METHOD AND DEVICE FOR MONITORING THE QUALITY OF GASEOUS MEDIA

Abstract

The invention relates to a method and to a device for monitoring the quality of gaseous media which can be dispensed by a filling station, in particular hydrogen, by means of an infrared measuring system (42), which is connected into the dispensing path of live respective gaseous medium running fom the filling station to a consumer, and which measures the transmission of infared radiation at different wavelengths and different pressures and calculates therefrom the concentration of contaminants, which influence the quality. At least when predeterminable quality parameters are exceeded, this is indicated.

Claims

1. A method for monitoring the quality of gaseous media dispensed from a filling station, in particular hydrogen, by means of an infrared measuring device (42), which is connected in the dispensing path of the gaseous medium, from the filling station to a consumer and which measures the transmission of infrared radiation at different wavelengths and pressures, computes the concentration of the quality influencing impurities therefrom and indicates the latter at least if predeterminable quality parameters are exceeded.

2. The method according to claim 1, characterized in that impurities are detected by means of the infrared measuring device (42), which are infrared active due to a dipole moment.

3. The method according to claim 1, characterized in that the infrared measuring device (42) uses the infrared spectroscopy to determine the type of contamination from the position of absorption bands of a sample and to determine the concentration of the respective impurities from the attenuation of the infrared radiation when passing through the sample.

4. The method according to claim 1, characterized in that the Lambert-Beer law is applied for determining the concentration of the respective impurity in the sample.

5. The method according to claim 1, characterized in that the sample analysis is performed by means of the infrared measuring device (42) at very high pressures, preferably >500 bar, more preferably >700 bar.

6. The method according to claim 1, characterized in that the infrared measuring device (42) is connected in such a way in the hydrogen dispensing path that a valve device (46) in the bypass to this discharge path is used to take sequential samples and check them for impurities without interrupting the concurrent dispensing of hydrogen from the filing station to the connected consumer.

7. The method according to claim 1, characterized in that a control and arithmetic unit (52) of the infrared measuring device (42) buffers transmission measurements of the respective samples at different densities and subtracts them from each other for determining a measured value and that a pressure measurement and in addition, if necessary, a temperature measurement of the sample is made for determining the sample density.

8. Device for performing the method according to claim 1, characterized in that it consists of an infrared measuring device, having at least the following components: high-pressure resistant infrared cuvette (10); infrared emitter (28); infrared detector (40); pressure sensor (P); and control and processing unit (52).

9. A device according to claim 8, characterized in that the high-pressure-resistant infrared cuvette (10) has at least the following components: pressure-resistant pipe section (12); ports (16; 18) for sample inlet and outlet; and Infrared waveguide (14) in the interior of the pipe section (12).

10. The device according to claim 8, characterized in that at least one flange part (22; 24) at the tube end of the high-pressure resistant infrared cuvette (10) has a pressure-proof infrared radiation transmissive window (30) and/or an infrared radiation reflecting mirror (56).

Description

[0012] Below, the method according to the invention will be explained in more detail with reference to a device according to the invention for performing this method. In the schematic figures, which are not to scale.

[0013] FIGS. 1 and 2 show two different types of measuring devices according to the invention;

[0014] FIG. 3 shows a supplemented device solution for the embodiment according to FIG. 1; and

[0015] FIGS. 4 to 6 show different infrared spectra for carbon monoxide, carbon dioxide and ethane, wherein the ordinate showing absorbance A is plotted above the abscissa showing the wavenumbers in 1/cm.

[0016] The device according to the invention according to FIG. 1 shows a highly pressure-resistant infrared cuvette 10 having a pressure-resistant pipe section 12. An infrared wave guide 14, which is preferably formed as a galvanically gold-plated inner tube is located inside the pipe section 12, in the pipe sections 12 inserted and attached there according to the illustration of FIG. 1. Below the waveguide 14 a media-conducting tubular connection 16 opens into the pipe section 12, plus another tubular connection 18 above the waveguide 14. The port 16, as the arrow shows, is used for the supply of a gaseous medium and the port 18 is used for the discharge of the gas volume introduced into the pipe section 12. In principle, any gaseous media can be introduced and removed for investigation purposes; below, however, only hydrogen gas is considered, which is supplied from a hydrogen filling station (not shown) at very high pressure, for instance in the range of 700 bar, as a sample to the infrared cuvette 10.

[0017] Flange parts assigned in pairs 20, 22 and 24, 26 adjoin at the opposite free ends of the pipe section 12. The first flange 20 arranged at the top in FIG. 1 has a central recess for receiving a high-power infrared emitter 28. Underneath and received in a recess of the second flange 22 is an infrared transmissive, high-pressure resistant window 30, at the front of which an annular seal 32 is arranged for sealing the interior of the pipe section 12 from the environment. As further indicated in FIG. 1, the two flange parts 20 and 22 are connected to each other via a screw connection 34, including the annular seal 32 in a pressure-tight manner. Materials used for the window 30 are in particular silicon and germanium, which permit the passage of infrared radiation in a predeterminable wave range.

[0018] The flange part 24 terminating the tubular piece 12 at the bottom in turn has a central recess, into which a further infrared transmissive window 36 is inserted frontally on the upper side, which window ensures the sealing of the interior of the pipe section 12 towards the environment based on a soldered connection 38. An infrared detector 40 is then inserted in a central recess of the flange portion 26 beneath for the evaluation of the received infrared spectrum. Consequently, the infrared emitter 28 or the infrared detector 40 is located in the unpressurized area behind the respective windows 30, 36.

[0019] In the high-pressure resistant cuvette 10, the volume concentration of the gaseous impurities increases in proportion to the pressure, such that e.g. for an inlet pressure of the hydrogen of 500 bar, the infrared absorption in the measuring cell is 500 times that of an inlet pressure of 1 bar. This measuring effect of the illustrated robust and cost-effective IR infrared measuring technology is based on this multiplication.

[0020] The measuring arrangement or measuring device shown in FIG. 1 thus forms the infrared measuring device 42 provided for the method as a whole.

[0021] As the embodiment of FIG. 3 shows by way of example, the infrared measuring device 42 according to FIG. 1 is part of a total measuring device 44, which can be connected for the online measurement of gas impurities at a dispensing filling station, for example for hydrogen, with little installation effort. Solenoid 2/2-way valves 46 are connected in the ports 16, 18 to shut off the inflow and outflow of hydrogen gas. Consequently, the measuring device 44 can be used to take hydrogen gas from the discharge line of the tank (not shown) and introduce it for a measurement process in the infrared cuvette 10 for an evaluation process after closing the directional control valves 46.

[0022] In this case, both the infrared emitter 28 and the infrared detector 40 are connected to signal processing electronics via respective electrical connecting lines 48 and 50, which electronics are shown in FIG. 3 in the form of a black box as a control and processing unit 52. In the relevant signal processing unit, the respective pressure value or the temperature value in the measuring section, formed by the interior of the pipe section 12, can be detected via corresponding sensors P, T and used for the evaluation of the results determined optically. An output device 54 may be connected to the output side of the signal-processing control and processing unit 52, in turn, for example, which generates a measurement log on the quality (degree of contamination and nature of impurities) of the hydrogen dispensed by the filling station and preferably triggers an alarm if pre-definable quality parameters of the gas are exceeded.

[0023] The embodiment of FIG. 2 largely corresponds to the infrared measuring device 42 according to the embodiment of FIG. 1 with the proviso that both the infrared emitter 28 and the infrared detector 40 are housed side by side in the upper flange portion 20 in the center recess. A further difference is a mirror 46 reflecting infrared rays, said mirror now being received at the lower end of the pipe section 12 in the third flange section 24 via a soldered connection 38. A screwed connection, not shown in greater detail, comparable to the screwed connection 34, is used to firmly connect the lower two flanges 24 and 26 to each other, such that the lower solder joint 38 achieves a pressure-tight termination of the interior of the pipe section 12 towards the environment. As the double-arrow representation in the interior of the pipe section 12 shows, the mirror 56 doubles the length of the travel measuring section between the emitter 28 and the detector 40 compared to the solution according to FIG. 1, which in this respect increases the measuring accuracy of the measuring device 42 according to the embodiment of FIG. 2 accordingly.

[0024] The proposed solution according to the invention is used to perform a method for monitoring the hydrogen quality at a hydrogen filling station not shown in detail, having an overall measuring device 44 according to the exemplary embodiment of FIG. 3, consisting essentially of the high-pressure-resistant infrared cuvette 10 introduced above, an infrared emitter 28, an infrared detector 40 and at least one pressure sensor P and a control and processing unit 52, wherein the measuring device 44 is integrated as a whole in the hydrogen filling station and is for measuring processes on demand periodically filled with hydrogen and vented by means of the valves 46. The infrared measuring device 42, 44 is then used to measure the transmission of infrared radiation or infrared light at different wavelengths and pressures, and the concentration of, in particular, gaseous impurities in the hydrogen is computed therefrom. If the determined measured values give cause for concern, the output device 54 connected to the control and computing unit 52 in the form of an electronic signal processing can trigger an alarm if predefined limit values are exceeded.

[0025] Preferably, the control and computing unit 52 performs transmission measurements at different densities, buffers them and then subtracts them from each other. As already stated, a pressure sensor P can perform the pressure measurement to determine the density, wherein the pressure measurement can be supplemented by a temperature measurement by means of a temperature sensor T.

[0026] The use of an infrared emitter 28, preferably a hotplate emitter, which emits a broadband infrared beam, has been found to be particularly advantageous for performing the method according to the invention. Furthermore, it is advantageous if the infrared detector 40 is a multi-channel detector having filters in the range between 1000 and 4000 wavenumbers. Advantageously, the infrared detector 40 is a spectrometer. If, as shown in FIG. 2, the emitter 28 and the detector 40 are located on the same side of the pipe section 12, i.e. in the upper flange part 20, only common electronics for the pertinent components 28 and 40 are required.

[0027] As will be explained in more detail below, the distribution of the detected infrared-active bands of the individual contaminants, plotted against the wave number, indicates the type of the individual impurity. For instance, ammonia gas is found as an impurity for wave numbers around 1000 and, the contaminants formic acid, water, carbon monoxide and carbon dioxide occur in the range of 2000 wave numbers. Wave numbers around 3000 [indicate] formaldehyde and hydrocarbons and wave numbers just below 4000 again indicate water. As stated above, the relevant measurement range is between 1000 and 4000 wavenumbers, i.e. at wavelengths between 2.5 m and 10 m of the infrared radiation. The position of the absorption bands can therefore be used to identify a substance as such, and the attenuation of the infrared radiation as it passes through the hydrogen sample yields the concentration from Lambert-Beers law as follows:

A=Ig(I.sub.0/I.sub.1,)=Ig(I/T)= () c.Math.d

where: [0028] A: absorbance [0029] I.sub.0: intensity of irradiated light [W/m.sup.2] [0030] I.sub.1: intensity of the attenuated light [W/m.sup.2] [0031] T=I.sub.1/I.sub.0: transmittance [0032] (): molar (decadal) absorption coefficient [m.sup.2/mol] [0033] c: concentration [mol/l] [0034] d: travel length of the light beam through the sample [m]

[0035] The dependence of the absorption on the wavelength is reflected in the dependence of the molar absorption coefficient on the wavelength in Lambert-Beers law.

[0036] Lambert-Beers law outlines the standard approach for measuring small concentrations. At low concentrations, the length of travel d of the infrared light beam through the sample is increased. This can be effected by extending the measuring cell in the form of the cuvette 10 or by repeatedly irradiating the cuvette 10 using a mirror device with the mirror 56 as shown in FIG. 2. For the application mentioned here, however, the extension of the travel length d is a practical limit and it has proved to be advantageous to form the pipe section 12 formed as a measuring section of FIGS. 1 and 2 preferably at a length of 500 mm, lengths of 100 mm to 1500 mm are equally possible, too. Further, the diameter of the pipe section is 10, preferably 3 to 15 mm, more preferably 5 mm.

[0037] Furthermore, it is necessary to consider the concentration c, which constitutes yet another controllable quantity on the right-hand side of the above Lambert-Beer equation; c, as stated, denotes the concentration of the substance to be detected in the infrared cuvette 10 in mol/l. This parameter c can easily be increased significantly by an increase in pressure, which is particularly advantageous in the case of the hydrogen filling station, as the gas to be analyzed is already at very high pressure, for example of the order of 700 to 800 bar. The infrared spectra according to FIGS. 4 to 6 indicate that at the very high pressures of 700 bar, a significant measurement pattern (solid lines) immediately results, which is not the case at 1 bar (measurement lines shown in dashed lines).

[0038] The absorbance of the IR spectrum measured in FIG. 4 of about 0.06 for CO gas, at a concentration of 100 ppm, a pressure of 1 bar absolute and a path length of 10 m means that approx. 87% of intensity are transmitted at 2200 wavenumbers. However, the carbon monoxide limit set by standard SAE J2719 is only 0.2 ppm, i.e. one five-hundredth of the concentration of the measurement shown in FIG. 4. At this concentration the absorbance is 0.00012 and the transmission is 99.97%. This small change in transmission would be extremely difficult to detect using laboratory equipment. If the pressure is then increased to 700 bar in accordance with the solid line drawn in FIG. 4, the absorbance increases by a factor of 700. For a reduction of the travel length d from about 10 m to 500 cm according to the length of the pipe section 12 for the infrared cuvette 10, a factor of 20 for the absorbance is lost again and resulting in a value of 0.0042. However, this value again corresponds to a transmission of 99.03%. This reduction of almost 1% is easily detectable even using standard optical components. Similar estimates for water, hydrocarbons, carbon dioxide (see FIG. 5), formaldehyde, formic acid, ammonia and ethane (see FIG. 6) confirm the above observation and show that the deciding factor is the increase in concentration within the high pressure IR Cuvette 10, caused by the dispensing pressure of the hydrogen at the filling station.

[0039] As FIGS. 4 to 6 finally show, gaseous impurities such as carbon monoxide (FIG. 4), carbon dioxide (FIG. 5) or ethane (FIG. 6) can be reliably detected in the hydrogen gas at high pressures using the device according to the invention described above according to FIGS. 1 to 3 and, if pre-definable limit values are exceeded, the hydrogen tank operation can advantageously be interrupted.