Source: https://patents.google.com/patent/US9857699B2/en
Timestamp: 2019-08-24 10:04:13
Document Index: 686399471

Matched Legal Cases: ['Application No. 201010143405', 'Application No. 05747245', 'Application No. 2005', 'Application No. 05256461', 'application No. 2007', 'Application No. 2010', 'Application No. 10']

US9857699B2 - Vacuum system for immersion photolithography - Google Patents
Vacuum system for immersion photolithography Download PDF
US9857699B2
US9857699B2 US15/362,530 US201615362530A US9857699B2 US 9857699 B2 US9857699 B2 US 9857699B2 US 201615362530 A US201615362530 A US 201615362530A US 9857699 B2 US9857699 B2 US 9857699B2
US15/362,530
US20170075233A1 (en
Andrew John Harpham
Paul John Shechter
Paul Alan Stockman
2004-06-16 Priority to US10/869,191 priority Critical patent/US7481867B2/en
2008-12-19 Priority to US12/340,326 priority patent/US8164734B2/en
2011-07-20 Priority to US13/187,166 priority patent/US8830440B2/en
2014-08-26 Priority to US14/469,389 priority patent/US9507270B2/en
2016-11-28 Priority to US15/362,530 priority patent/US9857699B2/en
2016-11-28 Application filed by ASML Netherlands BV filed Critical ASML Netherlands BV
2016-11-29 Assigned to THE BOC GROUP PLC reassignment THE BOC GROUP PLC ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: SHECHTER, PAUL JOHN, STOCKMAN, PAUL ALAN, HARPHAM, ANDREW JOHN
2016-11-29 Assigned to EDWARDS LIMITED reassignment EDWARDS LIMITED ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: THE BOC GROUP PLC/BOC LIMITED
2016-11-29 Assigned to ASML NETHERLANDS B.V. reassignment ASML NETHERLANDS B.V. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: EDWARDS LIMITED
2017-03-16 Publication of US20170075233A1 publication Critical patent/US20170075233A1/en
2018-01-02 Publication of US9857699B2 publication Critical patent/US9857699B2/en
A vacuum system for extracting a stream of a multi-phase fluid from a photo-lithography tool comprises a pumping arrangement for drawing the fluid from the tool, and an extraction tank located upstream from the pumping arrangement for separating the fluid drawn from the tool into gas and liquid phases. The pumping arrangement comprises a first pump for extracting gas from the tank, and a second pump for extracting liquid from the tank. In order to minimize any pressure fluctuations transmitted from the vacuum system back to the fluid within the tool, a pressure control system maintains a substantially constant pressure in the tank by regulating the amounts of liquid and gas within the tank.
The present application is a continuation of co-pending U.S. patent application Ser. No. 14/469,389, filed Aug. 26, 2014, which is a continuation of U.S. patent application Ser. No. 13/187,166, filed Jul. 20, 2011, now U.S. Pat. No. 8,830,440, which is a continuation of U.S. patent application Ser. No. 12/340,326, filed Dec. 19, 2008, now U.S. Pat. No. 8,164,734, which is a continuation of U.S. patent application Ser. No. 10/869,191, filed on Jun. 16, 2004, now U.S. Pat. No. 7,481,867. The entire content of each of the foregoing applications is herein fully incorporated by reference.
This invention relates to a vacuum system for extracting a multi-phase fluid, and more particularly for extracting a multi-phase fluid from an immersion photolithography exposure tool.
Photolithography is an important process step in semiconductor device fabrication. In photolithography, a circuit design is transferred to a wafer through a pattern imaged onto a photoresist layer deposited on the wafer surface. The wafer then undergoes various etch and deposition processes before a new design is transferred to the wafer surface. This cyclical process continues, building up multiple layers of the semiconductor device.
The minimum feature that may be printed using photolithography is determined by the resolution limit W, which is defined by the Rayleigh equation as:
W = k 1 ⁢ λ NA ( 1 )
where k1 is the resolution factor, λ is the wavelength of the exposing radiation and NA is the numerical aperture. In lithographic processes used in the manufacture of semiconductor devices, it is therefore advantageous to use radiation of very short wavelength in order to improve optical resolution so that very small features in the device may be accurately reproduced. Monochromatic visible light of various wavelengths have been used, and more recently radiation in the deep ultra violet (DUV) range has been used, including radiation at 193 nm as generated using an ArF excimer laser.
The value of NA is determined by the acceptance angle (α) of the lens and the index of refraction (n) of the medium surrounding the lens, and is given by the equation:
NA=n sin α (2)
For clean dry air (CDA), the value of n is 1, and so the physical limit to NA for a lithographic technique using CDA as a medium between the lens and the wafer is 1, with the practical limit being currently around 0.9.
Immersion photolithography is a known technique for improving optical resolution by increasing the value of NA. With reference to FIG. 1, in this technique a liquid 10 having a refractive index n>1 is placed between the lower surface of the objective lens 12 of a projection device 14 and the upper surface of a wafer 16 located on a moveable wafer stage 18. The liquid placed between lens 12 and wafer 16 should, ideally, have a low optical absorption at 193 nm, be compatible with the lens material and the photoresist deposited on the wafer surface, and have good uniformity. These criteria are met by ultra-pure, degassed water, which has a refractive index n≈1.44. The increased value of n, in comparison to a technique where the medium between lens and wafer is CDA, increases the value of NA, which in turn decreases the resolution limit W, enabling smaller features to be reproduced.
Due to outgassing from the photoresist layer and the generation of particulates during photolithography, it is desirable to maintain a steady flow of water between the lens 12 and the wafer 16. For example, as described in US 2004/0075895 the lens and wafer could be immersed in a bath of water supported by the wafer stage, with a pump used to recirculate the water within the bath. However, due to the weight of the water bath acting on the wafer stage, this technique is generally considered undesirable.
An alternative technique, as shown in FIG. 1, is to use a nozzle or showerhead device 20 connected to a water source and a vacuum system, shown generally at 22, to produce a localized stream of ultra-pure, degassed water between the lens 12 and the wafer 16. To prevent the ingress of water into other parts of the tool, for example, the mechanism used to move the wafer stage 18, one or more differential air seals 24 are used. As a result, the vacuum system 22 extracts from the tool a multi-phase mixture of water and CDA. However, the extraction of such a multi-phase mixture from the tool using a single vacuum pump, especially in slug or churn regime flows, can generate undesirable pressure and flow fluctuations upstream of the pump, which could be transmitted back to the tool. This could lead to errors in the photolithography process, for example, through variations in the refractive index of the medium located between the lens and the wafer, or through the transmission of mechanical vibrations to the tool.
It is an object of the present invention to provide a vacuum system for extracting a stream of a multi-phase fluid from a photolithography tool and which can minimize any pressure fluctuations imparted thereby to fluid within the tool.
In a first aspect, the present invention provides a system for extracting a stream of multi-phase fluid from a photo-lithography tool, the system comprising a pumping arrangement for drawing the fluid from the tool, separating means located upstream from the pumping arrangement for separating the fluid drawn from the tool into gas and liquid phases, the pumping arrangement comprising a first pumping unit for extracting gas from the separating means and a second pumping unit for extracting liquid from the separating means, and a pressure control system for controlling the pressure within the separating means by regulating the amounts of gas and liquid therewithin.
In order to minimize any pressure fluctuations transmitted from the system back to the fluid within the tool, the pressure control system can maintain a substantially constant pressure in the separating means by regulating the amounts of liquid and gas within the separating means.
In order to control the amount of gas within the separating means, the pressure control system preferably comprises means for supplying gas to the separating means from a source thereof, and control means for controlling the flow of gas to the separating means. For example, where there is a variation in the flow of fluid into the separating means, and/or a variation in the flow of gas from the separating means, gas can be introduced into the separating means from the external source to compensate for such variations. In a preferred embodiment, the pressure control system comprises a variable flow control device, such as a butterfly or other control valve, through which gas is supplied to the separating means, with the control means being configured to vary the conductance of the valve to control the pressure within the separating means. For example, a controller may be configured to receive a signal indicative of the pressure within the separating means, and to control the conductance of the valve in dependence on the received signal. This signal may be received from a pressure sensor, capacitance manometer or other form of sensor of sufficient sensitivity to achieve the required level of pressure control.
As well as, or as an alternative to, controlling the supply of gas to the separating means, the controller is preferably configured to control the flow of gas from the separating means in dependence on the received signal. For example, another variable flow control device may be provided, through which gas is extracted from the tank by the first pumping unit, with the controller being configured to control the conductance of this variable flow control device.
In order to control the amount of liquid in the separating means, the pressure control system preferably comprises means for supplying liquid to the separating means from a source thereof, and control means for controlling the flow of liquid to the separating means. For example, in order to minimize pressure variations due to the extraction of liquid from the separating means by the second pumping unit, the control means is preferably configured to maintain a substantially constant level of liquid within the separating means. In another preferred embodiment, the liquid supply means comprises a variable flow control device such as a butterfly or other control valve, through which liquid is supplied to the separating means, with the control means being configured to vary the conductance of the valve to control the level of liquid within the separating means. For example, a controller may be configured to receive a signal indicative of the level of liquid within the separating means, and to control the conductance of the valve in dependence on the received signal. This signal may be received from a level meter, float detector, or other form of sensor of sufficient sensitivity to allow a substantially constant level of liquid to be maintained within the separating means.
One or more flexible tubes are preferably used to convey fluid (single and/or multi-phase) between the components of the system. For example, a flexible tube may be used to convey the multi-phase fluid to the separating means. Further flexible tubes may also be used to convey the single phase streams from the separating means to respective pumping units. This can minimize the transmission of vibrations generated during use of the system back to the fluid within the tool.
In another aspect of the present invention, a method is provided for extracting a stream of multi-phase fluid from a photo-lithography tool, the method comprising the steps of: connecting a pumping arrangement to the tool via an extraction tank; operating the pumping arrangement to draw the fluid from the tool; separating the fluid drawn from the tool into gas and liquid phases within the extraction tank, the pumping arrangement extracting separately gas and liquid from the extraction tank; and controlling the pressure within the extraction tank by regulating the amounts of gas and liquid therewithin.
Features described above in relation to system aspects of the invention are equally applicable to method aspects, and vice versa.
FIG. 1 schematically illustrates a known system for immersion photolithography; and
FIG. 2 schematically illustrates the present invention vacuum system for extracting a multi-phase fluid from an immersion photolithography tool.
With reference to FIG. 2, a system 30 for extracting a multi-phase fluid from an immersion photolithography tool comprises a separating means depicted for purposes of illustration as an extraction tank 32 for receiving the multi-stream fluid drawn from the tool by a pumping arrangement located downstream from the tank 32. The tank 32 is connected to the tool by flexible tubing 34 so as to minimize the amount of mechanical coupling between the system 30 and the tool, and thereby minimize the transmission of vibrations generated during use of the system 30 back to the tool.
The tank 32 is configured to separate the liquid and gas phases within the fluid received from the tool. In this example, the fluid received from the tool comprises a mixture of clean dry air (CDA) and ultra-pure water, and so the tank 32 contains any suitable material and/or structure for affecting the separation of the CDA from the water. However, the tank 32 may be configured to separate a different liquid-gas mixture received from the tool. For example, the liquid may comprise an aqueous or non-aqueous solution, and the gas may be other than CDA.
The pumping arrangement comprises a first pumping unit 36 for extracting gas from the tank 32, and a second pumping unit 38 for extracting liquid from the tank 32.
The first pumping unit 36 may comprise any suitable pump for extracting the gas from the tank 32, and is preferably chosen for compatibility with the gas extracted from the tank 32, which is likely to be saturated with liquid vapour, for minimum transmission of pressure fluctuations back to the gas contained in the tank 32, and for relatively long maintenance periods. In this embodiment, the first pumping unit 36 may conveniently comprise an air-powered ejector pump or a water-based liquid ring pump for extracting CDA from the tank 32. In order to inhibit the transfer of vibrations to the tank 32 during use, the first pumping unit 36 is connected to the tank using flexible tubing 40. As the gas exhaust from the first pumping unit 36 may be saturated or supersaturated with liquid vapour, in this embodiment water vapour, a separator vessel 42 may be connected to the exhaust of the first pumping unit 36, the vessel 42 containing any suitable material and/or structure for affecting the separation of water vapour from the CDA. The water extracted from the CDA is exhaust to a drain, and the CDA is vented to the atmosphere.
The second pumping unit 38 may comprise any suitable pump for extracting the liquid from the tank 32, and is preferably chosen for compatibility with the liquid extracted from the tank 32 and for relatively long maintenance periods. In this embodiment where the liquid is water, the second pumping unit 38 may conveniently comprise a water-powered ejector pump or a diaphragm pump for extracting water from the tank 32. In order to inhibit the transfer of vibrations to the tank 32 during use, the second pumping unit 38 is connected to the tank using flexible tubing 44. The internal diameter of the flexible tubing 44 may be chosen to restrict the flow rate of liquid from the tank 32 to the second pumping unit 38. Alternatively, or in addition, a fixed or variable flow restrictor may be located between the tank 32 and the second pumping unit 38.
In order to minimize any pressure fluctuations transmitted from the system 30 back to the fluid within the tool, the system 30 includes a pressure control system for maintain a substantially constant pressure in the tank 32. In this embodiment, this is achieved by regulating the amounts of liquid and gas within the tank 32.
The amount of liquid contained in the tank 32 is maintained at a substantially constant level by a controller 46, thereby maintaining a substantially constant volume of gas in the tank 32. The controller 46 is connected to a sensor 48 for detecting the amount of liquid with the tank 32. The sensor 48 may comprise, for example, a level meter, float meter or other form of suitable sensor. The sensor 48 outputs a signal to the controller 46 indicative of the level of the liquid within the tank 32. In response to this signal, the controller 46 outputs to a variable flow control device 50 located between the tank 32 and a pressurised external liquid source 52 connected to the tank 32 a signal which causes the device 50 to vary the flow of liquid, in this embodiment water, to the tank 32. For example, the device 50 may be a butterfly or other control valve having a conductance that can be varied in dependence on, preferably in proportion to, the signal received from the controller 46. By varying the flow rate of the water to the tank from the external source 52, the controller 46 can compensate for any variation in the flow rate of fluid to the tank 32 from the tool and/or any variation in the rate of extraction of liquid from the tank 32 by the second pumping unit 38, and thus maintain the liquid in the tank 32 at a substantially constant level. The controller 46 may be arranged to process the signal received from the sensor 48 to compensate for any ripples generated in the surface of the liquid during use.
With the gas occupying a substantially constant volume within the tank 32, any variations in the amount of gas contained in the multi-phase fluid received from the tank, and/or any in the rate of extraction of gas from the tank 32 by the first pumping unit 36, and any temperature fluctuations within the tank 32, could vary the pressure of the gas within the tank 32, and impart pressure and flow fluctuations to the fluid in the tool. The pressure control system is therefore configured to maintain a substantially constant pressure within the tank 32 by also regulating the amount of gas within the tank 32.
To achieve this, the pressure control system comprises a controller 54 connected to a sensor 56 for detecting the gas pressure with the tank 32. The sensor 56 may comprise, for example, a pressure sensor, a capacitance manometer or other form of sensor of sufficient sensitivity to achieve the required level of pressure control. The sensor 56 outputs a signal to the controller 54 indicative of the gas pressure within the tank 32. In response to this signal, the controller 54 outputs to a variable flow control device 58 located between the tank 32 and a pressurised external gas source 60 connected to the tank 32 a signal which causes the device 58 to vary the flow of gas, in this embodiment CDA, to the tank 32. A further variable flow control device 62 may be located between the tank 32 and the first pumping unit 36 and configured to receive a signal from the controller 54 to vary the flow of gas from the tank 32. For example, the devices 58, 62 may also be butterfly or other control valves having a conductance that can be varied in dependence on, preferably in proportion to, the signal received from the controller 54. By controlling the flow of gas into and out from the tank 32, the controller 54 can maintain a substantially constant gas pressure within the tank 32.
System 30 provides the capability of extracting a multi-phase fluid from the immersion lithography tool while minimizing any pressure fluctuations imparted thereby to the fluid within the tool.
a projection device configured to project a radiation beam onto a substrate; and
a system to extract multi-phase fluid from a part of the lithographic apparatus, the system comprising:
a separator configured to separate the multi-phase fluid drawn from the part into gas and liquid phases, and
a pump arrangement comprising a first pump system configured to extract gas from the separator and a second pump system configured to extract liquid from the separator, wherein the pump arrangement is configured to draw multi-phase fluid from the part into the separator.
2. The apparatus of claim 1, further comprising a control system configured to control a pressure within the separator by regulating the gas and/or liquid therein.
3. The apparatus of claim 1, further comprising a control system configured to control flow of gas from the separator.
4. The apparatus of claim 1, further comprising a control system configured to control an amount of liquid within the separator.
5. The apparatus of claim 1, further comprising an outlet configured to remove the multi-phase fluid from a space between the projection device and the substrate.
6. The apparatus of claim 1, further comprising an inlet configured to supply liquid to a space between the projection device and a surface facing the projection device, wherein the pump arrangement is configured to remove the multi-phase fluid from the space between the projection device and the surface facing the projection device.
7. The apparatus of claim 1, wherein the separator comprises an extraction tank.
8. The apparatus of claim 1, wherein an outlet from the separator for separated gas is higher than an outlet from the separator for separated liquid.
9. The apparatus of claim 1, further comprising a flow restriction in a fluid path from the separator to a pump fluidly connected to the separator.
10. A method of extracting a stream of multi-phase fluid from a part of a photolithography tool, the method comprising:
operating a pump arrangement to draw the multi-phase fluid from the part of the tool into a separator;
separating the multi-phase fluid drawn from the part of the tool into gas and liquid phases within the separator;
extracting gas from the separator using a first pump system of the pump arrangement; and
extracting liquid from the separator using a second pump system of the pump arrangement,
wherein the pump arrangement is configured to draw multi-phase fluid from the part into the separator.
11. The method of claim 10, further comprising controlling a pressure within the separator by regulating the gas and/or liquid therein.
12. The method of claim 10, further comprising controlling flow of gas from the separator.
13. The method of claim 10, further comprising controlling an amount of liquid within the separator.
14. The method of claim 10, comprising removing the multi-phase fluid from a space between a projection device of the tool and a substrate via an outlet.
15. The method of claim 10, further comprising supplying liquid to a space between a projection device of the tool and a surface facing the projection device via an inlet, wherein the pump arrangement is configured to remove the multi-phase fluid from the space between the projection device and the surface facing the projection device.
16. The method of claim 10, wherein an outlet from the separator for separated gas is higher than an outlet from the separator for separated liquid.
17. The method of claim 10, further comprising a flow restriction in a fluid path from the separator to a pump fluidly connected to the separator.
a separator configured to separate the fluid drawn from the part into gas and liquid phases,
a first outlet configured to exhaust separated gas from the separator,
a second outlet configured to exhaust separated liquid from the separator, the first outlet being located higher than the second outlet, and
a pump arrangement configured to draw multi-phase fluid from the part into the separator and configured to extract separated gas via the first outlet and/or extract separated liquid via the second outlet, from the separator.
19. The apparatus of claim 18, wherein the pump arrangement comprises a pump system configured to extract separated liquid, via the second outlet, from the separator.
20. The apparatus of claim 18, further comprising a control system configured to control a pressure within the separator by regulating the gas and/or liquid therein.
US15/362,530 2004-06-16 2016-11-28 Vacuum system for immersion photolithography Active US9857699B2 (en)
US10/869,191 US7481867B2 (en) 2004-06-16 2004-06-16 Vacuum system for immersion photolithography
US12/340,326 US8164734B2 (en) 2004-06-16 2008-12-19 Vacuum system for immersion photolithography
US13/187,166 US8830440B2 (en) 2004-06-16 2011-07-20 Vacuum system for immersion photolithography
US14/469,389 US9507270B2 (en) 2004-06-16 2014-08-26 Vacuum system for immersion photolithography
US15/362,530 US9857699B2 (en) 2004-06-16 2016-11-28 Vacuum system for immersion photolithography
US15/857,368 US10168624B2 (en) 2004-06-16 2017-12-28 Vacuum system for immersion photolithography
US16/202,170 US20190094715A1 (en) 2004-06-16 2018-11-28 Vacuum system for immersion photolithography
US14/469,389 Continuation US9507270B2 (en) 2004-06-16 2014-08-26 Vacuum system for immersion photolithography
US15/857,368 Continuation US10168624B2 (en) 2004-06-16 2017-12-28 Vacuum system for immersion photolithography
US20170075233A1 US20170075233A1 (en) 2017-03-16
US9857699B2 true US9857699B2 (en) 2018-01-02
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US10/869,191 Active 2026-08-29 US7481867B2 (en) 2004-06-16 2004-06-16 Vacuum system for immersion photolithography
US12/340,326 Active 2025-12-19 US8164734B2 (en) 2004-06-16 2008-12-19 Vacuum system for immersion photolithography
US13/187,166 Active 2025-05-06 US8830440B2 (en) 2004-06-16 2011-07-20 Vacuum system for immersion photolithography
US14/469,389 Active 2024-11-26 US9507270B2 (en) 2004-06-16 2014-08-26 Vacuum system for immersion photolithography
US15/362,530 Active US9857699B2 (en) 2004-06-16 2016-11-28 Vacuum system for immersion photolithography
US15/857,368 Active US10168624B2 (en) 2004-06-16 2017-12-28 Vacuum system for immersion photolithography
US16/202,170 Pending US20190094715A1 (en) 2004-06-16 2018-11-28 Vacuum system for immersion photolithography
US (7) US7481867B2 (en)
EP (1) EP1756672B1 (en)
JP (3) JP4772787B2 (en)
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CN (2) CN101794081B (en)
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DE (1) DE602005020619D1 (en)
GB (1) GB0414967D0 (en)
TW (1) TWI339131B (en)
WO (1) WO2005124464A2 (en)
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