Claims
- 1. A process for preparing 4,6-dinitroresorcinol which minimizes side reactions catalyzed by the nitrosonium ion, comprising the steps of:
- providing a resorcinol-based starting material having the structure ##STR4## wherein R.sup.1 and R.sup.2 are independently selected from the group consisting of hydrogen and --C--R, R is hydrogen or lower alkyl, and R.sup.3 is selected from the group consisting of hydrogen, nitro and nitroso, with the proviso that R.sup.1, R.sup.2 and R.sup.3 are not all hydrogen;
- purging a reaction medium containing nitric acid with an inert gas so as to remove substantially all NO.sub.2 and nitrous acid therefrom;
- adding to the reaction medium an amount of a nitrosonium ion control agent effective to minimize nitrosonium ion-catalyzed side reactions;
- cooling the reaction medium to a temperature of between about -20.degree. C. and about 25.degree. C.;
- adding the resorcinol-based starting material to the cooled reaction medium; and
- allowing the starting material to react with the nitric acid while maintaining the temperature between about -20.degree. C. and about 25.degree. C. for a period of time selected so as to minimize styphnic acid production while sufficient to produce substantially complete precipitation of 4,6-dinitroresorcinol.
- 2. The process of claim 1, wherein the reaction medium is concentrated nitric acid.
- 3. The process of claim 2, wherein the temperature of the solution is maintained between about -10.degree. C. and about 0.degree. C.
- 4. The process of claim 2, wherein the resorcinol compound is selected from the group consisting of resorcinol monoacetate, resorcinol diacetate, 4-nitroresorcinol, 4-nitroresorcinol monoacetate and 4-nitroresorcinol diacetate.
- 5. The process of claim 2, wherein the nitrosonium ion control agent is a compound containing a primary amine group.
- 6. The process of claim 6, wherein the nitrosonium ion control agent is selected from the group consisting of urea, hydrazine, sulfamic acid, 4-nitroaniline, 2,4-dinitroaniline, hydroxylamine, sulfanilic acid, hydrazoic acid and sulfanilamide.
- 7. The process of claim 2, wherein the concentrated nitric acid is initially present at a concentration of between about 70 wt.% and about 90 wt.%.
- 8. The process of claim 7, wherein the concentrated nitric acid is initially present at a concentration of approximately 70 wt.%.
- 9. The process of claim 2, wherein after the addition of the starting material to the reaction medium, additional nitric acid is added to the reaction medium in an amount sufficient to bring the overall nitric acid concentration of the solution to at least about 80 wt.%.
- 10. The process of claim 9, wherein the additional nitric acid has a concentration of approximately 90 wt.%.
- 11. The process of claim 1, wherein the reaction medium is concentrated sulfuric acid.
- 12. The process of claim 11, wherein the sulfuric acid has an initial concentration of between about 60 wt.% and about 96 wt.%.
- 13. The process of claim 12, wherein the initial sulfuric acid concentration is between about 75 wt.% and 83 wt.%.
- 14. The process of claim 11, wherein the temperature of the solution is maintained between about -10.degree. C. and about 0.degree. C.
- 15. The process of claim 11, wherein the resorcinol compound is selected from the group consisting of resorcinol monoacetate, resorcinol diacetate, 4-nitroresorcinol, 4-nitroresorcinol monoacetate and 4-nitroresorcinol diacetate.
- 16. The process of claim 11, wherein the nitrosonium ion control agent is a compound containing a primary amine group.
- 17. The process of claim 16, wherein the nitrosonium ion control agent is selected from the group consisting of urea, hydrazine, sulfamic acid, 4-nitroaniline, 2,4-dinitroaniline, hydroxylamine, sulfanilic acid, hydrazoic acid and sulfanilamide.
- 18. The process of claim 11, wherein the reaction medium additionally includes a nitrating agent selected from the group consisting of sodium nitrate, potassium nitrate, N.sub.2 O.sub.5 and mixtures thereof. 22.
Government Interests
This invention was made with government support under contract F49620-83-K-0036 awarded by the United States Air Force. The government has certain rights in this invention.
US Referenced Citations (4)
Foreign Referenced Citations (2)
Number |
Date |
Country |
573768 |
Apr 1959 |
CAX |
1098932 |
Jun 1984 |
SUX |
Non-Patent Literature Citations (1)
Entry |
Fitzpatrick et al., J. Chem. Soc. Perkin Trans. II: 927-932 (1984). |