1. Field of the Invention
Embodiments of the invention generally relate to a temperature controlled lid assembly for a processing chamber and a method for depositing tungsten-containing materials on a substrate by vapor deposition processes.
2. Description of the Related Art
Modern integrated circuits contain large numbers of transistors. These transistors are generally field effect transistors that contain a source region and a drain region with a gate electrode located in between the source and drain regions.
A typical gate structure contains a thin polysilicon electrode that lies on top of a thin layer of gate oxide such as silicon oxide. The gate electrode and gate oxide are formed between semi-conducting source and drain regions, that define an underlying well of p-type or n-type silicon. The source and drain regions are doped opposite to the well to define the gate location, a layer of insulating material such as silicon oxide, silicon nitride, or silicon oxynitride is deposited on top of the source and drain regions and an aperture or via is formed in the insulating material between the source and drain regions. The gate structure within the via contains a thin oxide layer, a polysilicon layer and a metal plug. The metal plug is typically formed by vapor depositing a metal such as tungsten on top of the polysilicon gate electrode. To complete the connection, the silicon then is caused to diffuse into the tungsten during a thermal annealing process forming a layer of relatively uniform tungsten silicide as the connection to the gate electrode. Without annealing, the silicon will ultimately diffuse into the tungsten forming a non-uniform layer of tungsten silicide.
A gate electrode having an electrical connection made of pure tungsten would be more desirable than a tungsten silicide electrode since tungsten has a lower resistivity than tungsten silicide. Unfortunately, silicon diffuses into the tungsten forming tungsten silicide. The diffusion can be prevented by depositing a layer of tungsten nitride as a diffusion barrier between the tungsten and the silicon. Tungsten nitride is a good conductor as well as an excellent diffusion barrier material. Such a barrier layer is typically formed by reducing tungsten hexafluoride (WF6) with ammonia (NH3) in a chemical vapor deposition (CVD) process or an atomic layer deposition (ALD) process.
Unfortunately, the above described process results in the formation of contaminant particles in the form of solid byproducts. These byproducts include ammonia adducts of tungsten hexafluoride ((NH3)4.WF6), ammonium fluoride (NH4F), and other ammonium complexes. Many of these particles become attached to the interior of the deposition chamber. During temperature fluctuations within the chamber, the deposits flake off the walls and contaminate the wafer. Further, the tungsten nitride that is deposited using the above described process has a polycrystalline structure in which there are many grain boundaries. As a result, the diffusion barrier properties of the tungsten nitride are compromised. In addition, tungsten nitride films deposited by the traditional method tend not to adhere very well to the substrate upon which they are deposited.
Therefore, there is a need for an apparatus and a process for depositing tungsten-containing materials, wherein a tungsten precursor may be flowed with or exposed to another reagent without contaminating the processing chamber or the substrate surface.
In one embodiment, a processing chamber for depositing a material by vapor deposition is provided which includes a lid assembly attached to a chamber body, wherein the lid assembly contains a lid plate, a showerhead, a mixing cavity, and a distribution cavity, and a resistive heating element contained within the lid plate. In one example, the resistive heating element is configured to provide the lid plate at a temperature within a range from about 120° C. to about 180° C., preferably, from about 140° C. to about 160° C., more preferably, from about 145° C. to about 155° C., such as about 150° C. The mixing cavity is in fluid communication with a tungsten precursor source and a nitrogen precursor source, wherein the tungsten precursor source generally contains tungsten hexafluoride and the nitrogen precursor source generally contains ammonia. In some embodiments, the lid assembly further contains a liquid channel attached to a temperature regulating system. Also, the chamber body further contains a substrate support pedestal having a heater.
In another embodiment, a processing chamber for depositing a tungsten-containing material by vapor deposition is provided which includes a lid assembly attached to a chamber body, wherein the lid assembly contains a lid plate, a showerhead, a mixing cavity, and a distribution cavity, a resistive heating element contained within the lid plate, a tungsten precursor source coupled to and in fluid communication with the lid assembly, and a nitrogen precursor source coupled to and in fluid communication with the lid assembly.
In other embodiments, the processing chamber contains a reducing agent precursor source coupled to and in fluid communication with the lid assembly. The reducing agent precursor source contains a reducing agent, such as silane, hydrogen, diborane, disilane, phosphine, derivatives thereof, or combinations thereof. In one embodiment, a first valve is positioned between the tungsten precursor source and the lid assembly, a second valve is positioned between the nitrogen precursor source and the lid assembly, and a third valve is positioned between the reducing agent precursor source and the lid assembly. Each of the first valve, the second valve, and the third valve is independently controlled by a programmable logic controller. In one example, the programmable logic controller is configured to sequentially open and close the first and third valves while forming a tungsten nucleation layer during an atomic layer deposition process. In another example, the programmable logic controller is configured to simultaneously open and close the first and second valves while forming a tungsten nitride layer during a chemical vapor deposition process. In another example, the programmable logic controller is configured to sequentially open and close the first and second valves while forming a tungsten nitride layer during a second atomic layer deposition process. In another example, the programmable logic controller is configured to open and close the third valve during a pre-nucleation soak process or a post-nucleation soak process.
In one embodiment, a method for forming a tungsten-containing material on a substrate is provided which includes positioning a substrate within a processing chamber comprising a lid plate, heating the lid plate to a temperature within a range from about 120° C. to about 180° C., depositing a tungsten nitride layer on the substrate during a vapor deposition process within the processing chamber, and depositing a tungsten nucleation layer on the tungsten nitride layer during an atomic layer deposition process within the processing chamber.
In another embodiments, a method for forming a tungsten-containing material on a substrate is provided which includes positioning a substrate within a processing chamber containing a lid plate, heating the lid plate to a temperature within a range from about 120° C. to about 180° C., depositing a first tungsten nucleation layer on the substrate during a first atomic layer deposition process within the processing chamber, depositing a tungsten nitride layer on the first tungsten nucleation layer during a vapor deposition process within the processing chamber, and depositing a second tungsten nucleation layer on the tungsten nitride layer during a second atomic layer deposition process within the processing chamber.
In another embodiments, a method for forming a tungsten-containing material on a substrate is provided which includes positioning a substrate within a processing chamber containing a lid plate, heating the lid plate to a temperature within a range from about 120° C. to about 180° C., exposing the substrate to a reducing gas during a pre-nucleation soak process, depositing a first tungsten nucleation layer on the substrate during a first atomic layer deposition process within the processing chamber, depositing a tungsten nitride layer on the first tungsten nucleation layer during a vapor deposition process within the processing chamber, and depositing a second tungsten nucleation layer on the tungsten nitride layer during a second atomic layer deposition process within the processing chamber.
In another embodiments, a method for forming a tungsten-containing material on a substrate is provided which includes positioning a substrate within a processing chamber containing a lid plate, heating the lid plate to a temperature within a range from about 120° C. to about 180° C., exposing the substrate to a reducing gas during a pre-nucleation soak process, depositing a first tungsten nucleation layer on the substrate during a first atomic layer deposition process within the processing chamber, depositing a tungsten nitride layer on the first tungsten nucleation layer during a vapor deposition process within the processing chamber, depositing a second tungsten nucleation layer on the tungsten nitride layer during a second atomic layer deposition process within the processing chamber, and exposing the substrate to another reducing gas during a post-nucleation soak process.
In other embodiments, the method provides that the lid plate is heated to a temperature within a range from about 140° C. to about 160° C., preferably, from about 145° C. to about 155° C., more preferably, at about 150° C. The tungsten nitride layer may be deposited during a chemical vapor deposition process, wherein a tungsten precursor and a nitrogen precursor are co-flowed during the chemical vapor deposition process. In one embodiment, the tungsten precursor contains tungsten hexafluoride and the nitrogen precursor contains ammonia.
In other embodiments, the method provides that the substrate is exposed to a reducing agent during the pre-nucleation soak process or the post-nucleation soak process. The reducing agent may contain silane, hydrogen, diborane, disilane, phosphine, derivatives thereof, or combinations thereof. Other examples provide that a bulk tungsten layer is deposited on the tungsten nucleation layer during a thermal chemical vapor deposition process.
In other embodiments, an angled mixer and a lid assembly that may be utilized on a processing chamber are disclosed herein. The lid assembly may have both heating elements and cooling channels to permit rapid heating and cooling of the chamber lid so that multiple depositions may occur within the same processing chamber at different temperatures. The mixer may be angled to be disposed within a central area of the lid assembly. The mixer may have an opening at the top to permit cleaning gas to enter the processing chamber, a second opening to permit introduction of a first deposition gas, and a third opening to permit introduction of a second deposition gas perpendicular to the flow of the first deposition gas so that the first and second deposition gases effectively mix within the mixer before being exposed to the substrate.
In one embodiment, a mixer contains a mixer body having a base portion, a shaft portion substantially perpendicular to the base portion, one or more first gas introduction holes having a first diameter along the shaft portion, and one or more second gas introduction holes having a second diameter less than the first diameter disposed along the shaft portion.
In another embodiment, a lid assembly contains one or more heating elements, one or more cooling channels, a hole disposed about the center axis of the lid assembly and through the lid assembly, a notch disposed adjacent to and coupled with the hole, and a cavity disposed adjacent to and coupled with the hole.
In another embodiment, a lid assembly contains a lid body and a mixer body coupled with the lid body. The lid body contains one or more heating elements, one or more cooling channels, and a notch disposed within an upper surface of the lid body. The a mixer body contains a base portion, a shaft portion substantially perpendicular to the base portion, one or more first gas introduction holes having a first diameter along the shaft portion, and one or more second gas introduction holes having a second diameter less than the first diameter disposed along the shaft portion.
So that the manner in which the above recited features of the invention can be understood in detail, a more particular description of the invention, briefly summarized above, may be had by reference to embodiments, some of which are illustrated in the appended drawings. It is to be noted, however, that the appended drawings illustrate only typical embodiments of this invention and are therefore not to be considered limiting of its scope, for the invention may admit to other equally effective embodiments.
To facilitate understanding, identical reference numerals have been used, where possible, to designate identical elements that are common to the figures. It is contemplated that elements disclosed in one embodiment may be beneficially utilized on other embodiments without specific recitation.
Embodiments of the invention provide a processing chamber for depositing a material by vapor deposition. In one embodiment, the processing chamber includes a lid assembly attached to a chamber body, wherein the lid assembly contains a lid plate, a showerhead, a mixing cavity, a distribution cavity, and a resistive heating element contained within the lid plate. In one example, the resistive heating element is configured to provide the lid plate at a temperature within a range from about 120° C. to about 180° C., preferably, from about 140° C. to about 160° C., more preferably, from about 145° C. to about 155° C., such as about 150° C. The mixing cavity is in fluid communication with a tungsten precursor source and a nitrogen precursor source, wherein the tungsten precursor source generally contains tungsten hexafluoride and the nitrogen precursor source generally contains ammonia.
Embodiments of the apparatuses and processes as described herein are useful to deposit tungsten-containing materials while avoiding contamination of the processing chamber or substrate of various byproducts, including ammonia adducts of tungsten hexafluoride ((NH3)4.WF6), ammonium fluoride (NH4F), and other ammonium complexes.
Embodiments of the invention provide an angled mixer and lid assembly for a processing chamber. The lid assembly may have both heating elements and cooling channels to permit rapid heating and cooling of the chamber lid so that multiple depositions may occur within the same processing chamber at different temperatures. The mixer may be angled to be disposed within a central area of the lid assembly. The mixer may have an opening at the top to permit a cleaning gas to enter the processing chamber, a second opening to permit introduction of a first deposition gas, and a third opening to permit introduction of a second deposition gas perpendicular to the flow of the first deposition gas so that the first and second deposition gases effectively mix within the mixer before being exposed to the substrate.
As described below, the angled mixer and the lid assembly may be used to form tungsten-containing materials by vapor deposition processes as described herein. The tungsten-containing materials may contain metallic tungsten, tungsten nitride, tungsten silicide, tungsten boride, tungsten phosphide, derivatives thereof, or combinations thereof. A processing chamber may be used to perform chemical vapor deposition (CVD), plasma-enhanced CVD (PE-CVD), pulsed-CVD, atomic layer deposition (ALD), plasma-enhanced ALD (PE-ALD), derivatives thereof, or combinations thereof. Processing chambers for CVD and ALD processes are commercially available from Applied Materials, Inc., located in Santa Clara, Calif. In some embodiments, the processing chamber for depositing tungsten-containing materials may contain an in situ plasma source or a remote plasma source.
Inner lid 112 may also contain one or more cooling channels 114. Additionally, inner lid 112 may contain one or more heating elements 116. Both the cooling channels 114 and heating elements 116 may be embedded in inner lid 112. The presence of both heating elements 116 and cooling channels 114 in inner lid 112 permit the rapid increase in temperature and decrease in temperature that may be necessary to deposit both tungsten and tungsten nitride at different temperatures within the same processing chamber 100 as well as cleaning processing chamber 100.
Angled mixer 110 may be disposed within inner lid 112 for introduction of both deposition gases and cleaning gases into processing chamber 100. Cleaning gases may be provided from cleaning gas panel 122 through top 124 of angled mixer 110. A first deposition gas may be provided to angled mixer 110 from first gas panel 126 through opening 128 disposed on a side surface of angled mixer 110. A second deposition gas may be provided to angled mixer 110 from second gas panel 130 to notch 132 disposed in inner lid 112 adjacent angled mixer 110. Notch 132 permits the second gas to travel around the outside of angled mixer 110 and then inject into angled mixer 110 through one or more holes.
In one embodiment, the ratio of the widths of vacuum channels 210a and 210b may be within a range from about 1.6 to about 2.0, preferably, from about 1.75 to about 1.95, and more preferably, from about 1.85 to about 1.90. In one example, the ratio of the widths of vacuum channels 210a and 210b may be about 1.875. Openings 208a and 208b may be offset on angled mixer 206 such that one opening 208a may be spaced a distance “B” from the center of angled mixer 206 and the other opening 208b may be spaced a second, different distance “C” from the center of angled mixer 206. In one embodiment, the ratio of the distance “C” to the distance “B” may be about 1.3. Openings 208a and 208b may be offset so angled mixer 206 may be coupled with lid 202 in the correct orientation.
Angled mixer 206 also contains shaft portion 230 having inner wall 212 having a substantially constant diameter “D” and outer wall 216 that is angled relative to inner wall 212. Additionally, outer wall 216 is angled relative to wall 218 of lid 202 and wall 220 of gas inlet manifold 204. Outer wall 216 is angled as shown by arrows “A”. The angled outer wall 216 relative to the substantially straight walls 218 and 220 of lid 202, and gas inlet manifold 204 respectively permit angled mixer 206 to be easily inserted into lid assembly 200 without outer wall 216 scraping walls 218 and 220 while also permitting a tight fit at a location corresponding to where shaft portion 230 meets base portion 228 of angled mixer 206.
A cleaning gas may be introduced to the processing chamber through opening 222 in angled mixer 206 that is coupled with a cleaning gas introduction tube 232. Opening 222 may be disposed at the top of shaft portion 230 of angled mixer 206 such that the cleaning gas may clean the entire angled mixer 206. A first deposition gas may be provided to angled mixer 206 through opening 224 in shaft portion 230 of angled mixer 206. The first deposition gas flows downward through shaft portion 230 of angled mixer 206 as shown by the arrows “E”. A second deposition gas may be introduced to notch 214 formed between outer wall 216 of shaft portion 230 of angled mixer 206 and walls 218 and 220 of lid 202 and gas inlet manifold 204. The second deposition gas may flow around the outside of angled mixer 206 and then inject into angled mixer 206 through holes 226 formed in notch 214 of shaft portion 230 in a direction substantially perpendicular to the flow of the first deposition gas as shown by the arrows “F”. In one embodiment, eight holes 226 may be present. The cross-flow of the second deposition gas may permit the first and secondary gases to sufficiently mix as they collectively flow down through angled mixer 206 as shown by the arrows “G”. In one embodiment, the diameter of holes 226 is less than the diameter of opening 224. Opening 222 may have a diameter that is different than the diameter of opening 224 and holes 226.
Notch 314 may be present to permit deposition gas to be provided to the mixer once inserted into lid assembly 300. Sealing cavity 310 may be present to permit lid assembly 300 to be coupled with a gas inlet manifold (not shown). A cavity portion 316 may be present for the base portion of a mixer to be coupled to lid assembly 300.
Heating element 318 may be disposed within lid assembly 300 to heat the processing gas and lid assembly 300. Heating element 318 may have multiple turns and winds through lid assembly 300 and may even turn back upon itself. In one embodiment, heating element 318 may contain aluminum. Heating elements 318 containing aluminum may be beneficial because the aluminum, as compared to conventional stainless steel heating elements, may prevent warping. One or more cooling channels 320 may also be present outside heating element 318 to rapidly cool lid assembly 300. One or more thermocouples 322 may be coupled with the lid to measure the temperature of lid assembly 300. Having both heating elements 318 and cooling channels 320 coupled within the same lid permits the rapid cooling and rapid heating necessary to perform both tungsten and tungsten nitride deposition with the same processing chamber. The rapid heating and cooling can permit successive deposition processes of tungsten and tungsten nitride to occur within the same chamber without sacrificing throughput.
In one embodiment, cooling channels 320 may be used to regulate the temperature of lid assembly 300 during the vapor deposition process for depositing a tungsten-containing material. In one embodiment, lid assembly 101 may be heated or maintained at a temperature within a range from about 120° C. to about 180° C., preferably, from about 140° C. to about 160° C., and more preferably, from about 145° C. to about 155° C., such as about 150° C., during the vapor deposition process of a tungsten-containing material.
Temperature control may be useful to deposit both metallic tungsten and tungsten nitride materials in the same chamber. For example, to deposit metallic tungsten, lid assembly 300 may be maintained at a temperature of about 25° C. Thus, during tungsten deposition, heating elements 318 may be turned off and lid assembly 300 may be cooled by flowing a cooling fluid through cooling channel 320. The cooling fluid may contain water, glycol based fluid, or combinations thereof. Following the tungsten deposition, the chamber may be purged of the tungsten deposition gases. During the purging, the cooling fluid may be turned off and removed from cooling channel 320 by forcing air or an inert gas through cooling channel 320. The tungsten nitride deposition may occur at about 150° C. During the tungsten nitride deposition, heating elements 318 may be turned on while the cooling channel does not have a cooling fluid circulating therethrough.
A controller (not shown) may control the heating and cooling. A series of valves may be used to control when the cooling fluid is supplied to lid assembly 300. When the cooling fluid is supplied to lid assembly 300, heating element 318 may not be on. Similarly, when the cooling fluid is purged from cooling channel 320, heating element 318 may not be on. When the tungsten nitride is deposited, cooling fluid may not be supplied to lid assembly 300. When the cooling fluid is supplied to cooling channel 320, the air and/or inert gas may not be supplied to cooling channel 320. When the air and/or inert gas is supplied to cooling channel 320, cooling fluid may not be supplied to cooling channel 320. If the temperature of lid assembly 300 as measured by thermocouples 322 is greater than about 85° C., cooling fluid may not be supplied to the cooling channels 320. If the temperature of lid assembly 300 is greater than about 180° C., then heating elements 318 may be turned off. If the lid assembly temperature is greater than about 65° C., the chamber may not be vented.
In one embodiment, the primary lid discussed above in reference to
In another embodiment,
Showerhead 556 has a relatively short upwardly extending rim 558 screwed to gas box plate 560. Both showerhead 556 and gas box plate 560 may be formed from or contain a metal, such as aluminum, stainless steel, or alloys thereof. Convolute liquid channel 562, illustrated in
Processing chamber 450 further contains heater pedestal 552 connected to pedestal stem 554 that may be vertical moved within processing chamber 450. The heater portion of heater pedestal 552 may be formed of a ceramic. In its upper, deposition position, pedestal 552 holds the substrate in close opposition to lower surface 582 of showerhead 556, processing region 426 being defined between pedestal 552 and lower surface 582 of showerhead 556. Showerhead 556, has a large number of apertures or holes 580 communicating between lower cavity 430 and processing region 426 to allow the passage of processing gas. The processing gas is supplied through gas port 432 formed at the center of water-cooled gas box plate 560 made of aluminum. The upper side of gas box plate 560 is covered by water cooling cover plate 434 surrounding the upper portion of gas box plate 560 that includes gas port 432. Gas port 432 supplies the processing gases to upper cavity 438 separated from lower cavity 430 by blocker plate 440, also having a large number of holes 580 therethrough. One purpose of cavities 430 and 438, showerhead 556, and blocker plate 440 is to evenly distribute the processing gas over the upper face of the substrate.
The substrate may be supported on pedestal 552, which is illustrated in a raised, deposition position. In a lowered, loading position, lifting ring 416 attached to lift tube 417 lifts four lift pins 418 fit to slide into pedestal 552 so that lift pins 418 can receive the substrate loaded into the chamber through loadlock port 419 in chamber body 420. In one embodiment, pedestal 552 may contain an optional confinement ring 610, such as during plasma-enhanced vapor deposition processes.
Lid isolator 574 is interposed between showerhead 556 and lid rim 466, which can be lifted off chamber body 420 to open processing chamber 450 for maintenance access. The vacuum within processing chamber 450 is maintained by vacuum pump 470 connected to pump plenum 472 within processing chamber 450, which connects to annular pumping channel 474.
As illustrated in
In another embodiment,
In other embodiments, processing chamber 750 is connected to and in fluid communication with sources 720, 722, 724, and 726. In one configuration, source 720 is a carrier gas source and contains a carrier gas, source 722 is a tungsten gas source and contains a tungsten precursor, source 724 is a nitrogen source and contains a nitrogen precursor, source 726 is a reducing agent gas source and contains a reducing agent. Valve 730 may be positioned between source 720 and gas port 432, valve 732 may be positioned between source 722 and gas port 432, valve 734 may be positioned between source 724 and gas port 432, and valve 736 may be positioned between source 726 and gas port 432. Programmable logic controller (PLC) 738 may be used to control the opening and closing of valves 730, 732, 734, and 736 during a CVD process, a pulsed-CVD process, or an ALD process. Valve 730 may be left turned on to provide a steady stream or flow of a carrier gas from source 720.
In one example, source 720 may contain a carrier gas such as nitrogen, argon, hydrogen, forming gas, or mixtures thereof. Source 722 may have a tungsten precursor, such as tungsten hexafluoride and source 724 may have a nitrogen precursor such as ammonia. A reducing agent may be contained within source 726, which is coupled to and in fluid communication with lid assembly 700. The reducing agent may be silane, hydrogen, diborane, disilane, phosphine, derivatives thereof, or combinations thereof.
Valve 732 may be positioned between source 722 containing the tungsten precursor and lid assembly 700, valve 734 positioned between source 724 containing the nitrogen precursor and lid assembly 700, and valve 736 positioned between source 726 and the reducing agent and lid assembly 700. Each of valves 720, 722, 724, and 726 is independently controlled by PLC 738. In one example, PLC 738 is configured to sequentially open and close valves 722 and 726 while forming a tungsten nucleation layer during an ALD process. In another example, PLC 738 is configured to simultaneously open and close valves 722 and 724 while forming a tungsten nitride layer during a CVD process. In another example, PLC 738 is configured to sequentially open and close valves 722 and 744 while forming a tungsten nitride layer during a second ALD process. In another example, PLC 738 is configured to open and close valve 736 during a pre-nucleation soak process or a post-nucleation soak process while the substrate is exposed to a reducing agent delivered from source 726.
The tungsten-containing materials may contain metallic tungsten, tungsten nitride, tungsten silicide, tungsten boride, tungsten phosphide, derivatives thereof, or combinations thereof. Processing chamber 750 may be used to perform CVD, PE-CVD, pulsed-CVD, ALD, PE-ALD, derivatives thereof, or combinations thereof. Controller 780 and resistive heating element 770 may be used to regulate the temperature of lid assembly 700 during the vapor deposition process for depositing a tungsten-containing material. In one embodiment, lid assembly 700 or gas box plate 760 may be heated or maintained at a temperature within a range from about 120° C. to about 180° C., preferably, from about 140° C. to about 460° C., and more preferably, from about 145° C. to about 155° C., such as about 150° C., during the vapor deposition process of a tungsten-containing material. Convolute liquid channel 562 may be used to heat or cool lid assembly 700.
Showerhead 556 has a relatively short upwardly extending rim 558 screwed to gas box plate 760. Both showerhead 556 and gas box plate 760 may be formed of a metal, such as aluminum, stainless steel, or alloys thereof. Convolute liquid channel 562, illustrated in
Water ports 448 and 449 through water cooling cover plate 434 are illustrated in
Several CVD processing chambers that may be useful for some of the deposition processes described herein may be further described in commonly assigned U.S. Pat. Nos. 5,846,332, 6,079,356, 6,162,715, and 6,827,815, which are incorporated herein by reference in their entirety. Several ALD processing chambers that may be useful for some of the deposition processes described herein may be further described in commonly assigned U.S. Pat. Nos. 6,660,126, 6,716,287, 6,821,563, 6,878,206, 6,916,398, 6,936,906, 6,998,014, 7,175,713, and 7,204,886, commonly assigned U.S. Ser. No. 09/798,258, filed Mar. 2, 2001, and published as 2002-0121241; U.S. Ser. No. 10/032,293, filed Dec. 21, 2001, and published as 2003-0116087; U.S. Ser. No. 10/356,251, filed Jan. 31, 2003, and published as 2004-0065255; U.S. Ser. No. 10/268,438, filed Oct. 9, 2002, and published as 2004-0069227; U.S. Ser. No. 11/127,753, filed May 12, 2005, and published as 2005-0271812; U.S. Ser. No. 10/281,079, filed Oct. 25, 2002, and published as 2003-0121608, and commonly assigned U.S. Ser. Nos. 11/556,745, 11/556,752, 11/556,756, 11/556,758, and 11/556,763, each filed on Nov. 6, 2006, and published as 2007-0119370, 2007-0119371, 2007-0128862, 2007-0128863, 2007-0128864, which are incorporated herein by reference in their entirety.
In one embodiment, a processing chamber for depositing tungsten-containing materials contains a lid plate containing an embedded heating element disposed therein. In another embodiment, a processing chamber for depositing tungsten-containing materials contains a gas box plate containing an embedded heating element disposed therein. In another embodiment, a processing chamber for depositing tungsten-containing materials contains an insulating jacket heater containing heating element disposed thereon. Heating elements may be configured to generate more heat near a particular region of lid plate, such as an inner region or an outer region. A controller may be used to regulate the temperature of lid plate by adjusting power levels to the heating element. In various embodiments, the processing chamber for depositing tungsten-containing materials may contain an in situ plasma source or a remote plasma source.
In one embodiment, a tungsten nitride layer and a tungsten nucleation layer are deposited during a vapor deposition process. The lid plate may be heated to a temperature within a range from about 140° C. to about 160° C., preferably, about 150° C. A substrate may be exposed to a pre-soak gas containing silane during a pre-soak process. The pre-soak process may last for a time period within a range about 10 seconds to about 30 seconds, preferably about 20 seconds, while the processing chamber may have an internal pressure within a range from about 50 Torr to about 150 Torr, preferably, about 90 Torr. A tungsten nitride layer is deposited at a process temperature within a range from about 375° C. to about 425° C., preferably, about 400° C. The pre-soak process and the tungsten nitride deposition may be repeated about 25 times to form a tungsten nitride material. Subsequently, a tungsten nucleation layer may be deposited by an ALD process by repeating about 15 cycles of exposing the substrate to the tungsten precursor and a reducing agent (e.g., SiH4 or B2H6).
In one example, the tungsten nitride is deposited by a CVD process wherein the tungsten precursor (e.g., WF6) is co-flowed with the nitrogen precursor (e.g., NH3). The lid assembly contains a lid plate heated to a temperature within a range from about 120° C. to about 180° C., preferably, from about 140° C. to about 160° C., and more preferably, from about 145° C. to about 155° C., such as about 150° C. The processing chamber may have an internal pressure within a range from about 2 Torr to about 20 Torr, such as about 6 Torr. In another example, the tungsten nitride is deposited by an ALD process wherein the tungsten precursor (e.g., WF6) is sequentially pulsed with the nitrogen precursor (e.g., NH3). The substrate may be exposed to multiple ALD cycles, wherein each ALD cycle exposes the substrate to a pre-soak gas containing a reducing agent (e.g., SiH4 or B2H6) for about 0.5 seconds, purge gas for about 2 seconds, tungsten precursor for about 1.5 seconds, purge gas for about 2 seconds, nitrogen precursor for about 2.5 seconds, and purge gas for about 2 seconds.
While the foregoing is directed to embodiments of the invention, other and further embodiments of the invention may be devised without departing from the basic scope thereof, and the scope thereof is determined by the claims that follow.
This application claims benefit of U.S. Ser. No. 60/887,142, filed Jan. 29, 2007, and U.S. Ser. No. 60/944,085, filed Jun. 14, 2007, which are herein incorporated by reference in their entirety.
Number | Name | Date | Kind |
---|---|---|---|
4058430 | Suntola et al. | Nov 1977 | A |
4389973 | Suntola et al. | Jun 1983 | A |
4413022 | Suntola et al. | Nov 1983 | A |
4415275 | Dietrich | Nov 1983 | A |
4761269 | Conger et al. | Aug 1988 | A |
4825809 | Mieno et al. | May 1989 | A |
4834831 | Nishizawa et al. | May 1989 | A |
4947790 | Gartner et al. | Aug 1990 | A |
4975252 | Nishizawa et al. | Dec 1990 | A |
4993357 | Scholz et al. | Feb 1991 | A |
5027746 | Frijlink et al. | Jul 1991 | A |
5173327 | Sandhu et al. | Dec 1992 | A |
5178681 | Moore et al. | Jan 1993 | A |
5224202 | Arnold et al. | Jun 1993 | A |
5225366 | Yoder | Jul 1993 | A |
5261959 | Gasworth | Nov 1993 | A |
5281274 | Yoder | Jan 1994 | A |
5294286 | Nishizawa et al. | Mar 1994 | A |
5338362 | Imahashi et al. | Aug 1994 | A |
5374570 | Nasu et al. | Dec 1994 | A |
5441703 | Jurgensen et al. | Aug 1995 | A |
5443647 | Aucoin et al. | Aug 1995 | A |
5480818 | Matsumoto et al. | Jan 1996 | A |
5483919 | Yokoyama et al. | Jan 1996 | A |
5503875 | Imai et al. | Apr 1996 | A |
5558717 | Zhao et al. | Sep 1996 | A |
5580421 | Hiatt et al. | Dec 1996 | A |
5674786 | Turner et al. | Oct 1997 | A |
5711811 | Suntola et al. | Jan 1998 | A |
5730802 | Ishizumi et al. | Mar 1998 | A |
5796116 | Nakata et al. | Aug 1998 | A |
5807792 | Ilg et al. | Sep 1998 | A |
5835677 | Li et al. | Nov 1998 | A |
5846332 | Zhao et al. | Dec 1998 | A |
5855680 | Soininen et al. | Jan 1999 | A |
5879459 | Gadgil et al. | Mar 1999 | A |
5882411 | Zhao et al. | Mar 1999 | A |
5906683 | Chen et al. | May 1999 | A |
5916365 | Sherman | Jun 1999 | A |
5972430 | DiMeo, Jr. et al. | Oct 1999 | A |
5989345 | Hatano et al. | Nov 1999 | A |
6001267 | Os et al. | Dec 1999 | A |
6015590 | Suntola et al. | Jan 2000 | A |
6042652 | Hyun et al. | Mar 2000 | A |
6071572 | Mosely et al. | Jun 2000 | A |
6079356 | Umotoy et al. | Jun 2000 | A |
6099904 | Mak et al. | Aug 2000 | A |
6139700 | Kang et al. | Oct 2000 | A |
6143082 | McInerney et al. | Nov 2000 | A |
6156382 | Rajagopalan et al. | Dec 2000 | A |
6162715 | Mak et al. | Dec 2000 | A |
6174377 | Doering et al. | Jan 2001 | B1 |
6183563 | Choi et al. | Feb 2001 | B1 |
6197683 | Kang et al. | Mar 2001 | B1 |
6200893 | Sneh | Mar 2001 | B1 |
6206967 | Mak et al. | Mar 2001 | B1 |
6231672 | Choi et al. | May 2001 | B1 |
6251190 | Mak et al. | Jun 2001 | B1 |
6270572 | Kim et al. | Aug 2001 | B1 |
6270839 | Onoe et al. | Aug 2001 | B1 |
6296711 | Loan et al. | Oct 2001 | B1 |
6302965 | Umotoy et al. | Oct 2001 | B1 |
6305314 | Sneh et al. | Oct 2001 | B1 |
6306216 | Kim et al. | Oct 2001 | B1 |
6309713 | Mak et al. | Oct 2001 | B1 |
6309966 | Govindarajan et al. | Oct 2001 | B1 |
6433314 | Mandrekar et al. | Aug 2002 | B1 |
6447607 | Soininen et al. | Sep 2002 | B2 |
6452338 | Horsky | Sep 2002 | B1 |
6454860 | Metzner et al. | Sep 2002 | B2 |
6478872 | Chae et al. | Nov 2002 | B1 |
6481945 | Hasper et al. | Nov 2002 | B1 |
6511539 | Raaijmakers et al. | Jan 2003 | B1 |
6579372 | Park | Jun 2003 | B2 |
6593484 | Yasuhara et al. | Jul 2003 | B2 |
6630030 | Suntola et al. | Oct 2003 | B1 |
6630201 | Chiang et al. | Oct 2003 | B2 |
6660126 | Nguyen et al. | Dec 2003 | B2 |
6716287 | Santiago et al. | Apr 2004 | B1 |
6718126 | Lei | Apr 2004 | B2 |
6720027 | Yang et al. | Apr 2004 | B2 |
6734020 | Lu et al. | May 2004 | B2 |
6772072 | Ganguli et al. | Aug 2004 | B2 |
6773507 | Jallepally et al. | Aug 2004 | B2 |
6777352 | Tepman et al. | Aug 2004 | B2 |
6778762 | Shareef et al. | Aug 2004 | B1 |
6797108 | Wendling | Sep 2004 | B2 |
6815285 | Choi et al. | Nov 2004 | B2 |
6818094 | Yudovsky | Nov 2004 | B2 |
6821563 | Yudovsky | Nov 2004 | B2 |
6827815 | Hytros et al. | Dec 2004 | B2 |
6841200 | Kraus et al. | Jan 2005 | B2 |
6861356 | Matsuse et al. | Mar 2005 | B2 |
6866746 | Lei et al. | Mar 2005 | B2 |
6868859 | Yudovsky | Mar 2005 | B2 |
6878206 | Tzu et al. | Apr 2005 | B2 |
6881437 | Ivanov et al. | Apr 2005 | B2 |
6902624 | Seidel et al. | Jun 2005 | B2 |
6905541 | Chen et al. | Jun 2005 | B2 |
6905737 | Verplancken et al. | Jun 2005 | B2 |
6911093 | Stacey et al. | Jun 2005 | B2 |
6915592 | Guenther | Jul 2005 | B2 |
6916398 | Chen et al. | Jul 2005 | B2 |
6921062 | Gregg et al. | Jul 2005 | B2 |
6932871 | Chang et al. | Aug 2005 | B2 |
6936906 | Chung et al. | Aug 2005 | B2 |
6946033 | Tsuei et al. | Sep 2005 | B2 |
6955211 | Ku et al. | Oct 2005 | B2 |
6983892 | Noorbakhsh et al. | Jan 2006 | B2 |
6994319 | Yudovsky | Feb 2006 | B2 |
6998014 | Chen et al. | Feb 2006 | B2 |
7066194 | Ku et al. | Jun 2006 | B2 |
7085616 | Chin et al. | Aug 2006 | B2 |
7175713 | Thakur et al. | Feb 2007 | B2 |
7186385 | Ganguli et al. | Mar 2007 | B2 |
7201803 | Lu et al. | Apr 2007 | B2 |
7204886 | Chen et al. | Apr 2007 | B2 |
7222636 | Nguyen et al. | May 2007 | B2 |
7228873 | Ku et al. | Jun 2007 | B2 |
7270709 | Chen et al. | Sep 2007 | B2 |
7294208 | Guenther | Nov 2007 | B2 |
7408225 | Shinriki et al. | Aug 2008 | B2 |
20010000866 | Sneh et al. | May 2001 | A1 |
20010009140 | Bondestam et al. | Jul 2001 | A1 |
20010011526 | Doering et al. | Aug 2001 | A1 |
20010013312 | Soininen et al. | Aug 2001 | A1 |
20010014371 | Kilpi | Aug 2001 | A1 |
20010042523 | Kesala | Nov 2001 | A1 |
20010042799 | Kim et al. | Nov 2001 | A1 |
20010054377 | Lindfors et al. | Dec 2001 | A1 |
20020000196 | Park | Jan 2002 | A1 |
20020005168 | Kraus et al. | Jan 2002 | A1 |
20020007790 | Park | Jan 2002 | A1 |
20020009544 | McFeely et al. | Jan 2002 | A1 |
20020009896 | Sandhu et al. | Jan 2002 | A1 |
20020017242 | Hamaguchi et al. | Feb 2002 | A1 |
20020041931 | Suntola et al. | Apr 2002 | A1 |
20020052097 | Park | May 2002 | A1 |
20020066411 | Chiang et al. | Jun 2002 | A1 |
20020073924 | Chiang et al. | Jun 2002 | A1 |
20020076481 | Chiang et al. | Jun 2002 | A1 |
20020076507 | Chiang et al. | Jun 2002 | A1 |
20020076508 | Chiang et al. | Jun 2002 | A1 |
20020086106 | Park et al. | Jul 2002 | A1 |
20020092471 | Kang et al. | Jul 2002 | A1 |
20020094689 | Park | Jul 2002 | A1 |
20020104481 | Chiang et al. | Aug 2002 | A1 |
20020108570 | Lindfors | Aug 2002 | A1 |
20020110991 | Li | Aug 2002 | A1 |
20020115886 | Yasuhara et al. | Aug 2002 | A1 |
20020121241 | Nguyen et al. | Sep 2002 | A1 |
20020121342 | Nguyen et al. | Sep 2002 | A1 |
20020127745 | Lu et al. | Sep 2002 | A1 |
20020134307 | Choi | Sep 2002 | A1 |
20020144655 | Chiang et al. | Oct 2002 | A1 |
20020144657 | Chiang et al. | Oct 2002 | A1 |
20020145210 | Tompkins et al. | Oct 2002 | A1 |
20020146511 | Chiang et al. | Oct 2002 | A1 |
20020197856 | Matsuse et al. | Dec 2002 | A1 |
20030004723 | Chihara | Jan 2003 | A1 |
20030010451 | Tzu et al. | Jan 2003 | A1 |
20030017697 | Choi et al. | Jan 2003 | A1 |
20030023338 | Chin et al. | Jan 2003 | A1 |
20030042630 | Babcoke et al. | Mar 2003 | A1 |
20030053799 | Lei | Mar 2003 | A1 |
20030057527 | Chung et al. | Mar 2003 | A1 |
20030072913 | Chou et al. | Apr 2003 | A1 |
20030075273 | Kilpela et al. | Apr 2003 | A1 |
20030075925 | Lindfors et al. | Apr 2003 | A1 |
20030079686 | Chen et al. | May 2003 | A1 |
20030089308 | Raaijmakers | May 2003 | A1 |
20030101927 | Raaijmakers | Jun 2003 | A1 |
20030101938 | Ronsse et al. | Jun 2003 | A1 |
20030106490 | Jallepally et al. | Jun 2003 | A1 |
20030113187 | Lei et al. | Jun 2003 | A1 |
20030116087 | Nguyen et al. | Jun 2003 | A1 |
20030121469 | Lindfors et al. | Jul 2003 | A1 |
20030121608 | Chen et al. | Jul 2003 | A1 |
20030140854 | Kilpi | Jul 2003 | A1 |
20030143328 | Chen et al. | Jul 2003 | A1 |
20030143747 | Bondestam et al. | Jul 2003 | A1 |
20030153177 | Tepman et al. | Aug 2003 | A1 |
20030167612 | Kraus et al. | Sep 2003 | A1 |
20030172872 | Thakur et al. | Sep 2003 | A1 |
20030194493 | Chang et al. | Oct 2003 | A1 |
20030198740 | Wendling | Oct 2003 | A1 |
20030198754 | Xi et al. | Oct 2003 | A1 |
20030213560 | Wang et al. | Nov 2003 | A1 |
20030216981 | Tillman | Nov 2003 | A1 |
20030219942 | Choi et al. | Nov 2003 | A1 |
20030221780 | Lei et al. | Dec 2003 | A1 |
20030224107 | Lindfors et al. | Dec 2003 | A1 |
20030235961 | Metzner et al. | Dec 2003 | A1 |
20040005749 | Choi et al. | Jan 2004 | A1 |
20040011404 | Ku et al. | Jan 2004 | A1 |
20040011504 | Ku et al. | Jan 2004 | A1 |
20040013577 | Ganguli et al. | Jan 2004 | A1 |
20040014320 | Chen et al. | Jan 2004 | A1 |
20040015300 | Ganguli et al. | Jan 2004 | A1 |
20040016404 | Gregg et al. | Jan 2004 | A1 |
20040025370 | Guenther | Feb 2004 | A1 |
20040065255 | Yang et al. | Apr 2004 | A1 |
20040067641 | Yudovsky | Apr 2004 | A1 |
20040069227 | Ku et al. | Apr 2004 | A1 |
20040071897 | Verplancken et al. | Apr 2004 | A1 |
20040143370 | Lu et al. | Jul 2004 | A1 |
20040144308 | Yudovsky | Jul 2004 | A1 |
20040144309 | Yudovsky | Jul 2004 | A1 |
20040144311 | Chen et al. | Jul 2004 | A1 |
20040144431 | Yudovsky | Jul 2004 | A1 |
20040170403 | Lei | Sep 2004 | A1 |
20040203254 | Conley et al. | Oct 2004 | A1 |
20040211665 | Yoon et al. | Oct 2004 | A1 |
20040219784 | Kang et al. | Nov 2004 | A1 |
20040224506 | Choi et al. | Nov 2004 | A1 |
20040231799 | Lee et al. | Nov 2004 | A1 |
20040235285 | Kang et al. | Nov 2004 | A1 |
20040253375 | Ivanov et al. | Dec 2004 | A1 |
20050006799 | Gregg et al. | Jan 2005 | A1 |
20050059240 | Choi et al. | Mar 2005 | A1 |
20050064207 | Senzaki et al. | Mar 2005 | A1 |
20050070126 | Senzaki | Mar 2005 | A1 |
20050092247 | Schmidt et al. | May 2005 | A1 |
20050095859 | Chen et al. | May 2005 | A1 |
20050104142 | Narayanan et al. | May 2005 | A1 |
20050115675 | Tzu et al. | Jun 2005 | A1 |
20050139160 | Lei et al. | Jun 2005 | A1 |
20050139948 | Chung et al. | Jun 2005 | A1 |
20050153571 | Senzaki | Jul 2005 | A1 |
20050173068 | Chen et al. | Aug 2005 | A1 |
20050189072 | Chen et al. | Sep 2005 | A1 |
20050208217 | Shinriki et al. | Sep 2005 | A1 |
20050229969 | Nguyen et al. | Oct 2005 | A1 |
20050233156 | Senzaki et al. | Oct 2005 | A1 |
20050252449 | Nguyen et al. | Nov 2005 | A1 |
20050255243 | Senzaki | Nov 2005 | A1 |
20050257735 | Guenther | Nov 2005 | A1 |
20050271812 | Myo et al. | Dec 2005 | A1 |
20050271814 | Chang et al. | Dec 2005 | A1 |
20060018639 | Ramamurthy et al. | Jan 2006 | A1 |
20060035025 | Verplancken et al. | Feb 2006 | A1 |
20060075966 | Chen et al. | Apr 2006 | A1 |
20060156979 | Thakur et al. | Jul 2006 | A1 |
20060213557 | Ku et al. | Sep 2006 | A1 |
20060213558 | Ku et al. | Sep 2006 | A1 |
20060223286 | Chin et al. | Oct 2006 | A1 |
20060257295 | Chen et al. | Nov 2006 | A1 |
20070020890 | Thakur et al. | Jan 2007 | A1 |
20070044719 | Ku et al. | Mar 2007 | A1 |
20070067609 | Chen et al. | Mar 2007 | A1 |
20070079759 | Lee et al. | Apr 2007 | A1 |
20070089817 | Ganguli et al. | Apr 2007 | A1 |
20070095285 | Thakur et al. | May 2007 | A1 |
20070110898 | Ganguli et al. | May 2007 | A1 |
20070119370 | Ma et al. | May 2007 | A1 |
20070119371 | Ma et al. | May 2007 | A1 |
20070128862 | Ma et al. | Jun 2007 | A1 |
20070128863 | Ma et al. | Jun 2007 | A1 |
20070128864 | Ma et al. | Jun 2007 | A1 |
20070151514 | Chen et al. | Jul 2007 | A1 |
20070235085 | Nakashima et al. | Oct 2007 | A1 |
20070252500 | Ranish et al. | Nov 2007 | A1 |
20080202425 | Gelatos et al. | Aug 2008 | A1 |
20080206987 | Gelatos et al. | Aug 2008 | A1 |
Number | Date | Country |
---|---|---|
0497267 | Aug 1992 | EP |
1167569 | Jan 2002 | EP |
58098917 | Jun 1983 | JP |
04291916 | Oct 1992 | JP |
05047666 | Feb 1993 | JP |
05206036 | Aug 1993 | JP |
05234899 | Sep 1993 | JP |
05270997 | Oct 1993 | JP |
06224138 | Aug 1994 | JP |
2000212752 | Aug 2000 | JP |
2000319772 | Nov 2000 | JP |
2001020075 | Jan 2001 | JP |
WO-9617107 | Jun 1996 | WO |
WO-9901595 | Jan 1999 | WO |
WO-9965064 | Dec 1999 | WO |
WO-0054320 | Sep 2000 | WO |
WO-0079576 | Dec 2000 | WO |
WO-0117692 | Mar 2001 | WO |
WO-0136702 | May 2001 | WO |
WO-0208488 | Jan 2002 | WO |
WO-0245871 | Jun 2002 | WO |
WO-03023835 | Mar 2003 | WO |
WO-2004008491 | Jan 2004 | WO |
WO-2004106584 | Dec 2004 | WO |
Number | Date | Country | |
---|---|---|---|
20080202425 A1 | Aug 2008 | US |
Number | Date | Country | |
---|---|---|---|
60887142 | Jan 2007 | US | |
60944085 | Jun 2007 | US |