US20030159713A1 - Method and apparatus for cleaning and drying semiconductor wafer - Google Patents

Method and apparatus for cleaning and drying semiconductor wafer Download PDF

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Publication number
US20030159713A1
US20030159713A1 US10/373,684 US37368403A US2003159713A1 US 20030159713 A1 US20030159713 A1 US 20030159713A1 US 37368403 A US37368403 A US 37368403A US 2003159713 A1 US2003159713 A1 US 2003159713A1
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US
United States
Prior art keywords
cleaning solution
isopropyl alcohol
tanks
semiconductor wafer
treating bath
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Abandoned
Application number
US10/373,684
Inventor
Jin-Koo Park
Joong-Yeon Lee
Neung-goo Yoon
Chang-Keun Lee
Sang-Ho Lee
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
A-TECH Ltd
A Tech Ltd Republic of Korea
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A Tech Ltd Republic of Korea
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from KR10-2002-0010969A external-priority patent/KR100431186B1/en
Priority claimed from KR1020020059764A external-priority patent/KR20040032200A/en
Priority claimed from KR1020020059765A external-priority patent/KR100413030B1/en
Application filed by A Tech Ltd Republic of Korea filed Critical A Tech Ltd Republic of Korea
Assigned to A-TECH LTD. reassignment A-TECH LTD. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: LEE, CHANG-KEUN, LEE, JOONG-YEON, LEE, SANG-HO, PARK, JIN-KOO, YOON, NEUNG-GOO
Publication of US20030159713A1 publication Critical patent/US20030159713A1/en
Abandoned legal-status Critical Current

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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01LSEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
    • H01L21/00Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
    • H01L21/02Manufacture or treatment of semiconductor devices or of parts thereof
    • H01L21/02041Cleaning
    • H01L21/02043Cleaning before device manufacture, i.e. Begin-Of-Line process
    • H01L21/02052Wet cleaning only
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01LSEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
    • H01L21/00Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
    • H01L21/67Apparatus 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
    • H01L21/67005Apparatus not specifically provided for elsewhere
    • H01L21/67011Apparatus for manufacture or treatment
    • H01L21/67017Apparatus for fluid treatment
    • H01L21/67028Apparatus for fluid treatment for cleaning followed by drying, rinsing, stripping, blasting or the like
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01LSEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
    • H01L21/00Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
    • H01L21/67Apparatus 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
    • H01L21/67005Apparatus not specifically provided for elsewhere
    • H01L21/67011Apparatus for manufacture or treatment
    • H01L21/67017Apparatus for fluid treatment
    • H01L21/67028Apparatus for fluid treatment for cleaning followed by drying, rinsing, stripping, blasting or the like
    • H01L21/6704Apparatus for fluid treatment for cleaning followed by drying, rinsing, stripping, blasting or the like for wet cleaning or washing
    • H01L21/67057Apparatus for fluid treatment for cleaning followed by drying, rinsing, stripping, blasting or the like for wet cleaning or washing with the semiconductor substrates being dipped in baths or vessels

Definitions

  • the present invention relates to a method and apparatus for cleaning and drying a semiconductor wafer, and more particularly, to a method and apparatus for cleaning and drying a semiconductor wafer using a mixture of isopropyl alcohol and deionized water as a cleaning solution by which cleaning and drying effects can be increased due to premixing isopropyl alcohol and deionized water in an accurate ratio before supplying them into a treating bath in which a cleaning process is performed and the cleaning solution used in the cleaning process can be circulated and reused.
  • a typical cleaning method of removing pollutants remaining on a semiconductor wafer includes a standard clean-1 (SC1) process of removing particles and organic pollutants at an ambient temperature or a high temperature using a mixture of 1:4:20 of ammonia, hydrogen peroxide, and water and a standard clean-2 (SC2) process of removing transient metal pollutants at a high temperature using a mixture of 1:1:5 of hydrochloric acid, hydrogen peroxide, and water.
  • SC1 standard clean-1
  • SC2 standard clean-2
  • a piranha cleaning process is first performed to remove an organic pollutant such as a sensitizer or a surfactant at a high temperature using a mixture of sulphuric acid and hydrogen peroxide and an HF cleaning process is lastly performed to effectively remove a natural oxide layer from the surface of a wafer, and simultaneously, a metal pollutant from the natural oxide layer.
  • an organic pollutant such as a sensitizer or a surfactant at a high temperature
  • an HF cleaning process is lastly performed to effectively remove a natural oxide layer from the surface of a wafer, and simultaneously, a metal pollutant from the natural oxide layer.
  • the above-described conventional cleaning methods have problems in that a chemical solution in a large amount is used during a cleaning process, and the chemical solution is mainly a mixture of an acid and a base, a base material of the mixture being a hydrogen peroxide, and thus wastewater cannot be easily treated.
  • the use of a large amount of chemical solution and a large amount of cleaning water results in increasing cleaning costs and is environmentally regulated.
  • a process of drying the wafer is performed.
  • the drying process includes spin drying, isopropyl alcohol (IPA) vapor drying, IPA layer drying, and so forth.
  • Spin drying is performed to remove a cleaning solution remaining on the wafer using a centrifugal force by spinning the wafer at a high speed.
  • IPA vapor drying is performed so that IPA vapors contact the surface of the wafer, and a residual liquid such as moisture remaining on the surface of the wafer is substituted for IPA, and then removed.
  • IPA drying is performed so that a wafer is dipped into a cleaning solution having a DIW layer and an IPA layer, DIW and IPA sequentially contact the wafer to clean residual liquid with DIW, and the residual liquid is substituted for IPA.
  • IPA layer drying is also called marangoni drying.
  • dust generated in the spinning apparatus may be adsorbed onto the semiconductor wafer due to the charging of the semiconductor wafer.
  • moisture remains in the notch lines for dicing the semiconductor wafer into individual chips, trenches or contact holes, and creates water marks.
  • marangoni drying can somewhat solve problems occurring during spin drying or IPA vapor drying.
  • marangoni drying is not effective in removing various types of pollutants, such as particles, which may remain on the surface of the wafer.
  • the present invention provides an apparatus and method for cleaning and drying a semiconductor wafer using a mixture of IPA and DIW as a cleaning solution by which cleaning and drying effects can be increased due to premixing IPA and DIW in an accurate ratio before supplying them into a treating bath in which a cleaning process is performed and the cleaning solution used in the cleaning process can be circulated and reused to prevent waste and reduce environmental pollution.
  • an apparatus for cleaning and drying a semiconductor wafer includes a treating bath, a cleaning solution mixing unit, a cleaning solution supplying unit, and a return line.
  • the treating bath is supplied with a cleaning solution from an external source and in which the semiconductor wafer is cleaned and dried.
  • the cleaning solution mixing unit mixes cleaning solutions to be supplied into the treating bath in a predetermined ratio and includes isopropyl alcohol tanks that are supplied with isopropyl alcohol from an external source, mixing tanks that are supplied with deionized water from an external source, are connected to the isopropyl alcohol tanks to be supplied with isopropyl alcohol contained in the isopropyl alcohol tanks and mix isopropyl alcohol and deionized water, and level sensing means that sense the amount of isopropyl alcohol supplied into the IPA tanks and the amount of deionized water supplied into the mixing tanks.
  • the cleaning solution supplying unit connects the mixing tanks to the treating bath and supplies the cleaning solution mixed in the mixing tanks into the treating bath.
  • the return line returns the cleaning solution that was used in the cleaning of the semiconductor wafer back to the mixing tanks.
  • Two or more isopropyl alcohol tanks of the cleaning solution mixing unit are interconnected in parallel, the mixing tanks are connected to the isopropyl alcohol tanks, respectively, and disposed in parallel so that each of the isopropyl alcohol tanks and each of the mixing tanks make a group, and the cleaning solution circulates through a mixing tank in a group selected from two or more groups.
  • the level sensing means are a plurality of level sensors that are installed at the isopropyl alcohol tanks and a plurality of level sensors that are installed at the mixing tanks.
  • the cleaning solution mixing unit further includes a nitrogen bubble generator that injects a nitrogen gas into the mixing tanks so as to completely mix deionized water and isopropyl alcohol.
  • Isopropyl alcohol supplementing pumps additionally supply isopropyl alcohol in the isopropyl alcohol tanks into the mixing tanks by a desired amount are further installed between the isopropyl alcohol tanks and the mixing tanks.
  • the cleaning solution supplying unit includes a circulating pump, a filter, an isopropyl alcohol concentration measurer, and a liquid particle counter.
  • the circulating pump pumps the cleaning solution in the mixing tanks into the treating bath.
  • the filter filters the cleaning solution flowing via the circulating pump off impurities.
  • the isopropyl alcohol concentration measurer checks the concentration of isopropyl alcohol contained in the cleaning solution that has passed through the filter.
  • the liquid particle counter detects the amount of liquid particle contained in the cleaning solution flowing into the treating bath.
  • the return line includes a liquid particle counter that detects liquid particle contained in the cleaning solution returning from the treating bath back to the mixing tanks.
  • the apparatus further includes a heating tank, an isopropyl alcohol filter, an isopropyl alcohol collecting tank, a deionized water filter, and a deionized water collecting tank.
  • the heating tank is connected to the cleaning solution mixing unit, is supplied the cleaning solution from the mixing tanks, and heats the cleaning solution, and evaporates isopropyl alcohol from the cleaning solution using a difference between boiling points of isopropyl alcohol and deionized water to decompose the cleaning solution into pure isopropyl alcohol and deionized water.
  • the isopropyl alcohol filter is connected to the heating tank and filters vapor isopropyl alcohol off impurities.
  • the isopropyl alcohol collecting tank is supplied with isopropyl alcohol filtered through the isopropyl alcohol filter and condenses isopropyl alcohol.
  • the deionized water filter is connected to the heating tank and passes deionized water remaining in the heating tank to filter impurities of deionized water.
  • the deionized water collecting tank is supplied with deionized water filtered through the deionized water filter and temporarily stores deionized water.
  • a sink that is supplied with deionized water from an external source and sinks a lower portion of the treating bath under deionized water is further installed beneath the treating bath.
  • the sink includes an ultrasonic generator that generates ultrasonic waves, passes the ultrasonic waves through deionized water and the treating bath to the semiconductor wafer that is being cleaned in the treating bath.
  • a method of cleaning and drying a wafer Dionized water and isopropyl alcohol are mixed to make a cleaning solution.
  • the cleaning solution is supplied into a treating bath so that the cleaning solution contacts the semiconductor wafer in the treating bath to clean the semiconductor wafer.
  • the semiconductor wafer is separated from the cleaning solution.
  • the semiconductor wafer separated from the cleaning solution is dried to remove the cleaning solution remaining on the semiconductor wafer.
  • the semiconductor wafer Before the cleaning solution is supplied into the treating bath, the semiconductor wafer may be put into the treating bath.
  • the semiconductor wafer may be dipped into the cleaning solution.
  • the semiconductor wafer may be lifted up from the treating bath so that the semiconductor wafer is separated from the cleaning solution.
  • the cleaning solution may be discharged from the treating bath so that the semiconductor wafer is separated from the cleaning solution.
  • the concentration of isopropyl alcohol in the cleaning solution varies according to time to adjust the concentration of isopropyl alcohol to a target concentration.
  • a hot nitrogen gas is sprayed on the surface of the semiconductor wafer, contacts, and dries the surface of the semiconductor wafer.
  • FIG. 1 is a schematic view of an apparatus for cleaning and drying a semiconductor wafer according to an embodiment of the present invention
  • FIG. 2 is a view for explaining a step of dipping a semiconductor wafer into a treating bath during cleaning and drying a semiconductor wafer, according to an embodiment of the present invention
  • FIG. 3 is a view for explaining a step of dipping a semiconductor wafer into a treating bath during cleaning and drying a semiconductor wafer, according to another embodiment of the present invention
  • FIGS. 4A through 4D are views illustrating examples of moving a semiconductor wafer within a cleaning solution to further effectively clean the semiconductor wafer put into a treating bath;
  • FIG. 5 is a view for explaining a method of separating a semiconductor wafer from a cleaning solution after the semiconductor wafer is cleaned in a treating bath using a method of cleaning and drying a semiconductor wafer according to an embodiment of the present invention
  • FIG. 6 is a view for explaining a step of separating a semiconductor wafer from a cleaning solution after the semiconductor wafer is cleaned in a treating bath in a method of cleaning and drying a semiconductor wafer according to another embodiment of the present invention
  • FIG. 7 is a view for explaining a step of separating a semiconductor wafer from a cleaning solution after the semiconductor wafer is cleaned in a treating bath in a method of cleaning and drying a semiconductor wafer according to still another embodiment of the present invention
  • FIG. 8 is a view for explaining a step of spraying a nitrogen gas for drying a semiconductor wafer in a method of cleaning and drying a semiconductor wafer according to an embodiment of the present invention
  • FIG. 9 is a view for explaining a step of spraying a nitrogen gas for drying a semiconductor wafer in a method of cleaning and drying a semiconductor wafer according to another embodiment of the present invention.
  • FIGS. 10 through 12 are views for explaining a step of changing the position of a semiconductor wafer with respect to a elevating support block when a nitrogen gas is sprayed on the semiconductor wafer;
  • FIGS. 13 through 20 are graphs illustrating various ways to adjust the concentration of IPA in a cleaning solution used for cleaning and drying a semiconductor wafer according to an embodiment of the present invention.
  • FIG. 1 is a schematic view of an apparatus for cleaning and drying a semiconductor wafer according to an embodiment of the present invention.
  • the apparatus includes a treating bath 11 , a cleaning solution mixing unit 50 , a cleaning solution supplying unit 52 , a return line 54 , a drain line 90 , and a collecting unit 82 .
  • a wafer W is cleaned and dried in the treating bath 11 .
  • the cleaning solution mixing unit 50 premixes cleaning solutions to be supplied into the treating bath 11 in a predetermined ratio.
  • the cleaning solution supplying unit 52 moves the cleaning solution mixed in the cleaning solution mixing unit 50 into the treating bath 11 and checks the state of the cleaning solution.
  • the return line 54 returns the cleaning solution, which overflows after being used in a cleaning process in the treating bath 11 , back to the cleaning solution mixing unit 50 .
  • the drain line 90 returns the cleaning solution from the treating bath 11 back to the cleaning solution mixing unit 50 .
  • the collecting unit 82 is connected to the cleaning solution mixing unit 50 and collects a polluted cleaning solution to decompose the polluted cleaning solution into IPA and DIW.
  • the treating bath 11 may accommodate one or more wafers to be cleaned and dried and is connected to the cleaning solution supplying unit 52 and the return line 54 .
  • the upper portion of the treating bath 11 is covered with a chamber cover 12 that is already known in the prior art.
  • the wafer W is supported by an elevating support block 92 shown in FIG. 10 in the treating bath 11 .
  • the elevating support block 92 is positioned inside the treating bath 11 when cleaning the wafer W so that the wafer W is sunk under the cleaning solution 5 . However, when drying the wafer W, the elevating support block 92 ascends over the treating bath 11 as shown in FIG. 11.
  • the chamber cover 12 covers the treating bath 11 and induces a cleaning solution overflowing from the treating bath 11 to the return line 54 .
  • the chamber cover 12 also includes a plurality of nitrogen spraying nozzles 14 .
  • the nitrogen spraying nozzles 14 are supplied with a nitrogen gas from an external source, and further supply the nitrogen gas into the chamber cover 12 to fill the chamber cover 12 with the nitrogen gas.
  • the nitrogen nozzles 14 spray the nitrogen gas on the wafer W when the wafer W rises onto the liquid surface of the cleaning solution in order to remove the cleaning solution attached to the surface of the wafer W.
  • a heater 80 is further installed to heat the nitrogen gas proceeding toward the nitrogen spraying nozzles 14 . If necessary, the heater 80 can heat the nitrogen gas to further effectively remove the cleaning solution sticking to the surface of the wafer W.
  • a sink 84 is installed under the treating bath 11 .
  • the sink 84 contains DIW at a predetermined wafer level so that the lower portion of the treating bath 11 is sunk under the wafer surface of DIW.
  • a wafer level sensor 88 is installed inside the sink 84 . The level sensor 88 senses the level of DIW so that the lower portion of the treating bath 11 is always positioned under the level of DIW.
  • An ultrasonic generator 86 is installed beneath the sink 84 .
  • the ultrasonic generator 86 may be a general ultrasonic generator. Ultrasonic waves generated by the ultrasonic generator 86 pass through DIW in the sink 84 , and then are transmitted to the wafer W through a case of the treating bath 11 and the cleaning solution 5 .
  • the cleaning solution mixing unit 50 includes IPA tanks 18 and 19 and mixing tanks 24 and 25 respectively connected to the IPA tanks 18 and 19 . Since the IPA tanks 18 and 19 are disposed in parallel, IPA can be supplied simultaneously into the IPA tanks 18 and 19 from an external source. Also, since the mixing tanks 24 and 25 are disposed in parallel, DIW can be supplied simultaneously into the mixing tanks 24 and 25 from an external source.
  • Each of the IPA tanks 18 and 19 has a plurality of level sensors 20 .
  • the level sensors 20 sense the amount of IPA supplied into the IPA tanks 18 and 19 so that the desired amount of IPA is supplied.
  • Each of the mixing tanks 24 and 25 also has a plurality of level sensors 21 .
  • the level sensors 21 sense the amount of DIW supplied into the mixing tanks 24 and 25 so that a desired amount of DIW is supplied.
  • Reference numeral 44 denotes an overflow drainpipe. As will be described later, the overflow drainpipe 44 discharges the cleaning solution outside the mixing tanks 24 and 25 when the cleaning solution returning back via the return line 54 or the drain line 90 rises above a predetermined level in the mixing tanks 24 and 25 .
  • the IPA tanks 18 and 19 are respectively connected to the mixing tanks 24 and 25 via connecting pipes 56 .
  • IPA in the IPA tanks 18 and 19 moves into the mixing tanks 24 and 25 through the connecting pipes 56 .
  • the necessary amount of DIW is separately supplied into the mixing tanks 24 and 25 .
  • IPA supplied from the IPA tanks 18 and 19 are mixed with DIW at a predetermined ratio.
  • the amount of IPA supplied into the IPA tanks 18 and 19 and the amount of DIW supplied into the mixing tanks 24 and 25 can be respectively measured by the level sensors 20 and 21 .
  • the concentration of IPA to DIW can be adjusted, and thus cleaning solutions having a desired concentration can be obtained in the mixing tanks 24 and 25 .
  • the concentration of IPA illustrated in graphs of FIGS. 12 through 19 can be obtained.
  • Each of the connecting pipes 56 is split into two pipes.
  • IPA supplementing pumps 22 and 23 are respectively installed at one of the two split connecting pipes 56 .
  • the IPA supplementing pumps 22 and 23 are used to additionally and quickly supply the accurate amount of IPA from the IPA tanks 18 and 19 into the mixing tanks 24 and 25 .
  • IPA Since IPA is volatile, IPA may gradually volatilize during the circulation of the cleaning solution. When IPA volatilizes, the concentration of IPA in the cleaning solution becomes low. Thus, the IPA supplementing pumps 22 and 23 supplement IPA by a shortage of IPA.
  • IPA and DIW are mixed in a desired ratio.
  • a nitrogen bubble generator 26 is additionally installed in order to completely mix IPA and DIW.
  • the nitrogen bubble generator 26 is supplied with a nitrogen gas from an external source, sprays the nitrogen gas into the lower portions of the mixing tanks 24 and 25 so that DIW and IPA contained in the mixing tanks 24 and 25 are completely mixed.
  • the cleaning solution mixing unit 50 includes the IPA tanks 18 and 19 and the mixing tanks 24 and 25 .
  • the number of IPA tanks and the number of mixing tanks may increase.
  • the mixing tanks 24 and 25 are connected to a supplying pipe 58 via mixed solution supplying valves 28 and 29 .
  • the mixed solution supplying valves 28 and 29 are opened alternately not simultaneously. In other words, when the mixed solution supplying valve 28 is opened, the mixed solution supplying valve 29 is closed. Alternatively, when the mixed solution supplying valve 28 is closed, the mixed solution supplying valve 29 is opened. This means that while the cleaning solution in the mixing tank 24 is circulated and supplied into the treating bath 11 , the cleaning solution in the mixing tank 25 is not circulated.
  • the mixed solution supplying valve 28 is opened to clean the wafer W using only the cleaning solution contained in the mixing tank 24 , and after a predetermined period of time, the cleaning solution is polluted more than the allowed pollution level, the mixed solution supplying valve 28 is closed, the mixed solution supplying valve 29 is opened, and the cleaning solution contained in the mixing tank 25 is circulated to continue cleaning of the wafer W.
  • a mixed solution discharging valve 30 of the mixing tank 24 is opened to discharge the polluted cleaning solution in the mixing tank 24 .
  • the mixed solution discharging valve 30 is closed, IPA and DIW are newly supplied from external sources, IPA and DIW are mixed in a desired ratio, and the mixture is maintained in the mixing tank 24 .
  • a pure cleaning solution can be continuously supplied without stopping the apparatus for cleaning and drying a semiconductor wafer.
  • a wafer can be quickly and effectively cleaned and dried.
  • Discharging pipes 64 and 65 which are respectively installed beneath the mixing tanks 24 and 25 , discharge the cleaning solution in the mixing tanks 24 and 25 to the collecting unit 82 and are opened and closed by the mixed solution discharging valves 30 and 31 .
  • the collecting unit 82 basically collects the cleaning solution that is polluted at an allowed pollution level or above due to the cleaning of a wafer and remakes the polluted cleaning solution into pure IPA and DIW.
  • the collecting unit 82 includes a heating tank 70 , which is connected to the discharging pipes 64 and 65 and receives the polluted cleaning solution, an IPA collecting tank 74 and a DIW collecting tank 78 , which are connected to the heating tank 70 , an IPA filter 72 , which removes impurities contained in IPA flowing from the heating tank 70 to the IPA collecting tank 74 , and a DIW filter 76 , which removes impurities contained in DIW flowing from the heating tank 70 to the DIW collecting tank 78 .
  • the heating tank 70 receives and heats a cleaning solution and evaporates IPA in the cleaning solution having a relatively low boiling point to decompose the cleaning solution into DIW and IPA. In other words, the heating tank 70 decomposes a cleaning solution into IPA and DIW using a difference between boiling points of IPA and DIW.
  • IPA turning into a gaseous state in the heating tank 70 is filtered through the IPA filter 72 , moves into the IPA collecting tank 74 , is cooled, and is condensed into a liquid state in time.
  • An additional cooler may be installed to condense IPA.
  • IPA collected in the IPA collecting tank 74 is supplied into the IPA tanks 18 and 19 of the cleaning solution mixing unit 50 and reused.
  • the cleaning solution supplying unit 52 which moves the cleaning solution of a predetermined concentration supplied from the cleaning solution mixing unit 50 into the treating bath 11 , includes a circulating pump 36 , a filter 38 , an IPA concentration measurer 40 , and a liquid particle counter 42 .
  • the circulating pump 36 is connected to the mixing tanks 24 and 25 via the mixed solution supplying valves 28 and 29 .
  • the circulating pump 36 pumps the cleaning solutions in the mixing tanks 24 and 25 into the treating bath 11 through the cleaning solution supplying unit 52 .
  • the cleaning solution moving into the treating bath 11 via the circulating pump 36 is purified through the filter 38 .
  • the filter 38 passes the cleaning solution and filters off impurities contained in the cleaning solution so that the usable period of the cleaning solution is prolonged at its maximum.
  • the IPA concentration measurer 40 connected to the filter 38 checks the concentration of IPA in the cleaning solution that is circulating. Since IPA is volatile, the concentration of IPA may gradually become low during the circulation of the cleaning solution. Due to this, the IPA concentration measurer 40 is installed to continuously check the concentration of IPA in the cleaning solution. When IPA measurer 40 perceives that the concentration of IPA is reduced, the IPA supplementing pumps 22 and 23 operate to supplement IPA contained in the IPA tanks 18 and 19 into the mixing tanks 24 and 25 so that the cleaning solution returns to an optimum concentration level.
  • the liquid particle counter 42 detects the amount of liquid particle in the cleaning solution that is circulating to determine whether the cleaning solution has to be replaced.
  • the liquid particle is a pollutant that is not filtered by the filter 38 .
  • the cleaning solution supplied into the treating bath 11 through the cleaning solution supplying unit 52 cleans the wafer W in the treating bath 11 , overflows from the treating bath 11 , and flows to the return line 54 .
  • the cleaning solution flowing through the return line 54 passes through the liquid particle counter 43 again.
  • the liquid particle counter 42 detects liquid particle contained in the cleaning solution, which passed through the treating bath 11 , and rechecks the pollution level of the cleaning solution that underwent the cleaning of the wafer W.
  • the cleaning solution passing through the return line 54 returns back into the mixing tanks 24 and 25 via the return valve 60 or 61 .
  • Drying the wafer W is accomplished by lifting the wafer W up over the liquid surface of the cleaning solution. In other words, when the wafer W is lifted up over the liquid surface of the cleaning solution, drying the wafer W is firstly achieved due to the surface tension of the cleaning solution. Next, while the wafer W is rising, the nitrogen gas is sprayed on the wafer W through the nitrogen nozzles 14 to secondly achieve the drying of the wafer W.
  • the procedure of lifting a wafer up over the liquid surface of a cleaning solution includes: moving the wafer over the liquid surface of the cleaning solution using an elevating support block 92 (shown in FIG. 10) while maintaining the level of the cleaning solution and reducing the level of the cleaning solution without moving the wafer.
  • the drain line 90 is just an apparatus for reducing the level of the cleaning solution without moving the wafer.
  • the drain line 90 is connected to the lower portion of the treating bath 11 and the mixing tank 24 or 25 and discharges the cleaning solution 5 in the treating bath 11 downward, so that the wafer is firstly dried.
  • the drain line 90 controls the return values 60 and 61 to return the cleaning solution back to one of the mixing tanks 24 and 25 being used.
  • an apparatus for cleaning and drying a semiconductor wafer includes the cleaning solution mixing unit 50 , which premixes cleaning solutions in a desired ratio, the cleaning solution supplying unit 52 , which is supplied with the cleaning solution from the cleaning solution mixing unit 50 and supplies the cleaning solution into the treating bath 11 , and the return line 54 , which returns the cleaning solution used in the cleaning of the semiconductor wafer in the treating bath 11 back to the cleaning solution mixing unit 50 .
  • the cleaning solution can be always maintained at an accurate concentration, effects of cleaning and drying the semiconductor wafer are good.
  • the apparatus Since the cleaning solution discharged from the cleaning solution mixing unit 50 returns back through the return line 50 , and then is reused to perform a cleaning process, the apparatus is economic.
  • the collecting unit 82 decomposes a cleaning solution that is polluted at an allowed pollution level or above into pure IPA and DIW.
  • the cleaning solution can be reused, the discarded amount of the cleaning solution can be remarkably reduced, and environmental pollution can be reduced.
  • a method of cleaning and drying a semiconductor wafer using the cleaning and drying apparatus can be basically divided into four steps. The four steps will be described below.
  • DIW and IPA are mixed.
  • the mixture of DIW and IPA is carried out by the cleaning solution mixing unit 50 .
  • the mixing tanks 24 and 25 are supplied with IPA and DIW, and then IPA and DIW is completely mixed by the nitrogen bubble generator 26 .
  • a cleaning solution made by mixing IPA and DIW in the first step is supplied into the treating bath 11 so as to contact the wafer in the treating bath 11 .
  • the cleaning solution may contact a wafer according to two ways.
  • a wafer W is put into the treating bath 11 in advance, and then a cleaning solution is supplied into the treating bath 11 to gradually raise the liquid surface of the cleaning solution so that the wafer W is dipped into the cleaning solution.
  • a cleaning solution is continuously supplied into the treating bath 11 to maintain the cleaning solution at a predetermined level, the wafer W descends to be dipped into the cleaning solution.
  • FIGS. 2 and 3 illustrate a wafer W descending into a cleaning solution.
  • FIG. 2 illustrates a wafer W that vertically descends
  • FIG. 3 illustrates a wafer W that descends while swaying from side to side.
  • the wafer W rubs on a cleaning solution 5 , which results in an increase in a cleaning effect.
  • the method of dipping a wafer into a cleaning solution may be modified into various forms.
  • the treating bath 11 In order to supply a cleaning solution into the treating bath 11 with a wafer placed in the treating bath 11 in advance so that the wafer is dipped into the cleaning solution, the treating bath 11 has to be pre-emptied. To empty the treating bath 11 , the drain line 90 is opened to return the cleaning solution in the treating bath 11 back to the mixing tanks 24 and 25 .
  • FIGS. 4A through 4D illustrate a wafer that moves in the cleaning solution.
  • FIG. 4A illustrates a wafer W that vertically sways
  • FIG. 4B illustrates a wafer W horizontally sways
  • FIG. 4C illustrates a wafer W that turns around the axis (Y-axis) of the vertical direction
  • FIG. 4D illustrates a wafer W that turns around the axis (X-axis) of the horizontal direction.
  • impurities such as various types of particles can be effectively removed from the surface of a wafer by moving the wafer within a cleansing solution.
  • FIGS. 5 through 7 illustrate a method of separating the wafer W from the cleaning solution 5 .
  • FIGS. 5 and 6 the wafer W is lifted up with the liquid surface of the cleaning solution 5 maintained, and in FIG. 7, the cleaning solution 5 is discharged with the wafer W left in the treating bath 11 . Also, in FIG. 5, the wafer W is vertically lifted up, and in FIG. 6, the wafer W sways from side to side when being lifted up so that the friction between the wafer W and the cleaning solution 5 increases.
  • paths for taking the wafer W out of the treating bath 11 may be changes in other various forms.
  • the fourth step is performed.
  • the remaining cleaning solution is removed from the surface of the wafer W separated from the cleaning solution 5 .
  • the fourth step is carried out in the treating bath 11 from which the cleaning solution 5 is removed or over the treating bath 11 when the cleaning solution 5 remains in the treating bath 11 .
  • a nitrogen gas having a high temperature preferably a temperature within a range of 50-150° C., is sprayed on the surface of the wafer W at a predetermined pressure so as to remove the cleaning solution remaining on the surface of the wafer W.
  • FIG. 8 illustrates a state where when the wafer W is lifted up over the treating bath 11 , a hot nitrogen gas is concentratedly sprayed on the surface of the wafer W. In this state, the remaining cleaning solution is removed due to the pressure of spraying the nitrogen gas and heat transmitted from the nitrogen gas.
  • FIG. 9 illustrates a state where a hot nitrogen gas is sprayed on the wafer W in the vertical laminar flow. Thereafter, the hot nitrogen gas contacts the surface of the wafer W to transmit heat to the surface of the wafer W so that a mixed solution is evaporated and dried.
  • FIGS. 10 and 13 are views for explaining a step of changing the position of a wafer relative to an elevating support block and side support blocks when a nitrogen gas is sprayed on the wafer.
  • elevating support block and the side support blocks various types of elevating support blocks and side support blocks have been proposed.
  • the elevating support block 92 ascends and descends while vertically supporting a plurality of wafers.
  • Side support blocks 94 temporarily separate a wafer W from the elevating support block 92 when the wafer W goes up, so that a lower edge Z of the wafer W is separated from the elevating support block 92 as shown in FIG. 12.
  • the elevating support block 92 ascends, the side support blocks 94 are fully apart from the wafer W so that the wafer W passes through a space between the side support blocks 94 .
  • the wafer W is dipped under the cleaning solution 5 when being supported by the elevating support block 92 .
  • the side support blocks 94 are positioned over the treating bath 11 .
  • the side support blocks 94 are parallel and can move along directions indicated by arrows. If necessary, the side support blocks 94 support sides of the wafer W as shown in FIG. 12.
  • the elevating support 92 completely moves up over the treating bath 11 and the wafer W is positioned between the-side support blocks 94 .
  • the nitrogen gas does not reaches the lower edge Z, and thus the lower edge Z is not completely dried.
  • the side support blocks 94 moves along direction A indicated by arrow so as to support the sides of the wafer W, while the elevating support block 92 temporarily descends as shown in FIG. 12.
  • the side support blocks 94 support the sides of the wafer W and the elevating support block 92 goes down, so that the nitrogen gas is sprayed on the lower edge Z.
  • the elevating support block 92 must not sink under the cleaning solution 5 .
  • the elevating support 92 ascends and the side support blocks 94 are separated from the wafer W so that the elevating support block 92 re-supports the wafer W, and then the wafer W is taken out from the elevating support block 92 .
  • FIGS. 13 through 20 are graphs illustrating ways to adjust the concentration of IPA with respect to variations in the time required for supplying a cleaning solution into a treating bath.
  • concentration of IPA is properly adjusted to work conditions or other requirements, an improved cleaning effect can be achieved.
  • the adjustment of the concentration of IPA can be realized by the IPA supplementing pumps 22 and 23 described with reference to FIG. 1.
  • FIG. 13 illustrates a state where a cleaning solution containing IPA and DIW of a predetermined ratio is supplied into a treating bath without varying the concentration of IPA.
  • FIG. 14 illustrates a state where when only DIW is first supplied into a treating bath, and then the addition of IPA to DIW is gradually increased and the concentration of IPA reaches a predetermined level, the supply of IPA stops.
  • FIG. 15 illustrates a state where when the concentration of IPA of a cleaning solution supplied into a treating bath is gradually increased and reaches a predetermined level, the addition of IPA stops.
  • FIG. 16 illustrates a state where the concentration of IPA to DIW is increased at regular intervals not gradually.
  • FIG. 17 illustrates a state where only pure IPA is first supplied into a treating bath, and then DIW is supplied into the treating bath at predetermined time intervals, so that the concentration of IPA becomes low.
  • FIG. 18 illustrates a state where a cleaning solution containing IPA of a predetermined concentration is supplied into a treating bath, and then the addition of IPA is reduced from a predetermined point of time, so that only DIW is supplied.
  • FIG. 19 illustrates a state where a cleaning solution containing IPA of a predetermined concentration is first supplied into a treating bath, and then the addition of IPA is gradually increased, so that the concentration of IPA becomes higher.
  • FIG. 20 illustrates a state where a cleaning solution containing IPA of a predetermined concentration is first supplied into a treating bath, and then the addition of IPA is gradually reduced, so that the concentration of IPA becomes lower.
  • IPA and DIW are completely mixed so that cleaning and drying works are effectively performed. Also, a cleaning solution can be reused to prevent waste of the cleaning solution.
  • the semiconductor wafer is taken as an example of an object to be cleaned.
  • the object to be cleaned is not limited to the semiconductor wafer, and the present invention may be applied to various objects including a substrate for a liquid crystal display device only, a substrate for a recording disc only, a substrate for a mask only, or the like.

Abstract

Provided is an apparatus and method for cleaning and drying a semiconductor wafer. Isopropyl alcohol and deionized water are premixed in a desired ratio before a cleaning solution containing isopropyl alcohol and deionized water is supplied into a treating bath. Accordingly, a chemical compound remaining due to deionized water can be effectively removed and the creation of water marks due to isopropyl alcohol can be effectively prevented. As a result, cleaning and drying effects can be increased and a cleaning solution can be reused.

Description

    BACKGROUND OF THE INVENTION
  • This application claims the priority of Korean Patent Application Nos. 2002-10969, 2002-59765, and 2002-59764 filed on February 28, October 1, and Oct. 1, 2002, respectively, in the Korean Intellectual Property Office, the disclosure of which is incorporated herein in its entirety by reference. [0001]
  • 1. Field of the Invention [0002]
  • The present invention relates to a method and apparatus for cleaning and drying a semiconductor wafer, and more particularly, to a method and apparatus for cleaning and drying a semiconductor wafer using a mixture of isopropyl alcohol and deionized water as a cleaning solution by which cleaning and drying effects can be increased due to premixing isopropyl alcohol and deionized water in an accurate ratio before supplying them into a treating bath in which a cleaning process is performed and the cleaning solution used in the cleaning process can be circulated and reused. [0003]
  • 2. Description of the Related Art [0004]
  • Generally, most semiconductor wafer cleaning methods were developed in the 1970s, and use large amounts of chemical solutions. A typical cleaning method of removing pollutants remaining on a semiconductor wafer includes a standard clean-1 (SC1) process of removing particles and organic pollutants at an ambient temperature or a high temperature using a mixture of 1:4:20 of ammonia, hydrogen peroxide, and water and a standard clean-2 (SC2) process of removing transient metal pollutants at a high temperature using a mixture of 1:1:5 of hydrochloric acid, hydrogen peroxide, and water. [0005]
  • In another cleaning method, a piranha cleaning process is first performed to remove an organic pollutant such as a sensitizer or a surfactant at a high temperature using a mixture of sulphuric acid and hydrogen peroxide and an HF cleaning process is lastly performed to effectively remove a natural oxide layer from the surface of a wafer, and simultaneously, a metal pollutant from the natural oxide layer. [0006]
  • The above-described conventional cleaning methods have problems in that a chemical solution in a large amount is used during a cleaning process, and the chemical solution is mainly a mixture of an acid and a base, a base material of the mixture being a hydrogen peroxide, and thus wastewater cannot be easily treated. The use of a large amount of chemical solution and a large amount of cleaning water results in increasing cleaning costs and is environmentally regulated. [0007]
  • Since most cleaning processes are performed at a high temperature, a chemical solution used for cleaning decomposes and evaporates, which decreases the life span of the cleaning solution and a cleaning effect. In addition, the reuse rate of the cleaning solution is reduced due to the excessive use of deionized water (DIW). Also, since the above-described conventional cleaning process is composed of multi-steps, a huge piece of equipment is necessary for performing the cleaning process. [0008]
  • After such a cleaning process, a process of drying the wafer is performed. The drying process includes spin drying, isopropyl alcohol (IPA) vapor drying, IPA layer drying, and so forth. Spin drying is performed to remove a cleaning solution remaining on the wafer using a centrifugal force by spinning the wafer at a high speed. IPA vapor drying is performed so that IPA vapors contact the surface of the wafer, and a residual liquid such as moisture remaining on the surface of the wafer is substituted for IPA, and then removed. IPA drying is performed so that a wafer is dipped into a cleaning solution having a DIW layer and an IPA layer, DIW and IPA sequentially contact the wafer to clean residual liquid with DIW, and the residual liquid is substituted for IPA. IPA layer drying is also called marangoni drying. [0009]
  • However, during spin drying, dust generated in the spinning apparatus may be adsorbed onto the semiconductor wafer due to the charging of the semiconductor wafer. In particular, moisture remains in the notch lines for dicing the semiconductor wafer into individual chips, trenches or contact holes, and creates water marks. [0010]
  • During IPA vapor drying, since a vapor area is instable, IPA vapors cannot uniformly contact the semiconductor wafer. Thus, the possibility that water marks will be created is high. Also, since flammable IPA vapors are used, accidental fires may break out. [0011]
  • Furthermore, marangoni drying can somewhat solve problems occurring during spin drying or IPA vapor drying. However, marangoni drying is not effective in removing various types of pollutants, such as particles, which may remain on the surface of the wafer. [0012]
  • SUMMARY OF THE INVENTION
  • Accordingly, the present invention provides an apparatus and method for cleaning and drying a semiconductor wafer using a mixture of IPA and DIW as a cleaning solution by which cleaning and drying effects can be increased due to premixing IPA and DIW in an accurate ratio before supplying them into a treating bath in which a cleaning process is performed and the cleaning solution used in the cleaning process can be circulated and reused to prevent waste and reduce environmental pollution. [0013]
  • According to an aspect of the present invention, there is provided an apparatus for cleaning and drying a semiconductor wafer. The apparatus includes a treating bath, a cleaning solution mixing unit, a cleaning solution supplying unit, and a return line. The treating bath is supplied with a cleaning solution from an external source and in which the semiconductor wafer is cleaned and dried. The cleaning solution mixing unit mixes cleaning solutions to be supplied into the treating bath in a predetermined ratio and includes isopropyl alcohol tanks that are supplied with isopropyl alcohol from an external source, mixing tanks that are supplied with deionized water from an external source, are connected to the isopropyl alcohol tanks to be supplied with isopropyl alcohol contained in the isopropyl alcohol tanks and mix isopropyl alcohol and deionized water, and level sensing means that sense the amount of isopropyl alcohol supplied into the IPA tanks and the amount of deionized water supplied into the mixing tanks. The cleaning solution supplying unit connects the mixing tanks to the treating bath and supplies the cleaning solution mixed in the mixing tanks into the treating bath. The return line returns the cleaning solution that was used in the cleaning of the semiconductor wafer back to the mixing tanks. [0014]
  • Two or more isopropyl alcohol tanks of the cleaning solution mixing unit are interconnected in parallel, the mixing tanks are connected to the isopropyl alcohol tanks, respectively, and disposed in parallel so that each of the isopropyl alcohol tanks and each of the mixing tanks make a group, and the cleaning solution circulates through a mixing tank in a group selected from two or more groups. [0015]
  • The level sensing means are a plurality of level sensors that are installed at the isopropyl alcohol tanks and a plurality of level sensors that are installed at the mixing tanks. [0016]
  • The cleaning solution mixing unit further includes a nitrogen bubble generator that injects a nitrogen gas into the mixing tanks so as to completely mix deionized water and isopropyl alcohol. [0017]
  • Isopropyl alcohol supplementing pumps additionally supply isopropyl alcohol in the isopropyl alcohol tanks into the mixing tanks by a desired amount are further installed between the isopropyl alcohol tanks and the mixing tanks. [0018]
  • The cleaning solution supplying unit includes a circulating pump, a filter, an isopropyl alcohol concentration measurer, and a liquid particle counter. The circulating pump pumps the cleaning solution in the mixing tanks into the treating bath. The filter filters the cleaning solution flowing via the circulating pump off impurities. The isopropyl alcohol concentration measurer checks the concentration of isopropyl alcohol contained in the cleaning solution that has passed through the filter. The liquid particle counter detects the amount of liquid particle contained in the cleaning solution flowing into the treating bath. [0019]
  • The return line includes a liquid particle counter that detects liquid particle contained in the cleaning solution returning from the treating bath back to the mixing tanks. [0020]
  • The apparatus further includes a heating tank, an isopropyl alcohol filter, an isopropyl alcohol collecting tank, a deionized water filter, and a deionized water collecting tank. The heating tank is connected to the cleaning solution mixing unit, is supplied the cleaning solution from the mixing tanks, and heats the cleaning solution, and evaporates isopropyl alcohol from the cleaning solution using a difference between boiling points of isopropyl alcohol and deionized water to decompose the cleaning solution into pure isopropyl alcohol and deionized water. The isopropyl alcohol filter is connected to the heating tank and filters vapor isopropyl alcohol off impurities. The isopropyl alcohol collecting tank is supplied with isopropyl alcohol filtered through the isopropyl alcohol filter and condenses isopropyl alcohol. The deionized water filter is connected to the heating tank and passes deionized water remaining in the heating tank to filter impurities of deionized water. The deionized water collecting tank is supplied with deionized water filtered through the deionized water filter and temporarily stores deionized water. [0021]
  • A sink that is supplied with deionized water from an external source and sinks a lower portion of the treating bath under deionized water is further installed beneath the treating bath. The sink includes an ultrasonic generator that generates ultrasonic waves, passes the ultrasonic waves through deionized water and the treating bath to the semiconductor wafer that is being cleaned in the treating bath. [0022]
  • According to another aspect of the present invention, there is also provided a method of cleaning and drying a wafer. Dionized water and isopropyl alcohol are mixed to make a cleaning solution. The cleaning solution is supplied into a treating bath so that the cleaning solution contacts the semiconductor wafer in the treating bath to clean the semiconductor wafer. After the semiconductor wafer is cleaned, the semiconductor wafer is separated from the cleaning solution. The semiconductor wafer separated from the cleaning solution is dried to remove the cleaning solution remaining on the semiconductor wafer. [0023]
  • Before the cleaning solution is supplied into the treating bath, the semiconductor wafer may be put into the treating bath. [0024]
  • After the supply of the cleaning solution into the cleaning bath is completed, the semiconductor wafer may be dipped into the cleaning solution. [0025]
  • The semiconductor wafer may be lifted up from the treating bath so that the semiconductor wafer is separated from the cleaning solution. [0026]
  • The cleaning solution may be discharged from the treating bath so that the semiconductor wafer is separated from the cleaning solution. [0027]
  • The concentration of isopropyl alcohol in the cleaning solution varies according to time to adjust the concentration of isopropyl alcohol to a target concentration. [0028]
  • A hot nitrogen gas is sprayed on the surface of the semiconductor wafer, contacts, and dries the surface of the semiconductor wafer.[0029]
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • The above features and advantages of the present invention will become more apparent by describing in detail exemplary embodiments thereof with reference to the attached drawings in which: [0030]
  • FIG. 1 is a schematic view of an apparatus for cleaning and drying a semiconductor wafer according to an embodiment of the present invention; [0031]
  • FIG. 2 is a view for explaining a step of dipping a semiconductor wafer into a treating bath during cleaning and drying a semiconductor wafer, according to an embodiment of the present invention; [0032]
  • FIG. 3 is a view for explaining a step of dipping a semiconductor wafer into a treating bath during cleaning and drying a semiconductor wafer, according to another embodiment of the present invention [0033]
  • FIGS. 4A through 4D are views illustrating examples of moving a semiconductor wafer within a cleaning solution to further effectively clean the semiconductor wafer put into a treating bath; [0034]
  • FIG. 5 is a view for explaining a method of separating a semiconductor wafer from a cleaning solution after the semiconductor wafer is cleaned in a treating bath using a method of cleaning and drying a semiconductor wafer according to an embodiment of the present invention; [0035]
  • FIG. 6 is a view for explaining a step of separating a semiconductor wafer from a cleaning solution after the semiconductor wafer is cleaned in a treating bath in a method of cleaning and drying a semiconductor wafer according to another embodiment of the present invention; [0036]
  • FIG. 7 is a view for explaining a step of separating a semiconductor wafer from a cleaning solution after the semiconductor wafer is cleaned in a treating bath in a method of cleaning and drying a semiconductor wafer according to still another embodiment of the present invention; [0037]
  • FIG. 8 is a view for explaining a step of spraying a nitrogen gas for drying a semiconductor wafer in a method of cleaning and drying a semiconductor wafer according to an embodiment of the present invention; [0038]
  • FIG. 9 is a view for explaining a step of spraying a nitrogen gas for drying a semiconductor wafer in a method of cleaning and drying a semiconductor wafer according to another embodiment of the present invention; [0039]
  • FIGS. 10 through 12 are views for explaining a step of changing the position of a semiconductor wafer with respect to a elevating support block when a nitrogen gas is sprayed on the semiconductor wafer; and [0040]
  • FIGS. 13 through 20 are graphs illustrating various ways to adjust the concentration of IPA in a cleaning solution used for cleaning and drying a semiconductor wafer according to an embodiment of the present invention.[0041]
  • DETAILED DESCRIPTION OF THE INVENTION
  • Hereinafter, a preferred embodiment of the present invention will be described in detail with reference to the attached drawings. [0042]
  • FIG. 1 is a schematic view of an apparatus for cleaning and drying a semiconductor wafer according to an embodiment of the present invention. Referring to FIG. 1, the apparatus includes a treating [0043] bath 11, a cleaning solution mixing unit 50, a cleaning solution supplying unit 52, a return line 54, a drain line 90, and a collecting unit 82. A wafer W is cleaned and dried in the treating bath 11. The cleaning solution mixing unit 50 premixes cleaning solutions to be supplied into the treating bath 11 in a predetermined ratio. The cleaning solution supplying unit 52 moves the cleaning solution mixed in the cleaning solution mixing unit 50 into the treating bath 11 and checks the state of the cleaning solution. The return line 54 returns the cleaning solution, which overflows after being used in a cleaning process in the treating bath 11, back to the cleaning solution mixing unit 50.
  • If necessary, the [0044] drain line 90 returns the cleaning solution from the treating bath 11 back to the cleaning solution mixing unit 50. The collecting unit 82 is connected to the cleaning solution mixing unit 50 and collects a polluted cleaning solution to decompose the polluted cleaning solution into IPA and DIW.
  • The treating [0045] bath 11 may accommodate one or more wafers to be cleaned and dried and is connected to the cleaning solution supplying unit 52 and the return line 54. The upper portion of the treating bath 11 is covered with a chamber cover 12 that is already known in the prior art.
  • The wafer W is supported by an elevating [0046] support block 92 shown in FIG. 10 in the treating bath 11. The elevating support block 92 is positioned inside the treating bath 11 when cleaning the wafer W so that the wafer W is sunk under the cleaning solution 5. However, when drying the wafer W, the elevating support block 92 ascends over the treating bath 11 as shown in FIG. 11.
  • The chamber cover [0047] 12 covers the treating bath 11 and induces a cleaning solution overflowing from the treating bath 11 to the return line 54. The chamber cover 12 also includes a plurality of nitrogen spraying nozzles 14. The nitrogen spraying nozzles 14 are supplied with a nitrogen gas from an external source, and further supply the nitrogen gas into the chamber cover 12 to fill the chamber cover 12 with the nitrogen gas. In particular, the nitrogen nozzles 14 spray the nitrogen gas on the wafer W when the wafer W rises onto the liquid surface of the cleaning solution in order to remove the cleaning solution attached to the surface of the wafer W.
  • A [0048] heater 80 is further installed to heat the nitrogen gas proceeding toward the nitrogen spraying nozzles 14. If necessary, the heater 80 can heat the nitrogen gas to further effectively remove the cleaning solution sticking to the surface of the wafer W.
  • A [0049] sink 84 is installed under the treating bath 11. The sink 84 contains DIW at a predetermined wafer level so that the lower portion of the treating bath 11 is sunk under the wafer surface of DIW. A wafer level sensor 88 is installed inside the sink 84. The level sensor 88 senses the level of DIW so that the lower portion of the treating bath 11 is always positioned under the level of DIW.
  • An [0050] ultrasonic generator 86 is installed beneath the sink 84. The ultrasonic generator 86 may be a general ultrasonic generator. Ultrasonic waves generated by the ultrasonic generator 86 pass through DIW in the sink 84, and then are transmitted to the wafer W through a case of the treating bath 11 and the cleaning solution 5.
  • In other words, when DIW is supplied into the [0051] sink 84 and the lower portion of the treating bath 11 is dipped into DIW, ultrasonic waves generated by the ultrasonic generator 86 are transmitted to the treating bath 11 through DIW during cleaning of the wafer W.
  • The cleaning [0052] solution mixing unit 50 includes IPA tanks 18 and 19 and mixing tanks 24 and 25 respectively connected to the IPA tanks 18 and 19. Since the IPA tanks 18 and 19 are disposed in parallel, IPA can be supplied simultaneously into the IPA tanks 18 and 19 from an external source. Also, since the mixing tanks 24 and 25 are disposed in parallel, DIW can be supplied simultaneously into the mixing tanks 24 and 25 from an external source.
  • Each of the [0053] IPA tanks 18 and 19 has a plurality of level sensors 20. The level sensors 20 sense the amount of IPA supplied into the IPA tanks 18 and 19 so that the desired amount of IPA is supplied. Each of the mixing tanks 24 and 25 also has a plurality of level sensors 21. The level sensors 21 sense the amount of DIW supplied into the mixing tanks 24 and 25 so that a desired amount of DIW is supplied.
  • [0054] Reference numeral 44 denotes an overflow drainpipe. As will be described later, the overflow drainpipe 44 discharges the cleaning solution outside the mixing tanks 24 and 25 when the cleaning solution returning back via the return line 54 or the drain line 90 rises above a predetermined level in the mixing tanks 24 and 25.
  • The [0055] IPA tanks 18 and 19 are respectively connected to the mixing tanks 24 and 25 via connecting pipes 56. Thus, IPA in the IPA tanks 18 and 19 moves into the mixing tanks 24 and 25 through the connecting pipes 56.
  • The necessary amount of DIW is separately supplied into the mixing [0056] tanks 24 and 25. Thus, in the mixing tanks 24 and 25, IPA supplied from the IPA tanks 18 and 19 are mixed with DIW at a predetermined ratio. Here, the amount of IPA supplied into the IPA tanks 18 and 19 and the amount of DIW supplied into the mixing tanks 24 and 25 can be respectively measured by the level sensors 20 and 21. Thus, the concentration of IPA to DIW can be adjusted, and thus cleaning solutions having a desired concentration can be obtained in the mixing tanks 24 and 25. In other words, the concentration of IPA illustrated in graphs of FIGS. 12 through 19 can be obtained.
  • Each of the connecting [0057] pipes 56 is split into two pipes. IPA supplementing pumps 22 and 23 are respectively installed at one of the two split connecting pipes 56. The IPA supplementing pumps 22 and 23 are used to additionally and quickly supply the accurate amount of IPA from the IPA tanks 18 and 19 into the mixing tanks 24 and 25.
  • Since IPA is volatile, IPA may gradually volatilize during the circulation of the cleaning solution. When IPA volatilizes, the concentration of IPA in the cleaning solution becomes low. Thus, the IPA supplementing pumps [0058] 22 and 23 supplement IPA by a shortage of IPA.
  • As described above, in each of the mixing [0059] tanks 24 and 25, IPA and DIW are mixed in a desired ratio. A nitrogen bubble generator 26 is additionally installed in order to completely mix IPA and DIW. The nitrogen bubble generator 26 is supplied with a nitrogen gas from an external source, sprays the nitrogen gas into the lower portions of the mixing tanks 24 and 25 so that DIW and IPA contained in the mixing tanks 24 and 25 are completely mixed.
  • Also, in the present embodiment, the cleaning [0060] solution mixing unit 50 includes the IPA tanks 18 and 19 and the mixing tanks 24 and 25. However, the number of IPA tanks and the number of mixing tanks may increase.
  • The mixing [0061] tanks 24 and 25 are connected to a supplying pipe 58 via mixed solution supplying valves 28 and 29.
  • The mixed [0062] solution supplying valves 28 and 29 are opened alternately not simultaneously. In other words, when the mixed solution supplying valve 28 is opened, the mixed solution supplying valve 29 is closed. Alternatively, when the mixed solution supplying valve 28 is closed, the mixed solution supplying valve 29 is opened. This means that while the cleaning solution in the mixing tank 24 is circulated and supplied into the treating bath 11, the cleaning solution in the mixing tank 25 is not circulated. In other words, in a case where only the mixed solution supplying valve 28 is opened to clean the wafer W using only the cleaning solution contained in the mixing tank 24, and after a predetermined period of time, the cleaning solution is polluted more than the allowed pollution level, the mixed solution supplying valve 28 is closed, the mixed solution supplying valve 29 is opened, and the cleaning solution contained in the mixing tank 25 is circulated to continue cleaning of the wafer W.
  • As described above, while the cleaning solution in the [0063] mixing tank 25 is supplied into the treating bath 11, a mixed solution discharging valve 30 of the mixing tank 24 is opened to discharge the polluted cleaning solution in the mixing tank 24. When the mixing tank 24 is completely emptied, the mixed solution discharging valve 30 is closed, IPA and DIW are newly supplied from external sources, IPA and DIW are mixed in a desired ratio, and the mixture is maintained in the mixing tank 24.
  • By alternately using the mixing [0064] tanks 24 and 25, a pure cleaning solution can be continuously supplied without stopping the apparatus for cleaning and drying a semiconductor wafer. Thus, a wafer can be quickly and effectively cleaned and dried.
  • Discharging [0065] pipes 64 and 65, which are respectively installed beneath the mixing tanks 24 and 25, discharge the cleaning solution in the mixing tanks 24 and 25 to the collecting unit 82 and are opened and closed by the mixed solution discharging valves 30 and 31.
  • The collecting [0066] unit 82 basically collects the cleaning solution that is polluted at an allowed pollution level or above due to the cleaning of a wafer and remakes the polluted cleaning solution into pure IPA and DIW.
  • The collecting [0067] unit 82 includes a heating tank 70, which is connected to the discharging pipes 64 and 65 and receives the polluted cleaning solution, an IPA collecting tank 74 and a DIW collecting tank 78, which are connected to the heating tank 70, an IPA filter 72, which removes impurities contained in IPA flowing from the heating tank 70 to the IPA collecting tank 74, and a DIW filter 76, which removes impurities contained in DIW flowing from the heating tank 70 to the DIW collecting tank 78.
  • The [0068] heating tank 70 receives and heats a cleaning solution and evaporates IPA in the cleaning solution having a relatively low boiling point to decompose the cleaning solution into DIW and IPA. In other words, the heating tank 70 decomposes a cleaning solution into IPA and DIW using a difference between boiling points of IPA and DIW.
  • IPA turning into a gaseous state in the [0069] heating tank 70 is filtered through the IPA filter 72, moves into the IPA collecting tank 74, is cooled, and is condensed into a liquid state in time.
  • An additional cooler may be installed to condense IPA. IPA collected in the [0070] IPA collecting tank 74 is supplied into the IPA tanks 18 and 19 of the cleaning solution mixing unit 50 and reused.
  • After IPA flows out of the [0071] heating tank 70, polluted DIW remains in the heating tank 70. Polluted DIW is filtered through the DIW filter 76, and then is temporarily stored in the DIW collecting tank 78. DIW collected in the DIW collecting tank 78 is supplied into the mixing tanks 24 and 25 of the cleaning solution mixing unit 50 and reused. Thus, the reuse of the cleaning solution can save considerably the cleaning solution.
  • The cleaning [0072] solution supplying unit 52, which moves the cleaning solution of a predetermined concentration supplied from the cleaning solution mixing unit 50 into the treating bath 11, includes a circulating pump 36, a filter 38, an IPA concentration measurer 40, and a liquid particle counter 42.
  • The circulating [0073] pump 36 is connected to the mixing tanks 24 and 25 via the mixed solution supplying valves 28 and 29. The circulating pump 36 pumps the cleaning solutions in the mixing tanks 24 and 25 into the treating bath 11 through the cleaning solution supplying unit 52.
  • The cleaning solution moving into the treating [0074] bath 11 via the circulating pump 36 is purified through the filter 38. The filter 38 passes the cleaning solution and filters off impurities contained in the cleaning solution so that the usable period of the cleaning solution is prolonged at its maximum.
  • The [0075] IPA concentration measurer 40 connected to the filter 38 checks the concentration of IPA in the cleaning solution that is circulating. Since IPA is volatile, the concentration of IPA may gradually become low during the circulation of the cleaning solution. Due to this, the IPA concentration measurer 40 is installed to continuously check the concentration of IPA in the cleaning solution. When IPA measurer 40 perceives that the concentration of IPA is reduced, the IPA supplementing pumps 22 and 23 operate to supplement IPA contained in the IPA tanks 18 and 19 into the mixing tanks 24 and 25 so that the cleaning solution returns to an optimum concentration level.
  • The [0076] liquid particle counter 42 detects the amount of liquid particle in the cleaning solution that is circulating to determine whether the cleaning solution has to be replaced. The liquid particle is a pollutant that is not filtered by the filter 38.
  • The cleaning solution supplied into the treating [0077] bath 11 through the cleaning solution supplying unit 52 cleans the wafer W in the treating bath 11, overflows from the treating bath 11, and flows to the return line 54.
  • The cleaning solution flowing through the [0078] return line 54 passes through the liquid particle counter 43 again. The liquid particle counter 42 detects liquid particle contained in the cleaning solution, which passed through the treating bath 11, and rechecks the pollution level of the cleaning solution that underwent the cleaning of the wafer W. The cleaning solution passing through the return line 54 returns back into the mixing tanks 24 and 25 via the return valve 60 or 61.
  • Drying the wafer W is accomplished by lifting the wafer W up over the liquid surface of the cleaning solution. In other words, when the wafer W is lifted up over the liquid surface of the cleaning solution, drying the wafer W is firstly achieved due to the surface tension of the cleaning solution. Next, while the wafer W is rising, the nitrogen gas is sprayed on the wafer W through the [0079] nitrogen nozzles 14 to secondly achieve the drying of the wafer W.
  • The procedure of lifting a wafer up over the liquid surface of a cleaning solution includes: moving the wafer over the liquid surface of the cleaning solution using an elevating support block [0080] 92 (shown in FIG. 10) while maintaining the level of the cleaning solution and reducing the level of the cleaning solution without moving the wafer.
  • The [0081] drain line 90 is just an apparatus for reducing the level of the cleaning solution without moving the wafer. The drain line 90 is connected to the lower portion of the treating bath 11 and the mixing tank 24 or 25 and discharges the cleaning solution 5 in the treating bath 11 downward, so that the wafer is firstly dried.
  • The [0082] drain line 90 controls the return values 60 and 61 to return the cleaning solution back to one of the mixing tanks 24 and 25 being used.
  • As described above, an apparatus for cleaning and drying a semiconductor wafer according to the present invention includes the cleaning [0083] solution mixing unit 50, which premixes cleaning solutions in a desired ratio, the cleaning solution supplying unit 52, which is supplied with the cleaning solution from the cleaning solution mixing unit 50 and supplies the cleaning solution into the treating bath 11, and the return line 54, which returns the cleaning solution used in the cleaning of the semiconductor wafer in the treating bath 11 back to the cleaning solution mixing unit 50. Thus, since the cleaning solution can be always maintained at an accurate concentration, effects of cleaning and drying the semiconductor wafer are good.
  • Since the cleaning solution discharged from the cleaning [0084] solution mixing unit 50 returns back through the return line 50, and then is reused to perform a cleaning process, the apparatus is economic. In particular, the collecting unit 82 decomposes a cleaning solution that is polluted at an allowed pollution level or above into pure IPA and DIW. Thus, the cleaning solution can be reused, the discarded amount of the cleaning solution can be remarkably reduced, and environmental pollution can be reduced.
  • A method of cleaning and drying a semiconductor wafer using the cleaning and drying apparatus can be basically divided into four steps. The four steps will be described below. [0085]
  • In the first step, DIW and IPA are mixed. As described above, the mixture of DIW and IPA is carried out by the cleaning [0086] solution mixing unit 50. In other words, the mixing tanks 24 and 25 are supplied with IPA and DIW, and then IPA and DIW is completely mixed by the nitrogen bubble generator 26.
  • In the second step, a cleaning solution made by mixing IPA and DIW in the first step is supplied into the treating [0087] bath 11 so as to contact the wafer in the treating bath 11.
  • The cleaning solution may contact a wafer according to two ways. In one of the two ways, a wafer W is put into the treating [0088] bath 11 in advance, and then a cleaning solution is supplied into the treating bath 11 to gradually raise the liquid surface of the cleaning solution so that the wafer W is dipped into the cleaning solution. In the other way, when a cleaning solution is continuously supplied into the treating bath 11 to maintain the cleaning solution at a predetermined level, the wafer W descends to be dipped into the cleaning solution.
  • FIGS. 2 and 3 illustrate a wafer W descending into a cleaning solution. [0089]
  • FIG. 2 illustrates a wafer W that vertically descends, and FIG. 3 illustrates a wafer W that descends while swaying from side to side. When the wafer W descends while swaying from side to side, the wafer W rubs on a [0090] cleaning solution 5, which results in an increase in a cleaning effect.
  • Besides the two methods, the method of dipping a wafer into a cleaning solution may be modified into various forms. [0091]
  • In order to supply a cleaning solution into the treating [0092] bath 11 with a wafer placed in the treating bath 11 in advance so that the wafer is dipped into the cleaning solution, the treating bath 11 has to be pre-emptied. To empty the treating bath 11, the drain line 90 is opened to return the cleaning solution in the treating bath 11 back to the mixing tanks 24 and 25.
  • When wafer is dipped into a cleaning solution, it is preferable that the wafer moves so as to rub the wafer on the cleaning solution till the wafer is separated from the cleaning solution. [0093]
  • FIGS. 4A through 4D illustrate a wafer that moves in the cleaning solution. [0094]
  • FIG. 4A illustrates a wafer W that vertically sways, FIG. 4B illustrates a wafer W horizontally sways, FIG. 4C illustrates a wafer W that turns around the axis (Y-axis) of the vertical direction, FIG. 4D illustrates a wafer W that turns around the axis (X-axis) of the horizontal direction. [0095]
  • As described above, impurities such as various types of particles can be effectively removed from the surface of a wafer by moving the wafer within a cleansing solution. [0096]
  • In the third step, the wafer W is separated from a [0097] cleaning solution 5. FIGS. 5 through 7 illustrate a method of separating the wafer W from the cleaning solution 5.
  • In FIGS. 5 and 6, the wafer W is lifted up with the liquid surface of the [0098] cleaning solution 5 maintained, and in FIG. 7, the cleaning solution 5 is discharged with the wafer W left in the treating bath 11. Also, in FIG. 5, the wafer W is vertically lifted up, and in FIG. 6, the wafer W sways from side to side when being lifted up so that the friction between the wafer W and the cleaning solution 5 increases.
  • As shown in FIGS. 5 and 6, paths for taking the wafer W out of the treating [0099] bath 11 may be changes in other various forms.
  • The supply of the [0100] cleaning solution 5 into the treating bath 11 has to stop and the drain line 90 has to be opened in order to discharge the cleaning solution 5 as shown in FIG. 7. When the drain line 90 is opened, the cleaning solution 5 in the treating bath 11 returns back to mixing tanks that are operating.
  • After the wafer W is completely separated from the [0101] cleaning solution 5, the fourth step is performed. In the fourth step, the remaining cleaning solution is removed from the surface of the wafer W separated from the cleaning solution 5. Also, the fourth step is carried out in the treating bath 11 from which the cleaning solution 5 is removed or over the treating bath 11 when the cleaning solution 5 remains in the treating bath 11.
  • In the fourth step, a nitrogen gas having a high temperature, preferably a temperature within a range of 50-150° C., is sprayed on the surface of the wafer W at a predetermined pressure so as to remove the cleaning solution remaining on the surface of the wafer W. [0102]
  • FIG. 8 illustrates a state where when the wafer W is lifted up over the treating [0103] bath 11, a hot nitrogen gas is concentratedly sprayed on the surface of the wafer W. In this state, the remaining cleaning solution is removed due to the pressure of spraying the nitrogen gas and heat transmitted from the nitrogen gas.
  • FIG. 9 illustrates a state where a hot nitrogen gas is sprayed on the wafer W in the vertical laminar flow. Thereafter, the hot nitrogen gas contacts the surface of the wafer W to transmit heat to the surface of the wafer W so that a mixed solution is evaporated and dried. [0104]
  • FIGS. 10 and 13 are views for explaining a step of changing the position of a wafer relative to an elevating support block and side support blocks when a nitrogen gas is sprayed on the wafer. As the elevating support block and the side support blocks, various types of elevating support blocks and side support blocks have been proposed. [0105]
  • The elevating [0106] support block 92 ascends and descends while vertically supporting a plurality of wafers. Side support blocks 94 temporarily separate a wafer W from the elevating support block 92 when the wafer W goes up, so that a lower edge Z of the wafer W is separated from the elevating support block 92 as shown in FIG. 12. When the elevating support block 92 ascends, the side support blocks 94 are fully apart from the wafer W so that the wafer W passes through a space between the side support blocks 94.
  • As can seen in FIG. 10, the wafer W is dipped under the [0107] cleaning solution 5 when being supported by the elevating support block 92. The side support blocks 94 are positioned over the treating bath 11. The side support blocks 94 are parallel and can move along directions indicated by arrows. If necessary, the side support blocks 94 support sides of the wafer W as shown in FIG. 12.
  • As shown in FIG. 10, when the wafer W is completely cleaned under the [0108] cleaning solution 5, the elevating support block 92 goes up in direction U indicated by arrow so that the wafer W is separated from the cleaning solution 5. Thereafter, a nitrogen gas is sprayed on the wafer W.
  • Referring to FIG. 11, the elevating [0109] support 92 completely moves up over the treating bath 11 and the wafer W is positioned between the-side support blocks 94. Here, since the lower edge Z of the wafer W contacts the elevating support block 92, the nitrogen gas does not reaches the lower edge Z, and thus the lower edge Z is not completely dried. Thus, the side support blocks 94 moves along direction A indicated by arrow so as to support the sides of the wafer W, while the elevating support block 92 temporarily descends as shown in FIG. 12.
  • Referring to FIG. 12, the side support blocks [0110] 94 support the sides of the wafer W and the elevating support block 92 goes down, so that the nitrogen gas is sprayed on the lower edge Z. Here, the elevating support block 92 must not sink under the cleaning solution 5.
  • When the wafer W is completely dried, the elevating [0111] support 92 ascends and the side support blocks 94 are separated from the wafer W so that the elevating support block 92 re-supports the wafer W, and then the wafer W is taken out from the elevating support block 92.
  • Finally, a wafer is completely cleaned and dried through the first through fourth steps. [0112]
  • FIGS. 13 through 20 are graphs illustrating ways to adjust the concentration of IPA with respect to variations in the time required for supplying a cleaning solution into a treating bath. When the concentration of IPA is properly adjusted to work conditions or other requirements, an improved cleaning effect can be achieved. In addition, the adjustment of the concentration of IPA can be realized by the IPA supplementing pumps [0113] 22 and 23 described with reference to FIG. 1.
  • FIG. 13 illustrates a state where a cleaning solution containing IPA and DIW of a predetermined ratio is supplied into a treating bath without varying the concentration of IPA. [0114]
  • FIG. 14 illustrates a state where when only DIW is first supplied into a treating bath, and then the addition of IPA to DIW is gradually increased and the concentration of IPA reaches a predetermined level, the supply of IPA stops. [0115]
  • FIG. 15 illustrates a state where when the concentration of IPA of a cleaning solution supplied into a treating bath is gradually increased and reaches a predetermined level, the addition of IPA stops. [0116]
  • FIG. 16 illustrates a state where the concentration of IPA to DIW is increased at regular intervals not gradually. [0117]
  • FIG. 17 illustrates a state where only pure IPA is first supplied into a treating bath, and then DIW is supplied into the treating bath at predetermined time intervals, so that the concentration of IPA becomes low. [0118]
  • FIG. 18 illustrates a state where a cleaning solution containing IPA of a predetermined concentration is supplied into a treating bath, and then the addition of IPA is reduced from a predetermined point of time, so that only DIW is supplied. [0119]
  • FIG. 19 illustrates a state where a cleaning solution containing IPA of a predetermined concentration is first supplied into a treating bath, and then the addition of IPA is gradually increased, so that the concentration of IPA becomes higher. [0120]
  • FIG. 20 illustrates a state where a cleaning solution containing IPA of a predetermined concentration is first supplied into a treating bath, and then the addition of IPA is gradually reduced, so that the concentration of IPA becomes lower. [0121]
  • In an apparatus and method for cleaning and drying a semiconductor wafer according to the present invention, before DIW and IPA are supplied into a treating bath, IPA and DIW are completely mixed so that cleaning and drying works are effectively performed. Also, a cleaning solution can be reused to prevent waste of the cleaning solution. [0122]
  • In addition, the semiconductor wafer is taken as an example of an object to be cleaned. However, the object to be cleaned is not limited to the semiconductor wafer, and the present invention may be applied to various objects including a substrate for a liquid crystal display device only, a substrate for a recording disc only, a substrate for a mask only, or the like. [0123]
  • While the present invention has been particularly shown and described with reference to exemplary embodiments thereof, it will be understood by those of ordinary skill in the art that various changes in form and details may be made therein without departing from the spirit and scope of the present invention as defined by the following claims. [0124]

Claims (16)

What is claimed is:
1. An apparatus for cleaning and drying a semiconductor wafer, the apparatus comprising:
a treating bath supplied with a cleaning solution from an external source and in which the semiconductor wafer is cleaned and dried;
a cleaning solution mixing unit wherein cleaning solutions to be supplied into the treating bath are mixed in a predetermined ratio and including isopropyl alcohol tanks that are supplied with isopropyl alcohol from an external source, mixing tanks that are supplied with deionized water from an external source, are connected to the isopropyl alcohol tanks to be supplied with isopropyl alcohol contained in the isopropyl alcohol tanks and mix isopropyl alcohol and deionized water, and level sensing means that sense the amount of isopropyl alcohol supplied into the IPA tanks and the amount of deionized water supplied into the mixing tanks;
a cleaning solution supplying unit that connects the mixing tanks to the treating bath and supplies the cleaning solution mixed in the mixing tanks into the treating bath; and
a return line through which the cleaning solution that was used in the cleaning of the semiconductor wafer is returned back to the mixing tanks.
2. The apparatus of claim 1, wherein two or more isopropyl alcohol tanks of the cleaning solution mixing unit are interconnected in parallel, the mixing tanks are connected to the isopropyl alcohol tanks, respectively, and disposed in parallel so that each of the isopropyl alcohol tanks and each of the mixing tanks make a group, and the cleaning solution circulates through a mixing tank in a group selected from two or more groups.
3. The apparatus of claim 1 or 2, wherein the level sensing means are a plurality of level sensors that are installed at the isopropyl alcohol tanks and a plurality of level sensors that are installed at the mixing tanks.
4. The apparatus of claim 1 or 2, wherein the cleaning solution mixing unit further comprises a nitrogen bubble generator that injects a nitrogen gas into the mixing tanks so as to completely mix deionized water and isopropyl alcohol.
5. The apparatus of claim 1 or 2, wherein isopropyl alcohol supplementing pumps that additionally supply isopropyl alcohol in the isopropyl alcohol tanks into the mixing tanks by a desired amount are further installed between the isopropyl alcohol tanks and the mixing tanks.
6. The apparatus of claim 1 or 2, wherein the cleaning solution supplying unit comprises:
a circulating pump that pumps the cleaning solution in the mixing tanks into the treating bath;
a filter that filters the cleaning solution flowing via the circulating pump off impurities;
an isopropyl alcohol concentration measurer that checks the concentration of isopropyl alcohol contained in the cleaning solution that has passed through the filter; and
a liquid particle counter that detects the amount of liquid particle contained in the cleaning solution flowing into the treating bath.
7. The apparatus of claim 1 or 2, wherein the return line comprises a liquid particle counter that detects liquid particle contained in the cleaning solution returning from the treating bath back to the mixing tanks.
8. The apparatus of claim 1 or 2, further comprising:
a heating tank that is connected to the cleaning solution mixing unit, is supplied the cleaning solution from the mixing tanks, and heats the cleaning solution, and evaporates isopropyl alcohol from the cleaning solution using a difference between boiling points of isopropyl alcohol and deionized water to decompose the cleaning solution into pure isopropyl alcohol and deionized water;
an isopropyl alcohol filter that is connected to the heating tank and filters vapor isopropyl alcohol off impurities;
an isopropyl alcohol collecting tank that is supplied with isopropyl alcohol filtered through the isopropyl alcohol filter and condenses isopropyl alcohol;
a deionized water filter that is connected to the heating tank and passes deionized water remaining in the heating tank to filter impurities of deionized water; and
a deionized water collecting tank that is supplied with deionized water filtered through the deionized water filter and temporarily stores deionized water.
9. The apparatus of claim 1 or 2, wherein a sink that is supplied with deionized water from an external source and sinks a lower portion of the treating bath under deionized water is further installed beneath the treating bath, wherein the sink includes an ultrasonic generator that generates ultrasonic waves, passes the ultrasonic waves through deionized water and the treating bath to the semiconductor wafer that is being cleaned in the treating bath.
10. A method of cleaning and drying a wafer, the method comprising:
(a) mixing deionized water and isopropyl alcohol to make a cleaning solution;
(b) supplying the cleaning solution into a treating bath so that the cleaning solution contacts the semiconductor wafer in the treating bath to clean the semiconductor wafer;
(c) after the semiconductor wafer is cleaned, separating the semiconductor wafer from the cleaning solution;
(d) drying the semiconductor wafer separated from the cleaning solution to remove the cleaning solution remaining on the semiconductor wafer.
11. The method of claim 10, wherein in step (b), before the cleaning solution is supplied into the treating bath, the semiconductor wafer is put into the treating bath.
12. The method of claim 10, wherein in step (b), after the supply of the cleaning solution into the cleaning bath is completed, the semiconductor wafer is dipped into the cleaning solution.
13. The method of claim 10, wherein in step (c), the semiconductor wafer is lifted up from the treating bath so that the semiconductor wafer is separated from the cleaning solution.
14. The method of claim 10, wherein in step (c), the cleaning solution is discharged from the treating bath so that the semiconductor wafer is separated from the cleaning solution.
15. The method of claim 10, wherein in step (a), the concentration of isopropyl alcohol in the cleaning solution varies according to time to adjust the concentration of isopropyl alcohol to a target concentration.
16. The method of claim 10, wherein in step (d), a hot nitrogen gas is sprayed on the surface of the semiconductor wafer, contacts, and dries the surface of the semiconductor wafer.
US10/373,684 2002-02-28 2003-02-27 Method and apparatus for cleaning and drying semiconductor wafer Abandoned US20030159713A1 (en)

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KR10-2002-0010969A KR100431186B1 (en) 2002-02-28 2002-02-28 Cleaning and drying method for wafer
KR2002-10969 2002-02-28
KR1020020059764A KR20040032200A (en) 2002-10-01 2002-10-01 Apparatus for washing and drying wafer and method of washing and drying wafer using that
KR1020020059765A KR100413030B1 (en) 2002-10-01 2002-10-01 Semiconductor wafer cleaning and drying apparatus
KR2002-59765 2002-10-01
KR2002-59764 2002-10-01

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Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20060048798A1 (en) * 2004-09-09 2006-03-09 Honeywell International Inc. Methods of cleaning optical substrates
US20070289611A1 (en) * 2006-06-19 2007-12-20 Toyohide Hayashi Substrate treatment method and substrate treatment apparatus
US20080023444A1 (en) * 2006-07-25 2008-01-31 Atsushi Osawa Substrate processing apparatus and substrate processing method
EP1909313A1 (en) * 2005-06-22 2008-04-09 Tokyo Electron Limited Substrate processing apparatus and substrate processing method
US20080118995A1 (en) * 2006-11-17 2008-05-22 Dnyanesh Chandrakant Tamboli Method and composition for restoring dielectric properties of porous dielectric materials
WO2008060069A1 (en) * 2006-11-14 2008-05-22 Mujin Electronics Co., Ltd Method for cleaning a substrate
US20080190455A1 (en) * 2005-05-13 2008-08-14 Sez Ag Method for Drying a Surface
US20080271749A1 (en) * 2007-05-02 2008-11-06 Lam Research Corporation Substrate cleaning technique employing multi-phase solution
US20090095327A1 (en) * 2007-10-10 2009-04-16 Dong-Soon Hwang Substrate support unit, and substrate treating apparatus and method using the same
US20100122713A1 (en) * 2007-05-10 2010-05-20 Tadaharu Tanaka Washing method and apparatus for use therein
WO2012116270A2 (en) * 2011-02-24 2012-08-30 Quantum Global Technologies LLC Real time liquid particle counter (lpc) end point detection system
CN102768972A (en) * 2012-07-11 2012-11-07 清华大学 Wafer drying device
US8404056B1 (en) 2009-05-27 2013-03-26 WD Media, LLC Process control for a sonication cleaning tank
US8863763B1 (en) 2009-05-27 2014-10-21 WD Media, LLC Sonication cleaning with a particle counter
US20150004741A1 (en) * 2009-01-13 2015-01-01 Kabushiki Kaisha Watanabe Shoko Wafer separation method, wafer separation and transfer method, and solar cell wafer separation and transfer method
US9811096B2 (en) 2013-05-14 2017-11-07 Shibaura Mechatronics Corporation Liquid feeding device and substrate treating device
WO2017196493A1 (en) * 2016-05-13 2017-11-16 Applied Materials, Inc. Liquid particle counting of semiconductor component parts
US10081036B2 (en) 2016-09-19 2018-09-25 Applied Materials, Inc. Methods and systems for liquid particle prequalification

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* Cited by examiner, † Cited by third party
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US7247579B2 (en) * 2004-12-23 2007-07-24 Lam Research Corporation Cleaning methods for silicon electrode assembly surface contamination removal
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Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5234504A (en) * 1991-11-25 1993-08-10 Grc Environmental, Inc. Methods for removing contaminants from contaminated solids (II)
US5415191A (en) * 1991-01-28 1995-05-16 Kabushiki Kaisha Toshiba Arrangement for cleaning semiconductor wafers using mixer
US5716458A (en) * 1995-02-07 1998-02-10 Nikon Corporation Method of washing and drying an article
US5845660A (en) * 1995-12-07 1998-12-08 Tokyo Electron Limited Substrate washing and drying apparatus, substrate washing method, and substrate washing apparatus
US5858106A (en) * 1996-01-12 1999-01-12 Tadahiro Ohmi Cleaning method for peeling and removing photoresist
US5908509A (en) * 1993-10-20 1999-06-01 Verteq, Inc. Semiconductor wafer cleaning system
US6221167B1 (en) * 1998-02-13 2001-04-24 Applied Science Karasawa Lab. & Co., Ltd. Process and system for treatments by fluids
US6334470B2 (en) * 1999-03-19 2002-01-01 Healy Systems, Inc. Coaxial vapor flow indicator with pump speed control
US6695926B1 (en) * 1997-07-09 2004-02-24 Ses Co., Ltd. Treatment method of semiconductor wafers and the like and treatment system for the same

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3138901B2 (en) * 1993-08-06 2001-02-26 大日本スクリーン製造株式会社 Substrate immersion processing equipment
JPH0861846A (en) * 1994-08-22 1996-03-08 Sony Corp Method and apparatus for drying semiconductor wafer
JP2663899B2 (en) * 1995-02-28 1997-10-15 日本電気株式会社 Wafer cleaning apparatus and wafer cleaning method
JPH09153475A (en) * 1995-09-27 1997-06-10 Komatsu Ltd Semiconductor cleaning/drying method and device
JPH10128094A (en) * 1996-10-31 1998-05-19 Dainippon Screen Mfg Co Ltd Chemical treating device for substrate
JPH1116873A (en) * 1997-06-25 1999-01-22 Mitsubishi Chem Corp Method and equipment for drying
JP3343651B2 (en) * 1998-02-17 2002-11-11 東京エレクトロン株式会社 Cleaning treatment method
JP2001308058A (en) * 2000-04-26 2001-11-02 Tamotsu Mesaki Drier for semiconductor material, and the like

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5415191A (en) * 1991-01-28 1995-05-16 Kabushiki Kaisha Toshiba Arrangement for cleaning semiconductor wafers using mixer
US5234504A (en) * 1991-11-25 1993-08-10 Grc Environmental, Inc. Methods for removing contaminants from contaminated solids (II)
US5908509A (en) * 1993-10-20 1999-06-01 Verteq, Inc. Semiconductor wafer cleaning system
US5716458A (en) * 1995-02-07 1998-02-10 Nikon Corporation Method of washing and drying an article
US5845660A (en) * 1995-12-07 1998-12-08 Tokyo Electron Limited Substrate washing and drying apparatus, substrate washing method, and substrate washing apparatus
US5858106A (en) * 1996-01-12 1999-01-12 Tadahiro Ohmi Cleaning method for peeling and removing photoresist
US6695926B1 (en) * 1997-07-09 2004-02-24 Ses Co., Ltd. Treatment method of semiconductor wafers and the like and treatment system for the same
US6221167B1 (en) * 1998-02-13 2001-04-24 Applied Science Karasawa Lab. & Co., Ltd. Process and system for treatments by fluids
US6334470B2 (en) * 1999-03-19 2002-01-01 Healy Systems, Inc. Coaxial vapor flow indicator with pump speed control

Cited By (33)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20060048798A1 (en) * 2004-09-09 2006-03-09 Honeywell International Inc. Methods of cleaning optical substrates
US20080190455A1 (en) * 2005-05-13 2008-08-14 Sez Ag Method for Drying a Surface
US8038804B2 (en) * 2005-05-13 2011-10-18 Lam Research Ag Method for drying a surface
EP1909313A1 (en) * 2005-06-22 2008-04-09 Tokyo Electron Limited Substrate processing apparatus and substrate processing method
US8303724B2 (en) 2005-06-22 2012-11-06 Tokyo Electron Limited Substrate processing method and non-transitory storage medium for carrying out such method
EP1909313A4 (en) * 2005-06-22 2011-11-09 Tokyo Electron Ltd Substrate processing apparatus and substrate processing method
US20090101186A1 (en) * 2005-06-22 2009-04-23 Koukichi Hiroshiro Substrate Processing Apparatus and Substrate Processing Method
US8015984B2 (en) * 2005-06-22 2011-09-13 Tokyo Electron Limited Substrate processing apparatus including a drying mechanism using a fluid mixture of purified water and a volatile organic solvent
US7785421B2 (en) * 2006-06-19 2010-08-31 Dainippon Screen Mfg. Co., Ltd. Substrate treatment method and substrate treatment apparatus
US20070289611A1 (en) * 2006-06-19 2007-12-20 Toyohide Hayashi Substrate treatment method and substrate treatment apparatus
US20080023444A1 (en) * 2006-07-25 2008-01-31 Atsushi Osawa Substrate processing apparatus and substrate processing method
WO2008060069A1 (en) * 2006-11-14 2008-05-22 Mujin Electronics Co., Ltd Method for cleaning a substrate
US7977121B2 (en) 2006-11-17 2011-07-12 Air Products And Chemicals, Inc. Method and composition for restoring dielectric properties of porous dielectric materials
US20080118995A1 (en) * 2006-11-17 2008-05-22 Dnyanesh Chandrakant Tamboli Method and composition for restoring dielectric properties of porous dielectric materials
US20080271749A1 (en) * 2007-05-02 2008-11-06 Lam Research Corporation Substrate cleaning technique employing multi-phase solution
US8388762B2 (en) * 2007-05-02 2013-03-05 Lam Research Corporation Substrate cleaning technique employing multi-phase solution
US20100122713A1 (en) * 2007-05-10 2010-05-20 Tadaharu Tanaka Washing method and apparatus for use therein
US20090095327A1 (en) * 2007-10-10 2009-04-16 Dong-Soon Hwang Substrate support unit, and substrate treating apparatus and method using the same
US8297293B2 (en) * 2007-10-10 2012-10-30 Semes Co. Ltd Substrate support unit, and substrate treating apparatus and method using the same
US20150004741A1 (en) * 2009-01-13 2015-01-01 Kabushiki Kaisha Watanabe Shoko Wafer separation method, wafer separation and transfer method, and solar cell wafer separation and transfer method
US8863763B1 (en) 2009-05-27 2014-10-21 WD Media, LLC Sonication cleaning with a particle counter
US8404056B1 (en) 2009-05-27 2013-03-26 WD Media, LLC Process control for a sonication cleaning tank
WO2012116270A3 (en) * 2011-02-24 2013-02-21 Quantum Global Technologies LLC Real time liquid particle counter (lpc) end point detection system
US20120216833A1 (en) * 2011-02-24 2012-08-30 Applied Materials, Inc. Real time liquid particle counter (lpc) end point detection system
WO2012116270A2 (en) * 2011-02-24 2012-08-30 Quantum Global Technologies LLC Real time liquid particle counter (lpc) end point detection system
US20160056061A1 (en) * 2011-02-24 2016-02-25 Quantum Global Technologies LLC Real time liquid particle counter (lpc) end point detection system
CN102768972A (en) * 2012-07-11 2012-11-07 清华大学 Wafer drying device
US9811096B2 (en) 2013-05-14 2017-11-07 Shibaura Mechatronics Corporation Liquid feeding device and substrate treating device
WO2017196493A1 (en) * 2016-05-13 2017-11-16 Applied Materials, Inc. Liquid particle counting of semiconductor component parts
US10453709B2 (en) 2016-05-13 2019-10-22 Applied Materials, Inc. Liquid particle counting of semiconductor component parts
US10081036B2 (en) 2016-09-19 2018-09-25 Applied Materials, Inc. Methods and systems for liquid particle prequalification
TWI739900B (en) * 2016-09-19 2021-09-21 美商應用材料股份有限公司 Methods and systems for liquid particle prequalification
US11192153B2 (en) 2016-09-19 2021-12-07 Applied Materials, Inc. Methods and systems for liquid particle prequalification

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