Pure paliperidone and processes for preparing thereof

Abstract

The present invention provides pure paliperidone as well as purification processes to obtain thereof.

Description

FIELD OF INVENTION

The present invention relates to a process for the purification of Paliperidone from its impurities. Also, the present invention relates to pure paliperidone.

BACKGROUND

Paliperidone, 3-[2-[4-(6-fluorobenzo[d]isoxazol-3-yl)-1-piperidyl]ethyl]-7-hydroxy-4-methyl-1,5-diazabicyclo[4.4.0]deca-3,5-dien-2-one, is a 5-HT antagonist belonging to the chemical class of benzisoxazole derivatives and a racemic mixture having the following structural formula:

Paliperidone is a metabolite of Risperidone. Marketed under the name, Invega®, Paliperidone is a psychotropic agent approved in the United States for the treatment of schizophrenia.

Processes for the synthesis of Paliperidone, are described in U.S. Pat. No. 5,158,952. Another process for the synthesis of a precursor of Paliperidone, (3-(2-chloroethyl)-2-methyl-9-benzyloxy-4H-pyrido[1,2-a]-pyrimidine-4-one), is described in the above publications.

Like any synthetic compound, paliperidone can contain extraneous compounds or impurities that can come from many sources. They can be unreacted starting materials, by-products of the reaction, products of side reactions, or degradation products. Impurities in paliperidone or any active pharmaceutical ingredient (API) are undesirable and, in extreme cases, might even be harmful to a patient being treated with a dosage form containing the API.

It is also known in the art that impurities in an API may arise from degradation of the API itself, which is related to the stability of the pure API during storage, and the manufacturing process, including the chemical synthesis. Process impurities include unreacted starting materials, chemical derivatives of impurities contained in starting materials, synthetic by-products, and degradation products.

In addition to stability, which is a factor in the shelf life of the API, the purity of the API produced in the commercial manufacturing process is clearly a necessary condition for commercialization. Impurities introduced during commercial manufacturing processes must be limited to very small amounts, and are preferably substantially absent. For example, the International Conference on Harmonization of Technical Requirements for Registration for Human Use (“ICH”) Q7A guidance for API manufacturers requires that process impurities be maintained below set limits by specifying the quality of raw materials, controlling process parameters, such as temperature, pressure, time, and stoichiometric ratios, and including purification steps, such as crystallization, distillation, and liquid-liquid extraction, in the manufacturing process.

The product mixture of a chemical reaction is rarely a single compound with sufficient purity to comply with pharmaceutical standards. Side products and by-products of the reaction and adjunct reagents used in the reaction will, in most cases, also be present in the product mixture. At certain stages during processing of the API, paliperidone, it must be analyzed for purity, typically, by HPLC, TLC or GC analysis, to determine if it is suitable for continued processing and, ultimately, for use in a pharmaceutical product. The API need not be absolutely pure, as absolute purity is a theoretical ideal that is typically unattainable. Rather, purity standards are set with the intention of ensuring that an API is as free of impurities as possible, and, thus, are as safe as possible for clinical use. As discussed above, in the United States, the Food and Drug Administration guidelines recommend that the amounts of some impurities be limited to less than 0.1 percent.

Generally, side products, by-products, and adjunct reagents (collectively “impurities”) are identified spectroscopically and/or with another physical method, and then associated with a peak position, such as that in a chromatogram, or a spot on a TLC plate. (Strobel p. 953, Strobel, H. A.; Heineman, W. R., Chemical Instrumentation: A Systematic Approach, 3rd dd. (Wiley & Sons: New York 1989)). Thereafter, the impurity can be identified, e.g., by its relative position in the chromatogram, where the position in a chromatogram is conventionally measured in minutes between injection of the sample on the column and elution of the particular component through the detector. The relative position in the chromatogram is known as the “retention time.”

The retention time can vary about a mean value based upon the condition of the instrumentation, as well as many other factors. To mitigate the effects such variations have upon accurate identification of an impurity, practitioners use the “relative retention time” (“RRT”) to identify impurities. (Strobel p. 922). The RRT of an impurity is its retention time divided by the retention time of a reference marker. It may be advantageous to select a compound other than the API that is added to, or present in, the mixture in an amount sufficiently large to be detectable and sufficiently low as not to saturate the column, and to use that compound as the reference marker for determination of the RRT.

Two impurities of paliperidone are found: 3-[2-[4-(6-fluorobenzo[d]isoxazol-3-yl)-1-oxypiperidin-1-yl]ethyl]-7-hydroxy-4-methyl-1,5-diazabicyclo[4.4.0]deca-3,5-dien-2-one (PLP-NO) and 2-[4-(6-fluoro-1,2-benzisoxazol-3-yl)piperidin-1-carboxylicacid]-7-hydroxy-2-methyl-6,7,8,9-tetrahydro-4H-pyrido[1,2-a]pyrimidin-4-one-3-yl-ethyl ester (PLP-car):

These impurities remain in the final product.

Additionally, the commercial tablet Invega® appears to contain 0.10% of PLP-NO.

There is a need in the art for paliperidone having a higher purity, as well as purification processes for obtaining thereof.

SUMMARY OF THE INVENTION

In one embodiment, the present invention provides paliperidone containing less than about 0.2% of the impurity PLP-NO. Preferably the paliperidone of the present invention contains less than about 0.1%, more preferably less than 0.05% and most preferably less than 0.02% of the impurity PLP-NO.

In another embodiment, the present invention provides paliperidone having a total purity of at least about 98%. Preferably, the total purity is at least about 99%, most preferably at least about 99.9%.

In another embodiment, the present invention provides processes for purifying paliperidone.

DETAILED DESCRIPTION OF THE INVENTION

As used herein, the term “CMHTP” refers to 3-(2-chloroethyl)-6,7,8,9-tetrahydro-9-hydroxy-2-methyl-4H-pyrrido[1,2-a]-pyrimidin-4-one of the following structure:

As used herein, the term “FBIP” refers to 6-fluoro-3-piperidino-1,2-benisoxazole of the following structure:

As used herein, the term “PLP-NO” refers to 3-[2-[4-(6-fluorobenzo[d]isoxazol-3-yl)-1-oxypiperidin-1-yl]ethyl]-7-hydroxy-4-methyl-1,5-diazabicyclo[4.4.0]deca-3,5-dien-2-one of the following structure:

As used herein, the term “PLP-car” refers to 2-[4-(6-fluoro-1,2-benzisoxazol-3-yl)piperidin-1-carboxylicacid]-7-hydroxy-2-methyl-6,7,8,9-tetrahydro-4H-pyrido[1,2-a]pyrimidin-4-one-3-yl-ethyl ester of the following structure:

As used herein, the term “reduced pressure” refers to a pressure of under 100 mm Hg.

The present invention provides pure paliperidone, as well as processes for preparing thereof. As used herein, “pure paliperidone” refers to paliperidone containing less than about 0.2% of the impurity PLP-NO. Preferably the paliperidone of the present invention contains less than about 0.1%, more preferably less than 0.05% and most preferably less than 0.02% of the impurity PLP-NO. For example, the pure paliperidone of the present invention contains PLP-NO at less than about 0.2%, preferably less than about 0.1%, more preferably less than 0.05% and most preferably less than 0.02%. The purity is preferably measured by HPLC, and is presented as % area as shown in the HPLC chromatogram.

The pure paliperidone of the present invention has a total purity of at least about 98%. Preferably, the total purity is at least about 99%, most preferably at least about 99.9%. For example, the total purity of the pure paliperidone of the present invention can be about 98% to about 99.95%, about 98% to about 99.99%, about 99% to about 99.95%, or about 99% to about 99.99%. The purity is preferably measured as described above.

The present invention further provides a process for the purification of paliperidone. This process comprises crystallizing paliperidone from a solvent selected from the group consisting of: C_3-6 ketone or a mixture thereof with water, N-methylpyrrolidone, C_3-6 amides, halo-substituted C_6-12 aromatic hydrocarbons propylene glycole, dimethyl sulfoxide, di-methyl carbonate, C_1-4 alkyl alcohols, a mixture of a C_1-8 alkyl alcohol and water, acetonitrile or a mixture thereof with water, C_2-6 alkyl acetates or their mixture with water, cellosolve, dimethyl carbonate, polyethylene glycol methyl ether and C_2-8 ethers. The crystallization is preferably performed by dissolving paliperidone in the above solvent, preferably by heating the reaction mixture to allow complete dissolution, followed by cooling of the obtained solution, whereby paliperidone crystallizes. Preferred C_3-6 ketones are acetone, methyl ethyl ketone (MEK) and methyl iso-butyl ketone (MIBK). Preferred C_3-6 amides are dimethylacetamide and dimethylformamide. Preferred halo-substituted C_6-12 aromatic hydrocarbons are chlorobenzene and dichlorobenzene. Preferred C_1-4 alkyl alcohols are methanol, ethanol, n-propanpl, isopropanol, n-butanol, isobutanol and 2-butanol. Preferred C_2-6 alkyl acetates are ethyl acetate and isobutyl acetate. Preferred C_2-8 ethers are dibutyl ether and polyethylene glycol (PGME). Most preferably, the solvent is a mixture of acetone and water. When a mixture is used (such as acetone:water, ethanol:water etc.), the ratio between the solvents is between about 1:1 to about 3:1 by volume. The ratio of acetone to water is preferably about 3:1 by volume. Following crystallization, the obtained product is preferably recovered by filtering, washing of the obtained crystals, and drying, preferably overnight under reduced pressure.

Paliperidone obtained by the above process preferably contains PLP-NO and PLP-car, each one in an amount of less than about 0.2%. The above crystallization process may be repeated in order to further purify the obtained paliperidone, so that the PLP-NO and PLP-car levels may be reduced to less than about 0.02%.

The total purity of the paliperidone obtained by the above processes is of at least about 98%, more preferably, at least about 99% and most preferably at least about 99.9%. Preferably, the purity is measured as described above.

The present invention provides a process for the purification of paliperidone comprising crystallizing paliperidone by combining a solution of paliperidone in a first solvent with an anti-solvent. Preferably, the solution is obtained by dissolving paliperidone in dichloromethane, preferably at a reflux temperature. The obtained solution is then cooled, preferably to a temperature of about 0° C. to about 30° C., preferably to a temperature of about 20° C. to about 30° C., and most preferably of about 25° C., followed by admixing with the anti-solvent described above. The admixing may be done in any order, for example, the anti-solvent may be added to the solution, or alternatively, the solution may be added to the anti-solvent. When the hot solution is added to the anti-solvent, the temperature difference causes the fast crystallization. The addition may be added dropwise or in one volume. Preferably the first solvent is selected from the group consisting of: dichloromethane, dioxane and C_1-4 alkyl alcohols. Most preferably the first solvent is selected from the group consisting of: dichloromethane, dioxane, butanol and n-propanol. Preferably, the anti-solvent is selected from the group consisting of C_3-6 ketones, C_3-6 ethers, acetonitrile, C_3-7 straight and cyclic carbohydrates, C_6-12 aromatic carbohydrates and water. More preferably, the anti-solvent is selected from the group consisting of: methyl t-butyl ether (MTBE), MEK, acetone, MIBK, acetonitrile, cyclohexane, hexane, heptane, toluene, benzene, xylene and water. Even more preferably, the anti solvent is selected from the group consisting of MTBE, MEK, acetonitrile, cyclohexane, heptane, toluene and water. Most preferably, the anti-solvent is selected from the group consisting of acetonitrile, MEK, toluene and MTBE. The obtained mixture is then preferably maintained for at least about 5 minutes or till crystallization occurs, more preferably between about 5 minutes and about 6 hours, most preferably for about 1.5 hours, and preferably under stirring. The obtained product is preferably recovered by filtering.

Paliperidone obtained by the above process preferably contains PLP-NO in an amount of less than about 0.2% and PLP-car in an mount of less than about 0.04%. The above crystallization process may be repeated in order to further purify the obtained paliperidone, so that the PLP-NO and PLP-car levels may be reduced to less than about 0.02%.

The total purity of the paliperidone obtained by the above processes is of at least about 98%, more preferably, at least about 99% and most preferably at least about 99.9%. Preferably, the purity is measured as described above.

The present invention provides a process for the purification of paliperidone comprising slurrying paliperidone in an organic solvent. Preferably the slurrying is performed at a temperature of about 20° C. to about 70° C., more preferably at a temperature of about 25° C. to about 65° C. Preferably, the slurrying is performed for a period of time sufficient for purifying paliperidone, more preferably from about 30 minutes to about 24 hours. Preferably the organic solvent is selected from C_1-4 alkyl alcohols, C_3-5 ketones and water. Preferably the organic solvent is selected from ethanol, methanol, isopropanol, acetone and water. The obtained product is preferably recovered by filtering.

Paliperidone obtained by the above process preferably contains PLP-NO in an amount of less than about 0.3%, and PLP-Car in an amount of less than about 0.04%. The above slurrying process may be repeated in order to further purify the obtained paliperidone, so that the PLP-NO and PLP-car levels may be reduced to less than about 0.02%.

The total purity of the paliperidone obtained by the above processes is of at least about 98%, more preferably, at least about 99% and most preferably at least about 99.9%. Preferably, the purity is measured as described above.

The present invention further provides a process for the purification of paliperidone comprising providing a paliperidone solution containing more than about 0.1% PLP-NO or more than about 2% of any other impurity; admixing the solution with finely powdered carbon; and filtrating the admixture to obtain pure paliperidone. The filtering step is performed in order to remove the finely powdered carbon. Preferably the solution is obtained by dissolving paliperidone in an organic solvent. The organic solvent is preferably a mixture of acetone:water. Preferably, finely powdered carbon is an active carbon. The active carbon is preferably selected from the group consisting of HB ultra, CGP super, GBG, SX plus, ROX 0.8 and A super eur. The filtration is preferably done through hi-flow.

Paliperidone obtained by the above process preferably contains PLP-NO in an amount of less than about 0.12% and PLP-car in an amount of less than about 0.05%. The above crystallization process may be repeated in order to further purify the obtained paliperidone, so that the PLP-NO and PLP-car levels may be reduced to less than about 0.02%.

The total purity of the paliperidone obtained by the above processes is of at least about 98%, more preferably, at least about 99% and most preferably at least about 99.9%. Preferably, the purity is measured as described above.

Having described the invention with reference to certain preferred embodiments, other embodiments will become apparent to one skilled in the art from consideration of the specification. The invention is further defined by reference to the following examples describing in detail the purification of paliperidone. It will be apparent to those skilled in the art that many modifications, both to materials and methods, may be practiced without departing from the scope of the invention.

EXAMPLES

HPLC Method:

Column & Packing:	Zorbax SB-Phenyl 250 × 4.6 mm, 5μ
	Part No: 880975-912
Buffer:	0.04M KH2PO4 pH 2.0 adjusted with H3PO4
Eluent A:	85% Buffer: 15% Acetonitrile
Eluent B:	65% Buffer: 35% Acetonitrile
Gradient:	Time	% Eluent A	% Eluent B
	0	100	0
	20	100	0
	21	100	0
	40	0	100
	60	0	100
Flow	1 mL/min
Run time:	60 min
Equilibrium time:	10 min
Sample volume:	20 μL
Detector:	238 nm
Column	25° C.
temperature:
Diluent	Eluent A

Sample Solution Preparation

Weigh accurately about 10 mg Paliperidone sample into 10 mL volumetric flask, add 1 mL acetonitrile, sonicate until no chunks are observed (a few minutes) and dilute to volume with diluent.

Calculation

Calculate the amount of unknown impurities as follows:

$\%\mathrm{impurity}i=\frac{\mathrm{area}\mathrm{impurity}i\mathrm{in}\mathrm{samp}.\times 100}{\sum \left(\mathrm{area}\mathrm{of}\mathrm{all}\mathrm{peaks}\right)}$

Example 1

Purification of Paliperidone from PLP-NO by Crystallization

A slurry of paliperidone contaminated with PLP-NO, in the indicated solvent, at the indicated volumes was heated to the indicated temperatures until complete dissolution, wherein each of the ratios presented in the table below represents volume ratio of the two solvents named immediately preceding the ratio. After the compound was dissolved, the oil bath was removed and the solution was cooled to room temperature (excepted where is indicated). The solid was filtrated and analyzed as shown in the next table.

	Volumes		PLP-NO	PLP-NO
	of		before	after
	solvent	Heating	Crystal-	Crystal-
Solvent	(ml/g)	temp.	lization (%)	lization (%)
acetone	155	reflux	0.53	0.27
NMP	21	65° C.	0.53	0.19
Acetone/water (3:1)	25	reflux	0.41	0.22
ethanol	80	70° C.	0.41	0.32
NMP1	21	65° C.	0.41	0.23
Acetone/water (3:1)1	40	reflux	0.67	0.35
1Cooled to 0° C.

Example 2

Preparation of Paliperidone Free of PLP-NO

A slurry of 28 g Paliperidone (containing 0.26% of PLP-NO) in a 1120 ml of a mixture of acetone/water (3:1) was heated to reflux till complete dissolution. After one hour, the solution was cooled to 0-4° C., filtrated, and washed with 60 ml. of acetone. The procedure was repeated three times and finally the material was dried in a vacuum oven at 50° C. under reduced pressure for overnight to give 15.2 g of Paliperidone containing less than 0.02% of PLP-NO.

Example 3

Purification of Paliperidone from PLP-NO by Addition of a Different Solvent

Slurry of Paliperidone (containing 0.41% of PLP-NO) in 20 volumes (ml/g) of dichloromethane was heated to reflux until complete dissolution. The solution was cooled to room temperature and the indicated anti-solvent was gradually added until precipitation. The mixture was stirred at room temperature for 1.5 h and the solid was collected by vacuum filtration, and analyzed as shown in the next table.

		Volumes of anti-	PLP-NO after
	Anti-solvent	solvent (ml/g)	Crystallization (%)
	MTBE	15	0.26
	MEK	20	0.20
	Acetonitrile	25	0.17
	Cyclohexane	30	0.24
	heptane	15	0.25
	toluene	15	0.24

Example 4

Purification of Paliperidone from PLP-NO by Slurry in Different Solvents

Slurry of Paliperidone (containing 0.41% of PLP-NO) in the indicated volumes of the indicated solvents was stirred at the indicated temperatures and the indicated times. The solid was collected by vacuum filtration and analyzed. The results are displayed in the next table.

	Volumes of	Stirring	Stirring	PLP-NO after
Solvent	solvent (ml/g)	temp.	time	Crystallization (%)
ethanol	10	65° C.	35 min	0.30
methanol	5	60° C.	1 h	0.29
methanol	5	r.t.	1 h	0.34

Example 5

Purification of Paliperidone from PLP-NO by Addition of a Different Solvent at a Different Temperature

Slurry of Paliperidone (containing 0.41% of PLP-NO) in 7 volumes (ml/g) of the indicated solvent was heated to reflux until complete dissolution. The cooled anti-solvent was added at once. The resulting solid was collected by vacuum filtration, and analyzed as shown in the next table.

		Anti-	Volumes of anti-	PLP-NO after
	Solvent	solvent	solvent (ml/g)	Crystallization (%)
	dioxane	water	15	0.35
	butanol	water	70	0.39

Example 6

Purification of Paliperidone from PLP-NO by Addition of a Different Hot Solvent

Slurry of Paliperidone (containing 0.41% of PLP-NO) in the indicated solvent was heated to reflux until complete dissolution. The hot solution was added dropwise into an anti-solvent that was previously cooled in an ice bath. The resulting solid was collected by vacuum filtration, and analyzed as shown in the next table.

				PLP-NO
	Volumes		Volumes of	after
	of solvent	Anti-	anti-solvent	Crystal-
Solvent	(ml/g)	solvent	(ml/g)	lization (%)
n-propanol	30	water	50	0.24
dichloromethane	17	hexane	50	0.33
dioxane	10	water	50	0.35

Example 7

Purification of Paliperidone from PLP-NO by Filtration through Activated Carbon

A slurry of paliperidone (contaminated with 0.67% PLP-NO) in 40 volumes (i.e., g/40 ml) of acetone/water (3:1, volume ratio) was heated to reflux until complete dissolution. After the compound was dissolved, the hot solution was filtrated through hi-flow and cooled in an ice bath. The solid was filtrated and analyzed as shown in the next table.

                      PLP-NO after
Type of active carbon Crystallization (%)
HB ultra              0.16
CGP super             0.42
GBG                   0.24
SX plus               0.24
ROX 0.8               0.29
A super eur           0.12

Example 8

Purification of Paliperidone from PLP-Car by Crystallization

A slurry of paliperidone contaminated with PLP-Car, in the indicated solvent, at the indicated volumes was heated to the indicated temperatures until complete dissolution, wherein each of the ratios presented in the table below represents volume ratio of the two solvents named immediately preceding the ratio. After the compound was dissolved, the oil bath was removed and the solution was cooled to room temperature (except where is indicated). The solid was filtrated and analyzed as shown in the next table.

			PLP-car	PLP-car
	Volumes		before	after
	of solvent	Heating	Crystal-	Crystal-
Solvent	(ml/g)	temp.	lization (%)	lization (%)
DMF	5	reflux	1.51	N/D
Dimethyl acetamide	5	reflux	1.51	0.16
Dichlorobenzene	5	reflux	1.51	0.63
Propylene glycole	5	reflux	1.51	0.92
DMSO	5	reflux	1.51	0.38
Acetone/water 3:1	40	reflux	1.51	0.44
DMC	33	reflux	1.51	0.25
2-butanol	20	reflux	1.51	0.51
MIPK	54	reflux	1.51	0.37
Iso-butanol	26	reflux	1.51	0.57
NMP	5	140° C.	1.51	N/D
Ethanol/water 3:1	12	reflux	1.51	0.76
MEK	69	reflux	1.51	0.22
acetonitrile	100	reflux	1.51	0.21
EtOAc/water 3:1	50	reflux	1.51	0.21
acetone	155	reflux	1.51	0.17
Acetonitrile/water 1:1	40	reflux	1.31	0.79
n-butanol	23	135° C.	1.31	0.45
cellosolve	8	115° C.	1.31	0.33
chlorobenzene	7	115° C.	1.31	0.36
DMSO	5	110° C.	1.31	0.22
dichlorobenzene	5	120° C.	1.31	0.56
Propylene glycol	7	120° C.	1.31	0.60
Dibutyl ether	140	130° C.	1.31	1.07
PGME	7	130° C.	1.31	0.32
Iso-butyl acetate	35	reflux	1.31	0.45
n-propanol	30	90° C.	1.31	0.48
ethanol	80	70° C.	1.31	0.68
Acetone/water (3:1)1	40	reflux	1.31	0.09
IP A/water (1:1)1	19	reflux	0.57	0.07
Methanol/water(3:1)1	37	reflux	0.57	0.10

Example 9

Purification of Paliperidone from PLP-Car by Addition of a Different Solvent

Slurry of Paliperidone (containing 1.31% of PLP-Car) in 20 volumes (ml/g) of dichloromethane was heated to reflux until complete dissolution. The resulting solution was cooled to room temperature and the indicated anti-solvent was gradually added until precipitation. The mixture was stirred at room temperature for 1.5 h and the solid was collected by vacuum filtration, and analyzed as shown in the next table.

		Volumes of
		anti-solvent	PLP-Car after
	Anti-solvent	(ml/g)	Crystallization (%)
	MTBE	15	0.17
	MEK	20	0.16
	Acetonitrile	25	0.12
	Cyclohexane	30	0.28
	heptane	15	0.18
	toluene	15	0.09

Example 10

Purification of Paliperidone from PLP-Car by Slurrying in Different Solvents

Slurry of Paliperidone in the indicated volumes of the indicated solvents was stirred at the indicated temperatures and the indicated times. The solid was collected by vacuum filtration and analyzed. The results are displayed in the next table.

				PLP-CAR	PLP-CAR
	Volumes			before	after
	of solvent	Stirring	Stirring	Crystal-	Crystal-
Solvent	(ml/g)	temp.	time	lization (%)	lization (%)
Ethanol	10	RT	40 min	1.31	1.15
Ethanol	10	65° C.	35 min	1.31	0.77
Acetone	10	60° C.	17 h	0.13	N/D
IPA	10	60° C.	17 h	0.13	N/D
Acetone	10	60° C.	24 h	1.31	0.47
IPA	10	60° C.	24 h	1.31	0.74
Water	10	60° C.	25 h	1.31	1.20
Acetone	10	RT	47 h	0.13	0.04
IPA	10	RT	47 h	0.13	0.04
Methanol	5	60° C.	1 h	1.31	0.89
Methanol	5	RT	1 h	1.31	1.08

Example 11

Purification of Paliperidone from PLP-Car by Addition of a Different Solvent at a Different Temperature

Slurry of Paliperidone (containing 1.31% of PLP-Car) in 7 volumes (ml/g) of the indicated solvent was heated to reflux until complete dissolution. The cooled anti-solvent (cooled in an ice bath) was added at once. The resulting solid was collected by vacuum filtration, and analyzed as shown in the next table.

		Anti-	Volumes of anti-	PLP-Car after
	Solvent	solvent	solvent (ml/g)	Crystallization (%)
	dioxane	water	15	0.69
	toluene	water	35	1.18
	butanol	water	70	0.04

Example 12

Purification of Paliperidone from PLP-Car by Addition of a Different Hot Solvent

Slurry of Paliperidone (containing 1.31% of PLP-Car) in the indicated solvent was heated to reflux until complete dissolution. The hot solution was added dropwise into an anti-solvent that was previously cooled in an ice bath. The resulting solid was collected by vacuum filtration, and analyzed as shown in the next table.

				PLP-Car
	Volumes		Volumes of	after
	of solvent	Anti-	anti-solvent	Crystal-
Solvent	(ml/g)	solvent	(ml/g)	lization (%)
n-propanol	30	water	50	0.05
dichloromethane	17	hexane	50	0.04
dioxane	10	water	50	0.10

Example 13

Purification of Paliperidone from PLP-Car by Filtration through Activated Carbon

A slurry of paliperidone (contaminated with 0.57% PLP-Car) in 40 volumes (g/ml) of acetone/water (3:1) was heated to reflux until complete dissolution. After the compound was dissolved, the hot solution was filtrated through hi-flow and cooled in an ice bath. The solid was filtrated and analyzed as shown in the next table.

                      PLP-Car after
Type of active carbon Crystallization (%)
HB ultra              N/D
CGP super             N/D
GBG                   N/D
SX plus               N/D
ROX 0.8               0.10
A super eur           0.05

As used in this patent application, N/D represents not detected.

Claims

1. Paliperidone comprising less than about 0.2% of the impurity PLP-NO.

2. Paliperidone of claim 1 comprising less than about 0.02% of the impurity PLP-NO.

3. Paliperidone of claim 1 comprising PLP-NO at less than about 0.2%.

4. Paliperidone of claim 3, comprising PLP-NO at less than about 0.1%.

5. Paliperidone of claim 4, comprising PLP-NO at less than about 0.05%.

6. Paliperidone of claim 5 comprising PLP-NO at less than about 0.02%.

7. Paliperidone of anyone of claims 3-6, further comprising PLP-Car at less than about 0.2%.

8. Paliperidone of anyone of claims 3-6, further comprising PLP-Car at less than about 0.1%.

9. Paliperidone of anyone of claims 3-6, further comprising PLP-Car at less than about 0.05%.

10. Paliperidone of anyone of claims 3-6, further comprising PLP-Car at less than about 0.02%.

11. Paliperidone having a total purity of at least about 98%.

12. Paliperidone of claim 11 having a total purity of at least about 99%.

13. Paliperidone of claim 12 having a total purity of at least about 99.9%.

14. Paliperidone of claim 11 having a total purity of about 98% to about 99.9%.

15. Paliperidone of claim 14 having a total purity of about 99% to about 99.9%.

16. Paliperidone of claim 11 having a total purity of about 98% to about 99.99%.

17. Paliperidone of claim 16 having a total purity of about 99% to about 99.99%.

18. Paliperidone of anyone of claims 11-17, comprising PLP-NO at less than about 0.2%.

19. Paliperidone of anyone of claims 11-17, comprising PLP-NO at less than about 0.1%.

20. Paliperidone of anyone of claims 11-17, comprising PLP-NO at less than about 0.02%.

21. Paliperidone of claim 18, further comprising PLP-car at less than about 0.2%.

22. Paliperidone of claim 20, further comprising PLP-car at less than about 0.02%.

23. A process for purifying paliperidone, comprising crystallizing paliperidone from at least one solvent selected from the group consisting of C3-6 ketones, a mixture of a C3-6 ketone and water, N-methylpyrrolidone, C3-6 amides, halo-substituted C6-12 aromatic hydrocarbons, propylene glycol, dimethyl sulfoxide, di-methyl carbonate, C1-4 alkyl alcohols, a mixture of a C1-4 alkyl alcohol and water, acetonitrile, a mixture of acetonitrile and water, C2-6 alkyl acetates, a mixture of a C2-6 alkyl acetate and water, cellosolve, dimethyl carbonate, polyethylene glycol methyl ether and C2-8 ethers to obtain the purified paliperidone, wherein the total purity of the purified paliperidone is higher than the total purity of the starting paliperidone.

24. The process of claim 23, wherein the C3-6 ketone(s) is selected from the group consisting of acetone, methyl ethyl ketone and methyl iso-butyl ketone; the C3-6 amides are selected from the group consisting of dimethylacetamide and dimethylformamide; the halo-substituted C6-12 aromatic hydrocarbons are selected from the group consisting of chlorobenzene and dichlorobenzene; the C1-4 alkyl alcohol(s) is selected from the group consisting of methanol, ethanol, n-propanol, isopropanol, n-butanol, isobutanol and 2-butanol; the C2-6 alkyl acetate(s) is selected from the group consisting of ethyl acetate and isobutyl acetate; and the C2-8 ethers are selected from the group consisting of dibutyl ether and polyethylene glycol.

25. The process of claim 23, wherein the at least one solvent is a mixture of acetone and water.

26. The process of claim 25, wherein the at least one solvent is a mixture of solvents at a volume ratio of between about 1:1 to about 3:1.

27. The process of claim 26, wherein the at least one solvent is a mixture of acetone and water, or a mixture of ethanol and water.

28. The process of claim 27, wherein the at least one solvent is a mixture of acetone and water.

29. The process of claim 28, wherein the at least one solvent is acetone/water at a volume ratio of about 3:1.

30. The process of claim 23, wherein the crystallizing step comprises heating the at least one solvent and paliperidone to form a solution by complete dissolution, and thereafter precipitating paliperidone in the solution to obtain the purified paliperidone.

31. The process of claim 30, wherein the precipitating step is performed by cooling the solution to a temperature ranging from about 0° C. to about 30° C.

32. The process of claim 31, wherein the cooling is to a temperature of about 25° C.

33. The process of claim 30, wherein the precipitating step is performed by solvent removal from the solution via evaporation.

34. A process for purifying paliperidone, comprising crystallizing paliperidone from a solvent, wherein the crystallizing step comprises dissolving the paliperidone in the solvent to obtain a solution;mixing the solution with an anti-solvent to form a mixture in order to induce crystallization of paliperidone as purified paliperidone, wherein the total purity of the purified paliperidone is higher than the total purity of the starting paliperidone.

35. The process of claim 34, wherein the dissolving step is performed at reflux and thereafter the solution is cooled.

36. The process of claim 35, wherein the solution is cooled to a temperature of about 0° C. to about 30° C.

37. The process of claim 36, wherein the solution is cooled to a temperature of about 20° C. to about 30° C.

38. The process of claim 37, wherein the solution is cooled to a temperature of about 25° C.

39. The process of claim 34, wherein the mixture is maintained for at least about 5 minutes.

40. The process of claim 39, wherein the mixture is stirred.

41. The process of claim 34, wherein the solvent is selected from the group consisting of dichloromethane, dioxane and C1-4 alkyl alcohols.

42. The process of claim 41, wherein the solvent is selected from the group consisting of dichloromethane, dioxane, n-propanol and butanol.

43. The process of claim 34, wherein the anti-solvent is selected from the group consisting of methyl t-butyl ether (MTBE), methyl ethyl ketone (MEK), acetone, methyl iso-butyl ketone (MIBK), acetonitrile, cyclohexane, hexane, heptane, toluene, benzene, xylene and water.

44. The process of claim 43, wherein the anti-solvent is selected from the group consisting of MTBE, MEK, acetonitrile, cyclohexane, heptane, toluene and water.

45. The process of claim 44, wherein the anti-solvent is selected from the group consisting of MTBE, MEK, acetonitrile and toluene.

46. A process for purifying paliperidone, comprising slurrying paliperidone in an organic solvent to obtain purified paliperidone, wherein the total purity of the purified paliperidone is higher than the total purity of the starting paliperidone.

47. The process of claim 46, wherein the organic solvent is selected from the group consisting of C1-4 alkyl alcohols, C3-5 ketones and water.

48. The process of claim 47, wherein the organic solvent is selected from the group consisting of methanol, ethanol, isopropanol, acetone and water.

49. The process of claim 46, wherein the slurrying is performed at a temperature of about 20° C. to about 70° C.

50. The process of claim 46 wherein the slurrying is performed for about 30 minutes to about 24 hours.

51. The process of claim 50, wherein the slurrying is performed for about 35 minutes to about 1 hour.

52. A process for purifying paliperidone, comprising (a) providing a paliperidone solution containing more than about 0.1% PLP-NO;(b) admixing the solution with finely powdered carbon; and(c) filtrating the admixture obtained from step (b) to obtain purified paliperidone, wherein the total purity of the purified paliperidone is higher than the total purity of the starting paliperidone.

53. The process of claim 52, wherein the paliperidone solution in step (a) is obtained by dissolving paliperidone in at least one organic solvent.

54. The process of claim 53, wherein the at least one organic solvent is a mixture of acetone and water.

55. The process of claim 54, wherein the finely powdered carbon is an active carbon.

56. The process of claim 55, wherein the active carbon is selected from the group consisting of HB ultra, CGP super, GBG, SX plus, ROX 0.8 and A super eur.

57. The process of claim 52, wherein the filtration is done through hi-flow.

58. The process of anyone of claims 23, 34, 46 and 52, wherein the total purity of the purified paliperidone is at least about 98%.

59. The process of claim 58, wherein the total purity of the purified paliperidone is at least about 99%.

60. The process of claim 59, wherein the total purity of the purified paliperidone is at least about 99.9%.