Recombinant alpha-L-iduronidase, methods for producing and purifying the same and methods for treating diseases caused by deficiencies thereof

a technology of recombinant alpha-l-iduronidase and purification method, which is applied in the field of recombinant alpha-l-iduronidase, can solve the problems of high morbidity and mortality, low production level, and low clinical efficacy, and achieves preservation or enhancement of the biological activity of the enzyme and high production level

Inactive Publication Date: 2006-12-21
BIOMARIN PHARMA INC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Benefits of technology

[0017] In one aspect, the present invention features a method to produce α-L-iduronidase in amounts which enable using the enzyme therapeutically. In a broad embodiment, the method comprises the step of transfecting a cDNA encoding for all or a part of an α-L-iduronidase into a cell suitable for the expression thereof. In some embodiments, a cDNA encoding for a complete α-L-iduronidase is used, preferably a human α-L-iduronidase. However, in other embodiments, a cDNA encoding for a biologically active fragment or mutant thereof may be used. Specifically, one or more amino acid substitutions may be made while preserving or enhancing the biological activity of the enzyme. In other preferred embodiments, an expression vector is used to transfer the cDNA into a suitable cell or cell line for expression thereof. In one particularly preferred embodiment, the cDNA is transfected into a Chinese hamster ovary cell to create cell line 2.131. In yet other preferred embodiments, the production procedure features one or more of the following characteristics which have demonstrated particularly high production levels: (a) the pH of the cell growth culture may be lowered to about 6.5 to 7.0, preferably to about 6.7-6.8 during the production process, (b) about ⅔ to ¾ of the medium may be changed approximately every 12 hours, (c) oxygen saturation may be optimized at about 80% using intermittent pure oxygen sparging, (d) microcarriers with about 10% serum initially may be used to produce cell mass followed by a rapid washout shift to protein-free medium for production, (e) a protein-free or low protein medium such as a JRH Biosciences PF-CHO product may be optimized to include supplemental amounts of one or more ingredients selected from the group consisting of glutamate, aspartate, glycine, ribonucleosides and deoxyribonucleosides, (f) a perfusion wand such as a Bellco perfusion wand may be used in a frequent batch-feed process rather than a standard intended perfusion process, and (g) a mild sodium butyrate induction process may be used to induce increased α-L-iduronidase expression.
[0021] In a fifth aspect, the present invention features a novel method to purify α-L-iduronidase. According to a first embodiment, a cell mass may be grown in about 10% serum containing medium followed by a switch to a modified protein-free production medium without any significant adaptation to produce a high specific activity starting material for purification. Preferably, a concentration / diafiltration scheme is employed that allows for the removal of exogenous materials that may be required for recombinant production of the same such as, for example, Pluronics F-68, a commonly used surfactant for protecting cells from sparging damage. Such exogenous materials should normally be separated from the crude bulk to prevent fouling of the columns. In another preferred embodiment, a first column load is acidified to minimize the competitive inhibition effect of uronic acids found in protein-free medium formulations. In other preferred embodiments, a heparin, phenyl and sizing column purification scheme is used to produce pure enzyme using automatable steps and validatable media. In other preferred embodiments, the heparin and phenyl column steps are used to eliminate less desirable α-L-iduronidase that is nicked or degraded. In yet other preferred embodiments, a three step column chromatography may be used to purify the enzyme. Such a three step column chromatography may include using a blue sepharose FF, a Cu++ chelating sepharose chromatography and a phenyl sepharose HP chromatography. In another preferred embodiment, an acid pH treatment step is used to inactivate potential viruses without harming the enzyme.

Problems solved by technology

In an intermediate form known as Hurler-Scheie syndrome, mental function is generally not severely affected, but physical problems may lead to death by the teens or twenties.
Scheie syndrome is the mildest form of MPS I. It is compatible with a normal life span, but joint stiffness, corneal clouding and heart valve disease cause significant problems.
It is likely that worldwide the disease is underdiagnosed either because the patient dies of a complication before the diagnosis is made or because the milder forms of the syndrome may be mistaken for arthritis or missed entirely.
Except for bone marrow transplantation, there are no significant therapies available for MPS I. Bone marrow transplants can be effective in treating some of the symptoms of the disorder but have high morbidity and mortality in MPS I and often are not available to patients because of a lack of suitable donors.
Application of this therapy to humans has previously not been possible due to inadequate sources of α-L-iduronidase in tissues.

Method used

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  • Recombinant alpha-L-iduronidase, methods for producing and purifying the same and methods for treating diseases caused by deficiencies thereof
  • Recombinant alpha-L-iduronidase, methods for producing and purifying the same and methods for treating diseases caused by deficiencies thereof
  • Recombinant alpha-L-iduronidase, methods for producing and purifying the same and methods for treating diseases caused by deficiencies thereof

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example 1

Producing Recombinant Iduronidase

[0072] Standard techniques such as those described by Sambrook et al. (1987) “Molecular Cloning: A Laboratory Manual”, 2nd ed., Cold Spring Harbor Laboratory, Cold Spring Harbor, N.Y. may be used to clone cDNA encoding human α-L-iduronidase. The human α-L-iduronidase cDNA previously cloned was subcloned into PRCCMV (InVitrogen) as a HindIII-XbaI fragment from a bluescript KS subclone. An intron cassette derived from the murine immunoglobulin Cot intron between exons 2 and 3 was constructed using PCR amplification of bases 788-1372 (Tucker et al., Proc. Natl. Acad. Sci. USA 78: 7684-7688 (1991) of clone pRIR14.5 (Kakkis et al., Nucleic Acids Res. 16:7796 (1988)). The cassette included 136 bp of the 3′ end of exon 2 and 242 bp of the 5′ end of exon 3, which would remain in the properly spliced cDNA. No ATG sequences are present in the coding, region of the intron cassette. The intron cassette was cloned into the HindIII site 5′ of the α-L-iduronidase ...

example 2

[0077] Seed train: A vial of working cell bank (WCB) CHO cells 2.131 is partially thawed in a 37° C. water bath. The thawed cells are added to seven mL of fresh cell culture medium (DMEM / F12) containing thymidine (7.6 mg / L), hypoxanthine (13.6 mg / L), G418 (375 mg / mL) and fetal bovine serum (5%). The cells are collected by gentle centrifugation (400 r.p.m. for 5 minutes). The pelleted cells are resuspended in fresh DMEM / F12 medium substituted as described above and the cells are placed in a T-75 cm flask in 25 mL of the medium.

[0078] After 2 to 3 days of incubation at 37° C. and 5% carbon dioxide, the cells are placed in a T-225 flask with 50 mL of fresh medium. The next split of cells is into a 250 mL spinner (100 mL of cells and medium) and the agitator (spinner) is rotated at 50 r.p.m. The inoculum volume and cell number is increased by a series of incubations (cell density increases) and subculturing (cell volume increases). The subculturing is performed such that the final cell...

example 3

[0083] Recombinant iduronidase over-expressed in a Chinese Hamster Ovary (CHO) cell line, has been purified to near homogeneity following a 3 step column chromatography process. The first column involves an affinity chromatography step using Blue Sepharose 6 FF. The Blue eluate is then further purified by another affinity chromatography step using Cu++ Chelating Sepharose FF. The final polish of the highly purified enzyme is achieved by hydrophobic interaction chromatography using Phenyl Sepharose High Performance (HP). The over-all yield ranges from 45 to 55 percent and the purity of the final product is >99%. The process is robust, reproducible, and scalable for large-scale manufacturing. The purified enzyme has been characterized with respect to its enzymatic activity using a fluorescence-based substrate, and its functional uptake by fibroblast cells. The enzyme has also been characterized for substrate specificity, carbohydrate profiles, and isoelectric focusing (IEF) profiles. ...

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Abstract

The present invention provides a recombinant α-L-iduronidase and biologically active fragments and mutants thereof, methods to produce and purify this enzyme as well as methods to treat certain genetic disorders including—α-L-iduronidase deficiency and mucopolysaccharidosis I (MPS 1).

Description

[0001] This application is a continuation application of U.S. patent application Ser. No. 09 / 439,923, filed Nov. 12, 1999, now U.S. Pat. No. 6,426,208, issued Jul. 30, 2002, which is incorporated herein by reference.FIELD OF THE INVENTION [0002] The present invention is in the field of molecular biology, enzymology, biochemistry and clinical medicine. In particular, the present invention provides a recombinant α-L-iduronidase, methods to produce and purify this enzyme as well as methods to treat certain genetic disorders including α-L-iduronidase deficiency and mucopolysaccharidosis I (MPS I). BACKGROUND OF THE INVENTION [0003] Carbohydrates play a number of important roles in the functioning of living organisms. In addition to their metabolic roles, carbohydrates are structural components of the human body covalently attached to numerous other entities such as proteins and lipids (called glycoconjugates). For example, human connective tissues and cell membranes comprise proteins, c...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): A61K38/47C07H21/04C12P21/06C12N9/36C12N15/09A61K9/08A61K38/00A61K38/43A61K47/02A61K47/10A61K48/00A61P3/00A61P19/00A61P43/00C12N9/24C12N9/88
CPCA61K38/47A61K48/00C12N9/88C12N9/2402C12Y302/01075C12Y402/02004C12Y302/01076C12Y302/01014A61P1/16A61P19/00A61P3/00A61P37/02A61P37/08A61P43/00
Inventor KAKKIS, EMILTANAMACHI, BECKY
Owner BIOMARIN PHARMA INC
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