WO1993003048A1 - Process for purifying pentostatin - Google Patents
Process for purifying pentostatin Download PDFInfo
- Publication number
- WO1993003048A1 WO1993003048A1 PCT/US1992/005946 US9205946W WO9303048A1 WO 1993003048 A1 WO1993003048 A1 WO 1993003048A1 US 9205946 W US9205946 W US 9205946W WO 9303048 A1 WO9303048 A1 WO 9303048A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- pentostatin
- anion exchange
- concentrate
- resin
- exchange resin
- Prior art date
Links
- FPVKHBSQESCIEP-UHFFFAOYSA-N (8S)-3-(2-deoxy-beta-D-erythro-pentofuranosyl)-3,6,7,8-tetrahydroimidazo[4,5-d][1,3]diazepin-8-ol Natural products C1C(O)C(CO)OC1N1C(NC=NCC2O)=C2N=C1 FPVKHBSQESCIEP-UHFFFAOYSA-N 0.000 title claims abstract description 34
- FPVKHBSQESCIEP-JQCXWYLXSA-N pentostatin Chemical compound C1[C@H](O)[C@@H](CO)O[C@H]1N1C(N=CNC[C@H]2O)=C2N=C1 FPVKHBSQESCIEP-JQCXWYLXSA-N 0.000 title claims abstract description 34
- 229960002340 pentostatin Drugs 0.000 title claims abstract description 34
- 238000000034 method Methods 0.000 title claims abstract description 18
- 239000003957 anion exchange resin Substances 0.000 claims abstract description 13
- 239000012141 concentrate Substances 0.000 claims abstract description 13
- URSLCTBXQMKCFE-UHFFFAOYSA-N dihydrogenborate Chemical group OB(O)[O-] URSLCTBXQMKCFE-UHFFFAOYSA-N 0.000 claims abstract description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 6
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 4
- 125000001453 quaternary ammonium group Chemical group 0.000 claims description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims description 3
- 239000000706 filtrate Substances 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 239000002904 solvent Substances 0.000 claims 4
- 238000001953 recrystallisation Methods 0.000 claims 1
- 239000011347 resin Substances 0.000 description 19
- 229920005989 resin Polymers 0.000 description 19
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical group O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 14
- 238000000855 fermentation Methods 0.000 description 8
- 230000004151 fermentation Effects 0.000 description 8
- 239000008367 deionised water Substances 0.000 description 7
- 229910021641 deionized water Inorganic materials 0.000 description 7
- 235000013405 beer Nutrition 0.000 description 5
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical group OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 description 5
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical group Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- FZQSLXQPHPOTHG-UHFFFAOYSA-N [K+].[K+].O1B([O-])OB2OB([O-])OB1O2 Chemical compound [K+].[K+].O1B([O-])OB2OB([O-])OB1O2 FZQSLXQPHPOTHG-UHFFFAOYSA-N 0.000 description 4
- 239000000908 ammonium hydroxide Substances 0.000 description 4
- 238000002955 isolation Methods 0.000 description 4
- 229920001467 poly(styrenesulfonates) Polymers 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 238000000746 purification Methods 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- CHRJZRDFSQHIFI-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;styrene Chemical compound C=CC1=CC=CC=C1.C=CC1=CC=CC=C1C=C CHRJZRDFSQHIFI-UHFFFAOYSA-N 0.000 description 3
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 description 3
- BTBUEUYNUDRHOZ-UHFFFAOYSA-N Borate Chemical compound [O-]B([O-])[O-] BTBUEUYNUDRHOZ-UHFFFAOYSA-N 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- 238000002425 crystallisation Methods 0.000 description 3
- 230000008025 crystallization Effects 0.000 description 3
- 238000004128 high performance liquid chromatography Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 241000186988 Streptomyces antibioticus Species 0.000 description 2
- 150000001450 anions Chemical class 0.000 description 2
- 229920001429 chelating resin Polymers 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- OPTASPLRGRRNAP-UHFFFAOYSA-N cytosine Chemical compound NC=1C=CNC(=O)N=1 OPTASPLRGRRNAP-UHFFFAOYSA-N 0.000 description 2
- 238000010828 elution Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- -1 2''--deoxyguanosine Chemical compound 0.000 description 1
- 229940080778 Adenosine deaminase inhibitor Drugs 0.000 description 1
- YOOVTUPUBVHMPG-UHFFFAOYSA-N Coformycin Natural products OC1C(O)C(CO)OC1N1C(NC=NCC2O)=C2N=C1 YOOVTUPUBVHMPG-UHFFFAOYSA-N 0.000 description 1
- OIRDTQYFTABQOQ-UHTZMRCNSA-N Vidarabine Chemical compound C1=NC=2C(N)=NC=NC=2N1[C@@H]1O[C@H](CO)[C@@H](O)[C@@H]1O OIRDTQYFTABQOQ-UHTZMRCNSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 239000002487 adenosine deaminase inhibitor Substances 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 239000000063 antileukemic agent Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 150000001491 aromatic compounds Chemical class 0.000 description 1
- 150000001642 boronic acid derivatives Chemical class 0.000 description 1
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 description 1
- 229910052794 bromium Inorganic materials 0.000 description 1
- 125000001246 bromo group Chemical group Br* 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004587 chromatography analysis Methods 0.000 description 1
- YOOVTUPUBVHMPG-LODYRLCVSA-O coformycin(1+) Chemical compound O[C@@H]1[C@H](O)[C@@H](CO)O[C@H]1N1C([NH+]=CNC[C@H]2O)=C2N=C1 YOOVTUPUBVHMPG-LODYRLCVSA-O 0.000 description 1
- 230000001143 conditioned effect Effects 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 229940104302 cytosine Drugs 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- IDGUHHHQCWSQLU-UHFFFAOYSA-N ethanol;hydrate Chemical compound O.CCO IDGUHHHQCWSQLU-UHFFFAOYSA-N 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000002329 infrared spectrum Methods 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000000655 nuclear magnetic resonance spectrum Methods 0.000 description 1
- 238000005325 percolation Methods 0.000 description 1
- 230000003389 potentiating effect Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000002510 pyrogen Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000012265 solid product Substances 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000012607 strong cation exchange resin Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 125000001424 substituent group Chemical group 0.000 description 1
- 239000010414 supernatant solution Substances 0.000 description 1
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 description 1
- 238000002211 ultraviolet spectrum Methods 0.000 description 1
- 229960003636 vidarabine Drugs 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K31/00—Medicinal preparations containing organic active ingredients
- A61K31/33—Heterocyclic compounds
- A61K31/395—Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins
- A61K31/435—Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins having six-membered rings with one nitrogen as the only ring hetero atom
- A61K31/44—Non condensed pyridines; Hydrogenated derivatives thereof
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K31/00—Medicinal preparations containing organic active ingredients
- A61K31/65—Tetracyclines
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K38/00—Medicinal preparations containing peptides
- A61K38/04—Peptides having up to 20 amino acids in a fully defined sequence; Derivatives thereof
- A61K38/05—Dipeptides
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07H—SUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
- C07H19/00—Compounds containing a hetero ring sharing one ring hetero atom with a saccharide radical; Nucleosides; Mononucleotides; Anhydro-derivatives thereof
- C07H19/02—Compounds containing a hetero ring sharing one ring hetero atom with a saccharide radical; Nucleosides; Mononucleotides; Anhydro-derivatives thereof sharing nitrogen
- C07H19/04—Heterocyclic radicals containing only nitrogen atoms as ring hetero atom
- C07H19/052—Imidazole radicals
Definitions
- Pentostatin is (R)-3-(2-deoxy- ⁇ -D-erythro- pentof ranosyl)-3,6,7,8-tetrahydroimidazo[4,5-d]' [1,3]diazepin-8-ol having the structure:
- U.S. Patent 3,923,785 issued December 2, 1975, describes the production of pentostatin by fermentation of a strain of Streptomyces antibioticus which is on deposit as NRRL 3238.
- U.S. 3,923,785 also describes the isolation and purification of pentostatin from the fermentation beer.
- the present invention provides a markedly improved procedure for the isolation and purification of pentostatin.
- the present invention utilizes a combination of ion exchange resins and Sepabeads 207 which has proven to increase dramatically the amount of pure compound recovered from the fermentation broth. Without this improved recovery process the commercialization of pentostatin would be impractical due to the high cost of production of the compound in pure form.
- the present invention provides a novel process for isolating pentostatin. More particularly, the present invention provides a process for chromatographically isolating pentostatin from a crude concentrate which comprises applying the concentrate to a strongly basic borate anion exchange resin followed by application to an activated bed of Sepabeads SP207, or the equivalent thereof, and collection of the fractions containing pentostatin.
- the crude fermentation concentrate is obtained by retaining pentostatin from the fermentation beer on a strong cation exchange resin followed by elution with ammonium hydroxide and concentration of the eluate to a volume approximately 1/200 of the starting beer volume.
- This concentrate which contains several known contaminants including the "S" isomer (the C-8 epimer) of pentostatin, coformycin, 2''--deoxyguanosine, vidarabine, and cytosine, is then processed in 3 phases: 1) a precipitation step to remove gross impurities, 2) chromatography using a strongly basic anion exchange resin in the borate form and then Sepabeads SP207, or the equivalent thereof, and 3) crystallization.
- the anion exchange resins useful in the present process contain a quaternary ammonium functionality and are strongly basic anion exchange resins .
- anion exchange resins are commercially available as Dowex-lXl, Dowex-lX2, Dowex-lX4, etc., and normally supplied in the chloride form where X ⁇ is Cl ⁇ or the hydroxide form where X ⁇ is
- Rohm and Haas Company series of anion exchange resins containing a quaternary ammonium functionality may also be used- These resins are of two different types, one being a gel type and the other being a macroreticular type, and both are strongly basic.
- the literature describes the Amberlite series of resins as having quaternary ammonium groups attached to a styrenic or an acrylic type backbone.
- the anion (X-) in the commercially available, strongly basic anion exchange resin is chloride.
- This resin can be converted to the borate form for use in the present invention by treatment with a borate salt such as potassium tetraborate.
- a borate salt such as potassium tetraborate.
- the commercially available resin can be placed in a column through which is percolated several bed volumes of an aqueous solution of potassium tetraborate, after which any excess borate can be removed by passing several volumes of deionized water through the column. After use, the resin can be regenerated by washing with dilute hydrochloric acid followed by deionized water followed by a solution of potassium tetraborate.
- Diaion Sepabeads (Trademark of Mitsubishi) SP207, which are used in the presently claimed process, are depicted in the trade literature as being a styrene-divinylbenzene type of resin groups. Sepabeads SP207 have an affinity for aromatic compounds. The product is generally represented as follows:
- Purolite A425 resin is used which is a strongly basic anion gel and is equivalent to Dowex 1X2 with, for example, a mesh size of 100.
- the resin is purchased in the chloride form and is converted to the borate form as follows. Purolite A425 (chloride) resin is charged to a column and converted to the borate form by percolation of 15—16 bed volumes of ca 0.7 M KB 4 0 7 solution.
- bed volume refers to the apparent volume of resin in the column after charging a suspension of new resin in water and allowing about 1 hour for settling. All subsequent references relate to this volume.
- Purolite A425 is supplied in the chloride form; conversion to the borate form, followed by rinsing and backflushing, and finally settling for one hour, leads to a bed volume increase of about 20%.
- ammonium hydroxide eluates containing the major quantity of pentostatin are pooled and concentrated in vacuo to 250 L at a temperature less than 50°C.
- a 50 L aliquot of the above dark, viscous concentrate is stirred with 500 L of 3A ethanol and 250 L of acetone and then allowed to stand for about 24 hours. The supernatant solution is carefully removed from a dark, tarry residue, filtered through a Celite 545 coated filter, and concentrated in vacuo to 20 L at a temperature less than 28°C.
- the above, darkly colored concentrate (20 L) is applied to a column containing 135 L Purolite A425 (borate) resin prepared as described above. Passage of the charge through the column removes a great deal of color that is retained on the resin.
- the resin is then eluted with 7 bed volumes of deionized water. After a forerun of about one bed volume the pH of the eluate rises abruptly and a yellow color is observed. About 90% of the pentostatin applied to the resin is eluted in the next 3 bed volumes.
- the pentostatin- rich fractions are pooled and applied to a column containing 120 L of Diaion Sepabeads SP207 previously washed with aqueous ethanol followed by a thorough water wash.
- the Sepabead resin is washed with 3-4 bed volumes of deionized water and then eluted with ethanol-water (10:90 w/w) . After a forerun of one bed volume pentostatin begins to emerge and is essentially completely eluted in the next 2.5-3.0 bed volumes. The fractions containing the major amount of pentostatin are pooled and concentrated in vacuo to give 12 to 13% w/w solution of pentostatin. This concentrate is treated with charcoal (5% w/w with respect to pentostatin) and then filtered through Celite 545, followed by filtration through 0.45 micron and 0.22 micron membrane filters.
- the final filtrate is concentrated in vacuo to a slurry containing 60% pentostatin (w/w) to which is added 10 volumes (based on the calculated water content) of methanol.
- the resulting suspension is stirred at 0°C for 2 hours and the solid product is collected by filtration, washed with methanol, and dried at 50°C for 24 hours.
- HPLC analysis showed that this product is pentostatin contaminated with a 1.1% of the C—8 epimer of pentostatin.
- This material is recrystallized by dissolving it in 1.2 to 1.5 parts hot (82°C) water followed b ⁇ dilution with 10 volumes of methanol with stirring.
- the resulting mixture is allowed to cool, chilled at 0°C for 2 hours, and then filtered.
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- Veterinary Medicine (AREA)
- Animal Behavior & Ethology (AREA)
- Epidemiology (AREA)
- Pharmacology & Pharmacy (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Proteomics, Peptides & Aminoacids (AREA)
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- Bioinformatics & Cheminformatics (AREA)
- Biotechnology (AREA)
- Gastroenterology & Hepatology (AREA)
- Molecular Biology (AREA)
- Genetics & Genomics (AREA)
- Biochemistry (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
- Peptides Or Proteins (AREA)
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Abstract
A process for chromatographically isolating pentostatin from a crude concentrate which comprises applying the concentrate to a strongly basic borate anion exchange resin followed by application to an activated bed of Sepabeads SP207, or the equivalent thereof, and collection of the fractions containing pentostatin.
Description
PROCESS FOR PURIFYING PENTOSTATIN
BACKGROUND OF THE INVENTION
Pentostatin is (R)-3-(2-deoxy-β-D-erythro- pentof ranosyl)-3,6,7,8-tetrahydroimidazo[4,5-d]' [1,3]diazepin-8-ol having the structure:
It is a potent adenosine deaminase inhibitor and is useful as an antileukemic agent. U.S. Patent 3,923,785, issued December 2, 1975, describes the production of pentostatin by fermentation of a strain of Streptomyces antibioticus which is on deposit as NRRL 3238. U.S. 3,923,785 also describes the isolation and purification of pentostatin from the fermentation beer.
The present invention provides a markedly improved procedure for the isolation and purification of pentostatin. The present invention utilizes a combination of ion exchange resins and Sepabeads 207 which has proven to increase dramatically the amount of pure compound recovered from the fermentation broth. Without this improved recovery process the commercialization of pentostatin would be impractical
due to the high cost of production of the compound in pure form.
SUMMARY OF THE INVENTION
The present invention provides a novel process for isolating pentostatin. More particularly, the present invention provides a process for chromatographically isolating pentostatin from a crude concentrate which comprises applying the concentrate to a strongly basic borate anion exchange resin followed by application to an activated bed of Sepabeads SP207, or the equivalent thereof, and collection of the fractions containing pentostatin.
DETAILED DESCRIPTION OF THE INVENTION
As set forth above the fermentation process for producing pentostatin is described in U.S. 3,923,785, which patent is incorporated herein by reference.
The crude fermentation concentrate is obtained by retaining pentostatin from the fermentation beer on a strong cation exchange resin followed by elution with ammonium hydroxide and concentration of the eluate to a volume approximately 1/200 of the starting beer volume. This concentrate, which contains several known contaminants including the "S" isomer (the C-8 epimer) of pentostatin, coformycin, 2''--deoxyguanosine, vidarabine, and cytosine, is then processed in 3 phases: 1) a precipitation step to remove gross impurities, 2) chromatography using a strongly basic anion exchange resin in the borate form and then Sepabeads SP207, or the equivalent thereof, and 3) crystallization. In particular, it is the chromatographic phase that gives rise to the present invention. It has been found that the use of a
strongly basic anion exchange resin in combination with Sepabeads (Trademark of Mitsubishi) SP207 gives higher yields of pure product not realized heretofore.
The anion exchange resins useful in the present process contain a quaternary ammonium functionality and are strongly basic anion exchange resins . There are many such resins commercially available. Typical are the Purolite A-425 (Trademark of Purolite) and the Dowex (Trademark of Dow Chemical Company) series of strongly basic anion exchange resins which may be used and which comprise a styrene-divinylbenzene (S-DVB) polymeric backbone and a trimethylammonium or a dimethylethanolammonium side chain as generally depicted below:
The above depicted anion exchange resins are commercially available as Dowex-lXl, Dowex-lX2, Dowex-lX4, etc., and normally supplied in the chloride form where X~ is Cl~ or the hydroxide form where X~ is
OH".
A commercially available Amberlite (Trademark of
Rohm and Haas Company) series of anion exchange resins containing a quaternary ammonium functionality may
also be used- These resins are of two different types, one being a gel type and the other being a macroreticular type, and both are strongly basic. The literature describes the Amberlite series of resins as having quaternary ammonium groups attached to a styrenic or an acrylic type backbone.
There are many other commercially available resins that are equivalent to those described above and would be recognized readily by one skilled in the art as useful in the presently claimed process.
Generally, the anion (X-) in the commercially available, strongly basic anion exchange resin is chloride. This resin can be converted to the borate form for use in the present invention by treatment with a borate salt such as potassium tetraborate. To accomplish this modification the commercially available resin can be placed in a column through which is percolated several bed volumes of an aqueous solution of potassium tetraborate, after which any excess borate can be removed by passing several volumes of deionized water through the column. After use, the resin can be regenerated by washing with dilute hydrochloric acid followed by deionized water followed by a solution of potassium tetraborate. Diaion Sepabeads (Trademark of Mitsubishi) SP207, which are used in the presently claimed process, are depicted in the trade literature as being a styrene-divinylbenzene type of resin groups. Sepabeads SP207 have an affinity for aromatic compounds. The product is generally represented as follows:
wherein the X substituent is bromine. The following example illustrates the process of the present invention including the preparation of the initial concentrate, precipitation and the final clean-up chromatographic and crystallization phases. For all of the isolation and purification steps described below the course of each operation is monitored by assaying the several collected fractions for pentostatin content by high pressure liquid chromatography using the system:
Column: 250 x 4.6 mm Phenomenex, Ultremex 5 C-8 column.
Mobile Phase: 2.5 parts methanol
2.5 parts acetonitrile 95.0 parts 0.05 M aqueous (NH4)2 HP04 adjusted to pH 7.4 with phosphoric acid.
Flow rate: 1.0 mL per minute Detection: 270 nm (282 nm is used for measuring the purity of the final pentostatin product) Retention time: 10.7 minutes
As is known by those skilled in analytical chromatographic procedures, the above parameters may be modified according to the nature and condition of the column used. In the following example, Purolite A425 resin is used which is a strongly basic anion gel and is equivalent to Dowex 1X2 with, for example, a mesh size of 100. The resin is purchased in the chloride form and is converted to the borate form as follows. Purolite A425 (chloride) resin is charged to a column and converted to the borate form by percolation of 15—16 bed volumes of ca 0.7 M KB407 solution. It is most convenient to dissolve the potassium tetraborate in warm (60°C) deionized water and then cool the resulting solution to room temperature. The excess borate is rinsed from the column using deionized water (7-10 bed volumes) until a total dissolved solids meter reads 0.00 for the eluate. The column is then back washed with deionized water to remove fines and is ready for use.
In the following example the expression "bed volume" refers to the apparent volume of resin in the column after charging a suspension of new resin in water and allowing about 1 hour for settling. All subsequent references relate to this volume.
Purolite A425 is supplied in the chloride form; conversion to the borate form, followed by rinsing and backflushing, and finally settling for one hour, leads to a bed volume increase of about 20%.
EXAMPLE Production lots of Streptomyces ant-ibioticus NRRL 3238 fermentation beer containing pentostatin are prepared according to the procedure described in U.S. Patent 3,923,789, issued December 2, 1975. In a typical run, 50,000 L of fermentation beer is adjusted
to pH 8.5, stored at or below +15°C for about 20 hours, and then filtered using Celite 545. The cold filtrate is adjusted to pH 6.0 and passed through a column containing 5,000 L of Dowex 50X4 (NH4 +) that was previously conditioned with cold (about 15°C) water. The Dowex 50 resin is then washed with water and eluted with 0.1 M ammonium hydroxide followed by 0.2 M ammonium hydroxide. Throughout this elution step and subsequent isolation and purification steps the course of the operation is monitored by HPLC as described above. The ammonium hydroxide eluates containing the major quantity of pentostatin are pooled and concentrated in vacuo to 250 L at a temperature less than 50°C.
Precipitation
A 50 L aliquot of the above dark, viscous concentrate is stirred with 500 L of 3A ethanol and 250 L of acetone and then allowed to stand for about 24 hours. The supernatant solution is carefully removed from a dark, tarry residue, filtered through a Celite 545 coated filter, and concentrated in vacuo to 20 L at a temperature less than 28°C.
Chromatoqxaphy
The above, darkly colored concentrate (20 L) is applied to a column containing 135 L Purolite A425 (borate) resin prepared as described above. Passage of the charge through the column removes a great deal of color that is retained on the resin. The resin is then eluted with 7 bed volumes of deionized water. After a forerun of about one bed volume the pH of the eluate rises abruptly and a yellow color is observed. About 90% of the pentostatin applied to the resin is eluted in the next 3 bed volumes. The pentostatin- rich fractions are pooled and applied to a column
containing 120 L of Diaion Sepabeads SP207 previously washed with aqueous ethanol followed by a thorough water wash. After all of the pentostatin charge is applied, the Sepabead resin is washed with 3-4 bed volumes of deionized water and then eluted with ethanol-water (10:90 w/w) . After a forerun of one bed volume pentostatin begins to emerge and is essentially completely eluted in the next 2.5-3.0 bed volumes. The fractions containing the major amount of pentostatin are pooled and concentrated in vacuo to give 12 to 13% w/w solution of pentostatin. This concentrate is treated with charcoal (5% w/w with respect to pentostatin) and then filtered through Celite 545, followed by filtration through 0.45 micron and 0.22 micron membrane filters.
Crystallizations
The final filtrate is concentrated in vacuo to a slurry containing 60% pentostatin (w/w) to which is added 10 volumes (based on the calculated water content) of methanol. The resulting suspension is stirred at 0°C for 2 hours and the solid product is collected by filtration, washed with methanol, and dried at 50°C for 24 hours. HPLC analysis showed that this product is pentostatin contaminated with a 1.1% of the C—8 epimer of pentostatin. This material is recrystallized by dissolving it in 1.2 to 1.5 parts hot (82°C) water followed b^ dilution with 10 volumes of methanol with stirring. The resulting mixture is allowed to cool, chilled at 0°C for 2 hours, and then filtered. The collected solid is washed with methanol and dried at 50°C in vacuo to give 648.5 g pentostatin of greater than 99.7% purity. This final product is pyrogen free and exhibits ultraviolet, infrared, and NMR spectra that are identical to the corresponding
pentostatin spectra reported in Ann. N.Y. Acad. Sci. 284:21-29 (1977) .
Claims
1. A process for chromatographically isolating pentostatin from a crude concentrate which comprises applying the concentrate to a strongly basic borate anion exchange resin followed by application to an activated bed of
Sepabeads SP207, or the equivalent thereof, and collection of the fractions containing pentostatin.
2. The process of Claim 1 wherein the crude concentrate is diluted with a suitable solvent or mixture of solvents, filtered, and the filtrate containing the pentostatin is concentrated.
3. The process of Claim 2 wherein the solvent or mixture of solvents is acetone and ethanol.
4. The process of Claim 3 wherein the anion exchange resin contains a quaternary ammonium f nctionality.
5. The process of Claim 4 wherein the anion exchange resin is Purolite A425 (chloride) converted to a borate anion.
6. The process of Claim 5 wherein the collected fractions of pentostatin are further purified by recrystallization.
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP05503590A JP3141029B2 (en) | 1991-07-31 | 1992-07-16 | Method for purifying pentostatin |
| DE69215375T DE69215375T2 (en) | 1991-07-31 | 1992-07-16 | METHOD FOR PURIFYING PENTOSTATIN |
| EP92916090A EP0596943B1 (en) | 1991-07-31 | 1992-07-16 | Process for purifying pentostatin |
| GR960403293T GR3022387T3 (en) | 1991-07-31 | 1997-01-29 | Process for purifying pentostatin. |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US73871591A | 1991-07-31 | 1991-07-31 | |
| US738,715 | 1991-07-31 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO1993003048A1 true WO1993003048A1 (en) | 1993-02-18 |
Family
ID=24969187
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/US1992/005946 WO1993003048A1 (en) | 1991-07-31 | 1992-07-16 | Process for purifying pentostatin |
Country Status (15)
| Country | Link |
|---|---|
| US (1) | US5463035A (en) |
| EP (1) | EP0596943B1 (en) |
| JP (1) | JP3141029B2 (en) |
| AT (1) | ATE145404T1 (en) |
| AU (1) | AU2381792A (en) |
| DE (1) | DE69215375T2 (en) |
| DK (1) | DK0596943T3 (en) |
| ES (1) | ES2094919T3 (en) |
| GR (1) | GR3022387T3 (en) |
| HU (1) | HU215126B (en) |
| IE (1) | IE80618B1 (en) |
| MX (1) | MX9204460A (en) |
| PT (1) | PT100755B (en) |
| WO (1) | WO1993003048A1 (en) |
| ZA (1) | ZA925732B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2007073908A1 (en) * | 2005-12-29 | 2007-07-05 | Evultis S.A. | A process for the isolation of pharmacologically active principles of vegetable and animal origin |
| CN101798330A (en) * | 2009-02-06 | 2010-08-11 | 杭州华东医药集团生物工程研究所有限公司 | Extraction and purification method of pentostatin |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| ES2292927T3 (en) * | 2003-01-16 | 2008-03-16 | Adorkem Technology Spa | IMMOBILIZED BIOCATALIZERS USED FOR THE PRODUCTION OF NATURAL NUCLEOSIDS AND MODIFIED ANALOGS THROUGH TRANSGLICOSILATION ENZYMATIC REACTIONS. |
| CN101792722B (en) * | 2009-02-04 | 2013-04-10 | 杭州华东医药集团生物工程研究所有限公司 | Streptomyces coelicolor and application thereof |
| US20100261666A1 (en) * | 2009-04-14 | 2010-10-14 | The Board Of Trustees Of The University Of Illinois | Compositions and methods for the treatment of myocardial dysfunction associated with sirs or sepsis |
| CN102453065B (en) * | 2010-10-29 | 2014-12-17 | 上海医药工业研究院 | Method for removing impurities in pentostatin fermentation liquid |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0270017A2 (en) * | 1986-12-01 | 1988-06-08 | Syngene, Inc. | Method of isolating and purifying nucleic acids from biological samples |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3923785A (en) * | 1974-04-22 | 1975-12-02 | Parke Davis & Co | (R)-3-(2-deoxy-{62 -D-erythro-pentofuranosyl)-3,6,7,8-tetrahydroimidazo{8 4,5-d{9 {8 1,3{9 diazepin-8-ol |
| US4713372A (en) * | 1984-03-16 | 1987-12-15 | Warner-Lambert Company | 2-chloropentostatin compound having adenosine diaminase inhibitory activity |
| IT1182764B (en) * | 1985-06-26 | 1987-10-05 | Pietro Crocoli | WATER CLOSET, PARTICULARLY SUITABLE FOR VEHICLES |
| US4908441A (en) * | 1988-07-19 | 1990-03-13 | Warner-Lambert Company | Deoxyadenosine compounds and methods of making and using the same |
-
1992
- 1992-07-16 DE DE69215375T patent/DE69215375T2/en not_active Expired - Lifetime
- 1992-07-16 HU HU9400257A patent/HU215126B/en unknown
- 1992-07-16 JP JP05503590A patent/JP3141029B2/en not_active Expired - Lifetime
- 1992-07-16 AU AU23817/92A patent/AU2381792A/en not_active Abandoned
- 1992-07-16 AT AT92916090T patent/ATE145404T1/en active
- 1992-07-16 ES ES92916090T patent/ES2094919T3/en not_active Expired - Lifetime
- 1992-07-16 EP EP92916090A patent/EP0596943B1/en not_active Expired - Lifetime
- 1992-07-16 WO PCT/US1992/005946 patent/WO1993003048A1/en active IP Right Grant
- 1992-07-16 DK DK92916090.1T patent/DK0596943T3/en active
- 1992-07-30 MX MX9204460A patent/MX9204460A/en unknown
- 1992-07-30 IE IE922507A patent/IE80618B1/en not_active IP Right Cessation
- 1992-07-30 ZA ZA925732A patent/ZA925732B/en unknown
- 1992-07-31 PT PT100755A patent/PT100755B/en not_active IP Right Cessation
-
1995
- 1995-02-28 US US08/396,443 patent/US5463035A/en not_active Expired - Lifetime
-
1997
- 1997-01-29 GR GR960403293T patent/GR3022387T3/en unknown
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0270017A2 (en) * | 1986-12-01 | 1988-06-08 | Syngene, Inc. | Method of isolating and purifying nucleic acids from biological samples |
Non-Patent Citations (2)
| Title |
|---|
| ANALYTICAL BIOCHEMISTRY, Vol. 55, 1973 Joseph G. Cory et al: "A Convenient Assay for ADP Reductase Activity Using Dowex-1-Borate Columns ", * |
| J. STEROID BIOCHEM, Vol. 18, No. 3, 1983 T. Fotsis et al: "Selective chromatographic fractionation of catechol estrogens on anion exchangers in borate form ", * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2007073908A1 (en) * | 2005-12-29 | 2007-07-05 | Evultis S.A. | A process for the isolation of pharmacologically active principles of vegetable and animal origin |
| CN101798330A (en) * | 2009-02-06 | 2010-08-11 | 杭州华东医药集团生物工程研究所有限公司 | Extraction and purification method of pentostatin |
Also Published As
| Publication number | Publication date |
|---|---|
| PT100755B (en) | 1999-07-30 |
| PT100755A (en) | 1993-10-29 |
| ES2094919T3 (en) | 1997-02-01 |
| ZA925732B (en) | 1994-01-31 |
| MX9204460A (en) | 1993-04-01 |
| EP0596943B1 (en) | 1996-11-20 |
| US5463035A (en) | 1995-10-31 |
| ATE145404T1 (en) | 1996-12-15 |
| EP0596943A1 (en) | 1994-05-18 |
| JP3141029B2 (en) | 2001-03-05 |
| HU215126B (en) | 1998-09-28 |
| JPH06509355A (en) | 1994-10-20 |
| DK0596943T3 (en) | 1997-04-21 |
| HUT65981A (en) | 1994-08-29 |
| AU2381792A (en) | 1993-03-02 |
| DE69215375T2 (en) | 1997-03-13 |
| DE69215375D1 (en) | 1997-01-02 |
| IE80618B1 (en) | 1998-10-21 |
| HU9400257D0 (en) | 1994-05-30 |
| IE922507A1 (en) | 1993-02-10 |
| GR3022387T3 (en) | 1997-04-30 |
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