Purified adenoviral compositions

Details Purified adenoviral compositions Purified adenoviral compositions

2000-04-24

2004-04-27

Mosher, Mary E. (Department: 1648)

Drug, bio-affecting and body treating compositions

Whole live micro-organism, cell, or virus containing

Genetically modified micro-organism, cell, or virus

C424S233100, C424S199100, C424S093600, C435S235100, C435S320100, C435S239000

Reexamination Certificate

active

06726907

ABSTRACT:

BACKGROUND OF THE INVENTION
1. Field of the Invention
The present invention relates generally to the fields of cell culture and virus production. More particularly, it concerns improved methods for the culturing of mammalian cells, infection of those cells with adenovirus and the production of infectious adenovirus particles therefrom.
2. Description of Related Art
Adenoviral vectors, which express therapeutic proteins, are currently being evaluated in the clinic for the treatment of a variety of cancer indications, including lung and head and neck cancers. As the clinical trials progress, the demand for clinical grade adenoviral vectors is increasing dramatically. The projected annual demand for a 300 patient clinical trial could reach approximately 6×10
14
PFU.
Traditionally, adenoviruses are produced in commercially available tissue culture flasks or “cellfactories.” Virus infected cells are harvested and freeze-thawed to release the viruses from the cells in the form of crude cell lysate. The produced crude cell lysate (CCL) is then purified by double CsCl gradient ultracentrifugation. The typically reported virus yield from 100 single tray cellfactories is about 6×10
12
PFU. Clearly, it becomes unfeasible to produce the required amount of virus using this traditional process. New scaleable and validatable production and purification processes have to be developed to meet the increasing demand.
The purification throughput of CsCl gradient ultracentrifugation is so limited that it cannot meet the demand for adenoviral vectors for gene therapy applications. Therefore, in order to achieve large scale adenoviral vector production, purification methods other than CsCl gradient ultracentrifugation have to be developed. Reports on the chromatographic purification of viruses are very limited, despite the wide application of chromatography for the purification of recombinant proteins. Size exclusion, ion exchange and affinity chromatography have been evaluated for the purification of retroviruses, tick-borne encephalitis virus, and plant viruses with varying degrees of success (Crooks, et al., 1990; Aboud, et al., 1982; McGrath et al., 1978, Smith and Lee, 1978; O'Neil and Balkovic, 1993). Even less research has been done on the chromatographic purification of adenovirus. This lack of research activity may be partially attributable to the existence of the effective, albeit non-scalable, CsCl gradient ultracentrifugation purification method for adenoviruses.
Recently, Huyghe et al. (1996) reported adenoviral vector purification using ion exchange chromatography in conjunction with metal chelate affinity chromatography. Virus purity similar to that from CsCl gradient ultracentrifugation was reported. Unfortunately, only 23% of virus was recovered after the double column purification process. Process factors that contribute to this low virus recovery are the freeze/thaw step utilized by the authors to lyse cells in order to release the virus from the cells and the two column purification procedure.
Clearly, there is a demand for an effective and scaleable method of adenoviral vector production that will recover a high yield of product to meet the ever increasing demand for such products.
SUMMARY OF THE INVENTION
The present invention describes a new process for the production and purification of adenovirus. This new production process offers not only scalability and validatability but also virus purity comparable to that achieved using CsCl gradient ultracentrifugation.
Thus the present invention provides a method for producing an adenovirus comprising growing host cells in media at a low perfusion rate, infecting the host cells with an adenovirus, harvesting and lysing the host cells to produce a crude cell lysate, concentrating the crude cell lysate, exchanging buffer of crude cell lysate, and reducing the concentration of contaminating nucleic acids in the crude cell lysate.
In particular embodiments, the method further comprises isolating an adenoviral particle from the lysate using chromatography. In certain embodiments, the isolating consists essentially of a single chromatography step. In other embodiments, the chromatography step is ion exchange chromatography. In particularly preferred embodiments, the ion exchange chromatography is carried out at a pH range of between about 7.0 and about 10.0. In more preferred embodiments, the ion exchange chromatography is anion exchange chromatography. In certain embodiments the anion exchange chromatography utilizes DEAE, TMAE, QAE, or PEI. In other preferred embodiments, the anion exchange chromatography utilizes Toyopearl Super Q 650M, MonoQ, Source Q or Fractogel TMAE.
In certain embodiments of the present invention the glucose concentration in the media is maintained between about 0.7 and about 1.7g/L. In certain other embodiments, the exchanging buffer involves a diafiltration step.
In preferred embodiments of the present invention, the adenovirus comprises an adenoviral vector encoding an exogenous gene construct. In certain such embodiments, the gene construct is operatively linked to a promoter. In particular embodiments, the promoter is SV40 IE, RSV LTR, &bgr;-actin or CMV IE, adenovirus major late, polyoma F9-1, or tyrosinase. In particular embodiments of the present invention, the adenovirus is a replication-incompetent adenovirus. In other embodiments, the adenovirus is lacking at least a portion of the E1-region. In certain aspects, the adenovirus is lacking at least a portion of the E1A and/or E1B region. In other embodiments, the host cells are capable of complementing replication. In particularly preferred embodiments, the host cells are 293 cells.
In preferred a embodiment of the present invention it is contemplated that the exogenous gene construct encodes a therapeutic gene. For example, the therapeutic gene may encode antisense ras, antisense myc, antisense raf antisense erb, antisense src, antisense fins, antisense jun, antisense trk, antisense ret, antisense gsp, antisense hst, antisense bcl antisense abl, Rb, CFTR, p16, p21, p27, p57, p73, C-CAM, APC, CTS-1, zac1, scFV ras, DCC, NF-1, NF-2, WT-1, MEN-I, MEN-II, BRCA1, VHL, MMAC1, FCC, MCC, BRCA2, IL-1, IL-2, IL-3, IL-4, IL-5, IL-6, IL-7, IL-8, IL-9, IL-10, IL-11 IL-12, GM-CSF G-CSF, thymidine kinase or p53.
In certain aspects of the present invention, the cells may be harvested and lysed ex situ using a hypotonic solution, hypertonic solution, freeze-thaw, sonication, impinging jet, microfluidization or a detergent. In other aspects, the cells are harvested and lysed in situ using a hypotonic solution, hypertonic solution, or a detergent. As used herein the term “in situ” refers to the cells being located within the tissue culture apparatus for example CellCube™ and “ex situ” refers to the cells being removed from the tissue culture apparatus.
In particular embodiments, the cells are lysed and harvested using detergent. In preferred embodiments the detergent may be Thesit®, NP-40®, Tween-20®, Brij-58®, Triton X®-100 or octyl glucoside. In other aspects of the present invention lysis is achieved through autolysis of infected cells. In certain other aspects of the present invention the cell lysate is treated with Benzonase®, or Pulmozyme®.
In particular embodiments, the method further comprises a concentration step employing membrane filtration. In particular embodiments, the filtration is tangential flow filtration. In preferred embodiments, the filtration may utilize a 100 to 300K NMWC, regenerated cellulose, or polyether sulfone membrane.
The present invention also provides an adenovirus produced according to a process comprising the steps of growing host cells in media at a low perfusion rate, infecting the host cells with an adenovirus, harvesting and lysing the host cells to produce a crude cell lysate, concentrating the crude cell lysate, exchanging buffer of crude cell lysate, and reducing the concentration of contaminating nucleic acids in the crude cell lysate.
Other aspects of the present invention provide a method for the purification

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