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.