Patent Application
20080047578
These and other features and advantages of the present invention will be more fully disclosed in, or rendered obvious by, the following detailed description of the preferred embodiment of the invention, which is to be considered together with the accompanying drawings wherein like numbers refer to like parts, and further wherein:
Referring to
The reaction chamber 12 may be a CVD chamber, in which gases are introduced into the reaction chamber 12 and a plasma may be formed from the gases in the reaction chamber 12. In a heterogeneous, or surface-catalyzed reaction, the gas or plasma deposits a solid film on the surface of the wafer 34. By regulating the flow of gases from the interior of the reaction chamber 12 to the vacuum pump 24, the throttle valve 26 of the system 10 may be used to control the interior pressures of the reaction chamber 12.
Referring to
The cleaning gas may be added to the exhaust line 38 upstream of the plasma cleaning unit 36 via a dedicated cleaning gas supply line 37. Alternatively, and as illustrated in
A scrubber 40 may be connected to the discharge side of the vacuum pump 24. In one exemplary embodiment, the scrubber 40 may comprise a wet scrubber employing water. Thus, the scrubber 40 may combine the exhaust gas and its constituents with water to produce various aqueous species that can be treated using well-known waste treatment methods.
Alternatively, the scrubber 40 may comprise a first scrubbing stage comprising a heater element for heating the exhaust gas to a desired elevated temperature, combined with a second scrubbing stage comprising a water scrubbing section. Thus, the first scrubbing section may comprise a high temperature heater element for increasing the temperature of the exhaust gas in the range of about 800 degrees Celsius to about 1000 degrees Celsius. Most exhaust gases (e.g., HCl, HBr, Cl2, and the like) can be decomposed or oxidized at such elevated temperatures, while still remaining soluble in water, so that they may be more easily removed from the system using the water scrubbing section of the scrubber 40.
When activated, the plasma cleaning unit 36 creates a voltage field that excites molecules of residual matter deposited on the interior surfaces of the unit 36 and molecules of exhaust gases passing through the unit into a plasma state. The plasma enhances decomposition of the matter within unit 36 into gaseous products and byproducts that may be pumped out through the exhaust line thus preventing residue build-up.
For example, in the case where residue build-up within the exhaust line 38 is in the form of ammonium chloride (NH4Cl), the plasma formed by the plasma cleaning unit 36 breaks the residue down into components such as ammonia (NH3) and hydrochloric acid HCl.
Thus, an exemplary reaction mechanism may be described according to the formula AB(g)-->A(g)+B(g). For the embodiment in which the residue buildup comprises ammonium chloride, the reaction mechanism is: NH4Cl-->NH3(g)+HCl(g) (where the reaction is with Ar gas).
The voltage field created within the plasma cleaning unit 36 for forming the plasma may be generated using a variety of known methods such as radio frequency (RF) or microwave techniques. Where RF techniques are used, the RF power may be set at about 3000 kilo-watts in order to effect a desired byproduct removal.
The plasma cleaning unit 36 may be operated while the chamber cleaning operation in being performed, or it may be operated during the period in which film deposition is occurring within the reaction chamber 12.
It will be appreciated that multiple plasma cleaning units 36 may be installed in a single exhaust line 38 in order to enhance elimination of residue buildup in the exhaust line and vacuum pump 24. Where multiple plasma cleaning units 36 are installed, they may be identical or they may have different operational characteristics. Thus, in one embodiment, different plasma cleaning units 36 may be used in series and/or in parallel in order to remove different constituent byproducts from the exhaust gas. Additionally, where a single reaction chamber 12 is used for multiple processes, multiple different plasma cleaning units 36 may be included in the exhaust line 36, and each may be brought “on line” (or taken “off line”) depending on the process being performed within the reaction chamber so that a desired exhaust byproduct may be removed according to the process being performed.
The plasma cleaning unit 36 may be installed adjacent to the throttle valve 26 of the reaction chamber 12 to decompose the byproduct (which in one embodiment is NH4Cl) in the exhaust gas. The byproduct may then be condensed and removed via the scrubber 40. An appropriate gas, which in one embodiment is Argon, may then be added for plasma ignition. Argon gas may be supplied from an appropriate container and injected or directed into to the exhaust line 38 upstream of the plasma cleaning unit 36. Alternatively, the gas may be supplied directly to the plasma cleaning unit 36 (as shown in
One substantial advantage afforded by the plasma cleaning unit 10 is that it works to maintain the process chamber servo at stable pressure for production. To do this, the generator 36 must be capable of reacting to the changing characteristics of the plasma, thus ensuring that power remains stable during operation. This is because the plasma generator 36 is used to ignite and maintain a plasma that may vary continuously, and/or that may or may not be stable. Thus, a high degree of control is required in order to maintain such balance or stability during operation.
In addition to preventing clogging of the exhaust line 38, the plasma cleaning unit 36 may eliminate or reduce pump and local scrubber clogging, which may cause undesirable backpressure in the process chamber exhaust lines 38. Such pump and scrubber clogging may interrupt production, and ultimately may lead to undesirable wafer scrap. Additionally, the plasma cleaning unit 10 reduces the total manpower required to maintain the pumping system operational, and reduces vacuum leakage resulting from out-gassing of exhaust gas byproducts.
While the foregoing invention has been described with reference to the above embodiments, various modifications and changes can be made without departing from the spirit of the invention. Accordingly, all such modifications and changes are considered to be within the scope and range of equivalents of the appended claims.
