Title of Invention

"PROCESS FOR THE PREPARATION OF 5-FORMYLPHTHALIDE"

Abstract There is described a process for the preparation of 5-formylphthalide by hydrogenation of a halide of 5-carboxyphthalide, dissolved in a dipolar aprotic solvent, in the presence of a catalyst. Furthermore, the use of 5-formylphthalide in the preparation of citalopram is described. (FIG. NIL)
Full Text PROCESS FOR THE PREPARATION OF 5-FORMYLPHTHALIDE
The present invention concerns a process for the preparation of 5-
formylphthalide or 1-oxo-l,3-dihydro-5-isobenzofurancarbaldehyde by
hydrogenation of a halide of 5-carboxyphthalide.
The 5-formylphthalide is a known compound of formula
used as an intermediate in various processes of synthesis.
For example, in the European patent application entitled "Process for the
preparation of 5-substituted isobenzofurans", concurrently filed in the name of
the same applicant and incorporated herein by reference, 5-formylphthalide is
employed as starting material in the synthesis of l-[3-(dimethylamino)propyl]-
l-(4-fluorophenyl)-1,3-dihydro-5-isobenzofurancarbonitrile, represented by
formula
an active substance known under its International Non-proprietary Name
"citalopram", used in form of its hydrobromide for the preparation of
pharmaceutical compositions indicated for the treatment of depression.
in particular, such an application discloses a process for the preparation of
citalopram consisting of treating 5-formylphthalide with a O-substituted
hydroxylamine, submitting the O-substituted oxime thus obtained, stable in the
conditions of a Grignard reaction, to two subsequent Grignard reactions, one
with a 4-fluorophenylmagnesium halide and the other, on the product thus
obtained, with a [3-(dimethylamino)propyl]magnesium halide.
The O-substituted 3-hydroxymethyl-4-[a-hydroxy-a-3-
(dimethylamino)propyl-4-fluoro benzyl]benzaldoxime thus prepared is
cyclized, the corresponding O-substituted l-[3-(dimethylamino)propyl]-l-(4-
fluorophenyl)-l,3-dihydro-5-isobenzofurancarbaldoxime is O-deprotected and
the l-[3-(dimethylamino)propyl]-l-(4-fluorophenyl)-l,3-dihydro-5-
isobenzofurancarbaldoxime thus obtained is finally transformed into
citalopram. Alternatively, the l-[3-(dime1hylaniino)propyl]-l-(4-fluorophenyl)-
l,3-dihydro-5-isobenzofurancarbaldoxime, O-substituted with a
diphenylmethyl or triphenyhnethyl group, can be concurrently deprotected and
converted into citalopram in only one step, by treatment for example with
formic-acetic anhydride.
The only method disclosed in the literature for the preparation of 5-
formylphthalide is that described in J. Chem. Soc. (1925), 127, 2275-2297,
whereby the 5-formylphthalide is obtained, in admixture with 2,4-
diformylbenzoic acid, by chlorination of 2,4-dimethylbenzoyl chloride and
treatment of the resulting mixture with chalk in water. This synthesis, however,
does not allow the desired product to be obtained in satisfactory yields. A
further disadvantage is represented by the difficulties in isolating the desired
product from the complex reaction mixture.
Literature discloses various, generally applicable methods for the
preparation of aldehydes and, in particular, various reduction methods such as
Rosenmund reaction [Encyclopaedia of Organic Reagents for Organic
Synthesis, vol. 6, pages 3861-3865, J. Wiley & Sons (1995)]. Such a reaction
involves the hydrogenation of acyl halides, preferably chlorides, dissolved in
apolar aromatic solvents such as benzene, toluene or xylene or in ethers such as
tetrahydrofuran or dioxane, in the presence of partially inactivated catalytic
systems. Inactivation of the catalyst, made for example by addition of solutions
of sulphur dissolved in quinoline or thiourea, is necessary in order to avoid the
further reduction of the aldehyde function to primary alcohol. However, such
classic method cannot be used for the industrial preparation of 5-
formylphthalide. In fact, owing to the partial precipitation of the product and of
the consequent inactivation of the catalyst which occurs under the classic
conditions of Rosenmund, the reaction proceeds more and more slowly, until to
its stopping, before it is completed. In order to bring the conversion yields to
acceptable levels, it becomes therefore necessary to make repeated additions of
fresh catalyst, with consequent increase of costs and greater difficulties in
isolating and wasting the exhausted catalyst. Furthermore, the hydrogenation
carried out in apolar aromatic solvents or in ethers, notwithstanding the partial
inactivation of the catalyst, gives rise to the formation of significant amounts of
alcohol which, beside reducing the yields in desired product, complicates its
purification.
Finally, the formation of a precipitate in the presence of a supported
catalyst renders the final working of the reaction mixture and the recovery of 5-
formylphthalide particularly difficult.
We have now found a new, particularly simple process for preparing 5-
formylphthalide of high purity in good yields, which, in respect of the classical
reaction of Rosenmund, not only solves the above mentioned drawbacks of
poor conversion, of alcohol formation and of difficult working up, but also
makes it possible to avoid the inactivation of the catalyst and the use of
additional basic compounds.
Thus, the present invention provides, a process for the preparation of
5-formylphthalide of formula
which comprises submitting a halide of formula
wherein Hal represents chlorine, bromine or iodine, dissolved in a dipolar aprotic
solvent to hydrogenation,
where the dipolar aprotic solvent is selected from the group consisting of N,
N-dimethylformamide (DMF), N, N-dimeithylacctamide (DMA), Dimethylsulfoxide
(DMSO) and acetonitrile, and
where the hydrogenation is carried out in the presence of a hydrogenation
catalyst selected from the group consisting of palladium on charcoal(Pd/C) and
palladium on barium sulphate (Pd/BaSO4).
The halide of formula II, in its turn, can be obtained by treatment of 5-
carboxyphthalide or of an alkaline salt thereof, with a phosphor or sulphur halide such
as phosphorus pentachloride, phosphorus trichloride, phosphor tribromide, phosphoryl
chloride, sulphuryl chloride or, preferably, thionyl chloride, in an organic solvent.
A particularly preferred halide of formula II is the chloride which can be
prepared, for example, as described in J.Chem. Soc, (1931), 867-871.
The 5-carboxyphthalide starting material is known from the literature (US
3,607,884- DE 2.630.097) and can be easily prepared in very good yields for example
as described in Italian patent application MI2000A000050.
Practically, it is preferable to treat 5-carboxyphthalide, optionally dissolved in an
organic solvent, with thionyl chloride in the presence of catalytic amounts of N, N-
dimethyl formamide, heating until the development of hydrogen chloride is no longer
observed. Then, the chloride of formula II is preferably isolated and used in the present
process.
According to the present invention, the halide of formula H, preferably the
5-chloro carbonylphthalide, dissolved in a dipolar aprotic solvent, selected
among N,N-dimethyl formamide, dimethylsulfoxide, acetonitrile or,
preferably, N,N-dimethylacetamide, is hydrogenated in the presence of a
hydrogenation catalyst, preferably of palladium on a support As a suitable
support, charcoal or barium sulphate are preferably used.
Hydrogenation can be carried out at ambient pressure or under pressure,
practically at a pressure of from 1 to 5 bar, preferably between 2.5 and 3.5 bar.
The reaction temperature may generally vary from room temperature to 120°C,
advantageously between 40 and 80°C, preferably it is of about 60°C.
The concentration of the halide of formula II is generally comprised
between 50 and 90 g/l, preferably between 60 and 80 g/l, Advantageously, it is
of about 70 g/l.
The supported catalyst is generally used in a weight by weight (w : w)
ratio, in respect of the halide of formula II, comprised between 0.4:1 and
0.01:1, advantageously between 0.2:1 and 0.05:1, preferably of about 0.1:1.
After removal of the catalyst, 5-formylphmalide (I) is isolated according to
the known techniques, for example by evaporating the solvent, taking up the
residue with a suitable solvent and crystallizing, or by diluting the reaction
mixture with a suitable solvent and recovering the precipitated product.
According to the process of the present invention, 5-formylphthalide (I) is
prepared in a sufficiently pure state for its use as intermediate, and in
satisfactory global yields, generally higher than 60%.
According to its preferential aspect, the present invention provides a
process for the preparation of the 5-formylphthalide (I) which comprises
submitting the 5-chlorocarbonyl phthalide, dissolved in N,N-
dimethylacetamide, to hydrogenation in the presence of 5% Pd/BaSO4 the
catalyst : 5-chlorocarbonylphthalide (w : w) ratio being of about 0.1:1, at a
pressure of 3 bar and at a temperature of 60°C.
The isolation conditions are those illustrated hereinabove.
The following examples illustrate the invention without, however, limiting
1H-NMR spectra have been registered by a Varian 300 MHz spectrometer
in DMSO-d6 or CDCl3.
EXAMPLE 1
(a) 5-Chlorocarbonylphthalide
To a mixture of 1800 ml of thionyl chloride and 8.1 ml of N,N-
dimethylformamide, 750 g (4.21 moles) of 5-carboxyphthalide are added under
stirring. The mixture is heated slowly to reach an inner temperature of 60°C in
one hour, then it is kept at this temperature for another hour and finally it is
brought to the reflux. After refluxing for 6 hours, about 600 ml of thionyl
chloride are distilled off at a temperature of 80¸85°C, by replacing them by
addition of toluene. Distillation is continued for a total of 2800 ml with
concurrent replacement of the solvent by addition of 3800 ml of toluene. The
mixture is slowly cooled and, at 80°C, the crystallization of the product begins.
Cool to 10¸15°C by continuing stirring for 15 hours. The hygroscopic product
is filtered, washing with a total of 1500 ml of toluene, then it is dried under
vacuum at 55°C to give 710 g (86%) of 5-chlorocarbonylphthalide with a
purity of 99% (HPLC).
(b) 5-Formylphthalide : hydrogenation in N,N-dimethylacetamide
In a hydrogenator, 23 1 of N,N-dimethylacetamide, 1.65 Kg (8.39 moles) of
5-chloro carbonylphthalide and 200 g of 5% Pd/BaSO4 are charged, then
hydrogen is charged at 3 bar thereinto and the mixture is heated at 60±3oC for
a total of 48 hours. The mixture is cooled and, after removal of the catalyst by
filtration, concentrated under vacuum at 75°C to a solid residue. The product is
treated with 8 1 of deionized water and, at 5¸10°C under stirring, the pH of the
mixture is adjusted to 7.0¸7.5 by addition of 2.3 1 of 10% ammonium
hydroxide solution. After a 30-minute stirring, the product is filtered, washed
with deionized water and dried under vacuum at 50°C to give 885 g (65%) of
desired product having m.p. = 163¸165°C (in J. Chem. Soc. 1925, page 2290 a
m.p. = 159¸160°C is given).
1H-NMR (DMSO-d6) d ppm : 5.51 (s, 2H, CH2O), 8.00¸8.12 (m, 2H,
arom.), 8.18 (s,.lH, arom.), 10-17 (s, 1H, CHO).
EXAMPLE 2
5-Formylphthalide: hydrogenation in N,N-dimethylacetamide
To a solution of 8,58"g (0.043 mole) of 5-chlorocarbonylphthalide in 120
ml of N,N-dimethylacetamide in a hydrogenator 1 g of 5% Pd/BaSO4 is added
and hydrogen at 2.5 bar is charged thereinto. The mixture is heated to 60°C,
kept at this temperature for 40 hours at 2.5¸3 bar, then cooled, filtered to
remove the catalyst and concentrated under vacuum at 75°C. The residue is
taken up with 50 ml of deionized water, then the suspension is neutralized with
10% ammonium hydroxide solution to a pH = 7.5 and the product is filtered to
give 4.4 g (63%) of 5-fomylphthatide with m.p. = 162¸163°C.
The mixture qumoline-sulfur used to partially inactivate the catalyst in the
following comparative examples has been prepared according to Org. Synth.
Coll. 3,627.
EXAMPLE 3
Comparative example: hydrogenation in toluene
In a hydrogenator a mixture of 7 g (0.036 mole) of 5-
chlorocarbonylphthalide, 50 ml of toluene, 0.1 ml of the quinoline/sulfur
mixture and 0.7 g of previously reduced 5% Pd/BaSO4 is charged. The mixture
is hydrogenated at 80°C under 3.5 bar for 7 hours. At this point the reaction no
longer proceeds because of the co-precipitation of the formed product. Thus, it
is stopped and the mixture is filtered in the warm in order to put the product
into solution again. A second amount of 0.7 g of 5% Pd/BaSO4 is added to the
filtrate and the hydrogenation starts again under the above described
conditions. After 15 minutes, no more absorption of hydrogen is observed.
Hydrogenation is stopped and the catalyst is filtered off in the warm. After
cooling, the solution is concentrated under vacuum to a residue which is taken
up with ethyl acetate. The organic phase is washed with a 5% aqueous solution
of NaHCO3, concentrated to a little volume and the separated product is
filtered. There is obtained 4.2 g of 5-formylphthaIide with a purity (HPLC)
42% (yield 30%).
EXAMPLE 4
Comparative example: hydrogenation in tetrahydrqfuran
A mixture of 7 g (0.036 mole) of 5-chlorocarbonylphthalide, 50 ml of
tetrahydrofuran, 0.1 ml of the quinoline/sulfbr mixture and 1 g of 10% Pd/C is
hydrogenated at 3.5 bar and 35¸40°C for 3 hours. After 3 hours a stoppage of
the hydrogen absorption is observed. Thus, the mixture is cooled, diluted with
dichloromethane, filtered, and by a HPLC control the presence of equivalent
amounts of alcohol and aldehyde is observed. The mixture is concentrated
tinder vacuum and the residue is taken up with ethyl acetate. The crystalline
product is filtered and dried to obtain 4 g of 5-formylphthalide with a purity
(HPLC) = 44% (yield 30%).
EXAMPLE 5
Comparative example: hydrogenatian in dioxane
In a hydrogenator, 8,2 g (0.042 mole) of 5-chlorocarbonylphthalide, 50 ml
of dioxane and 0.77 g of 5% Pd/BaSO4 are charged and the mixture is
hydrogenated at 4 bar and 70oC for 7 hours. After this period of time, the
reaction no longer proceeds because of the co-precipitation of the formed
product; thus, the hydrogenation is stopped, the mixture is diluted with 120 ml
of tetrahydrofuran and stirred at 40°C for 20 minutes. The solid is filtered off
and the solution is concentrated to a little volume. The crystalline product is
recovered by filtration and dried to give 33 g of 5-formylphthalide with a
purity (HPLC) = 82% (yield 40%).
EXAMPLE 6
Use of 5-formylphthalide for the preparation of citalopram hydrobromide
(a) To a suspension of 35 g (0.216 mole) of 5-formylphthalide in 800 ml of
dichloro methane, 800 ml of a solution of 65.4 g of triphenylmethoxyamine
(0.25 mole) in 350 ml of dichloromethane are added in 45 minutes. After about
2 hours at 25¸27°C, the obtained solution is concentrated under vacuum to a
volume of about 100 ml, whereby the crystallization of the product begins. A
volume of 200 ml of methanol is added to the mixture, which is concentrated
again to a little volume, then it is diluted with further 300 ml of methanol and
let to stand at 20¸25oC for 2 hours to complete the crystallization. A further
volume of 700 ml of methanol is added to the think
methanol and dried under vacuum at 40°C to give 75.2 g of O-triphenylmethyl-
2-oxo-l,3-dihydro-5-isobeanzo furancarbaldoxime with m.p. = 203¸206°C and
purity (HPLC) = 95.1%. From the mother liquors, by concentration to a little
volume, further 10.9 g of product having a purity of 98.2% are recovered Total
yield: 86.1 g (90%).
lH-NMR (CDC13) d ppm : 5.23 (s, 2H, CH2O), 7.22-7.40 (m, 15H, arom.,
triphenylmethyl), 7.58 (m, 1H, arom., phthalide), 7.83 (d, 1H, arom.,
phthalide), 838 (s, 1H, CH=N).
(b) To a solution of 25 g (0.06 mole) of O-triphenylmethyl-2-oxo-l,3-
dihydro-5-isobenzo furancarbaldoxime in 125 ml of tetrahydrofuran, 92.8 ml
of a 14.5% solution of 4-fluoro pnenylmagnesium bromide in tetrahydrofuran
are slowly added in 3 hours and a half, at 15°C and under nitrogen atmosphere.
After a control by HPLC to verify that the unreacted starting material is lower
than 2% (area), the mixture is slowly cooled to 10°C, then 65 ml of a 30%
solution of [3-(dimemylamino)propy]magnesium chloride in tetrahydrofuran
are slowly added at 5¸10°C thereinto. After a HPLC control showing that the
content in diol is of 23.1 g, 1400 g of a 15% aqueous solution of ammonium
chloride is added at 5¸10°C to the mixture under stirring. Said mixture is
stirred for 30 minutes, then the phases are separated. The aqueous phase is
extracted with 150+130 ml of toluene, the organic phase is concentrated and
the residue is finally taken up with 200 ml of toluene. The toluene phases are
collected, treated with 200 ml of deionized water and the pH is adjusted to 3.0
by addition of acetic acid. The phases are separated and the organic one is
extracted with a mixture of 120 ml of acetic acid and 190 ml of deionized
water. The aqueous phase containing the diol in form of its salt is collected
and, under stirring, 300 ml of toluene are added thereinto, then the pH of the
mixture is brought to about 10 by addition of 30% aqueous ammonium
hydroxide. The phases are separated, the organic one is collected and the
aqueous phase is extracted with 2 x 60 ml of toluene. The collected toluene
phases are washed with 3 x 60 ml of deionized water. The organic phase is
concentrated under vacuum at about 50°C and 27.2 g (75%) of O-
fluorobenzyl]benzaldoxime as a light yellow product with a purity (HPLC) =
94.5% are obtained.
1H-NMR (CDCl3) d ppm : 1.45¸1.75 (2m, 2H, CH2-CN), 4.07 and 4.31
(2d, 2H, CH2O), 6,92 (pseudo t, 2H, H in ortho to F), 7.20¸7.40 (m, 20H,
arom), 8.22 (s,1H, CH=CN).
(c) To a solution of 23.3 g (0.039 mole) of O-triphenylmethyl-3-
hydroxymethyl-4-[a-hydroxy-a-3-(dimethylamino)propyl-4-
fluorobenzyl]benzaldoxime in 260 ml of dichloro methane, 25.5 ml of
triethylamine are added. The mixture is cooled to 5°C and a solution of 6 ml of
methanesulfonyl chloride in 300 ml of dichloromethane are slowly (in 3 hours)
added thereinto, by keeping the temperature at 5¸7°C. After a control by
HPLC showing a content in diol lower than 2%, 230 ml of 0.1N NaOH are
added to the reaction mixture, by maintaining its temperature at 0¸5°C. The
phases are separated, the organic phase is washed three times with a mixture of
200 ml of deionized water and 25 ml of a 20% solution of sodium chloride.
The aqueous phase is discarded, the organic one is collected and concentrated
under vacuum to a solid residue. Thus, 22.3 g (97%) of O-triphenyhnethyl-1-
[3-(dimethylamino)propyl]-l-(4-fluorophenyl)-l,3-dihydro-5-
isobenzofurancarbaldoxime as a pale yellow product with purity (HPLC) =
90.8%.
lH-NMR (CDCl3) 8 ppm : 1.15+1.55 (2m, 2H, CH2-C-N), 2.15 (s, 6H,
N(CH3)2), 2.15¸2.35 (m, 4H, CH2-C-CH2-N), 5.08 (2d, 2H, CH2-O), 6.93
(pseudo t, 2H, H in ortho to F), 7.20¸7.50 (m, 20H, arom.), 8.23 (s, 1H,
CH=N).
(d) A mixture of 640 ml of acetic anhydride and 220 ml of 98% formic acid
is heated one hour at 110°C, then it is cooled to 60°C and 17.6 g (0.03 mole) of
O-triphenyhnethyl-1 -[3-(dimethylamino)propyl]-l -(4-fluorophenyl)-1,3-
dihydro-5-isobenzofurancarbaldoxime are added thereinto. The obtained
mixture is heated at 120°C for 5 hours. After a HPLC control showing a
conversion into citalopram of 88.2% (area), the mixture is concentrated under
vacuum at 60°C to an oil which is taken up with 170 ml of ethyl acetate and
addition of about 10 ml of 10% HC1. The phases are separated, the aqueous one
is extracted with 170 ml of ethyl acetate. The organic phases are discarded and
the pH of the aqueous phase is brought to 8.5 by addition of about 45 ml of
10% aqueous ammonium hydroxide; 90 ml of toluene are added thereinto and
the mixture is kept under stirring for 2 hours. The phases are separated and the
aqueous one is extracted with 3 x 100 ml of toluene. The toluene phases are
collected and concentrated under vacuum at 50°C to a solid residue which is
taken up with 35 ml of dichloromethane and loaded on a SiO2 column by
eluting with a dichloromethane/methanol = 9/1 mixture. By concentration of
the eluate, 7.1 g (73%) of citalopram base with purity (HPLC) = 98.2% is
obtained.
(e) To a solution of 7.1 g of citalopram base in 35 ml of dichloromethane a
solution of 7 g of sodium metabisulphite in 25 ml of deionized water is added.
The pH of the mixture is brought to 6.0 by addition of 5% aqueous ammonium
hydroxide, then the organic phase is discarded, the aqueous one is brought to
pH = 7.0 by addition of sodium bicarbonate and extracted with 2 x 10 ml of
toluene. The organic extracts are concentrated under vacuum at 50°C to give
6.9 g of citalopram base with purity (HPLC) = 99.8% (area). These 6.9 g of
citalopram base are dissolved in 30 ml of acetone and 48% HBr is added to the
solution to a pH of 4¸5. The obtained solution is evaporated under vacuum at
45°C and the residue is crystallized with acetone to give 5.6 g of citalopram
hydrobromide with purity (HPLC) = 99.4% (area) and m.p. 185¸187°C.
1H-NMR (DMSO-de) d ppm : 1.30¸1.60 (m, 2H, C-CH2-C-N); 2.21 (t,
2H, CH2-C-C-N); 2.66 (s, 6H, N(CH3)2); 3.01 (t, 2H, CH2-N); 5.20 (2d, 2H,
CH2O); 7.18 (pseudo t, 2H, H in ortho to F); 7.55¸7.62 (dd, 2H, H in meta to
F); 7.27¸7.83 (m, 3H, H arom., phthalide); 9.22 (br s, 1H, NH exchanged with
D2O).
We Claim :
1. A process for the preparation of 5-formylphthalide of formula
which comprises submitting a halide of formula
wherein Hal represents chlorine, bromine or iodine, dissolved in a dipolar aprotic
solvent to hydrogenation, where the dipolar aprotic solvent is selected from the group
consisting of N, N-dimethylformamide (DMF), N, N-dimeithylacctamide (DMA),
Dimethylsulfoxide (DMSO) and acetonitrile, and
where the hydrogenation is carried out in the presence of a hydrogenation catalyst
selected from the group consisting of palladium on charcoal(Pd/C) and palladium on
barium sulphate (Pd/BaSO4).
2. A process as claimed in claim 1,wherein said dipolar aprotic solvent is N,
N-dimethyl acetamide.
3. A process as claimed in claim 1, wherein said hydrogenation catalyst is
used, compared to the halide of formula II in a weight/weight ratio between 0.2:1 and
0.05:1.
4. A process as claimed in claim 1, wherein the halide of formula II is 5-
chlorocarbonyl phthalide.
5. A process as claimed in claim 1, wherein the concentration of the halide of
formula II is between 60 and 80 g/1.
6. A process as claimed in claim 1, wherein the hydrogenation is carried out at
a pressure between 1 and 5 bar.
7. A process as claimed in claim 1, wherein the hydrogenation is carried out at
a temperature between room remperantre and 120 °C.
8. A process as claimed in claim 3, where said hydrogenation catalyst is used,
compared to the halide of formula II in a weight/ weight ratio of 0.1:1.
9. A process as claimed in claim 5, wherein the concentration of the halide of
formula II is 70g/l.
10. A process as claimed in claim 6, wherein the hydrogenation is carried out at
a pressure between 2.5 and 3.5 bar.
The present invention provides, a process for the preparation of
5-formylphthalide of formula

which comprises submitting a halide of formula
wherein Hal represents chlorine, bromine or iodine, dissolved in a dipolar aprotic
solvent to hydrogenation,
where the dipolar aprotic solvent is selected from the group consisting of N,
N-dimethylformamide (DMF), N, N-dimeithylacctamide (DMA), Dimethylsulfoxide
(DMSO) and acetonitrile, and
where the hydrogenation is carried out in the presence of a hydrogenation
catalyst selected from the group consisting of palladium on charcoal(Pd/C) and
palladium on barium sulphate (Pd/BaSO4).

Documents:

00130-kolnp-2004-abstract.pdf

00130-kolnp-2004-assignment.pdf

00130-kolnp-2004-claims.pdf

00130-kolnp-2004-correspondence.pdf

00130-kolnp-2004-description (complete).pdf

00130-kolnp-2004-form 1.pdf

00130-kolnp-2004-form 18.pdf

00130-kolnp-2004-form 3.pdf

00130-kolnp-2004-form 5.pdf

00130-kolnp-2004-gpa.pdf

00130-kolnp-2004-letter patent.pdf

00130-kolnp-2004-reply first examination report.pdf


Patent Number 216830
Indian Patent Application Number 00130/KOLNP/2004
PG Journal Number 12/2008
Publication Date 21-Mar-2008
Grant Date 19-Mar-2008
Date of Filing 04-Feb-2004
Name of Patentee INFOSINT S.A.
Applicant Address VIA CANTONALE 658A, CH-7745 POSHIAVO CANTONI DELGRIGIONAL, SWITZERLAND.
Inventors:
# Inventor's Name Inventor's Address
1 COTTICELLI GIAVANNI VIA PENATI 8,1-20063 CERNUSCO SUL NAVIGLIO, ITALY
2 DALL ! ASTA LEONE VIA FRIULI11,1-20135 MILANO, ITALY
PCT International Classification Number C07D307/80
PCT International Application Number PCT/EP02/08551
PCT International Filing date 2002-07-29
PCT Conventions:
# PCT Application Number Date of Convention Priority Country
1 01830518.5 2001-08-02 EUROPEAN UNION