METHOD FOR PROCESSING SUBSTRATE
20260091417 ยท 2026-04-02
Inventors
Cpc classification
B08B3/14
PERFORMING OPERATIONS; TRANSPORTING
B08B7/0021
PERFORMING OPERATIONS; TRANSPORTING
B08B3/08
PERFORMING OPERATIONS; TRANSPORTING
International classification
B08B3/08
PERFORMING OPERATIONS; TRANSPORTING
B08B3/14
PERFORMING OPERATIONS; TRANSPORTING
B08B7/00
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A method for processing a substrate includes providing the substrate into a processing chamber, adding a processing fluid into the processing chamber, adding a dry fluid to the processing chamber while draining the processing fluid from the processing chamber, and releasing the dry fluid from the processing chamber in a gaseous phase.
Claims
1. A method for processing a substrate, the method comprising: providing the substrate into a processing chamber; adding isopropyl alcohol into the processing chamber; adding carbon dioxide to the processing chamber in a liquid phase while draining the isopropyl alcohol from the processing chamber; and releasing the carbon dioxide from the processing chamber in a gaseous phase.
2. The method of claim 1, wherein draining the isopropyl alcohol from the processing chamber comprises recovering the isopropyl alcohol for recycling.
3. The method of claim 1, wherein releasing the carbon dioxide from the processing chamber comprises depressurizing the processing chamber.
4. The method of claim 1, wherein releasing the carbon dioxide from the processing chamber further comprises venting the carbon dioxide in the gaseous phase.
5. The method of claim 1, wherein the carbon dioxide is added to the processing chamber in the liquid phase under a pressure in a range of 4.5 MPa to 5 MPa.
6. The method of claim 1, further comprising bringing the carbon dioxide to a supercritical condition in the processing chamber.
7. The method of claim 6, wherein bringing the carbon dioxide to a supercritical condition in the processing chamber comprises increasing the pressure in the processing chamber to 7.38 MPa or above.
8. The method of claim 6, wherein bringing the carbon dioxide to a supercritical condition in the processing chamber comprises increasing the temperature in the processing chamber to 30.98 C. or above.
9. A method for processing a substrate, the method comprising: providing the substrate into a processing space of a processing chamber; injecting isopropyl alcohol into the processing space; dispensing liquid carbon dioxide into the processing space while removing the isopropyl alcohol from the processing space; maintaining the processing space at a pressure of 5 MPa or less while filling the processing space with the liquid carbon dioxide; and releasing the liquid carbon dioxide from the processing space with a transition of the liquid carbon dioxide to a gaseous phase.
10. The method of claim 9, wherein the processing space is maintained at a pressure in a range of 4.5 MPa to 5 MPa while filling the processing space with the liquid carbon dioxide.
11. The method of claim 9, further comprising recovering the isopropyl alcohol for recycling after removing the isopropyl alcohol from the processing space.
12. The method of claim 9, wherein releasing the liquid carbon dioxide from the processing chamber further comprises depressurizing the processing chamber.
13. The method of claim 9, wherein releasing the liquid carbon dioxide from the processing chamber further comprises venting gaseous carbon dioxide.
14. A method for processing a substrate, the method comprising: providing the substrate into a processing chamber; injecting isopropyl alcohol into the processing chamber; draining the isopropyl alcohol from the processing chamber while adding liquid carbon dioxide to the processing chamber; after draining the isopropyl alcohol, bringing the liquid carbon dioxide to a supercritical condition; and after performing a supercritical dry process on the substrate, removing the carbon dioxide from the processing chamber.
15. The method of claim 14, wherein bringing the carbon dioxide to a supercritical condition in the processing chamber comprises increasing the pressure in the processing chamber to 7.38 MPa or above.
16. The method of claim 14, wherein bringing the carbon dioxide to a supercritical condition in the processing chamber comprises increasing the temperature in the processing chamber to 30.98 C. or above.
17. The method of claim 14, wherein draining the isopropyl alcohol further comprises recovering the isopropyl alcohol for recycling.
18. The method of claim further comprising maintaining the processing chamber at a pressure of 5 MPa or less while adding the liquid carbon dioxide into the processing chamber.
19. The method of claim 14, wherein removing the carbon dioxide from the processing chamber comprises depressurizing the processing chamber.
20. The method of claim 14, wherein removing the carbon dioxide from the processing chamber comprises venting gaseous carbon dioxide.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0012] For a more complete understanding of the present invention, and the advantages thereof, reference is now made to the following descriptions taken in conjunction with the accompanying drawings, in which:
[0013]
[0014]
[0015]
[0016]
[0017]
[0018]
[0019]
[0020] Corresponding numerals and symbols in the different figures generally refer to corresponding parts unless otherwise indicated. The figures are drawn to clearly illustrate the relevant aspects of the embodiments and are not necessarily drawn to scale. The edges of features drawn in the figures do not necessarily indicate the termination of the extent of the feature.
DETAILED DESCRIPTION OF ILLUSTRATIVE EMBODIMENTS
[0021] The making and using of various embodiments are discussed in detail below. It should be appreciated, however, that the various embodiments described herein are applicable in a wide variety of specific contexts. The specific embodiments discussed are merely illustrative of specific ways to make and use various embodiments, and should not be construed in a limited scope.
[0022] According to one or more embodiments of the present disclosure, this application relates to methods of wet and dry processing of a substrate, such as a semiconductor wafer. Current processing of substrates with supercritical fluid after a cleaning and rinse process (e.g., with a rinsing fluid such as isopropyl alcohol (IPA)) may use carbon dioxide (CO.sub.2) for pressurizing the chamber above 7 MPa in order to allow supercritical CO.sub.2 to be deposited onto the substrate. However, this may use a large amount of CO.sub.2 and lead to waste of the rinsing fluid, which is not recovered. In embodiments of the current disclosure, a processing chamber is filled with a rinsing fluid and then a liquid (e.g., liquid CO.sub.2) is dispensed into the processing chamber. While the liquid is being dispensed, the rinsing fluid may be recovered by being drained from the processing chamber. This is advantageous by allowing the rinsing fluid to be reused or recycled. The liquid (e.g., liquid CO.sub.2) may have a lower surface tension than the rinsing fluid (e.g., IPA), which may reduce the risk of pattern collapse on the substrate.
[0023] Performing the process at a lower pressure (e.g., less than a pressure needed for IPA to be supercritical) and at a lower temperature (e.g., room temperature) may increase throughput. Removing the rinsing fluid (e.g., IPA) without bringing it to a supercritical state may allow the processing chamber to operate at lower pressures, thereby reducing cost.
[0024] Embodiments of the disclosure are described in the context of the accompanying drawings. An example of a processing chamber for wet and dry processing of a substrate will be described using
[0025]
[0026] The upper working surface 125 inside the processing chamber 105 is spaced above the lower working surface 120 and separated by a gap (g).
[0027] The processing chamber 105 further includes one or more structure(s) for supporting the substrate 50 in the processing space 106. In various examples, the one or more structure(s) for supporting the wafer includes a plurality of pins 123 that extend through the bottom plate 110 into the processing space 106 and supports the substrate 50 from the bottom, as shown in
[0028] When a substrate 50 to be processed is inserted and mounted within the processing space 106, an upper gap (g.sub.U) is present between the upper working surface 125 of the processing chamber 105 and the top surface of the wafer, and a lower gap (g.sub.L) is present between the lower working surface 120 of the processing chamber 105 and the bottom surface of the wafer. It may be desirable that the upper gap (g.sub.U) and the lower gap (g.sub.L) be substantially equal to maintain a similar distance (or uniform gap) between the upper working surface 125 and the top surface of the substrate 50 and the lower working surface 120 and the bottom surface of the substrate 50. In some examples, the upper gap (g.sub.U) and the lower gap (g.sub.L) may be in a range between 0.01 mm and 10.0 mm.
[0029] In some examples, the upper gap (g.sub.U) and the lower gap (g.sub.L) can be adjusted before or during a process to increase the gap (g) between the upper working surface 125 and the lower working surface 120, and thus, increase the interior volume of the processing space 106, as shown in
[0030] As shown in
[0031] In some examples, the at least one opening 130 passing through the lower working surface 120 includes one or more backside nozzles for dispensing a processing fluid into the processing space 106 above the lower working surface 120. In one example, the at least one opening 130 includes a backside nozzle, which is centered in the bottom plate 110 for dispensing the processing fluid into the processing space 106 near a center of the substrate 50, as shown in
[0032] The top plate 115 also includes at least one opening 135 that passes through the upper working surface 125 of the processing chamber 105. When processing a substrate 50 mounted within the processing space 106, the at least one opening 135 passing through the upper working surface 125 may be in fluid flow communication with at least one processing fluid (e.g., a liquid and/or a gas), and may be configured to direct the at least one processing fluid into the processing space 106 below the upper working surface 125 for processing a top surface of the substrate 50.
[0033] In some examples, the at least one opening 135 passing through the upper working surface 125 includes one or more frontside nozzles for dispensing the processing fluid into the processing space 106 below the upper working surface 125. In one example, the at least one opening 135 includes a frontside nozzle, which is centered in the top plate 115 for dispensing the processing fluid into the processing space 106 near a center of the substrate 50, as shown in
[0034] Regardless of the number of frontside nozzles utilized, the processing fluid(s) dispensed from the frontside nozzle(s) is/are directed onto the top surface of the substrate 50 and thereafter flow radially towards the edge of the substrate 50. Similar to the backside nozzle(s), the frontside nozzle(s) may be coupled to a controller (such as controller 160) that is configured for selecting a second processing fluid (e.g., a liquid or a gas) that is introduced into the processing space.
[0035] Although
[0036] In some examples, the processing system 100 shown in
[0037] According to one example, the processing system 100 shown in
[0038] According to one example, the processing system 100 shown in
[0039] According to one example, the processing system 100 shown in
[0040] According to one example, the substrate 50 is not rotated during wet or dry processing. According to another example, the processing system 100 comprises means for rotating the wafer (not shown) and the wafer is rotated during wet processing, dry processing or both wet and dry processing.
[0041] In some examples, the at least one opening 130 passing through the upper working surface 125 of the processing chamber 105 and the at least one opening 135 passing through the lower working surface 120 of the processing chamber 105 are in fluid flow communication with supply lines for one or more liquids 140 and liquid supply valves 145, as shown further in
[0042] In some examples, the processing system 100 includes a controller 160 that is coupled to the liquid supply valves 145 and gas supply valves 155 for selectively providing the one or more liquids 140 and/or the one or more gases 150 to the processing space 106 defined within the processing chamber 105. A wide variety of liquids and gases may be selectively provided to the processing space 106 depending on the process, or process step, being performed within the processing chamber 105.
[0043] During a cleaning process, for example, the controller 160 may supply control signals to the liquid and gas supply valves 145/155 to selectively provide a cleaning solution and/or a rinse solution to the processing space 106 for cleaning and/or rinsing at least one surface of the substrate 50. Examples of cleaning solutions include, but are not limited to, an ammonia/peroxide mixture (APM), a hydrochloric/peroxide mixture (HPM) and a sulfuric peroxide mixture (SPM). Examples of rinse solutions include, but are not limited to, deionized (DI) water and isopropyl alcohol (IPA). Other cleaning solutions and rinse solutions may also be utilized. After cleaning and/or rinsing the surface(s) of the substrate 50, the controller 160 may supply control signals to the liquid and gas supply valves 145/155 to selectively provide a gas (such as, but not limited to, air, nitrogen, carbon dioxide, or the like) to the processing space 106 to remove any remaining liquid the wafer surface(s), thereby drying the wafer surface(s). The gas may be vented to outside the processing chamber through the openings 130, 135, or any other suitable opening or vent that couples the processing space 106 to the outside of the processing chamber 105.
[0044] In some examples, the controller 160 supplies control signals to the liquid and gas supply valves 145/155 to selectively provide a low surface tension liquid (such as IPA) to the processing space 106, before the cleaning step is performed, to pre-wet the wafer surface, as well as the upper working surface 125 and the lower working surface 120 of the processing chamber 105.
[0045] In some optional examples, the controller 160 (or another controller included within the processing system 100) may be configured to adjust a vertical position of the top plate 115, a vertical position of the bottom plate 110 and/or the gap (g) between the top and bottom plates. In the example shown in
[0046] The control signals supplied from the controller 160 to the lifting mechanisms 170/175 can be used to adjust a vertical position of the top plate 115 and/or a vertical position of the bottom plate 110. In some examples, for example, the controller 160 may supply a control signal to the lifting mechanism 175 to raise the top plate 115, so that a substrate 50 may be inserted with the processing space 106, as illustrated for example in
[0047] The upper gap (g.sub.U) and the lower gap (g.sub.L) can be adjusted for a wide variety of purposes. In some examples, the upper gap (g.sub.U) and the lower gap (g.sub.L) can be decreased, as shown in
[0048] In some examples, additional feature(s) may be added to the top plate 115 and/or the bottom plate 110 of the processing chamber 105. For example, a sonic transducer may be added to the top plate 115 and/or the bottom plate 110 to enhance the wet (e.g., cleaning) process. The sonic transducer can be embedded within the entire top/bottom plate, or within only a portion of the top/bottom plate. In another example, the top plate 115 and/or the bottom plate 110 include one or more heating element(s) to control the temperature of the substrate 50 and heat the liquid/gas dispensed onto the surface of the substrate 50. The one or more heating element(s) may be used, such as in conjunction with pressurized gas through the gas inlets 204 and valves 202 or other suitable valves and inlets, to bring a fluid (e.g., liquid carbon dioxide) within the processing space 106 to a supercritical state. Alternatively, an additional nozzle may be embedded within the top plate 115 and/or the bottom plate 110 to inject steam into the processing space to heat the liquid/gas dispensed onto the wafer surface. In yet another example, the top plate 115 and/or the bottom plate 110 may include one or more sensors used to inspect the wafer and/or the liquids dispensed onto the wafer surface(s). For example, a conductive meter may be added to the top/bottom plate to monitor the liquids dispensed onto the wafer surface.
[0049] The processing system 100 illustrated by
[0050] The processing system 100 and processing chamber 105 illustrated by
[0051]
[0052] As illustrated in
[0053] Next, in
[0054] After the substrate 50 is inserted within the processing space 106 and mounted on the plurality of pins 123, a control signal may be supplied to the lifting mechanism 175 to lower the top plate 115 and enclose the processing chamber 105. In some embodiments, additional control signals may be supplied to the lifting mechanisms 170/175 to adjust the upper gap (g.sub.U) between the upper working surface 125 of the processing chamber 105 and the top surface of the wafer and the lower gap (g.sub.L) between the lower working surface 120 of the processing chamber 105 and the bottom surface of the wafer.
[0055] In
[0056] Next, in
[0057] Injecting the fluid 260 at a lower pressure (e.g., less than a pressure needed for the processing fluid 250, such as IPA, to be supercritical) and at a lower temperature (e.g., room temperature) may be advantageous by increasing throughput. Removing the processing fluid 250 (e.g., IPA) without bringing it to a supercritical state may allow the processing chamber 105 to operate at lower pressures, thereby reducing cost. For example, liquid CO.sub.2 at room temperature (e.g., around 25 C.) needs to be at a pressure above 4.5 MPa, while IPA does not reach a supercritical state until 235.6 C. at 5.37 MPa. By inserting the fluid 260 without bringing it to a supercritical state, the pressure in the processing chamber 105 may be kept at 5 MPa or less, such as in a range of 4.5 MPa to 5 MPa, while adding the fluid 260 and recovering the processing fluid 250, thereby allowing the processing chamber 105 to have a lower tolerance for high pressures. As tolerances may be, for example, three times the desired pressure, the processing chamber 105 could have a tolerance of 15 MPa, which could reduce costs.
[0058] While the fluid 260 is injected into the processing chamber 105, the processing fluid 250 may be drained from the processing chamber 105, such as through the conduits 195 of the drainage system 190. The processing fluid 250 may be recovered and reused. This is advantageous for recycling the processing fluid 250 and thereby saving costs. Removing the rinsing fluid (e.g., IPA) without bringing it to a supercritical state (also referred to as a supercritical condition) may allow the processing chamber to operate at lower pressures, thereby reducing cost.
[0059] In
[0060] In some embodiments, the fluid 260 is brought to a supercritical condition, such as by increasing the temperature and pressure in the processing space 106. For example, liquid CO.sub.2 may be brought to supercriticality by increasing the temperature to 30.98 C. or above and increasing the pressure to 7.38 MPa or above. Using a supercritical fluid to treat the substrate 50 may be advantageous to improve substrate drying and avoiding pattern collapse that sometimes occurs when using a processing fluid (e.g., IPA) to dry substrate surfaces. Since supercritical fluids have zero surface tension, pattern collapse may not occur when the wafer is dried in a supercritical fluid environment. Bringing the fluid 260 to supercriticality in the processing chamber 105 allows for a full processing of the substrate 50 (e.g., a treatment such as a rinse with the processing fluid 250) and a subsequent supercritical fluid dry treatment in the same processing chamber. The supercritical dry process may allow for uniform clearing of the processing chamber 105 after processing.
[0061] The processing chamber 105 may be pressurized with gas through the gas inlets 204 and valves 202 and have temperature increased by one or more heating element(s) of the top plate 115 and/or the bottom plate 110, as described above with respect to
[0062] Next, in
[0063] In
[0064]
[0065]
[0066]
[0067] Example embodiments of the disclosure are summarized here. Other embodiments can also be understood from the entirety of the specification as well as the claims filed herein.
[0068] Example 1. A method for processing a substrate, the method including: providing the substrate into a processing chamber; adding isopropyl alcohol into the processing chamber; adding carbon dioxide to the processing chamber in a liquid phase while draining the isopropyl alcohol from the processing chamber; and releasing the carbon dioxide from the processing chamber in a gaseous phase.
[0069] Example 2. The method of example 1, where draining the isopropyl alcohol from the processing chamber includes recovering the isopropyl alcohol for recycling.
[0070] Example 3. The method of one of examples 1 or 2, where releasing the carbon dioxide from the processing chamber includes depressurizing the processing chamber.
[0071] Example 4. The method of one of examples 1 to 3, where releasing the carbon dioxide from the processing chamber further includes venting the carbon dioxide in the gaseous phase.
[0072] Example 5. The method of one of examples 1 to 4, where the carbon dioxide is added to the processing chamber in the liquid phase under a pressure in a range of 4.5 MPa to 5 MPa.
[0073] Example 6. The method of one of examples 1 to 5, further including bringing the carbon dioxide to a supercritical condition in the processing chamber.
[0074] Example 7. The method of example 6, where bringing the carbon dioxide to a supercritical condition in the processing chamber includes increasing the pressure in the processing chamber to 7.38 MPa or above.
[0075] Example 8. The method of one of examples 6 or 7, where bringing the carbon dioxide to a supercritical condition in the processing chamber includes increasing the temperature in the processing chamber to 30.98 C. or above.
[0076] Example 9. A method for processing a substrate, the method including: providing the substrate into a processing space of a processing chamber; injecting isopropyl alcohol into the processing space; dispensing liquid carbon dioxide into the processing space while removing the isopropyl alcohol from the processing space; maintaining the processing space at a pressure of 5 MPa or less while filling the processing space with the liquid carbon dioxide; and releasing the liquid carbon dioxide from the processing space with a transition of the liquid carbon dioxide to a gaseous phase.
[0077] Example 10. The method of example 9, where the processing space is maintained at a pressure in a range of 4.5 MPa to 5 MPa while filling the processing space with the liquid carbon dioxide.
[0078] Example 11. The method of one of examples 9 or 10, further including recovering the isopropyl alcohol for recycling after removing the isopropyl alcohol from the processing space.
[0079] Example 12. The method of one of examples 9 to 11, where releasing the liquid carbon dioxide from the processing chamber further includes depressurizing the processing chamber.
[0080] Example 13. The method of one of examples 9 to 12, where releasing the liquid carbon dioxide from the processing chamber further includes venting gaseous carbon dioxide.
[0081] Example 14. A method for processing a substrate, the method including: providing the substrate into a processing chamber; injecting isopropyl alcohol into the processing chamber; draining the isopropyl alcohol from the processing chamber while adding liquid carbon dioxide to the processing chamber; after draining the isopropyl alcohol, bringing the liquid carbon dioxide to a supercritical condition; and after performing a supercritical dry process on the substrate, removing the carbon dioxide from the processing chamber.
[0082] Example 15. The method of example 14, where bringing the carbon dioxide to a supercritical condition in the processing chamber includes increasing the pressure in the processing chamber to 7.38 MPa or above.
[0083] Example 16. The method of one of examples 14 or 15, where bringing the carbon dioxide to a supercritical condition in the processing chamber includes increasing the temperature in the processing chamber to 30.98 C. or above.
[0084] Example 17. The method of one of examples 14 to 16, where draining the isopropyl alcohol further includes recovering the isopropyl alcohol for recycling.
[0085] Example 18. The method of one of examples 14 to 17, further including maintaining the processing chamber at a pressure of 5 MPa or less while adding the liquid carbon dioxide into the processing chamber.
[0086] Example 19. The method of one of examples 14 to 18, where removing the carbon dioxide from the processing chamber includes depressurizing the processing chamber.
[0087] Example 20. The method of one of examples 14 to 19, where removing the carbon dioxide from the processing chamber includes venting gaseous carbon dioxide.
[0088] While this invention has been described with reference to illustrative embodiments, this description is not intended to be construed in a limiting sense. Various modifications and combinations of the illustrative embodiments, as well as other embodiments of the invention, will be apparent to persons skilled in the art upon reference to the description. It is therefore intended that the appended claims encompass any such modifications or embodiments.