GB2036975A - Process for producing a solid electrolyte oxygen gas sensor element - Google Patents

Abstract

An activated solid electrolyte oxygen gas sensing element with increased voltage output, shortened switching time and reduced internal resistance, the sensing element having inner and outer conductive catalyst electrodes thereon, is produced by subjecting the outer surface with the outer electrode of such a sensor to a nonoxidizing atmosphere at a temperature above 450 DEG C and, at the same time applying a direct current to the element with the outer electrode as an anode, the current density being at least 5 milliamps per square centimeter of the planar surface of the outer electrode layer. Preferred conditions are a temperature of 60-900 DEG C, and a current density of 20-150 mA/cm<2>. The non-oxidising atmosphere may be neutral e.g. nitrogen or reducing.

Description

SPECIFICATION Process for producing a solid electrolyte oxygen gas sensor element The invention relates to a process for producing a solid electrolyte oxygen gas sensor element.

The solid electrolyte-type oxygen sensor, in conjunction with a three-way catalyst converter, has been demonstrated to be an effective device for reduction of objectionable automotive emission by closed-loop control of the air-fuel mixture for the engine. The sensor comprises a sensor element which is generally formed as a stabilized zirconia solid electrolyte body in a thimble shape with both its inner and outer surfaces coated with a layer of a conductive catalyst electrode, such as a layer of platinum.

When heated in the exhaust manifold with the outer electrode subjected to the exhaust gas and the inner electrode exposed to the ambient air, the sensor develops an electrochemical potential between the two electrodes which varies with the oxygen concentration in the exhaust gas stream. A large step change in the electrical potential occurs when the exhaust gas changes its composition from rich to lean or lean to rich passing through the point of stoichiometry. The voltage switching is used as a feedback signal to control the inlet air-fuel ratio within a narrow band around stoichiometry.

The sensor characteristics which are necessary or desirable for effective closed-loop control of inlet air-fuel mixture are high voltage outputs, fast voltage switching in response to exhaust gas variation, and low internal resistance. Typically, for an effective sensor operating at 3500C electrolyte temperature, the desired voltage outputs are 600 to 1000 millivolts on rich and -200 to 200 millivolts on lean; the switching response (defined to be the transient time between 300 and 600 millivolts of sensor voltage when the exhaust condition is suddenly changed from rich to lean or lean to rich) less than 300 milliseconds; and the internal resistance less than 200 kiloohms.At 8000C, the desired voltage outputs are 700 to 900 millivolts on rich and 0 to 1 50 millivolts on lean; the switching response less than 100 milliseconds; and the internal resistance less than 100 ohms.

The present invention relates to a process for improving the sensor performance in terms of voltage output, switching response time and internal resistance. The process involves the current activation treatment of the sensors under controlled conditions with an external direct current applied to the sensor element with the outer electrode connected to the positive terminal of the electrical supply, or, in other words, with the outer electrode as an anode and the inner electrode as a cathode. The applied current appears to activate both the outer and the inner electrodes and the electrode-electrolyte interfaces, while at the same time polarizing the solid electrolyte.

The present process provides for a one time treatment of the solid electrolyte oxygen gas sensor element which provides improved properties to the sensor, namely a high positive voltage output, a fast switching response and a low internal resistance.

Solid electrolyte oxygen gas sensor elements are activated so as to provide improved properties, the element comprising a solid electrolyte body having an inner conductive catalyst electrode on the inner surface thereof and an outer conductive catalyst electrode on the outer surface thereof, by subjecting the outer surface of the element, with its outer conductive catalyst electrode coating, to a nonoxidizing atmosphere and heating the element to an elevated temperature in excess of 4500 C. While at said elevated temperature and with the outer conductive catalyst electrode in contact with a nonoxidizing atmosphere, a direct current is applied to the sensor element, with the outer electrode as an anode, with the current density thereof being at least 5 milliamps per square centimeter of the outer conductive catalyst electrode planar surface.

The gas sensor element is generally in the shape of a closed tubular member, thimble-like, and is formed of a solid electrolyte, such as zirconium dioxide containing various stabilizing materials such as calcium oxide or yttrium oxide. The general shape of the sensor element and the compositions usable in forming such elements are known, with such conventional design described in U.S. 3,978,006 and other published literature. The preferred composition is a solid electrolyte body formed from a mixture of zirconium dioxide and stabilizing materials, such as calcium oxide or yttrium oxide.

To both the inner and outer surfaces of the solid electrolyte oxygen gas sensor element there are applied conductive catalyst electrodes. Generally, the inner conductive catalyst electrode is applied to the inner surface such as by applying a platinum paste, which may contain a glass frit, with the paste preferably covering the interior surface of the closed terminal end of the sensor element and extending to the shoulder of the electrolyte body. The electrolyte body, with the applied paste, is then fired at a temperature of 600--10000C or higher, as known in the art, to convert the platinum paste coating into an electrically conductive catalytic inner electrode. The outer conductive catalyst electrode is applied to the outer surface of the electrolyte body by known means, such as thermal vapor deposition.Because of the intended exposure of the outer electrode to high temperatures and gas velocities during operation of the sensors, the same may be provided with a porous protective outer layer such as a layer of porous Al203-Mg0 spinel.

The conductive catalyst electrodes are preferably formed from a platinum family-metal catalyst such as platinum, palladium, rhodium or mixtures thereof, with platinum being the preferred catalyst material.

In the present process, the solid electrolyte sensor element is treated by application of a direct current charge thereto, in a particular manner and under particular conditions which improve the properties of the element relative to untreated sensor elements and sensor elements of the prior art. The direct current charge is applied to the sensor element while the outer surface thereof, having the outer conductive catalyst coating, is at an elevated temperature and is subjected to a nonoxidizing gaseous atmosphere.

The elevated temperature to which the outer surface of the sensor element must be heated is in excess of about 4500 C, with a temperature in the range of 600-9000C preferred. The temperature may be higher than this range and may be as high as about 1 1000C, with the upper temperature limit for a particular sensor element being dependent upon the effect of such high temperatures upon the electrolyte composition. Too high a temperature would also cause deterioration of the catalytic layer of the sensor element.

While the outer surface of the sensor element, with its outer conductive catalyst electrode, is at such an elevated temperature, that electrode is subjected to a nonoxidizing atmosphere. It has been found that while a reducing, a neutral or an inert atmosphere is useful in the present invention, an oxidizing atmosphere, such as air, does not provide the results desired. Examples of reducing gases which may be used are carbon monoxide, hydrogen, or rich exhaust gas mixtures, while neutral gases, such as nitrogen, inert gases, such as argon, are also useful to provide the gaseous atmosphere during treatment under the present process. A small amount of water vapor may be present but it is not necessary. The preferred atmosphere is a neutral atmosphere comprising nitrogen.

While the outer surface of the sensor element, with its outer conductive catalyst coating, is at the elevated temperature and subjected to a nonoxidizing atmosphere, a direct current is applied to the sensor element with the outer electrode as an anode and the inner electrode as a cathode. A direct current power supply is thus connected to the conductive catalyst electrodes, with the outer electrode connected to the positive terminal and the inner electrode connected to the negative terminal of the power source.

The current charge is such that a current density is provided which is greater than 5 milliamperes per square centimeter of the outer conductor catalyst electrode planar surface. The term "current density" as used herein is determined by dividing the current (in milliamperes) by the planar surface area of the outer conductive catalyst electrode (cm2) on the outer surface of the solid electrolyte body.

The term "planar surface of the outer electrode" is used to define the surface that would be present if the conductive catalyst electrode were a smooth coating without porosity.

The preferred range of current density used in the present process is between about 20 to 1 50 milliamperes per square centimeter of the outer conductive catalyst electrode surface. Current densities below 5 ma/cm2 are not effective in the present princess, while current densities of much higher value can be used, to a point where the sensor element cannot withstand the shock and may shatter. The preferred range, however, has been found to provide the desired properties to the sensor element without deleterious effects upon the catalytic electrode or the solid electrolyte body.

The direct current is applied to the sensor element at the required elevated temperature and while the outer electrode is in the presence of a nonoxidizing gas for a period of time which will vary dependent upon the temperature, current density and other conditions. A period of current application, as low as two seconds, has been found to be sufficient, while much longer times may be used. A preferred time of application of the current, with the preferred temperature range and current density, is about six seconds to ten minutes. Where the longer time periods of current application are used, the sensor element may require a recovery treatment, that is holding the sensor element at the elevated temperature for a period of time after the current is turned off.

The following examples further illustrate the present invention. In these examples. the testing of thimbles, as sensor elements, to determine their performance in terms of voltage output under rich and lean conditions, the switching response to gas variation and their internal resistance, was made by inserting the thimbles into protective housings with conductive leads connected to the inner and outer electrodes to form sensors. The tests were conducted at 3500C and at 8000C with the 8000C testing effected first.

The sensor performance tests were conducted by inserting the sensors into a cylindrical metal tube and exposing them to oxidizing and reducing gaseous atmospheres within the tube through use of a gas burner adjustable to produce such atmospheres. Sensors placed in the desired positions in the tube were heated to testing temperature and the voltage output measured using a volt meter. The output was also connected to an oscilloscope to measure the speed of response of the sensor when the burner flame was changed from rich to lean and from lean to rich.A routine test consisted of setting the flame to rich condition, measuring the voltage output of the sensor, switching the flame suddenly to lean condition triggering the oscilloscope sweep at the same time to record the rich to lean switch of the sensor, switching the flame suddenly back to rich condition, again triggering the oscillosocpe to record the sensor output change, and finally adjusting the flame to a lean condition and measuring the sensor output voltage. The switching time is defined as the time period required for the output voltage, as recorded on the oscilloscope to sweep between 600 and 300 millivolts. When the sensor output voltage under rich gas condition is less than 600 millivolts, the switching response time is not determinable (n/d) according to the criteria used for this switching response measurement. Rich voltage output measurements were then made with different known values of shunting resistance across the sensor terminals. These measurements provided data for calculating the internal resistance of the sensors.

A series of gas sensors electrolyte body thimbles was prepared, for use in the following examples, from ball-milled zirconia, yttria and alumina in a ratio of 80%, 14% and 6% by weight respectively, by isostatically pressing the same in the desired thimble shape and firing at high temperature.

EXAMPLE I Six of the series of electrolyte body thimbles (PA-2, PA-3, PA-S, PA-9, PA14 and PA-i 5) had an inner electrode applied to the inner surface thereof by coating the inner surface with a platinum suspension containing a glass frit for bonding purposes. The thimbles, with their inner electrodes, were then heated in an oxidizing atmosphere to burn off the organic constituents of the suspension and bond the platinum to the zirconia surface. The external platinum catalyst electrode was next applied to the outer surface of the thimble by known vapor deposition. A porous ceramic coating was applied over the external catalyst layer for protection. The thimbles were then formed into sensors and tested as to voltage output, switching response and internal resistance, as hereinbefore described.

The results of the tests are listed in Table I under the designation "No Treatment." The thimbles were then subjected to a current activation by inserting the thimbles, as sensors in a protective housing and with conductive leads, into a manifold, with the outer surface of the sensor elements thereof having the outer conductive catalyst coating thereon exposed, while preheated during a ten-minute period to a temperature of 7500C, in a flow of 0.5% CO in nitrogen, (with 0.01 mg/cm3 water vapor when indicated as "wet"), at a flow rate of 710 cm3/min. The inner conductive catalyst electrode was in contact with air, and the temperature of the sensor was taken at the bottom of the inner region of the sensor element.The sensors were then subjected to a direct current, as indicated, for a ten-minute period, the direct current charge applied at a current density of 100 milliamperes/cm2 of the outer electrode planar surface. The direct current was then stopped and the sensor elements allowed a recovery period of ten minutes at said temperature and with the outer electrodes in said gas flow.

These sensors were then again tested as to voltage output, switching response and internal resistance. The results of these tests are listed in Table I under the heading "After Current Activation." TABLE I Sensor Treatment 350 Testing 800 Testing Voltage Switching Internal Voltage Switching Internal Output Response Resis- Output Response Resis Rich Lean RL LR tance Rich Lean RL LR tance (mv) (mv) (ms) (ms) (k#) (mv) (mv) (ms) (ms) (#) PA-2 No Treatment 66 -269 n/d n/d 616 755 56 15 75 778 PA-3 No Treatment 275 -148 n/d n/d 529 759 77 15 55 224 PA-8 No Treatment 277 -101 n/d n/d 513 767 59 10 40 211 PA-9 No Treatment 285 -143 n/d n/d 431 771 77 10 45 260 PA-14 No Treatment 160 -199 n/d n/d 467 778 51 10 40 131 PA-15 No Treatment 131 -239 n/d n/d 462 780 88 15 70 384 After Current Activation PA-2 Outer Electrode as Cathode wet CO 225 -228 n/d n/d 645 776 57 30 50 230 PA-3 Outer Electrode as Cathode wet CO 243 -241 n/d n/d 454 755 48 25 40 105 PA-8 Outer Electrode as Anode wet CO 868 -39 70 50 25 809 73 10 15 15 PA-9 Outer Electrode.

as Anode wet CO 881 -31 50 40 23 814 79 10 20 14 PA-14 Outer Electrode as Anode dry CO 926 12 70 50 16 816 79 25 35 12 PA-15 Outer Electrode as Anode dry CO 905 -9 100 65 25 805 66 20 25 14 As illustrated in Table I, the current activation treatment of the present process, where the outer conductive catalyst electrode is subjected to a non-oxidizing atmosphere, and with the sensor elements subjected to a direct current charge with the outer electrode as an anode, results in exceptional and consistent properties of high voltage output in the rich gas condition, fast switching response and very low internal resistance. The properties are achieved whether or not water vapor is present in the non oxidizing gas in contact with the outer electrode.It should be noted, however, that such current treatment where the outer electrode is connected to the negative terminal of the power source, acting as a cathode, does not provide the exceptional properties achieved following the present claimed process.

EXAMPLE II Seven further electrolyte body thimbles of the series (PA-1 6, PA-1 7, PA-1 8, PA-1 9, PA-1 2, PA-1 3 and PA-20) had inner and outer catalytic electrodes applied thereto as such application was effected in Example I, and formed into sensors and tested as in Example I. The results of these tests are listed in Table II under the designation "No Treatment." These sensor elements were then current activated as in Example I, except that the gaseous atmosphere contacting the outer surface of the sensor elements was not carbon monoxide but rather that indicated in Table II for each sensor ("wet" gas contained about 0.01 mg/cm3 of water vapor). All of these seven sensor elements were subjected to the direct current with the outer electrode as an anode.The sensors were again tested as to voltage output, switching response and internal resistance. The results of these tests are listed in Table II under the designation "After Current Activation." TABLE II Sensor Treatment 350 Testing 800 Testing Voltage Switching Internal Voltage Switching Internal Output Response Resis- Output Response Resis Rich Lean RL LR tance Rich Lean RL LR tance (mv) (mv) (ms) (ms) (k#) (mv) (mv) (ms) (ms) (#) PA-16 No Treatment 239 -69 n/d n/d 713 782 83 10 50 405 PA-17 No Treatment 129 -206 n/d n/d 896 771 62 15 55 467 PA-18 No Treatment 156 -190 n/d n/d 755 788 79 15 50 292 PA-19 No Treatment 92 -244 n/d n/d 950 781 78 15 55 289 PA-12 No Treatment 225 -111 n/d n/d 483 768 52 15 45 198 PA-13 No Treatment 119 -192 n/d n/d 972 753 53 15 45 405 PA-20 No Treatment 82 -278 n/d n/d 655 792 72 20 50 414 After Current Activation Gaseous Atrnosphere PA-16 Wet N2 884 -33 70 50 25 819 81 10 15 16 PA-17 Wet N2 913 -12 60 40 17 813 81 15 15 12 PA-18 Dry N2 923 0 60 40 17 815 78 25 30 12 PA-19 Dry N2 925 0 80 60 17 816 76 20 20 11 PA-12 Wet Air 896 93# 1,900 50 29 867# 83 10 30 46 PA-13 Wet Air 902 132# 3,00 40 18 863# 79 10 30 48 PA-20 Dry air 871 146# 8,700 50 28 895# 84 30 45 66 As indicated by the test results listed in Table II, the present process is not effective if an oxidizing gas, such as air, is present in contact with the outer conductive catalyst electrode during the current application. As shown, while increase in voltage output is obtainable, as is reduction in internal resistance, where oxidizing gases are present, the switching response time is high and unacceptable.

The arrows shown in the table indicate that the values with which they are associated were not stable but continuing to decrease.

EXAMPLE Ill Six additional electrolyte body thimbles of the series (AE 26-5, AE 26-8, AE 26-3, AE 26-4, AE 26-6 and AE 26-7) had an inner electrode applied to the inner surfaces thereof by coating the inner surfaces with a platinum metal suspension without any glass frit present in the suspension. The thimbles and inner electrodes were then heated in an oxidizing atmosphere for a period of time, during which the organic constituents in the suspension were burned off and the platinum bonded to the zirconia surfaces. The external catalyst layer (platinum) was next applied to the outer surface of the thimbles by known thermal vapor deposition. A porous ceramic coating was applied over the external catalyst layer for protection.These thimbles were then formed into sensors and tested, as hereinbefore described, to determine the voltage output, switching response and internal resistance. The results of the tests are listed in Table Ill under the designation "No Treatment." These thimbles were then subjected to a current activation by inserting the thimbles, as sensors in a protective housing and with conductive leads, into a manifold, with the outer surfaces of the sensor elements thereof having the outer conductive catalyst coating thereon exposed, while preheated during a ten-minute period to a temperature of 7500C, to a flow of dry nitrogen (71 0 cm3/min.). The sensors were then subjected to a direct current, for a time period as indicated in Table Ill, with the outer electrodes as anodes, the direct current charge applied at a current density as indicated in Table lil. The direct current was then stopped and the sensor elements allowed a recovery period of ten minutes at said temperature and with the outer electrodes in said nitrogen flow.

These sensor elements were then tested again. The results of the tests are listed in Table Ill under the designation "After Current Activation." TABLE III Sensor Treatment 350 Testing 800 Testing Voltage Switching Internal Voltage Switching Internal Output Response Resis- Output Response Resis Rich Lean RL LR tance Rich Lean RL LR tance (mv) (mv) (ms) (ms) (k#) (mv) (mv) (ms) (ms) (#) Ae 26-5 No Treatment 848 252 8,500 120 89 806 73 40 50 43 AE 26-8 No Treatment 721 248 2,000 220 346 791 76 25 55 85 AE 26-3 No Treatment 623 65 590 560 274 793 91 25 30 72 AE 26-4 No Treatment 907 180 4,100 100 50 801 89 30 45 47 AE 26-6 No Treatment 472 86 n/d n/d 549 780 75 25 55 67 AE 26-7 No Treatment 600 81 650 700 391 772 67 25 55 59 After Current Activation Current Time of Density Applying Current (ma/cm2) (Min.) AE 26-5 4 10 813 200 5,000 110 47 805 89 20 50 45 AE 26-8 8 10 961 60 170 60 10 801 83 15 15 17 AE 26-3 20 10 868 33 60 40 33 810 84 25 15 11 AE 26-4 100 10 961 54 100 50 26 821 86 20 15 11 AE 26-6 100 0.5 939 39 90 50 34 818 85 25 25 11 AE 26-7 100 0.1 795 51 75 65 80 803 87 15 20 14 The test results of Table Ill illustrate the effect of the current density upon the present process, wherein current densities below about 5 ma/cmZ of the planar,surface of the outer conductive catalyst electrode do not give the desired results. Also, as illustrated, a time of application of the current as low as 0.1 minute (6 seconds) under the process conditions is effective, as shown by the improved properties of sensor element AE 26-7.

EXAMPLE IV Four additional electrolyte body thimbles of the series (AP-1 7, AP-1 8, PA-4 and PA-1 1) had inner and outer catalytic electrodes applied thereto as such application was effected in Example I, and were formed into sensors and tested as in Example I. The results of these tests are listed in Table IV under the designation "No Treatment." Two of the sensor elements, AP-1 7 and AP-1 8, were then subjected to a direct current, as in Example I, except that dry nitrogen was used in place of carbon monoxide, and the current application time was five minutes with the outer electrode as an anode, followed by five minutes with the outer electrode as a cathode (100 ma/cm2).

The other two sensor elements, PA-4 and PA-1 1, were subjected to the current activation steps of Example I, except that instead of using a direct current of the density indicated in Example I, the current applied was 60-cycle, 5 volt alternating current.

After these treatments, the sensors were again tested as to voltage output, switching response and internal resistance. The results of the tests are listed in Table IV under the designation "After Treatment." TABLE IV Sensor Treatment 350 Testing 800 Testing Voltage Switching Internal Voltage Switching Internal Output Response Resis- Output Response Resis Rich Lean RL LR tance Rich Lean RL LR tance (mv) (mv) (ms) (ms) (k#) (mv) (mv) (ms) (ms) (#) AP-17 No Treatment 266 -99 n/d n/d 641 796 84 20 30 60 AP-18 No Treatment 112 -198 n/d n/d 2,107 799 70 20 45 210 PA-4 No Treatment 243 -62 n/d n/d 418 749 69 10 25 62 PA-11 No Treatment 236 -108 n/d n/d 919 728 66 15 60 443 After Treatment Gaseous Atmosphere Current AP-17 Dry N2 . 881 -21 50 45 18 823 72 25 35 19 AP-18 Dry N2 . 884 -25 45 50 19 812 75 25 11 PA-4 Wet Co Alt. 728 12 570 230 108 806 81 20 20 34 current 5v PA-11 Wet CO Alt. 553 -103 n/d n/d 190 801 59 15 20 81 current 5v *5 min. outer electrode as anode & 5 min.

outer electrode as cathode It is evident from the test results of Table IV that the 60-cycle alternating current does not give the beneficial properties achieved by the direct current treatment of the present process, especially fast switching response. While some increase in voltage output and some lowering of internal resistance are effected, the results are not nearly as beneficial, note PA-4 and PA-1 1. In the process, however, an additional current treatment with the outer electrode as cathode, so long as a period of direct current activation with the outer electode as anode is effected, does not give results as poor as those obtained when a 60-cycle alternating current is used.

EXAMPLE V Three additional electrolyte body thimbles of the series (AP-1 1, AP-52 and AP-54) had inner and outer electrodes applied thereto following the procedure of Example I. The sensor elements were then tested for voltage output, switching response and internal resistance as in Example I; the results of these tests being listed in Table V under the designation "No Treatment." These thimbles were then subjected to a current activation step by inserting the thimbles, as sensors in a protective housing and with conductive leads, into a manifold with the outer surfaces of the sensor elements having the outer conductive catalyst coating thereon exposed to a flow of dry nitrogen gas (710 cm3/min.). The sensors were preheated to the temperature indicated in Table IV during a ten minute period and, at that temperature and with the flow of nitrogen gas continuing, a direct current was applied, with the outer electrodes as anodes for ten minutes at a current density of 100 ma/cm2. A ten-minute recovery period followed after the current ceased, with the outer electrodes at the temperature indicated and in contact with the nitrogen.

These sensor elements were then again tested. The test results are listed in Table V under the heading "After Current Activation." TABLE V Sensor Treatment 350 Testing 800 Testing Voltage Switching Internal Voltage Switching Internal Output Response Resis- Output Response Resis Rich Lean RL LR tance Rich Lean RL LR tance (mv) (mv) (ms) (ms) (k#) (mv) (mv) (ms) (ms) (#) AP-11 No Treatment 81 -206 n/d n/d 1,739 808 85 25 45 375 AP-52 No Treatment 327 13 n/d n/d 805 758 60 20 50 80 AP-54 No Treatment 128 -256 n/d n/d 1,751 741 72 20 70 328 After Current Activation Temp. C AP-11 750 910 -3 65 17 814 77 25 25 15 AP-52 600 790 -130 40 60 13 778 70 15 20 13 AP-54 450 284 -258 n/d n/d 391 730 47 20 110 369 As is shown by the test results, the use of temperatures of about 4500C and below do not give the desired improved properties, even where the other parameters of the present process are present, for sensor elements that have an inner catalytic coating containing a flux material. Where no flux material is present on the inner coating, temperatures in the range of 4500C are acceptable but, in any event, a temperature in excess of 4500C is required for proper processing.

EXAMPLE VI A further six solid electrolyte thimbles of the series (AP 45, AP-46, AP-47, AP-48, AP-49 and AP-1 2) had inner and outer electrodes applied as in Example I. The sensor elements were then tested and the results of these tests are listed in Table VI under the designation "No Treatment". The sensor elements were then subjected to a current activation step as in Example V, except that the elevated temperature was 7500C for each of the sensor elements while the time of current application and the time allowed for a recovery period were varied as indicated in Table VI. The sensor elements were then again tested, except that testing at 3500C was effected first, followed by testing at 8000C.

The results of the tests are listed in Table VI under the heading "After Current Treatment." TABLE VI Sensor Treatment 350 Testing 800 Testing Voltage Switching Internal Voltage Switching Output Response Resis- Output Response Resis Rich Lean RL LR tance Rich Lean RL LR tance (mv) (mv) (ms) (ms) (k#) (mv) (mv) (ms) (ms) (#) AP-45 No Treatment 66 -289 n/d n/d 711 745 53 15 75 185 AP-46 No Treatment 125 -189 n/d n/d 1,759 752 59 20 55 66 AP-47 No Treatment 214 -131 n/d n/d 793 754 57 25 60 75 AP-48 No Treatment 241 -159 n/d n/d 959 761 63 25 75 264 AP-49 No Treatment 69 -303 n/d n/d 1,942 745 59 25 55 96 AP-12 No Treatment 75 -221 n/d n/d 1,485 801 79 25 60 656 After Current Activation Time of Time of Current Recovery (Min.) (Min.) AP-45 0.1 0 752 -115 150 50 24 760 56 15 30 20 AP-46 0.1 10 701 -50 60 90 107 768 59 15 25 53 AP-47 1 0 -944 -1878 n/d n/d -- 785 81 15 15 22 AP-48 1 10 870 -45 200 600 20 791 62 20 40 30 AP-49 10 0 -1194 -2110 n/d n/d -- 767 60 15 25 12 AP-12 10 10 898 -8 120 80 8 810 75 15 20 18 As shown by the results in Table VI, where a short current application is used, less than one minute, the need for a recovery period may be obviated. Where a one minute or more application of the direct current is effected, however, a recovery period during which the sensor element is maintained at the elevated temperature and where the outer electrode is in contact with a nonoxidizing gas may be needed, the time of such recovery varying depending upon the other parameters of the current activation step. It should be noted that the internal resistance values of AP-47 and APW9 at 3500C are not includable since, due to the highly negative character of the output voltages, such values are not deemed representative.

There has been described a novel process for producing a solid electrolyte oxygen sensor element wherein the same is activated to give significantly improved properties.

Claims (9)

1. A process for producing a solid electrolyte oxygen gas sensor element so as to increase the voltage output under rich gas conditions, shorten the switching response time, and reduce the internal resistance thereof, the sensor element comprising a solid electrolyte body having an inner conductive catalyst electrode on the inner surface and an outer conductive catalyst electrode coating on the outer surface thereof, characterized in that it comprises two steps: a) heating the sensor element to an elevated temperature in excess of 4500 and subjecting the outer surface thereof, with said outer conductive catalyst coating, to a nonoxidizing atmosphere; and b) applying a direct current to the sensor element, with said outer electrode as an anode, while said outer surface is at said elevated temperature and subjected to said nonoxidizing atmosphere, the current density thereof being at least 5 milliamperes per square centimeter of the planar surface of said outer conductive catalyst electrode.

2. A process for producing a solid electrolyte oxygen gas sensor element according to claim 1, characterized in that said sensor element is heated to a temperature in the range of 600900 C.

3. A process for producing a solid electrolyte oxygen gas sensor element according to claim 1, characterized in that said nonoxidizing gas is a reducing gas.

4. A process for producing a solid electrolyte oxygen gas sensor element according to claim 1, characterized in that said nonoxidizing gas is a neutral gas.

5. A process for producing a solid electrolyte oxygen gas sensor element according to claim 4, characterized in that said neutral gas comprises nitrogen.

6. A process for producing a solid electrolyte oxygen gas sensor element according to claim 1, characterized in that said current density is in the range of 20-1 50 milliamperes per square centimeter of the planar surface of said outer conductive catalyst electrode.

7. A process for producing a solid electrolyte oxygen gas sensor element according to claim 1, characterized in that, following the application of the direct current, the sensor element is maintained at said elevated temperature for a period of time after cessation of said current.

8. A process for producing a solid electrolyte oxygen gas sensor element substantially as hereinbefore described.

9. A solid electrolyte oxygen gas sensor element when produced according to the process of any one of the preceding claims.