US20040224533A1 - Method for increasing polysilicon granin size - Google Patents
Method for increasing polysilicon granin size Download PDFInfo
- Publication number
- US20040224533A1 US20040224533A1 US10/431,120 US43112003A US2004224533A1 US 20040224533 A1 US20040224533 A1 US 20040224533A1 US 43112003 A US43112003 A US 43112003A US 2004224533 A1 US2004224533 A1 US 2004224533A1
- Authority
- US
- United States
- Prior art keywords
- furnace
- flow
- nitrogen
- grain size
- polysilicon
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
Links
- 238000000034 method Methods 0.000 title claims abstract description 16
- 229910021420 polycrystalline silicon Inorganic materials 0.000 title claims abstract description 16
- 229920005591 polysilicon Polymers 0.000 title claims abstract description 15
- 102000007345 Chromogranins Human genes 0.000 title 1
- 108010007718 Chromogranins Proteins 0.000 title 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 28
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 14
- 230000008021 deposition Effects 0.000 claims abstract description 6
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 4
- 229910052814 silicon oxide Inorganic materials 0.000 claims abstract description 3
- 239000004065 semiconductor Substances 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 3
- 239000007789 gas Substances 0.000 description 16
- 235000012431 wafers Nutrition 0.000 description 15
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 5
- 238000000151 deposition Methods 0.000 description 5
- 229910052710 silicon Inorganic materials 0.000 description 5
- 239000010703 silicon Substances 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical group [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 238000005229 chemical vapour deposition Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- BLRPTPMANUNPDV-UHFFFAOYSA-N Silane Chemical compound [SiH4] BLRPTPMANUNPDV-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000005137 deposition process Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000004767 nitrides Chemical class 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000000059 patterning Methods 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/02—Pretreatment of the material to be coated
- C23C16/0209—Pretreatment of the material to be coated by heating
- C23C16/0218—Pretreatment of the material to be coated by heating in a reactive atmosphere
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/22—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the deposition of inorganic material, other than metallic material
- C23C16/24—Deposition of silicon only
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01L—SEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
- H01L21/00—Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
- H01L21/02—Manufacture or treatment of semiconductor devices or of parts thereof
- H01L21/04—Manufacture or treatment of semiconductor devices or of parts thereof the devices having potential barriers, e.g. a PN junction, depletion layer or carrier concentration layer
- H01L21/18—Manufacture or treatment of semiconductor devices or of parts thereof the devices having potential barriers, e.g. a PN junction, depletion layer or carrier concentration layer the devices having semiconductor bodies comprising elements of Group IV of the Periodic Table or AIIIBV compounds with or without impurities, e.g. doping materials
- H01L21/28—Manufacture of electrodes on semiconductor bodies using processes or apparatus not provided for in groups H01L21/20 - H01L21/268
- H01L21/283—Deposition of conductive or insulating materials for electrodes conducting electric current
- H01L21/285—Deposition of conductive or insulating materials for electrodes conducting electric current from a gas or vapour, e.g. condensation
- H01L21/28506—Deposition of conductive or insulating materials for electrodes conducting electric current from a gas or vapour, e.g. condensation of conductive layers
- H01L21/28512—Deposition of conductive or insulating materials for electrodes conducting electric current from a gas or vapour, e.g. condensation of conductive layers on semiconductor bodies comprising elements of Group IV of the Periodic Table
- H01L21/28525—Deposition of conductive or insulating materials for electrodes conducting electric current from a gas or vapour, e.g. condensation of conductive layers on semiconductor bodies comprising elements of Group IV of the Periodic Table the conductive layers comprising semiconducting material
Definitions
- the present invention relates generally to semiconductor device manufacturing, and, more particularly, to a method for controlling device speed by adjusting polysilicon grain size.
- wafers such as silicon wafers
- the processing steps include depositing or forming layers, patterning the layers, and removing portions of the layers to define features on the wafer.
- One such process used to form the layers is a procedure known as chemical vapor deposition (CVD), where reactive gases are introduced into a vessel containing the semiconductor wafers. The reactive gases facilitate a chemical reaction that causes a layer to form on the wafers.
- CVD chemical vapor deposition
- One deposition process involves the formation of polycrystalline silicon (polysilicon) layers on the wafer by decomposing SiH 4 molecules to Si atoms, which in turn combine to form Si grains, or “polysilicon.”.
- polysilicon polycrystalline silicon
- Polysilicon furnaces both within and without a nitrogen box may play an important role in controlling polysilicon grain size, thereby governing device speed.
- An important consideration is the actual N 2 (nitrogen) flow which continuously treats the silicon wafer surface in the N 2 box.
- N 2 nitrogen
- the present invention relates to a method for increasing the grain size of a polysilicon layer in a furnace, which includes exposing a silicon oxide wafer in a deposition chamber to an amount, effective for the purpose, of nitrogen at a flow rate of at least about 240 standard liters per minute (slm).
- FIG. 1 is a graph of the effect of increased nitrogen flow in a furnace.
- FIG. 2 is a graph of polysilicon film volume fraction versus control wafer resistivity in a furnace.
- a maximizing of polysilicon grain size results in an increase in device speed.
- an oxide wafer i.e., a surface capped with a thin O 2 boundary layer
- the wafer was exposed to bulk N 2 flow, with absorbed O 2 being removed as a result.
- absorbed oxygen bonded with oxide molecules, and the oxygen depletion site was filled with N 2 molecules.
- a prototypical furnace includes four tube furnaces, which are used for curing polymers, sintering, and growing oxides and nitrides on silicon wafers. There are also four gas flow timers for the furnace. The orientation of the timers matches the orientation of the tubes with which they correspond; with a maximum time of twelve hours, the flow timers are used to control the time the gas flows in the furnaces. The minimum amount of time for the process to function correctly is about two hours. When the timer reaches zero, the gas discontinues to flow.
- each of the flow meters There are three flow meters located just below the gas flow timers. Beneath each of the flow meters are two flow meter valves. The cut-off valves are the valves closest to the flow meters. The handles are at a 90° angle when the flow meters are closed. When the handles are parallel with the flow meter, they are open. The lower valves are the needle valves, which control the gas flow into the flow meters. To the right of the flow meters is the three-way valve. This valve controls which gas flows into the middle flow meter (tube 2 ). The two selectable gases are oxygen and nitrogen. The narrow, pointed end of the handle points to the gas that is being used. When tube 2 is not in use, the valve is turned to the off position.
- the oxygen cylinder in the chase behind the furnace is on. Note that in order to check that the gas pressure is sufficient, the cylinder gauge closest to the cylinder is read. The gauge to the left indicates the gas line pressure; it is set to approximately 25 psi.
- the furnace temperature is controlled by a programmable temperature control unit. There is one control for every furnace; there are programmable temperature controllers on each of the temperature control units. These controllers monitor each of the furnace zone heaters, and allow the programming of several process steps. Thus, in order to operate the furnaces, the following steps are performed: (1) set the appropriate atmosphere, (2) load the furnace, (3) set the temperature program, (4) run the process, (5) end the run.
- the first step in setting the atmosphere is to set the gas flow timer to the length of the particular run. This prevents the waste of gas in the system.
- the next step is to set the flow of gas using the flow meters.
- the first step in loading the furnace is to place a sample into a quartz boat, which is found in the nitrogen box next to the furnace.
- the cap on the end of the tube is removed, and the boat placed just inside the opening.
- a metal rod is used in order to carefully push the boat to the middle of the furnace tube.
- the desired temperature in degrees Celsius is set for the controllers, and the temperature cooled to about room temperature when the program is done. In order to remove the boat from the furnace, the loading procedure is reversed.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Physics & Mathematics (AREA)
- Condensed Matter Physics & Semiconductors (AREA)
- General Physics & Mathematics (AREA)
- Manufacturing & Machinery (AREA)
- Computer Hardware Design (AREA)
- Microelectronics & Electronic Packaging (AREA)
- Power Engineering (AREA)
- Formation Of Insulating Films (AREA)
Abstract
The present invention relates to a method for increasing the grain size of a polysilicon layer, which includes exposing a silicon oxide wafer in a deposition chamber to an amount, effective for the purpose, of nitrogen at a flow rate of at least about 240 standard liters per minute (slm).
Description
- The present invention relates generally to semiconductor device manufacturing, and, more particularly, to a method for controlling device speed by adjusting polysilicon grain size.
- In the manufacture of semiconductor devices, wafers, such as silicon wafers, are subjected to a number of processing steps. The processing steps include depositing or forming layers, patterning the layers, and removing portions of the layers to define features on the wafer. One such process used to form the layers is a procedure known as chemical vapor deposition (CVD), where reactive gases are introduced into a vessel containing the semiconductor wafers. The reactive gases facilitate a chemical reaction that causes a layer to form on the wafers.
- One deposition process involves the formation of polycrystalline silicon (polysilicon) layers on the wafer by decomposing SiH4 molecules to Si atoms, which in turn combine to form Si grains, or “polysilicon.”. There are numerous factors that affect the deposition rate and deposition polysilicon film characteristics of a deposition tool. These factors include, e.g., the flow rate of reactive gases through the chamber and the temperature/pressure of the chamber.
- Polysilicon furnaces both within and without a nitrogen box (the furnace wafer loading area immediately below the furnace main body) may play an important role in controlling polysilicon grain size, thereby governing device speed. An important consideration is the actual N2 (nitrogen) flow which continuously treats the silicon wafer surface in the N2 box. A continual need exists for effective mechanisms for increasing the grain size of a silicon wafer.
- The present invention relates to a method for increasing the grain size of a polysilicon layer in a furnace, which includes exposing a silicon oxide wafer in a deposition chamber to an amount, effective for the purpose, of nitrogen at a flow rate of at least about 240 standard liters per minute (slm).
- The present invention may be understood by reference to the following description taken in conjunction with the accompanying drawings, in which:
- FIG. 1 is a graph of the effect of increased nitrogen flow in a furnace; and
- FIG. 2 is a graph of polysilicon film volume fraction versus control wafer resistivity in a furnace.
- According to the method of the present invention, a maximizing of polysilicon grain size results in an increase in device speed. In the method of the present invention, when an oxide wafer (i.e., a surface capped with a thin O2 boundary layer) was placed in an N2 box, the wafer was exposed to bulk N2 flow, with absorbed O2 being removed as a result. Upon treatment with the N2 flow, absorbed oxygen bonded with oxide molecules, and the oxygen depletion site was filled with N2 molecules. Nitrogen molecules “interfere” with silicon in forming a polysilicon seed; therefore fewer seeds, and a larger grain size was the result.
- A prototypical furnace includes four tube furnaces, which are used for curing polymers, sintering, and growing oxides and nitrides on silicon wafers. There are also four gas flow timers for the furnace. The orientation of the timers matches the orientation of the tubes with which they correspond; with a maximum time of twelve hours, the flow timers are used to control the time the gas flows in the furnaces. The minimum amount of time for the process to function correctly is about two hours. When the timer reaches zero, the gas discontinues to flow.
- There are three flow meters located just below the gas flow timers. Beneath each of the flow meters are two flow meter valves. The cut-off valves are the valves closest to the flow meters. The handles are at a 90° angle when the flow meters are closed. When the handles are parallel with the flow meter, they are open. The lower valves are the needle valves, which control the gas flow into the flow meters. To the right of the flow meters is the three-way valve. This valve controls which gas flows into the middle flow meter (tube2). The two selectable gases are oxygen and nitrogen. The narrow, pointed end of the handle points to the gas that is being used. When tube 2 is not in use, the valve is turned to the off position. When furnace tube 2 is used, which performs oxidation, the oxygen cylinder in the chase behind the furnace is on. Note that in order to check that the gas pressure is sufficient, the cylinder gauge closest to the cylinder is read. The gauge to the left indicates the gas line pressure; it is set to approximately 25 psi.
- The furnace temperature is controlled by a programmable temperature control unit. There is one control for every furnace; there are programmable temperature controllers on each of the temperature control units. These controllers monitor each of the furnace zone heaters, and allow the programming of several process steps. Thus, in order to operate the furnaces, the following steps are performed: (1) set the appropriate atmosphere, (2) load the furnace, (3) set the temperature program, (4) run the process, (5) end the run.
- The first step in setting the atmosphere is to set the gas flow timer to the length of the particular run. This prevents the waste of gas in the system. The next step is to set the flow of gas using the flow meters.
- The first step in loading the furnace is to place a sample into a quartz boat, which is found in the nitrogen box next to the furnace. The cap on the end of the tube is removed, and the boat placed just inside the opening. A metal rod is used in order to carefully push the boat to the middle of the furnace tube. The desired temperature in degrees Celsius is set for the controllers, and the temperature cooled to about room temperature when the program is done. In order to remove the boat from the furnace, the loading procedure is reversed.
- In the testing of the present invention, an analysis of the effect of an increase in nitrogen flow, via nitrogen shower or other acceptable method was conducted in a furnace. As shown in FIG. 1, the Vf (the polysilicon film volume fraction, which is an index of polysilicon grain size) trends down (i.e., larger grain size, as nitrogen flow increased). In FIG. 2, note that Rs (control wafer resistivity) trends down (i.e., higher speed) as Vf trends down (i.e., a larger grain size). Therefore, it is apparent that device speed is significantly enhanced by the amount of the N2 flow rate in a furnace.
- While this invention has been described with respect to particular embodiments thereof, it is apparent that numerous other forms and modifications of this invention will be obvious to those skilled in the art. The appended claims and this invention generally should be construed to cover all such obvious forms and modifications which are within the true spirit and scope of the present invention.
Claims (3)
1. In the manufacture of semiconductor devices, a method for increasing the grain size of a polysilicon layer in a furnace, which comprises exposing a silicon oxide wafer in a deposition chamber of the furnace to an amount, effective for the purpose, of nitrogen at a flow rate of at least about 240 standard liters per minute.
2. The method as recited in claim 1 , wherein the flow of nitrogen is achieved through nitrogen shower.
3. The method as recited in claim 1 , wherein the increasing of grain size results in an increase in semiconductor device speed.
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/431,120 US20040224533A1 (en) | 2003-05-07 | 2003-05-07 | Method for increasing polysilicon granin size |
TW093112939A TWI231532B (en) | 2003-05-07 | 2004-05-07 | Method for enhancing the speed of semiconductor device |
US11/293,709 US7446056B2 (en) | 2003-05-07 | 2005-12-01 | Method for increasing polysilicon grain size |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/431,120 US20040224533A1 (en) | 2003-05-07 | 2003-05-07 | Method for increasing polysilicon granin size |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US11/293,709 Continuation-In-Part US7446056B2 (en) | 2003-05-07 | 2005-12-01 | Method for increasing polysilicon grain size |
Publications (1)
Publication Number | Publication Date |
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US20040224533A1 true US20040224533A1 (en) | 2004-11-11 |
Family
ID=33416387
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US10/431,120 Abandoned US20040224533A1 (en) | 2003-05-07 | 2003-05-07 | Method for increasing polysilicon granin size |
US11/293,709 Expired - Fee Related US7446056B2 (en) | 2003-05-07 | 2005-12-01 | Method for increasing polysilicon grain size |
Family Applications After (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US11/293,709 Expired - Fee Related US7446056B2 (en) | 2003-05-07 | 2005-12-01 | Method for increasing polysilicon grain size |
Country Status (2)
Country | Link |
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US (2) | US20040224533A1 (en) |
TW (1) | TWI231532B (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
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TWI711728B (en) * | 2016-08-29 | 2020-12-01 | 聯華電子股份有限公司 | Method for forming lattice structures |
US9852912B1 (en) | 2016-09-20 | 2017-12-26 | United Microelectronics Corp. | Method of manufacturing semiconductor device for reducing grain size of polysilicon |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5242855A (en) * | 1991-09-30 | 1993-09-07 | Nec Corporation | Method of fabricating a polycrystalline silicon film having a reduced resistivity |
US5804473A (en) * | 1995-09-26 | 1998-09-08 | Fujitsu Limited | Thin film semiconductor device having a polycrystal active region and a fabrication process thereof |
US6514879B2 (en) * | 1999-12-17 | 2003-02-04 | Intel Corporation | Method and apparatus for dry/catalytic-wet steam oxidation of silicon |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5447893A (en) * | 1994-08-01 | 1995-09-05 | Dow Corning Corporation | Preparation of high density titanium carbide ceramics with preceramic polymer binders |
US6287988B1 (en) * | 1997-03-18 | 2001-09-11 | Kabushiki Kaisha Toshiba | Semiconductor device manufacturing method, semiconductor device manufacturing apparatus and semiconductor device |
US20030049372A1 (en) * | 1997-08-11 | 2003-03-13 | Cook Robert C. | High rate deposition at low pressures in a small batch reactor |
US6450116B1 (en) * | 1999-04-22 | 2002-09-17 | Applied Materials, Inc. | Apparatus for exposing a substrate to plasma radicals |
US6812081B2 (en) * | 2001-03-26 | 2004-11-02 | Semiconductor Energy Laboratory Co.,.Ltd. | Method of manufacturing semiconductor device |
US6803330B2 (en) * | 2001-10-12 | 2004-10-12 | Cypress Semiconductor Corporation | Method for growing ultra thin nitrided oxide |
US7005160B2 (en) * | 2003-04-24 | 2006-02-28 | Asm America, Inc. | Methods for depositing polycrystalline films with engineered grain structures |
-
2003
- 2003-05-07 US US10/431,120 patent/US20040224533A1/en not_active Abandoned
-
2004
- 2004-05-07 TW TW093112939A patent/TWI231532B/en not_active IP Right Cessation
-
2005
- 2005-12-01 US US11/293,709 patent/US7446056B2/en not_active Expired - Fee Related
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5242855A (en) * | 1991-09-30 | 1993-09-07 | Nec Corporation | Method of fabricating a polycrystalline silicon film having a reduced resistivity |
US5804473A (en) * | 1995-09-26 | 1998-09-08 | Fujitsu Limited | Thin film semiconductor device having a polycrystal active region and a fabrication process thereof |
US6514879B2 (en) * | 1999-12-17 | 2003-02-04 | Intel Corporation | Method and apparatus for dry/catalytic-wet steam oxidation of silicon |
Also Published As
Publication number | Publication date |
---|---|
US20060134926A1 (en) | 2006-06-22 |
TW200425308A (en) | 2004-11-16 |
US7446056B2 (en) | 2008-11-04 |
TWI231532B (en) | 2005-04-21 |
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AS | Assignment |
Owner name: TAIWAN SEMICONDUCTOR MANUFACTURING CO., LTD., TAIW Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:HUANG, YAO-HUI;LEE, TUNG-LI;LIN, CHIH-HAO;AND OTHERS;REEL/FRAME:014053/0466;SIGNING DATES FROM 20030415 TO 20030416 |
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STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |