Process for the removal of a silyloxy protecting group from...

Organic compounds -- part of the class 532-570 series – Organic compounds – Heterocyclic carbon compounds containing a hetero ring...

Reexamination Certificate

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Reexamination Certificate

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06509479

ABSTRACT:

THIS APPLICATION IS A 371 OF PCT/IB00/00105 FILED FEB. 2, 2000.
FIELD OF THE INVENTION
This invention relates to a novel method for the removal of a slilyl protecting group from the 4-hydroxy group of tetrahydropyran-2-ones, which method is particularly suitable in the process for the preparation of simvastatin and derivatives and analogs thereof.
BACKGROUND OF THE INVENTION
Lovastatin, pravastatin, simvastatin, mevastatin, atorvastatin, fluvastatin, cervastatin, derivatives and analogs thereof are known as HMG-CoA reductase inhibitors and are used as antihypercholesterolemic agents. The majority of them are produced by fermentation using microorganisms of different species identified as species belonging to Aspergillus, Monascus, Nocardia, Amycolatopsis, Mucor or Penicillium genus, and some are obtained by treating the fermentation products using the methods of chemical synthesis (simvastatin) or they are the products of total chemical synthesis (atorvastatin, fluvastatin).
Processes for the preparation of simvastatin and derivatives and analogs thereof generally involve silyl group protection of the 4-hydroxy group which must be eventually removed, typically in the last step of the synthetic route. In the literature processes for the deprotection (desylation) are disclosed using either tetra-n-butylammonium fluoride in acetic acid (U.S. Pat. No. 4,444,7184) or in acetic/trifluoroacetic acid (EP 0 349 063), or with hydrogen fluoride in pyridine (EP 0 349 063), or in acetonitrile (EP 0 331 240). In one of more recent processes (EP 0 444 888) the deprotection has been accomplished with boron trifluoride etherate. The deprotection may also be accomplished using methanesulfonic acid that causes opening of the lactone ring which necessitates the introduction of a lactonization step into the synthesis step.
Use of hydrogen fluoride on a large scale should be avoided due to its strong corrosive and toxic properties. Tetra-n-butylammonium fluoride is less corrosive and toxic, however, it is very expensive and its use strongly increases the cost of the process for the preparation of the final product. Additionally, it imposes a problem in regeneration of the solvents since the fluoride ions remain both in the aqueous and organic phases which is undesirable in view of the ecology and the economy of the process itself. Boron trifluoride etherate is a highly inflammable fluid which diminishes its usable value in the industrial process. Apart from the aforementioned, a number of colored by-products formed during the deprotection reaction result from using the above procedures. Since it is the final step in the synthesis and the final product should be of pharmaceutically acceptable purity, it is desirable the final product of the synthesis is as pure as possible thereby avoiding the introduction of additional isolation steps, such as recrystallization, chromatography or extraction. In the process of purification of the desired final product side products, which by their chemical and physical properties are very similar to the final product, also impose a problem and it is very difficult to separate them from the final product in the industrially acceptable procedure.
DESCRIPTION OF THE INVENTION
In order to solve the above problems of the prior art, the present invention provides a novel deprotection method for the preparation of a compound of the following formula (I)
wherein
R
1
and R
2
are independently hydrogen or alkyl with one to ten C atoms;
R
3
and R
4
are independently hydrogen or alkyl with one to three C atoms;
R
5
is hydrogen, halogen or alkyl with one to three C atoms;
wherein the method comprises contacting ammonium fluoride or ammonium hydrogen difluoride with a compound of formula (II)
wherein
R
1
′, R
2
′ and R
3
′ may be the same or different and may denote alkyl, aryl or aralkyl; and
R represents:
wherein R
1
, R
2
, R
3
, R
4
and R
5
are as defined above;
in an organic solvent to yield said compound of formula (I).
The above method is carried out as one of the steps in the preparation of simvastatin and derivatives and analogs thereof.
The instant invention is advantageous over the prior art because of negligible corrosion to pilot plant and smaller contents of colored side products generated in the deprotection step. Use of the present invention makes the process of synthesis of simvastatin and derivatives and analogs thereof economically and ecologically acceptable, since used ammonium fluoride or ammonium hydrogen difluoride completely remains in the toluene phase and is not distributed into all solvents such as tetra-n-butylammonium fluoride, thus reducing the problems of solvent regeneration and making the process ecologically more acceptable. Also, the quantities of used solvents are considerably smaller in comparison with the conventional procedures.
The process of deprotection, the subject of the present invention, comprises the contacting of a compound of formula II dissolved in an organic solvent with ammonium fluoride or ammonium hydrogen difluoride.
The organic residues R
1
′, R
2
′ and R
3
′ of the silyloxy protecting group of the compound of formula II may, independently from each other, denote alkyl, aryl or aralkyl. The alkyl group is preferably a lower, straight chain or branched alkyl group, such as methyl, ethyl, n-propyl or iso-propyl and t-butyl; the aryl group is preferably phenyl; and the aralkyl group is preferably triphenylmethyl, benzyl, xylyl and tolyl. Examples for the silyloxy protecting group include t-butyldimethylsilyloxy, trimethylsilyloxy, triethylsilyloxy, isopropyldimethyl-silyloxy, (triphenylmethyl)-dimethylsilyloxy, t-butyldiphenylsilyloxy, methyldiisopropylsilyloxy, tribenzylsilyloxy, tri-p-xylylsilyloxy, triiso-propylsilyloxy or triphenylsilyloxy.
Compounds of formula II may be prepared according to the procedures disclosed in U.S. Pat. No. 4,444,784. The protection reaction is described therein for t-butyldimethylsilyl as the silyloxy protecting group by using a reaction with the corresponding t-butyldimethyl-chlorosilane, but other protecting groups can be prepared in an analogous manner with the corresponding alkyl, aryl and/or laralkyl substituted chlorosilane.
The reaction of deprotection is carried out at an approprLiate temperature, suitably in the range of 30° to 80° C. and preferably in the range of 40° to 50° C., for an appropriate time, for example for 2 to 8 hours.
The organic solvent is preferably an organic acid or a mixture of an organic acid with another organic solvent. As the organic acid, acetic acid is particularly perferred, but other organic acids can be used as well, such as methanoic acid, trifluoroacetic acid and others, or mixtures thereof with organic solvents such as an acetic acid/ethyl acetate mixture.
The mole ratio of a compound of formula II to ammonium fluoride and ammonium.hydrogen difluoride, respectively, may vary between 1 to 5 and 1 to 15, and preferably between 1 to 8 and to 1 to 12.
The desired reaction product (I) is then isolated and/or purified from the reaction mixture by suitable methods. These methods preferably include extraction steps and crystallization or precipitation steps. In particular, combined double or multiple extraction steps may be carried out, wherein one type of extraction specifically removes non-polar impurities, whereas another type of extraction specifically removes polar impurities. For example, the reaction mixture is first extracted with an alkane solvent such as n-heptane, n-pentane and petrolether, aimed at extracting the non-polar impurities, and the product is then suitably re-extracted, preferably with toluene or a toluene/ethyl acetate mixture. The resulting organic phases are washed with an aqueous medium such as aqueous sodium hydroxide carbonate solution, the organic solvent such as toluene is removed, e.g. by means of evaporation on a rotary evaporator, and the desired substance is then allowed to crystallize from a suitable solvent or solvent mixture. Accordingly, crystallization can be effected, for exa

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