WO2017015793A1 - Method for separating diastereoisomer a of bedaquiline - Google Patents
Method for separating diastereoisomer a of bedaquiline Download PDFInfo
- Publication number
- WO2017015793A1 WO2017015793A1 PCT/CN2015/085075 CN2015085075W WO2017015793A1 WO 2017015793 A1 WO2017015793 A1 WO 2017015793A1 CN 2015085075 W CN2015085075 W CN 2015085075W WO 2017015793 A1 WO2017015793 A1 WO 2017015793A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- aqueous solution
- diastereomer
- solvent
- acid
- reaction
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract description 51
- QUIJNHUBAXPXFS-XLJNKUFUSA-N bedaquiline Chemical compound C1([C@H](C2=CC3=CC(Br)=CC=C3N=C2OC)[C@@](O)(CCN(C)C)C=2C3=CC=CC=C3C=CC=2)=CC=CC=C1 QUIJNHUBAXPXFS-XLJNKUFUSA-N 0.000 title abstract description 7
- 229960000508 bedaquiline Drugs 0.000 title abstract 6
- 238000006243 chemical reaction Methods 0.000 claims abstract description 66
- 239000002904 solvent Substances 0.000 claims abstract description 32
- 239000002994 raw material Substances 0.000 claims abstract description 12
- 239000007864 aqueous solution Substances 0.000 claims description 42
- 239000000243 solution Substances 0.000 claims description 31
- RKOTXQYWCBGZLP-UHFFFAOYSA-N N-[(2,4-difluorophenyl)methyl]-2-ethyl-9-hydroxy-3-methoxy-1,8-dioxospiro[3H-pyrido[1,2-a]pyrazine-4,3'-oxolane]-7-carboxamide Chemical compound CCN1C(OC)C2(CCOC2)N2C=C(C(=O)NCC3=C(F)C=C(F)C=C3)C(=O)C(O)=C2C1=O RKOTXQYWCBGZLP-UHFFFAOYSA-N 0.000 claims description 30
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 24
- 239000002253 acid Substances 0.000 claims description 23
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims description 21
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 20
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 claims description 18
- ZCSHNCUQKCANBX-UHFFFAOYSA-N lithium diisopropylamide Chemical compound [Li+].CC(C)[N-]C(C)C ZCSHNCUQKCANBX-UHFFFAOYSA-N 0.000 claims description 16
- WMFHVNYOCKTDMX-UHFFFAOYSA-N 3-benzyl-6-bromo-2-methoxyquinoline Chemical compound COC1=NC2=CC=C(Br)C=C2C=C1CC1=CC=CC=C1 WMFHVNYOCKTDMX-UHFFFAOYSA-N 0.000 claims description 15
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical group CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 claims description 15
- 239000007858 starting material Substances 0.000 claims description 15
- UOXDGEUQIKPEPE-UHFFFAOYSA-N 1-(dimethylamino)-3-naphthalen-1-ylpropan-2-one Chemical compound C1=CC=C2C(CC(=O)CN(C)C)=CC=CC2=C1 UOXDGEUQIKPEPE-UHFFFAOYSA-N 0.000 claims description 14
- 239000005457 ice water Substances 0.000 claims description 14
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 12
- SMWDFEZZVXVKRB-UHFFFAOYSA-N Quinoline Chemical compound N1=CC=CC2=CC=CC=C21 SMWDFEZZVXVKRB-UHFFFAOYSA-N 0.000 claims description 12
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 claims description 9
- 150000001335 aliphatic alkanes Chemical class 0.000 claims description 8
- ZAFNJMIOTHYJRJ-UHFFFAOYSA-N Diisopropyl ether Chemical group CC(C)OC(C)C ZAFNJMIOTHYJRJ-UHFFFAOYSA-N 0.000 claims description 6
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 6
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 6
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 claims description 6
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 claims description 6
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 claims description 6
- 239000011324 bead Substances 0.000 claims description 5
- BZLVMXJERCGZMT-UHFFFAOYSA-N Methyl tert-butyl ether Chemical compound COC(C)(C)C BZLVMXJERCGZMT-UHFFFAOYSA-N 0.000 claims description 4
- 239000003960 organic solvent Substances 0.000 claims description 4
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 claims description 3
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 3
- 235000019253 formic acid Nutrition 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 235000019260 propionic acid Nutrition 0.000 claims description 3
- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical compound O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 claims description 3
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 claims description 2
- 239000002798 polar solvent Substances 0.000 claims description 2
- 239000002244 precipitate Substances 0.000 claims description 2
- 238000000926 separation method Methods 0.000 abstract description 15
- 238000000746 purification Methods 0.000 abstract description 8
- 238000004440 column chromatography Methods 0.000 abstract description 4
- 239000012295 chemical reaction liquid Substances 0.000 abstract description 3
- 239000012535 impurity Substances 0.000 abstract description 3
- 238000002360 preparation method Methods 0.000 abstract 1
- 239000012044 organic layer Substances 0.000 description 36
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Natural products CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 32
- 239000000047 product Substances 0.000 description 24
- 239000000706 filtrate Substances 0.000 description 20
- 150000003839 salts Chemical class 0.000 description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 18
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 16
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 15
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 description 15
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 15
- 239000010410 layer Substances 0.000 description 15
- 239000012065 filter cake Substances 0.000 description 10
- 238000001914 filtration Methods 0.000 description 10
- 238000004128 high performance liquid chromatography Methods 0.000 description 10
- 230000007935 neutral effect Effects 0.000 description 10
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 10
- 238000001556 precipitation Methods 0.000 description 9
- 238000003756 stirring Methods 0.000 description 9
- 229910019142 PO4 Inorganic materials 0.000 description 5
- 239000012230 colorless oil Substances 0.000 description 5
- 238000001816 cooling Methods 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 238000005580 one pot reaction Methods 0.000 description 5
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 5
- 239000010452 phosphate Substances 0.000 description 5
- 229910000027 potassium carbonate Inorganic materials 0.000 description 5
- TYJJADVDDVDEDZ-UHFFFAOYSA-M potassium hydrogencarbonate Chemical compound [K+].OC([O-])=O TYJJADVDDVDEDZ-UHFFFAOYSA-M 0.000 description 5
- 239000008213 purified water Substances 0.000 description 5
- 238000010791 quenching Methods 0.000 description 5
- 230000000171 quenching effect Effects 0.000 description 5
- 239000011541 reaction mixture Substances 0.000 description 5
- 238000010992 reflux Methods 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
- 238000013517 stratification Methods 0.000 description 5
- 238000001291 vacuum drying Methods 0.000 description 5
- 238000005406 washing Methods 0.000 description 5
- 208000012839 conversion disease Diseases 0.000 description 4
- ZKHQWZAMYRWXGA-KQYNXXCUSA-J ATP(4-) Chemical compound C1=NC=2C(N)=NC=NC=2N1[C@@H]1O[C@H](COP([O-])(=O)OP([O-])(=O)OP([O-])([O-])=O)[C@@H](O)[C@H]1O ZKHQWZAMYRWXGA-KQYNXXCUSA-J 0.000 description 3
- ZKHQWZAMYRWXGA-UHFFFAOYSA-N Adenosine triphosphate Natural products C1=NC=2C(N)=NC=NC=2N1C1OC(COP(O)(=O)OP(O)(=O)OP(O)(O)=O)C(O)C1O ZKHQWZAMYRWXGA-UHFFFAOYSA-N 0.000 description 3
- 238000004537 pulping Methods 0.000 description 3
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 2
- AFVFQIVMOAPDHO-UHFFFAOYSA-N Methanesulfonic acid Chemical compound CS(O)(=O)=O AFVFQIVMOAPDHO-UHFFFAOYSA-N 0.000 description 2
- 241000187479 Mycobacterium tuberculosis Species 0.000 description 2
- 239000012670 alkaline solution Substances 0.000 description 2
- 235000011114 ammonium hydroxide Nutrition 0.000 description 2
- 238000010009 beating Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 229940072185 drug for treatment of tuberculosis Drugs 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 201000009671 multidrug-resistant tuberculosis Diseases 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 201000008827 tuberculosis Diseases 0.000 description 2
- 206010034133 Pathogen resistance Diseases 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Natural products N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 1
- 230000008485 antagonism Effects 0.000 description 1
- ZLVSPMRFRHMMOY-WWCCMVHESA-N bedaquiline fumarate Chemical group OC(=O)\C=C\C(O)=O.C1([C@H](C2=CC3=CC(Br)=CC=C3N=C2OC)[C@@](O)(CCN(C)C)C=2C3=CC=CC=C3C=CC=2)=CC=CC=C1 ZLVSPMRFRHMMOY-WWCCMVHESA-N 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- GKIRPKYJQBWNGO-OCEACIFDSA-N clomifene Chemical compound C1=CC(OCCN(CC)CC)=CC=C1C(\C=1C=CC=CC=1)=C(\Cl)C1=CC=CC=C1 GKIRPKYJQBWNGO-OCEACIFDSA-N 0.000 description 1
- 239000012043 crude product Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 210000002540 macrophage Anatomy 0.000 description 1
- 230000010534 mechanism of action Effects 0.000 description 1
- 229940098779 methanesulfonic acid Drugs 0.000 description 1
- 239000012452 mother liquor Substances 0.000 description 1
- UFWIBTONFRDIAS-UHFFFAOYSA-N naphthalene-acid Natural products C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 1
- 238000005554 pickling Methods 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 229940048026 sirturo Drugs 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- 125000003944 tolyl group Chemical group 0.000 description 1
- 239000000814 tuberculostatic agent Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D215/00—Heterocyclic compounds containing quinoline or hydrogenated quinoline ring systems
- C07D215/02—Heterocyclic compounds containing quinoline or hydrogenated quinoline ring systems having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen atoms or carbon atoms directly attached to the ring nitrogen atom
- C07D215/16—Heterocyclic compounds containing quinoline or hydrogenated quinoline ring systems having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen atoms or carbon atoms directly attached to the ring nitrogen atom with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
- C07D215/20—Oxygen atoms
- C07D215/22—Oxygen atoms attached in position 2 or 4
- C07D215/227—Oxygen atoms attached in position 2 or 4 only one oxygen atom which is attached in position 2
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
- C07F1/00—Compounds containing elements of Groups 1 or 11 of the Periodic Table
- C07F1/02—Lithium compounds
Definitions
- the present invention relates to the field of pharmaceuticals, and more particularly to a method for isolating Bidaquinoline diastereomer A.
- Bedaquinine is an anti-tuberculosis drug with the structural formula shown in Figure 1:
- bedaquinoline is (1R,2S)-1-(6-bromo-2-methoxy-3-quinolinyl)-4-dimethylamino-2-(1-naphthyl)-1 -Phenyl-2-butanol, the first drug developed by Johnson & Johnson to inhibit mycobacterial adenosine triphosphate (ATP) synthase, was first marketed in the United States in December 2012 for the treatment of adult multidrug-resistant tuberculosis.
- the trade name is Sirturo.
- Bedaquinoline shows strong selectivity for ATP synthase of Mycobacterium tuberculosis, and its new mechanism of action makes it resistant to cross-resistance with other anti-tuberculosis drugs, which will greatly reduce the resistance of Mycobacterium tuberculosis. It shows good activity against multidrug-resistant tuberculosis in macrophages, suggesting that it has the effect of shortening the treatment time.
- the ratio of diastereomer B to diastereomer A obtained by the method is between 1:1 and 1:3, for the next chiral decomposing. It has an impact; sometimes even the conversion rate is as low as 50%.
- the conversion rate is as low as 50%, since the amount of the product in the reaction liquid is small, the separation product can hardly be purified by the method of the patent WO2006125769, even if the product is separated and purified by the purification method disclosed in the patent, the final The purity of the resulting diastereomer A is also very low.
- the present invention provides a method for separating bedaquinoline diastereomer A which is simple in operation and stable in method. Regardless of the reaction conversion rate of the prepared betaxazoline, the method can make the betadarquinoline diastereomer B and the desired diastereomer A The ratio is between 1:8-1:23, thus ensuring the high purity and yield of the desired diastereomer A, which facilitates the next chiral resolution and successfully achieves the non-antagonism of the betaxipaline. Separation of isomer A.
- the present invention provides a method for isolating bead quinoline diastereomer A comprising the steps of:
- the diastereomer B precipitated in the step (1) is removed to obtain a diastereomer A;
- the diastereomer A is:
- the diastereomer B is:
- the reverse phase solvent is an organic solvent miscible with the solvent of the betadarquinoline reaction solution.
- the reverse phase solvent is a non-polar or weakly polar solvent.
- the reverse phase solvent is a C5-C16 alkane, or a C4-C8 ether solvent, or a mixture of a C5-C16 alkane and a C4-C8 ether solvent.
- the C5-C16 alkane is n-heptane or n-hexane;
- the C4-C8 ether solvent is isopropyl ether, petroleum ether or methyl tert-butyl ether.
- the C5-C16 alkane is n-heptane; the C4-C8 ether solvent is isopropyl ether.
- the solvent of the bead quinoline reaction solution is tetrahydrofuran; and the betadaquinoline reaction solution is obtained by reacting a reaction raw material with lithium diisopropylamide (LDA) in tetrahydrofuran.
- LDA lithium diisopropylamide
- the reaction raw materials are 3-benzyl-6-bromo-2-methoxyquinoline and 3-dimethylamino-1-(naphthalen-5-yl)acetone.
- a weak acid aqueous solution is first added to the bead quinoline reaction solution to remove the residual starting material 3-dimethylamino-1-(naphthalen-5-yl)acetone, and then the anti-addition is added.
- Phase solvent is added.
- the bead quinoline reaction solution is added to the reverse phase solvent to precipitate the diastereomer B, and further subjected to an ice water bath step to further precipitate the diastereomer B.
- the ice water bath step is carried out at 0-5 °C.
- a weak acid aqueous solution is added to the solution after removing the diastereomer B precipitated in the step (1) to remove the residual starting material 3-dimethylamino-1-(naphthalene). -5-yl)acetone; then a strong acid aqueous solution was added to remove the residual starting material 3-benzyl-6-bromo-2-methoxyquinoline to give the diastereomer A.
- the step (2) after adding a strong acid aqueous solution to remove the raw material 3-benzyl-6-bromo-2-methoxyquinoline, it is made alkaline with an alkaline solution, and added and diastereomeric
- the organic solvent which is mutually miscible and water-immiscible is extracted and concentrated to obtain diastereomer A; preferably, the alkaline solution is ammonia water or sodium hydroxide, and the diastereomer
- the organic solvent in which A is mutually soluble and immiscible with water is toluene or dichloromethane.
- the diastereomer A has a purity of at least 88%; further preferably, the purity is 88-96%.
- the volume ratio of the reverse phase solvent to the solvent of the betadarquinoline reaction solution is from 1:10 to 10:1; preferably, the volume ratio is from 1:5 to 5:1; further preferably, The volume ratio is from 1:2 to 2:1.
- the percentage concentration of the weak acid aqueous solution is 10%-60%, the percentage concentration of the strong acid aqueous solution is 5%-40%; further preferably, the weak acid aqueous solution has a percentage concentration of 30%-50%, The percentage concentration of the aqueous strong acid solution is 15%-25%.
- the weak acid aqueous solution is an aqueous formic acid solution, an aqueous solution of acetic acid or an aqueous solution of propionic acid; and the aqueous solution of strong acid is an aqueous solution of sulfonic acid, an aqueous solution of hydrochloric acid, an aqueous solution of sulfuric acid or an aqueous solution of phosphoric acid.
- the weak acid aqueous solution is an aqueous acetic acid solution
- the strong acid aqueous solution is an aqueous hydrochloric acid solution.
- the separation method used in the present invention has more industrial value than the separation and purification by column chromatography;
- the separation product can hardly be purified by the method of the patent WO2006125769, even if the product is separated and purified by the purification method disclosed in the patent, and finally The purity of the resulting diastereomer A is also very low.
- the undesired diastereomer B is precipitated from the betaacene racemate by adding a reverse phase solvent to the betadarquinoline reaction solution, regardless of the conversion conversion rate of the prepared betaxazoline.
- the ratio of the betaactoline diastereomer B to the desired diastereomer A can be between 1:8 and 1:23 to ensure the desired diastereomer.
- A has higher purity and yield, which is beneficial to the next chiral separation.
- the bidaquinoline diastereomer B is removed, and then the raw material is removed by pickling, thereby achieving the purpose of further purification, compared with the patent.
- the ethanol pulping and purifying method used in the step C of the embodiment part of WO2006125769 is more advantageous, on the one hand, the product residue is prevented from causing loss in the beating mother liquor; on the other hand, when the conversion rate of the prepared betaxazoline reaction is not good, the reaction end point is caused.
- the diastereomer A obtained by the method of the present invention is further resolved to obtain a qualified end product of betaxaquinoline having a purity of ⁇ 99.0%, wherein the diastereomer impurity is ⁇ 0.1%. Therefore, the invention has more application value than the prior art in practical applications, and is simple in operation and stable in method.
- the diastereomer A isolated by the method of the present invention can be resolved by a prior art method to further obtain the betaxipaquinine of the desired configuration.
- the separation method of the invention has more industrial value than the separation and purification by the conventional column chromatography
- the separation method of the present invention can overcome the technical problem that the reaction conditions of the betaxazoline are severe, the conversion rate is difficult to be ensured, and the amount of the product is small when the conversion rate is low, and it is difficult to purify and separate it;
- the reverse phase solvent is added to precipitate the undesired diastereomer B from the beta-quinoline racemate, and the beta-quinoline diastereomeric can be ensured regardless of the reaction conversion rate of the prepared betaxazoline.
- the ratio of isomer B to the desired diastereomer A is between 1:8 and 1:23, thereby ensuring that the desired diastereomer A has higher purity and yield, which is advantageous for the next Step chiral splitting;
- the separation method of the invention can easily remove the residue of the raw material, the yield is high, the purity of the diastereomer A is also high, and the separation is facilitated, and the qualified bedaquinoline can be prepared by further resolution.
- the product has a purity of ⁇ 99.0%, wherein the diastereomer impurity is ⁇ 0.1%.
- the separation method of the present invention is simple in operation and stable in method.
- the obtained filtrate was washed with a 50% aqueous acetic acid solution to remove the starting material 3-dimethylamino-1-(naphthalen-5-yl)acetone, and a 15% aqueous hydrochloric acid solution was added to the organic layer to stir to form a salt in the aqueous layer. In the middle of precipitation. Filtration and stratification of the filtrate, at which time the product was transferred to the aqueous layer, and the material, 3-benzyl-6-bromo-2-methoxyquinoline, remained in the organic layer and the organic layer was discarded.
- the filtered product is combined with the aqueous layer obtained by layering the filtrate with the filtrate, adjusted to basic with aqueous ammonia, extracted with toluene, and the organic layer is washed with water until neutral, and the organic layer is concentrated under reduced pressure to obtain a product.
- Isomer A (4.9 g), purity 89%.
- the obtained diastereomer A was resolved by the method of WO2006125769 to obtain the desired bedaquinoline.
- the specific method is as follows:
- the split salt (2.07 g), toluene (37 ml), potassium carbonate (1.51 g) and water (13 ml) were mixed, heated to 90 ° C and stirred until fully dissolved; hot layered, the organic layer was treated with 10% aqueous potassium carbonate solution ( 5 ml), 1 time, the organic layer was monitored by TLC; washed with purified water until pH was neutral (20 ml ⁇ 3 times); the organic layer was concentrated under reduced pressure to give a colorless oil (1.5 g); The mixture was stirred and stirred at room temperature for 0.5 h to precipitate a solid, which was stirred for 1 hour in ice-water bath, filtered, and the filter cake was washed with ethanol, and dried under vacuum at 50-60 ° C to obtain bedaquinoline (1.07 g) with an HPLC purity of >99%. .
- the obtained filtrate was washed with a 10% aqueous solution of formic acid to remove the starting material 3-dimethylamino-1-(naphthalen-5-yl)acetone, and a 5% aqueous solution of sulfuric acid was added to the organic layer to stir to form a salt in the aqueous layer. In the middle of precipitation. Filtration and stratification of the filtrate, at which time the product was transferred to the aqueous layer, and the starting material, 3-benzyl-6-bromo-2-methoxyquinoline, remained in the organic layer and the organic layer was discarded.
- the filtered product is combined with the aqueous layer obtained by layering the filtrate with the filtrate, adjusted to a weak basic with sodium hydroxide, extracted with dichloromethane, and the organic layer is washed with water until neutral, and the organic layer is concentrated under reduced pressure.
- the product diastereomer A (5.7 g) was obtained with a purity of 92%.
- the obtained diastereomer A was resolved by the method of WO2006125769 to obtain the desired bedaquinoline.
- the specific method is as follows:
- the obtained filtrate was washed with a 60% aqueous solution of propionic acid to remove the starting material 3-dimethylamino-1-(naphthalen-5-yl)acetone, and 40% aqueous methanesulfonic acid was added to the organic layer to stir to form a salt. Precipitated in the water layer. Filtration and stratification of the filtrate, at which time the product was transferred to the aqueous layer, and the material, 3-benzyl-6-bromo-2-methoxyquinoline, remained in the organic layer and the organic layer was discarded.
- the filtered product is combined with the aqueous layer obtained by layering the filtrate with the filtrate, adjusted to a weak basic with sodium hydroxide, extracted with dichloromethane, and the organic layer is washed with water until neutral, and the organic layer is concentrated under reduced pressure.
- the product diastereomer A (6.0 g) was obtained with a purity of 94%.
- the obtained diastereomer A was resolved by the method of WO2006125769 to obtain the desired bedaquinoline.
- the specific method is as follows:
- the split salt (2.59g), toluene (40ml), potassium carbonate (1.60g) and water (14ml) were mixed, heated to 90 ° C and stirred until fully dissolved; layered hot, the organic layer was treated with 10% potassium carbonate solution ( Washed once with 5 ml), washed with purified water until the pH was neutral (20 ml ⁇ 3 times); the organic layer was concentrated under reduced pressure to give a colorless oil (1.7 g); toluene (1 ml) Stir at room temperature for 0.5h The solid was precipitated, stirred in an ice water bath for 1 h, filtered, and the filter cake was washed with ethanol, and dried under vacuum at 50-60 ° C to give bedaquinoline (1.20 g) with HPLC purity >99%.
- the obtained filtrate was washed with a 30% aqueous solution of acetic acid to remove the raw material 3-dimethylamino-1-(naphthalen-5-yl)acetone, and a 25% aqueous phosphoric acid solution was added to the organic layer to stir to form a salt in the aqueous layer. In the middle of precipitation. Filtration and stratification of the filtrate, at which time the product was transferred to the aqueous layer, and the material, 3-benzyl-6-bromo-2-methoxyquinoline, remained in the organic layer and the organic layer was discarded.
- the filtered product is combined with the aqueous layer obtained by layering the filtrate with the filtrate, adjusted to a weak basic with sodium hydroxide, extracted with dichloromethane, and the organic layer is washed with water until neutral, and the organic layer is concentrated under reduced pressure.
- the product diastereomer A (5.72 g) was obtained with a purity of 88%.
- the obtained diastereomer A was resolved by the method of WO2006125769 to obtain the desired bedaquinoline.
- the specific method is as follows:
- the split salt (2.43g), toluene (40ml), potassium carbonate (1.60g) and water (14ml) were mixed, heated to 90 ° C and stirred until fully dissolved; hot layered, the organic layer was treated with 10% potassium carbonate solution ( Washed once with 5 ml), washed with purified water until the pH was neutral (20 ml ⁇ 3 times); the organic layer was concentrated under reduced pressure to give a colorless oil (1.5 g); toluene (1 ml) The solid was precipitated by stirring at room temperature for 0.5 h, stirred in an ice-water bath for 1 h, filtered, and the filter cake was washed with ethanol, and dried under vacuum at 50-60 ° C to obtain bedaquinoline (1.16 g) with HPLC purity >99%.
- the obtained filtrate was washed with a 40% aqueous solution of acetic acid to remove the raw material 3-dimethylamino-1-(naphthalen-5-yl)acetone, and a 20% aqueous hydrochloric acid solution was added to the organic layer to stir to form a salt in the aqueous layer. In the middle of precipitation. Filtration and stratification of the filtrate, at which time the product was transferred to the aqueous layer, and the material, 3-benzyl-6-bromo-2-methoxyquinoline, remained in the organic layer and the organic layer was discarded.
- the filtered product is combined with the aqueous layer obtained by layering the filtrate with the filtrate, adjusted to a weak basic with sodium hydroxide, extracted with dichloromethane, and the organic layer is washed with water until neutral, and the organic layer is concentrated under reduced pressure.
- the product diastereomer A (6.1 g) was obtained with a purity of 96%.
- the obtained diastereomer A was resolved by the method of WO2006125769 to obtain the desired bedaquinoline.
- the specific method is as follows:
- split salt (2.69 g), toluene (40 ml), potassium carbonate (1.60 g) and water (14 ml) were mixed, heated to 90 ° C and stirred until fully dissolved; hot layered, organic layer with 10% aqueous potassium carbonate solution ( Washed once with 5 ml), washed with purified water until the pH was neutral (20 ml ⁇ 3 times); the organic layer was concentrated under reduced pressure to give a colorless oil (1.8 g); toluene (1 ml) The solid was precipitated by stirring at room temperature for 0.5 h, stirred in an ice water bath for 1 h, filtered, and the filter cake was washed with ethanol, and dried under vacuum at 50-60 ° C to obtain bedaquinoline (1.28 g) with an HPLC purity of >99%.
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Abstract
Disclosed is a method for separating a diastereoisomer A of Bedaquiline. The method comprises the following steps: (1) adding a reversed-phase solvent into a Bedaquiline reaction liquid comprising diastereoisomers A and B, so as to precipitate out the diastereoisomer B; and (2) removing the diastereoisomer B precipitated out in step (1), so as to obtain the diastereoisomer A. The separation method of the present invention is easy to operate and is stable, and has higher industrialization value compared with separation and purification in a conventional column chromatography method, and can resolve the problems of difficulty in purifying and separating Bedaquiline due to the small amount of a product caused by an excessively low conversion rate because preparation condition of Bedaquiline is harsh and the conversion rate is difficult to ensure; raw material residuals can be easily removed, the yield is high, and the purity of the diastereoisomer A is high, which facilitates the split; split can be further carried out to obtain a qualified Bedaquiline product with a purity greater than or equal to 99.0%, wherein the impurities of the diastereoisomers are lower than or equal to 0.1%.
Description
本发明涉及药物领域,更具体地说,涉及一种贝达喹啉非对映异构体A的分离方法。The present invention relates to the field of pharmaceuticals, and more particularly to a method for isolating Bidaquinoline diastereomer A.
贝达喹啉(Bedaquiline)是一种抗结核病药,其结构式如1所示:Bedaquinine is an anti-tuberculosis drug with the structural formula shown in Figure 1:
贝达喹啉的化学名为(1R,2S)-1-(6-溴-2-甲氧基-3-喹啉基)-4-二甲氨基-2-(1-萘基)-1-苯基-2-丁醇,是美国强生公司开发的首款抑制分枝杆菌三磷酸腺苷(ATP)合成酶的药物,于2012年12月在美国首次上市,用于治疗成人耐多药性结核病,其商品名为Sirturo。贝达喹啉对结核分枝杆菌的ATP合成酶显示出很强的选择性,其全新作用机制,使其与其他抗结核药物不存在交叉耐药性,这将大大降低结核杆菌的抗药性。在巨噬细胞内显示出良好的对抗多药耐药结核病菌的活性,提示它具有缩短治疗时间的作用。The chemical name of bedaquinoline is (1R,2S)-1-(6-bromo-2-methoxy-3-quinolinyl)-4-dimethylamino-2-(1-naphthyl)-1 -Phenyl-2-butanol, the first drug developed by Johnson & Johnson to inhibit mycobacterial adenosine triphosphate (ATP) synthase, was first marketed in the United States in December 2012 for the treatment of adult multidrug-resistant tuberculosis. The trade name is Sirturo. Bedaquinoline shows strong selectivity for ATP synthase of Mycobacterium tuberculosis, and its new mechanism of action makes it resistant to cross-resistance with other anti-tuberculosis drugs, which will greatly reduce the resistance of Mycobacterium tuberculosis. It shows good activity against multidrug-resistant tuberculosis in macrophages, suggesting that it has the effect of shortening the treatment time.
贝达喹啉的合成方法已有文献报道,具体合成路线如下:
The synthesis method of bedaquinoline has been reported in the literature, and the specific synthetic route is as follows:
在专利WO2004011436中提到用柱层析法分离纯化粗品,但该方法不利于工业化;另外,在专利WO2006125769实施例部分步骤C中有公开分离纯化贝达喹啉非对映异构体A的方法。但尽管该专利披露的分离纯化方法所得到的非对映异构体A的纯度为82%,实际上只有反应转化率大于80%以上,才有可能达到。实际研究发现,由于制备贝达喹啉的反应条件控制较难,反应对水分、温度、滴料速度的控制条件苛刻,反应不稳定,不能保证转化率每批次都达到80%以上,通常转化率在60-80%之间时,该方法所得到的非对映异构体B与非对映异构体A的比例在1∶1-1∶3之间,对下一步的手性拆分有影响;甚至有时转化率还会低至50%左右。当转化率低至50%时,由于反应液中产物的量较少,如使用专利WO2006125769的方法,几乎不能纯化分离产物,即使利用该专利披露的纯化方法对产物进行了分离纯化,其最终所得到的非对映异构体A的纯度也很低。In the patent WO2004011436, it is mentioned that the crude product is separated and purified by column chromatography, but the method is not advantageous for industrialization; in addition, the method for separating and purifying the betatraquinoline diastereomer A is disclosed in the step C of the example of the patent WO2006125769. . However, although the purity of the diastereomer A obtained by the separation and purification method disclosed in the patent is 82%, it is actually possible to achieve only the reaction conversion ratio of more than 80%. The actual research found that due to the difficult control of the reaction conditions for preparing betaxazoline, the control conditions of the reaction on water, temperature and dropping speed are harsh, the reaction is unstable, and the conversion rate cannot be guaranteed to reach more than 80% per batch, usually conversion. When the ratio is between 60-80%, the ratio of diastereomer B to diastereomer A obtained by the method is between 1:1 and 1:3, for the next chiral decomposing. It has an impact; sometimes even the conversion rate is as low as 50%. When the conversion rate is as low as 50%, since the amount of the product in the reaction liquid is small, the separation product can hardly be purified by the method of the patent WO2006125769, even if the product is separated and purified by the purification method disclosed in the patent, the final The purity of the resulting diastereomer A is also very low.
发明内容Summary of the invention
为了克服现有技术的不足,本发明提供一种操作简便、方法稳定的分离贝达喹啉非对映异构体A的方法。不论制备贝达喹啉的反应转化率高低,该方法均可使贝达喹啉非对映异构体B与所需的非对映异构体A
的比例在1∶8-1∶23之间,从而保证所需的非对映异构体A纯度和收率较高,利于下步手性拆分,成功实现对贝达喹啉非对映异构体A的分离。In order to overcome the deficiencies of the prior art, the present invention provides a method for separating bedaquinoline diastereomer A which is simple in operation and stable in method. Regardless of the reaction conversion rate of the prepared betaxazoline, the method can make the betadarquinoline diastereomer B and the desired diastereomer A
The ratio is between 1:8-1:23, thus ensuring the high purity and yield of the desired diastereomer A, which facilitates the next chiral resolution and successfully achieves the non-antagonism of the betaxipaline. Separation of isomer A.
本发明采用以下技术方案予以实现:The invention is implemented by the following technical solutions:
本发明提供一种分离贝达喹啉非对映异构体A的方法,包括如下步骤:The present invention provides a method for isolating bead quinoline diastereomer A comprising the steps of:
(1)向含有非对映异构体A和B的贝达喹啉反应液中,加入反相溶剂,析出非对映异构体B;(1) adding a reverse phase solvent to the reaction solution of the betaacene containing the diastereomers A and B to precipitate the diastereomer B;
将步骤(1)析出的非对映异构体B除去,得到非对映异构体A;The diastereomer B precipitated in the step (1) is removed to obtain a diastereomer A;
其中,among them,
优选地,所述步骤(1)中,所述反相溶剂为与所述贝达喹啉反应液的溶剂互溶的有机溶剂。Preferably, in the step (1), the reverse phase solvent is an organic solvent miscible with the solvent of the betadarquinoline reaction solution.
优选地,所述反相溶剂为非极性或者弱极性溶剂。Preferably, the reverse phase solvent is a non-polar or weakly polar solvent.
进一步优选地,所述反相溶剂为C5-C16烷烃、或者C4-C8醚溶剂、或者C5-C16烷烃与C4-C8醚溶剂的混合物。Further preferably, the reverse phase solvent is a C5-C16 alkane, or a C4-C8 ether solvent, or a mixture of a C5-C16 alkane and a C4-C8 ether solvent.
优选地,所述C5-C16烷烃为正庚烷或者正己烷;所述C4-C8醚溶剂为异丙醚、石油醚或者甲基叔丁基醚。Preferably, the C5-C16 alkane is n-heptane or n-hexane; the C4-C8 ether solvent is isopropyl ether, petroleum ether or methyl tert-butyl ether.
优选地,所述C5-C16烷烃为正庚烷;所述C4-C8醚溶剂为异丙醚。Preferably, the C5-C16 alkane is n-heptane; the C4-C8 ether solvent is isopropyl ether.
优选地,所述贝达喹啉反应液的溶剂为四氢呋喃;所述贝达喹啉反应液是反应原料在四氢呋喃中与二异丙基胺基锂(LDA)反应得到。
Preferably, the solvent of the bead quinoline reaction solution is tetrahydrofuran; and the betadaquinoline reaction solution is obtained by reacting a reaction raw material with lithium diisopropylamide (LDA) in tetrahydrofuran.
优选地,所述步骤(1)中,所述反应原料是3-苄基-6-溴-2-甲氧基喹啉和3-二甲氨基-1-(萘-5-基)丙酮。Preferably, in the step (1), the reaction raw materials are 3-benzyl-6-bromo-2-methoxyquinoline and 3-dimethylamino-1-(naphthalen-5-yl)acetone.
优选地,所述步骤(1)中,先向所述贝达喹啉反应液中加入弱酸水溶液,除去残留原料3-二甲氨基-1-(萘-5-基)丙酮,之后再加入反相溶剂。Preferably, in the step (1), a weak acid aqueous solution is first added to the bead quinoline reaction solution to remove the residual starting material 3-dimethylamino-1-(naphthalen-5-yl)acetone, and then the anti-addition is added. Phase solvent.
优选地,所述步骤(1)中,所述贝达喹啉反应液加入所述反相溶剂析出非对映异构体B后,进一步进行冰水浴步骤,进一步析出非对映异构体B;所述冰水浴步骤在0-5℃下进行。Preferably, in the step (1), the bead quinoline reaction solution is added to the reverse phase solvent to precipitate the diastereomer B, and further subjected to an ice water bath step to further precipitate the diastereomer B. The ice water bath step is carried out at 0-5 °C.
优选地,所述步骤(2)中,向除去所述步骤(1)析出的非对映异构体B之后的溶液中,加入弱酸水溶液,除去残留原料3-二甲氨基-1-(萘-5-基)丙酮;然后加入强酸水溶液,除去残留原料3-苄基-6-溴-2-甲氧基喹啉,得到非对映异构体A。Preferably, in the step (2), a weak acid aqueous solution is added to the solution after removing the diastereomer B precipitated in the step (1) to remove the residual starting material 3-dimethylamino-1-(naphthalene). -5-yl)acetone; then a strong acid aqueous solution was added to remove the residual starting material 3-benzyl-6-bromo-2-methoxyquinoline to give the diastereomer A.
优选地,所述步骤(2)中,加入强酸水溶液除去原料3-苄基-6-溴-2-甲氧基喹啉之后,用碱性溶液调至碱性,并加入与非对映异构体A互溶、与水不互溶的有机溶剂提取,浓缩,即得非对映异构体A;优选地,所述碱性溶液为氨水或者氢氧化钠,所述与非对映异构体A互溶、与水不互溶的有机溶剂为甲苯或者二氯甲烷。Preferably, in the step (2), after adding a strong acid aqueous solution to remove the raw material 3-benzyl-6-bromo-2-methoxyquinoline, it is made alkaline with an alkaline solution, and added and diastereomeric The organic solvent which is mutually miscible and water-immiscible is extracted and concentrated to obtain diastereomer A; preferably, the alkaline solution is ammonia water or sodium hydroxide, and the diastereomer The organic solvent in which A is mutually soluble and immiscible with water is toluene or dichloromethane.
优选地,所述非对映异构体A的纯度至少为88%;进一步优选地,所述纯度为88-96%。Preferably, the diastereomer A has a purity of at least 88%; further preferably, the purity is 88-96%.
优选地,所述反相溶剂与所述贝达喹啉反应液的溶剂的体积比为1∶10-10∶1;优选地,该体积比为1∶5-5∶1;进一步优选地,该体积比为1∶2-2∶1。Preferably, the volume ratio of the reverse phase solvent to the solvent of the betadarquinoline reaction solution is from 1:10 to 10:1; preferably, the volume ratio is from 1:5 to 5:1; further preferably, The volume ratio is from 1:2 to 2:1.
优选地,所述弱酸水溶液的百分比浓度为10%-60%,所述强酸水溶液的百分比浓度为5%-40%;进一步优选地,所述弱酸水溶液的百分比浓度为30%-50%,所述强酸水溶液的百分比浓度为15%-25%。Preferably, the percentage concentration of the weak acid aqueous solution is 10%-60%, the percentage concentration of the strong acid aqueous solution is 5%-40%; further preferably, the weak acid aqueous solution has a percentage concentration of 30%-50%, The percentage concentration of the aqueous strong acid solution is 15%-25%.
优选地,所述弱酸水溶液为甲酸水溶液、醋酸水溶液、或者丙酸水溶液;所述强酸水溶液为磺酸水溶液、盐酸水溶液、硫酸水溶液、或者磷酸水溶液。Preferably, the weak acid aqueous solution is an aqueous formic acid solution, an aqueous solution of acetic acid or an aqueous solution of propionic acid; and the aqueous solution of strong acid is an aqueous solution of sulfonic acid, an aqueous solution of hydrochloric acid, an aqueous solution of sulfuric acid or an aqueous solution of phosphoric acid.
优选地,所述弱酸水溶液为醋酸水溶液;所述强酸水溶液为盐酸水溶液。
Preferably, the weak acid aqueous solution is an aqueous acetic acid solution; and the strong acid aqueous solution is an aqueous hydrochloric acid solution.
相对于现有技术,本发明的优点在于:The advantages of the present invention over the prior art are:
首先,本发明所采用的分离方法比柱层析法分离纯化更有工业化价值;First, the separation method used in the present invention has more industrial value than the separation and purification by column chromatography;
其次,经过研究发现,由于制备贝达喹啉的反应对水分、温度、滴料速度的控制条件苛刻,并不能保证转化率达到80%以上,通常转化率在60-80%之间,有时还会低至50%左右,所以采用WO2006125769专利文献实施例部分步骤C披露的方法所得到的非对映异构体B与非对映异构体A的比例一般在1∶1-1∶3之间,当反应转化率较低时,由于反应液中产物的量较少,如使用专利WO2006125769的方法,几乎不能纯化分离产物,即使利用该专利披露的纯化方法对产物进行了分离纯化,其最终所得到的非对映异构体A的纯度也很低。然而本发明通过在贝达喹啉反应液中加入反相溶剂,使不需要的非对映异构体B从贝达喹啉消旋体中析出,不论制备贝达喹啉的反应转化率高低,均可使贝达喹啉非对映异构体B与所需的非对映异构体A的比例在1∶8-1∶23之间,从而保证所需的非对映异构体A具有较高纯度和收率,利于下步手性拆分。Secondly, it has been found through research that the control conditions for preparing bedaquinoline are harsh on the control conditions of moisture, temperature and dropping speed, and the conversion rate is not guaranteed to be above 80%. Usually, the conversion rate is between 60-80%, sometimes It will be as low as about 50%, so the ratio of diastereomer B to diastereomer A obtained by the method disclosed in Example C of the example of WO2006125769 is generally between 1:1 and 1:3. In the meantime, when the reaction conversion rate is low, since the amount of the product in the reaction liquid is small, the separation product can hardly be purified by the method of the patent WO2006125769, even if the product is separated and purified by the purification method disclosed in the patent, and finally The purity of the resulting diastereomer A is also very low. However, in the present invention, the undesired diastereomer B is precipitated from the betaacene racemate by adding a reverse phase solvent to the betadarquinoline reaction solution, regardless of the conversion conversion rate of the prepared betaxazoline. The ratio of the betaactoline diastereomer B to the desired diastereomer A can be between 1:8 and 1:23 to ensure the desired diastereomer. A has higher purity and yield, which is beneficial to the next chiral separation.
更进一步地,本发明通过在贝达喹啉反应液中加入反相溶剂,除去贝达喹啉非对映异构体B后,再通过酸洗去除原料,从而达到进一步纯化的目的,比专利WO2006125769实施例部分步骤C中采用的乙醇打浆纯化方法更有优势,一方面避免了产物残留在打浆母液中造成损失;另一方面当制备贝达喹啉反应的转化率不好时,导致反应终点总有原料残留,如用乙醇打浆方法纯化,残留的原料对打浆收率影响很大,而用本发明方法纯化,当转化率不好时,残留的原料可以很容易去除,故收率更高,比乙醇打浆方法更有优势。最后通过本发明方法分离得到的非对映异构体A,经进一步拆分可制备得到合格的贝达喹啉终产物,纯度≥99.0%,其中非对映异构体杂质≤0.1%。故本发明在实际应用中比现有技术更有应用价值,并且操作简便、方法稳定。Further, in the present invention, by adding a reverse phase solvent to the reaction reaction solution of the bedaquinoline, the bidaquinoline diastereomer B is removed, and then the raw material is removed by pickling, thereby achieving the purpose of further purification, compared with the patent. The ethanol pulping and purifying method used in the step C of the embodiment part of WO2006125769 is more advantageous, on the one hand, the product residue is prevented from causing loss in the beating mother liquor; on the other hand, when the conversion rate of the prepared betaxazoline reaction is not good, the reaction end point is caused. There are always raw material residues, such as purification by ethanol pulping method. The residual raw materials have great influence on the beating yield, and are purified by the method of the present invention. When the conversion rate is not good, the residual raw materials can be easily removed, so the yield is higher. It has advantages over the ethanol pulping method. Finally, the diastereomer A obtained by the method of the present invention is further resolved to obtain a qualified end product of betaxaquinoline having a purity of ≥99.0%, wherein the diastereomer impurity is ≤0.1%. Therefore, the invention has more application value than the prior art in practical applications, and is simple in operation and stable in method.
可采用现有技术的方法对本发明方法分离得到的非对映异构体A拆分,进一步得到所需构型的贝达喹啉。The diastereomer A isolated by the method of the present invention can be resolved by a prior art method to further obtain the betaxipaquinine of the desired configuration.
本发明的有益效果在于:
The beneficial effects of the invention are:
1.本发明的分离方法,比传统的柱层析法分离纯化更有工业化价值;1. The separation method of the invention has more industrial value than the separation and purification by the conventional column chromatography;
2.本发明的分离方法,可克服由于贝达喹啉的制备反应条件苛刻,转化率难以保证,进而导致转化率低时产物量少而难以对其进行纯化分离的技术问题;通过向反应体系中加入反相溶剂,使不需要的非对映异构体B从贝达喹啉消旋体中析出,不论制备贝达喹啉的反应转化率高低,均可以保证贝达喹啉非对映异构体B与所需的非对映异构体A的比例在1∶8-1∶23之间,从而保证所需的非对映异构体A具有较高纯度和收率,利于下步手性拆分;2. The separation method of the present invention can overcome the technical problem that the reaction conditions of the betaxazoline are severe, the conversion rate is difficult to be ensured, and the amount of the product is small when the conversion rate is low, and it is difficult to purify and separate it; The reverse phase solvent is added to precipitate the undesired diastereomer B from the beta-quinoline racemate, and the beta-quinoline diastereomeric can be ensured regardless of the reaction conversion rate of the prepared betaxazoline. The ratio of isomer B to the desired diastereomer A is between 1:8 and 1:23, thereby ensuring that the desired diastereomer A has higher purity and yield, which is advantageous for the next Step chiral splitting;
3.本发明的分离方法,可轻易地去除原料残留,收率高、非对映异构体A的纯度也高,有利于拆分,经进一步拆分可制备得到合格的贝达喹啉终产物,纯度≥99.0%,其中非对映异构体杂质≤0.1%。3. The separation method of the invention can easily remove the residue of the raw material, the yield is high, the purity of the diastereomer A is also high, and the separation is facilitated, and the qualified bedaquinoline can be prepared by further resolution. The product has a purity of ≥99.0%, wherein the diastereomer impurity is ≤0.1%.
4.本发明的分离方法,操作简便、方法稳定。4. The separation method of the present invention is simple in operation and stable in method.
实施例1Example 1
反应原料3-苄基-6-溴-2-甲氧基喹啉(10g)与3-二甲氨基-1-(萘-5-基)丙酮(10g),在四氢呋喃(80ml)中与LDA(20g)反应,一步反应得到消旋的贝达喹啉反应液。经HPLC分析得该反应的转化率为56%。反应结束淬灭后,往反应液中加正庚烷(40ml),冰水浴0℃下析出不需要的非对映异构体B,过滤,去除非对映异构体B。所得滤液用50%的醋酸水溶液洗涤有机层,去除原料3-二甲氨基-1-(萘-5-基)丙酮,加15%的盐酸水溶液至有机层中搅拌,使产物成盐在水层中析出。过滤,滤液分层,此时产物转移至水层,原料3-苄基-6-溴-2-甲氧基喹啉留在有机层中,弃去有机层。将所滤得的产物成盐固体与滤液分层所得的水层合并,用氨水调至碱性,加甲苯萃取游离,再将有机层水洗至中性,减压浓缩有机层,得产物非对映异构体A(4.9g),纯度89%。Reaction material 3-benzyl-6-bromo-2-methoxyquinoline (10 g) with 3-dimethylamino-1-(naphthalen-5-yl)acetone (10 g) in tetrahydrofuran (80 ml) with LDA (20 g) reaction, one-step reaction to obtain a racemic bedaquinoline reaction solution. The conversion of the reaction was analyzed by HPLC to be 56%. After quenching the reaction, n-heptane (40 ml) was added to the reaction mixture, and the desired diastereomer B was precipitated from ice-water bath at 0 ° C, and filtered to remove diastereomer B. The obtained filtrate was washed with a 50% aqueous acetic acid solution to remove the starting material 3-dimethylamino-1-(naphthalen-5-yl)acetone, and a 15% aqueous hydrochloric acid solution was added to the organic layer to stir to form a salt in the aqueous layer. In the middle of precipitation. Filtration and stratification of the filtrate, at which time the product was transferred to the aqueous layer, and the material, 3-benzyl-6-bromo-2-methoxyquinoline, remained in the organic layer and the organic layer was discarded. The filtered product is combined with the aqueous layer obtained by layering the filtrate with the filtrate, adjusted to basic with aqueous ammonia, extracted with toluene, and the organic layer is washed with water until neutral, and the organic layer is concentrated under reduced pressure to obtain a product. Isomer A (4.9 g), purity 89%.
参照专利WO2006125769的方法,对得到的非对映异构体A进行拆分得到所需要的贝达喹啉,具体方法如下所述:
The obtained diastereomer A was resolved by the method of WO2006125769 to obtain the desired bedaquinoline. The specific method is as follows:
向得到的贝达喹啉的非对映异构体A(4.9g)中加入丙酮(40ml)、DMSO(4.9ml)、R-联萘酚磷酸酯(2.62g)后,加热回流2小时,冷却,析出拆分盐;室温下过滤,用丙酮洗滤饼,50-60℃真空干燥得拆分盐(2.07g);To the obtained diastereomer A (4.9 g) of bedaquinoline, acetone (40 ml), DMSO (4.9 ml) and R-binaphthol phosphate (2.62 g) were added, followed by heating under reflux for 2 hours. Cooling, precipitation of the split salt; filtration at room temperature, washing the filter cake with acetone, vacuum drying at 50-60 ° C to obtain a split salt (2.07 g);
将拆分盐(2.07g)、甲苯(37ml)、碳酸钾(1.51g)与水(13ml)混合,加热至90℃搅拌至全溶;趁热分层,有机层用10%碳酸钾水溶液(5ml)洗1次,此时有机层TLC监控;用纯化水洗至pH为中性(20ml×3次);有机层减压浓缩得无色油状物(1.5g);加甲苯(1ml)加热全溶,加乙醇(12ml)室温搅拌0.5h析出固体,冰水浴搅拌1h,过滤,用乙醇洗滤饼,50-60℃真空干燥得贝达喹啉(1.07g),其HPLC纯度>99%。。The split salt (2.07 g), toluene (37 ml), potassium carbonate (1.51 g) and water (13 ml) were mixed, heated to 90 ° C and stirred until fully dissolved; hot layered, the organic layer was treated with 10% aqueous potassium carbonate solution ( 5 ml), 1 time, the organic layer was monitored by TLC; washed with purified water until pH was neutral (20 ml × 3 times); the organic layer was concentrated under reduced pressure to give a colorless oil (1.5 g); The mixture was stirred and stirred at room temperature for 0.5 h to precipitate a solid, which was stirred for 1 hour in ice-water bath, filtered, and the filter cake was washed with ethanol, and dried under vacuum at 50-60 ° C to obtain bedaquinoline (1.07 g) with an HPLC purity of >99%. .
实施例2Example 2
原料3-苄基-6-溴-2-甲氧基喹啉(10g)与3-二甲氨基-1-(萘-5-基)丙酮(10g),在四氢呋喃(80ml)中与LDA(20g)反应,一步反应得到消旋的贝达喹啉反应液。经HPLC分析得该反应的转化率为65%。反应结束淬灭后,往反应液中加异丙醚(160ml),冰水浴5℃下析出不需要的非对映异构体B,过滤,去除非对映异构体B。所得滤液用10%的甲酸水溶液洗涤有机层,去除原料3-二甲氨基-1-(萘-5-基)丙酮,加5%的硫酸水溶液至有机层中搅拌,使产物成盐在水层中析出。过滤、滤液分层,此时产物转移至水层,原料3-苄基-6-溴-2-甲氧基喹啉留在有机层中,弃去有机层。将所滤得的产物成盐固体与滤液分层所得的水层合并,用氢氧化钠调至弱碱性,加二氯甲烷萃取游离,再将有机层水洗至中性,减压浓缩有机层,得产物非对映异构体A(5.7g),纯度92%。Starting material 3-benzyl-6-bromo-2-methoxyquinoline (10 g) with 3-dimethylamino-1-(naphthalen-5-yl)acetone (10 g) in tetrahydrofuran (80 ml) with LDA ( 20 g) reaction, one-step reaction to obtain a racemic bedaquinoline reaction solution. The conversion of the reaction was analyzed by HPLC to be 65%. After quenching at the end of the reaction, isopropyl ether (160 ml) was added to the reaction mixture, and the desired diastereomer B was precipitated in an ice water bath at 5 ° C, and filtered to remove the diastereomer B. The obtained filtrate was washed with a 10% aqueous solution of formic acid to remove the starting material 3-dimethylamino-1-(naphthalen-5-yl)acetone, and a 5% aqueous solution of sulfuric acid was added to the organic layer to stir to form a salt in the aqueous layer. In the middle of precipitation. Filtration and stratification of the filtrate, at which time the product was transferred to the aqueous layer, and the starting material, 3-benzyl-6-bromo-2-methoxyquinoline, remained in the organic layer and the organic layer was discarded. The filtered product is combined with the aqueous layer obtained by layering the filtrate with the filtrate, adjusted to a weak basic with sodium hydroxide, extracted with dichloromethane, and the organic layer is washed with water until neutral, and the organic layer is concentrated under reduced pressure. The product diastereomer A (5.7 g) was obtained with a purity of 92%.
参照专利WO2006125769的方法,对得到的非对映异构体A进行拆分得到所需要的贝达喹啉,具体方法如下所述:The obtained diastereomer A was resolved by the method of WO2006125769 to obtain the desired bedaquinoline. The specific method is as follows:
向得到的贝达喹啉的非对映异构体A(5.7g)中加入丙酮(45ml)、DMSO(5.7ml)、R-联萘酚磷酸酯(3.04g)后,加热回流2小时,冷却,析出拆分盐;室温下过滤,用丙酮洗滤饼,50-60℃真空干燥得拆分盐(2.6g);
To the obtained diastereomer A (5.7 g) of bedaquinoline, acetone (45 ml), DMSO (5.7 ml) and R-binaphthol phosphate (3.04 g) were added, followed by heating under reflux for 2 hours. Cooling, precipitation of the split salt; filtration at room temperature, washing the filter cake with acetone, vacuum drying at 50-60 ° C to obtain a split salt (2.6 g);
将拆分盐(2.41g)、甲苯(39ml)、碳酸钾(1.58g)和水(14ml)混合,加热至90℃搅拌至全溶;趁热分层,有机层用10%碳酸钾水溶液(5ml)洗1次,用纯化水洗至pH为中性(20ml×3次);有机层减压浓缩得无色油状物(1.6g);加甲苯(1ml)加热全溶,加乙醇(12ml)室温搅拌0.5h析出固体,冰水浴搅拌1h,过滤,用乙醇洗滤饼,50-60℃真空干燥得贝达喹啉(1.19g),其HPLC纯度>99%。The split salt (2.41 g), toluene (39 ml), potassium carbonate (1.58 g) and water (14 ml) were mixed, heated to 90 ° C and stirred until fully dissolved; hot layered, organic layer with 10% aqueous potassium carbonate solution ( Washed once with 5 ml), washed with purified water until the pH was neutral (20 ml × 3 times); the organic layer was concentrated under reduced pressure to give a colorless oil (1.6 g); toluene (1 ml) The solid was precipitated by stirring at room temperature for 0.5 h, stirred in an ice-water bath for 1 h, filtered, and the filter cake was washed with ethanol, and dried under vacuum at 50-60 ° C to obtain bedaquinoline (1.19 g) with HPLC purity >99%.
实施例3Example 3
原料3-苄基-6-溴-2-甲氧基喹啉(10g)与3-二甲氨基-1-(萘-5-基)丙酮(10g),在四氢呋喃(80ml)中与LDA(20g)反应,一步反应得到消旋的贝达喹啉反应液。经HPLC分析得该反应的转化率为75%。反应结束淬灭后,往反应液中加异丙醚(400ml),冰水浴2℃下析出不需要的非对映异构体B,过滤,去除非对映异构体B。所得滤液用60%的丙酸水溶液洗涤有机层,去除原料3-二甲氨基-1-(萘-5-基)丙酮,加40%的甲磺酸水溶液至有机层中搅拌,使产物成盐在水层中析出。过滤,滤液分层,此时产物转移至水层,原料3-苄基-6-溴-2-甲氧基喹啉留在有机层中,弃去有机层。将所滤得的产物成盐固体与滤液分层所得的水层合并,用氢氧化钠调至弱碱性,加二氯甲烷萃取游离,再将有机层水洗至中性,减压浓缩有机层,得产物非对映异构体A(6.0g),纯度94%。Starting material 3-benzyl-6-bromo-2-methoxyquinoline (10 g) with 3-dimethylamino-1-(naphthalen-5-yl)acetone (10 g) in tetrahydrofuran (80 ml) with LDA ( 20 g) reaction, one-step reaction to obtain a racemic bedaquinoline reaction solution. The conversion of the reaction was analyzed by HPLC to be 75%. After quenching the reaction, isopropyl ether (400 ml) was added to the reaction mixture, and the desired diastereomer B was precipitated in an ice water bath at 2 ° C, and filtered to remove the diastereomer B. The obtained filtrate was washed with a 60% aqueous solution of propionic acid to remove the starting material 3-dimethylamino-1-(naphthalen-5-yl)acetone, and 40% aqueous methanesulfonic acid was added to the organic layer to stir to form a salt. Precipitated in the water layer. Filtration and stratification of the filtrate, at which time the product was transferred to the aqueous layer, and the material, 3-benzyl-6-bromo-2-methoxyquinoline, remained in the organic layer and the organic layer was discarded. The filtered product is combined with the aqueous layer obtained by layering the filtrate with the filtrate, adjusted to a weak basic with sodium hydroxide, extracted with dichloromethane, and the organic layer is washed with water until neutral, and the organic layer is concentrated under reduced pressure. The product diastereomer A (6.0 g) was obtained with a purity of 94%.
参照专利WO2006125769的方法,对得到的非对映异构体A进行拆分得到所需要的贝达喹啉,具体方法如下所述:The obtained diastereomer A was resolved by the method of WO2006125769 to obtain the desired bedaquinoline. The specific method is as follows:
向得到的贝达喹啉的非对映异构体A(6.0g)中加入丙酮(48ml)、DMSO(6.0ml)、R-联萘酚磷酸酯(3.09g)后,加热回流2小时,冷却,析出拆分盐;室温下过滤,用丙酮洗滤饼,50-60℃真空干燥得拆分盐(2.59g);To the obtained diastereomer A (6.0 g) of bedaquinoline, acetone (48 ml), DMSO (6.0 ml) and R-binaphthol phosphate (3.09 g) were added, followed by heating under reflux for 2 hours. Cooling, precipitation of the split salt; filtration at room temperature, washing the filter cake with acetone, vacuum drying at 50-60 ° C to obtain a split salt (2.59 g);
将拆分盐(2.59g)、甲苯(40ml)、碳酸钾(1.60g)和水(14ml)混合,加热至90℃搅拌至全溶;趁热分层,有机层用10%碳酸钾水溶液(5ml)洗1次,用纯化水洗至pH为中性(20ml×3次);有机层减压浓缩得无色油状物(1.7g);加甲苯(1ml)加热全溶,加乙醇(12ml)室温搅拌0.5h
析出固体,冰水浴搅拌1h,过滤,用乙醇洗滤饼,50-60℃真空干燥得贝达喹啉(1.20g),其HPLC纯度>99%。The split salt (2.59g), toluene (40ml), potassium carbonate (1.60g) and water (14ml) were mixed, heated to 90 ° C and stirred until fully dissolved; layered hot, the organic layer was treated with 10% potassium carbonate solution ( Washed once with 5 ml), washed with purified water until the pH was neutral (20 ml × 3 times); the organic layer was concentrated under reduced pressure to give a colorless oil (1.7 g); toluene (1 ml) Stir at room temperature for 0.5h
The solid was precipitated, stirred in an ice water bath for 1 h, filtered, and the filter cake was washed with ethanol, and dried under vacuum at 50-60 ° C to give bedaquinoline (1.20 g) with HPLC purity >99%.
实施例4Example 4
原料3-苄基-6-溴-2-甲氧基喹啉(10g)与3-二甲氨基-1-(萘-5-基)丙酮(10g),在四氢呋喃(80ml)中与LDA(20g)反应,一步反应得到消旋的贝达喹啉反应液。经HPLC分析得该反应的转化率为70%。反应结束淬灭后,往反应液中加石油醚(16ml),冰水浴3℃下析出不需要的非对映异构体B,过滤,去除非对映异构体B。所得滤液用30%的醋酸水溶液洗涤有机层,去除原料3-二甲氨基-1-(萘-5-基)丙酮,加25%的磷酸水溶液至有机层中搅拌,使产物成盐在水层中析出。过滤,滤液分层,此时产物转移至水层,原料3-苄基-6-溴-2-甲氧基喹啉留在有机层中,弃去有机层。将所滤得的产物成盐固体与滤液分层所得的水层合并,用氢氧化钠调至弱碱性,加二氯甲烷萃取游离,再将有机层水洗至中性,减压浓缩有机层,得产物非对映异构体A(5.72g),纯度88%。Starting material 3-benzyl-6-bromo-2-methoxyquinoline (10 g) with 3-dimethylamino-1-(naphthalen-5-yl)acetone (10 g) in tetrahydrofuran (80 ml) with LDA ( 20 g) reaction, one-step reaction to obtain a racemic bedaquinoline reaction solution. The conversion of the reaction was analyzed by HPLC to be 70%. After quenching the reaction, petroleum ether (16 ml) was added to the reaction mixture, and the desired diastereomer B was precipitated in an ice water bath at 3 ° C, and filtered to remove the diastereomer B. The obtained filtrate was washed with a 30% aqueous solution of acetic acid to remove the raw material 3-dimethylamino-1-(naphthalen-5-yl)acetone, and a 25% aqueous phosphoric acid solution was added to the organic layer to stir to form a salt in the aqueous layer. In the middle of precipitation. Filtration and stratification of the filtrate, at which time the product was transferred to the aqueous layer, and the material, 3-benzyl-6-bromo-2-methoxyquinoline, remained in the organic layer and the organic layer was discarded. The filtered product is combined with the aqueous layer obtained by layering the filtrate with the filtrate, adjusted to a weak basic with sodium hydroxide, extracted with dichloromethane, and the organic layer is washed with water until neutral, and the organic layer is concentrated under reduced pressure. The product diastereomer A (5.72 g) was obtained with a purity of 88%.
参照专利WO2006125769的方法,对得到的非对映异构体A进行拆分得到所需要的贝达喹啉,具体方法如下所述:The obtained diastereomer A was resolved by the method of WO2006125769 to obtain the desired bedaquinoline. The specific method is as follows:
向得到的贝达喹啉的非对映异构体A(5.72g)中加入丙酮(45ml)、DMSO(5.7ml)、R-联萘酚磷酸酯(3.04g)后,加热回流2小时,冷却,析出拆分盐;室温下过滤,用丙酮洗滤饼,50-60℃真空干燥得拆分盐(2.43g);To the obtained diastereomer A (5.72 g) of bedaquinoline, acetone (45 ml), DMSO (5.7 ml), and R-binaphthol phosphate (3.04 g) were added, followed by heating under reflux for 2 hours. Cooling, precipitation and resolution of the salt; filtration at room temperature, washing the filter cake with acetone, vacuum drying at 50-60 ° C to obtain a split salt (2.43 g);
将拆分盐(2.43g)、甲苯(40ml)、碳酸钾(1.60g)和水(14ml)混合,加热至90℃搅拌至全溶;趁热分层,有机层用10%碳酸钾水溶液(5ml)洗1次,用纯化水洗至pH为中性(20ml×3次);有机层减压浓缩得无色油状物(1.5g);加甲苯(1ml)加热全溶,加乙醇(12ml)室温搅拌0.5h析出固体,冰水浴搅拌1h,过滤,用乙醇洗滤饼,50-60℃真空干燥得贝达喹啉(1.16g),其HPLC纯度>99%。The split salt (2.43g), toluene (40ml), potassium carbonate (1.60g) and water (14ml) were mixed, heated to 90 ° C and stirred until fully dissolved; hot layered, the organic layer was treated with 10% potassium carbonate solution ( Washed once with 5 ml), washed with purified water until the pH was neutral (20 ml × 3 times); the organic layer was concentrated under reduced pressure to give a colorless oil (1.5 g); toluene (1 ml) The solid was precipitated by stirring at room temperature for 0.5 h, stirred in an ice-water bath for 1 h, filtered, and the filter cake was washed with ethanol, and dried under vacuum at 50-60 ° C to obtain bedaquinoline (1.16 g) with HPLC purity >99%.
实施例5
Example 5
原料3-苄基-6-溴-2-甲氧基喹啉(10g)与3-二甲氨基-1-(萘-5-基)丙酮(10g),在四氢呋喃(80ml)中与LDA(20g)反应,一步反应得到消旋的贝达喹啉反应液。经HPLC分析得该反应的转化率为80%。反应结束淬灭后,往反应液中加正己烷(80ml),冰水浴1℃下析出不需要的非对映异构体B,过滤,去除非对映异构体B。所得滤液用40%的醋酸水溶液洗涤有机层,去除原料3-二甲氨基-1-(萘-5-基)丙酮,加20%的盐酸水溶液至有机层中搅拌,使产物成盐在水层中析出。过滤,滤液分层,此时产物转移至水层,原料3-苄基-6-溴-2-甲氧基喹啉留在有机层中,弃去有机层。将所滤得的产物成盐固体与滤液分层所得的水层合并,用氢氧化钠调至弱碱性,加二氯甲烷萃取游离,再将有机层水洗至中性,减压浓缩有机层,得产物非对映异构体A(6.1g),纯度96%。Starting material 3-benzyl-6-bromo-2-methoxyquinoline (10 g) with 3-dimethylamino-1-(naphthalen-5-yl)acetone (10 g) in tetrahydrofuran (80 ml) with LDA ( 20 g) reaction, one-step reaction to obtain a racemic bedaquinoline reaction solution. The conversion of the reaction was analyzed by HPLC to be 80%. After quenching the reaction, n-hexane (80 ml) was added to the reaction mixture, and the desired diastereomer B was precipitated in an ice water bath at 1 ° C, and filtered to remove the diastereomer B. The obtained filtrate was washed with a 40% aqueous solution of acetic acid to remove the raw material 3-dimethylamino-1-(naphthalen-5-yl)acetone, and a 20% aqueous hydrochloric acid solution was added to the organic layer to stir to form a salt in the aqueous layer. In the middle of precipitation. Filtration and stratification of the filtrate, at which time the product was transferred to the aqueous layer, and the material, 3-benzyl-6-bromo-2-methoxyquinoline, remained in the organic layer and the organic layer was discarded. The filtered product is combined with the aqueous layer obtained by layering the filtrate with the filtrate, adjusted to a weak basic with sodium hydroxide, extracted with dichloromethane, and the organic layer is washed with water until neutral, and the organic layer is concentrated under reduced pressure. The product diastereomer A (6.1 g) was obtained with a purity of 96%.
参照专利WO2006125769的方法,对得到的非对映异构体A进行拆分得到所需要的贝达喹啉,具体方法如下所述:The obtained diastereomer A was resolved by the method of WO2006125769 to obtain the desired bedaquinoline. The specific method is as follows:
向得到的贝达喹啉的非对映异构体A(6.1g)中加入丙酮(48ml)、DMSO(6.1ml)、R-联萘酚磷酸酯(3.09g)后,加热回流2小时,冷却,析出拆分盐;室温下过滤,用丙酮洗滤饼,50-60℃真空干燥得拆分盐(2.69g);To the obtained diastereomer A (6.1 g) of bedaquinoline, acetone (48 ml), DMSO (6.1 ml) and R-binaphthol phosphate (3.09 g) were added, followed by heating under reflux for 2 hours. Cooling, precipitation of the separated salt; filtration at room temperature, washing the filter cake with acetone, vacuum drying at 50-60 ° C to obtain a split salt (2.69 g);
将拆分盐(2.69g)、甲苯(40ml)、碳酸钾(1.60g)和水(14ml)混合,加热至90℃搅拌至全溶;趁热分层,有机层用10%碳酸钾水溶液(5ml)洗1次,用纯化水洗至pH为中性(20ml×3次);有机层减压浓缩得无色油状物(1.8g);加甲苯(1ml)加热全溶,加乙醇(12ml)室温搅拌0.5h析出固体,冰水浴搅拌1h,过滤,用乙醇洗滤饼,50-60℃真空干燥得贝达喹啉(1.28g),其HPLC纯度>99%。
The split salt (2.69 g), toluene (40 ml), potassium carbonate (1.60 g) and water (14 ml) were mixed, heated to 90 ° C and stirred until fully dissolved; hot layered, organic layer with 10% aqueous potassium carbonate solution ( Washed once with 5 ml), washed with purified water until the pH was neutral (20 ml × 3 times); the organic layer was concentrated under reduced pressure to give a colorless oil (1.8 g); toluene (1 ml) The solid was precipitated by stirring at room temperature for 0.5 h, stirred in an ice water bath for 1 h, filtered, and the filter cake was washed with ethanol, and dried under vacuum at 50-60 ° C to obtain bedaquinoline (1.28 g) with an HPLC purity of >99%.
Claims (12)
- 一种分离贝达喹啉非对映异构体A的方法,其特征在于,所述方法包括如下步骤:A method for separating betaxipolin diastereomer A, characterized in that the method comprises the following steps:(1)向含有非对映异构体A和B的贝达喹啉反应液中,加入反相溶剂,析出非对映异构体B;(1) adding a reverse phase solvent to the reaction solution of the betaacene containing the diastereomers A and B to precipitate the diastereomer B;(2)除去步骤(1)析出的非对映异构体B,得到非对映异构体A;(2) removing the diastereomer B precipitated in the step (1) to obtain a diastereomer A;其中,among them,
- 根据权利要求1所述的方法,其特征在于,所述步骤(1)中,所述反相溶剂为与所述贝达喹啉反应液的溶剂互溶的有机溶剂;优选地,所述反相溶剂为非极性或者弱极性溶剂;进一步优选地,所述反相溶剂为C5-C16烷烃、或者C4-C8醚溶剂、或者C5-C16烷烃与C4-C8醚溶剂的混合物。The method according to claim 1, wherein in the step (1), the reverse phase solvent is an organic solvent miscible with the solvent of the betadarquinoline reaction solution; preferably, the reverse phase The solvent is a non-polar or weakly polar solvent; further preferably, the reverse phase solvent is a C5-C16 alkane, or a C4-C8 ether solvent, or a mixture of a C5-C16 alkane and a C4-C8 ether solvent.
- 根据权利要求2所述的方法,其特征在于,所述C3-C10烷烃为正庚烷或者正己烷,所述C4-C8醚溶剂为异丙醚或者甲基叔丁基醚;优选地,所述C3-C10烷烃为正庚烷,所述C4-C8醚溶剂为异丙醚。The method according to claim 2, wherein the C3-C10 alkane is n-heptane or n-hexane, and the C4-C8 ether solvent is isopropyl ether or methyl tert-butyl ether; preferably, The C3-C10 alkane is n-heptane and the C4-C8 ether solvent is isopropyl ether.
- 根据权利要求2所述的方法,其特征在于,所述贝达喹啉反应液的溶剂为四氢呋喃;所述贝达喹啉反应液是反应原料在四氢呋喃中与二异丙基胺基锂反应得到。The method according to claim 2, wherein the solvent of the betadarquinoline reaction solution is tetrahydrofuran; and the betadaquinoline reaction solution is obtained by reacting a reaction raw material with lithium diisopropylamide in tetrahydrofuran. .
- 根据权利要求4所述的方法,其特征在于,所述步骤(1)中,所 述反应原料是3-苄基-6-溴-2-甲氧基喹啉和3-二甲氨基-1-(萘-5-基)丙酮。The method according to claim 4, wherein in the step (1), the The starting materials for the reaction are 3-benzyl-6-bromo-2-methoxyquinoline and 3-dimethylamino-1-(naphthalen-5-yl)acetone.
- 根据权利要求5所述的方法,其特征在于,所述步骤(1)中,先向所述贝达喹啉反应液中加入弱酸水溶液,除去残留原料3-二甲氨基-1-(萘-5-基)丙酮,之后再加入反相溶剂。The method according to claim 5, wherein in the step (1), a weak acid aqueous solution is first added to the bead quinoline reaction solution to remove the residual starting material 3-dimethylamino-1-(naphthalene- 5-Base) Acetone, followed by the addition of a reversed phase solvent.
- 根据权利要求1-6任一项所述的方法,其特征在于,所述步骤(1)中,加入所述反相溶剂析出非对映异构体B后,进一步进行冰水浴步骤,进一步析出非对映异构体B;所述冰水浴步骤在0-5℃下进行。The method according to any one of claims 1 to 6, wherein in the step (1), after adding the reverse phase solvent to precipitate the diastereomer B, the ice water bath step is further carried out to further precipitate. Diastereomer B; the ice water bath step is carried out at 0-5 °C.
- 根据权利要求5所述的方法,其特征在于,所述步骤(2)为:除去步骤(1)析出的非对映异构体B,在除去非对映异构体B之后的溶液中,加入弱酸水溶液,除去残留原料3-二甲氨基-1-(萘-5-基)丙酮;然后加入强酸水溶液,除去残留原料3-苄基-6-溴-2-甲氧基喹啉,得到非对映异构体A。The method according to claim 5, wherein the step (2) is: removing the diastereomer B precipitated in the step (1), in the solution after removing the diastereomer B, Adding a weak acid aqueous solution to remove the residual starting material 3-dimethylamino-1-(naphthalen-5-yl)acetone; then adding a strong acid aqueous solution to remove the residual starting material 3-benzyl-6-bromo-2-methoxyquinoline, Diastereomer A.
- 根据权利要求1-8任一项所述的方法,其特征在于,所述步骤(2)中,所述非对映异构体A的纯度至少为88%;优选地,所述纯度为88-96%。The method according to any one of claims 1-8, wherein in the step (2), the purity of the diastereomer A is at least 88%; preferably, the purity is 88. -96%.
- 根据权利要求1所述的方法,其特征在于,所述反相溶剂与所述贝达喹啉反应液的溶剂的体积比为1∶10-10∶1;优选地,该体积比为1∶5-5∶1;进一步优选地,该体积比为1∶2-2∶1。The method according to claim 1, wherein the volume ratio of the reverse phase solvent to the solvent of the betadarquinoline reaction solution is from 1:10 to 10:1; preferably, the volume ratio is 1: 5-5:1; further preferably, the volume ratio is from 1:2 to 2:1.
- 根据权利要求1所述的方法,其特征在于,所述弱酸水溶液的百分比浓度为10%-60%,所述强酸水溶液的百分比浓度为5%-40%;优选地,所述弱酸水溶液的百分比浓度为30%-50%,所述强酸水溶液的百分比浓度为15%-25%。The method according to claim 1, wherein the weak acid aqueous solution has a percentage concentration of 10% to 60%, and the strong acid aqueous solution has a percentage concentration of 5% to 40%; preferably, the percentage of the weak acid aqueous solution The concentration is from 30% to 50%, and the percentage concentration of the strong acid aqueous solution is from 15% to 25%.
- 根据权利要求8所述的方法,其特征在于,所述弱酸水溶液为甲酸水溶液、醋酸水溶液、或者丙酸水溶液,优选地,所述弱酸水溶液为醋酸水溶液;所述强酸水溶液为磺酸水溶液、盐酸水溶液、硫酸水溶液、或者磷酸水溶液,优选地,所述强酸水溶液为盐酸水溶液。 The method according to claim 8, wherein the weak acid aqueous solution is an aqueous solution of formic acid, an aqueous solution of acetic acid, or an aqueous solution of propionic acid. Preferably, the aqueous solution of weak acid is an aqueous solution of acetic acid; and the aqueous solution of strong acid is an aqueous solution of sulfonic acid or hydrochloric acid. An aqueous solution, an aqueous solution of sulfuric acid, or an aqueous solution of phosphoric acid, preferably, the aqueous solution of strong acid is an aqueous solution of hydrochloric acid.
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CN109422679A (en) * | 2017-08-30 | 2019-03-05 | 武汉武药科技有限公司 | A kind of shellfish is up to the purifying of quinoline and the preparation method of stable crystal form |
CN114085185A (en) * | 2020-07-01 | 2022-02-25 | 东亚St 株式会社 | Process for preparing bedaquiline and pharmaceutically acceptable salts thereof |
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CN109422679A (en) * | 2017-08-30 | 2019-03-05 | 武汉武药科技有限公司 | A kind of shellfish is up to the purifying of quinoline and the preparation method of stable crystal form |
CN109422679B (en) * | 2017-08-30 | 2021-06-25 | 武汉武药科技有限公司 | Purification of bedaquiline and preparation method of stable crystal form |
CN107857727A (en) * | 2017-10-26 | 2018-03-30 | 江苏天和制药有限公司 | It is a kind of(1R, 2S)With(1S, 2R)Shellfish reaches the preparation method of quinoline |
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