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CVD of silicon oxide using TEOS decomposition and in-situ planarization process    
United States Patent4872947   
Link to this pagehttp://www.wikipatents.com/4872947.html
Inventor(s)Wang; David N. (Cupertino, CA); White; John M. (Hayward, CA); Law; Kam S. (Union City, CA); Leung; Cissy (Union City, CA); Umotoy; Salvador P. (Pittsburg, CA); Collins; Kenneth S. (San Jose, CA); Adamik; John A. (San Ramon, CA); Perlov; Ilya (Mountain View, CA); Maydan; Dan (Los Altos Hills, CA)
AbstractA high pressure, high throughput, single wafer, semiconductor processing reactor is disclosed which is capable of thermal CVD, plasma-enhanced CVD, plasma-assisted etchback, plasma self-cleaning, and deposition topography modification by sputtering, either separately or as part of in-situ multiple step processing. A low temperature CVD process for forming a highly conformal layer of silicon dioxide is also disclosed. The process uses very high chamber pressure and low temperature, and TEOS and ozone reactants. The low temperature CVD silicon dioxide deposition step is particularly useful for planarizing underlying stepped dielectric layers, either along or in conjunction with a subsequent isotropic etch. A preferred in-situ multiple-step process for forming a planarized silicon dioxide layer uses (1) high rate silicon dioxide deposition at a low temperature and high pressure followed by (2) the deposition of the conformal silicon dioxide layer also at high pressure and low temperature, followed by (3) a high rate isotropic etch, preferably at low temperature and high pressure in the same reactor used for the two oxide deposition steps. Various combinations of the steps are disclosed for different applications, as is a preferred reactor self-cleaning step.
   














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Drawing from US Patent 4872947
CVD of silicon oxide using TEOS decomposition and in-situ planarization

     process - US Patent 4872947 Drawing
CVD of silicon oxide using TEOS decomposition and in-situ planarization process
Inventor     Wang; David N. (Cupertino, CA); White; John M. (Hayward, CA); Law; Kam S. (Union City, CA); Leung; Cissy (Union City, CA); Umotoy; Salvador P. (Pittsburg, CA); Collins; Kenneth S. (San Jose, CA); Adamik; John A. (San Ramon, CA); Perlov; Ilya (Mountain View, CA); Maydan; Dan (Los Altos Hills, CA)
Owner/Assignee     Applied Materials, Inc. (Santa Clara, CA)
Patent assignment
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Publication Date     October 10, 1989
Application Number     07/262,992
PAIR File History     Application Data   Transaction History
Image File Wrapper   Patent Term   Fees
Litigation
Filing Date     October 26, 1988
US Classification     216/38 118/50.1 118/620 118/728 204/192.12 204/192.37 204/298.33 204/298.35 216/63 216/67 216/79 257/E21.274 427/248.1 427/294 427/574 427/585 438/697 438/699 438/763 438/790
Int'l Classification     B44C 001/22 C03C 015/00 C03C 025/06
Examiner     Powell; William A.
Assistant Examiner    
Attorney/Law Firm     Schlemmer Dalton Associates
Address
Parent Case     This is a division of application Ser. No. 944,492, filed Dec. 19, 1986.
Priority Data    
USPTO Field of Search     427/38 427/39 427/248.1 427/294 118/728 118/50.1 118/620 118/623 156/643 156/646 156/653 156/657 156/345 204/192.12 204/192.32 204/192.35 204/192.37 204/298 252/79.1
Patent Tags     cvd silicon oxide teos decomposition in-situ planarization
   
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What is claimed is:

1. A process for depositing a conformal layer of silicon dioxide onto a substrate, comprising exposing the substrate to a reactive species formed from ozone, oxygen and tetraethylorthosilicate within a chamber, the pressure within the chamber being within the approximate range 10 torr to 200 torr and the substrate temperature being within the approximate range 200.degree. C. and 500.degree. C.

2. A process for forming a silicon oxide overlayer on a substrate within a chamber, comprising: positioning the substrate within a chamber and closely adjacent a manifold having a multiplicity of closely-spaced outlet holes closely-adjacent the substrate; and applying a mixture comprising ozone, oxygen and tetraethylorthosilicate to the manifold for communicating reactive nitrogen and oxygen species into the chamber via the outlet holes, while maintaining the substrate within the approximate range 200.degree. to 500.degree. C. and the chamber within the approximate range 10 to 200 torr.

3. The process of claim 2, further comprising communicating a purging gas into the chamber from the periphery of the manifold in a flow radially away from the substrate to confine the reactive species to the substrate.

4. The process of claim 2, wherein the substrate comprises a coating selected from silicon oxide, silicon nitride, silicon oxynitride and polysilicon, the process further comprising isotropically etching at least the silicon oxide overlayer in the chamber without breaking vacuum in the chamber following formation of the silicon oxide overlayer.

5. The process of claim 4, wherein the substrate coating is silicon oxide and is deposited by a plasma formed from a gas mixture which includes tetraethylorthosilicate, by communicating the gas mixture into the manifold while applying RF energy between the manifold and the substrate support and maintaining the pressure in the chamber within the range of about 1 to 50 torr and the temperature of the substrate within the range of about 200.degree. C. to 500.degree. C.

6. The process of claim 2, 3, 4 or 5, wherein the silicon oxide overlayer is formed using a chamber pressure of 40 to 120 torr and the silicon oxide substrate coating is formed using a chamber pressure of about 1 to 12 torr.

7. The process of claim 2, 3, 4 or 5, wherein the silicon oxide overlayer is formed using a chamber pressure of 40 to 120 torr and the silicon oxide substrate coating is formed using a chamber pressure of about 1 to 12 torr and the substrate temperature is maintained at about 375.degree. C. during the formation of both silicon oxide layers.

8. The process of claim 4 or claim 5, wherein the step of isotropically etching the silicon oxide comprises exposing the silicon oxide to a plasma formed from fluorinated gas selected from NF.sub.3, CF.sub.4 and C.sub.2 F.sub.6 in a carrier gas inlet to the chamber, with the substrate temperature being maintained within the range of about 100.degree. C. to 500.degree. C.

9. A process for planarizing a dielectric layer formed on a substrate in-situ in a chamber, comprising:

first, depositing a first, conformal, relatively thick layer of silicon oxide by exposing the substrate to a reactive plasma by positioning the substrate on a support within a chamber and adjacent a gas inlet manifold which is an RF electrode and includes a multiplicity of closely-spaced gas outlet holes closely adjacent the substrate; and communicating a gas mixture containing tetraethylorthosilicate into the manifold while applying RF energy between the manifold and the substrate support, with the pressure in the chamber being within the range of about 1 to 50 torr and heating the substrate to within the range of about 200.degree. C. to 500.degree. C.;

second, depositing a second, relatively thin silicon oxide layer on the first silicon oxide layer by applying a mixture comprising ozone, oxygen and tetraethylorthosilicate to the gas inlet manifold for communicating reactive nitrogen and oxygen species into the vacuum chamber via the outlet holes, while heating the substrate to within the approximate range 200.degree. C. to 500.degree. C. with the chamber pressure within the approximate range 10 to 200 torr; and

third, isotropically etching the resulting composite film by exposing the composite to a plasma formed within said chamber, by communicating a reactive gas selected from fluorinated gases such as NF.sub.3, CF.sub.4 and C.sub.2 F.sub.6 into the gas inlet manifold, and applying RF energy between the gas inlet manifold and the substrate support and heating the substrate to within the approximate range 200.degree. C. to 500.degree. C. while maintaining the chamber pressure within the approximate range 200 mt to 20 torr.

10. The method of claim 9, further comprising communicating a purging gas into the vacuum chamber from the periphery of the gas inlet manifold in a flow radially away from the substrate to confine the reactive species to the substrate.

11. The method of claim 9, further comprising communicating purging gas into the vacuum chamber in upwardly and downwardly directed flows merging about the periphery of the substrate and then proceeding radially outwardly thereof for confining the reactive deposition species to the substrate.

12. The method of claim 9, further comprising:

prior to the first step, positioning the substrate on the support and depositing on the dielectric layer a relatively thin silicon oxide layer using a reactive species formed from tetraethylorthosilicate, ozone and oxygen, a chamber pressure within the range of about 10 torr to 200 torr and while heating the substrate to within the range of about 200.degree. C. to 500.degree. C.; and

between said second and third steps, depositing a relatively thick layer of silicon oxide onto the second silicon layer oxide using plasma formed from tetraethylorthosilicate and oxygen, chamber pressure within the range of about 1 torr to 50 torr and while heating the substrate to the range of about 200.degree. C. to 500.degree. C.

13. The method of claim 2 or 9, further comprising communicating an inert gas into the chamber.

14. The method of claim 13, wherein the inert gas is communicated into the chamber via the base inlet manifold.
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BACKGROUND OF THE INVENTION

The present invention relates to a reactor and methods for performing single and in-situ multiple integrated circuit processing steps, including thermal CVD, plasma-enhanced chemical vapor deposition (PECVD), reactor self-cleaning, film etchback, and modification of profile or other film property by sputtering. The present invention also relates to a process for forming conformal, planar dielectric layers on integrated circuit wafers and to an in-situ multi-step process for forming conformal, planar dielectric layers that are suitable for use as interlevel dielectrics for multi-layer metallization interconnects.

I. Reactor

The early gas chemistry deposition reactors that were applied to semiconductor integrated circuit fabrication used relatively high temperature, thermally-activated chemistry to deposit from a gas onto a heated substrate. Such chemical vapor deposition of a solid onto a surface involves a heterogeneous surface reaction of gaseous species that adsorb onto the surface. The rate of film growth and the film quality depend on the wafer surface temperature and on the gaseous species available.

More recently, low temperature plasma-enhanced deposition and etching techniques have been developed for forming diverse materials, including metals such as aluminum and tungsten, dielectric films such as silicon nitride and silicon dioxide, and semiconductor films such as silicon.

The plasma used in the available plasma-enhanced chemical vapor deposition processes is a low pressure reactant gas discharge which is developed in an RF field The plasma is, by definition, an electrically neutral ionized gas in which there are equal number densities of electrons and ions. At the relatively low pressures used in PECVD, the discharge is in the "glow" region and the electron energies can be quite high relative to heavy particle energies The very high electron temperatures increase the density of disassociated species within the plasma which are available for deposition on nearby surfaces (such as substrates). The enhanced supply of reactive free radicals in the PECVD processes makes possible the deposition of dense, good quality films at lower temperatures and at faster deposition rates (300-400 Angstroms per minute) than are typically possible using purely thermally-activated CVD processes (100-200 Angstroms per minute) However, the deposition rates available using conventional plasma-enhanced processes are still relatively low.

Presently, batch-type reactors are used in most commercial PECVD applications. The batch reactors process a relatively large number of wafers at once and, thus, provide relatively high throughput despite the low deposition rates. However, single-wafer reactors have certain advantages, such as the lack of within-batch uniformity problems, which make such reactors attractive, particularly for large, expensive wafers such as 5-8 inch diameter wafers. In addition, and quite obviously, increasing the deposition rate and throughput of such single wafer reactors would further increase their range of useful applications.

II. Thermal CVD of SiO.sub.2 ; Planarization Process

Recently, integrated circuit (IC) technology has advanced from large scale integration (LSI) to very large scale integration (VLSI) and is projected to grow to ultra-large integration (ULSI) over the next several years. This advancement in monolithic circuit integration has been made possible by improvements in the manufacturing equipment as well as in the materials and methods used in processing semiconductor wafers into IC chips However, the incorporation into IC chips of, first, increasingly complex devices and circuits and, second, greater device densities and smaller minimum feature sizes and smaller separations, imposes increasingly stringent requirements on the basic integrated circuit fabrication steps of masking, film formation, doping and etching.

As an example of the increasing complexity, it is projected hat, shortly, typical MOS (metal oxide semiconductor) memory circuits will contain two levels of metal interconnect layers, while MOS logic circuits may well use two to three metal interconnect layers and bipolar digital circuits may require three to four such layers. The increasing complexity, thickness/depth and small size of such multiple interconnect levels make it increasingly difficult to fabricate the required conformal, planar interlevel dielectric layers materials such as silicon dioxide that support and electrically isolate such metal interconnect layers

The difficulty in forming planarized conformal coatings on small stepped surface topographies is illustrated in FIG. 16. There, a first film such as a conductor layer 171 has been formed over the existing stepped topography of a partially completed integrated circuit (not shown) and is undergoing the deposition of an interlayer dielectric layer 172 such as silicon dioxide. This is done preparatory to the formation of a second level conductor layer (not shown). Typically, where the mean-free path of the depositing active species is long compared to the step dimensions and where there is no rapid surface migration, the deposition rates at the bottom 173, the sides 174 and the top 175 of the stepped topography are proportional to the associated arrival angles. The bottom and side arrival angles are a function of and are limited by the depth and small width of the trench. Thus, for very narrow and/or deep geometries the thickness of the bottom layer 173 tends to be deposited to a lesser thickness than is the side layer 174 which, in turn, is less than the thickness of top layer 175.

Increasing the pressure used in the deposition process typically will increase the collision rate of the active species and decrease the mean-free path. This would increase the arrival angles and, thus, increase the deposition rate at the sidewalls 714 and bottom 173 of the trench or step. However, and referring to FIG. 17A, this also increases the arrival angle and associated deposition rate at stepped corners 176. For steps separated by a wide trench, the resulting inwardly sloping film configuration forms cusps 177-177 at the sidewall-bottom interface. It is difficult to form conformal metal and/or dielectric layers over such topographies. As a consequence, it is necessary to separately planarize the topography.

In addition, and referring to FIG. 17B, where the steps are separated by a narrow trench, for example, in dense 256 kilobit VLSI structures, the increased deposition rate at the corner 176 encloses a void 178. Such voids are exposed by subsequent planarization procedures and may allow the second level conductor to penetrate and run along the void and short the conductors and devices along the void.

SUMMARY OF THE INVENTION

Objects

In view of the above discussion, it is one object to provide a semiconductor processing reactor which provides uniform deposition over a wide range of pressures, including very high pressures.

It is another related object to provide a versatile single wafer semiconductor processing reactor which can be used for a multiplicity of processes including thermal chemical vapor deposition, plasma-enhanced chemical vapor deposition, plasma-assisted etchback, plasma self-cleaning and sputter topography modification, either alone or in-situ in a multiple process sequence.

It is a related object to provide such a reactor which accomplishes the above objectives and also is adapted for using unstable gases such as TEOS and ozone.

It is another object of the present invention to provide a process for forming highly conformal silicon dioxide layers, even over small dimension stepped topographies in VLSI and ULSI devices, using ozone and TEOS gas chemistry and thermal CVD.

It is also an object of the present invention to provide a planarization process which provides excellent conformal coverage and eliminates cusps and voids.

It is still another object of the present invention to provide a planarization process which can be performed in-situ using a multiple number of steps, in the same plasma reactor chamber, by simply changing the associated reactant gas chemistry and operation conditions.

It is yet another object of the present invention to provide an in-situ multiple step process including plasma deposition and isotropic etching of a wafer for the purpose of optimizing coating conformality and planarization, along with process throughput and wafer characteristics such as low particulates.

Another object is to provide the above-described versatile process characteristics along with the ability to vary the process sequence and the number of steps, including but not limited to the addition of reactor self-cleaning.

SUMMARY

In one specific aspect, our invention relates to a semiconductor processing reactor defining a chamber for mounting a wafer therein and an inlet gas manifold for supplying reactant gases to the wafer. The chamber also incorporates a uniform radial pumping system which includes vacuum exhaust pump means; a gas distributor plate mounted peripherally about the wafer mounting position within the chamber and including a circular array of exhaust holes therein; and a circular channel beneath and communicating with the hole array and having at least a single point connection to the vacuum exhaust pump for flowing gases radially from the inlet manifold across the wafer and through the exhaust port. The channel is of sufficiently large volume and conductance relative to the holes to enable controlled uniform radial gas flow across the wafer to the exhaust holes, thereby promoting uniform flow and processing (etching and deposition) over a wide range of pressures, including very high pressures up to about one atmosphere.

In another aspect, the present invention is directed to a semiconductor processing reactor which comprises a housing forming a chamber for mounting a wafer horizontally, a vacuum exhaust pumping system communicating with the chamber, and an inlet gas manifold oriented horizontally over the wafer mounting position The manifold has a central array of process gas apertures configured for dispensing reactant gas uniformly over the wafer and a second peripheral array of purging gas apertures configured for directing purging gas downward to the periphery of the wafer. The hole arrays are also arranged to eliminate radial alignment of holes.

In another aspect, the reactor incorporates a system for circulating fluid of controlled temperature within the manifold for maintaining the internal surfaces within a selected temperature range to prevent condensation and reactions within the manifold and for maintaining the external manifold surfaces above a selected temperature range for eliminating unwanted deposition thereon.

In still another aspect, the reactor of the present invention comprises a thin susceptor for supporting a wafer, susceptor support means for mounting the susceptor in a horizontal position precisely parallel to the gas inlet manifold and means for selectively moving the wafer support means vertically to position the susceptor and support parallel to the gas manifold at selected variable-distance positions closely adjacent the gas manifold In particular, the variable parallel close spacing can be 0.5 centimeter and smaller.

In still another aspect, the semiconductor processing reactor of the present invention comprises a housing defining a chamber therein adapted for the gas chemistry processing of a wafer positioned within the chamber. A transparent window forms the bottom of the chamber. A thin high emissivity susceptor is used for supporting a wafer within the chamber. A radiant heating module comprising a circular array of lamps mounted in a reflector module is mounted outside the housing for directing a substantially collimated beam of near-infrared radiant energy through the window onto the susceptor with an incident power density substantially higher at the edge of the susceptor than at the center thereof, to heat the wafer uniformly.

Preferably, a second, purge gas manifold is positioned beneath the wafer processing area for providing purging gas flow across the window and upward and across the bottom of the wafer. The combination of the high pressure, the purge flow from the inlet gas manifold and that from the purge gas manifold substantially eliminates deposition on chamber surfaces.

In still another aspect, the reactor of the present invention comprises a deposition gas feed-through device connected to the gas inlet manifold which comprises tube means adapted for providing co-axial flow of deposition gas on the inside of the tube and purge gas on the outside thereof into the gas inlet manifold. The tube is adapted for connection to ground at the inlet end and to an RF power supply at the outlet or manifold end to provide RF power to the manifold, and has a controlled electrical impedance along its length from the inlet to the outlet end for establishing a constant voltage gradient to prevent breakdown of the gas even at high RF frequencies and voltages.

These and other features discussed below permit reactor operation over a wide pressure regime, that is, over a wide of pressures including high pressures up to approximately one atmosphere. The features also provide uniform susceptor and wafer temperatures, including both absolute temperature uniformity and spatial uniformity across the susceptor/wafer; uniform gas flow distribution across the wafer; and effective purging. The variable parallel close spacing between the electrodes adapts the reactor to various processes. These features and the temperature control of the internal and external gas manifold temperatures enable the advantageous use of very sensitive unstable gases such as ozone and TEOS in processes such as the following.

That is, the present invention also relates to a method for depositing a conformal layer of silicon dioxide onto a substrate by exposing the substrate to a reactive species formed from ozone, oxygen, tetraethylorthosilicate, and a carrier gas within a vacuum chamber, using a total gas pressure within the chamber 10 torr to 200 torr and a substrate temperature within the range of about 200.degree. C. to 500.degree. C. Preferably, a substrate temperature of about 375.degree. C. .+-.20.degree. C. is used to obtain maximum deposition rates and the chamber pressure is about 40 torr to 120 torr. In still another aspect, the present invention is embodied in a method for depositing silicon dioxide onto a film or substrate by exposing the substrate to the plasma formed from tetraethylorthosilicate, oxygen and a carrier gas in a chamber using a total gas pressure within the range of about 1 to 50 torr, and a substrate temperature in the range of about 200.degree. C. to 500.degree. C. Preferably, the chamber pressure is 8-12 torr and the substrate temperature is about 375.degree. C..+-.20.degree. C.

In still another aspect, the invention is directed to a method for isotropically etching a silicon dioxide surface comprising the step of exposing a silicon dioxide surface to a plasma formed from fluorinate gas such as NF.sub.3, CF.sub.4 and C.sub.2 F.sub.6 in a carrier gas in a chamber using a wafer temperature in the range of from about 200.degree. C. to 500.degree. C. Preferably, the chamber pressure is within the range of about 200 mT to 20 torr, and 500 mT to 10 torr.

The invention is also embodied in a method for planarizing a non-planar dielectric coating or composite within a vacuum chamber by depositing a conformal layer of silicon dioxide onto the coating by exposing the coating to a reactive species formed from ozone, oxygen, tetraethylorthosilicate and a carrier gas, the total chamber gas pressure being within the approximate range 10 torr to 200 torr and the substrate temperature being within the approximate range 200.degree. C. to 500.degree. C., to thereby form a composite of the conformal layer on the substrate; and isotropically etching the outer surface of the resulting composite layer. Preferably, this planarizing process uses the plasma oxide deposition to first form a layer of silicon oxide and also uses the isotropic etch described above

BRIEF DESCRIPTION OF THE DRAWINGS

The above and other aspects and advantages of the present invention are described in conjunction with the following drawing figures, in which:

FIG. 1 is a top plan view of a preferred embodiment of the combined CVD/PECVD reactor of the present invention, shown with the cover pivoted open;

FIG. 2 is a vertical cross-section, partly in schematic, taken along line 2--2 in FIG. 1, with the reactor cover closed;

FIG. 3 is a vertical cross-section through the wafer elevator mechanism, taken along line 3-3 in FIG. 1;

FIGS. 4-8 are sequential, highly schematized representations of the operation of the wafer transport system in positioning wafers within, and removing wafers from the reactor susceptor;

FIG. 9 is a reduced scale, horizontal cross-section through the circular-array, radiant lamp heating assembly, taken along line 9--9 in FIG. 2;

FIG. 10 is an enlarged, partial depiction of FIG. 2 showing the process gas and purge gas distribution systems in greater detail;

FIG. 11 is a partial, enlarged bottom plan view of the gas distribution head or manifold;

FIG. 12 depicts an enlarged, vertical cross-section of the RF/gas feed-through system shown in FIG. 2;

FIGS. 13A-13C schematically depict various alternative embodiments of the gas feed-through;

FIG. 14 illustrates breakdown voltage as a function of pressure for low frequency and high frequency RF power without a constant voltage gradient device;

FIG. 15 illustrates breakdown voltage as a function of pressure with and without a constant voltage gradient device;

FIG. 16 is a schematic cross-sectional representation of an integrated circuit which illustrates the arrival angles associated with the deposition of a layer of material such as dielectric onto a surface of stepped topography;

FIGS. 17A and 17B are schematic cross-sections, similar to FIG. 16, which illustrate the effect of trench width on planarization;

FIGS. 18 and 19 are cross-sections of the surface topology of an integrated circuit, in the manner of FIG. 16, illustrating the conformal, planar qualities of oxide films resulting from the application of our planarization process; and

FIGS. 20 and 21 depict the deposition rate as a function of temperature and pressure, respectively, for our present oxide deposition process.

DETAILED DESCRIPTION OF THE INVENTION

I. CVD/PECVD Reactor

A. Overview of CVD/PECVD Reactor FIGS. 1 and 2 are, respectively, a top plan view of the preferred embodiment of the single wafer, reactor 10 of our present invention, shown with the cover pivoted open, and a vertical cross-section of the reactor 10.

Referring primarily to these two figures and to others indicated parenthetically, the reactor system 10 comprises a housing 12 (also termed a "chamber"), typically made of aluminum, which defines an inner vacuum chamber 13 that has a plasma processing region 14 (FIG. 6). The reactor system 10 also includes a wafer-holding susceptor 16 and a unique wafer transport system 18 (FIG. 1) that includes vertically movable wafer support fingers 20 and susceptor support fingers 22. These fingers cooperate with an external robotic blade 24 (FIG. 1) for introducing wafers 15 into the process region or chamber 14 and depositing the wafers 15 on the susceptor 16 for processing, then removing the wafers 15 from the susceptor 16 and the chamber 12. The reactor system 10 further comprises a process/purge gas manifold or "box" 26 that applies process gas and purging gas to the chamber 13, an RF power supply and matching network 28 for creating and sustaining a process gas plasma from the inlet gas and a lamp heating system 30 for heating the susceptor 16 and wafer 15 positioned on the susceptor to effect deposition onto the wafer. Preferably, high frequency RF power of 13.56 MHz is used, but low frequencies can be used.

The gas manifold 26 is part of a unique process and purge gas distribution system 32 (FIGS. 2 and 10) that is designed to flow the process gas evenly radially outwardly across the wafer 15 to promote even deposition across the wafer and to purge the spent gas and entrained products radially outwardly from the edge of the wafer 15 at both the top and bottom thereof to substantially eliminate deposition on (and within) the gas manifold or box 26 and the chamber 12.

A liquid cooling system 34 controls the temperature of the components of the chamber 12 including, in particular, the temperature of the gas manifold or box 26. The temperature of the gas box components is selected to eliminate premature deposition within the gas box/manifold 26 upstream from the process chamber 14.

The reactor system 10 includes a unique, RF/gas feed-through device 36 (FIGS. 2 and 12) that supplies process and purge gas to the RF-driven gas manifold 26 from an electrically ground supply. Applying the RF energy to the gas box or manifold 26 has the advantage of the wafer residing on the grounded counter electrode or susceptor 16, which makes possible a high degree of plasma confinement that would not be achievable if the RF energy were applied to the wafer and the gas box were grounded. Additionally, the hardware is mechanically and electrically simpler since electrical isolation between wafer/susceptor and chamber is not required (or permitted) Temperature measurement and control of the susceptor/wafer in the presence of high frequency electric and magnetic fields is greatly simplified with the susceptor 16 grounded. Also, the feed-through 36 is rigid, eliminating flexible gas connections and the purge gas flow path safely carries any leaking process gas into the chamber to the chamber exhaust. The capability to apply RF power to the gas manifold is made possible (despite the inherent tendency of high potential RF operation to form a deposition plasma within the feed-through) by the unique design of the feed-through, which drops the RF potential evenly along the length of the feed-through, thus preventing a plasma discharge within.

B. Wafer Transport System 18

As mentioned, this system is designed to transfer individual wafers 15 between the external blade, FIG. 2, and the susceptor 16 and to position the susceptor 16 and wafer 15 for processing. Referring further to FIG. 1, the wafer transport system 18 comprises a plurality of radially-extending wafer-support fingers 20 which are aligned with and spaced about the periphery of susceptor 16 and are mounted to a semi-circular mounting bar or bracket 38. Similarly, an array of radially-extending susceptor-support fingers 22 are spaced circumferentially about the susceptor 16, interdigitated with the wafer support fingers 20, and are mounted to a semi-circular bar 40 positioned just outside bar 38. The arcuate mounting bars 38 and 40 are mounted within a generally semi-circular groove 42 formed in the housing, and are actuated respectively, by vertically movable elevator assemblies 44 and 46.

As shown in FIG. 3, the susceptor elevator mechanism 44 includes a vertically movable shaft 48 that mounts the bar 38 at the upper end thereof. The shaft can be moved vertically up and down by various moving means 56, including a pneumatic cylinder, or, preferably, a stepper motor operating via suitable gear drive. Wafer elevator mechanism 46 is similar to the elevator 44.

The operation of the wafer transport system 18 is summarized by the sequence depicted schematically in FIGS. 4-8. In FIG. 4, the external blade 24 (with the wafer 15 to be processed supported thereon) is inserted via opening 56 into chamber 13 to a position over the susceptor 16. One example of a suitable blade 24 and associated robot wafer handling system (and door 25, FIG. 6) is described in co-pending, commonly assigned U.S. patent application Ser. No. 944,803 (A-44974), entitled "Multiple Chamber Integrated Process System", filed concurrently in the name of Dan Maydan, Sasson Somekh, David N. K. Wang, David Cheng, Masato Toshima, Isaac Harari, and Peter Hoppe which application is hereby incorporated by reference in its entirety. In this starting position, the wafer fingers 20-20 are positioned between the susceptor 16 and the blade 24.

Next, as shown in FIG. 5, the wafer elevator mechanism 44 raises the wafer-support fingers 20--20 above the blade 24 to pick up the wafer 15. The blade 24 is then withdrawn from the chamber 13.

As shown in FIG. 6, after retraction of the blade 24, a pneumatic cylinder closes door 25 over the blade access slot 56 to seal chamber 13. The susceptor elevator mechanism 46 is actuated to raise the susceptor-support fingers 22 and susceptor 16 so that the susceptor 16 lifts the wafer 15 from the fingers 20--20 into position for processing in the area 14 immediately adjacent the gas distribution manifold 26. The spacing, d, between the wafer 15 and manifold 26 is readily selected by adjusting the travel of the elevator 46. At the same time, the susceptor fingers 22 and elevator mounting 46 maintains the horizontal orientation of the susceptor 16 and wafer 15 and parallelism between the wafer 15 and manifold 26 independent of the spacing, d.

After processing, and referring to FIG. 7, the susceptor elevator mechanism 46 lowers the susceptor fingers 22 and the susceptor 16 to deposit the wafer 15 on the wafer support fingers 20--20. The door 25 is then opened and blade 24 is again inserted into the chamber 13. Next, as shown in FIG. 8, elevator mechanism 44 lowers the wafer-support fingers 20--20 to deposit the wafer 15 on the blade 24. After the downwardly moving fingers 20--20 clear the blade 24, the blade is retracted, leaving the fingers 20 and 22 in the position shown in FIG. 4 preparatory to another wafer insertion, processing and withdrawal cycle.

C. Near-IR Radiant Heating System 30

The radiant heating system shown in FIGS. 2 and 9 provides a reliable, efficient and inexpensive means for heating the circular susceptor 16 and wafer 15 (e.g., silicon) in a manner that provides uniform wafer temperature, accurate absolute wafer temperature and rapid thermal response at low temperatures, preferably .ltoreq.600.degree. C. In achieving these objectives, a number of requirements must be met. First, achieving uniform wafer temperature requires compensating the radiation losses at the edge of the wafer. Secondly, high efficiency at low wafer temperatures (.ltoreq.600.degree. C.) requires a high emissivity, high thermal conductivity susceptor 16 because silicon wafers have low emissivity at low temperatures in the near-infrared spectrum. In addition, near-infrared radiation is used to obtain fast heating response and for transmission through the inexpensive materials such as quartz window 70. The circular thin susceptor 16 is low thermal capacitance for fast heating and cooling response. These and the other objectives discussed below are achieved by the radiation heating system 30 shown in FIGS. 2 and 9.

The heating system 30 preferably comprises an annular array of small, inexpensive, single-ended vertically oriented lamps 58--58 which provide radiation in the near-infrared portion of the electromagnetic spectrum. 30 The lamps 58--58 are mounted within an annular circular reflector module 60, preferably of aluminum. The module base 60 is formed from a block of aluminum, and has a polished annular reflecting channel 62 machined therein. The channel 62 has an arcuate, generally semi-circular reflecting base 64. The module 60 and lamps 58--58 are cooled by an annular cooling passage 66 that is formed within the collimating annular reflector 62. Connections are provided for the inlet and outlet of cooling liquid which, typically, is chilled water from a pressurized supply. Power is supplied to the lamp sockets 63 and associated lamps 58 by an electrical supply cable 68, typically from a variable power supply which automatically varies the lamp power based upon a predetermined program setting that is adapted to the requirements of the particular deposition process

The annularly-collimated light from the vertical oriented lamps 58--58 is admitted into the chamber via a quartz window 70. Quartz is transparent to near-IR radiation The transparent quartz window 70 is mounted to the housing 13 at the bottom of the process chamber 13 using annular seals 72--72 to provide a vacuum-tight interface between the window 70 and the housing. This mounting arrangement positions the radiant energy heating source 30 outside the chamber 13 at atmospheric pressure and isolates the vacuum of the processing chamber and the particulate-sensitive processing therein from the lamps. A bracket 74 can be joined to the lamp mounting base 60 and pivotally mounted by pivot pin 76 to a mating bracket 78, which is joined to the housing 12. (Alternatively, the lamp module can be bolted in place.) As a consequence of this pivotal mounting of the lamp assembly 30 external to and isolated from the process chamber 13, the lamp assembly is readily accessible for maintenance, lamp replacement, etc., by simply disengaging a clamp 79 to allow the assembly to pivot downwardly about pin 76.

As mentioned, the lamps 58--58 are small single-ended commercially available quartz-tungsten-halogen lamps which provide the required near-infrared radiation. One suitable lamp is the Ansi type "FEL" supplied by Sylvania, G.E., Ushio or Phillips. Presently, fourteen 0.5 to 1 kilowatt quartz-tungsten-halogen lamps that provide a wavelength of about 0.9 to 1.5 micron provide an annularly-collimated power density of up to about 94 W/cm.sup.2 at the top of the lamp module. The maximum power density at the susceptor (substantially directed to the outer .about.1.5 in. radius of a 6 in. diameter susceptor) is .about.17 W/cm.sup.2 taking all efficiency into account (.about.15-16% efficiency). More generally, lamps concentrating their radiation in the range of about 0.7 to 2.5 microns wavelength would be particularly useful. The aluminum base 60 and concave-bottom, annular groove 62 provide a high collection-efficiency collimating reflector which directs a higher radiation power density at the susceptor edge than at the middle. This non-uniform, concentrated radiation heats the susceptor wafer circumferentially, which compensates the wafer edge heat losses and, thus, provides uniform wafer temperature over a wide range of chamber gas pressures and wafer temperatures.

In short, the desired uniform radiant wafer heating is provided by small, inexpensive lamps mounted in a compact simple aluminum module 60 that is easily cooled and maintained at a low temperature, and does not require plating. In addition, the use of the near-IR lamps and a thin, low mass, low thermal capacity, high emissivity susceptor of material such as graphite, provides maximum efficiency, fast thermal response, excellent temperature uniformity and transmission through the quartz window 70. Other susceptor materials include anodized aluminum, graphite coated with layers such as aluminum oxide (Al.sub.2 O.sub.3), or silicon carbide, or a composite ceramic coated with Al.sub.2 O.sub.3 or SiC or other materials. Also, interchangeable modules 60 having channels of different heights or diameters can be used to accommodate different susceptor and wafer diameters. A present version of the reactor is designed for 5-6 in. wafers. However, different lamp modules can be provided for smaller or larger diameter wafers by changing the module height and/or the radius of the module and the filament circle. Finally, the heating system 30 may employ a controller (not shown) such as a closed loop temperature control system using phase angle power control to provide rapid thermal response and rapid wafer temperature stability.

It should be noted that the simplicity, low mass and high performance characteristics of the heating system 30 are in contrast to prior wafer heating approaches which typically use a rectangular array of double-ended quartz-tungsten-halogen lamps. Conventional radiation heating practice has been to use a more massive susceptor and, if excellent temperature uniformity is required, to merely block radiation from the wafer center, thus sacrificing efficiency, rather than redirecting radiation. The advantages of the radiant heating system 30 over the conventional practices include in addition to the aforementioned uniform wafer temperature and much faster response time (both heating and cooling), smaller, less bulky more easily maintained equipment of higher reliability (long lamp lifetime); more efficient operation; and lower cost.

The use of the easily accessible, external radiant heat source 30 is facilitated and maintained by a gas purge system. As described in the succeeding section, this system directs purge gas flow across the vacuum side of the quartz window 70 to prevent deposition on the window and keep the window clean. Thus, the purge is a major contributor to lamp efficiency. This increases the number of process cycles between cleaning and, as a result, decreases the associated system downtime required for cleani