Abstract:
A multiwafer chemical vapor deposition (CVD) reactor providing improved material deposition uniformity through use of improved gas injection and exhaust apparatus. The reactor includes a wafer boat for supporting a vertical stack of wafers, spaced apart for passage of a reactant gas. A preferred embodiment of the gas injector is in the form of a vertically oriented body having at a first end a gas inlet, and extending inward from a wall of the reactor towards the wafer boat, terminating in a widened injector outlet. The injector body and outlet extend vertically a distance approximating the height of the wafer boat, and the outlet is widened to provide an improved flow of gas across the wafer. A face of the injector outlet contains a plurality of gas ejecting holes, arranged to provide a uniform supply of reactant gas over each wafer surface. The exhaust manifold is similarly configured, having a plurality of exhaust ports distributed over the height of the manifold to assist in preserving the uniform flow of reactant gas across each wafer.

Description:
This application claims the benefit of U.S. Provisional Application No. 60/071,570 filed Jan. 15, 1998 and No. 60/071,571 filed Jan. 15, 1998, and is a continuation-in-part of copending U.S. application Ser. No. 08/909,461 filed Aug. 11, 1997 and Ser. No. 09/228,840 filed Jan. 12, 1999. 
    
    
     BACKGROUND OF THE INVENTION 
     1. Field of the Invention 
     The present invention relates generally to chemical vapor deposition methods and apparatus, and more particularly to a CVD reactor having an improved reactant gas injection and exhaust system for achieving more rapid and uniform material deposition. 
     2. Brief Description of the Prior Art 
     There are a large number of CVD processes that are performed inside of enclosed chambers wherein the pressure, temperature, composition of gases and other factors are controlled to produce the desired thin film deposition of various materials onto substrates such as semiconductor wafers and flat panel displays. For convenience the term wafer(s) will be used with the understanding that the following would apply to the manufacture of flat panel displays and other types of substrates. 
     For instance, amorphous, polycrystalline and epitaxial silicon is typically deposited onto silicon wafers by injecting silane or dichlorosilane, with or without other gases, into an enclosed vessel where the temperatures, pressure, gas flow, RF plasma intensity (when used) and wafer motion (when employed) are precisely controlled. Such processes are carried out in a wide variety of commercially available hot wall and cold wall reactors. Some of these process a single wafer at a time while others process a batch of two or more wafers at a time. 
     To obtain the best thickness uniformity, the operating regime of the process chamber is often chosen to be completely dominated either by the chemical reaction at the wafer surface (surface reaction rate limited) or by mass transport of the reactant to the wafer surface (mass transport limited) to make the overall deposition process least sensitive to variables which are poorly controlled in a given reactor. However, other factors such as the need for high deposition rate, high wafer capacity, or small grain size sometimes make operation near the transition region (between surface reaction-rate limited and mass transport limited) desirable. In the case of operation in either the mass transport limited regime or the transition region for a given temperature and pressure, the diffusion rate of the reactant species through the boundary layer that exists between the wafer&#39;s surface and the bulk gas, and the relative local concentration of the desired species at the surface, have major impact upon the rate of reaction at the surface and hence upon the deposition rate. 
     In the prior art, methods to increase the velocity of the gas over the wafer surface have been employed to effectively decrease the thickness of the boundary layer and increase the relative concentration of the desired species at the surface for a given temperature, pressure and relative concentration of the desired species in the bulk gas. 
     For example, a batch reactor in the form of a conventional vertical furnace  10  is shown in FIG.  1 . The furnace  10  includes a quartz envelope  12 , heating coil  14 , a wafer boat  16 , a gas inlet  18  to a gas injection tube  20 , and an exhaust  22 . The tube  20  is constructed of high temperature material such as quartz, and has holes  24  (FIG. 2) along its length. The gas(es) is injected via the tube(s)  20  and directed toward the wafer boat holding wafers  26  resulting in an increased velocity of gas(es) across the wafers and a more uniform concentration of the desired reactant(s) in the bulk gas flow up and down the boat load. Although deposition rates can thereby be improved, this technique has its problems and limitations. Because the injection tube(s)  20  is contained within an isothermal chamber  28 , the injection tube(s)  20  is at the same temperature as the wafers  26 . Thus, unwanted deposition occurs on the tube(s)  20 , especially at the injection holes  24 . As the gas flow rate (velocity) is increased to achieve higher deposition rates, the localized velocity and pressure at the holes  24  can increase to the point where both excessive deposition at the holes  24  and excessive gas phase reaction within the chamber  28  occurs. The excessive gas phase reaction causes particles to be generated which can fall onto the wafers&#39; surfaces causing defects. Also, the excessive deposition on the injection tube  20  flakes off and these particles can also fall onto the wafers. Thus, the maximum deposition rate which yields acceptable results on the wafers is limited. 
     A prior art technique of rotating a wafer  30  at high speed (500 to 1500 RPM) is illustrated in a single wafer cold wall CVD reactor  32  in FIG. 3. A gas injector  34 , called a showerhead directs reactant gas  36  perpendicularly toward the spinning wafer surface, thereby thinning the boundary layer for the gas flowing radially outwardly from a stagnation point at the wafer center. Again the deposition rate does increase, but this technique also has its problems and limitations. First is the problem of holding the wafer on the susceptor while rotating at such high speeds and the complexity of design for achieving such high rates of rotation in an evacuated chamber. Second is the problem of heating the wafer uniformly while allowing for the injection of the gas perpendicular to the rotating wafer&#39;s surface which limits the maximum temperature. In addition, there is the problem of minimizing the gas turbulence to achieve the laminar type gas flow toward the wafer as required by this technique to achieve the desired uniformity. This can limit the maximum flow rate and hence the deposition rate. 
     In view of the above discussion, it is apparent that there is a need for an improved method and apparatus for achieving a uniform deposition rate in the process of chemical vapor deposition. 
     SUMMARY OF THE INVENTION 
     It is therefore an object of the present invention to provide an improved apparatus for chemical vapor deposition. 
     It is a further object of the present invention to provide an improved apparatus for applying reactant gas to a multiwafer stack. 
     It is a further object of the present invention to provide improved apparatus for control of the flow rate of injected and exhausted gases. 
     It is a still further object of the present invention to provide a heated exhaust apparatus for preventing material condensation. 
     It is another object of the present invention to provide removable injection and exhaust apparatus for replacement or for cleaning of material deposits. 
     Briefly, a preferred embodiment of the present invention includes a multiwafer chemical vapor deposition (CVD) reactor providing improved material deposition uniformity through use of improved gas injection and exhaust apparatus. The reactor includes a wafer boat for supporting a vertical stack of wafers, spaced apart for passage of a reactant gas. A preferred embodiment of the gas injector is in the form of a vertically oriented body having at a first end a gas inlet, and extending inward from a wall of the reactor towards the wafer boat, terminating in a widened injector outlet. The injector body and outlet extend vertically a distance approximating the height of the wafer boat, and the outlet is widened to provide an improved flow of gas across the wafer. A face of the injector outlet contains a plurality of gas ejecting holes, arranged to provide a uniform supply of reactant gas over each wafer surface. The exhaust manifold is similarly configured, having a plurality of exhaust ports distributed over the height of the manifold to assist in preserving the uniform flow of reactant gas across each wafer. 
    
    
     IN THE DRAWING 
     FIG. 1 shows a gas injection system in a prior art vertical furnace; 
     FIG. 2 is a detail view of FIG. 1; 
     FIG. 3 illustrates a single wafer CVD reactor with a showerhead injector and rotating susceptor; 
     FIG. 4 shows a reactor with a dual chamber and a boat providing vertical stacking of wafers, as described in U.S. patent application Ser. No. 08/909,461; 
     FIG. 5 is a cross-sectional view of the wafer chamber of the reactor of FIG. 4; 
     FIG. 6 shows a vertically oriented gas injector and exhaust in position to provide reactant gas to a vertical stack, and use of individual metering valves for tuning gas flow; 
     FIG. 7 is a cross-sectional view of the upper chamber of the reactor of FIG. 4 illustrating an elongated gas injector; 
     FIG. 8 shows detail of an elongated vertical injector; 
     FIG. 9 shows further detail of water coolant channels in a vertical, elongated injector; 
     FIG. 10A is a cross-sectional view of a gas injector having an output port in the shape of a vertical slot as described in U.S. patent application Ser. No. 08/909,461; 
     FIG. 10B is a front view of the gas injector of FIG. 10A; 
     FIG. 11A is a cross-sectional view of an injector with an output port in the shape of a vertical slot with a shutter plate; 
     FIG. 11B is a front view of the gas injector of FIG. 11A; 
     FIG. 12A is a cross-sectional view of a gas injector with output ports in the from of a plurality of holes through a plate; 
     FIG. 12B is a front view of an embodiment of the gas injection plate of FIG. 12A; 
     FIG. 12C is a front view of another embodiment of a gas injection plate of FIG. 12A; 
     FIG. 13 is a view of still another embodiment of the gas injection system of FIG. 6; 
     FIG. 14A is a cross-sectional view of an alternate embodiment of a gas injector; 
     FIG. 14B shows a gas outlet plate used on the injector of FIG. 14A; 
     FIG. 14C shows a view of the face of the body of the injector of FIG. 14A; and 
     FIG. 15 shows an elongated injector with a widened gas outlet, mounted on a reactor. 
    
    
     DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT 
     The present invention relates to apparatus providing improved distribution of reactant gas over wafers in a multiple wafer stack, resulting in more uniform chemical vapor deposition. FIG. 4 shows a CVD reactor  38  as described in detail in U.S. patent Ser. No. 08/909,461, the content of which is incorporated herein by reference. The reactor  38  has a boat  40  for holding a plurality of wafers during processing that takes place in an upper chamber  42 . For loading and unloading, the reactor includes apparatus  44  for lowering the boat  40  into a lower chamber  46 . 
     The novel features to be described in the following detailed description also apply equally as well with the reactor described in U.S. patent application Ser. No. 09/228,840 which is similar to the reactor of FIG. 4 except for the incorporation of RF plates in the wafer boat, apparatus for supplying RF power to the plates, and a novel apparatus for lifting the wafers from the susceptors. The details of the reactor walls and chamber described in Ser. No. 09/228,840 are the same as shown in FIG. 4 to the extent that applies for incorporation of the novel injector and exhaust system disclosed in the present application. The disclosure of U.S. patent application Ser. No. 09/228,840 is therefore incorporated herein by reference, and is to be included in combination with the novel injector and exhaust system disclosed herein as a novel and useful invention. 
     FIG. 5 is a cross-sectional view of the reactor  38  upper chamber, showing a gas injector  48 , and a gas exhaust  50 . 
     FIG. 6 shows a cross-sectional view of a gas injector  52  and a gas exhaust  54 , arranged to illustrate their orientation and proximity to boat  40  holding a plurality of wafers  56 . 
     The gas injector of FIG. 6 is explained in U.S. patent Ser. No. 08/909,461 included herein by reference. Process gases to be used in depositing layers on wafers  56  are provided via ducts  58  to a mixing chamber  60 . The gas then continues at a rate determined in part by gas flow control devices  62  through a water-cooled injection plate  64  and out ports  66  into chamber  42  and towards wafers  56 . 
     The exhaust manifold  54  includes an exhaust plate  67  having a plurality of exhaust ports  68 , an exhaust plenum  70 , a control throttle valve  72 , and gate valve  74 . Process gases are removed from the reaction chamber  42  through the plurality of ports  68  and are provided to exhaust plenum  70  via a plurality of associated exhaust flow control devices  76  which, in some embodiments, are similar to flow rate control devices  62 . Process gases then flow through control throttle valve  72  and gate valve  74  to an external vacuum pump system (not shown). Exhaust plate  67  may be either cooled or heated via recirculating liquid or other means, depending upon the particular process employed. Note that for certain CVD processes it is desirable to heat the exhaust manifold  54  (and thus exhaust ports  68 ) in order to minimize condensation thereon. Flow rate control devices  62  and exhaust flow control devices  76  may be independently adjusted to allow for an optimum process gas flow pattern within the reaction chamber  42 . 
     FIG. 7 illustrates a gas injector  78  having a body  80  extending into the chamber  42  so as to place the gas outlet face  82  in close proximity to the wafer boat  40  (FIG. 4) and wafers. As with the injector described in FIG. 6, injector  78  also extends vertically to provide gas flow for all of the wafers on the wafer boat. A preferred embodiment of the injector  78  is shown in a cross-sectional view A—A (refer to FIG. 7) in FIG.  8 A. Two gas fittings  84 ,  86  are shown, providing input for reactant gas to gas channels  88 ,  90 . A water channel  92  is shown between the channels  88 ,  90  for passage of water to cool the injector  78 . FIG. 8B is an end view of the injector, showing the face  82 . A plurality of gas outlet holes  94  are provided from each of the channels  88  and  90 . FIG. 8B also clearly shows mounting holes  95  and an O-ring groove  96  for sealing the injector to a wall of the reactor. 
     FIG. 9 is a cross-sectional view B—B (refer to FIG. 8B) of the injector  78  showing the path of the water passage holes  92 . The water is supplied through a coolant fitting  97 . Intersections of alternate holes  92  at the surface  99  are sealed with a plate  98 . 
     An alternate embodiment of an injector similar to injector  52  of FIG. 6 is an injector  100  shown in FIGS. 10A and 10B. Injector  100  has gas inlets  102 , providing passage to a chamber  104 . The chamber  104  is attached to a flange  106  having a single elongated slot  108  providing outlet for the gas into the reactor chamber  42 . The slot  108  preferably extends in length over the entire height of the wafer boat. FIG. 10B is an end view of the injector  100 , and more clearly shows the slot  108 , as well as flange mounting holes  110  and an O-ring groove  112 . 
     FIGS. 11A and 11B illustrate a further embodiment of an injector  114 , similar to the injector of FIGS. 10A and 10B. A shutter  116  is used to adjust the effective opening of slot  108  to control the rate of flow of reactant gases. In another embodiment, FIG. 12A shows the shutter plate  116  of FIGS. 11A-B replaced with either of plates  118  or  120  of FIGS. 12B and 12C respectively. Each of plates  118 ,  120  has a plurality of holes  122 , arranged to distribute the gases as required. The plates  118 ,  120  are given by example. Other arrangements of holes  122  are also included in the spirit of the present invention. The plates  118 ,  120  can also be liquid cooled, the details of which will be apparent to those skilled in the art, such as by running water channels similar to channels  92  of FIG. 9 between holes  122 . 
     Referring again to FIG. 6, it is apparent that the exhaust manifold requirements are similar to the injector. The similarity applies also to FIGS. 10-12, whereby the structures shown can also be applied to an exhaust manifold i.e. a plate similar to plate  116  of FIGS. 11 and 12 can be applied to the exhaust manifold. 
     FIG. 13 shows another embodiment  123  of an injector or exhaust manifold. The embodiment  123  replaces plate  106  of FIGS. 10-12, and the chamber  104  and inlets  102 . Injector  123  is attached to the reactor in a similar manner to plate  106  of FIG. 10, with bolts  126 , and sealed with an O-ring  128 . An injector plate  124  may include one or more vertical gas supply shafts  125  into which are coupled a plurality of horizontal gas ducts  129 . Sintered metal disks  130  may be press fitted into counterbores at an end of ducts  129  to produce a more laminar gas flow and to reduce the entry of undesirable particles into reaction chamber  42 . Each of ducts  129  has provided therein a gas flow adjustment screw  132  which, by varying the cross-sectional area of ducts  129  through which process gas flows, controls the flow of reactant gas to reaction chamber  42 . Screws  132  are sealed to associated ducts  129  via O-rings (not shown). Of course, a similar duct structure may be employed to control the removal of process gases from reaction chamber  42  via an exhaust manifold. 
     In another injector embodiment  134  shown in FIGS. 14A-C, the process gases separately enter the reaction chamber  42  and are mixed therein. An injection plate  136  has formed therein on the side facing the interior of chamber  42  a plurality (two shown) of slots  138  and  140  shown in the cross-section view A—A of FIG.  14 A. An O-ring groove  139  is shown in FIG. 14A, but omitted in FIG. 14C for clarity of illustration of other features. A thinner plate  142  (FIG. 14B) having a plurality of holes  144  which line up over the slots  138  and  140  is bolted to injection plate  136 . The size, number and spacing of the holes in plate  142  may be varied throughout its length in order to produce the desired gas flow pattern to achieve uniform and consistent depositions onto all of the wafers  56  in wafer boat  40 . The gases enter the channels  138  and  140  via holes drilled from the exterior side into which are gas fittings  146 . Hole  148  is provided and tapped on both ends to accept fittings to allow liquid to flow through injection plate  136  for cooling. During processing of one or more wafers  56 , inert gas is injected into lower chamber portion  46  (FIG. 4) via a gas inlet  150  (FIG. 4) to retard process gases escaping process chamber  42  and entering lower chamber portion  46  (FIG.  4 ). Electric motor  152  is activated and rotates shaft  154  and wafers  56  at a desired rate such as, for instance, between approximately 3 and 30 rpms. Power provided to the independent zones of heaters including  156  and  158  and others as described in U.S. patent application Ser. No. 08/909,461 is adjusted to bring the temperature of reaction chamber  42  to a desired processing temperature, as described above. Once the temperature of wafers  56  has stabilized in a uniform manner at the desired process temperature, reactant gases are injected into reaction chamber process portion  42  of reactor  38  via gas injector  48  (FIG. 5) and are exhausted therefrom via exhaust  50 , as discussed above. 
     A still further embodiment of the injector of the present invention is shown in FIG.  15 . The injector  160  is elongated in the vertical direction similar to the injector described above. In addition, injector  160  has a widened outlet  162  to more uniformly supply reactant gas over the wafer surfaces. The widened outlet can be bolted onto the injector body  164  from the inside of the chamber, or the widened outlet  162  and the elongated body  164  can be fashioned from a single piece of material and O-ring sealed to the injector&#39;s mounting plate  166 . Additionally, liquid cooling inlet and outlet pipes  168  can protrude through holes in the mounting plate for more efficient cooling of the widened face. If necessary, the two side heater lamps  156  that face toward the widened injector can be removed or disconnected to reduce heat transfer to the injector  160 . 
     The features and advantages of the present invention will now be presented in further detail. The apparatus described above, results in improved uniformity of material deposition, an advantage not only in deposition processes such as CVD and PECVD, but also in etching processes and other processes where gases must efficiently be brought to the wafer surface and/or efficiently removed from a surface, such as annealing and degassing processes and other heat treating processes. For convenience, the following will refer to CVD and/or PECVD processes with the understanding that the features of the present invention would apply to reactive ion etching, photo-resist ashing and other processes as well. In addition to the enhanced CVD and PECVD deposition rates, other advantages of the present invention include smoother surface texture of deposited films, enhanced conformity of the films over the device structures at lower pressures and at the higher deposition rates, enhanced film purity via reduced concentration of unwanted impurities, and reduction of contaminating particles generated that end up on the wafer surface. 
     The greatly accelerated deposition rates realized with the present invention are a result of a number of factors influenced by the ability to inject the reactant gas(es) at very high velocities without the above mentioned deleterious side effects found in the prior art. First, the high velocity gas stream passing across the wafer has the effect of thinning the boundary layer, resulting in faster delivery of the desired reactant(s) to the surface. Second, the very high gas flow provides an enhanced source of fresh gas with highest concentration(s) of the desired species of reactant to the wafer&#39;s surface. Third, this high velocity flow of the gas(es) results in a very low residence time of the gas in the area of interest (that is, over the wafer surface) which sweeps out unwanted reaction by-products, resulting in a further increase in the relative concentration of the desired species. All these factors contribute to enhanced deposition rates. As a result, deposition rates on the order of 10 to 50 times faster than the prior art are realized. 
     The very high rates of deposition enabled by the present invention at relatively low overall chamber pressures (e.g. 3,000 Angstroms/minute for polysilicon at 250 millitorr at typical process temperatures) moves the reaction into the regime where the deposition rate exceeds the crystallization rate. CVD depositions of, for example, polysilicon, in this regime can result in a much smoother surface, caused by the deposited film having a two layered structure with amorphous silicon at the top. It is well known in the art that for the CVD deposition of silicon at a given pressure, there is a transition temperature above which a polycrystalline structure develops in each layer as that layer is deposited, and the atoms are unlikely to continue rearranging after they have been covered by other silicon atoms. However, in films deposited slightly below the transition temperature, each layer of the film can be deposited in an amorphous form and crystallize during continued deposition because of the lower energy of the polycrystalline structure. Nucleation of crystallites is most likely to occur by heterogeneous nucleation at the lower silicon-silicon dioxide interface. Crystallization of the amorphous silicon then continues on these initial nuclei, with the crystalline region propagating upward into the film by solid-phase epitaxial growth. When the crystallization rate is less than the deposition rate, only the lower portion of the film crystallizes during deposition, although the crystallization continues during the heat cycle after the deposition itself is terminated by stopping the silane flow. Thus, the film can be crystalline near the bottom and amorphous near the top, resulting in a very smooth surface texture. 
     Since very high deposition rates can be realized at very low pressures, it has the effect of enhancing the deposited films&#39; conformality over a wafer&#39;s topography. This is a result of the ability to provide a higher concentration of the desired reactant(s) on all surfaces of the wafer including sidewalls and bottoms of vias. The accelerated deposition rate achievable via this invention at reduced pressures results in an effective increase of the mean free path in the gas phase, which allows more penetration of the reactant to the bottom and along the walls of device features. The very low gas residence times achieved via this invention and the resultant sweeping of unwanted reaction by products (e.g. hydrogen) out of the gas phase has the effect of increasing the diffusion of the desired silicon producing species in both the gas phase and on the surface which enhances the deposited films while, at the same time, providing more absorption sites available for the desired silicon producing species such as SiH 4  and SiH 2  since less of the absorption sites are occupied by the unwanted by-products, thereby increasing the rate of deposition on all surfaces. SEM photomicrographs of polysilicon depositions (2,000 angstroms per minute a 250 milli-torr and 650 C.) in the single wafer chamber of this invention into 0.25 micron vias exhibit very uniform thickness conforming to the vias&#39; walls and bottom without cusping at the top edges of the vias. 
     In addition, the CVD films produced with the present invention are of higher quality in terms of a reduced incorporation of unwanted impurities within the film. All CVD reactors have some level of impurity molecules, such as water vapor, oxygen, nitrogen, etc., within the chamber. This is particularly true of cold wall reactors for impurities such as H 2 O (moisture) and others which tend to adhere to the cooled chamber walls and are released from the walls when the chamber is evacuated and when the interior surface of the walls are warmed from the heat of the wafer, the susceptor, and other heated surfaces within the chamber&#39;s interior. Although the levels of such unwanted molecules can be reduced through heating of the chamber&#39;s walls to elevated temperatures (above 100 C.) while evacuating the chamber with turbo or cryo pumps to very low pressures on the order of 10E-6 to 10E-7 Torr while alternating such evacuation cycles with high flow purge cycles of impurity free inert gas such as nitrogen, these procedures are costly, time consuming, and there still remains some level of such unwanted impurities. The amount of incorporation of unwanted impurities in CVD films is proportional to the partial pressure of such impurity molecules, the rate of reaction or entrapment of the impurities as the desired film is deposited, and the deposition time. The reduction of impurities in the films produced with the present invention is due to (a) the reduced partial pressure of the impurities in the gas stream above the wafer&#39;s surface resulting from the increased concentration of the desired reactant species in the gas stream, (b) the enhanced rate of removal of the unwanted impurities due to the very high gas velocities and resultant low residence time, and (c) the greatly reduced process time resulting from the high deposition rates that are achieved. 
     In addition to supplying an enhanced concentration of the desired reactant(s) to the surface and the accelerated sweeping away of unwanted reaction by-products and impurity molecules, this very high velocity gas flowing generally in parallel to the surface is believed to be, in part, responsible for the low quantity of particles on the wafers processed in this fashion. 
     The multilayer reactor of FIG. 4 provides the ability to process one or more wafers at a time and a method of heating the wafers uniformly in a cold wall chamber to minimize wall deposits for ease of cleaning (e.g. via plasma enhanced reaction of NF 3 , other such etchant gases, or via the injection of etchant gases such as HCl at high temperatures without plasma). The elongated injectors described above provide the advantage of positioning of a temperature controlled gas injector at relatively close proximity to the subject wafers within the chamber to produce the desired and controlled localized high velocity gas flow. The reactor also has the ability to rotate the wafers while the gas is being swept into the chamber on one side and exhausted out the other side, which causes a near mono-directional flow which, without rotation, would result in a very non-uniform deposition across the surface topography of the wafers. The reactor disclosed herein also has the ability to induce a very uniform plasma (glow discharge) in close proximity to the wafers&#39; surfaces for PECVD processing. See the U.S. patent application Ser. No. 09/228,840 titled “Vertical Plasma Enhanced Process Apparatus and Method”, the disclosure of which is incorporated herein by reference. The reactor has the capability to deposit CVD films on one side of a wafer and not the other, and the ability to exclude edge deposition around the periphery of the wafer, which is desired for certain films such as tungsten, and the ability to load and unload wafers via robotics permitting automatic operation and the capability for clustering one or more such chambers around a central transfer chamber or enhanced process control, higher throughputs, the minimization of particles and the capability for sequential processing. 
     Referring again to FIG. 5, the gas(es) is injected toward the wafers via a temperature controlled injection plate which bolts onto and is vacuum sealed to one of the shorter width sides of the eight sided chamber. The injection plate may be elongated within the chamber in the direction toward the wafers as shown in FIGS. 7 and 15. 
     FIG. 8 shows an injector design  78  which allows for the elongation of the injector toward the wafers such that the outlet face  82  of the injector  78  can be held in close proximity to the wafers while at the same time permitting the flow of liquid through passages  92  in the injector  78  to maintain the injector at a uniform and constant temperature. Usually, for gaseous sources such as silane, it is desired to maintain the injector  78  at a low temperature (typically 25 to 100 C.) while the wafers are maintained at a temperature in excess of 600 C. for the deposition of polysilicon. This reduced injector temperature prevents the deposition along the outlet face  82  and at the outlets  94  of the injector. For CVD depositions using a vaporized liquid precursor (such as TEOS), the temperature of the injector can be maintained at higher temperatures (e.g. 100 C. or above) to prevent the condensation of the vapor in and on the injector  78  while still preventing the deposition on the injector  78  or at its outlets  94 . FIG. 8 shows such an injector which allows for the separation of gases to preclude premature reaction of, for example, oxidizers and reducers before they enter the reaction chamber  42  (FIG.  4 ). In this case, gas channels  88 ,  90  are milled from the atmospheric side of the injector toward the outlet face  82 . A series of holes  94  are drilled from the outlet face  82  through to the milled channels  88 ,  90  (in this depiction, the hole spacing is shown to differ for the two channels which may be desired for some processes). Plates  170  are welded to the input side of the injector  78  for gas tight sealing of the channels  88 ,  90  and are tapped to accept gas fittings  84 ,  86 . To provide the flow of temperature controlled liquid through the injector, holes  92  are drilled at angles such that they intersect to form a continuous passage as more clearly shown in FIG.  9 . Bosses  172  are welded at the ends of the uppermost and bottom most holes and tapped to accept fluid fittings  97 . Cover plates  98  are welded over the outside intersecting ends of the holes  92  to produce the leak tight passage way. 
     The alternative high velocity gas injector designs described in the various figures are adaptable to the reactor of FIG.  4  and described in U.S. patent application Ser. No. 08/909,461, and can be such that the quantity of gas(es) flowing out of the injector&#39;s face can be varied along the vertical axis (up and down the load of wafers  56 ) to overcome any non-symmetrical gas flow dynamics in the vicinity of the upper and lower regions of the batch of wafers to achieve desired velocities and concentration of reactant(s) above the surfaces of the individual wafers in the load for uniform process results on the individual wafers. To achieve this, the alternate designs can include (a) a variation of the outlet hole size along the vertical axis of the injector&#39;s outlet face, for example, holes  94  in FIG.  8  and holes  122  in FIG. 12; (b) a variation of the spacing of the outlet holes drilled into the axis of the outlet face; (c) the use of a multitude of individual holes drilled into the injector from the outside to provide the variation of gas flow along the vertical axis via the use of individual metering valves  62  or mass flow controllers as shown in FIG. 6; or (d) a variation of the type of tunable injector of U.S. Pat. No. 5,551,985 where the flow from each outlet can be adjusted and/or the injection angle from each outlet can be adjusted along the vertical axis. The use of the tunable injectors described in U.S. Pat. No. 5,551,985 in the injector of the present invention for providing reactant gas in a vertical wafer stack is a novel application. The details disclosed in U.S. Pat. No. 5,551,985 are included in the present application by reference. 
     While particular embodiments of the present invention have been shown and described, it will be obvious to those skilled in the art that changes and modifications may be made without departing from this invention in its broader aspects and, therefore, the appended claims are to encompass within their scope all such changes and modifications as fall within the true spirit and scope of this invention.