Claims
- 1. A reactor which uses process gasses, said reactor comprising:
a reactor chamber; an electrode located in said reactor chamber; a heater that heats said electrode in order to effect materials deposited thereon.
- 2. The reactor of claim 1 wherein:
said heater is incorporated into said electrode.
- 3. The reactor of claim 1 wherein:
said electrode is an upper electrode.
- 4. The reactor of claim 1 wherein:
said electrode is an upper electrode; a chuck located in said reactor chamber; and a lower electrode associated with said chuck.
- 5. The reactor of claim 1 wherein:
said heater includes a plurality of heater elements which are disposed along radii of said electrode.
- 6. The reactor of claim 1 wherein:
said electrode has bores provided therein; said heater includes a plurality of heater elements which are located through said bores of said electrode.
- 7. The reactor of claim 1 wherein:
a thermocouple is associated with said heater.
- 8. The reactor of claim 1 wherein:
said electrode is comprised of aluminum and the heater can heat the electrode to a maximum temperature of about 300° C. to about 350° C.
- 9. The reactor of claim 1 wherein:
said electrode is comprised of graphite and the heater can heat the electrode to a maximum temperature of about 400° C. to about 500° C.
- 10. The reactor of claim 1 wherein:
said electrode is comprised of silicon and the heater can heat the electrode to a maximum temperature of about 400° C. to about 500° C.
- 11. The reactor of claim 1 wherein:
said electrode is an electrical resistance heater.
- 12. A method of operating a reactor which comprises a reactor chamber, an electrode, a heater that heats said electrode, and gas inlets and outlets, the method comprising:
introducing process gas into said reactor chamber; providing powerto said electrode in order to facilitate a reaction with said process gas and a workpiece contained in said reactor chamber; and heating the electrode with said heaterto a temperature which encourages the growth of a stable layer of material on said electrode.
- 13. The method of claim 12 wherein said heating step includes:
heating the electrode to a temperature above a floating temperature that the electrode would otherwise attain during operation of the reactor without the heater.
- 14. The method of claim 12 wherein said heating step includes:
heating the electrode to about 300° C. to about 500° C.
- 15. The method of claim 12 wherein:
the method of operation of the reactor is an etch method.
- 16. The method of claim 12 wherein:
the method of operation of the reactor is a platinum etch method.
- 17. The reactor of claim 1 wherein:
said reactor is an etch reactor.
- 18. The reactor of claim 1 wherein:
said reactor is a platinum etch reactor.
- 19. The method of claim 16 wherein oxygen and chlorine are present in the reactor, the method includes:
heating the electrode in order to cause deposits of oxygen and chlorine to de-absorb from the electrode in order to leave mostly platinum deposited on the electrode.
- 20. A reactor which uses process gasses, said reactor comprising:
a reactor chamber; an electrode located in said reactor chamber; said electrode being textured in orderto encourage deposits to adhere to the surface of the electrode.
- 21. The reactor of claim 20 wherein the reactor is an etch reactor.
- 22. The reactor of claim 20 wherein the reactor is a platinum etch reactor.
- 23. The reactor of claim 20 wherein said electrode is an upper electrode.
- 24. The reactor of claim 20 wherein said electrode is textured in an irregular pattern.
- 25. The reactor of claim 20 wherein said electrode is textured so as to have a scalloped surface and wherein said scallops are at least one of concave scallops and convex scallops.
- 26. The reactorof claim 20 wherein said electrode is textured so that the surface of the electrode has a multiplicity of peaks and a multiplicity of valleys.
- 27. The reactor of claim 26 wherein:
there is an average peak to peak width and an average valley depth; an aspect ratio is defined as the average peak to peak width divided by the mean valley depth; and the aspect ratio is chosen in order to maximize the formation of a deposit on the surface of the electrode which will cause good adherence of the by-products of the reaction carried on in the reactor onto the surface of the electrode.
- 28. The reactor of claim 1 including a non-volatile material etch reactor.
- 29. The reactor of claim 20 including a non-volatile material etch reactor.
- 30. The method of claim 12 including a non-volatile material etch process.
- 31. The reactor of claim 12 including the step of etching one of the group consisting of titanium (Ti), titanium nitride (TiN), platinum (Pt), iridium (Ir), iridium oxide (IrO2), barium strontium titanate (BST), strontium bismuth tantalate (SBT), strontium titanate (STO), ruthenium (Ru), ruthenium oxide (RuO2), and lead zirconium titanate (PZT).
- 32. A reactor which uses process gasses, said reactor comprising:
a reactor chamber; a surface located in said reactor chamber; a heater that heats said surface in order to effect a material film deposited thereon.
- 33. The reactor of claim 32 wherein:
said surface is textured.
- 34. A reactor which uses process gasses, said reactor comprising:
a reactor chamber; a surface located in said reactor chamber; said surface being textured in order to encourage materials to adhere to the surface.
- 35. The reactor of claim 1 wherein said electrode is precoated with a film adhesion promoter.
- 36. The reactor of claim 35 wherein said film adhesion promoter includes one of titanium (Ti) and titanium nitride (TiN).
- 37. A reactor which uses process gases, said reactor comprising:
a reactor chamber; and precoating at least some internal surface of the reactor chamber with a adhesion promoter in order to encourage the development of durable deposits thereon which will be less likely to interfere with the deposit of a film on a workpiece.
- 38. The reactor of claim 37 wherein said film adhesion promoter includes one of titanium (Ti), titanium nitride (TiN), platinum (Pt), iridium (Ir), iridium oxide (IrO2), barium strontium titanate (BST), strontium bismuth tantalate (SBT), strontium titanate (STO), ruthenium (Ru), ruthenium oxide (RuO2), and lead zirconium titanate (PZT).
- 39. The reactor of claim 20 wherein said electrode is precoated with a film adhesion promoter.
- 40. The reactor of claim 39 wherein said film adhesion promoter includes at least one of titanium (Ti), titanium nitride (TiN), platinum (Pt), iridium (Ir), iridium oxide (IrO2), barium strontium titanate (BST), strontium bismuth tantalate (SBT), strontium titanate (STO), ruthenium (Ru), ruthenium oxide (RuO2), and lead zirconium titanate (PZT).
- 41. The reactor of claim 32 wherein said surface is a deposition shield.
- 42. The reactor of claim 34 wherein said surface is a deposition shield.
- 43. A reactor which uses process gasses, said reactor comprising:
a reactor chamber; a surface located in said reactor chamber; said surface is matt finished in order to encourage materials to adhere to the surface.
- 44. The reactor of claim 37 wherein said precoating is a non-volatile film.
- 45. A replaceable component for a reactor comprising:
a replaceable element; said element including devices adapted to receive heaters for heating the element in order to encourage the deposition of films.
- 46. The replaceable component of claim 45 including:
heaters incorporated in the replaceable element.
- 47. The replaceable component of claim 45 wherein said replaceable component is one of an electrode, and a deposition shield.
- 48. A replaceable component of a reactor comprising:
a replaceable element; said element being textured in order to encourage the deposit of films.
- 49. The replaceable component of claim 48 wherein said textured element includes a textured surface which has at least one of scallops, peaks, perforations, grooves, channels, a screened surface, and a matt-finished surface.
- 50. The replaceable component of claim 48 wherein said replaceable element is one of an electrode and a deposition shield.
- 51. A replaceable component of a reactor comprising:
a replaceable element; said element being a precoating in order to encourage the adherence thereto of a deposit.
- 52. The replaceable component of claim 51 wherein said precoating is of a non-volatile material.
- 53. The replaceable component of claim 52 wherein said precoating is provided and one of a replaceable electrode and a replaceable shield.
- 54. The replaceable component of claim 51 wherein said precoating is one of titanium (Ti), titanium nitride (TiN), platinum (Pt), iridium (Ir), iridium oxide (IrO2), barium strontium titanate (BST), strontium bismuth tantalate (SBT), strontium titanate (STO), ruthenium (Ru), ruthenium oxide (RuO2), and lead zirconium titanate (PZT).
- 55. A reactor which uses process gasses, said reactor comprising:
a reactor chamber; an electrode located in said reactor chamber; a heating means for heating said electrode in order to effect materials deposited thereon.
CROSS-REFERENCE
[0001] Cross-referenced and incorporated by reference are pending U.S. patent applications entitled A METHOD FOR MINIMIZING THE CRITICAL DIMENSION GROWTH OF A FEATURE ON A SEMICONDUCTOR WAFER filed on Nov. 19,1997, and with Ser. No. 08/974,089; and pending U.S. patent application entitled PLASMA REACTOR WITH A DEPOSITION SHIELD, filed on Dec. 5, 1997, and with Ser. No. 08/985,730; and pending U.S. patent application entitled PLASMA REACTOR WITH A DEPOSITION SHIELD filed on Dec. 1, 1998, and with Ser. No. 09/204,020.
Continuations (1)
|
Number |
Date |
Country |
Parent |
09453842 |
Dec 1999 |
US |
Child |
09888365 |
Jun 2001 |
US |