US 7,993,954 B2Grant
Thermal management and method for large scale processing of CIS and/or CIGS based thin films overlying glass substrates
Issue Date:2011-08-09
•20 Claims
•12 Drawing Sheets
Abstract
The thermal management and method for large scale processing of CIS and/or CIGS based thin film overlaying glass substrates. According to an embodiment, the present invention provides a method for fabricating a copper indium diselenide semiconductor film. The method includes providing a plurality of substrates, each of the substrates having a copper and indium composite structure. The method also includes transferring the plurality of substrates into a furnace, each of the plurality of substrates provided in a vertical orientation with respect to a direction of gravity, the plurality of substrates being defined by a number N, where N is greater than 5. The method further includes introducing a gaseous species including a selenide species and a carrier gas into the furnace and transferring thermal energy into the furnace to increase a temperature from a first temperature to a second temperature, the second temperature ranging from about 350° C. to about 450° C. to at least initiate formation of a copper indium diselenide film from the copper and indium composite structure on each of the substrates.
Metadata
Assignee
- Stion Corporation
Inventor
- Robert D. Wieting
Application Information
Application Number:US 12/953,674
Filing Date:2010-11-24
Priority Date:2008-09-30
Art Unit:2812
Classifications
IPC:
H01L21/00
Patent Drawings (12 sheets)
Description
Cross-References to Related Applications
[0001] This application is a division of U.S. patent application Ser. No. 12/568,641 filed on Sep. 28, 2009, which claims priority to U.S. Provisional Patent Application No. 61/101,567, filed Sep. 30, 2008, entitled “THERMAL MANAGEMENT AND METHOD FOR LARGE SCALE PROCESSING OF CIS AND/OR CIGS BASED THIN FILMS OVERLYING GLASS SUBSTRATES”, the disclosures of which are incorporated by reference herein in their entirety for all purposes.
Background of the Invention
[0002] The present invention relates generally to photovoltaic techniques. More particularly, the present invention provides a method and structure for a thin film photovoltaic device using a copper indium diselenide species (CIS), copper indium gallium diselenide species (CIGS), and/or others. The invention can be applied to photovoltaic modules, flexible sheets, building or window glass, automotive, and others.
[0003] In the process of manufacturing CIS and/or CIGS types of thin films, there are various manufacturing challenges, such as maintaining structure integrity of substrate materials, ensuring uniformity and granularity of the thin film material, etc. While conventional techniques in the past have addressed some of these issues, they are often inadequate in various situations. Therefore, it is desirable to have improved systems and method for manufacturing thin film photovoltaic devices.
Brief Summary of the Invention
[0004] The present invention relates generally to photovoltaic techniques. More particularly, the present invention provides a method and structure for a thin film photovoltaic device using a copper indium diselenide species (CIS), copper indium gallium diselenide species (CIGS), and/or others. The invention can be applied to photovoltaic modules, flexible sheets, building or window glass, automotive, and others.
[0005] According to an embodiment, the present invention provides a method for fabricating a copper indium diselenide semiconductor film. The method includes providing a plurality of substrates, each of the substrates having a copper and indium composite structure. The method also includes transferring the plurality of substrates into a furnace, each of the plurality of substrates provided in a vertical orientation with respect to a direction of gravity, the plurality of substrates being defined by a number N, where N is greater than 5. The method further includes introducing a gaseous species including a selenide species and a carrier gas into the furnace and transferring thermal energy into the furnace to increase a temperature from a first temperature to a second temperature, the second temperature ranging from about 350° C. to about 450° C. to at least initiate formation of a copper indium diselenide film from the copper and indium composite structure on each of the substrates. The method additionally includes maintaining the temperature at about the second temperature for a period of time. The method also includes removing at least the residual selenide species from the furnace. The method further includes introducing a sulfide species into the furnace. The method also includes increasing a temperature to a third temperature, the third temperature ranging from about 500 to 525° C. while the plurality of substrates are maintained in an environment including a sulfur species to extract out one or more selenium species from the copper indium diselenide film.
[0006] It is to be appreciated that the present invention provides numerous benefits over conventional techniques. Among other things, the systems and processes of the present invention are compatible with conventional systems, which allow cost effective implementation. In various embodiments, the temperature control method maintains structure integrity of substrates while providing allows various reactions to occur. There are other benefits as well.
Brief Description of the Drawings
[0007] FIG. 1 is a simplified diagram of a transparent substrate with an overlying electrode layer according to an embodiment of the present invention;
[0008] FIGS. 2 and 2A are simplified diagram of a composite structure including a copper and indium film according to an embodiment of the present invention;
[0009] FIG. 3 is a simplified diagram of a furnace according to an embodiment of the present invention;
[0010] FIG. 4 is a simplified diagram of a process for forming a copper indium diselenide layer according to an embodiment of the present invention;
[0011] FIGS. 5 and 5A are simplified diagrams of a temperature profile of the furnace according to an embodiment of the present invention; and
[0012] FIGS. 6A and 6B are simplified diagrams of a thin film copper indium diselenide device according to an embodiment of the present invention.
[0013] FIG. 7 shows exemplary furnace temperature profiles measured by in-situ thermal couples according to an embodiment of the present invention.
[0014] FIG. 8 shows exemplary temperature profile set points at various zones in a furnace according to an embodiment of the present invention.
[0015] FIG. 9 shows an exemplary furnace temperature profile and substrate temperature uniformity according to an embodiment of the present invention.
[0016] FIG. 10 shows an exemplary cell open-circuit voltage distribution from ten substrates in a furnace according to an embodiment of the present invention.
Detailed Description of the Invention
[0017] The present invention relates generally to photovoltaic techniques. More particularly, the present invention provides a method and structure for a thin film photovoltaic device using a copper indium diselenide species (CIS), copper indium gallium diselenide species (CIGS), and/or others. The invention can be applied to photovoltaic modules, flexible sheets, building or window glass, automotive, and others.
[0018] FIG. 1 is a simplified diagram of a transparent substrate with an overlying electrode layer according to an embodiment of the present invention. This diagram is merely an example, which should not limit the scope of the claims herein. As shown, structure 100 includes a transparent substrate 104. In an embodiment, substrate 104 can be a glass substrate, for example, a soda lime glass. However, other types of substrates can also be used. Examples of substrates include borosilicate glass, acrylic glass, sugar glass, specialty Corning™ glass, and others. As shown, a contact layer comprising a metal electrode layer 102 is deposited upon substrate 104. According to an embodiment, the metal electrode layer 102 comprises metal material that is characterized by a predetermined conductivity that is optimized for thin-film based solar cell applications. Depending on the application, the metal electrode layer 102 may be deposited in various ways. For example, the metal electrode layer 102 comprises primarily a film of molybdenum that is deposited by sputtering. For example, the thickness of the electrode layer 102 may range from 200 to 700 μm. A sputtering apparatus, such as a DC magnetron sputtering apparatus, can be used to deposit a thin film of materials upon a substrate. Such apparatus is well known and commercially available. But it is to be understood that other types of equipments and/or processes, such as evaporation in vacuum based environment may be used as well. As an example, the sputtering deposition process is described below.
[0019] Sputter deposition is a physical vapor deposition (PVD) method of depositing thin films by sputtering, or ejecting, material from a “target”, or source, which then deposits onto a substrate, such as a silicon wafer or glass. Sputtered atoms ejected from the target have a wide energy distribution, typically up to 10's of eV's (100000 K). The entire range from high-energy ballistic impact to low-energy thermalized motion is accessible by changing the background gas pressure. The sputtering gas is often an inert gas such as argon. For efficient momentum transfer, the atomic weight of the sputtering gas should be close to the atomic weight of the target, so for sputtering light elements neon is preferable, while for heavy elements krypton or xenon are used. Reactive gases can also be used to sputter compounds. The compound can be formed on the target surface, in-flight or on the substrate depending on the process parameters. The availability of many parameters that control sputter deposition make it a complex process, but also allow experts a large degree of control over the growth and microstructure of the film.
[0020] FIG. 2 is a simplified diagram of a composite structure including copper and indium material according to an embodiment of the present invention. This diagram is merely an example, which should not limit the scope of the claims herein. In this embodiment, structure 200 is includes a glass substrate 208, preferably soda lime glass, which is about 1 to 3 millimeters thick. For example, the glass substrate 208 serves as a supporting layer. The metal layer 206 is deposited upon substrate 208. For example, the metal layer 206 serves as a metal electrode layer to provide electrical contact. For example, the layer 206 comprises primarily a film of molybdenum which has been deposited by sputtering to a thickness of from 200 to 700 nm. In a specific embodiment, an initial film of chromium is first deposited upon glass 208. For example, the chromium is used to insure good adhesion of the overall structure to the substrate 208. Other types of material may also be used in a barrier layer, such as silicon dioxide, silicon nitride, etc. Layers 204 and 202 include primarily a copper layer and an indium layer deposited upon metal layer 206 by a sputtering process. As shown in FIG. 2 , the indium layer overlays the copper layer. But it is to be understood that other arrangements are possible. In another embodiment, the copper layer overlays the indium layer. As an example, a sputtering apparatus, such as a DC magnetron sputtering apparatus, is used to deposit the thin film (e.g., layer 202, 204, and/or 206) of materials upon a substrate. It is to be appreciated that various types of sputtering apparatus may be used. Such apparatus is well known and commercially available. Other material can also be used. It is to be appreciated that techniques described throughout the present application are flexible and that other types of equipments and/or processes, such as evaporation in vacuum based environment may be used as well for depositing copper and indium material. In certain embodiments, gallium material (not shown in FIG. 2 ) may be formed deposited in addition to the copper and indium material. According to an embodiment, the ratio between the copper and indium+gallium material is less than 1 (e.g., Cu/III<0.92˜0.96, here III means group III); that is, less than one part of copper per one part of indium material.
[0021] As an example, the structure 200 is formed by processing the structure 100. For example, the Cu and In are deposited onto the structure 100 to form the structure 200. As described, sputtering process is used for forming the copper and/or indium layer. In the embodiment illustrated in FIG. 2 , the Cu film and the In film are shown as two separate layers. In another embodiment, a Cu/In composite or Cu/In alloy is formed during the sputtering process, as shown in FIG. 2A . It is to be appreciated that techniques described throughout the present application are flexible and that other types of equipments and/or processes, such as evaporation in vacuum based environment may be used as well for depositing copper and indium material. In certain embodiments, gallium material (not shown in FIG. 2 ) may be formed deposited in addition to the copper and indium material
[0022] FIG. 2A is a simplified diagram of a composite structure 210 including a copper and indium composite film according to another embodiment of the present invention. This diagram is merely an example, which should not limit the scope of the claims herein. As shown, the structure 210 includes a transparent substrate 216. In an embodiment, substrate 216 can be a glass substrate, for example, a soda lime glass. A back contact comprises a metal electrode layer 214 is deposited upon substrate 216. For example, the layer 214 comprises primarily a film of molybdenum material is deposited by sputtering. In a specific embodiment, an initial film of chromium is deposited upon glass 216 before depositing the molybdenum material to provide for good adhesion of the overall structure to the substrate 210. The layer 212 comprises primarily a copper (and gallium) indium alloy or copper (gallium) indium composite material. For example, the mixing or alloying of copper indium results in an improved homogeneity or advantageous morphology of the composite copper and indium film. This improved structure is carried over into the desired CIS film after the selenization step. According to an embodiment, a copper (or CuGa alloy) indium alloy material is formed from separate layers of copper (or CuGa alloy) material and indium material, which diffuse into each layer. For example, the process of forming of copper indium (or CuInGa) alloy material is performed by subjecting the structure to a high temperature annealing in an environment containing gaseous selenium species.
[0023] FIG. 3 is a simplified diagram of a furnace according to an embodiment of the present invention. This diagram is merely an example, which should not limit the scope of the claims herein. As shown, a furnace 300 includes a process chamber 302 and an end cap 304. According to an embodiment, the reaction chamber 302 is characterized by a volume of more than 200 liters. As shown in FIG. 3 , the furnace 300 includes a vacuum-pumping machine that comprises a turbo molecular pump 310 and a rotary pump 312. Depending on the application, the vacuum-pumping machine can be implemented by way of a combination of a mechanical booster pump and a dry pump. For example, the raw material gas and/or a diluting gas such as helium, nitrogen, argon, or hydrogen can be introduced in process chamber 302 via a gas injection pipe 314, if demanded by the specific applications and/or processes. The chamber 302 is evacuated by the turbo molecular pump 310 via the rotary pump 312 that is connected with a manifold 316 via a gate valve and a conductance valve 318. For example, there are no special partitions in the manifold or in the reaction furnaces. A heating element 306 is mounted outside the reaction chamber 302.
[0024] In a specific embodiment, the end cap 304 of the chamber is a lid with embedded temperature control elements. For example, the lid is built with lamps for generating heat and cooling water pipes for actual temperature control. The lid also includes quartz baffles (not shown) that serves an element for controlling exchange of heat and mass (gases) between a main spatial region of the chamber 302 and a spatial region surrounding the lid. By controlling the lid temperature through the embedded elements and heat/mass flow through the baffles, the reactive chemistry in the main spatial region of the chamber, where the substrates with copper indium gallium composite film are loaded, is under controlled.
[0025] The furnace 300 can be used for many applications. According to an embodiment, the furnace 300 is used to apply thermal energy to various types of substrates and to introduce various types of gaseous species, among others. In an embodiment, one or more glass plates or substrates are positioned vertically near the center of chamber 302. As an example, substrates 308 can be similar to those described in FIGS. 2 and 2A (e.g., Cu/In layers or composite Cu/In layer overlying a metal contact layer on a substrate). These layers placed in the process chamber in the presence of a gas containing selenium, such as hydrogen selenide H2Se. After annealing the material for a given period of time, the copper, indium and selenium interdiffuse and react to form a high quality copper indium diselenide (CIS) film.
[0026] FIG. 4 is a simplified diagram of a process for forming a copper indium diselenide layer according to an embodiment of the present invention. This diagram is merely an example, which should not limit the scope of the claims herein. One of ordinary skill in the art would recognize many other variations, modifications, and alternatives. It is also understood that the examples and embodiments described herein are for illustrative purposes only and that various modifications or changes in light thereof will be suggested to persons skilled in the art and are to be included within the spirit and purview of this process and scope of the appended claims.
[0027] As shown in FIG. 4 , the present method can be briefly outlined below.
-
- [0028] 1. Start;
- [0029] 2. Provide a plurality of substrates having a copper and indium composite structure
- [0030] 3. Introduce a gaseous species including a selenide species and a carrier gas into the furnace;
- [0031] 4. Transfer thermal energy into the furnace to increase a temperature from a first temperature to a second temperature;
- [0032] 5. Maintain the temperature at about the second temperature for a period of time;
- [0033] 6. Remove at least the residual selenide species from the furnace;
- [0034] 7. Form vacuum in the process chamber;
- [0035] 8. Introduce a sulfide species into the furnace while;
- [0036] 9. Increasing the temperature to a third temperature;
- [0037] 10. Maintain the temperature at about the third temperature for a period of time;
- [0038] 11. Ramp down the temperature from the third temperature to about the first temperature;
- [0039] 12. Remove gas; and
- [0040] 13. Stop.
[0041] These steps are merely examples and should not limit the scope of the claims herein. One of ordinary skill in the art would recognize many other variations, modifications, and alternatives. For example, various steps outlined above may be added, removed, modified, rearranged, repeated, and/or overlapped, as contemplated within the scope of the invention. As shown, the method 400 begins at start, step 402. Here, the user of the method begins at a process chamber, such as the one noted above, as well as others. The process chamber can be maintained at about room temperature before proceeding with the present method. But the process chamber can start temperature ramping from a temperature higher than room temperature, such as 100° C.
[0042] A plurality of substrates is transferred into the process chamber, step 402. Each of the plurality of substrates can be provided in a vertical orientation with respect to gravity. The plurality of substrates can be defined by a number N, where N is greater than 5. The plurality of substrates can comprise 5 or more individual substrates. In another embodiment, the plurality of substrates can comprise 40 or more individual substrates. For example, each substrate can have a dimension of 65 cm×165 cm or smaller. But it is understood that other dimensions are possible. Each of the substrates is maintained in substantially a planar configuration free from warp or damage. For example, if the substrates were provided in an orientation other than vertical with respect to gravity, the gravitational force could cause the substrates to sag and warp unless they are placed on a supporting structure such as shelves. This occurs when the substrate material reaches a softening temperature, compromising the structural integrity of the substrate. Typically, glass substrates, particular soda lime glass substrates, begin to soften at 480° C. In an embodiment, the substrates are also separate from one another according to a predetermined spacing to ensure even heating and reactions with gaseous species that are to be introduced to the furnace.
[0043] After the substrates are positioned into the process chamber, gaseous species, including a selenide species, and/or a carrier gas, are introduced into the process chamber in step 406. In an embodiment, the gaseous species includes at least H2Se and nitrogen. In another embodiment, the gaseous species other types of chemically inert gas, such as helium, argon, etc. For example, the substrates are placed in the presence of a gas containing selenium, such as H2Se.
[0044] The furnace is then heated up to a second temperature ranging from about 350° C. to 450° C. in step 408. The transfer of thermal energy for the purpose of heating the process chamber can be done by heating elements, heating coils, and the like. For example, step 408, among other things, at least starts the formation of a copper indium diselenide film by reactions between the gaseous species and the copper and indium composite (or layered) structure on each of the substrates. In a specific embodiment, separate layers of copper and indium material are diffused into each other to corm a single layer of copper indium alloy material. The second temperature is maintained for 10 to 90 minutes at the heat treatment interval between 350° C. and 450° C., step 410. In another embodiment, the second temperature range can be from 390° C. to 410° C. For example, the period of time for maintaining the temperature at step 410 is provided to allow formation of the CIS film material. As the temperature increases, the pressure inside the furnace may increase as well. In a specific embodiment, a pressure release valve is used to keep the pressure within the furnace at approximately 650 torr.
[0045] As the temperature is maintained at the second temperature (step 410) or at least when the temperature above certain threshold, the removal of the residual selenide species begins, in step 412. A vacuum is formed in the process chamber through a vacuum pump, in step 414. Once the vacuum is created in the process chamber (step 414), a sulfide species is introduced, in step 416. In a specific embodiment, the residual selenide removal process may continue until the process chamber is in vacuum configuration. After the gas ambience in the furnace has been changed such that the residual selenide species is removed and the sulfide species is introduced, a second temperature ramp up process is initiated, step 418. But, an optional step may include waiting before the temperature is ramped up to allow the temperature uniformity to improve for all substrates in the main spatial region of the chamber. In a specific embodiment, the sulfide species is introduced with nitrogen, which functions as a carrier gas occupying approximately 70 to 75% of furnace. The temperature of the furnace is increased to a third temperature ranging from about 500° C. to 525° C. For example, the third temperature is calibrated for reaction between the sulfide species and the substrates in furnace.
[0046] At step 420, temperature is maintained at the third temperature for a period of time until the formation of the copper indium diselenide CIS (or CIGS if gallium is included) layer is completed. The step is set up for the purpose of extracting out one or more selenium species from the copper indium diselenide film in the ambient of the furnace comprising the sulfur species. It is to be appreciated that a predetermined amount of selenium are removed. In a specific embodiment, approximately 5% of the selenium is removed from the CIS film and is replaced by about 5% of sulfur. According to an embodiment, a complete reaction between the selenium with the CIS film is desired. After the removal of residual selenium, a controlled temperature ramp down process is initiated, in step 422. The furnace is cooled to the first temperature of about room temperature, and the remaining gaseous species are removed from the furnace, in step 424. For example, the gaseous species are removed by a vacuum pumping machine. The temperature sequence described above can be illustrated in the temperature profile in FIG. 5 .
[0047] After step 420, additional steps may be performed depending on the desired end product. For example, if a CIS or CIGS type of thin-film solar cell is desired, additional processes are provided to provide additional structures, such as a transparent layer of material such as ZnO overlaying the CIS layer.
[0048] It is also understood that the examples and embodiments described herein are for illustrative purposes only and that various modifications or changes in light thereof will be suggest to persons skilled in the art and are to be included within the spirit and purview of this application and scope of the appended claims.
[0049] FIG. 5 is a simplified diagram of a temperature profile of the furnace according to an embodiment of the present invention. This diagram is merely an example, which should not limit the scope of the claims herein. The temperature profile further details the temperature ramping process in the above-described method outline (FIG. 4 ) and specification. An optimized temperature profile (FIG. 5 ) is provided to illustrate a heating process according to an embodiment of the present invention. In an embodiment, the process chamber is configured to include independently controlled temperature zones with heater elements properly disposed near the corresponding zones. This enables the derivation of the optimized temperature profile. The optimized profile regulates the process chamber in order to prevent the warping of large substrates at high temperatures. If the temperature is ramped up too high too quickly, warping or damage may occur due to the softening of glass. In addition, the total amount of thermal energy is determined in consideration of total thermal budget available to the substrates and to maintain the uniformity and structure integrity of the glass substrate. For example, by periodically controlling the temperature of the heating process in steps, the substrate stays at a level of stabilization and relaxing in which the requisite structure integrity is maintained. As explained above, material such as glass tends to deform at a temperature of 480° C. or higher, and thus caution is exercised to avoid prolong exposure of substrate at high temperatures. Referring to FIG. 5 , while the ambience of a process chamber is maintained with a gaseous species including a selenide species and a carrier gas, a plurality of substrates is put into the furnace. The plurality of substrates is provided in a vertical orientation with respect to a direction of gravity, with the plurality of substrates being defined by a number N, where N is greater than 5. In certain implementation, the number N is greater than 40. In an embodiment, the substrates include glass substrates, such as soda lime glass. The furnace starts the process with a first temperature of about 30° C. (i.e., around room temperature). The furnace of course can start with a higher temperature, such as 100° C. The furnace is then heated up to a second temperature ranging from about 350° C. to 450° C.
[0050] The second temperature is maintained for 10 to 90 minutes at the heat treatment interval between 350° C. to 450° C. The size of glass substrate can be 65 cm×165 cm or smaller. A challenge in processing large substrate is the warping of the substrate at high temperatures. If the temperature is ramped up directly to T3, warping or damage may occur. In an embodiment, all substrates are loaded in a substrate holder or boat that sets them in substantially a planar configuration free of warp or damage. In an example, each substrate is disposed in the boat in substantially vertical direction relative to gravity and has a predetermined spacing from its nearest neighbor. As shown in FIG. 5 , the slope of ramping up from T2 to T3 is calibrated to reduce and/or eliminate the risk of damaging the substrate. By maintaining the temperature in the process chamber at T2 for a period of time, the substrate can relax and stabilize. The maintaining time at this interval is set up according to the purpose of at least initiating formation of the copper indium diselenide film from the copper and indium composite structure on each of the substrates.
[0051] While the second temperature is maintained, the ambient of the furnace is changed such that the selenide species is removed and a sulfide species is introduced.
[0052] After the gas ambient in the furnace has been changed such that the selenide species is removed and the sulfide species is introduced, a second temperature ramp up process is initiated. There can be a delay in the ramp of furnace temperature in order to improve substrate temperature uniformity. Then, the temperature of the furnace is increased to a third temperature ranging from about 500° C. to 525° C.
[0053] After the temperature ramp-up process, the temperature of the furnace is maintained for 10 to 60 minutes at the heat treatment interval between 500° C. and 525° C. The time interval with the temperature in a plateau in an ambient comprising a sulfur species, e.g., hydrogen sulfide gas, is set up for the purpose of extracting out one or more selenium species from the copper indium diselenide film. In particular, the residual selenide species can be thermally cranked or decomposed to elemental selenium particles, which can be carried away by a convective current from relative hot main spatial region of the chamber to a relative cold region such as the end cap region. Additionally, an exchange reaction occurs to replace sulfur species for the selenium species in the film overlying the substrate. As explained above, a predetermined amount (e.g., 5 to 10%) of selenium can be extracted to provide a proper amount of selenium concentration within the CIS film.
[0054] After partial replacement of selenium by sulfur, a controlled temperature ramp-down process is initiated, as the furnace is then cooled to the first temperature of about room temperature. According to an embodiment, the cooling process is specifically calibrated. As a result of this process, the copper, indium, and selenium interdiffuse and react to form a high quality copper indium diselenide film.
[0055] FIG. 5A is a simplified diagram of a temperature profile of the furnace according to an embodiment of the present invention. This diagram is merely an example, which should not limit the scope of the claims herein. The temperature profile further details the temperature ramping process in the above-described method outline (FIG. 4 ) and specification. An optimized temperature profile (FIG. 5A ) is provided to illustrate a heating process according to an embodiment of the present invention.
[0056] As shown in FIG. 5A , T1 is approximately set at room temperature. But it can be set as high as 100° C. At this temperature, substrates are loaded into a furnace. Air is pumped out (e.g., by vacuum device) from the furnace, and H2Se and N2 gas species are introduced into the furnace. For example, these gas species are introduced to the furnace so that at pressure of approximate 650 torr is reached.
[0057] Next temperature increases from T1 to T2 inside the furnace. For example, the rate of temperature ramping up is optimized to allow the relative uniform reaction between selenium and copper and indium (and possibly with addition of gallium). According to embodiments, the T2 temperature is approximately between 350° C. and 450° C. For example, the furnace stays at the T2 temperature for about 10 to 60 minutes. The time staying at the T2 temperature is to allow for reaction between selenium and copper indium material. In a specific embodiment, separate layers of copper and indium material form copper indium alloy while reacting with selenium material. As shown, CIS and/or CIGS material is formed at T2. During the temperature ramping up process, the pressure inside the furnace is controlled to sustain a relative uniform pressure level of approximate 650 torr. For example, a gas escape valve is used to release gases when the furnace heat up, where pressure increases due to gas expansion at high temperature.
[0058] After the CIS or CIGS material formed, various gaseous species are again pumped out from the furnace. Then, the sulfide gas along with certain inert gases (e.g., nitrogen, argon, helium, etc.) is introduced to the furnace, and the temperature inside the furnace increases from T2 to T3. However, there can be an optional time delay in the ramp of furnace temperature in order to improve substrate temperature uniformity. For example, T3 is approximately 500° C. to 550° C. In a specific embodiment, the temperature stays at T3 to allow the sulfide gas to interact with the CIGS and/or CIS material. For example, the sulfur replaces approximately 3 to 10% of the selenium material from the CIGS and/or CIS material. After the reaction, the furnace is cools down in the ambient of sulfide gas which is removed at last.
[0059] FIG. 7 shows exemplary furnace temperature profiles measured by in-situ thermal couples according to an embodiment of the present invention. This diagram is merely an example, which should not limit the scope of the claims herein. As shown, a large furnace is chosen to be the process chamber where a plurality of substrates has been loaded. Temperature sensors are pre-installed for monitoring all substrates on bottom, middle, and top regions. FIG. 7 just shows the measured temperature profile during an actual processing run. It schematically illustrates realization of the temperature profile preset in FIG. 5 or FIG. 5A . Of course there can be many variations, modifications, and alternatives.
[0060] In an embodiment, the furnace temperature profile, as seen in FIG. 7 , is controlled by adjusting the heaters surrounding the process chamber. Additionally, depending on the internal structural design and substrate configuration when loaded in the substrate holder or boat, the temperature distribution may not be plainly uniform. In fact, several temperature zones can be identified through an experiment. Therefore, the temperature profile set point for corresponding zones can be separately controlled in order to achieve an actual temperature profile with improved uniformity. FIG. 8 just shows exemplary temperature profile set points at various zones in a furnace according to an embodiment of the present invention.
[0061] For achieving desired cell performance for such large sized substrate (65 cm×165 cm), controlling the process with improved temperature uniformity is very important. As mentioned above, identifying various temperature zones in the furnace for setting independent temperature control is one method. Other methods of improving temperature uniformity include designing proper internal structural arrangement and substrate loading configuration. For example, adding certain baffles inside the furnace inner surface can partially isolate main processing zone for achieving better temperature uniformity and controlling the internal convective flow. Adding temperature control elements to an end cap (or lid) so that it can act as a “cryopump” inside the process chamber for reduce contamination and enhance chemistry control of the reactive annealing of the film on substrate. FIG. 9 shows exemplary furnace temperature profile and substrate temperature uniformity according to an embodiment of the present invention. This diagram is merely an example, which should not limit the scope of the claims herein. As shown, the temperature uniformity, described by a temperature difference from bottom to top of the substrate, can be substantially improved by adding certain structural baffle to the furnace internal surface and adjusting the substrate position in the substrate loading boat. Of course, there can be many variations, modifications, and alternatives.
[0062] FIG. 6 is a simplified diagram of a thin film copper indium diselenide device according to an embodiment of the present invention. This diagram is merely an example, which should not limit the scope of the claims herein. As shown, structure 600 is supported on a glass substrate 610. According to an embodiment, the glass substrate comprises soda lime glass, which is about 1 to 3 millimeters thick. A back contact including a metal layer 608 is deposited upon substrate 610. According to an embodiment, layer 608 comprises primarily a film of molybdenum which has been deposited by sputtering. The first active region of the structure 600 comprises a semiconductor layer 606. In an embodiment, the semiconductor layer includes p-type copper indium diselenide (CIS) material. It is to be understood that other the semiconductor layer may include other types of material, such as CIGS, as shown. The second active portion of the structure 600 comprises layers 604 and 602 of n-type semiconductor material, such as CdS or ZnO. For example, in solar cell applications, the CdS and/or ZnO layers function as a winder layers. In FIG. 6 , ZnO is shown overlaying the CdS layer. However, it should be understood that other variations are possible. In an alternative embodiments, the ZnO layer 602 overlays another ZnO layer that is characterized by a different resistivity.
[0063] A photovoltaic cell, or solar cell, such as device 600 described above, is configured as a large-area p-n junction. When photons in sunlight hit the photovoltaic cell, the photons may be reflected, pass through the transparent electrode layer, or become absorbed. The semiconductor layer absorbs the energy causing electron-hole pairs to be created. A photon needs to have greater energy than that of the band gap in order to excite an electron from the valence band into the conduction band. This allows the electrons to flow through the material to produce a current. The complementary positive charges, or holes, flow in the direction opposite of the electrons in a photovoltaic cell. A solar panel having many photovoltaic cells can convert solar energy into direct current electricity.
[0064] Semiconductors based on the copper indium diselenide (CIS) configuration are especially attractive for thin film solar cell application because of their high optical absorption coefficients and versatile optical and electrical characteristics. These characteristics can in principle be manipulated and tuned for a specific need in a given device. Selenium allows for better uniformity across the layer and so the number of recombination sites in the film are reduced which benefits the quantum efficiency and thus the conversion efficiency.
[0065] The present invention provides methods for making CIS-based and/or CIGS-based solar cells on a large glass substrate for a solar panel. The device structure described in FIG. 6 can be patterned into individual solar cells on the glass substrate and interconnected to form the solar panel. The present invention thus provides a cost-effective method for making thin film solar cell panel.
[0066] FIG. 10 shows an exemplary cell open-circuit voltage distribution from ten substrates in a furnace according to an embodiment of the present invention. This diagram is merely an example, which should not limit the scope of the claims herein. As shown, 10 soda lime glass substrates have been loaded into a furnace described before and been carried out a series of large scale selenization and sufurization processes for forming a CIS based photovoltaic absorber film. As the results, eventually the photovoltaic cells made from these films are tested on their IV characteristics. A key parameter, cell open-circuit voltages Voc, is measured around 0.5 V for cells made from those films out of the 10 substrates. FIG. 10 just shows that the Voc value distribution has achieved desired uniformity across all substrates in this large scale production process.
[0067] It will be appreciated that all of the benefits of the present invention can be achieved regardless of the order of deposition of the copper and indium films. That is, the indium could be deposited first or the films could be deposited as a sandwich or stack of thinner layers.
[0068] It is also understood that the examples and embodiments described herein are for illustrative purposes only and that various modifications or changes in light thereof will be suggest to persons skilled in the art and are to be included within the spirit and purview of this application and scope of the appended claims. Although the above has been generally described in terms of a specific structure for CIS and/or CIGS thin film cells, other specific CIS and/or CIGS configurations can also be used, such as those noted in issued U.S. Pat. No. 4,611,091 and U.S. Pat. No. 4,612,411, which are hereby incorporated by reference herein, without departing from the invention described by the claims herein.
Claims
What is claimed is:
1. A method for fabricating a thin film photovoltaic solar energy collector film comprising:
providing a plurality of substrates, each of the substrates having a copper and indium composite structure;
transferring the plurality of substrates into a furnace, each of the plurality of substrates provided in a vertical orientation with respect to a direction of gravity, the plurality of substrates being defined by a number N, where N is greater than 5;
introducing a gaseous species including a selenide species and a carrier gas into the furnace and transferring thermal energy into the furnace to increase a temperature from a first temperature to a second temperature, the second temperature ranging from about 350° C. to about 450° C. to at least initiate formation of a copper indium diselenide film from the copper and indium composite structure on each of the substrates;
maintaining the temperature at about the second temperature for a period of time;
removing at least residual selenide species from the furnace;
introducing a sulfide species into the furnace; and
increasing a temperature to a third temperature, the third temperature ranging from about 500 to 525° C. while the plurality of substrates are maintained in an environment including a sulfur species to extract out one or more selenium species from the copper indium diselenide film;
wherein the furnace is characterized by a temperature profile having a uniformity of about less than 5% difference throughout the furnace during the period of time.
2. The method of claim 1 wherein the copper and indium composite structure comprises a copper layer and an indium layer.
3. The method of claim 1 wherein a first amount of the selenium is replaced by a second amount of sulfur at the copper indium diselenide film.
4. The method of claim 3 wherein the first amount is about 5%.
5. The method of claim 1 wherein the copper and indium composites structure forms a copper indium alloy material in the furnaces.
6. The method of claim 1 further comprising maintaining a substantially constant pressure level of between 600 and 700 torr within the furnace.
7. The method of claim 1 wherein the substrates are stabilized during the period of time.
8. The method of claim 1 further comprising depositing ZnO material.
9. The method of claim 1 further comprising sputtering the copper material on the substrates.
10. The method of claim 1 further comprising evaporating the copper material on the substrates.
11. The method of claim 1 wherein the second temperature ranges from about 390° C. to about 410° C.
12. The method of claim 1 wherein the first temperature ranges from room temperature to about 100° C.
13. The method of claim 1 wherein the second temperature is maintained for about 10 to 60 minutes.
14. The method of claim 1 wherein the selenide species comprises H2Se gas.
15. The method of claim 1 wherein the carrier gas comprises nitrogen gas.
16. The method of claim 1 wherein the sulfide species comprise H2S gas.
17. The method of claim 1 wherein each of the substrates is maintained in substantially a planar configuration free from warp or damage.
18. The method of claim 1 wherein the substrates further comprises gallium material.
19. The method of claim 1 further comprising providing temperature sensors to monitor temperature reading at one or more zones within the furnace.
20. The method of claim 1 further comprising providing a plurality of temperature controls, each of the temperature controls being associated with one or more zones within the furnace.
Patent Citations (42)
| Patent | Date | Inventor | Cited By |
|---|---|---|---|
| US4335266(A) | 1982-06-01 | Mickelsen et al. | Applicant |
| US4442310(A) | 1984-04-01 | Carlson et al. | Applicant |
| US4581108(A) | 1986-04-01 | Kapur et al. | Applicant |
| US4996108(A) | 1991-02-01 | Divigalpitiya et al. | Applicant |
| US5125984(A) | 1992-06-01 | Kruehler et al. | Applicant |
| US5261968(A) | 1993-11-01 | Jordan | Applicant |
| US5501744(A) | 1996-03-01 | Albright et al. | Examiner |
| US5536333(A) | 1996-07-01 | Foote et al. | Applicant |
| US5665175(A) | 1997-09-01 | Safir | Applicant |
| US6307148(B1) | 2001-10-01 | Takeuchi | Applicant |
| US6328871(B1) | 2001-12-01 | Ding et al. | Applicant |
| US6635307(B2) | 2003-10-01 | Huang et al. | Examiner |
| US7179677(B2) | 2007-02-01 | Ramanathan et al. | Examiner |
| US7442413(B2) | 2008-10-01 | Zwaap et al. | Applicant |
| US7544884(B2) | 2009-06-01 | Hollars | Examiner |
| US7855089(B2) | 2010-12-01 | Farris, III et al. | Applicant |
| US7863074(B2) | 2011-01-01 | Wieting | Applicant |
| US7910399(B1) | 2011-03-01 | Wieting | Applicant |
| US7955891(B2) | 2011-06-01 | Wieting | Applicant |
| US7960204(B2) | 2011-06-01 | Lee | Applicant |
| US2005/0109392(A1) | 2005-05-01 | Hollars | Examiner |
| US2006/0220059(A1) | 2006-10-01 | Satoh et al. | Applicant |
| US2007/0089782(A1) | 2007-04-01 | Scheuten et al. | Applicant |
| US2007/0116892(A1) | 2007-05-01 | Zwaap et al. | Examiner |
| US2007/0151596(A1) | 2007-07-01 | Nasuno et al. | Applicant |
| US2007/0169810(A1) | 2007-07-01 | Van Duren et al. | Applicant |
| US2008/0041446(A1) | 2008-02-01 | Wu et al. | Applicant |
| US2008/0092945(A1) | 2008-04-01 | Munteanu et al. | Applicant |
| US2008/0092953(A1) | 2008-04-01 | Lee | Applicant |
| US2009/0087942(A1) | 2009-04-01 | Meyers | Examiner |
| US2009/0145746(A1) | 2009-06-01 | Hollars | Examiner |
| US2009/0234987(A1) | 2009-09-01 | Lee et al. | Applicant |
| US2009/0235983(A1) | 2009-09-01 | Girt et al. | Examiner |
| US2009/0235987(A1) | 2009-09-01 | Akhtar et al. | Examiner |
| US2009/0293945(A1) | 2009-12-01 | Peter | Examiner |
| US2010/0087016(A1) | 2010-04-01 | Britt et al. | Examiner |
| US2010/0087026(A1) | 2010-04-01 | Winkeler et al. | Examiner |
| US2010/0096007(A1) | 2010-04-01 | Mattmann et al. | Examiner |
| US2010/0101648(A1) | 2010-04-01 | Morooka et al. | Examiner |
| US2010/0101649(A1) | 2010-04-01 | Huignard et al. | Examiner |
| US2011/0070690(A1) | 2011-03-01 | Wieting | Applicant |
| US2011/0073181(A1) | 2011-03-01 | Wieting | Applicant |
Non-Patent Literature (23)
- Ellmer et al., Copper Indium Disulfide Solar Cell Absorbers Prepared in a One-Step Process by Reactive Magnetron Sputtering from Copper and Indium Targets; Elsevier Science B.V; Thin Solid Films 413 (2002) pp. 92-97.Applicant
- Onuma et al., Preparation and Characterization of CuInS2 Thin Films Solar Cells with Large Grain, Elsevier Science B.V; Solar Energy Materials & Solar Cells 69 (2001) pp. 261-269.Applicant
- International Search Report & Written Opinion for PCT Application No. PCT/US2009/46802, mailed on Jul. 31, 2009, 11 pages.Applicant
- International Search Report & Written Opinion for PCT Application No. PCT/US2009/46161, mailed on Jul. 27, 2009, 14 pages.Applicant
- Supplemental Notice of Allowability of Dec. 10, 2010 for U.S. Appl. No. 12/568,641; 3 pages.Applicant
- Notice of Allowance of Nov. 19, 2010 for U.S. Appl. No. 12/568,641; 6 pages.Applicant
- Restriction Requirement of Oct. 18, 2010 for U.S. Appl. No. 12/568,641; 7 pages.Applicant
- Non-Final Office Action of May 27, 2010 for U.S. Appl. No. 12/568,641; 10 pages.Applicant
- Final Office Action of May 31, 2011 for U.S. Appl. No. 12/621,489, 13 pages.Applicant
- Notice of Allowance of May 25, 2011 for U.S. Appl. No. 12/566,651, 8 pages.Applicant
- Non-Final Office Action of May 2, 2011 for U.S. Appl. No. 12/953,729, 9 pages.Applicant
- Non-Final Office Action of May 2, 2011 for U.S. Appl. No. 12/953,725, 9 pages.Applicant
- Non-Final Office Action of May 2, 2011 for U.S. Appl. No. 12/953,721, 9 pages.Applicant
- Non-Final Office Action of May 2, 2011 for U.S. Appl. No. 12/953,716, 9 pages.Applicant
- Non-Final Office Action of May 2, 2011 for U.S. Appl. No. 12/953,708, 9 pages.Applicant
- Non-Final Office Action of May 2, 2011 for U.S. Appl. No. 12/953,701, 9 pages.Applicant
- Non-Final Office Action of Apr. 28, 2011 for U.S. Appl. No. 12/237,369, 17 pages.Applicant
- Notice of Allowance of Apr. 27, 2011 for U.S. Appl. No. 12/564,886, 11 pages.Applicant
- Notice of Allowance of Apr. 26, 2011 for U.S. Appl. No. 12/564,046, 11 pages.Applicant
- Notice of Allowance of Apr. 25, 2011 for U.S. Appl. No. 12/563,065, 11 pages.Applicant
- Notice of Allowance of Apr. 19, 2011 for U.S. Appl. No. 12/567,715, 11 pages.Applicant
- Notice of Allowance of Apr. 8, 2011 for U.S. Appl. No. 12/953,697, 11 pages.Applicant
- Notice of Allowance of Apr. 5, 2011 for U.S. Appl. No. 12/953,679, 11 pages.Applicant