WO2005086214A1 - 基板洗浄用2流体ノズル及び基板洗浄装置 - Google Patents
基板洗浄用2流体ノズル及び基板洗浄装置 Download PDFInfo
- Publication number
- WO2005086214A1 WO2005086214A1 PCT/JP2005/004072 JP2005004072W WO2005086214A1 WO 2005086214 A1 WO2005086214 A1 WO 2005086214A1 JP 2005004072 W JP2005004072 W JP 2005004072W WO 2005086214 A1 WO2005086214 A1 WO 2005086214A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- outlet
- cross
- cleaning
- sectional area
- fluid nozzle
- Prior art date
Links
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 at least one potential-jump barrier or surface barrier, e.g. PN junction, depletion layer or carrier concentration layer
- H01L21/18—Manufacture or treatment of semiconductor devices or of parts thereof the devices having at least one potential-jump barrier or surface barrier, e.g. PN junction, depletion layer or carrier concentration layer the devices having semiconductor bodies comprising elements of Group IV of the Periodic System 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
- H01L21/304—Mechanical treatment, e.g. grinding, polishing, cutting
-
- 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
- H01L21/67—Apparatus specially adapted for handling semiconductor or electric solid state devices during manufacture or treatment thereof; Apparatus specially adapted for handling wafers during manufacture or treatment of semiconductor or electric solid state devices or components ; Apparatus not specifically provided for elsewhere
- H01L21/67005—Apparatus not specifically provided for elsewhere
- H01L21/67011—Apparatus for manufacture or treatment
- H01L21/67017—Apparatus for fluid treatment
- H01L21/67028—Apparatus for fluid treatment for cleaning followed by drying, rinsing, stripping, blasting or the like
- H01L21/6704—Apparatus for fluid treatment for cleaning followed by drying, rinsing, stripping, blasting or the like for wet cleaning or washing
- H01L21/67051—Apparatus for fluid treatment for cleaning followed by drying, rinsing, stripping, blasting or the like for wet cleaning or washing using mainly spraying means, e.g. nozzles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/21—Mixing gases with liquids by introducing liquids into gaseous media
- B01F23/213—Mixing gases with liquids by introducing liquids into gaseous media by spraying or atomising of the liquids
- B01F23/2132—Mixing gases with liquids by introducing liquids into gaseous media by spraying or atomising of the liquids using nozzles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B7/00—Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas
- B05B7/02—Spray pistols; Apparatus for discharge
- B05B7/04—Spray pistols; Apparatus for discharge with arrangements for mixing liquids or other fluent materials before discharge
- B05B7/0416—Spray pistols; Apparatus for discharge with arrangements for mixing liquids or other fluent materials before discharge with arrangements for mixing one gas and one liquid
- B05B7/0433—Spray pistols; Apparatus for discharge with arrangements for mixing liquids or other fluent materials before discharge with arrangements for mixing one gas and one liquid with one inner conduit of gas surrounded by an external conduit of liquid upstream the mixing chamber
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B08—CLEANING
- B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
- B08B3/00—Cleaning by methods involving the use or presence of liquid or steam
- B08B3/02—Cleaning by the force of jets or sprays
-
- Y—GENERAL 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S134/00—Cleaning and liquid contact with solids
- Y10S134/902—Semiconductor wafer
Definitions
- the present invention relates to a two-fluid nozzle for cleaning a substrate used for a cleaning process for removing contaminants adhering to the surface of, for example, a semiconductor substrate, and a substrate cleaning device provided with the two-fluid nozzle for cleaning a substrate. It concerns the device.
- a semiconductor wafer (hereinafter, referred to as a "wafer") is washed with a cleaning solution such as a chemical solution or pure water, and contamination of particles, organic contaminants, and metal impurities adhered to the wafer.
- a substrate cleaning device that removes shion is used.
- a substrate cleaning device which uses a two-fluid nozzle to form a cleaning liquid in droplet form and sprays the liquid onto the surface of the substrate.
- a two-fluid nozzle for cleaning a substrate is an internal mixing type in which a gas and a liquid are mixed inside the nozzle to form a droplet, and a gas and a liquid are mixed outside the nozzle to form a droplet.
- An external mixed type is known (for example, see Patent Document 1).
- an internal mixing type there has been proposed a type in which droplets and gas formed inside are passed through a straight pipe to accelerate the droplets, and are jetted into the air at a sufficient speed ( For example, see Patent Document 2).
- Patent document 1 Japanese Patent Application Laid-Open No. 2003-197597
- Patent Document 2 Japanese Patent No. 3315611
- the droplets are not sufficiently atomized or if the droplets are collected into large droplets, the number of droplets is small and the contaminant removal performance is low. Is a problem.
- the gas flow rate is increased to accelerate the droplets at high speed in order to improve the contaminant removal performance, the wafer surface will be damaged because large droplets are also ejected at high speed. Therefore, there was a limit to the improvement of the contaminant removal performance.
- the internal mixing type nozzle has a problem in that the jetting speed of the droplets varies greatly. High-speed droplets risk damaging the surface of the wafer. Also, low-speed droplets have a problem of poor contaminant removal performance.
- An object of the present invention is to suitably clean a substrate using a two-fluid nozzle for cleaning a substrate and a two-fluid nozzle for cleaning a substrate that can make the particle diameter and speed of droplets uniform. It is an object of the present invention to provide a substrate cleaning apparatus capable of performing the above.
- a two-fluid nozzle for cleaning a substrate in which a gas and a liquid are mixed inside and a droplet is ejected with the gas to clean the substrate.
- a liquid supply path for supplying liquid, a liquid supply path for supplying liquid, and a discharge path for discharging droplets formed inside, and an ejection port for discharging the liquid droplets to the outside is provided at a tip of the discharge path.
- the cross-sectional area Sb of the injection port is formed smaller than the cross-sectional area Sa of the outlet passage, and the cross-sectional area of the outlet of the gas supply passage Se is formed smaller than the cross-sectional area Sa of the outlet passage.
- a unique two-fluid nozzle for cleaning substrates is provided.
- the ratio Sa: Sb of the cross-sectional area Sa of the outlet passage to the cross-sectional area Sb of the injection port is 1: 0.25-0.
- the cross-sectional area Sc of the outlet of the gas supply path may be equal to or smaller than the cross-sectional area Sb of the injection port.
- the ratio Sb: Sc of the cross-sectional area Sb of the injection port to the cross-sectional area Sc of the outlet of the gas supply path may be 1: 0.16-0.87.
- the cross-sectional area Sc of the outlet of the gas supply path may be 1.13-6.16 mm 2 .
- the cross-sectional area Sc of the exit of the gas supply passage, 1. 77-4. May be 91 mm 2.
- the guide path may be formed linearly, and the sectional area Sa of the guide path may be constant.
- the length L1 of the guide path may be 10 to 90 mm.
- the length L2 of the injection port may be 30 mm or less.
- the two-fluid nozzle for cleaning a substrate according to the present invention includes, for example, an annular liquid introduction path surrounding the gas supply path, the gas supply path is arranged coaxially with the lead-out path, and the liquid supply path is provided.
- An opening is formed in the outer peripheral surface of the liquid introduction path, and a taper portion is formed in the liquid introduction path, the diameter of which decreases toward the distal end, and the taper portion is provided between the gas supply path and the outlet path.
- a configuration may be adopted in which the droplets are formed by mixing the gas supplied from the gas supply path and the liquid introduced from the liquid introduction path to form droplets, and the droplets are derived through the discharge path.
- the injection port may be formed such that the vertical cross-sectional shape of the peripheral edge on the outlet side is a right angle or an acute angle.
- the two-fluid nozzle for cleaning a substrate a spin chuck for holding the substrate substantially horizontally, and a drive mechanism for moving the two-fluid nozzle for cleaning over the substrate.
- a substrate cleaning apparatus characterized by comprising:
- the droplet can be sufficiently finely divided. Even if large droplets are formed on the inner wall of the outlet passage during the outlet passage, the droplets are re-atomized at the injection port, and the droplet diameter becomes uniform. Also, by setting the diameters of the outlet path, the injection port, the liquid supply path, and the gas supply path to appropriate sizes, the liquid and gas are mixed at an appropriate flow rate, and the droplets are sufficiently finely sprayed. be able to. By setting the outlet path and the injection port to appropriate lengths, sufficiently atomized droplets can be jetted at an appropriate speed.
- the contaminant removal performance of the two-fluid nozzle for cleaning substrates can be improved. Further, the speed of the droplet can be made uniform. Further, according to the substrate cleaning apparatus of the present invention, the performance of removing contaminants can be improved without damaging the substrate surface.
- FIG. 1 is a schematic vertical sectional view of a cleaning apparatus according to an embodiment of the present invention.
- FIG. 2 is a schematic plan view of a cleaning device according to the present embodiment.
- FIG. 3 is a schematic longitudinal sectional view of a two-fluid nozzle working on the present embodiment.
- FIG. 4 is an explanatory diagram showing an internal configuration of a two-fluid nozzle.
- FIG. 6 is an explanatory diagram of a gas supply pipe and a liquid supply pipe.
- FIG. 7 is an enlarged longitudinal sectional view showing a shape of a tip portion of a two-fluid nozzle that works in another embodiment.
- ⁇ 8] is an explanatory view of an embodiment in which an injection port or a throttle portion is formed in a plurality of holes (porous).
- FIG. 9 is a photograph showing a mist generation state when the diameter c of the outlet of the gas supply path is 1.5 mm, 2. Omm, and 3. Omm.
- a substrate cleaning apparatus 1 configured to clean the surface of a wafer W as an example of a substrate.
- a substrate cleaning apparatus 1 that is powerful in the embodiment of the present invention mixes a gas and a liquid inside a spin chuck 2 that holds a substantially disk-shaped wafer W substantially horizontally. And ejects droplets with gas A two-fluid nozzle 5 according to an embodiment of the present invention and a cup 6 surrounding the wafer W held by the spin chuck 2 are provided.
- the spin chuck 2 has three holding members 10 on the upper part, and the three holding members 10 are brought into contact with three peripheral edges of the wafer W, respectively. It holds the wafer W.
- the spin chuck 2 is connected to a motor 12. When the motor 12 is driven, the spin chuck 2 is rotated, and the wafer W is rotated integrally with the spin chuck 2 in a substantially horizontal plane.
- the two-fluid nozzle 5 is attached to the tip of a nozzle arm 15 arranged substantially horizontally above the wafer W held by the spin chuck 2.
- the base end of the nozzle arm 15 is fixed to a rotating shaft 16 arranged substantially vertically outside the cup 6, and a driving unit 17 is connected to the rotating shaft 16.
- the drive mechanism 18 for moving the two-fluid nozzle 5 is composed of the nozzle arm 15, the rotary shaft 16, and the drive unit 17.
- the nozzle arm 15 is rotated about a rotation axis 16 in a substantially horizontal plane, and the two-fluid nozzle 5 is integrated with the nozzle arm 15 at least from above the central portion of the wafer W. It can be moved up to the periphery.
- the rotating shaft 16 can be moved up and down by driving the driving unit 17, and the two-fluid nozzle 5 can be moved up and down integrally with the nozzle arm 15 and the rotating shaft 16.
- the two-fluid nozzle 5 is provided inside the two-fluid nozzle 5 with, for example, nitrogen (N).
- a gas supply path 21 for supplying gas a liquid supply path 22 for supplying a liquid such as pure water (DIW) into the two-fluid nozzle 5, and a droplet D formed inside the two-fluid nozzle 5.
- DIW pure water
- An ejection port 24 for ejecting the droplet D to the outside is formed at the tip of the outlet path 23.
- the gas supply path 21 is arranged coaxially with the outlet path 23.
- a throttle 31 is formed at the outlet of the gas supply passage 21.
- the constricted portion 31 is formed to have a smaller cross-sectional area than the upstream portion.
- the outlet of the throttle 31 is arranged close to the inlet of the outlet channel 23.
- the cross-sectional area of the throttle 31 is preferably constant from the inlet to the outlet, and the cross-sectional shape of the throttle 31 is preferably, for example, circular or elliptical. As shown, if the cross-sectional area of the constricted portion 31 is constant from the inlet to the outlet, the cross-sectional area Sc of the outlet of the gas supply passage 23 is equal to the cross-sectional area of the constricted portion 31.
- an annular liquid introduction path 32 is formed so as to surround the throttle 31 of the gas supply path 21.
- the liquid supply path 22 is connected to the liquid introduction path 32 so that pure water is supplied to the liquid introduction path 32.
- the gas supply passage 21 is arranged so as to pass through the inside of the liquid introduction passage 32.
- the liquid introduction passage 32 is formed in a cylindrical shape having an annular cross-sectional shape.
- the liquid introduction passage 32 is formed with an annular groove 36 and a tapered portion 37 formed such that the inner diameter and the outer diameter become smaller toward the distal end (downward in FIG. 3).
- the tapered portion 37 is formed on the distal end side of the annular groove 36, and the outlet of the tapered portion 37 opens in an annular shape between the outlet of the throttle portion 31 of the gas supply passage 21 and the inlet of the outlet passage 23. I have. Therefore, the pure water introduced into the liquid introduction passage 32 mixes with the nitrogen gas supplied from the constricted portion 31 of the gas supply passage 21 near the inlet of the outlet passage 23 to form a droplet D. I have. The proximal end (the upper side in FIG. 3) of the liquid introduction passage 32 is closed. The inclination of the tapered portion 37 should be, for example, approximately 45 ° with respect to the gas supply passage 21 and the outlet passage 23! ,.
- the liquid supply path 22 is provided at an appropriate angle with respect to the annular groove 36 of the liquid introduction path 32, and opens on the outer peripheral surface of the annular groove 36.
- the liquid supply passage 22 is provided at a substantially perpendicular angle to the outer peripheral surface of the annular groove 36 substantially parallel to the gas supply passage 21.
- a throttle portion 38 is formed at the outlet of the liquid supply passage 22.
- the throttle portion 38 is formed in an orifice shape having a smaller cross-sectional area than the upstream portion.
- the outlet of the throttle section 38 is provided so as to open to the inner surface of the annular groove 36.
- the cross-sectional area of the constricted portion 38 is preferably constant from the entrance to the exit, and the cross-sectional shape of the constricted portion 38 is preferably, for example, circular or elliptical. As shown in the figure, when the cross-sectional area of the throttle section 38 is constant from the inlet to the outlet, the cross-sectional area Sd of the outlet of the liquid supply passage 22 is equal to the cross-sectional area of the throttle section 38.
- the outlet passage 23 is disposed coaxially with the throttle 31 of the gas supply passage 21 as described above, and communicates with the gas supply passage 21 and the liquid introduction passage 32. It is preferable that the outlet 23 is formed in a straight line, and that the cross-sectional area Sa of the outlet 23 is constant from the inlet to the outlet.
- the surface shape is preferably, for example, circular or elliptical. As shown in Fig. 4, the nitrogen gas N supplied from the gas supply path 21 and the DIW DIW introduced from the liquid introduction path 32 were introduced.
- the water is mixed near the inlet of the outlet 23, whereby innumerable droplets of pure water D are formed, and the formed droplets D are discharged through the outlet 23 together with the nitrogen gas N.
- the injection port 24 has a smaller sectional area than the outlet path 23 and is formed in an orifice shape. As described above, in the case where the cross-sectional area is smaller than that of the outlet channel 23 and the orifice-shaped injection port 24 is not provided, the mist-shaped droplet D grown along the inner wall of the outlet channel 23 is discharged as it is.
- the cross-sectional area Sb of the injection port 24 is preferably constant from the inlet to the outlet, and the cross-sectional shape of the injection port 24 is preferably, for example, circular or elliptical.
- the droplet D passing through the outlet channel 23 is atomized again and ejected while passing through the ejection port 24. Therefore, even if the droplet D grows large while moving along the inner wall of the outlet channel 23, the droplet D can be made to have a sufficiently small particle size by passing through the injection port 24. It can be sprayed.
- the two-fluid nozzle 5 is formed so that the vertical cross-sectional shape of a portion along the outlet side peripheral edge of the injection port 24 is a right angle. That is, it is preferable that the inner surface of the injection port 24 and the outer surface of the tip of the two-fluid nozzle 5 are formed to be perpendicular to each other. This makes it easier for the droplet D ejected from the ejection port 24 to proceed straight in the direction in which the outlet path 23 and the ejection port 24 face.
- the droplet D will follow the rounded or tapered surface. Then, the liquid droplet D jumps out obliquely with respect to the injection port 24, and the number of the droplets D increases outward of the injection port 24.
- the straightness of the droplet D is improved, and the droplet D can be intensively and intensively jetted to the wafer W. Can be improved. Even if the outlet edge of the injection port 24 is formed at an acute angle, the straightness of the droplet D is similarly improved.
- the two-fluid nozzle 5 has a gas supply path 21, an outlet path 23, and an injection port 24 oriented in a direction perpendicular to the upper surface of the wafer W held by the spin chuck 2. It is supported at the tip of the nozzle arm 15 by force. That is, the jet of the droplet D is jetted substantially perpendicularly to the upper surface of the wafer W. [0025] If the length LI of the outlet path 23 in the flow direction of the droplets D is too long, the droplets D moving along the inner wall of the outlet path 23 tend to gather and become large.
- the length L1 of the outlet passage 23 is preferably about 10 to 90 mm.
- the formation of the droplet D near the entrance of the outlet channel 23 is not performed properly, and the formed droplet D may be larger than the desired particle size. Therefore, it is necessary to form the cross-sectional area Sa of the outlet channel 23 to an appropriate size so that the droplet D can be supplied to the injection port 24 in a sufficiently atomized state.
- the diameter a of the outlet channel 23 is preferably about 117 mm, and more preferably about 315 mm.
- the cross-sectional area of the outlet channel 23 is preferably about 0.785-38.5 mm 2 , and more preferably about 7.07-19. 6mm 2 about is good.
- the formation of the droplet D in the vicinity of the entrance of the lead-out path 23 is not suitably performed, and the formed droplet D may be larger than a desired particle diameter.
- the cross-sectional area S b of the injection port 24 is too large, the injection speed of the droplet D from the injection port 24 becomes slow, and the droplet D may not be sufficiently re-fine-granulated at the injection port 24. There is. Therefore, it is necessary to form the cross-sectional area Sb of the injection port 24 to an appropriate size so that the droplet D can be jetted at a sufficient speed in a sufficiently small and atomized state.
- the diameter b of the injection port 24 is preferably about 0.5-6 mm, and more preferably about 2-4 mm. If the injection port 24 has a cross-sectional shape other than a circle, such as an ellipse, If the cross-sectional area Sb of the injection port 24 is between about 0. 996- 28. 3mm 2 about well, even more preferably, about 3. 14- 12. 6mm 2 about good.
- the uniformity of the mist speed is high, it is difficult to re-fine the mist because the squeeze is loose. As a result, a large amount of large diameter mist is discharged. For this reason, the number of mist is reduced, and as a result, the cleaning performance is lowered, which is not preferable.
- b 0.5a-0.9a
- the ratio of the cross-sectional area of the output channel 23 to the cross-sectional area of the injection port 24 is 1 : 0.25-0.81 is preferred.
- the length L2 of the injection port 24 in the flow direction of the droplet D is formed shorter than the length L1 of the outlet path 23. If the length L2 of the injection port 24 is too long, the droplets D that move along the inner wall of the injection port 24 may collect and become large. Therefore, the length L2 of the injection port 24 must be set to an appropriate length.
- the length L2 of the injection port 24 is preferably about 30 mm or less.
- the droplet D cannot be sufficiently accelerated in the outlet channel 23, and the ejection speed of the droplet D from the ejection port 24 is reduced.
- the cross-sectional area Sc at the outlet of the gas supply passage 21 is too large, the formation of the droplet D in the vicinity of the inlet of the outlet passage 23 is not performed properly, and the formed droplet D is larger than the desired particle size. May become Therefore, it is necessary to form the cross-sectional area Sc at the outlet of the gas supply passage 21 to an appropriate size so that the droplet D can be sufficiently accelerated in a sufficiently small and finely divided state.
- the cross-sectional area Sc is preferably formed smaller than the cross-sectional area Sa of the lead-out passage 23.
- the effect of mistying pure water DIW introduced from entrance 32 is increased. It also has the effect of equalizing the mist speed.
- the diameter c of the outlet (the constricted portion 31) of the gas supply channel 21 is preferably about 1.2 to 2.8 mm, and more preferably about 1.2 to 2.8 mm. 1. 5-2. 5mm is good.
- FIG. 5 is a graph showing the relationship between the diameter c and the cleaning performance (particle removal performance) when the cross-sectional shape of the outlet of the gas supply path 21 was examined in an example described later. It can be seen that the cleaning performance is high when the diameter c is about 1.2 to 2.5 mm, preferably about 1.5 to 2.5 mm.
- Sectional shape elliptical outlet of the gas supply passage 21 or the like when a shape other than a circle, the cross-sectional area Sc of the exit of the gas supply passage 21 (throttle portion 31) is about 1. 13-6. 16 mm 2 around the Good, more preferably about 1.77-4.19 mm 2 . Further, it is preferable that the cross-sectional area Sc of the outlet of the gas supply path 21 (throttle section 31) is formed to have the same force as the cross-sectional area Sb of the injection port 24 or smaller than the cross-sectional area Sb of the injection port 24.
- the cross-sectional area Sc of the outlet (throttle section 31) of the gas supply path 21 is set to be equal to or smaller than the cross-sectional area Sb of the injection port 24, and the nitrogen gas N It is effective to increase the flow rate of N in the mixing section of pure water and DIW. Especially miniaturization
- the diameter b of the injection port 24 is 3 mm, and if c is 0.4b, the N supply pressure is normally used.
- the mist flow rate becomes slow, and sufficient cleaning power cannot be obtained, which is not preferable.
- the diameter c of the outlet (throttle section 31) of the gas supply channel 21 is c> 0.93b, the N flow rate in the mixing section is low,
- Either the cross-sectional shape of the outlet of the supply path 21 or the cross-sectional shape of the injection port 24 is elliptical or other than circular
- the flow rate of the nitrogen gas N flowing out from the outlet of the gas supply path 21 (throttle section 31) is, for example, about 5
- the flow rate of the nitrogen gas N supplied from the outlet of the gas supply channel 21 (throttle portion 31) is changed by the pure water DIW supplied from the outlet of the liquid supply channel 22 (throttle portion 38).
- the cross-sectional area Sd of the outlet of the liquid supply passage 22 that is, the cross-sectional area of the constricted portion 38 is too small, the flow rate of the pure water DIW flowing out of the constricted portion 38 is limited to a small amount. Thus, the number of droplets D formed is reduced. Conversely, if the cross-sectional area Sd at the outlet of the liquid supply passage 22 is too large, the formed droplets D may be larger than desired. Therefore, it is necessary to form the droplets D with the desired number and particle size by forming the cross-sectional area Sd of the outlet of the liquid supply passage 22 (throttle portion 38) to an appropriate size.
- the diameter d of the outlet of the liquid supply channel 22 (throttle portion 38) is preferably about 0.5-5 mm, more preferably. Should be about 11 to 3 mm.
- the cross-sectional shape of the outlet of the liquid supply passage 22 (throttle portion 38) is a shape other than a circle such as an ellipse
- the cross-sectional area Sd of the outlet of the liquid supply passage 22 (throttle portion 38) is about 0.196-19. . 6 25 mm 2 around the well, and more preferably, from about 0. 785- 7. 065mm 2 about good.
- the flow rate of the pure water DIW which also supplies the force of the constricting section 38 (liquid supply path 22)
- the number of the droplets D is small
- the cleaning effect is reduced.
- the flow rate of the DIW DIW supplied from the constriction unit 38 is large, it is difficult to sufficiently form the droplet D into fine particles, and the average particle diameter of the droplet D becomes large.
- the flow rate of the DIW DIW supplied from the restrictor 38 is preferably, for example, about 20 to 500 mLZmin., And more preferably about 100 to 200 mLZmin.
- the two-fluid nozzle 5 includes a nozzle main body 41 in which a liquid supply passage 22, a liquid introduction passage 32, a discharge passage 23, and an injection port 24 are formed, and a nozzle in which a gas supply passage 21 is formed. It is constituted by an engagement member 42 that is engaged with the main body 41. On the base end side of the nozzle main body 41, a hollow portion 43 formed in a circular cross section and opening to the outer surface on the base end side of the nozzle main body 41 is formed. The outlet path 23 is formed on the tip side of the nozzle body 41. The cavity 43 is formed coaxially with the guide path 23.
- a tapered surface 45 is formed between the tip of the cavity 43 and the entrance of the outlet passage 23 so that the force on the cavity 43 side also narrows toward the outlet passage 23 side.
- a thread groove 46 is formed on the opening side of the cavity 43.
- the liquid supply passage 22 opens on the inner surface of the cavity 43 between the tapered surface 45 and the thread groove 46.
- the engaging member 42 is composed of an insert 51 inserted into the hollow portion 43 and a head 52 disposed on the base end side of the nozzle body 41.
- the insert 51 is, for example, a large cylindrical portion 53 having an outer diameter substantially the same as the inner diameter of the hollow portion 43, and a large cylindrical portion 53 provided at the distal end of the large cylindrical portion 53.
- a small cylindrical portion 54 having a smaller outer diameter and a cylindrical shape, and a truncated cone portion 55 formed at the distal end of the small cylindrical portion 54 so as to be tapered toward the distal end with a reduced force 55 It has.
- On the outer surface of the large cylindrical portion 53 there is provided a screw groove 56 which is screwed with the screw groove 46 of the hollow portion 43.
- the head 52 has an outer diameter larger than the inner diameter of the cavity 43 and the outer diameter of the large column 53.
- the gas supply passage 21 is provided so as to pass through the central part of the large cylinder part 53, the small cylinder part 54, and the truncated cone part 55 from the base end side surface of the head body 52, and the outlet of the throttle part 31 is connected to the truncated cone part.
- the portion 55 is formed so as to open to the plane at the tip of the portion.
- An annular gap that is, a liquid introduction passage 32 is formed in the hole.
- An annular gap that is, a tapered portion 37 is formed between the outer surface of the truncated cone portion 55 and the tapered surface 45.
- the head 52 is provided so as to close the cavity 43 and to be in close contact with the surface around the opening of the cavity 43.
- a fluorine resin such as PTFE (polytetrafluoroethylene), for example.
- PTFE polytetrafluoroethylene
- a gas supply pipe 62 for supplying nitrogen gas from a nitrogen gas supply source 61 is connected to the gas supply path 21.
- the gas supply pipe 62 is provided with a flow meter 63, a flow control valve 65, and a filter 66, and the nitrogen gas supply source 61 side force is also interposed in this order.
- a liquid supply pipe 72 for supplying pure water from a pure water supply source 71 is connected to the liquid supply path 22.
- a flow meter 73, a flow control valve 75, and a filter 76 are provided, and the pure water supply source 71 side force is also provided in this order.
- a flow control valve 65 and a control unit 80 for outputting a command for operating the flow control valve 75 are provided.
- the flow rate detected by the flow meters 63 and 73 is monitored by the control unit 80.
- the controller 80 outputs a command to adjust the opening of the flow control valve 65 based on the detected flow rate of the flow meter 63 so that the nitrogen gas flows into the gas supply pipe 62 at a desired flow rate.
- the control unit 80 outputs a command to adjust the opening of the flow control valve 75 based on the detected flow rate of the flow meter 73 so that the pure water flows in the liquid supply pipe 72 at a desired flow rate. It's like that.
- the wafer W is still cleaned by a transfer arm (not shown).
- the wafer W is loaded into the cleaning apparatus 1, and the wafer W is transferred to the spin chuck 2 as shown in FIG. Hand over.
- the wafer W is held by the spin chuck 2 with the front surface (the surface on which the pattern is formed) as the upper surface.
- the two-fluid nozzle 5 and the nozzle arm 15 are retracted outside the cup 6, as shown by the two-dot chain line in FIG.
- the driving unit 17 is driven to rotate the nozzle arm 15, and as shown by the solid line in FIG. It is moved above wafer W to start spraying droplet D.
- the spin chuck 2 is rotated by driving the motor 12 shown in FIG. Then, while moving the two-fluid nozzle 5 from above the central portion of the wafer W to above the peripheral portion of the wafer W, a jet is jetted against the surface of the rotating wafer W. As a result, a jet is sprayed on the entire surface of the wafer W, and contaminants adhering to the surface of the wafer W are removed.
- the jet is formed as described below.
- the flow control valve 65 is opened to allow the nitrogen gas N supplied from the nitrogen gas supply source 61 to flow through the gas supply pipe 62 and the gas supply path 21.
- the desired value is controlled by adjusting the flow control valve 65 based on the detection value of the one 63. Therefore, the nitrogen gas N can be supplied to the gas supply path 21 at an appropriate flow rate.
- the nitrogen gas N that has passed through the gas supply channel 21 is released from the throttle 31 as shown in Fig. 4.
- the pure water DIW supplied from the pure water supply source 71 flows through the liquid supply path 22.
- the flow rate of the DIW DIW in the liquid supply pipe 72 is controlled to a desired value by adjusting the flow control valve 75 based on the detection value of the flow meter 73 according to a command from the control unit 80. Therefore, pure water DIW can be supplied to the liquid supply path 22 at an appropriate flow rate.
- the pure water DIW that has passed through the liquid supply channel 22 is discharged from the throttle portion 38 in a substantially vertical direction toward the annular groove 36 of the liquid introduction channel 32 and flows into the annular groove 36 as shown in FIG.
- the annular water 36 extends annularly along the inner surface of the annular groove 36, and the DIW DIW flows annularly into the entire tapered portion 37. Then, pure water DIW is obliquely discharged from the tapered portion 37 toward the entrance of the outlet passage 23.
- the nitrogen gas N2 that has passed through the gas supply path 21 and the DIW DIW that has passed through the tapered portion 37 are respectively discharged to the inlet of the discharge path 23 and mixed.
- Nitrogen gas N2 is linearly discharged from the constricted portion 31 of the gas supply passage 21 toward the outlet passage 23, and the pure water is directed toward the inlet of the outlet passage 23 and the overall force around the inlet of the outlet passage 23 is also reduced. Released at an angle.
- the pure water DIW colliding with the nitrogen gas N2 becomes fine particles, and the pure water DIW A droplet D is formed.
- Nitrogen gas N2 and DIW DIW are supplied at appropriate flow rates from the constricted portion 31 and the tapered portion 37, respectively, so that the droplet D is formed with a sufficient number of droplets with a sufficiently small particle size.
- the jet of the droplet D and the nitrogen gas N is led out through the outlet 23 and heads toward the injection port 24.
- the droplet D is accelerated by the flow of the nitrogen gas N while passing through the outlet 23.
- the length L1 of the path 23 is long enough to accelerate the droplet D sufficiently.
- the length L1 of the outlet channel 23 is set to an appropriate length so that the droplets D are prevented from gathering and becoming large particles while passing through the outlet channel 23. It is led out to the injection port 24 as it is.
- a droplet D that has not been formed with a small particle size or a droplet D that has grown large along the inner wall of the outlet channel 23 while passing through the outlet channel 23 may be included. Even if these large droplets D are mixed, they are again atomized while passing through the injection port 24, become sufficiently small and break up into droplets D! / Large droplets D can be prevented from colliding with the surface. Therefore, it is possible to prevent the surface of the wafer W from being damaged. Further, since the large droplet D is split into a plurality of droplets D at the injection port 24, the number of droplets D increases. Therefore, since a large number of fine droplets D can collide with the surface of the wafer W, the surface force of the wafer W can also remove contaminants appropriately.
- the particle diameter of the droplet D and the injection speed are made uniform. That is, it is possible to reduce the number of droplets D whose ejection speed is slow and is not involved in removing contaminants, droplets D whose ejection speed is too fast and may damage the surface of the wafer W, and large droplets D. A large number of droplets D can be ejected at an ejection speed suitable for removing contaminants. Therefore, it is possible to prevent the surface of the wafer W from being damaged by the large droplet D or the high-speed droplet D while improving the contaminant removal performance.
- the droplet D has a particle size of about 100 m or less. Is preferably about 80 mZsec or less. More preferably, the average value of the particle diameter of the droplet D is about 50 / zm or less, the maximum particle diameter is about 100 / zm or less, and the average value of the velocity of the droplet D is about 40 mZsec or more. It is preferable to set it to about 80 mZsec or less.
- the vertical cross-sectional shape of the outlet side peripheral edge of the injection port 24 is a right angle, the straightness of the droplet D is good, and the droplet D collides vigorously with the surface of the wafer W. Contaminants can be suitably removed from the surface of the substrate.
- the jet of the droplet D is generated in the two-fluid nozzle 5 and the entire surface of the wafer W is cleaned by the jet, and the flow control valve 65 and the flow control valve 75 are instructed by the control unit 80. Is closed, and the injection of the jet from the two-fluid nozzle 5 is stopped. Then, as shown by a two-dot chain line in FIG. 2, the two-fluid nozzle 5 and the nozzle arm 15 are retracted outside the cup 6. Also, the drive of the motor 12 is stopped, and the rotation of the spin chuck 2 and the Ueno and W is stopped. Then, the transfer arm (not shown) enters the cleaning device 1, and the transfer arm (not shown) receives the wafer W from the spin chuck 2 and unloads the wafer W from the cleaning device 1. Thus, the processing in the cleaning device 1 is completed.
- an orifice-shaped injection port 24 is provided at the end of the lead-out path 23, and the droplet D is passed through the injection port 24, so that the droplet D has a sufficiently small particle size.
- the particles can be sprayed in the form of fine particles. Even if a large droplet D is formed, the droplet D is re-micronized at the injection port 24, so that the droplet D can be ejected with a uniform particle diameter of a small diameter. Accordingly, it is possible to prevent the large droplets D from colliding with the surface of the wafer W, and to prevent the surface of the wafer W from being damaged.
- a large number of fine droplets D are formed by the re-fine graining, and the large number of droplets D can collide with the surface of the wafer W, so that the performance of removing contaminants is improved.
- the droplets D that are sufficiently finely divided can be jetted at an appropriate speed. Therefore, good contaminant removal performance can be obtained.
- the speed of the droplet D can be made uniform. That is, since a large number of droplets D can be ejected at an appropriate ejection speed, the surface of the wafer W can be prevented from being damaged while improving the contaminant removal performance. Further, according to the cleaning apparatus 1 of the present invention, the contaminant removal performance can be improved without damaging the surface of the wafer W. You can do it.
- the present invention is not limited to the mode described here.
- the liquid is pure water and the gas is nitrogen gas.
- the liquid is not limited to this, and the liquid may be a cleaning chemical or the like, and the gas may be air or the like. May be.
- the substrate is not limited to a semiconductor wafer, but may be another glass for an LCD substrate, a CD substrate, a printed substrate, a ceramic substrate, or the like.
- the arrangement and shape of the gas supply path 21, the liquid supply path 22, and the liquid introduction path 32 are not limited to those described in the embodiment.
- the two-fluid nozzle 5 is constituted by a nozzle body 41 and an engagement member 42, and is formed by a small cylindrical portion 54 of the nozzle body 41 and a hollow portion 43 of the nozzle body 41.
- the configuration in which the liquid introduction path 32 is formed therebetween has been described, the configuration of the two-fluid nozzle 5 is not limited to a powerful configuration.
- the vertical section of the portion along the outlet side peripheral edge of the injection port 24 is formed to be a right angle, but the portion along the outlet side peripheral edge of the injection port 24 is formed.
- the shape of the vertical cross section may be an acute angle as shown in Fig. 7.
- the periphery of the injection port 24 having a substantially circular cross section is formed so that the outer diameter decreases toward the tip, and a substantially frustoconical surface is formed along the periphery of the outlet of the injection port 24.
- the droplet D ejected from the ejection port 24 is easy to travel straight with the outgoing path 23 and the ejection port 24 directed in the direction of the force, and the droplet D is vigorously concentrated on the wafer W. Injection can improve contaminant removal performance.
- the cross-sectional shape of the injection port 24 and the cross-sectional shape of the constricted portion 31 have all been described as being circular, these shapes are not limited to circular shapes, and may take any shape.
- the injection port 24 and the throttle section 31 may be formed in a plurality of holes (porosity).
- the cross-sectional shape of the outlet channel 23, the cross-sectional shape of the injection port 24, the cross-sectional shape of the throttle unit 31, and the cross-sectional shape of the throttle unit 38 are all circular.
- the particle removal rate considered to be optimal could be secured. It was also found that the smaller the diameter c of the outlet of the gas supply channel 21 (throttle section 31), the smaller the mist diameter and the more uniform the velocity distribution. In particular, to make the mist fine at a low flow rate, the smaller the diameter c, the better. As shown in Fig. 9, when the diameter c was 3.0 mm, it was more difficult to generate fine mist than when the diameter c was 1.5 mm and 2.0 mm.
- the present invention can be suitably used, for example, for removing contaminants adhering to the surface of a semiconductor substrate or the like.
Abstract
Description
Claims
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP05720344A EP1724820B1 (en) | 2004-03-09 | 2005-03-09 | Two-fluid nozzle for cleaning substrate and substrate cleaning device |
US10/591,474 US8037891B2 (en) | 2004-03-09 | 2005-03-09 | Two-fluid nozzle for cleaning substrate and substrate cleaning apparatus |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2004-066392 | 2004-03-09 | ||
JP2004066392 | 2004-03-09 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2005086214A1 true WO2005086214A1 (ja) | 2005-09-15 |
Family
ID=34918327
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2005/004072 WO2005086214A1 (ja) | 2004-03-09 | 2005-03-09 | 基板洗浄用2流体ノズル及び基板洗浄装置 |
Country Status (6)
Country | Link |
---|---|
US (1) | US8037891B2 (ja) |
EP (1) | EP1724820B1 (ja) |
KR (1) | KR100760893B1 (ja) |
CN (1) | CN100479107C (ja) |
TW (1) | TWI251857B (ja) |
WO (1) | WO2005086214A1 (ja) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100739425B1 (ko) | 2006-02-21 | 2007-07-13 | 김종련 | 2 유체를 혼합하기 위한 제트노즐과 이를 이용한 세정 장치 |
KR101823646B1 (ko) | 2016-04-29 | 2018-01-31 | 주식회사 케이씨텍 | 기판 세정 장치 |
CN111162023A (zh) * | 2018-11-08 | 2020-05-15 | 北京北方华创微电子装备有限公司 | 喷淋装置及清洗设备 |
TWI837760B (zh) | 2021-12-28 | 2024-04-01 | 大陸商西安奕斯偉材料科技股份有限公司 | 二流體噴嘴及清洗裝置 |
Families Citing this family (41)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4763575B2 (ja) * | 2006-01-26 | 2011-08-31 | 大日本スクリーン製造株式会社 | 基板処理装置および基板処理方法 |
WO2007134056A2 (en) * | 2006-05-08 | 2007-11-22 | Akrion Technologies, Inc. | Spray jet cleaning apparatus and method |
JP2008153322A (ja) * | 2006-12-15 | 2008-07-03 | Dainippon Screen Mfg Co Ltd | 二流体ノズル、基板処理装置および基板処理方法 |
KR101354548B1 (ko) * | 2006-12-29 | 2014-01-23 | 엘지디스플레이 주식회사 | 포토공정 파티클 제거장치 |
JP5016351B2 (ja) * | 2007-03-29 | 2012-09-05 | 東京エレクトロン株式会社 | 基板処理システム及び基板洗浄装置 |
KR20080005942U (ko) * | 2007-05-31 | 2008-12-04 | 주식회사 케이씨텍 | 기판 세정용 이류체 공급모듈 및 이를 이용한 세정장치 |
US9159593B2 (en) * | 2008-06-02 | 2015-10-13 | Lam Research Corporation | Method of particle contaminant removal |
JP5036664B2 (ja) * | 2008-09-04 | 2012-09-26 | 東京エレクトロン株式会社 | 液処理におけるノズル洗浄、処理液乾燥防止方法及びその装置 |
US8844546B2 (en) * | 2008-10-01 | 2014-09-30 | Applied Materials, Inc. | Apparatus and method for cleaning semiconductor substrate using pressurized fluid |
CN102000676A (zh) * | 2009-08-31 | 2011-04-06 | 日立电线株式会社 | 金属元件的表面处理方法及清洁喷嘴 |
CN101850343A (zh) * | 2010-06-10 | 2010-10-06 | 中国电子科技集团公司第四十五研究所 | 晶片双流体清洗装置 |
GB2483438A (en) * | 2010-09-06 | 2012-03-14 | Framo Eng As | Homogenising a multiphase fluid |
JP2013026490A (ja) * | 2011-07-22 | 2013-02-04 | Tokyo Electron Ltd | 基板処理装置 |
US9221081B1 (en) | 2011-08-01 | 2015-12-29 | Novellus Systems, Inc. | Automated cleaning of wafer plating assembly |
US9228270B2 (en) | 2011-08-15 | 2016-01-05 | Novellus Systems, Inc. | Lipseals and contact elements for semiconductor electroplating apparatuses |
US10066311B2 (en) | 2011-08-15 | 2018-09-04 | Lam Research Corporation | Multi-contact lipseals and associated electroplating methods |
US9988734B2 (en) | 2011-08-15 | 2018-06-05 | Lam Research Corporation | Lipseals and contact elements for semiconductor electroplating apparatuses |
CN102319647A (zh) * | 2011-09-19 | 2012-01-18 | 中国烟草总公司郑州烟草研究院 | 一种小流量双流体定量雾化喷嘴装置 |
CN102500487A (zh) * | 2011-11-20 | 2012-06-20 | 江苏博际环境工程科技有限公司 | 远射程锥形气力喷嘴 |
KR102112881B1 (ko) * | 2012-03-28 | 2020-05-19 | 노벨러스 시스템즈, 인코포레이티드 | 전자도금 기판 홀더들을 세정하기 위한 방법들 및 장치들 |
TWI609100B (zh) | 2012-03-30 | 2017-12-21 | 諾發系統有限公司 | 使用反向電流除鍍以清洗電鍍基板夾持具 |
US9746427B2 (en) | 2013-02-15 | 2017-08-29 | Novellus Systems, Inc. | Detection of plating on wafer holding apparatus |
US10416092B2 (en) | 2013-02-15 | 2019-09-17 | Lam Research Corporation | Remote detection of plating on wafer holding apparatus |
DE102013204646B4 (de) | 2013-03-15 | 2018-04-05 | Leica Biosystems Nussloch Gmbh | Gerät zum Bearbeiten von histologischen Proben |
CN103480622B (zh) * | 2013-09-18 | 2016-06-08 | 合肥京东方光电科技有限公司 | 基板清洗装置及其工作方法、基板清洗系统 |
US10090189B2 (en) * | 2013-11-19 | 2018-10-02 | Ebara Corporation | Substrate cleaning apparatus comprising a second jet nozzle surrounding a first jet nozzle |
US9776216B2 (en) * | 2013-11-27 | 2017-10-03 | Taiwan Semiconductor Manufacturing Co., Ltd. | Dispensing apparatus and dispensing method |
US9789448B2 (en) | 2014-01-24 | 2017-10-17 | Taiwan Semiconductor Manufacturing Co., Ltd. | Process for treating fluid |
JP6496186B2 (ja) * | 2015-05-26 | 2019-04-03 | 株式会社Screenホールディングス | 基板処理装置 |
US10053793B2 (en) | 2015-07-09 | 2018-08-21 | Lam Research Corporation | Integrated elastomeric lipseal and cup bottom for reducing wafer sticking |
US10304705B2 (en) * | 2015-12-10 | 2019-05-28 | Beijing Naura Microelectronics Equipment Co., Ltd. | Cleaning device for atomizing and spraying liquid in two-phase flow |
KR102338647B1 (ko) | 2016-05-09 | 2021-12-13 | 가부시키가이샤 에바라 세이사꾸쇼 | 기판 세정 장치 |
CN107684986A (zh) * | 2017-08-10 | 2018-02-13 | 深圳市华星光电技术有限公司 | 一种新型双流体喷嘴装置 |
KR102553350B1 (ko) * | 2018-05-10 | 2023-07-10 | 삼성전자주식회사 | 세정액 노즐, 세정 장치 및 그를 이용한 반도체 소자의 제조 방법 |
KR102461911B1 (ko) * | 2018-07-13 | 2022-10-31 | 삼성전자주식회사 | 플라즈마 제네레이터, 이를 포함하는 세정수 처리 장치, 반도체 세정 장치 및 세정수 처리 방법 |
CN109908712B (zh) * | 2019-04-24 | 2024-04-02 | 攀钢集团钛业有限责任公司 | 用于四氯化钛吸收的气液混合器 |
KR102591953B1 (ko) | 2019-05-31 | 2023-10-23 | 스프레이시스템코리아 유한회사 | 필터가 구비된 연주기용 2유체 노즐 |
JP7314634B2 (ja) * | 2019-06-11 | 2023-07-26 | 東京エレクトロン株式会社 | 塗布装置及び塗布方法 |
KR20210113816A (ko) * | 2020-03-09 | 2021-09-17 | 주식회사 에이치에스하이테크 | 기판 세정용 2류체 노즐 |
TWI824314B (zh) * | 2020-10-13 | 2023-12-01 | 南韓商未來股份有限公司 | 晶片加工方法、系統及裝置 |
KR102358688B1 (ko) * | 2021-05-25 | 2022-02-08 | (주)미래컴퍼니 | 웨이퍼 가공 방법 |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4511087A (en) | 1982-04-08 | 1985-04-16 | Kyoritsu Gokin Mfg. Co., Ltd. | Air mist nozzle apparatus |
DE19740996A1 (de) | 1996-12-02 | 1998-06-04 | Mitsubishi Electric Corp | Zweifluid-Reinigungsstrahldüse sowie Reinigungsvorrichtung und Anwendungsverfahren dafür |
JP2001252604A (ja) * | 2000-03-13 | 2001-09-18 | Tokyo Electron Ltd | 処理液吐出ノズルおよび液処理装置 |
JP2003203892A (ja) * | 2001-11-01 | 2003-07-18 | Tokyo Electron Ltd | 基板洗浄装置及び基板洗浄方法 |
Family Cites Families (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3315611A (en) | 1965-06-28 | 1967-04-25 | Thompson Tank And Mfg Co Inc | Portable vacuum and pressure liquid tank truck |
JPS525367B2 (ja) | 1973-01-31 | 1977-02-12 | ||
JPS59179259A (ja) | 1983-03-31 | 1984-10-11 | Sumitomo Heavy Ind Ltd | 連続鋳造機の鋳片冷却用気水噴霧方法及び気水噴霧ノズル |
GB8724973D0 (en) | 1987-10-24 | 1987-11-25 | Bp Oil Ltd | Fire fighting |
JPH0828684B2 (ja) | 1992-02-19 | 1996-03-21 | 富士通株式会社 | 二重平衡偏波ダイバーシティ受信装置 |
JPH07116561A (ja) | 1993-10-28 | 1995-05-09 | Ozaki Junzo | 噴射ノズル |
JP2000272698A (ja) * | 1999-03-19 | 2000-10-03 | Fuji Electric Co Ltd | シロップ飲料供給ノズル装置 |
US6951221B2 (en) * | 2000-09-22 | 2005-10-04 | Dainippon Screen Mfg. Co., Ltd. | Substrate processing apparatus |
TW561516B (en) | 2001-11-01 | 2003-11-11 | Tokyo Electron Ltd | Substrate processing apparatus and substrate processing method |
JP2003197597A (ja) | 2001-12-26 | 2003-07-11 | Dainippon Screen Mfg Co Ltd | 基板処理装置および基板処理方法 |
JP4349606B2 (ja) * | 2002-03-25 | 2009-10-21 | 大日本スクリーン製造株式会社 | 基板洗浄方法 |
JP4339561B2 (ja) * | 2002-08-16 | 2009-10-07 | 大日本スクリーン製造株式会社 | 基板処理装置および基板処理方法 |
-
2005
- 2005-03-08 TW TW094107010A patent/TWI251857B/zh active
- 2005-03-09 KR KR1020067005750A patent/KR100760893B1/ko active IP Right Grant
- 2005-03-09 WO PCT/JP2005/004072 patent/WO2005086214A1/ja not_active Application Discontinuation
- 2005-03-09 US US10/591,474 patent/US8037891B2/en active Active
- 2005-03-09 CN CNB2005800078768A patent/CN100479107C/zh active Active
- 2005-03-09 EP EP05720344A patent/EP1724820B1/en not_active Expired - Fee Related
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4511087A (en) | 1982-04-08 | 1985-04-16 | Kyoritsu Gokin Mfg. Co., Ltd. | Air mist nozzle apparatus |
DE19740996A1 (de) | 1996-12-02 | 1998-06-04 | Mitsubishi Electric Corp | Zweifluid-Reinigungsstrahldüse sowie Reinigungsvorrichtung und Anwendungsverfahren dafür |
JP2001252604A (ja) * | 2000-03-13 | 2001-09-18 | Tokyo Electron Ltd | 処理液吐出ノズルおよび液処理装置 |
JP2003203892A (ja) * | 2001-11-01 | 2003-07-18 | Tokyo Electron Ltd | 基板洗浄装置及び基板洗浄方法 |
Non-Patent Citations (1)
Title |
---|
See also references of EP1724820A4 |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100739425B1 (ko) | 2006-02-21 | 2007-07-13 | 김종련 | 2 유체를 혼합하기 위한 제트노즐과 이를 이용한 세정 장치 |
KR101823646B1 (ko) | 2016-04-29 | 2018-01-31 | 주식회사 케이씨텍 | 기판 세정 장치 |
CN111162023A (zh) * | 2018-11-08 | 2020-05-15 | 北京北方华创微电子装备有限公司 | 喷淋装置及清洗设备 |
CN111162023B (zh) * | 2018-11-08 | 2023-03-21 | 北京北方华创微电子装备有限公司 | 喷淋装置及清洗设备 |
TWI837760B (zh) | 2021-12-28 | 2024-04-01 | 大陸商西安奕斯偉材料科技股份有限公司 | 二流體噴嘴及清洗裝置 |
Also Published As
Publication number | Publication date |
---|---|
EP1724820A1 (en) | 2006-11-22 |
US8037891B2 (en) | 2011-10-18 |
KR20060087580A (ko) | 2006-08-02 |
EP1724820A4 (en) | 2008-12-17 |
TWI251857B (en) | 2006-03-21 |
US20070141849A1 (en) | 2007-06-21 |
KR100760893B1 (ko) | 2007-09-27 |
CN1930666A (zh) | 2007-03-14 |
TW200531145A (en) | 2005-09-16 |
EP1724820B1 (en) | 2012-07-25 |
CN100479107C (zh) | 2009-04-15 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2005086214A1 (ja) | 基板洗浄用2流体ノズル及び基板洗浄装置 | |
JP4464850B2 (ja) | 基板洗浄用2流体ノズル及び基板洗浄装置 | |
US10854443B2 (en) | Substrate cleaning method and substrate cleaning apparatus | |
TWI443722B (zh) | 基板處理裝置及基板處理方法 | |
TWI632001B (zh) | 二相流霧化噴射清洗裝置 | |
JP4763575B2 (ja) | 基板処理装置および基板処理方法 | |
KR100276620B1 (ko) | 세정용 2류체제트노즐 및 이것을 이용한 세정장치와 세정방법 | |
JP2008108829A (ja) | 二流体ノズルおよびそれを用いた基板処理装置 | |
JP2008159989A (ja) | ノズル、基板処理装置および基板処理方法 | |
KR20170137928A (ko) | 기판 처리 장치 | |
JP2004349501A (ja) | 基板処理方法および基板処理装置 | |
JP4222876B2 (ja) | 基板処理装置 | |
JP2012035166A (ja) | 流体噴出ノズル及びそれを用いた洗浄装置 | |
JP2009054755A (ja) | 基板処理装置 | |
JP4259939B2 (ja) | 基板処理装置および基板処理方法 | |
JP2004288858A (ja) | 基板処理方法および基板処理装置 | |
JP4253200B2 (ja) | 湿式洗浄装置及びそれに用いるノズル | |
JPH09270410A (ja) | 液吐出ノズル及びこのノズルを備えた洗浄装置 | |
JPH05168982A (ja) | 処理液供給ノズル |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BW BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE EG ES FI GB GD GE GH GM HR HU ID IL IN IS KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NA NI NO NZ OM PG PH PL PT RO RU SC SD SE SG SK SL SM SY TJ TM TN TR TT TZ UA UG US UZ VC VN YU ZA ZM ZW |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): GM KE LS MW MZ NA SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LT LU MC NL PL PT RO SE SI SK TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
WWE | Wipo information: entry into national phase |
Ref document number: 1020067005750 Country of ref document: KR |
|
WWP | Wipo information: published in national office |
Ref document number: 1020067005750 Country of ref document: KR |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2007141849 Country of ref document: US Ref document number: 10591474 Country of ref document: US |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2005720344 Country of ref document: EP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 200580007876.8 Country of ref document: CN |
|
NENP | Non-entry into the national phase |
Ref country code: DE |
|
WWW | Wipo information: withdrawn in national office |
Country of ref document: DE |
|
WWP | Wipo information: published in national office |
Ref document number: 2005720344 Country of ref document: EP |
|
WWP | Wipo information: published in national office |
Ref document number: 10591474 Country of ref document: US |