Synthesis of N
View Patent ↗The present disclosure generally relates to a new process for the preparation of high purity 5-nitro-isophthalamide compounds, which are useful as intermediates for the preparation of imaging agents, such as iodinated x-ray contrast imaging agents like ioversol, iohexyl and iopamidol.
1. A process for preparing a diamide compound of formula (2), the process comprising:
(i) forming a reaction mixture comprising a diester of formula (1),
a primary amine of formula RNH.sub. 2 , a basic catalyst and a solvent; and
(ii) heating the reaction mixture to a reaction temperature of from about 25° C. to less than 65° C. and holding the reaction mixture at the reaction temperature for a reaction time sufficient to generate a reaction product mixture comprising diamide compound formula (2)
wherein,
R, R 1 and R 2 independently selected from C 1 to C 18 straight or branched chain hydrocarbyl or substituted hydrocarbyl, and
the molar ratio of the primary amine to the diester is from 2:1 to about 2.4:1;
wherein the reaction product mixture comprises the diamide of formula (2) and at least one of the diester of formula (1), an acid amide of formula (3), an amide ester of formula (4) or an amide ester of formula (5)
wherein the wherein the content of the acid amide of formula (3) is about 2% or or less, by weight of the sum of the content of formulae (1) through (5).
2. R is selected from 2-hydroxyethyl, 2,3-dihydroxypropyl, 3-hydroxypropyl, 3,4-dihydroxybutyl, 4-hydroxybutyl and 1,3-dihydroxy isopropyl.
3. The process of claim 1 , wherein R 1 and R 2 are independently selected from methyl, ethyl, n-propyl, i-propyl, n-butyl, i-butyl and t-butyl.
4. The process of claim 1 , wherein the solvent comprises methanol, ethanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, 2-methoxymethanol, 2-ethoxyethanol, 3-methoxypropanol, formamide, N-methylformamide, or combinations thereof.
5. The process of claim 1 , wherein the basic catalyst is a salt of an alkali metal and an alkoxide or an alkaline earth metal and an alkoxide.
6. The process of claim 5 , wherein the metal is selected from sodium, potassium, lithium and magnesium, and the alkoxide is selected from methoxide, ethoxide, i-propoxide, t-butoxide and amoxide.
7. The process of claim 1 , wherein the molar ratio of the primary amine to the diester is from 2:1 to about 2.4:1, from about 2.1:1 to about 2.2:1, from about 2.1:1 to about 2.3:1, or between about 2:1 and about 2.1:1.
8. The process of claim 1 , wherein the molar ratio of the catalyst, on an equivalent basis, to the diester is from about 0.03:1 to about 0.1:1, from about 0.04:1 to about 0.1:1, from about 0.05:1 to about 0.09:1, or from about 0.06:1 to about 0.08:1.
9. The process of claim 1 , wherein the concentration of the diester of formula (1) in the reaction mixture is from about 1 to about 10 moles per liter, from about 2 to about 10 moles per liter, from about 3 to about 10 moles per liter, from about 4 to about 10 moles per liter, or from about 4 to about 8 moles per liter.
10. The process of claim 1 , wherein the reaction temperature is from about 25° C. to about 60° C., from about 25° C. to about 50° C., from about 25° to about 40° C., from about 25° C. to about 35° C., or from about 30° C. to about 40° C.
11. The process of claim 1 , wherein the reaction time is from about 1 hour to about 12 hours, from about 1 hour to about 8 hours, from about 1 hour to about 6 hours, from about 1 hour to about 4 hours, from about 1 hour to about 3 hours, from about 1 hour to about 2 hours, from about 2 hours to about 6 hours, or from about 2 hours to about 4 hours.
12. The process of claim 1 , wherein the content of the diamide of formula (2) is about 95%, about 96%, about 97%, about 98%, about 99% or more by weight of the sum of the content of formulae (1) through (5), as measured by high pressure liquid chromatography.
13. The process of claim 1 , wherein the content of the diester of formula (1) is about 1%, about 0.5%, about 0.3%, about 0.1%, about 0.05%, about 0.03%, about 0.01%, or less by weight of the sum of the content of formulae (1) through (5), or is non-detectable by high pressure liquid chromatography.
14. The process of claim 1 , wherein the content of the amide ester of formulae (4) and (5) is about 0.5%, about 0.3%, about 0.1%, about 0.08% about 0.06%, about 0.04%, about 0.02%, about 0.01% or less by weight of the sum of the content of formulae (1) through (5), or is non-detectable by high pressure liquid chromatography.
15. The process of claim 1 , wherein:
R is 2,3-dihydroxypropyl;
R 1 and R 2 are —-CH 3 ;
the catalyst is sodium methoxide;
the solvent comprises methanol;
the molar ratio of the primary amine to the diester is from about 2.04 to about 2.08;
the molar ratio of the catalyst, on an equivalent basis, to the diamide is from about 0.05:1 to about 0.09:1;
the reaction temperature is from about 25° C. to about 40° C.; and
the reaction time is from about 1 hour to about 3 hours.
16. The process of claim 15 , wherein the content of the diamide of formula (2) is at least about 96% by weight, the content of the diester of formula (1) is less than about 0.1% by weight, the content of the acid amide of formula (3) is less than about 2% by weight, and the content of the amide ester of formulae (4) and (5) is less than about 0.1% by weight of the content of the sum of the content of formulae (1) through (5).
17. The process of claim 1 , further comprising
isolating the diamide compound of formula (2);
purifying the isolated diamide compound; and
reducing the purified diamide compound by hydrogenation to form a 5-amino isophthalamide of formula (6):
18. The process of claim 17 , wherein the purification is carried out by ion exchange chromatography.