Patexia. Research
Patent No. US 04564405
Issue Date Jan 14, 1986
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Patent 04564405 - PYX Purification technique > Claims

  • 1. A process for synthesizing crystals of 2,6-bis(picrylamino)-3,5-dinitropyridine, the process comprising the steps of: (a) dissolving 2,6-bis(picrylamino)-3,5-dinitropyridine in dimethyl sulfoxide to form an adduct of 2,6-bis(picrylamino)-3,5 dinitropyridine and dimethyl sulfoxide; (b) cooling the resultant solution to obtain a slurry of dimethyl sulfoxide and 2,6-bis(picrylamino)-3,5 dinitropyridine adduct; (c) filtering the slurry to remove excess dimethyl sulfoxide; and (d) dissociating the dimethyl sulfoxide and 2,6-bis(picrylamino)-3,5 dinitropyridine adduct to form particles of 2,6-bis(picrylamino)-3,5 dinitropyridine.
    • 2. The process of claim 1 wherein said step of dissociating is carried out by slurrying the adduct in a solvent miscible with dimethyl sulfoxide.
      • 3. The process of claim 2 wherein the solvent is selected from the group consisting of water, acetone, methanol and mixtures thereof.
    • 4. The process of claim 1 wherein said step of dissociating is carried out by subjecting the adduct to heat.
    • 5. The process of claim 1 wherein said step of dissociating is carried out by subjecting the adduct to a vacuum.
    • 6. The process of claim 1 wherein said step of dissociating is carried out by a combination of heat and vacuum.
    • 7. A cubic crystal particle form of 1,2,6-bis(picrylamino)-3,5 dinitropyridine produced in accordance with the process of claim 1, 4, 5, or 6.
    • 8. A agglomerate crystal particle form of 2,6-bis(picrylamino)-3,5 dinitropyridine produced in accordance with the process of claim 1, 2 or 3.
    • 9. The process of claim 1 in which further comprises the step of recycling the dimethyl sulfoxide recovered from after the filteration step for use in dissolving the crude 2,6-bis(picrylamino)-3,5 dinitropyridine.
    • 10. The process of claim 1 or 9 which further comprises the step of washing 2,6-bis(picrylamino)-3,5 dinitropyridine with a nitric acid solution.
    • 11. The process of claim 1 or 10 wherein the particle size of 2,6-bis(picrylamino)-3,5 dinitropyridine is controlled.
  • 12. A flowable granular explosive comprising 2,6-bis(picrylamino)-3,5 dinitropyridine, at least 80 percent of said 2,6-bis(picrylamino)-3,5 dinitropyridine being in cubic particle form.
    • 17. The explosive of claim 12 wherein said cubic form of 2,6-bis(picrylamino)-3,5, dinitropyridine is in discrete particle form.
  • 13. A flowable granular explosive comprising 2,6-bis(picrylamino)-3,5 dinitropyridine, at least 80 percent of said 2,6-bis(picrylamino)-3,5 dinitropyridine being in agglomerate particle form.
  • 14. A flowable granular explosive comprising 2,6-bis(picrylamino)-3,5 dinitropyridine, at least 80 percent of said 2,6-bis(picrylamino)-3,5 dinitropyridine being in cubic or agglomerate particle form and mixtures thereof.
  • 15. The explosive of claims 12, 13 or 14 wherein said particle form of 2,6-bis(picrylamino)-3,5 dinitropyridine is formed by removing the solvent from a solution of 2,6-bis(picrylamino)-3,5 dinitropyridine and dimethyl sulfoxide, said particle form of 2,6-bis(picrylamino)-3,5 dinitropyridine having greater bulk density and improved flow characteristics, thermal stability and sensitivity to shock stimulus than that of particles of 2,6-bis(picrylamino)-3,5 dinitropyridine prior to formation of said 2,6-bis(picrylamino)-3,5 dinitropyridine and dimethyl sulfoxide solution and removal of solvent therefrom.
    • 16. The explosive of claim 15 wherein said particle forms of 2,6-bis(picrylamino)-3,5 dinitropyridine are in solid, crystalline form.