Process for the preparation of ketorolac tromethamine

Organic compounds -- part of the class 532-570 series – Organic compounds – Heterocyclic carbon compounds containing a hetero ring...

Reexamination Certificate

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C203S056000, C203S060000

Reexamination Certificate

active

06191285

ABSTRACT:

TECHNICAL FIELD OF THE INVENTION
This invention relates to a process for the preparation of ketorolac tromethamine.
BACKGROUND OF THE INVENTION
Ketorolac tromethamine has the following structure:
Ketorolac tromethamine is useful as an analgesic and anti-inflammatory agent. There exist a number of prior art methods for the production of amine salts of ketorolac, see, for example, U.S. Pat. Nos. 4,347,185 and 4,089,969. Typically these salts are prepared by solubilizing ketorolac acid and tromethamine in a nonpolar organic solvent and isolating the resulting tromethamine salt. However, these procedures rely on the low solubility of tromethamine in most nonpolar organic solvents, and results in inconsistent yields, incomplete salt formation, low potency, and inconsistent and unacceptable bulk densities of the final product.
For example, in U.S. Pat. No. 4,089,969, is disclosed a process for preparing amine salt derivatives of ketorolac acid wherein the process is conducted in a single or binary solvent system, i.e., in water, alone or in combination with an inert, water-miscible organic solvent. Exemplified is a process for preparing an amine salt of ketorolac acid where in the organic solvent utilized is benzene. However, benzene has the problem of being a carcinogen and therefore undesirable for use in preparing in a pharmaceutical product.
Alternate approaches have substituted acetonitrile as the reaction solvent and resulted in a product having good yields and high purity; however, like benzene, acetonitrile must be controlled at extremely low levels in the final product.
Further, such processes of the prior art yield lots of final product with inconsistent and unacceptable bulk densities. Bulk density is of great importance in preparing pharmaceutical products for oral administration, for example, when one considers the size of a high-dose capsule or the homogeniety of a low-dose formulation in which there are large differences in drug and excipient bulk densities. In addition, for the manufacture of solid dosage forms, it is desirable to have the bulk density in the range of about 0.3 to about 0.7 g/mL, or more preferrably about 0.35 to about 0.5 g/mL. The solid product obtained by such single or binary solvent distillation methods yields such product with such varied degree of bulk density that is not suitable or useful for oral formulations.
Thus there continues to be a need for improved methods for producing ketorolac tromethamine which provide a product of high quality and potency while avoiding undesirable solvents, and also yields a product of suitable bulk density for oral formulations.
BRIEF SUMMARY OF THE INVENTION
The present invention provides a process of producing ketorolac tromethamine in a three-part solvent system, i.e., in the presence of a lower alkyl alcohol, a lower alkyl acetate, and water. Because of the high solubility of tromethamine and ketorolac acid in the water/lower alkyl alcohol system, the addition of a lower alkyl acetate, increases the recovery of ketorolac tromethamine. As used herein, the term “lower alkyl” refers to a C
1
-C
4
straight or branched, unsubstituted or substituted, alkyl chain. The solid product obtained by such a ternary distillation method yields product of consistent bulk density that is suitable for oral formulations.
In one aspect of the invention, ketorolac acid is dissolved in the lower alkyl alcohol. Tromethamine, previously dissolved in water, is mixed with the ketorolac acid solution. The binary mixture is placed under vacuum or atmospheric distillation. When approximately one-half of the volume of the mixture has been distilled, another portion of of the lower alkyl alcohol is added. Distillation is continued until approximately one-half the volume has been distilled. At this point, the lower alkyl acetate is added and the resulting mixture is again distilled until approximately half the volume is removed. The lower alkyl acetate distillation step is repeated again one or more times. After one-half the volume has been again distilled, the resulting mixture is cooled and the solid product is isolated by filtration.
Optionally, in a second aspect of the invention, the ketorolac acid is dissolved in the lower alkyl alcohol. Tromethamine, previously dissolved in water, is mixed with the ketorolac acid solution. To this mixture is added the lower alkyl acetate. The resulting ternary mixture is placed under vacuum or atmospheric distillation. When approximately one-half of the volume of the mixture has been distilled, another portion of of the lower alkyl acetate is added. Distillation is continued until approximately one-half the volume has been distilled. The lower alkyl acetate distillation step is repeated again one or more times. After one-half the volume has been again distilled, the resulting mixture is cooled and the solid product is isolated by filtration.
DETAILED DESCRIPTION OF THE INVENTION
The present invention relates to a process of producing ketorolac tromethamine which results in a product of consistently high quality and potency. Unlike the solvents used in the prior art, the solvents employed in the present invention are suitable for large scale processing, and give higher yields much more consistent bulk densities of final product. In addition, because of the high solubility of tromethamine and ketorolac acid in the water/isopropanol system, the quantities of solvents employed are minimized.
Ketorolac acid can be synthesized according to methods described in the following U.S. Pat. Nos. 4,087,539, 4,089,969, 4,097,579, 4,140,698, 4,232,038, 4,344,943, 4,347,185, 4,347,186, 4,353,829, 4,454,151, 4,458,829, 4,835,288, 4,873,340, 4,874,871, 4,937,368, 4,988,822, and 4,496,741, the above incorporated by reference herein, or by other methods known to those skilled in the art.
The synthesis of ketorolac acid can be conveniently accomplished by treating a bicyclic nitrile compound (I)
with N,N-dimethylbenzamide (the use of dimethylbenzamide being described in U.S. Pat. No. 4,344,943), to form 5-benzoyl-1,2-dihydro-3H-pyrrolo[1,2-a]pyrrole-1-nitrile. The nitrile is hydrolyzed to the corresponding acid as described in U.S. Pat. No. 4,353,829.
In accordance with the process of the invention, one aspect is described briefly here and in more detail below. One part ketorolac acid is dissolved in from three to twelve parts of a suitable solvent, typically a lower alkyl alcohol. Such preferred alcohols include ethanol, methanol, n-propanol, or, more preferably, isopropanol. Alternatively, ethers, e.g., tetrahydrofuran, can be employed. The preferred range is 4-8 parts solvent to one part ketorolac acid (w/w). In a separate container, one part tromethamine is dissolved in two to four, preferably two, parts water (w/w). The resulting mixture is combined with the ketorolac acid solution and mixed until a solution results. Alternatively, the ketorolac acid, solvent, tromethamine, and water can be combined in a single flask. The mixture is placed under vacuum distillation at a temperature of 20 to 60° C., or atmospheric distillation. When approximately one half of the volume has been distilled, conveniently determined by monitoring the volume of the distillate, a second portion of solvent, i.e., lower alkyl alcohol, equal to the remaining volume is added. Distillation is resumed under the conditions previously described and continues until approximately one half the volume has again been distilled. At this point an organic solvent, e.g., a lower alkyl acetate, preferably ethyl- or isopropyl acetate, etc., is added, and the resulting solution is again placed under distillation which continues until approximately half the volume is removed.
Alternatively, toluene or xylene may be used as the third solvent. This step is repeated one or more times and distillation resumed until approximately one half the volume has again been distilled. After half the volume has been distilled, the solution is cooled, preferably to −20 to +20° C. and the resulting solid product is isolated by filtration.
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