MXPA99009970A - Microbial reduction stereoselectiva of a tetralone racém - Google Patents
Microbial reduction stereoselectiva of a tetralone racémInfo
- Publication number
- MXPA99009970A MXPA99009970A MXPA/A/1999/009970A MX9909970A MXPA99009970A MX PA99009970 A MXPA99009970 A MX PA99009970A MX 9909970 A MX9909970 A MX 9909970A MX PA99009970 A MXPA99009970 A MX PA99009970A
- Authority
- MX
- Mexico
- Prior art keywords
- formula
- compound
- atcc
- microorganism
- enzyme
- Prior art date
Links
- XHLHPRDBBAGVEG-UHFFFAOYSA-N 1-Tetralone Chemical compound C1=CC=C2C(=O)CCCC2=C1 XHLHPRDBBAGVEG-UHFFFAOYSA-N 0.000 title claims abstract description 105
- 238000006722 reduction reaction Methods 0.000 title claims abstract description 82
- 230000001603 reducing Effects 0.000 title claims abstract description 81
- 230000000813 microbial Effects 0.000 title claims abstract description 27
- 244000005700 microbiome Species 0.000 claims abstract description 118
- 150000001875 compounds Chemical class 0.000 claims abstract description 115
- 108090000790 Enzymes Proteins 0.000 claims abstract description 67
- 102000004190 Enzymes Human genes 0.000 claims abstract description 67
- 238000000034 method Methods 0.000 claims abstract description 49
- 239000000203 mixture Substances 0.000 claims abstract description 19
- VGKDLMBJGBXTGI-SJCJKPOMSA-N Sertraline Chemical compound C1([C@@H]2CC[C@@H](C3=CC=CC=C32)NC)=CC=C(Cl)C(Cl)=C1 VGKDLMBJGBXTGI-SJCJKPOMSA-N 0.000 claims abstract description 11
- 229960002073 Sertraline Drugs 0.000 claims abstract description 11
- 230000015572 biosynthetic process Effects 0.000 claims abstract description 8
- 238000003786 synthesis reaction Methods 0.000 claims abstract description 6
- 230000002194 synthesizing Effects 0.000 claims abstract description 6
- 238000002360 preparation method Methods 0.000 claims description 30
- 241000320412 Ogataea angusta Species 0.000 claims description 28
- 239000001963 growth media Substances 0.000 claims description 24
- 230000000707 stereoselective Effects 0.000 claims description 24
- CSCPPACGZOOCGX-UHFFFAOYSA-N acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 18
- 240000004808 Saccharomyces cerevisiae Species 0.000 claims description 17
- 235000014680 Saccharomyces cerevisiae Nutrition 0.000 claims description 17
- 241000293029 Absidia caerulea Species 0.000 claims description 10
- 239000002904 solvent Substances 0.000 claims description 9
- 244000168141 Geotrichum candidum Species 0.000 claims description 7
- 235000017388 Geotrichum candidum Nutrition 0.000 claims description 7
- 238000004587 chromatography analysis Methods 0.000 claims description 6
- 239000000843 powder Substances 0.000 claims description 6
- 241000192237 [Candida] schatavii Species 0.000 claims description 5
- 238000000926 separation method Methods 0.000 claims description 5
- 238000002425 crystallisation Methods 0.000 claims description 4
- 230000005712 crystallization Effects 0.000 claims description 4
- 241000223678 Aureobasidium pullulans Species 0.000 claims description 3
- 241001489166 Cyberlindnera fabianii Species 0.000 claims description 3
- 241001539803 Magnusiomyces capitatus Species 0.000 claims description 3
- 235000003534 Saccharomyces carlsbergensis Nutrition 0.000 claims description 3
- 229940081969 Saccharomyces cerevisiae Drugs 0.000 claims description 3
- 241001123649 Schwanniomyces polymorphus Species 0.000 claims description 3
- 241000306282 Umbelopsis isabellina Species 0.000 claims description 3
- 241000180122 Umbelopsis vinacea Species 0.000 claims description 3
- 241000235389 Absidia Species 0.000 claims description 2
- 239000003960 organic solvent Substances 0.000 claims description 2
- 230000001590 oxidative Effects 0.000 claims description 2
- 241000228150 Penicillium chrysogenum Species 0.000 claims 1
- 241000187419 Streptomyces rimosus Species 0.000 claims 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 39
- XEKOWRVHYACXOJ-UHFFFAOYSA-N acetic acid ethyl ester Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 33
- PEDCQBHIVMGVHV-UHFFFAOYSA-N glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 22
- 239000000284 extract Substances 0.000 description 20
- 239000002609 media Substances 0.000 description 18
- 238000000855 fermentation Methods 0.000 description 17
- 230000004151 fermentation Effects 0.000 description 17
- FAPWRFPIFSIZLT-UHFFFAOYSA-M sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 14
- 230000000875 corresponding Effects 0.000 description 11
- 150000002576 ketones Chemical class 0.000 description 11
- 210000004027 cells Anatomy 0.000 description 10
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 10
- 239000011780 sodium chloride Substances 0.000 description 10
- 239000011550 stock solution Substances 0.000 description 10
- 241000233866 Fungi Species 0.000 description 8
- 235000011187 glycerol Nutrition 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 239000012138 yeast extract Substances 0.000 description 7
- WQZGKKKJIJFFOK-VFUOTHLCSA-N β-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 description 7
- 229940041514 Candida albicans extract Drugs 0.000 description 6
- VTYYLEPIZMXCLO-UHFFFAOYSA-L calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 6
- 238000004296 chiral HPLC Methods 0.000 description 6
- 230000002255 enzymatic Effects 0.000 description 6
- 238000000605 extraction Methods 0.000 description 6
- 235000010469 Glycine max Nutrition 0.000 description 5
- 238000007792 addition Methods 0.000 description 5
- 238000004128 high performance liquid chromatography Methods 0.000 description 5
- 229910052757 nitrogen Inorganic materials 0.000 description 5
- 230000003647 oxidation Effects 0.000 description 5
- 238000007254 oxidation reaction Methods 0.000 description 5
- 108090000854 Oxidoreductases Proteins 0.000 description 4
- 102000004316 Oxidoreductases Human genes 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 150000001298 alcohols Chemical class 0.000 description 4
- 238000004458 analytical method Methods 0.000 description 4
- 239000008121 dextrose Substances 0.000 description 4
- 239000012153 distilled water Substances 0.000 description 4
- 239000011521 glass Substances 0.000 description 4
- 210000003702 immature single positive T cell Anatomy 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 235000011149 sulphuric acid Nutrition 0.000 description 4
- WQZGKKKJIJFFOK-GASJEMHNSA-N D-Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 3
- 241000235575 Mortierella Species 0.000 description 3
- 241000209149 Zea Species 0.000 description 3
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 3
- 235000010216 calcium carbonate Nutrition 0.000 description 3
- 229910000019 calcium carbonate Inorganic materials 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 235000005822 corn Nutrition 0.000 description 3
- 235000005824 corn Nutrition 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 235000013312 flour Nutrition 0.000 description 3
- 239000008103 glucose Substances 0.000 description 3
- 239000007924 injection Substances 0.000 description 3
- 238000002347 injection Methods 0.000 description 3
- -1 ketone compound Chemical class 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 235000013372 meat Nutrition 0.000 description 3
- 235000008935 nutritious Nutrition 0.000 description 3
- 239000012071 phase Substances 0.000 description 3
- 229920001690 polydopamine Polymers 0.000 description 3
- 229920000136 polysorbate Polymers 0.000 description 3
- KWYUFKZDYYNOTN-UHFFFAOYSA-M potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 239000000758 substrate Substances 0.000 description 3
- 239000003643 water by type Substances 0.000 description 3
- JGMBHJNMQVKDMW-UHFFFAOYSA-N 4-(3,4-dichlorophenyl)-3,4-dihydro-2H-naphthalen-1-one Chemical compound C1=C(Cl)C(Cl)=CC=C1C1C2=CC=CC=C2C(=O)CC1 JGMBHJNMQVKDMW-UHFFFAOYSA-N 0.000 description 2
- 241000186361 Actinobacteria <class> Species 0.000 description 2
- 240000007842 Glycine max Species 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N HCl Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 239000007836 KH2PO4 Substances 0.000 description 2
- GUBGYTABKSRVRQ-YOLKTULGSA-N Maltose Natural products O([C@@H]1[C@H](O)[C@@H](O)[C@H](O)O[C@H]1CO)[C@@H]1[C@H](O)[C@@H](O)[C@@H](O)[C@@H](CO)O1 GUBGYTABKSRVRQ-YOLKTULGSA-N 0.000 description 2
- GNSKLFRGEWLPPA-UHFFFAOYSA-M Monopotassium phosphate Chemical compound [K+].OP(O)([O-])=O GNSKLFRGEWLPPA-UHFFFAOYSA-M 0.000 description 2
- 241000235648 Pichia Species 0.000 description 2
- LPNYRYFBWFDTMA-UHFFFAOYSA-N Potassium tert-butoxide Chemical compound [K+].CC(C)(C)[O-] LPNYRYFBWFDTMA-UHFFFAOYSA-N 0.000 description 2
- 235000019764 Soybean Meal Nutrition 0.000 description 2
- 241000187747 Streptomyces Species 0.000 description 2
- 244000052616 bacterial pathogens Species 0.000 description 2
- UIIMBOGNXHQVGW-UHFFFAOYSA-M buffer Substances [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 2
- 239000005018 casein Substances 0.000 description 2
- 235000021240 caseins Nutrition 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 2
- 230000004059 degradation Effects 0.000 description 2
- 238000006731 degradation reaction Methods 0.000 description 2
- 238000005755 formation reaction Methods 0.000 description 2
- VLKZOEOYAKHREP-UHFFFAOYSA-N hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 2
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 125000000468 ketone group Chemical group 0.000 description 2
- YMWUJEATGCHHMB-UHFFFAOYSA-N methylene dichloride Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 2
- 229910000402 monopotassium phosphate Inorganic materials 0.000 description 2
- 235000019796 monopotassium phosphate Nutrition 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- WQDUMFSSJAZKTM-UHFFFAOYSA-N sodium methoxide Chemical compound [Na+].[O-]C WQDUMFSSJAZKTM-UHFFFAOYSA-N 0.000 description 2
- 239000004455 soybean meal Substances 0.000 description 2
- 239000007858 starting material Substances 0.000 description 2
- 241001446247 uncultured actinomycete Species 0.000 description 2
- HVYWMOMLDIMFJA-DPAQBDIFSA-N (3β)-Cholest-5-en-3-ol Chemical compound C1C=C2C[C@@H](O)CC[C@]2(C)[C@@H]2[C@@H]1[C@@H]1CC[C@H]([C@H](C)CCCC(C)C)[C@@]1(C)CC2 HVYWMOMLDIMFJA-DPAQBDIFSA-N 0.000 description 1
- QQZOPKMRPOGIEB-UHFFFAOYSA-N 2-Hexanone Chemical compound CCCCC(C)=O QQZOPKMRPOGIEB-UHFFFAOYSA-N 0.000 description 1
- VGKDLMBJGBXTGI-UHFFFAOYSA-N 4-(3,4-dichlorophenyl)-N-methyl-1,2,3,4-tetrahydronaphthalen-1-amine Chemical compound C12=CC=CC=C2C(NC)CCC1C1=CC=C(Cl)C(Cl)=C1 VGKDLMBJGBXTGI-UHFFFAOYSA-N 0.000 description 1
- UCTNTYHJFWMUBD-UHFFFAOYSA-M 4-chloro-3-oxobutanoate Chemical compound [O-]C(=O)CC(=O)CCl UCTNTYHJFWMUBD-UHFFFAOYSA-M 0.000 description 1
- 125000004172 4-methoxyphenyl group Chemical group [H]C1=C([H])C(OC([H])([H])[H])=C([H])C([H])=C1* 0.000 description 1
- 241000208140 Acer Species 0.000 description 1
- 206010002855 Anxiety Diseases 0.000 description 1
- 206010057666 Anxiety disease Diseases 0.000 description 1
- 241000219310 Beta vulgaris subsp. vulgaris Species 0.000 description 1
- 241000252867 Cupriavidus metallidurans Species 0.000 description 1
- CZMRCDWAGMRECN-UGDNZRGBSA-N D-sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 1
- 229920001353 Dextrin Polymers 0.000 description 1
- 239000004375 Dextrin Substances 0.000 description 1
- ZPWVASYFFYYZEW-UHFFFAOYSA-L Dipotassium phosphate Chemical compound [K+].[K+].OP([O-])([O-])=O ZPWVASYFFYYZEW-UHFFFAOYSA-L 0.000 description 1
- YPZRHBJKEMOYQH-UYBVJOGSSA-N FADH2 Chemical compound C1=NC2=C(N)N=CN=C2N1[C@@H]([C@H](O)[C@@H]1O)O[C@@H]1COP(O)(=O)OP(O)(=O)OC[C@@H](O)[C@@H](O)[C@@H](O)CN1C(NC(=O)NC2=O)=C2NC2=C1C=C(C)C(C)=C2 YPZRHBJKEMOYQH-UYBVJOGSSA-N 0.000 description 1
- YTNIXZGTHTVJBW-SCRDCRAPSA-N FMNH2 Chemical compound OP(=O)(O)OC[C@@H](O)[C@@H](O)[C@@H](O)CN1C=2C=C(C)C(C)=CC=2NC2=C1NC(=O)NC2=O YTNIXZGTHTVJBW-SCRDCRAPSA-N 0.000 description 1
- 241000193385 Geobacillus stearothermophilus Species 0.000 description 1
- 210000001822 Immobilized Cells Anatomy 0.000 description 1
- OZWKMVRBQXNZKK-UHFFFAOYSA-N Ketorolac Chemical compound OC(=O)C1CCN2C1=CC=C2C(=O)C1=CC=CC=C1 OZWKMVRBQXNZKK-UHFFFAOYSA-N 0.000 description 1
- 244000285963 Kluyveromyces fragilis Species 0.000 description 1
- 235000014663 Kluyveromyces fragilis Nutrition 0.000 description 1
- GUBGYTABKSRVRQ-UUNJERMWSA-N Lactose Natural products O([C@@H]1[C@H](O)[C@H](O)[C@H](O)O[C@@H]1CO)[C@H]1[C@@H](O)[C@@H](O)[C@H](O)[C@H](CO)O1 GUBGYTABKSRVRQ-UUNJERMWSA-N 0.000 description 1
- 208000010125 Myocardial Infarction Diseases 0.000 description 1
- 229940052665 NADH Drugs 0.000 description 1
- BAWFJGJZGIEFAR-NNYOXOHSSA-N Nicotinamide adenine dinucleotide Chemical compound NC(=O)C1=CC=C[N+]([C@H]2[C@@H]([C@H](O)[C@@H](COP([O-])(=O)OP(O)(=O)OC[C@@H]3[C@H]([C@@H](O)[C@@H](O3)N3C4=NC=NC(N)=C4N=C3)O)O2)O)=C1 BAWFJGJZGIEFAR-NNYOXOHSSA-N 0.000 description 1
- XJLXINKUBYWONI-NNYOXOHSSA-N Nicotinamide adenine dinucleotide phosphate Chemical compound NC(=O)C1=CC=C[N+]([C@H]2[C@@H]([C@H](O)[C@@H](COP([O-])(=O)OP(O)(=O)OC[C@@H]3[C@H]([C@@H](OP(O)(O)=O)[C@@H](O3)N3C4=NC=NC(N)=C4N=C3)O)O2)O)=C1 XJLXINKUBYWONI-NNYOXOHSSA-N 0.000 description 1
- 101710012892 PIGK Proteins 0.000 description 1
- 241000228143 Penicillium Species 0.000 description 1
- 239000001888 Peptone Substances 0.000 description 1
- 108010080698 Peptones Proteins 0.000 description 1
- 206010036596 Premature ejaculation Diseases 0.000 description 1
- 108010009736 Protein Hydrolysates Proteins 0.000 description 1
- 241000235350 Schizosaccharomyces octosporus Species 0.000 description 1
- 240000006394 Sorghum bicolor Species 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- CZMRCDWAGMRECN-GDQSFJPYSA-N Sucrose Natural products O([C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@H](CO)O1)[C@@]1(CO)[C@H](O)[C@@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-GDQSFJPYSA-N 0.000 description 1
- 240000008529 Triticum aestivum Species 0.000 description 1
- 241000863486 Vinca minor Species 0.000 description 1
- 241000235029 Zygosaccharomyces bailii Species 0.000 description 1
- 241000222292 [Candida] magnoliae Species 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K [O-]P([O-])([O-])=O Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 150000003863 ammonium salts Chemical class 0.000 description 1
- 239000000935 antidepressant agent Substances 0.000 description 1
- 230000036506 anxiety Effects 0.000 description 1
- 239000002830 appetite depressant Substances 0.000 description 1
- 239000008346 aqueous phase Substances 0.000 description 1
- RPZUBXWEQBPUJR-UHFFFAOYSA-N bicyclo[4.2.0]octane Chemical class C1CCCC2CCC21 RPZUBXWEQBPUJR-UHFFFAOYSA-N 0.000 description 1
- 230000036983 biotransformation Effects 0.000 description 1
- 239000007853 buffer solution Substances 0.000 description 1
- 201000011510 cancer Diseases 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 229910052803 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- 238000004440 column chromatography Methods 0.000 description 1
- 235000012343 cottonseed oil Nutrition 0.000 description 1
- 238000010192 crystallographic characterization Methods 0.000 description 1
- 150000003997 cyclic ketones Chemical class 0.000 description 1
- 230000003247 decreasing Effects 0.000 description 1
- 235000019425 dextrin Nutrition 0.000 description 1
- QSJXEFYPDANLFS-UHFFFAOYSA-N diacetyl Chemical group CC(=O)C(C)=O QSJXEFYPDANLFS-UHFFFAOYSA-N 0.000 description 1
- 229910000396 dipotassium phosphate Inorganic materials 0.000 description 1
- 235000019797 dipotassium phosphate Nutrition 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 239000002552 dosage form Substances 0.000 description 1
- 238000001640 fractional crystallisation Methods 0.000 description 1
- 239000008079 hexane Substances 0.000 description 1
- 150000002440 hydroxy compounds Chemical class 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- KFZMGEQAYNKOFK-UHFFFAOYSA-N iso-propanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 1
- 108010084715 isopropanol dehydrogenase (NADP) Proteins 0.000 description 1
- 235000015110 jellies Nutrition 0.000 description 1
- 239000008274 jelly Substances 0.000 description 1
- 239000008101 lactose Substances 0.000 description 1
- GUBGYTABKSRVRQ-XLOQQCSPSA-N lactose Chemical compound O[C@@H]1[C@@H](O)[C@@H](O)[C@@H](CO)O[C@H]1O[C@@H]1[C@@H](CO)O[C@H](O)[C@H](O)[C@H]1O GUBGYTABKSRVRQ-XLOQQCSPSA-N 0.000 description 1
- 235000015073 liquid stocks Nutrition 0.000 description 1
- 238000003819 low-pressure liquid chromatography Methods 0.000 description 1
- 238000002803 maceration Methods 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 229910052943 magnesium sulfate Inorganic materials 0.000 description 1
- CSNNHWWHGAXBCP-UHFFFAOYSA-L magnesium sulphate Substances [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 description 1
- 235000019341 magnesium sulphate Nutrition 0.000 description 1
- 235000020429 malt syrup Nutrition 0.000 description 1
- 235000012054 meals Nutrition 0.000 description 1
- 230000002906 microbiologic Effects 0.000 description 1
- 235000019713 millet Nutrition 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 235000013379 molasses Nutrition 0.000 description 1
- 230000035772 mutation Effects 0.000 description 1
- 150000002825 nitriles Chemical class 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 230000003287 optical Effects 0.000 description 1
- 239000012074 organic phase Substances 0.000 description 1
- 235000019319 peptone Nutrition 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 238000002953 preparative HPLC Methods 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000003638 reducing agent Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 238000004007 reversed phase HPLC Methods 0.000 description 1
- 150000003333 secondary alcohols Chemical class 0.000 description 1
- KEAYESYHFKHZAL-UHFFFAOYSA-N sodium Chemical compound [Na] KEAYESYHFKHZAL-UHFFFAOYSA-N 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 235000012424 soybean oil Nutrition 0.000 description 1
- 239000003549 soybean oil Substances 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008174 sterile solution Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 125000001424 substituent group Chemical group 0.000 description 1
- 239000005720 sucrose Substances 0.000 description 1
- 235000000346 sugar Nutrition 0.000 description 1
- 238000004809 thin layer chromatography Methods 0.000 description 1
- 230000001131 transforming Effects 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 235000021307 wheat Nutrition 0.000 description 1
Abstract
The present invention relates to processes for carrying out the following steroselective microbial reduction of a racemic tetralone, comprising: contacting a compound of formula (1) with a microorganism, or an enzyme reduction system capable of carrying out the present reduction, comprising an enzyme derived from said microorganism and a cofactor for said enzyme, and incubating the resulting mixture under conditions sufficient to produce the (4R) tetralol of formula (II) and leaving substantially unreacted the (4S) tetralone of formula (V) or "chiral tetralone." The chiral tetralone can be used in the synthesis of sertraline. The present process optionally further comprises separating the (4S) tetralone of formula (V) from (4R) tetralol of formula (II). The (4R) tetralol can be recycled to produce the compound of formula (I) and the present process is repeated to produce more desired (4S) tetralone of formula (
Description
STEREOSELECTIVE MICROBIAL REDUCTION OF A RACEMICA TETRALONE
FIELD OF THE INVENTION
The present invention relates to novel processes for preparing the (4S) enantiomer of 4- (3,4-dichlorophenyl) -3,4-dihydro-1 (2H) -naphthalenone (hereinafter referred to as "tetralone chiral" or "tetralone") (4S) ") and, more especially, refers to the stereoselective microbial reduction of racemic 4- (3,4-dichlorophenyl) -3,4-dihydro-1 (2H) -naphthalenone (hereinafter also referred to as" racemic tetralone ") ") to the chiral tetralone.
BACKGROUND OF THE INVENTION
The chiral tetralone prepared by the methods of the present invention can be further reacted to prepare cis- (1S) (4S) -N-methyl-4- (3,4-dichlorophenyl) -1, 2,3,4-tetrahydro -1-naphthalenamine pure, usually called sertraline. Sertraline is well known for its usefulness, for example, as an antidepressant and anorectic agent and in the treatment of chemical dependencies, disorders related to anxiety, premature ejaculation, cancer and after a myocardial infarction. For the preparation of sertraline, methods are known in the art, such as, for example, those described in U.S. Patent Nos. 4,536,518, 4,777,288, 4,839,104, 4,855,500, 4,940,731,
4. 962,128, 5,082,970, 5,130,338, 5,196,607, 5,248,699, 5,442,116,
. 463.126, 5.466.880, 5.597.826 and 5.750.794 and, in the W: M: Welch article,
Jr. et al., Which was published in the Journal of Medicinal Chemistry, vol. 27, No. 11, p. 1508 (1984). Some of the aforementioned patents refer to the synthesis of cis and trans isomer mixtures of racemic N-methyl-4- (3,4-dichlorophenyl) -1, 2,3,4-tetrahydro-1 -naphthalenamine. As described therein, the cis and trans isomers, as well as the (S) and (R) enantiomers, can be separated by methods known to those skilled in the art including, for example, fractional crystallization and chromatography. It is also known to select the chirality previously desired in the synthesis of sertraline. For example, the aforementioned U.S. Patent No. 5,750,794 describes a process for preparing chiral tetralone by reacting the racemic tetralone with a reducing agent based on an asymmetric ketone to provide the corresponding cis and trans alcohols, depending on the the chirality of the asymmetric reactant employed and, subsequently, separate the alcohols and oxidize the alcohols (1S, 4S) and / or (1 r, 4S) to the (4S) -tetralone. It is also known in the art that chiral compounds can be synthesized using microorganisms, such as fungi, for example, yeasts. For example, the use of yeasts to reduce ketones to chiral alcohols is well known. However, as is known to those skilled in the art, the chemical and optical yields, for example of the particular enantiomers and their amounts, of such microbial reductions, generally vary substantially depending on, for example, the particular microorganism. chosen, as well as the substituents of the starting material. U.S. Patent No. 5,049,497 describes a process for resolving a racemic derivative of bicyclo [4.2.0] octane by contacting the derivative with baker's yeast under conditions sufficient to give a mixture of a ketone and an alcohol of high enatomeric purity. As described in said document, only one enantiomer of the subject racemic ketone is reduced to an alcohol. U.S. Patent 5,576,764 discloses an asymmetric reduction process using an intact microorganism, or a preparation of used cells thereof, to convert a cyclic ketone into the corresponding chiral alcohol. U.S. Patent No. 5,618,707 describes a process for the stereoselective reduction of ketonic substrates by adding the substrates to a culture medium of Zygosaccharomyces bailii ATCC (American Type Culture Collection) No. 38924 or Schizosaccharomyces octosporus ATCC No. 2479, incubating the resulting mixture and isolating the hydroxy compound by conventional means such as, for example, extraction with organic solvents, adsorption on resins, or chromatography for later use as an intermediate in the preparation of an agent that lowers serum cholesterol. The isolated hydroxylated compound described in said document was analyzed by chiral high performance liquid chromatography (HPLC), reverse phase HPLC or both. Consistent with what would be appreciated by one skilled in the corresponding art, as described therein, many of the large number of microorganisms that were investigated for their ability to reduce the ketone group of the selected substrate failed to reduce the ketone group with specificity or desired productivity. It has now been unexpectedly discovered that a series of microorganisms, including fungi, for example yeasts and actinomycetes, substantially substantially reduces a racemic tetralone. More especially, the present stereoselective microbial reduction object selectively reduces the (4R) tetralone of the racemic mixture leaving the (4S) tetralone substantially unreacted. On the other hand, the unwanted tetralol (4R) produced by the present process can be oxidized and converted to the racemic tetralone and the present process repeated to provide even more (4S) tetralone. The (4S) tetralone produced by the present process can be used in the synthesis of sertraline. All documents cited in the present, including the foregoing, are incorporated herein by reference in their entirety.
SUMMARY OF THE INVENTION
The present invention relates to the microbiological reduction of carbonyl groups comprising, contacting a ketone compound, tetralone recémica of formula (I), with a microorganism, or an enzyme reduction system, capable of carrying out the present reduction , comprising an enzyme derived from said microorganism and a cofactor for said enzyme, and incubating the resulting mixture under suitable conditions so that a compound having a hydroxy group, specifically, (4R) tetralol can be formed and accumulated in the medium. of formula (II) and, a compound having the desired stereochemistry, the (4S) tetralone of formula (V) below, remains substantially unreacted. The tetralone (4S) of formula (V) below, that is, the chiral tetralone, can then be isolated by any suitable method, for example, chromatography or crystallization. In addition, the (4R) tetralol of formula (II) can be separated from the compounds of formulas (III) to (V), oxidized and form the racemic tetralone and the present stereoselective microbial reduction repeated to produce even more desired chiral ketone. Accordingly, the present invention provides procedures for carrying out the following stereospecific microbial reduction:
comprising: contacting a compound of formula (I) with a microorganism, an enzymatic reduction system capable of carrying out the present reduction, comprising an enzyme derived from said microorganism and a cofactor for said enzyme, and incubating the mixture resulting under conditions sufficient to produce more compound of formula (II) than compound of formula (III), thus leaving more compound of formula (V) unreacted than unreacted compound of formula (IV). The present stereospecific reduction can also be represented by: (0 (II) (V)
comprising: contacting a compound of formula (I) with a microorganism, or an enzyme reduction system capable of carrying out the present reduction, comprising an enzyme derived from said microorganism and a cofactor for said enzyme, and incubating the resulting mixture under conditions sufficient to produce the (4R) tetralol of formula
(II) and leave substantially unreacted the (4S) tetralone of formula (IV). The stereoselective reduction further comprises, optionally, the separation of the (4S) tetralone of formula (V) from the (4R) tetralol of formula (II). The (4R) tetralol can then be oxidized to produce the (4R) tetralone, which is then reacted, for example, with a base, to produce the racemic tetralone of formula (I) and the present stereoselective microbial reduction can be repeated for producing even more (4S) tetralone of formula (V), ie, the (4S) enantiomer of the racemic tetralone of formula (I). The present invention provides methods comprising the stereoselective microbial reduction of a compound of formula (I) to a compound of formula (II): by contacting a compound of formula (I) with a microorganism, or an enzyme reduction system capable of carrying out the present reduction, comprising an enzyme derived from said microorganism and a cofactor for said enzyme, and incubating the resulting mixture under conditions sufficient to produce a compound of formula (II), whereby substantially no further compound of formula (V) which is composed of formula (IV) and substantially more compound of formula (II) than compound of formula (III) is produced. In a preferred embodiment, the contacting of the compound of formula (I) is carried out with an enzymatic reduction system. In another preferred embodiment, the contacting of the compound of formula (I) is carried out with an enzymatic reduction system in which the enzyme is immobilized. In a particularly preferred embodiment, the contacting of the compound of formula (I) is carried out with an enzyme reduction system derived from Hansenula polymorpha ATCC No. 26012. In another preferred embodiment, the microorganism is a preparation of used cells thereof. In yet another preferred embodiment, the microorganism is an enzyme powder preparation in acetone thereof. In an especially preferred embodiment of the present invention intact microorganism is used. In a preferred embodiment in which the microorganism is an intact microorganism, the compound of formula (I) is contacted with a fermentation medium, culture broth or solvent, comprising the microorganism. In another preferred embodiment in which the microorganism is an intact microorganism, the compound of formula (I) is contacted with an intact washed microorganism. In another preferred embodiment in which the microorganism is intact, the compound of formula (I) is contacted with an immobilized intact microorganism.
In an especially preferred embodiment of the present invention, the microorganism is an intact microorganism that develops in a fermentation medium and the contact is produced by the addition of the compound of formula (I) thereto. In another especially preferred embodiment of the present invention, the microorganism is an intact microorganism that grows in a growth medium for about forty-eight hours, and contact occurs in said growth medium by the addition of the compound of formula (I). ) to the same one and the incubation lasts approximately five days. In another preferred embodiment of the present invention, the microorganism in a fungus, for example, a yeast, an actinomycete, or one of its mutants that can carry out the stereoselective reduction. In another preferred embodiment of the present invention, the microorganism is a fungus. In another still more preferred embodiment in which the microorganism is a fungus, the fungus is Absidia coerulea ATCC No. 20137. In a particularly preferred embodiment of the present invention, the microorganism is a yeast. In an especially preferred embodiment of the present invention wherein the microorganism is a yeast, the yeast is Hansenula polymorpha ATCC No. 26012, also deposited as ATCC No. 74449.
When Hansenula polymorpha ATCC No. 26012, also deposited as ATCC No. 74449, is used as microorganism, the present stereoselective microbial reduction appreciably reduces only one enantiomer of the compound of formula (I), giving the corresponding alcohol, ie, the compound of formula (II), while the other enantiomer of the compound of formula (I), ie, the compound of formula
(V) remains substantially unreacted. As described above, the methods of the present invention optionally further include separation, for example carried out using crystallization or chromatography, from the compound of formula (V) of the compounds of formula (II) to (IV) and the use of said separate compound of formula (V) in the synthesis of sertraline using any of the methods known for this. As also described above, it is preferred to oxidize the isolated (4R) tetralol of formula (II) to the (4R) tetralone of formula (IV). Next, it is further preferred to form the racemic, preferably by reacting the (4R) tetralone with a base, by transforming the (4R) tetralone of formula (IV) into the racemic tetralone of formula (I). Oxidation and racemic formation recycles the unwanted (4R) tetralol to another cycle of stereoselective microbial reduction according to the methods of the present invention. Recycling the desired (4S) tetralone and decreasing the amount of unwanted (4R) tetralol discarded. Oxidation and racemic formation of the oxidized product can be carried out using any of the methods known for this.
DETAILED DESCRIPTION OF THE INVENTION
Those skilled in the art will fully understand the terms used herein to describe the present invention; however, the following terms are used herein as described below. "Cofactor" means any suitable cofactor comprising the enzyme reduction system such as, for example, NADH, NADPH, FADH, FMNH and / or PQQ or any of the cofactors that occur with the enzyme in the microorganism. "Enzymatic reduction system" means any suitable microbial oxido-reductase enzyme and the reduced form of a cofactor for the enzyme oxido-reductase, the cofactor of the selected microorganism being derivable or being derived from any suitable source. The enzyme comprising the enzyme reduction system can be in free form or immobilized, for example, in a column or linked to spheres. "Microbial reduction" means the stereoselective reduction of the present invention, as carried out by the enzyme reduction system, the enzyme reduction system comprising the intact microorganism or any of its preparations and the like.
"Microorganism" includes any intact microorganism or its preparations, including for example, a preparation of used cells of the microorganism; a dehydrated preparation of the microorganism, for example, an enzyme preparation powder in acetone; microorganism washing event of, for example, fermentation medium, culture medium and the like; immobilized microorganism, for example, in a column, attached to spheres and the like. The methods provided by the present invention comprise the stereoselective microbial reduction of a compound of formula (I) to a compound of formula (II):
contacting a compound of formula (I) with a microorganism, or an enzymatic reduction system capable of carrying out the present reduction, comprising an enzyme derived from said microorganism and a cofactor for said enzyme, and incubating the resulting mixture under sufficient conditions to produce a compound of formula (II), whereby, more compound of formula (V) than compound of formula (IV) remains unreacted and substantially more compound of formula (II) than compound of formula (III) is produced ). As will be understood by those skilled in the art, the compound of formula (I), the racemic tetralone, is a mixture of the (4S) tetralone and (4R) tetralone as shown below:
(trans) (1 S. 4R) (cis) (1 R, 4R).
The compounds, or more especially, the tetraloles of formula (II) are:
(trans) (1 S.4R) (cis) (1 R, 4R) The compounds, or more especially, the tetraloles of formula
(III) are:
The compounds of formula (II) and (III) are described and claimed in the aforementioned U.S. Patent No. 5,750,794. The desired compound of formula (V) can be isolated as described below from the undesired compounds of formula (II) and any of the compounds of formula (II) or (IV) which may have been produced or will be left without react, respectively, depending on, for example, the microorganism selected and the incubation conditions. The compounds of formula (II) can be converted into a compound of formula (I), for example, by oxidizing or forming the racemic, and the present stereoselective microbial reduction carried out to produce additional amounts of the (4S) tetralone of formula ( V). The process of the present invention is carried out easily. Thus, the microorganism is fermented (intanus microorganism) or incubated (preparation of used cells, dehydrated preparation or any other suitable preparation of the microorganism) in the presence of the racemic tetralone, represented by the formula (I), to modify the racemic tetralone and , more especially, to reduce the undesired enantiomer (4R) of the racemic ketone to its corresponding alcohol, represented by the formula (II), leaving the desired (4S) enantiomer, represented by the formula (V), substantially unreacted, of this mode in one step, giving rise to the optically enriched enantiomer (4S). The (4S) enantiomer can be further reacted by methods well known to those skilled in the corresponding art as described, for example, in U.S. Patent Nos. 4,536,518, 4,777,288, 4,839,104, 4,855. 500, 4,940,731, 4,962,128, 5,082,970, 5,130,338, 5,196,607, 5,248,699, 5,442,116, 5,463,126, 5,466,880, 5,597,826, and 5,750,794 and, in the cited WM article Welch, Jr. and others, to finally produce sertraline. The activity, methods for assaying activities, dosages, dosage forms, administration procedures and prior information relating to sertraline are described, for example, in U.S. Patent Nos. 4,536,517, 4,777,288 and 4,839,104 previously. cited and in the WM article Welch, Jr. and others, previously cited. Any suitable microorganism can be used in the process of the present invention. As described before, the microorganism used in the present method may be intact, or in the form of any of its preparations, for example, a preparation of used cells thereof, a dehydrated preparation thereof and be free or immobilized. However, when a non-intact microorganism is employed in the present invention as, for example, a preparation of used cells, for example a cell extract, enzyme preparation powder in acetone or in enzyme derived therefrom, those skilled in the art They will understand that a cofactor for the enzyme will also be included. Those skilled in the art will understand from the description set forth herein and their related knowledge how to prepare a cell preparation used as described, for example, by R.N. Patel et al. In the article "Oxidation of Secondary Alcohols to Methyl Ketones by Yeast" published in Apllied and Enviromental Microbiology, 38 (2): 219-223 (197). Those skilled in the art will understand from the description set forth herein and their related knowledge how to prepare an enzyme preparation powder in acetone as described, for example, by K. Nakamura et al. In the article "Asymmetric Reduction of Ketones by the Acetone Powder of Geotrichum candidum "published in 'Tetrahedron Letters, 37 (10): 1629-1632 (1996). In addition, an enzyme (for example an oxide reductase) of any suitable microorganism can also be used in the present methods, and this enzyme can be isolated from the microorganism by any suitable method known to those skilled in the art and, as in the case of the intact microorganism can be used in the present process in free or immobilized form. Those skilled in the art will understand from the description set forth herein and their related knowledge as to isolate and purify the enzyme from the suitable microorganism as generally described, for example, in the articles of: M. Wada et al. " Purification and Characterization of NADPH-Dependent Carbonyl
Reduced, Involved in Stereoselective Reduction of Etyl 4-Chloro-3-oxobutanoate, from Candida magnoliae "published in Biosci, Biotechnol.
Biochem, 62 (2): 280-285 (1998), P. Trots et al., "Purification and Properties of NAP (P) H: (quinone-acceptor) oxidoreductase of sugarbeet cells" published in Eur. J. Biochem, 234 : 452-458 (1995), KM Madyastha and TL Gururaja, "Purification and Some of the Properties of a Novel Secondary Alcohol Dehydrogenase from Alcaligenes eutrophus", published in Biochemical and Biophysical Research Communications, 211 (2): 540-546 (1995 ), O. Bortolini et al., "Kinetic resolution of victools by Bacillus stearothermophilus diacetyl reducíase" published in Tetrahedron: Asymmetry, 9: 647-651 (1998), RN Patel et al., "Stereospecific microbial reduction of 4,5-dihydro- 4- (4-methoxyphenyl) -6- (trifluoromethyl-1 H-1) -benzazepin-2-one "published in Enzyme Microb. Technol., 3: 906-912 (1991) and R.N. Patel et al., "Stereoselecive microbial / enzymatic oxidation of (exo, exo) -7-oxabicyclo [2.2.2] hepyane-2,3-dimethanol to the corresponding chiral lacíol and lacfone" published in Enzyme Microb. Technol., 14: 778-784 (1992); and by U.S. Patent Nos. 5,523,223 and the aforementioned 5,580,764. Suitable microorganisms include Hansenula polymorpha ATCC No. 26012, Hansenula polymorpha ATCC No. 74449, Absidia coerulea ATCC No. 20137, Geotrichum candidum ATCC No. 34614, Geotrichum candidum ATCC No. 62401, Mortierella isabelina ATCC No. 42613, Mortierella isabellina ATCC No. 38063, Mortierella vinacea ATCC No. 09515, Pencillium notatum ATCC No. 36740, Blastoschizomyces capitatus ATCC No. 28575, Monosporium olivacerum v. ATCC No. 36300, Aureobasidium pullulans ATCC No. 16623, Debaryomyces polymorphus ATCC No. 20280, Saccharomyces cerevisiae ATCC No. 15248, Candida schatavii ATCC No. 24409, Pichia fabianii ATCC 16755 and Streptomyces rimmosus ss. RIMOSUS ATCC No. 10970; and their mutants which are known or can be obtained in any other way by those skilled in the corresponding art and can, in spite of said mutation, carry out the stereoselective microbial reduction described herein. Preferred intact microorganisms will be those that substantially reduce the (4R) tetralone by leaving the (4S) tetralone leaving the (4S) tetralone substantially unreacted, including the reduction reaction or any other intrinsic activity that may degrade or cause a negative impact on the (4R) tetralone. 4S) tetralone desired at any stage of the present process. As will be appreciated by those skilled in the art of the present disclosure, said undesired reaction of (4S) tetralone can be substantially prevented, for example, by using the enzyme derived from the microorganism selected against the intact microorganism. Suitable microorganisms for use in the present stereospecific microbial reduction can be prepared by any method known to those skilled in the corresponding art. The following is an example of a method suitable for the preparation of a microorganism from a commercially purchased stock solution. The method set out below can be used for any microorganism suitable for use in the present process and those skilled in the art will understand the description set forth herein to modify any part of the process, for example, a method for preparing the microorganism, intact or preparation, for example of used or dehydrated, free or immobilized cells; a process for preparing a suitable enzyme derived from said microorganisms; a method for contacting the racemic tetralone with the microorganism or the enzyme comprising the enzyme reduction system derived therefrom; the components of the growth medium and the conditions, for example, temperature, pH and the like; or the incubation conditions; to achieve the desired result in any particular procedure. Those skilled in the art will understand from the description set forth herein and their related knowledge how to prepare immobilized intact microorganisms as described, for example, by A. Bauer et al., in the article "Polyvinyl alcohol-immobilized whole-cell preparations for biotransformation of nitriles" published in Biotechnology Letters, 18 (3): 343-348 (March 1996). Any suitable method for contacting the compound of formula (I) with the microorganism or enzyme reduction system can be used in the present invention. The compound of formula
(I) can be contacted with the microorganism or enzyme reduction system in any suitable order. For example, the compound of formula (I) may be added to a medium, such as a culture medium, comprising the microorganism, free or immobilized, or any combination thereof; or the medium can comprise the compound of formula (I) and the microorganism can then be added to said medium; or the compound of formula (I) and the microorganism can be added together to said medium; or the compound of formula (I) can be added to a preparation of used cells thereof; or the compound of formula (I) can be added to a dehydrated preparation of the microorganism; or the compound of formula (I) or the microorganism or the enzyme reduction system can be added to a suitable solvent comprising the other; and similar. Those skilled in the art will understand from the description set forth herein to modify any of the parts of the present process according to their wish. It is especially preferred in the present invention that the microorganism, or the enzyme reduction system, is derived from Hansenula polymorpha ATCC No. 26012. A lyophilized sample of Hansenula polymorpha ATCC No. 26012 (originally provided by DW Levine) was deposited with the ATCC, located at 10801 University Boulevard, Manassas,
Virginia, 20110-2209, United States of America, under the conditions of
Budapest Treaty on June 26, 1998. This newly deposited crop was assigned the ATCC deposit number 74449. Therefore, it is also especially preferred in the present invention that the microorganism be
Hansenula polymorpha ATCC No. 74449. All limitations on the availability to the public of the culture of microorganisms thus deposited will be irrevocably removed after the granting of a patent from the specification of the present invention. The cultures of Hansenula polymorpha ATCC No. 26012 can be obtained from the ATCC and an example of a suitable process for its preparation from said commercially purchased stock solution is given below. A culture thus obtained is added to a suitable growth medium and incubated with agitation until growth occurs, both being as considered by those skilled in the art. The culture thus prepared can be used to inoculate tilted cultures, with portions of these frozen tilted cultures as stock solutions. Alternatively, cultures of the liquid stock can be prepared by adding about 10% to about 20% glycerol, then frozen at about -80 ° C, preferably in small cryogenic tubes.
As will be appreciated by those skilled in the art for any selected microorganism and as specifically set forth hereinbelow in the examples for Absidia coerulea ATCC No.
20137 and the especially preferred Hansenula polymorpha ATCC No. 26012 or ATCC No. 74449, a suitable method for preparing the microorganism is as follows: the microorganism is inoculated from a culture of the frozen stock solution as described above (approximately a 17% stock solution in glycerol) in flasks or in a glass tube with a metal closure containing a growth medium (containing an aliquot of a sterile solution including Tween® 80, glycerol and distilled water) whose composition is described in more detail later. The fermentation is carried out at temperatures ranging from about 22 ° C to about 32 ° C and, preferably at about 29 ° C, with suitable agitation, preferably from about 200 rpm to about 220 rpm, and, most preferably, at approximately 210 rpm. When desired, the pH of the growth medium can be maintained using suitable buffers incorporated in the fermentation medium and / or adjusted periodically by the addition of base or acid., as needed. In the present invention any suitable growth time of the microorganism can be used, by contacting the microorganism with the compound of formula (I) and incubating the compound of formula (I) with the microorganism. Proper growth of the microorganism can be achieved, for example, in about 24 hours, at which time a suitable aliquot of a racemic tetralone solution in a suitable solvent, preferably ethanol, can be added to the culture. The fermentation may then continue for, for example, from two to about six days and, preferably, for about five days, at which time the fermentation medium can be extracted using any suitable extraction procedure in which a suitable solvent, For example, ethyl acetate, methyl butyl ketone, metii etii ketone, methylene chloride and the like, preferably ethyl acetate, extract the organic components from the fermentation medium. After extraction of the fermentation medium and separation of the organic and aqueous phases, the compounds comprising the organic residue can be determined using any suitable method, such as, for example, chromatography, preferably chiral HPLC. Any suitable growth medium can be used in the process of the present invention and the suitable growth medium will contain a source or sources of assimilable carbon, assimilable nitrogen and inorganic salts containing the essential minerals. In general, many carbohydrates, such as glucose, maltose, sugar, sucrose, starch, glycerin, millet jelly, molasses, soybean seeds and the like, can be used as assimilable sources of carbon. Sources of assimilable nitrogen include, for example, materials such as yeast and casein hydrolysates, primary yeast, yeast extracts, cottonseed meal, soybean solids, wheat germ, meat extracts, peptone, maceration liquor of corn and ammonium salts. Nutrients of inorganic salts suitable for use in the culture medium of the present invention include, for example, the usual salts containing sodium, iron, magnesium, potassium, cobalt, phosphate and the like. More especially, growth media suitable for use in the present invention include, for example: (a) dextrose (approximately 20 g), yeast extract (approximately 5 g), soybean meal (approximately 5 g), NaCl (approximately 5 g), K2OP4 (approximately 5 g) and distilled water (approximately 1 liter (I)), pH adjusted to approximately pH 7.0 with aqueous H2SO4.; (b) dextrin (approximately 10 g), meat extract (approximately 3 g), ardamine pH (approximately 5 g), NZ type E amine (approximately 5 g), MgSO4 7H2O (approximately 0.5 g), KH2PO4 (approximately 0.37 g) ), CaCO3 (approximately 0.5 g) and distilled H2O (approximately 1 I), pH adjusted to approximately 7.1 with aqueous HCl, followed by a second glucose stage (approximately 10 g), Hy-Case SF® (approximately 2 g), meat extract (approximately 1 g), corn steep liquor (approximately 3 g) and distilled H2O (approximately 1 I), pH adjusted to approximately pH 7.0; (c) glucose (approximately 10 g), corn steep liquor (approximately 6 g), KH2PO4 (approximately 3 g), CaCO3 (approximately 3.5 g), soybean oil (crude, approximately 2.2 ml), yeast extract ( approximately 2.5 g) and distilled H2O
(about 1 I), adjusted pH from about pH 7.0 to about pH 7.3 with aqueous HCl; (d) malt syrup (approximately 20 g), soy flour
(approximately 5 g), casein (approximately 1 g), dried yeast
(approximately 1 g), NaCl (approximately 5 g) and distilled H2O
(approximately 1 I); (e) lactose (approximately 75 g), Pharmamedia® (substitute yeast extract, approximately 40 g), CaCO3 (approximately
g), Na 2 SO 4 (approximately 4 g) and distilled H 2 O (approximately 1; (f) ISP No. 2 (see for example page 460 of Handbook of Microbial Media by RM Atlas, published by LC Parks, CRC Press, Inc 1993 ("Handbook"); (g) ISP n ° 3 (see page 460 of Handbook); (h) ISP n ° 4 (see page 461 of Handbook); (i) ISP n ° 5 (see pages 461-462 of Handbook), and the like A particularly preferred culture medium is 2X from (a) discussed above With reference to buffers, media, reagents, contacting or culture conditions and the like, it is not intended be limiting, but will be construed to include all related materials that those of ordinary skill in the art may know as of interest or value in the particular context in which the present disclosure is presented.
For example, it is often possible to substitute a buffer system or culture medium for another, so that a different but known form is used to achieve the same purpose for which the suggested method, material or composition is directed. In addition, it will be understood that the present invention includes scaling up the present process for commercial purposes. Therefore, as will be understood by those skilled in the art, variations in the growth medium, fermentation conditions and / or the amount of racemic tetralone can be altered to control the performance of the resulting compounds and their relative production rates. . In general, the techniques employed in the present invention will be chosen with respect to industrial efficiency. The growth media, the fermentation conditions and the relative amounts of microorganisms or the enzyme reduction system and the racemic tetralone described herein are merely illustrative of the wide range of media, fermentation conditions and amounts of starting materials that they may be employed suitably in the present invention, as will be appreciated by those skilled in the art, and are not intended to be limiting in any way.
Any suitable process for isolating and / or purifying any of the products of the present process can be used in the present invention, including filtration, extraction, crystallization, column chromatography, thin layer chromatography, low pressure liquid chromatography or preparative HPLC or any suitable combination of such procedures. In addition, one skilled in the art will appreciate that the corresponding undesired alcohol of the (4R) tetralone, the compound of formula (II), produced by the methods described herein can be recycled, for example, oxidized and form the racemic as above. described herein, by any known method, forming the racemic tetralone of formula (I) and the methods of the present invention repeated to produce, again, the desired tetralone (4S) of formula (V). Oxidation of (4R) tetralol to (4R) ketone can be accomplished by methods known to those skilled in the art. The racemization reaction can be carried out in any suitable manner although it is generally carried out at a temperature from about 0 ° C to about 100 ° C, preferably from about 25 ° C to about 65 ° C. The (4R) tetralone is reacted with a base at a temperature of about 25 ° C to about 85 ° C, preferably about 50 ° C to about 65 ° C. Suitable bases for this racemization reaction include potassium t-butoxide, sodium hydroxide, sodium methoxide and potassium hydroxide. A preferred base is potassium t-butoxide. The detailed examples set forth below show that a series of microorganisms, including fungi, for example, yeasts and actinomycetes, stereoselectively reduce the racemic tetralone, providing the desired (4S) tetralone of formula (V), i.e., the chiral tetralone , which can then be separated from the undesired compounds and subsequently reacted according to procedures known in the art to provide sertraline. The present invention is illustrated by the following examples. The above and following description of the present invention and the different embodiments are not intended to limit the invention, but are merely illustrative thereof. Therefore, it will be understood that the invention is not limited to the specific details of these examples.
EXAMPLE 1 Reduction of a racemic tetralone using Hansenula polymorph ATCC No. 26012
A. Fermentation of yeast Hansenula polymorph ATCC No. 26012 A control culture (Cl) and a test culture (T1) were prepared as follows: about 2.5 ml of sterile growth medium (approximately 40 g / l of approximately 10 g / l of nutritious soy flour, approximately 10 g / l of yeast extract, approximately
g / l of NaCl and dextrose, approximately 10 g / l of K HPO 4, with the pH adjusted to approximately 7.0 with H2SO4) to each of two 16 x 125 mm glass tubes each having a metal plug (C1 , T1), followed by the addition of approximately 0.2 ml of a solution A
(approximately 25 g of Tween® 80, approximately 100 g of glycerol and approximately 250 ml of distilled water, sterilized by filtering), to each of the two cultures. T1 was inoculated in approximately 25 μl of a stock solution frozen in glycerol approximately 17% of Hansenula polymorpha ATCC no. 26012. The two tube cultures were incubated at approximately 29 ° C with shaking at approximately 210 rpm. After approximately 24 hours, approximately 50 μl of a stock solution (approximately 5 mg / ml in approximately 100% ethanol, final concentration approximately 100 μg / ml) of a racemic tetralone ( Formula (I) comprising the compounds of formulas (IV) and (V), at about 5 mg / ml in ethanol). After about five days, one ml of NaCl (saturated) was added to each of the two tube cultures. The fermentation medium from each tube culture (approximately 3.6 ml) was extracted with an equal volume of ethyl acetate (neat): ethyl acetate was added, the tube culture was vortexed and then centrifuged at approximately 2,000. rpm (IEC® centrifuge '300 Second Avenue, Needham Heights, Massachusetts 02194). The ethyl acetate layer was removed and the aqueous layer was extracted for a second period. The combined organic extracts were dried under nitrogen in a water bath at about 50 ° C.
B. Configuration of the residual ketone: Compounds of formulas (IV) and
Each extract, prepared as described above, was resuspended in approximately one ml of ethanol, and approximately 20 μl of each extract resuspended by injection was analyzed on an HPLC column: Chiralcel OK protection column (4.6 x 50 mm, Diacel Chemical Industries, LTD, 730 Springdale Drive, PO Box 564, Exton Pennsylvania 19341) coupled to a Chiralcel OK column (4.6 x 250 mm, Diacel). The compounds contained in each of the injected resuspended extracts were separated in a Socratic manner at approximately 0.8 ml per minute in a mobile phase (ethanol: ethyl acetate, 85:15) and the compounds included in the extracts were detected using a detector. 996 PDA (Waters®, 34 Maple Street, Milford, Massachusetts 01757) adjusted to 254 nm. As illustrated by the data of C1 and T1 in the following Table I, the chiral HPLC analysis showed that the inclusion of the microorganism, ie, Hansenula polymorpha ATCC No. 26012 gave a ratio of 16: 1 ((4S) tetralone of unreacted formula (V) against (4R), tetralone of formula (IV) without reacting), which further illustrates the stereospecific character of the present microbial reduction process. The results expressed below are based on the known amount of each added enantiomer (approximately 50 μg / ml of each of the compounds of formulas (IV) and (V)). As mentioned above, the starting racemic tetralone of formula (I) had a concentration of approximately 100 // lg / ml.
TABLE 1
The results of the chiral analysis show that the cultivation of Hansenula polymorpha ATCC No. 26012 (T1) substantially reduces the (4R) tetralone, the (4S) tetralone remaining almost unreacted (approximately 4.7% of (4R) tetralone remains against 76% of (4S) tetralone). It was determined that the (4S) tetralone was present in an ee of about 88% ("percentage amount of enantiomeric excess") by chiral HPLC. As also shown by the data in Table I, especially by the ratio (4S) :( 4R), that is, 16, remains substantially more (4S) unreacted tetralone than (4R) tetralone. Accordingly, the inclusion of the intact microorganism, ie Hansenula polymorpha ATCC No. 26012, produced a substantial stereospecific reduction of more starting (4R) tetralone of formula (IV) than starting (4S) tetralone of formula (V) ( (4S): (4R)) and provided mostly (4R) tetralol of formula (II) against (4S) tetralol of formula
(lll) (data not shown). The majority of the (4R) tetralol produced was (1S, 4R) tetralol and the majority of the minority amount of (4S) tetralol produced was (1S.4S) tetralol.
EXAMPLE II
REDUCTION OF A RACEMICA TETRALONE USING Absidia coerulea ATCC no. 20137
A. Fermentation of the fungus Absidia coerulea ATCC no. 20137
A control culture (C2) and a test culture were prepared
(T2) as follows: approximately 2.5 ml of sterile growth medium (approximately 20 g / l of dextrose, approximately 5 g / l of nutritious soybean meal, approximately 5 g / l of yeast extract, approximately 5 g / l) were added. l of NaCl and about 5 g / l of K2HPO4, with the pH adjusted to about 7.0 with H2SO4) to each of two 16 x 125 mm glass tubes each having a metal plug (C2, T2). Approximately 25 μl of a stock solution in frozen 17% giicerol of Absidia coerulea ATCC no. 20137. The two tube cultures were incubated at approximately 29 ° C with shaking at approximately 210 rpm. After about 48 hours, approximately 50 μl (approximately 5 mg / ml in ethanol, final concentration of approximately 100 // l / ml) of a racemic tetralone (as described in Example I, a) was added to C2 and T2. about 5 mg / ml in about 100% ethanol). After about five days, one ml of NaCl (saturated) was added to each of the two tube cultures. The fermentation medium of each tube culture (approximately 3.6 ml) was extracted with approximately 3 ml of ethyl acetate (neat): ethyl acetate was added, the tube culture was vortexed and then centrifuged at approximately 2,000. rpm (IEC centrifuge). The ethyl acetate layer was removed and the aqueous layer was extracted for a second period. The combined organic extracts were dried under nitrogen in a water bath at about 50 ° C.
B. Configuration of the residual ketone: Compounds of formula (IV) and (V).
Each extract, prepared as described above, was resuspended in approximately one ml of ethanol, and approximately 20 μl of each extract resuspended was analyzed by injection on an HPLC column: Chiralcel OK protection column (4.6 x 50 mm) coupled to a Chiracel OK column (4.6 x 250 mm). The compounds contained in each of the injected resuspended extracts were separated in a Socratic manner at approximately 0.8 ml per minute in a mobile phase (ethanol: ethyl acetate, 85:15) and the compounds included in the extracts were detected using a detector. 996 PDA (Waters®) adjusted to 254 nm. As illustrated by the HPLC data for Cl and TI, inclusion of the microorganism, ie, Absidia coerulea ATCC No. 20137 provided an estero-specific reduction of more (4R) tetralone starting formula
(IV) that of the starting tetralone (4S) of formula (V). More specifically, the results of the chiral analysis show that the culture of Absidia coerule ATCC No. 20137 reduces the (4R) tetralone while leaving substantially unreacted the (4S) tetralone (approximately 13.6% of (4R) tetralone remains against approximately 40.5% of the (4S) tetralone). It was determined that the (4S) tetralone was present in an ee of approximately 50% by this chiral HPLC. As illustrated by the data for C2 and T2 in Table II below, the chiral HPLC analysis showed that the inclusion of the microorganism, ie, Absidia coerulea ATCC No. 20137 (T2) produced a ratio of at least two times as much of (4S) tetralone that remained unreduced against the unreduced (4R) tetralone, further demonstrating the stereospecificity of the present microbial reduction process. The results expressed below are based on the known amount of each added enantiomer (approximately 50 μg / ml of each, as described in example 1 above). As mentioned above, the starting racemic tetralone had a concentration of about 10 μg / ml.
TABLE ll
EXAMPLE III Reduction of a racemic tetralone using fungi, yeasts and an actinomycete
As will be understood by those skilled in the corresponding art, the microorganisms listed in Table Ill, which were used in the present reduction, Geotrichum candidum ATCC No. 62401, Mortierella isabellin ATCC No. 38063, Mortierella vinacea ATCC No. 09515, Penicillium nonatum ATCC No. 36740, Blastoschizomyces capitatus ATCC No. 28757, Monosporium olivaceum v. major ATCC No. 36300, Aureobasidium pullulans ATCC No. 16623, Pichia fabianii ATCC No. 16755, and Streptomyces rimosis ss. rimosmos ATCC No. 10970 were separated as described in example II; Geotrichum candidum ATCC No. 34614, Mortierella isabellin ATCC No. 42613, Debaryomyces polymorphus ATCC No. 20280 and Saccharomyces cerevisiae ATCC No. 15248 were prepared as described in Example II, except that extraction was repeated; and Candida schatavii ATCC No. 24409 was prepared as indicated below. Candida schatavii ATCC No. 24409 was prepared and used according to the present invention as follows: about 2.5 ml of sterile growth medium (approximately 20 g / l of dextrose, approximately 5 g / l of nutritious soy flour, approximately 5 g / l of yeast extract, approximately 5 g / l of NaCl and approximately 5 g / l of K2PO4, with the pH adjusted to approximately 7.0 with H2SO4) to a glass tube of 16 x 125 mm with a metal stopper, followed by the addition of approximately 0.1 ml of a sterilized solution by filtration of approximately 25 g of Tween® 80, approximately 100 g of glycerol and approximately 250 ml of distilled water to the culture. Next, approximately 25 μl of a stock solution in glycerol to about 17% frozen of Candida schatavii ATCC No. 24409 was inoculated into the culture. The culture was developed at about 29 ° C, with stirring at about 210 rpm. After 48 hours, approximately 50 μl of a stock solution (approximately 5 mg / ml in approximately 100% ethanoi, final concentration of approximately 100 μl / ml of a racemic tetralone (compound of formula (I) comprising the compounds of formulas (IV) and (V), at about 5 mg / ml in about 100% ethanol).
After four more days, the culture fermentation medium (approximately 2.6 ml) was extracted with an equal volume of ethyl acetate (neat), the culture was vortexed and then centrifuged at approximately 2000 rpm (IEC® centrifuge) . The extraction was repeated. The extracts were dried under nitrogen in a water bath at about
50 ° C. The extract was resuspended in approximately one ml of ethanol, and approximately 5 μl of the resuspended extract was analyzed by injection on an HPLC column: Chiralcel OD protection column (4.6 x 50 mm, Diacel Chemical Industries LTD.) Coupled to a Chiralcel column OD (4.6 x 250 mm, Diacel). The compounds contained in the injected resuspended extract were separated in a Socratic manner at approximately 0.9 ml per minute in a mobile phase (hexane: isopropanol, 95: 5) and the compounds in the extract were detected using a 996 PDA detector (Waters®) set to 210 nm. As shown by the chiral HPLC (carried out as in Example I and II), the data set forth in Table III, each of the microorganisms listed in the following Table ll stereospecifically reduced more (4R) tetralone than ( 4S) tetralone and there was generally a ratio of at least about twice as much (4S) tetralone that remained unreacted with respect to the unreacted (4R) tetralone.
PICTURE
It will be appreciated that, while Monosporium olivaceum v. ATTC No. 36300, as illustrated by the data in Table III, reduces substantially more (4R) tetralone than (4S) tetralone and, as such would be a preferred microorganism for use in the present process, however, it is also disclosed for this culture undesirable degradation of (4R) tetralone and (4S) tetralone. The undesirable degradation may be due, for example, to other enzymes and the like comprising the intact microorganism. Therefore, as will be understood by those skilled in the art from the description set forth herein, the use of the enzyme isolated from Monosporium olivaceum v. Is preferred. ATCC major n °
36300 against Monosporium olivaceum v. ATCC major No. 36300 intact.
Claims (35)
1. - A process for the steroselective microbial reduction of a compound of formula (I) to compounds of formulas (II) and comprising: contacting a compound of formula (I) with a microorganism, or an enzyme reduction system capable of carrying out said reduction, comprising an enzyme derived from said microorganism and a cofactor for said enzyme, and incubating the mixture resulting under conditions sufficient to produce more compound of formula (II) than compound of formula (III), thus leaving more compound of formula (V) unreacted than unreacted compound of formula (IV), said microorganism being selected from the group consisting of: Hansenula polymorpha ATCC No. 26012, Hansenula polymorpha ATCC No. 74449, Absidia coerulea ATCC No. 20137, Geotrichum candidum ATCC No. 34614, Geotrichum candidum ATCC No. 62401, Mortierella isabellina ATCC No. 42613, Mortierella isabellina ATCC No. 38063, Mortierella vinacea ATCC No. 09515, Penicillium notatum ATCC No. 36740, Blastoschizomyces capitatus ATCC No. 28575,
Monosporium olivaceum v. ATCC No. 36300, Aureobasidium pullulans ATCC No. 16623, Debaryomyces polymorphus ATCC No. 20280,
Saccharomyces cerevisiae ATCC No. 15248, Candida schatavii ATCC nc 24409, Pichia fabianii ATCC 16755 and Streptomyces rimosus ss. RIMOSUS ATCC No. 10970; and its mutants capable of carrying out said reduction. 2. The process according to claim 1, wherein the compound of formula (V) is separated from the compounds of formulas (II), (III) and (IV). 3. Process according to claim 2, wherein said separation is carried out by chromatography.
4. Process according to claim 2, wherein said separation is carried out by crystallization.
5. Process according to claim 2, wherein said compound of formula (II) is separated from said compounds of formulas (III) and (IV).
6. The process according to claim 5, wherein said separate compound of formula (II) is recycled to a compound of formula (I) by oxidizing said separate compound of formula (II) and subjecting said oxidized compound to racemization said compound of formula (I).
7. The process according to claim 6, wherein said racemization comprises reacting said oxidized compound with a base.
8. The method according to claim 1, wherein said compound of formula (I) is prepared as defined in claim 6.
9. The method according to claim 1, wherein said contacting occurs with a microorganism. .
10. The method according to claim 1, wherein said contacting takes place with said enzyme reduction system.
11. The method according to claim 9, wherein said microorganism is an intact microorganism.
12. Method according to claim 9, wherein said microorganism is a preparation of used cells thereof.
13. Process according to claim 9, wherein said microorganism is a dehydrated preparation thereof.
14. The method according to claim 11, wherein said intact microorganism comprises washed cells of said intact microorganism.
15. The method according to claim 14, wherein said washed cells are immobilized.
16. The method according to claim 10, wherein said enzyme of said enzyme reduction system is immobilized.
17. - Process according to claim 13, wherein said dehydrated preparation is an enzyme preparation powder in acetone.
18. The method according to claim 9, wherein said microorganism is in a culture medium.
19. Process according to claim 18, wherein said contacting is carried out by adding said compound of formula (I) to said culture medium.
20. Process according to claim 10, wherein said enzyme reduction system is in a solvent.
21. Process according to claim 20, wherein said solvent is an appreciably organic solvent.
22. Process according to claim 10, wherein said contacting is carried out by adding said compound of formula (I) to said solvent.
23. The method according to claim 9, wherein said microorganism is said Hansenula polymorpha ATCC No. 26012 or said Hansenula polymorpha ATCC No. 74449 or its aforementioned mutants.
24. The method according to claim 10, wherein said enzyme comprising said enzyme reduction system is derived from said Hansenula polymorpha ATCC No. 26012 or Hansenula polymorpha ATCC No. 74449 or from said mutants.
25. The method according to claim 18, wherein said microorganism is said Hansenula polymorpha ATCC No. 26012 or said Hansenula polymorpha No. 74449 or its aforementioned mutants.
26. The method according to claim 19, wherein said microorganism is said Hansenula polymorpha ATCC No. 26012 or said Hansenula polymorpha No. 74449 or its aforementioned mutants.
27. The method according to claim 9, wherein said microorganism and Absidia coerule ATCC No. 20137 or its aforementioned mutants.
28. The method according to claim 10, wherein said enzyme comprising said enzyme reduction system is derived from said Absidia coerulea ATCC No. 20137 or its aforementioned mutants.
29. The method according to claim 10, wherein said enzyme comprising said enzyme reduction system is derived from said Monosporium olivaceum v. ATCC No. 36300 or its aforementioned mutants.
30. A process for the stereoselective microbial reduction of a compound of formula (I) to compounds of formulas (II) and (III) comprising: contacting a compound of formula (I) with a microorganism, and incubating the resulting mixture under conditions sufficient to produce more compound of formula (II) than compound of formula (III), thereby leaving more compound of formula (V) ) which is composed of unreacted formula (IV), said microorganism being selected from the group consisting of: Hansenula polymorpha ATCC No. 26012, Hansenula polymorpha ATCC No. 74449 and its mutants capable of carrying out said reduction.
31. The method according to claim 30, wherein said microorganism is in a culture medium.
32. The method according to claim 31, wherein said contacting is carried out by adding said compound of formula (I) to said culture medium. 33.- A procedure for stereoselective microbial reduction of a compound of formula (I) to compound of formulas (II) and (III) comprising: contacting a compound of formula (I) with an enzyme reduction system capable of carrying out said reduction comprising an enzyme derived from a microorganism and a cofactor for said enzyme, and incubating the resulting mixture under conditions sufficient to producing more compound of formula (II) than compound of formula (III), thus leaving more compound of formula (V) unreacted than unreacted compound of formula (IV), said microorganism being selected from the group consisting of: Hansenula polymorpha ATCC no. 26012, Hansenula polymorpha ATCC No. 74449 and its mutants capable of carrying out said reduction. 34. The method according to claim 33, wherein said enzyme reduction system is in a solvent. 35. The method according to claim 34, wherein said contacting is carried out by adding said compound of formula (I) to said solvent. SUMMARY OF THE INVENTION The present invention relates to methods for carrying out the following steroselective microbial reduction of a racemic tetralone: comprising: contacting a compound of formula (I) with a microorganism, or an enzyme reduction system capable of carrying out the present reduction, comprising an enzyme derived from said microorganism and a cofactor for said enzyme, and incubating the resulting mixture under conditions sufficient to produce the (4R) tetralol of formula (II) and leave substantially unreacted the (4S) tetralone of formula (V) or "chiral tetralone". The chiral tetralone can be used in the synthesis of sertraline. The present process optionally further comprises separating the (4S) tetralone of formula (V) from (4R) tetralol of formula (II). The (4R) tetralol can be recycled to produce the compound of formula (I) and the present procedure is repeated to produce more desired (4S) tetralone of formula (V). PF / all * P99 / 1350
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US60/106,233 | 1998-10-29 |
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