Method for dynamically removing recombinant human nerve growth factor precursor by hydrophobic interaction chromatography

Abstract

A method for removing precursors in recombinant human nerve growth factor (rhNGF) by hydrophobic interaction chromatography (HIC) is provided, where a Chinese hamster ovary (CHO) cell culture is processed by column chromatography for preliminary purification, and the pretreated sample obtained therefrom is further processed in a HIC column by washing the sample and then eluting the HIC column.

Claims

1. A method for removing a precursor in recombinant human nerve growth factor (rhNGF) by hydrophobic interaction chromatography (HIC), comprising: 1) processing a Chinese hamster ovary (CHO) cell culture by column chromatography for preliminary purification, thereby obtaining a product for further chromatographic separation; 2) loading the product obtained from step 1) in a HIC column, washing the product with a washing buffer and discarding the eluate containing the precursor, wherein the washing buffer comprises an alcohol and NaCl, and; and 3) eluting the HIC column used in step 2) using an elution buffer, thereby obtaining a purified rhNGF product; wherein said washing buffer satisfies each of the following conditions: A. having higher electrical conductivity than the chromatography elution buffer in step 3; B. having a lower alcohol content than the chromatography elution buffer in step 3); and C. being within a same pH range as the product obtained from step 1); and wherein said washing in step 2) comprises using a washing volume which is determined by the following linear equation of a peak area of the product obtained from step 1): washing volume (in the unit of CV)=8.5- the peak area/ml resin/1000.

2. The method of claim 1, wherein said alcohol is ethanol.

3. The method of claim 1, wherein said washing buffer has an ethanol content of from 4% to 6% by weight.

4. The method of claim 1, wherein said washing buffer has an NaCl content of from 200 to 400 mM.

5. The method of claim 1, wherein said elution buffer in step 3) comprises an alcohol, or is an aqueous solution comprising an alcohol and NaCl.

6. The method of claim 5, wherein said elution buffer has an ethanol content of from 7% to 20% by weight.

7. The method of claim 5, wherein said elution buffer has a NaCl content of from 0 to 100 mM.

Description

BRIEF DESCRIPTION OF THE SEVERAL VIEWS OF THE DRAWINGS

(1) FIG. 1 shows a process for purifying rhNGF by HIC, wherein the process includes equilibration, loading, washing, and elution.

(2) FIG. 2 shows the relationship between the peak areas of pre-HIC samples and the washing volumes measured in CV. The plot illustrates the relationship between the peak areas of the eluted samples in the step immediately before HIC and the washing volumes used in HIC. The larger the peak area, the smaller the washing volume.

(3) FIG. 3 shows the SEC-HPLC analysis results of a sample before loading and of an eluted sample. The plot provides the SEC-HPLC analysis results of samples taken from the HIC process. The analysis results show that the washing process removed most of the precursor variants.

(4) FIG. 4 shows a summary of precursor removal rates and product recovery rates. The plot provides the statistical analysis results of multiple batches of HIC-based purification. The analysis results show high precursor variant removal rates and high product recovery rates, indicating that the present invention has good process performance.

DETAILED DESCRIPTION OF THE INVENTION

(5) The following embodiments serve only to demonstrate the method and apparatus of the present invention and are not intended to be restrictive of the scope of the present invention.

(6) The technical terms used herein are defined as follows:

(7) “Recombinant human nerve growth factor (rhNGF)” refers to human nerve growth factor that is produced by a Chinese hamster ovary (CHO) cell and expressed by genetic engineering, wherein the expressed sequence includes the 1.sup.st-118.sup.th amino acids. During the expression process, a basic amino acid moiety at the C terminal may be cut off, resulting in molecules whose sequence includes only the 1.sup.st-117.sup.th amino acids; as a result, complexes composed of molecules whose sequences include only the 1.sup.st-117.sup.th amino acids and molecules whose sequences include the 1.sup.st-118.sup.th amino acids are formed.

(8) “rhNGF precursor” refers to any of a series of proteins that are expressed from the same rhNGF gene and are formed by post-translational modification during intracellular secretion, or by the chemical reaction of an amino acid residue side chain after secretion, or by the degradation of a peptide chain.

(9) “Precursor” refers to an unprocessed or partially processed form of an expressed rhNGF. Human nerve growth factor is generally synthesized in vivo in the form of precursors. The precursors form bioactive mature rhNGF after being hydrolyzed at particular sites with furin or prohormone convertase. A precursor herein may be a complete precursor or a partial precursor but is always glycosylated.

(10) “Hydrophobic interaction chromatography (HIC)” refers to a method of separation enabled by the reversible binding between the hydrophobic ligands coupled to a stationary-phase carrier and some hydrophobic molecules in the mobile phase. Commercially available HIC materials include agarose with an immobilized phenyl group, butyl group, or tert-butyl group, and polymethyl methacrylate (PMMA) with an immobilized phenyl group, butyl group, or ether group.

(11) “Load” refers to the crude product loaded on an HIC material.

(12) “Buffer” refers to a solution that, through the reaction between paired acid and alkaline ingredients, can resist pH variation.

(13) “Equilibration buffer” refers to a buffer that is used to equilibrate an HIC material before the HIC material is loaded with a crude product.

(14) “Washing buffer” refers to a buffer that is allowed to flow through an HIC material after the HIC material is loaded with a crude product and before the protein of interest is eluted.

(15) “Elution buffer” refers to a buffer that is used to elute rhNGF from a solid phase.

(16) A “regeneration buffer” can be used to regenerate an HIC filler so that the filler can be used again. The electrical conductivity and pH value of a regeneration buffer enable the buffer to remove virtually all the contaminants and rhNGF on an HIC filler.

(17) “Electrical conductivity” refers to the ability of an aqueous solution to conduct electric current between two electrodes. The electrical conductivity of a solution can be changed by varying the ion concentration of the solution.

(18) “To load” refers to allowing a crude product to flow through an HIC material so that rhNGF and certain contaminants are bound to the HIC material.

(19) “Overhead washing” refers to the process of washing an HIC column with an equilibration buffer after the column is loaded with a crude product, the objective being to wash the crude product out of the column.

(20) “Washing” refers to the process of a washing buffer flowing through an HIC material, and generally refers to the removal of contaminants.

(21) “Elution” refers to the process of an elution buffer flowing through an HIC material, and generally refers to the obtainment of a desired product.

(22) MES is 2-(N-morpholino)ethanesulfonic acid. MOPSO is 3-(N-morpholino)-2-hydroxypropanesulfonic acid. SEC-HPLC is size-exclusion high-performance liquid chromatography. PB refers to a phosphate buffer.

(23) An HIC-based purification method according to the present invention generally includes the steps, to be sequentially performed, of: (1) equilibrating an HIC material; (2) loading the HIC material with a crude product; (3) performing overhead washing with an equilibration buffer; (4) performing intermediate washing with a washing buffer; and (5) eluting the desired rhNGF with an elution buffer.

(24) The present invention uses HIC so that rhNGF precursors (mainly precursors) can be washed under various mobile-phase conditions. The mobile-phase conditions include lowering the concentration of a salt and may also include increasing the concentration of a polar solvent. pH affects the binding between rhNGF and resin, too, and a neutral pH value is preferably used. While implementing the present invention, the buffer salt in the buffers may be sodium acetate, a phosphate, MES, or MOPSO, and it is preferable that a phosphate is used as the buffer salt. The elution salt used in the buffers may be, but is not limited to, sodium chloride, sodium acetate, potassium chloride, or ammonium sulfate, and it is preferable that sodium chloride is used as the elution salt. The organic solvent used in the buffers may be, but is not limited to, ethanol, propylene glycol, ethylene glycol, or hexamethylene glycol, and it is preferable that ethanol is used as the organic solvent.

(25) Generally, the equilibration buffer is allowed to flow through the HIC material before the HIC material is loaded with the crude product, which contains rhNGF and one or more molecular variants of rhNGF. In one preferred embodiment of the present invention, the equilibration buffer has a pH value of about 5.5 to about 7.0, such as about 6.0. An excessively low pH value (e.g., lower than 5.0) will enhance the hydrophobic effect. The salt concentration of the equilibration buffer is controlled at about 0.8 M to 1.2 M NaCl, such as about 1.1 M NaCl. An illustrative equilibration buffer contains 20 mM MES and 1.1 M NaCl and has a pH value of 6.0. Another illustrative equilibration buffer contains 20 mM PB and 1 M NaCl and has a pH value of 7.0.

(26) Once equilibrium is achieved, the HIC material is loaded with the crude product, which contains rhNGF and one or more molecular variants of rhNGF. The crude product has a pH value ranging from 5.5 to 7.0, such as 6.0 or 7.0, and a salt concentration controlled at about 0.8 M to 1.2 M NaCl, such as about 1.1 M NaCl. In one embodiment, the HIC material is loaded with a crude product obtained from HIC elution, and the loading density is about 5˜10 g/L resin in order for rhNGF and its precursors to bind to the HIC filler.

(27) After loading, overhead washing is carried with the equilibration buffer. The overhead washing conditions are identical to the conditions of the equilibration step. Generally, the overhead washing volume is 2˜3 times the column volume.

(28) When overhead washing is completed, the HIC material is washed with the washing buffer. During the washing process, the washing buffer flows through the HIC material. The composition of the washing buffer is generally so chosen as to elute as large an amount of impurities (e.g., molecular variants such as precursors) from the resin as possible, but not to elute the desired rhNGF. The pH value of the washing buffer is controlled between 5.5 and 7.0, such as at about 6.0 or 7.0; the salt concentration of the washing buffer is controlled between about 0.2 and about 0.4 M NaCl, such as at about 0.25 M; and the organic solvent in the washing buffer is controlled at about 4% to about 6% ethanol, such as about 5% ethanol. The washing volume is dynamically controlled and is determined by the elution peak area in the chromatography step immediately before the HIC step, generally 5˜7 CV. It is preferable that the washing buffer contains 20 mM PB, 0.4 M NaCl, and 6% ethanol and has a pH value of 6.0, or that the washing buffer contains 20 mM PB, 0.25 M NaCl, and 5% ethanol and has a pH value of 7.0.

(29) After the washing step, the desired rhNGF is eluted from the HIC material. The elution of rhNGF can be achieved by lowering the salt concentration or increasing the organic solvent concentration. In one embodiment, the elution buffer contains about 0 to about 100 mM NaCl and about 7% to about 20% ethanol. In most cases, the elution buffer has generally the same pH value as the washing buffer. One preferred elution buffer contains 20 mM PB, 0.1 M NaCl, and 7% ethanol and has a pH value of 7.0. Another preferred elution buffer contains 20 mM PB and 20% ethanol and has a pH value of 6.0.

(30) While the HIC-based purification method disclosed herein may include other steps, it is preferable that the method is composed only of the following steps: equilibration; loading of the crude product, which contains rhNGF and its molecular variants; the washing step for eluting the molecular variants; and the elution step for eluting the rhNGF.

(31) If necessary, the rhNGF preparation obtained by the HIC method disclosed herein may be further purified. Illustrative further purification steps have been discussed above.

Embodiment 1: HIC of rhNGF

1.1 Overall Process

(32) A chromatography column was operated in the binding-eluting mode at ambient temperature. The chromatography column used Butyl Sepharose High Performance (which is a resin composed of a highly cross-linked agarose matrix coupled with the butyl functional group) as the HIC resin and was filled with the HIC resin to a bed height of 9˜11 cm. Before loading with an ion-exchange chromatography eluted product, the storage liquid in the chromatography column was washed away with the equilibration buffer, which also equilibrated the column. The equilibrated chromatography column was then loaded with the ion-exchange chromatography eluted product in order for the product to bind to the resin. After loading, overhead washing was carried out with the equilibration buffer to wash off the unbound load. Once the overhead washing was completed, the column was washed with the washing buffer to remove molecular variants. Then, elution was performed with an elution buffer, whose volume was 3 CV at most, and the eluted product was collected. After elution, the column was cleaned with the regeneration buffer (20% ethanol) and a cleaning liquid (0.5 N NaOH) and was subsequently stored in the storage liquid until the next use (see FIG. 1).

(33) Table 1 shows the process conditions of the HIC process of rhNGF according to the present invention.

(34) TABLE-US-00001 TABLE 1 HIC process of rhNGF Flow Process velocity Stage Buffer/solution parameter (cm/hr) Column bed N/A 10 cm N/A height Equilibration 20 mM MES/1.1M NaCl, pH 4 CV 100 7.0 Loading Eluted product obtained by 5~10 g 100 ion-exchange chromatography, rhNGF/L with electrical conductivity resin higher than 70 mS/cm Overhead 20 mM MES/1.1M NaCl, pH 2 CV 100 washing 7.0 Washing 20 mM PB/0.25M NaCl/5% 6 CV 100 ethanol, pH 7.0 Elution 20 mM MES/0.1M NaCl/7% 3 CV 100 ethanol, pH 7.0 Start of product collection Electrical N/A conductivity slope smaller than −2.999 End of product collection UV280 N/A 100~150 mAU Regeneration 20% ethanol 2 CV 100 Cleaning 0.5N NaOH 3 CV  50 Storage 20% ethanol 2 CV  50

1.2 Dynamic Control of Intermediate Washing Volume

(35) The washing volume in the isocratic washing process was variable with the loaded sample volume, and there was a particular relationship between the loaded sample volume and the intermediate washing volume. The loaded sample volume was substituted by the peak area of the eluted sample in the step preceding HIC, and this allowed the decision regarding the intermediate washing volume to be made online in real time. The washing volume corresponding to the first valley (indicated by the circle in FIG. 1) of the washing process was used as the datum, and the data of multiple batches of HIC-based purification was analyzed to obtain the washing volumes and the peak area of each eluted sample in the step before HIC. The relationship between the washing volumes and the peak areas is plotted in FIG. 2. As can be seen in FIG. 2, the largest washing volume was 8.5 CV, and the washing volume decreased as the loaded sample volume increased. Generally, the normal washing volume should be larger than the volume corresponding to the first valley.

1.3 Analysis and Comparison of Samples Before and After Chromatography

(36) The rhNGF recovery rate and the precursor variant removal rate were analyzed by the SEC-HPLC method. The chromatography column used was the TSK gel G2000SWXL column (7.8×300 mm). The mobile phase was a 0.15 M-dibasic sodium phosphate and 0.1 M-sodium dihydrogen phosphate solution/acetonitrile (in a volume ratio of 85:15). During the analysis, the loaded sample volume was 20 μL, flow velocity was 0.5 mL/min, column temperature was 25 degrees, and the detection wavelength was 280/214 nm. The analysis lasted for 40 min. Proportions were calculated by the area normalization method. As the solution system was mild and did not cause dissociation of the two subunits of the rhNGF, the peak corresponded to the dimer. The SEC-HPLC method distinguished the mature rhNGF from its precursor variants relatively well. The SEC-HPLC analysis results of the sample before loading for purification and after elution are presented in FIG. 3. As can be seen in FIG. 3, the precursor variants in the product were removed by the purification process of the present invention.

1.4 Statistical Data Analysis

(37) The precursor removal rate and the product recovery rate were calculated as follows, based on the SEC-HPLC analysis results of the to-be-loaded crude product and the eluted product: precursor variant removal rate=(1− the proportion of precursor variants in the eluted product/the proportion of precursor variants in the to-be-loaded crude product)×100%; product recovery rate=(main peak area of the eluted product per unit sample input amount×eluting volume)/(main peak area of the to-be-loaded crude product per unit sample input amount×loaded sample volume)×100%. The data of multiple batches of HIC-based purification was analyzed, and the analysis results are shown in FIG. 4. The aforesaid process conditions led to a precursor variant removal rate of 98.0%±0.9% and a recovery rate of 58%±7%, indicating good process performance.