JP2010267982A - Method and rotary disk type reactor for growing uniform epitaxial layer on the surface of substrate - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a reactor and a method that provides a uniform distribution of a reaction gas over the entire processing surface of a substrate carrier and can avoid turbulent flow caused by the speeds of the reaction gas being different. <P>SOLUTION: A gas flow generator is configured, such that one or a plurality of gas flow include a carrier gas and a reaction gas, and a different part includes the reaction gas having different concentration. The gas flow generator is configured such that, when a substrate carrier is rotatably provided about an axis, the one or a plurality of gas flow containing the reaction gas having different concentration are supplied at a different radial direction distance from the axis. While the gas flowing toward the near part of the axis of the substrate carrier contains a relatively high-concentration carrier gas and a relatively low-concentration reaction gas, the gas flowing toward the distant part from the axis of the substrate carrier contains the relatively high-concentration reaction gas. As a result, the gas flow generator is provided configured so as to deliver a gas having a substantially uniform speed toward the substrate carrier inside the chamber. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

  The present invention relates to a reactor for metalorganic chemical vapor deposition. More particularly, the present invention relates to a rotating disk reactor in which one or a plurality of types of gas are injected onto the surface of a rotating substrate and an epitaxial layer is grown on the surface.

  Vertical high speed rotating disk reactors in which one or more types of gases are injected downwardly onto the surface of a rotating substrate in the reactor are often used for metal organic chemical vapor deposition (MOCVD). In particular, vertical disk CVD reactors have been found to be useful for a wide range of epitaxial compounds including various combinations of semiconductor monolayer and multilayer structures such as lasers and LEDs. In these reactors, one or more injectors spaced above the substrate carrier provide a predetermined gas flow that contacts the substrate and deposits a layer of epitaxial material on the surface of the substrate. To do.

  For large wafers, the rotating disk reactor uses several injectors spaced upward from the substrate. The injectors are typically spaced above the wafer at various locations along one or more radial axes of the wafer relative to the central axis of the substrate carrier. In many cases, the proportion of the raw material reactive material injected into the reactor varies from injector to injector so that the same molar amount of reactant can reach the surface of the substrate. Thus, some reactant injectors will have different gas velocities than other reactant injectors. More specifically, this reactant velocity variation is due to the relative placement of the injectors. Since the carrier of the reactor holding the substrate rotates at a predetermined speed, the injector near the outer edge of the carrier is a region of a larger surface area on the carrier than the injector near the center of the carrier at any point in time. Occupy. Thus, to maintain the desired uniformity, the outer injector typically uses a larger reactant gas velocity than the inner injector. For example, the gas velocities of individual injectors can differ by 3 to 4 times between adjacent injectors.

  This variation in gas velocity helps to ensure a more uniform layer thickness, but different velocities can cause turbulence during the injector flow. Also, the potential for side effects such as non-uniform layer thickness, reactant dissipation, or premature condensation of reactants may be increased.

  One aspect of the present invention is to provide a reactor. The reactor according to this aspect of the invention preferably comprises a chamber and a substrate carrier mounted for movement in the chamber, most preferably for rotation about an axis. The substrate carrier is configured to hold one or more substrates, most preferably in a position where the surface of the substrate to be processed is substantially perpendicular to the axis. The reactor according to this aspect of the invention desirably comprises a gas flow generator configured to deliver one or more gas flows at a substantially uniform rate toward the substrate carrier in the chamber. ing.

  Most preferably, the gas flow generator is configured such that the one or more gas streams includes a carrier gas and a reactive gas, and different portions of the one or more gas streams include different concentrations of the reactive gas. . When the substrate carrier is provided to be rotatable about an axis, it is desirable to generate the gas flow so as to supply the one or more gas flows containing different concentrations of reactant gas at different radial distances from the axis. The vessel is configured. The gas toward the portion close to the axis of the substrate carrier desirably includes a relatively high concentration carrier gas and a relatively low concentration of the reactive gas, and the gas toward the portion far from the axis of the substrate carrier is desirably high concentration. Of reactive gases.

  The gas flow generator includes a plurality of gas inlets in communication with chambers at different distances from the axis, one or more gas sources of reactive gases connected to the inlets, and a carrier connected to at least one of the inlets. A gas source of gas.

  Yet another aspect of the invention includes a method of processing a substrate. The method according to this aspect of the invention desirably includes supporting one or more substrates to be processed on a substrate support, such that the surface of the substrate is positioned substantially perpendicular to the axis. Rotating the support around the axis. This method allows the reactant gas and carrier gas to flow toward the substrate surface in the chamber in one or more streams having substantially uniform velocities at different radial distances from the axis. And a step of introducing into the chamber. The one or more gas flows are set so that different portions of the substrate surface at different radial distances from the axis receive substantially the same amount of the reaction gas per unit time and per unit area. Most preferably, the step of introducing the carrier gas and the reactive gas is more than the gas flowing toward the radially inner portion of the substrate surface, that is, the portion closer to the axis, than the gas flowing toward the radially outer portion of the substrate surface. A step of mixing at least a part of the reaction gas with the carrier gas so as to include a high concentration of the reaction gas.

Preferred reactors and methods according to the foregoing aspects of the present invention provide a uniform distribution of reaction gas across the processing surface of the substrate carrier, for example, across the surface of the substrate carrier of the rotating disk, and the reaction gas velocity is increased. Turbulence caused by different things can be avoided.

It is a schematic diagram which shows the reactor which concerns on one Embodiment of this invention. 1B is a plan view of a substrate carrier used in the embodiment of FIG. 1A. FIG. It is a fragmentary longitudinal cross-section which shows the reactor which concerns on other embodiment of this invention. FIG. 3 is a partial view taken along line 3-3 in FIG. 2. It is a partial bottom view of the board used for the reactor which concerns on further another embodiment of this invention. It is a fragmentary longitudinal cross-section which shows the reactor which concerns on further another embodiment of this invention. FIG. 5B is a cross-sectional view taken along line 5B-5B in FIG. 5A. FIG. 5 is a view similar to FIG. 4 showing a portion of a plate used in a reactor according to an additional embodiment of the invention. FIG. 5 is a view similar to FIG. 4 showing a portion of a plate used in a reactor according to an additional embodiment of the invention. FIG. 5 is a view similar to FIG. 4 showing a portion of a plate used in a reactor according to an additional embodiment of the invention.

  The apparatus according to one embodiment of the invention schematically shown in FIG. 1 comprises a reaction chamber 1 and a substrate carrier 2. The chamber includes an upper wall 16 and an exhaust port 11. The substrate carrier 2 is mounted in the chamber 1 so as to be rotatable about a central axis 14 and is connected to a rotational drive system 12 so that the substrate carrier 2 can be rotated about the axis 14. The substrate carrier 2 defines a processing surface 18 in the form of a substantially flat disk that is orthogonal to the axis 14 and faces the upper wall 16. Only a portion of such a processing surface 18 is shown in FIG. The reaction chamber 1 comprises other conventional elements (not shown) for facilitating the desired epitaxial growth reaction, such as a heating system, a temperature monitoring device, and a pressure monitoring device for holding the substrate carrier at a high temperature. Yes. These features of the apparatus may be of the type used in a reactor marketed under the registered trademark of TURBODISC from Emcore Corporation, Somerset, New Jersey.

  The reactor has a plurality of gas inlets 8 a to 8 d that communicate with the inside of the chamber through the upper wall 16. In the embodiment of FIG. 1, each inlet is in the form of a single hole directed downward toward the carrier processing surface 18 along a direction parallel to the central axis 14, and each inlet hole has the same size. Have. The gas inflow ports 8 a to 8 d are arranged along a common plane extending in the radial direction from the central axis 14. This common plane is a plane defined by the axis 14 and a radial line 17 extending perpendicular to the axis 14. The gas inlets 8a to 8d are separated from each other by a uniform interval h in the radial direction, for example. Each inlet 8 is aligned with a different annular zone of the processing surface 18. Thus, the outermost inlet, i.e., the first inlet 8a is aligned straight with the outermost zone 10a furthest from the axis 14, the inlet 8b is aligned straight with the next zone 10b, and the inlet 8c is aligned straight with the zone 10c. The inlet 8d is aligned with the innermost zone 10d closest to the shaft 14 in a straight line. Zone boundaries are shown by dashed lines in FIG. 1 for clarity of illustration, but these zones are typically not clearly visible due to the prominent features of the substrate carrier.

  The reactor includes a plurality of reaction gas sources 6a to 6d. Each such gas source is adapted to supply a reaction gas at a predetermined mass flow rate. Any device that can supply the reaction gas at a predetermined flow rate may be used. In the arrangement shown, each reaction gas source 6a-6d is a flow restrictor, all of which is connected to a common source 4 of the reaction gas, for example a tank holding such gas under pressure. Has been. Any conventional flow control structure such as a fixed orifice, a manual adjustment valve, an automatic control valve connected to a feedback control system (not shown), or a metering pump as a flow restriction device included in each gas source 6a-6d Is mentioned. If the reaction gas is produced by evaporation from the liquid phase, each reaction gas source may comprise a separate evaporator configured to control the rate of evaporation, or each reaction gas source All of these flow restriction devices may be connected to a common evaporator, including the aforementioned flow restriction devices.

  The reaction gas may be any gas, vapor, or material that is desired to be injected into the reactor and injected into the reactor to participate in the deposition of the substrate. More specifically, the reactive gas may be any gas suitable for treating the substrate surface. For example, when the desired treatment is growth of a semiconductor layer, such as epitaxial growth, the reaction gas contains one or more components of the semiconductor to be grown. For example, the reaction gas may include one or more alkyl metals for compound semiconductor deposition. The reaction gas may be a mixture of a plurality of chemical species and may include inert, i.e. non-reactive components. When the desired reaction includes etching the substrate surface, the reaction gas may include a component that is reactive with the material on the substrate surface.

  Examples of material systems to which the present invention can be applied include epitaxial growth of III-V semiconductors such as GaAs, GaP, GaAs1-xPx, Ga1-yInyAs, AlAs, InAs, InP, InGaP, InSb, GaN, and InGaN. It is done. However, the present invention can be applied to other systems. These systems include II-VI group compounds such as ZnSe, CdTe, HgCdTe, CdZnTe, CdSeTe, IV-IV group compounds such as SiC, diamond, and SiGe, and YBCO, BaTiO, MgO2, ZrO, SiO2, ZnO, And oxides such as ZnSiO and metals such as Al, Cu and W. The resulting materials also have a wide range of electronic and photoelectron applications including high intensity light emitting diodes (LEDs), lasers, solar cells, photocathodes, HEMTs, and MESFETs.

  Carrier gas sources 7a-7d are also provided. The carrier gas sources 7a to 7d may have the same structure as the reactive gas source, and may be connected to the common carrier gas supply source 5. Each gas inflow port 8a-8d is connected to one reaction gas source 6a-6d and one carrier gas source 7A-7d. For example, the inlet 8a is connected to the reactive gas source 6a and the carrier gas source 7a, and the inlet 8d is connected to the reactive gas source 6d and the carrier gas source 7d.

  The carrier gas may be any desired carrier gas that does not participate in the deposition reaction in the chamber provided by the reactive gas supplied to the substrate, for example, an inert gas or a gas that does not participate in the reaction. Alternatively, the carrier gas acts as such, for example, as a gas that does not participate in the rate-limiting step of the reaction, so that whatever amount is desired, such amount is at the desired temperature, pressure, and reaction. It may be a reaction gas that can be supplied as long as the rate-limiting amount is exceeded in the reactor under the conditions.

  In the method according to an embodiment of the invention, the substrate 3 in the form of a flat thin disk is placed on the processing surface 18 of the substrate carrier 2 with the substrate 3 covering the processing surface and the surface to be processed of the substrate 3 being up. It arrange | positions so that it may face upward toward the wall 16. FIG. Desirably, the exposed surface of the substrate 3 is the same or substantially the same plane as the peripheral portion of the processing surface. For example, the substrate 3 in the form of a relatively thin wafer disposed on the processing surface 18 has an upwardly exposed surface that is raised from the peripheral portion of the processing surface 18 by the thickness of the wafer 3. The processing surface 18 of the substrate carrier 2 may be provided with pockets or depressions (not shown) having a depth substantially equal to the thickness of the wafer.

  When the substrate carrier 2 and the substrate 3 are at a desired reaction temperature and the inside of the chamber 1 is under a desired reduced pressure for obtaining a specific reaction, the reaction gas sources 6a to 6d and the carrier gas sources 7a to 7d are activated. , Gas is supplied to the inlets 8a to 8d. The reaction gas 4 and the carrier gas 5 supplied to each inlet are mixed to generate combined gas streams 9a to 9d flowing out from the respective inlets 8a to 8d. The gas flows 9 a to 9 d flowing out from the inlet flow downward in the chamber along the axial direction parallel to the shaft 14 and collide with the processing surface and the exposed surface of the substrate 3. Gas streams 9a-9d from different inlets 8a-8d impinge on different zones 10a-10d of the processing surface 18. For example, the flow 9a flowing out from the inlet 8a mainly collides with the innermost zone 10a, and the flows 9b, 9c, and 9d collide with the zones 10b, 10c, and 10d, respectively. Thus, the flows 9a-9d merge together and form a substantially continuous radially expanding flow, i.e. a curtain of gas flowing towards the substrate carrier, but individual flows from different inlets 8a-8d. 9 a to 9 d go to different zones 10 a to 10 d of the processing surface 18. In other words, the gas impinging on the innermost zone 10d of the processing surface 18 mainly consists of the gas in the flow 9d from the inlet 8d, and the gas impinging on the zone 10b is mainly in the flow 9b from the inlet 8b. Composed of gas. Others are the same. Since the substrate carrier 2 is rotating at a predetermined rotational speed α, different portions of the carrier 2 at different circumferential positions around the axis 14 are aligned with the gas flows 9a-9d, thereby causing the treatment surface 18 to The exposure to the gas flows 9a-9d is the same at every circumferential position.

  In order to provide equal reaction rates for the various regions of the exposed surface of the substrate 3, all regions 10a to 10d of the processing surface 18 have an equal amount of reaction gas 4 per unit time and per unit area of the processing surface. Should be supplied. However, the zones 10a to 10d supplied with gas from various gas outlets have unequal areas. For example, the zone 10a adjacent to the periphery of the processing surface has a larger surface than the zone 10d adjacent to the axis. Accordingly, the flow rates of the reaction gases supplied by the reaction gas sources 6a-6d are selected to provide different flow rates of reaction gases in the streams 9a-9d flowing out of the various inlets 8a-8d. Unless otherwise specified, the “flow rate” referred to in this description is the molar flow rate. The molar flow rate refers to the number of gas molecules per unit time (or the number of atoms of a monoatomic gas). The reactive gas source 6a supplies a relatively large flow rate of reactive gas to the inlet 8a to obtain the flow 9a, and the reactive gas source 6d applies a relatively small flow rate of reactive gas to the inlet 8d to obtain the flow 9d. To supply. The reactive gas sources 6b and 6c supply an intermediate flow rate of reactive gas. In other words, the flow rate of the reaction gas increases in close relation to the distance between the rotation center axis 14 of the substrate carrier 2 of the reactor 1 and the gas inlets 8a to 8d to which the reaction gas is supplied.

  The carrier gas sources 7a to 7d are set so as to supply different flow rates of the carrier gas 5 to the various inlets 8a to 8d. The flow rate of the carrier gas is selected so that the velocities of the different flows 9a to 9d are equal to each other. In the case of identically configured inlets resulting in equal cross-sectional flow, the volume flow rates of the streams 9a-9d exiting from each inlet 8a-8d should be equal.

  In the first approximation, assuming that the gas is a nearly ideal gas, the volumetric flow rate of each stream gas is directly related to the total molar flow rate of the stream, i.e., the sum of the reactant and carrier gas molar flow rates. Is proportional to Thus, to provide multiple streams with equal total molar flow rate and therefore equal velocity, the molar flow rate of carrier gas supplied from carrier gas source 7d to inlet 8d is supplied from carrier gas source 7a to inlet 8a. Must be greater than the molar flow rate of the carrier gas. The flow rate of the larger carrier gas supplied to the inlet 8d and contained in the stream 9d is smaller than the flow rate of the reactive gas supplied from the reactive gas source 6d to the flow rate of the reactive gas supplied from the reactive gas source 6a to the inlet 8a. Make up for flow.

  In other words, the various streams have the same total flow rate but different concentrations of reaction gas. The flow 9a that collides with the maximum zone 10a has the maximum reaction gas flow rate and the minimum carrier gas flow rate, and the flow 9d that collides with the minimum zone 10d has the minimum reaction gas concentration and the maximum carrier gas flow rate. Yes.

  This configuration is schematically shown in FIG. 1 by rods 13a-13d. The total length C of the rod portion 13d represents the total molar flow rate of the flow 9d flowing out from the inlet 8d, that is, the volume flow rate. The length of the dark part of the bar represents the molar flow rate va of the reaction gas in the flow, and the white part of the bar represents the flow rate ia of the carrier gas in the same flow 9d. Similarly, bar portions 13a, 13b, and 13c represent the composition and flow rate of streams 9a, 9b, and 9c, respectively. Although the total length C of all the rod portions 13 is equal, the rod portions 13a, 13b and 13c are gradually reduced with the molar flow rates vc, vb and va of the reaction gas which are gradually increased in the flows 9c, 9b and 9a. The carrier gas flow rates ic, ib, and ia are shown. By supplying various streams 9a-9d that contain different concentrations of reactant gas but the same total flow velocity, the system avoids turbulence and other flow irregularities that may be caused by different velocity flows. However, a substantially equal molar flow rate of reaction gas is supplied to various zones of the processing surface per unit time.

  Accordingly, the exposed surface of the wafer 3 in any part of the processing surface 18 receives substantially the same amount of reaction gas per unit time and per unit area. Thus, the reaction proceeds at a substantially uniform rate across all of the exposed surface of the wafer 3. For example, if this reaction involves the deposition of layers such as epitaxial growth, the deposited layers grow on the various exposed surfaces at a substantially uniform rate.

  The system can be modified to deliver unequal amounts of reactant gas per unit time and per unit surface. For example, the gas flow pattern in the reactor may include a flow radially outward from the axis 14 at or near the processing surface. Such a flow tends to carry a portion of the untreated reaction gas from the innermost zone 10d toward the outermost zone 10d. In order to compensate for this effect, the gas source, for example, has a slight effect by making the reaction gas concentration of the innermost flow 9d per unit time greater than the reaction gas concentration required to achieve an exactly equal reaction gas flow. Can be adjusted to deliver more reactive gas to the innermost zone. In this case, the flow of reactant gas and the concentration of reactant gas are not exactly proportional to the radial distance from the shaft 14. However, because the system uses multiple gas flows at different concentrations and at the same speed, it has a downward, i.e. axial, direction with substantially uniform velocity and unequal gas concentrations at different radial locations. Bring a flowing gas curtain.

  In another variation, the concentration of the reaction gas in the gas flow from the outermost inlet 8a is set to 100%, and the downward flowing gas that collides with the outermost zone does not include the carrier gas and is completely composed of the reaction gas. May be. In this case, the carrier gas source 7a related to the inlet 8a may be omitted. The principles described above are also applicable to having more or fewer entrances than described above that are directed to more or fewer zones than described above.

  In the apparatus according to still another embodiment of the present invention shown in FIGS. 2 and 3, the gas inlet is not arranged on one radial surface of the rotating shaft as described above with reference to FIG. Instead, in the embodiment of FIGS. 2 and 3, the outermost gas inlet 108a is disposed on one side of the rotation axis 114 of the substrate carrier 102 at a radial distance greatly away from the axis, and the next gas inlet 108b is , On the opposite side of the shaft 114, at a radial distance that is less apart from the shaft. Inlet 108c and 108d, located at a radial distance smaller away from shaft 114, are also located on either side of the shaft along common diameter 219 (FIG. 3). Again, different gas flows 109a-109d collide with different zones having different areas of the processing surface 118. The carrier gas flow from the carrier gas sources 107a to 107d and the reaction gas flow from the reaction gas sources 106a to 106d are selected in the same manner as described above, and the gas flow having the same speed while having different concentrations and flow rates of the reaction gas. 109a-109d. In still other variations, the gas inlets may be provided as two complete sets with one inlet located on each side of the central axis, each such set providing gas to any of the processing surfaces. Make a complete complement gas inlet suitable for leading to the zone. Two or more sets, for example, four sets of gas inlets arranged in two diameters may be provided. In yet another variation (FIG. 4), the various gas inlets 36a-36g may be distributed at different radial distances from the central axis 114 along different radii 17a-17g.

  In the aforementioned apparatus, each gas stream is generated by mixing the carrier gas and the reactive gas before introducing the mixed gas to the reaction chamber. However, this is not an essential condition. In the apparatus of FIGS. 5A and 5B, the innermost gas inlet 208d includes two separate holes that open into the upper wall 216 of the reactor, namely, a reaction gas hole 230d and a carrier gas hole 232d. The reactive gas hole 230d is connected to the reactive gas source 206d, and the carrier gas hole 232d is connected to the carrier gas source 207d. Since these gas holes 230d and 232d are disposed adjacent to each other, the carrier gas introduced through the gas hole 232d is a reaction gas introduced through the gas hole 230d, and these gases are inside the reaction chamber 201. Immediately after entering, the combined gas stream is combined to produce a combined gas stream that flows downward into the relevant zone of the processing surface 218. Each of the other inlets 208a-208c is configured by a similar pair of gas holes and operates in a similar manner.

  The apparatus of FIGS. 5A and 5B also includes a perforated plate 215 attached between the upper wall 216 and the processing surface in the reaction chamber 210. As discussed in more detail in US Pat. No. 6,197,121, such perforated plates include, for example, wire mesh screens supported by a set of refrigerant conduits. It should be noted that the disclosure of this patent is incorporated herein by reference. The perforated plate has an upstream side facing the top wall 216, ie, an inlet side, and a downstream side facing the substrate carrier 202 (facing the bottom in FIG. 5A). The perforated plate 215 is separated from the upper wall. A set of barrier walls 250 extends between the top wall 216 and the perforated plate 215 in the vicinity of the inlets 208a-208d. The barrier wall 250 subdivides the space upstream of the perforated plate into spaces 254a to 254d. Each gas inlet 208a-208d opens into one such space. Additional walls 256 separate the spaces 254a-254d from other spaces 258 (FIG. 5B) located upstream of the perforated plate.

  In operation, carrier gas and reactant gas supplied through each inlet are mixed in a space 254 associated with the inlet and pass through a region of the perforated plate that is aligned with such a space. For example, the combination gas supplied by the inlet 208d, that is, the combination gas of the reaction gas from the gas hole 230d and the carrier gas from the gas hole 232d, passes downward through a region of the perforated plate 215, and the injection plate From the downstream side, a flow 209d is directed to the processing surface, and this flow mainly collides with the innermost region 210d of the processing surface 218. Similarly, gases from inlets 208c, 208b, and 208d mix in spaces 254c, 254b, and 254a, respectively, to produce streams 209c, 209b, and 209a, which are the other areas of the processing surface. Clash with. For clarity of illustration, the individual flows are depicted separately in FIG. 5A, but in practice these flows spread radially and on the way from the perforated plate 215 to the treatment surface. , Join each other. Again, the respective flow rates of the carrier gas and the reactive gas supplied from each of the gas sources are the total flow rate of each stream 209, and thus the speed of each stream is substantially equal, but the reactive gas flow rate in the various streams. Concentrations are chosen so that they are not equal. Even in this configuration, an additional set of inlets 208 ′ for the carrier gas and the reactive gas may be provided at other locations spaced circumferentially about the central axis 214. Each such set may be arranged in the same manner as the inlets 208a-208d. Other gases used in the growth process may also be introduced through an additional inlet (not shown) connected to the additional space 258. Such other gases can be introduced at the same time as the carrier gas and reaction gas, or can be introduced at other times in other steps of the process.

  Similar perforated plates may be used with the inlet as described with reference to FIGS. 1A and 2.

  In a device according to yet another embodiment (FIG. 6), the holes constituting the inlets act to control the amount of gas in each gas stream. In this embodiment, the outermost gas inlet 308a includes a reaction gas hole 330a and a carrier gas hole 332a, and each of the other gas inlets 308b, 308c, and 308d includes a similar pair of gas holes. Again, the gas holes that make up each gas inlet are located adjacent to each other. These gas holes are arranged along a common radial line 317. All of the reaction gas holes 330a, 330b, 330c, and 330d are connected to a common conduit 306, which is connected to a source of reaction gas. Accordingly, the reaction gas having substantially the same pressure is supplied to the reaction gas hole. Similarly, all of the carrier gas holes 332a, 332b, 332c, and 332d are connected to a common conduit 307, which is connected to a source of carrier gas. Accordingly, carrier gas having substantially the same pressure is supplied to the carrier gas port. The size of the gas holes and hence the flow resistance of the gas holes are different. The reaction gas hole 330a of the outermost gas inlet 308a is relatively large and has a relatively low flow resistance, and the carrier gas hole 332a of the outermost gas inlet is relatively small and has a high flow resistance. As a result, the gas flow exiting these gas holes, and hence the gas inlet 308a, includes a large amount of reaction gas and a small amount of carrier gas. Conversely, the reaction gas hole 330d at the innermost gas inlet 308d is relatively small and has a high flow resistance, and the carrier gas hole 332d at the same inlet is relatively large and has a high flow resistance. The gas flow flowing out from the inlet 308d has a relatively large amount of carrier gas. Referring to FIG. 6, it is apparent that the dimensions of the reaction gas holes 330 gradually increase from the axis 314 outward in the radial direction, that is, from the smallest zone to the largest zone of the processing surface, The flow resistance of the reaction gas hole gradually decreases in this direction. In contrast, the flow resistance of the carrier gas hole gradually increases in the same direction. Thus, the apparatus has substantially the same total flow rate (carrier gas + reactive gas) and contains different concentrations of reactive gas, resulting in gas flows impinging on different zones of the processing surface. Multiple sets of gas holes as described above can be provided along multiple radial lines to provide multiple such flows around the chamber.

  In yet another variation (FIG. 7), the individual gas holes and their inlets are replaced by carrier gas passages 432 and reaction gas passages 430 that extend through the top wall 416. The downstream ends of these passages (the ends of the passages opening into the reaction chamber) are visible in FIG. These passages are arranged side by side. The carrier gas passage 432 is connected to the carrier gas conduit 407, and the reaction gas passage 430 is connected to the reaction gas conduit 406. Conduits 407 and 406 are connected to a source of carrier gas and reactive gas, respectively. The carrier gas passage 432 has a width w432 that gradually decreases from the shaft 414 in the radially outward direction. Therefore, the resistance of the carrier gas passage with respect to the flow of the carrier gas in the downstream direction of the passage (the direction toward the back side of the sheet of FIG. 7) gradually increases outward in the radial direction. The reaction gas passage has a width w430 that gradually increases outward in the radial direction. Accordingly, the resistance of the reaction gas passage with respect to the flow of the reaction gas downstream gradually decreases outward in the radial direction. In operation, a relatively large amount of reactive gas passes through the radially outer portion of the reactive gas passage 430 and a relatively small amount of carrier gas passes through the radially outer portion of the carrier gas passage 432. Conversely, a small amount of reaction gas and a large amount of carrier gas pass through the radially inner portion of the passage. The carrier gas and the reaction gas merge to generate a gas flow that flows in the downstream direction (the direction toward the back side of the paper surface of FIG. 7). Such gas flow per unit radial distance is gradually outward in the radial direction with a substantially constant total flow rate and a substantially constant velocity at all radial locations. It has a reaction gas concentration that increases.

  A reactor according to still another embodiment of the present invention shown in FIG. 8 includes a reaction gas passage 530 and a carrier gas passage 532 similar to the passage described with reference to FIG. However, in the reactor of FIG. 8, the passages have a constant width over their radial length. The reaction gas passage 530 is filled with a mesh or other porous structure 531 having a porosity that gradually increases radially outward from the shaft 514. Accordingly, the resistance of the passage 530 to the downstream flow of the reaction gas decreases radially outward. The carrier gas passage 532 is filled with a porous structure 533 having a porosity that gradually decreases radially outward, and thus a flow resistance that gradually increases radially outward. The net effect is the same as described with reference to FIG. Other features of the passage can be changed by changing the flow resistance as well along the radial length of the passage. For example, the passage may comprise baffles or partial obstructions that are located at various radial locations. In yet another variation, each passage may have a different length at its inner and outer edges in the downstream direction of the passage. For example, if the passage passes through a plate, the thickness of the plate can be varied in the radial direction and the length of the passage, and thus the flow resistance of the passage, can be varied in the radial direction.

  Although the invention herein has been described with reference to specific embodiments, it is to be understood that these embodiments are merely illustrative of the principles and applications of the present invention. Accordingly, numerous modifications can be made to the illustrated embodiments, and other arrangements can be made without departing from the spirit and scope of the invention as defined by the appended claims. Should be understood.

  The present invention is applicable to an electronic device manufacturing industry in which it is desired to manufacture a large number of electronic components by epitaxial growth of materials. The present invention is applicable, for example, to a vertical disk reactor for epitaxial growth of materials on silicon wafers for electronic components.

1 Chamber 2, 102, 202 Substrate carrier 3 Substrate
4 Reaction gas 5 Common source of carrier gas
6a-6d, 106a-106d, 206d Reaction gas source 7a-7d, 107a-107d, 207d Carrier gas source
8a-8d, 108a-108d, 208a-208d, 308a-3008d Entrance
9a to 9d, 109a to 109d, 209a to 209d Gas flow 10a to 10d Zone 11 Exhaust port 12 Rotation drive system 13a to 13d Rod part 14, 114, 214, 314, 414 axis, rotation axis (central axis)
16, 216, 416 Upper wall 17a-17g Different radial lines
18, 118, 218 Treatment surface 36a-36g Gas inlet 210 Reaction chamber 215 Perforated plate 219 Common diameter 230d Reaction gas hole 232d Carrier gas hole 250 Barrier wall 254a-254d Space 256 Additional wall 258 Other space 307 Common conduit 330a- 330d reactive gas hole 332a-332d carrier gas hole
406 Reaction gas conduit 407 Carrier gas conduit
430, 530 Reaction gas passage 432, 532 Carrier gas passage 533 Porous structure

Claims (14)

A chamber;
A substrate carrier mounted rotatably in the chamber about an axis and adapted to hold one or more substrates;
A gas flow generator arranged to direct a gas flow in the gas chamber toward the substrate carrier in a direction substantially parallel to the axis, the gas flow having a substantially uniform velocity. A reactor for processing a substrate with a gas flow generator configured to have different concentrations of reactant gas at different radial distances from the axis.   The gas generator is configured to supply the gas flow containing the reactant gas at a concentration that is directly proportional to a radial distance from the axis of the gas flow generator. The reactor according to 1.   The gas flow generator comprises a plurality of gas inlets spaced apart from each other, and different gas sources connected to the gas inlets, wherein the gas sources have different concentrations of the gas supplied through the different inlets. The reactor according to claim 1, wherein the reactor is set to contain a reaction gas and maintain a substantially constant total gas velocity.   The gas flow generator has a structure defining a carrier gas passage having a downstream direction and a reaction gas passage having a downstream direction, and the reaction gas passage extends in the vicinity of the carrier gas passage; A carrier gas source communicating with the interior of the chamber through the carrier gas passage, and a reaction gas entering the chamber through the reaction gas passage so that the carrier gas entering the chamber flows downstream through the carrier gas passage. A reactive gas source that communicates with the interior of the chamber via a reactive gas passage in the previous period so as to flow in the downstream direction, and each of the gas passages has resistance to a gas flow in the downstream direction through the passage. The resistance of the carrier gas passage gradually increases outward from the shaft in the radial direction, and the resistance of the reaction gas passage increases. The reactor of claim 1, characterized in that gradually decreases radially outwardly from said axis.   The carrier gas passage is in the form of a carrier gas slot penetrating through the plate, and the reaction gas passage is in the form of a carrier gas slot penetrating through the plate. Each of the slots has a width orthogonal to a radially outward direction, the carrier gas slot gradually decreases in the outer direction, and the reaction gas slot gradually decreases in the inner direction. The reactor according to claim 4. While supporting one or more substrates on a substrate support such that one or more surfaces of the substrate to be processed are positioned substantially perpendicular to the axis, the substrate support is supported in the chamber within the axis. Rotating around the center,
Introducing a plurality of gas flows in the chamber toward the one or more surfaces into the chamber in a direction substantially parallel to the axis, each of the gas flows in the chamber. Flowing at a substantially uniform velocity toward one or more surfaces;
Mixing the reaction gas and the carrier gas so as to form each of the plurality of flows, wherein the gas flow flowing toward a radially outer portion of the one or more surfaces is the one or And a step of processing the substrate, wherein the gas is mixed so that the concentration of the reaction gas is higher than that of the gas flow flowing toward the radially inner portion of the plurality of surfaces.   The method of claim 6, wherein the introducing step includes discharging the gas flow into the chamber through a plurality of inlets disposed at different radial distances from the axis.   The mixing step mixes the carrier gas with the reaction gas before releasing from at least a portion of the inlets, and flows containing different concentrations of the carrier gas are released from different inlets of the plurality of inlets. 7. The method of claim 6, wherein the method is performed as follows.   Maintaining a reaction condition in the chamber such that the reaction gas reacts with the substrate and a layer containing a component derived from the reaction gas by an epitaxial reaction is grown on the one or more surfaces. The method of claim 6 comprising:   The method of claim 9, wherein the reaction gas comprises an alkyl metal.   9. A method according to claim 8, wherein the carrier gas comprises nitrogen.   9. The method of claim 8, wherein the mixing step is performed such that the reactant gas concentration of each stream is directly proportional to the radial distance of the stream from the axis.   In the mixing step, the carrier gas and the reaction gas are immediately discharged from at least a part of the inlet so that flows having different concentrations of the carrier gas flow in the chamber toward the one or more surfaces. 8. The method of claim 7, wherein the method is performed to mix. The chamber further includes a porous spray plate disposed between the inlet and the substrate support, and the porous spray plate has a downstream surface facing the substrate support,
The method according to claim 13, wherein the mixing step is performed such that flows having different concentrations of the carrier gas exit from the downstream surface of the injection plate and flow toward the one or more surfaces. .

Images