NZ213594A - Regeneration of 6-fluoro-4-chromanone from 6-fluoro-4-ureidochroman-4-carboxylic acid - Google Patents
Regeneration of 6-fluoro-4-chromanone from 6-fluoro-4-ureidochroman-4-carboxylic acidInfo
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- NZ213594A NZ213594A NZ21359485A NZ21359485A NZ213594A NZ 213594 A NZ213594 A NZ 213594A NZ 21359485 A NZ21359485 A NZ 21359485A NZ 21359485 A NZ21359485 A NZ 21359485A NZ 213594 A NZ213594 A NZ 213594A
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Description
New Zealand Paient Spedficaiion for Paient Number £13594
21359
n
Priority Dete(s):
Complete Specification F,led: 9*95 ci33s.- ••.^pr,Ov>A'j.^<.
^Q^tj./OX..
Publication Date: ..® JAN 19Q$ P.O. Jou-nal, Nc: , ' ^Q.3) j
NEW ZEALAND
ACT. 1953
NO DMWm
No.: Date:
COMPLETE SPECIFICATION
REGENERATION OF 6-FLU0R0-4-CHR0MAN0NE FROM 6-FLUORO-4-UREIDOCHROMAN-4-CARBOXYLIC ACID
K/We, PFIZER INC., a corporation organized under the laws of the State of
Delaware, United States of America, of 235 East 42nd Street, New York, State of New York, United States of America,
hereby declare the invention for which X / we pray that a patent may be granted to ooa/us, and the method by which it is to be performed, to be particularly described in and by the following statement: -
- 1 - (followed by Page 1A)
2 1359
-1A
REGENERATION OF 6-FLUORO-4-CHROMANONE FROM 6-FLUORO-4-UREIDOCHROMAN-4-CARBOXYLIC ACID
Diabetes mellitus is a metabolic disorder which afflicts a significant percentage of the human popu-5 lation. It is characterized by reduced carbohydrate utilization, leading to hyperglycemia, with resulting glycosuria and polyurea, giving symptoms of thirst,
hunger, emaciation and finally diabetic coma. Although the short-teem adverse effects of diabetes (e.g. diabetic 10 coma) can usually be controlled by the administration of an oral hypoglycemic agent or insulin, in many cases of diabetes long-term complications develop, especially neuropathy and ocular problems such as retinopathy and cataract formation.
One approach to the control of the long-term adverse effects of diabetes is treatment with an inhibitor of the aldose reductase enzyme, with a view to blocking the reduction of glucose to sorbitol. One such aldose reductase inhibitor which is of use in controlling the 20 chronic complications of diabetes is sorbinil, the chemical compound having the following structural formula:
o
JE&a.y.. :
213 59 4
(I)
Thus, sorbinil is one of the optical antipodes of 6-fluoro-spiro[chroman-4,4 *-imidazoline]—2',5 *-dione. Specifically, it is the dextrorotatory isomer of 6-5 fluoro-spiro(chroman-4,4'-imidazolidine]-2 *,5'-dione,
and it has the (S)-configuration at its asymmetric center based on the Cahn-Ingold-Prelog system of designating absolute configurations. (Sarges, U.S. Patent No.
4,130,714) .
A key raw material for the preparation of sorbinil is the bicyclic ketone, 6-fluoro-4-chromanone (II) . In one method of producing sorbinil, 6-fluoro-4-chromanone is converted in several steps into racemic (RS)-6-fluoro-4-ureidochroman-4-carboxylic acid (III) , from 15 which the desired isomer, (S)-6-fluoro-4-ureidochroman-4-carboxylic acid (IV), is obtained by resolution with an optically active amine, and cyclized to sorbinil using glacial acetic acid. Cue and Moore, U.S. Patent No. 4,435,578 - see SCHEME I.
However, resolution of the racemic ureido-acid
(III) produces, as a by-product, (R) -6-fluoro-4-ureidochroman-4-carboxylic acid (V), i.e. the isomer with the wrong stereochemistry at C-4 for cyclization to sorbinil. The (R)-ureido-acid (V) can be recovered from the 25 resolution step, and in practice it is usually contaminated with varying amounts of the (RS)-ureido-acid (III).
■T
Accordingly, it is an object of the present invention to provide a process for converting the (R)-ureido-acid (V), and mixtures thereof with (RS)-ureido-acid (III),
back into 6-fluoro-4-chromanone by oxidation with a 5 metal permanganate. The regenerated chromanone (II)
can be reconverted into racemic ureido-acid (III) and thence to additional sorbinil. This recycling technique of (R)-ureido-acid (V) avoids economic losses and waste disposal problems in sorbinil synthesis, and thereby 10 greatly increases overall synthesis efficiency.
SCHEME I
106
0»C-NH2 HN, COOH
'CO
v
I
ii ii
0-C-NH2 HNW COOH
III
0®C-NH2 HNa nv»COOH
IV
I
CH3COOH
sorbinil (I)
mTa3L1 a > /
wiLiiffi /
2 13594
One method for regenerating 6-fluoro-4-chromanone from (R)-ureido-acid (V), or a mixture with its racemic counterpart, has been described in United States Patent No. 4,431,828. However, the process of the 5 present invention possesses advantages over the prior regeneration process. The present process involves a single oxidation step, which is easy to carry out, operates directly on the ureido-acid, and produces the chromanone (II) in pure form. The prior art process 10 requires a hydrolysis step prior to oxidation, and the chromanone (II) produced contains a 4-chloroimino contaminant, which has to be removed by hydrogenation.
This invention provides a process for the regeneration of 6-fluoro-4-chromanone (II) from (R)-6-fluoro-4-15 ureidochroman-4-carboxylic acid (V) or a mixture of (R)- and (RS)-6-fluoro-4-ureidochroman-4-carboxylic acid (V and III), which comprises:
reacting said (R)-6-fluoro-4-ureidochroman-4-carboxylic acid or mixture of (R)- and (RS)-6-fluoro-4-20 ureidochroman-4-carboxylic acid with a metal permanganate, in an aqueous or partially aqueous solvent system, at a temperature in the range from 10 to 70°C, and at a pH in the range from 3 to 7, viz.:
2 1359
o«c-nh2
cooh o«c-nh2
h*l ^ cooh ii
III
Alkali metal and alkaline earth metal permaganates can be used for the process of present invention, but the preferred reagent is potassium permanganate. The 5 process is preferably carried out using 0.7 to 2.0
molar equivalents, especially 1.0 to 1.2 equivalents, of potassium permanganate in water-acetic acid mixtures.
The present invention provides a process for the oxidation of the (R)-ureido-acid (V), or a mixture of 10 the (R)-ureido-acid (V) and its corresponding racemate (III), to 6-fluoro-4-chromanone, using a permanganate, and it can be used irrespective of the source of the ureido-acid substrate. Moreover, when a mixture of (R)- and (RS)-ureido-acids is used, the process of this 15 invention can be used irrespective of the ratio of the (R)— and (RS)-substrates.
However, the process of this invention is particularly useful for recycling the by-product obtained after removal of (S)-ureido-acid (IV) from racemic ureido-20 acid (III) in a synthesis of sorbinil (D.S. Patent No.
4,435,578). Thus, in a typical sorbinil synthesis, the
213594
(RS)-ureido-acid (III) is contacted with about one molar equivalent of an optically-active amine in a suitable solvent, under conditions such that the diastereo-meric salt containing the (S)-ureido-acid (IV) precipitates 5 from the reaction medium and it can be removed by filtration. Typical optically-active amines which are used are D-(+)-(1-phenylethyl)amine and L-(-)-ephedrine, and a suitable solvent system is aqueous methanol. The precipitated salt containing the (S)-ureido-acid is 10 then converted into sorbinil, usually by treatment with glacial acetic acid. The mother liquors after removal of the salt containing the (S)-ureido-acid (IV) by filtration are then usually freed from the methanol, basified to a pH of about 10 or 11 and extracted with a 15 volatile, water-immiscible, organic solvent to remove the resolving amine. Acidification of the resulting aqueous solution causes precipitation of a mixture of (R)- and (RS)-6-fluoro-4-ureidochroman-4-carboxylic acid which is suitable for recycling to 6-fluoro-4-20 chromanone by the process of this invention. In such a mixture, the ratio of said (R)-ureido-acid (V) to said (RS)-ureido-acid (III) is usually in the range from 20:1 to 1:2, especially about 2:1.
The process of this invention involves a single 25 step; namely, oxidation with permanganate. The process is normally carried out simply by contacting the ureido-acid substrate with the permanganate in an appropriate solvent system, until conversion into the chromanone (II) is complete. An alkali metal permanganate, e.g. 30 lithium, sodium or potassium permanganate, or an alkaline earth metal permanganate, e.g. calcium or magnesium permanganate, can be used. However, the preferred reagent is potassium permanganate.
An appropriate solvent system is one which will 35 dissolve the ureido-acid substrate to a significant degree, does not have any adverse effect on the starting
_ _ ^
^ •• v-;' F?"5*
ureido-acid substrate or the chromanone product, is not oxidized by permanganate to a significant extent, and permits easy isolation of the chromanone product. In practice, water is a convenient solvent which is 5 commonly used. If desired certain organic co-solvents, such as tetrahydrofuran, dioxane, or low-molecular weight ethers of ethylene glycol or diethyleneglycol (e.g. 1,2-dimethoxyethane) can be added. However, it is usually preferable that the reaction medium remains 10 homogeneous. Moreover, it is usually advantageous to conduct the process of this invention at a neutral or acidic pH. In particular a pH in the range form 3.0 to 7.0 is preferred, and this is achieved by the addition of an acidifying agent. A wide variety of acidifying 15 agents can be added, the major requirement of such an agent being that it does not affect the ureido-acid substrate or chromanone product, and it is unaffected by the permanganate oxidant. Both inorganic and organic acidifying agents can be added, and typical agents are 20 hydrochloric acid, sulfuric acid, nitric acid, phosphoric acid, acetic acid, methanesulfonic acid and toluenesulfonic acids. A particularly convenient acidifying agent is glacial acetic acid. Indeed, water containing a small volume of acetic acid represents a preferred solvent 25 system for the process of this invention, especially water containing from 0.5 to 3 percent by volume of acetic acid.
The order of addition of the ureido-acid substrate and the permanganate oxidant to the solvent is not 30 critical, and the two reactants can be added in either order. Also, it is sometimes convenient to treat a solution of the ureido-acid substrate with the permanganate portionwise, either as a solid or as an aqueous solution, as the oxidation proceeds. In that way, permanganate 35 can be added in small amounts until a slight excess persists, i.e. the starting ureido-acid substrate is
' ' --"1 . S--
K>-,^Z.^.:. . " , ■'•■ '"A,*
■*$s
-i' i»^. "
'T
I
effectively titrated with the permanganate. This technique is particularly convenient when the ureido-acid substrate contains minor impurities which are also subject to permanganate oxidation.
The process of the present invention is carried out at a pH in the range from 3.0 to 7.0. Although this is normally achieved by adding the starting ureido-acid substrate in its free carboxylic acid form, the ureido-acid substrate can by introduced into the reaction 10 medium in the form of a carboxylate salt. The amount of added acidifying agent is then adjusted accordingly, to achieve the required pH for the oxidation. It is, of course, the pH at which the oxidation is run that determines the precise nature of the ureido-acid substrate 15 (free acid or carboxylate salt) which undergoes oxidation. The ureido-acid substrate can be introduced into the reaction medium as a variety of salts. However, it is preferable that the cationic counterion is not susceptible to permanganate oxidation. Thus, favorable salts of 20 the ureido-acid substrate which can be used are alkali metal salts (e.g. lithium, sodium or potassium salts) or alkaline earth metal salts (e.g. calcium or magnesium salts). On the other hand, amine salts, while still operable, are not generally favored.
The oxidation reaction of this invention can be carried out over a wide range of temperature. However, to ensure a convenient rate of reaction and achieve convenient reaction times, reaction temperatures from 10 to 70°C, and preferably 20 to 50°C, are commonly 30 used. At a reaction temperature of 20 to 50°C, reaction times of a few hours, e.g. 2 to 10 hours are quite common.
An advantageous feature of the process of this invention resides in the ease of isolation of the 35 product. At the completion of the oxidation, any excess permanganate and the manganese dioxide byproduct can be reduced and solubilized by the addition of bisulfite, e.g. solid sodium meta-bisulfite, and
4
then the 6-fluoro-4-chromanone can be recovered by standard techniques, e.g. filtration or extraction into a water-immiscible, volatile, organic solvent. Evaporation of the organic solvent then affords the desired chromanone II. The chromanone thus obtained directly from the process of this invention is usually of sufficient quality for use in further sorbinil synthesis, e.g. according to the methods of U.S. Patent Nos. 4,130,714 or 4,43 5,578? however, the chromanone product can be purified by standard procedure, such as chromatography or recrystallization e.g. from methanol, if desired.
Thus, the 6-fluoro-4-chromanone recovered from the process of this invention can be used according to U.S. Patent No. 4,435,578, as follows:
0
(NH4)2c°3 kcn
V
vi alkaline hydrolysis
I
KOCN
V
racemic ureido-acid (III)
The 6-fluoro-4-chromanone is reacted with an alkali metal cyanide (e.g. potassium cyanide) and ammonium carbonate in a polar solvent, such as aqueous ethanol, at about 65°C, for several hours, to give the racemic hydantoin (VI). The hydantoin (VI) is hydrolyzed to the racemic amino-acid (VII) under basic conditions,
^ <r- • ■ r""'
e.g. using about four molar equivalents of sodium hydroxide, or two molar equivalents of barium hydroxide octahydrate, in water, under reflux, for several hours. The ainino-acid (VII) is then treated with two molar 5 equivalents of potassium cyanate in water, at room temperature. The reaction proceeds quite rapidly to give the racemic ureido-acid (III) which is resolved by salt formation with an optically-active amine, as described previously. The amine salt of the (S)-10 ureido-acid (IV) can be converted into sorbinil by treatment with a large excess of glacial acetic acid at about 90°C for a few hours, e.g. about two hours.
As indicated hereinbefore, sorbinil is an aldose reductase inhibitor, and it is useful for administration IS to diabetic human subjects for the control of chronic complications of diabetes, such as neuropathy, retinopathy and cataract formation. For such purposes, sorbinil is normally compounded into pharmaceutical compositions, e.g. tablets, capsules, aqueous suspensions or injectable 20 solutions, according to standard pharmaceutical practice, and administered either orally or parenterally. Sorbinil is normally administered to a human patient at a dosage from about 0.05 mg to aoout 5.0 mg per kilogram of body weight per day, in single or multiple doses. See 25 further U.S. Patent No. 4,130,714.
The following examples and preparations are provided solely for the purpose of further illustration.
-13
EXAMPLE 1 6-Fluoro-4-chromanone
A mixture of 17.3 g (0.11 mole) of potassium permanganate, 7.2 g (0.12 mole) of glacial acetic acid 5 and 1 liter of water was stirred under an atmosphere of nitrogen at room temperature until a solution was obtained (10 minutes). To the resulting solution was then added, portionwise, with stirring, during about 2 minutes, 25.4 g (0.1 mole) of a mixture of (R)- and 10 (RS) -6-fluoro-4-ureidochroman-4-carboxylie acid (approximate composition: 70 parts (R); 30 parts (RS)). The resulting slurry was stirred for 10 minutes at 22°C, and then it was warmed slowly to 40°C and the heat source was removed. Stirring was continued for 3 0 15 minutes, during which time the reaction temperature rose slowly to 4 7°C and then it began to fall. The heat source was reapplied, and the reaction mixture was heated and stirred at 50°C for 30 minutes.
The reaction mixture was cooled to 23°C, and 41.6 20 9 (0.4 mole) of sodium bisulfite was added in portions during a 30 minute period, with stirring. Stirring was continued for 30 minutes at 22°C, and then the solid was recovered by filtration, washed with water and dried. This gave 30.3 g of a solid, mp 111-1138C. The 25 latter solid was suspended in 100 ml of water, and 15 ml of 12N hydrochloric acid was added which gave a stable pH of 1.5. The acidified mixture was extracted with dichloromethane, and the combined extracts were washed with water, dried (MgS04) and concentrated in 30 vacuo to ca 30 ml of a slurry. The slurry was diluted with 100 ml of hexane and the volume was reduced to ca 50 ml by evaporation. The resulting slurry was filtered, and the solid obtained was washed with hexane and dried. This afforded 11.0 g (66% yield) of 6-fluoro-4-35 chromanone, mp 112-114°C.
The nuclear magnetic resonance spectrum (60 MHz) of the product (in CDCl^) showed absorptions at 7.9-7.0 (multiplet, 3H), 4.65 (triplet, 2H) and 2.8 (triplet 2H) ppm, downfieId from internal tetramethylsilane.
EXAMPLE 2 6-Fluoro-4-chromanone
The title compound can be prepared by oxidation of (R)-6-fluoro-4-ureidochroman-4-carboxylic acid with potassium permanganate, using the procedure of Example 1.
EXAMPLE 3 6-Fluoro-4-chromanone
When the procedure of Example 1 is repeated, but the potassium permanganate used therein is replaced by an equimolar amount of lithium permanganate, sodium permanganate, calcium permanganate or magnesium permanganate, the title product is obtained.
EXAMPLE 4 6-Fluoro-4-chromanone
A solution 29.47 kg of potassium permanganate in 246 liters of water, preheated to 50°C, was added, with stirring, to 43.27 kg of a mixture of (R)- and (RS)-6-fluoro-4-ureidochroman-4-carboxylic acid (approximate composition: 70 parts (R); 30 parts (RS)) in 946 liters of water, also preheated to 50°C. The addition took 1.5 hours and after about half of the permanganate solution had been added, glacial acetic acid was added as necessary to maintain the pH in the range 4.5 to 5.0. Stirring was continued at 50°C and a pH of 4.5 to 5.0 for an additional 30 minutes, and then the pH
21359
was lowered to 1.5 by the addition of 31.7 liters of concentrated hydrochloric acid. To the resulting mixture was added with stirring 23.85 kg of solid sodium bisulfite, portionwise, at 50°C, while maintaining 5 the pH at 1.5 by the addition of concentrated hydrochloric acid (ca 51.5 liters). Stirring was continued at 50°C for 30 minutes and then the mixture was filtered. The residue was washed with water at 50°C and dried at 50°C, giving a first crop of the title product. The 10 mother liquors were stirred at 15-20°C for 3 days and then filtered. This afforded a second crop of the title product. The total yield was 25.2 kg (87% yield).
1 ' * t
/
2 1^; --»"
PREPARATION 1 (RS)-4-Amino-6-fluorochroman-4-carboxylic Acid
A stirred slurry of 78 g (0.33 mole) of (RS)-6-fluoro-spiro-(chroman-4,4'-imidazolidine]-2',5'-dione 5 and 208.3 g (0.66 mole) of barium hydroxide octahydrate in 585 ml of water was slowly heated to reflux over 3 hours and ^efluxed 16 hours. The slurry was cooled to 80°C and powdered NH4C03 (78 g) added portionwise over 5 minutes. Moderate foaming was noted. After stirring 10 1.5 hours at 80°C, the mixture was cooled to 60°C, and filtered over diatomaceous earth with 2x100 ml hot water for wash. The combined filtrate and washes were stripped to 200 ml and allowed to stand overnight. 2-Propanol (600 ml) was added and the mixture heated to 15 70°C to dissolve precipitated solids. The hot solution was treated with activated carbon, filtered over diatomaceous earth and washed with hot 1:1 water:2-propanol. The combined filtrate and washes were stripped to 200 ml, and water chased with 3x3 00 ml fresh 2-propanol. 20 The resulting thick slurry was diluted with 200 ml additional 2-propanol, cooled to 5°C, granulated for 0.5 hour, filtered and air dried to yield title product, 63.5 g, 91.2%, mp 252-253°C (dec).
PREPARATION 2
(RS)-6-Fluoro-4-ureidochroman-4-carboxylic Acid
METHOD A
To a stirred slurry of 21.1 g (0.1 mole) of (RS)-4-amino-6-fluorochroman-4-carboxylic acid in 250 ml of water was added, portionwise, 16.2 g (0.2 mole) of 30 potassium cyanate over 2.5 minutes. The almost complete solution was stirred 22 hours at 23°C, during which the
2
pH increased from 6.8 to 9.1 and complete solution occurred. Concentrated hc.1 (19.0 ml) was added over 1 hour, keeping temperature 25°-29° C. The resulting slurry was granulated 1 hour (pH 3.2-3.5), and title 5 product recovered by filtration with 150 ml water wash, partially dried in air and then for 18 hours at 50°-55° in.vacuo, 20.0 g, 79%.
METHOD B
A mixture of 47.2 g (0.2 mole) of (RS)-6-fluoro-10 spiroIchroman-4,4'-imidazoline]-21,5'-dione, 28 g (0.7 mole) of sodium hydroxide pellets and 600 ml of water was heated under reflux for 4 0 hours. The reaction mixture was cooled to 24°C, and the pH was lowered from 11.8 to 5.0 with 6N hydrochloric acid. Gassing was 15 noted below pH 8. After stirring the slurry for 20
minutes at pH 5, 32.5 g (0.4 mole) of potassium cyanate was added during 2 minutes. The mixture was stirred for 20 hours, and a small amount of solid was removed by filtration and washed with 50 ml of water. The 20 combined filtrate and washings were adjusted from pH 8.5 to pH 4.0 using 6N hydrochloric acid. The solid which precipitated was recovered by filtration, washed with warm water and air dried to give 3 9.7 g (78%
yield) of the title product, mp 198-199°c (dec.).
preparation 3
(R)(+)-(1-Phenylethyl)amine Salts of 6-Fluoro-4~ureido- chroman-4-carboxylic Acid
A slurry of 10.0 g (39.4 mmole) of (RS)-6-fluoro-4-ureidochroman-4-carboxylic acid in 40 ml of methanol 30 was stirred at 45-50°C. During 4 minutes, 4.87 g (40.1 mmole) of (R)(+)-(1-phenylethyl)amine in 45 ml of methanol was added to the resulting thin slurry, yielding a solution. The heating bath was removed, and the
I 9
mixture was cooled slowly to ambient temperature, granulated for 16 hours and filtered. This afforded 6.4 g (86.6% yield) of the (R)-(1-phenylethyl)amine salt of (S)-6-fluoro-4-ureidochroman-4-carboxylic acid, 5 mp 206-210°C, [alphaj^ *= + 54.3° (c*0.3, methanol).
The mother liquors from the filtration were evaporated in vacuo to give 8.3 g of a mixture of the (R)-(1-phenylethyl)amine salts of (R)-6-fluoro-4-ureidochroman-4-carboxylic acid and (RS)-6-fluoro-4-ureidochroman-4-10 carboxylic acid, mp 198-2008C, [alpha]^ » -35.4° (C=0.5, methanol).
The above mixture of salts is distributed between ethyl acetate and water, with the pH first adjusted to 10. The ethyl acetate layer is separated and optically 15 active amine recovered by evaporation. The pH of aqueous phase is then adjusted to 1-2 with hydrochloric acid and extracted with fresh ethyl acetate. The organic phase is washed with additional small portions of water, dried (MgS04) and evaporated to yield a 20 mixture of (R)- and (RS)-6-fluoro-4-ureidochroman-4-carboxylie acid.
PREPARATION 4
(1R,2S)(-)-Ephedrine Salts of 6-Fluoro-4-ureidochroman- 4-carboxylic Acid
METHOD A
A slurry of 35.6 g (0.14 mole) of 6-fluoro-4-ureidochroman-4-carboxylic acid in 1.07 liters of acetone was stirred at reflux (59°C) for 30 minutes, and then it was cooled to 54°C. To the resulting 30 slurry was added 24.4 g (0.148 mole) of (1R,2S)-ephedrine all in one portion. The slurry thinned and a near solution resulted. After less than two minutes at 55°C rapid crystallization began. The slurry was refluxed
for 2 hours, cooled to 4 0°C and the crystalline solid was recovered by filtration to give 26.1 g of the (1R,2S)-ephedrine salt of (S)-6-fluoro-4-ureidochroman-4-carboxylic acid, mp 204 (dec), [alphaj^5 • + 37.0 5 (c«l, methanol).
The mothers liquors were cooled to room temperature and the further solid was recovered by filtration to give 1.3 g of material, rap 180-185®C (dec), [alpha]^5 ■ 0 (Ol, methanol) . The filtrate was evaporated in 10 vacuo to give 32.9 g of a mixture of the (1R,2S)-ephedrine salts of (R)-6-fluoro-4-ureidochroman-4-carboxylic acid and (RS)-6-fluoro-4-ureidochroman-4-carboxylic acid, mp 72-90°C, [alpha]^5» - 55.7° (Ol, methanol).
The latter mixture of salts is partitioned between dichloromethane (150 ml) and water (150 ml) and the pH is adjusted to 11.5. The organic layer is removed and evaporated in vacuo to give recovered (1R,2S)-ephedrine. The pH of the aqueous layer is lowered to 3 to 4 and 20 the solid which precipitates is recovered by filtration to give a mixture of (R)-6-fluoro-4-ureidochroman-4-carboxylic acid and (RS)-6-fluoro-4-ureidochroman-4-carboxylic acid.
A slurry of 25 g of the (1R,2S)-ephedrine salt of 25 (S)-6-fluoro-4-ureidochroman-4-carboxylic acid from above in 250 ml of acetone was stirred and heated under reflux and then the mixture was cooled to 40°C. The solid was recovered by filtration to give 24 g of purified (1R,2S)-ephedrine salt of (S)-6-fluoro-4-
2 5
ureidochroman-4-carboxylic acid, mp 205°C, [alpha]£ = + 38.2° (c=l, methanol).
METHOD B
A mixture of 100 g of (RS)-6-fluoro-4-ureidochroman-4-carboxylic acid and 374 ml of methanol was heated 35 under reflux (65°C) for 30 minutes and then it was
Claims (13)
1. A process for the regeneration of 6-fluoro-4-chromanone from (r)-6-fluoro-4-ureidochroman-4-carboxylic acid or a mixture of (R)- and (RS)-6-fluoro-4-ureidochroman-4-carboxylic acid, which comprises: reacting said (R)-6-fluoro-4-ureidochroman-4-carboxylic acid or mixture of (R)- and (RS)-6-fluoro-4-ureidochroman-4-carboxylic acid with a metal permanganate, in an aqueous or partially aqueous solvent system, at a temperature in the range from 10 to 70°C, and at a pH in the range from 3.0 to 7.0.
2. The process according to claim 1, wherein said metal permanganate is an alkali metal permanganate.
3. The process according to claim 2, wherein said alkali metal permanganate is potassium permanganate.
4. The process according to claim 3, wherein the solvent system is substantially aqueous.
5. The process according to claim 4, wherein 0.7 to 2.0 molar equivalents of potassium permanganate is used.
6. The process according to claim 5, wherein 1.0 to 1.2 molar equivalents of potassium permanganate is used.
7. The process according to claim 5, wherein the pH of 3.0 to 7.0 is achieved by the addition of an acid selected from the group consisting of hydrochloric acid, sulfuric acid, nitric acid, phosphoric acid, acetic acid, methanesulfonic acid, benzenesulfonic acid and toluenesulfonic acids.
8. The process according to claim 7, wherein said acid is acetic acid.
9. The process according to claim 8, wherein the 6-fluoro-4-chromanone is regenerated from a mixture of (R)- and (RS)-6-fluoro-4-ureidochroman-4-carboxylic . acid. 2 135 94 -22-
10. The process according to claim 9, wherein the ratio of said (R)- to said (RS)-6-fluoro-4-ureidochroman-4-carboxylic acid is in the range from 20:1 to 1:2.
11. The process according to claim 10, wherein said solvent system is water containing from 0.5 to 3 percent of glacial acetic acid by volume.
12. A process as claimed in any one of claims 1 to 11 when performed substantially as hereinbefore described with reference to any example thereof.
13. 6-fluoro-4-chromanone from (R)-6-fluoro-4-ureidochroman -4-carboxylic acid or a mixture of (R)- and (RS)-6-fluror-4-ureidochroman-4-carboxylic acid when produced by a process as claimed in any one of the preceding claims. A. J. PARK 8l SON CANTS
Applications Claiming Priority (1)
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US65506684A | 1984-09-26 | 1984-09-26 |
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NZ213594A true NZ213594A (en) | 1988-01-08 |
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NZ21359485A NZ213594A (en) | 1984-09-26 | 1985-09-24 | Regeneration of 6-fluoro-4-chromanone from 6-fluoro-4-ureidochroman-4-carboxylic acid |
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1985
- 1985-09-24 NZ NZ21359485A patent/NZ213594A/en unknown
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