WO2022080271A1 - エッチングガス及びその製造方法、並びに、エッチング方法、半導体素子の製造方法 - Google Patents
エッチングガス及びその製造方法、並びに、エッチング方法、半導体素子の製造方法 Download PDFInfo
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- WO2022080271A1 WO2022080271A1 PCT/JP2021/037425 JP2021037425W WO2022080271A1 WO 2022080271 A1 WO2022080271 A1 WO 2022080271A1 JP 2021037425 W JP2021037425 W JP 2021037425W WO 2022080271 A1 WO2022080271 A1 WO 2022080271A1
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- etching
- gas
- fluorobutene
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- chf
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- 238000005530 etching Methods 0.000 title claims abstract description 330
- 238000000034 method Methods 0.000 title claims abstract description 82
- 238000004519 manufacturing process Methods 0.000 title claims description 38
- 239000004065 semiconductor Substances 0.000 title claims description 32
- WFOIWBGKCSYBJN-UHFFFAOYSA-N 1-fluorobut-1-ene Chemical compound CCC=CF WFOIWBGKCSYBJN-UHFFFAOYSA-N 0.000 claims abstract description 125
- SYNPRNNJJLRHTI-UHFFFAOYSA-N 2-(hydroxymethyl)butane-1,4-diol Chemical compound OCCC(CO)CO SYNPRNNJJLRHTI-UHFFFAOYSA-N 0.000 claims abstract description 60
- 229910052710 silicon Inorganic materials 0.000 claims abstract description 15
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- 239000007789 gas Substances 0.000 claims description 241
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- 238000011049 filling Methods 0.000 claims description 32
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- 208000005156 Dehydration Diseases 0.000 claims description 16
- 230000018044 dehydration Effects 0.000 claims description 16
- 238000006297 dehydration reaction Methods 0.000 claims description 16
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- 238000012545 processing Methods 0.000 claims description 7
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- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 claims description 3
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- SXKNYNUXUHCUHX-UHFFFAOYSA-N 1,1,2,3,3,4-hexafluorobut-1-ene Chemical compound FCC(F)(F)C(F)=C(F)F SXKNYNUXUHCUHX-UHFFFAOYSA-N 0.000 description 3
- GCNWWRIQEJNUIF-UHFFFAOYSA-N 1,1,3,3,4,4,4-heptafluorobut-1-ene Chemical compound FC(F)=CC(F)(F)C(F)(F)F GCNWWRIQEJNUIF-UHFFFAOYSA-N 0.000 description 3
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- 238000004566 IR spectroscopy Methods 0.000 description 2
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical compound CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 description 2
- 239000002033 PVDF binder Substances 0.000 description 2
- 229910000577 Silicon-germanium Inorganic materials 0.000 description 2
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- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
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Images
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01L—SEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
- H01L21/00—Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
- H01L21/02—Manufacture or treatment of semiconductor devices or of parts thereof
- H01L21/04—Manufacture 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
- H01L21/18—Manufacture 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
- H01L21/30—Treatment of semiconductor bodies using processes or apparatus not provided for in groups H01L21/20 - H01L21/26
- H01L21/302—Treatment of semiconductor bodies using processes or apparatus not provided for in groups H01L21/20 - H01L21/26 to change their surface-physical characteristics or shape, e.g. etching, polishing, cutting
- H01L21/306—Chemical or electrical treatment, e.g. electrolytic etching
- H01L21/3065—Plasma etching; Reactive-ion etching
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K13/00—Etching, surface-brightening or pickling compositions
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01L—SEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
- H01L21/00—Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
- H01L21/02—Manufacture or treatment of semiconductor devices or of parts thereof
- H01L21/04—Manufacture 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
- H01L21/18—Manufacture 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
- H01L21/30—Treatment of semiconductor bodies using processes or apparatus not provided for in groups H01L21/20 - H01L21/26
- H01L21/31—Treatment of semiconductor bodies using processes or apparatus not provided for in groups H01L21/20 - H01L21/26 to form insulating layers thereon, e.g. for masking or by using photolithographic techniques; After treatment of these layers; Selection of materials for these layers
- H01L21/3105—After-treatment
- H01L21/311—Etching the insulating layers by chemical or physical means
- H01L21/31105—Etching inorganic layers
- H01L21/31111—Etching inorganic layers by chemical means
- H01L21/31116—Etching inorganic layers by chemical means by dry-etching
Definitions
- the present invention relates to an etching gas and a method for manufacturing the same, an etching method, and a method for manufacturing a semiconductor element.
- dry etching is used for patterning and removing silicon compounds such as silicon oxide and silicon nitride.
- High etching selectivity is required for dry etching. That is, it is required that the silicon compound can be selectively etched as compared with the resist or mask used for patterning.
- Patent Document 1 discloses an etching gas made of hexafluorobutene.
- Patent Document 2 discloses an etching gas containing hexafluorobutene and hexafluorobutene.
- the present invention performs non-etching when an etching gas is brought into contact with a member to be etched having an etching target object to be etched by the etching gas and a non-etching target object not to be etched by the etching gas. It is an object of the present invention to provide an etching gas capable of selectively etching an object to be etched as compared with the object, a method for producing the same, an etching method, and a method for producing a semiconductor element.
- one aspect of the present invention is as follows [1] to [11].
- the method for producing the etching gas according to [1] or [2]. A dehydration step of dehydrating the crude fluorobutene, which is the fluorobutene containing water and oxygen gas, and The deoxidizing gas step of applying the deoxidizing gas treatment to the crude fluorobutene, and A method for producing an etching gas.
- the etching gas is filled in the filling container, and the gas phase portion in the filling container has a concentration of carbonyl fluoride of 100% by mass or less.
- the gas from the filling container is used.
- etching gas is a gas consisting only of the fluorobutene or a mixed gas containing the fluorobutene and a diluting gas.
- diluted gas is at least one selected from nitrogen gas, helium, argon, neon, krypton, and xenon.
- a method for manufacturing a semiconductor device wherein the semiconductor device is manufactured by using the etching method according to any one of [7] to [10].
- the member to be etched is a semiconductor substrate having the etching target and the non-etching target.
- a method for manufacturing a semiconductor device comprising a processing step of removing at least a part of the object to be etched from the semiconductor substrate by the etching.
- an etching target containing silicon can be selectively etched as compared with a non-etching target.
- the etching gas according to the present embodiment is applied to a member to be etched having an etching target object to be etched by the etching gas and a non-etching target object not to be etched by the etching gas. It is provided with an etching step of contacting the object and selectively etching the object to be etched as compared with the non-etched object. Then, in the etching method according to the present embodiment, the etching target contains silicon (Si).
- the etching target can be selectively etched as compared with the non-etching target (that is, high etching selectivity can be obtained).
- the fluorobutene is polymerized by reacting during dry etching, and the non-etched object is coated with the film of this polymer to be protected from etching. Therefore, since the etching of the non-etched object is more difficult to proceed, if the etching is performed using the etching gas containing fluorobutene, the etching selectivity is further improved.
- carbonyl fluoride has high reactivity with both an etching target such as silicon oxide and silicon nitride and a non-etching target such as a mask. Therefore, when the member to be etched is etched using an etching gas containing carbonyl fluoride, both the etching target and the non-etching target may be etched, resulting in insufficient etching selectivity. Therefore, in order to increase the etching selectivity, it is necessary to reduce the concentration of carbonyl fluoride in the etching gas.
- the concentration of carbonyl fluoride in the etching gas needs to be 100 mass ppm or less, preferably 50 mass ppm or less, and more preferably 10 mass ppm or less. If etching is performed using an etching gas having a concentration of carbonyl fluoride within the above range, the non-etched object is less likely to be etched, so that the etching selectivity of the etched object with respect to the non-etched object is increased.
- the method for measuring the concentration of carbonyl fluoride is not particularly limited, but it can be quantified by, for example, infrared spectroscopy.
- hydrogen fluoride has the same effect as carbonyl fluoride, and is reactive with both etched objects such as silicon oxide and silicon nitride and non-etched objects such as masks. Since it is high, it is preferable that the concentration of hydrogen fluoride in the etching gas is low. That is, when the etching gas further contains hydrogen fluoride as an impurity, the concentration of hydrogen fluoride in the etching gas is preferably 100 mass ppm or less, more preferably 50 mass ppm or less. It is more preferably mass ppm or less.
- the method for measuring the concentration of hydrogen fluoride is not particularly limited, but it can be quantified by, for example, infrared spectroscopy.
- the etching gas according to the present embodiment has a low concentration of carbonyl fluoride, if the etching object is dry-etched using the etching gas according to the present embodiment, the non-etched object is less likely to be etched.
- the etching target can be selectively etched as compared with the non-etching target, and the etching selectivity is improved.
- the etching selection ratio which is the ratio of the etching rate of the non-etched object to the etching rate of the etched object, tends to be 10 or more.
- the etching selectivity is preferably 10 or more, more preferably 30 or more, and even more preferably 50 or more.
- Carbonyl fluoride and hydrogen fluoride are impurities derived from the above fluorobutene. The reason why carbonyl fluoride and hydrogen fluoride are likely to be contained as impurities in the above fluorobutene will be described below.
- fluorobutene often contains a small amount of oxygen gas (O 2 ) and water (H 2 O), but when the oxygen concentration in the fluorobutene exceeds 1000 mass ppm, as shown in the following formula.
- Fluorobutene reacts with oxygen gas to produce carbonyl fluoride and hydrogen fluoride.
- the presence of water in fluorobutene promotes the reaction of the following formula.
- the reaction between the above fluorobutene and oxygen gas produces carbonyl fluoride and hydrogen fluoride. Therefore, in the case of producing the etching gas according to the present embodiment containing the above-mentioned fluorobutene, it is necessary to remove water and oxygen gas from the above-mentioned fluorobutene in order to reduce the concentration of carbonyl fluoride and hydrogen fluoride. be.
- the method for producing an etching gas according to the present embodiment includes a dehydration step of dehydrating the crude fluorobutene, which is the fluorobutene containing water and oxygen gas, and a deoxidizing process of deoxidizing the crude fluorobutene. It is equipped with a gas process.
- the order in which the dehydration step and the deoxidizing gas step are carried out is not particularly limited, and either step may be carried out first. Further, if possible, the dehydration step and the deoxidizing gas step may be performed at the same time.
- the etching in the present invention means that the member to be etched is processed into a predetermined shape (for example, a three-dimensional shape) by removing a part or all of the object to be etched (for example, the member to be etched). It means (to process a film-like etching object made of a silicon compound having a predetermined film thickness).
- the etching method according to the present embodiment can accurately etch the object to be etched, it can be used for manufacturing semiconductor elements such as 3D-NAND flash memory and logic devices, for example. Further, the etching method according to the present embodiment can be expected to contribute to further miniaturization and high integration of semiconductor devices.
- the fluorobutene contained in the etching gas according to the present embodiment is represented by the general formula C 4 H x F y , and x in the general formula is 1 or more and 7 or less and y is 1 or more and 7 or less. , X + y satisfies the three conditions of 8.
- fluorobutene is not particularly limited as long as it meets the above requirements, and linear fluorobutene and branched-chain fluorobutene (isobutene) can be used, but fluoro-1-butene is used. Similar substances and those similar to fluoro-2-butene can be preferably used.
- fluorobutenes may be used alone, or two or more types may be used in combination. Further, although some of the above fluorobutenes have cis-trans isomers, any of the cis-type and trans-type fluorobutenes can be used in the etching gas according to the present embodiment.
- fluorobutenes those having a boiling point of 50 ° C. or lower at 1 atm are preferable, and those having a boiling point of 40 ° C. or lower are more preferable.
- the boiling point is within the above range, when the fluorobutene gas is introduced into, for example, a plasma etching apparatus, the fluorobutene gas is difficult to liquefy inside a pipe or the like into which the fluorobutene gas is introduced. Therefore, it is possible to suppress the occurrence of troubles caused by the liquefaction of the fluorobutene gas, so that the plasma etching process can be efficiently performed.
- the etching gas is a gas containing the above fluorobutene.
- the etching gas may be a gas consisting only of the above-mentioned fluorobutene or a mixed gas containing the above-mentioned fluorobutene and a diluting gas.
- the diluted gas is preferably inert to fluorobutene and the member to be etched. Further, it may be a mixed gas containing the above-mentioned fluorobutene, a diluting gas and an added gas.
- the diluent gas is preferably an inert gas, and specifically, it is selected from nitrogen gas (N 2 ), helium (He), neon (Ne), argon (Ar), krypton (Kr), and xenon (Xe). At least one can be used.
- a fluorocarbon gas or a hydrofluorocarbon gas can be used as the additive gas.
- fluorocarbons include carbon tetrafluoride (CF 4 ), hexafluoromethane (C 2 F 6 ), and octafluoropropane (C 3 F 8 ).
- hydrofluorocarbons include CF 3 H, CF 2 H 2 , CF H 3 , C 2 F 4 H 2 , C 2 F 5 H, C 3 F 7 H, C 3 F 6 H 2 , C 3 F 5 Examples include H 3 , C 3 F 4 H 4 , and C 3 F 3 H 5 .
- One type of these additive gases may be used alone, or two or more types may be used in combination.
- the content of the diluted gas is preferably 90% by volume or less, more preferably 50% by volume or less, based on the total amount of the etching gas.
- the content of the added gas is preferably 50% by volume or less, more preferably 30% by volume or less, based on the total amount of the etching gas.
- the content of the fluorobutene is preferably 5% by volume or more, more preferably 10% by volume or more, based on the total amount of the etching gas, from the viewpoint of improving the etching rate. Further, from the viewpoint of suppressing the amount of fluorobutene used, 90% by volume or less is preferable, and 80% by volume or less is more preferable with respect to the total amount of etching gas.
- the method of dehydration treatment for removing water from crude fluorobutene is not particularly limited, and a known method can be adopted.
- a process of bringing the crude fluorobutene into contact with the adsorbent can be adopted.
- Dehydration can be performed by bringing the crude fluorobutene into contact with the adsorbent and adsorbing water on the adsorbent.
- at least one of carbonyl fluoride and hydrogen fluoride may be removed from the crude fluorobutene together with water.
- the type of adsorbent is not particularly limited as long as it can remove water from the fluorobutene, and examples thereof include molecular sheave 3A, molecular sheave 4A, molecular sheave 5A, activated carbon, and silica gel.
- molecular sieve 3A capable of selectively adsorbing water is more preferable.
- the adsorbent for removing carbonyl fluoride the above-mentioned various molecular sieves can be used. Further, as the adsorbent for removing hydrogen fluoride, the above-mentioned various molecular sieves and metal fluoride such as sodium fluoride can be used.
- the water concentration in the fluorobutene is preferably 500 mass ppm or less, more preferably 100 mass ppm or less, and further preferably 10 mass ppm or less. Then, the formation of carbonyl fluoride and hydrogen fluoride by the reaction of the above formula is less likely to occur.
- the method for measuring the water concentration in the fluorobutene is not particularly limited, and can be quantified by, for example, the Karl Fischer method.
- the method of deoxidizing gas treatment for removing oxygen gas from crude fluorobutene is not particularly limited, and for example, a treatment for distilling crude fluorobutene to separate oxygen gas can be adopted. By distilling the crude fluorobutene, at least one of carbonyl fluoride and hydrogen fluoride may be removed from the crude fluorobutene together with oxygen gas.
- the distillation method is not particularly limited as long as oxygen gas can be separated from the crude fluorobutene, and for example, a batch distillation method or a continuous distillation method can be adopted.
- the type of distillation column used for distillation is not particularly limited, and for example, a shelf column using a sheave tray, a bubble cap tray, or the like, or a packed column filled with a regular or irregular filling is used. Can be done.
- the distillation conditions are not particularly limited, but the number of theoretical plates is preferably 1 or more and 30 or less, and more preferably 3 or more and 10 or less.
- the temperature of the bottom (kettle) of the distillation column in which crude fluorobutene is charged during distillation is not particularly limited, but is preferably 10 ° C. or higher and 80 ° C. or lower, and 20 ° C. or higher and 60 ° C. or lower. It is more preferable to do so.
- the temperature at the top of the distillation column is not particularly limited, but is preferably ⁇ 60 ° C. or higher and 0 ° C. or lower, and more preferably ⁇ 50 ° C. or higher and ⁇ 20 ° C. or lower.
- the oxygen concentration in the fluorobutene is preferably 1000% by mass or less, more preferably 500% by mass or less, and further preferably 100% by mass or less. Then, the formation of carbonyl fluoride and hydrogen fluoride by the reaction of the above formula is less likely to occur.
- the method for measuring the oxygen concentration in the fluorobutene is not particularly limited, and can be quantified by, for example, gas chromatography.
- the method for producing the etching gas according to the present embodiment further includes a filling step of filling the filling container with the above-mentioned fluorobutene whose content of oxygen gas and water has been reduced by carrying out a dehydration step and a deoxidizing gas step. You may be prepared.
- the fluorobutene and the diluting gas may be mixed to form a mixed gas, and then the mixed gas may be filled in the filling container.
- the fluorobutene and the diluting gas may be separately filled in the filling container and used as a mixed gas in the filling container.
- the method for filling the fluorobutene in the filling container is not particularly limited, and for example, a gas phase filling method or a liquid phase filling method can be adopted. Further, when filling fluorobutene, oxygen gas in the filling container may be removed in advance by a heating vacuum drawing method or the like.
- the material of the filling container is not particularly limited, and examples thereof include manganese steel, stainless steel, Hastelloy (registered trademark), and Inconel (registered trademark).
- the etching of the present embodiment can be achieved by either plasma etching using plasma or plasmaless etching using plasma.
- plasma etching include reactive ion etching (RIE), inductively coupled plasma (ICP) etching, capacitively coupled plasma (CCP: Capacitive Coupled Plasma) etching, and electron etching.
- RIE reactive ion etching
- ICP inductively coupled plasma
- CCP capacitively coupled plasma
- electron etching Electron Cyclotron Resonance
- Plasma etching microwave plasma etching can be mentioned.
- etching may be performed using the etching gas filled in the filling container. That is, the etching gas is filled in the filling container, the gas phase portion in the filling container has a concentration of carbonyl fluoride of 100 mass ppm or less, and in the etching step, the gas phase portion is extracted from the filling container and etched.
- the object to be etched may be etched by contacting the member.
- the pressure condition of the etching step in the etching method according to the present embodiment is not particularly limited, but is preferably 10 Pa or less, and more preferably 5 Pa or less. When the pressure condition is within the above range, plasma is likely to be stably generated. On the other hand, the pressure condition in the etching step is preferably 0.05 Pa or more. When the pressure condition is within the above range, a large amount of ionized ions are generated and a sufficient plasma density can be easily obtained.
- the flow rate of the etching gas may be appropriately set so that the pressure in the chamber is kept constant according to the size of the chamber and the capacity of the exhaust equipment for depressurizing the inside of the chamber.
- the temperature condition of the etching step in the etching method according to the present embodiment is not particularly limited, but it is preferably 200 ° C. or lower in order to obtain high etching selectivity, and a non-etching object such as a mask is etched. It is more preferably 150 ° C. or lower in order to further suppress the etching, and further preferably 100 ° C. or lower in order to perform anisotropic etching.
- the temperature of the temperature condition is the temperature of the member to be etched, but the temperature of the stage that supports the member to be etched, which is installed in the chamber of the etching apparatus, can also be used.
- the above fluorobutene hardly reacts with a non-etching object such as a mask at a temperature of 200 ° C. or lower. Therefore, if the member to be etched is etched by the etching method according to the present embodiment, the object to be etched can be selectively etched with almost no etching of the non-etched object. Therefore, the etching method according to the present embodiment can be used as a method of processing a silicon-containing etching target into a predetermined shape by using a patterned non-etching target as a resist or a mask.
- the etching selectivity tends to be high.
- the etching selection ratio which is the ratio of the etching rate of the object to be etched containing silicon to the etching rate of the non-etched object, tends to be 10 or more.
- the bias power constituting the potential difference between the plasma generated during etching and the member to be etched may be selected from 0 to 10000 W depending on the desired etching shape, and 0 to 1000 W when selectively etching is performed. The degree is preferable. Anisotropic etching can be performed by this potential difference.
- the member to be etched by the etching method according to the present embodiment has an etching target and a non-etching target, but has a portion formed by the etching target and a portion formed by the non-etching target. It may be a member or a member formed of a mixture of an etching target and a non-etching target. Further, the member to be etched may have a member other than the object to be etched and the object to be etched.
- silicon oxide examples include silicon dioxide (SiO 2 ).
- silicon nitride refers to a compound having silicon and nitrogen in arbitrary proportions, and examples thereof include Si 3 N 4 .
- the purity of silicon nitride is not particularly limited, but is preferably 30% by mass or more, more preferably 60% by mass or more, and further preferably 90% by mass or more.
- the shape of the object to be etched is not particularly limited, and may be, for example, plate-shaped, foil-shaped, film-shaped, powder-shaped, or lump-shaped.
- the non-etching object does not substantially react with the fluorobutene, or the reaction with the fluorobutene is extremely slow, so that the etching hardly proceeds even if the etching is performed by the etching method according to the present embodiment.
- the non-etching object is not particularly limited as long as it has the above-mentioned properties, but for example, a photoresist, amorphous carbon (C), titanium nitride (TiN), copper (Cu), and nickel (Ni). ), Metals such as cobalt (Co), oxides of these metals, and nitrides. Among these, photoresist and amorphous carbon are more preferable from the viewpoint of handleability and availability.
- Photoresist means a photosensitive composition whose physical properties such as solubility are changed by light, electron beam, or the like.
- photoresists for g-line, h-line, i-line, KrF, ArF, F2, EUV and the like can be mentioned.
- the composition of the photoresist is not particularly limited as long as it is generally used in the semiconductor manufacturing process, and for example, chain olefin, cyclic olefin, styrene, vinylphenol, acrylic acid, methacrylate, epoxy, etc. Examples thereof include compositions containing a polymer synthesized from at least one monomer selected from melamine and glycol.
- the non-etching target can be used as a resist or a mask for suppressing etching of the etching target by the etching gas. Therefore, in the etching method according to the present embodiment, the patterned non-etched object is used as a resist or a mask to process the etched object into a predetermined shape (for example, the film-shaped etched object of the member to be etched). Since it can be used for a method such as (processing an object to a predetermined film thickness), it can be suitably used for manufacturing a semiconductor element. Further, since the non-etched object is hardly etched, it is possible to suppress the etching of the portion of the semiconductor element that should not be etched, and it is possible to prevent the characteristics of the semiconductor element from being lost by etching. can.
- the non-etching object remaining after patterning can be removed by a removal method generally used in the semiconductor device manufacturing process. For example, ashing with an oxidizing gas such as oxygen plasma or ozone, or dissolution using a chemical solution such as APM (mixed solution of ammonia water and hydrogen peroxide solution), SPM (mixed solution of sulfuric acid and hydrogen peroxide solution) or organic solvent. Removal is mentioned.
- ashing with an oxidizing gas such as oxygen plasma or ozone
- a chemical solution such as APM (mixed solution of ammonia water and hydrogen peroxide solution), SPM (mixed solution of sulfuric acid and hydrogen peroxide solution) or organic solvent. Removal is mentioned.
- the etching apparatus of FIG. 1 is a plasma etching apparatus that performs etching using plasma. First, the etching apparatus of FIG. 1 will be described.
- the etching apparatus of FIG. 1 supports a chamber 10 in which etching is performed internally, a plasma generator (not shown) that generates gas inside the chamber 10, and a member 12 to be etched to be etched inside the chamber 10.
- a thermometer 14 that measures the temperature of the stage 11 and the member 12 to be etched, an exhaust pipe 13 for discharging the gas inside the chamber 10, and a vacuum provided in the exhaust pipe 13 to reduce the pressure inside the chamber 10. It includes a pump 15 and a pressure gauge 16 for measuring the pressure inside the chamber 10. If the stage 11 is connected to a high frequency power supply, the stage 11 can be provided with a function of applying a high frequency to the member 12 to be etched.
- the type of plasma generation mechanism of the plasma generator is not particularly limited, and may be one in which a high frequency voltage is applied to a parallel plate or one in which a high frequency current is passed through a coil.
- a high frequency voltage is applied to the member 12 to be etched in plasma
- a negative voltage is applied to the member 12 to be etched, and positive ions are incident on the member 12 to be etched at high speed and vertically, so that anisotropic etching is possible.
- the etching apparatus of FIG. 1 is provided with an etching gas supply unit that supplies the etching gas inside the chamber 10.
- This etching gas supply unit is a fluorobutene gas supply unit 1 that connects a fluorobutene gas supply unit 1 that supplies a fluorobutene gas, a dilution gas supply unit 2 that supplies a dilution gas, a fluorobutene gas supply unit 1 and a chamber 10. It has a diluting gas supply pipe 6 for connecting a diluting gas supply unit 2 to an intermediate portion of the fluorobutene gas supply pipe 5 and a diluting gas supply pipe 5.
- the fluorobutene gas supply pipe 5 is provided with a fluorobutene gas pressure control device 7 for controlling the pressure of the fluorobutene gas and a fluorobutene gas flow rate control device 3 for controlling the flow rate of the fluorobutene gas.
- the diluted gas supply pipe 6 is provided with a diluted gas pressure control device 8 for controlling the pressure of the diluted gas and a diluted gas flow rate control device 4 for controlling the flow rate of the diluted gas.
- a facility for supplying the added gas may be provided in the same manner as the diluted gas supply unit 2, the diluted gas flow rate control device 4, the diluted gas supply pipe 6, and the diluted gas pressure control device 8 (not shown). ).
- the fluorobutene gas When the fluorobutene gas is supplied to the chamber 10 as the etching gas, the inside of the chamber 10 is depressurized by the vacuum pump 15, and then the fluorobutene gas is supplied from the fluorobutene gas supply unit 1 to the fluorobutene gas supply pipe 5. By sending out the fluorobutene gas, the fluorobutene gas is supplied to the chamber 10 through the fluorobutene gas supply pipe 5.
- the inside of the chamber 10 is depressurized by the vacuum pump 15, and then fluorobutene is supplied from the fluorobutene gas supply unit 1.
- the fluorobutene gas is sent out to the gas supply pipe 5, and the diluted gas is sent from the diluted gas supply unit 2 to the fluorobutene gas supply pipe 5 via the diluted gas supply pipe 6.
- the fluorobutene gas and the diluting gas are mixed in the middle portion of the fluorobutene gas supply pipe 5 to form a mixed gas, and this mixed gas is supplied to the chamber 10 via the fluorobutene gas supply pipe 5. It has become.
- the fluorobutene gas and the diluted gas may be separately supplied to the chamber 10 and used as a mixed gas in the chamber 10.
- the configuration of the fluorobutene gas supply unit 1 and the diluted gas supply unit 2 is not particularly limited, and may be, for example, a cylinder or a cylinder. Further, as the fluorobutene gas flow rate control device 3 and the diluted gas flow rate control device 4, for example, a mass flow controller or a flow meter can be used.
- the supply pressure of the etching gas is preferably 1 Pa or more and 0.2 MPa or less, more preferably 10 Pa or more and 0.1 MPa or less, and further preferably 50 Pa or more and 50 kPa or less.
- the supply pressure of the etching gas is within the above range, the etching gas is smoothly supplied to the chamber 10, and the load on the parts (for example, the various devices and the piping) of the etching device of FIG. 1 is small. ..
- the pressure of the etching gas supplied into the chamber 10 is preferably 1 Pa or more and 80 kPa or less, and more preferably 10 Pa or more and 50 kPa or less, from the viewpoint of uniformly etching the surface of the member 12 to be etched. , 100 Pa or more and 20 kPa or less is more preferable.
- the pressure of the etching gas in the chamber 10 is within the above range, a sufficient etching rate can be obtained and the etching selection ratio tends to be high.
- the pressure in the chamber 10 before supplying the etching gas is not particularly limited as long as it is equal to or lower than the supply pressure of the etching gas or lower than the supply pressure of the etching gas, but is not particularly limited, but is, for example, 10 -5 Pa or more. It is preferably less than 10 kPa, and more preferably 1 Pa or more and 2 kPa or less.
- the differential pressure between the supply pressure of the etching gas and the pressure in the chamber 10 before supplying the etching gas is preferably 0.5 MPa or less, more preferably 0.3 MPa or less, and 0.1 MPa or less. Is more preferable. When the differential pressure is within the above range, the etching gas can be smoothly supplied to the chamber 10.
- the supply temperature of the etching gas is preferably 0 ° C. or higher and 150 ° C. or lower.
- the etching processing time (hereinafter, also referred to as "etching time”) can be arbitrarily set depending on how much the object to be etched of the member 12 to be etched is desired to be etched, but the production efficiency of the semiconductor device manufacturing process is taken into consideration. Then, it is preferably within 60 minutes, more preferably within 40 minutes, and even more preferably within 20 minutes.
- the etching processing time refers to the time during which the etching gas is in contact with the member 12 to be etched inside the chamber 10.
- the etching method according to the present embodiment can be performed using a general plasma etching apparatus used in the semiconductor device manufacturing process, such as the etching apparatus of FIG. 1, and the configuration of the etchable apparatus that can be used is particularly limited. Not done.
- the positional relationship between the fluorobutene gas supply pipe 5 and the member 12 to be etched is not particularly limited as long as the etching gas can be brought into contact with the member 12 to be etched.
- the temperature control mechanism of the chamber 10 since the temperature of the member 12 to be etched may be adjusted to an arbitrary temperature, the temperature control mechanism of the member 12 to be etched may be directly provided on the stage 11 or outside. The attached temperature controller may heat or cool the chamber 10 from the outside of the chamber 10.
- the material of the etching apparatus of FIG. 1 is not particularly limited as long as it has corrosion resistance to the fluorobutene used and can reduce the pressure to a predetermined pressure.
- metals such as nickel, nickel-based alloys, aluminum, stainless steel, platinum, copper, and cobalt, ceramics such as alumina (Al 2 O 3 ), and fluororesins are used for the parts that come into contact with the etching gas. be able to.
- nickel-based alloys include Inconel (registered trademark), Hastelloy (registered trademark), Monel (registered trademark) and the like.
- fluororesin include polytetrafluoroethylene (PTFE), polychlorotrifluoroethylene (PCTFE), tetrafluoroethylene / perfluoroalkoxyethylene copolymer (PFA), polyvinylidene fluoride (PVDF), and Teflon.
- PTFE polytetrafluoroethylene
- PCTFE polychlorotrifluoroethylene
- PFA tetrafluoroethylene / perfluoroalkoxyethylene copolymer
- PVDF polyvinylidene fluoride
- Teflon Teflon
- Fluorobutene containing impurities such as carbonyl fluoride and hydrogen fluoride at various concentrations was prepared. Examples of preparation of fluorobutene will be described below.
- the oxygen concentration was measured using a gas chromatograph GC-2014 manufactured by Shimadzu Corporation.
- the water concentration was measured using a Karl Fischer water measuring device CA-310 manufactured by Mitsubishi Chemical Analytech Co., Ltd.
- a SUS distillation column a kettle with a capacity of 5 L, a condenser, and a distillate were used.
- the deoxidizing gas treatment was performed as follows using a purification device equipped with a receiver and the like. 500 g of 1,1,1,4,4,4-hexafluoro-2-butene dehydrated as described above was charged into a kettle, and the kettle was heated to 30 ° C. for distillation.
- the SUS distillation column used is filled with laboratory packing manufactured by Sulzer Chemtech, and has a theoretical plate number of 10. The temperature of the condenser was set to ⁇ 40 ° C.
- cylinder A SUS316 cylinder with a capacity of 1 L
- This cylinder A was filled with 400 g of 1,1,1,4,4,4-hexafluoro-2-butene remaining in the kettle of the purification apparatus after the deoxidizing gas treatment was completed by gas phase filling (). Filling process). Then, this cylinder A was allowed to stand in a room controlled at 20 ° C. for 30 days.
- the 1,1,1,4,4,4-hexafluoro-2-butene in the cylinder A after standing for 30 days is referred to as sample 1-1.
- cylinder B three SUS316 cylinders having a capacity of 500 mL are prepared (hereinafter referred to as "cylinder B", “cylinder C”, and “cylinder D"), and manganese steel containers are used in these cylinders B, C, and D.
- 100 g of 1,1,1,4,4,4-hexafluoro-2-butene was transferred from (filling step). Then, the cylinder B was allowed to stand for 10 days, the cylinder C for 20 days, and the cylinder D for 30 days in a room controlled at 20 ° C.
- the gas phase portion of 1,1,1,4,4,4-hexafluoro-2-butene of Sample 1-3 was extracted from the cylinder C, and the concentrations of carbonyl fluoride and hydrogen fluoride were measured.
- the concentration of carbonyl fluoride was 408 mass ppm, and the concentration of hydrogen fluoride was 392 mass ppm.
- the concentration of hydrogen fluoride was measured using an infrared spectrophotometer Nicolet iS10 manufactured by Thermo Fisher Scientific Co., Ltd.
- the concentration of carbonyl fluoride in Sample 2-1 was less than 10 mass ppm.
- the concentration of carbonyl fluoride in Sample 2-2 was 268 mass ppm.
- the concentration of carbonyl fluoride in Sample 2-3 was 478 mass ppm, and the concentration of hydrogen fluoride was 155 mass ppm.
- the concentration of carbonyl fluoride in Sample 2-4 was 653 mass ppm.
- Samples 3-1 to 3-4 were prepared in the same manner as in Preparation Example 1 except that 2,3,3,4,4,4-hexafluoro-1-butene was used as the fluorobutene. Prepared. Then, the concentrations of carbonyl fluoride of each sample and hydrogen fluoride of sample 3-3 were measured. The measuring method is the same as described above.
- the concentration of carbonyl fluoride in Sample 3-1 was less than 10 mass ppm.
- the concentration of carbonyl fluoride in Sample 3-2 was 235 mass ppm.
- the concentration of carbonyl fluoride in Sample 3-3 was 411 mass ppm, and the concentration of hydrogen fluoride was 408 mass ppm.
- the concentration of carbonyl fluoride in Sample 3-4 was 603 mass ppm.
- Samples 4-1 to 4- 4 was prepared. Then, the concentrations of carbonyl fluoride of each sample and hydrogen fluoride of sample 4-3 were measured. The measuring method is the same as described above.
- the concentration of carbonyl fluoride in Sample 4-1 was less than 10 mass ppm.
- the concentration of carbonyl fluoride in sample 4-2 was 268 mass ppm.
- the concentration of carbonyl fluoride in Sample 4-3 was 437 ppm by mass, and the concentration of hydrogen fluoride was 36 ppm by mass.
- the concentration of carbonyl fluoride in Sample 4-4 was 622 mass ppm. Table 1 shows the concentrations of carbonyl fluoride and hydrogen fluoride in each sample.
- Example 1 A silicon oxide film having a thickness of 1000 nm, a silicon nitride film having a thickness of 1000 nm, and a photoresist film having a thickness of 1000 nm are formed on the surface of the semiconductor wafer so as to be exposed on the surface without being laminated. This was used as a test body. Then, the test piece was etched using 1,1,1,4,4,4-hexafluoro-2-butene of Sample 1-1.
- the ICP etching apparatus As the etching apparatus, the ICP etching apparatus RIE-230iP manufactured by SAMCO Co., Ltd. was used. Specifically, sample 1-1 1,1,1,4,4,4-hexafluoro-2-butene was introduced into the chamber independently at a flow rate of 10 mL / min and argon at a flow rate of 40 mL / min. Then, the etching gas was prepared by mixing in the chamber, and a high frequency voltage was applied at 500 W to turn the etching gas into plasma in the chamber. Then, the test piece in the chamber was etched under the etching conditions of a pressure of 3 Pa, a temperature of 20 ° C., and a bias power of 100 W. When the concentrations of carbonyl fluoride and hydrogen fluoride of argon used here were measured, neither was detected.
- the test piece was taken out from the chamber, the thicknesses of the silicon oxide film, the silicon nitride film, and the photoresist film were measured, and the amount of decrease in the thickness from each film before etching was calculated.
- the etching rate of each film was calculated by dividing this decrease by the etching time. As a result, the etching rate of the photoresist film was less than 1 nm / min, the etching rate of the silicon oxide film was 43 nm / min, and the etching rate of the silicon nitride film was 51 nm / min. From this result, it was confirmed that the silicon oxide film and the silicon nitride film, which are the objects to be etched, are selectively etched as compared with the photoresist film, which is the object to be etched.
- Example 2 Etching of the test piece in the same manner as in Example 1 except that 1,1,1,4,4,4-hexafluoro-2-butene of Sample 1-2 was used instead of Sample 1-1. was performed, and the etching rate of each film was calculated.
- the etching rate of the photoresist film was 2 nm / min
- the etching rate of the silicon oxide film was 47 nm / min
- the etching rate of the silicon nitride film was 53 nm / min. From this result, it was confirmed that the silicon oxide film and the silicon nitride film, which are the objects to be etched, are selectively etched as compared with the photoresist film, which is the object to be etched.
- Example 3 Etching of the test piece in the same manner as in Example 1 except that 1,1,1,4,4,4-hexafluoro-2-butene of Sample 1-3 was used instead of Sample 1-1. Was performed, and the etching rate of each film was calculated.
- the etching rate of the photoresist film was 5 nm / min
- the etching rate of the silicon oxide film was 55 nm / min
- the etching rate of the silicon nitride film was 59 nm / min. From this result, it was confirmed that the silicon oxide film and the silicon nitride film, which are the objects to be etched, are selectively etched as compared with the photoresist film, which is the object to be etched.
- the etching rate of the photoresist film was 18 nm / min
- the etching rate of the silicon oxide film was 61 nm / min
- the etching rate of the silicon nitride film was 64 nm / min. From this result, it was confirmed that the etching selectivity of the silicon oxide film and the silicon nitride film, which are the objects to be etched, with respect to the photoresist film, which is the object to be etched, is lowered.
- Example 4 A SUS tube having a diameter of 0.5 inch and a length of 10 cm was filled with 10 mL of Molecular Sieve 5A manufactured by Union Showa Co., Ltd. Cylinder B containing 1,1,1,4,4,4-hexafluoro-2-butene of sample 1-2 after standing for 10 days was connected to the above-mentioned SUS tube filled with molecular sheave 5A. Sample 1-2 1,1,1,4,4,4-hexafluoro-2-butene was circulated from the cylinder B to the above SUS tube at a flow rate of 100 mL / min.
- Example 5 to 13 and Comparative Examples 2 to 4 The test piece was etched in the same manner as in Example 1 except that the sample shown in Table 2 was used instead of the sample 1-1, and the etching rate of each film was calculated. The results are shown in Table 2.
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Abstract
Description
本発明は、エッチングガスによるエッチングの対象であるエッチング対象物とエッチングガスによるエッチングの対象ではない非エッチング対象物とを有する被エッチング部材にエッチングガスを接触させてエッチングを行った場合に、非エッチング対象物に比べてエッチング対象物を選択的にエッチングすることができるエッチングガス及びその製造方法、並びに、エッチング方法、半導体素子の製造方法を提供することを課題とする。
[1] 一般式C4HxFyで表され且つ前記一般式中のxが1以上7以下、yが1以上7以下、x+yが8であるフルオロブテンを含有するエッチングガスであって、
フッ化カルボニルを不純物として含有し、フッ化カルボニルの濃度が100質量ppm以下であるエッチングガス。
[3] [1]又は[2]に記載のエッチングガスを製造する方法であって、
水及び酸素ガスを含有する前記フルオロブテンである粗フルオロブテンに脱水処理を施す脱水工程と、
前記粗フルオロブテンに脱酸素ガス処理を施す脱酸素ガス工程と、
を備えるエッチングガスの製造方法。
[5] 前記脱水処理は、前記粗フルオロブテンを吸着剤に接触させて前記吸着剤に水を吸着させる処理である[3]又は[4]に記載のエッチングガスの製造方法。
[10] 前記希釈ガスが、窒素ガス、ヘリウム、アルゴン、ネオン、クリプトン、及びキセノンから選ばれる少なくとも一種である[9]に記載のエッチング方法。
前記被エッチング部材が、前記エッチング対象物及び前記非エッチング対象物を有する半導体基板であり、
前記半導体基板から前記エッチング対象物の少なくとも一部を前記エッチングにより除去する処理工程を備える半導体素子の製造方法。
C4HxFy+(4-(y-x)/4)O2 → (y-x)/2COF2+xHF+(4-(y-x)/2)CO2
〔フルオロブテン〕
本実施形態に係るエッチングガスに含有されるフルオロブテンは、一般式C4HxFyで表されるものであり、且つ、一般式中のxが1以上7以下、yが1以上7以下、x+yが8との3つの条件を満たすものである。フルオロブテンの種類は、上記要件を満たしていれば特に限定されるものではなく、直鎖状のフルオロブテンでも分岐鎖状のフルオロブテン(イソブテン)でも使用可能であるが、フルオロ-1-ブテンに類するものとフルオロ-2-ブテンに類するものが好ましく使用可能である。
エッチングガスは、上記フルオロブテンを含有するガスである。エッチングガスは、上記フルオロブテンのみからなるガスであってもよいし、上記フルオロブテンと希釈ガスを含有する混合ガスであってもよい。希釈ガスは、フルオロブテンや被エッチング部材に対して不活性であることが好ましい。また、上記フルオロブテンと希釈ガスと添加ガスを含有する混合ガスであってもよい。
本実施形態に係るエッチングガスの製造方法は、前述のように、水及び酸素ガスを含有する上記フルオロブテンである粗フルオロブテンに脱水処理を施す脱水工程と、粗フルオロブテンに脱酸素ガス処理を施す脱酸素ガス工程と、を備える。
上記フルオロブテン中の水分濃度の測定方法は特に限定されるものではなく、例えばカールフィッシャー法により定量することができる。
蒸留条件は特に限定されるものではないが、理論段数は1段以上30段以下が好ましく、3段以上10段以下がより好ましい。
蒸留塔の塔頂の温度は特に限定されるものではないが、-60℃以上0℃以下とすることが好ましく、-50℃以上-20℃以下とすることがより好ましい。
上記フルオロブテン中の酸素濃度の測定方法は特に限定されるものではなく、例えばガスクロマトグラフィーにより定量することができる。
充填容器の材質は特に限定されるものではないが、例えば、マンガン鋼、ステンレス鋼、ハステロイ(登録商標)、インコネル(登録商標)が挙げられる。
本実施形態のエッチングは、プラズマを用いるプラズマエッチング、プラズマを用いないプラズマレスエッチングのいずれによっても達成できる。プラズマエッチングとしては、例えば、反応性イオンエッチング(RIE:Reactive Ion Etching)、誘導結合型プラズマ(ICP:Inductively Coupled Plasma)エッチング、容量結合型プラズマ(CCP:Capacitively Coupled Plasma)エッチング、電子サイクロトロン共鳴(ECR:Electron Cyclotron Resonance)プラズマエッチング、マイクロ波プラズマエッチングが挙げられる。
本実施形態に係るエッチング方法におけるエッチング工程の圧力条件は特に限定されるものではないが、10Pa以下とすることが好ましく、5Pa以下とすることがより好ましい。圧力条件が上記の範囲内であれば、プラズマを安定して発生させやすい。一方、エッチング工程の圧力条件は0.05Pa以上であることが好ましい。圧力条件が上記の範囲内であれば、電離イオンが多く発生し十分なプラズマ密度が得られやすい。
エッチングガスの流量は、チャンバーの大きさやチャンバー内を減圧する排気設備の能力に応じて、チャンバー内の圧力が一定に保たれるように適宜設定すればよい。
本実施形態に係るエッチング方法におけるエッチング工程の温度条件は特に限定されるものではないが、高いエッチング選択性を得るためには200℃以下とすることが好ましく、マスク等の非エッチング対象物がエッチングされることをより抑制するためには150℃以下とすることがより好ましく、異方性エッチングを行うためには100℃以下とすることがさらに好ましい。ここで、温度条件の温度とは、被エッチング部材の温度であるが、エッチング装置のチャンバー内に設置された、被エッチング部材を支持するステージの温度を使用することもできる。
本実施形態に係るエッチング方法によりエッチングする被エッチング部材は、エッチング対象物と非エッチング対象物を有するが、エッチング対象物で形成されている部分と非エッチング対象物で形成されている部分とを有する部材でもよいし、エッチング対象物と非エッチング対象物の混合物で形成されている部材でもよい。また、被エッチング部材は、エッチング対象物、非エッチング対象物以外のものを有していてもよい。
エッチング対象物は、ケイ素を含有する材料のみで形成されているものであってもよいし、ケイ素を含有する材料のみで形成されている部分と他の材質で形成されている部分とを有するものであってもよいし、ケイ素を含有する材料と他の材質の混合物で形成されているものであってもよい。ケイ素を含有する材料としては、例えば、酸化ケイ素、窒化ケイ素、ポリシリコン、シリコンゲルマニウム(SiGe)が挙げられる。
また、エッチング対象物の形状は、特に限定されるものではなく、例えば、板状、箔状、膜状、粉末状、塊状であってもよい。
非エッチング対象物は、上記フルオロブテンと実質的に反応しないか、又は、上記フルオロブテンとの反応が極めて遅いため、本実施形態に係るエッチング方法によりエッチングを行っても、エッチングがほとんど進行しないものである。非エッチング対象物は、上記のような性質を有するならば特に限定されるものではないが、例えば、フォトレジスト、アモルファスカーボン(C)、窒化チタン(TiN)や、銅(Cu)、ニッケル(Ni)、コバルト(Co)等の金属や、これら金属の酸化物、窒化物が挙げられる。これらの中でも、取扱性及び入手容易性の観点から、フォトレジスト、アモルファスカーボンがより好ましい。
容量10Lのマンガン鋼製容器に充填された1,1,1,4,4,4-ヘキサフルオロ-2-ブテンを用意した。
容量10Lのマンガン鋼製容器に充填された1,1,1,2,4,4,4-ヘプタフルオロ-2-ブテンを用意した。マンガン鋼製容器から1,1,1,2,4,4,4-ヘプタフルオロ-2-ブテンの気相部を抜き出して酸素濃度を測定したところ、1225質量ppmであった。また、マンガン鋼製容器から1,1,1,2,4,4,4-ヘプタフルオロ-2-ブテンの液相部を抜き出して水分濃度を測定したところ、382質量ppmであった。水分濃度と酸素濃度の測定方法は、前述と同様である。
サンプル2-2のフッ化カルボニルの濃度は268質量ppmであった。
サンプル2-3のフッ化カルボニルの濃度は478質量ppmであり、フッ化水素の濃度は155質量ppmであった。
サンプル2-4のフッ化カルボニルの濃度は653質量ppmであった。
容量10Lのマンガン鋼製容器に充填された2,3,3,4,4,4-ヘキサフルオロ-1-ブテンを用意した。マンガン鋼製容器から2,3,3,4,4,4-ヘキサフルオロ-1-ブテンの気相部を抜き出して酸素濃度を測定したところ、1313質量ppmであった。また、マンガン鋼製容器から2,3,3,4,4,4-ヘキサフルオロ-1-ブテンの液相部を抜き出して水分濃度を測定したところ、411質量ppmであった。水分濃度と酸素濃度の測定方法は、前述と同様である。
サンプル3-2のフッ化カルボニルの濃度は235質量ppmであった。
サンプル3-3のフッ化カルボニルの濃度は411質量ppmであり、フッ化水素の濃度は408質量ppmであった。
サンプル3-4のフッ化カルボニルの濃度は603質量ppmであった。
容量10Lのマンガン鋼製容器に充填された1,1,3,3,4,4,4-ヘプタフルオロ-1-ブテンを用意した。マンガン鋼製容器から1,1,3,3,4,4,4-ヘプタフルオロ-1-ブテンの気相部を抜き出して酸素濃度を測定したところ、1003質量ppmであった。また、マンガン鋼製容器から1,1,3,3,4,4,4-ヘプタフルオロ-1-ブテンの液相部を抜き出して水分濃度を測定したところ、391質量ppmであった。水分濃度と酸素濃度の測定方法は、前述と同様である。
サンプル4-2のフッ化カルボニルの濃度は268質量ppmであった。
サンプル4-3のフッ化カルボニルの濃度は437質量ppmであり、フッ化水素の濃度は36質量ppmであった。
サンプル4-4のフッ化カルボニルの濃度は622質量ppmであった。
なお、各サンプルのフッ化カルボニルとフッ化水素の濃度を、表1に示す。
半導体ウェハの表面上に、厚さ1000nmのシリコン酸化膜と、厚さ1000nmのシリコン窒化膜と、厚さ1000nmのフォトレジスト膜とを、積層せず、それぞれ表面に露出するように形成して、これを試験体とした。そして、サンプル1-1の1,1,1,4,4,4-ヘキサフルオロ-2-ブテンを用いて、試験体のエッチングを行った。
サンプル1-1の代わりにサンプル1-2の1,1,1,4,4,4-ヘキサフルオロ-2-ブテンを用いた点を除いては、実施例1と同様にして試験体のエッチングを行い、それぞれの膜のエッチング速度を算出した。
サンプル1-1の代わりにサンプル1-3の1,1,1,4,4,4-ヘキサフルオロ-2-ブテンを用いた点を除いては、実施例1と同様にして試験体のエッチングを行い、それぞれの膜のエッチング速度を算出した。
サンプル1-1の代わりにサンプル1-4の1,1,1,4,4,4-ヘキサフルオロ-2-ブテンを用いた点を除いては、実施例1と同様にして試験体のエッチングを行い、それぞれの膜のエッチング速度を算出した。
直径0.5インチ、長さ10cmのSUS製チューブに、ユニオン昭和株式会社製のモレキュラーシーブ5Aを10mL充填した。10日間静置後のサンプル1-2の1,1,1,4,4,4-ヘキサフルオロ-2-ブテンが入ったシリンダーBを、モレキュラーシーブ5Aを充填した上記SUS製チューブに接続し、シリンダーBから上記SUS製チューブへサンプル1-2の1,1,1,4,4,4-ヘキサフルオロ-2-ブテンを100mL/minの流量で流通した。そして、上記SUS製チューブの内部を通って出口から出てきた1,1,1,4,4,4-ヘキサフルオロ-2-ブテンのフッ化カルボニルとフッ化水素の濃度を測定した。測定方法は前述と同様である。その結果、フッ化カルボニルの濃度、フッ化水素の濃度ともに、10質量ppm未満であった。
サンプル1-1の代わりに、表2に記載のサンプルを用いた点を除いては、実施例1と同様にして試験体のエッチングを行い、それぞれの膜のエッチング速度を算出した。結果を、表2に示す。
2・・・希釈ガス供給部
3・・・フルオロブテンガス流量制御装置
4・・・希釈ガス流量制御装置
5・・・フルオロブテンガス供給用配管
6・・・希釈ガス供給用配管
7・・・フルオロブテンガス圧力制御装置
8・・・希釈ガス圧力制御装置
10・・・チャンバー
11・・・ステージ
12・・・被エッチング部材
13・・・排気用配管
14・・・温度計
15・・・真空ポンプ
16・・・圧力計
Claims (11)
- 一般式C4HxFyで表され且つ前記一般式中のxが1以上7以下、yが1以上7以下、x+yが8であるフルオロブテンを含有するエッチングガスであって、
フッ化カルボニルを不純物として含有し、フッ化カルボニルの濃度が100質量ppm以下であるエッチングガス。 - フッ化水素を不純物としてさらに含有し、フッ化水素の濃度が100質量ppm以下である請求項1に記載のエッチングガス。
- 請求項1又は請求項2に記載のエッチングガスを製造する方法であって、
水及び酸素ガスを含有する前記フルオロブテンである粗フルオロブテンに脱水処理を施す脱水工程と、
前記粗フルオロブテンに脱酸素ガス処理を施す脱酸素ガス工程と、
を備えるエッチングガスの製造方法。 - 前記脱水工程を行った後に前記脱酸素ガス工程を行う請求項3に記載のエッチングガスの製造方法。
- 前記脱水処理は、前記粗フルオロブテンを吸着剤に接触させて前記吸着剤に水を吸着させる処理である請求項3又は請求項4に記載のエッチングガスの製造方法。
- 前記脱水工程及び前記脱酸素ガス工程が実施された前記フルオロブテンを充填容器に充填する充填工程をさらに備える請求項3~5のいずれか一項に記載のエッチングガスの製造方法。
- 請求項1又は請求項2に記載のエッチングガスを、前記エッチングガスによるエッチングの対象であるエッチング対象物と前記エッチングガスによるエッチングの対象ではない非エッチング対象物とを有する被エッチング部材に接触させ、前記非エッチング対象物に比べて前記エッチング対象物を選択的にエッチングするエッチング工程を備え、前記エッチング対象物がケイ素を含有するエッチング方法。
- 前記エッチングガスが充填容器に充填されており、前記充填容器内の気相部は、フッ化カルボニルの濃度が100質量ppm以下であり、前記エッチング工程においては、前記充填容器から前記気相部を抜き出し前記被エッチング部材に接触させて前記エッチング対象物をエッチングする請求項7に記載のエッチング方法。
- 前記エッチングガスが、前記フルオロブテンのみからなるガス、又は、前記フルオロブテンと希釈ガスを含有する混合ガスである請求項7又は請求項8に記載のエッチング方法。
- 前記希釈ガスが、窒素ガス、ヘリウム、アルゴン、ネオン、クリプトン、及びキセノンから選ばれる少なくとも一種である請求項9に記載のエッチング方法。
- 請求項7~10のいずれか一項に記載のエッチング方法を用いて半導体素子を製造する半導体素子の製造方法であって、
前記被エッチング部材が、前記エッチング対象物及び前記非エッチング対象物を有する半導体基板であり、
前記半導体基板から前記エッチング対象物の少なくとも一部を前記エッチングにより除去する処理工程を備える半導体素子の製造方法。
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JP2015533029A (ja) * | 2012-10-30 | 2015-11-16 | レール・リキード−ソシエテ・アノニム・プール・レテュード・エ・レクスプロワタシオン・デ・プロセデ・ジョルジュ・クロード | 高アスペクト比酸化物エッチング用のフルオロカーボン分子 |
JP2014185111A (ja) * | 2013-03-25 | 2014-10-02 | Nippon Zeon Co Ltd | 高純度2,2−ジフルオロブタン |
JP2017092357A (ja) * | 2015-11-16 | 2017-05-25 | セントラル硝子株式会社 | ドライエッチングガスおよびドライエッチング方法 |
WO2017169809A1 (ja) * | 2016-03-30 | 2017-10-05 | 日本ゼオン株式会社 | フィルターおよびその製造方法、並びに、ドライエッチング用装置およびドライエッチング方法 |
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JPWO2022080271A1 (ja) | 2022-04-21 |
TW202224017A (zh) | 2022-06-16 |
CN116325088A (zh) | 2023-06-23 |
IL302125A (en) | 2023-06-01 |
TWI796803B (zh) | 2023-03-21 |
KR20230066073A (ko) | 2023-05-12 |
EP4231333A1 (en) | 2023-08-23 |
US20230374381A1 (en) | 2023-11-23 |
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