Claims
- 1. An apparatus for quantitatively reducing oxide gases, comprising:
a vial; a pre-selected amount of reductant in said vial; a tube in said vial; means for separating said reductant and said tube; a pre-selected amount of a catalyst in said tube; a closure for said vial that allows gas transfer in and out of said vial; means for trapping said oxide gases in said vial; and means for heating at least a portion of said vial, said tube, said reductant, said catalyst, and said oxide gases.
- 2. The apparatus of claim 1, wherein said means for trapping said oxide gases in said vial includes means for cryogenically cooling said vial, said tube, said reductant, said catalyst, and said oxide gases.
- 3. The apparatus of claim 1, wherein said oxide gases include products of combustion.
- 4. The apparatus of claim 1, wherein said oxide gases include carbon dioxide gas.
- 5. The apparatus of claim 1, wherein said oxide gases include water vapor.
- 6. The apparatus of claim 1, wherein said oxide gases contain a sample to be analyzed.
- 7. The apparatus of claim 1, wherein said vial is a glass vial.
- 8. The apparatus of claim 1, wherein said vial is a quartz glass vial.
- 9. The apparatus of claim 1, wherein said vial is a septa-sealed vial.
- 10. The apparatus of claim 1, wherein said tube is a glass tube.
- 11. The apparatus of claim 1, wherein said reductant is zinc.
- 12. The apparatus of claim 1, wherein said reductant is hydrogen gas.
- 13. The apparatus of claim 1, wherein said catalyst is cobalt.
- 14. The apparatus of claim 1, wherein said catalyst is iron.
- 15. The apparatus of claim 1, wherein said means for separating said reductant and said tube is a multiplicity of glass beads separating said reductant and said tube.
- 16. The apparatus of claim 1, wherein said vial is a reaction vial of sufficient size to contain said oxide gases at room temperature and at whatever temperature is required for additional chemical reactions to proceed.
- 17. The apparatus of claim 1, wherein said vial includes a piercable septa seal.
- 18. The apparatus of claim 1, wherein said vial includes reactant solids or liquids contained in said via.
- 19. The apparatus of claim 1, wherein said vial is an 80 mm×8 mm septa-capped borosilicate vial.
- 20. A method of quantitatively reducing combustion gases, comprising the steps of:
providing a pre-selected amount of zinc in a vial; providing a tube in said vial; separating said zinc and said tube; providing a pre-selected amount of a catalyst in said tube; sealing said vial with a cap incorporating a piercable septum; injecting said combustion gases into said vial; and heating at least a portion of said vial, said tube, said zinc, said catalyst, and said oxide gases.
- 21. The method of claim 20, including the step of cryogenically cooling said vial, said tube, said zinc, said catalyst, and said oxide gases.
- 22. The method of claim 20, wherein said oxide gases include carbon dioxide gas.
- 23. The method of claim 20, wherein said oxide gases contain a sample to be analyzed.
- 24. The method of claim 23, including the step of analyzing said sample.
- 25. The method of claim 24, wherein said step of analyzing said sample is performed by accelerator mass spectrometry.
- 26. The method of claim 20, wherein said vial is a glass vial.
- 27. The method of claim 26, wherein said vial is a quartz glass vial.
- 28. The method of claim 26, wherein said vial is a septa-sealed vial.
- 29. The method of claim 20, wherein said tube is a glass tube.
- 30. The method of claim 20, wherein said catalyst is cobalt.
- 31. The method of claim 20, wherein said catalyst is iron.
- 32. The method of claim 20, wherein said step of separating said zinc and said tube utilizes glass beads for separating said zinc and said tube.
- 33. The method of claim 20, wherein said step of injecting said oxide gases into said vial includes coupling said combustion gases through a disposable gas transfer manifold.
- 34. The method of claim 33, wherein said vial is a septa-sealed vial with a septa seal and including connecting said gas transfer manifold to said vial using a needle to pierce said septa seal.
- 35. The method of analyzing a sample of claim 20, wherein said step of injecting said combustion gases into said vial includes injecting water vapor into said vial.
- 36. The method of claim 20, wherein said step of trapping said combustion gases is performed utilizing liquid nitrogen to cryogenically cool said vial, said tube, said zinc, and said catalyst.
- 37. The method of claim 36, wherein said step of cryogenically cooling said vial, said tube, said zinc, said catalyst, and said oxide gases is performed by the placement of a sufficiently cold cryogen around said vial.
- 38. The method of claim 20, wherein said step of heating at least a portion of said vial, said tube, said zinc, said iron, and said combustion gases is performed utilizing a high temperature oven.
- 39. The method of analyzing a sample of claim 20, wherein said step of heating at least a portion of said vial, said tube, said zinc, said catalyst, and said combustion gases vaporizes said zinc.
- 40. The method of analyzing a sample of claim 20, wherein said oxide gases include carbon dioxide gas, and wherein said step of injecting said oxide gases into said vial includes injecting water vapor into said vial, and wherein said step of heating at least a portion of said vial, said tube, said zinc, said catalyst, and said oxide gases results in said carbon dioxide gas and said water reacting to form graphite.
- 41. The method of analyzing a sample of claim 20, wherein said step of heating at least a portion of said vial, said tube, said zinc, said catalyst, and said oxide gases is conducted using a muffle furnace at 550 to 900° C. for an appropriate one hour reaction time.
Government Interests
[0001] The United States Government has rights in this invention pursuant to Contract No. W-7405-ENG-48 between the United States Department of Energy and the University of California for the operation of Lawrence Livermore National Laboratory.