Claims
- 1. A process for preparing a compound of formula (IV): ##STR20## wherein Z represents H, halo, nitro or H.sub.3 CSO.sub.x.sup.-, wherein x is 0, 1 or 2, comprising
- a) contacting an oxazoline compound of formula (I): ##STR21## wherein Z is as defined hereinbefore, with sufficient quantity of an equilibrium driving reagent capable of causing an equilibrium between oxazoline compound (I) and an oxazoline compound of formula (II): ##STR22## wherein Z is as defined hereinbefore, and the reagent drives the equilibrium toward oxazoline compound (II) by preferential precipitation of oxazoline compound (II) from the equilibrium driving reagent such that the molar ratio of compound (II) to compound (I) is at least 80:20; wherein the equilibrium driving reagent is selected from a protic solvent and ammonia or an ammonium salt, wherein the protic solvent consists essentially of water, a C-1 to C-10 alkanoic acid, a C-1 to C-10 alcohol or mixtures thereof; and recovering the so precipitated oxazoline compound;
- b) contacting compound (II) with a fluorinating agent selected from the group consisting of fluorides of alkali and alkaline earth metals, fluorides of ammonia, fluorides of phosphonium, phosphorus fluoride, hydrofluoric acid, FAR (1-diethylamino-1,1-difluoro-2-chloro-2-fluoro-ethane), an alpha, alpha-difluoroalkylamine of the formula: ##STR23## wherein X.sub.1 is Chlorine or fluorine
- X.sub.2 is chlorine, fluorine or trifluoromethyl, R4 and R,5 taken individually are lower alkyl, and
- R.sub.4 and R.sub.5 taken together with the attached nitrogen atom represent the residue of a heterocyclic radical having five to seven ring atoms and Ishikawa reagent,
- to give a fluorinated oxazoline compound of formula (III): ##STR24## wherein Z is as defined hereinbefore; and c) hydrolyzing compound (III) to compound (IV).
- 2. The process of claim 1 wherein a cosolvent selected from the group consisting of C.sub.4-C.sub.10 alkanes, benzene, toluene, xylenes, chlorobenzene, diethylether, tert-butylmethylether, isopropylether and mixtures thereof is present in the equilibrium driving agent.
- 3. A process for preparing an oxazoline compound of formula (II): ##STR25## wherein Z represents H, halo, nitro or H.sub.3 CSO.sub.x.sup.-, wherein x is 0, 1 or 2, comprising contacting an oxazoline compound of formula (I): ##STR26## wherein Z is as defined herein before, with sufficient quantity of an equilibrium driving reagent capable of causing an equilibrium between oxazoline compound (I) and oxazoline compound (II), wherein the reagent drives the equilibrium toward oxazoline compound (II) by preferential precipitation of oxazoline compound (II) from the equilibrium driving reagent such that the molar ratio of compound (II) to compound (I) is at least 80:20; wherein the equilibrium driving reagent is selected from a protic solvent and ammonia or an ammonium salt, wherein the protic solvent consists essentially of water, a C-1 to C-10 alkanoic acid, a C-1 to C-10 alcohol or mixtures thereof; and recovering the so precipitated oxazoline compound.
- 4. The process of claim 3 wherein a cosolvent selected from the group consisting of C.sub.4 -C.sub.10 alkanes, benzene, toluene, xylenes, chlorobenzene, diethylether, tert-butylmethylether, isopropylether and mixtures thereof is present in the equilibrium driving agent.
- 5. The process of claim 1 wherein the protic solvent comprises isopropyl alcohol.
- 6. The process of claim 5 wherein the isopropanol is present in an amount of from 1.5 to 2 ml of isopropanol per gram of oxazoline (I).
- 7. The process of claim 1 wherein oxazoline (II) is recovered by filtering precipitated oxazoline (II) from the reaction mixture.
- 8. The process of claim 1 wherein oxazoline compound (I) is admixed with oxazoline compound (II) prior to contacting with the equilibrium driving reagent.
- 9. The process of claim 3 wherein the protic solvent comprises isopropyl alcohol.
- 10. The process of claim 9 wherein the isopropanol is present in an amount of from 1.5 to 2 ml of isopropanol per gram of oxazoline (I).
- 11. The process of claim 3 wherein Z represents H.sub.3 CSO.sub.2 --.
- 12. The process of claim 3 wherein oxazoline (II) is recovered by filtering precipitated oxazoline (II) from the reaction mixture.
- 13. The process of claim 3 wherein oxazoline compound (I) is admixed with oxazoline compound (II) prior to contacting with the equilibrium driving reagent.
- 14. The process of claim 1 Z represents H.sub.3 CSO.sub.2 --.
Parent Case Info
The present application is the U.S. national application corresponding to International application No. PCT/US91/07608, filed Oct. 23, 1991 and designating the U.S., which PCT application is in turn a continuation-in-part of U.S. application Ser. No. 07/603,575, filed Oct. 25, 1990 now abandoned the benefits of which applications are claimed pursuant to the provisions of 35 U.S.C. .sctn.120,363 and 365 (C).
PCT Information
Filing Document |
Filing Date |
Country |
Kind |
102e Date |
371c Date |
PCT/US91/07608 |
10/23/1991 |
|
|
4/22/1993 |
4/22/1993 |
US Referenced Citations (19)
Foreign Referenced Citations (4)
Number |
Date |
Country |
155135 |
Feb 1951 |
AUX |
0130633 |
Jan 1985 |
EPX |
1071077 |
Aug 1952 |
FRX |
90-02738 |
Mar 1990 |
WOX |
Non-Patent Literature Citations (3)
Entry |
Chemical Abstracts, 1958, vol. 52, Col. 10180 Abstracting US 3,820,041. |
H. Witte and W. Seeliger, Formation of Cyclic Imidic Esters by Reaction of Nitriles etc Ann. Chem. 1974, pp. 996-1009. |
Chemical Abstracts, 1956, vol. 50, Col. 13998 Abstracting US 2,718,520. |
Continuation in Parts (1)
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Number |
Date |
Country |
Parent |
603575 |
Oct 1990 |
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