Method and apparatus for thin films formation by CVD

Abstract: A method and apparatus for ramping down the deposition pressure in a SACVD process. The present invention also provides a method and apparatus for subsequently ramping up the pressure for a PECVD process in such a manner as to prevent unwanted reactions which could form a weak interlayer interface. In particular, the deposition pressure in the SACVD process is ramped down by stopping the flow of the silicon containing gas (preferably TEOS) and/or the carrier gas (preferably helium), while diluting the flow of ozone with oxygen. A ramp down of the pressure starts at the same time. The diluting of the ozone with oxygen limits reactions with undesired reactants at the end of a process.

Description: The present invention relates to reducing defects on the surface of a chemical vapor deposition (CVD) silicon dioxide film, and in particular, such a film formed using ozone-TEOS chemistry, and immediately followed by a plasma enhanced chemical vapor deposition (PECVD) silicon dioxide film. One of the primary steps in the fabrication of modern semiconductor devices is the formation of a thin film on the semiconductor substrate by chemical reaction of gases. Such a deposition process is referred to as chemical vapor deposition or "CVD" for short. Conventional thermal CVD processes supply reactive gases to the substrate surface where heat-induced chemical reactions take place to produce a desired film. The temperatures at which thermal CVD processes operate can damage device structures having metal layers. Plasma enhanced CVD (frequently referred to as PECVD) processes on the other hand, promote disassociation of the reactant gases by the application of radio frequency (RF) energy to a reaction zone proximate the substrate surface, thereby creating a plasma of highly-reactive ionic species. The high reactivity of the released ionic species reduces the energy required for a chemical reaction to take place, and thus lowers the required temperature for such CVD processes. The relatively low temperature of a PECVD process makes such processes useful, for example, for the formation of insulating layers over deposited metal layers. A two layer insulating or dielectric film is often used and provides certain advantages over a single layer film. A low pressure, or sub-atmospheric CVD (SACVD) process can form a film which fills gaps well, such as gaps between metal lines or between polysilicon or other areas. One example of an SACVD process used by Applied Materials uses ozone and is typically in a temperature range of 350-500° C and a pressure of 2666-82660 Pa (20-620 torr). A SACVD process has a slow deposition rate, and thus it is desirable to use a "sandwich" layer with a second, PECVD layer deposited on top of the first layer. The PECVD layer can be created much more quickly, reducing the time required to deposit a layer of desired thickness. The second layer can then be planarized using a chemical mechanical polish (CMP). Upon the termination of a SACVD process, it is possible for defects to form on the film surface due to reactions occurring after the termination of the process. These reactions can affect the integrity of the film, or the interface with any subsequent film. In particular, where a PECVD process is used to deposit a second silicon dioxide film on top of the film formed by the SACVD process, inter-layer defects can be problematic. In particular, a subsequent etch to form a metal connection through the layer may etch laterally into the weak interface, thus causing metal to be deposited where it is not desired and preventing clean, vertical lines for the metal connection. Each silicon dioxide layer may contain dopants which produce a particular type of dielectric layer. The layers can be undoped silica glass (USG), or can contain dopants such as phosphorous doped silicon glass (PSG) or boron and phosphorous doped silicon glass (BPSG). The dual layers can be used, for instance, for pre-metal dielectric (PMD) or for inter-metal dielectric (IMD) layers, or for an insulating or passivating layer. The two layers can be different combinations of PSG, BPSG or USG. In particular, a SACVD USG layer could be followed by a PECVD USG layer. Alternately, a SACVD PSG layer could be followed by a PECVD layer of USG or PSG. A SACVD BPSG layer could be followed by a PECVD layer of BPSG, PSG, or USG. A preferred silicon source is TEOS, while TMB or TEB may be used for the boron source and TEPO, TEP, TMP OR TMOP may be used for the phosphorous source. One method of creating the two layers is to deposit the first layer, and then move the wafer to a second reactor chamber for depositing the plasma enhanced film. The disadvantage of this method is the need for a second reactor chamber, and the need to move the wafer to the other chamber, requiring additional time. A second method uses a chamber which has the capability for both SACVD 2666-82660 Pa (20-620 torr) and PECVD 66.7-2666Pa (0.5-20 torr) processes. The chamber is first used for an SACVD process to deposit the first layer, and then the wafer is removed from the chamber and the chamber is cleaned. The wafer is subsequently brought back into the chamber to deposit the plasma enhanced film. This eliminates the forming of defects due to reactions with materials from the first process in the second process by having the chamber cleaned between processes. This process requires only a single chamber, but also requires the time for removing and replacing the wafer with the intermediate steps of cleaning the chamber. Simply doing the two depositions back to back in the same chamber without an intermediate clean has been found to produce a weak interface between the two silicon dioxide layers. Fig. 3 illustrates a cross-sectional view of a dual layer film having a lower layer 54 and an upper layer 56. A channel 58 is shown being etched through the two layers and filled with metallization. As can be seen, due to a poor interface 60, the etching can eat into the sidewalls at positions 62. As can be seen, the sidewalls are thus not clean, which can affect the performance and integrity of a circuit formed on the wafer. Defects can occur to cause a weak interface when, at the end of the SACVD step, during pump down, ozone reacts with different reactants in the chamber after the dopant gases and TEOS are turned off. On the start of the PECVD process, the dopants may react with oxygen to form B 2 O 3 or P 2 O 5 , in the interface, which could result in a weak interface. Boron and phosphorus oxides mixed in with the silicon oxide are desirable, but not if the boron and phosphorus oxides predominate over the silicon oxide. Interface problems between other dielectric layers have been addressed in different ways in the prior art. For instance, patent no. 5,271,972 discusses forming a PECVD layer first, and then depositing a thermal CVD layer. In order to reduce the surface sensitivity at the interface, the patent discusses doing a stepwise reduction of power at the end of the PECVD process. In patent no. 5,426,076, another method is discussed for forming a better interface with a PECVD layer being deposited first with a subsequent thermal CVD layer (THCVD). In this patent, an oxygen plasma (O 2 ) clean step is performed to remove deposits of liquid TEOS formed in the PECVD process. This prevents TEOS from reacting with the ozone in the subsequent THCVD process. The present invention is addressed to both a SACVD layer process and a dual dielectric layer in which the PECVD process comes second, not first. There is a need for improving the interface between the two layers while allowing the two processes to occur in-situ, or back-to-back, in the same chamber without an intermediate chamber cleaning step. Accordingly, in a first aspect, the present invention provides a method for depositing a layer of silicon oxide on a wafer disposed in a chemical vapour deposition (CVD) chamber using a sub-atmospheric chemical vapour deposition (SACVD) process followed by a plasma-enhanced chemical vapour deposition (PECVD) process without an intermediary cleaning step, which method comprises the following steps: (a) flowing a first silicon-containing gas, a carrier gas and ozone into the chamber to deposit a first portion of a layer of silicon oxide on the wafer in a SACVD deposition process; (b) thereafter, stopping the flow of the first silicon-containing gas and/or the carrier gas and diluting the flow of the ozone and subsequently decreasing the pressure in the chamber; and (c) thereafter, depositing a second portion of the silicon oxide layer on the wafer in a PECVD deposition process. In a second aspect, the present invention provides a chemical vapour deposition (CVD) apparatus comprising: a CVD chamber, supporting means for supporting a wafer mounted in the chamber; a gas discharge head mounted in the chamber; means for moving the supporting means relative to the gas discharge head; a plasma generating system comprising an RF source coupled between the gas discharge head and the supporting means for creating a plasma; a gas distribution system coupled to the gas discharge head for selectively introducing a silicon-containing gas, a carrier gas, ozone and oxygen into the chamber; a controller for controlling the gas distribution system, the RF source, the means for moving the supporting means and pressure in the chamber, and a memory coupled to the controller and storing a computer program for directing the operation of the chamber, wherein the computer program includes a set of instructions to: (a) flow a first silicon-containing gas, carrier gas and ozone into the chamber to deposit, in use, a first portion of a layer of silicon oxide on a wafer in a sub-atmospheric chemical vapour deposition (SACVD) process; and (b) thereafter, stop the flow of the first silicon-containing gas and/or the carrier gas and dilute the flow of the ozone and subsequently decrease the pressure in the chamber; and (c) thereafter, carry out a plasma-enhanced chemical vapour deposition (PECVD) process to deposit, in use, a second portion of the silicon oxide layer on the wafer. In a third aspect, the present invention provides a computer program stored on a computer readable medium, the computer program including instructions for a chemical vapour deposition controller in a chemical vapour deposition (CVD) apparatus to execute the following procedure: (a) flow a first silicon-containing gas, a carrier gas and ozone into a CVD chamber to deposit, in use, a first portion of a layer of silicon oxide on a wafer in a sub-atmospheric chemical vapour deposition (SAC VD) process; (b) thereafter, stop the flow of the first silicon-containing gas and/or the carrier gas and dilute the flow of the ozone and subsequently decrease the pressure in the chamber; and (c) thereafter, carry out a plasma-enhanced chemical vapour deposition (PECVD) process to deposit, in use, a second portion of the silicon oxide layer on the wafer. The deposition pressure in the SACVD process is ramped down by stopping the flow of the silicon containing gas (preferably TEOS) and/or the carrier gas (preferably helium), while diluting the flow of the oxygen reacting gas, such as diluting the flow of ozone with oxygen. A ramp down of the pressure starts at the same time. The diluting of the ozone with oxygen limits reactions with undesired reactants at the end of a process. If a dopant gas is used in the O 3 -TEOS process, preferably the dopant gas is turned off for about two seconds before turning off the TEOS and helium carrier flow, to allow the dopant gases to be consumed. Preferably, when the oxygen is introduced to dilute the ozone, the wafer is moved away from the gas discharge head. The pressure is preferably reduced at a rate of approximately 10 torr per second until the reaction chamber base pressure 53.3-267 Pa (0.4-2 torr) is reached. The present invention also prevents defects from forming during the ramping up of the PECVD process. This is done by first introducing oxygen and increasing the pressure. The susceptor with the wafer is concurrently or previously moved up to near the gas discharge head. Subsequently, the silicon containing gas (TEOS) is introduced and the plasma is ignited. Preferably, the plasma is started with oxygen and TEOS for about 1-2 seconds before introducing any dopants to be used in generating the silicon dioxide layer. For a fuller understanding of the objects and advantages of the present invention, reference should be made to the ensuing detailed description taken in conjunction with the accompanying drawings. Fig. 1 is a vertical, cross-sectional view of a simplified CVD reactor according to the present invention; Fig. 2 is a cross-sectional diagram of a two layer dielectric according to the present invention; Fig. 3 is a cross-sectional view of an etched channel through a dual layer film illustrating the effects of a defective interface; Fig. 4 is a diagram of a process system illustrating the different gas sources and mixes; Fig. 5 is a flowchart illustrating the SACVD ramp-down steps of the present invention; and Fig. 6 is a flowchart illustrating the PECVD ramp-up steps of the present invention. One suitable CVD system in which the method of the present invention can be carried out is shown in Fig. 1 which is a vertical, cross-sectional view of a simplified, parallel plate chemical vapor deposition system 10 having a vacuum chamber 15. System 10 contains a gas inlet manifold 11 for dispersing deposition gases to a wafer, not shown, that rests on a susceptor 12. Susceptor 12 is highly thermally responsive and is mounted on a support fingers 13 so that susceptor 12 (and the wafer supported on the upper surface of susceptor 12) can be controllably moved between a lower loading/off-loading position and an upper processing position 14 which is closely adjacent manifold 11. When susceptor 12 and the wafer are in processing position 14, they are surrounded by a baffle plate having a plurality of spaced holes 23 which exhaust into an annular vacuum manifold 24. During processing, gas inlet to manifold 11 is uniformly distributed radially across the surface of the wafer as indicated by arrows 21. The gas is then exhausted via ports 23 into the circular vacuum manifold 24 by a vacuum pump system (not shown). Before reaching manifold 11, deposition and carrier gases are input through gas lines 18 into a mixing system 19 where they are combined and then sent to manifold 11. This CVD system has the capability of performing, without hardware modification, both a SACVD process 2666-82660 Pa (20-620 torr) and a PECVD process 66.7-2666 Pa (0.5-20 torr). The deposition process performed in system 10 can be either a thermal process or a plasma enhanced process. The thermal process would typically be a SACVD process that uses ozone and TEOS in a temperature range of 350-500° C and a pressure range of 2666-82660 Pa (20-620 torr). In a plasma process, a controlled plasma is formed adjacent to the wafer by RF energy applied to inlet manifold 11 from RF power supply 25 (with susceptor 12 grounded). In one embodiment, the RF power is connected by a strap to a support for inlet manifold 11, although other connection points could be used. Inlet manifold 11 is also an RF electrode, while susceptor 12 is grounded. RF power supply 25 can supply either single or mixed frequency RF power to manifold 11 to enhance the decomposition of reactive species introduced into chamber 15. An external lamp module 26 provides a collimated annular pattern of light 27 through quartz window 28 onto an annular outer peripheral portion of susceptor 12. Such heat distribution compensates for the natural heat loss pattern of the susceptor and provides rapid thermal and uniform susceptor and wafer heating for effecting deposition. Typically, any or all of the chamber lining, gas inlet manifold faceplate, support fingers 13, and various other system hardware is made out of material such as anodized aluminum. An example of such a CVD apparatus is described in U.S. Patent 5,000,113 entitled "Thermal CVD/PECVD Reactor and Use for Thermal Chemical Vapor Deposition of Silicon Dioxide and In-situ Multi-step Planarized Process," issued to Chang et al. and assigned to Applied Materials, Inc., the assignee of the present invention, which is incorporated herein by reference for all purposes. A motor 32 raises and lowers susceptor 12 between a processing position 14 and a lower, wafer-loading position. Motor 32, gas mixing system 19 and RF power supply 25 are controlled by a processor 34 over control lines 36. Processor 34 operates under the control of a computer program stored in a memory 38. The computer program dictates the timing, mixture of gases, RF power levels, susceptor position, and other parameters of a particular process. Fig. 2 is a cross-sectional view of a portion of one example of a wafer formed according to the present invention. The cross-sectional view shows a number of metal or polysilicon lines 40 formed over a lower layer 42. Lower layer 42 would typically include transistors or other components which the metal or polysilicon lines 40 interconnect. In order to deposit a second layer of metal, or simply passivate the metal layer, an intermediate insulation layer is needed. This is formed in the present invention using two layers. The first layer is a SACVD layer 44. A SACVD process is used because it is good for filling in gaps such as gap 48 between the metal lines 40. The SACVD process could also be used to fill gaps between polysilicon or other structures as a pre-metal layer of other layer. In addition, the doped SACVD layer can be annealed to temperatures ranging from 750° C to 950° C to provide a planarized or partially planarized layer. Since the SACVD layer does not deposit very fast, a second plasma enhanced layer 46 is deposited, which can quickly form a thick layer. Top surface 52 can be planarized using CMP. As pointed out in the background above, to form a good interface 50, typically two chambers are used, or the wafer is removed from the chamber and a clean is done after the SACVD layer 44 is deposited, and before the plasma enhanced layer 46 is deposited. The present invention provides a process for forming a good interface 50 without removing the wafer from the chamber and without doing an intermediate cleaning step. This is accomplished by a novel procedure for the ramp-down of the pressure of a SACVD deposition step illustrated in Fig. 5 and a ramp-up procedure for the PECVD process as illustrated in Fig. 6. The SACVD procedure is also useful for avoiding surface defects for a single layer embodiment. Fig. 4 illustrates the gas mixing system 19 which supplies gas to process chamber 10. A first line 64 is used to mix TEOS from a line 66 along with any dopants that may be provided, such as TEPO through a valve 68 on a line 70, and TEB through a valve 72 on a line 74. Separately, a second line 76 delivers oxygen to the gas discharge manifold in process chamber 10 through a line 78 controlled by a valve 80, and/or ozone through a line 82 controlled by a valve 84, and possibly a fluorine containing gas, such as C 2 F 6 through a line 86 controlled by a valve 88. The process gases generated from the liquid sources (TEOS, TEB, TEPO, etc.) may be provided by a variety of methods. Two alternate methods are shown for one example, TEOS on line 66. Similar arrangements can be used to generate a gas from TEPO (or TEP, TMP or TMOP) to valve 68 or a gas from TEB (or TMB) to valve 72. In the TEOS examples, the TEOS generated gas can either be provided through a bubbler system 90 or an injection system 92. These are indicated with dotted lines, since one or the other would be used. In bubbler system 90, helium controlled by an automatic flow controller (AFC) 94 is provided through a line 96 into a vessel 98 containing liquid TEOS 100 at a temperature between 30-50° C. The bubbling of the helium into the vessel will carry TEOS vapor to the CVD chamber along line 102 which will connect to line 66. Alternately, liquid TEOS from TEOS source 108 is provided through a liquid flow meter (LFM) 106 to an injection valve 104. TEOS source 108 may include a degasser to remove helium where pressurized helium is used to pump the TEOS. A degasser may also be used in the bubbler embodiment. The liquid flow meter controls the flow rate of the liquid TEOS. Helium as a carrier gas is provided to injection valve 104 through an automatic flow controller 109 and a conduit 110. In injection valve 104, the liquid TEOS is vaporized due to a sudden pressure or volume change. The vaporized TEOS is carried to the process chamber by the Helium carrier gas along conduits 112 and 66. On the other side of the chamber, a vacuum pump 114 is connected to an exhaust line from the chamber through a variable or throttle valve 116 controlled by a stepper motor 118. When the stepper motor closes valve 116, the gas that is provided into process chamber 10 will increase the pressure in the chamber. When the valve 116 is open, the pressure in the chamber can be decreased. During a process, the proper pressure can be maintained by using a feedback loop and controlling valve 116 under servo control to maintain the desired pressure. A dual manometer 11 is used to measure the pressure in process . chamber 10. The manometer can measure pressures in the range of 0-13332 Pa (0-100 torr) (for the PECVD process) or in the range of 0-133322 Pa (0-1000 torr) (for the SACVD process). The measured pressure is provide to processor 34 of Fig. 1 for feedback control. Fig. 5 is a flowchart of one embodiment of a CVD ramp-down according to the present invention. As shown in step A, the SACVD deposition step is first completed. In one embodiment, this process involves a gas mixture of ozone (O 3 ) and TEOS being provided to the chamber with the chamber at a pressure of approximately 26664 Pa (200 torr). The susceptor is heated to a temperature of 400-500°C by the heating lamps, and no power is applied between the RF power supply and the susceptor since this is not a plasma enhanced process. If the process is one for a doped silicon glass, as opposed to undoped (USG), the gas mixture will also include gases containing phosphorous or phosphorous and boron, such as TEB (triethylborate) and TEPO (triethylphosphate). The susceptor is spaced from the gas discharge manifold by 200-300 mils. An ozone flow rate of 2000-5000 sccm is used. For an injection system process, one embodiment also includes 200-600 mgm of TEOS, 40-90 mgm of TEPO and 100-250 mgm of TEB. In the injection system, the flow of the helium carrier is 2000-8000 sccm. In one embodiment of a bubbler system, on the other hand, the flow of the Helium carrier into the liquid TEOS vessel is 2000-5000 sccm, the flow of the He carrier into the TEPO vessel is 2000-6000 sccm and the He carrier flow into the TEB vessel is 200-400 sccm. Once the process has been running for a sufficient amount of time to deposit a layer 44 (as shown in Fig. 2) of sufficient thickness, the flow of the dopant gases containing boron, or phosphorous and boron, is first stopped (step B in Fig. 5). After a delay of 1-5 seconds, preferably 2-3 seconds (step C), the flow of the silicon containing gas (TEOS) and/or the carrier gas (helium) is stopped (step D). This prevents the ozone from reacting with the dopant gases without sufficient TEOS being present. This amount of time has been empirically determined to be 1-5 seconds, preferably 2-3 seconds. Also in step D, the ozone flow is diluted with oxygen. Preferably, an O 2 flow of 3000 sccm is added for an ozone flow rate of 4000 sccm, and proportionate amounts for other flow rates. This prevents defects from forming because otherwise, if high concentration ozone is present at during pressure ramp-down, the dopants and TEOS could react in an undesired and uncontrolled way. After the oxygen flow is started, the susceptor and wafer are moved away from the gas discharge manifold (step D). This movement is started immediately after the oxygen flow starts, and the oxygen flow is started at the same time that the TEOS and the helium are stopped. Moving the susceptor downward not only reduces the likelihood of reaction, but also moves it away from the vacuum exhaust, thus making it less likely that defects will be pulled across it. Next, as the susceptor starts moving from its processing spacing of approximately 230 mils from the gas discharge faceplate, to a position of 600 mils from the gas discharge faceplate, the pressure is also decreased. The decrease in pressure is preferably done at a rate of approximately 1333 Pa (10 torr) per second until the pressure is dropped to the reaction chamber base pressure of approximately 53.3-267 Pa (0.4-2 torr) This process takes approximately 10-20 seconds depending upon the processing pressure. After the flow of oxygen and ozone is stopped, the pressure reaches the chamber base pressure of 0.05-0.3 Pa (0.4-2 millitorr) (step E). The ramp down process of the present invention, by turning off the dopant flow before turning off the ozone/TEOS flow, will cause a surface layer to not have dopant reactants predominate. In fact, silicon dioxide alone may form the surface layer, which is preferable to having an excess of dopants on the surface layer. In an alternate embodiment, instead of using oxygen to dilute the ozone, nitrogen could be used instead. The PECVD process can be started approximately 2-3 seconds after the completion of the SACVD process by turning off the oxygen and ozone flow. During that time, the temperature is maintained so that the PECVD process will be quickly started. Fig. 6 illustrates the steps for the ramp-up of a PECVD process to minimize interface defects between two layers. The susceptor is first moved from 600 mils to 230-260 mils from the gas discharge head (step G). Next, the pressure is increased again for the PECVD ramp-up (step H) with a flow of oxygen, preferably around 1000 sccm. This occurs at a rate of approximately 133 Pa (1 torr) per second to increase it from the chamber base pressure of 53.3-267 Pa (0.4-2 toor) to an operating pressure of between 667 and 2000 Pa (5 and 15 torr), and typically takes 10-15 seconds. Next, the TEOS for the formation of the next film is introduced into the chamber (step I) preferably at approximately 600-700 sccm, and the pressure is raised to the final process pressure, preferably 933-1600 Pa (7-12 torr). After the TEOS has been introduced for about 14-20 second, the plasma is ignited by being turned on at a power of approximately 550-600 watts (step J). After about 2 seconds, with the plasma thus ignited, any dopants are introduced into the chamber (step K) and the deposition process proceeds (step L). For one embodiment, a flow rate of TEOP at 580 sccm may be used for PSG, and TEB at 50 sccm with TEPO at 1100 sccm for BPSG. Alternately, other flow rates may be used, or a bubbler process may be used. By doing the ramp-up in pressure and spacing, and by introducing TEOS and O 2 before the dopants, the formation of compounds of boron with oxygen and phosphorous with oxygen, such as B 2 O 2 and P 2 O 5 is avoided at the interface of the two layers. These compounds, if formed, would weaken the interface between the two layers. The strength of the interface between two layers in the wafer formed according to the present invention was tested by the inventors. After the films were deposited, the wafer was annealed at 316°C (600°F). Next, the wafer was put in acid, KOH, which etches the polysilicon but not the silicon dioxide. After about 20 seconds of the hot acid etch, the strength of the interface was observed under a scanning electron microscope. The etch pattern revealed the lack of any defects such as that shown in Fig. 3. The susceptor could be moved toward the manifold later in the PECVD ramp-up.

Claims: A method for depositing a layer of silicon oxide on a wafer (40,42) disposed in a chemical vapour deposition (CVD) chamber (15) using a sub-atmospheric chemical vapour deposition (SACVD) process followed by a plasma-enhanced chemical vapour deposition (PECVD) process without an intermediary cleaning step, which method comprises the following steps: (a) flowing a first silicon-containing gas, a carrier gas and ozone into the chamber (15) to deposit a first portion (44) of a layer of silicon oxide on the wafer (40,42) in a SACVD deposition process; (b) thereafter, stopping the flow of the first silicon-containing gas and/or the carrier gas and diluting the flow of the ozone and subsequently decreasing the pressure in the chamber (15); and (c) thereafter, depositing a second portion (46) of the silicon oxide layer on the wafer (40,42) in a PECVD deposition process. A method as claimed in claim 1, wherein the PECVD deposition process in step (c) comprises the following steps: (i) flowing oxygen into the chamber (15) and increasing the pressure in the chamber (15); and (ii) thereafter, flowing a second silicon-containing gas into the chamber (15) and igniting a plasma. A method as claimed in claim 1 or claim 2, wherein a dopant-containing gas is flowed into the chamber (15) during deposition of the first portion (44) in step (a), whereby the first portion (44) of the layer of silicon oxide is doped with a dopant, and wherein the flow of the dopant-containing gas is stopped prior to stopping the flow of the first silicon-containing gas and/or the carrier gas in step (b). A method as claimed in claim 2 or claim 3, wherein the plasma is ignited in step (ii) of the PECVD deposition process in step (c) for between 15 and 20 seconds after the flow of the second silicon-containing gas is started. A method as claimed in any one of claims 2 to 4, wherein the pressure in the chamber (15) is increased in step (i) of the PECVD deposition process in step (c) at a rate of between 66.7 pa (0.5 Torr) and 666.6 pa (5 Torr) per second. A method as claimed in any one of the preceding claims, wherein said gases are flowed into the chamber (15) from a gas discharge head (11) and the step of diluting the flow of the ozone in step (b) further includes moving the wafer away from the gas discharge head (11). A method as claimed in any one of claims 2 to 6, wherein a dopant-containing gas is flowed into the chamber (15) after igniting the plasma in step (ii) of the PECVD deposition process in step (c), whereby the second portion (46) of the silicon oxide layer is doped with a dopant. A method as claimed in any one of claims 3 to 7, wherein the flow of the first silicon-containing gas and/or the carrier gas is stopped between 1 to 5 seconds after the flow of the dopant-containing gas is stopped. A method as claimed in any one of the preceding claims, wherein the pressure in the chamber (15) is decreased in step (b) at a rate of between 667 pa (5 Torr) and 6666 pa (50 Torr) per second. A method as claimed in any one of the preceding claims, wherein the pressure in the chamber (15) is decreased in step (b) to a base pressure in the range of from 53.3 pa (0.4 Torr) to 266.6 pa (2 Torr). A method as claimed in any one of the preceding claims, wherein the pressure in the chamber (15) in the SACVD deposition process in step (a) is between 2666 pa (20 Torr) and 82660 pa (620 Torr). A method as claimed in any one of the preceding claims, wherein the pressure in the chamber (15) in the PECVD deposition process in step (c) is between 66.7 pa (0.5 Torr) and 2666 pa (20 Torr), preferably between 933 pa (7 Torr) and 1600 pa (12 Torr). A method as claimed in any one of the preceding claims, wherein the ozone flow is diluted with nitrogen or oxygen. A method as claimed in any one of the preceding claims, wherein the first and/or second silicon-containing sources are tetraethylorthosilicate (TEOS). A method as claimed in any one of the preceding claims, wherein the carrier gas is helium. A chemical vapour deposition (CVD) apparatus (10) comprising: a CVD chamber (15); supporting means for supporting a wafer mounted in the chamber (15); a gas discharge head (11) mounted in the chamber (15); means for moving the supporting means relative to the gas discharge head (11); a plasma generating system comprising an RF source (25) coupled between the gas discharge head (11) and the supporting means for creating a plasma; a gas distribution system (18,19) coupled to the gas discharge head (11) for selectively introducing a silicon-containing gas, a carrier gas, ozone and oxygen into the chamber (15); a controller (34) for controlling the gas distribution system (18,19), the RF source (25), the means for moving the supporting means and pressure in the chamber (15); and a memory (38) coupled to the controller (34) and storing a computer program for directing the operation of the chamber (15), wherein the computer program includes a set of instructions to: (a) flow a first silicon-containing gas, carrier gas and ozone into the chamber (15) to deposit, in use, a first portion (44) of a layer of silicon oxide on a wafer (40,42) in a sub-atmospheric chemical vapour deposition (SACVD) process; and (b) thereafter, stop the flow of the first silicon-containing gas and/or the carrier gas and dilute the flow of the ozone and subsequently decrease the pressure in the chamber (15); and (c) thereafter, carry out a plasma-enhanced chemical vapour deposition (PECVD) process to deposit, in use, a second portion (46) of the silicon oxide layer on the wafer (40,42). An apparatus as claimed in claim 16, wherein the supporting means for supporting a wafer is a susceptor (12) and the means for moving the susceptor (12) relative to the gas discharge head (11) is a motor (32). An apparatus as claimed in claim 16 or claim 17, wherein the instructions for the PECVD deposition process comprise: (i) flow oxygen into the chamber (15) and increase the pressure in the chamber (15); and (ii) thereafter, flow a second silicon-containing gas into the chamber (15) and ignite a plasma. An apparatus as claimed in any one of claims 16 to 18, wherein the computer program includes an instruction to set the pressure in the chamber (15) at between 2666 pa (20 Torr) and 82660 pa (620 Torr) during the SACVD process. An apparatus as claimed in any one of claims 16 to 19, wherein the computer program includes an instruction to decrease the pressure in the chamber (15) to a pressure of from 53.3 pa (0.4 Torr) to 266.6 pa (2 Torr) after the flow of the first silicon-containing gas and/or the carrier gas is stopped and the flow of the ozone is diluted. An apparatus as claimed in any one of claims 18 to 20, wherein the computer program includes an instruction to set the pressure in the chamber (15) at between 66.7 pa (0.5 Torr) and 2666 pa (20 Torr), preferably between 933 pa (7 Torr) and 1600 pa (12 Torr) during the PECVD process. An apparatus as claimed in any one of claims 18 to 21, wherein the computer program includes an instruction to ignite the plasma in the PECVD process for between 15 and 20 seconds after the second silicon-containing gas is flowed into the chamber (15). An apparatus as claimed in any one of claims 18 to 22, wherein the computer program includes an instruction to increase the pressure in the chamber (15) at a rate of between 66.7 pa (0.5 Torr) and 666.6 pa (5 Torr) per second when the oxygen is flowed into the chamber (15). An apparatus as claimed in any one of claims 16 to 23, wherein the gas discharge head (11) is adapted to flow gases into the chamber (15) in a radial flow above the supporting means, and wherein the gas discharge head (11) is adapted to function as an RF electrode of the plasma generating system and the supporting means is adapted to be grounded. An apparatus as claimed in any one of claims 16 to 24, wherein the computer program includes an instruction to move the supporting means away from the gas discharge head (11) after the flow of ozone is diluted. An apparatus as claimed in any one of claims 16 to 25, wherein the computer program includes an instruction to flow a dopant-containing gas into the chamber (15) with the first silicon-containing gas, the carrier gas and the ozone in the (SACVD) process, and an instruction to stop the flow of the dopant-containing gas before stopping the flow of the first silicon-containing gas and/or the carrier gas. An apparatus as claimed in claim 26, wherein the instruction that stops the flow of the first silicon-containing gas and/or the carrier gas does so between 1 and 5 seconds after stopping the flow of the dopant containing gas. An apparatus as claimed in any one of claims 16 to 27, wherein the computer program includes an instruction to decrease the pressure in the chamber (15) at a rate of between 667 pa (5 Torr) and 6666 pa (50 Torr) per second after the flow of the first silicon-containing gas and/or the carrier gas is stopped and the flow of the ozone is diluted. A computer program stored on a computer readable medium, the computer program including instructions for a chemical vapor deposition controller (34) in a chemical vapour deposition (CVD) apparatus (10) to execute the following procedure: (a) flow a first silicon-containing gas, a carrier gas and ozone into a CVD chamber (15) to deposit, in use, a first portion (44) of a layer of silicon oxide on a wafer (40,42) in a sub-atmospheric chemical vapour deposition (SACVD) process; (b) thereafter, stop the flow of the first silicon-containing gas and/or the carrier gas and dilute the flow of the ozone and subsequently decrease the pressure in the chamber (15); and (c) thereafter, carry out a plasma-enhanced chemical vapour deposition (PECVD) process to deposit, in use, a second portion (46) of the silicon oxide layer on the wafer (40,42). A computer program as claimed in claim 29, wherein the instructions for the PECVD deposition process comprise: (i) flow oxygen into the chamber (15) and increase the pressure in the chamber (15); and (ii) thereafter, flow a second silicon-containing gas into the chamber (15) and ignite a plasma.

Inventors: GALIANO MARIA, KITHCART VICTORIA, ROBLES STUARDO, SIVARAMAKRISHNAN VISWESWAREN, GALIANO, MARIA, KITHCART, VICTORIA, ROBLES, STUARDO, SIVARAMAKRISHNAN, VISWESWAREN
Applicants: APPLIED MATERIALS INC, APPLIED MATERIALS, INC.
Application year: 1996
Main classification: C23C16
IPC codes: H01L21, C23C16