PROCESS FOR ETCHING POLYSILICON WITH FREON 11 AND ANOTHER GAS

Abstract: A process for etching polysilicon wherein CFCl3 (Freon 11) and another gas, typically SF6, is pre-mixed in a storage chamber (1) before routing to an etching chamber (5). This process prevents condensation of the Freon 11 in a routing line and resultant failure of a mass flow controller (3) due to liquid ingestion. Furthermore, since the gases are pre-mixed and only one mass flow controller is used, the accuracy of the mixture is not dependent on the precision of the mass flow controller.

Description: PROCESS FOR ETCHING POLYSILICON WITH FREON 11 AND ANOTHER GAS Background of the Invention Field of the Invention This invention relates generally to an improved process for etching polysilicon and, more particularly, to a process of pre-mixing CFCI3 (Freon 11) and SF5 for etching polysilicon. Background Art The manufacturing of semiconductor chips and related thin film circuitry involves the etching of different layers such as polysilicon and silicon. Typically, the area to be etched is masked by material such as photoresist with the mask forming a pattern of lines and areas exposing the layer to be etched. Earlier methods accomplished this etching by a wet chemical process using large amounts of various acids, alkalis, organic solvents and the like which contacted the exposed surface. However, many times this wet process resulted in contamination by impurities contained in the chemicals and swelling of the resist film used as a mask causing an irregular shape and occurrences of undercut. Undercutting occurs when the etσhant acts horizontally as well as vertically, thereby removing material below the photoresist. As technology advances and the trend toward miniaturization continues, an increased degree of integration requires more precise etching processes. More recent processes employ gas plasmas, particularly fluorine based gases selected from the saturated halocarbon series such as CF4, CCI4, and BCI3. These gases are mixed with inert gases such as O2, N2, or Ar in a chamber in which the etching is to be accomplished. One particular known process comprises the mixing of CFCI3 (Freon 11) and SFg in the etching chamber which results in etched geometries with less than 0.3 micron total resist mask undercut. Freon 11 is stored in a tank in liquid form and remains a liquid at ambient temperatures, approximately 20°C, because its boiling point is 23.7°C at one atmosphere pressure. As Freon 11 boils off creating a vapor, the vapor is removed along a line to a mass flow controller (MFC) . The MFC precisely measures and provides for a predetermined flow of Freon 11 vapor to the etching chamber. The SFg is stored in a second tank in gas form and is also transported along a line to another MFC, wherein a predetermined flow is provided to the etching chamber. However, a temperature or pressure gradient along the line transporting the Freon vapor may cause the vapor to condense into a liquid. This condensed liquid may enter the MFC, causing temporary or permanent failure due to liquid ingestion. Furthermore, it is possible for the liquid to accumulate causing a blockage in the line, thereby preventing any Freon 11 vapor from reaching the MFC. In either case, the end result is production yield loss, costly system downtime, and costly MFC replacement if damage is permanent. Attempts to eliminate the occurrence of this condensation by controlling the temperature of the line have not always been successful. Furthermore, the accuracy of the mix is dependent upon the correction operation of the two MFCs. Thus, what is needed is an improved process for mixing Freon 11 and SFg that prevents failure of the process due to liquid forming in the vapor transportation lines, and where the accuracy of the percent mix of gases is independent of the MFCs. Summary of the Invention Accordingly, it is an object of the present invention to provide an improved process for etching semiconductor materials. mixture of Freon 11 and another gas wherein the Freon 11 vapor does not condense in the lines supplying the Freon 11 to the etching chamber. Still another object of the present invention is to provide an improved process for etching semiconductor materials with a mixture of Freon 11 and another gas wherein the accuracy of the percent mix of the gases is independent of MFCs. In carrying out the above and other objects of the invention in one form, there is provided a process for etching semiconductor material comprising the steps of mixing Freon 11 gas with a second gas and routing the mixed gases into an etching chamber. The above and other objects, features, and advantages of the present invention will be better understood from the following detailed description. Brief Description of the Drawing The single figure is a block diagram illustrating an apparatus suitable for use in carrying out the inventive process. Detailed Description of the Preferred Embodiment SFg, as well as other fluorine based gases selected from the saturated halocarbon series, provides for a fast etch rate of semiconductor materials and provides for excellent selectivity of oxides (better etch rate of the primary material, i.e., polysilicon, to the secondary material, i.e., silicon dioxide). However", SFg, when used alone, causes unacceptable undercut of the photoresist mask. Freon 11 has a slow etch rate but causes little undercut. When the SFg and Freon 11 are pre-mixed in accordance with the present invention, a sufficiently fast etch rate and selectivity are obtained while minimizing the underσut. A mixture of 12.0% of Freon 11 and 88.0% SFg provides good results; however, it is expected that a ' percent range for Freon 11 from 8.0% to 17.0% would provide beneficial results. This mixture precludes the condensation of the Freon 11 and the resultant failure of the MFC. Since the gases are pre-mixed, only one line and one MFC are required for supplying the mixture to the etch chamber. Therefore, the MFC has no bearing on the accuracy of the percent mix of the Freon 11 and SFg. Referring to the single figure, storage chamber 1 is substantially evacuated and then filled with Freon 11 to a vapor pressure of 75.0%. At approximately 20° C, the absolute pressure of this Freon 11 is approximately 62 kPa. The remainder of storage chamber 1 is then filled with SFg to approximately 414 kPa. Once mixed, Freon 11 will not condense at room temperature. The gas mixture flows through a line 2 to a single MFC 3 and then through line 4 to etching chamber 5. The gas mixture will not condense in the line or the MFC; therefore, there is no blockage of the line or failure of the MFC. Furthermore, since the gas is pre-mixed and there is only one MFC, the accuracy of the percent mix of gases is independent of the MFCs. Another embodiment comprises a two step etch process in which Freon 11 and SFg, mixed as described above, is used first to etch the material. This mixture is then removed from the etching chamber and a mixture of Freon 11 and Argon is used for "overetching" the material. Storage chamber 1 is again filled with Freon 11 to a vapor pressure of 75.0%.. The remainder of storage chamber 1 is then filled with Argon to approximately 138 kPa. Although other inert gases could be used, argon is desirable since it inhibits Freon 11 polymerization effects. A 39.0% mixture of Freon 11 in argon has proven satisfactory, although other percentages would work as well. By mixing Freon 11 and the inert gas, condensation in the lines is prevented, thereby preventing blockage of the lines and failure of the MFC. By now it should be appreciated that there has been provided an improved process of pre-mixing Freon 11 with another gas for etching polysilicon. This process prevents condensation of the Freon 11, thereby preventing blockage of the line and failure of the MFC. Furthermore, by pre-mixing the gases, the accuracy of the mix is not dependent upon the MFCs. The above description is given by way of example only. Changes in form and details may be made by one skilled in the art without parting from the spirit and scope of the invention. For example, the pressure and percent of the gas mixtures may vary.

Claims: AMENDED CLAIMS [received by the International Bureau on 12 January 1986 (21.01.86); original claims 1-7 cancelled and replaced by new claims 8-14 (2 pages)] 1 (cancelled) . 2 (cancelled) . 3 (cancelled) . 4 (cancelled) . 5 (cancelled) . 6 (cancelled) . 7 (cancelled) . 8 (new) . A process for etching a semiconductor material comprising the steps of: storing CFCI3 in gaseous state at ambient temperature; supplying said gas to a mass flow controller; supplying said gas from the mass flow controller to a plasma reactor; and etching a semiconductor material using a plasma comprising said gas. 9 (new) . The process as set forth in claim 8 wherein said gaseous state is obtained by the step of: mixing said CFCI3 with a fluorine based gas. 10 (new) . The process according to claim 9 wherein the fluorine based gas is SFg. 11 (new) . The process according to claim 10 wherein- the percent mixture of the CFCI3 gas is in the range of 8.0 to 17.0 percent. 12 (new) . The process as set forth in claim 8 wherein said gaseous state is obtained by the step of: mixing said CFCI 3 with inert gas. 13 (new) . The process as set forth in claim 12 wherein said inert gas is argon. 14 (new) . A process for etching a semiconductor material in a plasma reactor comprising the steps of: storing CFCI3 in a gaseous state at ambient temperature as a mixture with a fluorine based gas; supplying said gas to a mass flow controller; supplying said gas to said reactor from said mass flow controller; etching said semiconductor material; terminating the flow of said gas; storing CFCI3 in a gaseous state at ambient temperature as a second mixture, said second mixture including an inert gas; supplying said second mixture to a mass flow controller; supplying said second mixture to said reactor from the mass flow controller; and etching said semiconductor material with said second mixture.

Inventors: SCANNELL JACK WAYNE, SCANNELL, JACK, WAYNE
Applicants: TEGAL CORP, TEGAL CORPORATION
Application year: 1985
Main classification: H01L21
IPC codes: H01L21