ELECTROCHEMICAL GAS SENSOR, FILTER AND METHODS
20170276634 · 2017-09-28
Inventors
Cpc classification
Y02A50/20
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
G01N33/0024
PHYSICS
G01N27/413
PHYSICS
G01N33/0059
PHYSICS
International classification
G01N27/413
PHYSICS
Abstract
The invention relates to an electrochemical gas sensing apparatus for sensing one or more analytes, such as NO.sub.2 and/or O.sub.3, in a sample gas and a method of using same. The apparatus uses Mn.sub.2O.sub.3 as a filter for ozone. The Mn.sub.2O.sub.3 may take the form of a powder which may be unmixed, mixed with various PTFE particles sizes, formed into a solid layer deposited onto a membrane and/or pretreated with NO.sub.2.
Claims
1. Electrochemical gas sensing apparatus for sensing at least one gaseous analyte and comprising a housing having an inlet, a sensing electrode and an ozone filter interposed between the sensing electrode and the inlet, wherein the ozone filter comprises Mn.sub.2O.sub.3.
2. Electrochemical gas sensing apparatus according to claim 1, wherein the Mn.sub.2O.sub.3 is Mn.sub.2O.sub.3 powder.
3. Electrochemical gas sensing apparatus according to claim 1 wherein the Mn.sub.2O.sub.3 is NO.sub.2 treated.
4. Electrochemical gas sensing apparatus according to claim 3, wherein the Mn.sub.2O.sub.3 is Mn.sub.2O.sub.3 powder which has at least 10.sup.12 molecules of NO.sub.2 adsorbed thereto per cm.sup.2 of surface.
5. Electrochemical gas sensing apparatus according to claim 2, wherein the ozone filter comprises Mn.sub.2O.sub.3 powder mixed with binder.
6. Electrochemical gas sensing apparatus according to claim 5, wherein the ozone filter comprises binder particles coated with the Mn.sub.2O.sub.3 powder.
7. Electrochemical gas sensing apparatus according to claim 1, wherein the ozone filter comprises a solid microporous layer which comprises Mn.sub.2O.sub.3.
8. Electrochemical gas sensing apparatus according to claim 1 for sensing NO.sub.2 and/or ozone.
9. Electrochemical gas sensing apparatus according to claim 1, further comprising a second sensing electrode, wherein the second working electrode is in gaseous communication with a gas sample without an intervening ozone filter.
10. Electrochemical gas sensing apparatus according to claim 9, wherein the at least one said analyte comprises ozone.
11. A method of forming an electrochemical gas sensing apparatus for sensing at least one gaseous analyte, the method comprising providing a housing having an inlet and a sensing electrode and providing an ozone filter interposed between the sensing electrode and the inlet, wherein the ozone filter comprises Mn.sub.2O.sub.3.
12. A method of forming an electrochemical gas sensing apparatus according to claim 11, wherein the ozone filter comprises Mn.sub.2O.sub.3 powder.
13. A method of forming an electrochemical gas sensing apparatus according to claim 12, comprising the step of treating the Mn.sub.2O.sub.3 powder with NO.sub.2.
14. A method of forming an electrochemical gas sensing apparatus according to claim 11, wherein the Mn.sub.2O.sub.3 is Mn.sub.2O.sub.3 powder is mixed with binder particles.
15. A method according to claim 14 wherein the Mn.sub.2O.sub.3 powder coats the binder particles.
16. A method of forming an electrochemical gas sensing apparatus according to claim 11, wherein the filter comprises a solid microporous layer of Mn.sub.2O.sub.3.
17. A method of forming an electrochemical gas sensing apparatus according to claim 16, wherein the method comprises depositing a layer of Mn.sub.2O.sub.3 on a gas porous membrane.
18. A method of forming an electrochemical gas sensing apparatus according to claim 11, comprising providing a second sensing electrode in gaseous communication with a gas sample without an intervening ozone filter.
19. A method of sensing NO.sub.2 and/or ozone comprising forming an electrochemical gas sensing apparatus by the method of claim 18, and exposing the gas sensing apparatus to a gas sample, wherein the difference in the signals from the sensing electrodes is representative of ozone in the gas sample, and thereby determining from the signals from the first and second sensing electrodes the concentration of NO.sub.2 and/or ozone in the gas sample.
20. A method of sensing NO.sub.2 and/or ozone comprising forming an electrochemical gas sensing apparatus by the method of claim 18, and exposing the gas sensing apparatus to a gas sample, wherein the difference in the signals from the sensing electrodes is representative of ozone in the gas sample, and thereby determining from the signals from the first and second sensing electrodes the concentration of NO.sub.2 and/or ozone in the gas sample.
21. A method of sensing NO.sub.2 and/or ozone comprising forming electrochemical gas sensing apparatus according to claim 1 and bringing the inlet into gaseous communication with a gas sample.
22. A method of sensing NO.sub.2 and/or ozone comprising forming electrochemical gas sensing apparatus by the method of claim 11 and bringing the inlet into gaseous communication with a gas sample.
Description
BRIEF DESCRIPTION OF THE FIGURES
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DETAILED DESCRIPTION OF EXAMPLE EMBODIMENTS
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[0085] A series of circular separator discs, wicks or wetting filters (15) separate the working electrode from the counter electrode and the reference electrode. The circular separator discs, wicks or wetting filters (15) are made of a hydrophilic, non-conductive material permeable to the electrolyte which functions to transport electrolyte by capillary action. Typically the material is glass fibre. The circular separator discs, wicks or wetting filters serve to ensure that each of the electrodes is in contact with the electrolyte.
[0086] The working electrode (11) is a carbon electrode and typically comprise a catalytic layer of carbon mixed with polytetrafluoroethylene (PTFE) binder which is then bonded to a gas porous, but hydrophobic, PTFE support to allow gas support to the catalyst, i.e. the electrode active material, but avoid electrolyte leakage or flooding of the electrode. The carbon electrodes can be manufactured using common conventional technologies such as pressing, screen printing, inkjetting and spraying a carbon slurry onto a porous membrane. Here the working electrode catalyst will typically have a diameter of 14 mm. A mixture of carbon and microparticulate polytetrafluoroethylene (PTFE) is sintered and is preferably prepared by pressing the resulting mixture onto a support in the form of a gas porous membrane, such as PTFE sheet. Where carbon is pressed at the normal pressure used in the field, i.e. around 200 kg/cm.sup.2, the amount of catalyst is preferably between 5 and 30 mg per cm.sup.2 of electrode surface area. Preferably the binder is a Fluon matrix (Fluon is a Trade Mark) of around 0.002 ml per cm.sup.2. Other electrodes used in the gas sensing apparatus of the invention, such as the Platinum black electrodes can be prepared in a similar way.
[0087] An O ring is located at the top of the porous membrane (21) and acts to seal the sensor and to aid compressing the stack of components when the sensor is sealed. Also present are a number of platinum strips that serve to connect each electrode to one of the terminal pins (24) provided at the base of the sensor. Closing housing is a dust filter (25) to prevent dust and other foreign objects from entering.
[0088] The ozone filter (19) is formed of MnO.sub.2 powder which has been treated with NO.sub.2 as described below and the sensor is useful to sense NO.sub.2 in the presence of gases such as SO.sub.2, CO, NO, NH.sub.3, H.sub.2 and O.sub.3, which were it not for the choice of electrode and the presence of the ozone filter, would otherwise interfere with the measurement.
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[0090] The first gas sensor (2) has an ozone filter (19) in internal chamber (23) above the working electrode (11A), functioning as the first working electrode. Again, the ozone filter is prepared by the method set out below. The second gas sensor (4) has a working electrode (11B), which is the same as the working electrode (11A) of the first gas sensor (4) but functions as the second working electrode, and has no ozone filter in the internal chamber (23). The two working electrodes (11A), (11B) correspond to those described above in relation to
[0091] The embodiment of
[0092] In some of the embodiments discussed below, the sensor of
[0093]
[0094] Example circuitry for the gas sensing apparatus of the invention in the embodiment of
Forming the Ozone Filter
[0095] In order to form the ozone filter, Mn.sub.2O.sub.3 filter powder (99% purity) is treated by passing a flow of NO.sub.2 gas therethrough. With reference to
[0096] In an illustrative example, 20 g of Mn.sub.2O.sub.3 or 30 g or 50 g of Mn.sub.2O.sub.3/PTFE filter powder was treated in a 250 ml gas washing bottle. The NO.sub.2 gas was passed through the filter powder at a concentration of 100 ppm and a flow rate of 0.5 l.Math.min.sup.−1 for 2 hours.
[0097] By monitoring the concentration of NO.sub.2 gas leaving the bottle, we therefore calculated the amount of NO.sub.2 which was adsorbed before the Mn.sub.2O.sub.3 was saturated. This experiment was repeated. It was found that 1.78×10.sup.−8 moles of NO.sub.2 were adsorbed per gram of Mn.sub.2O.sub.3. Using the value of surface area of the MnO.sub.3 powder obtained from BET analysis of 2.42 m.sup.2/g we estimated that 2.41×10.sup.12 molecules of NO.sub.2 were adsorbed per cm.sup.2 of Mn.sub.2O.sub.3 surface. This is consistent with the values repeated in the paper J. Phys. Chem. C 2014, 118, 23011-23021 where the number of NO.sub.2 molecules adsorbed on TiO.sub.2 are in the order of 10.sup.13 molecules/cm.sup.2.
[0098] The resulting material is advantageous in that it filters ozone with minimal degradation of the NO.sub.2 signal compared to untreated Mn.sub.2O.sub.3. The layer remains gas permeable. Furthermore, it filters ozone efficiently, enabling a relatively low proportion of Mn.sub.2O.sub.3 mixed with PTFE to function effectively, reducing cost. An image of the resulting Mn.sub.2O.sub.3 coated PTFE particles is shown in
[0099] A mixture of Mn.sub.2O.sub.3 and PTFE particles having a size of having a size range of 710 μm to 1500 μm was prepared by manually mixing Mn.sub.2O.sub.3 powder with PTFE in a glass container until all Mn.sub.2O.sub.3 powder coats the PTFE. In some of the examples below, Mn.sub.2O.sub.3 and PTFE were mixed in a weight ratio of 1:10. The resultant mixture is then sieved through a 710 micron sieve stack using a motorised mechanical sieve for 1 hour. The portion that did not fall through the 710 micron sieve is then collected while the remaining material that did fall through the 710 micron sieve is discarded.
[0100] In some examples below, Mn.sub.2O.sub.3 and PTFE were also mixed in a weight ratio of 1.6:8.4 (16% by weight). In those examples, the resultant mixture was then sieved through a 500 micron sieve stack using a motorised mechanical sieve for 1 hour. The portion that did not fall through the 500 micron sieve was then collected while the remaining material that did fall through the 500 micron sieve was discarded.
[0101] In the examples where the Mn.sub.2O.sub.3 was mixed with 100 micron PTFE in a weight ratio of 1.6:8.4 (16% by weight), resultant mixture was then thoroughly shaken using a motorised mechanical sieve for 1 hour.
Filter in the Form of a Solid Layer of Powdered Mn.sub.2O.sub.3:
[0102] For examples 13 to 15, solid filter layers of powdered Mn.sub.2O.sub.3 were formed with a diameter of 14 mm and 19 mm. A mixture of powdered Mn.sub.2O.sub.3 and microparticulate polytetrafluoroethylene (PTFE) was sintered and the resulting mixture was pressed onto a support PTFE sheet, acting as a gas porous membrane. Mn.sub.2O.sub.3 was pressed at the normal pressure used in the field, i.e. around 400-600 kg/cm.sup.2, and the amount of Mn.sub.2O.sub.3 was in the range 15 to 30 mg per cm.sup.2 of surface area. The Mn.sub.2O.sub.3 was mixed with a Fluon matrix (Fluon is a Trade Mark) of around 0.0065 ml per cm.sup.2, which contains PTFE which acted as binder. In these examples Fluon with a PTFE particle size in the range of 200-300 microns diameter was used. Mn.sub.2O.sub.3 was 74% by weight of the solid microporous layer, with the balance being PTFE.
EXPERIMENTAL SECTION
[0103] The sensors used in the following experiments were tested on standard potentiostatic circuit boards (
[0104] The following materials were used in the filter powder. These materials were used in each following experiment unless indicated to the contrary.
[0105] Manganese (III) oxide (Mn.sub.2O.sub.3), 99% purity, approx. 325 mesh (44 micrometers) powder, from Sigma Aldrich, product number 377457. BET analysis on the sample gives a surface area of 2.242 m.sup.2/g.
[0106] Manganese (IV) oxide (MnO.sub.2), 99.9% purity, approx. 325 mesh (44 micrometers) powder, from Alpha Aesar, product number 42250. BET analysis on the sample gives a surface area of 2.08 m.sup.2/g.
[0107] PTFE binder (Fluon PTFE G307 (median particle size 500 to 1500 microns) (Fluon is a trade mark). The powder was sieved to collect only particles with a size of at least 710 microns. Also: Fluon PTFE G201 (median particle size 500 microns) and Fluon PTFE G204 (median particle size 100 microns).
[0108] The working electrodes were made from carbon graphite (particle size <20 μm, Aldrich, product code 282863).
[0109] Calibration of the sensors according to the invention was carried out as follows. The sensor output is given in nA. Amperometric gas sensors have a linear output with target gas analyte concentration. This makes possible to use a simple calibration procedure where the relation between the sensor output and the gas concentration is determined by exposing the sensor to a known concentration of gas analyte. For this application the sensitivity to both the first and the first working electrodes is determined for each of the target gases, NO.sub.2 and O.sub.3. The sensor output can then be used to calculate the concentration of NO.sub.2 and O.sub.3.
[0110] If the following parameters are defined as follows: [0111] i.sub.1 is the current observed on the second working electrode. [0112] I.sub.2 is the current observed on the first working electrode. [0113] S.sub.1(NO2) is the second working electrode sensitivity to NO.sub.2. [0114] S.sub.1(O3) is the second working electrode sensitivity to O.sub.3. [0115] S.sub.2(NO2) is the first working electrode sensitivity to NO.sub.2. [0116] S.sub.2(O3) is the first working electrode sensitivity to O.sub.3. [0117] C.sub.(NO2) is the NO.sub.2 analyte concentration to determine. [0118] C.sub.(O3) is the O.sub.3 analyte concentration to determine.
[0119] Then, by definition and taking into account the linear relationship between the sensor output and the analyte concentration, the following can be written:
i.sub.1=S.sub.1(NO2).Math.C.sub.(NO2)+S.sub.1(O3).Math.C.sub.(O3)
i.sub.2=S.sub.2(NO2).Math.C.sub.(NO2)+S.sub.2(O3).Math.C.sub.(O3)
[0120] The ozone filter on top of the first working electrode means that S.sub.2(O3)=0. So C.sub.(NO2) can be calculated using the simple relation:
C.sub.(NO2)=i.sub.2/S.sub.2(NO2)
[0121] The NO.sub.2 analyte concentration being now known it is then possible to calculate the O.sub.3 analyte concentration using the second working electrode output:
C.sub.(O3)=(i.sub.1−S.sub.1(NO2).Math.C.sub.(NO2))/S.sub.1(O3)
or C.sub.(O3)=(i.sub.1−S.sub.1(NO2).Math.(i.sub.2/S.sub.2(NO2)))/S.sub.1(O3)
Experiment 1
[0122] In a first example, sensors according to
[0123] For these and subsequent experiments the first working electrode, the second working electrode, the additional electrode and the reference electrode are made of carbon graphite and the counter electrode is made of platinum black.
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[0127] It is apparent from the results that the untreated Mn.sub.2O.sub.3 filter efficiently removes O.sub.3. No signal is observed in the presence of 500 ppb of O.sub.3 (
Experiment 2
[0128] In this example, sensing apparatus comprised a sensor according to
[0129] For this and all subsequent experiments, the Mn.sub.2O.sub.3 had been treated with NO.sub.2 gas described above.
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[0131] This figure shows that with a mixture of NO.sub.2 and O.sub.3, the filtered sensor senses only NO.sub.2, whereas the unfiltered sensor detects both gases and, in the presence of both gases simultaneously, the output of the unfiltered sensor corresponds to the sum of the output expected for each of the gases. Accordingly, Mn.sub.2O.sub.3 is suitable as a filter material to remove ozone without affecting the signal due to NO.sub.2.
Experiment 3
[0132] Sensors according to
[0133] This shows that the cross-sensitivity to NO is systematically lower with Mn.sub.2O.sub.3 than MnO.sub.2, and that this improvement persists.
Experiment 4
[0134] Sensors according to
Experiment 5
[0135] The ozone filtering capacity of the sensors was further tested and
[0136] These results again demonstrate that Mn.sub.2O.sub.3 powder, whether unmixed or mixed with mg of PTFE particles having a size range of 710 μm to 1500 μm forms an efficient ozone filter.
Experiment 6
[0137] Experiments were carried out to assess the cross sensitivity of the sensors to common interferents. Table 1, below, shows the cross sensitivity of sensors formed with (a) mg of powdered Mn.sub.2O.sub.3 and (b) 25 mg of powdered Mn.sub.2O.sub.3 mixed with 225 mg of PTFE particles having a size range of 710 μm to 1500 μm (i.e. 10% by weight of Mn.sub.2O.sub.3 in binder) to specific gases, relative to NO.sub.2, at the concentrations stated. Two sensors of each type were formed and tested.
TABLE-US-00001 TABLE 1 500 mg Mn.sub.2O.sub.3 25 mg Mn.sub.2O.sub.3 GAS ppm Sensor 1 Sensor 2 Sensor 1 Sensor 2 SO2 5 1.53% 0.81% 0.86% 0.79% CO 5 1.25% 0.85% 1.41% 1.39% H2 100 0.24% 0.04% 0.06% 0.00% CO2 50000 0.00% 0.00% 0.00% 0.00% NH3 20 0.42% 0.18% 0.09% 0.06%
[0138] Further experiments demonstrated that the quality of ozone filtering was unsatisfactory if the Mn.sub.2O.sub.3 powder was reduced to 5% or less by mass of the combined mixture of Mn.sub.2O.sub.3 and PTFE binder particles. Mixture of Mn.sub.2O.sub.3 powder with at least the same mass, and ideally more, of PTFE particles leads to the Mn.sub.2O.sub.3 coating the particles rather than forming solid masses.
[0139] For unmixed Mn.sub.2O.sub.3 powder (as specified in the Experimental Section above) we found that the ratio of the active surface area of filter material (by BET analysis) to the cross-sectional area of the filter (perpendicular to the gas path through the filter) was about 0.85 m.sup.2 per cm.sup.2. For Mn.sub.2O.sub.3 mixed with PTFE binder to 10% by mass of the combined mixture of Mn.sub.2O.sub.3 and binder, this ratio was 0.025 m.sup.2 per cm.sup.2 and for Mn.sub.2O.sub.3 mixed with PTFE binder to 8% by mass of the combined mixture it was 0.02 m.sup.2 per cm.sup.2.
Experiment 7
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Experiment 8
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[0142] The results demonstrate that sensors using NO.sub.2 treated Mn.sub.2O.sub.3 powder, with or without dilution, shows a good and reproducible response to NO.sub.2 6 months after NO.sub.2 treatment.
Experiment 9
[0143] Table 2 below shows the change with time (in days) of the cross sensitivity to 2 ppm NO (i.e. the ratio of the current response to 2 ppm NO to the current response to 2 ppm NO.sub.2) of sensors according to
TABLE-US-00002 TABLE 2 Age 25 mg 450 mg 25 mg 500 mg (days) ppm MnO.sub.2 MnO.sub.2 Mn.sub.2O.sub.3 Mn.sub.2O.sub.3 10 2 1.6 9.7 1.3 1.7 110 2 5.7 13.9 2.2 4.5 210 2 9.2 13.3 4.4 5.7
[0144] This shows that the cross-sensitivity to NO is lower when the ozone filter comprises powdered Mn.sub.2O.sub.3 than when the ozone filter comprises powdered MnO.sub.2, and that the sensors in which Mn.sub.2O.sub.3 is mixed with PTFE give the best (lowest) cross-sensitivity to NO. Of particular benefit, the NO cross-sensitivity increases with time but this deterioration is reduced with powdered Mn.sub.2O.sub.3 in comparison to powdered MnO.sub.2 and is minimised when powdered Mn.sub.2O.sub.3 is mixed with PTFE.
Experiment 10
[0145] Experiments were carried out to assess the temperature sensitivity of sensors according to
TABLE-US-00003 TABLE 3 10 w/w % 10 w/w % 100 w/w % Temp. No No Mn.sub.2O.sub.3 NO.sub.2 Mn.sub.2O.sub.3 not Mn.sub.2O.sub.3 NO.sub.2 ° C. filter filter treated treated treated −30 70 68 70 39 −2 −20 75 73 80 56 6 −10 82 79 88 75 45 0 89 87 94 90 85 10 95 94 98 98 97 20 100 100 100 100 100 30 105 104 104 101 103 40 110 107 103 99 107 50 112 117 102 100 128
Experiment 11
[0146] In order to demonstrate that the ozone filter is useful with analytes other than NO.sub.2, we modified a commercial electrochemical sensor for SO.sub.2, having gold/ruthenium working and reference electrodes and a platinum black counter electrode (brand SO2-A4 available from Alphasense Limited, Great Notley, UK) by replacing an H.sub.2S filter with 25 mg of Mn.sub.2O.sub.3 powder mixed with 225 mg PTFE particles having a size range of 710 μm to 1500 μm, treated with NO.sub.2 as above.
[0147]
[0148]
[0149] The results demonstrate that the ozone filter can be used to remove ozone from a gas sample in an SO.sub.2 sensor. Again, O.sub.3 may be measured with a first sensor which has an electrode which is sensitive to SO.sub.2 and O.sub.3 and ozone filter according to the invention and a second sensor, also having an electrode which is sensitive to SO.sub.2 and O.sub.3, but no ozone filter, and comprising output signals.
Experiment 12
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[0151] No signal is observed in the presence of 500 ppb of O.sub.3 (
Experiment 13
[0152]
[0153] Fluon comprises PTFE and a solvent and the resulting solid layer has about 26% PTFE by mass. Most of the Mn.sub.2O.sub.3 is therefore not associated with the PTFE particles and the purpose of the PTFE is to provide some porosity, as well as to make the material easier to handle in a manufacturing setting than unmixed Mn.sub.2O.sub.3.
[0154] No signal is observed in the presence of 500 ppb of O.sub.3 (
Experiment 14
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[0156] This demonstrates that powdered Mn.sub.2O.sub.3 pressed into a solid layer may form an effective ozone filter.
Experiment 15
[0157] Sensors according to
[0158] The sensors were exposed to 2 ppm NO.sub.2 for 10 minutes and then to 500 ppb ozone O.sub.3 for 5 minutes.
[0159] These results demonstrate that Mn.sub.2O.sub.3 powder, whether unmixed, mixed with various PTFE particles sizes or as a solid layer deposited onto a membrane, forms an efficient ozone filter.
[0160] Although in the examples shown which use a solid layer, the layer comprises some PTFE in addition to Mn.sub.2O.sub.3, it is provided simply to ensure that the solid layer is microporous and can therefore be penetrated by analyte gas. Alternatively, Mn.sub.2O.sub.3 may be deposited by other means to give a microporous structure, for example by depositing Mn.sub.2O.sub.3. microparticles without binder, or screen printing optionally with glass or other particles. The PTFE is not required.
[0161] Furthermore, in further example embodiments, Mn.sub.2O.sub.3 powder, whether unmixed, or mixed with binder as described above, may be used in combination with a microporous solid Mn.sub.2O.sub.3 layer, to give a more robust sensor, for example for use in atmospheres with a particularly high concentration of O.sub.3.
CONCLUSIONS
[0162] In the case of gas sensing apparatus for detecting NO.sub.2 and/or O.sub.3, the results demonstrate that Mn.sub.2O.sub.3 is useful as an ozone filter, whether as a powder or as a solid microporous layer. The cross sensitivity to NO can be reduced by mixing the Mn.sub.2O.sub.3 powder with binder, or by treating it with sufficient NO.sub.2. Although these mixing or treatment steps could compromise ozone filtering, we have found that they have a greater effect in reducing cross sensitivity to NO and that it is therefore possible to obtain an efficient ozone filter with low cross sensitivity to NO.