U.S. patent application number 15/488888 was filed with the patent office on 2017-08-03 for process for the preparation of (1r,2r)-3-(3-dimethylamino-1-ethyl-2-methyl-propyl)-phenol.
The applicant listed for this patent is GRUNENTHAL GMBH. Invention is credited to Helmut Heinrich BUSCHMANN, Stefan GLADOW, Wolfgang HELL, Jorg HOLENZ, Oswald ZIMMER.
Application Number | 20170217875 15/488888 |
Document ID | / |
Family ID | 37198995 |
Filed Date | 2017-08-03 |
United States Patent
Application |
20170217875 |
Kind Code |
A1 |
HELL; Wolfgang ; et
al. |
August 3, 2017 |
PROCESS FOR THE PREPARATION OF
(1R,2R)-3-(3-DIMETHYLAMINO-1-ETHYL-2-METHYL-PROPYL)-PHENOL
Abstract
The present invention relates to a process for the preparation
of (1R,2R)-3-dimethylamino-1-ethyl-2-methyl-propyl)-phenol.
Inventors: |
HELL; Wolfgang; (Aachen,
DE) ; ZIMMER; Oswald; (Wurselen, DE) ;
BUSCHMANN; Helmut Heinrich; (Sant Just Desvern, ES) ;
HOLENZ; Jorg; (Enhorna, SE) ; GLADOW; Stefan;
(Buchs, CH) |
|
Applicant: |
Name |
City |
State |
Country |
Type |
GRUNENTHAL GMBH |
Aachen |
|
DE |
|
|
Family ID: |
37198995 |
Appl. No.: |
15/488888 |
Filed: |
April 17, 2017 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
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15096986 |
Apr 12, 2016 |
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15488888 |
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14478797 |
Sep 5, 2014 |
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15096986 |
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12374874 |
Oct 22, 2009 |
8877974 |
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PCT/EP2007/006515 |
Jul 23, 2007 |
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14478797 |
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Current U.S.
Class: |
1/1 |
Current CPC
Class: |
C07B 57/00 20130101;
C07C 213/00 20130101; C07C 213/08 20130101; C07C 221/00 20130101;
C07C 213/00 20130101; C07C 215/54 20130101; C07C 213/00 20130101;
C07C 217/62 20130101; C07C 213/08 20130101; C07C 215/54 20130101;
C07C 213/08 20130101; C07C 217/62 20130101 |
International
Class: |
C07C 213/00 20060101
C07C213/00; C07C 221/00 20060101 C07C221/00; C07C 213/08 20060101
C07C213/08 |
Foreign Application Data
Date |
Code |
Application Number |
Jul 24, 2006 |
EP |
06015338.4 |
Claims
1. A process for preparing
(1R,2R)-3-(3-dimethylamino-1-ethyl-2-methyl-propyl)-phenol, or an
acid addition salt thereof, comprising the step of (a) reacting a
compound of general formula (I), ##STR00011## wherein R represents
--C.sub.1-6-alkyl, --C.sub.3-8-cycloalkyl,
--C.sub.1-3-alkylene-phenyl, --C.sub.1-3-alkylene-naphthyl,
tetrahydropyranyl or --C(.dbd.O)--C.sub.1-6-alkyl, with ethyl
magnesium halide in an inert reaction medium under Grignard
conditions, (b) transferring the thus obtained compound of general
formula (II), ##STR00012## wherein R has the above defined meaning,
to a compound of general formula (III), ##STR00013## wherein R has
the above defined meaning, optionally in form of an acid addition
salt, (c) deprotecting the thus obtained compound of general
formula (III) to obtain
(1R,2R)-3-(3-dimethylamino-1-ethyl-2-methyl-propyl)-phenol of
formula (IV), ##STR00014## (d) optionally converting the thus
obtained (1R,2R)-3-(3-dimethylamino-1-ethyl-2-methyl-propyl)-phenol
into an acid addition salt.
2. A process according to claim 1, characterized in that R
represents methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl,
tert-butyl, n-pentyl, cyclopropyl, cyclobutyl, cyclopentyl,
cyclohexyl, cycloheptyl, benzyl, phenethyl, tetrahydropyranyl,
--C(.dbd.O)--CH.sub.3, --C(.dbd.O)--C.sub.2H.sub.5,
--C(.dbd.O)--CH(CH.sub.3).sub.2 or
--C(.dbd.O)--C(CH.sub.3).sub.3.
3. A process according to claim 1 or 2, characterized in that R
represents methyl, ethyl, cyclopropyl, cyclobutyl, cyclopentyl,
cyclohexyl, benzyl, phenethyl, tetrahydropyranyl or
--C(.dbd.O)--CH.sub.3.
4. A process according to any of claims 1 to 3, characterized in
that R represents methyl, benzyl or tetrahydropyranyl.
5. A process according to any of claims 1 to 4, characterized in
that the ethyl magnesium halide used in step (a) is the chloride or
bromide.
6. A process according to any one of claims 1 to 5, characterized
in that the inert reaction medium is selected from the group
consisting of diethyl ether, tetrahydrofuran,
2-methyltetrahydrofuran, tert-butyl-methylether, diisopropylether
or any mixture thereof.
7. A process according to any one of claims 1 to 6, characterized
in that a compound of general formula (I) was obtained by (a')
reacting a compound of general formula (V), ##STR00015## wherein R
represents --C.sub.1-6-alkyl, --C.sub.3-8-cycloalkyl,
--C.sub.1-3-alkylene-phenyl, --C.sub.1-3-alkylene-naphthyl,
tetrahydropyranyl or --C(.dbd.O)--C.sub.1-6-alkyl, with
dimethylamine hydrochloride and paraformaldehyde in an inert
reaction medium under Mannich conditions and (a'') subsequent
resolution of the thus obtained compound of general formula (VI),
##STR00016## wherein R has the above defined meaning.
8. A process according to claim 7, characterized in that R
represents methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl,
tert-butyl, n-pentyl, cyclopropyl, cyclobutyl, cyclopentyl,
cyclohexyl, cycloheptyl, benzyl, phenethyl, tetrahydropyranyl,
--C(.dbd.O)--CH.sub.3, --C(.dbd.O)--C.sub.2H.sub.5,
--C(.dbd.O)--CH(CH.sub.3).sub.2 or
--C(.dbd.O)--C(CH.sub.3).sub.3.
9. A process according to claim 7 or 8, characterized in that R
represents methyl, ethyl, cyclopropyl, cyclobutyl, cyclopentyl,
cyclohexyl, benzyl, phenethyl, tetrahydropyranyl or
--C(.dbd.O)--CH.sub.3.
10. A process according to any of claims 7 to 9, characterized in
that R represents methyl, benzyl or tetrahydropyranyl.
11. A process according to any of claims 7 to 10, characterized in
that the resolution in step (a'') is performed by reacting a
compound of general formula (VI) with a chiral acid selected from
the group consisting of L-(-)-dibenzoyl tartaric acid,
L-(-)-dibenzoyl tartaric acid.H.sub.2O and D-(-)-tartaric acid,
subsequent separation of the thus obtained salt and liberation of
the corresponding compound of general formula (I) in form of the
free base.
12. A process according to claim 11, characterized in that the
resolution is performed in an alcoholic reaction medium selected
from the group consisting of methanol, ethanol, 1-propanol,
2-propanol and any mixture thereof.
13. A process according to any of claims 1 to 12, characterized in
that the transfer according to step (b) is performed by (b')
subjecting the compound of general formula (II) to dehydration and
(b'') hydrogenation of the thus obtained compound of general
formula (VII), ##STR00017## wherein R represents --C.sub.1-6-alkyl,
--C.sub.3-8-cycloalkyl, --C.sub.1-3-alkylene-phenyl,
--C.sub.1-3-alkylene-naphthyl, tetrahydropyranyl or
--C(.dbd.O)--C.sub.1-6-alkyl, using a suitable catalyst in an inert
reaction medium in the presence of hydrogen.
14. A process according to claim 13, characterized in that R
represents methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl,
tert-butyl, n-pentyl, cyclopropyl, cyclobutyl, cyclopentyl,
cyclohexyl, cycloheptyl, benzyl, phenethyl, tetrahydropyranyl,
--C(.dbd.O)--CH.sub.3, --C(.dbd.O)--C.sub.2H.sub.5,
--C(.dbd.O)--CH(CH.sub.3).sub.2 or
--C(.dbd.O)--C(CH.sub.3).sub.3.
15. A process according to claim 13 or 14, characterized in that R
represents methyl, ethyl, cyclopropyl, cyclobutyl, cyclopentyl,
cyclohexyl, benzyl, phenethyl, tetrahydropyranyl or
--C(.dbd.O)--CH.sub.3.
16. A process according to any of claims 13 to 15, characterized in
that R represents methyl, benzyl or tetrahydropyranyl.
17. A process according to any of claims 13 to 16, characterized in
that after the dehydration step (b') the hydrogenation in step
(b'') is effected via homogeneous catalysis.
18. A process according to any of claims 13 to 17, characterized in
that the dehydration step (b') is acid-catalysed.
19. A process according to claim 18, characterized in that the acid
is selected from the group consisting of formic acid, hydrochloric
acid, sulfuric acid, methanesulfonic acid, hydrobromic acid or any
mixture thereof.
20. A process according to any of claims 13 to 16, characterized in
that the hydrogenation of step (b'') is effected via heterogeneous
catalysis.
21. A process according to claim 20, characterized in that the
catalyst used for hydrogenation is selected from the group
consisting of Raney nickel, palladium, palladium on carbon,
platinum, platinum on carbon, ruthenium on carbon or rhodium on
carbon.
22. A process according to any of claims 13 to 21, characterized in
that the reaction medium is selected from the group consisting of
diethyl ether, tetrahydrofuran, 2-methyltetrahydrofuran,
tert-butyl-methylether, diisopropylether or any mixtures
thereof.
23. A process according to any of claims 1 to 12 characterized in
that step b) is a direct replacement reaction of the OH group by H,
preferably carried out in a one-pot reaction.
Description
[0001] The present invention relates to a process for the
preparation of
(1R,2R)-3-(3-dimethylamino-1-ethyl-2-methyl-propyl)-phenol.
[0002] A class of active ingredients having excellent analgesic
effectiveness and very good tolerability are the substituted
dimethyl-(3-aryl-butyl)-amine compounds, which are known inter alia
from EP 0 693 475. In particular,
(1R,2R)-3-(3-dimethylamino-1-ethyl-2-methyl-propyl)-phenol has
proven to be a very promising candidate for the development of an
analgesic in clinical trials.
[0003] An object of the present invention was, therefore, to
provide a process which allows for the preparation of
(1R,2R)-3-(3-dimethylamino-1-ethyl-2-methyl-propyl)-phenol via a
short route with good overall yield under environmentally
acceptable conditions.
[0004] In particular, in the process of the present invention all
stereocenters can be established via substrate control with almost
exclusive formation of only a single diastereomer thus sparing
elaborate purification steps to separate stereoisomers and costly
chiral reagents, catalysts or ligands. As there are not any
undesired side products formed in the process of the present
invention, each batch can work at its optimal capacity.
[0005] The object of the present invention is met by providing a
process for preparing
(1R,2R)-3-(3-dimethylamino-1-ethyl-2-methyl-propyl)-phenol, or an
acid addition salt thereof, comprising the step of (a) reacting a
compound of general formula (I),
##STR00001##
wherein R represents --C.sub.1-6-alkyl, --C.sub.3-8-cycloalkyl,
--C.sub.1-3-alkylene-phenyl, --C.sub.1-3-alkylene-naphthyl,
tetrahydropyranyl or --C(.dbd.O)--C.sub.1-6-alkyl, with ethyl
magnesium halide in an inert reaction medium under Grignard
conditions.
[0006] Preferably R represents methyl, ethyl, n-propyl, isopropyl,
n-butyl, isobutyl, tert-butyl, n-pentyl, cyclopropyl, cyclobutyl,
cyclopentyl, cyclohexyl, cycloheptyl, benzyl, phenethyl,
tetrahydropyranyl, --C(.dbd.O)--CH.sub.3,
--C(.dbd.O)--C.sub.2H.sub.5, --C(.dbd.O)--CH(CH.sub.3).sub.2 or
--C(.dbd.O)--C(CH.sub.3).sub.3 in the compounds of general formula
(I). Particularly preferably R represents methyl, ethyl,
cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, benzyl,
phenethyl, tetrahydropyranyl or --C(.dbd.O)--CH.sub.3 in the
compounds of general formula (I). More particularly preferably R
represents methyl, benzyl or tetrahydropyranyl in the compounds of
general formula (I).
[0007] Yet more preferably R in general formula (I) represents
methyl. Thus, very preferably
(S)-3-(dimethylamino)-1-(3-methoxyphenyl)-2-methylpropan-1-one is
reacted with ethyl magnesium halide in an inert reaction medium
under Grignard conditions.
[0008] Preferably ethyl magnesium bromide or ethyl magnesium
chloride are used as ethyl magnesium halide in step a).
[0009] The reaction according to step (a) is preferably carried out
in an inert reaction medium, preferably in an organic ether, for
example, selected from the group consisting of diethyl ether,
tetrahydrofuran, 2-methyltetrahydrofuran, tert-butylmethyl ether or
any mixture thereof. The reaction is particularly preferably
carried out in tetrahydrofuran with ethyl magnesium chloride at a
concentration from 0.5 M to 2 M of the ethyl magnesium chloride.
Particularly preferably the reaction is carried out at a
concentration of 1 M or 2 M of the ethyl magnesium chloride.
[0010] Another object of the present invention is a process for
preparing
(1R,2R)-3-(3-dimethylamino-1-ethyl-2-methyl-propyl)-phenol, or an
acid addition salt thereof, comprising the step of (a) reacting a
compound of general formula (I),
##STR00002##
wherein R represents --C.sub.1-6-alkyl, --C.sub.3-8-cycloalkyl,
--C.sub.1-3-alkylene-phenyl, --C.sub.1-3-alkylene-naphthyl,
tetrahydropyranyl or --C(.dbd.O)--C.sub.1-6-alkyl, with ethyl
magnesium halide in an inert reaction medium under Grignard
conditions, (b) transferring the thus obtained compound of general
formula (II),
##STR00003##
wherein R has the above defined meaning, to a compound of general
formula (III),
##STR00004##
wherein R has the above defined meaning, optionally in form of an
acid addition salt, (c) deprotecting the thus obtained compound of
general formula (III) to obtain
(1R,2R)-3-(3-dimethylamino-1-ethyl-2-methyl-propyl)-phenol of
formula (IV),
##STR00005##
(d) optionally converting the thus obtained
(1R,2R)-3-(3-dimethylamino-1-ethyl-2-methyl-propyl)-phenol into an
acid addition salt.
[0011] Preferably R represents methyl, ethyl, n-propyl, isopropyl,
n-butyl, isobutyl, tert-butyl, n-pentyl, cyclopropyl, cyclobutyl,
cyclopentyl, cyclohexyl, cycloheptyl, benzyl, phenethyl,
tetrahydropyranyl, --C(.dbd.O)--CH.sub.3,
--C(.dbd.O)--C.sub.2H.sub.5, --C(.dbd.O)--CH(CH.sub.3).sub.2 or
--C(.dbd.O)--C(CH.sub.3).sub.3 in the compounds of general formulae
(I), (II) and (III). Particularly preferably R represents methyl,
ethyl, cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, benzyl,
phenethyl, tetrahydropyranyl or --C(.dbd.O)--CH.sub.3 in the
compounds of general formulae (I), (II) and (III). More
particularly preferably R represents methyl, benzyl or
tetrahydropyranyl in the compounds of general formulae (I), (II)
and (III).
[0012] Even more particularly preferably R represents methyl in the
general formulae (I), (II) and (III). Thus,
(S)-3-(dimethylamino)-1-(3-methoxyphenyl)-2-methylpropan-1-one (Ia)
is transformed to
(1R,2R)-3-(3-dimethylamino-1-ethyl-2-methyl-propyl)-phenol by the
following sequence of steps (scheme 1).
##STR00006##
[0013] In case R represents methyl in the general formula (III),
compound (IIIa) is preferably reacted with hydrobromic acid or
methanesulfonic acid and methionine or diisobutylaluminium hydride
in a reaction medium, preferably in a reaction medium selected from
the group consisting of diethylether, tetrahydrofuran, toluene,
2-methyltetrahydrofuran, dioxane, tert-butyl-methylether and
mixtures thereof to yield
(1R,2R)-3-(3-dimethylamino-1-ethyl-2-methyl-propyl)-phenol of
formula (IV).
[0014] In case R represents C.sub.1-6-alkyl except methyl in the
general formula (III), the respective compound of general formula
(III) is preferably reacted with hydrobromic acid or
diisobutylaluminium hydride in a reaction medium, preferably in a
reaction medium selected from the group consisting of diethylether,
tetrahydrofuran, toluene, 2-methyltetrahydrofuran, dioxane,
tert-butyl-methylether and mixtures thereof to yield
(1R,2R)-3-(3-dimethylamino-1-ethyl-2-methyl-propyl)-phenol of
formula (IV).
[0015] In case R represents tetrahydropyranyl in the general
formula (III), the respective compound of general formula (III) is
preferably reacted with at least one inorganic acid, preferably
with at least one inorganic acid selected from the group consisting
of hydrochloric acid, hydrobromic acid, sulfuric acid and
phosphoric acid, optionally in the presence of at least one salt,
preferably at least one salt selected from the group consisting of
ammonium chloride and potassium hydrogensulfate, in a reaction
medium, preferably in a reaction medium selected from the group
consisting of diethylether, tetrahydrofuran, toluene,
2-methyltetrahydrofuran, dioxane, tert-butyl-methylether, water and
mixtures thereof to yield
(1R,2R)-3-(3-dimethylamino-1-ethyl-2-methyl-propyl)-phenol of
formula (IV).
[0016] In case R represents --C-.sub.3-8-cycloalkyl in the general
formula (III), the respective compound of general formula (III) is
preferably reacted with hydrobromic acid or diisobutylaluminium
hydride in a reaction medium, preferably in a reaction medium
selected from the group consisting of diethylether,
tetrahydrofuran, toluene, 2-methyltetrahydrofuran, dioxane,
tert-butyl-methylether and mixtures thereof to yield
(1R,2R)-3-(3-dimethylamino-1-ethyl-2-methyl-propyl)phenol of
formula (IV).
[0017] In case R represents --C.sub.1-3-alkylene-phenyl or
--C.sub.1-3-alkylene-naphthyl, a compound of general formula (III)
is reacted with hydrobromic acid or diisobutylaluminium hydride in
a reaction medium, preferably in a reaction medium selected from
the group consisting of diethylether, tetrahydrofuran, toluene,
2-methyltetrahydrofuran, dioxane, tert-butyl-methylether and
mixtures thereof or in the presence of hydrogen and at least one
catalyst, preferably in the presence of at least one catalyst based
on palladium or platinum, more preferably in the presence of
palladium on charcoal, in a reaction medium, preferably in a
reaction medium selected from the group consisting of diethylether,
tetrahydrofuran, toluene, 2-methyltetrahydrofuran, dioxane,
tert-butyl-methylether and mixtures thereof to yield
(1R,2R)-3-(3-dimethylamino-1-ethyl-2-methyl-propyl)-phenol of
formula (IV).
[0018] In case R represents --C(.dbd.O)--C.sub.1-6-alkyl in the
general formula (III), the respective compound of general formula
(III) is preferably reacted with at least one inorganic acid,
preferably with at least one inorganic acid selected from the group
consisting of hydrochloric acid, hydrobromic acid, sulfuric acid
and phosphoric acid, or with at least one inorganic base,
preferably with at least one inorganic base selected from the group
consisting of sodium hydroxide, potassium hydroxide, sodium
carbonate and potassium carbonate in a reaction medium, preferably
in a reaction medium selected from the group consisting of
diethylether, tetrahydrofuran, toluene, 2-methyltetrahydrofuran,
dioxane, tert-butyl-methylether, water and mixtures thereof to
yield (1R,2R)-3-(3-dimethylamino-1-ethyl-2-methyl-propyl)-phenol of
formula (IV).
[0019] In another embodiment of the present invention the agent for
deprotecting according to step c) of the inventive process are
selected from the group consisting of iodotrimethylsilane, sodium
ethyl sulphide, lithium iodide and hydrobromic acid, preferably
hydrobromic acid.
[0020] The compound
(1R,2R)-3-(3-dimethylamino-1-ethyl-2-methyl-propyl)-phenol may be
present in form of an acid addition salt, whereby any suitable acid
capable of forming such an addition salt may be used.
[0021] The conversion of the compound
(1R,2R)-3-(3-Dimethylamino-1-ethyl-2-methyl-propyl)-phenol into a
corresponding addition salt via reaction with a suitable acid may
be effected in a manner well known to those skilled in the art.
Suitable acids include but are not limited to hydrochloric acid,
hydrobromic acid, sulphuric acid, methanesulfonic acid, formic
acid, acetic acid, oxalic acid, succinic acid, tartaric acid,
mandelic acid, fumaric acid, lactic acid, citric acid, glutamic
acid and aspartic acid. In a preferred embodiment the acid addition
salt is the hydrochloride salt.
[0022] The salt formation may preferably be effected in a suitable
solvent including diethyl ether, diisopropyl ether, alkyl acetates,
acetone, 2-butanone or any mixture thereof. Also preferably,
reaction with trimethylchlorosilane in a suitable solvent may be
used for the preparation of the hydrochloride addition salt.
[0023] Preferably a compound of general formula (I) can be obtained
by (a') reacting a compound of general formula (V),
##STR00007##
wherein R represents --C.sub.1-6-alkyl,
--C.sub.1-3-alkylene-phenyl, --C.sub.1-3-alkylene-naphthyl,
tetrahydropyranyl or --C(.dbd.O)--C.sub.1-6-alkyl, with
dimethylamine hydrochloride and paraformaldehyde in an inert
reaction medium under Mannich conditions and (a'') subsequent
resolution of the thus obtained compound of general formula
(VI),
##STR00008##
wherein R has the above defined meaning.
[0024] Preferably R represents methyl, ethyl, n-propyl, isopropyl,
n-butyl, isobutyl, tert-butyl, n-pentyl, cyclopropyl, cyclobutyl,
cyclopentyl, cyclohexyl, cycloheptyl, benzyl, phenethyl,
tetrahydropyranyl, --C(.dbd.O)--CH.sub.3,
--C(.dbd.O)--C.sub.2H.sub.5, --C(.dbd.O)--CH(CH.sub.3).sub.2 or
--C(.dbd.O)--C(CH.sub.3).sub.3 in the compounds of general formulae
(V) or (VI). Particularly preferably R represents methyl, ethyl,
cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, benzyl,
phenethyl, tetrahydropyranyl or --C(.dbd.O)--CH.sub.3 in the
compounds of general formulae (V) or (VI). More particularly
preferably R represents methyl, benzyl or tetrahydropyranyl in the
compounds of general formulae (V) or (VI).
[0025] Even more particularly preferably R represents methyl in the
general formulae (V) and (VI). Thus,
1-(3-methoxyphenyl)propan-1-one is converted to
3-(dimethylamino)-1-(3-methoxyphenyl)-2-methylpropan-1-one (VIa)
with dimethylamine hydrochloride and paraformaldehyde in an inert
reaction medium under Mannich conditions.
[0026] Preferably the resolution in step (a'') is performed by
reacting a compound of general formula (VI) with a chiral acid
selected from the group consisting of L-(-)-dibenzoyl tartaric
acid, L-(-)-dibenzoyl tartaric acid.H.sub.2O and D-(-)-tartaric
acid, subsequent separation of the thus obtained salt and
liberation of the corresponding compound of general formula (I) in
form of the free base.
[0027] It is preferred that the resolution is performed in an
alcoholic reaction medium selected from the group consisting of
methanol, ethanol, 1-propanol, 2-propanol and any mixture thereof
or in a mixture of an alcoholic reaction medium selected from the
group consisting of methanol, ethanol, 1-propanol, 2-propanol and
acetone.
[0028] Preferably transfer according to step (b) is performed by
(b') subjecting the compound of general formula (II) to dehydration
and (b'') hydrogenation of the thus obtained compound of general
formula (VII),
##STR00009##
wherein R represents --C.sub.1-6-alkyl, --C.sub.3-8-cycloalkyl,
--C.sub.1-3-alkylene-phenyl, --C.sub.1-3-alkylene-naphthyl,
tetrahydropyranyl or --C(.dbd.O)--C.sub.1-5-alkyl, using a suitable
catalyst in an inert reaction medium in the presence of
hydrogen.
[0029] Preferably R represents methyl, ethyl, n-propyl, isopropyl,
n-butyl, isobutyl, tert-butyl, n-pentyl, cyclopropyl, cyclobutyl,
cyclopentyl, cyclohexyl, cycloheptyl, benzyl, phenethyl,
tetrahydropyranyl, --C(.dbd.O)--CH.sub.3,
--C(.dbd.O)--C.sub.2H.sub.5, --C(.dbd.O)--CH(CH.sub.3).sub.2 or
--C(.dbd.O)--C(CH.sub.3).sub.3 in the compound of general formula
(II). Particularly preferably R represents methyl, ethyl,
cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, benzyl,
phenethyl, tetrahydropyranyl or --C(.dbd.O)--CH.sub.3 in the
compound of general formula (II).
[0030] More particularly preferably R represents methyl, benzyl or
tetrahydropyranyl in the compound of general formula (II).
[0031] Even more particularly preferably R represents methyl in the
compound of general formula (II). Thus,
(2S,3R)-1-(dimethylamino)-3-(3-methoxyphenyl)-2-methylpentan-3-ol
is transferred to
(2R,3R)-3-(3-methoxyphenyl)-N,N,2-trimethylpentan-1-amine by
dehydration (step (b')) and subsequent hydrogenation (step
(b'')).
[0032] Preferably the hydrogenation in step (b'') is effected via
homogeneous catalysis in the presence of hydrogen after the
dehydration step (b'). The hydrogen is preferably in gaseous form,
although it is also possible for at least part of it to be
dissolved in a liquid phase.
[0033] Preferably the homogeneous catalyst used for hydrogenation
in step (b'') according to the present invention is a transition
metal complex of rhodium, iridium or ruthenium, particularly
preferably a transition metal complex of rhodium or iridium, more
particularly a transition metal complex of rhodium with diphosphine
ligands.
[0034] Diphosphine ligands which can preferably be used are, for
example known from the following literature references: a) H.
Brunner, W. Zettlmeier, Handbook of Enantioselective Catalysis. VCH
Weinheim, 1993, vol. 2; b) R. Noyori et al. in Catalytic Asymmetric
Synthesis Second Edition (I. Ojima, Ed.), Wiley-VCH, Weinheim,
2000; c) E. N. Jacobsen, A. Pfaltz, H. Yamamoto (Eds.),
Comprehensive Asymmetric Catalysis Vol I-III, Springer Berlin,
1999, and the references cited therein.
[0035] Particularly preferably the catalyst is chosen from the
group consisting of rhodium (-)-DIPAMP
[(R,R)-(+1,2-Bis[(2-methoxyphenyl)(phenyl)phosphino]ethane],
rhodium (+)-DIPAMP
[(S,S)-(+)-1,2-Bis[(2-methoxyphenyl)(phenyl)phosphino]ethane],
rhodium R-Solphos
[R-(+)-N,N'-Dimethyl-7,7'-bis(diphenylphosphino)-3,3',4,4'-tetrahydro-8,8-
'-bi-2H-1,4-benzoxazine] and rhodium S-Solphos
[S-(-)-N,N'-Dimethyl-7,7'-bis(diphenylphosphino)-3,3',4,4'-tetrahydro-8,8-
'-bi-2H-1,4-benzoxazine]. The reaction parameters for the
homogeneous hydrogenation in step (b''), such as, for example,
pressure, temperature or reaction time, can vary over a wide
range.
[0036] Preferably, the temperature during the homogeneous
hydrogenation in step (b'') can be in each case from 0 to
250.degree. C., particularly preferably from 10 to 40.degree. C.
and very particularly preferably from 15 to 25.degree. C.
[0037] The homogeneous hydrogenation in step (b'') can preferably
be carried out at reduced pressure, at normal pressure or at
elevated pressure, preferably in the range from 0.01 to 300 bar. It
is particularly preferred to carry out the reactions under pressure
in a range from 3 to 20 bar, in particular from 8 to 12 bar.
[0038] The reaction time can vary in dependence on various
parameters, such as, for example, temperature, pressure, nature of
the compound to be reacted or the properties of the catalyst, and
can be determined for the process in question by the person skilled
in the art using preliminary tests.
[0039] The dehydration step (b') is preferably acid-catalysed.
Preferably the acid is selected from the group consisting of formic
acid, hydrochloric acid, acetic acid, sulfuric acid, hydrobromic
acid, methanesulfonic acid or any mixture thereof. It is preferable
if the acid is employed in a high concentration. Particularly
preferably the concentration of the hydrochloric acid is >20%,
preferably >30%, particularly preferably >35% by weight.
Alternatively, the acid can also be used in gaseous form.
[0040] The compounds of general formula II and VII used in step
(b') according to the present invention are preferably in liquid
phase and to that end are preferably mixed with or dissolved in a
reaction medium that is liquid under the particular reaction
conditions.
[0041] Examples of suitable reaction media are water, acetic acid,
formic acid, toluene, hydrochloric acid, sulfuric acid, hydrobromic
acid, methanesulfonic acid or any mixture thereof. Of course, it is
also possible to use mixtures or multiphase systems comprising two
or more of the above-mentioned liquids in the processes according
to the present invention. A reaction in supercritical CO.sub.2 as
solvent is also possible.
[0042] The reaction parameters for the dehydration in step (b'),
such as, for example, pressure, temperature or reaction time, can
vary over a wide range.
[0043] It is preferable if the reaction temperature in step (b') is
between 35 and 100.degree. C., particularly preferably 45 and
80.degree. C., more particularly preferably between 50 and
60.degree. C.
[0044] The dehydration step (b') can preferably be carried out at
reduced pressure, at normal pressure or at elevated pressure,
preferably in the range from 0.01 to 300 bar. It is particularly
preferred to carry out the reactions under pressure in a range from
0.5 to 5 bar, in particular from 0.5 to 1.5 bar.
[0045] The reaction time can vary in dependence on various
parameters, such as, for example, temperature, pressure, nature of
the compound to be reacted or the properties of the catalyst, and
can be determined for the process in question by the person skilled
in the art using preliminary tests. It is preferable if the
reaction time of step (b') is between 2 and 10 h, particularly
preferably between 3 and 8 h, more particularly preferably between
4 and 6 h.
[0046] The continuous removal of samples in order to monitor the
reaction, for example by means of gas chromatography methods, is
also possible, optionally in combination with regulation of the
corresponding process parameters.
[0047] The concentration of the acid in the reaction medium is
preferably 20 to 26 M in case of formic acid, 5 to 18 M in case of
acetic acid, 8 to 14 M in case of hydrochloric acid and 4 to 36 M,
more preferably 4 to 18 M, in case of sulfuric acid.
[0048] The particular compound of general formula (VII) obtained
can be isolated and/or purified by conventional methods known to
the person skilled in the art.
[0049] Alternatively, the dehydration step (b') can also be carried
out in the presence of at least one acidic catalyst, which can
preferably be selected from the group consisting of ion-exchange
resins, zeolites, heteropoly acids, phosphates, sulfates and
optionally mixed metal oxides.
[0050] The term catalyst within the context of the present
invention includes both catalytically active materials themselves
and inert materials that are provided with a catalytically active
material. Accordingly, the catalytically active material can, for
example, be applied to an inert carrier or can be present in a
mixture with an inert material. There come into consideration as
inert carrier or inert material, for example, carbon and other
materials known to the person skilled in the art.
[0051] Suitable catalysts and their preparation are known per se to
the person skilled in the art, for example from Venuto, P. B.,
Microporous Mater., 1994, 2, 297; Holderich, W. F., van Bekkum, H.,
Stud. Surf. Sci. Catal., 1991, 58, 631, Holderich, W. F.,
Proceedings of the 10th International Congress on Catalysis, 1992,
Budapest, Guczi, L. et al. (editors), "New Frontiers in Catalysis",
1993, Elsevier Science Publishers, Kozhenikov, I. V., Catal. Rev.
Sci. Eng., 1995, 37, 311, Song, X., Sayari, A., Catal. Rev. Sci.
Eng., 1996, 38, 329. The corresponding literature descriptions are
incorporated herein by reference and form part of the
disclosure.
[0052] They are suitable for the dehydration in particular those
ion-exchange resins that carry sulfonic acid groups are used.
[0053] Preference is given to ion-exchange resins based on
tetrafluoroethylene/perfluorovinyl ether copolymers, optionally in
the form of their silica nanocomposites, as are described, for
example, in the literature publications of Olah et al. Synthesis,
1996, 513-531 and Harmer et al. Green Chemistry, 2000, 7-14, the
corresponding descriptions of which are incorporated herein by
reference and form part of the disclosure. Corresponding products
are available commercially, for example under the name Nafion.RTM.,
and can also be used in that form in the processes according to the
present invention.
[0054] Preference is further given to ion-exchange resins based on
styrene/divinylbenzene copolymers, which can be prepared by
conventional processes known to the person skilled in the art.
[0055] There come into consideration for the dehydration
particularly preferably sulfonic-acid-group-carrying ion-exchange
resins based on styrene/divinylbenzene copolymers, as are marketed,
for example, under the name Amberlyst.RTM. by Rohm & Haas and
which can also be used as such in the processes according to the
present invention. These ion-exchange resins are distinguished in
particular by their stability towards water and alcohols, even at
elevated temperatures, for example from 130 to 160.degree. C.
[0056] The degree of crosslinking and the structure of these
ion-exchange resins can vary. For example, mention may be made of
macroporous ion-exchange resins having heterogeneous pore diameter
distribution, isoporous ion-exchange resins having virtually
uniform pore diameter distribution, or gel-like ion-exchange resins
having no or virtually no pores. The macroporous resins in
particular can be used with particular advantage for heterogeneous
catalysis in the liquid phase.
[0057] Particularly suitable macroporous resins having a mean pore
diameter of from 20 to 30 nm and a minimum concentration of active
groups of from 4.70 to 5.45 equivalents per kg of resin are
available commercially under the names Amberlyst.RTM. 15,
Amberlyst.RTM. 35 and Amberlyst.RTM. 36 and accordingly can also be
used in the processes according to the present invention.
[0058] It is likewise preferred to carry out the dehydration in the
presence of an acidic catalyst based on metal oxides such as, for
example, SiO.sub.2, Al.sub.2O.sub.3, TiO.sub.2, Nb.sub.2O.sub.5,
B.sub.2O.sub.3 or based on mixed metal oxides such as, for example,
Al.sub.2O.sub.3/SiO.sub.2 or Al.sub.2O.sub.3/B.sub.2O.sub.3.
[0059] Preferably, the temperature for dehydration (b') when using
an acidic catalyst as describe above is in each case from 20 to
250.degree. C., particularly preferably from 50 to 180.degree. C.
and very particularly preferably from 100 to 160.degree. C.
[0060] The ratio of acidic catalyst and compound of general formula
(II) is preferably in the range from 1:200 to 1:1, in particular
from 1:4 to 1:2.
[0061] After the dehydration, the catalyst can be separated from
the reaction mixture in a simple manner, preferably by filtration.
The particular compound of general formula (VII) obtained be
isolated and/or purified by conventional methods known to the
person skilled in the art.
[0062] Alternatively, the dehydration step (b') can also be carried
out by subjecting a compound of general formula (II) to an excess
of thionyl chloride, optionally in a reaction medium, preferably in
a reaction medium selected from the group consisting of
diethylether, tetrahydrofuran, toluene, 2-methyltetrahydrofuran,
dioxane, tert-butyl-methylether and mixtures thereof, and
subsequent heating of the thus obtained reaction mixture to
40.degree. C. to 120.degree. C., preferably to 80.degree. C. to
120.degree. C.
[0063] The hydrogenation of step (b'') can also be effected via
heterogeneous catalysis with hydrogen. The hydrogen is preferably
in gaseous form, although it is also possible for at least part of
it to be dissolved in a liquid phase.
[0064] Heterogeneous catalysis within the context of the present
invention means that the catalysts used in step (b'') are in each
case present in the solid state of aggregation.
[0065] Preferably the heterogeneous catalyst used for hydrogenation
in step (b'') according to the present invention contains one or
more transition metals, these metals can preferably be selected
from the group consisting of Cu, Ag, Au, Zn, Cd, Hg, V, Nb, Ta, Cr,
Mo, W, Fe, Ru, Os, Co, Rh, Ir, Ni, Pd, Pt, particularly preferably
from the group consisting of Ru, Rh, Pd, Pt and Ni.
[0066] The corresponding catalysts can preferably contain one or
more of the above-mentioned transition metals in the same or
different oxidation states. It may also be preferable for the
corresponding catalysts to contain one or more of the
above-mentioned transition metals in two or more different
oxidation states.
[0067] The preparation of catalysts doped with transition metals
can be carried out by conventional processes known to the person
skilled in the art.
[0068] Preferably the catalyst used for hydrogenation in step (b'')
is selected from the group consisting of Raney nickel, palladium,
palladium on carbon (1-10 wt. %, preferably 5 wt. %), platinum,
platinum on carbon (1-10 wt. %, preferably 5 wt. %), ruthenium on
carbon (1-10 wt. %, preferably 5 wt. %) and rhodium on carbon (1-10
wt. %, preferably 5 wt. %), more preferably palladium on carbon
(1-10 wt. %, preferably 5 wt. %) is used as the catalyst for
hydrogenation in step (b'').
[0069] The compounds of general formula VII or III used in step
(b'') according to the present invention are preferably in liquid
phase and to that end are preferably mixed with or dissolved in a
reaction medium that is liquid under the particular reaction
conditions.
[0070] Examples of suitable reaction media are methanol, ethanol,
isopropanol, n-butanol, n-propanol, toluene, heptane, hexane,
pentane, acetic acid, ethyl acetate, formic acid, hydrochloric
acid, hydrobromic acid, sulfuric acid and mixtures thereof. More
preferably ethanol is used as the reaction medium in step (b''). Of
course, it is also possible to use mixtures or multiphase systems
comprising two or more of the above-mentioned liquids in the
processes according to the present invention. A reaction in
supercritical CO.sub.2 as solvent is also possible.
[0071] The reaction parameters for the heterogeneous hydrogenation
in step (b''), such as, for example, pressure, temperature or
reaction time, can vary over a wide range both.
[0072] Preferably, the temperature during the heterogeneous
hydrogenation in step (b'') is in each case from 0 to 250.degree.
C., particularly preferably from 15 to 180.degree. C. and very
particularly preferably from 15 to 30.degree. C.
[0073] The heterogeneous hydrogenation in step (b'') can preferably
be carried out at reduced pressure, at normal pressure or at
elevated pressure, preferably in the range from 1 to 300 bar. It is
particularly preferred to carry out the reactions under pressure in
a range from 2 to 10 bar, in particular from 4 to 10 bar.
[0074] The reaction time can vary in dependence on various
parameters, such as, for example, temperature, pressure, nature of
the compound to be reacted or the properties of the catalyst, and
can be determined for the process in question by the person skilled
in the art using preliminary tests.
[0075] The continuous removal of samples in order to monitor the
reaction, for example by means of gas chromatography methods, is
also possible, optionally in combination with regulation of the
corresponding process parameters.
[0076] The total amount of the catalyst(s) used depends on various
factors, such as, for example, the ratio of the catalytically
active component to any inert material present, or the nature of
the surface of the catalyst(s). The optimal amount of catalyst(s)
for a particular reaction can be determined by the person skilled
in the art using preliminary tests.
[0077] The particular compound of general formula (III) obtained
can be isolated and/or purified by conventional methods known to
the person skilled in the art.
[0078] In another embodiment of the invention step b) (scheme 1) is
a direct replacement reaction of the OH group by H, preferably
carried out in a one-pot reaction. More preferably an OH is
replaced by H.
[0079] The steps according to the present invention can each be
carried out discontinuously (batchwise) or continuously, preference
being given to the discontinuous procedure.
[0080] There come into consideration as the reactor for the
discontinuous procedure, for example, a slurry reactor, and for the
continuous procedure a fixed-bed reactor or loop reactor.
[0081] In the following a process for the preparation of
(1R,2R)-3-(3-dimethylamino-1-ethyl-2-methyl-propyl)-phenol
hydrochloride is described.
EXAMPLE
Preparation of
(1R,2R)-3-(3-dimethylamino-1-ethyl-2-methyl-propyl)-phenol
Hydrochloride
##STR00010##
[0082] Step (a'): Preparation of
3-(dimethylamino)-1-(3-methoxyphenyl)-2-methyl propan-1-one
(VIa)
[0083] 1-(3-Methoxyphenyl)propan-1-one (16.42 kg, 100 mol),
dimethylamine hydrochloride (8.97 kg, 110 mol), paraformaldehyde
(3.30 kg, 110 mol) and aqueous hydrochloric acid (32% by weight,
1.14 kg) were dissolved in ethanol under a nitrogen atmosphere in a
100 L (L=liter) double jacket vessel equipped with an electrical
impeller stirrer, a gas transition line, Pt100 temperature
measuring equipment and an oil based cooling/heating system. The
reaction mixture was refluxed for 16 hours, cooled to 25.degree. C.
within 3.5 hours and stirred for 1 hour at that temperature. The
suspension was separated via a centrifuge and washed three times
with 7 L acetone each.
3-(Dimethylamino)-1-(3-methoxyphenyl)-2-methylpropan-1-one
hydrochloride was dissolved in water (12.5 L) and
tert-butyl-methyl-ether (8.5 L) and stirred at room
temperature.
[0084] Aqueous sodium hydroxide solution (32% by weight) was added
until a pH value between 10.0 and 10.5 was reached and the phases
were allowed to separate. The organic phase was distilled off under
reduced pressure until at a temperature of 40.degree. C. a pressure
of 5 mbar was reached.
3-(Dimethylamino)-1-(3-methoxyphenyl)-2-methylpropan-1-one was
obtained as a pale yellow oil (20.75 kg, 94%) that was used in the
next step without further purification.
Step (a''): Preparation of
(S)-3-(dimethylamino)-1-(3-methoxyphenyl)-2-methylpropan-1-one
(Ia)
1. a. Preparation of
(S)-3-(dimethylamino)-1-(3-methoxyphenyl)-2-methylpropan-1-one
(2R,3R)--O,O'-dibenzoyltartrate in Acetone
[0085] (2R,3R)--O,O'-Dibenzoyl tartaric acid monohydrate (189.1 g,
0.5 mol) was dissolved in acetone (550 mL) in a 2 L reaction plant
equipped with a mechanical stirrer, temperature measuring equipment
and an oil bath and
3-(dimethylamino)-1-(3-methoxyphenyl)-2-methylpropan-1-one (110.6
g, 0.5 mol) was added. The reaction mixture was heated to
35.degree. C. to 40.degree. C. for 27 hours and allowed to cool to
25.degree. C. The suspension was siphoned off and
(S)-3-(dimethylamino)-1-(3-methoxyphenyl)-2-methylpropan-1-one
(2R,3R)--O,O'-dibenzoyltartrate was obtained as a colorless solid
(233.2 g, 80.5%, ee 96.9%, ee=enantiomeric excess).
1. b. Preparation of
(S)-3-(dimethylamino)-1-(3-methoxyphenyl)-2-methylpropan-1-one
(2R,3R)--O,O'-dibenzoyltartrate in Acetone/Methanol
[0086] (2R,3R)--O,O'-Dibenzoyl tartaric acid monohydrate (2.1 kg,
5.5 mol) was dissolved in a mixture of methanol (555 mL) and
acetone (3340 mL) in a 10 L double jacket vessel equipped with an
electrical impeller stirrer, a gas transition line, Pt100
temperature measuring equipment and an oil based cooling/heating
system and
3-(dimethylamino)-1-(3-methoxyphenyl)-2-methylpropan-1-one (1.23
kg, 5.56 mol) was added. The reaction mixture was heated to
35.degree. C. to 40.degree. C. for 24 hours and allowed to cool to
25.degree. C. The suspension was siphoned off and
(S)-3-(dimethylamino)-1-(3-methoxyphenyl)-2-methylpropan-1-one
(2R,3R)--O,O'-dibenzoyltartrate was obtained as a colorless solid
(2.38 kg, 74%, ee 98.4%).
2. Preparation of
(S)-3-(dimethylamino)-1-(3-methoxyphenyl)-2-methylpropan-1-one
(Ia)
[0087]
(S)-3-(Dimethylamino)-1-(3-methoxyphenyl)-2-methylpropan-1-one
(2R,3R)--O,O'-dibenzoyltartrate (968 g, 1.67 mmol, ee 98%) was
suspended in tert-butylmethyl ether (6 L) in a 10 L double jacket
vessel equipped with an electrical impeller stirrer, a gas
transition line, Pt100 temperature measuring equipment and an oil
based cooling/heating system and diethylamine (384 g, 5.25 mol) was
added. The reaction mixture was stirred at 20.degree. C. to
25.degree. C. for 90 minutes and a solid was siphoned off. The
filtrate was concentrated at a temperature of 40.degree. C. in
vacuo until a pressure of 4 mbar was reached.
(S)-3-(dimethylamino)-1-(3-methoxyphenyl)-2-methylpropan-1-one was
obtained as a colorless oil (356.7 g, 96.5%, ee 98%).
Step (a): Preparation of
(2S,3R)-1-(dimethylamino)-3-(3-methoxyphenyl)-2-methylpentan-3-ol
(IIa)
[0088] 1. Magnesium turnings (93.57 g, 3.85 mol) were suspended in
dry ethyl ether (2 L) in a 10 L double jacket vessel equipped with
an electrical impeller stirrer, a gas transition line, Pt100
temperature measuring equipment and an oil based cooling/heating
system and ethyl bromide (25 g, 0.23 mol) was added. After the
reaction has started further ethyl bromide (438.6 g, 4.02 mol) was
added within 90 minutes below a temperature of 35.degree. C. and
the reaction mixture was stirred for another hour. The reaction
mixture was cooled to 10.degree. C. to 15.degree. C.,
(S)-3-(dimethylamino)-1-(3-methoxyphenyl)-2-methylpropan-1-one
(774.6 g, 3.5 mol, ee 98%) dissolved in diethyl ether (0.8 L) was
added and the reaction mixture was stirred for another two hours.
The reaction mixture was cooled to 5.degree. C. and aqueous
ammonium hydrogensulfate solution (10% by weight, 2 L) was added.
The phases were separated and the organic phase was concentrated in
vacuo at 40.degree. C. until a pressure of 5 mbar was reached.
(2S,3R)-1-(Dimethylamino)-3-(3-methoxyphenyl)-2-methylpentan-3-ol
(862.3 g, 98%) was obtained as a colorless oil (ee 98%).
[0089] 2.
(S)-3-(Dimethylamino)-1-(3-methoxyphenyl)-2-methylpropan-1-one
(774.6 g, 3.5 mol, ee 95%) was dissolved in dry tetrahydrofuran
(800 mL) in a 10 L double jacket vessel equipped with an electrical
impeller stirrer, a gas transition line, Pt100 temperature
measuring equipment and an oil based cooling/heating system and
ethyl magnesium bromide (2 L, 2 M in THF) was added at a
temperature of 15.degree. C. within 2 hours. The reaction mixture
was stirred for two hours at that temperature, cooled to 5.degree.
C. and aqueous ammonium hydrogen sulfate solution (10% by weight, 2
L) was added. The phases were separated and the organic phase was
concentrated in vacuo at 40.degree. C. until a pressure of 5 mbar
was reached.
(2S,3R)-1-(Dimethylamino)-3-(3-methoxyphenyl)-2-methylpentan-3-o- l
(871.1 g, 99%) was obtained as a colorless oil (ee 95%).
Step (b'): Preparation of
(R)-3-(3-methoxyphenyl)-N,N,2-trimethylpent-3-en-1-amine (VIIa)
[0090] 1.
(2S,3R)-1-(Dimethylamino)-3-(3-methoxyphenyl)-2-methylpentan-3-o- l
(754.1 g, 3 mol, ee 95%) were dissolved in acetone (5 L) in a 10 L
double jacket vessel equipped with an electrical impeller stirrer,
a gas transition line, Pt100 temperature measuring equipment and an
oil based cooling/heating system. Hydrogen chloride (110 g, 3.0
mol) was transferred within 15 minutes at a temperature of
15.degree. C. through the reaction mixture. The reaction mixture
was cooled to 0.degree. C. to 5.degree. C. and after 24 hours at
that temperature siphoned off. The product was stored at 40.degree.
C. and 10 mbar for 14 hours in a drying oven.
(2S,3R)-1-(Dimethylamino)-3-(3-methoxyphenyl)-2-methylpentan-3-ol
hydrochloride was obtained as a colorless solid (722.3 g, 83.7%, ee
100%).
[0091] 2.
(2S,3R)-1-(Dimethylamino)-3-(3-methoxyphenyl)-2-methylpentan-3-o- l
hydrochloride obtained as described above was put into a 250 mL
three necked flask equipped with a thermometer, a mechanical
compressed air stirrer, reflux condenser and oil bath and aqueous
hydrogen chloride solution (150 mL, 36% by weight) was added. The
reaction mixture was heated to 55.degree. C. for 5 hours and
allowed to cool to 20.degree. C. Aqueous sodium hydroxide solution
(33% by weight) was added while cooling until a pH value of 11 was
reached. Ethyl acetate (150 mL) was added, the reaction mixture was
stirred for 10 minutes, the phases were separated and ethyl acetate
was removed in vacuo at 60.degree. C. until a pressure of 10 mbar
was reached.
(R)-3-(3-Methoxyphenyl)-N,N,2-trimethylpent-3-en-1-amine (21 g,
90%) was obtained as an oily residue (Z/E ratio 4.5:1).
Step (b''): Preparation of
(2R,3R)-3-(3-methoxyphenyl)-N,N,2-trimethylpentan-1-amine
Hydrochloride (IIIa)
[0092] 1. (R)-3-(3-Methoxyphenyl)-N,N,2-trimethylpent-3-en-1-amine
(5 kg, 21.43 mmol) was dissolved in dry ethanol (13 L) at a
temperature of 25.degree. C. and rotational stirring frequency of
850.+-.150 per minute in a double jacket hydrogenation apparatus
equipped with a stationary mounted lid having a hydrogen and
nitrogen supply, electric gassing stirrer, Pt100 temperature
measuring equipment, inspecting glass and gas controller "Buchi
bpc". The hydrogenation apparatus was flooded with nitrogen.
Palladium on charcoal (375 g, 5% by weight) was suspended in
aqueous hydrogen chloride (675 g, 32% by weight) and added to the
reaction mixture. The hydrogenation apparatus was flooded again
with nitrogen and the reaction was carried out at a primary
pressure of hydrogen of 5 bar and an internal hydrogen pressure of
1 bar until the reaction was complete. The hydrogenation apparatus
was flooded with nitrogen and the catalyst was filtered off on a
one layered filter with filtering earth. The filtrate was
concentrated in vacuo. The residue was take up in ethyl acetate and
aqueous sodium hydroxide (10% by weight, 3.7 L) was added at
20.degree. C. until a pH value of 10 to 12 was reached. The organic
phase was concentrated in vacuo at 45.degree. C. to 50.degree. C.
until a pressure of 5 mbar was reached. The oily residue was a
mixture of
(2R,3R)-3-(3-methoxyphenyl)-N,N,2-trimethylpentan-1-amine and
(2R,3S)-3-(3-methoxyphenyl)-N,N,2-trimethylpentan-1-amine (4.5 kg,
95%, ratio 5.5 (R,R):1 (R,S)).
[0093] 2. A mixture of
(2R,3R)-3-(3-methoxyphenyl)-N,N,2-trimethylpentan-1-amine and
(2R,3S)-3-(3-methoxyphenyl)-N,N,2-trimethylpentan-1-amine (10 kg,
42.56 mol, ratio 5.5:1) was dissolved in acetone (50 L) in a 100 L
double jacket vessel equipped with an electrical impeller stirrer,
a gas transition line, Pt100 temperature measuring equipment and an
oil based cooling/heating system. Hydrogen chloride (1.55 kg, 42.51
mol) was transferred within 15 minutes at a temperature of
5.degree. C. to 25.degree. C. through the reaction mixture. The
reaction mixture was cooled to 0.degree. C. to 5.degree. C. and
centrifuged after 2 hours of stirring. The humid solid was put into
a stirring vessel, acetone (30 L) was added and the reaction
mixture was heated to reflux for 15 minutes. After cooling to
15.degree. C. to 20.degree. C. the product was centrifuged and
stored at 40.degree. C. to 50.degree. C. and 150 mbar for 14 hours
in a drying oven.
(2R,3R)-3-(3-Methoxyphenyl)-N,N,2-trimethylpentan-1-amine
hydrochloride (7.17 kg, 63%) was obtained as a colorless solid with
a diastereomeric excess of 100%).
Step (c): Preparation of
(1R,2R)-3-(3-dimethylamino-1-ethyl-2-methyl-propyl)-phenol
Hydrochloride (IV)
[0094] 1. (2R,3R)-3-(3-Methoxyphenyl)-N,N,2-trimethylpentan-1-amine
hydrochloride (5 kg, 18.4 mol) was dissolved in methane sulfonic
acid (19.5 L) in a 100 L double jacket vessel equipped with an
electrical impeller stirrer, a gas transition line, Pt100
temperature measuring equipment and an oil based cooling/heating
system and methionine (3.35 kg, 22.5 mol) was added. The reaction
mixture was stirred at a temperature of 75.degree. C. to 80.degree.
C. for 16 hours, cooled to 15.degree. C. to 25.degree. C. and water
(12.5 L) was slowly added at that temperature. Aqueous sodium
hydroxide solution (ca. 28 L, 32% by weight) was added until a pH
value of 10 to 12 was reached while the temperature was kept below
50.degree. C. Ethyl acetate (15 L) was added and the reaction
mixture was stirred for 15 minutes at a rotational stirring
frequency of 150 per minute. The phases were separated and the
organic phase was washed with water (15 L). Activated charcoal
(0.05 kg) was added to the organic phase and filtered off after 30
minutes of stirring. The solvent was removed in vacuo at a
temperature of 40.degree. C. to 50.degree. C. until a pressure of
50 mbar was reached. The residue was used in the next step without
further purification.
[0095] 2. The residue obtained as described above was dissolved in
acetone (25 L) while stirring and hydrogen chloride (0.78 kg, 21.4
mol) was transferred through the reaction mixture at a temperature
of 20.degree. C. to 25.degree. C. The suspension was stirred for 3
hours at a temperature of 0.degree. C. to 5.degree. C. and
centrifuged. Isopropanol (35 L) was added to the humid solid in a
reaction vessel and the reaction mixture was heated to reflux for
15 minutes. The reaction mixture was cooled to 0.degree. C. to
5.degree. C. and stirred for 3 hours at that temperature. After
centrifugation the product was stored at 30.degree. C. to
40.degree. C. and 150 mbar for 16 hours in a drying oven.
(1R,2R)-3-(3-Dimethylamino-1-ethyl-2-methyl-propyl)-phenol
hydrochloride (4.18 kg, 88%) were obtained as a colorless solid
with a purity of 100%.
* * * * *