High purity...

Organic compounds -- part of the class 532-570 series – Organic compounds – Amino nitrogen containing

Reexamination Certificate

Rate now

  [ 0.00 ] – not rated yet Voters 0   Comments 0

Details

C564S305000, C564S338000, C514S650000, C514S646000

Reexamination Certificate

active

06335469

ABSTRACT:

The invention relates to high purity (1R,2S,4R)-(−)-2-[(2′-{N,N-dimethylamino}-ethoxy)]-2-[phenyl]-1,7,7-tri-[methyl]-bicyclo[2.2.1]heptane and pharmaceutically acceptable acid addition salts thereof and a process for the preparation of these compounds as well as medicaments containing 1 or more of these compounds and their use.
The 2-(E)-butenedioate (1:1) salt (fumarate) of (1R,2S,4R)-(−)-2-[(2′-{N,N-dimethylamino)-ethoxy)]-2-[phenyl]-1,7,7-tri-[methyl]-bicyclo[2.2.1]heptane of Formula
is a known anxiolytic active principle having the INN “deramciclane fumarate”.
The compound of Formula I falls under the general Formula I of Hungarian patent No. 179,164 but has not been actually and explicitly disclosed in this patent specification, nor the preparation thereof has been exemplified. According to Hungarian patent No. 179,164 the alkanol amine cycloalkyl ethers of its general Formula I are prepared by reacting (+)-1,7,7-tri-[methyl]-bicyclo[2.2.1]heptane-2-one, i. e. (+)-camphor of Formula
with the corresponding organic metal compound, subjecting the adduct obtained to hydrolysis and introducing onto the hydroxy group of the product obtained the basic side chain by etherification. As organic metal compound a Grignard compound or an organic alkali metal compound, preferably lithium or sodium compound, is used.
The preparation of the compound of Formula I has been actually disclosed in Hungarian patent No. 212,574. The essence of this process is that purification of the product is carried out at a later stage of the synthesis. According to the process (+)-camphor of Formula II is subjected to Grignard reaction with phenyl magnesium bromide in diethyl ether to give (1R,2S,4R)-(−)-2-[phenyl]-1,7,7-tri-[methyl]-bicyclo[2.2.1]heptane-2-ol of Formula
with a yield of 28% (according to GC). The compound (1R,2S,4R)-(−)-2-[phenyl]-1,7,7-tri-[methyl]-bicyclo[2.2.1]heptane-2-ol of Formula III is in the reaction mixture and is not isolated. The complex is decomposed, the reaction mixture is converted without purification into the sodium salt by reaction with sodium amide or sodium hydride and the sodium salt obtained is reacted with anhydrous (2-{chloro}-ethyl)-dimethylamine in toluene as medium. The reaction mixture contains beside the base (1R,2S,4R)-(−)-2-[(2′-{N,N-dimethylamino}-ethoxy)]-2-[phenyl]-1,7,7-tri-[methyl]-bicyclo[2.2]heptane of Formula I (being present in an amount of 20 to 30% ) a considerable amount of impurities and starting materials, e.g. unreacted (+)-camphor of Formula II, (1R,2S,4R)-(−)-2-[phenyl]-1,7,7-tri-[methyl]-bicyclo[2.2.1]heptane-2-ol, 1,7,7-tri-[methyl]-bicyclo[2.2.1]heptane-2-ol and biphenyl, triphenyl impurities, etc. The base (1R,2S,4R)-(−)-2-[(2′-{N,N-dimethylamino}-ethoxy)]-2-[phenyl]-1,7,7-tri-[methyl]-bicyclo[2.2.1]heptane of Formula I is separated from said contaminations by extraction with aqueous tartaric acid, whereupon the base is set free and the fumarate salt is formed. The total amount of unreacted (+)-camphor of Formula II and (1R,2S,4R)-(−)-2-[phenyl]-1,7,7-tri-[methyl]-bicyclo[2.2.1]heptane-2-ol of Formula III remains in the organic phase of the tartaric acid extraction step, which can be re-used in the Grignard reaction after removing the solvent and water (i.e. it can be re-circulated into the process). Thus the (+)-camphor used can be more efficiently utilized; without re-circulation only about 16% by weight of the (+)-camphor used can be utilized, while in case of a one-fold and three-fold re-circulation this value is increased to 22% by weight and 25% by weight, respectively.
It is very important and is to be emphasized that a considerable part of (+)-camphor of Formula II used in the Grignard reaction does not react and this starting material cannot be technically removed from the desired product because of the physical properties of (+)-camphor and the lability of the compound (1R,2S,4R)-(−)-2-[phenyl]-1,7,7-tri-[methyl]-bicyclo[2.2.1]heptane-2-ol of Formula III formed since compound (1R,2S,4R)-(−)-2-[phenyl]-1,7,7-tri-[methyl]-bicyclo[2.2.1]heptane-2-ol of Formula III is susceptible to decomposition. For this reason according to the process disclosed in Hungarian patent No. 212,574 the alkylation step always takes place in the presence of (+)-camphor of Formula II.
The aforesaid gives rise to the drawbacks of the process disclosed in Hungarian patent No. 212,574. The alkali hydrides and amides used in the first step of the alkylation reaction form salts not only with the alcohol (1R,2S,4R)-(−)-2-[phenyl]-1,7,7-tri-[methyl]-bicyclo[2.2.1]heptane-2-ol of Formula III but also with (+)-camphor of Formula II and other compounds containing an active hydrogen atom being present in the reaction mixture. For this reason beside the desired compound (1R,2S,4R)-(−)-2-[(2′-{N,N-dimethylamino}-ethoxy)3-2-[phenyl]-1,7,7-tri-[methyl]-bicyclo[2.2.1]heptane of Formula I further alkylated derivatives formed, e.g. from unreacted (+)-camphor, are obtained and the desired compound (1R,2S,4R)-(−)-2-[(2′-{N,N-dimethylamino}-ethoxy)]-2-[phenyl]-1,7,7-tri-methyl]-bicyclo[2.2.1]heptane of Formula I is to be recovered from a mixture containing such impurities and also unreacted compounds (+)-camphor and (1R,2S,4R)-(−)-2-[phenyl]-1,7,7-tri-[methyl]-bicyclo[2.2.1]heptane-2-ol of Formulae II and III. The crude compound (1R,2S,4R)-(−)-2-[(2′-{N,N-dimethylamino}-ethoxy)]-2-[phenyl]-1,7,7-tri-[methyl]-bicyclo[2.2.1]heptane of Formula I can only be purified, though incompletely, by means of recrystallization from dimethyl formamide. However, with the aid of said recrystallization only non-basic contaminations can be completely removed, which do not form salts.
A further disadvantage of recrystallization from dimethyl formamide is that the traces of the solvent cannot be removed from the desired pharmaceutical active principle to the required extent. In this regard it is to be noted that according to ICH (International analytical requirements accepted by the US, Japan and the EU) the limit of dimethyl formamide is 880 ppm (0.088% by weight). The reason for that the dimethyl formamide cannot be removed to such an extent but a greater amount of it remains in the product is the high boiling point of dimethyl formamide, on the one hand, and the sensitivity of (1R,2S,4R)-(−)-2-[(2′-{N,N-dimethylamino}-ethoxy)]-2-[phenyl]-1,7,7-tri-[methyl]-bicyclo[2.2.1]heptane of Formula I to thermal treatment, on the other hand.
It has been found that in case of the alkylation reaction of (1R,2S,4R)-( )-)-2-[phenyl]-1,7,7-tri-[methyl]-bicyclo[2.2.1]heptane-2-ol of Formula III carried out with (2-{chloro}-ethyl)-dimethylamine (+)-camphor of Formula II being always present gives rise to the formation of considerable amounts of by-products, e.g. (1R,3S,4R)-3-[(2′-(N,N-dimethylamino}-ethyl)]-1,7,7-tri-[methyl]-bicyclo[2.2.1]heptane-2-one of Formula
The by-product (1R,3S,4R)-3-[(2′-{N,N-dimethylamino}-ethyl)]-1,7,7-tri-[methyl]-bicyclo[2.2.1]heptane-2-one of Formula V is formed as follows: under the conditions used in the etherification reaction (+)-camphor of Formula II forms an alkali

LandOfFree

Say what you really think

Search LandOfFree.com for the USA inventors and patents. Rate them and share your experience with other people.

Rating

High purity... does not yet have a rating. At this time, there are no reviews or comments for this patent.

If you have personal experience with High purity..., we encourage you to share that experience with our LandOfFree.com community. Your opinion is very important and High purity... will most certainly appreciate the feedback.

Rate now

     

Profile ID: LFUS-PAI-O-2816675

  Search
All data on this website is collected from public sources. Our data reflects the most accurate information available at the time of publication.