Claims
- 1. A method for fabricating a thermally stable ultralow dielectric constant film comprising the steps of:providing a plasma enhanced chemical vapor deposition (PECVD) reactor; positioning a substrate in said PECVD reactor; flowing a first precursor gas comprising cyclic siloxane molecules into said PECVD reactor; flowing at least a second precursor gas comprising organic molecules with ring structures having C, H and O atoms into said PECVD reactor; and depositing a film comprising Si, C, O and H and a multiplicity of nanometer-sized pores on said substrate, said depositing is performed in the presence of an inert gas.
- 2. The method according to claim 1, further comprising the step of:mixing said first precursor gas with said inert carrier gas.
- 3. The method according to claim 1, wherein said PECVD reactor is of a parallel plate type reactor.
- 4. The method for fabricating a thermally stable ultralow dielectric constant film according to claim 3, said method further comprising the step of:applying a RF power to an electrode of said parallel plate PECVD reactor.
- 5. The method according to claim 1, wherein said film is optionally heated after deposition at a temperature not less than about 300° C. for at least about 0.25 hours.
- 6. The method according to claim 1, wherein said film has a dielectric constant of not more than about 2.8.
- 7. The method according to claim 1, wherein said film has a dielectric constant of not more than about 2.3.
- 8. The method according to claim 1, wherein said film has a dielectric constant in a range from about 1.5 to about 2.5.
- 9. The method according to claim 1, wherein said film comprises:between about 5 and about 40 atomic percent of Si; between about 5 and about 45 atomic percent of C; between 0 and about 50 atomic percent of O; and between about 10 and about 55 atomic percent of H.
- 10. The method according to claim 1, further comprising the step of:providing a parallel plate reactor having an area of a substrate chuck between about 300 cm2 and about 800 cm2, and a gap between the substrate and a top electrode between about 1 cm and about 10 cm.
- 11. The method according to claim 10, wherein a change in the area of said substrate chuck by a factor, X, changes the RF power by a factor, X.
- 12. The method according to claim 10, wherein a change in the area of the substrate chuck by a factor, Y, and a change in the gap between a gas distribution plate and the substrate chuck by a factor, Z, changes gas flow rates by a factor, YZ, such that residence time in plasma is maintained.
- 13. The method according to claim 1, further comprising a step of:heat treating said film at a temperature not higher than about 300° C. for a first time period and heat treating said film at a temperature not lower than about 300° C. for a second time period, said second time period being longer than said first time period.
- 14. The method according to claim 13, wherein said second time period is at least about ten times that of said first time period.
- 15. The method according to claim 1, wherein said cyclic siloxane is selected from the group consisting of: tetramethylcyclotetrasiloxane and octamethylcyclotetrasiloxane.
- 16. The method according to claim 1, wherein said cyclic siloxane is tetramethylcyclotetrasiloxane.
- 17. The method according to claim 1, wherein said organic molecules comprise species of fused rings including ring structures that impart significant ring strain, wherein said ring structures that impart significant ring strain include rings of 3, 4, 7 or more atoms.
- 18. The method according to claim 1, wherein said organic molecules are cyclopentene oxide.
- 19. The method according to claim 1, wherein said step of depositing the film further comprises the steps of:setting a temperature for said substrate at between about 25° C. and about 400° C.; and setting an RF power density at between 0.05 W/cm2 to about 4.0 W/cm2.
- 20. The method according to claim 1, wherein said step of depositing the film further comprises:setting flow rates for said cyclic siloxane at between about 5 sccm and about 1000 sccm and setting a flow rate for said inert gas at between about 25 sccm and 10,000 sccm.
- 21. The method according to claim 20, wherein said flow rates for said cyclic siloxane are at between about 25 sccm and about 500 sccm.
- 22. The method according to claim 20, wherein when said PECVD reactor includes a plurality of depositions stations then the flow rates of said cyclic siloxane are multiplied by a total number of deposition stations in said PECVD reactor.
- 23. The method according to claim 1, wherein said step of depositing said film further comprises:setting flow rates said for said organic molecules at between about 5 sccm and about 50,000 sccm.
- 24. The method claim 23, wherein said flow rates for said organic molecules are at between about 25 sccm and about 10,000 sccm.
- 25. The method according to claim 1, wherein said step of depositing said film further comprises:setting a pressure for said PECVD reactor at between about 50 mTorr and about 5000 mTorr.
- 26. The method according to claim 25, wherein said pressure for said PECVD reactor is between about 100 mTorr and about 5000 mTorr.
- 27. The method according to claim 1, wherein said step of depositing said film further comprises:setting a flow rate ratio of organic molecules of cyclopentene oxide to cyclic siloxane of tetramethylcyclotetrasiloxane to between about 1 and about 80.
- 28. The method for fabricating a thermally stable ultralow dielectric constant film according to claim 27, wherein said flow rate ratio of said cyclopentene oxide to said tetramethylcyclotetrasiloxane is between about 10 and about 60.
- 29. The method according to claim 1, said method further comprising:providing a parallel plate plasma enhanced chemical vapor deposition chamber.
- 30. The method according to claim 1, wherein plasma in said PECVD reactor is run in a continuous mode.
- 31. The method according to claim 1, wherein plasma in said PECVD reactor is run in a pulsed mode.
- 32. A method for fabricating a thermally stable ultralow-k film comprising the steps of:providing parallel plate type plasma enhanced chemical vapor deposition (PECVD) reactor; positioning a pre-processed wafer on a substrate chuck having an area between about 300 cm2 and about 800 cm2 and maintaining a gap between said wafer and a top electrode between about 1 cm and about 10 cm; flowing a first precursor gas comprising cyclic siloxane molecules into said PECVD reactor; flowing at least a second precursor gas comprising organic molecules with ring structures having C, H and O atoms; and depositing an ultralow-k film on said wafer in the presence of an inert gas.
- 33. A method for fabricating a thermally stable ultralow-k film comprising the steps of:providing a parallel plate type plasma enhanced chemical vapor deposition (PECVD) reactor; positioning a wafer on a substrate chuck having an area between about 300 cm2 and about 800 cm2, and maintaining a gap between the wafer and a top electrode between about 1 cm and about 10 cm; flowing into said reactor over said wafer kept at a temperature between about 25° C. and about 400° C., a precursor gas of a cyclic siloxane at a flow rate between about 5 sccm and about 1000 sccm, and a second precursor gas of organic molecules at a flow rate between about 5 sccm and about 50,000 sccm, while keeping a pressure in said reactor between about 50 mTorr and about 5000 mTorr; depositing an ultralow-k film on said wafer under a RF power density between about 0.05 W/cm2 and about 4.0 W/cm2; and annealing said ultralow-k film at a temperature not less than about 300° C. for at least about 0.25 hour.
- 34. A method for fabricating a thermally stable ultralow-k film comprising the steps of:providing a parallel plate type plasma enhanced chemical vapor deposition (PECVD) reactor; positioning a wafer on a substrate chuck having an area between about 500 cm2 and about 600 cm2, and maintaining a gap between the wafer and a top electrode between about 1 cm and about 7 cm; flowing a precursor gas of a cyclic siloxane into said reactor over said wafer kept at a temperature between about 60° C. and about 200° C. at a flow rate between about 25 sccm and about 200 sccm and a second precursor of organic molecules at a flow rate between about 25 sccm and about 10,000 sccm while keeping a pressure in said reactor between about 100 mTorr and about 3000 mTorr; depositing an ultralow-k film on said wafer under a RF power density between about 0.25 W/cm2 and about 4 W/cm2; and annealing said ultralow-k film at a temperature not less than about 300° C. for at least about 0.25 hour.
CROSS-REFERENCE TO RELATED APPLICATIONS
The present application is a continuation-in-part application of U.S. Ser. No. 10/176,438, filed Jun. 19, 2002, now U.S. Pat. No. 6,541,398 which is a divisional application of U.S. Ser. No. 09/769,089, filed Jan. 25, 2001, now U.S. Pat. No. 6,441,491 and the present application also claims benefit of U.S. Provisional Application Serial No. 60/243,169, filed Oct. 25, 2000.
US Referenced Citations (2)
Number |
Name |
Date |
Kind |
6541398 |
Grill et al. |
Apr 2003 |
B2 |
20030017635 |
Apen et al. |
Jan 2003 |
A1 |
Provisional Applications (1)
|
Number |
Date |
Country |
|
60/243169 |
Oct 2000 |
US |
Continuation in Parts (1)
|
Number |
Date |
Country |
Parent |
10/176438 |
Jun 2002 |
US |
Child |
10/357134 |
|
US |