CA2166794C - Magnesium omeprazole - Google Patents
Magnesium omeprazoleInfo
- Publication number
- CA2166794C CA2166794C CA002166794A CA2166794A CA2166794C CA 2166794 C CA2166794 C CA 2166794C CA 002166794 A CA002166794 A CA 002166794A CA 2166794 A CA2166794 A CA 2166794A CA 2166794 C CA2166794 C CA 2166794C
- Authority
- CA
- Canada
- Prior art keywords
- magnesium omeprazole
- magnesium
- omeprazole
- crystals
- process according
- 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.)
- Expired - Lifetime
Links
- KWORUUGOSLYAGD-UHFFFAOYSA-N magnesium 5-methoxy-2-[(4-methoxy-3,5-dimethyl-2-pyridinyl)methylsulfinyl]benzimidazol-1-ide Chemical compound [Mg+2].N=1C2=CC(OC)=CC=C2[N-]C=1S(=O)CC1=NC=C(C)C(OC)=C1C.N=1C2=CC(OC)=CC=C2[N-]C=1S(=O)CC1=NC=C(C)C(OC)=C1C KWORUUGOSLYAGD-UHFFFAOYSA-N 0.000 title claims abstract description 34
- 238000000034 method Methods 0.000 claims abstract description 35
- 238000004519 manufacturing process Methods 0.000 claims abstract description 10
- 239000008194 pharmaceutical composition Substances 0.000 claims abstract 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical group OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 33
- 150000003839 salts Chemical class 0.000 claims description 22
- 239000013078 crystal Substances 0.000 claims description 14
- SUBDBMMJDZJVOS-UHFFFAOYSA-N 5-methoxy-2-{[(4-methoxy-3,5-dimethylpyridin-2-yl)methyl]sulfinyl}-1H-benzimidazole Chemical compound N=1C2=CC(OC)=CC=C2NC=1S(=O)CC1=NC=C(C)C(OC)=C1C SUBDBMMJDZJVOS-UHFFFAOYSA-N 0.000 claims description 8
- 229960000381 omeprazole Drugs 0.000 claims description 8
- 239000002245 particle Substances 0.000 claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- 239000011777 magnesium Substances 0.000 claims description 7
- 239000002904 solvent Substances 0.000 claims description 7
- 241000124008 Mammalia Species 0.000 claims description 6
- 229910052749 magnesium Inorganic materials 0.000 claims description 6
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims description 5
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 claims description 5
- 238000003860 storage Methods 0.000 claims description 5
- 201000010099 disease Diseases 0.000 claims description 4
- 239000003814 drug Substances 0.000 claims description 4
- 230000027119 gastric acid secretion Effects 0.000 claims description 4
- 230000002401 inhibitory effect Effects 0.000 claims description 4
- 239000000843 powder Substances 0.000 claims description 4
- 238000001035 drying Methods 0.000 claims description 3
- 210000001156 gastric mucosa Anatomy 0.000 claims description 3
- 238000002955 isolation Methods 0.000 claims description 3
- 239000002798 polar solvent Substances 0.000 claims description 3
- 230000001681 protective effect Effects 0.000 claims description 3
- 238000001914 filtration Methods 0.000 claims description 2
- 238000000634 powder X-ray diffraction Methods 0.000 claims description 2
- 239000011541 reaction mixture Substances 0.000 claims description 2
- 239000004480 active ingredient Substances 0.000 claims 3
- 239000003085 diluting agent Substances 0.000 claims 3
- 210000004211 gastric acid Anatomy 0.000 claims 3
- 238000004817 gas chromatography Methods 0.000 claims 2
- 239000003795 chemical substances by application Substances 0.000 claims 1
- 238000002425 crystallisation Methods 0.000 claims 1
- 230000008025 crystallization Effects 0.000 claims 1
- 238000001704 evaporation Methods 0.000 claims 1
- 238000000892 gravimetry Methods 0.000 claims 1
- 238000010438 heat treatment Methods 0.000 claims 1
- 238000000746 purification Methods 0.000 claims 1
- 238000000926 separation method Methods 0.000 claims 1
- 239000007916 tablet composition Substances 0.000 claims 1
- 238000002560 therapeutic procedure Methods 0.000 claims 1
- 238000005406 washing Methods 0.000 claims 1
- 150000001875 compounds Chemical group 0.000 abstract description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 6
- 238000010586 diagram Methods 0.000 description 4
- 239000007788 liquid Substances 0.000 description 3
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 238000004448 titration Methods 0.000 description 2
- 208000007882 Gastritis Diseases 0.000 description 1
- 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 description 1
- 208000007107 Stomach Ulcer Diseases 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000002775 capsule Substances 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 238000001311 chemical methods and process Methods 0.000 description 1
- MCWXGJITAZMZEV-UHFFFAOYSA-N dimethoate Chemical compound CNC(=O)CSP(=S)(OC)OC MCWXGJITAZMZEV-UHFFFAOYSA-N 0.000 description 1
- 208000035475 disorder Diseases 0.000 description 1
- 208000000718 duodenal ulcer Diseases 0.000 description 1
- 230000001747 exhibiting effect Effects 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 201000005917 gastric ulcer Diseases 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 229910003480 inorganic solid Inorganic materials 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 229960004592 isopropanol Drugs 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000003826 tablet Substances 0.000 description 1
- 238000010626 work up procedure Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D401/00—Heterocyclic compounds containing two or more hetero rings, having nitrogen atoms as the only ring hetero atoms, at least one ring being a six-membered ring with only one nitrogen atom
- C07D401/02—Heterocyclic compounds containing two or more hetero rings, having nitrogen atoms as the only ring hetero atoms, at least one ring being a six-membered ring with only one nitrogen atom containing two hetero rings
- C07D401/12—Heterocyclic compounds containing two or more hetero rings, having nitrogen atoms as the only ring hetero atoms, at least one ring being a six-membered ring with only one nitrogen atom containing two hetero rings linked by a chain containing hetero atoms as chain links
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K31/00—Medicinal preparations containing organic active ingredients
- A61K31/33—Heterocyclic compounds
- A61K31/395—Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins
- A61K31/435—Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins having six-membered rings with one nitrogen as the only ring hetero atom
- A61K31/44—Non condensed pyridines; Hydrogenated derivatives thereof
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P1/00—Drugs for disorders of the alimentary tract or the digestive system
- A61P1/04—Drugs for disorders of the alimentary tract or the digestive system for ulcers, gastritis or reflux esophagitis, e.g. antacids, inhibitors of acid secretion, mucosal protectants
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Organic Chemistry (AREA)
- Medicinal Chemistry (AREA)
- Pharmacology & Pharmacy (AREA)
- Life Sciences & Earth Sciences (AREA)
- Animal Behavior & Ethology (AREA)
- General Health & Medical Sciences (AREA)
- Public Health (AREA)
- Veterinary Medicine (AREA)
- Epidemiology (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Nuclear Medicine, Radiotherapy & Molecular Imaging (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
- Plural Heterocyclic Compounds (AREA)
- Conductive Materials (AREA)
- Contacts (AREA)
- Electroplating Methods And Accessories (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Fats And Perfumes (AREA)
- Medicinal Preparation (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
- Powder Metallurgy (AREA)
- Glass Compositions (AREA)
Abstract
A novel compound form of magnesium omeprazole useful in the manufacture of pharmaceutical formulations, the use of the product and the process for its production are described.
Description
I wo 951019M 2 ~ ~ 6 7 g 4 PCT/SE94/00680 MAGNESIUM OMEPRAZOLE
Field of the invention The present invention relates to a novel process for ' g the .0 salt of ~ r, the IIIA~ salt o~ r in a novel physical form, especially the ,, salt as a product of the novel process; the use of the novel form of the ~ ~ c~ salt of ~ lr in the, r ~ of ~o , ~ 1 r ~ and to the use of the novel form of the rna~n~ci~lrn salt of ~ '''`'If in medicine.
l~a.,~K., ' of the invention 15 The compound known under the generic name ",".I..",.,lr is described i.a. in European patent ~ . ;fi~ 0005129.
~m.-rr:l7rll~ is useful for inhibiting gastric acid secretion and has gastric mucosa protective activity in marnmals and man. In a more general sense, ~ml-rr:~7r~1r may 20 be used for prevention and treatment of gastlic acid related disorders and Oa~ n ' y diseases in mammal and man, including e.g. gastritis, gastric ulcer and duodenal ulcer.
The term ".. ~ lr.~ as used in this ~I~ ;ri~ designates the neutral form of 25 the compound, that is the form without a sait forming cation present.
Certain salts of ~""~ "lr are described in European patent ~ ;r~ 0124495.
In said patent ~ . ;ri~ .n the .~ I and importance regarding storage stability of 1)~ ua~l~ are . ."1.~ .l Sa~ts possessing superior 30 properties with regard i.a. to storage stability are described in the said European patent~ ;ri ~ ;f~'~
WO 95/019M ~,1 S ~ 7 g l~ PCT/SE94/00680 In EP 0124495; examples 5 and 6 disclose the synthesis of a mA~nFci-lm salt of ulll~ lLUle.
The isolation and y~lircaLivll in full - ' ~ scale of the described 11~ salts presents one major problem in that II~
r salt crystals are very fragile making processes utilising such crystals less attractive in full scale production. P~rfomling the process without crystallizavion of the I~Ag~ ;1..ll Ulll~lJIA OIe gives a product which is less suitable as a 1,~ ;I A1 substance.
In order to use the ... ~ - .. salt of ~... I..A".lF, in this ~ l;., denoted omeprazole, in full ."-- -,rA, l...; ~ scale in preparing yll~ ,c~lih,~l r -, .,.--lA~ primarily for oral a~ such as tablets, it is necessary that sa~d IIIA~ 11 omeprazole possesses a ..~,.1.;. -~;~. of properties which makes 15 such full scale, r ,, feasible. One object of the present invention is to provide a process for full scale production of ~, I-m~ rr~7~ 1F A further object of the present invention is to provide a novel form of the mo.~nF~illm salt of U,l,.l"~,Lule which can be used in full scale ,.,- rA~ l. ;,.~ o fu~lll.llaliulla, such as tablets.
The frlmhinorion of physical properties of the novel -".~ . ~:-,.,.. ,. I.l,.~.-lF.
product of the present invention with respect to the degree of crystallinity, particle diameter, density, hy~;lua~ulJh,i~y, water content and content of other solvents are favorable and permit the ' c of "''`L"' ` ""' Oll~ /lAL.UIe in a form which 25 possesses the desired properties.
The novel form of ~ r can also be formulated into other forms fo} oral ad."ll.;a~ ion and other types of Alll~ such as rectal Alllll; l;~l~Al;--l) Examples of rul"",l_~iu--s are tablets, pellets, granules, capsules, ~ c and ~ I-yO~ C
~66~94 WO 95/01977 PCT~SE94~00680 'IAhe invention We now provide a novel form of ~he mApA.. Sillm salt of v.,.. 1",.,.~1~ exhibiting the desired ~O~ of physical properties. Al'his makes full scale production of 5 ~ ir as well as full scale production of ~ ullld~c~icd r....,..,lAI;.. -- thereof feasible.
The novel process for the r ~ of ",AL,.. " nm~rA7rl~ also l~ilUUII~
the above described r ' ~ problems and renders possible the recovery and 10 work-up of the ~ L -- ~ u~ lr, substdnce in traditional chemical process equipment.
It has been found that the following property is significant to obtdin such product:
15 a) Crystdlline form, with a degree of crystdllinity of not less than 70%, preferably higher than 75% as ~r-~rmiArd by X-rAly powder diffraction It is desirable that the product aiso exhibits the following properties;
20 b) Particle si_e measured as mean mass diameter (MMD) less than 30,um, preferably less than 20 ,um as ~' ' by laser diffrdction technique.
c) Density between 1.33 g/cm3 and 1.35 g/cm3 as detemlined by powder I'Y'~
d) Hy~u~ y not exceeding 2% increase of weight upon storage for one month up to 94% relative -- . ' ' humidity as determinec vi~ lly.
30 e) A content of water of between 5% and 10% by weight as determined by titration according to Karl Fischer.
WO 95/019~7 PCT/SE94/00680 ~1~6~ 4 f) A content of methanol less than 0.1% preferably less than 0.05% by weight as determined by gas ~h~ull~a~u~ y, in case methanol is used as solvent.
In a further aspect, the invention also relates to a process for m~ f:ir~llnn~ the 5 novel form of ~ "A~ r This process is described in more detail below.
The invention relates to all of the aspects given under Field of the invention.
0 The process for producing the novel form of ""'L"' ~ is t- ..7~,'1 by the following ~ulls~ulive steps a) treating ~ r or a salt thereof with ~IIA~I-- `;"'~1 alcoholate in a solution 15 b) separating inorganic salts from the reaction mixture c) crystdllizing m~n-~ci~m ~
d) isolating the obtdined crystalline .. ~.. ~:.. ~IIA~OIr~ and, optionally,0 e) purifying and drying the crystalline ~ lA~Olr using uu...~lLiulldl methods.
The process for ,.. l.rA, 1.--;.. ~, the new product can be described in the following 25way.
A lower alcohol, such as methanol, ethanol, n-propanol or iso-propanol, preferably methanol, is treated in a solution of polar solvents with a weighed amount of 111- at t~..,-p~ uc~ between 0C and reflux l~ l4~UIti. The t~ ul~
30 should preferably be between 10 and 30C. After addition of the magnesium to the solution the t~ "AL~ can, in a second step be raised further to between 0C and reflux t ll~ UU~;, preferably 20-50C. After termination of the reaction the ~--` 2~.~6~
temperature 18 reduced to 0-40C, preferably 10-25C.
Omeprazole or a salt of omeprazole 18 then added to the solutlon and after terminatlon of the reaction the mlxture 18 cooled to -10C to +20C, preferably -5C to +5C. The solvent 18 then evaporated to 40-60% of the lnltlal volume, whlch makes the lnorganlc salts preclpitate. The preclpltate 18 separated from the reactlon solutlon for example by centrlfugatlon or flltratlon and the solutlon 18 heated to 5C to 30C whereafter the solutlon 18 seeded wlth magneslum omeprazole crystals. An amount of water, whlch 18 approxlmately egual to the volume of the solut lon, 18 added to start the crystalllzatlon. The solutlon 18 cooled to -10 to +20C, preferably 0-10C to complete the crystalllzatlon.
The crystals are then separated from the mother llquld for example by centrlfugatlon or flltratlon and washed wlth polar solvents preferably an agueous lower alcohol such as agueous methanol. Flnally, the produced crystals are drled uslng reduced pressure or heatlng or preferably a comblnatlon thereof .
The process for manufacturlng the new form of magneslum omeprazole dlffers from the earller known processes ln that the product is recovered after a controlled crystalllzation step ln agueous alcohol, preferably methanol by, first, separatlng the lnorganlc salts from the mother llguor. The crystalllnlty resultlng from thls step 18, unexpectedly, hlgher and the product possesses a hlgher degree of purlty and 18 more stable to ~ ltlon from uptake of molsture. The drylng step can be performed wlthout = .
23940-871 ( S) 21 667Q~
- 5a -caklng. The new process 18 posslble to perform ln convent lonal chemical proce3s equlpment and glves a product wlth a hlgher yleld than the proces~es hltherto known.
The followlng detalled Exa~ple 1 wlll serve to more fully lllustrate the process for manufacturlng magneslum omeprazole ln full scale accordlng to the present lnventlon.
In Flgures 1 and 2 sample A 18 manufactured accordlng to thls example .
r --2394Q-871 ( S ) WO 95/01977 216 ~ 7 9 ~ PCTISE94/00680 Example 1 A reactor was filled with 2026 litres of methanol. The stirrer was started and the t~ Lul~ was adjusted to 20C. 3,90 kg of magnesium was added to the vessel and ' 'y thereafter 1,0 litre of CH2C12. The reactor was heated to 40C
and kept aî this t~."~ u-~ for 60 min. It was then cooled to 15C before the addition of 99,9 kg of ~ r The reactor was kept at this L,~ for 60 min and then cooled to 0C. The h.~ ulc was kept at this level for 30 minutes before 10001 of methanol were evaporated under vacuum and the inorganic solid salt was separated from the liquid first by ~ I ;r. c~ l.. and then by filtration. The liquid was heated to 10C and the liquid was seeded with magnesium omepra_ole crystals whereafter the ,, u..~. l....,..lr salt was ~ . ' by addition of 9001 of water. The mixture was then cooled to 5C. After the crystalli_ation hadbeen completed the ~;c~ - r-...- ~ lr crystals were centrifuged off and then washed with a mixture of 501 of methanol and 1501 of water. Tbe produced "",~". ,: ", ,J,~.r~ r was dried under reduced pressure fLnally producing 92,5 kg of crystalline product u-lui"~u--Ji~g to a yield of 81,4%.
The novel form of the ~ salt of nmr~rr~7nl~ according to Example I
20 possesses the following properties:
a) Crystalline form, with a degree of crystallinity of 76%, as determined by X-ray powder diffraction.
25 b) Particle si_e measured as mean mass diameter (MMD) of 19pm as determined by laser diffraction technique.
c) Density of 1.342 g/cm3 as determined by powder ~ ,L..
30 d) ~ .u~u~il,i~y of 1.62% increase of weight upon storage for one month at 94% relative, ~ l ;c humidity as determined gravimetrically.
79~
~WO 95/OI977 PCT/SE94/00680 e) Content of moisture water of 7.6 by weight as determined by titration according to Karl Fischer.
i ) Content of methanol of 0.006% by weight as determined by gas A ~u~ u~ between two different samples of the novel form of m:l~n.
o,l~ ".lLule of the present invention obtained from two laboratory scale by prior art methods and .. ~ -.. u~ ulc goes forth from 10 diagrams I and 2. In these diagrams sample A represents the novel form of the present invention as ' ~i.l in full scale process equipment. Sample B
represents the product of preparation via synthesis by treatment of .. ".. ~ with Mg(OCH3)2. Sample C represens the product of preparation via treatment of sodium ~.".. I,,~,.-lr with MgC12.
Figure I shows in diagram I that the particle size measured as mean mass diameter of the product of method A is 19 pm which is smaller than the ~u..e~u,.di..~, particle size for the products of method B which is 25 ,um and of method C which is greater than 600 ,um.
hgure 2 shows in diagram 2 that the degree of crystallinity of the particles of the product of method A is 76% which is higher than the ~ r~ g figure for the product of sample B, which is 0% and also higher than the cu.-t~l,u...l;..g figure of sample C, which 67%.
.
Field of the invention The present invention relates to a novel process for ' g the .0 salt of ~ r, the IIIA~ salt o~ r in a novel physical form, especially the ,, salt as a product of the novel process; the use of the novel form of the ~ ~ c~ salt of ~ lr in the, r ~ of ~o , ~ 1 r ~ and to the use of the novel form of the rna~n~ci~lrn salt of ~ '''`'If in medicine.
l~a.,~K., ' of the invention 15 The compound known under the generic name ",".I..",.,lr is described i.a. in European patent ~ . ;fi~ 0005129.
~m.-rr:l7rll~ is useful for inhibiting gastric acid secretion and has gastric mucosa protective activity in marnmals and man. In a more general sense, ~ml-rr:~7r~1r may 20 be used for prevention and treatment of gastlic acid related disorders and Oa~ n ' y diseases in mammal and man, including e.g. gastritis, gastric ulcer and duodenal ulcer.
The term ".. ~ lr.~ as used in this ~I~ ;ri~ designates the neutral form of 25 the compound, that is the form without a sait forming cation present.
Certain salts of ~""~ "lr are described in European patent ~ ;r~ 0124495.
In said patent ~ . ;ri~ .n the .~ I and importance regarding storage stability of 1)~ ua~l~ are . ."1.~ .l Sa~ts possessing superior 30 properties with regard i.a. to storage stability are described in the said European patent~ ;ri ~ ;f~'~
WO 95/019M ~,1 S ~ 7 g l~ PCT/SE94/00680 In EP 0124495; examples 5 and 6 disclose the synthesis of a mA~nFci-lm salt of ulll~ lLUle.
The isolation and y~lircaLivll in full - ' ~ scale of the described 11~ salts presents one major problem in that II~
r salt crystals are very fragile making processes utilising such crystals less attractive in full scale production. P~rfomling the process without crystallizavion of the I~Ag~ ;1..ll Ulll~lJIA OIe gives a product which is less suitable as a 1,~ ;I A1 substance.
In order to use the ... ~ - .. salt of ~... I..A".lF, in this ~ l;., denoted omeprazole, in full ."-- -,rA, l...; ~ scale in preparing yll~ ,c~lih,~l r -, .,.--lA~ primarily for oral a~ such as tablets, it is necessary that sa~d IIIA~ 11 omeprazole possesses a ..~,.1.;. -~;~. of properties which makes 15 such full scale, r ,, feasible. One object of the present invention is to provide a process for full scale production of ~, I-m~ rr~7~ 1F A further object of the present invention is to provide a novel form of the mo.~nF~illm salt of U,l,.l"~,Lule which can be used in full scale ,.,- rA~ l. ;,.~ o fu~lll.llaliulla, such as tablets.
The frlmhinorion of physical properties of the novel -".~ . ~:-,.,.. ,. I.l,.~.-lF.
product of the present invention with respect to the degree of crystallinity, particle diameter, density, hy~;lua~ulJh,i~y, water content and content of other solvents are favorable and permit the ' c of "''`L"' ` ""' Oll~ /lAL.UIe in a form which 25 possesses the desired properties.
The novel form of ~ r can also be formulated into other forms fo} oral ad."ll.;a~ ion and other types of Alll~ such as rectal Alllll; l;~l~Al;--l) Examples of rul"",l_~iu--s are tablets, pellets, granules, capsules, ~ c and ~ I-yO~ C
~66~94 WO 95/01977 PCT~SE94~00680 'IAhe invention We now provide a novel form of ~he mApA.. Sillm salt of v.,.. 1",.,.~1~ exhibiting the desired ~O~ of physical properties. Al'his makes full scale production of 5 ~ ir as well as full scale production of ~ ullld~c~icd r....,..,lAI;.. -- thereof feasible.
The novel process for the r ~ of ",AL,.. " nm~rA7rl~ also l~ilUUII~
the above described r ' ~ problems and renders possible the recovery and 10 work-up of the ~ L -- ~ u~ lr, substdnce in traditional chemical process equipment.
It has been found that the following property is significant to obtdin such product:
15 a) Crystdlline form, with a degree of crystdllinity of not less than 70%, preferably higher than 75% as ~r-~rmiArd by X-rAly powder diffraction It is desirable that the product aiso exhibits the following properties;
20 b) Particle si_e measured as mean mass diameter (MMD) less than 30,um, preferably less than 20 ,um as ~' ' by laser diffrdction technique.
c) Density between 1.33 g/cm3 and 1.35 g/cm3 as detemlined by powder I'Y'~
d) Hy~u~ y not exceeding 2% increase of weight upon storage for one month up to 94% relative -- . ' ' humidity as determinec vi~ lly.
30 e) A content of water of between 5% and 10% by weight as determined by titration according to Karl Fischer.
WO 95/019~7 PCT/SE94/00680 ~1~6~ 4 f) A content of methanol less than 0.1% preferably less than 0.05% by weight as determined by gas ~h~ull~a~u~ y, in case methanol is used as solvent.
In a further aspect, the invention also relates to a process for m~ f:ir~llnn~ the 5 novel form of ~ "A~ r This process is described in more detail below.
The invention relates to all of the aspects given under Field of the invention.
0 The process for producing the novel form of ""'L"' ~ is t- ..7~,'1 by the following ~ulls~ulive steps a) treating ~ r or a salt thereof with ~IIA~I-- `;"'~1 alcoholate in a solution 15 b) separating inorganic salts from the reaction mixture c) crystdllizing m~n-~ci~m ~
d) isolating the obtdined crystalline .. ~.. ~:.. ~IIA~OIr~ and, optionally,0 e) purifying and drying the crystalline ~ lA~Olr using uu...~lLiulldl methods.
The process for ,.. l.rA, 1.--;.. ~, the new product can be described in the following 25way.
A lower alcohol, such as methanol, ethanol, n-propanol or iso-propanol, preferably methanol, is treated in a solution of polar solvents with a weighed amount of 111- at t~..,-p~ uc~ between 0C and reflux l~ l4~UIti. The t~ ul~
30 should preferably be between 10 and 30C. After addition of the magnesium to the solution the t~ "AL~ can, in a second step be raised further to between 0C and reflux t ll~ UU~;, preferably 20-50C. After termination of the reaction the ~--` 2~.~6~
temperature 18 reduced to 0-40C, preferably 10-25C.
Omeprazole or a salt of omeprazole 18 then added to the solutlon and after terminatlon of the reaction the mlxture 18 cooled to -10C to +20C, preferably -5C to +5C. The solvent 18 then evaporated to 40-60% of the lnltlal volume, whlch makes the lnorganlc salts preclpitate. The preclpltate 18 separated from the reactlon solutlon for example by centrlfugatlon or flltratlon and the solutlon 18 heated to 5C to 30C whereafter the solutlon 18 seeded wlth magneslum omeprazole crystals. An amount of water, whlch 18 approxlmately egual to the volume of the solut lon, 18 added to start the crystalllzatlon. The solutlon 18 cooled to -10 to +20C, preferably 0-10C to complete the crystalllzatlon.
The crystals are then separated from the mother llquld for example by centrlfugatlon or flltratlon and washed wlth polar solvents preferably an agueous lower alcohol such as agueous methanol. Flnally, the produced crystals are drled uslng reduced pressure or heatlng or preferably a comblnatlon thereof .
The process for manufacturlng the new form of magneslum omeprazole dlffers from the earller known processes ln that the product is recovered after a controlled crystalllzation step ln agueous alcohol, preferably methanol by, first, separatlng the lnorganlc salts from the mother llguor. The crystalllnlty resultlng from thls step 18, unexpectedly, hlgher and the product possesses a hlgher degree of purlty and 18 more stable to ~ ltlon from uptake of molsture. The drylng step can be performed wlthout = .
23940-871 ( S) 21 667Q~
- 5a -caklng. The new process 18 posslble to perform ln convent lonal chemical proce3s equlpment and glves a product wlth a hlgher yleld than the proces~es hltherto known.
The followlng detalled Exa~ple 1 wlll serve to more fully lllustrate the process for manufacturlng magneslum omeprazole ln full scale accordlng to the present lnventlon.
In Flgures 1 and 2 sample A 18 manufactured accordlng to thls example .
r --2394Q-871 ( S ) WO 95/01977 216 ~ 7 9 ~ PCTISE94/00680 Example 1 A reactor was filled with 2026 litres of methanol. The stirrer was started and the t~ Lul~ was adjusted to 20C. 3,90 kg of magnesium was added to the vessel and ' 'y thereafter 1,0 litre of CH2C12. The reactor was heated to 40C
and kept aî this t~."~ u-~ for 60 min. It was then cooled to 15C before the addition of 99,9 kg of ~ r The reactor was kept at this L,~ for 60 min and then cooled to 0C. The h.~ ulc was kept at this level for 30 minutes before 10001 of methanol were evaporated under vacuum and the inorganic solid salt was separated from the liquid first by ~ I ;r. c~ l.. and then by filtration. The liquid was heated to 10C and the liquid was seeded with magnesium omepra_ole crystals whereafter the ,, u..~. l....,..lr salt was ~ . ' by addition of 9001 of water. The mixture was then cooled to 5C. After the crystalli_ation hadbeen completed the ~;c~ - r-...- ~ lr crystals were centrifuged off and then washed with a mixture of 501 of methanol and 1501 of water. Tbe produced "",~". ,: ", ,J,~.r~ r was dried under reduced pressure fLnally producing 92,5 kg of crystalline product u-lui"~u--Ji~g to a yield of 81,4%.
The novel form of the ~ salt of nmr~rr~7nl~ according to Example I
20 possesses the following properties:
a) Crystalline form, with a degree of crystallinity of 76%, as determined by X-ray powder diffraction.
25 b) Particle si_e measured as mean mass diameter (MMD) of 19pm as determined by laser diffraction technique.
c) Density of 1.342 g/cm3 as determined by powder ~ ,L..
30 d) ~ .u~u~il,i~y of 1.62% increase of weight upon storage for one month at 94% relative, ~ l ;c humidity as determined gravimetrically.
79~
~WO 95/OI977 PCT/SE94/00680 e) Content of moisture water of 7.6 by weight as determined by titration according to Karl Fischer.
i ) Content of methanol of 0.006% by weight as determined by gas A ~u~ u~ between two different samples of the novel form of m:l~n.
o,l~ ".lLule of the present invention obtained from two laboratory scale by prior art methods and .. ~ -.. u~ ulc goes forth from 10 diagrams I and 2. In these diagrams sample A represents the novel form of the present invention as ' ~i.l in full scale process equipment. Sample B
represents the product of preparation via synthesis by treatment of .. ".. ~ with Mg(OCH3)2. Sample C represens the product of preparation via treatment of sodium ~.".. I,,~,.-lr with MgC12.
Figure I shows in diagram I that the particle size measured as mean mass diameter of the product of method A is 19 pm which is smaller than the ~u..e~u,.di..~, particle size for the products of method B which is 25 ,um and of method C which is greater than 600 ,um.
hgure 2 shows in diagram 2 that the degree of crystallinity of the particles of the product of method A is 76% which is higher than the ~ r~ g figure for the product of sample B, which is 0% and also higher than the cu.-t~l,u...l;..g figure of sample C, which 67%.
.
Claims (31)
PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:
1. Magnesium omeprazole characterized in having a degree of crystallinity which is higher than 70% as determined by X-ray powder diffraction.
2. Magnesium omeprazole according to claim 1 wherein the degree of crystallinity is higher than 75%.
3. Magnesium omeprazole according to claim 1 wherein the mean particle diameter as determined by laser diffraction technique is less than 30µm.
4. Magnesium omeprazole according to claim 3 wherein the mean particle diameter is less than 20µm.
5. Magnesium omeprazole according to claim 1 wherein the density is between 1.33 g/cm3 and 1.35 g/cm3 as determined by powder pycnometer.
6. Magnesium omeprazole according to claim 1 wherein the hygroscopicity is less than 2% increase of weight upon storage for one month at up to 94% relative atmospheric humidity as determined by gravimetry.
7. Magnesium omeprazole according to claim 1 wherein the water content is between 5% and 10% by weight.
8. Magnesium omeprazole according to claim 1 containing less than 0.1% by weight of solvent as determined by gas chromatography.
9. Magnesium omeprazole according to claim 1 containing less than 0.05% by weight of solvent as determined by gas chromatography.
10. A process for the manufacture of magnesium omeprazole according to any one of claims 1 to 8 characterized by in consecutive steps a) treating omeprazole or a salt thereof with magnesium alcoholate in a solution, b) separating inorganic salts from the reaction mixture, c) crystallizing magnesium omeprazole, d) isolating the obtained crystalline magnesium omeprazole and, optionally, e) purifying and drying the crystalline magnesium omeprazole.
11. A process according to claim 9 wherein the magnesium alcoholate is magnesium methyl alcoholate.
12. A process according to claim 9 wherein the solvent is methanol.
13. A process according to claim 9 wherein the crystallization is accomplished by addition of water.
14. A process according to claim 9 wherein the isolation of the magnesium omeprazole is performed by centrifugal separation of the crystals.
15. A process according to claim 9 wherein the isolation of the magnesium omeprazole is performed by filtration of the crystals.
16. A process according to claim 9 wherein the purification of the magnesium omeprazole crystals is performed by washing the crystals with a solution of polar solvents.
17. A process according to claim 9 wherein the magnesium omeprazole crystals are dried.
18. A process according to claim 17 wherein the magnesium omeprazole crystals are dried under reduced pressure.
19. A process according to claim 9 wherein the drying of the magnesium omeprazole crystals is performed by evaporating the remaining solvent by heating.
20. A pharmaceutical composition containing magnesium omeprazole according to any one of claims 1 to 8 as active ingredient, together with a pharmaceutically acceptable diluent or carrier.
21. A pharmaceutical formulation for oral administration containing magnesium omeprazole according to any one of claims 1 to 8 as active ingredient, together with a pharmaceutically acceptable diluent or carrier.
22. A tablet formulation containing magnesium omeprazole according to any one of claims 1 to 8 as active ingredient, together with a pharmaceutically acceptable diluent or carrier.
23. Magnesium omeprazole according to any one of claims 1 to 8 for use in therapy.
24. Magnesium omeprazole according to any one of claims 1 to 8 for use in inhibiting gastric acid secretion in mammals and man.
25. Magnesium omeprazole according to any one of claims 1 to 8 for use as an agent with gastric mucosa protective activity in mammals and man.
26. Magnesium omeprazole according to any one of claims 1 to 8 for use in the treatment of gastric acid related diseases in mammals and man.
27. The use of magnesium omeprazole according to any one of claims 1 to 8 in the manufacture of a medicament for inhibiting gastric acid secretion.
28. The use of magnesium omeprazole according to any one of claims 1 to 8 in the manufacture of a medicament for obtaining gastric mucosa protective activity.
29. The use of magnesium omeprazole according to any one of claims 1 to 8 in the manufacture of a medicament for the treatment of gastric acid related diseases.
30. Use of magnesium omeprazole according to any one of claims 1 to 8 for inhibiting gastric acid secretion in mammals and man.
31. Use of magnesium omeprazole according to any one of claims 1 to 8 for the treatment of gastric acid related diseases in mammals and man.
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| SE19939302396A SE9302396D0 (en) | 1993-07-09 | 1993-07-09 | A NOVEL COMPOUND FORM |
| SE9302396-8 | 1993-07-09 |
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| Application Number | Title | Priority Date | Filing Date |
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| CA002166794A Expired - Lifetime CA2166794C (en) | 1993-07-09 | 1994-07-08 | Magnesium omeprazole |
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| UA (1) | UA43343C2 (en) |
| WO (1) | WO1995001977A1 (en) |
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Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6077541A (en) * | 1997-11-14 | 2000-06-20 | Andrx Pharmaceuticals, Inc. | Omeprazole formulation |
| US6096340A (en) * | 1997-11-14 | 2000-08-01 | Andrx Pharmaceuticals, Inc. | Omeprazole formulation |
| US6780435B2 (en) | 1997-11-14 | 2004-08-24 | Andrx Pharmaceuticals, Inc. | Omeprazole formulation |
| US6048981A (en) * | 1998-04-22 | 2000-04-11 | Torcan Chemical Ltd. | Magnesium omeprazole and process for its preparation |
| US6174548B1 (en) | 1998-08-28 | 2001-01-16 | Andrx Pharmaceuticals, Inc. | Omeprazole formulation |
| US6855336B2 (en) | 1998-08-28 | 2005-02-15 | Andrx Pharmaceuticals, Inc. | Omeprazole formulation |
| US6733778B1 (en) | 1999-08-27 | 2004-05-11 | Andrx Pharmaceuticals, Inc. | Omeprazole formulation |
| US6713495B1 (en) | 1999-11-16 | 2004-03-30 | Bernard Charles Sherman | Magnesium omeprazole |
| EP2147918A1 (en) | 2008-07-21 | 2010-01-27 | LEK Pharmaceuticals D.D. | Process for the preparation of S-omeprazole magnesium in a stable form |
| US8362259B2 (en) | 2008-07-21 | 2013-01-29 | Lek Pharmaceuticals, D.D. | Process for the preparation of esomeprazole magnesium in a stable form |
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