Cat-CVD Technology

1. Features of Cat-CVD

 Most of industrial consumer products are coated by various thin films. Some of products may be covered with painting or plating films. Thin film coating is also seen in modern electronic products. In such cases, quite often, the quality of coating films decides the performance of the electronic products themselves. For instance, in liquid crystal display (LCD), transistors made by semiconductor thin films are working as a key device to control the brightness and colors of pictures. Ultra-large scale integrated circuits (ULSI), used in computers, contain so many thin films and the quality of such thin films decides the performance of ULSI. In solar cells, also, the quality of thin films determines their energy conversion efficiency.
 Thin films used in such electronic products are often required to be prepared at temperatures as low as 300℃ or less, keeping film quality as high as possible. The plasma enhanced chemical vapor deposition (PECVD) method, so far, appears used to obtain thin films satisfying such requirements. In PECVD, source gases are introduced into a vacuum chamber, where the molecules of source gases are decomposed by the physical collisions with energetic electrons generated in plasma, and the decomposed species are transported to the substrates to form films. This PECVD method is one of the most successful thin film technologies; however, because of the progress of industry society, the requirements are getting even severe. In PECVD, the surfaces of substrates or of previously deposited thin films always suffer from the damages by the collisions with ions generated in plasma along with energetic electrons. For the further improvement of performance of consumer electronic products, this plasma-induced damage becomes a serious problem in PECVD. Thus, the development of a new method obtaining high quality thin films at temperatures below 300℃ with no plasma-damages is strongly required.
 Our developed new CVD method, named as Catalytic Chemical Vapor Deposition (Cat-CVD) method, is to satisfy these requirements. In Cat-CVD, the molecules of source gases are decomposed in a vacuum chamber by the catalytic cracking reaction with heated catalyzers, and the cracked species are transported to the substrates to form films there. In the mechanism of gas decomposition in Cat-CVD, the films or substrates are free from plasma damages. Since metal wires are often used as catalyzers, this method is also known as “Hot-Wire CVD”, or “HWCVD”.

 Fig.1 Schematic view of PECVD and Cat-CVD apparatuses.

 Figure 1 shows schematic view of PECVD and Cat-CVD apparatuses. In PECVD, the two parallel electrodes have to be electrically insulated from the chamber to generate glow discharge between these two electrodes. In most cases, the glow discharge plasma is excited by radio frequency (RF) alternative wave of 13.56 MHz, and a matching system to transfer the RF power to the electrodes has to be equipped, in addition to a RF power generator. Thus, the system of PECVD is complicated. On the other hand, in Cat-CVD, only catalyzing wires are installed inside the chamber, and the deposition system becomes very simple.
 Recently, it has been reported that the quality of PECVD films can be improved by increasing plasma frequency from RF to Very High Frequency (VHF) range. The increase of plasma frequency makes it even complicated to adjust the stable plasma generation. Particularly, since the films deposited on the electrode or other area of the chamber cause the change of plasma conditions, the chamber has to be cleaned quite often to keep the same stable plasma. In addition, by increasing plasma frequency, it becomes even harder to realize uniform film deposition in large area over 1.5 m square.
 There have been so many reports and papers demonstrating promising effects of the increase of plasma frequency; however, it is not so easy to install VHF plasma into the mass-production without adapting particular structures such as ladder electrodes.
 Particularly, when the frequency used in mass-production system becomes higher than 27 MHz, the adjustment of plasma for long times is getting even more difficult without frequent cleaning. When we introduce VHF plasma into the mass-production, we have to carefully estimate the film-preparation cost including cleaning gas cost.
 On the other hand, there are substantially the following advantages in Cat-CVD:

  • 1)There is no worry about plasma damage.
  • 2)Since there are no special insulators at the electrodes, the mechanical system for mass-production can be easily installed in the substrate holders or other parts.
  • 3) Since we need not worry about abnormal glow discharge, the film can be deposited uniformly on the samples with various shapes including sharp edge. This advantage is used to deposit Poly-Tetra-Fluoro-Ethylene (PTFE, or Teflon in commercial name) films on razors to make their surface smooth.
  • 4) The cost of apparatus can be lowered in principle, since the deposition system is so simple.
  • 5) Large area deposition is easy by simply expanding the spanning area of catalyzing wires.
  • 6) When the catalyzing wires are hung vertically, the films are deposited on the both sides of the catalyzer and the productivity becomes double.

 Figure 2 demonstrates the images of the interface between amorphous-silicon (a-Si) and crystalline-silicon (c-Si) observed by the Scanning Transmission Electron Micro-scope (STEM) with a spatial resolution as high as 0.08 nm. The figure shows the images of both Cat-CVD a-Si/c-Si interface and PECVD a-Si/c-Si interface. The STEM machine used here, JEOL JEM-ARM200F, is one of the top grade experimental equipments possessed by JAIST. The machine was, used be, the world’s first operating machine. To keep the spatial resolution of 0.08 nm, the room is specially designed to avoid the vibration conducted from the land and the vibration made even by the sound or voice in the room. The room has a heavy concrete floor with a thickness more than 1 m and all walls are covered with the sound absorbers to be kept silent.
 In this case, the samples are observed from the direction of (110), and thus, many Si-Si pairs with an atom-distance of 0.15 nm are observed in c-Si regions as predicted by the crystalline model of c-Si.
 In case of Cat-CVD a-Si/c-Si interface, the c-Si image is fading into a-Si dark image with a transition layer of 0.6 nm, but in case of PECVD, it is 1.8 nm. In the observation by STEM, the image is drawn by electrons transmitted through the sample with a thickness of 10 to 20 nm. That is, the wider transition layer seen in the PECVD a-Si/c-Si interface means larger fluctuation or roughness at the interface than that in Cat-CVD a-Si/c-Si interface. The depth of damages created by collisions with Si atoms can be evaluated theoretically by using the formula of nuclear stopping power of Si atoms in c-Si. The depth of damages by Si atoms with energy of about 50 eV is estimated to be 1 to 2 nm. The collision energy of 50 eV is quite common as the energy often seen at the sheath of plasma. In case of PECVD, it is natural to think that Si atoms at the surface with a layer thickness of 1 to 2 nm are removed or scattered to make rough surface or interface. This is the real figure of plasma damages.
 This observation has been carried out several times by using PECVD samples made by outside of JAIST. As a result, it is found that the reproducibility is very high, and that the transition layer from c-Si to PECVD a-Si is always 1.8 to 2.0 nm.
 So far, the roughness at the interface between PECVD films and c-Si substrates has been accepted in industry or many cases. However, when really plasma-damage-less interface is required for achieving top grade device performance, this difference between Cat-CVD and PECVD interfaces would have serious meaning.

 Fig.2 STEM images of Cat-CVD a-Si/c-Si interface (left), and PECVD a-Si/c-Si interface (right). Intensities from crystalline signals are
      also shown in the lower figures.

 In addition to this, 5) is also a great advantage in Cat-CVD. In PECVD, when the deposition area is expanded, as mentioned briefly above, the uniformity is lost because of generation of standing wave of RF wave. For instance, the wavelength of 13.56 MHz frequency is about 22 m in a vacuum. The length between the position of peak power and that of power 0 should be 1/4 of wavelength, and thus, it is about 5 m. The length is shortened when the chamber is filled by source gases, since the velocity of electromagnetic waves decreases in medium. When the size of sample tray is about 2 m in mass-production system, the value is no longer negligible for uniform deposition. If the plasma frequency is increased to 60 MHz for improving the film quality, for instance, it is even harder to realize uniform deposition on large area. For improvement of productivity for film deposition to reduce the film preparation cost, large area deposition is inevitable approach. This is a strong obstacle for PECVD, particularly, for VHF PECVD.
  Here, we have to mention some of useful and effective attempts to overcome the demerit of PECVD. One idea is the introduction of “Hollow-Cathode” system, carried out in PECVD machine used in fabrication of thin film transistors of LCD production. In a large electrode-plate, small holes with a diameter less than 10 mm and a depth about also 10 mm are formed. In such a small hole, a small gas inlet hole and insulated small electrode are installed. Glow discharge is generated inside such a small holes. This type of system is called as “Hollow Cathode”. If such small Hollow Cathodes are arrayed on the electrode-plate keeping a distance of two Hollow Cathodes at 100 mm or less, large area deposition becomes possible without worry about standing wave problems, although high level technology is required to keep uniform glow discharges in many arrayed small Hollow Cathodes. By this technology, already, the apparatus for 3 m size deposition, so called “10th generation PECVD machine”, has been installed in LCD industry.
  Even in this case, keeping plasma stably is still a big issue. When films are deposited near electrodes at Hollow Cathodes, plasma conditions are changed. Thus, the frequent cleaning of the chamber and also of the areas near electrodes are necessary. In the mass-production system, the etching gases such as nitrogen tri-fluoride (NF3) are excited by microwave-plasma at the outside of the chamber and such excited species are introduced into the Hollow Cathodes through gas inlet holes, in order to clean up the Hollow Cathodes and the area surrounding them. This production system is quite successful in LCD industry; however, it should be noticed that the cost of NF3 is not negligible. In addition, when we use halogen gas such as NF3, vacuum system should be prepared for it. All these things are reason for cost increase in this system. In case of LCD industry, the increase in cost can be absorbed by mixing with other costs. However, in solar cell industry, that should be difficult since further lowering the production cost is always required.
  Please notice that there are no worries about constructing such complicated and expensive systems in Cat-CVD.

 Fig.3 Schematic view of vertical type Cat-CVD apparatus. This system is used in large area mass-production machines.

 Figure 3 shows schematic view of the Cat-CVD apparatus with catalyzers hung vertically in the deposition chamber, as mentioned at above 6). Here, two sample trays are set in parallel at the both sides of hanging catalyzing wires. After a-Si films are deposited for more than 1 month continuously, the hanging parts of catalyzing wires and the mechanical parts for moving trays are all slid out from the deposition chamber for chemical cleaning carried out at elsewhere outside of the chamber. The same parts which have been cleaned up are re-used and newly set at the top of the chamber. Since the most of areas inside chamber are all covered with trays, there is no place of chamber cleaning. We need not to use halogen gas at all and cleaning frequency is very low. This is one of the big advantages in Cat-CVD.

 Apart from 6 advantages described above, there is one more important advantage in Cat-CVD.

7) The efficiency of source gas use is by 5 to 10 times higher than that of the conventional PECVD.

 In PECVD, molecules of source gases are decomposed by the physical collisions with energetic electrons. This means that the collisions of a point with another point in 3-dimensional space occur in PECVD as illustrated in Fig. 4, left. The probability of such collisions is not so high, and some of molecules are evacuated without any collisions. On the other hand, in Cat-CVD, molecules are collided with 2-dimensional solid surface; the collisions of a point with 2-dimenasional area is utilized as shown in Fig.4, right. The probability of the collisions becomes high and in general deposition conditions a molecules is collided with the surface of catalyzer by more than 10 times before evacuation. Thus, the efficiency of gas use in Cat-CVD becomes much higher than that of PECVD.

Fig.4 Collisions in PECVD (left) and in Cat-CVD (right)

 The data of gas efficiency in factory is not open in any companies. However, it is guessed that the gas efficiency in PECVD is only several % to obtain high quality films with a cost-effective deposition rate, but that the gas efficiency in Cat-CVD reaches to 30 % or more. In addition, the films with same quality to PECVD films are obtained with almost double the deposition rates in case of Cat-CVD.
 When the saline (SiH4) gas is used as a source gas particularly for large area deposition, this advantage of high efficiency of gas use becomes more remarkable. The volume of exhaust gas after deposition can be reduced and the amounts of dangerous SiH4 gas storage in factory can be also much reduced. These advantages make the film deposition cost low. The superiority of Cat-CVD to PECVD appears clear particularly when large area deposition is carried out without any plasma damages.

2. Reactions on Surface of Catalyzer

 Next, let’s consider what happened in the surface of catalyzer. Although there are various cases for the reactions of gas molecules with the surface of catalyzer, here, at first, we like to concentrate on the decomposition of SiH4 molecules with tungsten (W) catalyzer for simple explanation.

 When a gas molecule reaches at the surface of catalyzer, two types of reactions are expected. One is that the molecule connects with atoms of catalyzer surface by physical-adsorption. The other is that the molecule makes a bond with an atom at the catalyzer surface, by chemical adsorption. In some probabilities, physically adsorbed molecules are converted to chemical-adsorbed ones, although the most of physically adsorbed molecules are desorbed.
 Let’s consider the case when a molecule approaches into a certain distance from the surface of catalyzer. If the sum of the energy of a molecule and the energy of atoms at the catalyzer is larger than the total energy of bonds formed with decomposed molecules and catalyzer atoms, the molecule is likely to be decomposed to lower the total energy of the system and the dissociative adsorption is constructed with catalyzer atoms.
 Figure 5 shows illustration of this dissociative adsorption of SiH4 with W catalyzer for catalyzer temperatures at room temperature (RT) (left) and at over 1,000℃ (right).

Fig. 5  Schematic illustration of chemical dissociative adsorption for SiH4 and W catalyzer system. The temperature of catalyzer is room temperature (RT) (left) and over 1,000℃ (right).

 When a SiH4 molecule approaches to the surface of W catalyzer, even at RT, it is decomposed as SiH4→SiH3+H, to form W-SiH3 and W-H bonds. That is, we have to notice that the decomposition of SiH4 is not happened by the heat but by chemically controlled dissociative adsorption.
 This is a story when the catalyzer temperature is RT. Then, when it is elevated, how does it changes? When the catalyzer temperature is elevated, the W-SiH3 bond starts to vibrate strongly. However, because of the strong binding of W-Si, most of SiH3 remains on the surface with large vibration amplitude. Finally, H atoms in SiH3 are reaching to other W atoms and SiH3 is decomposed to make W-H bonds. It is believed that this happens when the catalyzer temperatures exceeds over 1,000℃. That is, when the catalyzer temperature exceeds over 1,000℃, SiH4 is adsorbed with a configuration of W-Si and 4(W-H) bonds using totally 5 sites on W catalyzer. In other words, when the catalyzer temperature is higher than 1,000℃, SiH4 cannot exist on the W catalyzer surface without forming W-Si and 4 of W-H bonds.
 The bond configuration of dissociative adsorption is determined by the type of molecule and catalyzer materials. In the case of SiH4, as mentioned above, W-Si and W-H is the final form. However, for instance, in case of decomposition of ammonia (NH3), after forming W-NH2 and W-H, NH2 cannot stay on the W catalyzer anymore and desorbs from the catalyzer to supply H and NH2 in space. Decomposition of NH3 needs only 2 sites on W catalyzer. The bond configuration is determined by how long dissociative adsorption can be hold keeping adsorbed states.
 When W-H and W-Si bonds are formed at over 1,000℃, H atoms are soon desorbed into the chamber; however, the most of Si atoms are likely to remain on W surface. If a Si atom remains on W surface for a certain time which is enough to form many W-Si bonds around the first single W-Si bond, and if the number of W-Si bonds exceeds the critical threshold size for forming a silicide block, a part of W surface is covered with silicide. To avoid it, the temperature of catalyzer has to be even more elevated over 1,750 to 1,800℃. This is the reason why the catalyzer temperatures should be elevated over 1,750℃ in case when a-Si films are obtained by Cat-CVD from SiH4 gas with W catalyzer. The heat is not used for decomposition of SiH4, but used only for avoiding silicide formation. Actually, when Tantalum (Ta) is used instead of W as the catalyzer, the temperature can be lowered by about 100℃ from the temperature of W catalyzer. For such a reason, in mass-production systems to prepare a-Si films by Cat-CVD, Ta catalyzers are widely used instead of W catalyzer.

Fig.6  Infrared absorption spectra of PTFE films prepared by Cat-CVD from HFPO with various catalyzing materials and temperatures, The peak height of infrared absorption peaks simply corresponds to the film thickness.

 The story mentioned above is just for explanation of a-Si film deposition. If we change the story for the deposition of PTFE films, relationship between catalyzer and source gas will becomes even clearer.

 Next, let’s consider the case of deposition of PTFE (Teflon) films from HFPO (Hexa-Fluoro-Propylene-Oxide) gas by Cat-CVD. Figure 6 shows the infrared absorption spectra of PTFE films which are prepared from HFPO gas but with various catalyzing metal wires. In the figure, the catalyzers and their temperatures during the deposition are described. This figure simply shows the infrared absorption spectra of various films prepared with the same deposition times. The peak height simply corresponds to the thickness of deposited films with the same deposition times. That is, the figure simply shows the deposition rates of PTFE films when various catalyzing materials are used.

 At first, from the figure, it should be noted that the deposition rates depend on catalyzing materials but not on the temperatures of catalyzer. It is found that PTFE films are easily obtained with larger deposition rates when Nichrome (NiCr), Inconel (commercial name of Nichel (Ni) containing special metal alloys produced by Special Metals Corp.) and Stainless-Steel (SUS) are used as catalyzers. These materials contain Ni atoms. That is, when Catalyzer includes Ni atoms, the deposition rate appears to increase.
 Interesting phenomena can be seen in the figure. When a pure Ni wire is used, the deposition rate is not so faster than that obtained by Ni alloys. This suggests that Ni atoms are essentially needed, but other different atoms are also required probably for reducing the energy for dissociative adsorption of HFPO molecule.
 Figure 7 demonstrates our one speculation for the dissociative adsorption of HFPO on NiCr catalyzer, for better understanding of the phenomena, although there have not been verified at all at the moment. At first, just for explanation of image, HFPO, F3C-FC-O-CF2, is assumed to be dissociatively adsorbed as configuration of Ni-CF3 and Cr-FC-O-CF2. Here, if other metal atom such as Chromium (Cr) is better to make bond with –FC-O-CF2 than Ni, NiCr is better catalyzer than pure Ni. Although it is widely known that HFPO, F3C-FC-O-CF2, is usually decomposed to F3C-(=O)-CF + CF2, we do not know at the moment how such decomposed configuration changes when catalyzing metals exist near HFPO. Please understand that this explanation is completely based on imagination.
 Anyway, this demonstrates that the decomposition of source gas molecule is completely depending on the reaction at the surface of the catalyzer and not depending on only heat. This is the reason why we use the term of “Cat-CVD” instead of simple “Hot-Wire CVD”, “Hot Filament CVD” or other terms.

Fig.7  An imaginary drawing of dissociative adsorption of HFPO on NiCr catalyzer.

 Figure 8 demonstrates the movie showing a drop of water on SUS substrates coated with PTFE by Cat-CVD (left) and without PTFE (right), and Fig.9 demonstrates another movie showing a drop of water on cotton with PTFE coated by Cat-CVD and without coating of PTFE.
 Recently, Cat-CVD technology has been expanding to prepare high quality organic films. This area appears promising for future development.

Fig.8  Hydrophobic property of SUS substrates coated by Cat-CVD PTFE films.


Fig.9  Hydrophobic property of cotton after coating with Cat-CVD PTFE films.
 a) A drop of water on cotton with PTFE coated by Cat-CVD


 b) Without coating of PTFE




3. Features of Cat-CVD Films and Their Application

  Different mechanism of film deposition in Cat-CVD from that of PECVD sometimes makes the property of Cat-CVD films different from that of PECVD. As mentioned above, the probability of gas decomposition in Cat-CVD is much higher than that of PECVD. In the most of deposition for device films, such as a-Si and silicon-nitride (SiNx) films, hydrogenated gases such as SiH4 and NH3 are used as source gases. Since decomposition of these gases are completed, so many H atoms are supplied into the chamber. Consequently, compared with PECVD, the density of H atoms in gas phase is higher, and these excess H atoms work as special role to subtract other H atoms from growing surface of films by forming H2. All PECVD films prepared by hydrogenated source gases have 10 to 20 % H atoms inside films. However, because of this subtraction of H atoms, the contents of remained H atoms inside the films are lowered to a few atomic %. Then, usually, Cat-CVD films are denser than PECVD films.
 Figure 10 shows the density of SiNx films prepared by Cat-CVD, thermal CVD and PECVD. In Cat-CVD, the temperatures of substrates is at 100℃and 300℃, but in thermal CVD, it is at 760℃ and 450℃ and in PECVD at 125℃ and 300℃. It is shown that the density of Cat-CVD films is almost equivalent to that of high temperature thermal CVD and that it is not so degraded even when substrate temperature is lowered to 100℃.

Fig.10  Density of SiNx films prepared by various methods, such as Cat-CVD, Thermal CVD and PECVD.

 Since the density of Cat-CVD films is kept high enough even when the substrate temperatures are lowered to 100℃, the films can be used as gas barrier films protecting organic devices such as organic electro-luminescence (Organic EL or OLED).

 Fig.11 Photographs of organic EL covered with SiNx based films prepared by Cat-CVD at substrate temperatures lower than 100℃ (right) and by the conventional PECVD (left).

  Figure 11 shows the photographs of organic EL after exposed in air of 90% humidity and temperature of 60oC. When the conventional PECVD films are used, after only 40 hours the device is damaged. However, when Cat-CVD films are used, it is not damaged at all, even after 1,000 hours. The acceleration coefficient of this circumstance to common circumstance is about 15. That is, this shows that organic device can be used at least for more than 15,000 hours when Cat-CVD films are used as moisture protecting films.
 Cat-CVD SiNx films are also used for passivation on compound semiconductor devices such as ultra-high frequency transistors and semiconductor lasers and this application is now implemented in industry.
 Table I below summarizes examples of various applications along with the explanation of present status of industrial implementation.

Table I. Applications of Cat-CVD technology along with the present status of actual industrial implementation.

Application Field Places where Cat-CVD is used Results of using Cat-CVD Status for industrial implementation
Si ULSI 1) Gate side-wall and insulators used in ultra-small MOS  transistors.

2) Linar insulator.
1) Lifetimes of MOS transistors can be en-longed by 2 orders of magnitude by suppressing NBTI (Negative Bias Temperature Instability), because of low H content in SiNx films. Competition with ALD (Atomic Layer Deposition)
Not yet implemented in mass-production.
Compound semiconductor devices 1) Passivation on ultra high frequency transistors of GaN, GaAs etc.

2) Passivatoin on laser for optical communication
1) Increase of cut-off frequency and usable powers of GaN , GaAs transistors by reducing surface damages below passivation layers.

2) Increase of power and lifetime by reducing damages, because such damages cause the creation of starting points of degradation.
1) and 2) are both in commercial.
Displays 1) a-Si TFT (Thin Film Transistor)

2) As deposited poly-Si TFT.

3) Gas barrier films on OLED.

4) Photo-sensitive drum for copy machines.
1) Low off-current and high stability can be achieved with large on-off ratio.
2) Mobility over 40 cm2/Vs is obtained by using as deposited poly-Si.
3) Lifetimes over 1,000 hours for Cat-CVD films coated on OLED in 90% humidity and 60oC circumstances.
4) High rate deposition is achieved with high efficiency of gas use.
1) Not yet implemented.

2) Not yet implemented.

3) In checking the possibility.

4) Small scale production is planned.
Solar cells 1) Thin film solar cells.

2) Anti-reflection and passivation coating on c-Si solar cells.

3) a-Si/c-Si hetero-junction cells.
1) Deposition rate is 4 times larger and gas usable efficiency is 1 order higher for Cat-CVD than PECVD.
2) Extremely low surface recombination velocity <0.2 cm/s can be realized by Cat-CVD films.
3) Damage-less deposition of a-Si below c-Si.
Large scale mass-production is going on.
Mechanical engineering 1) Coating method alternative to metalizing plating used for auto-mobile.
2) Coating on razors.
1) Lifetime of coating ability can be en-longed by 1 order by Cat-CVD than conventional metalizing plating for hybrid-car.
2) Low friction surface is made without sacrifice of sharpness.
1) Only trial, at the moment. The conventional way is still usable.

2) In commercial for high grade razors.
Application of high density radicals 1) Removal of photo-resist.


2) Surface cleaning.

3) Improvement of resistivity of ink-jetted or screen-printed metal lines.

4) Low temperature P or B doping into c-Si by newly invented Cat-doping
1) Photo-resist after high dose ion-implantation can be removed without any residuals.
2) Surface of mirrors for EUV lithography is cleaned up.
3) Low resistivity Cu or Ag metal lines can be formed at RT by exposure in high density H atoms generated in Cat-CVD apparatus.
4) By using catalytically cracked species of PH3 or B2H6, P or B atoms can be doped into c-Si at 80oC.
1) Commercial machines have been made. Not so well sold.

2) Already used in apparatus of EUV lithography.

3) In plan for industrial implementation.


4) Research just starts.

4. Development in Cat-CVD Technology;Birth of “Cat-doping”

 As described at final column in the above Table I, we recently discovered that phosphorus (P) atoms or boron (B) atoms could be doped into c-Si at temperatures as low as only 80oC, when c-Si samples are exposed in species generated by catalytic cracking reaction of phosphine (PH3) or diborane (B2H6). That is, we discovered a new impurity doping method apart from the conventional thermal diffusion method, ion-implantation method and Plasma doping method. We named the method as “Catalytically Cracked Impurity Doping (Cat-doping)”.
 Figure 12 shows the sheet carrier density after P Cat-doping into p-type c-Si, measured by Van der Pauw method, as a function of temperature of W catalyzer. Substrate temperature, Ts, is kept at only 80oC, and process time is 10 min. It is known that the conduction type of samples are kept at original p-type for the catalyzer temperature below 800oC. However, the surface of p-type c-Si substrate is converted to n-type when the catalyzer temperature exceeds over 1,000oC and the sheet carrier density is likely to increase as the catalyzer temperature is elevated. This clearly demonstrates the effect of catalytic cracking of doping gas.

Fig.12  Conduction type and sheet carrier density after Cat-doping of P atoms into p-type c-Si as a function of temperature of catalyzer.

  As similar doping method, the plasma doping method has been widely known. In that case, however, the bias voltage is applied onto substrates and then it is regarded as a kind of ion-implantation. Even if the bias voltage is reduced to 0 V, because of the existence of sheath voltage in plasma, there is still an acceleration voltage. The mechanism of this Cat-doping is under the study at the moment. Recently some facts have been known. Doping depth is limited at shallow region of substrate surface even if we change various doping parameters. However, this Cat-doping is very effective to control the surface potential of c-Si.
 There is a lot of unknown factors in Cat-doping and the research is just started. However, we have already known that nitrogen (N) atoms can be doped into silicon-carbide (SiC) at only 350℃ although N atoms could not doped at such low temperatures before. We have just opened the window of the feasibility for various promising futures.