flocculation” means that individual flocculation particles could be seen by visual inspection.
The data in Table 1 show that both conjugates tested are not stable after application of shear stress in any buffer tested except histidine. In histidine, a pH above pH 7.0 achieved stability even upon application of shear stress.
The buffer of conjugates T069 and T096 was changed to 20 mM histidine pH 7.4, 0.01% Tween 80 during the workup of the conjugation reaction for storage. For the tests of this example, the buffers of the conjugates were changed to the following ones.
These formulations were prepared with or without Tween 80 (0.1%), Pluronic® F68 (0.1%) or Tween 20 (0.1%). Filtration was performed using a membrane filter (Millipoore, Millex GV, filter unit 0.22 μm. Shear stress was applied by as described in Example 2. DSC assays were performed as described in Example 2 using a VP-Capillary DSC System (Microcal). Thermal stress was applied in differential scanning fluorimetry (DSF) experiments using ThermoFluor™ assays, where the impact of external factors on the stability of a protein in solution can be determined by measuring its unfolding temperature. This technology is based on the interaction of a hydrophobic fluorescent dye (Sypro Orange) with hydrophobic domains upon heating. Csurf indicates the surfactant concentration.
In the above examples, histidine buffer showed the best stabilisation at pH 7.4. Histidine buffer was further tested in the presence of 0.01% Tween 80 with six further conjugates. The conjugates used were T038, T069, T096, T113, T117, T118 at the concentration of 1 mg/ml. Solutions were isotonised with trehalose. The test solutions were made by exchanging a phosphate buffer used for purification of the conjugates into 20 mM histidine pH 7.4 mit 0.01% Tween 80, trehalose. Tests were performed as described above.
The data of Table 6 show that a buffer containing 20 mM histidine, 0.01% Tween 80 stabilises all conjugates tested against temperature and shear stress.
Conjugate T038 was tested in 20 mM histidine pH 7.4 containing various surfactants. The following surfactants were separately tested in this buffer: Tween80 (Polysorbat 80), Tween20 (Polysorbat 20), Synperonic F68. Additionally, HP-β-CD was used as alternative stabiliser. Results are shown in the following tables.
GenBank entry Q53IP9
3408 aa, calculated molecular weight: 391.5 kDa
Gen Bank entry CAG28308
3421 aa, calculated molecular weight: 391.5 kDa
“Keyhole limpet hemocyanin: Structural and functional characterization of two different subunits and multimers”; Swerdlow R D et al.; Comparative Biochemistry and Physiology Part B: Biochemistry and Molecular Biology, Volume 113, Issue 3, March 1996, Pages 537-548
Number | Date | Country | Kind |
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11 002 145.8 | Mar 2011 | EP | regional |