CA2558198A1 - Crystalline composition containing escitalopram oxalate - Google Patents
Crystalline composition containing escitalopram oxalate Download PDFInfo
- Publication number
- CA2558198A1 CA2558198A1 CA002558198A CA2558198A CA2558198A1 CA 2558198 A1 CA2558198 A1 CA 2558198A1 CA 002558198 A CA002558198 A CA 002558198A CA 2558198 A CA2558198 A CA 2558198A CA 2558198 A1 CA2558198 A1 CA 2558198A1
- Authority
- CA
- Canada
- Prior art keywords
- escitalopram
- particle size
- oxalate
- crystalline particles
- citalopram
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
Links
- KTGRHKOEFSJQNS-BDQAORGHSA-N (1s)-1-[3-(dimethylamino)propyl]-1-(4-fluorophenyl)-3h-2-benzofuran-5-carbonitrile;oxalic acid Chemical compound OC(=O)C(O)=O.C1([C@]2(C3=CC=C(C=C3CO2)C#N)CCCN(C)C)=CC=C(F)C=C1 KTGRHKOEFSJQNS-BDQAORGHSA-N 0.000 title claims abstract description 98
- 229960005086 escitalopram oxalate Drugs 0.000 title claims abstract description 97
- 239000000203 mixture Substances 0.000 title claims description 30
- 239000002245 particle Substances 0.000 claims abstract description 131
- 229960004341 escitalopram Drugs 0.000 claims abstract description 74
- WSEQXVZVJXJVFP-FQEVSTJZSA-N escitalopram Chemical compound C1([C@]2(C3=CC=C(C=C3CO2)C#N)CCCN(C)C)=CC=C(F)C=C1 WSEQXVZVJXJVFP-FQEVSTJZSA-N 0.000 claims abstract description 74
- 238000000034 method Methods 0.000 claims abstract description 69
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims abstract description 54
- 229960001653 citalopram Drugs 0.000 claims abstract description 50
- WSEQXVZVJXJVFP-HXUWFJFHSA-N (R)-citalopram Chemical compound C1([C@@]2(C3=CC=C(C=C3CO2)C#N)CCCN(C)C)=CC=C(F)C=C1 WSEQXVZVJXJVFP-HXUWFJFHSA-N 0.000 claims abstract description 42
- 239000012535 impurity Substances 0.000 claims abstract description 38
- 238000009826 distribution Methods 0.000 claims abstract description 19
- IAICSOQOSARWDY-PVOVUMCXSA-N 4-[(z)-4-(dimethylamino)-1-(4-fluorophenyl)but-1-enyl]-3-(hydroxymethyl)benzonitrile Chemical compound C=1C=C(C#N)C=C(CO)C=1C(=C/CCN(C)C)\C1=CC=C(F)C=C1 IAICSOQOSARWDY-PVOVUMCXSA-N 0.000 claims abstract description 17
- 238000004519 manufacturing process Methods 0.000 claims abstract description 17
- 238000007907 direct compression Methods 0.000 claims abstract description 14
- 238000001816 cooling Methods 0.000 claims description 37
- 239000000243 solution Substances 0.000 claims description 32
- 239000007892 solid unit dosage form Substances 0.000 claims description 29
- 239000013078 crystal Substances 0.000 claims description 27
- 238000002425 crystallisation Methods 0.000 claims description 25
- 239000002904 solvent Substances 0.000 claims description 22
- 239000004480 active ingredient Substances 0.000 claims description 17
- 239000002516 radical scavenger Substances 0.000 claims description 17
- HQKMJHAJHXVSDF-UHFFFAOYSA-L magnesium stearate Chemical compound [Mg+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O HQKMJHAJHXVSDF-UHFFFAOYSA-L 0.000 claims description 16
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical group CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 15
- 238000010992 reflux Methods 0.000 claims description 11
- 239000000945 filler Substances 0.000 claims description 10
- 239000000546 pharmaceutical excipient Substances 0.000 claims description 10
- 238000006798 ring closing metathesis reaction Methods 0.000 claims description 10
- 238000000926 separation method Methods 0.000 claims description 10
- 239000011230 binding agent Substances 0.000 claims description 9
- 239000002775 capsule Substances 0.000 claims description 8
- 238000006243 chemical reaction Methods 0.000 claims description 8
- 235000019359 magnesium stearate Nutrition 0.000 claims description 8
- 150000003891 oxalate salts Chemical class 0.000 claims description 8
- 239000007787 solid Substances 0.000 claims description 8
- 239000000454 talc Substances 0.000 claims description 8
- 229910052623 talc Inorganic materials 0.000 claims description 8
- 235000012222 talc Nutrition 0.000 claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- 230000002378 acidificating effect Effects 0.000 claims description 7
- 239000000314 lubricant Substances 0.000 claims description 7
- 238000005550 wet granulation Methods 0.000 claims description 7
- GUBGYTABKSRVRQ-QKKXKWKRSA-N Lactose Natural products OC[C@H]1O[C@@H](O[C@H]2[C@H](O)[C@@H](O)C(O)O[C@@H]2CO)[C@H](O)[C@@H](O)[C@H]1O GUBGYTABKSRVRQ-QKKXKWKRSA-N 0.000 claims description 6
- 239000008101 lactose Substances 0.000 claims description 6
- 238000010899 nucleation Methods 0.000 claims description 6
- 238000007909 melt granulation Methods 0.000 claims description 5
- -1 preferably dibasic Substances 0.000 claims description 5
- FALRKNHUBBKYCC-UHFFFAOYSA-N 2-(chloromethyl)pyridine-3-carbonitrile Chemical compound ClCC1=NC=CC=C1C#N FALRKNHUBBKYCC-UHFFFAOYSA-N 0.000 claims description 4
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims description 4
- 229920000168 Microcrystalline cellulose Polymers 0.000 claims description 4
- 229920002472 Starch Polymers 0.000 claims description 4
- 230000002902 bimodal effect Effects 0.000 claims description 4
- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical class [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 claims description 4
- 238000005056 compaction Methods 0.000 claims description 4
- 238000007908 dry granulation Methods 0.000 claims description 4
- 229940016286 microcrystalline cellulose Drugs 0.000 claims description 4
- 235000019813 microcrystalline cellulose Nutrition 0.000 claims description 4
- 239000008108 microcrystalline cellulose Substances 0.000 claims description 4
- 239000003960 organic solvent Substances 0.000 claims description 4
- 239000008107 starch Substances 0.000 claims description 4
- 235000019698 starch Nutrition 0.000 claims description 4
- 229940014800 succinic anhydride Drugs 0.000 claims description 4
- 239000001828 Gelatine Substances 0.000 claims description 3
- 229920000881 Modified starch Polymers 0.000 claims description 3
- 239000007864 aqueous solution Substances 0.000 claims description 3
- 238000011049 filling Methods 0.000 claims description 3
- 238000001914 filtration Methods 0.000 claims description 3
- 229920000159 gelatin Polymers 0.000 claims description 3
- 235000019322 gelatine Nutrition 0.000 claims description 3
- 239000012452 mother liquor Substances 0.000 claims description 3
- GUBGYTABKSRVRQ-XLOQQCSPSA-N Alpha-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 claims description 2
- 239000004135 Bone phosphate Substances 0.000 claims description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims description 2
- FBPFZTCFMRRESA-FSIIMWSLSA-N D-Glucitol Natural products OC[C@H](O)[C@H](O)[C@@H](O)[C@H](O)CO FBPFZTCFMRRESA-FSIIMWSLSA-N 0.000 claims description 2
- FBPFZTCFMRRESA-KVTDHHQDSA-N D-Mannitol Chemical compound OC[C@@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-KVTDHHQDSA-N 0.000 claims description 2
- FBPFZTCFMRRESA-JGWLITMVSA-N D-glucitol Chemical compound OC[C@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-JGWLITMVSA-N 0.000 claims description 2
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 claims description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims description 2
- 229930195725 Mannitol Natural products 0.000 claims description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 2
- 235000021355 Stearic acid Nutrition 0.000 claims description 2
- CZMRCDWAGMRECN-UGDNZRGBSA-N 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 claims description 2
- 229930006000 Sucrose Natural products 0.000 claims description 2
- 150000001298 alcohols Chemical class 0.000 claims description 2
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-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 claims description 2
- 239000011575 calcium Substances 0.000 claims description 2
- 229910052791 calcium Inorganic materials 0.000 claims description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 claims description 2
- 239000001506 calcium phosphate Substances 0.000 claims description 2
- 235000011010 calcium phosphates Nutrition 0.000 claims description 2
- 239000008116 calcium stearate Substances 0.000 claims description 2
- 235000013539 calcium stearate Nutrition 0.000 claims description 2
- 239000008119 colloidal silica Substances 0.000 claims description 2
- 125000004122 cyclic group Chemical group 0.000 claims description 2
- 239000008121 dextrose Substances 0.000 claims description 2
- 238000000605 extraction Methods 0.000 claims description 2
- 239000008172 hydrogenated vegetable oil Substances 0.000 claims description 2
- 239000011777 magnesium Substances 0.000 claims description 2
- 229910052749 magnesium Inorganic materials 0.000 claims description 2
- 239000000594 mannitol Substances 0.000 claims description 2
- 235000010355 mannitol Nutrition 0.000 claims description 2
- 235000019426 modified starch Nutrition 0.000 claims description 2
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 claims description 2
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 claims description 2
- 229910052708 sodium Inorganic materials 0.000 claims description 2
- 239000011734 sodium Substances 0.000 claims description 2
- 239000000600 sorbitol Substances 0.000 claims description 2
- 239000008117 stearic acid Substances 0.000 claims description 2
- 239000005720 sucrose Substances 0.000 claims description 2
- 235000000346 sugar Nutrition 0.000 claims description 2
- 150000008163 sugars Chemical class 0.000 claims description 2
- QORWJWZARLRLPR-UHFFFAOYSA-H tricalcium bis(phosphate) Chemical class [Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O QORWJWZARLRLPR-UHFFFAOYSA-H 0.000 claims description 2
- 239000001993 wax Substances 0.000 claims description 2
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 claims 2
- 235000011132 calcium sulphate Nutrition 0.000 claims 1
- 239000007788 liquid Substances 0.000 claims 1
- 239000007909 solid dosage form Substances 0.000 claims 1
- 239000002552 dosage form Substances 0.000 abstract description 6
- 239000003826 tablet Substances 0.000 description 28
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 17
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 12
- 238000005469 granulation Methods 0.000 description 12
- 230000003179 granulation Effects 0.000 description 12
- 239000000047 product Substances 0.000 description 11
- 150000003839 salts Chemical class 0.000 description 9
- 238000002360 preparation method Methods 0.000 description 7
- WIHMBLDNRMIGDW-UHFFFAOYSA-N 1-[3-(dimethylamino)propyl]-1-(4-fluorophenyl)-3h-2-benzofuran-5-carbonitrile;hydron;bromide Chemical compound [Br-].O1CC2=CC(C#N)=CC=C2C1(CCC[NH+](C)C)C1=CC=C(F)C=C1 WIHMBLDNRMIGDW-UHFFFAOYSA-N 0.000 description 6
- 229960000584 citalopram hydrobromide Drugs 0.000 description 6
- 238000001035 drying Methods 0.000 description 5
- 230000002000 scavenging effect Effects 0.000 description 5
- 239000013543 active substance Substances 0.000 description 4
- 150000002148 esters Chemical class 0.000 description 4
- 239000008187 granular material Substances 0.000 description 4
- 239000004615 ingredient Substances 0.000 description 4
- 235000006408 oxalic acid Nutrition 0.000 description 4
- 239000012071 phase Substances 0.000 description 4
- PYRCEPBRCYHQGX-UHFFFAOYSA-N CN(CCC=C(C1=CC=C(C=C1)F)/C1=C(C(=C(C#N)C=C1)C)O)C Chemical compound CN(CCC=C(C1=CC=C(C=C1)F)/C1=C(C(=C(C#N)C=C1)C)O)C PYRCEPBRCYHQGX-UHFFFAOYSA-N 0.000 description 3
- CPELXLSAUQHCOX-UHFFFAOYSA-N Hydrogen bromide Chemical compound Br CPELXLSAUQHCOX-UHFFFAOYSA-N 0.000 description 3
- 239000000935 antidepressant agent Substances 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 239000007884 disintegrant Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- QZAYGJVTTNCVMB-UHFFFAOYSA-N serotonin Chemical compound C1=C(O)C=C2C(CCN)=CNC2=C1 QZAYGJVTTNCVMB-UHFFFAOYSA-N 0.000 description 3
- 229940032147 starch Drugs 0.000 description 3
- IAICSOQOSARWDY-RMOCHZDMSA-N 4-[(e)-4-(dimethylamino)-1-(4-fluorophenyl)but-1-enyl]-3-(hydroxymethyl)benzonitrile Chemical group C=1C=C(C#N)C=C(CO)C=1C(=C/CCN(C)C)/C1=CC=C(F)C=C1 IAICSOQOSARWDY-RMOCHZDMSA-N 0.000 description 2
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Natural products N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 239000008346 aqueous phase Substances 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- ILAHWRKJUDSMFH-UHFFFAOYSA-N boron tribromide Chemical compound BrB(Br)Br ILAHWRKJUDSMFH-UHFFFAOYSA-N 0.000 description 2
- 244000309466 calf Species 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 150000002009 diols Chemical class 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000007888 film coating Substances 0.000 description 2
- 238000009501 film coating Methods 0.000 description 2
- 239000012065 filter cake Substances 0.000 description 2
- 239000012074 organic phase Substances 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 239000002243 precursor Substances 0.000 description 2
- 238000005204 segregation Methods 0.000 description 2
- 238000000638 solvent extraction Methods 0.000 description 2
- 125000001424 substituent group Chemical group 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- SYTBZMRGLBWNTM-SNVBAGLBSA-N (R)-flurbiprofen Chemical compound FC1=CC([C@H](C(O)=O)C)=CC=C1C1=CC=CC=C1 SYTBZMRGLBWNTM-SNVBAGLBSA-N 0.000 description 1
- QCQCHGYLTSGIGX-GHXANHINSA-N 4-[[(3ar,5ar,5br,7ar,9s,11ar,11br,13as)-5a,5b,8,8,11a-pentamethyl-3a-[(5-methylpyridine-3-carbonyl)amino]-2-oxo-1-propan-2-yl-4,5,6,7,7a,9,10,11,11b,12,13,13a-dodecahydro-3h-cyclopenta[a]chrysen-9-yl]oxy]-2,2-dimethyl-4-oxobutanoic acid Chemical compound N([C@@]12CC[C@@]3(C)[C@]4(C)CC[C@H]5C(C)(C)[C@@H](OC(=O)CC(C)(C)C(O)=O)CC[C@]5(C)[C@H]4CC[C@@H]3C1=C(C(C2)=O)C(C)C)C(=O)C1=CN=CC(C)=C1 QCQCHGYLTSGIGX-GHXANHINSA-N 0.000 description 1
- HBAQYPYDRFILMT-UHFFFAOYSA-N 8-[3-(1-cyclopropylpyrazol-4-yl)-1H-pyrazolo[4,3-d]pyrimidin-5-yl]-3-methyl-3,8-diazabicyclo[3.2.1]octan-2-one Chemical class C1(CC1)N1N=CC(=C1)C1=NNC2=C1N=C(N=C2)N1C2C(N(CC1CC2)C)=O HBAQYPYDRFILMT-UHFFFAOYSA-N 0.000 description 1
- 229910015845 BBr3 Inorganic materials 0.000 description 1
- 229910015844 BCl3 Inorganic materials 0.000 description 1
- 229910016280 BI3 Inorganic materials 0.000 description 1
- 229920002785 Croscarmellose sodium Polymers 0.000 description 1
- 102000020897 Formins Human genes 0.000 description 1
- 108091022623 Formins Proteins 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- 229920002153 Hydroxypropyl cellulose Polymers 0.000 description 1
- WHNWPMSKXPGLAX-UHFFFAOYSA-N N-Vinyl-2-pyrrolidone Chemical compound C=CN1CCCC1=O WHNWPMSKXPGLAX-UHFFFAOYSA-N 0.000 description 1
- 229910019201 POBr3 Inorganic materials 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- VJHCJDRQFCCTHL-UHFFFAOYSA-N acetic acid 2,3,4,5,6-pentahydroxyhexanal Chemical compound CC(O)=O.OCC(O)C(O)C(O)C(O)C=O VJHCJDRQFCCTHL-UHFFFAOYSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 150000008064 anhydrides Chemical class 0.000 description 1
- 230000001430 anti-depressive effect Effects 0.000 description 1
- 229940005513 antidepressants Drugs 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- YMEKEHSRPZAOGO-UHFFFAOYSA-N boron triiodide Chemical compound IB(I)I YMEKEHSRPZAOGO-UHFFFAOYSA-N 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 239000007891 compressed tablet Substances 0.000 description 1
- 229960005168 croscarmellose Drugs 0.000 description 1
- 229960000913 crospovidone Drugs 0.000 description 1
- 239000001767 crosslinked sodium carboxy methyl cellulose Substances 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 230000001186 cumulative effect Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- HWTUHTNZLQJJEV-UHFFFAOYSA-N dihydroxyphosphinothioyl dihydrogen phosphate Chemical compound OP(O)(=O)OP(O)(O)=S HWTUHTNZLQJJEV-UHFFFAOYSA-N 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- WIHMBLDNRMIGDW-BDQAORGHSA-N escitalopram hydrobromide Chemical compound Br.C1([C@]2(C3=CC=C(C=C3CO2)C#N)CCCN(C)C)=CC=C(F)C=C1 WIHMBLDNRMIGDW-BDQAORGHSA-N 0.000 description 1
- 235000003599 food sweetener Nutrition 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 150000003840 hydrochlorides Chemical class 0.000 description 1
- 239000001863 hydroxypropyl cellulose Substances 0.000 description 1
- 235000010977 hydroxypropyl cellulose Nutrition 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000003801 milling Methods 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 235000019198 oils Nutrition 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000008194 pharmaceutical composition Substances 0.000 description 1
- 239000000825 pharmaceutical preparation Substances 0.000 description 1
- UXCDUFKZSUBXGM-UHFFFAOYSA-N phosphoric tribromide Chemical compound BrP(Br)(Br)=O UXCDUFKZSUBXGM-UHFFFAOYSA-N 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 235000013809 polyvinylpolypyrrolidone Nutrition 0.000 description 1
- 229920000523 polyvinylpolypyrrolidone Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 238000001953 recrystallisation Methods 0.000 description 1
- 229940076279 serotonin Drugs 0.000 description 1
- 239000008109 sodium starch glycolate Substances 0.000 description 1
- 229920003109 sodium starch glycolate Polymers 0.000 description 1
- 229940079832 sodium starch glycolate Drugs 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
- 229910021653 sulphate ion Inorganic materials 0.000 description 1
- 239000003765 sweetening agent Substances 0.000 description 1
- FAQYAMRNWDIXMY-UHFFFAOYSA-N trichloroborane Chemical compound ClB(Cl)Cl FAQYAMRNWDIXMY-UHFFFAOYSA-N 0.000 description 1
- 238000010977 unit operation Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000000080 wetting agent Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D307/00—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom
- C07D307/77—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom ortho- or peri-condensed with carbocyclic rings or ring systems
- C07D307/87—Benzo [c] furans; Hydrogenated benzo [c] furans
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P25/00—Drugs for disorders of the nervous system
- A61P25/24—Antidepressants
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Nuclear Medicine, Radiotherapy & Molecular Imaging (AREA)
- Pharmacology & Pharmacy (AREA)
- Biomedical Technology (AREA)
- Neurology (AREA)
- Neurosurgery (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Medicinal Chemistry (AREA)
- Psychiatry (AREA)
- Pain & Pain Management (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Life Sciences & Earth Sciences (AREA)
- Animal Behavior & Ethology (AREA)
- General Health & Medical Sciences (AREA)
- Public Health (AREA)
- Veterinary Medicine (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
- Medicinal Preparation (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Acyclic And Carbocyclic Compounds In Medicinal Compositions (AREA)
Abstract
The present invention discloses crystalline particles of escitalopram oxalate which either have a broad particle size distribution or comprise at least 0.01 % (w/w) of Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxymethyl-benzonitrile, said particles being suitable for use in direct compression.
Furthermore, the invention discloses a novel pharmaceutical unit dosage form containing such crystalline particles of escitalopram oxalate as well as methods for manufacture of such crystalline particles of escitalopram oxalate.
Finally, the invention provides a method for reduction of the amount of hydroxyl containing impurities in a solution of citalopram or escitalopram.
Furthermore, the invention discloses a novel pharmaceutical unit dosage form containing such crystalline particles of escitalopram oxalate as well as methods for manufacture of such crystalline particles of escitalopram oxalate.
Finally, the invention provides a method for reduction of the amount of hydroxyl containing impurities in a solution of citalopram or escitalopram.
Description
CRYSTALLINE COMPOSITTON CONTAINING ESCTTALOPRAM OXALATE
The present invention relates to crystalline preparations of the oxalate salt of the compound escitalopram (INN-name), which is the S-enantiomer of the well-known antidepressant drug citalopram, i.e. (S)-1-[3-(dimethylamino)propyl]-1-(4-fluorophenyl)-1,3-dihydro-5-isobenzofurancarbonitrile oxalate.
Background of the Invention.
1o Citalopram is a well-known antidepressant drug that has the following structure:
i H3 N~
CHg It is a selective, centrally active serotonin (5-hydroxytryptamine; 5-HT) reuptake inhibitor, accordingly having antidepressant activities.
Citalopram was first disclosed in DE 2,657,013, corresponding to US 4,136,193.
This patent publication describes the preparation of citalopram by one method and outlines 2o a further method, which may be used for preparing citalopram. The citalopram prepared was isolated in crystalline form as the oxalate, the hydrobromide and the hydrochloride salt, respectively. Furthermore, the citalopram base was obtained as an oil (B.P. 175 °C/0.03 mmHg). The publication also outlines the manufacture of tablets containing salts of citalopram. Citalopram is marketed as the hydrobromide and the hydrochloride, respectively.
Escitalopram, the pharmaceutical activity thereof and crystalline escitalopram oxalate are disclosed in US Patent No 4,943,590. Methods for preparation of pharmaceutical preparations of escitalopram are outlined.
Citalopram is marlceted in a number of countries as a tablet prepared by compression of granulated citalopram hydrobromide, lactose and other excipients.
The present invention relates to crystalline preparations of the oxalate salt of the compound escitalopram (INN-name), which is the S-enantiomer of the well-known antidepressant drug citalopram, i.e. (S)-1-[3-(dimethylamino)propyl]-1-(4-fluorophenyl)-1,3-dihydro-5-isobenzofurancarbonitrile oxalate.
Background of the Invention.
1o Citalopram is a well-known antidepressant drug that has the following structure:
i H3 N~
CHg It is a selective, centrally active serotonin (5-hydroxytryptamine; 5-HT) reuptake inhibitor, accordingly having antidepressant activities.
Citalopram was first disclosed in DE 2,657,013, corresponding to US 4,136,193.
This patent publication describes the preparation of citalopram by one method and outlines 2o a further method, which may be used for preparing citalopram. The citalopram prepared was isolated in crystalline form as the oxalate, the hydrobromide and the hydrochloride salt, respectively. Furthermore, the citalopram base was obtained as an oil (B.P. 175 °C/0.03 mmHg). The publication also outlines the manufacture of tablets containing salts of citalopram. Citalopram is marketed as the hydrobromide and the hydrochloride, respectively.
Escitalopram, the pharmaceutical activity thereof and crystalline escitalopram oxalate are disclosed in US Patent No 4,943,590. Methods for preparation of pharmaceutical preparations of escitalopram are outlined.
Citalopram is marlceted in a number of countries as a tablet prepared by compression of granulated citalopram hydrobromide, lactose and other excipients.
It is well recognised that preparation of tablets with a reproducible composition requires that all the dry ingredients have good flow properties. In cases, where the active ingredient has good flow properties, tablets can be prepared by direct compression of the ingredients. However, in many cases the particle size of the active substance is small, the active substance is cohesive or has poor flow properties.
Further, active substances with a small particle size mixed with excipients having a larger particle size will typically segregate or de-mix during the tabletting process.
to The pxoblem of small particle size and poor flowability is conventionally solved by enlarging the particle size of the active substance, usually by granulation of the active ingredient either alone or in combination with a filler and/or other conventional tablet ingredients.
One such granulation method is the "wet" granulation process. Using this method, the dry solids (active ingredients, filler, binder etc.) are blended and moistened with water or another wetting agent (e.g. an alcohol) and agglomerates or granules are built up of the moistened solids. Wet massing is continued until a desired homogenous particle size has been achieved whereupon the granulated product is dried.
An alternative to the "wet" granulation method is the "melt" granulation, which is also known as the "thermal plastic" granulation process, where a low melting solid is used as the granulation agent. Initially, the dry solids are blended and heated until the binder melts. As the binder is liquefied and spreads over the surface of the particles, the particles will adhere to each other and form granules. The binder solidifies upon cooling forming a dry granular product.
Wet granulation as well as melt granulation are energy intensive unit operations requiring complicated and expensive equipment as well as technical skill.
If the active ingredient, however, has suitable flow properties, then the granulation step can be avoided and tablets may be prepared by direct compression, which is a cheaper production method.
Further, active substances with a small particle size mixed with excipients having a larger particle size will typically segregate or de-mix during the tabletting process.
to The pxoblem of small particle size and poor flowability is conventionally solved by enlarging the particle size of the active substance, usually by granulation of the active ingredient either alone or in combination with a filler and/or other conventional tablet ingredients.
One such granulation method is the "wet" granulation process. Using this method, the dry solids (active ingredients, filler, binder etc.) are blended and moistened with water or another wetting agent (e.g. an alcohol) and agglomerates or granules are built up of the moistened solids. Wet massing is continued until a desired homogenous particle size has been achieved whereupon the granulated product is dried.
An alternative to the "wet" granulation method is the "melt" granulation, which is also known as the "thermal plastic" granulation process, where a low melting solid is used as the granulation agent. Initially, the dry solids are blended and heated until the binder melts. As the binder is liquefied and spreads over the surface of the particles, the particles will adhere to each other and form granules. The binder solidifies upon cooling forming a dry granular product.
Wet granulation as well as melt granulation are energy intensive unit operations requiring complicated and expensive equipment as well as technical skill.
If the active ingredient, however, has suitable flow properties, then the granulation step can be avoided and tablets may be prepared by direct compression, which is a cheaper production method.
The process used for the preparation of citalopram hydrobromide results in a product with a very small particle size around 2-20 ~,m that, as many other particulate products with a small particle size, has very poor flow properties. Thus, in order to achieve appropriate dosing of the citalopram hydrobromide during tabletting, it was considered necessary to make a granulate of citalopram hydrobromide with larger particle size and improved flow properties.
The citalopram tablet that is marketed is a tablet made from granulated citalopram hydrobromide with various excipients.
We have found that escitalopram has significantly different solubility and salt formation properties from the citalopram racemate. For example, the only pharmaceutically crystalline salt known so far is the oxalate, whereas the citalopram racemate forms crystalline hydrobromide and hydrochloride salts as well.
Crystalline escitalopram hydrobromide has now been disclosed in W02004/056791 A1.
The escitalopram oxalate product prepared by crystallisation from acetone as outlined in US Patent No 4,943,590 has, as the citalopram hydrobromide product described above, a very small particle size around 2-20 ~,m resulting in similarly poor flow properties.
W003/000672 discloses a process for the preparation of racemic as well as enantiomerically pure citalopram from the compound R-4-[4-(dimethylamino)-1-(4'-fluorophenyl)-1-hydroxybutyl]-3-(hydroxymethyl)-benzonitrile by ring-closure under acidic conditions.
W003/011278 discloses crystalline particles of escitalopram oxalate with a particle size of at least 40~,m. Method for the manufacture of said crystalline particles and pharmaceutical compositions comprising said crystalline particles are also disclosed.
The inventors of the present invention have now surprisingly realised that the particle sizes obtained if escitalopram prepared according to the process disclosed in W003/000672 is precipitated as the oxalate salt according to the method disclosed in W003/01127~, are significantly smaller than those obtained from escitalopram prepared by ring-closure of S-4-[4-(dimethylamino)-1-(4'-fluorophenyl)-1-hydroxybutyl]-3-(hydroxymethyl)-benzonitrile via a labile ester under alkaline conditions and precipitated under otherwise identical precipitation conditions.
They have furthermore realised that the reduction in particle size of the escitalopram oxalate crystals is related to the presence of a specific impurity, Z-4-(4-dimethyl-amino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxymethyl-benzonitrile. This impurity is unique for the acidic ring-closure process as compared to the ring-closure via a labile ester under alkaline conditions.
l0 In view of the fact that direct compression is much simpler and cheaper than the processes involving granulation there is a continued desire for large crystals of escitalopram or pharmaceutical acceptable addition salts thereof.
Laboratory and full-scale research have now resulted in a new and inventive process producing large crystalline particles of escitalopram oxalate, i.e. particles of a size comparable to the size of the filler, by a novel and inventive process for reduction of the amount of Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxy-methyl-benzonitrile in the solution of escitalopram prior to crystallisation of the oxalate. Said particles are useful for the manufacture of directly compressed tablets.
Accurate dosing in capsules may also be with such large particles.
Objects of the Invention One aspect of the present invention is to provide crystalline particles of escitalopram oxalate with a broad particle size distribution, said particles being suitable for use in direct compression.
A second aspect of the invention is to provide large crystalline particles of 3o escitalopram oxalate comprising at least 0.01 % (w/w) of Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxymethyl-benzonitrile, said particles being suitable for use in direct compression.
A third aspect of the invention is to provide a novel pharmaceutical unit dosage form containing crystalline particles of escitalopram oxalate, wherein said particles have a broad particle size distribution and said unit dosage form may be a tablet, which preferably may be prepared by direct compression, or a capsule.
The citalopram tablet that is marketed is a tablet made from granulated citalopram hydrobromide with various excipients.
We have found that escitalopram has significantly different solubility and salt formation properties from the citalopram racemate. For example, the only pharmaceutically crystalline salt known so far is the oxalate, whereas the citalopram racemate forms crystalline hydrobromide and hydrochloride salts as well.
Crystalline escitalopram hydrobromide has now been disclosed in W02004/056791 A1.
The escitalopram oxalate product prepared by crystallisation from acetone as outlined in US Patent No 4,943,590 has, as the citalopram hydrobromide product described above, a very small particle size around 2-20 ~,m resulting in similarly poor flow properties.
W003/000672 discloses a process for the preparation of racemic as well as enantiomerically pure citalopram from the compound R-4-[4-(dimethylamino)-1-(4'-fluorophenyl)-1-hydroxybutyl]-3-(hydroxymethyl)-benzonitrile by ring-closure under acidic conditions.
W003/011278 discloses crystalline particles of escitalopram oxalate with a particle size of at least 40~,m. Method for the manufacture of said crystalline particles and pharmaceutical compositions comprising said crystalline particles are also disclosed.
The inventors of the present invention have now surprisingly realised that the particle sizes obtained if escitalopram prepared according to the process disclosed in W003/000672 is precipitated as the oxalate salt according to the method disclosed in W003/01127~, are significantly smaller than those obtained from escitalopram prepared by ring-closure of S-4-[4-(dimethylamino)-1-(4'-fluorophenyl)-1-hydroxybutyl]-3-(hydroxymethyl)-benzonitrile via a labile ester under alkaline conditions and precipitated under otherwise identical precipitation conditions.
They have furthermore realised that the reduction in particle size of the escitalopram oxalate crystals is related to the presence of a specific impurity, Z-4-(4-dimethyl-amino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxymethyl-benzonitrile. This impurity is unique for the acidic ring-closure process as compared to the ring-closure via a labile ester under alkaline conditions.
l0 In view of the fact that direct compression is much simpler and cheaper than the processes involving granulation there is a continued desire for large crystals of escitalopram or pharmaceutical acceptable addition salts thereof.
Laboratory and full-scale research have now resulted in a new and inventive process producing large crystalline particles of escitalopram oxalate, i.e. particles of a size comparable to the size of the filler, by a novel and inventive process for reduction of the amount of Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxy-methyl-benzonitrile in the solution of escitalopram prior to crystallisation of the oxalate. Said particles are useful for the manufacture of directly compressed tablets.
Accurate dosing in capsules may also be with such large particles.
Objects of the Invention One aspect of the present invention is to provide crystalline particles of escitalopram oxalate with a broad particle size distribution, said particles being suitable for use in direct compression.
A second aspect of the invention is to provide large crystalline particles of 3o escitalopram oxalate comprising at least 0.01 % (w/w) of Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxymethyl-benzonitrile, said particles being suitable for use in direct compression.
A third aspect of the invention is to provide a novel pharmaceutical unit dosage form containing crystalline particles of escitalopram oxalate, wherein said particles have a broad particle size distribution and said unit dosage form may be a tablet, which preferably may be prepared by direct compression, or a capsule.
A fourth aspect of the invention is to provide a method for manufacture of large crystalline particles of escitalopram oxalate with a broad particle size distribution.
A fifth aspect of the invention is to provide a method for manufacture of large to crystalline particles of escitalopram oxalate comprising reduction of the amount of hydroxyl containing impurities in a solution of escitalopram and crystallising the resulting escitalopram as the oxalate salt.
A sixth aspect of the invention is to provide a method for reduction of the amount of hydroxyl containing impurities in a solution of citalopram or escitalopram.
Detailed description of the invention The invention then, inter alia, comprises the following alone or in combination:
Crystalline particles of escitalopram oxalate having a ratio between the median particle size and the particle size at the 95% quantile that is less than 0.42, preferably less than 0.40. Such particles are suitable for use in a solid unit dosage form.
Crystalline particles of escitalopram oxalate having a median particle size of at least 20 qm and a content of E- or Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxymethyl-benzonitrile of at least 0.01 % (w/w), preferably the median particle size of the crystals is at least 40 ~m and more preferred in the range of 50-200 ~.m.
Such particles are suitable for use in a solid unit dosage form.
Crystalline particles of escitalopram oxalate having a median particle size of at least 20 ~,m and being crystallised from a solution wherein the content of E- or Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3 -hydroxymethyl-benzonitrile prior to the crystallisation is at least 0.01 % (w/w) relative to escitalopram, preferably the median particle size of the crystals is at least 40 ~m and more preferred in the range of 50-200 Vim. Such particles are suitable for use in a solid unit dosage form.
A solid unit dosage form comprising crystalline particles of escitalopram oxalate wherein said crystalline particles of escitalopram oxalate are according to the invention as described above.
A solid unit dosage form comprising crystalline particles of escitalopram oxalate 1 o manufactured from crystalline particles of escitalopram oxalate according to the invention as described above.
A method for manufacture of crystalline particles of escitalopram oxalate which crystalline particles of escitalopram oxalate are as described above and said method comprises the steps of:
a) Treating a solution comprising escitalopram together with one or more hydroxyl containing impurities with a hydroxyl group scavenger, b) separating the escitalopram from the products resulting from reaction of said hydroxyl containing impurities with said hydroxyl group scavenger, 2o c) optionally transferring the escitalopram into its oxalate salt if the escitalopram is not already in the form of its oxalate salt, d) optionally transferring the escitalopram to a solvent system suitable for the crystallisation process if the escitalopram is not already in such a solvent system, and e) gradual cooling of the solution of escitalopram oxalate in said suitable solvent system from a first temperature to a second temperature while maintaining a controlled cooling profile and seeding said solution of escitalopram oxalate by addition of crystals of escitalopram oxalate during said cooling followed by a holding time at said second temperature.
A method for manufacture of crystalline particles of escitalopram oxalate which crystalline particles of escitalopram oxalate are as described above and said method comprises gradual cooling of a solution of escitalopram oxalate in a suitable solvent system from a first temperature to a second temperature while maintaining a controlled cooling profile and seeding said solution of escitalopram oxalate by addition of crystals of escitalopram oxalate during said cooling followed by a holding time at said second temperature wherein said solution of escitalopram comprises at least 1 ppm, particularly at least 10 ppm, and more particularly at least 0.01 % by weight of E- or Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxy-methyl-benzonitrile relative to the total weight of the crystallisation batch.
A method for reducing the amount of hydroxyl containing impurities in citalopram or l0 escitalopram comprising the steps of:
a) Treating a solution comprising citalopram or escitalopram together with one or more such impurities with a hydroxyl group scavenger and b) separating said citalopram or escitalopram from the products resulting from reaction of said hydroxyl containing impurities with said hydroxyl group scavenger.
The direct compression of escitalopram, a filler and other pharmaceutically acceptable excipients into tablets has the great advantage, that the granulation and a drying step are avoided. Further, as the granulation step is avoided, it is no longer necessary to add a binding agent.
As used herein, "escitalopram oxalate" means any addition salt consisting of escitalopram, oxalic acid and optionally water. Examples of such salts are the hydrogen oxalate salt of escitalopram, i.e. the salt consisting of one molecule of escitalopram per molecule of oxalic acid, as well as the oxalate salt of escitalopram, i.e. the salt consisting of two molecules of escitalopram per molecule of oxalic acid.
As used herein, "crystalline particles" means any combination of single crystals, aggregates and agglomerates.
As used herein, "direct compression" means that the solid unit dosage form is prepared by compression of a simple mixture of the active ingredient and excipients, without the active ingredient having been subjected to an intermediate granulation process in order to embed it in a larger particle and improve its fluidity properties.
As used herein, "binder" means an agent, which is used in wet or melt granulation processes and acts as a binder in the granulated product.
As used herein, "particle size distribution" means the cumulative volume size distribution of equivalent spherical diameters as determined by laser diffraction at 1 bar dispersive pressure in a Sympatec Helos equipment. "Median particle size"
to "MPS" and "X50" refer, correspondingly, each to the median or 50% quantile of said particle size distribution. "X10" and "X95" refer, correspondingly, to the 10%
respectively the 95% quantile. "X10/X50" and "X50/X95" refer to the ratio between X10 and X50 respectively~X50 and X95.
Particle size distributions may be unimodal, i. e. the density volume size distribution contains only one peak, bimodal, i. e. the density volume size distribution contains two peaks, or polymodal, i. e. the density volume size distribution contains more than two peaks. Particle size distributions may be bimodal or multimodal inter alia if the crystalline particles is a mixture of single crystals and aggregates or agglomerates.
As used herein, "refluxing temperature" means the temperature at which the solvent or solvent system refluxes or boils at atmospheric pressure.
As used herein, "cooling profile" means the temperature of the crystallisation batch as a function of time.
As used herein, "cooling rate" means the decrease in temperature per time unit.
As used herein, "hydroxyl group scavenger" means a molecule or reactant, which is able to react with a hydroxyl group and transform it into another substituent.
The hydroxyl group scavenger is preferably selected such that the substituent, which the hydroxyl group is transformed into, facilitates separation of the transformed molecule or impurity from the escitalopram or citalopram. The hydroxyl group scavenger is preferably selected among those reacting fast with hydroxyl groups under mild conditions without affecting citalopram or escitalopram. Examples of hydroxyl group scavengers are cyclic anhydrides, POC13, PC15, POBr3, PBrs, POI3, PIS, BCl3, BBr3 and BI3, which all will introduce an acidic group into the impurity molecule whereupon it may be separated from citalopram and/or escitalopram by extraction into an alkaline aqueous solution from an organic solvent.
Thus in one embodiment of the present invention the crystalline particles of escitalopram oxalate have a median particle size of at least 20 Vim, in particular of at l0 least 40 Vim, and preferably in the range of 50 - 200 Vim.
Thus in a particular embodiment of the present invention the particle size distribution of the crystalline particles of escitalopram oxalate is bimodal or polymodal and the peak at the lowest particle size is located at a particle size of at least 20 ~,m, in particular of at least 40 Vim, and preferably in the range of 50 - 200 Vim.
In one embodiment, the escitalopram oxalate crystals comprise at least 0.01 %
(w/w) relative to escitalopram of E- or Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxymethyl-benzonitrile. In particular embodiments the amount of E- or 2o Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxymethyl-benzonitrile in the crystals is in the range of 0.01 to 0.3%, more particularly 0.02 to 0.2%, and most particularly 0.03 to 0.1%.
In a particular embodiment, the hydroxyl containing impurity is Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxymethyl-benzonitrile.
In another particular embodiment, the hydroxyl containing impurity is E-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3 -hydroxymethyl-benzonitrile.
Flow, segregation and demixing properties and, hence, the suitability of the escitalopram oxalate crystals for direct compression depends, besides the median particle size, on the particle side distribution. It may for certain purposes such as wet granulation be advantageously to have a broad particle size distribution.
Small particles may dissolve during wet granulation and then solidify between the larger crystals upon drying and hence impart strength to the granulate. Further, in certain tabletting processes such as dry granulation (compaction) it may be desirable to have a broader particle size distribution so as to increase the packing efficiency of the 5 particles, and thus the inherent binding capability.
Another aspect of the invention is to provide a method for reduction of the amount of hydroxyl containing impurities in citalopram, escitalopram or a non-racemic mixture of R- and S-citalopram. Citalopram, escitalopram or a non-racemic mixture of R-and to S-citalopram containing a hydroxyl group containing impurity such as E- or Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3 -hydroxymethyl-benzonitrile is dissolved in a suitable solvent such as dry toluene. A hydroxyl group scavenger, such as a cyclic anhydride e.g. succinic anhydride in amount sufficient to scavenge the hydroxyl group containing impurity is added to the solution and the mixture is stirred at a suitable temperature, e.g. 45 °C, for a suitable period, e.g. 120 minutes.
The impurity is then separated from the citalopram, escitalopram or non-racemic mixture of R- and S-citalopram in a suitable way. Those skilled in the art will know such ways. If the impurity is transformed into an acidic compound, e.g. by reaction with a cyclic anhydride, preferably a cyclic C4_$-anhydride, more preferred succinic 2o anhydride, the separation may be done by partitioning between the organic solvent and an aqueous phase, in particular by partitioning between the organic solvent and an alkaline aqueous phase. Water and a base, such as aqueous ammonia are added to a suitable pH, e.g. pH = 10,5-11,0. The phases are separated and the organic phase is washed with water. The organic phase is evaporated to yield the citalopram, escitalopram or non-racemic mixture of R- and S-citalopram.
In a particular embodiment the invention provides a method for reduction of the amount of hydroxyl containing impurities in citalopram.
3o In another equally particular embodiment the invention provides a method for reduction of the amount of hydroxyl containing impurities in escitalopram.
In yet another equally particular embodiment the invention provides a method for reduction of the amount of hydroxyl containing impurities in a non-racemic mixture of R- and S-citalopram.
In another aspect of the present invention crystalline particles of escitalopram oxalate as described above and suitable for use in a solid unit dosage form are crystallised from a solution of escitalopram oxalate in a suitable solvent system. Such crystalline particles may ihte~ alia have a ratio between the median particle size and the particle size at the 95% quantile that is less than 0.42, preferably less than 0.40;
and/or have a l0 median particle size of at least 20 Vim, preferably at least 20 ~.m and more preferred in the range of 50 - 200 wm. In a particular embodiment such crystalline particles have a median particle size of at least 20 ~m and a content of E- or Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxymethyl-benzonitrile of at least 0.01%
(w/w) Said solvent system may comprise one or more alcohols and optionally water, preferably the solvent system is ethanol. Escitalopram oxalate is preferably dissolved in the solvent system at a temperature in the range between 50 °C and the refluxing temperature of the solvent system, preferably between 60 °C and the refluxing temperature and more preferred between 70 °C and the refluxing temperature, suitably the escitalopram oxalate is dissolved at the refluxing temperature. The amounts of 2o pharmaceutically acceptable salt of escitalopram and solvent used are preferably corresponding to a solute:solvent weight ratio in the range of 0.05:1 to 0.6:1, more preferred 0.1:1 to 0.5:1 and most preferred 0.2:1 to 0.4:1. The solution of escitalopram oxalate is gradually cooled down to the temperature, at which the crystals will be isolated from the mother liquor, in the range of 0-20 °C, preferably 0-15 °C, and more preferred 7-15 °C maintaining a controlled cooling profile so that the cooling rate in an initial cooling period does not exceed 0.6 °C/min, and preferably the cooling rate is lcept within the range of 0.2 - 0.4 °C/min, and said initial cooling period extends until the temperature of the crystallisation batch is below 60 °C, preferably below 50 °C
and more preferred below 40 °C, suitably the cooling rate may be kept in this range 3o for the entire cooling. The crystallisation batch is seeded by addition of crystals of escitalopram oxalate at least once during the cooling time in order to avoid excessive supersaturation with respect to escitalopram oxalate and resulting spontaneous crystallisation into small crystalline particles. The seeding is preferably repeated in order to ensure constant presence of crystalline escitalopram oxalate during the cooling; suitably the crystallisation batch is seeded semicontinuosly until crystallisation has started. The crystallisation batch is optionally kept at said second temperature for a holding time during which there may occur crystal growth. In a particular embodiment said holding time is at least 1 hour, preferably in the range of 4 to 24 hours and more preferred 6 to 12 hours. Finally, the crystalline particles of escitalopram oxalate are isolated from the mother liquor using conventional separation techniques, e.g. filtration.
to In a particular embodiment, the solution from which the escitalopram oxalate is crystallised comprises at least 0.01 % of E- or Z-4-(4-dimethylamino-1-(4-fluoro-phenyl)-but-1-enyl)-3-hydroxymethyl-benzonitrile. In particular embodiments the amount of E- or Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxy-methylbenzonitrile in the crystals is in the range of 0.01 to 0.5%, more particularly 0.01 to 0.3%, even more particularly 0.02 to 0.2%, and most particularly 0.03 to 0.1%.
In a particular embodiment, the hydroxyl containing impurity is Z-4-(4-dimethyl-amino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxymethyl-benzonitrile.
In another particular embodiment, the hydroxyl containing impurity is E-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3 -hydroxymethyl-benzonitrile.
The escitalopram, which is to be crystallised as escitalopram oxalate, is in another particular embodiment the product of a method of manufacture comprising the method described above for reduction of the content hydroxyl group containing impurities by reaction with a hydroxyl group scavenger.
The methods described above for reduction of the amount of hydroxyl group containing impurities and crystallisation may be combined with each other and/or with the process for the preparation of racemic citalopram and/or S- or R-citalopram by separation of a mixture of R- and S-citalopram with more than 50 % of one of the enantiomers into a fraction of racemic citalopram and/or a fiaction of S-citalopram or R-citalopram containing low amounts of the other enantiomer as disclosed in W003/000672 which is hereby included by reference.
Such combinations include but are not limited to: hydroxyl scavenging followed by crystallisation of escitalopram oxalate; hydroxyl scavenging followed by separation of racemic citalopram and escitalopram followed by crystallisation of escitalopram oxalate; separation of racemic citalopram and escitalopram followed by hydroxyl scavenging followed by crystallisation of escitalopram oxalate; and separation of racemic citalopram and escitalopram followed by crystallisation of escitalopram oxalate.
In one embodiment of the invention the escitalopram is manufactured by a process comprising ring-closure of R-4-[4-(dimethylamino)-1-(4'-fluorophenyl)-1-hydroxy-butyl]-3-(hydroxymethyl)-benzonitrile under acidic conditions as disclosed in W003/000672 which is hereby included by reference.
In one embodiment of the invention, the present invention relates to a tablet prepared from a mixture of crystalline particles of escitalopram oxalate and pharmaceutically acceptable excipients wherein said crystalline particles of escitalopram oxalate are 2o according to the invention as described above. Such tablets may be made by one of the following tabletting methods: Direct compression, dry granulation (compaction), wet granulation or melt granulation. In a particular embodiment, the tablet is prepared by direct compression. In another particular embodiment, the tablet is prepared by dry granulation (compaction). In yet another particular embodiment, the tablet is prepared by wet granulation. In yet another particular embodiment, the tablet is prepared by melt granulation.
In a particular embodiment the tablet is coated.
3o In another embodiment, the present invention relates to a solid unit dosage form prepared by filling a mixture of crystalline particles of escitalopram oxalate and pharmaceutically acceptable excipients into a capsule wherein said crystalline particles of escitalopram oxalate are according to the invention as described above, preferably the capsule is a hard gelatine capsule.
Preferably, the solid unit dosage forms according to the invention do not contain a binder.
The solid unit dosage form according to the invention may contain 1-60% w/w active ingredient calculated as escitalopram base, particularly 4-40% w/w active ingredient calculated as escitalopram base, evenly particularly 1-30% w/w active ingredient to calculated as escitalopram base, more particularly 4-20% w/w active ingredient calculated as escitalopram base and most particularly 6-10% w/w active ingredient calculated as escitalopram base. Suitably, the solid unit dosage form of the invention contains 8% w/w active ingredient calculated as escitalopram base.
The solid unit dosage form according to the invention may contain a filler selected from lactose, or other sugars e.g. sorbitol, mannitol, dextrose and sucrose, calcium phosphates (dibasic, tribasic, hydrous and anhydrous), starch, modified starches, microcrystalline cellulose, calciwn sulphate and/or calcium carbonate. In a preferred embodiment, the solid unit dosage form of the invention does not contain lactose.
Suitably the filler is a microcrystalline cellulose such as ProSolv SMCC90 manufactured by Penwest Pharmaceuticals or Avicel PH 200 manufactured by FMC
Corporation.
Besides the active ingredient and filler, the solid pharmaceutical unit dosage forms may include various other conventional excipients such as disintegrants and optionally minor amounts of lubricants, colorants and sweeteners.
Lubricants used according to the invention may suitably be one or more selected from 3o the group comprising metallic stearates (magnesium, calcium, sodium), stearic acid, wax, hydrogenated vegetable oil, talc and colloidal silica.
Preferably the lubricant is one or more selected from the group comprising talc, magnesium stearate or calcium stearate. Suitably the lubricant is a combination of talc and magnesium stearate. The weight percent of magnesium stearate in the solid unit dosage form is preferably in the range of 0.4% to 2%, and more preferred in the range 5 of 0.7% to 1.4%.
In a particular embodiment the solid unit dosage form is substantially free of lactose.
Disintegrants include sodium starch glycolate, croscarmellose, crospovidone, low l0 substituted hydroxypropylcellulose, modified cornstarch, pregelatizined starch and natural starch. Suitably the disintegrant is crosscarmellose such Ac-Di-Sol manufactured by FMC.
Optionally the solid, pharmaceutical unit dosage form of the invention may be coated.
15 Suitably the coating is a film coating based on conventional coating mixtures such as Opadry OY-S-28849, white manufactured by Colorcon.
The solid, pharmaceutical unit dosage form of the invention may be prepared by conventional methods using a tablet press with forced feed capability.
The filled, hard gelatine capsule of the invention may be prepared by conventional methods using a capsule filler suitable for powder filling.
Examples In the following, the invention is illustrated by way of examples. However, the examples are merely intended to illustrate the invention and should not be construed as limiting.
Example 1 Scavenging of hydroxyl containing impurity by succinic anhydride A mixture of R- and S-Citalopram (55,5 g) containing 0,6% of Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxymethyl-benzonitrile is dissolved in dry toluene (145,0 g). Succinic anhydride (0,5 g) is added to the solution and the mixture is stirred at 45 °C (120 minutes). Water (230 ml) and aqueous ammonia (25% by weight) (3 ml) is added (pH = 10,5-11,0). The phases are separated and the toluene phase is washed with water (3 x 120 ml). The toluene phase is evaporated and the yield is 53,0 g (95%). The product contains 0,06% of Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3 -hydroxymethyl-benzonitrile.
Example 2 Production scale crystallisation of escitalopram oxalate to A large number of batches of crude escitalopram oxalate have been recrystallised in production scale according to the procedure described below. The batches comprises:
a) Escitalopram prepared by acidic ring-closure of the R-form of the diol precursor as described in W003/000672 followed by scavenging of hydroxyl containing impurity by a production scale version of the process described in example 1 followed by separation of racemic citalopram and escitalopram as described in W003/000672. These batches contain Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxymethyl-benzonitrile, typically in the range of 0.05%
(w/w) relative to escitalopram. These batches are referred to as R-diol batches.
2o b) Escitalopram prepared by ring-closure of the S-form of the diol precursor via an activated ester under alkaline conditions as described in US Patent No.
4,943,590.
These batches do not contain Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxymethyl-benzonitrile. These batches are referred to as S-diol batches.
Production procedure:
100 lcg to 300 kg, of crude escitalopram oxalate is charged to a first reactor, R1. 4,1 -4,3 L ethanol per kg crude escitalopram oxalate is charged to Rl. The solution is mixed and heated to the boiling point (~80°C). When every thing is dissolved the solution is transferred through a filter to a second reactor, R2.
The agitator on R2 is started (40-60 rpm) and the solution is heated to the boiling point once again. When everything is dissolved in R2, the automatic cooling is started and the solution is cooled gradually according to the cooling rates in table 1.
Table 1: Cooling rate setpoints for automatic cooling during recrystallisation of escitalopram oxalate Interval Rate [C/min]
[C]
Above 0.151 70.0 70.0 66.0 0.250 -66.0 60.0 0.300 -60.0 56.4 0.327 -56.4 52.0 0.400 -52.0 - 47.60.550 47.6 - 35.00.700 35.0 -10.0 0.830 The solution is seeded with 0.02 - 0.04 kg, escitalopram oxalate for every 3 °C the temperature is decreased until crystallization is noticed. The solution is automatically 1o cooled until 15 °C.
The suspension is pumped to a filter dryer, where it is washed and dried. If the suspension is not transferred immediately the temperature must be kept at 0 -15 °C.
The filter calve is dried by vacuum. When the cake is dry, it is washed with 1,1 - 1,2 L
ethanol per kg crude escitalopram oxalate charged. The cake is dried once again and the calve is heated for final drying for approximately 12 hours. Temperature =
60 °C, pressure < 0.13 Bar (abs.).
The filter dryer is emptied and the escitalopram oxalate is sent to deagglomeration, for deagglomeration of agglomerates formed during drying of the crystals. The dried escitalopram oxalate is milled to separate the crystals from each other.
During the milling the size and shape of the individual crystals is not changed.
The resulting escitalopram oxalate batches had particle characteristics as shown in table 2.
Table 2: Particle characteristics for escitalopram oxalate crystals.
S-diol R-diol batches batches Batch X50 X10/X50 X50/X95Batch X50 X10IX50X501X95 1 171 0,13 0,44 47 93 0,12 0,33 2 153 0,07 0,43 48 91 0,11 0,33 3 158 0,09 0,43 49 74 0,11 0,26 4 171 0,15 0,44 50 116 0,14 0,39 166 0,10 0,47 51 74 0,09 0,29 6 165 0,13 0,46 52 93 0,11 0,38 7 163 0,10 0,47 53 92 0,17 0,38 8 171 0,15 0,44 54 90 0,20 0,37 9 171 0,15 0,47 55 108 0,09 0,39 166 0,11 0,47 56 100 0,09 0,39 11 174 0,11 0,46 57 98 0,08 0,36 12 162 0,07 0,44 58 102 0,09 0,33 13 180 0,11 0,46 59 76 0,11 0,30 14 165 0,11 0,44 60 92 0,10 0,36 178 0,13 0,48 61 96 0,08 0,35 16 162 0,12 0,47 17 138 0,14 0,43 18 168 0,11 0,44 19 166 0,11 0,46 160 0,12 0,44 21 121 0,07 0,36 22 141 0,08 0,41 23 166 0,08 0,43 24 126 0,08 0,42 123 0,09 0,42 26 159 0,11 0,44 27 156 0,12 0,46 28 147 0,12 0,46 29 169 0,12 0,47 181 0,08 0,44 31 147 0,07 0,39 32 184 0,09 0,45 33 173 0,10 0,43 34 161 0,09 0,42 171 0,11 0,44 36 159 0,12 0,43 37 160 0,13 0,45 38 157 0,11 0,45 3g 153 0,08 0,44 163 0,10 0,44 41 157 0,11 0,45 42 156 0,12 0,45 43 129 0,10 0,40 44 139 0,12 0,40 150 0,12 0,42 46 195 0,09 0,46 Comparative Example 1 A wet filter cake obtained by precipitation of crude escitalopram oxalate by mixing of ethanolic solutions of escitalopram prepared by ring-closure via a labile ester under to alkaline conditions and oxalic acid, respectively, and containing approximately 35 kg escitalopram oxalate was suspended in 322 L ethanol. The material was dissolved by heating to reflux, and 150 L ethanol was removed by distillation. Cooling was applied, and the mixture was cooled from reflux to 15 °C with a cooling rate between 0.2 and 0.5 °C/min in the temperature interval 80 to 40 °C.
During cooling, the mixture was seeded with escitalopram oxalate at 75, 65 and 60 °C (10 g each time).
The crystallisation mixture was kept at 15 °C for 10 hours before the crystalline escitalopram oxalate was isolated. Purified escitalopram oxalate (27.7 kg, 79%) was obtained by filtration of the crystallisation mixture, washing with ethanol and drying of the filter cake. Particle size distribution for the resulting escitalopram oxalate is listed in table 3.
Table 3: Particle size distribution (Sympatec Helos) for escitalopram oxalate crystals and ProSolv SMCC90 Quantile Comparative ExampleProSolv SMCC90 (%) 1 (gym) (N~m) Comparative Example 2 Tablet prepared by direct compression of large crystalline particles of escitalopram oxalate.
Tablet ingredients:
Tablet core Escitalopram oxalate 2554 ~ (10.2 %
w/w) 1 o Talc 14_ 00 ~ (5.6 % w/w) ProSolv SMCC90 19896 ~ (79.6 %
w/w) Ac-Di-Sol 9_ 00 ~ (3.6 Magnesium stearate 250 ~ (1.0 % w/w) 15 Film coating Opadry OY-S-28849, white 625 ~ (2.5 % w/w of core weight) Crystalline particles of escitalopram oxalate from example 1 and talc were sieved through 710 ~m screen and blended at 6 rpm for 15 min in a 100 litre Bohle PTM
2o mixer. ProSolv SMCC90 and Ac-Di-Sol were added and blending continued for min. Magnesium stearate was sieved through 710 ~m screen and added and blending continued for 3 min.
kg of the resulting mixture was tabletted (125.000 tablets/hour) on a Korsch PH
25 230 tablet press fitted with oblong, embossed, scored 5,5 x 8 mm punches.
Tablet core weight was set to 125 mg. The nominal yield was 200.000 tablets. The tablet press was run until the mixture level was just above the forced feeder, i.e. the tabletting was continued as long as possible in order to identify possible segregation tendencies in the last quantities of mixture. The tablets produced had satisfactory technical properties.
Those skilled in the art will easily realise that crystals according to the invention can be used in the manufacture of tablets in similar ways.
A fifth aspect of the invention is to provide a method for manufacture of large to crystalline particles of escitalopram oxalate comprising reduction of the amount of hydroxyl containing impurities in a solution of escitalopram and crystallising the resulting escitalopram as the oxalate salt.
A sixth aspect of the invention is to provide a method for reduction of the amount of hydroxyl containing impurities in a solution of citalopram or escitalopram.
Detailed description of the invention The invention then, inter alia, comprises the following alone or in combination:
Crystalline particles of escitalopram oxalate having a ratio between the median particle size and the particle size at the 95% quantile that is less than 0.42, preferably less than 0.40. Such particles are suitable for use in a solid unit dosage form.
Crystalline particles of escitalopram oxalate having a median particle size of at least 20 qm and a content of E- or Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxymethyl-benzonitrile of at least 0.01 % (w/w), preferably the median particle size of the crystals is at least 40 ~m and more preferred in the range of 50-200 ~.m.
Such particles are suitable for use in a solid unit dosage form.
Crystalline particles of escitalopram oxalate having a median particle size of at least 20 ~,m and being crystallised from a solution wherein the content of E- or Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3 -hydroxymethyl-benzonitrile prior to the crystallisation is at least 0.01 % (w/w) relative to escitalopram, preferably the median particle size of the crystals is at least 40 ~m and more preferred in the range of 50-200 Vim. Such particles are suitable for use in a solid unit dosage form.
A solid unit dosage form comprising crystalline particles of escitalopram oxalate wherein said crystalline particles of escitalopram oxalate are according to the invention as described above.
A solid unit dosage form comprising crystalline particles of escitalopram oxalate 1 o manufactured from crystalline particles of escitalopram oxalate according to the invention as described above.
A method for manufacture of crystalline particles of escitalopram oxalate which crystalline particles of escitalopram oxalate are as described above and said method comprises the steps of:
a) Treating a solution comprising escitalopram together with one or more hydroxyl containing impurities with a hydroxyl group scavenger, b) separating the escitalopram from the products resulting from reaction of said hydroxyl containing impurities with said hydroxyl group scavenger, 2o c) optionally transferring the escitalopram into its oxalate salt if the escitalopram is not already in the form of its oxalate salt, d) optionally transferring the escitalopram to a solvent system suitable for the crystallisation process if the escitalopram is not already in such a solvent system, and e) gradual cooling of the solution of escitalopram oxalate in said suitable solvent system from a first temperature to a second temperature while maintaining a controlled cooling profile and seeding said solution of escitalopram oxalate by addition of crystals of escitalopram oxalate during said cooling followed by a holding time at said second temperature.
A method for manufacture of crystalline particles of escitalopram oxalate which crystalline particles of escitalopram oxalate are as described above and said method comprises gradual cooling of a solution of escitalopram oxalate in a suitable solvent system from a first temperature to a second temperature while maintaining a controlled cooling profile and seeding said solution of escitalopram oxalate by addition of crystals of escitalopram oxalate during said cooling followed by a holding time at said second temperature wherein said solution of escitalopram comprises at least 1 ppm, particularly at least 10 ppm, and more particularly at least 0.01 % by weight of E- or Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxy-methyl-benzonitrile relative to the total weight of the crystallisation batch.
A method for reducing the amount of hydroxyl containing impurities in citalopram or l0 escitalopram comprising the steps of:
a) Treating a solution comprising citalopram or escitalopram together with one or more such impurities with a hydroxyl group scavenger and b) separating said citalopram or escitalopram from the products resulting from reaction of said hydroxyl containing impurities with said hydroxyl group scavenger.
The direct compression of escitalopram, a filler and other pharmaceutically acceptable excipients into tablets has the great advantage, that the granulation and a drying step are avoided. Further, as the granulation step is avoided, it is no longer necessary to add a binding agent.
As used herein, "escitalopram oxalate" means any addition salt consisting of escitalopram, oxalic acid and optionally water. Examples of such salts are the hydrogen oxalate salt of escitalopram, i.e. the salt consisting of one molecule of escitalopram per molecule of oxalic acid, as well as the oxalate salt of escitalopram, i.e. the salt consisting of two molecules of escitalopram per molecule of oxalic acid.
As used herein, "crystalline particles" means any combination of single crystals, aggregates and agglomerates.
As used herein, "direct compression" means that the solid unit dosage form is prepared by compression of a simple mixture of the active ingredient and excipients, without the active ingredient having been subjected to an intermediate granulation process in order to embed it in a larger particle and improve its fluidity properties.
As used herein, "binder" means an agent, which is used in wet or melt granulation processes and acts as a binder in the granulated product.
As used herein, "particle size distribution" means the cumulative volume size distribution of equivalent spherical diameters as determined by laser diffraction at 1 bar dispersive pressure in a Sympatec Helos equipment. "Median particle size"
to "MPS" and "X50" refer, correspondingly, each to the median or 50% quantile of said particle size distribution. "X10" and "X95" refer, correspondingly, to the 10%
respectively the 95% quantile. "X10/X50" and "X50/X95" refer to the ratio between X10 and X50 respectively~X50 and X95.
Particle size distributions may be unimodal, i. e. the density volume size distribution contains only one peak, bimodal, i. e. the density volume size distribution contains two peaks, or polymodal, i. e. the density volume size distribution contains more than two peaks. Particle size distributions may be bimodal or multimodal inter alia if the crystalline particles is a mixture of single crystals and aggregates or agglomerates.
As used herein, "refluxing temperature" means the temperature at which the solvent or solvent system refluxes or boils at atmospheric pressure.
As used herein, "cooling profile" means the temperature of the crystallisation batch as a function of time.
As used herein, "cooling rate" means the decrease in temperature per time unit.
As used herein, "hydroxyl group scavenger" means a molecule or reactant, which is able to react with a hydroxyl group and transform it into another substituent.
The hydroxyl group scavenger is preferably selected such that the substituent, which the hydroxyl group is transformed into, facilitates separation of the transformed molecule or impurity from the escitalopram or citalopram. The hydroxyl group scavenger is preferably selected among those reacting fast with hydroxyl groups under mild conditions without affecting citalopram or escitalopram. Examples of hydroxyl group scavengers are cyclic anhydrides, POC13, PC15, POBr3, PBrs, POI3, PIS, BCl3, BBr3 and BI3, which all will introduce an acidic group into the impurity molecule whereupon it may be separated from citalopram and/or escitalopram by extraction into an alkaline aqueous solution from an organic solvent.
Thus in one embodiment of the present invention the crystalline particles of escitalopram oxalate have a median particle size of at least 20 Vim, in particular of at l0 least 40 Vim, and preferably in the range of 50 - 200 Vim.
Thus in a particular embodiment of the present invention the particle size distribution of the crystalline particles of escitalopram oxalate is bimodal or polymodal and the peak at the lowest particle size is located at a particle size of at least 20 ~,m, in particular of at least 40 Vim, and preferably in the range of 50 - 200 Vim.
In one embodiment, the escitalopram oxalate crystals comprise at least 0.01 %
(w/w) relative to escitalopram of E- or Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxymethyl-benzonitrile. In particular embodiments the amount of E- or 2o Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxymethyl-benzonitrile in the crystals is in the range of 0.01 to 0.3%, more particularly 0.02 to 0.2%, and most particularly 0.03 to 0.1%.
In a particular embodiment, the hydroxyl containing impurity is Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxymethyl-benzonitrile.
In another particular embodiment, the hydroxyl containing impurity is E-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3 -hydroxymethyl-benzonitrile.
Flow, segregation and demixing properties and, hence, the suitability of the escitalopram oxalate crystals for direct compression depends, besides the median particle size, on the particle side distribution. It may for certain purposes such as wet granulation be advantageously to have a broad particle size distribution.
Small particles may dissolve during wet granulation and then solidify between the larger crystals upon drying and hence impart strength to the granulate. Further, in certain tabletting processes such as dry granulation (compaction) it may be desirable to have a broader particle size distribution so as to increase the packing efficiency of the 5 particles, and thus the inherent binding capability.
Another aspect of the invention is to provide a method for reduction of the amount of hydroxyl containing impurities in citalopram, escitalopram or a non-racemic mixture of R- and S-citalopram. Citalopram, escitalopram or a non-racemic mixture of R-and to S-citalopram containing a hydroxyl group containing impurity such as E- or Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3 -hydroxymethyl-benzonitrile is dissolved in a suitable solvent such as dry toluene. A hydroxyl group scavenger, such as a cyclic anhydride e.g. succinic anhydride in amount sufficient to scavenge the hydroxyl group containing impurity is added to the solution and the mixture is stirred at a suitable temperature, e.g. 45 °C, for a suitable period, e.g. 120 minutes.
The impurity is then separated from the citalopram, escitalopram or non-racemic mixture of R- and S-citalopram in a suitable way. Those skilled in the art will know such ways. If the impurity is transformed into an acidic compound, e.g. by reaction with a cyclic anhydride, preferably a cyclic C4_$-anhydride, more preferred succinic 2o anhydride, the separation may be done by partitioning between the organic solvent and an aqueous phase, in particular by partitioning between the organic solvent and an alkaline aqueous phase. Water and a base, such as aqueous ammonia are added to a suitable pH, e.g. pH = 10,5-11,0. The phases are separated and the organic phase is washed with water. The organic phase is evaporated to yield the citalopram, escitalopram or non-racemic mixture of R- and S-citalopram.
In a particular embodiment the invention provides a method for reduction of the amount of hydroxyl containing impurities in citalopram.
3o In another equally particular embodiment the invention provides a method for reduction of the amount of hydroxyl containing impurities in escitalopram.
In yet another equally particular embodiment the invention provides a method for reduction of the amount of hydroxyl containing impurities in a non-racemic mixture of R- and S-citalopram.
In another aspect of the present invention crystalline particles of escitalopram oxalate as described above and suitable for use in a solid unit dosage form are crystallised from a solution of escitalopram oxalate in a suitable solvent system. Such crystalline particles may ihte~ alia have a ratio between the median particle size and the particle size at the 95% quantile that is less than 0.42, preferably less than 0.40;
and/or have a l0 median particle size of at least 20 Vim, preferably at least 20 ~.m and more preferred in the range of 50 - 200 wm. In a particular embodiment such crystalline particles have a median particle size of at least 20 ~m and a content of E- or Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxymethyl-benzonitrile of at least 0.01%
(w/w) Said solvent system may comprise one or more alcohols and optionally water, preferably the solvent system is ethanol. Escitalopram oxalate is preferably dissolved in the solvent system at a temperature in the range between 50 °C and the refluxing temperature of the solvent system, preferably between 60 °C and the refluxing temperature and more preferred between 70 °C and the refluxing temperature, suitably the escitalopram oxalate is dissolved at the refluxing temperature. The amounts of 2o pharmaceutically acceptable salt of escitalopram and solvent used are preferably corresponding to a solute:solvent weight ratio in the range of 0.05:1 to 0.6:1, more preferred 0.1:1 to 0.5:1 and most preferred 0.2:1 to 0.4:1. The solution of escitalopram oxalate is gradually cooled down to the temperature, at which the crystals will be isolated from the mother liquor, in the range of 0-20 °C, preferably 0-15 °C, and more preferred 7-15 °C maintaining a controlled cooling profile so that the cooling rate in an initial cooling period does not exceed 0.6 °C/min, and preferably the cooling rate is lcept within the range of 0.2 - 0.4 °C/min, and said initial cooling period extends until the temperature of the crystallisation batch is below 60 °C, preferably below 50 °C
and more preferred below 40 °C, suitably the cooling rate may be kept in this range 3o for the entire cooling. The crystallisation batch is seeded by addition of crystals of escitalopram oxalate at least once during the cooling time in order to avoid excessive supersaturation with respect to escitalopram oxalate and resulting spontaneous crystallisation into small crystalline particles. The seeding is preferably repeated in order to ensure constant presence of crystalline escitalopram oxalate during the cooling; suitably the crystallisation batch is seeded semicontinuosly until crystallisation has started. The crystallisation batch is optionally kept at said second temperature for a holding time during which there may occur crystal growth. In a particular embodiment said holding time is at least 1 hour, preferably in the range of 4 to 24 hours and more preferred 6 to 12 hours. Finally, the crystalline particles of escitalopram oxalate are isolated from the mother liquor using conventional separation techniques, e.g. filtration.
to In a particular embodiment, the solution from which the escitalopram oxalate is crystallised comprises at least 0.01 % of E- or Z-4-(4-dimethylamino-1-(4-fluoro-phenyl)-but-1-enyl)-3-hydroxymethyl-benzonitrile. In particular embodiments the amount of E- or Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxy-methylbenzonitrile in the crystals is in the range of 0.01 to 0.5%, more particularly 0.01 to 0.3%, even more particularly 0.02 to 0.2%, and most particularly 0.03 to 0.1%.
In a particular embodiment, the hydroxyl containing impurity is Z-4-(4-dimethyl-amino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxymethyl-benzonitrile.
In another particular embodiment, the hydroxyl containing impurity is E-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3 -hydroxymethyl-benzonitrile.
The escitalopram, which is to be crystallised as escitalopram oxalate, is in another particular embodiment the product of a method of manufacture comprising the method described above for reduction of the content hydroxyl group containing impurities by reaction with a hydroxyl group scavenger.
The methods described above for reduction of the amount of hydroxyl group containing impurities and crystallisation may be combined with each other and/or with the process for the preparation of racemic citalopram and/or S- or R-citalopram by separation of a mixture of R- and S-citalopram with more than 50 % of one of the enantiomers into a fraction of racemic citalopram and/or a fiaction of S-citalopram or R-citalopram containing low amounts of the other enantiomer as disclosed in W003/000672 which is hereby included by reference.
Such combinations include but are not limited to: hydroxyl scavenging followed by crystallisation of escitalopram oxalate; hydroxyl scavenging followed by separation of racemic citalopram and escitalopram followed by crystallisation of escitalopram oxalate; separation of racemic citalopram and escitalopram followed by hydroxyl scavenging followed by crystallisation of escitalopram oxalate; and separation of racemic citalopram and escitalopram followed by crystallisation of escitalopram oxalate.
In one embodiment of the invention the escitalopram is manufactured by a process comprising ring-closure of R-4-[4-(dimethylamino)-1-(4'-fluorophenyl)-1-hydroxy-butyl]-3-(hydroxymethyl)-benzonitrile under acidic conditions as disclosed in W003/000672 which is hereby included by reference.
In one embodiment of the invention, the present invention relates to a tablet prepared from a mixture of crystalline particles of escitalopram oxalate and pharmaceutically acceptable excipients wherein said crystalline particles of escitalopram oxalate are 2o according to the invention as described above. Such tablets may be made by one of the following tabletting methods: Direct compression, dry granulation (compaction), wet granulation or melt granulation. In a particular embodiment, the tablet is prepared by direct compression. In another particular embodiment, the tablet is prepared by dry granulation (compaction). In yet another particular embodiment, the tablet is prepared by wet granulation. In yet another particular embodiment, the tablet is prepared by melt granulation.
In a particular embodiment the tablet is coated.
3o In another embodiment, the present invention relates to a solid unit dosage form prepared by filling a mixture of crystalline particles of escitalopram oxalate and pharmaceutically acceptable excipients into a capsule wherein said crystalline particles of escitalopram oxalate are according to the invention as described above, preferably the capsule is a hard gelatine capsule.
Preferably, the solid unit dosage forms according to the invention do not contain a binder.
The solid unit dosage form according to the invention may contain 1-60% w/w active ingredient calculated as escitalopram base, particularly 4-40% w/w active ingredient calculated as escitalopram base, evenly particularly 1-30% w/w active ingredient to calculated as escitalopram base, more particularly 4-20% w/w active ingredient calculated as escitalopram base and most particularly 6-10% w/w active ingredient calculated as escitalopram base. Suitably, the solid unit dosage form of the invention contains 8% w/w active ingredient calculated as escitalopram base.
The solid unit dosage form according to the invention may contain a filler selected from lactose, or other sugars e.g. sorbitol, mannitol, dextrose and sucrose, calcium phosphates (dibasic, tribasic, hydrous and anhydrous), starch, modified starches, microcrystalline cellulose, calciwn sulphate and/or calcium carbonate. In a preferred embodiment, the solid unit dosage form of the invention does not contain lactose.
Suitably the filler is a microcrystalline cellulose such as ProSolv SMCC90 manufactured by Penwest Pharmaceuticals or Avicel PH 200 manufactured by FMC
Corporation.
Besides the active ingredient and filler, the solid pharmaceutical unit dosage forms may include various other conventional excipients such as disintegrants and optionally minor amounts of lubricants, colorants and sweeteners.
Lubricants used according to the invention may suitably be one or more selected from 3o the group comprising metallic stearates (magnesium, calcium, sodium), stearic acid, wax, hydrogenated vegetable oil, talc and colloidal silica.
Preferably the lubricant is one or more selected from the group comprising talc, magnesium stearate or calcium stearate. Suitably the lubricant is a combination of talc and magnesium stearate. The weight percent of magnesium stearate in the solid unit dosage form is preferably in the range of 0.4% to 2%, and more preferred in the range 5 of 0.7% to 1.4%.
In a particular embodiment the solid unit dosage form is substantially free of lactose.
Disintegrants include sodium starch glycolate, croscarmellose, crospovidone, low l0 substituted hydroxypropylcellulose, modified cornstarch, pregelatizined starch and natural starch. Suitably the disintegrant is crosscarmellose such Ac-Di-Sol manufactured by FMC.
Optionally the solid, pharmaceutical unit dosage form of the invention may be coated.
15 Suitably the coating is a film coating based on conventional coating mixtures such as Opadry OY-S-28849, white manufactured by Colorcon.
The solid, pharmaceutical unit dosage form of the invention may be prepared by conventional methods using a tablet press with forced feed capability.
The filled, hard gelatine capsule of the invention may be prepared by conventional methods using a capsule filler suitable for powder filling.
Examples In the following, the invention is illustrated by way of examples. However, the examples are merely intended to illustrate the invention and should not be construed as limiting.
Example 1 Scavenging of hydroxyl containing impurity by succinic anhydride A mixture of R- and S-Citalopram (55,5 g) containing 0,6% of Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxymethyl-benzonitrile is dissolved in dry toluene (145,0 g). Succinic anhydride (0,5 g) is added to the solution and the mixture is stirred at 45 °C (120 minutes). Water (230 ml) and aqueous ammonia (25% by weight) (3 ml) is added (pH = 10,5-11,0). The phases are separated and the toluene phase is washed with water (3 x 120 ml). The toluene phase is evaporated and the yield is 53,0 g (95%). The product contains 0,06% of Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3 -hydroxymethyl-benzonitrile.
Example 2 Production scale crystallisation of escitalopram oxalate to A large number of batches of crude escitalopram oxalate have been recrystallised in production scale according to the procedure described below. The batches comprises:
a) Escitalopram prepared by acidic ring-closure of the R-form of the diol precursor as described in W003/000672 followed by scavenging of hydroxyl containing impurity by a production scale version of the process described in example 1 followed by separation of racemic citalopram and escitalopram as described in W003/000672. These batches contain Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxymethyl-benzonitrile, typically in the range of 0.05%
(w/w) relative to escitalopram. These batches are referred to as R-diol batches.
2o b) Escitalopram prepared by ring-closure of the S-form of the diol precursor via an activated ester under alkaline conditions as described in US Patent No.
4,943,590.
These batches do not contain Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxymethyl-benzonitrile. These batches are referred to as S-diol batches.
Production procedure:
100 lcg to 300 kg, of crude escitalopram oxalate is charged to a first reactor, R1. 4,1 -4,3 L ethanol per kg crude escitalopram oxalate is charged to Rl. The solution is mixed and heated to the boiling point (~80°C). When every thing is dissolved the solution is transferred through a filter to a second reactor, R2.
The agitator on R2 is started (40-60 rpm) and the solution is heated to the boiling point once again. When everything is dissolved in R2, the automatic cooling is started and the solution is cooled gradually according to the cooling rates in table 1.
Table 1: Cooling rate setpoints for automatic cooling during recrystallisation of escitalopram oxalate Interval Rate [C/min]
[C]
Above 0.151 70.0 70.0 66.0 0.250 -66.0 60.0 0.300 -60.0 56.4 0.327 -56.4 52.0 0.400 -52.0 - 47.60.550 47.6 - 35.00.700 35.0 -10.0 0.830 The solution is seeded with 0.02 - 0.04 kg, escitalopram oxalate for every 3 °C the temperature is decreased until crystallization is noticed. The solution is automatically 1o cooled until 15 °C.
The suspension is pumped to a filter dryer, where it is washed and dried. If the suspension is not transferred immediately the temperature must be kept at 0 -15 °C.
The filter calve is dried by vacuum. When the cake is dry, it is washed with 1,1 - 1,2 L
ethanol per kg crude escitalopram oxalate charged. The cake is dried once again and the calve is heated for final drying for approximately 12 hours. Temperature =
60 °C, pressure < 0.13 Bar (abs.).
The filter dryer is emptied and the escitalopram oxalate is sent to deagglomeration, for deagglomeration of agglomerates formed during drying of the crystals. The dried escitalopram oxalate is milled to separate the crystals from each other.
During the milling the size and shape of the individual crystals is not changed.
The resulting escitalopram oxalate batches had particle characteristics as shown in table 2.
Table 2: Particle characteristics for escitalopram oxalate crystals.
S-diol R-diol batches batches Batch X50 X10/X50 X50/X95Batch X50 X10IX50X501X95 1 171 0,13 0,44 47 93 0,12 0,33 2 153 0,07 0,43 48 91 0,11 0,33 3 158 0,09 0,43 49 74 0,11 0,26 4 171 0,15 0,44 50 116 0,14 0,39 166 0,10 0,47 51 74 0,09 0,29 6 165 0,13 0,46 52 93 0,11 0,38 7 163 0,10 0,47 53 92 0,17 0,38 8 171 0,15 0,44 54 90 0,20 0,37 9 171 0,15 0,47 55 108 0,09 0,39 166 0,11 0,47 56 100 0,09 0,39 11 174 0,11 0,46 57 98 0,08 0,36 12 162 0,07 0,44 58 102 0,09 0,33 13 180 0,11 0,46 59 76 0,11 0,30 14 165 0,11 0,44 60 92 0,10 0,36 178 0,13 0,48 61 96 0,08 0,35 16 162 0,12 0,47 17 138 0,14 0,43 18 168 0,11 0,44 19 166 0,11 0,46 160 0,12 0,44 21 121 0,07 0,36 22 141 0,08 0,41 23 166 0,08 0,43 24 126 0,08 0,42 123 0,09 0,42 26 159 0,11 0,44 27 156 0,12 0,46 28 147 0,12 0,46 29 169 0,12 0,47 181 0,08 0,44 31 147 0,07 0,39 32 184 0,09 0,45 33 173 0,10 0,43 34 161 0,09 0,42 171 0,11 0,44 36 159 0,12 0,43 37 160 0,13 0,45 38 157 0,11 0,45 3g 153 0,08 0,44 163 0,10 0,44 41 157 0,11 0,45 42 156 0,12 0,45 43 129 0,10 0,40 44 139 0,12 0,40 150 0,12 0,42 46 195 0,09 0,46 Comparative Example 1 A wet filter cake obtained by precipitation of crude escitalopram oxalate by mixing of ethanolic solutions of escitalopram prepared by ring-closure via a labile ester under to alkaline conditions and oxalic acid, respectively, and containing approximately 35 kg escitalopram oxalate was suspended in 322 L ethanol. The material was dissolved by heating to reflux, and 150 L ethanol was removed by distillation. Cooling was applied, and the mixture was cooled from reflux to 15 °C with a cooling rate between 0.2 and 0.5 °C/min in the temperature interval 80 to 40 °C.
During cooling, the mixture was seeded with escitalopram oxalate at 75, 65 and 60 °C (10 g each time).
The crystallisation mixture was kept at 15 °C for 10 hours before the crystalline escitalopram oxalate was isolated. Purified escitalopram oxalate (27.7 kg, 79%) was obtained by filtration of the crystallisation mixture, washing with ethanol and drying of the filter cake. Particle size distribution for the resulting escitalopram oxalate is listed in table 3.
Table 3: Particle size distribution (Sympatec Helos) for escitalopram oxalate crystals and ProSolv SMCC90 Quantile Comparative ExampleProSolv SMCC90 (%) 1 (gym) (N~m) Comparative Example 2 Tablet prepared by direct compression of large crystalline particles of escitalopram oxalate.
Tablet ingredients:
Tablet core Escitalopram oxalate 2554 ~ (10.2 %
w/w) 1 o Talc 14_ 00 ~ (5.6 % w/w) ProSolv SMCC90 19896 ~ (79.6 %
w/w) Ac-Di-Sol 9_ 00 ~ (3.6 Magnesium stearate 250 ~ (1.0 % w/w) 15 Film coating Opadry OY-S-28849, white 625 ~ (2.5 % w/w of core weight) Crystalline particles of escitalopram oxalate from example 1 and talc were sieved through 710 ~m screen and blended at 6 rpm for 15 min in a 100 litre Bohle PTM
2o mixer. ProSolv SMCC90 and Ac-Di-Sol were added and blending continued for min. Magnesium stearate was sieved through 710 ~m screen and added and blending continued for 3 min.
kg of the resulting mixture was tabletted (125.000 tablets/hour) on a Korsch PH
25 230 tablet press fitted with oblong, embossed, scored 5,5 x 8 mm punches.
Tablet core weight was set to 125 mg. The nominal yield was 200.000 tablets. The tablet press was run until the mixture level was just above the forced feeder, i.e. the tabletting was continued as long as possible in order to identify possible segregation tendencies in the last quantities of mixture. The tablets produced had satisfactory technical properties.
Those skilled in the art will easily realise that crystals according to the invention can be used in the manufacture of tablets in similar ways.
Claims (46)
1. Crystalline particles of escitalopram oxalate, characterised in that the ratio between the median particle size and the particle size at the 95% quantile is less than 0.42.
2. Crystalline particles of escitalopram oxalate according to claim 1, characterised in that the ratio between the median particle size and the particle size at the 95% quantile is less than 0.40.
3. Crystalline particles of escitalopram oxalate according to claim 1 or 2, characterised in that the median particle size is at least 20 µm.
4. Crystalline particles according to claim 3, characterised in that the median particle size of the crystals is at least 40 µm, preferably in the range of 50-200 µm.
5. Crystalline particles according to claim 3 or 4, characterised in that the particle size distribution of the crystalline particles of escitalopram oxalate is bimodal or polymodal and the peak at the lowest particle size is located at a particle size of at least 20 µm, in particular of at least 40 µm, and preferably in the range of 50 - 200 µm.
6. Crystalline particles of escitalopram oxalate, characterised in that the median particle size is at least 20 µm and the content of E- or Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxymethyl-benzonitrile is at least 0.01%
(w/w).
(w/w).
7. Crystalline particles according to claim 6, characterised in that the median particle size of the crystals is at least 40 µm, and preferably in the range of 50-200 µm.
8. Crystalline particles of escitalopram oxalate according to claim 6 or 7, characterised in that the ratio between the median particle size and the particle size at the 95% quantile is less than 0.42, preferably less than 0.40.
9. Crystalline particles of escitalopram oxalate, characterised in that the median particle size is at least 20 µm and the content of E- or Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3-hydroxymethyl-benzonitrile in the solution, from which the escitalopram oxalate is crystallised, prior to the crystallisation is at least 0.01% (W/W) relative to the total weight of the crystallisation batch.
10. Crystalline particles according to claim 9, characterised in that the median particle size of the crystals is at least 40 µm, and preferably in the range of 50-200 µm.
11. Crystalline particles of escitalopram oxalate according to claim 9 or 10, characterised in that the ratio between the median particle size and the particle size at the 95% quantile is less than 0.42, preferably less than 0.40.
12. A solid unit dosage form comprising crystalline particles of escitalopram oxalate according to any one of claims 1-11.
13. A solid unit dosage form manufactured from crystalline particles of escitalopram oxalate according to any one of claims 1-11.
14. The solid unit dosage form according to claim 12 or 13, characterised in that it is a tablet prepared by direct compression, dry granulation (compaction), wet granulation or melt granulation of a mixture of escitalopram oxalate and pharmaceutically acceptable excipients.
15. The solid unit dosage form according to claim 14, characterised in that the tablet is coated.
16. The solid unit dosage form according to claim 12 or 13, characterised in that it is prepared by filling a mixture of escitalopram oxalate and pharmaceutically acceptable excipients in a hard gelatine capsule.
17. The solid unit dosage form according to any of claims 12-16, characterised in that it does not contain a binder.
18. The solid unit dosage form according to any of claims 12-17, characterised in that it contains 1-60% w/w active ingredient calculated as escitalopram base, particularly 1-30% w/w active ingredient calculated as escitalopram base, more particularly 4-20% w/w active ingredient calculated as escitalopram base and most particularly 6-10% w/w active ingredient calculated as escitalopram base.
19. The solid unit dosage form according to any of claims 12-18, characterised in that it contains a filler selected from lactose, sugars, preferably sorbitol, mannitol, dextrose, and/or sucrose, calcium phosphates, preferably dibasic, tribasic, hydrous and/or anhydrous, starch, modified starches, microcrystalline cellulose, calcium sulfate and/or calcium carbonate.
20. The solid unit dosage form according to claim 19, characterised in that the filler is a microcrystalline cellulose, such as ProSolv SMCC90 or Avicel PH 200.
21. The solid unit dosage form according to any of claims 12-20, characterised in that it contains a lubricant selected from metallic stearates (magnesium, calcium, sodium), stearic acid, wax, hydrogenated vegetable oil, talc and colloidal silica.
22. The solid unit dosage form according to claim 21, characterised in that the lubricant is one or more selected from the group of talc, magnesium stearate and calcium stearate.
23. The solid unit dosage form according to claim 22, characterised in that the lubricant is a combination of talc and magnesium stearate.
24. The solid unit dosage form according to claim 23, characterised in that the weight percent of magnesium stearate calculated on the weight of the solid dosage form is preferably in the range of 0.4% to 2%, preferably 0.7% to 1.4%.
25. The solid unit dosage form according to any of claims 12-24, characterised in that it is substantially free of lactose.
26. Method for manufacture of crystalline particles of escitalopram oxalate according to any one of claims 1-11 comprising the steps of:
a) Treating a solution comprising escitalopram together with one or more hydroxyl containing impurities with a hydroxyl group scavenger, b) separating the escitalopram from the products resulting from reaction of said hydroxyl containing impurities with said hydroxyl group scavenger, c) optionally transferring the escitalopram into its oxalate salt if the escitalopram is not already in the form of its oxalate salt, d) optionally transferring the escitalopram to a solvent system suitable for the crystallisation process if the escitalopram is not already in such a solvent system, and e) gradual cooling of the solution of escitalopram oxalate in said suitable solvent system from a first temperature to a second temperature while maintaining a controlled cooling profile and seeding said solution of escitalopram oxalate by addition of crystals of escitalopram oxalate during said cooling.
a) Treating a solution comprising escitalopram together with one or more hydroxyl containing impurities with a hydroxyl group scavenger, b) separating the escitalopram from the products resulting from reaction of said hydroxyl containing impurities with said hydroxyl group scavenger, c) optionally transferring the escitalopram into its oxalate salt if the escitalopram is not already in the form of its oxalate salt, d) optionally transferring the escitalopram to a solvent system suitable for the crystallisation process if the escitalopram is not already in such a solvent system, and e) gradual cooling of the solution of escitalopram oxalate in said suitable solvent system from a first temperature to a second temperature while maintaining a controlled cooling profile and seeding said solution of escitalopram oxalate by addition of crystals of escitalopram oxalate during said cooling.
27. Method for manufacture of crystalline particles of escitalopram oxalate according to any one of claims 1-11 comprising gradual cooling of a solution of escitalopram oxalate in a suitable solvent system from a first temperature to a second temperature while maintaining a controlled cooling profile and seeding said solution of escitalopram oxalate by addition of crystals of escitalopram oxalate during said cooling wherein said solution of escitalopram comprises at least 1 ppm, particularly at least 10 ppm, and more particularly at least 0.01 % by weight of E- or Z-4-(4-dimethylamino-1-(4-fluorophenyl)-but-1-enyl)-3 -hydroxymethyl-benzonitrile relative to the total weight of the crystallisation batch.
28. The method according to any of claims 26-27, characterised in that said solvent system comprises one or more alcohols and optionally water.
29. The method according to claim 28, characterised in that the solvent system is ethanol.
30. The method according to any of claims 26-29, characterised in that the solute:solvent weight ratio is in the range of 0.05:1 to 0.6:1, preferably 0.1:1 to 0.5:1 and more preferred 0.2:1 to 0.4:1.
31. The method according to any of claims 26-30, characterised in that said first temperature is in the range between 50 °C and the refluxing temperature of the solvent system, preferably between 60 °C and the refluxing temperature and more preferred between 70 °C and the refluxing temperature.
32. The method according to any of claims 26-31, characterised in that said second temperature is in the range of 0-20 °C, preferably 0-15 °C and more preferred 7-15 °C.
33. The method according to any of claims 26-32, characterised in that said controlled cooling profile comprises an initial cooling period where the cooling rate is kept within a fixed range.
34. The method according to claim 33characterised in that said initial cooling period covers the period until the temperature is below 60 °C, preferably below 50°C, and more preferred below 40 °C.
35. The method according to any of claims 33-34, characterised in that said cooling rate is kept within the range of 0 - 0.9 °C/min, preferably in the range of 0 -0.6 °C/min, and more preferably range of 0.2 - 0.4 °C/min.
36. The method according to any of claims 26-35, characterised in that said seeding is done two or more times during the initial cooling.
37. The method according to any of claims 26-36, characterised in that the crystalline particles after said holding time is isolated from the mother liquor by conventional solid/liquid separation techniques, preferably by filtration.
38. The method according to any of claims 26-37, characterised in that the escitalopram is manufactured by a process comprising ring-closure of R-4-[4-(dimethylamino)-1-(4'-fluorophenyl)-1-hydroxybutyl]-3-(hydroxymethyl)-benzonitrile under acidic conditions.
39. Method for reducing the amount of hydroxyl containing impurities in citalopram, escitalopram or a non-racemic mixture of R- and S-citalopram comprising the steps of:
c) Treating a solution comprising citalopram, escitalopram or a non-racemic mixture of R- and S-citalopram together with one or more such impurities with a hydroxyl group scavenger, and d) separating said citalopram, escitalopram or a non-racemic mixture of R- and S-citalopram from the products resulting from reaction of said hydroxyl containing impurities with said hydroxyl group scavenger.
c) Treating a solution comprising citalopram, escitalopram or a non-racemic mixture of R- and S-citalopram together with one or more such impurities with a hydroxyl group scavenger, and d) separating said citalopram, escitalopram or a non-racemic mixture of R- and S-citalopram from the products resulting from reaction of said hydroxyl containing impurities with said hydroxyl group scavenger.
40. Method for reducing the amount of hydroxyl containing impurities in escitalopram according to claim 39.
41. Method for reducing the amount of hydroxyl containing impurities in citalopram according to claim 39.
42. Method for reducing the amount of hydroxyl containing impurities in a non-racemic mixture of R- and S-citalopram.
43. Method according to any of claims 26 and 39-42 wherein the hydroxyl group scavenger is selected from the group consisting of cyclic anhydrides.
44. Method according to claim 43 wherein the hydroxyl group scavenger is a cyclic C4-8-anhydride, preferably succinic anhydride.
45. Method according to any of claims 39-44 wherein the separation of citalopram or escitalopram from the products resulting from reaction of the hydroxyl containing impurities with said hydroxyl group scavenger is performed by extraction of said products resulting from reaction of said hydroxyl containing impurities with said hydroxyl group scavenger into an aqueous solution, particularly an alkaline aqueous solution, from a solution of said citalopram or escitalopram in an organic solvent.
46. The method according to any of claims 39-45, characterised in that the escitalopram and/or citalopram is manufactured by a process comprising ring-closure of R-4-[4-(dimethylamino)-1-(4'-fluorophenyl)-1-hydroxybutyl]-3-(hydroxymethyl)-benzonitrile under acidic conditions.
Applications Claiming Priority (5)
Application Number | Priority Date | Filing Date | Title |
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US55090904P | 2004-03-05 | 2004-03-05 | |
DKPA200400382 | 2004-03-05 | ||
DKPA200400382 | 2004-03-05 | ||
US60/550,909 | 2004-03-05 | ||
PCT/DK2005/000115 WO2005084643A1 (en) | 2004-03-05 | 2005-02-21 | Crystalline composition containing escitalopram oxalate |
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CA2558198A1 true CA2558198A1 (en) | 2005-09-15 |
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CA002558198A Abandoned CA2558198A1 (en) | 2004-03-05 | 2005-02-21 | Crystalline composition containing escitalopram oxalate |
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EP (1) | EP1732514A1 (en) |
JP (1) | JP2007526262A (en) |
AU (1) | AU2005218713B2 (en) |
BR (1) | BRPI0508266A (en) |
CA (1) | CA2558198A1 (en) |
EA (1) | EA200601641A1 (en) |
NO (1) | NO20064499L (en) |
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TWI347942B (en) * | 2005-06-22 | 2011-09-01 | Lundbeck & Co As H | Crystalline base of escitalopram and orodispersible tablets comprising escitalopram base |
US8252336B2 (en) | 2006-10-20 | 2012-08-28 | Ratiopharm Gmbh | Escitalopram and solid pharmaceutical composition comprising the same |
EP2116231A1 (en) * | 2008-05-07 | 2009-11-11 | Hexal Ag | Granulate comprising escitalopram oxalate |
JP2018016569A (en) * | 2016-07-26 | 2018-02-01 | 株式会社トクヤマ | Production method of (1s)-1-[3-(dimethylamino)propyl]-1-(4-fluorophenyl)-1,3-dihydroisobenzofuran-5-carbonitrile oxalate |
JP6554245B1 (en) * | 2019-01-31 | 2019-07-31 | 第一工業製薬株式会社 | 2,2'-bis (2-hydroxyethoxy) -1,1'-binaphthalene powder |
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GB8814057D0 (en) * | 1988-06-14 | 1988-07-20 | Lundbeck & Co As H | New enantiomers & their isolation |
IL158031A0 (en) * | 2001-05-01 | 2004-03-28 | Lundbeck & Co As H | The use of enantiomeric pure escitalopram |
AR034612A1 (en) * | 2001-06-25 | 2004-03-03 | Lundbeck & Co As H | PROCESS FOR THE PREPARATION OF RACEMIC CITALOPRAM AND / OR OF THE S- OR R-CITALOPRAM THROUGH THE SEPARATION OF A MIXING OF R- AND S-CITALOPRAM |
DE60217932T2 (en) * | 2001-07-31 | 2007-08-30 | H. Lundbeck A/S, Valby | Crystalline composition containing escitalopram |
PE20040991A1 (en) * | 2002-08-12 | 2004-12-27 | Lundbeck & Co As H | SEPARATION OF INTERMEDIARIES FOR THE PREPARATION OF ESCITALOPRAM |
NZ540281A (en) * | 2002-12-23 | 2008-07-31 | Lundbeck & Co As H | Escitalopram hydrobromide and a method for the preparation thereof |
US20050154052A1 (en) * | 2003-03-24 | 2005-07-14 | Hetero Drugs Limited | Novel crystalline forms of (s)-citalopram oxalate |
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- 2005-02-21 AU AU2005218713A patent/AU2005218713B2/en not_active Withdrawn - After Issue
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