CN104418848B - Preparation method of rivaroxaban - Google Patents

Preparation method of rivaroxaban Download PDF

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CN104418848B
CN104418848B CN201310395570.0A CN201310395570A CN104418848B CN 104418848 B CN104418848 B CN 104418848B CN 201310395570 A CN201310395570 A CN 201310395570A CN 104418848 B CN104418848 B CN 104418848B
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CN104418848A (en
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徐苗焕
黄悦
张敏
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Shanghai Jingxin Biological Medical Co ltd
Shaoxing Jingxin Pharmaceutical Co ltd
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Shangyu Jingxin Pharmaceutical Co Ltd
SHANGHAI JINGXIN BIOLOGICAL MEDICAL CO Ltd
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    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D413/00Heterocyclic compounds containing two or more hetero rings, at least one ring having nitrogen and oxygen atoms as the only ring hetero atoms
    • C07D413/14Heterocyclic compounds containing two or more hetero rings, at least one ring having nitrogen and oxygen atoms as the only ring hetero atoms containing three or more hetero rings

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Abstract

The invention provides a preparation method of rivaroxaban. The preparation method comprises the following steps: coupling and performing ring-closing on a compound as shown in formula II described in the specification and a compound as shown in formula III described in the specification in the presence of an organic solvent and lithium tert-butoxide to generate a compound as shown in formula IV; (2) directly adding the reactants which are not subjected to after-treatment and obtained in the last-step reaction into hydrochloric acid to hydrolyze to generate a compound as shown in formula V; after the hydrolysis is completed, extracting the reactants by an organic solvent, removing an organic phase and keeping a water phase for later use; and (3) adding inorganic alkali and the compound as shown in formula VI into the water phase, and reacting to obtain the compound rivaroxaban as shown in formula I. The preparation method of the rivaroxaban disclosed by the invention can be used for greatly reducing the technological operation steps, and is simple in after-treatment; only one organic solvent is used in the reaction and the after-treatment thereof, so that the environmental pollution is reduced and the production cost is lowered, and therefore, the preparation method is suitable for large-scale industrial production and has a great application value.

Description

A kind of preparation method of razaxaban
Technical field
The present invention relates to the preparation of medicine, and in particular to a kind of preparation method of small molecule anti-coagulants razaxaban.
Background technology
Razaxaban(Rivaroxaban), the chloro- N- of chemical name 5- { [(5S) -2- oxos -3- [4- (3- oxomorpholin -4- Base) phenyl] -1,3- oxazolidone -5- bases] methyl } thiophene -2- carboxylic acid amides, No. CAS is 366789-02-8, with following structural It is shown:
Razaxaban is the global first oral directly Xa factor inhibitor of Beyer Co., Ltd's exploitation, has height to Xa factor Selectivity, can both suppress the Xa factor in free state, may also suppress the Xa factor of bonding state, it combines the Ⅹ a factors Active site more closely but with invertibity, while there is no direct effect to platelet aggregation.The profit of in September, 2008 cuts down sand Class goes through to list in Canada, for selective full hip or the venous thromboembolism of Total knee arthroplasty postoperative patient person(VTE)'s Prevention.Razaxaban in 2009 in Discussion on Chinese Listed, ratify it and be applied to atrial fibrillation stroke prevention by U.S. FDA in 2011.
The preparation of related razaxaban it has been reported that such as US7157456, US7351823 and other documents, but, this A little methods have that synthetic route is long, and total recovery is low, is unfavorable for environmental protection, is unsuitable for realizing industrialized defect.
Ying Tekuimu(INTERQUIM S.A.)It is shorter that patent WO2012159992 of company discloses a kind of route, yield Higher razaxaban preparation method:
But, the method be present, such as:Due to the facile hydrolysis of compound IV, cause in compound II and chemical combination Post processing during thing III Suo He Cheng azolactone rings can not be with the tert-butyl alcohol lithium during sour neutralization reaction, otherwise will causing Compound IV is hydrolyzed into amine, into water layer, is greatly reduced yield;And if acid adding is not directly extracted, due to depositing in a large number for highly basic , cause extraction process easily to emulsify, bring great difficulty to post-processing operation.The preparation method is used in whole process Various organic solvents such as dichloromethane, ethyl acetate, isopropanol, mixed organic solvents are difficult to recovery, not only increased into This, is also unfavorable for environmental protection, and industrialization is difficult to.
Hunan China normal university also discloses that method similar to the above in patent application CN102786516, public at it In the embodiment of cloth, process is made and is walked in the post processing of prepare compound IV and follow-up hydrolysis, in order to avoid described hydrolysis Cause the problem of yield decline into amine, employ benzene sulfonic acid, p-methyl benzenesulfonic acid neutralization, so, but cause unnecessary organic acid Residual, while substantially prolongs hydrolysis time, causes intermediate to darken, and in follow-up reaction and post processing behaviour In work, it is difficult to remove color;In addition, not adding water in the post processing of the method prepare compound IV and follow-up hydrolysis, adopt With directly plus ethanol and concentrated hydrochloric acid method, and in this two-step reaction, used ethyl acetate, dichloromethane, methyl alcohol, ethanol Etc. several organic solvents, and the hydrochloride of compound V easy moisture absorption in filter process, cause filtration difficulty, also can not possibly be real Construction Industry.It is, thus, sought for preparing the effective ways of razaxaban.
The content of the invention
The technical problem to be solved is to overcome above-mentioned weak point, and research and design is less using organic molten Agent, post processing is simple, reduces technological operation step, effectively reduces the preparation method of the razaxaban of environmental pollution, is suitable for work Industry metaplasia is produced.
The invention provides a kind of preparation method of razaxaban.
The inventive method is comprised the following steps:
(1)Formula II compound(4-(Morpholine -3- ketone phenyl)- benzyq carbamate)With formula III compound(S)The chloro- 3- of -1- [(4- chlorine benzals)- amino] in the presence of organic solvent, tert-butyl alcohol lithium, coupling cyclization generates formula IV compound to -propyl- 2- alcohol ((S)- 5- { [(4- chlorine benzals)- amino]-methyl } -3- (4- morpholines -3- ketone groups-phenyl)-oxazolidine -2- ketone);
(2)The reactant of upper step reaction is not post-treated, is directly added into hydrochloric acid hydrolysis, generates Formula V compound(4-{4- [(5S) -5- (amino methyl) -2- oxos -1,3- oxazolidine -3- bases] phenyl } morpholine -3- ketone);Hydrolysis is finished, and reactant is with organic Solvent extraction, removes organic phase, retains water mutually standby;
(3)Inorganic base and Formula IV compound 5- chlorothiophene formyl chlorides are added in water phase, compound of formula I profit is obtained after reaction and is cut down Sha Ban.
In the inventive method, the alkali described in step (1) is tert-butyl alcohol lithium;The mol ratio of tert-butyl alcohol lithium and compound II is 5: 1-1:1, preferably 4:1-2:The mol ratio of 1, compound II and compound III is 1:1-1:5, preferably 1:1-1:2, You Jirong Agent is selected from dichloromethane, chloroform, toluene, preferably methyl tertbutyl ketone, dichloromethane, Formula II compound and organic solvent used Mass/volume ratio be 1:5-1:20, preferably 1:5-1:10;Reaction temperature is 60 DEG C -150 DEG C, preferably solvent refluxing temperature Degree;Reaction time is 5-20 hours, preferably 10-20 hours.
Step(2)Described concentration of hydrochloric acid is 3.7%-37%, and hydrochloric acid is 5 with the mol ratio of formula IV compound:1-1:1, water The time of solution is -5 hours 10 minutes, and preferably -1 hour 10 minutes, hydrolysising reacting temperature was 0-50 DEG C, preferably 5-30 DEG C; The described organic solvent for extraction is selected from dichloromethane, chloroform, toluene, methyl tertbutyl ketone;Extraction times are 1-3 time, The quantity of solvent for extracting every time and step(1)The volume ratio of organic solvent amount is 1:5-1:1;
Step(3)Described inorganic base is selected from potassium carbonate, sodium carbonate, saleratus, sodium acid carbonate, potassium hydroxide or hydrogen-oxygen Change sodium, preferably potassium carbonate and sodium carbonate;The consumption of inorganic base is 3 with the mol ratio of Formula IV compound:1-1:1, preferably 3: 1-2:1;The mol ratio of compound V and compound VI is 1:1-1:5, preferably 1:1-1:2;Reaction temperature is 0-50 DEG C, preferably For 0-30 DEG C;Reaction time is 1-5 hours, preferably 2-5 hours.
The effect of the present invention:
(1)A kind of organic solvent is only used in the three-step reaction of the inventive method and its post processing, due to being single organic molten Agent, therefore recovery can be easy to, so as to greatly reduce environmental pressure, reduce production cost.
(2)Step(3)The reaction of 5- chlorothiophenes formyl chloride and compound V is carried out in water phase, generally, acyl chlorides and amine Reaction, it is fat-soluble due to acyl chlorides, the reason for water is mutually difficult to disperse and acyl chlorides meets sour facile hydrolysis, be usually difficult in list Aqueous phase system realizes the reaction of acyl chlorides and amine.However, surprisingly, it was found that in single aqueous phase system, 5- chlorothiophene first Acyl chlorides has enough decentralization, and the speed of its hydrolysis is far smaller than the speed with compound V into acid amides, and the acid amides of generation exists Separate out in water, easily by simple filter operation can obtain razaxaban with higher yields, this has significant Feature and be significant progress in the synthesis technology field of razaxaban.
(3)Step(1)In, it is to ensure that the reaction of compound II is complete, using excessive compound III;Generally, After condensation ring closure reaction is finished, excessive compound III can be in follow-up acid hydrolysis step(2)In, it is hydrolyzed into amine(Formula VII Compound), impurity compound VIII is further produced in next step reaction:
But, it has surprisingly been found that the hydrolysate compound VII of residual compounds III when the present inventor implements this scheme, The Highly solvated that the simultaneous hydroxyl of its close position and amino are likely due in water phase and water is acted on, and causes its amino Reactivity is far smaller than compound V, therefore, in subsequent step(3)During reaction, just it is not detected by compound VIII's Exist.
(4)The step of the present invention program(1), due to not carrying out the post processing such as extracting and direct acid hydrolysis, so as to avoid The emulsification occurred when being difficult to the extraction evaded in prior art(Alkalescence condition)Or acid condition causes under intermediate yield The problem of drop;
(5)The present invention program operating procedure is simple, step(1)With(2)The continuous operation that realization is treated different things alike, eliminates centre The process of body.
Therefore, the inventive method greatly reduces technological operation step, and post processing is simple, only uses in reaction and its post processing Organic solvent, reduces environmental pollution, reduces production cost, is suitable for scale industrialized production, there is larger application Value.
Specific embodiment
First,(S)- 5- { [(the chloro- benzals of 4-)- amino]-methyl } -3- (4- morpholines -3- ketone groups-phenyl)-oxazolidine -2- Ketone(IV)Preparation
2nd, embodiment 1
Compound II is added in 100 milliliters of there-necked flasks(4-(Morpholine -3- ketone phenyl)- benzyq carbamate)(3.0 grams, 9.2 MM), dichloromethane(30 milliliters), add tert-butyl alcohol lithium(1.63 grams, 20.4 mMs), compound III((S)- 1- is chloro- 3-[(4- chlorine benzals)- amino] -propyl- 2- alcohol)(2.2 grams, 9.2 mMs), it is heated to reflux 20 hours, it is cooled to 10 DEG C, without Process, be directly used in next step reaction.
Embodiment 2
Compound II is added in 100 milliliters of there-necked flasks(3.0 gram, 9.2 mMs), chloroform(42 milliliters), add the tert-butyl alcohol Lithium(2.45 grams, 30.4 mMs), compound III(3.2 grams, 13.8 mMs), it is heated to reflux 15 hours, it is cooled to 20 DEG C, no Jing process, is directly used in next step reaction.
Embodiment 3
Compound II is added in 100 milliliters of there-necked flasks(3.0 grams, 9.2 mMs), methyl tertbutyl ketone(42 milliliters), plus Enter tert-butyl alcohol lithium(3.7 grams, 46.3 mMs), compound III(4.3 grams, 18.4 mMs), it is heated to reflux 20 hours, it is cooled to 0 DEG C, without process, it is directly used in next step reaction.
Embodiment 4
Compound II is added in 100 milliliters of there-necked flasks(3.0 grams, 9.2 mMs), toluene(21 milliliters), add the tert-butyl alcohol Lithium(0.76 gram, 9.2 mMs), compound III(2.2 grams, 9.2 mMs), it is heated to reflux 16 hours, it is cooled to 10 DEG C, without Process, be directly used in next step reaction.
3rd, 4- { 4- [(5S) -5- (amino methyl) -2- oxos -1,3- oxazolidine -3- bases] phenyl } morpholine -3- ketone(V)'s Prepare
Embodiment 5
In the system of embodiment 1,20 milliliters of the hydrochloric acid that concentration is 3.7% is added, stirred 20 minutes, divided and go oil phase, water phase Washed twice with dichloromethane, 10 milliliters every time.Organic phase is removed, merges water mutually standby.
Embodiment 6
In the system of embodiment 2,14 milliliters of the hydrochloric acid that concentration is 7.4% is added, stirred 15 minutes, divided and go oil phase, water phase Washed twice with chloroform, 10 milliliters every time.Organic phase is removed, merges water mutually standby.
Embodiment 7
In the system of embodiment 3,8.4 milliliters of the hydrochloric acid that concentration is 18.5% is added, stirred 30 minutes, divided and remove oil phase, water Washed twice with methyl tertbutyl ketone, 10 milliliters every time.Organic phase is removed, merges water mutually standby.
Embodiment 8
In the system of embodiment 4,12 milliliters of the hydrochloric acid that concentration is 3.7% is added, stirred 40 minutes, divided and go oil phase, water phase Washed twice with toluene, 10 milliliters every time.Organic phase is removed, merges water mutually standby.
4th, razaxaban(Rivaroxaban)(I)Preparation
Embodiment 9
In the water phase that embodiment 5 is obtained, 2.16 grams of sodium carbonate is added(20.4 mMs), stirring and dissolving, dropwise addition chemical combination VI1.665 gram of thing(9.2 mM), maintain the temperature at 5 DEG C and stir 3 hours, to filter, filter cake washing, 60 DEG C of forced air dryings are got profit Cut down 2.8 grams of husky class, three step total recoverys 70%.
Razaxaban is confirmed as after testing:
1H-NMR:(Brucker AVANCE400K, solvent D-DMSO):δ 8.994 (t, 1H), 7.702 (d, 1H), 7.577 (d, 2H), 7.422 (d, 2H), 7.198 (d, 1H), 4.867~4832 (q, 1H), 4.216~4.172 (m, 3H), 3.987~ 3.962 (m, 2H), 3.978~3.841 (m, 1H), 3.728~3.7032 (m, 2H), 3.631~3.604 (m, 2H)
13C-NMR:δ 166.437,161.283,154.569,138.929,137.548,136.964,133.747, 128.915,128.603,126.403,118.816,71.803,68.206,63.948,49.485,47.915,42.688
MS(ESI):m/z=436.17(M+H+
Embodiment 10
In the water phase that embodiment 6 is obtained, 2.54 grams of potassium carbonate is added(18.4 mMs), stirring and dissolving, dropwise addition chemical combination VI1.665 gram of thing(9.2 mM), maintain the temperature at 10 DEG C and stir 3 hours, to filter, filter cake washing, 80 DEG C of forced air dryings are obtained 3.0 grams of razaxaban, three step total recoverys 75%.
Razaxaban is confirmed as after testing.
Embodiment 11
In the water phase that embodiment 7 is obtained, 1.1 grams of NaOH is added(27.6 mMs), stirring and dissolving, dropwise addition chemical combination VI1.665 gram of thing(9.2 mM), maintain the temperature at 20 DEG C and stir 2 hours, to filter, filter cake washing, 60 DEG C of forced air dryings are obtained 2.9 grams of razaxaban crude product, three step total recoverys 72%.
Razaxaban is confirmed as after testing.
Embodiment 12
In the water phase that embodiment 8 is obtained, 1.23 grams of potassium hydroxide is added(22 mMs), stirring and dissolving, dropwise addition chemical combination VI1.665 gram of thing(9.2 mM), maintain the temperature at 30 DEG C and stir 1.5 hours, filter, filter cake washing, 80 DEG C of forced air dryings, Obtain 2.5 grams of razaxaban crude product, three step total recoverys 62%.
Razaxaban is confirmed as after testing.

Claims (4)

1. a kind of preparation method of razaxaban, it is characterised in that the method is comprised the following steps:
(1) Formula II compound (4- (morpholine -3- ketone phenyl)-benzyq carbamate) and chloro- the 3- [(4- of formula III compound (S) -1- Chlorine benzal)-amino] -propyl- 2- alcohol, in the presence of organic solvent, tert-butyl alcohol lithium, coupling cyclization generation formula IV compound ((S)- 5- { [(the chloro- benzals of 4-)-amino]-methyl } -3- (4- morpholines -3- ketone groups-phenyl)-oxazolidine -2- ketone);
(2) reactant that reaction is walked on is not post-treated, is directly added into hydrochloric acid and hydrolyzes, generation Formula V compound (4- 4- [(5S)- 5- (amino methyl) -2- oxo -1,3- oxazolidine -3- bases] phenyl } morpholine -3- ketone);Hydrolysis is finished, and reactant is extracted with organic solvent Take, remove organic phase, retain water mutually standby;
(3) inorganic base and Formula IV compound 5- chlorothiophene formyl chlorides are added in water phase, compound of formula I profit is obtained after reaction and is cut down sand Class;
The mol ratio of step (1) tert-butyl alcohol lithium and compound II is 5:1-1:1, compound II and compound III mole Than for 1:1-1:5, organic solvent is selected from dichloromethane, chloroform, toluene, methyl tertbutyl ketone;Formula II compound and described organic The mass/volume ratio of solvent is 1:5-1:20, reaction temperature is 60 DEG C -150 DEG C, and the reaction time is 5-20 hours;Step (2) institute The concentration of hydrochloric acid stated is 3.7%-37%, and hydrochloric acid is 5 with the mol ratio of formula IV compound:1-1:1, the time of hydrolysis is 10 points Clock -5 hours, hydrolysising reacting temperature is 0 DEG C -50 DEG C, and the described organic solvent for extraction is selected from dichloromethane, chloroform, first Benzene or methyl tertbutyl ketone, extraction times are 1-3 time, every time the volume ratio of the quantity of solvent of extraction and step (1) organic solvent amount For 1:5-1:1;Inorganic base described in step (3) is selected from potassium carbonate, sodium carbonate, saleratus, sodium acid carbonate, potassium hydroxide or hydrogen Sodium oxide molybdena, the consumption of inorganic base is 3 with the mol ratio of Formula IV compound:1-1:The mol ratio of 1, compound V and compound VI is 1:1-1:5, reaction temperature is 0 DEG C -50 DEG C, and the reaction time is 1-5 hours.
2. the preparation method of a kind of razaxaban according to claim 1, it is characterised in that step (1) tert-butyl alcohol lithium and The mol ratio of compound II is 4:1-2:The mol ratio of 1, compound II and compound III is 1:1-1:2, organic solvent is dichloro The mass/volume ratio of methane, Formula II compound and organic solvent used is 1:5-1:10, reaction temperature is solvent reflux temperature, Reaction time is 10-20 hours.
3. a kind of preparation method of razaxaban according to claim 1, it is characterised in that the hydrochloric acid described in step (2) It is 4 with the mol ratio of formula IV compound:1-2:1, hydrolysis time is -1 hour 10 minutes, and hydrolysising reacting temperature is 5 DEG C -30 DEG C.
4. the preparation method of a kind of razaxaban according to claim 1, it is characterised in that inorganic described in step (3) Alkali is selected from potassium carbonate or sodium carbonate;The consumption of inorganic base is 3 with the mol ratio of Formula IV compound:1-2:1, compound V and chemical combination The mol ratio of thing VI is 1:1-1:2;Reaction temperature is 0 DEG C -30 DEG C;Reaction time is 2-5 hours.
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CN109232551B (en) * 2018-10-11 2020-06-02 东南大学 Rivaroxaban isopropylidene impurity reference substance and preparation method thereof
CN110551111B (en) * 2019-08-29 2022-04-26 上海海翔医药科技发展有限公司 Preparation method of rivaroxaban intermediate

Citations (4)

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Publication number Priority date Publication date Assignee Title
CN102786516A (en) * 2012-08-21 2012-11-21 湖南师范大学 Method for synthesizing rivaroxaban
WO2012159992A1 (en) * 2011-05-20 2012-11-29 Interquim, S.A. Process for obtaining rivaroxaban and intermediate thereof
CN102827154A (en) * 2011-06-14 2012-12-19 上海科胜药物研发有限公司 New method for synthesizing rivaroxaban intermediate 4-{4-[(5S)-5-(aminomethyl)-2-oxo-1,3-oxazolidine-3-yl]phenyl}morpholine-3-ketone
WO2013120465A1 (en) * 2012-02-16 2013-08-22 Zentiva, K.S. A process for the preparation of rivaroxaban based on the use of (s)-epichlorohydrin

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012159992A1 (en) * 2011-05-20 2012-11-29 Interquim, S.A. Process for obtaining rivaroxaban and intermediate thereof
CN102827154A (en) * 2011-06-14 2012-12-19 上海科胜药物研发有限公司 New method for synthesizing rivaroxaban intermediate 4-{4-[(5S)-5-(aminomethyl)-2-oxo-1,3-oxazolidine-3-yl]phenyl}morpholine-3-ketone
WO2013120465A1 (en) * 2012-02-16 2013-08-22 Zentiva, K.S. A process for the preparation of rivaroxaban based on the use of (s)-epichlorohydrin
CN102786516A (en) * 2012-08-21 2012-11-21 湖南师范大学 Method for synthesizing rivaroxaban

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