AMPEROMETRIC APPARATUS, CELL AND METHOD FOR DETERMINATION OF DIFFERENT GASEOUS SPECIES

Abstract: A method for determination of a first electroactive and norm­ ally gaseous species (EAGS) and a second EAGS in a fluid medi­ um containing both EAGS; the medium is contacted with a first working el­ ectrode (11) that is sensitive but to the first EAGS and gen­ erates a first amperometric signal that is indicative of the first EAGS concentration; the medium is also contacted with a second work­ ing electrode (21) that is sensitive to both EAGS and produces a second amperometric signal that is indicative of the sum of both EAGS concentrations; the second EAGS concentration is calculated from the difference between the first and the sec­ ond signal. For example, hydrogen can be measured in the pre­ sence of oxygen and this can be applied to monitor a fluid ambient or stream to prevent formation of explosive mixtures or corrosive conditions. The method can be carried out by means of an apparatus compris­ ing two separate membrane-enclosed amperometric cells (1,2) (1, 2) each having a generally convent­ ional structure, or by means of a novel integrated cell struct­ ure (4) comprising at least two sensing electrodes (41, 42) and at least one counter electrode (45).

Description: This invention relates to an amperometric method for quantitative determination of elemental hydrogen in a normally fluid medium that may be gaseous or liquid. The term "normally fluid" is used herein to indicate that the substance or phase is gaseous or liquid when at normal temperatures and pressures of typically 20°C and one bar. The term "elemental" is used to include the said elements in a molecular or atomic state. The normally fluid medium may be a mixture of gases, such as air, or a process gas containing both elemental oxygen and hydrogen, and may be at reduced, normal or elevated pressures and at temperatures within a typical range of from about -10°C to about 95°C; alternatively, the fluid medium may be a liquid, such as water that contains oxygen and hydrogen in a dissolved state. Reliable measuring or monitoring methods for determining the concentration of elemental hydrogen in the presence of oxygen are of importance wherever hydrogen is generated or used, e.g. in connection with electrolytical processes or when producing or reacting hydrogen in petrochemical or other operations because a gas mixture in which the fractions of oxygen and hydrogen exceed certain threshold limits of typically about 4 % by volume may become explosive and may be dangerously unstable. Another problem that can be at least as critical as preventing formation of explosive gas mixtures is corrosiveness of water that is subjected to water-decomposing (i.e. oxygenolytic and hydrogenolytic) conditions such as, typically, exposure to radiolytic, e.g. neutronic radiation. For example, the water used in water-moderated nuclear reactors is subject to radiolytic generation of oxygen and hydrogen but since the latter is relatively more "volatile" in such systems the oxygen concentration tends to increase and this, in turn, can be a cause for the water becoming corrosive to metallic components in contact therewith. One of the most effective methods to prevent such corrosiveness is the addition of elemental hydrogen in well-controlled quantities so that the hydrogen will act as a scavenger for the elemental oxygen. Of course, amperometric methods for determining hydrogen and oxygen individually, i.e. not in the same fluid medium or only after chemically or otherwise separating one from the other, are conventional, and membrane-enclosed amperometric cells (also termed "MEACs" for short) have been used for detection of either oxygen and hydrogen, notably since a simple and reliable hydrogen sensing method and apparatus has been disclosed by Applicant (cf. EP-A-124 818). EP - A - 0 122 511 discloses an amperometric method for measuring the concentrations of dissolved oxygen and dissolved hydrogen in core water of nuclear reactors by means of a membrane-enclosed cell. This method is carried out by means of a single sensing (or "working") electrode operated at different potentials so as to be selective for the species of interest, i.e. oxygen and hydrogen. As specified in this document (page 5, lines 19-25) a membrane is needed that has a larger enough thickness to overlap potential regions producing both limiting current plateaus of hydrogen oxidation and oxygen reduction. A range of membrane thickness of from 70 to 350 µm is said to be generally useful and a teflon membrane of 150 µm thickness is cited as an example. EP - A - 0 027 005 discloses an amperometric method for determining the concentrations of oxygen, halothane and nitrous oxide in a stream of an anaesthetic gas as typically used in hospitals for purposes of surgery. According to this method, a first current is measured at a first potential on a sensing electrode made of platinum or gold to determine oxygen reduction only; a second current is measured to determine reduction of both oxygen and halothane and a cathode made of silver is used for this purpose; further, a third current indicating reduction of oxygen plus halothane plus nitrous oxide is measured at a second potential and, again, the electrode is the one made of silver. There is no indication in this document that the method could be used for analysis of other gases, nor that the electrode used for sensing of the mixtures of oxygen with halothane, on the one hand, and oxygen/halothane/nitrous oxide, on the other hand, could be made of a non-consumable metal. Now, it is an object of the present invention to provide an amperometric method of the type defined in the opening paragraph without the limitations of the prior art amperometric methods suitable for determining the concentrations of gases in mixtures. These objects are achieved according to the present invention by a method as defined in claim 1. Preferred method embodiments are as defined in claims 2 to 5 while an apparatus for carrying out the inventive method is as defined in claims 6 to 8. The invention is of particular advantage for use in monitoring potentially hazardous mixtures that will become highly corrosive or highly explosive if hydrogen is either below or above a critical limit. The invention will now be explained in more detail with reference to the enclosed drawings in which: Fig. 1 is a diagrammatic illustration of an apparatus for carrying out the novel method; Fig. 2 is a diagrammatic illustration of a novel cell for use in the inventive method; and Fig. 3 is a diagram of a hydrogen/oxygen determination run according to a preferred example set forth in detail below and showing the hydrogen concentration in percent by volume on the ordinate and the oxygen concentration, again in percent by volume, on the abscissa for a series of testing fluids. The diagram of Fig. 1 shows a first MEAC 1 of a generally conventional structure as disclosed, for example, in US - A - 4 096 047 having a sensing face 10 exposed to a fluid medium provided within enclosure 3, a working electrode (e.g. cathode) 11 being made of Au or having its active surface 110 made of this metal. A counter electrode (e.g. anode) 15, e.g. of the conventional Ag/Ag-Cl-type is arranged within the electrolyte space 112 containing a conventional electrolyte (not shown) while a constant DC-voltage is maintained between the counter electrode and the working electrode in a manner known per se. Additional electrodes, e.g. guard electrodes for the sensing or working electrode may be used but are not shown. The sensing face 10 of MEAC 1 is provided by the surface of a conventional semi-permeable membrane, i.e. one that is substantially impermeable to the electrolyte but is permeable to hydrogen and oxygen, but a masked sensor as disclosed in EP - A - 205 399 is suitable as well and may be preferred if no guard electrode is to be used. The second MEAC 2 has a structure similar to that of MEAC 1 except that the working electrode 21, or its active surface 210, is made of platinum, a platinum metal or an alloy of platinum group metals (platinum being considered to belong to the platinum group). The sensing face 20 of MEAC 2 again is a semi-permeable membrane of the type known (e.g. as disclosed in EP - A - 124 818) and the sensing face 20 is exposed to the medium within enclosure 3. As shown, enclosure 3 may be provided with an inlet 31 and an outlet 32 both of which could also be the "ends" of a tubular enclosure 3 if the latter is a conduit or the like fluid-passing means. In other words, no particular diameters are critical for enclosure 3 and/or its feeding ends. Leads 28 are provided between working electrode 21 and counter electrode 25 to carry the amperometric signal generated at the working electrode 21 by reaction of both oxygen and hydrogen to control instrument 8. The resulting signals may then be evaluated by an operator or fed, via conduits 79 and 89, to an evaluating device that converts the signals from instruments 7, 8 into a readout, monitoring signal, printer or the like output indicated schematically as output 91. A result obtained by a human operator from the readings of instruments 7 and 8 would also be considered as an "output 91". As diagrammatically shown in Fig. 2, the two MEACs 1, 2 of Fig. 1 can be integrated to form a new cell structure 4 comprising a first selective (e.g. for oxygen in the presence of hydrogen) working electrode 41 being made, or having an EAGS-exposed surface 411 made of Au and a second non-selective working electrode 42 being made, or having an EAGS-exposed surface 421 made of Pt, another metal of the platinum group, or an alloy thereof. At least one counter electrode 45 made, for example, of Ag/AgCl or another typical counter electrode material disclosed in the above mentioned US - A - 4 096 047, is provided within jacket 46 that encompasses an electrolyte space 44 covered by semi-permeable membrane 40 that permits passage of both gases contained in medium 43 but substantially prevents passage of the aqueous electrolyte that is contained in space 44. A single counter electrode 45 may be used in which case it will serve as the counter electrode for, and cooperate with both, sensing electrodes 41, 42 to produce first and second amperometric signals 491, 492 as outputs from control instruments 47, 48 of a generally conventional type for use with MEACs. Instrument 47 is connected with the first sensing electrode 41 and the counter electrode 45 via leads 451, 471, and the amperometric signal 471 produced by the first sensing electrode 41 with counter electrode 45 will be indicative but of the concentration of the oxygen contained in the fluid medium 43 which, in turn, is optionally included by a container, conduit or the like containment means 431. The amperometric signal 492 produced by the second sensing electrode 42 together with counter electrode 45 is indicative of the sum of the concentrations of both oxygen and hydrogen in medium 43. Since only one counter electrode 45 is used in the MEAC structure 4 of Fig. 2, each instrument 47, 48 will have an input lead 451, 452 connected with the one and only counter electrode 45 and an input lead 471, 472 from the first and the second sensing electrode, respectively. However, it is within the scope of the invention that each sensing electrode of an integrated cell as exemplified by Fig. 2 has a separate counter electrode (not shown). Further, both in the separate cells 1, 2 of Fig. 1 as well as in the integrated cell 4 of Fig. 2, each sensing electrode and counter electrode could consist of several segments or portions, and guard electrodes or physical guards could be used in a manner known per se for all sensing electrodes. Again, in Fig. 2, the outputs 491, 492 from instruments 47, 48 can be evaluated by a human operator or by an instrument 49 to produce, in either case, an output or signal 499 that is indicative of the difference of the amperometric signals produced by the two sensing electrodes and may, but need not, indicate the concentration of hydrogen or a derived parameter, such as a threshold value for indicating that explosive or corrosive conditions as explained above are approached and/or for triggering control or alarm signals to prevent that such conditions prevail. Example 1 When the selective working electrode surface 110 (or 411) is made of gold while the working electrode surface 210 (or 421) is made of platinum, electrode/gas reactions are as follows: When using an alkaline electrolyte, oxygen reacts at the selective electrode 11 or 41 or its surface 110 or 411 as follows: O2 + 2H2 O + 4e → 4 OH⁻ (1) At the non-selective platinum electrode 21 or 42 or its surface 210 or 421 the above reaction occurs as well but hydrogen reacts as H2 → 2H⁺ + 2e (2) Accordingly, the non-selective platinum electrode or surface reacts simultaneously as a cathode in the oxygen reaction and as an anode in the hydrogen reaction. Since the electron flow through the platinum/electrolyte-interface is in opposite directions in the two reactions, the partial currents associated with the two reactions will cancel each other so that there will be a difference between the magnitudes of the electric currents measured with the two sensing electrodes. By combining these two currents the partial pressure of O₂ and H₂ in the sample stream can be calculated as explained in detail below. For simplicity, the sensors or sensing electrodes are assumed to operate in the manner of conventional MEACs or their respective working or sensing electrodes, that is to say, the magnitude of the current measured is limited by the rate of diffusion of the electroactive gases from the sample through the membrane to the electrode surface. In the case of electrode 21 or 42 this means that both reactions specified above must proceed very rapidly at the electrode surface 210 or 421, respectively. The conventional relation between current and partial pressure of the electroactive gases in a MEAC may be written as follows: If the current is measured in microamperes and the partial pressure in kilopascals, the sensitivities will have units of microamperes per kilopascal. The symbol "i" is used for current, "S" for sensitivity and "p" for partial pressure; then, the relation may be written as follows: i = S · p (4) Generally, S will be dependent upon the temperature and the membrane. This relation is applied to the elective gold electrode surface with the following result: i g = S g,O2 · P O2 (5) As used herein, the symbols x H2 and x O2 represent the fractions of hydrogen and oxygen in the gas stream to be measured; y H2 represents the fraction of H₂ in a first calibration gas, and y O2 the fraction of O₂ in a second calibration gas and the "check-sum" as used below in equation (17) will be 100 %. At the non-selective platinum electrode both of the cathodic and anodic reactions may be described in this way, so that the net current becomes: x O2 = 100·P O2 /B = S p,O2 · P O2 - S p,H2 · P H2 (6) wherein B is the barometric pressure. In order to use these relations for determination of the partial pressures of oxygen and hydrogen, the sensitivities S g,O2' S p,O2 and S p,H2 must be determined. This is done by the following calibration procedure: First, both MEACs 1 and 2 are, or MEAC 4 is, exposed to the gas stream containing a known fraction y O2 of oxygen, but no hydrogen. Assuming that the stream passes the sensors at atmospheric pressure B, then the partial pressure p O2 in this calibration medium by Dalton's law is: P O2,1 = y O2 · B (7) It follows from equation (5) that S g,O2 = i g,1 / p O2,1 = i g,1 / (y O2 · B) (8) Furthermore, since p H2 = 0 in this calibration medium, it follows from equation (6) that S p,O2 = i p,1 /p O2,1 = i p,1 /(y O2 · B) (9) Subsequently, MEACs 1 + 2 or 4 are exposed to a mixed gas stream containing known fractions of O₂ and H₂ in order to determine S p,H2 . This stream is conveniently prepared by bleeding into the O₂-containing stream used for O₂ calibrating a second stream containing a known fraction of H₂, y H2 but no oxygen. Indicating by i g,2 and i p,2 the currents measured at MEACs 1 + 2 or 4 in this mixed stream: since S g,O2 is known, the O₂ partial pressure in the stream can be calculated from equation (5) p O2,2 = i g,2 / S g,O2 (10) Hence, the contribution to the total pressure represented by the original O₂ containing stream will be p O2,2 / Y O2 = i g,2 / (y O2 · S g,O2 ) (11) and that of the hydrogen containing stream will be: B - i g,2 / (y O2 · S g,O2 ) (12). From this, the hydrogen partial pressure of the mixed stream results as: p H2 = y H2 · {B - i g,2 / (y O2 · S g,O2 )} (13). Returning to equation (6), the unknown term S p,H2 can now be calculated as follows: S p,H2 = {S p,O2 ·i g,2 / S g,O2 - i p,2 } {y H2 ·[B - i g,2 /y O2 ·S g,O2 ]} (14). This completes the calibration procedure. Example 2 The MEACs 1 and 2 were standard probes manufactured by Orbisphere Laboratories Geneva, i.e. Model 21152 having a gold cathode, and Model 2230 having a platinum electrode. The electrolyte used in both sensors contained 1 mol/lit potassium chloride and 1 mol/lit potassium hydroxide. A membrane TEFZEL (registered trademark DuPont) having a thickness of 25,4 micrometers was used on the platinum sensor (MEAC 2) and TEFZEL of 12,7 micrometers on MEAC 1. The voltage applied to both sensors was -0.6 volts (platinum or gold negative) versus the silver/silver chloride reference electrodes 15, 25. Oxygen calibration was performed in pure O₂ (y O2 = 1). It was found that S g,O2 = 0.625 µA/kPa and S p,O2 = 0.291 µA/kPa (8-1) The mixed O₂ and H₂ containing stream was prepared by bleeding pure H₂ (y H2 = 1) into the oxygen. Very low flow rates of only several ml/min were used. Then it turned out that: S p,H2 = 0.494 µA/kPa (14-1). Once calibration had been completed, the fractions of O₂ and H₂ in the mixed stream were varied and the percentages of the constituent gases were calculated by application of equation (5) as: and x H2 = (100 / S p,H2 · B) {S p,O2 · i g / S g,O2 - i p } (16). The correctness of the measurement was checked in two ways. First, since the mixture is made from two component streams there should be a constant checksum: Checksum = (x O2 / y O2 ) + (x H2 / y H2 ) = 100 % (17). This was verified for all mixtures and the result is illustrated in Fig. 3. The rule is obeyed within 1 % for all mixtures (0-35 % H₂, 100-65 % O₂) tested. Secondly, combining equations (15), (16) and (17), it results that: B·y H2 · S p,H2 +i p = (i g /S g,O2 )· {(y H2 ·S p,H2 / y O2 ) + S p,O2 } (18) In the series of mixtures studied B,y O2 , y H2 , S p,O2 , S g,H2 and S p,O2 were all constant. Hence, the equation (18) is that of a straight line i p = a + b · i g . (19) The correctness of this relation was also tested and found to be valid. Example 3 In equations (5) and (6) different expressions were written for the currents measured at the gold and platinum electrodes 11, 12, respectively, even though assumed to be exposed to the same medium containing both oxygen and hydrogen. This comes about because the non-selective platinum electrode of MEAC 2 or 4 permits virtually instantaneous reaction of both hydrogen and oxygen at its surface 210/421, while the selective gold electrode 11 or 41 permits reaction but of oxygen. Thus, one can write an equation similar to (6) instead of (5) for the current at the gold cathode sensor but employing a sensitivity term S g,H2 which is practically zero. In order to quantify the difference between the gold and platinum electrodes 11 or 41 and 21 or 42, a suitable equation was found as follows: i = n F A p,H2 / [(1/k e S e ) + (z m /D m S m )] (20) and this supports the viability of the physicochemical basis of the inventive method. The symbols used in equation (20) are defined as follows: n = 2 = number of electrons participating in the oxidation electrochemical reaction of the second EAGs, e.g. hydrogen; F = 96,500 Coulombs per mole, the Faraday constant; A = the area of the working electrode; P H2 = the partial pressure of hydrogen in the medium; k e (cm/sec) = the rate constant of the hydrogen oxidation reaction; S e = the solubility of hydrogen dissolved in the electrolyte at the electrode surface; z m = the thickness of the membrane; D m = the diffusion coefficient of hydrogen in the membrane; and S m = the solubility of hydrogen in the membrane. The given equation is best understood in terms of an electrical analog: by Ohm's law, the observed current "i" equals the voltage applied divided by the resistance to current flow encountered. The numerator of the equation is then analogous to the voltage, and the denominator analogous to the resistance. The numerator of equation (20), i.e. the resistance term R = (l/k e S e ) + (Z m D m S m ) (21) is of main interest. Its first term on the right hand side can be designated as the "resistance of the electrode reaction" and the second term can be designated as the "resistance of the membrane". It should be noted that this "resistance" is not the "electrical" resistance but rather the resistance to transport of hydrogen. Hence, the difference between the selective and non-selective sensing electrodes used in the invention may be expressed as follows: The "resistance" of the hydrogen oxidation reaction on electrode 21 or 42, e.g. having a platinum surface 210, is negligible in comparison with the "resistance" of the membrane 20 or 40, e.g. amounts to one percent of the latter "resistance" or less. In contrast, the "resistance" of the electrode reaction on electrode 11 or 41, e.g. having a gold surface 110 or 411, exceeds by far the "resistance of the membrane 10 or 40, e.g. is a hundred times or more greater than the latter "resistance". In practice, the magnitude of the membrane "resistance" can be determined, according to the present invention, because the term (l/k e S e ) is negligible for the non-selective electrode 21 or 42 (see equation 20) and the current delivered may be written as: FA D m S m P H2 / z m (22) Equations (13) and (14) provide for determination of the term S p,H2 which, by comparison, is: S p,H2 = F A D m S m / z m (23) Since the area A of the sensing electrode is known or can easily be determined, it is possible to calculate directly the membrane resistance term (z m /D m S m ) and for Example 2 S p,H2 was determined as 0.494 µA/kPa since "A" of MEAC 2 was 0.3142 cm². Hence, the resistance term is as follows: (z m /D m S m ) = 1.272 · 10 cm²·kPa·S / mol. With regard to MEAC 1 exposed to the same partial pressure of the H₂, tables can be used to determine the solubility thereof in its electrolyte; for hydrogen in pure water the solubility is approximately 7.5 · 10⁻⁹ mol/(cm³ · kPa) at 25°C. The presence of salt in the electrolyte normally lowers the solubility in comparison with pure water but the effect is not large with normally used electrolyte compositions. Hence, the threshold magnitude of the electrode reaction rate constant can be calculated according to the invention as follows: k c / e = D m S m / z m Se = S p,H2 / n FAS e (24) and this permits classification of electrode metals into those suitable for non-selective electrodes of the non-selective electrode, i.e. sensitive to both oxygen and hydrogen. In the one class k e » k c / e (24-1) while in the other class k e « k c / e (24-2). Reaction rate constants k e are not always tabulated while the "exchange current density" for the electrode reaction is given more frequently. The exchange current density i o is defined as the partial current for oxidation of hydrogen at the equilibrium potential (where the net current is zero), when the activity of hydrogen is unity (p H2 = 100 kPa). Thus: i o = 2 F k o / e S e (p H2 = 100 kPa) (25) Where k o / e would be the value of the rate constant introduced earlier at the equilibrium potential. The rate constant varies with electrode potential in an exponential manner: k e = k e exp (-η / b) (26) wherein η = V-V o is the "overpotential" of the electrode, V is the electrode potential and V o is the equilibrium potential b called the Tafel constant (J. Tafel, Z. Physik. Chem. 50, 641, 1905) which determines the steepness of the variation of rate constant with electrode potential. Combining equations (24) and (28) the criterion for classification of electrode metals in terms of the exchange current can be expressed as: i o exp (η / b) = S p,H2 / A (27). From the experimentally determined magnitude of S p,H2 /A and the chosen value of the overpotential η applied to the sensor, a critical or threshold value of the exchange current density can be evaluated for various possible values of the Tafel constant b. Tables can then be consulted to determine which metals (having i o »i c / o) would be suitable for sensing both oxygen and hydrogen. A recent tabulation can be found in Chapter IX 2-3, "Hydrogen", by A. J. Appleby, H. Kita, M. Chemla and G. Bronoël, in "Encyclopedia of Electrochemistry of the Elements", edited by A. J. Bard, Volume IXA, Marcel Dekker, New York 1983, incorporated herein by reference. Preferred electrodes for the selective sensing electrode 11 or 41 should have a sufficiently high exchange current for reduction of oxygen, such that the rate of this process will be limited by the diffusion rate of oxygen through the membrane. Various modifications of the above described specifics, e.g. regarding currents, electrolytes and suitable MEAC materials are apparent to one skilled in the amperometric art. For example, wherever "hydrogen" or "oxygen" are mentioned herein, any isotopes thereof (deuterium, tritium etc.) are encompassed because the electrochemical behaviour depends upon the election shells of the elements in question. Further, "H2" and "O2" stand for "H₂" and "O₂" to simplify printing.

Claims: An amperometric method for quantitative determination of elemental oxygen and of elemental hydrogen in a normally fluid medium containing said elemental oxygen in a first concentration and said elemental hydrogen in a second concentration; said medium being in a gaseous or liquid state; said method consisting of: contacting said medium with a first and selective working electrode (11; 41) that is sensitive only to elemental oxygen to obtain a first amperometric signal that is indicative of said first concentration; contacting said medium with a second and non-selective working electrode (21; 42) that is sensitive both to elemental oxygen and elemental hydrogen to obtain a second amperometric signal that is indicative of a sum of said first concentration and said second concentration; and determining said second concentration of elemental hydrogen from a difference between said first amperometric signal and said second amperometric signal; wherein said first working electrode (11; 41) has a sensing surface (110; 411) made of gold and is operated with a counter electrode (15; 45) at a potential at which said sensing surface (110; 411) of said first working electrode (11; 41) is sensitive only to elemental oxygen; and wherein said second working electrode (21; 42) has a sensing surface (210; 421) made of a metal selected from platinum, platinum group metals and alloys thereof and is operated with a counter electrode (25; 45) at a potential at which said sensing surface (210; 421) of said second working electrode (21; 42) is sensitive to both elemental oxygen and elemental hydrogen. The method of claim 1 wherein said medium is gaseous and wherein said second concentration is monitored to indicate a threshold value of said second concentration for detecting formation of an explosive mixture of hydrogen and oxygen. The method of claim 1 wherein said medium is an aqueous fluid exposed to radiolytic radiation; and wherein said second concentration is monitored to indicate a threshold value of said first concentration for detecting formation of a corrosive state of said aqueous fluid. The method of claim 2 comprising additionally generating a warning signal if said hydrogen concentration exceeds a predetermined level. The method of claim 3 comprising additionally generating a signal when said hydrogen concentration is below a predetermined level required to scavenge said oxygen from said aqueous medium. An amperometric apparatus for carrying out the method of any of claims 1 to 5 comprising: means (3; 43) for contacting the fluid medium with a first and selective working electrode (11; 41) having a sensing surface (110; 411) made of gold and being operated with a counter electrode (15; 45) at a potential at which said sensing surface (110; 411) of said first working electrode (11; 41) is sensitive only to said oxygen to obtain a first amperometric signal that is indicative of said oxygen concentration; means (3; 43) for contacting said medium with a second and non-selective working electrode (21; 42) having a sensing surface (210; 421) made of a metal selected from platinum, platinum group metals and alloys thereof and being operated with a counter electrode (25; 45) at a potential at which said sensing surface (210; 421) of said second electrode (21; 42) is sensitive both to said oxygen as well as to said hydrogen to obtain a second amperometric signal that is indicative of a sum of said oxygen concentration and said hydrogen concentration; and means (7, 8, 9; 47, 48, 49) for determining said hydrogen concentration from a difference between said first amperometric signal and said second amperometric signal. The apparatus of claim 6 further comprising means for additionally generating a warning signal if said hydrogen concentration exceeds a predetermined level. The apparatus of claim 6 further comprising means for additionally generating a signal when said hydrogen concentration is below a level required to scavenge oxygen from said aqueous medium.

Inventors: HALE, JOHN MARTIN, DR.
Applicants: ORBISPHERE LABORATORIES (INC.), WILMINGTON, SUCCURSALE DE COLLONGE-BELLERIVE
Application year: 1987
Main classification: G01N27
IPC codes: G01N27