IP Library Granted Patent US 6,977,225
Granted Patent B2
US 6,977,225 · App. 10/706,244 · Granted Dec 20, 2005

Chemical vapor deposition of titanium from titanium tetrachloride and hydrocarbon reactants

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Quick Facts
Patent No.
US 6,977,225
App. No.
10/706,244
Granted
Dec 20, 2005
Kind
B2
Abstract

A new process for depositing titanium metal layers via chemical vapor deposition is disclosed. The process provides deposited titanium layers having a high degree of conformality, even in trenches and contact openings having aspect ratios greater than 1:5.

Claims (104)

1. A plasma enhanced chemical vapor deposition process comprising:

admitting a hydrocarbon gas into a deposition chamber;

admitting titanium tetrachloride gas into the deposition chamber;

forming a plasma in the deposition chamber having at a power level greater than a first ionization energy, but less than a second ionization energy, of the hydrocarbon gas for forming hydrocarbon radicals therein; and

heating a substrate to a temperature for some of the hydrocarbon radicals formed from the hydrocarbon gas to react with some of the chlorine atoms from the titanium tetrachloride gas for depositing titanium metal on a portion of a surface of the substrate.

2. The process of claim 1 , wherein the substrate is heated to a temperature within a range of about 200° C. to about 500° C.

3. The process of claim 1 , wherein the hydrocarbon gas is selected from a group of compounds comprising C n H 2n+2 , C n H 2n and C n H 2n−2 .

4. The process of claim 1 , wherein the hydrocarbon gas comprises an alkane having fewer than five carbon atoms per molecule.

5. The process of claim 4 , wherein the hydrocarbon gas includes methane.

6. The process of claim 1 , further comprising:

mounting the substrate on a susceptor;

heating the susceptor; and

heating the substrate using the susceptor.

7. The process of claim 1 , wherein the titanium tetrachloride gas includes a titanium tetrachloride gas mixed with a carrier gas selected from a group consisting of helium, argon and hydrogen.

8. The process of claim 7 , wherein the titanium tetrachloride gas includes titanium tetrachloride gas introduced into the carrier gas using a bubbler apparatus.

9. The process of claim 7 , wherein a liquid injector sprays the titanium tetrachloride and passes through a vaporizer.

10. The process of claim 1 , wherein the hydrocarbon gas includes a hydrocarbon gas mixed with a carrier gas selected from a group consisting of helium and argon.

11. The process of claim 1 , further comprising:

removing reaction products from the deposition chamber during the process.

12. The process of claim 11 , wherein an alkyl chloride gas comprises a reaction product.

13. The process of claim 1 , wherein the deposition chamber comprises a cold wall deposition chamber, with walls thereof maintained at a temperature within a preferred range of about 100° C. to about 200° C. for preventing condensation of the titanium tetrachloride gas thereon.

14. The process of claim 1 , wherein the deposition chamber comprises a hot wall deposition chamber.

15. The process of claim 1 , wherein the plasma comprises a plasma produced with a radio frequency source.

16. The process of claim 15 , wherein the radio frequency source comprises a radio frequency source having a power setting within a range of about 20 watts to about 100 watts.

17. The process of claim 15 , wherein the radio frequency source comprises a radio frequency source having a frequency greater than about 10 KHz.

18. The process of claim 1 , wherein the deposition chamber comprises a deposition chamber for maintaining a pressure within a range of about 2 torr to about 100 torr.

19. The process of claim 1 , wherein the deposition chamber comprises a deposition chamber for maintaining a pressure within a preferred range of about 2 torr to about 5 torr.

20. The process of claim 1 , further comprising:

premixing the titanium tetrachloride gas and the hydrocarbon gas before being admitted to the deposition chamber.

21. The process of claim 20 , wherein a ratio of the hydrocarbon gas to the titanium tetrachloride gas comprising the premixture thereof comprises a ratio of between about four and about one thousand to one.

22. The process of claim 1 , wherein the substrate comprises a semiconductor wafer.

23. A plasma enhanced chemical vapor deposition process comprising:

admitting hydrocarbon gas into a deposition chamber;

admitting titanium tetrachloride gas into the deposition chamber;

forming a plasma within the deposition chamber of the hydrocarbon gas for forming hydrocarbon radicals;

maintaining the plasma at a power level greater than a first ionization energy, but less than a second ionization energy, of the hydrocarbon gas for forming the hydrocarbon radicals; and

heating a semiconductor wafer to a temperature sufficient to induce some of the hydrocarbon radicals to react with some chlorine atoms from the titanium tetrachloride gas for forming chlorinated hydrocarbon molecules for depositing titanium metal on a portion of a surface of the semiconductor wafer.

24. The process of claim 23 , further comprising:

maintaining the deposition chamber at a pressure within a range of about 2 torr to about 10 torr.

25. The process of claim 23 , wherein the power level comprises a radio frequency source operating at a power setting within a range of about 20 watts to about 100 watts and at a frequency greater than about 10 KHz.

26. The process of claim 23 , further comprising:

premixing the titanium tetrachloride gas and the hydrocarbon gas for their admission to the deposition chamber in a ratio of hydrocarbon gas to the titanium tetrachloride gas being between about four and about one thousand to one.

27. The process of claim 23 , wherein the hydrocarbon gas includes methane.

28. The process of claim 23 , wherein the hydrocarbon gas includes a hydrocarbon gas selected from a group consisting of compounds C n H 2n+2 , C n H 2n and C n H 2n−2 .

29. A plasma enhanced chemical vapor deposition process comprising:

flowing a hydrocarbon gas into a deposition chamber;

flowing a titanium tetrachioride gas into the deposition chamber;

forming a plasma in the deposition chamber using a power level substantially in a range of greater than a first ionization energy of the hydrocarbon gas to less than a second ionization energy of the hydrocarbon gas for forming hydrocarbon radicals in the hydrocarbon gas; and

heating a substrate to a temperature for some of the hydrocarbon radicals formed from the hydrocarbon gas to react with some chlorine atoms from the titanium tetrachioride gas for depositing titanium metal on a portion of a surface of the substrate.

30. The process of claim 29 , wherein the substrate is heated to a temperature within a range of about 200° C. to about 500° C.

31. The process of claim 29 , wherein the hydrocarbon gas is selected from a group of compounds comprising C n H 2n+2, C n H 2n and C n H 2n−2 .

32. The process of claim 29 , wherein the hydrocarbon gas comprises an alkane having fewer than five carbon atoms per molecule.

33. The process of claim 32 , wherein the hydrocarbon gas includes methane.

34. The process of claim 29 , further comprising:

mounting the substrate on a susceptor;

heating the susceptor; and

heating the substrate using the susceptor.

35. The process of claim 29 , wherein the titanium tetrachioride gas includes a titanium tetrachioride gas mixed with a carrier gas selected from a group consisting of helium, argon and hydrogen.

36. The process of claim 35 , wherein the titanium tetrachioride gas includes titanium tetrachioride gas introduced into the carrier gas using a bubbler apparatus.

37. The process of claim 36 , wherein a liquid injector sprays the titanium tetrachloride gas and passes through a vaporizer.

38. The process of claim 29 , wherein the hydrocarbon gas includes a hydrocarbon gas mixed with a carrier gas selected from a group consisting of helium and argon.

39. The process of claim 29 , further comprising:

removing reaction products from the deposition chamber during the process.

40. The process of claim 39 , wherein an alkyl chloride gas comprises a reaction product.

41. The process of claim 29 , wherein the deposition chamber comprises a cold wall deposition chamber, the walls thereof maintained at a temperature within a preferred range of about 100° C. to about 200° C. for preventing condensation of titanium tetrachioride thereon.

42. The process of claim 29 , wherein the deposition chamber comprises a hot wall deposition chamber.

43. The process of claim 29 , wherein the plasma comprises plasma produced by a radio frequency source.

44. The process of claim 43 , wherein the radio frequency source comprises a radio frequency source having a power setting within a range of about 20 watts to about 100 watts.

45. The process of claim 43 , wherein the radio frequency source comprises a radio frequency source having a frequency greater than about 10 KHz.

46. The process of claim 29 , wherein the deposition chamber comprises a deposition chamber for maintaining a pressure within a range of about 2 torr to about 100 torr.

47. The process of claim 29 , wherein the deposition chamber comprises a deposition chamber for maintaining a pressure within a preferred range of about 2 torr to about 5 torr.

48. The process of claim 29 , further comprising:

premixing the titanium tetrachioride gas and the hydrocarbon gas before flowing into the deposition chamber.

49. The process of claim 48 , wherein a ratio of the hydrocarbon gas to the titanium tetrachioride gas comprising the premixture thereof comprises a ratio of between about four and about one thousand to one.

50. The process of claim 29 , wherein the substrate comprises a semiconductor wafer.

51. A deposition process having a hydrocarbon gas and a titanium tetrachioride gas in a chamber comprising:

providing a plasma for the chamber having a power level greater than a first ionization energy and less than a second ionization energy of the hydrocarbon gas for forming hydrocarbon radicals; and

heating a substrate to a temperature for some of the hydrocarbon radicals formed from the hydrocarbon gas to react with some chlorine atoms from the titanium tetrachloride gas for depositing titanium metal on a portion of a surface of the substrate.

52. The process of claim 51 , wherein the substrate is heated to a temperature within a range of about 200° C. to about 500° C.

53. The process of claim 51 , wherein the hydrocarbon gas is selected from a group of compounds comprising C n H 2n+2 , C n H 2n and C n H 2n−2 .

54. The process of claim 51 , wherein the hydrocarbon gas comprises an alkane having fewer than five carbon atoms per molecule.

55. The process of claim 54 , wherein the hydrocarbon gas includes methane.

56. The process of claim 51 , further comprising:

mounting the substrate on a susceptor;

heating the susceptor; and

heating the substrate using the susceptor.

57. The process of claim 51 , wherein the titanium tetrachioride gas includes a titanium tetrachioride gas mixed with a carrier gas selected from a group consisting of helium, argon and hydrogen.

58. The process of claim 57 , wherein the titanium tetrachioride gas includes titanium tetrachioride gas introduced into the carrier gas using a bubbler apparatus.

59. The process of claim 57 , wherein a liquid injector sprays the titanium tetrachloride gas and passes through a vaporizer.

60. The process of claim 51 , wherein the hydrocarbon gas includes a hydrocarbon gas mixed with a carrier gas selected from a group consisting of helium and argon.

61. The process of claim 51 , further comprising:

removing reaction products from the chamber during the process.

62. The process of claim 61 , wherein an alkyl chloride gas comprises a reaction product.

63. The process of claim 51 , wherein the chamber comprises a cold wall deposition chamber, with walls thereof maintained at a temperature within a preferred range of about 100° C. to about 200° C. for preventing condensation of the titanium tetrachioride gas thereon.

64. The process of claim 51 , wherein the chamber comprises a hot wall deposition chamber.

65. The process of claim 51 , wherein the plasma comprises a plasma produced with a radio frequency source.

66. The process of claim 65 , wherein the radio frequency source comprises a radio frequency source having a power setting within a range of about 20 watts to about 100 watts.

67. The process of claim 65 , wherein the radio frequency source comprises a radio frequency source having a frequency greater than about 10 KHz.

68. The process of claim 51 , wherein the chamber comprises a deposition chamber for maintaining a pressure within a range of about 2 torr to about 100 torr.

69. The process of claim 51 , wherein the chamber comprises a chamber for maintaining a pressure within a preferred range of about 2 torr to about 5 torr.

70. The process of claim 51 , further comprising:

premixing the titanium tetrachioride gas and the hydrocarbon gas before being admitted to the chamber.

71. The process of claim 70 , wherein a ratio of the hydrocarbon gas to the titanium tetrachloride gas comprising the premixture thereof comprises a ratio of between about four and about one thousand to one.

72. The process of claim 51 , wherein the substrate comprises a semiconductor wafer.

Assignments (8)
RELEASE OF U.S. PATENT AGREEMENT (FOR NON-U.S. GRANTORS) Recorded Oct 12, 2018
From: ROYAL BANK OF CANADA, AS LENDER
To: CONVERSANT INTELLECTUAL PROPERTY MANAGEMENT INC.
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U.S. PATENT SECURITY AGREEMENT (FOR NON-U.S. GRANTORS) Recorded Sep 9, 2014
From: CONVERSANT INTELLECTUAL PROPERTY MANAGEMENT INC.
To: CPPIB CREDIT INVESTMENTS INC., AS LENDER; ROYAL BANK OF CANADA, AS LENDER
Reel/Frame 033706/0367 →
CHANGE OF ADDRESS Recorded Sep 3, 2014
From: CONVERSANT INTELLECTUAL PROPERTY MANAGEMENT INC.
To: CONVERSANT INTELLECTUAL PROPERTY MANAGEMENT INC.
Reel/Frame 033678/0096 →
RELEASE OF SECURITY INTEREST Recorded Aug 7, 2014
From: ROYAL BANK OF CANADA
To: CONVERSANT INTELLECTUAL PROPERTY MANAGEMENT INC.; CONVERSANT IP N.B. 868 INC.; CONVERSANT IP N.B. 276 INC.
Reel/Frame 033484/0344 →
CHANGE OF NAME Recorded Mar 13, 2014
From: MOSAID TECHNOLOGIES INCORPORATED
To: CONVERSANT INTELLECTUAL PROPERTY MANAGEMENT INC.
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U.S. INTELLECTUAL PROPERTY SECURITY AGREEMENT (FOR NON-U.S. GRANTORS) - SHORT FORM Recorded Jan 10, 2012
From: 658276 N.B. LTD.; 658868 N.B. INC.; MOSAID TECHNOLOGIES INCORPORATED
To: ROYAL BANK OF CANADA
Reel/Frame 027512/0196 →
CORRECTIVE ASSIGNMENT TO CORRECT THE TO CORRECT THE ASSIGNEES' ADDRESS PREVIOUSLY RECORDED ON REEL 023220 FRAME 0243. ASSIGNOR(S) HEREBY CONFIRMS THE MOSAID TECHNOLOGIES INCORPORATED 6 SAUBLE DRIVE, SUITE 203, OTTAWA,ONTARIO, CANADA K2K 2X1. Recorded Apr 14, 2010
From: MICRON TECHNOLOGY, INC.
To: MOSAID TECHNOLOGIES INCORPORATED
Reel/Frame 024225/0878 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 14, 2009
From: MICRON TECHNOLOGY, INC.
To: MOSAID TECHNOLOGIES INCORPORATED
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