Title of Invention

"A PROCESS FOR THE PRODUCTION OF CIS-6-PHENYL-5-[4-(2-PYRROLIDIN-1-YL-ETHOXY)-PHENYL]-5,6,7,8-TETRAHYDRONAPHTHALENE-2-OL"

Abstract The present invention relates to the use of microorganisms of the Monosporium and Thamostylum genera to diastereoselectively O-demethylate pharmaceutical intermediates, to produce compounds of the formulae:
Full Text The present invention is directed to a process for the production of cis-6-phenyl-5-[4-(2-pyrrolidin-1-yl-ethoxy)-phenyl]-5,6,7,8-tetrahydronaphthalene-2-ol and more particularly, to the use of microbial biotransformation to O-demethylate certain pharmaceutical intermediate compounds. More specifically, it is directed to the use of certain microoganisms to O-demethylate certain pharmacetical intermediate compounds.
An article in Analytica Chimica Acta(1990) 233, 191-198 refers to the use of Cunninghamella elegans to demethylate certain n-propylnoraporphine compounds.
An article in Biomedical and Enviromental Mass Spectrometry (1986) 13, 223-229 refers to the use of Cunninghamella elegans to produce potential metabolites of W-n-propyl norapo morphine.
A review article published in Enzyme and Microbial Technology (1984) 6,242-253 at pages 250-252 broadly reviews the use of certain microorganisms, e.g. fungal species such as Cunninghamella, Aspergillus, Thamnostylum, Penicilium and Sepedonium to 0-dealkylate certain compounds.
Chapter 5.5 of Biotransformations in Preparative Organic Chemistry by H.G. Davies et al refers to the use of Sepedonium chrysospermum and Cunninghamella elegans to demethylate certain compounds, including vindoline and 10,11-dimethoxyaporphine.
An article in Phytochemistry (1997) 44 (8), 1479-1482, refers to the use of Aspergillus n/gerto produce (-)-pinoresinol through O-demethylation of (±)-eudesmin.
United States patent number 5,618,707 granted April 18, 1997 refers to the use of Zygosaccharomyces bailii ATCC 38924 to stereoselectively reduce a pentanoic acid compound to a phenyloxazolidinone product.
United States patent number 5,580,764 refers to the use of oxido/reductases from Lactobacillus plantarum, Pichia haplophila, Candida utilis, Lactobacillus buchmans, Aspergillus flavus and Neurospora crassa to reduce intermediates in the synthesis of carbonic anhydrase inhibitors.
Accordingly, there is provided a process for the production of cis-6-phenyl-5-[4-(2-pyrrolidin-l-yl-ethoxy)-phenyl]-5,6,7,8-tetrahydronaphthalene-2-ol of the formula:

(Formula Removed)
from a compound of the formula (Formula Removed)

comprising selectively demethylating a compound of formula II in the presence of an enzyme derived from a culture of a microorganism of the genus Thamnostylum piriforme ATCC 8992.
Brief Description of the Accompanying Drawings
FIGS 1-4 illustrate High Pressure Liquid Choromatography profiles generated using microbial biotransformation by 3 fungal cultures.
Summary of the Invention
In one embodiment, the present invention is directed to a process for the production of a compound of the formula:
(Formula Removed)
from a compound of the formula
(Formula Removed)
comprising selectively demethylating a compound of formula II in the presence of an enzyme derived from a culture of a microorganism of the genus Monosporium.
Preferred is the process wherein said microorganism is Monosporium oiivaceum.
Also preferred is the process wherein said Monosporium oiivaceum is Monosporium oiivaceum ATCC 36300.
In another embodiment, the present invention is directed to a process for the preparation of a compound of the formula
(Formula Removed)
comprising selectively demethylating a compound of formula II in the presence of an enzyme derived from a microorganism of the genus Thamnostylum.
Preferred is the process wherein said microorganism is Thamnostylum piriforme.
Also preferred is the process wherein said Thamnostylum piriforme is Thamnostylum] (piriforme ATCC 8992)
In another embodiment, the present invention is directed to the use of a compound of the formula
from a compound of the formula

(Formula Removed)
to produce a compound of the formula
(Formula Removed)
Preferred is the use wherein a compound of formula II is non-selectively demethylated.
Detailed Description of The Invention
This invention comprises using microorganisms to effect O-demethylation of an intermediate in the synthesis of CP-336,156 (estrogen agonist/osteoporosis). Use of microbes eliminates the chemical step which produces methyl bromide, a greenhouse gas which is difficult and expensive to trap, as a byproduct.
The biotransformation may be carried out using whole cell cultures of the micoorganisms, cell extracts of the microorganisms, or purified enzymes from the microorganisms.
The starting material for this microbial biotransformation is CP-324,098, which is a mixture of the c/s diastereomers. Three fungi have been found which carry out this reaction with different stereoselectivities. Cunninghamella echinulata O-demethylates both diastereomers to form the racemic mixture named CP-3 19,609, which is comprised of the diastereomers CP-
336,156 and CP-335,992. Monosporium olivaceum and Thamnostylum piriforme act on only one of the diastereomers in CP-324,098 and yield a single diastereomer product as indicated below.
(Formula Removed)
The starting material and the products made by these three organisms were determined by chiral HPLC as shown in FIGS 1-4. The final products of the reactions of all three microorganisms were isolated from the fementation broth and characterized by NMR MS, and chiral HPLC to confirm their identity
Having described the invention in general terms, reference is now made to specific examples. It is to be understood that these examples are not meant to limit the present invention, the scope of which is detemined by the appended claims
Monosporium olivaceum ATCC 36300 and Thammostylum piriforme ATCC 8992 can be obtained from the American Type Culture Collection. A culture so obtained is added to a suitable growth medium and is incubated with shaking until growth occurs. The cultures thus prepared are used to inoculate slants. Portions of these slants are frozen as master stocks. The respective microorganisms are inoculated from slants into two flasks containing a growth medium whose composition is shown below. The fermentation is carried out at temperatures ranging from about 22 to about 32; however, for optimum results it is preferable to conduct the fermentation at about
28. The pH of the medium is controlled at about pH 6-7 by the use of suitable organic or inorganic buffers incorporated into the fermentation medium or by periodic addition of a base. Good growth of the microorganism is achieved within 48 to 72 hours. The contents of the flasks are transferred to a Fernbach flask containing fresh growth medium having the same composition as the previously used growth medium. Variation of the medium will alter the yield of the compound and its rate of production. The preferred media composition is set forth in the example section. After shaking for one additional day, a sterile-filtered solution of rapamycin in a suitable solvent such as dimethyl sulfoxide or dimethylformamdide is added. The fermentation is continued for one to six days. It is preferred to continue the fermentation for about two days.
A suitable growth medium for use in the process of this invention will contain a source or sources of assimilable carbon, assimilable nitrogen and inorganic salts containing essential minerals. In general, many carbohydrates such as glucose, maltose, mannose, sucrose, starch, glycerin, millet jelly, molasses, soy bean and the like can be used as sources of assimilable carbon. Sources of assimilable nitrogen include such materials as yeast and casein hydrolysates, primary yeast, yeast extracts, cottonseed flour, soybean solids, wheat germ meat extracts, peptone, corn steep liquor, and ammonium salts. The inorganic salt nutrients which can be incorporated in the culture medium are the customary salts yielding sodium, iron, magnesium, potassium, cobalt, phosphate and the like. In general, of course, the techniques employed and are not intended to be limiting.
Suitable grow media include (a) dextrose (20 g), yeast extract (5g), soy flour (5 g), NaCI (5g), K2HPO4 (5g) and distilled water (1000 milliliters) where the pH is adjusted to 7.0 with aqueous HCI; (b) dextrin (10g), beef extract (3 g), ardamine pH (5g), N-Z amine type E (5 g), MgSO47H2O (0.,5 g), KH2PO4 (0.37 g), CaCO3 (0.5 g), distilled water (1000 milliliters) where the pH is adjusted to 7.1 with aqueous HCI followed by a second stage of glucose (10 g), Hy-Case SF (2 g), beef extract (1 g), corn steep liquor (3 g), distilled water (1000 milliliters) where the pH is adjusted to 7.0; (c) glucose (10 g), corn step liquor (6 g), KH2PO4 (3 g), CaCO3 (3.5 g), Soybean oil (crude, 2.2 milliliters), yeast extract (2.5 g), distilled water (1000 milliliters) where the pH is adjusted to 7.0 - 7.3 with aqueous HCI; (d) malt syrup (20 g), soybean mean (5 g), casein (1 g), dried yeast (1 g), NaCI (5g), distilled water (1000 milliliters); (e) lactose (75 g), Pharmamedia (substitute yeast extract, 40 g), CaCO3 (10 g), Na2SO3 (4 g), distilled water (1000 milliliters); (f) ISP #3; (h) ISP#4; (I) ISP#5 and the like. Procedures
Cultures: Cunninghamella echinulata ATCC 9244 and ATCC 36190; Monosporium olivaceum ATCC 36300 and Thamnostylum piriforme ATCC 8992. Biotransformation Growth medium (inoculum & biotransformation stages):

glucose 20 g/l pH to 7.0
soy flour or soy meal 5
yeast extract 5
NaCI 5
K2HPO4 5
25 ml per 125 ml Erlenmeyer flask for inoculum and biotransformation.
Inoculate from slants or frozen stock cultures into 25 ml of the medium above in a 125 ml Erlenmeyer flask and incubate with shaking at 28°C for 2-3 days. Transfer 2.5 ml into 25 ml of fresh broth in an Erlenmeyer flask and shake another day. Add CP-324,098 dissolved in DMSO and filter sterilized to a final concentration of 0.2 mg/ml. Additional substrate can be fed at 1 day intervals. Continue incubation with shaking for 1-6 days.
Extraction and purification
Broth was extracted with twice its volume of ethyl acetate in a separatory funnel. The phases were separated by centrifugation at 1000 x g for 5 minutes after which the upper ethyl acetate phase was carefully removed and evaporated to dryness. Methanol also works well as an extraction solvent. The product can be purified using solid phase extraction and preparative HPLC.
Chiral HPLC Assay
Column Chiral OD, 4.6 x 250 mm (Daicel, Chiral
Technologies)
Flow Rate 0.7 ml/min
Sample Size 20 µl
Concentration 0.1 mg/ml
Temperature 30°C
Detection UV at 220 nm
Mobile Phase 100 ml ethyl alcohol (USP, dehydrated, 200
proof) plus 900 ml hexane plus 1 ml N'N'-
diethyl amine
Samples are dissolved in ethanol,




WE CLAIM:-
1.
A process for the production of cis-6-phenyl-5-[4-(2-pyrrolidin-l-yl-ethoxy)-phenyl]-5,6,7,8-tetrahydronaphthalene-2-ol of the formula:
(Formula Removed)
from a compound of the formula
(Formula Removed)
comprising selectively demethylating a compound of formula II in the presence of an enzyme derived from a culture of a microorganism of the genus Thamnostylum piriforme ATCC 8992.
2. A process for the production of cis-6-phenyl-5-[4-(2-pyrrolidin-l-yl-ethoxy)-phenyl]-5,6,7,8-tetrahydronaphthalene-2-ol of the formula I substantially as herein described with reference to the accompanying drawings.

Documents:

157-del-2003-abstract.pdf

157-del-2003-claims.pdf

157-del-2003-correspondence-others.pdf

157-del-2003-correspondence-po.pdf

157-del-2003-description (complete).pdf

157-del-2003-drawings.pdf

157-del-2003-form-1.pdf

157-del-2003-form-2.pdf

157-del-2003-form-3.pdf

157-del-2003-form-4.pdf

157-del-2003-form-5.pdf

157-del-2003-gpa.pdf

157-del-2003-petition-137.pdf

abstract.jpg


Patent Number 213821
Indian Patent Application Number 157/DEL/2003
PG Journal Number 04/2008
Publication Date 25-Jan-2008
Grant Date 17-Jan-2008
Date of Filing 20-Feb-2003
Name of Patentee PFIZER PRODUCTS, INC.
Applicant Address EASTERN POINT ROAD, GROTON, CONNECTICUT 06340, U.S.A.
Inventors:
# Inventor's Name Inventor's Address
1 SUSAN JANE TRUESDELL 40 METCALF STREET, WARWICK, RHODE ISLAND 02888, U.S.A.
PCT International Classification Number C12P 17/18
PCT International Application Number N/A
PCT International Filing date
PCT Conventions:
# PCT Application Number Date of Convention Priority Country
1 60/098,255 1998-08-28 U.S.A.