초록 ▼

A method and apparatus for manufacture of NF3 by gas-liquid phase reaction of fluorine and ammonia in molten ammonium acid fluoride (AAF) in a static reactor in which the reactants are conveyed primarily by thermal conduction or siphon. Optimally, the reactor contains one or more static mixing eleme

A method and apparatus for manufacture of NF3 by gas-liquid phase reaction of fluorine and ammonia in molten ammonium acid fluoride (AAF) in a static reactor in which the reactants are conveyed primarily by thermal conduction or siphon. Optimally, the reactor contains one or more static mixing elements with little, if any, mechanical agitation. Reactant flow rate and reaction temperature are regulated by the rate of introduction of ammonia and cooling, as necessary The ratio of hydrogen fluoride (generated by the reaction) to ammonia in the reactor is significantly lower than taught in the prior art. This allows a lower reaction temperature. The present invention is an improved synthetic method that offers enhanced selectivity and higher yields, improved control of reaction kinetics, reduced operational and energy costs, and a greater margin of safety.

대표청구항 ▼

I claim: 1. A method of manufacturing NF3 comprising reacting NH3 with F2 in and with molten Ammonium Acid Fluoride with a molar ratio of NH3 to HF of 1:2.28 to 1:2.55 within a closed loop reactor with one or more spaced cooling zones, in which the reactants are conveyed by thermal conduction or si

I claim: 1. A method of manufacturing NF3 comprising reacting NH3 with F2 in and with molten Ammonium Acid Fluoride with a molar ratio of NH3 to HF of 1:2.28 to 1:2.55 within a closed loop reactor with one or more spaced cooling zones, in which the reactants are conveyed by thermal conduction or siphon, but with essentially no mechanical agitation. 2. The method of claim 1, including continuous flow of reactants and reaction products within the closed loop. 3. The method of claim 1 or 2 wherein the reactor is annular or rectangular in shape. 4. The method of claim 1 or 2 wherein one or more static mixing element(s) is disposed within the reactor. 5. The method of claim 4 where the number of static mixing elements is 8 to 10. 6. The method of claim 1 or 2 where the reactor operates under pressure of 10 kilograms per square centimeter or less. 7. The method of claim 6 where the reactor operates under pressure of 4 to 5 kilograms per square centimeter. 8. The method of claim 4, wherein differential cooling along the reactor provides circulation of the reactants by thermal conduction or siphon across the static mixing element(s). 9. The method of claim 1 or 2 where the reaction is performed with a ratio of NH3 to HF of 1:2.34 to 1:2.46. 10. The method of claim 1 or 2 where the reaction is performed with a ratio of NF3 to HF of about 1:2.345. 11. The method of claim 1 or 2 where the reaction is performed in a continuous manner with the NH3 continuously added such that the ratio of NH3 to HF is maintained at 1:2.28 to 1:2.55. 12. The method of claim 11 wherein the ratio of NH3 to HF is maintained at 1:2.34-1:2.40. 13. The method of claim 12 wherein the ratio of NH3 to HF is maintained at approximately 1:2.345. 14. The method of claim 1 or 2 where the reaction is conducted at a temperature approximately 5�� C. higher than the melting point of the Ammonium Acid Fluoride, but less than about 140�� C. 15. The method of claim 1 or 2 where the reaction is conducted at a temperature between 120�� C. and 137�� C. 16. The method of claim 1 or 2 wherein the NH3 and the F2 are introduced on a same side of a static mixing element. 17. The method of claim 1 or 2 wherein the NH3 and the F2 are introduced on opposite sides of a static mixing element. 18. The method of claim 1 or 2, wherein F2 and/or NH3 is fed to the reactor through a conduit or nozzle. 19. The method of claim 1 or 2 where thermal conduction or siphon of the reactants is supplemented by mechanical agitation of 5000 watts/cubic meter of reactor volume or less. 20. The method of-claim 1 or 2 where the reactor is constructed of stainless steel. 21. The method of claim 4 where the static mixing elements are constructed of carbon steel. 22. The method of claim 4, wherein differential cooling on opposite sides of the static mixing element removes exothermic heat of reaction and facilitates movement of the molten Ammonium Acid Fluoride reactant by thermal conduction or siphon. 23. The method of claim 1 or 2, wherein NF3, ammonium bifluoride, HF and unreacted F2 are continuously withdrawn from the closed loop reactor.