Patent Application
20120228144
The present invention relates to a high-purity fluorine gas and the production thereof, an apparatus for producing a fluorine gas, and a method for monitoring and controlling impurities in a fluorine gas, and use thereof.
Fluorine gas is an indispensable basic gas, and is used as an etching gas or a cleaning gas in the semiconductor industry, for the manufacture of photovoltaic cells and TFTs (thin film transistors) for liquid crystal displays because of its reaction properties. Particularly, in uses for annealing metal fluoride for optical materials or as a gas for an excimer laser, the optical properties of fluorine are also important and the amount of fluorine gas used for this purpose is increasing. Accompanying these demands, a high-purity fluorine gas is strongly required. For example, in the field of production of semiconductors, a fluorine gas having a high purity of 99.7% or more is demanded. In particularly, for optical uses, a high-purity fluorine gas reduced in impurities such as fluorocarbon, especially CF4, and having a purity of 99.9 to 99.99 vol % is demanded. Therefore, for this purpose, the requirement for diminishing the amount of fluorocarbon, especially CF4 a high-purity fluorine gas is increasing.
Generally, the fluorine gas supplied on a commercial basis contains about 1.5 vol % of impurities. The majority of the impurities are N2, O2, CO2, fluorocarbons such as CF4, and gases such as SF6, SiF4 and HF. In industrial manufacture, F2 is produced by electrolysis of molten compositions comprising KF and HF, and carbon anodes are frequently used. In optimal operation conditions F2 generating electrolysis cells produce less than 100 ppmv CF4. But sometimes the fluorocarbon, especially CF4 content in fluorine coming from a fluorine plant is much higher without a predictable or obvious reason. The daily practice showed that most times only one cell is responsible for increased CF4 production with the effect that the whole fluorine production is contaminated. The fluorocarbon, especially CF4 can be detected directly with FTIR (Fourier transform IR) spectroscopy, TDL (tunable diode laser) spectroscopy, GC (gas chromatography) and other methods with low detection limits in a wide concentration range. But the instruments are expensive, complex and need much space or cannot serve as a fast online analysis device (GC) or only with difficulties in installation with respect to small sample compartments or the need of an external detector (FTIR).
By a typical industrial fluorine generating electrolytic cell, a gas mixture is produced consisting of about 94 to 97 vol % fluorine, the rest is HF with only traces of the other impurities. If an anode “burn” occurs, the concentration of CF4 is mostly elevated to values between 1 vol % and 10 vol %; COF2 is elevated to concentrations up to some thousand ppmv; HF is slightly elevated. If OF2 is present, its concentration is reduced.
The method described in U.S. Pat. No. 6,955,801 B2 is a method for producing of and analyzing impurities in a high-purity fluorine gas, comprising filling a fluoronickel compound in a container comprising a metal material or a metal material having a nickel film, said container having a fluorinated layer formed on a surface of the metal material or nickel film, conducting a step of heating the fluoronickel compound to 250 to 600° C., and reducing the pressure inside the container to 0.01 MPa (absolute pressure) or less, and a step of allowing a fluorine gas reduced in a hydrogen fluoride content to 500 vol ppm or less to be occluded into the fluoronickel compound passed through the first step, respectively, at least once, and further conducting said first step, then contacting a fluorine gas containing impurity gases with the fluoronickel compound at 200 to 350° C. to fix and remove the fluorine gas, and analyzing the impurities by GC or IR.
However, using this method, the post-processing treatment and the instructions needed are very complex, and expensive. Moreover, using this method, it is not possible to analyze fluorine gas and control the quality of fluorine gas obtained simply, especially, on-line, semi on-line or at-line.
It has now been found an apparatus for producing such high-purity fluorine gas, a method for the manufacture of high purity fluorine gas and an analysis method for the fluorine gas (especially, on-line analysis method).
The present invention now makes available an apparatus for producing a high-purity fluorine gas. Another object of the present invention is to provide a method for producing a high-purity fluorine gas, as well as a method for analyzing the compositions of fluorine gas obtained. Moreover, the present invention also relates to uses thereof. It has now been found in particular a fast, reliable, inexpensive and relatively small analyzer or analyzing method, which can be run on-line, semi on-line or at-line close to each F2 generating electrolytic cell, to detect the fluorocarbon, especially CF4 producing cell/cells immediately.
In general, the production of fluorine can be carried out in fluorine generating cell, wherein at the startup of a fluorine generating cell (in conditioning mode) the content of fluorine is measured by a detector system, especially, in the present invention, by FTIR and/or UV. The term “fluorine generating cell” (used for the sake of simplicity) denotes a fluorine generating electrolytic cell, i.e. a cell in which fluorine is produced electrolytically, usually by the electrolysis of a molten composition of KF and HF.
In these cells, often carbon anodes are applied for the transport of electric current. Such anodes sometimes unpredictably undergo anode burn. An anode burn in the fluorine generating cell is indicated by a slightly elevated HF content (for example, measured by FTIR) and an extremely elevated CF4 content (the content of C2F6 and COF2 also increase, while the OF2 amount decreases, all monitored by a detector system, especially, in the present invention, by UV). During current efficiency measurements which, in the present invention, are performed preferably with a UV spectrometer, it has been surprisingly found that UV spectroscopy as a direct measurement tool only for fluorine shows a sharp decrease in fluorine concentration when an anode burn occurs. Therefore the burn can be detected easily by the sharp decrease of the F2 concentration during the burn, during which impurities are formed (mainly CF4 and COF2). The result of this burn (more CF4, C2F6, COF2, HF, less OF2) is not only the alteration of impurities' contents but also a sharp decrease in the content of fluorine monitored by a detector system, especially, in the present invention, by UV spectroscopy. During the measurement by UV spectroscopy, the whole UV spectrum can be used for measuring. Preferably, not the whole spectrum but only the absorption at this particular wavelength, particular UV spectroscopy with wavelengths between 200 and 400 nm, more preferred 250 to 330 nm, very preferred between 270 to 290 nm, especially preferably, between 275 and 285 nm, and even at about 280 nm is used for measuring, because it is more or less the maximum of the UV absorption of F2. The spectrum may comprise all wavelengths in said range, or only selected wavelengths. It is also possible to use a UV light source which only emits a single wavelength in that range, several single wavelengths or a very narrow band, e.g. a UV light band with a breadth of 1 to 5 nm. Potential impurities, for example, CF4, C2F6, COF2, HF and OF2 do not absorb at this range of wavelengths, so the decrease/increase of the F2 concentration can selectively be monitored; the surprising feature is that anode burn is detected not by the increase of the CF4 concentration, but by the decrease of the F2 content of the produced gas.
When the burn is over, CF4 (C2F6, COF2, and HF) concentration starts to decrease again while the OF2 amount starts to increase again. The end of the anode burn is also detectable by the rising of the fluorine content in the gas mixture leaving the cell.
Seen from the phases of the production of fluorine, if the anode burn is avoided, the impurities, for example, CF4, C2F6, COF2, HF and the like, can be decreased.
Particularly, in order to produce high-purity fluorine, immediately after detection of a decrease of the measured fluorine content (for example, more than 0.1 vol %, particular more than 0.3 vol %, or more than 0.5 vol %, even more than 1 vol %), the fluorine generating cell is separated from the production of the pure fluorine. This prevents a contamination of the produced fluorine with the impurities from the malfunctioning electrolytic cell. It is then observed if the fluorine content further decreases. If the fluorine content continues to decrease, the fluorine generating cell is shut down and cured (repaired); alternatively, the cell is kept producing fluorine which then is either destroyed, e.g. in a scrubber, or it is passed to a purifier to remove the impurities contained. If the fluorine content does not decrease when the cell is kept producing fluorine in this manner (with destruction or purification of the produced impure fluorine) but reaches the original fluorine content level again, it is again taken for the production of the pure fluorine (for example, by valve switch). Thus, the apparatus and the method of fluorine manufacture of the present invention differ from processes of the state of the art in that the contamination with impurities is prevented which obviates respective purification steps which otherwise would be necessary.
Moreover, during the production, the current efficiency can be measured for each cell by the means for independently measuring current efficiency of fluorine generating cell, for example, a flow meter. Decreases in current efficiency should indicate short circuits in the cell. As to the current efficiency measurements, it is essential to know the current put into the electrolysis during a time period (this gives a theoretical amount of fluorine which should have been produced during this period). By measuring the flow of the gas mixture and the content of F2 in it the produced amount of fluorine in a time period is determined. The relation of produced amount of fluorine and the theoretical produced amount of fluorine during the time period is multiplied by 100 and results in the current efficiency in %. The percentages which are missing are due to recombination reactions between F2 and H2 inside the fluorine generating cell and the electrolytic formation of O2, OF2 and all losses of F2 and/or current maybe due to short circuits. When the current efficiency decreases in the fluorine generating cell said fluorine generating cell can be separated from the line delivering produced F2. The cell may be shut down for maintenance or repair, or the cell may be kept operating and the F2 produced can be discarded until F2 is produced regularly; then, the cell can be reconnected.
In one aspect, the present invention provides an apparatus for producing a high-purity fluorine gas, comprising at least one fluorine generating cell and at least one fluorine generating cell detector for detecting components of products obtained by the fluorine generating cell, wherein at least one of the fluorine generating cells is connected with the fluorine generating cell detector. It has to be noted as pointed out above that the fluorine generating cells are electrolytic cells.
Preferably, the apparatus contains at least 2 electrolytic cells. More preferably, it contains at least 6 electrolytic cells. An apparatus with at least 8 electrolytic cells is very suitable. The apparatus may even contain more electrolytic cells, e.g. ten or more. The apparatus is preferably constructed such that, if desired, additional electrolytic cells can be added if the demand for fluorine gas is rising. The cells preferably comprise jackets through which cooling water can be circulated. The advantage of providing several electrolytic cells is that the separation and possible shut-down of one or even more cells for maintenance or repair can be compensated by raising the output other cells.
In the present invention, the fluorine gas preferably is a high-purity fluorine gas.
The apparatus according to the invention optionally, further comprises control means for independently opening or closing said fluorine generating cell. Valves are very suitable to open or separate each of the cells.
As to the fluorine generating cell, all types of the fluorine generating cells used routinely in this field can be used in the present invention. Preferably, the fluorine generating cell is an electrolysis cell producing fluorine by electrolysis of a molten electrolyte. Generally, fluorine gas is generated from the fluorine generating cell. The fluorine generating cell body is generally made of metals or metal alloys resistant to HF and F2, especially Ni, Monel, carbon steel, or the like. The fluorine generating cell body is filled with a molten electrolyte, for example, a mixed molten salt, for example, comprising a potassium fluoride-hydrogen fluoride system (i.e. “KF-HF system”) as an electrolytic bath, which can be regenerated by feeding suitable raw material, in particular HF. The fluorine generating cell body generally comprises an anode chamber and a cathode chamber. Fluorine gas is generated when electrolysis is conducted by applying a voltage between an anode disposed within the anode chamber and a cathode disposed within the cathode chamber, wherein feeding of raw material can be carried out continuously or periodically.
In one embodiment of the present invention, the fluorine generating cell includes an anode, preferably a carbon anode.
The electrolytic cells are connected to collectors for the F2 and the H2 produced. Typically, each cell comprises 20 to 30 anodes. Electric power is supplied to the anodes by rectifiers. The apparatus often will have a cooling water circuit supplying cooling water to the jackets of the cells.
Optionally, a settling box for F2 and a settling box for H2 are connected with each of the cells. The settling boxes serve to reduce the gas velocity of the F2 and H2 produced in the cell to avoid electrolyte dust to be carried over. Preferably, the settling boxes comprise a vibrator and a heating to melt the separated electrolyte dust for easy removal.
In another embodiment of the present invention, the fluorine generating cell detector is used for detecting impurities present in the fluorine obtained by the fluorine generating cell. If several fluorine generating cells are contained in the apparatus—which is the preferred embodiment—a cell detector is allocated to each fluorine generating cell, or a detector is used which allows the detection of several cells or all cells simultaneously or at least in quick succession.
In another embodiment of the present invention, the fluorine generating cell detector comprises:
In an embodiment of the present invention, the fluorine generating cell detector is used for detecting CF4 present in the fluorine obtained by the fluorine generating cell. As described above, the fluorine gas stream is treated such that fluorine and HF are removed and CF4 remains in the gas stream; it is the main component and can be analyzed, e.g. by a GC detector, a flame ionization detector, thermal conductivity detector, TDL-spectroscopy, FTIR or other detectors used routinely in this field.
In another embodiment of the present invention, the fluorine generating cell detector is a UV analyzer. With UV measurement provided for each fluorine generating cell it is feasible to produce nearly impurities-free fluorine gas without interruption in spite of using carbon anodes, wherein in particular the impurities refer to CF4. An apparatus with a UV detector which may operate with UV light in the ranges given above, especially using a wavelength of about 280 nm is especially preferred. As described above, UV light in this range of wavelengths serves to monitor the F2 content, but nevertheless may be used to identify anode burns with respective increase of contaminants, for example, of CF4. The advantage is that the CF4 content can be determined indirectly by analyzing and monitoring the F2 content without the need for purifying operations as described for the alternative embodiment above.
In another preferred embodiment of the present invention, the fluorine generating cell detector is an on-line, semi-online or at-line detector.
In the present invention, “online” means that the whole fluorine gas goes through the detector; “semi-online” means that part of the fluorine gas is forced through the detector and that this part is combined with the main stream after analyzing; and “at-line” means that part of the fluorine gas generated is taken out of the main stream and the analyzed part of the fluorine stream is treated, collected or otherwise used after analysis.
In the preferred embodiment of the present invention, each fluorine generating cell independently is connected with a fluorine generating cell detector, or several cells are connected with a detector, as mentioned above, capable of monitoring several samples simultaneously or in quick succession.
In another embodiment of the present invention, the fluorine generating cell detector or cell detectors is connected with the control means. As to the control means, all types of the means used routinely in this field can be used in the present invention, in particular a valve or switch.
For example, the cell detector or detectors may be connected to a control board which is also connected to the valve, valves, switch or switches, the rectifier and other parts of the apparatus. In case of the detection of a decrease of the F2 content (which is an indication of an irregular performance of the respective fluorine generating cell, possibly caused by anode burn), the control board may issue optical and/or acoustic warnings, or it may close the valve or valves automatically and thus, separate the respective cell from the others and thus prevent contamination of the F2 produced by the other cells which function in a regular manner.
In one embodiment of the present invention, the apparatus further comprises a NaF tower. In the NaF tower, HF can be absorbed by passing gas through it. Especially, F2 gas produced can be passed through the NaF towers to remove HF from it. The towers can be regenerated by applying heat and passing a purge gas through it.
In one embodiment of the present invention, the apparatus further comprises a particle filter. It was observed that the fluorine gas produced often contains solidified electrolyte salt which is entrained. The particle filter may be a porous body made from material which is resistant to HF and fluorine. Filters having pores with a diameter of, for example, up to 10 nm are very suitable. The fluorine gas may additionally be treated in a washer operated with liquid HF, for example, a jet scrubber.
In another embodiment of the present invention, the apparatus comprises a means for monitoring and controlling current efficiency of fluorine generating cells, for example, a flow meter. The current efficiency preferred is measured for each cell by the above means. During production of fluorine gas, if the current efficiency decreases, said fluorine generating cell can be closed (separated from the other cells), for example, by using the control means.
According to another aspect, the invention relates also to a process for manufacturing fluorine comprising use of the apparatus according to the invention as described herein before. In particular, the invention relates to a method for producing a high-purity fluorine gas comprising use of the apparatus according to the invention as described herein before.
Furthermore, the present invention relates to the use of the apparatus according to the invention in a semiconductor processing system, in a system for processing photovoltaic cells, or a system for the processing of TFTs (thin film transistors, used for liquid crystal displays), and especially, the use of the above apparatus in a process chamber cleaning system. It is well known that chambers used for said purposes, often undesired deposits form on the inner walls, parts inside the chamber and lines connected to the chamber. These deposits can be removed by treatment with fluorine gas, optionally diluted with inert gas, for example, N2, O2 and/or Ar, thermally or under assistance by a plasma.
In another embodiment of the present invention, the fluorine generating cell detector, especially UV analyzer, which is in combination with a NaF tower, and can be used as an indicator that only fluorine and HF (no CF4, C2F6 etc.) leave in the fluorine generating cell.
In another aspect, the present invention concerns a method for monitoring impurities, such as CF4, in manufacturing a high-purity fluorine gas by using a fluorine generating cell detector, for example, a UV analyzer. The fact that the fluorine concentration can be used to indirectly monitor the CF4 content is surprising and also advantageous because one has to perform one measurement to detect two impurities which otherwise would need two detectors.
In a still further aspect, the present invention concerns a method for detecting an anode burn in preparing a high-purity fluorine gas using fluorine generating cell detector, for example, a UV analyzer.
In still another aspect, the present invention relates to a process for the manufacture of a semiconductor, of a photovoltaic cell or a TFT, comprising (a) manufacturing fluorine by the present invention as described herein before or the apparatus of the present invention as described herein before; (b) feeding the fluorine obtained into a semiconductor processing system, a system for processing a photovoltaic cell or a system for processing a TFT. The term “processing” includes especially steps of etching the semiconductor, photovoltaic cell and TFT with elemental fluorine and the cleaning of process chambers during the manufacture of semiconductors, photovoltaic cells and TFTs.
The present invention also relates to a process for cleaning a process chamber, comprising (a) manufacturing fluorine by the present invention as described herein before; (b) feeding the fluorine obtained into a process chamber cleaning system.
Moreover, in another aspect, the present invention provides a method for monitoring of the fluorine produced of fluorine generating cells with FTIR and/or UV, especially, carried out by at-line, semi-online or online measurement.
Hereinafter, the present invention is described in considerable detail. The following examples are offered by way of illustration to help those skilled in the art to understand the present invention, and are not intended to limit the scope of the invention.
The apparatus comprises at least one fluorine generating cell 2, and a fluorine generating cell detector 6 for detecting components of products obtained by the fluorine generating cell; optionally, a control means 3 for independently opening or closing said fluorine generating cell 2, a means 5 for independently measuring current efficiency of fluorine generating cell 2, a particle filter 4, a system 7 for treating or purifying fluorine produced, a system 8 for treating or purifying impure fluorine gas and then collecting the same.
Particularly, the system 1 for feeding raw materials is connected with the fluorine generating cell 2; the fluorine generating cell 2 is connected with an optional control means 3; the control means 3 is connected with an optional particle filter 4; the particle filter 4 is connected with a means 5 for independently measuring current efficiency of fluorine generating cell; the means 5 is connected with a fluorine generating cell detector 6; the fluorine generating cell detector 6 respectively is connected with a system 7 for treating or purifying fluorine produced and a system 8 for treating or purifying impure fluorine gas and then collecting the same. Moreover, a system 7 is connected with a system 9 for discharging and collecting the fluorine. In addition, the system 7 or the system 8 can be, for example, is a scrubber containing an aqueous alkaline solution.
Particularly, a system 1 for feeding raw materials is connected with the fluorine generating cell 2; the fluorine generating cell 2 is connected with an optional control means 3; the control means 3 is connected with an optional particle filter 4; the particle filter 4 is connected with a means 5 for independently measuring current efficiency of fluorine generating cell; the means 5 is respectively connected with a system 7 for treating or purifying fluorine produced, a system 8 for treating or purifying impure fluorine gas and then collecting the same, and a fluorine generating cell detector 6 optionally via an optional particle filter 4; the fluorine generating cell detector 6 is respectively connected with a system 7 for treating or purifying fluorine produced, a system 8 for treating or purifying impure fluorine gas and then collecting the same. Moreover, a system 7 is connected with a system 9 for discharging and collecting the fluorine.
Particularly, a system 1 for feeding raw materials is connected with the fluorine generating cell 2; the fluorine generating cell 2 is connected with an optional control means 3; the control means 3 is connected with an optional particle filter 4; the particle filter 4 is connected with a means 5 for independently measuring current efficiency of fluorine generating cell; the means 5 is respectively connected with a system 7 for treating or purifying fluorine produced, a system 8 for treating or purifying impure fluorine gas and then collecting the same, and a fluorine generating cell detector 6 optionally via an optional particle filter 4; the fluorine generating cell detector 6 is connected with a system 10 for treating or collecting fluorine. Moreover, a system 7 is connected with a system 9 for discharging and collecting the fluorine.
Particularly, a system 1 for feeding raw materials is connected with the fluorine generating cell 2; the fluorine generating cell 2 is connected with an optional control means 3; the control means 3 is connected with an optional particle filter 4; the particle filter 4 is connected with a means 5 for independently measuring current efficiency of fluorine generating cell; the means 5 is respectively connected with a system 7 for treating or purifying fluorine produced, a system 8 for treating or purifying impure fluorine gas and then collecting the same, and a fluorine generating cell detector 6 optionally via a NaF tower 11, an optional particle filter 4 and a means 5; the fluorine generating cell detector 6 is respectively connected with a system 7 for treating or purifying fluorine produced, a system 8 for treating or purifying impure fluorine gas and then collecting the same. Moreover, a system 7 is connected with a system 9 for discharging and collecting the fluorine.
The apparatus schematically described in
A comparable arrangement of the apparatus with a multitude of electrolytic cells 2a to 2h is preferred in the apparatus of
In order to describe the present method,
The fluorine generating cell detector 6 is used to monitor the composition of the produced fluorine. When the fluorine generating cell detector 6 detects an anode burn, for example, slightly elevated HF content, a extremely elevated CF4 content (C2F6 and COF2 also increased, while OF2 amount decreased) or a decrease of the measured fluorine content (for example more than 0.1 vol %-0.5 vol %), which are measured by FTIR, GC and/or UV, the fluorine generating cell(s) is(are) separated from the production of the pure fluorine and observed if the fluorine content further decreases, for example, the valve to the system 8 for treating or purifying impure fluorine gas and then collecting the same is opened while the valve to the system 7 for treating or purifying fluorine produced is shut. If its fluorine content continues to decrease, the fluorine generating cell(s) 2 is (are) shut down (e.g. current=0 A), optionally, which can be repaired, for example, exchanged by fluorine generating cell, anode and so on. If the fluorine content does not continue to decrease but reaches the original fluorine content level again, the fluorine generating cell(s) 2 is (are) again taken for the production of the pure fluorine, for example, the valve to the system 7 for treating or purifying fluorine produced is opened again while the valve to the system 8 for treating or purifying impure fluorine gas and then collecting the same is closed. Then, the fluorine produced is discharged from the system 7 into the system 9 for discharging and collecting the fluorine.
Ten fluorine generating cells 2 filled with KHF2 electrolyte, and the fluorine gas is produced by electrolysis in the 10 cells 2. The fluorine gases obtained pass through a switch 3 for independently opening or closing said fluorine generating cell 2, a particle filter 4 and a flow meter 5 for independently measuring current efficiency of fluorine generating cell, and then are fed into a UV analyzer 6 detecting UV adsorption at 280 nm, which the UV analyzer 6 independently detects each fluorine generating cell. When the fluorine generating cell detector (UV analyzer) 6 detects a decrease of the measured fluorine content being more than 0.1 vol %, the valve to the scrubber system 8 for destroying impure fluorine gas is opened while the valve to the purification section 7 is shut down. If its fluorine content continues to decrease, the fluorine generating cells 2 are shut down (e.g. current=0 A) by the switch 3. If the fluorine content does not continue to decrease but reaches the original fluorine content level again, or after maintenance or repair, the valve to the purification section 7 is opened again while the valve to the scrubber system 8 for destroying impure fluorine gas is closed, wherein the system 8 is filled with aqueous alkaline solution. Then, the fluorine produced is discharged from the scrubber 7 into the system 9 for discharging and collecting the fluorine.
The result is shown in Table 1.
Same as Example 1, except five fluorine generating cells 2 are used as indicated in Table 1.
Same as Example 1, except the decrease of the measured fluorine content is more than 0.5 vol % as indicated in Table 1.
Same as Example 2, except the decrease of the measured fluorine content is more than 0.5 vol % as indicated in Table 1.
It can be seen from the examples, using the present method or the present apparatus, a production site for pure fluorine consisting of 10 fluorine generating cells can continuously be run with a maximum CF4 content of less than 111 ppmv.
Moreover, it can be seen from the examples, using the present method or the present apparatus, a production site for pure fluorine consisting of 5 fluorine generating cells can continuously be run with a maximum CF4 content of less than 250 ppmv.
It can also be seen from the examples that using an apparatus with a higher number of cells is advantageous. Finally, the maximum content of CF4 is in a lower range if the respective cell is separated from the others if the F2 content decreases by 0.1 vol %, compared to 0.5 vol %.
While various modifications and alterations within the technical sphere of the concept of this invention can be devised by the individual skilled in the art, it should be understood that such modifications and alterations also fall within the scope of this invention.
Should the disclosure of any patents, patent applications, and publications which are incorporated herein by reference conflict with the description of the present application to the extent that it may render a term unclear, the present description shall take precedence.
| Number | Date | Country | Kind |
|---|---|---|---|
| 09173332.9 | Oct 2009 | EP | regional |
This application is a U.S. national stage entry under 35 U.S.C. §371 of International Application No. PCT/EP2010/065334 filed Oct. 13, 2010, which claims priority to European Application No. 09173332.9 filed Oct. 16, 2009, the whole content of this application being incorporated herein by reference for all purposes.
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/EP2010/065334 | 10/13/2010 | WO | 00 | 5/31/2012 |
