Patent Number: 052884341
Section: claims

1. A process for reducing the volume of a contaminated HEPA filter comprising dissolving the HEPA filter media in hydrofluoric acid solution of a strength required to have a minimal amount of free hydrofluoric acid at the end of the dissolution to provide that filter dissolution is complete, silica gel (SiO.sub.2) is minimized, and silicon fluoride (SiF.sub.4) is maximized. 2. The process of claim wherein the dissolution chemical reaction equations are: ##STR2## 3. The process of claim 2 wherein free HF at the end of the dissolution is less than 0.1M. 4. The process of claim 3 further includes complexing the excess HF leftover from the dissolution step with aluminum nitrite (AlNO.sub.3) solution to form water soluble aluminum fluoride salts. 5. The process of claim 4 wherein the fluoride-to-silicon ratio is 7:1 to provide water soluble aluminum fluoride salts. 6. The process according to claim 4 wherein the complexing chemical reaction is: EQU Al(NO.sub.3).sub.3 +nHF-AlF.sub.n.sup.+3-n +nHNO.sub.3. 7. The process of claim 1 further includes baking the HEPA filter at 550.degree. C. for a minimum of 3 hours, previous to the dissolution step, to sublimate any Kevlar.TM. reinforcement material that may be present in the filter. 8. The process of claim 4 further includes mixing the dissolved and complexed HEPA filter solution with both sodium and fluorinel waste to provide a ratio of HEPA filter solution and fluorinel waste:sodium waste of 4:1. 9. A process for dissolving and calcining a radioactive contaminated HEPA filter comprising: a. baking the HEPA filter;  b. dissolving the HEPA filter media in a hydrofluoric (HF) acid solution of a strength required to minimize formation of both silica gel and precipitates, forming an HF/filter solution;  c. complexing the HF/filter solution with an aluminum nitrate (AlNO.sub.3) solution forming a complexed filter waste solution;  d. mixing the complexed filter waste solution with a radioactive solution forming a complexed filter/radioactive waste solution;  e. performing a second complexing on the complexed filter/radioactive waste solution by addition of calcium nitrate (Ca(NO.sub.3).sub.2), forming a blended feed solution; and then  f. calcining the blended feed solution, thereby forming a calcined particulate and fines.  a. baking the HEPA filter;  b. dissolving the HEPA filter media in a hydrofluoric (HF) acid solution in an amount that gives a molar ratio of fluoride-to-silicon of about 7:1, forming an HF/filter solution;  c. complexing the HF/filter solution with an aluminum nitrate (AlNO.sub.3) solution forming a complexed filter waste solution;  d. mixing the complexed filter waste solution with a radioactive solution forming a complexed filter/radioactive waste solution;  e. performing a second complexing on the complexed filter/radioactive waste solution by addition of calcium nitrate (Ca(NO.sub.3).sub.2), forming a blended feed solution; and then  f. calcining the blended feed solution, thereby forming a calcined particulate and fines.  a. baking the HEPA filter at about 550.degree. C. for about 3 hours;  b. dissolving the HEPA filter media in a hydrofluoric (HF) acid solution in an amount that gives a molar ratio of fluoride-to-silicon of about 7:1, forming an HF/filter solution;  c. complexing the HF/filter solution with an amount of 2.2 molar aluminum nitrate (AlNO.sub.3) solution that gives a fluoride-to-aluminum molar ratio of between 20:1 and 40:1, forming a complexed filter waste solution;  d. mixing the complexed filter waste solution with a radioactive solution forming a complexed filter/radioactive waste solution;  e. performing a second complexing on the complexed filter/radioactive waste solution by addition of an amount of calcium nitrate (Ca(NO.sub.3).sub.2), to obtain a calcium-to-fluoride molar ratio of about 0.7:1, forming a blended feed solution; and then  f. calcining the blended feed solution, thereby forming a calcined particulate and fines. 10. The process as recited in claim 9 wherein a baking temperature is about 550.degree. C. and a baking period is about 3 hours. 11. The process as recited in claim 9 wherein the hydrofluoric acid concentration is at a maximum of 2 molar solution and an amount of HF solution is added to obtain a molar ratio of fluoride/silicon of about 7:1. 12. The process as recited in claim 11 wherein an amount of 2.2 molar AlNO.sub.3 solution is added for complexing the HF/filter solution to obtain a fluoride-to-aluminum molar ratio of between 20:1 and 40:1. 13. The process as recited in claim 12 and wherein the radioactive waste comprises a mixture of fluorinel and a sodium waste. 14. The process as recited in claim 13 wherein an amount of calcium nitrate is added to the complexed filter/radioactive waste solution to obtain the blended feed solution having a calcium-to-fluoride molar ratio of about 0.70:1. 15. The process as recited in claim 14 wherein the blended feed solution has a maximum ratio of sodium waste-to-fluorinel waste and HF/filter solution of about 1:4 and a maximum ratio of HF/filter solution-to-fluorinel of about 1:5.5. 16. The process as recited in claim 11 wherein the filter dissolution is in the hydrofluoric acid at a temperature of about 70.degree. C. for about 1 hour and then in HF acid at 25.degree. C. for about 12 hours. 17. A process for dissolving and calcining a radioactive contaminated HEPA filter comprising: 18. The process as recited in claim 17 wherein a baking temperature is about 550.degree. C. and a baking period is about 3 hours. 19. The process as recited in claim 17 wherein the hydrofluoric acid concentration is at a maximum of 2 molar solution. 20. The process as recited in claim 19 wherein an amount of 2.2 molar AlNO.sub.3 solution is added for complexing the HF/filter solution in order to obtain a fluoride-to-aluminum molar ratio of between 20:1 to 40:1. 21. The process as recited in claim 20 wherein an amount of Ca(NO.sub.3).sub.2 is added to the complexed filter/radioactive waste solution to obtain a blended feed solution having a calcium-to-fluoride molar ratio of about 0.70:1. 22. The process as recited in claim 21 wherein the blended feed solution has a maximum ratio of sodium waste-to-fluorinel waste and HF/filter solution of about 1:4 and a maximum ratio of HF/filter solution-to-fluorinel of about 1:5.5. 23. A process for dissolving and calcining a radioactive contaminated HEPA filter comprising: 24. The process as recited in claim 23 wherein the filter dissolution is in the hydrofluoric acid at a temperature of about 70.degree. C. for about 1 hour and then in HF acid at 25.degree. C. for about 12 hours. 25. The process as recited in claim 24 wherein the blended feed solution has a maximum ratio of sodium waste-to-fluorinel and HF/filter solution of about 1:4 and a maximum ratio of HF/filter solution-to-fluorinel of about 1:5.5. 26. The process as recited in claim 25 wherein the overall HEPA waste volume reduction ratio is about 15:1.