This invention relates to semiconductor device fabrication processes. More specifically, the invention relates to plasma-based chemical vapor deposition and etch processes for forming dielectric layers, particularly in high aspect ratio, narrow width recessed features.
It is often necessary in semiconductor processing to fill high aspect ratio gaps with insulating material. This is the case for shallow trench isolation, inter-metal dielectric layers, passivation layers, etc. As device geometries shrink and thermal budgets are reduced, void-free filling of narrow width, high aspect ratio (AR) spaces (e.g., AR>3:1) becomes increasingly difficult due to limitations of existing deposition processes.
The deposition of silicon dioxide (SiO2) assisted by high-density plasma chemical vapor deposition (HDP CVD)—a directional (bottom-up) CVD process—has become the preferred method for high aspect ratio gap fill. The method deposits more material at the bottom of a high aspect ratio structure than on its sidewalls. It accomplishes this by directing charged dielectric precursor species downward, to the bottom of the gap. Thus, HDP CVD is not an entirely diffusion-based (isotropic) process.
An etch-enhanced (deposition-etch-deposition) gap fill technique which involves a sequence of deposition, etch and deposition steps using an HDP reactor has been developed to maintain the opening at the top of the gap wide enough for a subsequent deposition(s) to completely fill the gap. Such processes are described, for example, in U.S. Pat. Nos. 6,335,261 and 6,030,881, the disclosures of which are incorporated herein by reference for all purposes. A typical 3-step etch-enhanced process can be described as follows: First step—Deposition 1: a partial deposition of SiO2 thin film is conducted to obtain maximum bottom-up gap fill with the gap remaining unclosed; second step—Etch: in-situ etch back is carried out to remove depositions on the top and sidewall of the trench lines and keep the mouth of the gap open enough for the next deposition step with minimum bottom-up deposition loss; and, third step—Deposition 2: deposition of SiO2 film is carried out to further fill the partially filled gap to completion. In some cases it may be necessary to conduct additional etch and deposition steps to completely fill the gap.
The etch component of these etch-enhanced gap fill processes typically uses a fluorine-based etchant, such as NF3, CF4 or C2F6, etc., to achieve a fast etch rate. However, the application of those etchants may contaminate the dielectric (e.g., STI) film with foreign atoms, e.g., C, N and F, causing issues in the subsequent integration processes and device degradation.
Therefore, an etch-enhanced gap fill process that avoided the use of etchants which tend to contaminate the deposited dielectric film would be desirable.
The present invention addresses this need by providing chemical vapor deposition and plasma etch back processes that replace fluorine-based etchants with a halogen (e.g., fluorine)-free etch chemistry that combines hydrogen (H2) and a Noble gas, e.g., He, Ne or Ar. In particular, the invention provides a high density plasma chemical vapor etch-enhanced gap fill process using hydrogen as an etchant that can effectively fill high aspect ratio (typically at least 3:1, for example 6:1, and up to 10:1 or higher), narrow width (typically sub 0.11 micron, for example 0.1 micron or less) gaps while reducing or eliminating dielectric contamination by etchant chemical species.
Suitable plasma reactors, e.g., Novellus Speed, with inductively coupled plasma (ICP) sources are available to accomplish both deposition and etch steps of the etch-enhanced gap fill process of the present invention in a single plasma reactor chamber. The deposition part of the process may involve the use of any suitable high density plasma chemical vapor deposition (HDP CVD) chemistry.
The process achieves an enhanced etch rate relative to hydrogen-only etch chemistry, and results in the formation of a dielectric film free of contamination by etchant chemical species.
In one aspect, the invention pertains to a method of filling gaps on a semiconductor substrate. The method involves partially filling a gap on a semiconductor substrate with dielectric using a high density plasma chemical vapor deposition process, partially removing dielectric deposited in the gap from the gap opening by a plasma etch back process conducted with a halogen-free etch process chemistry consisting essentially of hydrogen (H2) and Noble process gases, and further filling of the partially filled gap by HDP CVD.
In another aspect, the invention pertains to a method of etching dielectric on a semiconductor substrate. The method involves partially removing dielectric on the substrate by a plasma etch back process conducted with a halogen-free etch process chemistry consisting essentially of hydrogen (H2) and Noble process gases.
These and other features and advantages of the present invention are described below where reference to the drawings is made.
Reference will now be made in detail to specific embodiments of the invention. Examples of the specific embodiments are illustrated in the accompanying drawings. While the invention will be described in conjunction with these specific embodiments, it will be understood that it is not intended to limit the invention to such specific embodiments. On the contrary, it is intended to cover alternatives, modifications, and equivalents as may be included within the spirit and scope of the invention as defined by the appended claims. In the following description, numerous specific details are set forth in order to provide a thorough understanding of the present invention. The present invention may be practiced without some or all of these specific details. In other instances, well known process operations have not been described in detail in order not to unnecessarily obscure the present invention.
Introduction
The present invention relates to chemical vapor deposition and plasma etch back processes that replace fluorine-based etchants with hydrogen and one or more Noble gases as etch stage process gases. In particular, the invention provides a high density plasma chemical vapor etch-enhanced gap fill process using hydrogen as the etchant that can effectively fill high aspect ratio (typically at least 3:1, for example 6:1, and up to 10:1 or higher), narrow width (typically sub 0.11 micron, for example 0.1 micron or less) gaps while reducing or eliminating dielectric contamination by etchant chemical species and increasing etch rate relative to H2 alone plasma etch.
Suitable plasma reactors, e.g., Novellus Speed, with inductively coupled plasma (ICP) sources are available to accomplish both deposition and etch steps of the etch-enhanced gap fill process of the present invention in a single plasma reactor chamber. The gap fill process of the present invention may also be accomplished in a plurality of processing chambers. The deposition part of the process may involve the use of any suitable high density plasma chemical vapor deposition (HDP CVD) chemistry.
The process results in the formation of a dielectric film free of contamination by etchant chemical species.
Etch-Enhanced Gap Fill Process
The present invention, while applicable to the filling of any gap requiring dielectric fill, is particularly suited to gap fill of high aspect ratio, narrow width gaps. For example, the gap 100 may have a high aspect ratio, for example about 6:1 and a narrow width, for example about 1000 Å.
In an initial step in a multi-step gap fill process in accordance with the present invention, the gap 100 is partially filled with a dielectric 110 deposited by high density plasma (HDP) chemical vapor deposition (CVD) process, as shown in
The deposition process gas will have a particular composition represented by flow rates of the constituent gases in units of standard cubic centimeter per minute (sccm). The process gas will include a precursor for the deposition layer. If the dielectric is a silicon-containing dielectric, like silicon dioxide (SiO2), then the process gas will include a silicon-bearing compound. Examples of silicon-containing dielectric precursors are well known in the art and include SiH4, SiF4, Si2H6, TEOS (tetraethyl orthosilicate), TMCTS (tetramethyl-cyclotetrasiloxane), OMCTS (octamethyl-cyclotetrasiloxane), methyl-silane, dimethyl-silane, 3MS (trimethylsilane), 4MS (tetramethylsilane), TMDSO (tetramethyl-disiloxane), TMDDSO (tetramethyl-diethoxyl-disiloxane), DMDMS (dimethyl-dimethoxyl-silane) and mixtures thereof. Where the purity of the dielectric is an issue, inorganic, non-fluorine-containing precursors for SiO2, such as SiH4 and Si2H6, are preferred. During deposition, the process decomposes the silicon-containing reactant to form a silicon-containing gas and plasma phase species, which can react on the surface of the substrate.
The process gas will also generally include a carrier gas. The carrier gas may be an inert gas, such as He, Ar and/or other noble gases. Or the carrier gas may be or include hydrogen (H2).
Oxygen to form the silicon dioxide or other dielectric material may be provided by the silicon-containing precursor itself or from another process gas such as oxygen (O2), nitric oxide (NO), and/or nitrous oxide (N2O). Again, where the purity of the dielectric is an issue, oxygen (O2) is the preferred oxygen source.
Typical flow rate ranges for deposition process gases of the present invention are listed below.
Generally, other oxygen and silicon-containing compounds can be substituted for those listed in this table. Depending upon the atom counts in the precursor gases, the flow rate ranges may have to be changed. While there are no precise rules for modifying flow rates as a function of molecular structure, generally the flow rate of the silicon-containing precursor may be reduced by a factor corresponding to the number of silicon atoms in the molecule. So, for example, if the molecule contains two silicon atoms, one may expect to reduce the flow rate of the silicon-containing precursor to a level of between about 5 and 150 sccm.
Reactor pressure is held at a value necessary to sustain the high-density plasma. Preferably the process vessel is maintained at a pressure of at most about 100 mTorr. In some cases, the process chamber pressure is maintained below 1 mTorr. For many applications, however, the pressure is maintained between about 1 and 100 mTorr; most preferably between about 1 and 30 mTorr.
The temperature within the process vessel should be maintained sufficiently high to ensure that the dielectric deposition reaction proceeds efficiently. Hence, the temperature preferably resides at values between about 30 and 1000° C. This temperature will vary depending upon the types of precursors employed in the reaction. Further, the temperature may be limited by process constraints, such as thermal budget limitations that preclude temperatures above 700-750° C. Such constraints become increasingly common with advanced technologies and corresponding smaller feature sizes. For such applications, the process temperature is preferably maintained between about 30 and 750° C. In particularly preferred embodiments, the substrate temperature is maintained between about 300 and 700° C., even more preferably between about 350 and 650° C.
As indicated, to control the substrate temperature, the reactor may supply a heat transfer gas between a surface of the substrate and a surface of the substrate holder on which the substrate is supported during film deposition. The heat transfer gas may include at least one of helium and argon. The back-side helium pressure is set by the temperature requirements of the process (a typical range being between 0-15 Torr).
For some applications, it may be desirable to preheat the wafer to a pre-specified relatively low temperature and then gradually raise the temperature. This allows for isothermal operation. The goal is to start the deposition and then maintain the wafer temperature within a narrow range during the entire deposition process.
The low frequency power applied to the induction coil typically varies from 1 kW to 20 kW, and the high frequency power (for biasing the wafer) typically varies from 0.5 kW to 10 kW depending on the substrate size (e.g., 200 or 300 mm diameter) and the requirements of the specific process being used.
The power source applied to the induction coil and substrate electrode is typically a radio frequency source. Applying radio frequency bias to the substrate involves supporting the substrate on a substrate holder having an electrode supplying a radio frequency bias to the substrate. For many embodiments, the radio frequency bias applied to the substrate is at the frequency range of between about 100 kHz and 27 MHz. The power source applied to the induction coil typically has a frequency range between about 300 kHz and 1 MHz. In a preferred embodiment, the deposition process chemistry is as follows:
The low frequency coil is powered at 3000 W and the high frequency substrate electrode is powered at 800 W. Further details of suitable HDP CVD deposition process gas chemistries are provided below.
The HDP CVD deposition results in beneficial filling of the trench from the bottom 104 up. However, there is still some problematic top and sidewall deposition resulting in narrowing of the entry region 108 of the gap 100 by the formation of an overhang 109 and the formation of a dielectric peak (the so-called “top-hat” feature) 109 on either side of the gap opening. This results from the non-directional deposition reactions of neutral species in the plasma reactor and from sputtering/redeposition processes. The overhang 109 and top-hat 111 features exacerbate the difficulties of filling the high aspect ratio gap.
To address these problems, following this initial deposition stage of the process, the detrimental overhang 109 is removed and the top-hat 111 substantially reduced in an etch back stage of the process to facilitate further void free filling of the trench in a subsequent deposition stage. In a preferred embodiment, the etch back process is carried out in the same reactor chamber as the deposition.
Halogen-Free H2/Noble Gas Plasma Etch Chemistry
According to the present invention, a combination of hydrogen (H2) and a Noble gas (e.g., Ar; and/or He or Ne) is used as an etching agent to replace conventional F-containing etchants in a plasma etch back stage of the gap fill process. The halogen-free etch chemistry process gases are introduced into the deposition chamber and ionized by source plasma power in the chamber. While it had previously been believed that Noble gases acted merely as inert carriers in many implementations of plasma etchs, it has now been recognized that Noble gases, including helium, and in particular, argon, are active participants in etchant chemistry. The ionized hydrogen and Noble gas acts as an etchant for deposited dielectric film on all exposed surfaces of the substrate 102 on which the gap 100 is being filled. In accordance with the present invention, H2 and Noble gas (e.g., Ar, He, Ne) are the only etchants in the etch process chemistry; the etch process chemistry may also generally includes a carrier gas, e.g., nitrogen, but no other etchant (e.g., F-based etchant) is used.
In the plasma etch back stage, the wafer is typically biased and exposed to a plasma, for example, a radio frequency based inductively coupled plasma, having H2/Ar etchant chemistry. As shown in
The chuck may be biased with a power range of about 500 to 7000 W. Biasing the chuck imparts some directionality to the etch plasma towards the wafer on the biased chuck. Thus, while the etch process of the present invention has a dominant isotropic character, it does favor the biased wafer/chuck. Increase in bias power enhances etch rate, but does not significantly alter the isotropic characteristic of H2/Noble gas etch. Bottom-up deposition is observed even with high bias power H2Noble gas etch processing in accordance with the invention.
The etch plasma chemistry includes only hydrogen (H2) and one or more Noble gases as etchants. The Noble gas etch plasma chemistry may consist of H2 with one or more of He, Ar or Ne, with Ar being preferred in many instances. O2 may optionally be included in the etch chemistry, but should only be used to the extent necessary to achieve plasma stability since its addition enhances the redeposition effect. N2 may also be used as a carrier gas.
Typical process parameter ranges for a halogen-free plasma etch process in accordance with the present invention are listed as follows:
In a specific embodiment, An H2/Ar-based etch chemistry is preferred. In this embodiment of the invention the plasma etch process chemistry and reactor conditions can be as follows:
In another specific embodiment, An H2/He-based etch chemistry is preferred. In this embodiment of the invention the plasma etch process chemistry and reactor conditions can be as follows:
The conditions are preferably set so that the etch is selective for the HDP CVD deposited dielectric (e.g., SiO2) relative to the silicon nitride barrier layer lining the trench and the hard mask (the pad nitride on the substrate surface surrounding the gap opening) so that neither is exposed and clipped by the etch. Adjustment of the process selectivity is within the skill in the art given the process parameters and description provided herein.
Following the biased etch back stage, an additional HDP CVD deposition is performed in order to further fill the gap 100 with dielectric 110, as shown in
Without limiting the invention described and claimed herein, some beneficial characteristics of the use of a halogen-free hydrogen as an etchant in accordance with the present invention are illustrated with reference to
The H2/Noble gas etchant chemistry has the important advantage that there is virtually no contamination of the dielectric with C, N and F from etching chemicals in an etch-enhanced gap fill process.
Another advantageous characteristic of the halogen-free H2Noble gas plasma etch-enhanced gap fill process of the invention is that the etch rate is increased relative to an H2 only plasma etch. This is illustrated in
Thus, this invention provides an etch-enhanced HDP gap fill (e.g., STI) process with an in situ high throughput etch step without C, N and F contamination.
Implementation: Plasma Processing Reactor
Various plasma reactor designs are suitable for use with this invention. The particular design is not critical to this invention. It merely needs to support HDP CVD dielectric layer formation and etch back on appropriate substrates. Examples of suitable reactors include the Novellus SPEED reactor, available from Novellus Systems, Inc. of San Jose, Calif., and the Ultima reactor, available from Applied Materials, Inc. of Santa Clara, Calif.
The principal components of most suitable reactors include a reaction chamber, a process gas delivery system, a support for the substrate, one or more electrodes or radio frequency power source coupled to an induction coil to generate an inductively coupled plasma, and a bias source for the substrate. A temperature control system is typically used to heat the substrate. Suitable plasma processing reactors and described, for example, in U.S. Pat. Nos. 5,346,578, 5,405,480 and 5,605,599, the disclosures of which are incorporated by reference herein in their entirety and for all purposes.
Within the reactor, a wafer pedestal 607 supports a substrate 609. The pedestal typically includes a chuck 608 to hold the substrate in place during the deposition reaction. The chuck may be an electrostatic chuck, a mechanical chuck or various other types of chuck as are available for use in the industry and/or research.
A heat transfer subsystem including a line 611 for supplying a heat transfer gas controls the temperature of substrate 609. In some embodiments, the heat transfer fluid comprises at least one of helium and argon gas. The heat transfer fluid is supplied to a space 613 between the surface of the substrate and a surface of the chuck.
A “high frequency” RF source 615 serves to electrically bias substrate 609 and draw charged precursor species onto the substrate for the deposition or etch reactions. Electrical energy from source 615 is coupled to substrate 609 via an electrode or capacitive coupling, for example. Note that the bias applied to the substrate need not be an RF bias. Other frequencies and DC bias may be used as well. In a specific embodiment, source 615 supplies a radio frequency bias to the substrate with a power ranges from 0.5 kW to 10 kW.
The process gases are introduced via one or more chamber inlets 617. The gases may be premixed or not. A source of hydrogen gas provides hydrogen for the deposition and etch process chemistry. A source of Noble gas (e.g., one or more of Ar, He or Ne) provides Noble gas for the etch process chemistry. Other sources of dielectric precursor gases and carrier gases are also provided. Preferably, the process gas is introduced through a gas supply inlet mechanism including orifices. The gas or gas mixture may be introduced from a primary gas ring, which may or may not direct the gas toward the substrate surface. In this embodiment, a ring inlet(s) 618 is connected to the primary gas ring 619 to supply gas or gas mixture into the chamber via the chamber inlets 617. This arrangement is further illustrated in the horizontal cross-section of
The process gas exits the chamber 603 via an outlet or outlets 620. A vacuum pump (e.g., a turbomolecular pump) or pumps 622 typically draws the gas out and maintains a suitably low pressure within the reactor.
As noted above, the gap fill process of the present invention is preferably accomplished in a single reactor process chamber, but it may also be accomplished in a plurality of processing chambers. When more than one processing chamber is used, a pressure controlled transfer module should be used to transfer the wafers from one chamber to another. Such transfer modules and procedures are known to those of skill in the art.
Process Parameters
A deposition process begins with an electrical subsystem applying electrical energy of appropriate power and frequency to one or more electrodes of a process chamber of the reactor. The power and frequency are chosen to generate a high density plasma in the chamber, given the process gas concentration, pressure, and other process parameters. Providing the substrate to the reactor may involve clamping the substrate to a pedestal or other support in the chamber. For this purpose, an electrostatic or mechanical chuck may be employed.
After the wafer is appropriately situated in the chamber, a gap on the substrate is partially filled by HDP CVD deposition of dielectric (603). The process adjusts the substrate temperature to a level promoting the deposition of the dielectric layer. Typically, this temperature is between about 30-1000° C. (more preferably about 300 to 680° C., for example 450-550° C.). The temperature control mechanism may gradually raise the temperature during deposition or it may preheat the wafer to first drive out certain interfering species. During deposition, the temperature may be maintained by supplying a heat transfer gas between a back surface of the substrate and a surface of the substrate holder on which the substrate is supported during the film growth operation.
The reactor system introduces a process gas to the reaction chamber via an inlet. The process gas includes dielectric precursor species such as high vapor pressure silicon-containing compounds. Molecular oxygen or another oxygenated compound will often be present. A carrier gas is also generally present. The carrier gas may be an inert carrier gas such as helium. However, in high aspect ratio gap fill applications the carrier gas preferably is or includes molecular hydrogen (H2) which inhibits precursor dissociation and promotes bottom-up gap fill. All the process gas components are introduced at specified flow rates.
An electrical subsystem applies a bias to the substrate, to thereby direct charged precursor species from the plasma onto the substrate and grow a dielectric film. Note that the substrate itself serves as an electrode here. Its bias accelerates charged species to it. Typically, the substrate electrode is powered by a high frequency RF bias and the induction coil is powered by a lower frequency RF source.
Dielectric is deposited in the gap or gaps on the substrate to a desired thickness, generally at the point where the overhang that forms at the gap entry point prevents further effective filling of the gap (603).
After finishing the deposition step, the flow of deposition chemistry is turned off and the hydrogen (H2) and Noble gas (e.g., Ar/He/Ne) etchant chemistry is introduced to the reaction chamber via an inlet. The H2 and Noble gas etchant gases should dissociate at a controlled rate consistent with isotropic etching. In a specific embodiment, an H2/Ar-based etch chemistry is typically used. Molecular oxygen and/or nitrogen may also be present in the etchant chemistry, but should be minimized. All the process gas components are introduced at specified flow rates within the parameters noted above. In a specific embodiment, the etch is conducted using an inductively coupled plasma source in the reactor. The RF bias power applied to the substrate in the reactor can be adjusted to between about 500 and 5000 W, for example 3000 W. It should be noted that the inductively coupled plasma (ICP) etch may alternatively be accomplished by a downstream microwave plasma etch. The etch back process preferentially removes dielectric overhang and top-hat features at the gap opening thereby decreasing the gap's aspect ratio and facilitating further filling in subsequent deposition processing.
Following the etch, etch process chemistry flows are turned off and further deposition process for filling the remaining gap is performed by introducing the deposition process gases into the reactor (607). The etch back and deposition process (605-607) is then repeated until the gap is filled (609). For a gap with about a 6:1 aspect ratio and about a 1000 Å width, three to five, for example four, iterations of the etch back and deposition steps are typical to obtain void free filling of the gap.
Substrates and Dielectric Materials
The above-described processes and apparatuses may deposit dielectric on any type of substrate that requires thin dielectric layers. Often, the substrate will be a semiconductor wafer having gaps in need of dielectric filling. The invention is not, however, limited to such applications. It may be employed in a myriad of other fabrication processes such as for fabricating flat panel displays.
As indicated above, this invention finds particular value in integrated circuit fabrication. The gap filling processes are performed on partially fabricated integrated circuits employing semiconductor substrates. In specific examples, the gap filling processes of this invention are employed to form shallow trench isolation (STI), pre-metal dielectric (PMD), inter-metal layer dielectric (ILD) layers, passivation layers, etc.
As indicated, the invention can effectively fill gaps having widths of 0.15 microns or less, for example 0.1 micron or less, and aspect ratios of 3:1 or greater, for example 5:1, 6:1, or even 10:1 or greater. More aggressive structures having, e.g., greater aspect ratios and smaller widths may also be used. In one example the gap width is 0.15 micrometers or less, e.g., between 0.11 micrometer and 0.08 micrometer.
The dielectrics employed to fill those gaps will often be a silicon oxide such as silicon dioxide, silicon oxynitride, silicon oxyfluoride, and doped variants of each of these. Therefore, the scope of the invention includes at least phosphorus-doped, boron/phosphorus-doped oxides. As indicated, the dielectric may also be a phosphorus- and boron-doped silicon oxide glass (BPSG).
While the invention is primarily described herein with reference to an etch-enhanced multi-step gap fill process, it should be understood that the halogen-free H2/Noble gas plasma etch may also be conducted independent of the other steps of the gap fill process. For example, the halogen-free H2/Noble gas plasma etch may be applied to etch a silicon-based dielectric in any appropriate context.
While this invention has been described in terms of a few preferred embodiments, it should not be limited to the specifics presented above. Many variations on the above-described preferred embodiments, may be employed. Therefore, the invention should be broadly interpreted with reference to the following claims.
This application is a continuation-in-part of U.S. patent application Ser. No. 10/733,858 filed Dec. 10, 2003 now U.S. Pat. No. 7,163,896, titled BIASED H2 ETCH PROCESS IN DEPOSITION-ETCH-DEPOSITION GAP FILL; and U.S. patent application Ser. No. 11/159,834 filed Jun. 22, 2005 now U.S. Pat. No. 7,344,996, titled HELIUM-BASED ETCH PROCESS IN DEPOSITION-ETCH-DEPOSITION GAP FILL. These prior applications are incorporated herein by reference in their entirety for all purposes.
Number | Name | Date | Kind |
---|---|---|---|
4361461 | Chang | Nov 1982 | A |
5129958 | Nagashima et al. | Jul 1992 | A |
5227191 | Nagashima | Jul 1993 | A |
5246885 | Braren et al. | Sep 1993 | A |
5252178 | Moslehi | Oct 1993 | A |
5270264 | Andideh et al. | Dec 1993 | A |
5282925 | Jeng et al. | Feb 1994 | A |
5342801 | Perry et al. | Aug 1994 | A |
5385857 | Solo de Zaldivar | Jan 1995 | A |
5494854 | Jain | Feb 1996 | A |
5516729 | Dawson et al. | May 1996 | A |
5532516 | Pasch et al. | Jul 1996 | A |
5621241 | Jain | Apr 1997 | A |
5622894 | Jang et al. | Apr 1997 | A |
5636320 | Yu et al. | Jun 1997 | A |
5641545 | Sandhu | Jun 1997 | A |
5702982 | Lee et al. | Dec 1997 | A |
5705419 | Perry et al. | Jan 1998 | A |
5711998 | Shufflebotham | Jan 1998 | A |
5789818 | Havemann | Aug 1998 | A |
5834068 | Chern et al. | Nov 1998 | A |
5851344 | Xu et al. | Dec 1998 | A |
5858876 | Chew | Jan 1999 | A |
5869902 | Lee et al. | Feb 1999 | A |
5872058 | Van Cleemput et al. | Feb 1999 | A |
5897370 | Joshi et al. | Apr 1999 | A |
5910020 | Yamada | Jun 1999 | A |
5911113 | Yao et al. | Jun 1999 | A |
5913140 | Roche et al. | Jun 1999 | A |
5920792 | Lin | Jul 1999 | A |
5937323 | Qrezyk et al. | Aug 1999 | A |
5953635 | Andideh | Sep 1999 | A |
5962923 | Xu et al. | Oct 1999 | A |
5963840 | Xia et al. | Oct 1999 | A |
5968610 | Liu et al. | Oct 1999 | A |
5972192 | Dubin et al. | Oct 1999 | A |
6027663 | Martin et al. | Feb 2000 | A |
6030881 | Papasouliotis et al. | Feb 2000 | A |
6037018 | Jang et al. | Mar 2000 | A |
6077451 | Takenaka et al. | Jun 2000 | A |
6077574 | Usami | Jun 2000 | A |
6100205 | Liu et al. | Aug 2000 | A |
6106678 | Shufflebotham et al. | Aug 2000 | A |
6124211 | Butterbaugh et al. | Sep 2000 | A |
6136703 | Vaartstra | Oct 2000 | A |
6149779 | Van Cleemput | Nov 2000 | A |
6184158 | Shufflebotham et al. | Feb 2001 | B1 |
6200412 | Kilgore et al. | Mar 2001 | B1 |
6211065 | Xi et al. | Apr 2001 | B1 |
6232196 | Raaijmakers et al. | May 2001 | B1 |
6265269 | Chen et al. | Jul 2001 | B1 |
6277764 | Shin et al. | Aug 2001 | B1 |
6331494 | Olson et al. | Dec 2001 | B1 |
6335261 | Natzle et al. | Jan 2002 | B1 |
6395150 | Van Cleemput et al. | May 2002 | B1 |
6400023 | Huang | Jun 2002 | B2 |
6410446 | Tsai et al. | Jun 2002 | B1 |
6451705 | Trapp et al. | Sep 2002 | B1 |
6479361 | Park | Nov 2002 | B1 |
6479396 | Xu et al. | Nov 2002 | B1 |
6486081 | Ishikawa et al. | Nov 2002 | B1 |
6500728 | Wang | Dec 2002 | B1 |
6531377 | Knorr et al. | Mar 2003 | B2 |
6566229 | Hong et al. | May 2003 | B2 |
6569777 | Hsu et al. | May 2003 | B1 |
6596653 | Tan et al. | Jul 2003 | B2 |
6596654 | Bayman et al. | Jul 2003 | B1 |
6599829 | Smith et al. | Jul 2003 | B2 |
6617207 | Kiryu et al. | Sep 2003 | B1 |
6642105 | Kim et al. | Nov 2003 | B2 |
6706541 | Toprac et al. | Mar 2004 | B1 |
6737334 | Ho et al. | May 2004 | B2 |
6787483 | Bayman et al. | Sep 2004 | B1 |
6794290 | Papasouliotis et al. | Sep 2004 | B1 |
6808748 | Kapoor et al. | Oct 2004 | B2 |
6812043 | Bao et al. | Nov 2004 | B2 |
6821905 | Pan et al. | Nov 2004 | B2 |
6845745 | Papasouliotis et al. | Jan 2005 | B2 |
6846391 | Papasouliotis et al. | Jan 2005 | B1 |
6852639 | Rudolph et al. | Feb 2005 | B2 |
6867086 | Chen et al. | Mar 2005 | B1 |
6903031 | Karim et al. | Jun 2005 | B2 |
6958112 | Karim et al. | Oct 2005 | B2 |
7001854 | Papasouliotis et al. | Feb 2006 | B1 |
7067440 | Bayman et al. | Jun 2006 | B1 |
7078312 | Sutanto et al. | Jul 2006 | B1 |
7122485 | Papasouliotis et al. | Oct 2006 | B1 |
7135409 | Komagata | Nov 2006 | B2 |
7148155 | Tarafdar et al. | Dec 2006 | B1 |
7163896 | Zhu et al. | Jan 2007 | B1 |
7176039 | Papasouliotis et al. | Feb 2007 | B1 |
7211525 | Shanker et al. | May 2007 | B1 |
7217658 | Bayman et al. | May 2007 | B1 |
20010019903 | Shufflebotham et al. | Sep 2001 | A1 |
20010044203 | Huang et al. | Nov 2001 | A1 |
20020052119 | Van Cleemput | May 2002 | A1 |
20020084257 | Bjorkman et al. | Jul 2002 | A1 |
20020179570 | Mathad et al. | Dec 2002 | A1 |
20020187657 | Morozumi | Dec 2002 | A1 |
20030003244 | Rossman | Jan 2003 | A1 |
20030003682 | Moll et al. | Jan 2003 | A1 |
20030087506 | Kirchhoff | May 2003 | A1 |
20030165632 | Lin et al. | Sep 2003 | A1 |
20030203652 | Bao et al. | Oct 2003 | A1 |
20030207580 | Li et al. | Nov 2003 | A1 |
20040002894 | Kocher | Jan 2004 | A1 |
20040020894 | Williams et al. | Feb 2004 | A1 |
20040058549 | Ho et al. | Mar 2004 | A1 |
20040082181 | Doan et al. | Apr 2004 | A1 |
20040110390 | Takagi et al. | Jun 2004 | A1 |
20040241342 | Karim et al. | Dec 2004 | A1 |
20050074946 | Chu et al. | Apr 2005 | A1 |
20050130411 | Bao et al. | Jun 2005 | A1 |
20050136576 | Ishihara et al. | Jun 2005 | A1 |
20050136686 | Kim et al. | Jun 2005 | A1 |
20050250346 | Schmitt | Nov 2005 | A1 |
Number | Date | Country |
---|---|---|
2003-031649 | Jan 2003 | JP |
Number | Date | Country | |
---|---|---|---|
Parent | 10733858 | Dec 2003 | US |
Child | 11366220 | US | |
Parent | 11159834 | Jun 2005 | US |
Child | 10733858 | US |