Title of Invention	"PROCESS FOR PURIFYING 20 (S)-CAMPTOTHECINE CONTAMINATED BY A VINYL-CAMPTOTHECINE DERIVATIVE"
Abstract	Process for purifying 20(S)-camptothecine contaminated by a vinyl-camptothecine derivative, which comprises the following steps: (a) combining an aqueous base and a starting material containing 20(S)-camptothecine, which is a natural plant product consisting essentially of a mixture of the compounds of formula (I), wherein R1 is ethyl or vinyl, thereby converting the lactone ring of the 20(S)-camptothecine into a carboxylate salt; (b) hydrogenating the resulting mixture in the presence of a transition metal catalyst at a temperature of 10 °C to 40 °C and at a pressure of 0.9 bar to 5.0 bar; (c) acidifying the aqueous phase of step (b) at a temperature of 0 °C to 100 CC, thereby forming camptothecine crystals; (d) adding at least one polar aprotic solvent at a temperature of 30 °C to 120 °C; and (e) separating off the 20(S)-camptothecine crystals of the compound of formula (I), wherein R1 is ethyl.

Title of Invention

"PROCESS FOR PURIFYING 20 (S)-CAMPTOTHECINE CONTAMINATED BY A VINYL-CAMPTOTHECINE DERIVATIVE"

Abstract

Process for purifying 20(S)-camptothecine contaminated by a vinyl-camptothecine derivative, which comprises the following steps: (a) combining an aqueous base and a starting material containing 20(S)-camptothecine, which is a natural plant product consisting essentially of a mixture of the compounds of formula (I), wherein R1 is ethyl or vinyl, thereby converting the lactone ring of the 20(S)-camptothecine into a carboxylate salt; (b) hydrogenating the resulting mixture in the presence of a transition metal catalyst at a temperature of 10 °C to 40 °C and at a pressure of 0.9 bar to 5.0 bar; (c) acidifying the aqueous phase of step (b) at a temperature of 0 °C to 100 CC, thereby forming camptothecine crystals; (d) adding at least one polar aprotic solvent at a temperature of 30 °C to 120 °C; and (e) separating off the 20(S)-camptothecine crystals of the compound of formula (I), wherein R1 is ethyl.

Full Text	The present invention relates to process for purifying 20(S)-camptothecine contaminated by a vinyl-camptothecine derivative. The invention relates to a process for purifying 20(S)-camptothecine contaminated by a vinyl-camptothecine derivative. Background to the invention 20(S)-camptothecine (20(S)-CPT) is a natural alkaloid of formula (I) (Formula Removed) wherein R1 denotes ethyl. 20(S)-CPT and its derivatives, being topoisomerase I inhibitors, have tumour-inhibiting properties (e.g. Giovanelle, B.C. et ah, Cancer Research, 51: 302-3055, 1991, European Patent applications EP 0 074 256, EP 0 088 642, US Patents US 4,473,692, US 4,545,880, US 4,604,463 and International Patent Application WO 92/05785). 20(S)-CPT can be obtained as a crude product from the Chinese tree Camptotheca acuminata (Nyssaceae) (Wall M. et ah, J. Am. Chem. Soc. 88: 3888-3890, 1966) or from the Indian tree Nothapodytes foetida (nimmoniana) (formerly known as: Mappiefoetida Miers) (Govindachari, T.R. et al., Phytochemistry 11: 3529-3531, 1972), inter alia. These crude products, particularly the one obtained from Nothapodytes foetida, contain 20(S)-CPT contaminated by a CPT derivative of formula (I) wherein R1 denotes vinyl (20-vinyl-CPT). Traditionally, the crude products are purified by complex chromatographic methods or by converting the camptothecine into the aqueous phase and eliminating impurities by extraction with water-insoluble solvents (e.g WO 94/19353). However, contamination by 20-vinyl-CPT cannot be efficiently dealt with by these methods The problem of the present invention is therefore to provide a process which allows the 20(S)-CFT starting product to be purified without using complex chromatographic methods. Description of the invention Surprisingly, it has been found that 20(S)-CPT can be virtually completely freed from contamination with 20-vinyl-CPT by first treating the starting material with an aqueous base, hydrogenating and subsequently acidifying it and then isolating the product. The invention thus relates to a process for purifying 20(S)-camptothecine which comprises ihe following steps (a) combining an aqueous base and a starting material containing 20(S)-camptothecine, thereby converting the lactone ring of the 20(S)-camptothecine into a carboxylate salt, (b) hydrogenating the resulting mixture in the presence of a transition metal catalyst; ( c) acidifying the aqueous phase, thereby forming camptothecine crystals; (d) adding a polar aprotic solvent, and (e) separating off the camptothecine crystals The invention further relates to a process for preparing 20(S)-camptothecine of formula (I) wherein R1 denotes ethyl, from 20-vinyl-camptothecine of formula (I) wherein R1 denotes vinyl, which comprises the following steps: (a) combining an aqueous base and the starting material containing 20(S)-camptothecine, forming a compound of formula (II), (Figure Removed) wherein R1 denotes vinyl, and Met denotes a metal; (b) hydrogenatmg the resulting mixture in the presence of a transition metal catalyst; (c) acidifying the aqueous phase to form camptothecme crystals; (d) adding at least one polar aprotic solvent; and (e) separating off the camptothecine crystals. [)eta^ed_d,escnpj:ion of the invention The term "starting material containing camptothecine " as used above and hereinafter refers to a contaminated material containing 20(S)-CPT, crude camptothecine, camptothecine-containing plant extracts, synthetic camptothecine, derivatives of camptothecine as described for example in International Patent Application WO 92/05785, or reaction products containing camptotheci ne Preferably, the starting material is a natural crude product which is obtained in particular from Vothapodyies foetidu. As a rule, it is a mixture of the compound of formula (I) wherein R1 denotes ethyl, and the compound of formula (I) wherein R1 denotes vinyl. It generally contains 0.9 ro 1 :; wt •-%, preferably 1.0 to 1.4 wt.-% of the vinyl compound. In addition, the starting material may contain other camptothecine derivatives such as, for example, 9-methoxy-CPT, 10-methoxy-CPT. 11-methoxy-CPT. 10-hydroxy-CPT and 11-hydroxy-CPT. As a rule, the starting material contains up to 1 wt.-% of one or more of these additional CPT derivatives, particularly 0,2 to 0.8 wt-% of 9-methoxy-CPT. The term "aqueous base" as used above and hereinafter in connection with step (a) of the purification process according to the invention relates to a base which generates enough hydroxide ions in the aqueous medium, preferably in pure water, to convert the lactone group of the camptothecine derivatives contained in the starting material completely into the corresponding hydroxycarboxylates. Metal hydroxides are preferred, particularly alkali metal or alkaline earth metal hydroxides such as lithium hydroxide, sodium hydroxide, potassium hydroxide or calcium hydroxide. Sodium hydroxide is most preferred. The metal hydroxide is preferably used in the form of a dilute aqueous solution, preferably in the form of a 1 to 25 %. particularly a 3 to 10 % aqueous solution. As a rule, sufficient metal hydroxide is used to make the camptothecine derivatives go completely into solution, preferably. ! to 20 mol, mure preferably 5 to 15 mol, particularly 7.5 to 12.5 mol of metal hydroxide are used per 1 mol of starting material. In step (b) a transition metal catalyst, preferably a heterogeneous transition metal catalyst, particularly platinum, platinum oxide, nickel, palladium or rhodium on a carrier material such as activated charcoal or aluminium oxide is added to the resulting mixture. Palladium on activated charcoal containing 1 to 15 wt-%, preferably 2 to 10 wt-%, particularly about 5 wt.-% of palladium is particularly preferred. The quantity of transition metal catalyst is selected so as to ensure total hydrogenation of the vinylic CPT derivative. Preferably, 0.01 to 0.50 parts by weight, particularly 0.02 to 0.10 parts by weighs of transition metal catalyst (including carrier materials) are used, based on 1 part by weight of the starting material. The resulting mixture is subjected to the action of hydrogen gas, preferably at a temperature of - 20 °C to 100 "C, particularly 10 °C to 40 °C, most preferably at about room temperature. 'The hydrogen pressure is not critical per se; the hydrogenation is preferably carried out at normal pressure or at slightly raised pressure, particularly at 0.9 to 5.0 bar, most preferably at about 1 bar. Under these conditions, hydrogenation is generally complete within 1 to 20 hours, preferably 4 to 15 hours, particularly 6 to 10 hours. After the hydrogenation has ended, the transition metal catalyst is preferably eliminated by filtration, and the resulting reaction mixture is acidified in step (c). The acidification can be done with an inorganic or organic acid. Preferred acids are inorganic acids such as HC1, HBr, HI, HNCO3, H?P04, H2SO4, or aliphatic carboxylic acids such as acetic acid and trifluoroacetic acid or mixtures of these acids, particularly concentrated hydrochloric acid. Using the chosen acid, the pH is adjusted to 3.0 to 6.0, preferably 3.5 to 5.0, particularly about 4.0 to 4.5. The reaction with the acid is generally earned out at a temperature of 0 °C to 100 °C, preferably 30 °C to 80 °C, particularly 50 °C to 60 °C. In a particularly preferred embodiment, acidification is carried out with 2 to 20 parts by weight, preferably 4 to 9 parts by weight, particularly 6 to 8 parts by weight of concentrated hydrochloric acid, based on 1 part by weight of starting material. Under the conditions described, lactonisation to form the CPT is generally complete within 10 to 180 minutes, preferably 15 to 60 hours, particularly within about 30 minutes. The reaction mixture obtained by acidification is generally in the form of a pure suspension. To improve the crystallisation in step (d) one or more polar aprotic solvents are added thereto. Suitable solvents of this kind are preferably sulphoxides such as dimethyls ulph oxide (DMSO) or amides and urea derivatives of formula (Figure Removed) wherein R2 denotes hydrogen or a C1-4 alkyl group, particularly hydrogen or methyl, R3 and R4 independently of each other denote a C1-4 alkyl group, particularly methyl, or R2 and R3 together denote a-(CJH2)m- or a -NR^CH?):!- group, while R5 denotes a C1-4 alkyl group; m is 3 or 4, particularly 3, and n is 2 or 3, particularly selected from among N,N-dimethylformamide (DMF), N,N-dimethylacetamide f DMA), N-methylpyiTolidone (NMP), N,N-dimemylethylene urea (DMEU) and N,N- climethylpropylene urea (DMPU) or mixtures of these solvents, most preferably DMF. As a rule, 10 to 100 parts by weight, preferably 20 to 80 parts by weight, particularly 30 to 50 parts by weight of the polar aprotic solvent are used, based on 1 part by weight of the starting material used. The treatment with the polar aprotic solvent may be earned out at any desired temperature. The reaction mixture is preferably stirred at a temperature of 30 °C to 120 °C, particularly 80 to 100 °C and then slowly cooled to ambient temperature. The CPT crystals thus obtained are easily separated from the liquid phase in step (e), preferably by decanting, centnfuging, spinning, squeezing out or filtration, particularly by filtration As a rule, the CPT crystals thus obtained are washed with an alcohol, preferably methanol, ethanol or isopropanol, particularly methanol, and dried. The advantage of the procedure according to the invention is the high space/time yield and the high yield and purity of the 20(S)-camptothecine produced, which is obtained without any chromatographic purification substantially free from contaminants containing vinyl groups. The Examples that follow serve to illustrate some processes for purifying camptothecine earned out by way of example They are intended only as possible methods given as examples, without restricting the invention to their content. Example J 1 0.45 g of a crude product containing camptothecine, obtained from Nothapodytes foetida, containing 1.33 % of 20-vinyl-CPT and 0.47 % of 9-methoxy-CPT, is taken up in 260 ml of a 2 N sodium hydroxide solution and 0.6 g of palladium/activated charcoal (5 %) are added. The mixture is treated with hydrogen for 8 hours at ambient temperature under a pressure of 1 bar. Then the reaction mixture is filtered and combined at 50-60 °C with 80 ml of concentrated hydrochloric acid and adjusted to a pH of 4.0 to 4.5. The suspension formed is combined with 400 ml of DMF and stirred for 2.5 hours at 90-100°C. The resulting suspension is slowly cooled to ambient temperature and filtered. The CPT crystals obtained are washed with 100 ml of methanol and dried at 55°C in vacua. 9.85 g (94.2 % of material put in) of 20(S)-camptothecine are obtained, containing less than (i 05 % of 20-vinyl-CPT and 0.11 % of 9-methoxy CPT. Example 2 10.45 g of a crude product containing camptothecine, obtained from Nothapodytes foetida, containing 1.33 % of 20-vinyl-CPT and 0.47 % of 9-methoxy-CPT is taken up in 260 ml of a 2 N sodium hydroxide solution and 0.6 g of palladium/activated charcoal (5 %) are added. The mixture is treated with hydrogen for 8 hours at ambient temperature under a pressure of 1 bar. Then the reaction mixture is filtered and combined at 50-60 °C with 300 ml of a 10% sulphuric acid and adjusted to a pH of 4.0 to 4.5. The suspension formed is combined with 500 ml of DMF and stirred for 2.5 hours at 90-1 ()0°C. The resulting suspension is slowly cooled to ambient temperature and filtered. The CPT crystals obtained are washed with IOC) ml of methanol and dried at 55°C in vacua. 9.67 g (92.6 % of material put in) of 20(S)-camptothecme are obtained, containing 0.09 % of 9-methoxy CPT, the content of 20-vinyl-CPT being below the detection threshold. We Claim: 1. Process for purifying 20(S)-camptothecine contaminated by a vinyl-camptothecine derivative, which comprises the following steps: (a) combining an aqueous base and a starting material containing 20(S)-camptothecine, which is a natural plant product consisting essentially of a mixture of the compounds of formula (I), (Formula Removed) wherein R1 is ethyl or vinyl, thereby converting the lactone ring of the 20(S)-camptothecine into a carboxylate salt; (b) hydrogenating the resulting mixture in the presence of a transition metal catalyst at a temperature of 10 °C to 40 CC and at a pressure of 0.9 bar to 5.0 bar; (c) acidifying the aqueous phase of step (b) at a temperature of 0 °C to 100 °C, thereby forming camptothecine crystals; (d) adding at least one polar aprotic solvent at a temperature of 30 °C to 120 °C; and (e) separating off the 20(S)-camptothecine crystals of the compound of formula (I), wherein R1 is ethyl. 2. Process for purifying 20(S)-camptothecine as claimed in claim 1, wherein the base in step (a) is sodium hydroxide. 3. Process for purifying 20(S)-camptothecine as claimed in one of the preceding claims, wherein the mixture obtained in step (a) is hydrogenated in the presence of a palladium catalyst at room temperature and at a pressure of about 1.0 bar. 4. Process for purifying 20(S)-camptothecine as claimed in one of the preceding claims, wherein the aqueous phase obtained in step (b) is treated with an acid selected from among HC1, HBr, HI, HNO3, H3PO4, H2SO4, acetic acid and trifluoroacetic acid or mixtures of these acids at a temperature of 30 °C to 80 °C. 5. Process for purifying 20(S)-camptothecine as claimed in one of the preceding claims, wherein the aqueous phase obtained in step (c) is treated with one or more polar aprotic solvents of formula (Formula Removed) wherein R2 is hydrogen or a C1-4 alkyl group; R3 and R4 independently of each other are a C1-4 alkyl group; or R2 and R3 together denote a -(CH2)m- or a -NR5-(CH2)n- group, while R5 is a C1-4 alkyl group; m is 3 or 4; and n is 2 or 3, at a temperature of 30 °C to 120 °C. 6. Process for purifying 20(S)-camptothecine as claimed in claim 5, wherein the polar aprotic solvent is selected from among N,N-dimethylformamide (DMF), N,N-dimethylacetamide (DMA), N-methylpyrrolidone (NMP), N,N- dimethylethylene urea (DMEU) and N,N-dimethylpropylene urea (DMPU) or mixtures of these solvents. 7. Process for purifying 20(S)-camptothecine as claimed in claim 1 wherein the 20(S)-camptothecine crystals in step (e) are separated off by filtration.

Full Text

The present invention relates to process for purifying 20(S)-camptothecine contaminated by a vinyl-camptothecine derivative.
The invention relates to a process for purifying 20(S)-camptothecine contaminated by a vinyl-camptothecine derivative.
Background to the invention
20(S)-camptothecine (20(S)-CPT) is a natural alkaloid of formula (I)
(Formula Removed)

wherein R1 denotes ethyl.
20(S)-CPT and its derivatives, being topoisomerase I inhibitors, have tumour-inhibiting properties (e.g. Giovanelle, B.C. et ah, Cancer Research, 51: 302-3055, 1991, European Patent applications EP 0 074 256, EP 0 088 642, US Patents US 4,473,692, US 4,545,880, US 4,604,463 and International Patent Application WO 92/05785).
20(S)-CPT can be obtained as a crude product from the Chinese tree Camptotheca acuminata (Nyssaceae) (Wall M. et ah, J. Am. Chem. Soc. 88: 3888-3890, 1966) or from the Indian tree Nothapodytes foetida (nimmoniana) (formerly known as: Mappiefoetida Miers) (Govindachari, T.R. et al., Phytochemistry 11: 3529-3531, 1972), inter alia.
These crude products, particularly the one obtained from Nothapodytes foetida, contain 20(S)-CPT contaminated by a CPT derivative of formula (I) wherein R1 denotes vinyl (20-vinyl-CPT).
Traditionally, the crude products are purified by complex chromatographic methods or by converting the camptothecine into the aqueous phase and eliminating impurities by extraction

with water-insoluble solvents (e.g WO 94/19353). However, contamination by 20-vinyl-CPT cannot be efficiently dealt with by these methods
The problem of the present invention is therefore to provide a process which allows the 20(S)-CFT starting product to be purified without using complex chromatographic methods.
Description of the invention
Surprisingly, it has been found that 20(S)-CPT can be virtually completely freed from contamination with 20-vinyl-CPT by first treating the starting material with an aqueous base, hydrogenating and subsequently acidifying it and then isolating the product.
The invention thus relates to a process for purifying 20(S)-camptothecine which comprises
ihe following steps
(a) combining an aqueous base and a starting material containing 20(S)-camptothecine,
thereby converting the lactone ring of the 20(S)-camptothecine into a carboxylate salt, (b) hydrogenating the resulting mixture in the presence of a transition metal catalyst; ( c) acidifying the aqueous phase, thereby forming camptothecine crystals;
(d) adding a polar aprotic solvent, and
(e) separating off the camptothecine crystals
The invention further relates to a process for preparing 20(S)-camptothecine of formula (I) wherein R1 denotes ethyl, from 20-vinyl-camptothecine of formula (I) wherein R1 denotes vinyl, which comprises the following steps:
(a) combining an aqueous base and the starting material containing 20(S)-camptothecine, forming a compound of formula (II),
(Figure Removed)

wherein
R1 denotes vinyl, and

Met denotes a metal;
(b) hydrogenatmg the resulting mixture in the presence of a transition metal catalyst;
(c) acidifying the aqueous phase to form camptothecme crystals;
(d) adding at least one polar aprotic solvent; and
(e) separating off the camptothecine crystals.
[)eta^ed_d,escnpj:ion of the invention
The term "starting material containing camptothecine " as used above and hereinafter refers to a contaminated material containing 20(S)-CPT, crude camptothecine, camptothecine-containing plant extracts, synthetic camptothecine, derivatives of camptothecine as described for example in International Patent Application WO 92/05785, or reaction products containing camptotheci ne
Preferably, the starting material is a natural crude product which is obtained in particular from Vothapodyies foetidu. As a rule, it is a mixture of the compound of formula (I) wherein R1 denotes ethyl, and the compound of formula (I) wherein R1 denotes vinyl. It generally contains 0.9 ro 1 :; wt •-%, preferably 1.0 to 1.4 wt.-% of the vinyl compound. In addition, the starting material may contain other camptothecine derivatives such as, for example, 9-methoxy-CPT, 10-methoxy-CPT. 11-methoxy-CPT. 10-hydroxy-CPT and 11-hydroxy-CPT. As a rule, the starting material contains up to 1 wt.-% of one or more of these additional CPT derivatives, particularly 0,2 to 0.8 wt-% of 9-methoxy-CPT.
The term "aqueous base" as used above and hereinafter in connection with step (a) of the purification process according to the invention relates to a base which generates enough hydroxide ions in the aqueous medium, preferably in pure water, to convert the lactone group of the camptothecine derivatives contained in the starting material completely into the corresponding hydroxycarboxylates. Metal hydroxides are preferred, particularly alkali metal or alkaline earth metal hydroxides such as lithium hydroxide, sodium hydroxide, potassium hydroxide or calcium hydroxide. Sodium hydroxide is most preferred.

The metal hydroxide is preferably used in the form of a dilute aqueous solution, preferably in the form of a 1 to 25 %. particularly a 3 to 10 % aqueous solution. As a rule, sufficient metal hydroxide is used to make the camptothecine derivatives go completely into solution, preferably. ! to 20 mol, mure preferably 5 to 15 mol, particularly 7.5 to 12.5 mol of metal hydroxide are used per 1 mol of starting material.
In step (b) a transition metal catalyst, preferably a heterogeneous transition metal catalyst, particularly platinum, platinum oxide, nickel, palladium or rhodium on a carrier material such as activated charcoal or aluminium oxide is added to the resulting mixture. Palladium on activated charcoal containing 1 to 15 wt-%, preferably 2 to 10 wt-%, particularly about 5 wt.-% of palladium is particularly preferred.
The quantity of transition metal catalyst is selected so as to ensure total hydrogenation of the vinylic CPT derivative. Preferably, 0.01 to 0.50 parts by weight, particularly 0.02 to 0.10 parts by weighs of transition metal catalyst (including carrier materials) are used, based on 1 part by weight of the starting material.
The resulting mixture is subjected to the action of hydrogen gas, preferably at a temperature of - 20 °C to 100 "C, particularly 10 °C to 40 °C, most preferably at about room temperature.
'The hydrogen pressure is not critical per se; the hydrogenation is preferably carried out at normal pressure or at slightly raised pressure, particularly at 0.9 to 5.0 bar, most preferably at about 1 bar.
Under these conditions, hydrogenation is generally complete within 1 to 20 hours, preferably 4 to 15 hours, particularly 6 to 10 hours.
After the hydrogenation has ended, the transition metal catalyst is preferably eliminated by filtration, and the resulting reaction mixture is acidified in step (c). The acidification can be done with an inorganic or organic acid. Preferred acids are inorganic acids such as HC1, HBr, HI, HNCO3, H?P04, H2SO4, or aliphatic carboxylic acids such as acetic acid and trifluoroacetic acid or mixtures of these acids, particularly concentrated hydrochloric acid. Using the chosen acid, the pH is adjusted to 3.0 to 6.0, preferably 3.5 to 5.0, particularly about 4.0 to 4.5. The

reaction with the acid is generally earned out at a temperature of 0 °C to 100 °C, preferably 30 °C to 80 °C, particularly 50 °C to 60 °C.
In a particularly preferred embodiment, acidification is carried out with 2 to 20 parts by weight, preferably 4 to 9 parts by weight, particularly 6 to 8 parts by weight of concentrated hydrochloric acid, based on 1 part by weight of starting material.
Under the conditions described, lactonisation to form the CPT is generally complete within 10 to 180 minutes, preferably 15 to 60 hours, particularly within about 30 minutes.
The reaction mixture obtained by acidification is generally in the form of a pure suspension. To improve the crystallisation in step (d) one or more polar aprotic solvents are added thereto. Suitable solvents of this kind are preferably sulphoxides such as dimethyls ulph oxide (DMSO) or amides and urea derivatives of formula
(Figure Removed)
wherein
R2 denotes hydrogen or a C1-4 alkyl group, particularly hydrogen or methyl,
R3 and R4 independently of each other denote a C1-4 alkyl group, particularly methyl, or
R2 and R3 together denote a-(CJH2)m- or a -NR^CH?):!- group, while
R5 denotes a C1-4 alkyl group;
m is 3 or 4, particularly 3, and
n is 2 or 3,
particularly selected from among N,N-dimethylformamide (DMF), N,N-dimethylacetamide
f DMA), N-methylpyiTolidone (NMP), N,N-dimemylethylene urea (DMEU) and N,N-
climethylpropylene urea (DMPU) or mixtures of these solvents, most preferably DMF.
As a rule, 10 to 100 parts by weight, preferably 20 to 80 parts by weight, particularly 30 to 50 parts by weight of the polar aprotic solvent are used, based on 1 part by weight of the starting material used.

The treatment with the polar aprotic solvent may be earned out at any desired temperature. The reaction mixture is preferably stirred at a temperature of 30 °C to 120 °C, particularly 80 to 100 °C and then slowly cooled to ambient temperature.
The CPT crystals thus obtained are easily separated from the liquid phase in step (e), preferably by decanting, centnfuging, spinning, squeezing out or filtration, particularly by filtration
As a rule, the CPT crystals thus obtained are washed with an alcohol, preferably methanol, ethanol or isopropanol, particularly methanol, and dried.
The advantage of the procedure according to the invention is the high space/time yield and the high yield and purity of the 20(S)-camptothecine produced, which is obtained without any chromatographic purification substantially free from contaminants containing vinyl groups.
The Examples that follow serve to illustrate some processes for purifying camptothecine earned out by way of example They are intended only as possible methods given as examples, without restricting the invention to their content.
Example J
1 0.45 g of a crude product containing camptothecine, obtained from Nothapodytes foetida,
containing 1.33 % of 20-vinyl-CPT and 0.47 % of 9-methoxy-CPT, is taken up in 260 ml of a
2 N sodium hydroxide solution and 0.6 g of palladium/activated charcoal (5 %) are added.
The mixture is treated with hydrogen for 8 hours at ambient temperature under a pressure of 1
bar.
Then the reaction mixture is filtered and combined at 50-60 °C with 80 ml of concentrated hydrochloric acid and adjusted to a pH of 4.0 to 4.5.
The suspension formed is combined with 400 ml of DMF and stirred for 2.5 hours at 90-100°C. The resulting suspension is slowly cooled to ambient temperature and filtered. The CPT crystals obtained are washed with 100 ml of methanol and dried at 55°C in vacua.

9.85 g (94.2 % of material put in) of 20(S)-camptothecine are obtained, containing less than (i 05 % of 20-vinyl-CPT and 0.11 % of 9-methoxy CPT.
Example 2
10.45 g of a crude product containing camptothecine, obtained from Nothapodytes foetida, containing 1.33 % of 20-vinyl-CPT and 0.47 % of 9-methoxy-CPT is taken up in 260 ml of a 2 N sodium hydroxide solution and 0.6 g of palladium/activated charcoal (5 %) are added. The mixture is treated with hydrogen for 8 hours at ambient temperature under a pressure of 1
bar.
Then the reaction mixture is filtered and combined at 50-60 °C with 300 ml of a 10% sulphuric acid and adjusted to a pH of 4.0 to 4.5.
The suspension formed is combined with 500 ml of DMF and stirred for 2.5 hours at 90-1 ()0°C. The resulting suspension is slowly cooled to ambient temperature and filtered. The CPT crystals obtained are washed with IOC) ml of methanol and dried at 55°C in vacua.
9.67 g (92.6 % of material put in) of 20(S)-camptothecme are obtained, containing 0.09 % of 9-methoxy CPT, the content of 20-vinyl-CPT being below the detection threshold.

We Claim:
1. Process for purifying 20(S)-camptothecine contaminated by a vinyl-camptothecine derivative, which comprises the following steps:
(a) combining an aqueous base and a starting material containing 20(S)-camptothecine, which is a natural plant product consisting essentially of a mixture of the compounds of formula (I),
(Formula Removed)

wherein R1 is ethyl or vinyl,
thereby converting the lactone ring of the 20(S)-camptothecine into a carboxylate salt;
(b) hydrogenating the resulting mixture in the presence of a transition metal catalyst at a temperature of 10 °C to 40 CC and at a pressure of 0.9 bar to 5.0 bar;
(c) acidifying the aqueous phase of step (b) at a temperature of 0 °C to 100 °C, thereby forming camptothecine crystals;
(d) adding at least one polar aprotic solvent at a temperature of 30 °C to 120 °C; and
(e) separating off the 20(S)-camptothecine crystals of the compound of formula (I), wherein R1 is ethyl.
2. Process for purifying 20(S)-camptothecine as claimed in claim 1, wherein the base in step (a) is sodium hydroxide.

3. Process for purifying 20(S)-camptothecine as claimed in one of the preceding claims, wherein the mixture obtained in step (a) is hydrogenated in the presence of a palladium catalyst at room temperature and at a pressure of about 1.0 bar.
4. Process for purifying 20(S)-camptothecine as claimed in one of the preceding claims, wherein the aqueous phase obtained in step (b) is treated with an acid selected from among HC1, HBr, HI, HNO3, H3PO4, H2SO4, acetic acid and trifluoroacetic acid or mixtures of these acids at a temperature of 30 °C to 80 °C.
5. Process for purifying 20(S)-camptothecine as claimed in one of the preceding claims, wherein the aqueous phase obtained in step (c) is treated with one or more polar aprotic solvents of formula
(Formula Removed)
wherein
R2 is hydrogen or a C1-4 alkyl group;
R3 and R4 independently of each other are a C1-4 alkyl group; or
R2 and R3 together denote a -(CH2)m- or a -NR5-(CH2)n- group, while
R5 is a C1-4 alkyl group;
m is 3 or 4; and
n is 2 or 3,
at a temperature of 30 °C to 120 °C.
6. Process for purifying 20(S)-camptothecine as claimed in claim 5, wherein
the polar aprotic solvent is selected from among N,N-dimethylformamide
(DMF), N,N-dimethylacetamide (DMA), N-methylpyrrolidone (NMP), N,N-

dimethylethylene urea (DMEU) and N,N-dimethylpropylene urea (DMPU) or mixtures of these solvents.
7. Process for purifying 20(S)-camptothecine as claimed in claim 1 wherein the 20(S)-camptothecine crystals in step (e) are separated off by filtration.

Documents:

1197-DELNP-2003-Abstract-(01-05-2009).pdf

1197-DELNP-2003-Abstract-(22-08-2008).pdf

1197-DELNP-2003-Abstract-05-12-2008.pdf

1197-delnp-2003-abstract.pdf

1197-DELNP-2003-Claims-(01-05-2009).pdf

1197-DELNP-2003-Claims-(22-08-2008).pdf

1197-DELNP-2003-Claims-05-12-2008.pdf

1197-delnp-2003-claims.pdf

1197-DELNP-2003-Correspondence-Others-(01-05-2009).pdf

1197-DELNP-2003-Correspondence-Others-(11-05-2009).pdf

1197-DELNP-2003-Correspondence-Others-(22-08-2008).pdf

1197-DELNP-2003-Correspondence-Others-05-12-2008.pdf

1197-delnp-2003-correspondence-others.pdf

1197-DELNP-2003-Description (Complete)-(01-05-2009).pdf

1197-delnp-2003-description (complete)-22-08-2008.pdf

1197-delnp-2003-description (complete).pdf

1197-DELNP-2003-Form-1-(01-05-2009).pdf

1197-DELNP-2003-Form-1-(22-08-2008).pdf

1197-DELNP-2003-Form-1-22-08-2008.pdf

1197-delnp-2003-form-1.pdf

1197-delnp-2003-form-18.pdf

1197-DELNP-2003-Form-2-(01-05-2009).pdf

1197-DELNP-2003-Form-2-(22-08-2008).pdf

1197-delnp-2003-form-2.pdf

1197-DELNP-2003-Form-3-(01-05-2009).pdf

1197-DELNP-2003-Form-3-(11-05-2009).pdf

1197-DELNP-2003-Form-3-(22-08-2008).pdf

1197-DELNP-2003-Form-3-05-12-2008.pdf

1197-delnp-2003-form-3.pdf

1197-delnp-2003-form-5.pdf

1197-DELNP-2003-GPA-(22-08-2008).pdf

1197-delnp-2003-gpa.pdf

1197-delnp-2003-pct-210.pdf

1197-delnp-2003-pct-304.pdf

1197-delnp-2003-pct-306.pdf

1197-delnp-2003-pct-308.pdf

1197-delnp-2003-pct-332.pdf

1197-delnp-2003-pct-409.pdf

1197-DELNP-2003-Petition-137-(22-08-2008).pdf

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Patent Number

234211

Indian Patent Application Number

1197/DELNP/2003

PG Journal Number

23/2009

Publication Date

05-Jun-2009

Grant Date

08-May-2009

Date of Filing

30-Jul-2003

Name of Patentee

BOEHRINGER INGELHEIM PHARMA GMBH & CO. KG.,

Applicant Address

BINGER STRASSE 173, D-55216 INGLHEIM AM RHEIN, GERMANY,

Inventors:

#	Inventor's Name	Inventor's Address
1	RAINER SOBOTTA,	LUDWIG-RICHTER-STR. 6, D-55218 INGELHEIM, GERMANY
2	ARMIN WALTER RAPP	EGGIOLTSTRASSE 27, D-55411 BINGEN-DROMERSHEIM, GERMANY

PCT International Classification Number

C07D 491/04

PCT International Application Number

PCT/EP2002/01375

PCT International Filing date

2002-02-09

PCT Conventions:

#	PCT Application Number	Date of Convention	Priority Country
1	101 06 969.3	2001-02-15	Germany