WO2014036886A1 - Reaction chamber for vapor deposition process - Google Patents

Reaction chamber for vapor deposition process Download PDF

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Publication number
WO2014036886A1
WO2014036886A1 PCT/CN2013/081816 CN2013081816W WO2014036886A1 WO 2014036886 A1 WO2014036886 A1 WO 2014036886A1 CN 2013081816 W CN2013081816 W CN 2013081816W WO 2014036886 A1 WO2014036886 A1 WO 2014036886A1
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WO
WIPO (PCT)
Prior art keywords
tray
reaction chamber
edge
chamber
heat insulating
Prior art date
Application number
PCT/CN2013/081816
Other languages
French (fr)
Chinese (zh)
Inventor
孙仁君
左然
何晓崐
叶芷飞
谭华强
田益西
Original Assignee
光达光电设备科技(嘉兴)有限公司
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Publication of WO2014036886A1 publication Critical patent/WO2014036886A1/en

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Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
    • C23C16/455Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for introducing gases into reaction chamber or for modifying gas flows in reaction chamber
    • C23C16/45502Flow conditions in reaction chamber
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
    • C23C16/455Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for introducing gases into reaction chamber or for modifying gas flows in reaction chamber
    • C23C16/45587Mechanical means for changing the gas flow
    • C23C16/45591Fixed means, e.g. wings, baffles
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
    • C23C16/458Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for supporting substrates in the reaction chamber
    • C23C16/4582Rigid and flat substrates, e.g. plates or discs
    • C23C16/4583Rigid and flat substrates, e.g. plates or discs the substrate being supported substantially horizontally
    • C23C16/4585Devices at or outside the perimeter of the substrate support, e.g. clamping rings, shrouds

Definitions

  • Reaction Chamber for Vapor Deposition Process This application claims priority to Chinese Patent Application entitled “Reaction Chamber for Vapor Deposition Process” submitted to the Chinese Patent Office on September 7, 2012, application number 201210330818. The entire contents of which are incorporated herein by reference.
  • TECHNICAL FIELD The present invention relates to deposition apparatus, and more particularly to a reaction chamber for a vapor deposition process.
  • Metal organic chemical vapor deposition is a chemical vapor deposition process developed on the basis of vapor phase epitaxy (VPE). It uses organic compounds of Group III and II elements and hydrides of Group V and VI elements as reaction gases for crystal growth, and performs epitaxial deposition processes on sapphire virgin land or other villages by thermal decomposition reaction.
  • FIG. 1 is a schematic view showing the structure of a reaction chamber of a prior art M0CVD apparatus.
  • the reaction chamber includes: a tray 10 having an upper surface 11 and a lower surface 12 opposite to the upper surface 11, the upper surface 11 for placing a substrate, the lower surface 12 forming a groove; the gas supply device 30 Located above the upper surface of the tray 10, the gas supply device 30 is configured to supply a reaction gas to the substrate; the chamber sidewall 20 surrounds the tray 10-week, the chamber sidewall 20 and the tray An exhaust passage is formed between the edges of the 10, and the reacted gas flows from the exhaust passage to the outside of the reaction chamber; a chamber cover 40 is located above the chamber sidewall 20 and the gas supply device 30, the cavity The chamber top cover 40 and the chamber side wall 20 define a space for the reaction chamber, and the reaction chamber is isolated from the outside; the heating unit 50 is located below the recess of the lower
  • the technical problem to be solved by embodiments of the present invention is to provide a reaction chamber for a vapor deposition process, which improves the uniformity of the airflow field, temperature field or concentration field on the tray in the reaction chamber, especially at the edge of the tray. Sexuality improves the uniformity of the layer of epitaxial material formed on the village floor.
  • an embodiment of the present invention provides a reaction chamber for a vapor deposition process, including: a tray having an upper surface for placing a substrate; a chamber sidewall surrounding the tray for one week, further comprising: a member At least a portion of the edge of the tray is used to improve the uniformity of the airflow field, temperature field, or concentration field at the edge of the tray.
  • the tray has a lower surface opposite the upper surface, and the thickness of the member in the direction of the lower surface of the upper surface gradually decreases.
  • an exhaust passage is formed between the member and the tray, the member having a side surface facing one side of the tray, and a side surface of the member is a smooth transition.
  • the side surface of the member is an inner curved surface.
  • an exhaust passage is formed between the member and the tray, the member having a side surface facing one side of the tray, the side surface being an inner curved surface.
  • the side surface extends above a plane in which the upper surface lies.
  • an air passage is formed between the member and the side wall of the chamber, and the member has a side surface facing one side of the side wall of the chamber, and the side surface is a convex curved surface.
  • the side surface does not exceed the upper surface of the tray.
  • the tray has a lower surface opposite the upper surface, the side surface extending below the plane of the lower surface.
  • a curved transition is made between the edge of the upper surface of the tray and the side of the tray.
  • the member has a side surface facing one side of the tray, a side view of the member
  • the reflectivity of the facing light is not less than the reflectivity of the sidewall of the chamber to the light.
  • the member has a side surface facing one side of the tray, and the side surface of the member faces the light having a reflectance not less than the reflectance of the edge of the tray to the light.
  • the side surface of the member has a roughness of not more than 0.08 m, so that the side surface of the member forms a mirror surface, and the reflection of the light is specular reflection.
  • the side surface of the member has a heat resistant reflective layer that remains stable during the vapor deposition process.
  • the material of the heat resistant reflective layer is silicon carbide.
  • the member is annular in cross section in a direction parallel to the upper surface of the tray.
  • the member is constructed by connecting two or more sub-members.
  • the member is a torus.
  • a heat insulating structure is embedded in the member for reducing heat loss from the edge of the tray to the side wall of the chamber.
  • a side surface of the heat insulating structure facing one side of the tray is an inward arc.
  • the heat insulating structure includes an insulating gas containing layer embedded in the member, and a heat insulating gas containing layer defining a space in the member.
  • the space is for accommodating the heat insulating gas, and the heat insulating coefficient of the heat insulating gas is lower than a thermal conductivity of the member.
  • the shape of the side of the insulating gas containing layer facing the side of the tray is a concave orphan.
  • the heat insulating structure is a heat insulating block embedded in the member, and the heat insulating block has a thermal conductivity lower than a thermal conductivity of the member.
  • the method further includes: a gas supply device located above the upper surface of the tray, the gas supply device for supplying a reaction gas to the substrate, one end of the member being fixed to the gas supply device.
  • the method further includes: a chamber top cover located above the upper surface of the tray, and one end of the member is fixed to the chamber top cover.
  • the member is fixed to the side wall of the chamber.
  • the embodiment of the invention has the following advantages:
  • the reaction chamber provided by the embodiment of the invention has a member at the edge of the tray, and the member improves the uniformity of the airflow field, the temperature field or the concentration field at the edge of the tray;
  • the member is used for heat insulation between the tray and the side wall of the chamber, effectively reducing the loss of heat from the edge of the tray to the side wall of the chamber, improving the efficiency of heating the tray, and the member along the tray
  • the thickness of the upper surface to the lower surface of the tray is gradually reduced, which compensates for the problem that the temperature of the edge of the tray is uneven due to the gradual decrease of the temperature of the lower surface of the tray to the upper surface of the tray, and better plays the side wall of the tray and the chamber
  • the effect of insulation, shielding and insulation between them improves the uniformity of the temperature field of the edge of the tray and the upper surface of the entire tray;
  • the member may also form an exhaust passage with the tray, and the side surface of the member facing the tray may be a smooth transition including the inner curved surface, so that the reacted gas is from the tray
  • the gas retention at the smooth transition is reduced or eliminated, thereby making the airflow field at the edge of the tray more uniform, since the temperature field and the airflow field also affect the concentration field of the reactive gas at the edge of the tray. Therefore, the concentration distribution of the reaction gas at the edge of the tray is also improved, and the uniformity of the epitaxial material layer formed on the village bottom at the edge of the tray is improved;
  • the member and the tray may also constitute an exhaust passage, the member having a side surface facing one side of the tray, the side surface being a concave curved surface so as to be in the exhaust passage at the edge of the tray Forming a smooth transition that facilitates reducing or eliminating the dead space of the gas at the edge of the tray, thereby improving the uniformity of the gas field at the edge of the tray; or/and the side walls of the tray and member and the chamber
  • the exhaust passage may also be formed, the member having a side surface facing one side of the tray, the side surface being a convex curved surface, thereby forming a smooth transition in the exhaust passage at the edge of the tray, the smooth transition facilitating Reduces or eliminates gas dead space at the edge of the tray, improving gas at the edge of the tray Field uniformity;
  • the side surface of the member extends above the upper surface of the tray or below the lower surface of the tray, thereby further improving the uniformity of the gas field, temperature field and concentration field at the edge of the tray;
  • a curved transition between the edge of the upper surface of the tray and the side of the tray further improves the uniformity of the gas field, temperature field and concentration field at the edge of the tray;
  • the member has a side surface facing one side of the tray, and a side surface of the member has a reflectance to light of not less than a reflectance of the side wall of the chamber to the light, and is not disposed between the side wall of the chamber and the tray.
  • the light from the tray can be reflected by the side surface of the member toward the tray, as the light from the member, part of the tray is absorbed by the side wall of the chamber, resulting in low heating efficiency to the tray, and the temperature at the edge of the tray is low.
  • Improved light utilization and heating efficiency of the tray improving the uniformity of the temperature field at the edge of the tray;
  • the side surface of the member facing the tray has a reflectivity to light that is not less than the reflectance of the edge of the tray to the light such that the side surface can reflect light from the edge of the tray back to the tray, further
  • the utilization of light at the edge of the tray and the heating efficiency of the tray are improved, and the uniformity of the temperature field at the edge of the tray is improved;
  • the side surface of the member facing the tray is specularly reflected by the light. Thereby, most of the light at the edge of the tray is reflected, so that the utilization of light at the edge of the tray and the heating efficiency of the tray are higher, and the uniformity of the temperature field at the edge of the tray is better;
  • the member has a ring shape in a section parallel to the direction of the upper surface of the tray, or the member has two or more sub-members connected or the member is a torus, or the member may Connected to the chamber side wall, the chamber top cover or the gas supply, or there may be a gap between the member and the tray and between the member and the chamber sidewall so that the structure, shape, size and The distribution is flexibly adjusted to obtain the optimum temperature, concentration, and airflow fields at the edge of the tray;
  • a heat insulating structure is formed in the member to make the member better
  • the sidewall of the chamber is isolated from the edge of the tray to reduce the heat loss from the edge of the tray to the side wall of the chamber, further improving the uniformity of the temperature field, the airflow field and the concentration field at the edge of the tray.
  • FIG. 1 is a schematic structural view of a reaction chamber of a prior art M0CVD apparatus
  • FIG. 2 is a schematic structural view of a reaction chamber according to a first embodiment of the present invention
  • Figure 3 is a schematic cross-sectional view of the reaction chamber along the AA line
  • Figure 4 is a schematic structural view of a member of a second embodiment of the present invention.
  • Figure 5 is a schematic view showing the structure of a reaction chamber according to a third embodiment of the present invention.
  • Figure 6 is a schematic structural view of a reaction chamber according to a fourth embodiment of the present invention.
  • Figure 7 is a schematic structural view of a reaction chamber according to a fifth embodiment of the present invention.
  • Figure 8 is a schematic structural view of a reaction chamber of a sixth embodiment of the present invention.
  • Figure 9 is a schematic structural view of a member of a first embodiment of the present invention.
  • Figure 10 is a schematic view showing the structure of a member of a second embodiment of the present invention.
  • the uniformity of the layer of epitaxial material formed on the substrate by the existing reaction chamber needs to be further improved, especially the uniformity of the layer of epitaxial material formed on the substrate at the edge of the tray needs to be improved. It has been found that the uniformity of temperature field, airflow field and concentration field at the edge of the tray has a great influence on the uniformity of the existing vapor deposition process. The prior art neglects the optimization of the structure at the edge of the tray, which cannot fully utilize the layer of epitaxial material formed on the bottom of the village, especially the edge of the tray. As the size of the tray becomes larger, the structure at the edge of the tray is opposite to the tray.
  • the inventor Before the design of the edge of the tray, the inventor compared the temperature of the prior art tray Field, concentration field and airflow field were studied and analyzed. Specifically, as shown in FIG. 1, when performing a vapor deposition process (such as a M0CVD process), the gas supply device 30 supplies a reaction gas to the substrate on the upper surface 11 of the tray 10, and the tray 10 is heated by the heating unit below it. 50 is heated to be in a high temperature state (temperature is usually greater than 500 degrees Celsius), the reaction gas supplied from the gas supply device 30 is usually in a low temperature state due to cooling (temperature is usually lower than 200 degrees Celsius), and the reaction gas flows from the gas supply device 30 to the bottom surface of the substrate.
  • a vapor deposition process such as a M0CVD process
  • the reacted gas flows out of the reaction chamber through an exhaust pipe between both sides of the edge of the tray 10 and the side wall 20 of the chamber.
  • the reaction gas exchanges heat with the upper surface 11 of the tray 10, and the heat exchange is more severe at the edge of the tray 10 due to the concentrated discharge of the gas, which causes the temperature at the edge of the tray 10 to be low, resulting in The temperature field of the upper surface 11 of the tray 10 is not uniform.
  • the heat dissipation rate at the edge of the tray 10 is faster than the heat dissipation rate in the middle of the tray 10, which also affects the uniformity of the temperature field at the edge of the tray 10.
  • the temperature difference between the chamber side wall 20 and the edge of the tray 10 also causes heat exchange between the two, which heat exchange is reduced on the one hand.
  • the temperature of the edge of the tray 10 causes the temperature distribution at the edge of the tray 10 to be uneven, and on the other hand, the heating efficiency of the tray 1 G by the heating unit 50 is also lowered.
  • the inventors have also found that since the heating unit 50 is placed under the tray 10, the temperature of the lower surface to the upper surface of the tray 10 is gradually lowered, so that the temperature of the upper surface 11 of the tray 10 is low, in the tray 10 The temperature drop at the edge is more pronounced.
  • the prior art does not consider the temperature change in the direction from the upper surface 11 to the lower surface 12 of the tray 10, which also causes uneven temperature distribution of the edge of the tray 10, which further causes the temperature of the edge of the upper surface 11 of the tray 10. The field is uneven.
  • the direction of the gas is changed along the horizontal direction of the upper surface 1 1 to In the vertical direction, a gas dead angle is formed at the corner between the gas supply device 30, the edge of the tray 10, and the side wall 20 of the chamber, and some of the gas will stay there, which will not only affect the deposition process (such as M0CVD) reaction process.
  • the switching of different reaction gases may even cause a backflow of gas, and the dead angle of the gas at the corners is also liable to cause vortexing of the gas at the edge of the tray 10, resulting in uneven airflow at the edge of the tray 10.
  • the concentration field at the edge of the tray 1 Q is hooked. Sexuality cannot be maintained, and eventually the uniformity of the layer of epitaxial material formed on the bottom of the substrate at the edge of the tray 10 is not ideal.
  • the present invention optimizes the internal structure of the reaction chamber by optimizing the edge of the tray, mainly to improve the edge of the tray, thereby improving the temperature field, the concentration field, and the uniformity of the airflow field at the edge of the tray.
  • Optimized in conjunction with problems with existing pallet structures including changes in temperature from the lower surface to the upper surface of the tray, heat dissipation at the edge of the tray, heat exchange between the tray and the sidewall of the chamber, and tray and Problems such as heat exchange between gases.
  • the reaction chamber for a deposition process proposed by the present invention includes: a tray having an upper surface for placing a substrate; a chamber sidewall surrounding the tray, further comprising: a member, at least a portion surrounding the The edge of the tray is used to improve the uniformity of the airflow field, temperature field or concentration field at the edge of the tray.
  • a tray having an upper surface for placing a substrate
  • a chamber sidewall surrounding the tray further comprising: a member, at least a portion surrounding the The edge of the tray is used to improve the uniformity of the airflow field, temperature field or concentration field at the edge of the tray.
  • Fig. 2 is a schematic view showing the internal structure of a reaction chamber according to a first embodiment of the present invention.
  • the reaction chamber is a reaction chamber of a chemical vapor deposition apparatus.
  • the reaction chamber is a reaction chamber of a M0CVD apparatus for the M0CVD process.
  • the reaction chamber has a chamber sidewall 200.
  • the chamber sidewall 200 has a chamber sidewall cooling unit (not shown) corresponding thereto.
  • the chamber sidewall cooling unit is configured to cool the chamber sidewall 200 such that the temperature of the chamber sidewall 200 does not exceed 800 degrees Celsius, preferably, the temperature of the chamber sidewall 200 does not exceed 200 degrees Celsius.
  • the chamber sidewall 200 temperature does not exceed 100 degrees Celsius.
  • a chamber top cover 400 is disposed above the chamber sidewall 200. The chamber top cover 400 and the chamber side wall 200 define the space of the reaction chamber and provide isolation of the reaction chamber from the exterior.
  • a gas supply device 300 is provided below the chamber top cover 400.
  • the gas supply device 300 may be a shower head.
  • the gas supply device 300 is a close-coupled shower head (CCS) capable of vertically injecting a reaction gas downward.
  • CCS close-coupled shower head
  • a tray 100 is disposed inside the reaction chamber.
  • the material of the tray 100 is graphite.
  • the surface of the tray 100 may be coated or plated with a silicon carbide coating (not shown), and the silicon carbide coating has good stability.
  • the silicon carbide coating does not react with the reaction gas, and the silicon carbide coating structure is dense, preventing the gas from reacting with the graphite to damage the tray 10 or generating particles, affecting the process yield, and carbonizing.
  • the coefficient of thermal expansion of the silicon coating is comparable to that of graphite, and does not fall off the graphite at high temperatures, affecting the yield of the process.
  • the tray 100 has an upper surface 101 and a lower surface 102 opposite the upper surface 101.
  • the upper surface 101 is the surface of the tray 100 facing the chamber top cover 400 and the gas supply device 300, and the upper surface 101 is for placing the substrate.
  • the edge of the upper surface 101 and the side surface of the tray 100 are arcuately transitioned, such that the reaction gas from the gas supply device 300 passes through the arc surface after flowing vertically to the upper surface 101. After the smooth transition to the vertical direction, the direction of the airflow at the edge of the tray 100 is prevented from being abrupt, and the uniformity of the airflow field at the edge of the tray 100 can be improved.
  • the lower surface 102 of the tray 100 is coupled to a rotary support mechanism 600 having a hollow cylindrical shape, and the rotary support mechanism 600 is used to support the tray 100.
  • the rotary support mechanism 600 is also used to drive the tray 100 to rotate at a certain speed.
  • a heating unit 500 is disposed below the tray 100.
  • the heating unit 500 is located within the rotating support structure 600, which saves space throughout the chamber.
  • a groove can be formed in the portion of the tray 100 facing the heating unit 500, which is advantageous in improving the efficiency of heating the heating unit 500 to the tray.
  • member 700 surrounds the edge of tray 100. As an alternative embodiment, the member 700 wraps around the edge of the tray 100.
  • member 700 is affixed to the edge of gas supply 300 On the chamber top wall 400.
  • the member 700 can also be secured only to the edge of the gas supply device 300 or to the chamber top wall 400, even though the member 700 can be supported within the reaction chamber by a separate support structure.
  • the member 700 and the tray 100 constitute an exhaust passage.
  • the reacted gas exits the reaction chamber through the edge 100 of the tray 100 and the member 700.
  • the member 700 has a side surface (not shown) facing one side of the tray, the side surface being a concave curved surface to form a smooth transition at the edge of the tray 100, reducing or eliminating gas at the edge of the tray 100
  • the dead space of the gas between the members 700 reduces or eliminates problems such as gas retention at the edges of the tray 100, gas vortexing, etc., and improves the uniformity of the airflow field at the edge of the tray 100.
  • the side surface of the member 700 facing the tray 100-side extends above the plane of the upper surface 101 of the tray 100, which improves the uniformity of the airflow field, temperature field and concentration field at the edge of the tray 100. .
  • the side surfaces also extend below the plane in which the lower surface 102 of the tray 100 is located, which improves the uniformity of the airflow field, temperature field, and concentration field at the edge of the tray 100.
  • the member 700 faces a side surface of the tray 100 as a part of the exhaust passage, and the air flow can be better guided to smoothly flow the gas from the upper surface 101 of the tray 100 along the exhaust passage.
  • the member 700 is also used for thermal insulation between the tray 100 and the chamber sidewall 200 due to the optimized configuration of the member 700, reducing the edge of the tray 100 and the chamber sidewall 200. The heat is lost, improving the efficiency with which the heating unit 500 heats the tray 100.
  • the side surface of the member 700 facing the tray 100-side has a reflectivity to light that is not less than the reflectivity of the chamber sidewall 200 to light, such that the side surface can be from the edge of the tray 100.
  • the light at the place is reflected back to the tray 101, which further improves the utilization of light at the edge of the tray 101 and the heating efficiency of the tray 101, improving the uniformity of the temperature field at the edge of the tray 101.
  • the reflectance of the side surface to the light should be not less than the reflectance of the edge of the tray 100 to the light, so that the side surface Light from the edge of the tray 100 can be reflected back
  • the tray 100 further improves the utilization of light at the edges of the tray 100 and the heating efficiency of the heating unit 500 to the tray 101, improving the uniformity of the temperature field at the edge of the tray 100.
  • the roughness of the side surface does not exceed 008 meters, so that the side surface forms a mirror surface, and the reflection of the light is specular reflection.
  • the member 700 is made of graphite or quartz.
  • a heat-resistant reflective layer (not shown) is further disposed on a side surface of the member 700 facing the tray 101, the heat-resistant reflective layer protects graphite or quartz, and the heat-resistant reflective layer remains stable during the deposition process.
  • the heat-resistant reflective layer does not fall off from the graphite or quartz of the member 700, and on the other hand, the heat-resistant reflective layer does not react with the gas in the reaction chamber.
  • the material of the heat resistant reflective layer is silicon carbide.
  • the member 700 can also be fabricated using silicon carbide regardless of manufacturing cost and processing difficulty.
  • the thickness of the member 700 in the direction from the upper surface 101 to the lower surface 102 of the tray 100 is gradually reduced, as shown in FIG. 2, along the upper surface 101 to the lower surface. In the direction of 102, the thickness of member 700 is gradually reduced from T1 to T2.
  • the thickness of the member 700 along the upper surface 101 to the lower surface 102 is reduced, so that the member 700 can compensate for the problem that the temperature of the lower surface 102 of the tray 100 to the upper surface 101 of the tray 100 gradually decreases to the temperature unevenness caused to the edge of the tray 100, and The effect of heat insulation, shielding and heat retention between the tray and the side walls of the chamber is well achieved, thereby improving the uniformity of the temperature field of the edge of the tray 100 and the upper surface 101 of the entire tray 100.
  • Figure 3 is a schematic cross-sectional view of Figure 2 along the ⁇ .
  • the member 700 surrounds the tray 100-week, and the chamber sidewall 200 surrounds the member 700 for one week.
  • the member 700 is a toroidal body, so that the heat insulation and heat insulation effect on the edge of the tray 100 and the airflow effect on the airflow at the edge of the tray 100 are better, so that the edge of the tray 100 can be further improved. Airflow field, temperature field and concentration field.
  • FIG. 4 is a schematic structural view of a reaction chamber according to a second embodiment of the present invention.
  • the same structures as those of the first embodiment are denoted by the same reference numerals.
  • This embodiment is substantially the same as the previous embodiment except that the member 700 is fixed to the chamber side wall 200, and The member 700 is provided with a heat insulating structure 710, so that the member 700 can better isolate the chamber sidewall 200 from the edge of the tray 100, reduce the heat loss from the edge of the tray 100 to the chamber sidewall 200, and further improve the tray.
  • the heat insulating structure 710 may be a torus provided in the annular body of the member 700.
  • the heat insulating structure 710 is a heat insulating block, and the heat insulating block 710 has a thermal conductivity lower than that of the member 710.
  • the heat insulating structure 710 may further be composed of an insulating gas containing layer and a heat insulating gas, the heat insulating gas containing layer being embedded in the member, the heat insulating gas containing layer being A space is defined in the member for accommodating the heat insulating gas, and the heat insulating coefficient of the heat insulating gas is lower than a thermal conductivity of the member.
  • FIG. 5 is a schematic illustration of the construction of a reaction chamber in accordance with a third embodiment of the present invention.
  • the same structures as those of the third embodiment are denoted by the same reference numerals.
  • This embodiment is basically the same as the second embodiment, except that the side surface of the heat insulating structure 710 in the member 700 facing the side of the tray 100 is inwardly concave, which further optimizes the edge of the tray 100.
  • Fig. 6 is a schematic view showing the structure of a reaction chamber according to a fourth embodiment of the present invention.
  • the same structures as those of the first embodiment are denoted by the same reference numerals.
  • the present embodiment differs from the first embodiment in that the member 700 is fixed to the chamber top cover 400, and the member 700 is located between the tray 100 and the chamber side wall 200, that is, the member 700 and the chamber side wall 200 and the tray. There is a gap between the 100, and an exhaust passage is formed between the member 700 and the tray 100.
  • the super-facing chamber side wall 200 of the member 700 has a convex curved surface.
  • the present embodiment differs from the first embodiment in that the member 700 is supported on the edge of the tray 100 by a special support structure (not shown).
  • the surface of the member 700 facing the chamber top cover 400 is flush with the upper surface 101 of the tray 100, such that the member 700 and the chamber sidewall 200 and the member 700 and the tray 100 respectively form an exhaust gas. aisle.
  • the side surface of the member 700 facing the side wall 200 side of the chamber does not exceed the level of the upper surface 101 of the tray 100. This helps to improve the uniformity of the gas field at the edge of the tray 100.
  • the side surface of the member 700 facing the tray 100 is an inward curved surface
  • the side surface of the member 700 facing the side wall of the chamber is a convex curved surface.
  • the coupling member 700 is between the chamber sidewall 200 and the tray 100 by adjusting the curvature of the side surface of the member 700 facing the chamber sidewall 200, the radius, and the curvature, radius of the side surface of the member 700 facing the chamber sidewall 200.
  • the position, the airflow field, the concentration field and the temperature field at the edge of the tray 101 are adjusted and optimized.
  • the thickness of the member 700 gradually decreases along the direction from the upper surface 101 to the lower surface 102 of the tray 100 to compensate for the gradual decrease in the temperature of the edge of the tray 100 from the lower surface 102 to the upper surface 101.
  • the edge of the upper surface 101 of 100 is better insulated.
  • the surface of the member 700 remote from the chamber top cover 400 is located above the plane of the lower surface 102 of the tray 100. In other embodiments, the surface of the member 700 that is away from the chamber top cover 400 can also extend below the plane of the lower surface 102.
  • the member 700 is connected to the chamber top cover 400, and the member 700 has a gap with the chamber side wall 200, and the member 700 faces the side wall 200 side of the chamber.
  • the side surface is parallel to the chamber side wall 200, and the side surface of the member 700 facing the tray 100 side is a flat surface.
  • the thickness of the member 700 in the direction from the upper surface 101 to the lower surface 102 of the tray 100 is gradually reduced, and by adjusting the thickness of the member 700 to be reduced, it is possible to achieve a better member 700 to the upper surface 101 to the lower surface 102 of the tray 100.
  • the compensation of the temperature change achieves isolation between the edge of the tray 100 and the chamber sidewall 200, further improving the uniformity of the temperature field, airflow field and concentration field at the edge of the tray.
  • FIG. 9 is a top plan view of a member 700 according to a first embodiment of the present invention.
  • Member 700 is annular and a tray (not shown) is placed within the annulus of member 700.
  • the member 700 includes a plurality of sub-members that are connected. Each sub-component may be the same size or different. In this embodiment, the member 700 includes four sub-members 701 of the same size.
  • FIG. 10 is a schematic structural diagram of a member 700 according to a second embodiment of the present invention.
  • the member 700 includes a plurality of sub-members 701.
  • the sub-members 701 have a space therebetween, and the sub-members 701 are independent of each other.
  • the reaction chamber provided by the embodiment of the present invention has a member at the edge of the tray, and the member improves the uniformity of the airflow field, the temperature field or the concentration field at the edge of the tray; further optimized, the member is used for the tray
  • the heat insulation between the side wall of the chamber effectively reduces the loss of heat from the edge of the tray to the side wall of the chamber, improves the efficiency of heating the tray, and the thickness of the member along the upper surface of the tray to the lower surface of the tray Gradually reducing, compensating for the problem of uneven temperature of the edge of the tray caused by the gradual decrease of the temperature of the lower surface of the tray to the upper surface of the tray, better shielding, shielding and heat insulation between the tray and the side wall of the chamber
  • the member may also form an exhaust passage with the tray, the member facing the side surface of the tray side It can be a smooth transition including the inner arc surface, so that
  • the gas retention phenomenon at the place is reduced or eliminated, so that the airflow field at the edge of the tray is more evenly hooked, because the temperature field and the airflow field also affect the concentration field of the reaction gas at the edge of the tray, so that the reaction gas at the edge of the tray
  • the uniformity of the concentration distribution is also improved, and the uniformity of the epitaxial material layer formed on the bottom of the substrate at the edge of the tray is improved;
  • the member and the tray may also constitute an exhaust passage, the member having a side surface facing one side of the tray, the side surface being a concave curved surface so as to be in the exhaust passage at the edge of the tray Forming a smooth transition that facilitates reducing or eliminating the dead space of the gas at the edge of the tray, thereby improving the uniformity of the gas field at the edge of the tray;
  • the tray and the member and the side wall of the chamber may also constitute an exhaust passage, the member having a side surface facing one side of the tray, the side surface being a convex curved surface so as to be at the edge of the tray A smooth transition is formed in the exhaust passage, which facilitates reducing or eliminating the dead space of the gas at the edge of the tray, thereby improving the uniformity of the gas field at the edge of the tray;
  • the side surface of the member extends above the upper surface of the tray or below the lower surface of the tray, thereby further improving the gas field, temperature field and Uniformity of the concentration field;
  • a curved transition between the edge of the upper surface of the tray and the side of the tray further improves the uniformity of the gas field, temperature field and concentration field at the edge of the tray;
  • the member has a side surface facing one side of the tray, and a side surface of the member has a reflectance to light of not less than a reflectance of the side wall of the chamber to the light, and is not disposed between the side wall of the chamber and the tray.
  • the light from the tray can be reflected by the side surface of the member toward the tray, as the light from the member, part of the tray is absorbed by the side wall of the chamber, resulting in low heating efficiency to the tray, and the temperature at the edge of the tray is low.
  • Improved light utilization and heating efficiency of the tray improving the uniformity of the temperature field at the edge of the tray;
  • the side surface of the member facing the tray has a reflectivity to light that is not less than the reflectance of the edge of the tray to the light such that the side surface can reflect light from the edge of the tray back to the tray, further Improves the utilization of light at the edge of the tray and the heating efficiency of the tray, improving the uniformity of the temperature field at the edge of the tray;
  • the side surface of the member facing the tray side reflects specularly with light, such that a substantial portion of the light at the edge of the tray is reflected, thereby utilizing and utilizing light at the edge of the tray
  • the heating efficiency of the tray is higher, and the uniformity of the temperature field at the edge of the tray is better;
  • the member has a ring shape in a section parallel to the direction of the upper surface of the tray, or the member has two or more sub-members connected or the member is a torus, or the member may Connected to the chamber side wall, the chamber top cover or the gas supply, or there may be a gap between the member and the tray and between the member and the chamber sidewall so that the structure, shape, size and The distribution is flexibly adjusted to obtain the optimum temperature, concentration, and airflow fields at the edge of the tray;
  • the member is formed with a heat insulating structure, so that the member can better isolate the side wall of the chamber from the edge of the tray, reduce heat loss from the edge of the tray to the side wall of the chamber, and further increase the edge of the tray.
  • the uniformity of the temperature field, airflow field and concentration field is not limited thereto. Any A person skilled in the art can make various changes and modifications without departing from the spirit and scope of the invention, and the scope of the invention should be determined by the scope defined by the claims.

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Abstract

The technical problem solved by embodiments of the present invention is to provide a reaction chamber for a vapor deposition process. The reaction chamber comprises: a tray, the upper surface of the tray being used for placing a substrate; a chamber side wall surrounding the tray; and a member, at least one part of the member surrounding the edge of the tray, and the member being used for improving uniformity of an airflow field, a temperature field or a concentration field at the edge of the tray. With the embodiments of the present invention, the uniformity of the airflow field, the temperature field or the concentration field on the tray, especially at the edge of the tray is improved, and uniformity of an epitaxial material layer formed on the substrate is improved.

Description

用于气相沉积工艺的反应腔室 本申请要求 2012 年 9 月 7 日提交中国专利局、 申请号为 201210330818. 0 , 发明名称为 "用于气相沉积工艺的反应腔室" 的中 国专利申请的优先权, 其全部内容通过引用结合在本申请中。 技术领域 本发明涉及沉积设备, 特别涉及用于气相沉积工艺的反应腔室。  Reaction Chamber for Vapor Deposition Process This application claims priority to Chinese Patent Application entitled "Reaction Chamber for Vapor Deposition Process" submitted to the Chinese Patent Office on September 7, 2012, application number 201210330818. The entire contents of which are incorporated herein by reference. TECHNICAL FIELD The present invention relates to deposition apparatus, and more particularly to a reaction chamber for a vapor deposition process.
背景技术 金属有机化学气相沉积( M0CVD )是在气相外延生长(VPE)的基础 上发展起来的一种化学气相沉积工艺。 它以 III族、 II族元素的有机化 合物和 V、 VI族元素的氢化物等作为晶体生长的反应气体, 以热分解 反应方式在蓝宝石处女地或其他村底上进行外延沉积工艺,生长各种BACKGROUND OF THE INVENTION Metal organic chemical vapor deposition (M0CVD) is a chemical vapor deposition process developed on the basis of vapor phase epitaxy (VPE). It uses organic compounds of Group III and II elements and hydrides of Group V and VI elements as reaction gases for crystal growth, and performs epitaxial deposition processes on sapphire virgin land or other villages by thermal decomposition reaction.
III -V族、 II _ VI族化合物半导体以及它们的多元固溶体的外延材料层。 图 1为现有技术的 M0CVD设备的反应腔室的结构示意图。所述反应腔 室包括: 托盘 10 , 具有上表面 11和与上表面 11相对的下表面 12 , 所述上表面 11用于放置村底, 所述下表面 12形成一凹槽; 气体供给 装置 30 , 位于所述托盘 10 的上表面的上方, 所述气体供给装置 30 用于向村底提供反应气体; 腔室侧壁 20 , 环绕所述托盘 10—周, 所 述腔室侧壁 20与托盘 1 0边缘之间构成排气通道,反应后的气体自所 述排气通道流向反应腔室的外部; 腔室顶盖 40 , 位于所述腔室侧壁 20和气体供给装置 30的上方, 腔室顶盖 40与腔室侧壁 20限定了反 应腔室的空间, 并且实现了反应腔室与外部的隔离; 加热单元 50 , 位于托盘 1 0的下表面的凹槽下方, 所述加热单元 50通过对托盘 1 0 进行加热; 支撑旋转结构 60 , 与所述下表面 12相连接, 所述支撑旋 转结构 60用于支撑托盘 1 0并且带动托盘 10进行转动。 Epitaxial material layers of III-V, II_VI compound semiconductors and their multiple solid solutions. BRIEF DESCRIPTION OF THE DRAWINGS Figure 1 is a schematic view showing the structure of a reaction chamber of a prior art M0CVD apparatus. The reaction chamber includes: a tray 10 having an upper surface 11 and a lower surface 12 opposite to the upper surface 11, the upper surface 11 for placing a substrate, the lower surface 12 forming a groove; the gas supply device 30 Located above the upper surface of the tray 10, the gas supply device 30 is configured to supply a reaction gas to the substrate; the chamber sidewall 20 surrounds the tray 10-week, the chamber sidewall 20 and the tray An exhaust passage is formed between the edges of the 10, and the reacted gas flows from the exhaust passage to the outside of the reaction chamber; a chamber cover 40 is located above the chamber sidewall 20 and the gas supply device 30, the cavity The chamber top cover 40 and the chamber side wall 20 define a space for the reaction chamber, and the reaction chamber is isolated from the outside; the heating unit 50 is located below the recess of the lower surface of the tray 10, and the heating unit 50 By heating the tray 10; supporting the rotating structure 60, connected to the lower surface 12, the supporting rotating structure 60 is used to support the tray 10 and drive the tray 10 to rotate.
继续参考图 1 , 气体自气体提供装置 30流向所述上表面 11 , 并 且在所述上表面 11的村底上发生反应, 反应后的气体沿腔室侧壁 20 与托盘 10之间的排气通道排出反应腔室的外部。 在实际中,发现利用现有的反应腔室在村底上形成的外延材料层 的均匀性需要进一步提高,尤其是托盘边缘处的村底上形成的外延材 料层的均匀性需要加以改善。 With continued reference to FIG. 1, gas flows from the gas supply device 30 to the upper surface 11, and a reaction occurs on the bottom of the upper surface 11, and the reacted gas is exhausted between the chamber sidewall 20 and the tray 10. The channel exits the exterior of the reaction chamber. In practice, it has been found that the uniformity of the layer of epitaxial material formed on the substrate by the existing reaction chamber needs to be further improved, especially the uniformity of the layer of epitaxial material formed on the substrate at the edge of the tray needs to be improved.
发明内容 本发明实施例解决的技术问题是提供了一种用于气相沉积工艺 的反应腔室, 提高了反应腔室中的托盘上尤其是托盘边缘处的气流 场、 温度场或浓度场的均匀性, 提高了村底上形成的外延材料层的均 匀性。 SUMMARY OF THE INVENTION The technical problem to be solved by embodiments of the present invention is to provide a reaction chamber for a vapor deposition process, which improves the uniformity of the airflow field, temperature field or concentration field on the tray in the reaction chamber, especially at the edge of the tray. Sexuality improves the uniformity of the layer of epitaxial material formed on the village floor.
为了解决上述问题,本发明实施例提供一种用于气相沉积工艺的 反应腔室, 包括: 托盘, 其上表面用于放置村底; 腔室侧壁, 环绕所 述托盘一周, 还包括: 构件, 至少有一部分环绕所述托盘的边缘, 所 述构件用于改进托盘的边缘的气流场、 温度场或浓度场的均匀性。  In order to solve the above problems, an embodiment of the present invention provides a reaction chamber for a vapor deposition process, including: a tray having an upper surface for placing a substrate; a chamber sidewall surrounding the tray for one week, further comprising: a member At least a portion of the edge of the tray is used to improve the uniformity of the airflow field, temperature field, or concentration field at the edge of the tray.
可选地, 所述托盘具有与上表面相对的下表面, 所述构件沿所述 上表面向下表面方向的厚度逐渐减小。  Optionally, the tray has a lower surface opposite the upper surface, and the thickness of the member in the direction of the lower surface of the upper surface gradually decreases.
可选地, 所述构件与托盘之间构成排气通道, 所述构件具有朝向 所述托盘的一侧的侧表面, 所述构件的侧表面为平滑过渡。  Optionally, an exhaust passage is formed between the member and the tray, the member having a side surface facing one side of the tray, and a side surface of the member is a smooth transition.
可选地, 所述构件的侧表面为内 的弧面。  Optionally, the side surface of the member is an inner curved surface.
可选地, 所述构件与托盘之间构成排气通道, 所述构件具有朝向 托盘的一侧的侧表面, 所述侧表面为内 的弧面。  Optionally, an exhaust passage is formed between the member and the tray, the member having a side surface facing one side of the tray, the side surface being an inner curved surface.
可选地, 所述侧表面延伸到所述上表面所在平面的上方。  Optionally, the side surface extends above a plane in which the upper surface lies.
可选地, 所述构件与腔室侧壁之间构成排气通道, 所述构件具有 朝向腔室侧壁一侧的侧表面, 所述侧表面为外凸的弧面。  Optionally, an air passage is formed between the member and the side wall of the chamber, and the member has a side surface facing one side of the side wall of the chamber, and the side surface is a convex curved surface.
可选地, 所述侧表面不超过托盘的上表面。  Optionally, the side surface does not exceed the upper surface of the tray.
可选地, 所述托盘具有与上表面相对的下表面, 所述侧表面延伸 到所述下表面所在平面的下方。  Optionally, the tray has a lower surface opposite the upper surface, the side surface extending below the plane of the lower surface.
可选地, 所述托盘的上表面的边缘与托盘的侧面之间为弧面过 渡。  Optionally, a curved transition is made between the edge of the upper surface of the tray and the side of the tray.
可选地, 所述构件具有朝向托盘一侧的侧表面, 所述构件的侧表 面对光线的反射率不小于腔室侧壁对光线的反射率。 Optionally, the member has a side surface facing one side of the tray, a side view of the member The reflectivity of the facing light is not less than the reflectivity of the sidewall of the chamber to the light.
可选地, 所述构件具有朝向托盘一侧的侧表面, 所述构件的侧表 面对光线的反射率不小于托盘的边缘对光线的反射率。  Optionally, the member has a side surface facing one side of the tray, and the side surface of the member faces the light having a reflectance not less than the reflectance of the edge of the tray to the light.
可选地, 所述构件的侧表面的粗糙度不超过 0. 008 米, 以便所 述构件的侧表面形成镜面, 对光线的反射为镜面反射。  Optionally, the side surface of the member has a roughness of not more than 0.08 m, so that the side surface of the member forms a mirror surface, and the reflection of the light is specular reflection.
可选地, 所述构件的侧表面具有耐热反射层, 所述耐热反射层在 气相沉积工艺过程中保持稳定状态。  Optionally, the side surface of the member has a heat resistant reflective layer that remains stable during the vapor deposition process.
可选地, 所述耐热反射层的材料为碳化硅。  Optionally, the material of the heat resistant reflective layer is silicon carbide.
可选地, 所述构件沿平行于托盘的上表面的方向的截面为环形。 可选地, 所述构件由两个以上的子构件相连接构成。  Optionally, the member is annular in cross section in a direction parallel to the upper surface of the tray. Optionally, the member is constructed by connecting two or more sub-members.
可选地, 所述构件为一圓环体。  Optionally, the member is a torus.
可选地, 所述构件中嵌入有隔热结构, 所述隔热结构用于减少托 盘的边缘向腔室侧壁的热量散失。  Optionally, a heat insulating structure is embedded in the member for reducing heat loss from the edge of the tray to the side wall of the chamber.
可选地,所述隔热结构的朝向所述托盘一侧的侧表面为向内 的 弧形。  Optionally, a side surface of the heat insulating structure facing one side of the tray is an inward arc.
可选地, 所述隔热结构包括隔热气体容纳层和隔热气体, 所述隔 热气体容纳层嵌入所述构件中,所述隔热气体容纳层在所述构件中限 定出空间, 所述空间用于容纳所述隔热气体, 所述隔热气体的导热系 数低于所述构件的导热系数。  Optionally, the heat insulating structure includes an insulating gas containing layer embedded in the member, and a heat insulating gas containing layer defining a space in the member. The space is for accommodating the heat insulating gas, and the heat insulating coefficient of the heat insulating gas is lower than a thermal conductivity of the member.
可选地,所述隔热气体容纳层的朝向托盘的一侧的侧面的形状为 内凹的孤面。  Optionally, the shape of the side of the insulating gas containing layer facing the side of the tray is a concave orphan.
可选地, 所述隔热结构为嵌入所述构件中的隔热块, 所述隔热块 的导热系数低于所述构件的导热系数。  Optionally, the heat insulating structure is a heat insulating block embedded in the member, and the heat insulating block has a thermal conductivity lower than a thermal conductivity of the member.
可选地,还包括: 气体供给装置,位于所述托盘的上表面的上方, 所述气体供给装置用于向所述村底提供反应气体,所述构件的一端固 定于气体供给装置上。  Optionally, the method further includes: a gas supply device located above the upper surface of the tray, the gas supply device for supplying a reaction gas to the substrate, one end of the member being fixed to the gas supply device.
可选地, 还包括: 腔室顶盖, 位于所述托盘的上表面的上方, 所 述构件的一端固定于所述腔室顶盖上。 可选地, 所述构件固定于腔室侧壁上。 Optionally, the method further includes: a chamber top cover located above the upper surface of the tray, and one end of the member is fixed to the chamber top cover. Optionally, the member is fixed to the side wall of the chamber.
可选地, 所述构件与腔室侧壁之间具有间隙。  Optionally, there is a gap between the member and the sidewall of the chamber.
可选地, 所述构件与托盘之间具有间隙。  Optionally, there is a gap between the member and the tray.
与现有技术相比, 本发明实施例具有以下优点:  Compared with the prior art, the embodiment of the invention has the following advantages:
本发明实施例提供的反应腔室, 在托盘的边缘具有构件, 所述构 件改善了托盘边缘的气流场、 温度场或浓度场的均匀性;  The reaction chamber provided by the embodiment of the invention has a member at the edge of the tray, and the member improves the uniformity of the airflow field, the temperature field or the concentration field at the edge of the tray;
进一步优化地, 所述构件用于托盘与腔室侧壁之间的隔热, 有效 减少了托盘边缘向腔室侧壁的热量的散失, 提高了对托盘加热的效 率, 并且所述构件沿托盘的上表面到托盘的下表面的厚度逐渐减小, 补偿了托盘的下表面到托盘的上表面温度逐渐降低造成的托盘边缘 温度不均匀的问题, 更好地起到了在托盘与腔室侧壁之间的隔热、 屏 蔽和保温的效果,从而改善了托盘的边缘以及整个托盘的上表面的温 度场的均匀性;  Further optimized, the member is used for heat insulation between the tray and the side wall of the chamber, effectively reducing the loss of heat from the edge of the tray to the side wall of the chamber, improving the efficiency of heating the tray, and the member along the tray The thickness of the upper surface to the lower surface of the tray is gradually reduced, which compensates for the problem that the temperature of the edge of the tray is uneven due to the gradual decrease of the temperature of the lower surface of the tray to the upper surface of the tray, and better plays the side wall of the tray and the chamber The effect of insulation, shielding and insulation between them improves the uniformity of the temperature field of the edge of the tray and the upper surface of the entire tray;
进一步优化地, 所述构件还可以与托盘之间构成排气通道, 所述 构件朝向托盘一侧的侧表面可以为包括内 的弧面在内的平滑过渡, 使得反应后的气体自托盘的上表面流向托盘的边缘时,在平滑过渡处 的气体滞留现象减少或消除, 从而使在托盘边缘处的气流场更为均 匀, 由于温度场和气流场也影响了托盘边缘处的反应气体的浓度场, 从而托盘边缘处的反应气体的浓度分布均勾性也得到改善,提高了托 盘边缘处的村底上形成的外延材料层的均匀性;  Further optimized, the member may also form an exhaust passage with the tray, and the side surface of the member facing the tray may be a smooth transition including the inner curved surface, so that the reacted gas is from the tray When the surface flows to the edge of the tray, the gas retention at the smooth transition is reduced or eliminated, thereby making the airflow field at the edge of the tray more uniform, since the temperature field and the airflow field also affect the concentration field of the reactive gas at the edge of the tray. Therefore, the concentration distribution of the reaction gas at the edge of the tray is also improved, and the uniformity of the epitaxial material layer formed on the village bottom at the edge of the tray is improved;
进一步优化地, 所述构件与托盘之间也可以构成排气通道, 所述 构件具有朝向托盘一侧的侧表面, 该侧表面为内凹的弧面, 从而在托 盘边缘处的排气通道中处形成平滑过渡,该平滑过渡有利于减小或消 除托盘边缘处的气体死角空间,从而改善了托盘边缘处的气体场的均 勾性; 或 /和所述托盘与构件与腔室侧壁之间也可以构成排气通道, 所述构件具有朝向托盘一侧的侧表面, 该侧表面为外凸的弧面, 从而 在托盘边缘处的排气通道中形成平滑的过渡,该平滑过渡有利于减小 或消除了托盘边缘处的气体死角空间,从而改善了托盘边缘处的气体 场的均匀性; Further preferably, the member and the tray may also constitute an exhaust passage, the member having a side surface facing one side of the tray, the side surface being a concave curved surface so as to be in the exhaust passage at the edge of the tray Forming a smooth transition that facilitates reducing or eliminating the dead space of the gas at the edge of the tray, thereby improving the uniformity of the gas field at the edge of the tray; or/and the side walls of the tray and member and the chamber The exhaust passage may also be formed, the member having a side surface facing one side of the tray, the side surface being a convex curved surface, thereby forming a smooth transition in the exhaust passage at the edge of the tray, the smooth transition facilitating Reduces or eliminates gas dead space at the edge of the tray, improving gas at the edge of the tray Field uniformity;
进一步优化地,构件的侧表面延伸至托盘的上表面的上方或托盘 的下表面的下方, 从而进一步改善了托盘边缘处的气体场、 温度场和 浓度场的均匀性;  Further optimized, the side surface of the member extends above the upper surface of the tray or below the lower surface of the tray, thereby further improving the uniformity of the gas field, temperature field and concentration field at the edge of the tray;
进一步优化地,所述托盘上表面的边缘与托盘的侧面之间为弧面 过渡, 从而进一步改善了托盘边缘的气体场、 温度场和浓度场的均匀 性;  Further optimized, a curved transition between the edge of the upper surface of the tray and the side of the tray further improves the uniformity of the gas field, temperature field and concentration field at the edge of the tray;
进一步优化地, 所述构件具有朝向托盘一侧的侧表面, 所述构件 的侧表面对光线的反射率不小于腔室侧壁对光线的反射率,与腔室侧 壁与托盘之间不设置构件、部分来托盘的光线会被腔室侧壁吸收而造 成对托盘的加热效率低、 以及托盘边缘处的温度偏低相比, 构件朝向 托盘一侧的侧表面能够将来自托盘的光线反射,提高了光线的利用率 和对托盘的加热效率, 改善了托盘边缘处的温度场的均匀性;  Further preferably, the member has a side surface facing one side of the tray, and a side surface of the member has a reflectance to light of not less than a reflectance of the side wall of the chamber to the light, and is not disposed between the side wall of the chamber and the tray The light from the tray can be reflected by the side surface of the member toward the tray, as the light from the member, part of the tray is absorbed by the side wall of the chamber, resulting in low heating efficiency to the tray, and the temperature at the edge of the tray is low. Improved light utilization and heating efficiency of the tray, improving the uniformity of the temperature field at the edge of the tray;
进一步优化地,所述构件的朝向托盘一侧的侧表面对光线的反射 率不小于托盘的边缘对光线的反射率,从而所述侧表面可以将来自托 盘的边缘处的光线反射回托盘,进一步提高了托盘边缘处的光线的利 用率和托盘的加热效率, 改善了托盘边缘处的温度场的均匀性; 进一步优化地,所述构件的朝向托盘一侧的侧表面对光线的反射 为镜面反射, 从而所述托盘的边缘处的光线的大部分被反射, 从而在 托盘边缘处的光线的利用率和对托盘的加热效率更高,托盘边缘处的 温度场的均匀性更好;  Further preferably, the side surface of the member facing the tray has a reflectivity to light that is not less than the reflectance of the edge of the tray to the light such that the side surface can reflect light from the edge of the tray back to the tray, further The utilization of light at the edge of the tray and the heating efficiency of the tray are improved, and the uniformity of the temperature field at the edge of the tray is improved; further precisely, the side surface of the member facing the tray is specularly reflected by the light. Thereby, most of the light at the edge of the tray is reflected, so that the utilization of light at the edge of the tray and the heating efficiency of the tray are higher, and the uniformity of the temperature field at the edge of the tray is better;
进一步优化地,所述构件沿平行于托盘的上表面的方向的截面为 环形, 或者, 所述构件有两个以上的子构件连接而成或所述构件为一 圓环体, 或者所述构件可以与腔室侧壁、腔室顶盖或气体供给装置相 连接, 或者, 所述构件与托盘之间以及构件与腔室侧壁之间可以有间 隙, 从而可以对构件的结构、 形状、 尺寸和分布进行灵活的调整, 以 获得托盘边缘处的最佳的温度场、 浓度场和气流场;  Further preferably, the member has a ring shape in a section parallel to the direction of the upper surface of the tray, or the member has two or more sub-members connected or the member is a torus, or the member may Connected to the chamber side wall, the chamber top cover or the gas supply, or there may be a gap between the member and the tray and between the member and the chamber sidewall so that the structure, shape, size and The distribution is flexibly adjusted to obtain the optimum temperature, concentration, and airflow fields at the edge of the tray;
进一步优化地, 所述构件中形成有隔热结构, 使得构件能够更好 地将腔室侧壁与托盘的边缘实现隔离,减小托盘边缘向腔室侧壁的热 量散失,进一步提高托盘边缘处的温度场、气流场和浓度场的均匀性。 Further optimized, a heat insulating structure is formed in the member to make the member better The sidewall of the chamber is isolated from the edge of the tray to reduce the heat loss from the edge of the tray to the side wall of the chamber, further improving the uniformity of the temperature field, the airflow field and the concentration field at the edge of the tray.
附图说明 DRAWINGS
图 1为现有技术的 M0CVD设备的反应腔室的结构示意图; 图 2是本发明第一实施例的反应腔室的结构示意图;  1 is a schematic structural view of a reaction chamber of a prior art M0CVD apparatus; FIG. 2 is a schematic structural view of a reaction chamber according to a first embodiment of the present invention;
图 3图 2所示的反应腔室沿 AA线的剖面结构示意图;  Figure 3 is a schematic cross-sectional view of the reaction chamber along the AA line;
图 4是本发明第二实施例的构件结构示意图;  Figure 4 is a schematic structural view of a member of a second embodiment of the present invention;
图 5是本发明第三实施例的反应腔室的结构示意图;  Figure 5 is a schematic view showing the structure of a reaction chamber according to a third embodiment of the present invention;
图 6是本发明第四实施例的反应腔室的结构示意图;  Figure 6 is a schematic structural view of a reaction chamber according to a fourth embodiment of the present invention;
图 7是本发明第五实施例的反应腔室的结构示意图;  Figure 7 is a schematic structural view of a reaction chamber according to a fifth embodiment of the present invention;
图 8是本发明第六实施例的反应腔室的结构示意图;  Figure 8 is a schematic structural view of a reaction chamber of a sixth embodiment of the present invention;
图 9是本发明第一实施例的构件结构示意图;  Figure 9 is a schematic structural view of a member of a first embodiment of the present invention;
图 1 0是本发明第二实施例的构件结构示意图。  Figure 10 is a schematic view showing the structure of a member of a second embodiment of the present invention.
具体实施方式 detailed description
利用现有的反应腔室在村底上形成的外延材料层的均勾性需要 进一步提高,尤其是托盘边缘处的村底上形成的外延材料层的均匀性 需要加以改善。 经过研究发现, 托盘边缘处的温度场、 气流场和浓度 场的均匀性对现有的气相沉积工艺均匀性影响较大。现有技术忽略了 对托盘边缘处的结构的优化,这对村底上形成的外延材料层尤其是托 边缘无法充分利用, 随着托盘的尺寸越来越大, 托盘的边缘处的结构 对托盘边缘的温度场、 浓度长和气流场的均勾性的影响更加明显, 并 且托盘边缘无法利用的面积加大。通常大尺寸的托盘的加工制造困难 并且成本高, 托盘边缘的面积无法利用, 更加增加了用户的成本。 因 此, 需要对现有的反应腔室尤其是托盘边缘处进行结构的优化设计, 以改善整个托盘上的气流场、 温度场、 浓度场的均勾性和气相沉积工 艺的均匀性。  The uniformity of the layer of epitaxial material formed on the substrate by the existing reaction chamber needs to be further improved, especially the uniformity of the layer of epitaxial material formed on the substrate at the edge of the tray needs to be improved. It has been found that the uniformity of temperature field, airflow field and concentration field at the edge of the tray has a great influence on the uniformity of the existing vapor deposition process. The prior art neglects the optimization of the structure at the edge of the tray, which cannot fully utilize the layer of epitaxial material formed on the bottom of the village, especially the edge of the tray. As the size of the tray becomes larger, the structure at the edge of the tray is opposite to the tray. The influence of the temperature field at the edge, the concentration length, and the uniformity of the airflow field is more pronounced, and the area that cannot be utilized at the edge of the tray is increased. Generally, large-sized pallets are difficult to manufacture and costly, and the area of the edge of the tray cannot be utilized, which further increases the cost of the user. Therefore, it is necessary to optimize the structure of the existing reaction chamber, especially at the edge of the tray, to improve the airflow field, the temperature field, the uniformity of the concentration field and the uniformity of the vapor deposition process on the entire tray.
在对托盘边缘处进行设计之前,发明人对现有技术的托盘的温度 场、 浓度场和气流场进行了研究分析。 具体地, 请结合图 1所示, 在 进行气相沉积工艺 (比如是 M0CVD工艺 ) 时, 气体供给装置 30向托 盘 10的上表面 11上的村底提供反应气体, 托盘 10被其下方的加热 单元 50加热而处于高温状态(温度通常大于 500摄氏度 ), 气体供给 装置 30提供的反应气体通常由于冷却而处于低温状态 (温度通常低 于 200摄氏度 ),反应气体自气体供给装置 30流向村底表面进行化学 反应,反应后的气体经过托盘 10的边缘的两侧与腔室侧壁 20之间的 排气管道流出反应腔室。 在此过程中, 反应气体与托盘 10的上表面 11会有热交换, 在托盘 1 0的边缘处由于气体集中排出因而热交换更 为严重, 这使得托盘 10的边缘处的温度偏低, 造成了托盘 10的上表 面 11的温度场不均匀。 托盘 10的边缘处散热速度比托盘 10中部的 散热速度快, 也影响了托盘 1 0的边缘处的温度场的均匀性。 由于腔 室侧壁 20通常为冷却状态 (温度不超过 200摄氏度), 腔室侧壁 20 与托盘 10的边缘处的温度差也会使得两者之间存在热交换, 该热交 换一方面会降低托盘 10的边缘的温度,使得托盘 10边缘的温度分布 不均匀, 另一方面也会降低了加热单元 50对托盘 1 G的加热效率。 Before the design of the edge of the tray, the inventor compared the temperature of the prior art tray Field, concentration field and airflow field were studied and analyzed. Specifically, as shown in FIG. 1, when performing a vapor deposition process (such as a M0CVD process), the gas supply device 30 supplies a reaction gas to the substrate on the upper surface 11 of the tray 10, and the tray 10 is heated by the heating unit below it. 50 is heated to be in a high temperature state (temperature is usually greater than 500 degrees Celsius), the reaction gas supplied from the gas supply device 30 is usually in a low temperature state due to cooling (temperature is usually lower than 200 degrees Celsius), and the reaction gas flows from the gas supply device 30 to the bottom surface of the substrate. In the chemical reaction, the reacted gas flows out of the reaction chamber through an exhaust pipe between both sides of the edge of the tray 10 and the side wall 20 of the chamber. During this process, the reaction gas exchanges heat with the upper surface 11 of the tray 10, and the heat exchange is more severe at the edge of the tray 10 due to the concentrated discharge of the gas, which causes the temperature at the edge of the tray 10 to be low, resulting in The temperature field of the upper surface 11 of the tray 10 is not uniform. The heat dissipation rate at the edge of the tray 10 is faster than the heat dissipation rate in the middle of the tray 10, which also affects the uniformity of the temperature field at the edge of the tray 10. Since the chamber side wall 20 is generally in a cooled state (temperature does not exceed 200 degrees Celsius), the temperature difference between the chamber side wall 20 and the edge of the tray 10 also causes heat exchange between the two, which heat exchange is reduced on the one hand. The temperature of the edge of the tray 10 causes the temperature distribution at the edge of the tray 10 to be uneven, and on the other hand, the heating efficiency of the tray 1 G by the heating unit 50 is also lowered.
更重要的是, 发明人还发现, 由于加热单元 50放置在托盘 10的 下方, 这使得托盘 10的下表面至上表面的温度逐渐降低, 从而托盘 10的上表面 11的温度偏低, 在托盘 10的边缘处的温度降低更为明 显。 现有技术没有考虑托盘 10的上表面 1 1至下表面 12的方向上温 度变化, 这也造成了托盘 10的边缘的温度分布不均勾, 更加导致托 盘 1 0的上表面 11的边缘的温度场不均匀。  More importantly, the inventors have also found that since the heating unit 50 is placed under the tray 10, the temperature of the lower surface to the upper surface of the tray 10 is gradually lowered, so that the temperature of the upper surface 11 of the tray 10 is low, in the tray 10 The temperature drop at the edge is more pronounced. The prior art does not consider the temperature change in the direction from the upper surface 11 to the lower surface 12 of the tray 10, which also causes uneven temperature distribution of the edge of the tray 10, which further causes the temperature of the edge of the upper surface 11 of the tray 10. The field is uneven.
对与气流场而言, 在气体自托盘 10 的上表面 11 流向腔室侧壁 20与托盘 10之间形成的排气通道的过程中, 气体的方向会沿上表面 1 1的水平方向转为竖直方向, 在气体供给装置 30、托盘 10的边缘以 及腔室侧壁 20之间的拐角处会形成气体死角,部分气体会滞留至此, 这不仅会影响沉积工艺过程 (比如 M0CVD )反应过程中不同的反应气 体的切换, 甚至会引起气体的回流, 该拐角处的气体死角也容易造成 托盘 10边缘处的气体的涡旋 ,造成托盘 10的边缘处的气流场不均匀。 由于沉积工艺特别是 M0CVD 工艺的温度场和气流场以及浓度场 会相互影响, 当托盘 10的边缘处的温度场和气流场不均匀的情况下, 托盘 1 Q的边缘处的浓度场的均勾性也无法保持均勾, 最终造成托盘 10边缘处的村底上形成的外延材料层的均勾性不够理想。 For the airflow field, during the flow of gas from the upper surface 11 of the tray 10 to the exhaust passage formed between the chamber side wall 20 and the tray 10, the direction of the gas is changed along the horizontal direction of the upper surface 1 1 to In the vertical direction, a gas dead angle is formed at the corner between the gas supply device 30, the edge of the tray 10, and the side wall 20 of the chamber, and some of the gas will stay there, which will not only affect the deposition process (such as M0CVD) reaction process. The switching of different reaction gases may even cause a backflow of gas, and the dead angle of the gas at the corners is also liable to cause vortexing of the gas at the edge of the tray 10, resulting in uneven airflow at the edge of the tray 10. Since the temperature field and the airflow field and the concentration field of the deposition process, particularly the M0CVD process, interact with each other, when the temperature field and the airflow field at the edge of the tray 10 are not uniform, the concentration field at the edge of the tray 1 Q is hooked. Sexuality cannot be maintained, and eventually the uniformity of the layer of epitaxial material formed on the bottom of the substrate at the edge of the tray 10 is not ideal.
本发明正是将托盘的边缘作为改善的重点,对反应腔室的内部结 构进行优化, 主要是对托盘的边缘进行改善, 从而改善托盘边缘处的 温度场、 浓度场、 气流场的均匀性。 在优化的过程中结合现有托盘结 构存在的问题进行优化,上述问题包括托盘的下表面到上表面的温度 的变化、 托盘边缘的散热、 托盘与腔室侧壁之间的热交换、 托盘与气 体之间的热交换等问题。  The present invention optimizes the internal structure of the reaction chamber by optimizing the edge of the tray, mainly to improve the edge of the tray, thereby improving the temperature field, the concentration field, and the uniformity of the airflow field at the edge of the tray. Optimized in conjunction with problems with existing pallet structures, including changes in temperature from the lower surface to the upper surface of the tray, heat dissipation at the edge of the tray, heat exchange between the tray and the sidewall of the chamber, and tray and Problems such as heat exchange between gases.
具体地, 本发明提出的用于沉积工艺的反应腔室包括: 托盘, 其 上表面用于放置村底; 腔室侧壁, 环绕所述托盘一周,还包括: 构件, 至少有一部分环绕所述托盘的边缘,所述构件用于改进托盘的边缘的 气流场、 温度场或浓度场的均匀性。 通过在托盘的边缘设置构件, 对 构件的形状、 结构、构造、 分布、布局、材质等进行优化选择和布局, 改善现有托盘边缘的温度场、 浓度场或气流场分布的均匀性。  Specifically, the reaction chamber for a deposition process proposed by the present invention includes: a tray having an upper surface for placing a substrate; a chamber sidewall surrounding the tray, further comprising: a member, at least a portion surrounding the The edge of the tray is used to improve the uniformity of the airflow field, temperature field or concentration field at the edge of the tray. By setting the components at the edge of the tray, the shape, structure, structure, distribution, layout, material, etc. of the components are optimally selected and laid out to improve the uniformity of temperature field, concentration field or airflow field distribution at the edge of the existing tray.
下面结合具体的实施例对本发明的技术方案进行详细的说明。首 先, 请参考图 2 , 图 2为本发明第一实施例的反应腔室的内部结构示 意图。作为一个实施例, 所述反应腔室为化学气相沉积设备的反应腔 室。本实施例中,所述反应腔室为 M0CVD设备的反应腔室,用于 M0CVD 工艺。 所述反应腔室具有腔室侧壁 200。 作为一个实施例, 所述腔室 侧壁 200具有与之对应的腔室侧壁冷却单元(图中未示出)。 所述腔 室侧壁冷却单元用于对所述腔室侧壁 200进行冷却,使得所述腔室侧 壁 200的温度不超过 800摄氏度, 优选地, 所述腔室侧壁 200的温度 不超过 200摄氏度。 在本发明的一个实施例中, 所述腔室侧壁 200的 温度不超过 100摄氏度。 所述腔室侧壁 200 的上方设置有腔室顶盖 400。 腔室顶盖 400与腔室侧壁 200限定了反应腔室的空间, 并且实 现了反应腔室与外部的隔离。  The technical solution of the present invention will be described in detail below with reference to specific embodiments. First, please refer to Fig. 2, which is a schematic view showing the internal structure of a reaction chamber according to a first embodiment of the present invention. As an embodiment, the reaction chamber is a reaction chamber of a chemical vapor deposition apparatus. In this embodiment, the reaction chamber is a reaction chamber of a M0CVD apparatus for the M0CVD process. The reaction chamber has a chamber sidewall 200. As an embodiment, the chamber sidewall 200 has a chamber sidewall cooling unit (not shown) corresponding thereto. The chamber sidewall cooling unit is configured to cool the chamber sidewall 200 such that the temperature of the chamber sidewall 200 does not exceed 800 degrees Celsius, preferably, the temperature of the chamber sidewall 200 does not exceed 200 degrees Celsius. In one embodiment of the invention, the chamber sidewall 200 temperature does not exceed 100 degrees Celsius. A chamber top cover 400 is disposed above the chamber sidewall 200. The chamber top cover 400 and the chamber side wall 200 define the space of the reaction chamber and provide isolation of the reaction chamber from the exterior.
作为一个实施例,所述腔室顶盖 400下方具有气体供给装置 300。 所述气体供给装置 300可以为喷淋头。 本实施例中, 所述气体供给装 置 300为近距离耦合喷淋头 (C lose Coup l e Showerhead , CCS ), 其 能够将反应气体垂直地向下方喷射。 As an embodiment, a gas supply device 300 is provided below the chamber top cover 400. The gas supply device 300 may be a shower head. In the present embodiment, the gas supply device 300 is a close-coupled shower head (CCS) capable of vertically injecting a reaction gas downward.
所述反应腔室内部设置有托盘 100。 作为一个实施例, 所述托盘 100的材质为石墨。 在本发明的优选实施例中, 所述托盘 100的表面 可以涂覆或镀碳化硅涂层(图中未示出), 碳化硅涂层具有良好的稳 定性。 具体地, 在进行 M0CVD工艺时, 碳化硅涂层不会与反应气体发 生反应, 并且碳化硅涂层结构致密, 能够防止气体与石墨反应而损伤 托盘 10或产生颗粒而影响工艺良率, 并且碳化硅涂层的热膨胀系数 与石墨相当, 在高温下不会从石墨上脱落, 影响工艺的良率。  A tray 100 is disposed inside the reaction chamber. As an embodiment, the material of the tray 100 is graphite. In a preferred embodiment of the invention, the surface of the tray 100 may be coated or plated with a silicon carbide coating (not shown), and the silicon carbide coating has good stability. Specifically, in the M0CVD process, the silicon carbide coating does not react with the reaction gas, and the silicon carbide coating structure is dense, preventing the gas from reacting with the graphite to damage the tray 10 or generating particles, affecting the process yield, and carbonizing. The coefficient of thermal expansion of the silicon coating is comparable to that of graphite, and does not fall off the graphite at high temperatures, affecting the yield of the process.
所述托盘 100具有上表面 101和与上表面 101相对的下表面 102。 所述上表面 101为托盘 1 00的朝向腔室顶盖 400和气体供给装置 300 一侧的表面, 所述上表面 101用于放置村底。 作为优选的实施例, 所 述上表面 101的边缘与托盘 100的侧面之间为弧面过渡, 这样, 来自 气体供给装置 300的反应气体在垂直流向所述上表面 101后,经过该 弧面过渡后平緩地转为竖直方向,防止托盘 100的边缘处的气流方向 突变, 可以改善托盘 100的边缘的气流场的均匀性。  The tray 100 has an upper surface 101 and a lower surface 102 opposite the upper surface 101. The upper surface 101 is the surface of the tray 100 facing the chamber top cover 400 and the gas supply device 300, and the upper surface 101 is for placing the substrate. As a preferred embodiment, the edge of the upper surface 101 and the side surface of the tray 100 are arcuately transitioned, such that the reaction gas from the gas supply device 300 passes through the arc surface after flowing vertically to the upper surface 101. After the smooth transition to the vertical direction, the direction of the airflow at the edge of the tray 100 is prevented from being abrupt, and the uniformity of the airflow field at the edge of the tray 100 can be improved.
继续参考图 2 , 托盘 1 00的下表面 102与旋转支撑机构 600相连 接, 该旋转支撑结构 600呈中空的圓筒状, 所述旋转支撑机构 600用 于支撑托盘 100。 作为可选的实施例, 旋转支撑机构 600还用于带动 托盘 100以一定的速度转动。  With continued reference to FIG. 2, the lower surface 102 of the tray 100 is coupled to a rotary support mechanism 600 having a hollow cylindrical shape, and the rotary support mechanism 600 is used to support the tray 100. As an alternative embodiment, the rotary support mechanism 600 is also used to drive the tray 100 to rotate at a certain speed.
所述托盘 100的下方设置有加热单元 500。 作为一个实施例, 所 述加热单元 500位于旋转支撑结构 600内,这样可以节约整个腔室的 空间。 为了加热单元 500能够更好的对上表面 101进行加热, 作为可 选的实施例, 可以在加热单元 500正对的托盘 100部分形成凹槽, 这 样有利于提高加热单元 500对托盘加热的效率。  A heating unit 500 is disposed below the tray 100. As an embodiment, the heating unit 500 is located within the rotating support structure 600, which saves space throughout the chamber. In order that the heating unit 500 can better heat the upper surface 101, as an alternative embodiment, a groove can be formed in the portion of the tray 100 facing the heating unit 500, which is advantageous in improving the efficiency of heating the heating unit 500 to the tray.
作为一个实施例, 构件 700环绕托盘 100的边缘。作为可选的实 施例, 所述构件 700环绕所述托盘 100的边缘一周。  As an embodiment, member 700 surrounds the edge of tray 100. As an alternative embodiment, the member 700 wraps around the edge of the tray 100.
作为可选的实施例,构件 700固定于气体供给装置 300的边缘与 腔室顶壁 400上。 在其他的实施例中, 构件 700还可以仅固定于气体 供给装置 300的边缘或腔室顶壁 400上,甚至所述构件 700可以通过 单独的支撑结构支撑于反应腔室内。 As an alternative embodiment, member 700 is affixed to the edge of gas supply 300 On the chamber top wall 400. In other embodiments, the member 700 can also be secured only to the edge of the gas supply device 300 or to the chamber top wall 400, even though the member 700 can be supported within the reaction chamber by a separate support structure.
本实施例中, 所述构件 700与托盘 100之间构成排气通道。反应 后的气体通过托盘 100的边缘 100和构件 700排出反应腔室。所述构 件 700具有朝向托盘一侧的侧表面 (未标出), 所述侧表面为内凹的 弧面, 从而在托盘 100的边缘处形成平滑过渡, 减少或消除气体在托 盘 100 的边缘与构件 700之间的气体的死角空间, 减少或消除托盘 100的边缘处气体滞留、 气体涡旋等问题, 提高托盘 100的边缘的气 流场的均匀性。 作为优选的实施例, 所述构件 700的朝向托盘 100— 侧的侧表面延伸至托盘 100的上表面 101所在平面的上方,这样可以 改善托盘 100边缘的气流场、 温度场和浓度场的均匀性。  In this embodiment, the member 700 and the tray 100 constitute an exhaust passage. The reacted gas exits the reaction chamber through the edge 100 of the tray 100 and the member 700. The member 700 has a side surface (not shown) facing one side of the tray, the side surface being a concave curved surface to form a smooth transition at the edge of the tray 100, reducing or eliminating gas at the edge of the tray 100 The dead space of the gas between the members 700 reduces or eliminates problems such as gas retention at the edges of the tray 100, gas vortexing, etc., and improves the uniformity of the airflow field at the edge of the tray 100. As a preferred embodiment, the side surface of the member 700 facing the tray 100-side extends above the plane of the upper surface 101 of the tray 100, which improves the uniformity of the airflow field, temperature field and concentration field at the edge of the tray 100. .
作为优选的实施例, 所述侧表面还延伸至托盘 100的下表面 102 所在的平面的下方, 这样可以改善托盘 100边缘的气流场、 温度场和 浓度场的均匀性。  As a preferred embodiment, the side surfaces also extend below the plane in which the lower surface 102 of the tray 100 is located, which improves the uniformity of the airflow field, temperature field, and concentration field at the edge of the tray 100.
构件 700朝向托盘 100的侧表面作为排气通道的一部分,可以更 好的引导气流,实现气体从托盘 100的上表面 101的平滑地沿排气通 道流动。作为本发明优选实施例, 由于对构件 700的结构进行了优化 设置, 所述构件 700还用于托盘 100与腔室侧壁 200之间的隔热, 减 少托盘 100的边缘与腔室侧壁 200的热量散失,提高加热单元 500对 托盘 100加热的效率。  The member 700 faces a side surface of the tray 100 as a part of the exhaust passage, and the air flow can be better guided to smoothly flow the gas from the upper surface 101 of the tray 100 along the exhaust passage. As a preferred embodiment of the present invention, the member 700 is also used for thermal insulation between the tray 100 and the chamber sidewall 200 due to the optimized configuration of the member 700, reducing the edge of the tray 100 and the chamber sidewall 200. The heat is lost, improving the efficiency with which the heating unit 500 heats the tray 100.
作为可选的实施例,所述构件 700的朝向托盘 100—侧的侧表面 对光线的反射率不小于腔室侧壁 200对光线的反射率,从而所述侧表 面可以将来自托盘 100的边缘处的光线反射回托盘 101 , 进一步提高 了托盘 101的边缘处的光线的利用率和托盘 101的加热效率,改善了 托盘 101边缘处的温度场的均匀性。  As an alternative embodiment, the side surface of the member 700 facing the tray 100-side has a reflectivity to light that is not less than the reflectivity of the chamber sidewall 200 to light, such that the side surface can be from the edge of the tray 100. The light at the place is reflected back to the tray 101, which further improves the utilization of light at the edge of the tray 101 and the heating efficiency of the tray 101, improving the uniformity of the temperature field at the edge of the tray 101.
在本发明的优选实施例中, 通过对所述侧表面的材料、粗糙度的 选择,所述侧表面对光线的反射率应不小于托盘 100的边缘对光线的 反射率,从而所述侧表面可以将来自托盘 100的边缘处的光线反射回 托盘 100 , 进一步提高了托盘 100边缘处的光线的利用率和加热单元 500对托盘 101的加热效率, 改善了托盘 100边缘处的温度场的均匀 性。 In a preferred embodiment of the present invention, by selecting the material and roughness of the side surface, the reflectance of the side surface to the light should be not less than the reflectance of the edge of the tray 100 to the light, so that the side surface Light from the edge of the tray 100 can be reflected back The tray 100 further improves the utilization of light at the edges of the tray 100 and the heating efficiency of the heating unit 500 to the tray 101, improving the uniformity of the temperature field at the edge of the tray 100.
本实施例中, 所述侧表面的粗糙度不超过 0. 008 米, 以便所述 侧表面形成镜面, 对光线的反射为镜面反射。  In this embodiment, the roughness of the side surface does not exceed 008 meters, so that the side surface forms a mirror surface, and the reflection of the light is specular reflection.
作为可选的实施例, 所述构件 700的材质为石墨或石英。 所述构 件 700 的朝向托盘 101 —侧的侧表面上还设置有耐热反射层(未示 出), 所述耐热反射层保护石墨或石英, 并且耐热反射层在沉积工艺 过程保持稳定状态,一方面所述耐热反射层不会从构件 700的石墨或 石英上脱落,另一方面所述耐热反射层不与反应腔室中的气体发生反 应。 本实施例中, 所述耐热反射层的材质为碳化硅。 当然, 在其他的 实施例中, 在不考虑制造成本和加工难度的情况下, 所述构件 700也 可以利用碳化硅制作。  As an alternative embodiment, the member 700 is made of graphite or quartz. A heat-resistant reflective layer (not shown) is further disposed on a side surface of the member 700 facing the tray 101, the heat-resistant reflective layer protects graphite or quartz, and the heat-resistant reflective layer remains stable during the deposition process. On the one hand, the heat-resistant reflective layer does not fall off from the graphite or quartz of the member 700, and on the other hand, the heat-resistant reflective layer does not react with the gas in the reaction chamber. In this embodiment, the material of the heat resistant reflective layer is silicon carbide. Of course, in other embodiments, the member 700 can also be fabricated using silicon carbide regardless of manufacturing cost and processing difficulty.
请继续参考图 2 , 作为可选的实施例, 所述构件 700沿托盘 100 的上表面 101至下表面 102方向的厚度逐渐减小, 如图 2所示, 沿所 述上表面 101至下表面 102的方向上, 构件 700的厚度由 T1逐渐减 小为 T2。 构件 700沿上表面 101至下表面 102的厚度减小, 这样构 件 700能够补偿托盘 100的下表面 102到托盘 100的上表面 101的温 度逐渐降低给托盘 100边缘造成的温度不均匀的问题,更好地起到了 在托盘与腔室侧壁之间的隔热、屏蔽和保温的效果, 从而改善了托盘 100的边缘以及整个托盘 100的上表面 101的温度场的均匀性。  With continued reference to FIG. 2, as an alternative embodiment, the thickness of the member 700 in the direction from the upper surface 101 to the lower surface 102 of the tray 100 is gradually reduced, as shown in FIG. 2, along the upper surface 101 to the lower surface. In the direction of 102, the thickness of member 700 is gradually reduced from T1 to T2. The thickness of the member 700 along the upper surface 101 to the lower surface 102 is reduced, so that the member 700 can compensate for the problem that the temperature of the lower surface 102 of the tray 100 to the upper surface 101 of the tray 100 gradually decreases to the temperature unevenness caused to the edge of the tray 100, and The effect of heat insulation, shielding and heat retention between the tray and the side walls of the chamber is well achieved, thereby improving the uniformity of the temperature field of the edge of the tray 100 and the upper surface 101 of the entire tray 100.
下面请参考图 3 , 图 3为图 2沿 ΑΑ的剖面结构示意图。 所述构 件 700环绕所述托盘 100—周, 所述腔室侧壁 200环绕所述构件 700 一周。 本实施例中, 所述构件 700为一圓环体, 这样对托盘 100的边 缘的隔热和保温效果以及对托盘 100边缘的气流的导流效果更好,从 而可以进一步改善托盘 100的边缘处的气流场、 温度场和浓度场。  Referring to Figure 3 below, Figure 3 is a schematic cross-sectional view of Figure 2 along the ΑΑ. The member 700 surrounds the tray 100-week, and the chamber sidewall 200 surrounds the member 700 for one week. In this embodiment, the member 700 is a toroidal body, so that the heat insulation and heat insulation effect on the edge of the tray 100 and the airflow effect on the airflow at the edge of the tray 100 are better, so that the edge of the tray 100 can be further improved. Airflow field, temperature field and concentration field.
下面请参考图 4 ,为本发明第二实施例的反应腔室的结构示意图。 与第一实施例相同的结构采用相同的标号表示。本实施例与前一实施 例基本相同, 区别在于, 所述构件 700固定于腔室侧壁 200上, 并且 构件 700内设置有隔热结构 710 , 使得构件 700能够更好地将腔室侧 壁 200与托盘 100的边缘实现隔离,减小托盘 100的边缘向腔室侧壁 200的热量散失, 进一步提高托盘 100的边缘处的温度场、 气流场和 浓度场的均匀性。 所述隔热结构 710可以为圓环体, 该圓环体设置于 构件 700的圓环体内。 4 is a schematic structural view of a reaction chamber according to a second embodiment of the present invention. The same structures as those of the first embodiment are denoted by the same reference numerals. This embodiment is substantially the same as the previous embodiment except that the member 700 is fixed to the chamber side wall 200, and The member 700 is provided with a heat insulating structure 710, so that the member 700 can better isolate the chamber sidewall 200 from the edge of the tray 100, reduce the heat loss from the edge of the tray 100 to the chamber sidewall 200, and further improve the tray. The uniformity of the temperature field, airflow field and concentration field at the edge of 100. The heat insulating structure 710 may be a torus provided in the annular body of the member 700.
作为本发明的一个的实施例, 所述隔热结构 710为隔热块, 所述 隔热块 710的导热系数低于构件 710的导热系数。作为本发明的又一 实施例, 所述隔热结构 710 还可以由隔热气体容纳层和隔热气体构 成, 所述隔热气体容纳层嵌入所述构件中, 所述隔热气体容纳层在所 述构件中限定出空间, 所述空间用于容纳所述隔热气体, 所述隔热气 体的导热系数低于所述构件的导热系数。  As an embodiment of the present invention, the heat insulating structure 710 is a heat insulating block, and the heat insulating block 710 has a thermal conductivity lower than that of the member 710. As still another embodiment of the present invention, the heat insulating structure 710 may further be composed of an insulating gas containing layer and a heat insulating gas, the heat insulating gas containing layer being embedded in the member, the heat insulating gas containing layer being A space is defined in the member for accommodating the heat insulating gas, and the heat insulating coefficient of the heat insulating gas is lower than a thermal conductivity of the member.
下面请参考图 5 , 图 5为本发明第三实施例的反应腔室的结构示 意图。 与第三实施例相同的结构采用相同的标号表示。 本实施例与第 二实施例基本相同, 区别在于, 所述构件 700内的隔热结构 710的朝 向所述托盘 100—侧的侧表面为向内凹的弧形,这样进一步优化托盘 100的边缘的气流场、 浓度场和温度场的均匀性。  Referring next to Figure 5, Figure 5 is a schematic illustration of the construction of a reaction chamber in accordance with a third embodiment of the present invention. The same structures as those of the third embodiment are denoted by the same reference numerals. This embodiment is basically the same as the second embodiment, except that the side surface of the heat insulating structure 710 in the member 700 facing the side of the tray 100 is inwardly concave, which further optimizes the edge of the tray 100. The uniformity of the airflow field, concentration field and temperature field.
下面请参考图 6 , 图 6为本发明第四实施例的反应腔室的结构示 意图。 与第一实施例相同的结构采用相同的标号表示。 本实施例与第 一实施例的区别在于, 构件 700 固定于腔室顶盖 400上, 所述构件 700位于托盘 100与腔室侧壁 200之间, 即构件 700与腔室侧壁 200 和托盘 100之间均有间隙, 构件 700与托盘 100之间形成排气通道。 所述构件 700的超向腔室侧壁 200—侧表面为外凸的弧面。  Referring next to Fig. 6, Fig. 6 is a schematic view showing the structure of a reaction chamber according to a fourth embodiment of the present invention. The same structures as those of the first embodiment are denoted by the same reference numerals. The present embodiment differs from the first embodiment in that the member 700 is fixed to the chamber top cover 400, and the member 700 is located between the tray 100 and the chamber side wall 200, that is, the member 700 and the chamber side wall 200 and the tray. There is a gap between the 100, and an exhaust passage is formed between the member 700 and the tray 100. The super-facing chamber side wall 200 of the member 700 has a convex curved surface.
下面请结合图 7所示的本发明第五实施例的托盘结构示意图。与 第一实施例相同的结构采用相同的标号表示。本实施例与第一实施例 的区别在于, 构件 700通过专门的支撑结构(图中未示出)支撑于托 盘 100边缘。 所述构件 700的朝向腔室顶盖 400—侧的表面与托盘 100的上表面 101齐平, 这样所述构件 700与腔室侧壁 200之间以及 构件 700与托盘 100之间分别构成排气通道。所述构件 700的朝向腔 室侧壁 200—侧的侧表面不超过所述托盘 100的上表面 101所在的平 面, 这样有利于提高托盘 100的边缘的气体场的均匀性。 Next, a schematic diagram of the structure of the tray of the fifth embodiment of the present invention shown in FIG. 7 will be described. The same structures as those of the first embodiment are denoted by the same reference numerals. The present embodiment differs from the first embodiment in that the member 700 is supported on the edge of the tray 100 by a special support structure (not shown). The surface of the member 700 facing the chamber top cover 400 is flush with the upper surface 101 of the tray 100, such that the member 700 and the chamber sidewall 200 and the member 700 and the tray 100 respectively form an exhaust gas. aisle. The side surface of the member 700 facing the side wall 200 side of the chamber does not exceed the level of the upper surface 101 of the tray 100. This helps to improve the uniformity of the gas field at the edge of the tray 100.
所述构件 700的朝向托盘 100的侧表面为向内 的弧面,所述构 件 700的朝向腔室侧壁的侧表面为外凸的弧面。通过调整构件 700的 朝向腔室侧壁 200的侧表面的弧度、半径和构件 700的朝向腔室侧壁 200的侧表面的弧度、半径,结合构件 700在腔室侧壁 200和托盘 100 之间的位置, 对托盘 101的边缘的气流场、 浓度场和温度场进行调整 和优化。 本实施例中, 构件 700的厚度沿托盘 100的上表面 101至下 表面 102方向的厚度逐渐减小, 以补偿托盘 100的边缘自下表面 102 到上表面 101的温度逐渐减小,实现对托盘 100的上表面 101边缘更 好的隔热。  The side surface of the member 700 facing the tray 100 is an inward curved surface, and the side surface of the member 700 facing the side wall of the chamber is a convex curved surface. The coupling member 700 is between the chamber sidewall 200 and the tray 100 by adjusting the curvature of the side surface of the member 700 facing the chamber sidewall 200, the radius, and the curvature, radius of the side surface of the member 700 facing the chamber sidewall 200. The position, the airflow field, the concentration field and the temperature field at the edge of the tray 101 are adjusted and optimized. In this embodiment, the thickness of the member 700 gradually decreases along the direction from the upper surface 101 to the lower surface 102 of the tray 100 to compensate for the gradual decrease in the temperature of the edge of the tray 100 from the lower surface 102 to the upper surface 101. The edge of the upper surface 101 of 100 is better insulated.
本实施例中,构件 700的远离腔室顶盖 400—侧的表面位于所述 托盘 100下表面 102所在平面的上方。 在其他的实施例中, 构件 700 的远离腔室顶盖 400—侧的表面还可以延伸至下表面 102所在平面的 下方。  In this embodiment, the surface of the member 700 remote from the chamber top cover 400 is located above the plane of the lower surface 102 of the tray 100. In other embodiments, the surface of the member 700 that is away from the chamber top cover 400 can also extend below the plane of the lower surface 102.
下面请参考图 8 所示的本发明第六实施例的反应腔室的结构示 意图。 与第一实施例相同的结构采用相同的标号表示。 本实施例与第 一实施例的区别在于, 所述构件 700与腔室顶盖 400相连接, 构件 700与腔室侧壁 200之间具有间隙, 构件 700的朝向腔室侧壁 200— 侧的侧表面与腔室侧壁 200平行,且所述构件 700的朝向托盘 100— 侧的侧表面为平面。该构件 700的沿托盘 100的上表面 101至下表面 102方向的厚度逐渐减小, 通过调整构件 700厚度减小的幅度, 可以 实现更好地构件 700对托盘 100的上表面 101至下表面 102的温度变 化的补偿, 实现将托盘 100的边缘与腔室侧壁 200之间的隔离, 进一 步改善托盘边缘的温度场、 气流场和浓度场的均匀性。  Referring next to the structural diagram of the reaction chamber of the sixth embodiment of the present invention shown in Fig. 8. The same structures as those of the first embodiment are denoted by the same reference numerals. The difference between this embodiment and the first embodiment is that the member 700 is connected to the chamber top cover 400, and the member 700 has a gap with the chamber side wall 200, and the member 700 faces the side wall 200 side of the chamber. The side surface is parallel to the chamber side wall 200, and the side surface of the member 700 facing the tray 100 side is a flat surface. The thickness of the member 700 in the direction from the upper surface 101 to the lower surface 102 of the tray 100 is gradually reduced, and by adjusting the thickness of the member 700 to be reduced, it is possible to achieve a better member 700 to the upper surface 101 to the lower surface 102 of the tray 100. The compensation of the temperature change achieves isolation between the edge of the tray 100 and the chamber sidewall 200, further improving the uniformity of the temperature field, airflow field and concentration field at the edge of the tray.
请参考图 9 ,为本发明第一实施例的构件 700的俯视结构示意图。 构件 700为环形, 托盘(未图示)放置于构件 700的环形内。 所述构 件 700包括相连接的多个子构件。各个子构件尺寸可以相同,或不同。 本实施例中, 所述构件 700包括 4个尺寸相同的子构件 701。  Please refer to FIG. 9, which is a top plan view of a member 700 according to a first embodiment of the present invention. Member 700 is annular and a tray (not shown) is placed within the annulus of member 700. The member 700 includes a plurality of sub-members that are connected. Each sub-component may be the same size or different. In this embodiment, the member 700 includes four sub-members 701 of the same size.
请参考图 10 , 图 10为本发明第二实施例的构件 700的结构示意 图。 所述构件 700包括多个子构件 701。 所述子构件 701之间具有间 隔, 各个子构件 701之间相互独立。 Please refer to FIG. 10, which is a schematic structural diagram of a member 700 according to a second embodiment of the present invention. Figure. The member 700 includes a plurality of sub-members 701. The sub-members 701 have a space therebetween, and the sub-members 701 are independent of each other.
综上, 本发明实施例提供的反应腔室, 在托盘的边缘具有构件, 所述构件改善了托盘边缘的气流场、 温度场或浓度场的均匀性; 进一步优化地, 所述构件用于托盘与腔室侧壁之间的隔热, 有效 减少了托盘边缘向腔室侧壁的热量的散失, 提高了对托盘加热的效 率, 并且所述构件沿托盘的上表面到托盘的下表面的厚度逐渐减小, 补偿了托盘的下表面到托盘的上表面温度逐渐降低造成的托盘边缘 温度不均匀的问题, 更好地起到了在托盘与腔室侧壁之间的隔热、 屏 蔽和保温的效果,从而改善了托盘的边缘以及整个托盘的上表面的温 度场的均勾性; 进一步优化地, 所述构件还可以与托盘之间构成排气 通道,所述构件朝向托盘一侧的侧表面可以为包括内 的弧面在内的 平滑过渡, 使得反应后的气体自托盘的上表面流向托盘的边缘时, 在 平滑过渡处的气体滞留现象减少或消除,从而使在托盘边缘处的气流 场更为均勾,由于温度场和气流场也影响了托盘边缘处的反应气体的 浓度场, 从而托盘边缘处的反应气体的浓度分布均匀性也得到改善, 提高了托盘边缘处的村底上形成的外延材料层的均匀性;  In summary, the reaction chamber provided by the embodiment of the present invention has a member at the edge of the tray, and the member improves the uniformity of the airflow field, the temperature field or the concentration field at the edge of the tray; further optimized, the member is used for the tray The heat insulation between the side wall of the chamber effectively reduces the loss of heat from the edge of the tray to the side wall of the chamber, improves the efficiency of heating the tray, and the thickness of the member along the upper surface of the tray to the lower surface of the tray Gradually reducing, compensating for the problem of uneven temperature of the edge of the tray caused by the gradual decrease of the temperature of the lower surface of the tray to the upper surface of the tray, better shielding, shielding and heat insulation between the tray and the side wall of the chamber The effect, thereby improving the uniformity of the temperature field of the edge of the tray and the upper surface of the entire tray; further optimally, the member may also form an exhaust passage with the tray, the member facing the side surface of the tray side It can be a smooth transition including the inner arc surface, so that the reacted gas flows smoothly from the upper surface of the tray to the edge of the tray. The gas retention phenomenon at the place is reduced or eliminated, so that the airflow field at the edge of the tray is more evenly hooked, because the temperature field and the airflow field also affect the concentration field of the reaction gas at the edge of the tray, so that the reaction gas at the edge of the tray The uniformity of the concentration distribution is also improved, and the uniformity of the epitaxial material layer formed on the bottom of the substrate at the edge of the tray is improved;
进一步优化地, 所述构件与托盘之间也可以构成排气通道, 所述 构件具有朝向托盘一侧的侧表面, 该侧表面为内凹的弧面, 从而在托 盘边缘处的排气通道中处形成平滑的过渡,该平滑过渡有利于减小或 消除了托盘边缘处的气体死角空间,从而改善了托盘边缘处的气体场 的均匀性;  Further preferably, the member and the tray may also constitute an exhaust passage, the member having a side surface facing one side of the tray, the side surface being a concave curved surface so as to be in the exhaust passage at the edge of the tray Forming a smooth transition that facilitates reducing or eliminating the dead space of the gas at the edge of the tray, thereby improving the uniformity of the gas field at the edge of the tray;
或 /和所述托盘与构件与腔室侧壁之间也可以构成排气通道, 所 述构件具有朝向托盘一侧的侧表面, 该侧表面为外凸的弧面, 从而在 托盘边缘处的排气通道中形成平滑的过渡,该平滑过渡有利于减小或 消除了托盘边缘处的气体死角空间,从而改善了托盘边缘处的气体场 的均匀性;  Or / and the tray and the member and the side wall of the chamber may also constitute an exhaust passage, the member having a side surface facing one side of the tray, the side surface being a convex curved surface so as to be at the edge of the tray A smooth transition is formed in the exhaust passage, which facilitates reducing or eliminating the dead space of the gas at the edge of the tray, thereby improving the uniformity of the gas field at the edge of the tray;
进一步优化地,构件的侧表面延伸至托盘的上表面的上方或托盘 的下表面的下方, 从而进一步改善了托盘边缘处的气体场、 温度场和 浓度场的均匀性; Further optimized, the side surface of the member extends above the upper surface of the tray or below the lower surface of the tray, thereby further improving the gas field, temperature field and Uniformity of the concentration field;
进一步优化地,所述托盘上表面的边缘与托盘的侧面之间为弧面 过渡, 从而进一步改善了托盘边缘的气体场、 温度场和浓度场的均匀 性;  Further optimized, a curved transition between the edge of the upper surface of the tray and the side of the tray further improves the uniformity of the gas field, temperature field and concentration field at the edge of the tray;
进一步优化地, 所述构件具有朝向托盘一侧的侧表面, 所述构件 的侧表面对光线的反射率不小于腔室侧壁对光线的反射率,与腔室侧 壁与托盘之间不设置构件、部分来托盘的光线会被腔室侧壁吸收而造 成对托盘的加热效率低、 以及托盘边缘处的温度偏低相比, 构件朝向 托盘一侧的侧表面能够将来自托盘的光线反射,提高了光线的利用率 和对托盘的加热效率, 改善了托盘边缘处的温度场的均匀性;  Further preferably, the member has a side surface facing one side of the tray, and a side surface of the member has a reflectance to light of not less than a reflectance of the side wall of the chamber to the light, and is not disposed between the side wall of the chamber and the tray The light from the tray can be reflected by the side surface of the member toward the tray, as the light from the member, part of the tray is absorbed by the side wall of the chamber, resulting in low heating efficiency to the tray, and the temperature at the edge of the tray is low. Improved light utilization and heating efficiency of the tray, improving the uniformity of the temperature field at the edge of the tray;
进一步优化地,所述构件的朝向托盘一侧的侧表面对光线的反射 率不小于托盘的边缘对光线的反射率,从而所述侧表面可以将来自托 盘的边缘处的光线反射回托盘,进一步提高了托盘边缘处的光线的利 用率和托盘的加热效率, 改善了托盘边缘处的温度场的均匀性;  Further preferably, the side surface of the member facing the tray has a reflectivity to light that is not less than the reflectance of the edge of the tray to the light such that the side surface can reflect light from the edge of the tray back to the tray, further Improves the utilization of light at the edge of the tray and the heating efficiency of the tray, improving the uniformity of the temperature field at the edge of the tray;
进一步优化地,所述构件的朝向托盘一侧的侧表面对光线的反射 为镜面反射, 从而所述托盘的边缘处的光线的大部分被反射, 从而在 托盘边缘处的光线的利用率和对托盘的加热效率更高,托盘边缘处的 温度场的均匀性更好;  Further preferably, the side surface of the member facing the tray side reflects specularly with light, such that a substantial portion of the light at the edge of the tray is reflected, thereby utilizing and utilizing light at the edge of the tray The heating efficiency of the tray is higher, and the uniformity of the temperature field at the edge of the tray is better;
进一步优化地,所述构件沿平行于托盘的上表面的方向的截面为 环形, 或者, 所述构件有两个以上的子构件连接而成或所述构件为一 圓环体, 或者所述构件可以与腔室侧壁、腔室顶盖或气体供给装置相 连接, 或者, 所述构件与托盘之间以及构件与腔室侧壁之间可以有间 隙, 从而可以对构件的结构、 形状、 尺寸和分布进行灵活的调整, 以 获得托盘边缘处的最佳的温度场、 浓度场和气流场;  Further preferably, the member has a ring shape in a section parallel to the direction of the upper surface of the tray, or the member has two or more sub-members connected or the member is a torus, or the member may Connected to the chamber side wall, the chamber top cover or the gas supply, or there may be a gap between the member and the tray and between the member and the chamber sidewall so that the structure, shape, size and The distribution is flexibly adjusted to obtain the optimum temperature, concentration, and airflow fields at the edge of the tray;
进一步优化地, 所述构件中形成有隔热结构, 使得构件能够更好 地将腔室侧壁与托盘的边缘实现隔离,减小托盘边缘向腔室侧壁的热 量散失,进一步提高托盘边缘处的温度场、气流场和浓度场的均匀性。 虽然本发明己以较佳实施例披露如上, 但本发明并非限定于此。任何 本领域技术人员, 在不脱离本发明的精神和范围内, 均可作各种更动 与修改, 因此本发明的保护范围应当以权利要求所限定的范围为准。 Further optimized, the member is formed with a heat insulating structure, so that the member can better isolate the side wall of the chamber from the edge of the tray, reduce heat loss from the edge of the tray to the side wall of the chamber, and further increase the edge of the tray. The uniformity of the temperature field, airflow field and concentration field. Although the invention has been disclosed above in the preferred embodiments, the invention is not limited thereto. Any A person skilled in the art can make various changes and modifications without departing from the spirit and scope of the invention, and the scope of the invention should be determined by the scope defined by the claims.

Claims

权 利 要 求 Rights request
1. 一种用于气相沉积工艺的反应腔室, 包括: 托盘, 其上表面用于 放置村底; 腔室侧壁, 环绕所述托盘一周; 其特征在于, 还包括: 构件, 至少有一部分环绕所述托盘的边缘, 所述构件用于改进托 盘的边缘的气流场、 温度场或浓度场的均匀性。  A reaction chamber for a vapor deposition process, comprising: a tray having an upper surface for placing a substrate; a chamber sidewall surrounding the tray; and characterized by: further comprising: a member, at least a portion Surrounding the edge of the tray, the member is used to improve the uniformity of the airflow field, temperature field or concentration field at the edge of the tray.
2. 如权利要求 1 所述的反应腔室, 其特征在于, 所述托盘具有与上 表面相对的下表面, 所述构件沿所述上表面向下表面方向的厚度 逐渐减小。  2. The reaction chamber according to claim 1, wherein the tray has a lower surface opposite to the upper surface, and a thickness of the member in a direction toward the lower surface of the upper surface gradually decreases.
3. 如权利要求 2 所述的反应腔室, 其特征在于, 所述构件与托盘之 间构成排气通道, 所述构件具有朝向所述托盘的一侧的侧表面, 所述构件的侧表面为平滑过渡。  3. The reaction chamber according to claim 2, wherein an exhaust passage is formed between the member and the tray, the member has a side surface facing one side of the tray, and a side surface of the member For a smooth transition.
4. 如权利要求 3所述的反应腔室, 其特征在于, 所述构件的侧表面 为内 的孤面。  4. The reaction chamber according to claim 3, wherein the side surface of the member is an inner orphan.
5. 如权利要求 1 所述的反应腔室, 其特征在于, 所述构件与托盘之 间构成排气通道, 所述构件具有朝向托盘的一侧的侧表面, 所述 侧表面为内 的弧面。  5. The reaction chamber according to claim 1, wherein an exhaust passage is formed between the member and the tray, the member has a side surface facing one side of the tray, and the side surface is an inner arc surface.
6. 如权利要求 5 所述的反应腔室, 其特征在于, 所述侧表面延伸到 所述上表面所在平面的上方。  6. The reaction chamber of claim 5, wherein the side surface extends above a plane in which the upper surface lies.
7. 如权利要求 5 所述的反应腔室, 其特征在于, 所述托盘具有与上 表面相对的下表面, 所述侧表面延伸到所述下表面所在平面的下 方。  7. The reaction chamber of claim 5, wherein the tray has a lower surface opposite the upper surface, the side surface extending below the plane of the lower surface.
8. 如权利要求 5 所述的反应腔室, 其特征在于, 所述托盘的上表面 的边缘与托盘的侧面之间为弧面过渡。  8. The reaction chamber of claim 5, wherein the edge of the upper surface of the tray and the side of the tray are arcuately transitioned.
9. 如权利要求 1 所述的反应腔室, 其特征在于, 所述构件具有朝向 托盘一侧的侧表面, 所述构件的侧表面对光线的反射率不小于腔 室侧壁对光线的反射率。  9. The reaction chamber according to claim 1, wherein the member has a side surface facing one side of the tray, and a side surface of the member has a reflectance to light of not less than a reflection of light from a side wall of the chamber. rate.
10. 如权利要求 9所述的反应腔室, 其特征在于, 所述构件的侧表 面的粗糙度不超过 0. 008微米, 以便所述构件的侧表面形成镜面, 对光线的反射为镜面反射。 The surface of the member is not more than 008 μm so that the side surface of the member forms a mirror surface, The reflection of light is specular.
1 1. 如权利要求 9所述的反应腔室, 其特征在于, 所述构件的侧表 面具有耐热反射层, 所述耐热反射层在气相沉积工艺过程中保持 稳定状态。 The reaction chamber according to claim 9, wherein the side surface of the member has a heat-resistant reflective layer, and the heat-resistant reflective layer maintains a stable state during the vapor deposition process.
12. 如权利要求 1所述的反应腔室, 其特征在于, 所述构件沿平行 于托盘的上表面的方向的截面为环形。 The reaction chamber according to claim 1, wherein the member has a ring shape in a section parallel to a direction of an upper surface of the tray.
1 3. 如权利要求 12所述的反应腔室, 其特征在于, 所述构件由两 个以上的子构件相连接构成。  The reaction chamber according to claim 12, wherein the member is composed of two or more sub-members connected to each other.
14. 如权利要求 12所述的反应腔室, 其特征在于, 所述构件中嵌 入有隔热结构, 所述隔热结构用于减少托盘的边缘向腔室侧壁的 热量散失。  14. The reaction chamber of claim 12, wherein the member is embedded with a heat insulating structure for reducing heat loss from the edge of the tray to the side wall of the chamber.
15. 如权利要求 14所述的反应腔室, 其特征在于, 所述隔热结构 的朝向所述托盘一侧的侧表面为向内 的弧形。  15. The reaction chamber according to claim 14, wherein a side surface of the heat insulating structure facing one side of the tray is an inward arc.
16. 如权利要求 15所述的反应腔室, 其特征在于, 所述隔热结构 包括隔热气体容纳层和隔热气体, 所述隔热气体容纳层嵌入所述 构件中, 所述隔热气体容纳层在所述构件中限定出空间, 所述空 间用于容纳所述隔热气体, 所述隔热气体的导热系数低于所述构 件的导热系数。  16. The reaction chamber according to claim 15, wherein the heat insulating structure comprises an insulating gas containing layer and a heat insulating gas, the heat insulating gas containing layer being embedded in the member, the heat insulating The gas accommodating layer defines a space in the member for accommodating the heat insulating gas, and the heat insulating coefficient of the heat insulating gas is lower than a thermal conductivity of the member.
17. 如权利要求 16所述的反应腔室, 其特征在于, 所述隔热结构 为嵌入所述构件中的隔热块, 所述隔热块的导热系数低于所述构 件的导热系数。  17. The reaction chamber of claim 16, wherein the thermal insulation structure is a thermal insulation block embedded in the member, the thermal insulation block having a thermal conductivity lower than a thermal conductivity of the member.
18. 如权利要求 1所述的反应腔室, 其特征在于, 还包括: 腔室顶 盖, 位于所述托盘的上表面的上方, 所述构件的一端固定于所述 腔室顶盖上。  18. The reaction chamber of claim 1 further comprising: a chamber cover above the upper surface of the tray, one end of the member being secured to the chamber top cover.
19. 如权利要求 1所述的反应腔室, 其特征在于, 所述构件固定于 腔室侧壁上。 19. The reaction chamber of claim 1 wherein the member is secured to the sidewall of the chamber.
20. 如权利要求 1所述的反应腔室, 其特征在于, 所述构件与腔室 侧壁之间具有间隙。  20. The reaction chamber of claim 1 wherein there is a gap between the member and the sidewall of the chamber.
PCT/CN2013/081816 2012-09-07 2013-08-20 Reaction chamber for vapor deposition process WO2014036886A1 (en)

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