US20090041650A1 - Method for removing metal impurity from quartz component part used in heat processing apparatus of batch type - Google Patents

Method for removing metal impurity from quartz component part used in heat processing apparatus of batch type Download PDF

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US20090041650A1
US20090041650A1 US12/222,241 US22224108A US2009041650A1 US 20090041650 A1 US20090041650 A1 US 20090041650A1 US 22224108 A US22224108 A US 22224108A US 2009041650 A1 US2009041650 A1 US 2009041650A1
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metal impurity
quartz
baking
container
substrates
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Masahisa Watanabe
Katsutoshi Ishii
Tetsuya Shibata
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Tokyo Electron Ltd
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Tokyo Electron Ltd
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Publication of US20090041650A1 publication Critical patent/US20090041650A1/en
Priority to US12/706,734 priority Critical patent/US8834817B2/en
Abandoned legal-status Critical Current

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    • 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
    • C23C16/4401Means for minimising impurities, e.g. dust, moisture or residual gas, in the reaction chamber
    • C23C16/4405Cleaning of reactor or parts inside the reactor by using reactive gases
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01LSEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
    • H01L21/00Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
    • H01L21/02Manufacture or treatment of semiconductor devices or of parts thereof
    • H01L21/04Manufacture or treatment of semiconductor devices or of parts thereof the devices having potential barriers, e.g. a PN junction, depletion layer or carrier concentration layer
    • H01L21/18Manufacture or treatment of semiconductor devices or of parts thereof the devices having potential barriers, e.g. a PN junction, depletion layer or carrier concentration layer the devices having semiconductor bodies comprising elements of Group IV of the Periodic Table or AIIIBV compounds with or without impurities, e.g. doping materials
    • H01L21/30Treatment of semiconductor bodies using processes or apparatus not provided for in groups H01L21/20 - H01L21/26
    • H01L21/324Thermal treatment for modifying the properties of semiconductor bodies, e.g. annealing, sintering
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02CCAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
    • Y02C20/00Capture or disposal of greenhouse gases
    • Y02C20/30Capture or disposal of greenhouse gases of perfluorocarbons [PFC], hydrofluorocarbons [HFC] or sulfur hexafluoride [SF6]
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

Definitions

  • the present invention relates to a method for removing a metal impurity, such as aluminum, from a quartz component part used in a heat processing apparatus of the batch type for performing a heat process on target substrates, such as semiconductor wafers, and particularly to a technique utilized in the semiconductor process field.
  • semiconductor process used herein includes various kinds of processes which are performed to manufacture a semiconductor device or a structure having wiring layers, electrodes, and the like to be connected to a semiconductor device, on a target substrate, such as a semiconductor wafer or a glass substrate used for an FPD (Flat Panel Display), e.g., an LCD (Liquid Crystal Display), by forming semiconductor layers, insulating layers, and conductive layers in predetermined patterns on the target substrate.
  • FPD Fer Panel Display
  • LCD Liquid Crystal Display
  • a vertical heat processing apparatus As a heat processing apparatus used for performing a process for manufacturing semiconductor devices, there is a vertical heat processing apparatus, which is a heat processing apparatus of the batch type.
  • a vertical heat processing apparatus of this kind includes a heating furnace formed of a vertical reaction container opened at the bottom and a heater surrounding the reaction container.
  • a number of semiconductor wafers (which will be referred to as wafers) are supported at intervals in the vertical direction on a wafer holder called a wafer boat.
  • the wafers supported on the wafer boat are loaded into the reaction container from below, and are subjected to a heat process, such as oxidation, diffusion, or film formation using CVD (Chemical Vapor Deposition).
  • CVD Chemical Vapor Deposition
  • some of the component parts such as a reaction container, a wafer boat, and a heat-insulating unit (heat-keeping unit), are typically made of quartz.
  • quartz products originally contain metal impurities, such as aluminum, which can be discharged when the products are heated. Accordingly, in the case of a vertical heat processing apparatus, when the quartz component parts are heated inside the reaction container, metal impurities are scattered into the heated atmosphere inside the reaction container and may be partly deposited on wafers being processed.
  • Patent Document 1 Jpn. Pat. Appln. KOKAI Publication No. 2002-313787: paragraphs 0017 to 0018) discloses a technique for removing copper from the surface of a quartz component part, such as a reaction container. According to this technique, before a heat processing apparatus is used for performing a heat process on product wafers, hydrogen chloride gas and oxygen gas are supplied into the reaction container set to have a heated atmosphere. However, as described later with reference to experimental results, the present inventors have found that aluminum removal is insufficient where the technique disclosed in Patent Document 1 is used.
  • An object of the present invention is to provide a method for removing a metal impurity, such as aluminum, from a quartz component part used in a heat processing apparatus of the batch type for performing a heat process on target substrates, such as semiconductor wafers.
  • a method for removing a metal impurity from a quartz component part in a heat processing apparatus of a batch type comprising a process container configured to accommodate a plurality of target substrates at intervals in a vertical direction and to form a heat process atmosphere therein, the process container including a quartz inner surface to be exposed to the heat process atmosphere, a heater configured to heat an interior of the process container, an exhaust system configured to exhaust gas from inside the process container, and a process gas supply system configured to supply a process gas into the process container, the method comprising: placing a plurality of dummy substrates for allowing the metal impurity to be deposited thereon inside the process container with no product target substrates placed therein; then, supplying a chlorine-containing gas and water vapor into the process container and heating the quartz inner surface of the process container at a process temperature, thereby applying a baking process onto the quartz inner surface to discharge the metal impurity from the quartz inner surface and deposit the metal impurity onto
  • a method for removing a metal impurity from a quartz component part in a heat processing apparatus of a batch type comprising a process container configured to accommodate a plurality of target substrates at intervals in a vertical direction and to form a heat process atmosphere therein, a predetermined member including a quartz portion to be exposed to the heat process atmosphere, a heater configured to heat an interior of the process container, an exhaust system configured to exhaust gas from inside the process container, and a process gas supply system configured to supply a process gas into the process container, the method comprising: placing the predetermined member along with a plurality of dummy substrates for allowing the metal impurity to be deposited thereon inside the process container with no product target substrates placed therein; then, supplying a chlorine-containing gas and water vapor into the process container and heating the quartz portion of the predetermined member at a process temperature, thereby applying a baking process onto the quartz portion to discharge the metal impurity from the quartz portion and deposit the
  • a method for removing a metal impurity from a holder member configured to hold a plurality of target substrates at intervals in a vertical direction and including a quartz portion in a heat processing apparatus of a batch type, the method comprising: placing the holder member holding a plurality of dummy substrates for allowing the metal impurity to be deposited thereon inside a process container with no product target substrates placed therein; then, supplying a chlorine-containing gas and water vapor into the process container and heating the quartz portion of the holder member at a process temperature, thereby applying a baking process onto the quartz portion to discharge the metal impurity from the quartz portion and deposit the metal impurity onto the dummy substrates; and then, unloading the holder member along with the dummy substrates with the metal impurity deposited thereon from the reaction container.
  • each of the method described above may be performed at a stage when the component part has not yet been used for a heat process on semiconductor substrates or a stage when metal contamination on semiconductor substrates has been found.
  • the stage when the component part has not yet been used for a heat process on semiconductor substrates includes a stage between a maintenance operation for the apparatus and a restart operation for a heat process.
  • FIG. 1 is a sectional view showing a vertical heat processing apparatus according to an embodiment of the present invention
  • FIG. 2 is a flow chart showing the process flow of a method for baking a quartz component part according to an embodiment of the present invention
  • FIG. 3 is a sectional view showing a baking apparatus according to another embodiment of the present invention.
  • FIG. 4 is a characteristic diagram showing a metal removing effect of the baking method, obtained by an experiment performed in the apparatus shown in FIG. 1 ;
  • FIG. 5 is a second characteristic diagram showing a metal removing effect of the baking method, obtained by an experiment performed in the apparatus shown in FIG. 1 ;
  • FIG. 6 is a third characteristic diagram showing a metal removing effect of the baking method, obtained by an experiment performed in the apparatus shown in FIG. 1 ;
  • FIG. 7 is a characteristic diagram showing an influence of a temperature change in the baking method, obtained by an experiment performed in the apparatus shown in FIG. 1 .
  • FIG. 1 is a sectional view showing a vertical heat processing apparatus according to an embodiment of the present invention.
  • a baking method according to an embodiment of the present invention is arranged to perform baking of quartz component parts while utilizing functions (such as a gas supply function and a heating function) provided in this vertical heat processing apparatus 1 for performing a process for manufacturing semiconductor devices.
  • functions such as a gas supply function and a heating function
  • the apparatus 1 includes a cylindrical reaction container 2 made of quartz, which has an opening at the bottom and an exhaust port 21 at the top.
  • the reaction container 2 is surrounded by a cylindrical casing 22 provided with a heating device or heater 23 disposed on the inner surface thereof.
  • the heater 23 comprises carbon wire heaters formed of woven bundles of high-purity carbon fibers and set to extend in the vertical direction.
  • a lid 24 having an upper surface covered with a quartz plate is disposed below the reaction container 2 to be moved up and down by a boat elevator 25 of an elevating mechanism, so that the opening of the reaction container 2 is opened and closed.
  • the lid 24 is configured to support thereon a wafer boat 3 used as a holder for holding a plurality of, such as 100 , wafers at intervals in the vertical direction.
  • a rotary shaft 23 is disposed below the wafer boat 3 and extends through a heat-insulating unit 31 .
  • the rotary shaft 32 is configured to be rotated by a rotary driving unit 33 , so that the wafer boat 3 can be rotated by the rotary driving unit 33 as a whole.
  • An injector 4 is disposed near the bottom of the reaction container 2 and extends upward.
  • the injector 4 is used for supplying a process gas into the reaction container 2 when a heat process is performed on the wafers.
  • the upstream side of the injector 4 extends outside from the reaction container 2 and forms a gas passage 41 divided into a plurality of branch lines, one of which is connected to a process gas supply unit 45 .
  • the process gas supply unit 45 includes a plurality of sets of a process gas source, a mass-flow controller for controlling the flow rate of the process gas, and a valve, although FIG. 1 shows them as a block for the sake of convenience. Further, the process gas supply unit 45 can supply purge nitrogen gas into the reaction container 2 before baking is started, as described later.
  • the vertical heat processing apparatus 1 includes a control section 5 for controlling operations of the heater 23 and process gas supply unit 45 described above.
  • the control section 5 is formed of a computer (not shown) comprising a CPU and a memory that stores programs and so forth.
  • Each of the programs contains a group of steps (commands) for controlling operations necessary for performing a heat process on the wafers or baking described later in the vertical heat processing apparatus 1 .
  • these operations include control of the temperature of the heater 23 , adjustment of the pressure inside the reaction container 2 , and adjustment of the flow rate of a process gas or baking gas supplied into the reaction container 2 .
  • the programs are stored in a storage medium, such as a hard disk, compact disk, magnetic optical disk, or memory card, and are installed therefrom into the computer.
  • the wafer boat 3 with a number of wafers supported thereon is loaded into the reaction container 2 , and the reaction container 2 is set to have a heated vacuum atmosphere. Then, a process gas is supplied from the process gas supply unit 45 into the reaction container 2 to perform a heat process for forming a predetermined film on the surface of the wafers.
  • the reaction container 2 and wafer boat 3 which are component parts of the vertical heat processing apparatus 1 , are made of quartz, i.e., they are quartz component parts.
  • metals such as aluminum, titanium, and copper, are present on and/or in the surface of the quartz component parts, and may be deposited on wafers during a heat process and thereby deteriorate characteristics of semiconductor devices.
  • the vertical heat processing apparatus 1 includes the function of performing baking for removing these metals from the surfaces of the wafer boat 3 and reaction container 2 at a stage when the quartz component parts have not yet been used for a heat process on wafers or a stage when metal contamination due to the metals has been found.
  • the structure of the apparatus concerning the baking function will be explained below.
  • the vertical heat processing apparatus 1 includes a hydrogen chloride gas supply unit 42 and a water vapor supply unit 43 for supplying a chlorine-containing gas, such as hydrogen chloride gas, and water vapor through the injector 4 into the reaction container 2 .
  • the hydrogen chloride gas supply unit 42 and water vapor supply unit 43 include a hydrogen chloride gas source, a water vapor source, mass-flow controllers, and valves, and are connected to branch lines on the upstream side of the gas passage 41 , as in the process gas supply unit 45 .
  • the hydrogen chloride gas is supplied from a hydrogen chloride gas source formed of a gas cylinder filled with hydrogen chloride gas in a high concentration.
  • the water vapor is supplied from a water vapor source of the catalyst type in which hydrogen gas and oxygen gas are heated and brought into contact with each other under the presence of a catalyst to generate water vapor.
  • the water vapor source may be of the combustion type in which oxygen gas and hydrogen gas are combusted to generate water vapor.
  • the water vapor source may be of the vaporizer type in which water is vaporized to generate water vapor. According to the catalyst type or combustion type, water vapor is generated under conditions richer in oxygen gas relative to the stoichiometric ratio, and so oxygen gas is contained in the water vapor thus generated by this type.
  • the gas passage 41 is connected to an oxygen gas supply unit 44 including an oxygen cylinder, a mass-flow controller, and so forth.
  • the oxygen cylinder is used for supplying purge oxygen gas into the reaction container 2 after the baking of the quartz component parts (such as the reaction container 2 and wafer boat 3 ) is finished.
  • steps of baking of the quartz component parts (such as the reaction container 2 and wafer boat 3 ), i.e., component parts of the vertical heat processing apparatus 1 , performed in the vertical heat processing apparatus 1 .
  • the flow chart of FIG. 2 shows steps of baking performed at a stage when the quartz component parts have not yet been used for a heat process on wafers. For example, this stage appears after component parts of the vertical heat processing apparatus 1 manufactured in a maker are delivered into a semiconductor device factory, and then the vertical heat processing apparatus 1 is assembled in the semiconductor device factory.
  • the vertical heat processing apparatus 1 is installed in the semiconductor manufacturing factory (step S 1 ), and is going to start running from now. Quartz component parts, such as the reaction container 2 and wafer boat 3 employed in the vertical heat processing apparatus 1 contain aluminum therein, and thus a baking process is performed thereon as follows before they are used for product wafers. At first, dummy wafers DW made of silicon are placed on the wafer boat 3 , wherein the number of dummy wafers DW is typically the same as that of wafers in a heat process, such as 100 .
  • step S 2 the lid 24 is moved up, so that the dummy wafers DW are loaded into the reaction container 2 , and the bottom opening of the reaction container 2 is closed by the lid 24 to set the reaction container 2 in an airtight sate.
  • nitrogen is supplied at a predetermined flow rate from the process gas supply unit 45 into the reaction container 2 to perform nitrogen gas purge inside the reaction container 2 .
  • the output to the heater 23 is controlled to raise the temperature inside the reaction container 2 .
  • a temperature detector such as a thermocouple, it is confirmed that the temperature inside the reaction container 2 reaches a baking temperature of, e.g., 550° C. or more and 1,200° C. or less, and preferably 1,050° C. or less, such as 750° C.
  • the hydrogen chloride gas set at a flow rate of, e.g., 0.1 to 3.0 L/min and the water vapor set at a flow rate of, 5.0 to 10 L/min are supplied to perform the baking of the quartz component parts 2 and 3 (step S 3 ).
  • the ratio of the hydrogen chloride gas relative to the all the gases (hydrogen chloride gas+water vapor) supplied to the reaction container 2 is set to be, e.g., 0.5 to 30 vol %, such as 10 vol %. If the concentration of the hydrogen chloride gas exceeds 30 vol %, corrosion of the apparatus may be undesirably caused.
  • metals such as aluminum
  • present on and in the inner surface of the reaction container 2 and the surface of the wafer boat 3 react with hydrogen chloride and are turned into chlorides, such as aluminum chloride, and they also react with water vapor and are turned into hydroxides, such as aluminum hydroxide (hereinafter, these chlorides and hydroxides are collectively called metal compounds).
  • the metal compounds thus generated are scattered from the quartz surface into the atmosphere inside the reaction container 2 , and are partly exhausted along with the baking gas (hydrogen chloride gas and water vapor) from the exhaust port 21 through an exhaust passage (not shown) out of the reaction container 2 .
  • step S 4 oxygen gas is supplied from the oxygen gas supply unit 44 into the reaction container 2 while gas is exhausted from the reaction container 2 to perform oxygen gas purge for, e.g., 30 minutes to 1 hour (step S 4 ). With this purge, the hydrogen chloride gas and water vapor are exhausted, so that a corrosion atmosphere is prevented from being formed inside the reaction container 2 .
  • the oxygen gas purge described above may be performed after a vacuum atmosphere is formed inside the reaction container 2 , so that the hydrogen chloride gas, which is a corrosion factor, is reliably exhausted.
  • step S 5 sample dummy wafers DW are picked up, and the concentration of an objective metal, such as aluminum, on the sample dummy wafers DW is measured by, e.g., an ICP-MS (Inductively Coupled Plasma-Mass Spectrometry) (step S 6 ).
  • ICP-MS Inductively Coupled Plasma-Mass Spectrometry
  • step S 7 if the measured aluminum concentration is higher than a target value (step S 7 ; N), the dummy wafers DW on the wafer boat 3 are replaced with new dummy wafers DW (step S 9 ). Then, the new dummy wafers DW are loaded into the reaction container 2 , and the baking and the measurement of the aluminum concentration on the dummy wafers DW are performed again (step S 2 to S 7 ).
  • step S 7 when the aluminum concentration on the dummy wafers DW becomes lower than the target value (step S 7 ; Y), product wafers for manufacturing semiconductor devices are placed on the wafer boat 3 in place of the dummy wafers DW. Then, an ordinary heat process starts being performed on the product wafers (step S 8 ). As described above, the baking of the quartz component parts 2 and 3 is performed.
  • the baking method according to the embodiment described above provides the following effects. Specifically, in general, aluminum scattered from quartz component parts, such as the reaction container 2 and wafer boat 3 , can be easily re-deposited on the quartz component parts. However, since the baking is performed with a number of dummy wafers DW placed inside the baking atmosphere, scattered aluminum is trapped by the dummy wafers DW, and so the amount of aluminum inside the quartz component parts is decreased. Consequently, when a heat process is performed on product wafers thereafter, aluminum contamination on the wafers can be suppressed.
  • the quartz component parts 2 and 3 are prevented from being contaminated by aluminum scattered from the dummy wafers DW, and aluminum is reliably removed from inside the vertical heat processing apparatus 1 .
  • the concentration of aluminum deposited on some of the dummy wafers DW unloaded from the reaction container 2 is measured, and this measurement result is used to make a judgment of whether or not the baking needs to be performed again with new dummy wafers DW. Consequently, the aluminum concentration in the quartz component parts can be reliably decreased, while dummy wafers DW are prevented from being unnecessary consumed.
  • the chlorine-containing gas supplied along with water vapor into the reaction container 2 is exemplified by hydrogen chloride gas.
  • the chlorine-containing gas may be another gas, such as chlorine gas or an organic chlorine compound, e.g., trans-dichloroethylene.
  • the timing for performing the baking of the quartz component parts 2 and 3 is not limited to a timing after the vertical heat processing apparatus 1 is assembled.
  • the concentration of aluminum deposited on heat-processed wafers may be periodically measured, so that, when the measurement result is found to exceed a set value, an ordinary heat process for wafers is temporarily stopped and the step S 2 to step S 9 shown in FIG. 2 are performed.
  • the objective metal which may cause contamination on wafers, is exemplified aluminum.
  • the objective metal may be another metal, such as titanium that is originally contained in quartz component parts by an amount next largest to aluminum.
  • a quartz component part, from which a metal, such as aluminum, is removed is not limited to the reaction container 2 or wafer boat 3 explained with reference to the flow chart of FIG. 2 .
  • the quartz plate covering the upper surface of the lid 24 and the heat-insulating unit 31 are also such quartz component parts used as component parts of the vertical heat processing apparatus 1 .
  • the vertical heat processing apparatus 1 assembled from quartz component parts may be exemplified by an oxidation furnace for oxidizing a silicon film, a diffusion furnace for diffusing an impurity into a semiconductor layer, and a CVD furnace.
  • FIG. 3 is a view showing a baking apparatus 10 for removing metals present on and in the wafer boat 3 (a quartz component part) before the wafer boat 3 is incorporated into the vertical heat processing apparatus 1 .
  • the baking apparatus 10 has a structure similar to that of the vertical heat processing apparatus 1 .
  • the baking apparatus 10 includes a quartz reaction container 51 having an exhaust port 511 at the top, a lid 52 having an upper surface covered with a quartz plate 521 , and a support member 53 for holding the wafer boat 3 to be baked.
  • the baking apparatus 10 includes a casing 61 , a heater 62 , and an elevator 63 for moving the lid 52 up and down.
  • a gas supply line 7 is disposed and connected at its upstream side to a hydrogen chloride gas supply unit 71 , a water vapor supply unit 72 , and an oxygen gas supply unit 73 .
  • the baking is performed by use of, e.g., steps S 2 to S 7 and S 9 after the wafer boat 3 is manufactured by a maker and before it is incorporated into the vertical heat processing apparatus 1 .
  • the wafer boat 3 with dummy wafers DW supported thereon is loaded into the reaction container 51 , and the heating, exhaust, and gas supply are performed as described above to execute the baking.
  • the concentration of metals on the dummy wafers DW is measured, and this measurement result is used to make a judgment of whether or not the baking needs to be performed again with new dummy wafers DW.
  • the baking is repeated, so that the wafer boat 3 is free from metals, such as aluminum.
  • FIG. 4 shows the atomic concentration of aluminum on the surface of the dummy wafer DW placed at the bottom of the wafer boat 3 after the predetermined time had elapsed, in the present example and comparative examples described above.
  • the horizontal axis denotes the heating time [min] and the vertical axis denotes the aluminum concentration [atoms/cm 2 ] by logarithm.
  • “ ⁇ ” represents the present example PE1
  • “ ⁇ ” represents the comparative example CE1
  • represents the comparative example CE2
  • represents the comparative example CE3.
  • Aluminum deposited on the dummy wafers DW originates from aluminum present on and in quartz component parts inside the reaction container 2 . Accordingly, as the amount of aluminum deposited on the dummy wafers DW is larger (the atomic concentration of aluminum is higher), the effect of removing aluminum from the quartz component parts is higher.
  • the effect of removing aluminum was the highest even with a short process time of ten and several minutes.
  • the oxygen gas was solely supplied (the comparative example CE1)
  • the effect was merely about one hundredth of that of the present example PE1 at a process time of, e.g., 5 minutes.
  • the water vapor was solely supplied (the comparative example CE2)
  • a process time of about 400 minutes was required to obtain the same effect of removing aluminum as that of the present example PE1.
  • a gas was supplied into the reaction container 2 while the interior of the container 2 was heated to perform baking. Thereafter, wafers were loaded into the reaction container 2 and subjected to a heat process. This sequence was repeatedly performed. The concentration of aluminum deposited on the wafers during the heat process was measured. In the baking of this experiment, no dummy wafers DW were placed inside the reaction container 2 .
  • One cycle of baking was arranged to solely supply water vapor at 10 L/min into the reaction container 2 and heat the interior of the reaction container 2 at 1,000° C. for 6 hours. Then, the first to tenth cycles of baking were repeatedly performed. Wafers were loaded into the reaction container 2 and subjected to a heat process before the first cycle of baking was started and after each cycle of baking was performed. The concentration of aluminum deposited on the wafers during the heat process was measured. The seventh and eighth cycles of baking were continuously performed for 12 hours without a heat process performed on wafers between these cycles.
  • One cycle of baking was arranged to supply water vapor at 10 L/min and hydrogen chloride gas at 0.6 L/min into the reaction container 2 and heat the interior of the reaction container 2 at 1,000° C. for 1 hour. Then, the first to second cycles of baking were performed after the heat process of the tenth cycle of the comparative example CE4. As in the comparative example CE4, a heat process was performed on wafers after each cycle of baking was performed. The concentration of aluminum deposited on the wafers during the heat process was measured.
  • FIG. 5 shows the concentration of aluminum deposited on the wafers heat-processed before start of baking and after each cycle of baking in the comparative example CE4 and present example PE2.
  • the concentration of aluminum deposited on the wafers merely decreased the concentration of aluminum deposited on the wafers to a half (about 5.0 ⁇ 10 10 atoms/cm 2 ) of that (about 1.0 ⁇ 10 11 atoms/cm 2 ) obtained before start of baking.
  • the concentration of aluminum deposited during each heat process after the fourth to tenth cycles the aluminum concentration was almost unchanged even where the number of cycles of baking was increased, i.e., the baking effect was not exhibited.
  • the aluminum concentration bottomed out by the tenth cycle of the comparative example CE4 was further nearly halved and decreased to one fifth (about 2.0 ⁇ 10 10 atoms/cm 2 ) of that (about 1.0 ⁇ 10 11 atoms/cm 2 ) obtained before start of baking. Accordingly, also from these results, it has been found that a method of simultaneously supplying the chlorine-containing gas and water vapor to perform baking is the most effective as a method for removing aluminum from a quartz component part.
  • FIG. 6 shows measurement results of the concentration of aluminum deposited on the wafers during the heat process performed thereon after the baking was performed under the conditions of each of the present examples and comparative examples.
  • the baking was performed by use of dummy wafers DW (the present examples PE3-1 and PE3-2 and the present examples PE4-1 and PE4-2)
  • the amount of aluminum deposited on the wafers during the heat process subsequent to the baking was smaller than those obtained by a case where no dummy wafers DW were used (the comparative examples CE5-1 and CE5-2).
  • the examples with a larger number of dummy wafers rendered a smaller amount of deposited aluminum than the examples with a smaller number of dummy wafers (the present examples PE4-1 and PE4-2). Accordingly, it has been found that, as the number of dummy wafers DW placed inside reaction container 2 during the baking is increased, the effect of removing aluminum is enhanced. In this experiment, trans-dichloroethylene was used as a chlorine-containing gas and was found to provide a sufficient effect of removing aluminum.
  • a gas hydrogen chloride gas set at 0.6 L/min and water vapor set at 10 L/min
  • a gas hydrogen chloride gas set at 0.6 L/min and water vapor set at 10 L/min
  • three wafers were respectively placed at the top, center, and bottom of the wafer boat 3 and subjected to a heat process.
  • the concentration of aluminum deposited on the wafers during the heat process was measured.
  • no dummy wafers DW were placed inside the reaction container 2 .
  • Heat process was performed on wafers inside reaction container not processed by baking.
  • FIG. 7 is a characteristic diagram showing an influence of a change in the temperature inside the reaction container, obtained by this experiment.
  • the concentration of aluminum deposited on the wafers during the heat process 2 was smaller than that obtained by the reaction container not processed by baking. Accordingly, these present examples exhibited a sufficient effect of removing aluminum from quartz component parts.
  • a lower temperature inside the reaction container 2 (the present example PE5) rendered a better effect of removing aluminum than a higher temperature (the present example PE6).
  • this temperature is set to be 1,200° C. or less, and preferably 1,050° C., in light of the heat resistance of quartz component parts.
  • baking of a quartz component part is performed inside a heated atmosphere with a number of dummy substrates placed therein, while a chlorine-containing gas and water vapor are supplied.
  • a metal scattered by the baking is deposited on the dummy substrates, which are then unloaded from the reaction container.
  • the metal thus scattered is prevented from being re-deposited on the quartz component part. Consequently, a heat process can be performed on semiconductor substrates by use of the quartz component part with a very small amount of metal present thereon, so that metal contamination on the semiconductor substrates is remarkably suppressed.

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US20150140835A1 (en) * 2012-07-30 2015-05-21 Hitachi Kokusai Electric Inc. Substrate processing apparatus, method for manufacturing semiconductor device, and recording medium
CN106082241A (zh) * 2016-08-10 2016-11-09 黄石万鑫塑胶有限公司 粉状石英砂提纯装置
WO2022212681A1 (en) * 2021-04-02 2022-10-06 Lam Research Corporation Control of metallic contamination from metal-containing photoresist
EP4245884A1 (en) * 2022-03-18 2023-09-20 Kokusai Electric Corp. Gas cleaning method, method of processing substrate, method of manufacturing semiconductor device, and substrate processing apparatus

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US9816182B2 (en) * 2012-07-30 2017-11-14 Hitachi Kokusai Electric Inc. Substrate processing apparatus, method for manufacturing semiconductor device, and recording medium
CN106082241A (zh) * 2016-08-10 2016-11-09 黄石万鑫塑胶有限公司 粉状石英砂提纯装置
WO2022212681A1 (en) * 2021-04-02 2022-10-06 Lam Research Corporation Control of metallic contamination from metal-containing photoresist
EP4245884A1 (en) * 2022-03-18 2023-09-20 Kokusai Electric Corp. Gas cleaning method, method of processing substrate, method of manufacturing semiconductor device, and substrate processing apparatus

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CN101372739B (zh) 2012-11-28
JP2009044091A (ja) 2009-02-26
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CN101372739A (zh) 2009-02-25
KR20090016425A (ko) 2009-02-13

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