CATALYTIC OXIDATION OF SOLID MATERIALS

Abstract: One or more monolayers of cerium arrayed on the surface of a niobium metal acts as a catalyst to oxidation of the nio­ bium at ambient temperature and results in a very thin, very high quality insulating layer which may be configured by pat­ terning of the catalyst. Significant amounts of Nb₂O₅ are formed at pressures as low as 6.6×10 -6Pa , promoted by the presence of the cerium. This catalytic activity is related to the trivalent to tetravalent valence change of the cerium during ox­ idation. The kinestics of Nb₂O₅ formation beneath the oxida­ tion cerium shows two stages: the first stage is fast growth limited by ion diffusion; the second stage is slow growth limited by electron tunnelling. Other catalytic rare earths usable instead of cerium are terbium and praseodymium; other substrate materials usable instead of niobium are aluminium, hafnium, silicon and tanta­ lum, or oxidizable alloys thereof.

Description: 1. Field of the Invention This invention relates to preparation of oxide layers on materials such as metals and semiconductors, and relates more particularly to catalytic oxidation of such materials, at temperatures near ambient, to form high quality ultrathin insulating materials on process intermediates useful in producing integrated circuit devices. 2. Description of the Prior Art In recent years, there has been considerable interest in the room temperature oxidation of polycrystalline niobium because of its application as tunnel barrier material in superconductive Josephson junctions. The prime concern was to find direct evidence for the existence of suboxides which are thought to be the cause of large excess currents. X-ray photoelectron spectroscopy (XPS) studies showed that the oxidation of niobium is characterized by an initial fast oxygen sorption, then the formation of a thin layer of NbO and NbO₂ followed at larger oxygen exposures by the formation of Nb₂O₅ on the surface. The lower oxides of niobium exhibit inferior insulating characteristics as contrasted to Nb₂O₅. Sanz and Hofmann determined the kinetics of Nb₂O₅ formation, which under ultrahigh-vacuum (UHV) conditions in dry oxygen followed a logarithmic growth law, attaining a thickness of 0.2 nanometer after an oxygen exposure of 10⁴ L (1L = 10⁻⁶ Torr.sec = 1.32 x 10⁻⁴ Pa.sec). J. M. Sanz & S. Hofmann, J. of the Less-Common Metals, Volume 92, p. 317 (1983). XPS and core electron energy loss spectroscopy studies of the surface oxidation of cerium suggest the initial formation of Ce₂O₃ followed by a thin layer of CeO₂ on the surface. Only trivalent oxide is formed upon oxidation with water vapor. See B. E. Koel et al., J. Electr. Spectr. Rel. Phen. Vol. 21, p.31 (1980), and G. Strasser and F. P. Netzer, J. Vac. Sci. Tech., Section A., Vol 2, page 826, April-May 1984. There are a number of metals, including aluminum and niobium, which form intrinsic oxides when exposed to air at ambient temperatures. However, there is no known catalytic oxidation of solids prior to that of laboratory work resulting in this patent specification. Further X-ray photoemission spectroscopy studies (XPS) showed that the air oxidation of niobium could be suppressed by the use of thin aluminum, thin yttrium or magnesium, yttrium or erbium overlayers. Techniques for preparing insulating oxide layers generally required elevated temperatures, even though these temperatures were known to be undesirable because they exascerbated other problems such as spread of contaminants or diffusion of dopants beyond the optimum. Studies of oxides were carried out in a great number of laboratories because of the great interest in integrated circuits. These studies did not result in the knowledge that ambient temperature oxidation of meaningful insulation layers could be accomplished at all, much less provide the knowledge of actual techniques for carrying out any such oxidation, still less provide the knowledge of actual catalyst and method choices. Oxide layers required for semiconductor integrated circuits and other integrated circuits, continued to require elevated temperatures. Certain catalysts, such as platinum, rhodium, palladium and cerium, but in particular platinum, have become common in the automobile industry for purifying exhaust gases. The exhaust catalytic reactions take place at elevated temperatures and involve gaseous components only. See, for example, U. S. Patent 4,274,981, Suzuki et al., CATALYST FOR PURIFYING EXHAUST GAS AND THE PROCESS FOR MANUFACTURE THEREOF, June 23, 1981. Certain rare earths and metals have known catalytic characteristics. Germanium, cerium, thorium, manganese, niobium, chromium, praseodymium, yttrium, zirconium, ruthenium, gallium, tin, indium, copper, lanthanum, tantalum and tungsten, plus others, have been listed in a context of oxidation promotion. See, for example, U. S. Patent 4,001,317, Grasselli et al, PROCESS FOR THE OXIDATION OF OLEFINS USING CATALYSTS CONTAINING VARIOUS PROMOTER ELEMENTS, January 4, 1977. The prior art deals with gaseous and organic materials, not with process intermediates used in production of semiconductors, and not with oxidation of solids. SUMMARY OF THE INVENTION The object of the invention is to prepare usable insulating layers by oxidizing materials catalytically at temperatures far below the process parameters of pressure and temperature normally required for such oxidation reactions via a method as disclosed in the claims. A feature of the invention is the use of some monolayers of cerium, or of other rare earth element which undergoes valence change from trivalent to tetravalent upon surface oxidation, to result in a smooth thin oxide layer of high quality. An advantage of the invention is that it provides usable insulating layers of high quality, at low cost, and without the need for high temperatures, in such fashion that the catalyst pattern is either acceptable in place or easily removable. The foregoing and other objects, features and advantages of the invention will be apparent from the more particular description of the preferred embodiments of the invention, as illustrated in the accompanying drawing. The invention will now be further described with reference to the accompanying drawings, in which FIG. 1 is a diagrammatic sketch of an integrated circuit process intermediate according to a preferred embodiment of the invention. FIG. 2 is a composite XPS spectrum of: (a) 25 nm freshly evaporated niobium showing only the electron levels of the clean metal, the Nb 3d 5/2 peak at 202.3 eV and the Nb 3d 3/2 peak at 205.1 eV binding energies. (b) After a 20 minute exposure to 6.6 x 10⁻⁶Pa pure oxygen at 300K, the Nb 3d levels show only the formation of a small amount of lower Nb-oxides. FIG. 3 is an XPS spectrum of 25 nm freshly evaporated niobium covered by 0.6 nm of cerium, showing: (a) The Nb 3d levels before exposure to oxygen; and (b) The Nb 3d levels after an exposure to 6.6 x 10⁻⁶Pa oxygen for 20 minutes at 300K, showing a significant amount of Nb₂O₅ formation characterized by a 5.1 eV chemical shift of the Nb 3d levels. Figure 4 is a composite XPS spectrum of the cerium overlayer before (a) and after (b) oxygen exposure; the metallic cerium is trivalent only, while the oxidized phase shows in addition the Ce⁴⁺ species. Figure 5 is a diagram of the thickness of the Nb₂O₅ layer as a function of the logarithm of the oxidation time at 300K. The diagram shows fast growth until around 4 nm thickness characterized by a 1/3 slope in log-log presentation (inset) which changes to slow growth characterized by a logarithmic time dependence. Fig. 6 is a diagram showing dependence of Nb₂O₅ oxide thickness on the logarithm of oxygen pressure with cerium, praseodymium and terbium catalysts on niobium. DESCRIPTION OF PREFERRED EMBODIMENTS OF THE INVENTION Cerium, arrayed as one or a few monolayers on a substrate surface of niobium metal, acts as a catalyst to oxidation of the niobium substrate at ambient temperature and results in a thin, very high quality insulating layer. Certain other catalysts, generally rare earths which experience a rising valence change during oxidation reactions, can be used, as can certain other substrate materials, generally oxidizable metals or semiconductors. Significant amounts of Nb₂O₅ are formed at pressures as low as 6.6 x 10⁻⁶Pa, promoted by the presence of the cerium. This catalytic activity is related to the trivalent to tetravalent valence change of the cerium during oxidation. The kinetics of Nb₂O₅ formation beneath the oxidized cerium shows two stages: the first stage is fast growth limited by ion diffusion; the second stage is slow growth limited by electron tunneling. Even a very thin overlayer of cerium enhances the oxidation of niobium metal. For example, after only 200L oxygen exposure, 4.5 nm of Nb₂O₅ forms underneath the oxidized cerium and no lower oxides are detected. To embody the invention, useful generally as a method for producing a process intermediate for integrated circuit manufacture, the preferred starting material is niobium which has been deposited from the vapor upon a suitable substrate. Processing is preferably carried out in a UHV system. Niobium films and cerium overlayers are evaporated and oxidized at 300K to form the process intermediate shown in Fig. 1. Substrate metal niobium 1 (which may in turn be supported on some other substrate) has been oxidized to include Nb₂O₅ layer 2; the thin catalyst layer of cerium has been oxidized to CeO₂+Ce₂O₃ layer 3. Subsequent analysis confirms the catalytic oxidation by analyzing in situ with XPS, performed with Mg K alpha excitation (1252.6 eV), the direction of observation being nearly perpendicular to the surface. First evaporate about 25 nm niobium; its XPS spectrum shows only the electron levels of the clean metal. A plot of the Nb 3d 5/2 peak at 202.3 eV and the Nb 3d 3/2 peak at 205.1 eV binding energies is given in Figure 2 trace (a). After a 20 minute exposure to 6.6 x 10⁻⁶ Pa pure oxygen the Nb 3d levels show only the formation of a small amount of lower Nb-oxides as seen in Figure 2 trace (b). Evaporate 25 nm niobium on any suitable substrate, and on top of the niobium evaporate 0.6 nm cerium. Figure 3 trace (a) shows the Nb 3d levels at this point. After an exposure to 6.6 x 10⁻⁶ Pa pure oxygen for 20 minutes, a significant amount of niobium oxide is formed, as shown in Figure 3 trace (b). The resulting niobium oxide is characterized by a 5.1 eV chemical shift of the Nb 3d levels. This binding energy at 207.4 eV for Nb 3d 5/2 and at 210.2 eV for Nb 3d 5/2 is characteristic of Nb₂O₅. The thickness of the oxide, t ox can be estimated as shown in Equation 1: where λ ox and λ m are electron mean free paths, I ox and I m integrated intensities, n ox and n m Nb atom densities, in the oxide and the metal respectively, and ϑ is the detection angle from the sample plane. The electron mean free paths employed in calculating the oxide thickness were 1.4 nm for niobium, 2.4 nm for Nb₂O₅ ; n m /n ox = 2.69. According to Eqation 1 the thickness of the Nb₂O₅ layer due to 20 minutes oxidation at 6.6 x 10⁻⁶ Pa is 3.5 nm. In a variation of the preferred embodiment, different thicknesses of cerium overlayers (0.5 nm, 1 nm and 2 nm) when exposed to the same oxidation treatment, produce identical amounts of Nb₂O₅; the catalytic action of cerium is independent of its thickness in the range 0.5-2 nm. When 25 nm of niobium covered by 0.5 nm of cerium is exposed for 20 minutes to 6.6 x 10⁻⁶Pa H₂O vapor instead of oxygen, no Nb₂O₅ is formed. Results confirm the formation of a mixture of Ce₂O₃ and CeO₂ on the surface, if oxidation takes place in pure oxygen. Fig. 4 shows the Ce 4d levels of the overlayer before (a) and after (b) exposure to oxygen. While the metallic cerium phase is trivalent (compare Y. Baer & C. Zuercher, Phys. Rev. Lett., Vol. 39. p. 956, 1977) the oxidized cerium shows both trivalent and tetravalent species. When oxidation takes place in water vapor, no evidence of tetravalent cerium in the Ce 4d spectrum is found, and the niobium does not oxidize underneath the cerium. It appears that the catalytic action of cerium is related to the valence change (trivalent to tetravalent) during surface oxidation. CeO₂ is known to have high catalytic activity in oxidation reactions, such as in the oxidation of hydrocarbons, where both the ease of the trivalent- to-tetravalent valence change and the high oxygen mobility in CeO₂ are well reflected. CeO₂ is an oxygen ion conductor, possibly more so in the amorphous than in the crystalline state. It is known that oxide films formed at low temperatures are amorphous; some of these, such as Nb₂O₅ form network structures, where a large oxygen ion can move more easily through the channels of the network than a tightly bound though smaller cation; therefore, these oxide films grow by oxygen ion diffusion. Because the Mott potential, which develops upon oxidation and aids ion diffusion, is larger in cerium than in niobium, cerium oxidizes more easily than niobium. The oxidized cerium on the surface contains a large fraction of CeO₂ which can be reduced to Ce₂O₃ by niobium, since the heat of decomposition of Nb₂O₅, referring to the formation of one mole of oxygen is 614.5 KJ (146.8 kcal), while that of CeO₂ is only 523 KJ (125 kcal) (because the heat of decomposition of Ce₂O₃ is 1280 KJ (305 kcal), niobium cannot reduce Ce₂O₃). With continuing oxygen exposure, the CeO₂ which lost oxygen to niobium will reoxidize at the surface, thereby providing oxygen ions for the further oxidation of niobium. In a second experiment, to study the kinetics of the catalytic oxidation of niobium at 6.6 x 10⁻⁶ Pa oxygen pressure, using a freshly deposited film of 50 nm niobium covered by 0.9 nm cerium, XPS spectra were taken at times between one minute and seven hours exposure. After 1 minute exposure (3L) the spectrum did not show Nb₂O₅ since the cerium on the surface oxidizes first. The next spectrum, taken after 3 minutes, representing 9L oxygen exposure, showed already 1.9 nm of Nb₂O₅ formed. This is to be compared with the oxidation of niobium without a catalyst. At 9L exposure, only a very small amount of NbO and NbO₂ form, and no Nb₂O₅ is detected. See Sanz and Hofmann, supra. Fig. 5 shows the thickness of the Nb₂O₅ layer (calculated by Eq. 1) as a function of the logarithm of the oxidation time. The diagram shows fast growth until around 40 minute oxidation time, which is equivalent to 120L oxygen exposure. Here already 4 nm pure Nb₂O₅ is formed. This is to be compared with the oxidation of niobium without a catalyst, where at 120L exposure to oxygen only 0.05 nm of Nb₂O₅ forms on top of 0.6 nm of NbO + NbO₂. See Sanz & Hofmann, supra. The fast growth is characterized by a 1/3 slope in the log-log representation (inset), which changes to slow growth characterized by a logarithmic time dependence. The thickness attained after seven hours (1,260L) is 4.8 nm. In the non-catalytic oxidation of niobium, only the slow growth regime is found. The formation of Nb₂O₅ is characterized by a logarithmic time dependence. At 1260L oxygen exposure only 0.2 nm Nb₂O₅ forms on top of 0.6 nm of NbO + NbO₂. See Sanz & Hofmann, supra. The catalytic oxidation experiments show that increasing the partial pressure of oxygen increases the thickness of the oxide layer. For example, a 20 minute oxidation at 6.6 x 10⁻⁶Pa oxygen pressure results in 3.5 nm thick Nb₂O₅, while the same time at 1.32 x 10⁴ Pa results in 6.7 nm Nb₂O₅. See Fig. 6. Increasing the temperature of oxidation from room temperature to somewhat higher temperatures increases oxide thickness exponentially. As described above, the catalytic activity of the cerium enables the growth of significant amounts of Nb₂O₅ under well controlled UHV conditions. The thickness is much larger than obtained with pure niobium at atmospheric pressure after comparable exposure times. Yet, the benefit of oxidizing a solid with the aid of a catalyst is not only that the kinetics change and equilibrium is reached in a shorter time, but that this equilibrium state brought about by a catalyst is more perfect with respect to stoichiometry (no lower oxides formed) than a nonequilibrium state. We found that an important characteristic of the cerium catalyst is its trivalent to tetravalent valence change during surface oxidation. The catalytic activity of other rare earths exhibiting trivalent to tetravalent valence change, such as praseodymium and terbium, is similar to that of cerium. Aluminum, hafnium, titanium, zirconium or tantalum substrate materials, which are oxidizable under controlled conditions to form protective or insulating oxide layers, are useful in place of niobium in certain applications, either as metals or as alloys. Silicon, which forms an SiO₂ oxide layer of useful insulating thickness only at extremely high oxidation temperatures, such as 1000C, can be oxidized at temperatures near ambient with the use of the aforementioned catalysts. Oxide patterns may be produced by patterning of the catalyst prior to oxidation, using masking or etching techniques.

Claims: A method of controllably preparing high quality insulating oxide layers on a solid surface of material that is not normally oxidizable to useful quality or thickness at temperatures near ambient within acceptable process time durations, characterised by (a) depositing on said solid surface a very thin layer, 1-10 monolayers thick, of a rare earth having catalytic activity related to a valence increase during oxidation; and (b) exposing said rare earth to oxygen in a humidity-free atmosphere at ambient or slightly elevated temperature to grow the desired oxide thickness of the material; whereby oxide layers are grown below the threshold values for oxidation of said solid surface in the absence of catalytic activity. A method as claimed in claim 1, wherein said very thin layer of catalyst is cerium of thickness less than 3 nm. A method as claimed in claim 2, wherein said very thin layer of catalyst is terbium of thickness less than 3 nm. A method as claimed in claim 2, wherein said very thin layer of catalyst is praseodymium of thickness less than 3 nm. A method as claimed in claim 2, 3 or 4, wherein said solid surface of material is one of aluminium, hafnium, silicon or tantalum, or alloys thereof. A method as claimed in any of claims 1 to 5, further characterised in that said catalyst is configured in a pattern.

Inventors: LATTA, ERNST-EBERHARD, RONAY, MARIA
Applicants: INTERNATIONAL BUSINESS MACHINES CORPORATION
Application year: 1985
Main classification: H01L21
IPC codes: C23C8, H01L39, C01B13, C01G1, H01L21, B01J23, C01G33