[특허]Purification of gaseous inorganic halide

Honeywell Intellectual Properties Inc.

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특허 상세정보

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Purification of gaseous inorganic halide

특허상세정보
국가/구분	United States(US) Patent 등록
국제특허분류(IPC7판)	C01B-035/06
미국특허분류(USC)	423/210; 423/240.S; 423/293; 423/292; 423/301; 423/462; 423/489
출원번호	US-0592030 (2000-06-12)
발명자 / 주소	Rajoria, Dalbir S.
출원인 / 주소	Honeywell Intellectual Properties Inc.
인용정보	피인용 횟수 : 0 인용 특허 : 18

초록

The present invention provides an apparatus and method for the purification of gaseous inorganic halides utilizing a reactive metal and molecular sieves to remove impurities.

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1. A process for purifying gaseous inorganic halides comprising contacting a crude gaseous inorganic halide with a substance comprising a reactive material, wherein the reactive material reacts with impurities in the crude gaseous inorganic halide to thereby remove the impurities from the gaseous inorganic halide, and wherein said gaseous inorganic halide is selected from the group consisting of BF 3 , BCl 3 , GeF 4 , PF 3 , PF 5 , AsF 3 , AsF 5 , SbF 3 , SbF 5 , and mixtures thereof. 2. A process according to claim 1 wherein the reactive material comprises a reactive metal. 3. A process according to claim 2 wherein the reactive metal has a high surface to volume ratio. 4. A process according to claim 2 wherein the reactive metal comprises an alkali metal, alkaline earth metal, or an alloy of such a metal with a Group III or Group IV element. 5. A process according to claim 2 wherein the reactive metal is selected from the group consisting of lithium and alloys of lithium with one or more of the elements silicon, aluminum, germanium, boron, and calcium. 6. A process according to claim 2 wherein the reactive metal is selected from the group consisting of calcium and alloys of calcium with one or more of the elements silicon, aluminum, germanium, and boron. 7. A process according to claim 1 wherein the contacting step is performed at a temperature between about 25 and about 300° C. 8. A process according to claim 7 wherein the crude gaseous inorganic halide is contacted with the reactive material for a time between about 0.5 minutes to about 30 minutes. 9. A process according to claim 7 wherein the crude gaseous inorganic halide is contacted with the reactive material for a time between about 5 minutes to about 15 minutes. 10. A process according to claim 7 wherein the crude gaseous inorganic halide is contacted with the reactive material for a time between about 8 minutes to about 10 minutes. 11. A process according to claim 1 wherein the crude gaseous inorganic halide is purified by distillation over an adsorbent material prior to being contacted with the reactive material. 12. A process according to claim 11 wherein the adsorbent material is a molecular sieve. 13. A process according to claim 11 wherein the adsorbent is a 5A molecular sieve. 14. A process according to claim 11 wherein the said distillation step includes condensing the crude inorganic halide at or below its melting point temperature and pumping off the uncondensed gases. 15. A process according to claim 1 wherein the process further comprises purifying the gaseous inorganic halide by distillation after being contacted with the reactive material. 16. A process according to claim 15 wherein said distillation is conducted over an adsorbent material. 17. A process according to claim 16 wherein the adsorbent material is a molecular sieve. 18. A process according to claim 15 wherein the said distillation step is conducted at a temperature at or below the melting point of the inorganic halide and the uncondensed gases are optionally pumped off. 19. A process according to claim 1 wherein said contacting step is performed at a consumption location of said purified gaseous inorganic halide. 20. A process for purifying BF 3 comprising contacting the crude BF 3 with a reactive metal selected from the group consisting of lithium and alloys of lithium with one or more of the elements silicon, aluminum, germanium, boron, and calcium at a temperature above room temperature. 21. A process according to claim 20 wherein said contacting comprises passing the crude BF 3 through a column packed with said reactive metal. 22. A process according to claim 20 wherein the reactive metal has a high surface to volume ratio. 23. A process according to claim 20 wherein the contacting step is performed at a temperature between about 25 and about 300° C. 24. A process according to claim 23 wherein the contacting step is performed at a temperature between about 50° C. and about 250° C. 25. A process according to claim 23 wherein the crude BF 3 is contacted with the heated reactive metal for a time between about 0.5 minutes to about 30 minutes. 26. A process according to claim 23 wherein the crude BF 3 is contacted with the heated reactive metal for a time between 5 minutes and about 15 minutes. 27. A process according to claim 23 wherein the impure BF 3 is contacted with the heated reactive metal for a time between about 8 minutes to about 10 minutes. 28. A process according to claim 20 wherein the process further comprises purifying the crude BF 3 by distillation over an adsorbent material prior to being contacted with the heated reactive metal. 29. process according to claim 28 wherein the adsorbent material is a molecular sieve. 30. A process according to claim 28 wherein the adsorbent material is a 5A molecular sieve. 31. A process according to claim 28 wherein the said distillation step is conducted at temperatures at or below the melting point of the BF 3 and optionally pumping off the uncondensed gases. 32. A process according to claim 29 or claim 30 wherein the BF 3 is condensed at temperatures between about −78° C. and about −190° C. during the said distillation step and the uncondensed gases are optionally pumped off. 33. A process according to claim 29 or claim 30 wherein the BF 3 , after being contacted with the adsorbent material, is held at a temperature between about −190 to about 0° C. before contacting it with the reactive metal. 34. A process according to claim 20 further comprising the step wherein the BF 3 is purified by distillation after being contacted with the reactive metal. 35. A process according to claim 34 wherein said distillation after contact with the heated reactive metal includes distillation over an adsorbent material. 36. A process according to claim 35 wherein the adsorbent is a molecular sieve. 37. A process according to claim 34 wherein, in said distillation step the BF 3 is condensed at a temperature at or below its melting point temperature and the uncondensed gases are pumped off. 38. A process according to claim 20 further comprising the step of utilizing the purified BF 3 at a consumption location, said contacting step being performed at said consumption location. 39. A process for purifying boron trifluoride comprising the steps:(a) condensing crude boron trifluoride at liquid nitrogen temperature in a vessel;(b) pumping off any uncondensed gas;(c) warming the condensed boron trifluoride to room temperature;(d) repeating the condensing and pumping steps (a), (b) and (c) at least one additional time;(e) contacting the boron trifluoride with molecular sieves in a vessel cooled to a temperature of about −80 to −20° C.;(f) contacting the boron trifluoride with lithium heated to a temperature of between about 100 to about 180° C.; and(g) optionally collecting the boron trifluoride into a vessel cooled to liquid nitrogen temperature. 40. A process according to claim 1 wherein said gaseous inorganic halide is BF 3 .

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Purification of gaseous inorganic halide

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Purification of gaseous inorganic halide

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