This application claims the benefit of Japanese Patent Applications Nos. 2014-153094 and 2015-094907, filed on Jul. 28, 2014 and May 7, 2015, respectively, in the Japan Patent Office, the disclosures of which are incorporated herein in their entirety by reference.
The present disclosure relates to a film forming apparatus for forming a film in a state in which a substrate holding part holding a plurality of substrates in a form of a shelf is disposed in a vertical reaction vessel.
Atomic layer deposition (ALD) is used as a method of forming a film on a substrate such as a semiconductor wafer (hereinafter, referred to as a “wafer”). In the ALD, a gas (source gas) that is a film forming source material is supplied to a surface of a wafer, thereby forming an atomic layer or molecular layer of the source gas adsorbed onto the surface of the wafer, and a reaction product is then generated by supplying a reaction gas for oxidizing/reducing the source gas. The process is repeated, thereby depositing layers of the reaction product. The ALD may be performed using a film forming apparatus in which each gas is supplied in a state where a wafer boat holding a plurality of wafers in a form of a shelf is loaded in a vertical reaction vessel.
In manufacturing semiconductor devices, semiconductor devices may need to be produced for various uses but in a small quantity for each use. In this case, a relatively small number of wafers in the same lot are held in holding areas (slots) of the wafer boat, and the ALD is then performed. In the wafer boat, a dummy wafer is held in the slot where no wafer is provided so as to prevent the state of a film formed on the wafer from being changed due to a change in the number of wafers.
However, a large number of dummy wafers are consumed in this process. Also, in the film forming apparatus, even when a film forming process is performed only once, a time taken to load and unload the wafer boat into and from the apparatus, a time taken to load and unload wafers and dummy wafers into and from slots of the wafer boat, a time taken to vacuumize the inside of a reaction vessel before the film forming process, a time taken to heat the wafers before the film forming process, and the like are required in addition to a time required to perform the film forming process. Therefore, if the number of wafers that can be held in the wafer boat is small, the number of times the film forming processes are performed should be increased for processing an arbitrary number of wafers and hence a time (overhead time) for the increased number of times performed is additionally required in the film forming process. As a result, a problem that the productivity of the apparatus degrades is caused. It may be considered to wait until many wafers to be subjected to the same film forming process become ready to be transferred into the wafer boat. However, even in this case, since the timing for starting the process also becomes late, it is difficult to improve the productivity of the apparatus.
For example, there is known a film forming apparatus in which a partition plate surrounding a wafer boat is installed in a reaction vessel to partition the inside of the reaction vessel. In the film forming apparatus, different gases are supplied into the respective divided areas, and a source gas, a purge gas, a reaction gas, and a purge gas are repeatedly supplied to the respective areas in this order, thereby performing processes. Accordingly, ALDs are performed in the respective divided areas such that timings of the ALDs become different between the respective areas by one step. Thus, the amount of gas supplied into each area per unit time can be large. However, even if the processes are performed in the above-described manner, it is impossible to resolve the problems associated with the productivity in the apparatus or waste of dummy wafers.
Some embodiments of the present disclosure provide a technology for enhancing the productivity of a film forming apparatus in which a film is formed in a state in which a substrate holding unit holding a plurality of substrates in a form of a shelf is disposed in a vertical reaction vessel.
According to one embodiment of the present disclosure, there is provided a film forming apparatus in which a film is formed by alternately supplying a source gas and a reaction gas reacting with the source gas to generate a reaction product into a vertical reaction vessel having a substrate holding unit disposed therein, the substrate holding part holding a plurality of substrates in a form of a shelf, the film forming apparatus including: a first source gas supply part and a second source gas supply part configured to limitedly supply the source gas only to a first substrate holding area and a second substrate holding area, respectively, among the first substrate holding area and the second substrate holding area disposed along an arrangement direction in which the substrates are arranged in the substrate holding part; a reaction gas supply part configured to supply the reaction gas to the first substrate holding area and the second substrate holding area; a purge gas supply part configured to supply a purge gas for preventing the source gas supplied to one of the first substrate holding area and the second substrate holding area from being supplied to the other substrate holding area; a division-purpose substrate held between the first substrate holding area and the second substrate holding area in the substrate holding part to divide the substrate holding part into the first substrate holding area and the second substrate holding area; and a control part configured to output a control signal such that a first cycle including supplying the source gas to the first substrate holding area and supplying the reaction gas to the first substrate holding area and a second cycle including supplying the source gas to the second substrate holding area and supplying the reaction gas to the second substrate holding area are each performed plural times.
According to another embodiment of the present disclosure, there is provided a film forming apparatus in which a film is formed by alternately supplying a source gas and a reaction gas reacting with the source gas to generate a reaction product into a vertical reaction vessel having a substrate holding unit disposed therein, the substrate holding part holding a plurality of substrates in a form of a shelf, the film forming apparatus including: a first reaction gas supply part and a second reaction gas supply part configured to limitedly supply the reaction gas only to a first substrate holding area and a second substrate holding area, respectively, among the first substrate holding area and the second substrate holding area disposed along an arrangement direction in which the substrates are arranged in the substrate holding part; a source gas supply part configured to supply the source gas to the first substrate holding area and the second substrate holding area; a purge gas supply part configured to supply a purge gas for preventing the reaction gas supplied to one of the first substrate holding area and the second substrate holding area from being supplied to the other substrate holding area; a division-purpose substrate held between the first substrate holding area and the second substrate holding area in the substrate holding part to divide the substrate holding part into the first substrate holding area and the second substrate holding area; and a control part configured to output a control signal such that a first cycle including supplying the source gas to the first substrate holding area and supplying the reaction gas to the first substrate holding area and a second cycle including supplying the source gas to the second substrate holding area and supplying the reaction gas to the second substrate holding area are each performed plural times.
According to another embodiment of the present disclosure, there is provided a film forming apparatus in which a film is formed by alternately supplying a source gas and a reaction gas reacting with the source gas to generate a reaction product into a vertical reaction vessel having a substrate holding part disposed therein, the substrate holding part holding a plurality of substrates in a form of a shelf, the film forming apparatus including: a first source gas supply part configured to limitedly supply the source gas at a first flow rate only to a first substrate holding area, among the first substrate holding area and a second substrate holding area disposed along an arrangement direction in which the substrates are arrange in the substrate holding part; a second source gas supply part configured to supply the source gas at a second flow rate greater than the first flow rate only to the second substrate holding area, in parallel with the supply of the source gas from the first source gas supply part; a gas supply part for pressure adjustment configured to supply a pressure adjustment gas for adjusting a pressure distribution in the first substrate holding area and the second substrate holding area to the first substrate holding area when the source gas is supplied to the first substrate holding area and the second substrate holding area; a division-purpose substrate held between the first substrate holding area and the second substrate holding area in the substrate holding part to divide the substrate holding part into the first substrate holding area and the second substrate holding area; and a control part configured to output a control signal such that a cycle including supplying the source gas to the first substrate holding area and supplying the reaction gas to the first substrate holding area and a cycle including supplying the source gas to the second substrate holding area and supplying the reaction gas to the second substrate holding area are each performed plural times.
The accompanying drawings, which are incorporated in and constitute a part of the specification, illustrate embodiments of the present disclosure, and together with the general description given above and the detailed description of the embodiments given below, serve to explain the principles of the present disclosure.
Reference will now be made in detail to various embodiments, examples of which are illustrated in the accompanying drawings. In the following detailed description, numerous specific details are set forth in order to provide a thorough understanding of the present disclosure. However, it will be apparent to one of ordinary skill in the art that the present disclosure may be practiced without these specific details. In other instances, well-known methods, procedures, systems, and components have not been described in detail so as not to unnecessarily obscure aspects of the various embodiments.
A film forming apparatus 1 according to an embodiment of the present disclosure will be described with reference to
The wafer boat 3 has, for example, three posts 30, and supports outer edge portions of wafers W and dummy wafers 10 serving as substrates for division, thereby holding the wafers W and the dummy wafers 10 in a form of a shelf. The boat elevator 22 is liftable by a lifting mechanism (not shown), and the rotating shaft 24 is rotatable around a vertical axis by a motor M constituting a driving unit. Reference numeral 25 in
A plasma generation unit 13 is installed at a portion of the sidewall of the reaction vessel 11. The plasma generation unit 13 is formed by airtightly joining a division wall 15 made of, e.g., quartz and having a concave cross section, to the outer wall of the reaction vessel 11 such that the division wall 15 covers a vertically elongated opening 14 formed through the sidewall of the reaction vessel 11. The opening 14 is formed in an elongated shape along the vertical direction in a range covering all the wafers W and the dummy wafers 10 held by the wafer boat 3. A pair of plasma electrodes 16 opposite to each other along the length direction (vertical direction) of the division wall 15 are installed on outer surfaces of both sidewalls of the division wall 15. A high-frequency power source 17 for plasma generation is connected to the plasma electrodes 16 through a feeding line 171, so that plasma can be generated by applying a high-frequency voltage of, e.g., 13.56 MHz to the plasma electrodes 16. An insulation protection cover 18 made of, e.g., quartz is installed on the outside of the division wall 15 to cover the division wall 15.
A vertically elongated opening 19 is formed in a portion of the circumferentially extending sidewall of the reaction vessel 11, i.e., an area opposite to the plasma generation unit 13 in this example, so as to vacuum-exhaust the atmosphere in the reaction vessel 11. The opening 19 is formed along an arrangement direction in which the wafers W and the dummy wafers 10 are arranged while facing the area in which the wafers W and the dummy wafers 10 are arranged in the wafer boat 3.
An exhaust cover member 31 made of, e.g., quartz in the shape of a U-shaped cross section, is installed to the opening 19 to cover the opening 19. The exhaust cover member 31 is configured, for example, to vertically extend along the sidewall of the reaction vessel 11. For example, an exhaust pipe 34 having a vacuum pump 32 and a pressure adjustment valve 33, which constitute a vacuum exhaust unit, is connected to a lower portion of the exhaust cover member 31.
A first source gas supply path 41 and a second source gas supply path 42 for supplying a silane-based gas serving as a source gas, for example, dichlorosilane (DCS: SiH2Cl2), are inserted into the sidewall of the manifold 2. A first source gas nozzle 43 (hereinafter, referred to as a “first nozzle”) and a second source gas nozzle 44 (hereinafter, referred to as a “second nozzle”) are installed at the leading portions of the first source gas supply path 41 and the second source gas supply path 42, respectively. Each of the first nozzle 43 serving as a first source gas supply unit and the second nozzle 44 serving as a second source gas supply unit is made of, for example, a quartz tube having a circular cross section and, as shown in
Next, the first nozzle 43 and the second nozzle 44 will be described in detail with reference to
On the other hand, a plurality of slots (holding areas) are vertically provided with equal intervals in the wafer boat 3, and the wafers W and the dummy wafers 10 are horizontally held in the respective slots. A plurality of wafers W are held in upper and lower portions of the wafer boat 3, respectively, while, for example, a plurality of dummy wafers 10 are held between the group of the wafers W in the upper portion and the group of the wafers W in the lower portion to divide the groups of the wafers. In this embodiment, the area in which the group of the wafers W in the upper portion is held is represented as a holding area W1 in the wafer boat 3, the area in which the group of the wafers W in the lower portion is held is represented as a holding area W2 in the wafer boat 3, and the area in which the dummy wafers 10 are held is represented as a holding area WO. The film forming apparatus 1 is configured such that silicon nitride (SiN) films having different film thicknesses can be formed by individually performing ALD on the wafers W of the holding area W1 and the wafers W of the holding area W2, respectively, in the same reaction vessel 11.
In
Referring back to
As shown in
Next, a gas supply system installed in the film forming apparatus 1 will be described with reference to
Similarly, the second source gas supply path 42 has one end connected to the first source gas supply path 41 between the valve V12 and the flow rate adjustment unit MF13 and is provided with a valve V21, a second tank 62, and a valve V22 in this order from the reaction vessel 11. Also, the second source gas supply path 42 branches at a downstream side of the valve V21 and is connected to the supply source 7 of the N2 gas through a second purge gas supply path 72 having a valve V23 and a flow rate adjustment unit MF24, which are provided in this order toward an upstream side.
The first tank 61 and the second tank 62 are configured such that when DCS gases are continuously introduced into the first tank 61 and the second tank 62, respectively, by closing the valves V11 and V21 at their downstream sides and opening the valves V12 and V22 at their upstream sides, the DCS gasses are stored in the first tank 61 and the second tank 62 to increase the pressures of the tanks 61 and 62. After the pressures of the first tank 61 and the second tank 62 are increased, the valves V11 and V21 at the downstream sides are opened in a state in which the valves V12 and V22 at the upstream sides are closed, thereby supplying the DCS gases in the first tank 61 and the second tank 62 into the reaction vessel 11 at a relatively high flow rate, e.g., about 300 cc/min
The reaction gas supply path 51 has one end connected to a supply source 5 of NH3 gas and is provided with a valve V31 and a flow rate adjustment unit MF32 in this order from the reaction vessel 11. The reaction gas supply path 51 branches at a downstream of the valve V31 and is connected to the supply source of nitrogen gas through a purge gas supply path 73 having a valve V33 and a flow rate adjustment unit MF34, which are provided in this order toward an upstream side.
The film forming apparatus 1 includes a control unit 100, as shown in
The timing chart of
As shown in
In this state, the valves V14, V23, and V33 are opened, and N2 gas is supplied as a purge gas into the reaction vessel 11 through the first nozzle 43, the second nozzle 44, and the reaction gas nozzle 52, thereby purging the inside of the reaction vessel 11 (
The DCS gas is limitedly supplied only to the holding area W1 while the supply thereof into the holding area W2 is prevented, due to various points, e.g., a point that the gas ejection holes 431 of the first nozzle 43 are limitedly opened only to the holding area W1 among the two holding areas W1 and W2, i.e., the gas ejection holes 431 is not opened to the holding area W2, a point that the purge gas is supplied to the holding area W2, and a point that the holding areas W1 and W2 are spaced apart from each other since the holding area W0 of the dummy wafers 10 is disposed between the holding areas W1 and W2. The DCS gas supplied to the holding area W1 flows from one side of a surface of each wafer W in the holding area W1 to the other side thereof, so that molecules of the DCS gas are adsorbed onto the surface of the wafer W. Remaining surplus DCS gas flows downward in the exhaust cover member 31 at the other side of the wafer W due to the exhaust through the exhaust pipe 34 and is removed through the exhaust pipe 34 together with the purge gas supplied to the holding area W2 and introduced into the exhaust cover member 31.
Thereafter, the valve V11 is closed to stop the supply of the DCS gas from the first nozzle 43. Then the valves V 14 and V33 are opened to supply the purge gas into the reaction vessel 11 from the first nozzle 43, the second nozzle 44, and the reaction gas nozzle 52, in the same manner as Step S1 shown in
The active species are supplied to the holding areas W1 and W2. Thus, in each wafer W of the holding area W1, the molecules of the DCS gas adsorbed onto the surface of the wafer W react with the active species, and silicon atoms in the DCS gas are nitrided, thereby generating a molecular layer of silicon nitride (SiN) (
Thereafter, the valve V31 is closed, so that the supply of the NH3 gas into the reaction vessel 11 is stopped, and simultaneously, the high-frequency power source 17 is turned off to stop the generation of plasma. Then, the valves V14, V23, and V33 are opened, and the purge gas is supplied into the reaction vessel 11 from the first nozzle 43, the second nozzle 44, and the reaction gas nozzle 52, in the same manner as Steps 51 and S3 shown in
Thereafter, the supply of the DCS gas is stopped by closing the valves V11 and V21, and the purge gas is supplied into the reaction vessel 11 through the first nozzle 43, the second nozzle 44, and the reaction gas nozzle 52 by opening the valves V14, V23 and V33, in the same manner as Steps S1, S3, and S5, so that the DCS gas remaining in the reaction vessel 11 is purged (Step S7). Then, the valves V11, V21, and V33 are closed, and simultaneously, the valve V31 is opened. Thus, in the same manner as Step S4 shown in
Thereafter, the high-frequency power source 17 is turned off, and simultaneously, the valve V31 is closed, so that the supply of the NH3 gas is stopped. Then, Steps S1 to S8 described above are repeatedly performed. Whenever a set of Steps S1 to S8 is performed once, two molecular layers of SiN are laminated in the holding area W1, and one molecular layer of SiN is laminated in the holding area W2. Since the numbers of molecular layers laminated in the holding areas W1 and W2 are different from each other after a single set of Steps S1 to S8, SiN films having different film thicknesses are formed in the holding area W1 and the holding area W2, respectively. After Steps S1 to S8 are performed a predetermined number of times, the pressure of the reaction vessel 11 is returned to an atmospheric pressure by supplying the nitrogen gas into the reaction vessel 11 from the first nozzle 43, the second nozzle 44, and the reaction gas nozzle 52, in the same manner as Step S1 described above. Then, the wafer boat 3 is carried out (unloaded), and the wafers 10 and the dummy wafers 10 are carried out from the slots of the wafer boat 3.
According to the film forming apparatus 1, the holding area W0 of the dummy wafers 10 is formed between the holding areas W1 and W2 of the wafers W in the wafer boat 3. In addition, the step in which the purge gas is supplied to the holding area W2 from the second nozzle 44 while the DCS gas is limitedly supplied only to the holding area W1 from the first nozzle 43, thereby preventing the DCS gas from being supplied to the holding area W2, and the step of supplying the DCS gas to both the holding areas W1 and W2 are performed. Accordingly, molecular layers of SiN, which are different in the laminated number, are laminated in the holding areas W1 and W2, thereby enabling to form SiN films having different film thicknesses. Thus, it is possible to improve the production efficiency of the film forming apparatus 1 and to decrease the number of dummy wafers 10 while reducing the cost required in the film forming process, by preventing the overhead time described in the BACKGROUND section from being repeatedly required, compared with the case where the wafers W are held and processed in only one holding area W1 or W2 in the wafer boat 3. In this embodiment and embodiments described later, the number of dummy wafers 10 of the holding area W0 is not limited to plural numbers and may be one.
Then, a film forming apparatus 8 as a modification of the film forming apparatus 1 will be described with reference to
In each diagram in
The supply of the DCS gas in the film forming cycle is limitedly performed only to a specified holding area, as described above. While the supply of the DCS gas is performed in a certain holding area, the purge gas is limitedly supplied only to a holding area in which the film forming cycle is not performed, so that the supply of the DCS gas to other holding areas is prevented. The holding area to which the purge gas is supplied as described above is indicated by “N2 purge” in the diagram and may be simply described as “a holding area in which the N2 purge is performed” in the following description. While the purge gas and reaction gas are supplied to the holding area in which the film forming cycle is performed, the purge gas and the reaction gas are also respectively supplied to other holding areas, in the same manner as the film forming apparatus 1.
The diagram indicated by “Process A1” in
Then, Process A2 of
Next, Process A3 of
On the other hand, the film forming cycle may be started from an arbitrary holding area. In Process A5 of
On the other hand, the holding area in which a film having large thickness is formed may be set to an upper portion or a lower portion of the wafer boat 3. Unlike Processes A1 to A6, in Processes A7 and A8 of
In the same manner as Processes A1 to A6, in Processes A9 to A14 shown in
Next, Process A10 will be described. The film forming cycle is performed in the holding areas W1 to W3 once in Sequence 1, the film forming cycle is performed only in the holding areas W2 and W3 once in Sequence 2, and the film forming cycle is performed only in the holding area W3 once in Sequence 3. Then, a cycle of Sequences 1 to 3 is repeatedly performed ten times. As described above, in Process A10, a cycle set including i) a film forming cycle set to be performed in one holding area and another holding area and ii) a film forming cycle set to be performed only in the another holding area without performing in the one holding area after the film forming cycle of i) is set to be performed plural times.
Then, Process A11 will be described. The film forming cycle is performed in the holding areas W1 to W3 once in Sequence 1, the film forming cycle is performed in the holding area W2 once in Sequence 2, and the film forming cycle is performed in the holding area W3 twice in Sequence 3. Then, a cycle of Sequences 1 to 3 is repeatedly performed ten times. Also, Process A12 will be described. The film forming cycle is performed in the holding area W1 once in Sequence 1, the film forming cycle is performed in the holding areas W2 and W3 twice in Sequence 2, and the film forming cycle is performed in the holding area W3 once in Sequence 3. Then, a cycle of Sequences 1 to 3 is repeatedly performed ten times.
In Processes A9 to A12, when a cycle set of Sequences 1 to 3 is repeated ten times, the holding areas W1, W2 and W3 are subjected to the film forming cycles a total of ten times, twenty times and thirty times, respectively. The number of times the film forming cycle is performed in the holding area W1, the number of times the film forming cycle is performed in the holding area W2 and the number of times the film forming cycle is performed in the holding area W3 in each cycle set can be determined by dividing the total numbers of times of the film forming cycles in the holding areas W1 to W3, i.e., ten times, twenty times and thirty times, by ten which means the number of times the cycle set of Sequences 1 to 3 is repeated, respectively.
In Process A13 of
In Processes A17 and A18 of
In Process A18, the film forming cycle is performed in the holding areas W1 to W3 once in Sequence 1, the film forming cycle is performed in the holding areas W2 and W3 once in Sequence 2, the film forming cycle is performed in the holding area W3 three times in Sequence 3. The film forming cycle is performed in the holding areas W2 and W3 three times in Sequence 4, and the film forming cycle is performed in the holding area W3 twice in Sequence 5. As described above, by appropriately setting the number of times the cycles repeating the sequences are performed and the number of times the film forming cycles are performed in one sequence, it is possible to appropriately adjust the thickness of a film formed on the wafer W of each holding area.
When each of the above-described processes or each of the later-described processes is performed, the output of the heater 35 may be controlled such that the wafers W in the holding areas W1 to W3 have the same temperature. Alternatively, the output of the heater 35 may be controlled such that the wafers W in the holding areas W1 to W3 are different in temperature. The output of the heater 35 may be controlled such that the holding area W0 for the dummy wafers 10 has the same temperature as the holding areas W1 to W3 or such that the holding areas W1 to W3 are different from the holding area W0 in temperature. In this manner, it is possible to independently control the temperature of each holding area of the wafers 10 and the dummy wafers 10.
Next, a film forming apparatus 81 shown in
In the film forming apparatus 81, DCS gases are supplied to the holding areas W1 and W2, for example, from the first nozzle 43 and the second nozzle 44 in parallel. Thereafter, NH3 gas is supplied from the reaction gas nozzle 52 and converted into plasma by the upper electrodes 16, so that active species are limitedly supplied only to the holding area W1. Accordingly, a molecular layer of SiN is formed on a surface of the wafer W of the holding area W1. During the supply of the NH3 gas from the reaction gas nozzle 52, a purge gas is limitedly supplied only to the holding area W2 from the reaction gas nozzle 53, so that it is possible to prevent the active species from reacting with DCS gas on a surface of each wafer W of the holding area W2. Then, NH3 gas is supplied from the reaction gas nozzle 53 and converted into plasma by the lower electrodes 16, so that active species are limitedly supplied only to the holding area W2. Accordingly, a molecular layer of SiN is formed on the surface of each wafer W of the holding area W2. During the supply of the NH3 gas from the reaction gas nozzle 53, a purge gas may be supplied to the holding area W1 from the reaction gas nozzle 52. However, since the DCS in the surface of the wafer W in the holding area W1 is in a reaction-completed state and hence there is no remaining DCS capable of reacting with the active species supplied to the holding area W2, the purge gas may not be supplied.
A film forming cycle including the supply of the DCS gas, the supply of the active species of the NH3 gas to the holding area W1, and the supply of the active species of the NH3 gas to the holding area W2 is repeatedly performed plural times. Since the concentrations of the NH3 gases supplied to the holding areas W1 and W2 are different from each other, SiN films having different film qualities can be formed in the holding areas W1 and W2 by repeatedly performing the film forming cycle. Specifically, it is possible to form SiN films which have, for example, different wet etching rates with respect to a predetermined liquid chemical. In this example, NH3 gas having a high concentration is supplied to the holding area W1 which is more spaced apart from an exhaust port defined by an exhaust pipe 34 than the holding area W2. This is because a gas exhaust rate is lower at an upstream side when viewed from the exhaust port, i.e., a holding area side which is more distant from the exhaust port, so that it is possible to prevent the concentration of the supplied NH3 gas from being lowered.
Instead of making the concentrations of the gases supplied from the reaction gas nozzles 52 and 53 different from each other, the time for which the gas is supplied in single film forming cycle, or the flow rates of the gas may be made different from each other, thereby forming SiN films having different film qualities. In this example, since the DCS gas only needs to be supplied to both the holding areas W1 and W2, the DCS gas may be supplied using a single nozzle which has ejection holes formed to cover the holding areas W1 and W2, as in the reaction gas nozzle 52 of the film forming apparatus 1.
In the film forming apparatus 82, the C2H4 gas is supplied to the holding area W2 in a downstream side as viewed from the exhaust port implemented by the exhaust pipe 34, among the holding areas W1 and W2. With this configuration, the C2H4 gas supplied to the reaction vessel 11 is prevented from being diffused into the holding area W1 and thus exhausted. Accordingly, in the holding area W1, the formation of the SiCN film is more surely suppressed. It is desirable to form a film that requires more many kinds of gases in its formation in the holding area closer to the exhaust port as described above.
In the film forming apparatus 82, a nozzle for limitedly supplying the C2H4 gas only to the holding area W1 may be provided. Along with the limited supply of the C2H4 gas only to the holding area W2, the purge gas is limitedly supplied only to the holding area W1 from the first nozzle 43. Thereafter, before the NH3 gas converted into plasma is supplied to the holding areas W1 and W2, the purge gas is limitedly supplied only to the holding area W2 from the first nozzle 43, along with the limited supply of the C2H4 gas only to the holding area W1. The concentrations of the C2H4 gases supplied to the holding areas W1 and W2, respectively, are different from each other. Accordingly, SiCN films having different doping quantity of carbon atoms may be formed on the wafer W of the holding area W1 and the wafer W of the holding area W2, respectively. The gases available in each embodiment are not limited to these examples. For example, a silicon oxide film may be formed using oxygen gas plasma and a silicon-based source gas.
Evaluation tests performed in relation to the present disclosure will be described. As Evaluation Test 1, a film forming process was performed using the film forming apparatus 1. However, in Evaluation Test 1, the holding area W0 for the dummy wafers 10 was not defined in the wafer boat 3, and wafers W were disposed even in the middle slots of the wafer boat 3. That is, an upper portion of the area mentioned as the holding area W0 for the dummy wafers 10 in the foregoing description on the film forming apparatus 1 was included in the holding area W1 while a lower portion thereof being included in the holding area W2. A silicon wafer having an exposed surface was used as the wafer W. The film forming process was performed according to Steps S1 to S8. However, in the step corresponding to Step S2, the purge gas was supplied to the holding area W1 and the DCS gas was supplied to the holding area W2, instead of supplying the DCS gas to the holding area W1 while supplying the purge gas to the holding area W2. Thus, the thickness of a film on the wafer W of the holding area W2 became greater than that of a film on the wafer W of the holding area W1. In Evaluation Test 1 and later-described Evaluation Tests 2 and 3, the target thicknesses of films formed on the wafers W of the holding areas W1 and W2 were 30 angstroms (3 nm) and 50 angstroms (5 nm), respectively. After the film forming process, the thickness of a film on the wafer W in each slot was measured.
In Evaluation Test 2, in the same manner as Evaluation Test 1, a film forming process was performed with wafers W mounted in the wafer boat 3. The film forming process will be described using the sequences described in
In Evaluation Test 3, a process was performed in approximately the same manner as Evaluation Test 1. That is, the process was performed according to Steps S1 to S8 already described above. However, in order to make the thickness of the film on the wafer W of the holding area W2 greater than that in the holding area W1, the process was performed such that the purge gas was supplied to the holding area W1 and the DCS gas was supplied to the holding area W2 in the step corresponding to Step S2. In this step, the DCS gas was supplied to the reaction vessel 11 without passing through the second tank 62. In the step corresponding to Step S6, as in the above-described embodiment, the source gas was supplied into the reaction vessel 11 from the first nozzle 43 and the second nozzle 44 through the first tank 61 and the second tank 62. Except these differences, Evaluation Test 3 was performed in the same manner as Evaluation Test 1.
The graph of
Next, another example of the process using the film forming apparatus 1 will be described, focusing on differences between this process and the process described in
Hereinafter, sequences of Process B1 will be described. First, if the wafer boat 3 in which the wafers C1 and C2 and the dummy wafers 10 are mounted is loaded into the reaction vessel 11 as already described above, the N2 gas (purge gas) is supplied from the first nozzle 43, the second nozzle 44, and the reaction gas nozzle 52, so that the inside of the reaction vessel 11 is purged (Step T1). Then, after the supply of the purge gas from each of the nozzles 43, 44, and 52 is stopped, the DCS gas is respectively supplied to the holding areas W1 and W2 from the first nozzle 43 and the second nozzle 44, so that molecules of the DCS gas are adsorbed onto the surfaces of the wafers C1 and C2 (Step T2). In Process B1, the DCS gas is supplied from the gas nozzles 43 and 44 at the same flow rate.
After the supply of the DCS gas to the holding area W1 from the first nozzle 43 is stopped, the N2 gas (purge gas) is supplied from the first nozzle 43. Meanwhile, the DCS gas is continuously supplied to the holding area W2 from the second nozzle 44. That is, the DCS is limitedly supplied only to the wafer C2, so that molecules of the DCS gas are continuously adsorbed onto the wafer C2 (Step T3). Thereafter, the supply of the DCS gas from the second nozzle 44 is stopped, and the N2 gas is supplied from the second nozzle 44 and the reaction gas nozzle 52. The N2 gas is also continuously supplied from the first nozzle 43, so that the DCS gas in the reaction vessel 11 is purged (Step T4).
Thereafter, the supply of the N2 gas from each of the nozzles 43, 44, and 52 is stopped. Subsequently, the NH3 gas is supplied from the reaction gas nozzle 52 and simultaneously the high-frequency power source 17 is turned on, so that plasma is generated and active species of the NH3 gas are generated. The active species are supplied to the wafers C1 and C2 to nitride the adsorbed DCS, and a molecular layer of SiN is formed on the surface of each of the wafers C1 and C2 (Step T5). Then, the supply of the NH3 gas is stopped, and simultaneously, the high-frequency power source 17 is turned off, so that the formation of the plasma is stopped. Thereafter, Steps T1 to T5 are repeatedly performed a predetermined repetition number, and molecular layers of SiN are laminated on each of the wafers C1 and C2, thereby forming a SiN film.
As described above, in Process B1, the apparatus 1 is operated such that the flow rates of the DCS gases supplied to the holding areas W1 and W2, respectively, are equal to each other, and the DCS gas is supplied to the wafer C2 of the holding area W2 for a longer time as compared with the wafer C1 of the holding area W1. Thus, with respect to the wafer C2 having a larger surface area, it is possible to prevent the lack of the amount of the DCS gas supplied from a side of the wafer C2. That is, it is possible to prevent the amount of molecules of the DCS gas adsorbed onto a central portion of the wafer C2 from getting smaller than that onto a peripheral portion of the wafer C2. As a result, films can be formed on each of the wafers C1 and C2 such that the deterioration of in-plane uniformity of the film thickness is suppressed. In Process B1, the thicknesses of the SiN films formed on the wafers C1 and C2, respectively, may be equal to or different from each other.
In order to prevent the adsorption amount of the DCS gas onto the central portion of the wafer C2 from getting small, it may be considered that a single gas nozzle having ejection holes formed to cover both the holding areas W1 and W2 is installed and that a relatively large amount of DCS gas is supplied to the gas nozzle such that the DCS gas is supplied to the holding areas W1 and W2 at the same flow rate for the same duration. That is, it may be considered that a large amount of DCS gas may be uniformly supplied to the holding areas W1 and W2. However, as already described above, when the ALD is performed, the DCS gas that is the source gas is adsorbed onto the surface of the wafer W and, in a practical process, the adsorption amount of the DCS gas is not saturated but varies depending on the amount of the DCS gas supplied to the wafer W. That is, even in performing the ALD, as in the chemical vapor deposition (CVD), a film is formed to have a thickness corresponding to the supply amount of the source gas. If a large amount of DCS gas is uniformly supplied to the holding areas W1 and W2 as described above, the thickness of the SiN film formed on the wafer C1 may be excessively increased. In this regard, Process B1 has effectiveness in increasing the in-plane uniformity of the thickness of the wafer C2 and forming SiN films having an appropriate thickness on the wafers C1 and C2. Like the case of the process of
Next, another process example using the film forming apparatus 1 will be described, focusing on differences between this process and Process B1 of
Hereinafter, sequences of Process B2 will be described. First, the wafer boat 3 having the wafers mounted therein is loaded into the reaction vessel 11, and the supply of the DCS gas into the first tank 61 and the second tank 62 is started. The supply of the DCS gas into the second tank 62 is continued even after the supply of the DCS gas into the first tank 61 is stopped, so that a larger amount of the DCS gas is stored in the second tank 62, as compared with the first tank 61. Accordingly, the pressure in the second tank 62 becomes higher than that in the first tank 61.
Then, the N2 gas is supplied from the first nozzle 43, the second nozzle 44, and the reaction gas nozzle 52, so that the inside of the reaction vessel 11 is purged (Step U1). Thereafter, the supply of the purge gas from each of the gas nozzles 43, 44, and 52 is stopped, and the DCS gas is supplied to the first nozzle 43 and the second nozzle 44 from the first tank 61 and the second tank 62, respectively. On the other hand, for the valves V14 and V23 interposed between the N2 gas supply source 7 and the respective nozzles 43 and 44 (see
As described above, since the DCS gas is stored in the tanks 61 and 62 such that the pressure in the tank 62 is higher than that in the tank 61, the flow rate of the DCS gas supplied from the second nozzle 44 is greater than that of the DCS gas supplied from the first nozzle 43. Thus, the DCS gas is supplied at a relatively high flow rate to the wafer C2 having a relatively large surface area, so that the DCS gas uniformly spreads in not only the peripheral portion but also the central portion of the wafer C2. Thus, molecules of the DCS gas are adsorbed onto the surface of the wafer C2 with high in-plane uniformity.
Since an N2 gas as a pressure adjustment gas is supplied to the first nozzle 43 from the gas supply source 7 at a flow rate relatively larger than that of the second nozzle 44, the difference between the total flow rate of the gas ejected from the first nozzle 43 and the total flow rate of the gas ejected from the second nozzle 44 is reduced. As a result, the pressure in the holding area W1 and the pressure in the holding area W2 become equal to each other, for example. Thus, pressure distribution in the holding areas W1 and W2 is adjusted in this manner, so that it is possible to prevent an accident that the DCS gas supplied from the second nozzle 44 is supplied to the holding area W1 due to the disturbance of the gas flow in the reaction vessel 11. For example, (total flow rate of gas ejected to holding area W1 from first nozzle 43)/(total flow rate of gas ejected to holding area W2 from second nozzle 44) ranges from 0.85 to 1.15.
Thereafter, the supply of the DCS gas from the gas nozzles 43 and 44 is stopped and the N2 gas is supplied from the gas nozzles 43, 44, and 52, so that the DCS gas in the reaction vessel 11 is purged (Step U3). Then, the supply of the N2 gas from each of the gas nozzles 43, 44, and 52 is stopped, and NH3 gas is supplied from the reaction gas nozzle 52 and simultaneously the high-frequency power source 17 is turned on, so that plasma is generated. The DCS gas in the surfaces of the wafers C1 and C2 are nitrided by active species of the NH3 gas, so that a molecular layer of SiN is formed (Step U4). While the nitriding process as described above is performed, the DCS gas is supplied and stored in the first tank 61 and the second tank 62.
Thereafter, the supply of the DCS gas into the first tank 61 is stopped while the supply of the DCS gas into the second tank 62 is continued (Step U5). Then, the supply of the DCS gas into the second tank 62 is also stopped. Thus, a larger amount of the DCS gas is stored in the second tank 62 than the first tank 61, and the pressure in the second tank 62 becomes higher than that in the first tank 61 (Step U6). Then, the supply of the NH3 gas from the reaction gas nozzle 52 is stopped and simultaneously the high-frequency power source 17 is turned off, so that the generation of the plasma is stopped. Thereafter, Steps U1 to U6 are repeatedly performed for a predetermined repetition number, and molecular layers of SiN are laminated on each of the wafers C1 and C2, thereby forming a SiN film. The effects described in Process B1 can be also obtained in Process B2 of
When Processes B1 and B2 are performed, wafers W having the same surface area may be mounted in the holding areas W1 and W2. In this case, SiN films having different thicknesses may be formed on the wafers W in the holding areas W1 and W2, respectively. Since, even in the case where the wafers C1 and C2 are mounted in the respective holding areas W1 and W2 in the process shown in
The configurations of the film forming apparatuses and the methods for forming a film already described above may be combined with each other. For example, Processes B1 and B2 of
According to the present disclosure, while a source gas is supplied to one of a first substrate holding area and a second substrate holding area in a state in which the first substrate holding area and the second substrate holding area are divided by substrates for division, a purge gas is supplied to the other substrate holding area. According to another embodiment of the present disclosure, the source gases are respectively supplied at different flow rates to the first substrate holding area and the second substrate holding area, and simultaneously, a gas for adjusting the pressure distribution in the substrate holding areas is supplied to the second substrate holding area. With this configuration, since the processes can be individually performed on the substrates in the first substrate holding area and the substrates in the second substrate holding area, respectively, films having different film thicknesses, different film qualities or different kinds can be formed. Further, the film forming can be performed at the same time even on substrates having different surface areas. Thus, many substrates can be mounted in a substrate holding unit when performing the process, thereby improving the productivity of the apparatus.
While certain embodiments have been described, these embodiments have been presented by way of example only, and are not intended to limit the scope of the disclosures. Indeed, the embodiments described herein may be embodied in a variety of other forms. Furthermore, various omissions, substitutions and changes in the form of the embodiments described herein may be made without departing from the spirit of the disclosures. The accompanying claims and their equivalents are intended to cover such forms or modifications as would fall within the scope and spirit of the disclosures.
Number | Date | Country | Kind |
---|---|---|---|
2014-153094 | Jul 2014 | JP | national |
2015-094907 | May 2015 | JP | national |