Method for microwave plasma assisted CVD diamond coating

Abstract: The invention relates to a method for diamond coating of a large number of discrete components by Microwave Plasma Assisted CVD equipped with a bowl shaped substrate table. Its geometrical shape and configuration results in a more stable plasma, the shape and position of which conform well with the individual components. This reactor geometry also enhances the flow of the excited gas mixtures and therefore a large number of discrete components can be coated simultaneously even at high microwave power.

Description: The present invention relates to a method for diamond deposition directly from a gas mixture excited by a microwave plasma, said method being characterized in that a larger number of individual components can be coated under identical conditions in one single reactor run as compared to what is possible using prior art technology. Production of diamond directly from the gas phase by CVD or PVD technique is of great interest for coating of cutting tools, drill bits, knives, etc. Gas phase deposition of diamond without formation of graphite was reported already in 1977 by Derjaguin and colleagues in Moscow. When the results were reproduced by a group of Japanese scientists in the early eighties, an intensive research in CVD diamond started all over the world. A series of new methods for diamond coating from gas phase has been described, including hot filament, microwave plasma, arc discharge plasma, gas flame, hollow cathode, and different forms of plasma jets. Usually pure hydrogen with the addition of 0.1 to 5.0 % CH₄ is used as gas mixture, but also other hydrocarbon gases can be used as carbon source. In addition, the purity and quality of the diamond film can be controlled by adding other gases, especially gases containing oxygen and/or nitrogen. Different noble gases can also be added to control the process, especially in plasma-based techniques. A relatively early patent is US 4,707,384 that contains references to the earliest work in this area. Low pressure deposition of diamond coatings has a large potential application in the coating of cutting tools like inserts, drills, end-mills etc. However, this method has not yet been applied in large industrial scale. One important reason is that the total area that can be coated under identical conditions is relatively small, frequently a few centimetres in diameter only using prior art technology. This is due to the fact that coating with diamond film needs excitation of the gas phase to temperatures around 2000°C. At the same time, the optimum substrate temperature for diamond deposition is 1000°C or less. This leads to a strong gradient in temperature and chemical composition in the gas. In the case of diamond deposition from a microwave plasma, the excited gas volume has a spherical or near-spherical shape. Toroid-shaped plasmas and other more complicated geometries can also be generated but they have not found any practical application since these types of plasmas tend to be unstable and therefore difficult to control during longer deposition times. Standard practice for diamond deposition is to place the components to be coated on a flat substrate table, which may be equipped with auxiliary facilities for heating and/or cooling of the table. Since a microwave reactor can be considered as a resonance cavity for microwaves, it is customary to use a flat substrate table in diamond coating according to prior art to obtain a standard resonator geometry. However, the combination of a spherical plasma and a flat substrate table results in a radial variation in deposition conditions due to the variation in distance between the plasma and the table, as illustrated by a₁ and a₂ in Fig 1. This is valid also when the table is equipped with extra facilities for heating although in this case it may be possible to obtain a uniform temperature over a 100 mm diameter table. An additional problem with a flat table reactor design is that there is a difficulty in maintaining a symmetric and stable plasma at high microwave powers. Surprisingly, it has now been discovered that it is possible to form a stable microwave plasma with substrate tables having other geometrical shapes. In particular, it is shown according to the invention that a constant distance and intensity between the outer surface of plasma and the inner surface of the table can be obtained with bowl-shaped table in which the components are placed on the inner surface of the bowl and with the plasma being generated inside the bowl and using a suitable combination of table geometry and process parameters. This means that the total number of substrates which can be coated in one process under identical conditions (growth rate, crystalline structure) is increased drastically according to the present invention. Surprisingly, it is also found that this new design of the substrate table leads to an improved stability of the plasma and that the shape and position of the plasma can easily be controlled with great accuracy by adjusting the position of the table horizontally and vertically relative to the microwave cavity and also by adjusting the shape and the inclination of the table walls which also gives a further improvement in the uniformity of the coating over the substrate table. Furthermore, it is found that the improved stability and control of the plasma using the present invention makes it possible to apply higher microwave powers (>1.5 kW) compared to what was possible using earlier technology without causing problems with plasma instabilities. Higher microwave powers result in a more intense plasma and, thus, increase the deposition rate. In addition, the diameter of the plasma ball increases with applied microwave power, making it possible to use a larger table and to further increase the total number of components, which can be coated in one and the same run. Further improvement in the control of the plasma and enhanced deposition rates is obtained according to the invention by placing auxiliary antennas and/or shaping the upper rim of the bowl so that direct coupling between the plasma and the substrate table occurs. With the reactor design according to the invention there is also the possibility to optimize the gas flow pattern by making channels in the substrate table. These channels can be used as gas inlets for all or parts of the incoming gas mixture which also results in preheating the incoming gases or for exhausting the gas from the reactor. Fig 1 shows a schematic drawing of a typical configuration for diamond coating of discrete components, typically cutting tool inserts, according to prior art using microwave plasma. Fig 2 shows a schematic drawing of a substrate table according to the present invention with details showing an example of a design for placing individual components like cutting tool inserts. Fig 3 shows a schematic drawing of an example of the invention in which the substrate table is equipped with a device for horizontal and vertical positioning relative to the inner surface of the microwave cavity. Fig 4 shows a substrate table according to the invention in which the substrate table height H and diameter D are defined. Fig 5 shows a further development of the invention in which the substrate table is equipped with a number of metal wires (antennas) to increase the intensity of the plasma near the substrate surfaces. Fig 6 demonstrates one embodiment according to the invention in which the substrate table is designed so that the plasma couples directly to the table. Fig 7 shows a design according to the invention in which the substrate table is equipped with channels for optimizing the gas flow. In the figures "1" designates the plasma, "2" the substrate table and "3" the individual components to be coated. According to the invention, there is now provided a microwave plasma CVD reactor for diamond deposition of a large number of individual components like cutting tool inserts, in which the components are placed, preferably uniformly, over the inner surface of a bowl-shaped substrate table. The inner surface can be essentially spherical or conical or have a more complex concave surface. Fig 2 shows an example of the invention, as above, in a relatively simple configuration. The bowl-shaped substrate table can be made in one solid piece or be made up by several separate segments. For adjusting optimum coating conditions, the substrate table can be equipped with facilities for x and y translation in the horizontal plane and z translation for vertical height adjustment as well as facilities for table rotation according to Fig 3. In those cases in which the substrate table is made of individual segments, the reactor may be equipped with facilities for translation of the individual segments in the horizontal plane and height positioning. The individual segments can be constructed so that it is possible to adjust the angle of the individual segments relative to horizontal plane. The total number of segments can be between 2 and 16, usually between 2 and 8. The exact shape of the inner surface of the table will vary depending on the number, size and geometry of the components to be coated, the reactor design and the process conditions used. The ratio between the inner surface height, H, and diameter, D, of the substrate table, as defined in Fig 4, can be used as a simple parameter for the characterization of the table. According to the invention, the H/D ratio should be between 0.1 and 2.0, preferably between 0.2 and 0.5. In order to place the components on the table, the inner surface is designed and manufactured with edges, compartments, rods, holes, etc depending on the shape of the component and also on which parts of the components that are the most critical for their function. As an example, in coating of cutting tools according to the invention, the surface of the table should be shaped so that the minimum distance between the cutting edge of the cutting tools to be coated and table surface is at least 1 mm and normally a minimum of 5 mm. One way to reach this goal is using a ledge design as demonstrated in Fig 2. According to the invention, the bowl-shaped substrate table may be equipped with a number of metallic wires and/or rods (antennas) preferably made of tungsten, tantalum, rhenium, graphite and/or some other high temperature material like ceramic materials such as aluminium oxide, silicon carbide, etc., for additional control of the plasma shape. The antennas are mounted on the table so that parts of them protrude from the table surface. The antennas can be curved with one or both ends fastened on the substrate table. They can also extend across the substrate table. The length of the antennas is normally between 2 and 20 mm but even lengths from 1 mm up to 500 mm can be used. Surprisingly, it has turned out that these wires or rods affect the microwave field in the reactor and can be used as elements for further control of the shape and position of the plasma by careful design of the pattern in which they are positioned. Antennas as control elements can therefore be used for further improvement of the uniformity of the plasma but it is also found that such control elements can drastically enhance the growth rate and improve coating quality. Fig 5 shows a schematic drawing of a substrate table equipped with antennas according to the invention. In a further embodiment of the bowl-shaped substrate table according to the invention, the upper rim of the table is extended and shaped differently as compared to the rest of the table. One example of this type of design is shown in Fig 6. Surprisingly it is found that the microwave plasma can be made to couple directly to the table by carefully designing the upper rim of the table. The plasma spreads itself over substrate table in direct contact with the components which are to be coated. With this configuration very high growth rates can be reached. The film obtains a uniform crystalline structure and thickness. It is also shown that a bowl shaped substrate table according to the invention can be used to obtain a more uniform gas flow pattern through the reactor. In one embodiment, the substrate table is equipped with a number of channels through which reactant gases can be introduced or exhausted. Usually between two and ten channels are drilled at suitable positions around the table but it is also possible to have more channels, for example, one at each component to be coated. With this configuration it is surprisingly found that an improvement regarding uniformity and quality of the coating is obtained and also that a remarkable increase in deposition rate can be achieved. In another embodiment of the invention, the reactor is equipped with separate gas inlets for hydrocarbon and hydrogen gas (or for different mixtures of these two gases) in which the hydrocarbon is released through the channels and hydrogen from above the substrate table. The reactive gases are pumped out around the sides of the substrate table or through additional channels in the substrate table. With this configuration not only coating rate and quality and uniformity is improved but also the graphite content of the film is reduced to a minimum. Fig 7 shows a schematic drawing of this embodiment of the invention. The bowl-shaped substrate table can be manufactured in graphite, boron nitride, quartz or other suitable high temperature material. The surfaces for the placing of the components to be coated can be manufactured in an easy-to-machine material such as graphite and subsequently coated with a material that is more suitable from chemical point of view, such as quartz, boron nitride, silicon carbide or aluminium oxide. The substrate table can also be equipped with facilities for separate heating, for example, induction heating or resistive heating. Alternatively, the reactor can be equipped with a separate system for heating, for example, conventional furnace heating or separate heating of the inlet gases. The substrate table itself can also be used to heat up the incoming gases by allowing the gas mixture or part of it to enter the reactor through channels in the heated substrate table. When coating at high microwave powers (>3kW), it may instead be necessary to cool the substrate table using cooling channels in order to avoid overheating of the substrates. In yet another further embodiment of the invention, the gas pressure in the reactor is cyclically varied during deposition. It has been found that cyclic variation of the pressure results in a further improvement of the coating uniformity within a batch. The frequency of the pressure fluctuation is typically between 2 cycles/min and 2 cycles/hour with a ratio between the maximum and minimum pressure usually between 1.2 and 2. Alternatively, a similar enhancement of batch uniformity can be obtained by a similar cyclic variation of the microwave power. In either case it may be required that the reactor is equipped with the necessary control functions to maintain a minimum reflected microwave power in spite of the variation in process conditions. The reactor can be constructed according to the known technology for microwave plasma CVD, for example, with a cylindrical stainless steel cavity with a quartz bell jar in which the microwave plasma is generated. The reactor can be of the "variable-mode" type but most common is a "fixed-mode" microwave applicator. The reactor is normally equipped with gas control system, vacuum pumps and pressure regulators according to conventional CVD technology. The inlet and outlet gases can be arranged according to the known technique for microwave plasma reactors where gases usually arrive from above to pass through the plasma and stream down by the substrate table. For many application it is advantageous that the substrate table is equipped with channels so that the gases are pumped out through the substrate table. In this embodiment of the invention it is even possible to change the gas flow path which allows incoming gases to flow through the substrate table and be pumped out at the top or out over the sides of the substrate table. Especially according to the invention, the microwave reactor can be equipped with two separate gas inlets for the hydrogen and the hydrocarbon gases, in which one gas enters through channels in the substrate table and the other gas arrives from the top or along the sides of the table. It is obvious for those experienced in diamond coating that this method can be used to divide the incoming gas in other proportions and also be applied to other gas mixtures for diamond deposition according to prior art. By optimizing the gas flow according to the method described in the invention, very good coating quality can be obtained over a large number of inserts. For process monitoring and control, the substrate table can be equipped with a number of thermocouples mounted in different positions on the substrate table. Alternatively, the temperature in selected points on the table can be measured with a pyrometer through one or several inspecting windows during the process. The measured temperatures can be used for adjusting the position of the substrate table as well as the angle and the position of each individual segments in those cases in which the table is made of individual segments for obtaining uniform deposition parameters. With the reactor according to the invention, different discrete components can be coated with diamond. In particular, the reactor design according to the invention is suitable for diamond coating of components made of high speed steel, cemented carbide, cermets, ceramics, cubic boron nitride, diamond and other typical tool materials. In addition, the reactor according to the invention is especially well suited for coating of tools such as inserts, end mills, twist drills, drill bits, knives, scalpels, tool-adhesive-bonding (TAB) tools, etc.. The common frequency for generating microwave plasma is 2.45 Hz and all the examples below are given for a reactor tuned to this frequency. However, it is obvious for those skilled in the art that the frequency determines the size of the plasma. For example, it is possible to obtain a spherical plasma with approximately three times larger diameter as compared to 2.45 GHz by using 915 MHz. Thus, it is possible with a reactor constructed according to the invention to directly increase the number of components that can be coated in a single run with approximately a factor of 10 by reducing the microwave frequency to 915 MHz. Example 1 In one embodiment of the invention, a conventional "fixed-mode" microwave plasma reactor made of stainless steel was used, equipped with a quartz bell-jar, a 1.5 kW microwave power supply and 3.5 kW power supply (10-100 kHz) for induction heating of the substrate table. A bowl-shaped substrate table made of graphite with an outer diameter of 120 mm and with the inner surface of the table inclined 45 degrees relative to the horizontal plane, in the following designated table design A, was used. The inner surface of the table was equipped with ledges at four different levels suitable for loading quadratic inserts, for example, SPUN 120304 geometry. Inserts were also placed on the bottom horizontal surface with a diameter of 40 mm. In total, 59 inserts can be loaded into the reactor using this table with the following number of inserts on each level, where level 1 is the lowest and level 5 is the top level: Level 1 2 3 4 5 Number of inserts 4 8 12 16 19 With the conventional technique a flat substrate table with 100 mm diameter can hold 24 inserts on three different radial distances from the centre of the table. Diamond deposition was performed with 1 % CH₄ in H₂ with a total gas flow of 1 l/min and 1500 W microwave power. Silicon nitride inserts were used as substrates. The temperature was adjusted so that an average temperature of 900°C on the inserts was reached. After 20 hours deposition, the following film thickness values were obtained at the different positions on the substrate table: Known technique According to the invention Radial distance, mm Film Thickness, µm Level Film Thickness, µm 7 12 1 8 22 8 2 11 40 4 3 10 4 9 5 3 With the demand on a maximum 25% variation in the film thickness, only 12 inserts were produced with the known technique while with the substrate table according to the invention, it increases to 38 inserts. In machining tests (face milling Al-18 % Si alloy, wet, cutting speed 1500 m/min, feed/tooth 0.15 mm/rev and depth of cut 1.0 mm) of inserts from different levels the following tool lives were obtained: Known technique According to the invention Radial distance, mm Tool life, minutes Level Tool life, minutes 7 10.2 1 7.1 22 3.3 2 12.6 40 0.3 3 11.3 4 9.8 5 0.2 With a demand on a tool life time of minimum 5 minutes and a maximum variation of 25% in tool life, only four accepted inserts were produced with the known technique whereas with the reactor design according to the invention a total of 34 accepted inserts were produced. Example 2 With the same microwave reactor as in example 1 and also with the same substrate tables according to the known technique and according to the invention, the microwave power was increased to 3500 W by using a 5 kW microwave power supply. The average substrate temperature was maintained at 900°C by adjusting the substrate table heating. In this case the following results were obtained: Known technique According to the invention Radial distance, mm Film Thickness, µm Level Film Thickness, µm 7 5 1 12 22 17 2 16 40 7 3 18 4 16 5 15 With a demand of a maximum variation in film thickness of 25%, this means that the known technique gave eight coated inserts while with the reactor design according to the invention 54 coated inserts were produced. Using the known technique also resulted in a large variation in film thickness between inserts placed at same distance from the centre. As an example, film thickness for inserts placed at a radial distance of 22 mm, typically varies from 11 to 22 µm measured on the edges facing toward the plasma and between 8 and 17 µm for those edges facing outward. When the inserts were placed according to the invention, the total variation in film thickness for all inserts on levels 2 to 5 was 5 µm with no measurable differences between the different edges on the same insert. In machining tests of inserts from different positions the following average tool lives were obtained: Known technique According to the invention Radial distance, mm Tool life, minutes Level Tool life, minutes 7 1.3 1 12.1 22 14.4 2 18.1 40 3.1 3 20.4 4 19.2 5 16.9 Example 3 In a further coating experiment, using the same process parameters as in example 2, the microwave power was increased to 4600 W. With a reactor according to the known technique, it was not possible to form a stable plasma since the plasma tends to jump to one side of the quartz bell-jar wall. This results in melting the quartz bell-jar in less than a minute. With the reactor according to the invention, the plasma was still stable as in the earlier examples and the higher power resulted in a further increase in the deposition rate. Under the same deposition period as in example 2, the following film thickness values were achieved: Level 1 2 3 4 5 Film thickness, µm 17 21 23 22 22 With a substrate table with the same geometry as the one described above, but with an outer diameter of 145 mm, the volume was increased to 86 inserts by placing 28 inserts on level 6. This table was in the following designated embodiment B of the invention. In an experiment with parameters as above but with the enlarged graphite table, embodiment B, the following film thickness values were obtained: Level 1 2 3 4 5 6 Film thickness, µm 15 17 18 18 16 16 Example 4 Another graphite table with the same basic geometry as embodiment B in example 3 but equipped with 172 holes, 6 mm in diameter, was manufactured. The holes were positioned at the points where the edge corners on two adjacent inserts were located during deposition. During deposition a fraction of the incoming gases was pumped out through these holes. This table was designated embodiment C of the invention. In one deposition experiment performed with this table and parameters as in example 3 the following results were achieved: Level 1 2 3 4 5 6 Film thickness, µm 20 22 22 21 21 20 Comparing the results with example 3 above shows that an increase in the deposition rate and further reduction in film thickness variation were obtained. Example 5 A graphite table with the same geometrical design as embodiment C was manufactured. This table was coated with 15±5 µm thick SiC film by conventional CVD process at 1100°C according to the known technique. This substrate was called embodiment D of the invention. In a deposition experiment with the same process parameters as in example 3, the following film thickness values were obtained: Level 1 2 3 4 5 6 Film thickness, µm 18 19 19 20 19 17 Substrate table D gives a slight reduction in deposition rate as compared with table C. However, investigation of the resulting coating by Scanning Electron Microscopy indicated an improved purity of the diamond film since severe charging-up occurred due to the irradiation of the electron beam. Example 6 Ceramic Si₃N₄ inserts with the geometry SPKN 12 03 EDR were coated with 12±1 µm thick diamond film in seven different deposition experiments. The reactor design and the process parameters for the different experiments are given below. A constant film thickness was obtained by control of the deposition time: 1) Coating with the known technique with 1.5 kW micro wave power and a flat substrate table with the inserts placed at 22 mm distance from the centre and process parameters as in example 1. 2) Coating according to the invention with 1.5 kW micro wave power and with table embodiment A. Test inserts were placed on levels 1-4 and dummy ones on level 5. Process parameters as in example 1. 3) Coating with the known technique with 3.5 kW microwave power and a flat substrate table with inserts placed at 22 mm distance from centre and process parameters as in example 2. 4) Coating according to the invention with 3.5 kW microwave power using table embodiment A. Test inserts were placed on the levels 2-5 and dummy ones on level 1. Process parameters as in example 2. 5) Coating according to the invention with 4.6 kW microwave power and with table embodiment B with test inserts on levels 1-6 (no dummy inserts). Process parameters were as in example 3. 6) Coating according to the invention with 4.6 kW microwave power and with table embodiment C. Test inserts were placed on levels 1-6 (no dummy inserts). Process parameters were as in example 4. 7) Coating according to the invention with 4.6 kW microwave power and with table embodiment D. Test inserts were placed on levels 1-6 (no dummy ones). Process parameters as in example 5. Ten inserts were randomly chosen from each deposition experiment. For coating with known technique, as in experiments 1 and 3, two runs were required to produce enough test inserts. Testing was performed in a milling operation of a water pump casing made of Al-8%Si-3.5%Cu. The machining conditions were as follows: v=2000 m/min s=0.05 mm/rev a=3 mm The coating was considered worn-out when extensive burr formation on the machined surface occurs. The total number of water pump casings which were produced for the different deposition experiments were as follows: Number of casings 1) 1.5 kW according to the known technique 3590 2) 1.5 kW according to the invention embodiment A 14122 3) 3.5 kW according to the known technique 6212 4) 3.5 kW according to the invention, embodiment A 29459 5) 4.6 kW according to the invention, embodiment B 41791 6) 4.6 kW according to the invention, embodiment C 43811 7) 4.6 kW according to the invention, embodiment D 58922

Claims: A method for diamond coating of a number of discrete components with a known technique of microwave plasma excited gas mixture characterized in a reactor equipped with a bowl shaped substrate table, preferably with an essentially conical or spherical shape with concave inner surface for placing of the components to be coated on said inner surface of said table. A method for diamond coating according to claim 1 characterized in that the geometrical shape, configuration and position of said table enable to stabilize the plasma and control its shape and position in such a way that its outer surface conforms well with the surfaces of components to be coated. A method for diamond coating according to any of the preceding claims, characterized in that the ratio of height H and diameter D of the bowl shaped substrate table is between 0.1 and 1.0, preferably between 0.2 and 0.5. A method for diamond coating according to any of the preceding claims characterized in that the substrate table is divided into 2 to 16 segments, preferably between 2 and 8, where each segment can be translated individually in the horizontal plane and/or inclined individually relative to the horizontal plane and central axis and/or rotated in the horizontal plane. A method for diamond coating according to any of the preceding claims characterized in that the bowl shaped table is equipped with a system of channels for optimized gas flow over the individual components. A method for diamond coating according to claim 5 characterized in that the reactor is equipped with one or more separate gas inlets where at least one of the inlets enters the reactor by channels in the substrate table. A method for diamond coating according to any of the preceding claims characterized in that a system of metallic and/or ceramic wires and/or rods is mounted on the bowl shaped table to further control the shape and position of the plasma as well as yield additional excitation of the gas mixture. A method for diamond coating according to any of the preceding claims characterized in that the upper edge of the bowl is shaped so that the plasma couples directly to the table and thereby stays in direct contact with whole table surface and on the components mounted thereon. A method for diamond coating according to any of the preceding claims characterized in that the bowl shaped substrate table is equipped with ledges, rods, compartments and/or holes adapted for coating of inserts, end-mill, twist drills, drill bits or other tools and similar components. A method for diamond coating according to claim 9 characterized in that the shape of the ledges, rods, compartments and/or holes used is such that the minimum distance between the cutting edge of the tools to be coated and table surface is at least 1 mm, preferably a minimum of 5 mm. A method for diamond coating according to any of the preceding claims characterized in that the gas pressure and/or microwave power is varied cyclically during the deposition. A substrate table for diamond coating of a number of discrete components with a known technique of microwave plasma excited gas mixture characterized in being bowl shaped, preferably essentially conical or spherical, with concave inner surface for placing of the components to be coated on said inner surface of said table.

Inventors: SHAHANI HAMID, SJOESTRAND MATS, SOEDERBERG STAFFAN, SHAHANI, HAMID, SJOESTRAND, MATS, SOEDERBERG, STAFFAN, Sjöstrand, Mats, Söderberg, Staffan
Applicants: SANDVIK AB, SANDVIK AKTIEBOLAG
Application year: 1992
Main classification: C23C16
IPC codes: C23C16, B23P15, B23B27, H01L21, C30B29