Method and Apparatus for Continuously Monitoring an Aqueous Flow to Detect and Quantify Ions

The present invention relates to the field of fluid contamination monitors and, in particular, to methods and apparatus for detecting specific contaminants in potable and non-potable water flows.

The Safe Drinking Water Act (SDWA) mandates that municipal water utilities monitor their water. Under the SDWA, the number of monitoring sites in the outgoing distribution system depends upon the number of customers served by the utility. For example, in large utilities serving more than 100,000 customers, the utilities must provide monitoring at 100 sites in the distribution system.

In the drinking water filtration industry, common contaminants of concern are trihalomethanes, biological contamination, nitrate and heavy metals, such as lead. Each are removed by different means within the filtration system. Trihalomethanes are effectively removed with charcoal. Biological contamination such as cysts are removed with fine mesh mechanical filtration. Nitrate and lead are removed by either of two methods, reverse osmosis (RO) or ion exchange resins.

RO systems are effective for removing nitrates and heavy metals. Most quality systems offer a monitor that indicates that there is a rupture in the RO membrane and thus the system requires membrane replacement. Such monitors generally measure the conductivity of the input water and the output water. When the membrane is intact, the conductivity of the input water will differ from that of the output water to the extent that the system is removing inorganic contaminants from the water. When the membrane ruptures, allowing the input water to flow through the membrane, the difference between the conductivity of the input water and the output water will lessen beyond a pre-set threshold and trigger a signal to the user. A disadvantage to RO systems is that they require about five gallons of water to back-flush the membrane for every filtered gallon available for use. For a typical system delivering five gallons of water per day, an RO system will use up to 25 gallons of water per day to back-flush. Thus, while effective for removing inorganic contaminants, RO systems are very wasteful of water.

Ion exchange resins come from the manufacturer in the form of beads, having ion exchange sites on the beads. A plurality of such beads are typically agglomerated together to form a resin bed. Cation resins commonly have sodium on the exchange sites and anion resins commonly have chloride ions on the exchange sites. In ion exchange resins, heavier ions displace lighter ions. The following table sets forth a list of cations together with their selectivity coefficients. Selectivity coefficients are indicators of the preference of the resin for each of the ions relative to hydrogen.

As can be seen from the chart, cations such as iron (Fe), zinc (Zn) and calcium (Ca) have lower preference ratings than mercury (Hg) and lead (Pb). For example, in a cation resin bed having Ca on the exchange sites, if Hg were introduced into the bed, the Hg ions would displace the Ca ions, since Hg is more highly preferred by the ion exchange resin than Ca. If Pb were subsequently introduced, the Pb would displace lighter ions on the resin, and so on.

There are some batch on-line analyzers available on the market that can detect and quantify the presence of contaminants. However, each of these systems is extremely expensive. One system, ChemScan Process Analyzers, available from Applied Spectrometry Associates, Inc. of Waukesha, Wis., uses ultraviolet-visible spectrometry to detect contaminants. This analyzer costs in the $20,000-$40,000 range depending on the contaminants being detected. Ionics, Inc. of Watertown, Mass. offers the OVA 3000 series Trace Chemical Analyzers using the Wet Chemical method for lighter metals and Anodic Stripping Voltammnetry for heavier metals. Those systems cost about $40,000. For a large system, having 100 sites, the capital cost of installing such systems would be $4,000,000, which, for a utility serving 100,000 customers, would effect a $40 per customer one time charge for water monitoring. Thus, there is a need for a continuous, on-line system that is economical.

Though water is monitored when it leaves the municipal water plant, some contaminants may get into the water before the water is dispensed from the household tap. One contaminant of special note, lead, is highly toxic. It is present in lead solder in household plumbing, sometimes in the plumbing itself and sometimes in the water's delivery system. Water filtration systems that rely on cation exchange resin technology to remove lead or other toxic heavy metals can work effectively until the ion exchange system is no longer able to capture all of the heavy metals. This point is called the break-through stage. Therefore, it is necessary to detect when the break-through stage is reached. However, the monitor used to detect rupture in an RO membrane will not work in this application as exchange resins saturate gradually with no clearly detectable event such as occurs when an RO membrane ruptures. Thus, there is a need for a monitor to detect the presence of a specific ion, which is a threshold ion in a water filtration system.

Referring to the table, the logical stage to detect cation breakthrough in water from municipal water systems is at the copper level, having the effect of maximizing the longevity of the filtration cartridge and minimizing the health risks. However, an earlier stage threshold ion of cation breakthrough, such as zinc, is preferred for well water users to protect from such harmful ions as cadmium, which would be removed by municipal systems but may be present in wells.

Until recent years, standard anion exchange resins were used to remove nitrate from water. However, sulfates, which are common in nature, had higher selectivity coefficients than nitrate. The result was nitrate sloughing or dumping. That is, if an anion resin column was saturated with nitrate and sulfate was introduced into the column, the sulfates would displace the nitrates, thus, dumping the previously accumulated nitrates into the output water of a filter. Since nitrate has no taste, color or smell, the user was unaware of this event. To correct the problem, ion exchange resin manufacturers developed nitrate selective anion exchange resins which reversed the selectivity coefficients of nitrate and sulfates and thus the problem was solved. However, a disadvantage to using nitrate selective anion resins is that they are about 33% less efficient, i.e., the nitrate selective resins last about a third less long than a conventional anion exchange resin column. Thus, a monitor using nitrate as a threshold ion would allow the use of the more efficient conventional anion resin, maximize its longevity, and provide an alert to the user that the filter cartridge needed replacement.

In addition to the SDWA, the Clean Water Act (CWA) requires that wastewater treatment plants monitor the influent to their plants for specified contaminants. The CWA also specifies that industrial companies monitor their effluent that feeds into the wastewater stream. Such companies are referred to as Significant Industrial Users or SIU's. These SIU's will typically enter into pre-treatment agreements with their wastewater treatment plants covering the frequency of their monitoring requirement and the contaminants to be monitored.

The following table shows the Maximum Contaminant Levels (MCL's) in parts per million (ppm) of selected inorganic contaminants as mandated by the Environmental Protection Agency (EPA) under the Clean Water Act:

The frequency of monitoring of wastewater by both the wastewater treatment plants and the SIU's can be annually or more frequently. The common practice for monitoring is to collect water samples in the wastewater stream and submit those samples to testing laboratories for analysis. While the current practice is sufficient to comply with the mandates of the Clean Water Act, there is a possibility that a surge or spike of a contaminant can get into the wastewater treatment plant sludge undetected. Such an event may result in a costly cleanup process and possible fines from the EPA. Thus, there is a need for an in-line, continuous monitor that will detect and quantify contamination spikes in a water flow.

As shown in the Table above, zinc, having an MCL of 5 parts per million is different from mercury, having an MCL of 2 parts per billion. A concentration of 100 parts per billion of mercury would be a spike requiring immediate action. However, a similar reading of 100 parts per billion of zinc would be well within limits and require no action. Therefore, a monitor for heavy metals needs to be sensitive enough to measure vastly differing concentration levels for different contaminants.

As noted above, the USEPA mandates specific MCL's for specific chemicals. However, individual states also have the authority to set their own standards, so long as their standard is at least as stringent as the Federal standard. Thus, monitoring systems must be adjustable to allow the monitoring to be sensitive to differing MCL's in different states.

There is not known in the art a continuous, in-line, contamination monitor for heavy metals that will detect contamination spikes in a water flow, is sensitive enough to measure vastly differing concentration levels for different contaminants, is adjustable to allow the monitoring to be sensitive to differing MCL's in different states, is economical, is not wastefull of water, is capable of detecting when a break-through of a heavy metal filter has occurred, and is capable of providing a user with an alarm to designate when such a filter needs to be replaced.

The present invention is a method and apparatus for detecting contaminants in an aqueous flow. In its most basic form, the method of the present invention involves providing a conduit having at least one ion collection portion, disposing the aqueous flow through the conduit, attracting target ions to the ion collection portion such that they are bonded to the ion collection portion, and detecting a contaminant, or contaminants, based upon a predetermined property of the plurality of target ions bonded to the ion collection portion. In the preferred embodiment of the method of the present invention, the predetermined property is a conductivity of the target ions, and the detecting step involves measuring an initial conductivity of the ion collection portion before the plurality of target ions are bonded to the ion collection portion and measuring the subsequent conductivity's of the ion collection portion while the target ions are bonded to the ion collection point, calculating a change in conductivity by comparing each of the subsequent conductivity's to the initial conductivity, and determining whether the change in conductivity differs from a predetermined change in conductivity. In some embodiments, the change in conductivity is measured by measuring the change in voltage of a constant current flow.

Another group of embodiments of the method of the present invention involve the additional step of disposing an ion exchange portion within the conduit by disposing a predetermined ion exchange resin within the conduit and doping the plurality of target ions onto the ion exchange resin. This resin performs the additional steps of attracting ions of contaminants having higher selectivity coefficients relative to the ion exchange resin than the selectivity coefficient of the target ions, and exchanging the ions of the contaminants for the target ions doped to the ion exchange resin such that the ions of the contaminants are bonded to the ion exchange resin and such that the target ions are disposed within the aqueous flow. Still other embodiments involve the steps of calculating values of predetermined properties and providing a display or alarm based upon the calculated values.

In its most basic form, the apparatus of the present invention includes a conduit into which an ion collection portion is disposed, a sensor that senses ions collected on the ion collection portion and sends a signal corresponding to a value of a predetermined property of the ions, and a microprocessor in communication with the sensor and programmed to process the signal and determine the presence of the at least one contaminant based upon the processed signal.

In the preferred embodiment of the apparatus, the predetermined property is the conductivity of the target ions and the sensor includes a sensor substrate comprising an insulator layer, conductive pads, and an ion collection layer that is selective for the target ion, a constant current power supply attached to the conductive pads, and a voltmeter for measuring a voltage from the constant current power supply and for providing a signal, corresponding to the voltage, to the microprocessor. In this embodiment, the target ions bond to the ion collection layer forming a conductive bridge between the conductive pads, the conductive bridge changes the voltage of the current flow through the conductive pads, the voltmeter detects this change in voltage and sends the corresponding signal to the microprocessor, and the microprocessor processes the signal and detects the presence of contaminants based upon the change in conductivity.

In some embodiments, the ion collection layer is a polymer, polyvinyl pyridine for example, which is selective for the target ions, copper for example. In other embodiments the sensor is adapted to sense specific ions such as iron, zinc, cadmium, calcium, strontium, copper, mercury, lead, nitrate, and sulfate ions. In one group of embodiments, the apparatus also includes an ion exchange portion, comprising an ion exchange resin doped with the target ions, disposed within the conduit at a position upstream of the ion collection portion. In still another group of embodiments, multiple sensors are employed to measure multiple contaminants.

Therefore, it is an aspect of the present invention to provide a water monitoring system that is on-line and continuous.

It is a further aspect of the invention to provide a monitor that is selective for individual contaminants.

Another aspect of the invention is to provide a monitor to detect the presence of threshold ions in water filtration systems.

Another aspect of the present invention is to provide a monitoring system that can detect and report different concentration levels for different contaminants.

Another aspect of the invention is to provide a monitoring system that is economic to the user.

These aspects of the invention are not meant to be exclusive and other features, aspects, and advantages of the present invention will be readily apparent to those of ordinary skill in the art when read in conjunction with the following description, appended claims and accompanying drawings.

FIG. 1 is an isometric view of a home water filtration system employing one embodiment of the monitor of the present invention.

FIG. 2 is an isometric section view of the preferred embodiment of the monitor of FIG. 1.

FIG. 3 is an isometric view of a monitor having a monitor base unit connected to a microprocessor and having two sensor cartridges.

FIG. 4 is an isometric view of the monitor base unit showing sensor cartridge engaging slots and the water and electrical connectors.

FIG. 5 is a rear elevation view of the monitor base unit showing a container of doped ion exchange resins and the water connections between two sensor cartridges.

FIG. 6 is a cut side view of a first sensor cartridge, showing a water inlet and outlet and a resin incorporated BAW device.

FIG. 7 is a cut side view of a second sensor cartridge, showing a water inlet and outlet and a resin incorporated BAW device.

The present invention is a monitor apparatus and method of detecting and quantifying specified ions in an aqueous flow. In its most basic form, the monitor of the present invention involves the doping of a target ion onto an ion exchange resin and measuring the presence of this target ion in the flow of analyte downstream of the resin.

Referring now to FIGS. 1 and 2, the preferred embodiment of the present invention, utilizing ion detection techniques as a monitor to detect failure of a water filter, is disclosed. As shown in FIG. 1, a monitor 10 is located at an outlet end 12 of a water filter system 14 having a conduit in which an ion exchange resin (not shown) is disposed. The water filtration system 14 has a water-dispensing faucet 16, which has a threaded male connector 18. A faucet collar 20 is located under the dispensing faucet 16 with the threaded male connector 18 extending through a faucet engaging hole 22 of the faucet collar 20. The faucet collar 20 has a green light 24 and a red light 26. The green light 24 is illuminated when water is dispensed from the faucet 16 until the monitor 10 detects the presence of a target ion T, at which time the red light 26 is illuminated on the faucet collar 20.

As shown in FIG. 2, the monitor 10 has a conduit 30. The conduit 30 has an inlet 32, an outlet 34, and a top region 36 and a bottom region 38 separated by a restraining screen 40. An ion exchange resin bed 42, doped with a target ion T, is contained in the top region 36 of the conduit 30. A sensor substrate 44 is positioned in the bottom region 38 of the conduit 30. The sensor substrate 44 has an insulator layer 46, conductive pads 48 and a polymer layer 50 which is selective for the target ion, T. The conductive pads 48 are connected to a constant current supply (not shown) and, in the preferred embodiment, are gold. However, other conductive materials commonly used in such applications may be used to achieve similar results.

Analyte water exiting the water filter 14 enters the monitor inlet 32 and passes into the ion exchange resin bed 42. Ions in the analyte having a selectivity coefficient higher than the target ion, T, will displace the target ion, while ions having selectivity coefficients lower than, T, will not displace target ions in the ion exchange resin bed 42. The analyte water passing from the ion exchange resin bed 42 passes across the polymer layer 50 of the sensor substrate 44. Any target ions in the analyte will affix to the polymer layer 50 in a conductive bridge 52 between the conductive pads 48, changing the voltage of the current flow in the constant current source. Ohm's Law states that:

where: I is the electrical current measured in amperes, and

E is the electromotive force expressed in volts, and R is the resistance, expressed in ohms, .OMEGA..

When the target ions, T, cause a change in conductivity between the conductive pads 48, the resultant change to the resistance, R, in the equation, necessitates a corresponding change in E to maintain a constant current I. The change in voltage is detected by a voltmeter. When the voltage change differs from a pre-set threshold level, the green light 24 on the faucet collar 20 is disabled and the red light 26 is enabled, effectively signaling the user that it is time to change the water filter cartridge.

The foregoing embodiment has been described in terms of the 8% cross-linked ion exchange resin set forth in Table 1, with the target ion being copper. In that embodiment, if either mercury, Hg or lead, Pb were present in the influent, they would displace the Cu ions on the ion exchange resin column and trigger the sensor. Table 1 sets forth another Purolite cation resin, a 4% cross-linked resin which has different selectivity coefficients from the 8% cross-linked resin.

In the 4% resin, the ions with higher selectivity coefficients than Cu are Ca, Sr, Hg and Pb. Thus, Ca and Sr are higher than Cu in the 4% resin and lower than Cu in the 8% resin. Thus, by employing the 4% resin in the monitor, the signal means would be triggered by the presence of Ca and Sr, whereas by employing the 8% resin, the signal means would not be triggered by the presence of either Ca or Sr. Thus, the present invention allows for selection of ions to be detected, based on the selection of the ion exchange resin selected for the ion exchange column.

In another embodiment of the present invention, two or more monitors are situated in parallel. Using the example in the preceding paragraph, if the monitor was employed to determine the presence of Ca or Sr in a water stream, one monitor would employ the 8% resin and the other would employ the 4% with Cu being the target ion. If neither monitor triggered the signal means, then the water stream would not be at a breakthrough state for Ca or Sr, for in this example, either Ca or Sr would trigger monitor 2. If monitor 2 was triggered but monitor 1 was not triggered, then the water stream must contain Ca or Sr, for if any other ions triggered monitor 2, then monitor 1 would be triggered also. Thus, by employing more than one monitor, each with different ion exchange resins in the resin column, the monitor of the present invention can isolate specific ions or groups of ions.

In one embodiment of the invention, the monitor employs reference ions, target ions and marker ions. The reference ions are ions having a selectivity coefficient immediately higher than the target ion on a chart of ion exchange resin selectivity coefficients. The target ions are the ions being detected and quantified. The marker ions are ions having a selectivity coefficient immediately lower than the target ion. Selectivity coefficients are measures of the attraction of an ion to an ion exchange resin. For cations, the coefficients are expressed as the attraction relative to hydrogen. For anions, the coefficients are expressed as the attraction relative to hydroxide.

To detect and quantify a first target ion, the monitor has a first sensor which, with calculations in a microprocessor, determines the number of first reference ions in the analyte. A second sensor, which employs first marker ions, and with calculations in the microprocessor, determines the total number of first target ions in the analyte. The monitor has a flow meter, which provides flow rate of the analyte. The microprocessor computes the concentration of the first target ions in the analyte, adjusted by the capture ratio of the ion exchange resin, by dividing the number of first target ions in the analyte by the flow rate of the analyte.

A third sensor is employed to detect and quantity a second target ion. The first target ion which was detected and quantified in the second sensor, becomes a second reference ion for the second target ion detected in the third sensor and the first marker ion used in the second sensor becomes the second target ion detected in the third sensor.

The number of different target ions that can be detected and quantified by a single monitor of the present invention is limited only by the availability of ion exchange resins to differentiate among ions. The monitor requires an ion having a selectivity coefficient immediately higher and immediately lower than the target ion. The detected ions can be cations or anions.

It is preferred that adjoining cations have the maximum separation in their selectivity coefficients. Thus, referring to Table 1, in a sensor with copper as a target ion, strontium is an adjoining ion, having the next lower selectivity coefficient, for both the 8% and 12% cross-linked resins. The preferred choice of resin is the 12%, because the separation (9.5-6.25=2.25) is greater than the 8% resin (5.3-4.95=0.35).

The monitor may be connected to a microprocessor and has a base unit comprising a base unit water inlet, a base unit water outlet and sensor cartridges. The sensor cartridges each have a water inlet, a sensor and a water outlet. In some embodiments, the sensors have a layer of ion exchange resin and a bulk acoustic wave (BAW) device to detect changes in mass in the ion exchange resin layer and an insulator. In these embodiments, the layer of resin is deposited on the bulk acoustic wave (BAW) device or a substrate in vibratory contact with the BAW device.

The BAW device consists of a thin, flat piezoelectric crystal having metal electrodes covering the top and bottom faces. Piezoelectric crystals are well known in the art and have been applied to a number of applications, including a variety of sensor applications. Since the BAW substrate is piezoelectric in nature, an applied potential results in a corresponding mechanical deformation. Furthermore, due to its elasticity, the substrate "springs" back to its original shape upon removal of this potential. Because of the finite inertia of the crystal, however, the crystal behaves as a mass on a spring, oscillating at a characteristic frequency for some time until the acoustic wave is finally damped out. Such a situation is analogous to a guitar string, oscillating at a specific pitch after it has been plucked. In this particular case, however, since the substrate is piezoelectric in nature, a corresponding electrical signal appears on the metal electrodes of the device. By amplifying this electrical signal and feeding it back to the crystal, an extremely stable oscillator can be realized. This oscillation frequency is almost exactly the resonant frequency of the BAW device, differing only enough to account for any electrical phase shift through the amplifier. The resonant frequency of the BAW device, however, is highly dependent upon a number of parameters, including the velocity, v, at which the wave travels through the bulk of the crystal, the thickness, t, of the crystal, and the interaction of the BAW with the surfaces of the device (i.e., the boundary conditions). To a first approximation, the first two parameters, v and t, remain constant. Upon application of any thin film to the surface of the device, however, the resonant frequency becomes highly dependent upon the elastic properties of the film, the electrical conductivity of the film, and the mass of the film. Thus, a BAW crystal oscillator can be utilized as a very sensitive microbalance for the measurement of masses in the nanogram range.

As a thin film of matter collects on the surface of the crystal, the change in mass is manifested as a change in BAW resonant frequency, which is, in turn, manifested as a change in the oscillation frequency. This frequency change can be modeled by Sauerbrey's equation, as follows, ##EQU1## where m is the mass loaded onto the device (in kg), f.sub.0 is the nominal resonant frequency of the device (in Hz), .DELTA.f is the change in frequency (in Hz), v.sub.s is the velocity of the BAW in the substrate (in m/s), .rho..sub.5 is the density of the substrate (in kg/m.sup.3), and A is the active surface area of the device (in cm.sup.2). While this equation neglects film elasticity and conductivity, it provides an excellent model for frequency changes due to mass loading of the device. For a 15 MHz AT-cut quartz crystal, the minimum detectable frequency change (1 Hz) corresponds to a change in mass of about 2 nanograms/cm.sup.2.

The mass change of an applied film on the BAW device will have a similar effect on the frequency of the device as described above for the deposition of a film on a bare device. Thus, in the present invention, a first metal electrode is coated with a layer of ion exchange resin, preferably of a thickness of about one micron. The layer is subsequently doped with the target ion, T, the reference ion, R or the marker ion, M.

In a monitor base unit configured to detect and quantify a target ion, the base unit has a container of ion exchange resin, doped with a reference ion, R, with R having selectivity coefficient immediately higher than a first target ion, T, a first sensor cartridge and a second sensor cartridge. The first sensor cartridge has a first sensor. The second sensor cartridge has a second sensor. The first sensor has a layer of ion exchange resin incorporated on a top electrode of a first BAW device doped with the target ion, T. A second ion exchange resin layer incorporated on a second electrode of the second sensor is doped with a marker ion, M, the ion having the next lower selectivity coefficient in the ion exchange resin table from the target ion, T.

The analyte passes from a monitor base unit water inlet into the container of ion exchange resin. All ions in the analyte having selectivity coefficients higher than the reference ion, R, will affix to the ion exchange resin and exchange for the reference ion, R. Thus, the output water from the container may contain R, or ions having selectivity coefficients less than R, including the target ion, T. The water, exiting the container, passes into the first sensor cartridge, having the first sensor with a layer of ion exchange resin doped with the target ion, T.

The reference ions R, in the water will affix to the layer and exchange with target ions, T, on the layer. Any target ions, T, in the water will either displace the target ion, T, on the first layer or they will pass by the first layer without displacing any target ions. In either case, the net effect to the mass of the layer will be zero. Ions having lower selectivity coefficients will not displace target ions, T, on the first layer. Thus, the water, having passed the first sensor, will contain either target ions extant in the analyte, the displaced target ions, or ions having selectivity coefficients lower than the target ions. The exchange of reference ions, R, on the first layer will increase the mass of the first layer to the extent that reference ions, R, are present in the water, less the mass of the target ions, T, displaced by the reference ions, R.

In operation, the water passes from the container into the first sensor cartridge and passes over the first layer of ion exchange resin incorporated on the top electrode of the BAW device. In this embodiment, it is preferred that a bed of ion exchange resin be downstream from each sensor, with the resin being doped with the same ion as the doped ion on the preceding sensor. When the output water from the first sensor passes by the second layer on the second sensor doped with the marker ions, M, the target ions, T, in the water will exchange with the marker ions, M, residing on the layer.

The exchange of target ions, T, on the second ion exchange resin layer will increase the mass of the second layer, less the mass of the marker ions, M, displaced to the extent that target ions, T, are present in the water. The mass change, m.sub.1, of the first sensor, will be the mass of the reference ions, R, less the target ions, T, displaced and can be expressed as follows:

where: R.sub.A is the number of reference ions

W.sub.R is the atomic weight of the reference ions and

W.sub.T is the atomic weight of the target ions.

Thus, the number of reference ions, R.sub.A is expressed as: ##EQU2##

The mass change, m.sub.2, on the second sensor, will be the mass of the target ions displaced by the reference ions, R, plus the mass of the target ions, T, in the analyte less the weight of the marker ions, M, displaced by the target ions, M, and can be expressed as follows:

where: T.sub.A is the number of target ions in the analyte and

W.sub.M is the atomic weight of the marker ions.

Thus, the number of target ions in the analyte is expressed as follows: ##EQU3## The increase in mass on the second layer will result in a decrease in the frequency of the BAW device measured in MHz. The frequency decrease is recorded by the microprocessor in one-second intervals. The decreased frequency is converted to m.sub.2, the mass change on the second sensor layer during the interval. Simultaneously, the microprocessor accepts input from a flow meter, recording the passing of water into the monitor base unit in ml/sec. The microprocessor will convert the change in frequency to the number of atoms per second, adjust the number of atoms by the capture ratio of the ion exchange resin and divide by the ml/sec recorded from the flow meter. The result is a reading of the presence of the target ion, T. Since the BAW records the mass changes in the sub-pictogram to microgram range, the resultant measurement will be in parts-per-billion (ppb).

For the detection and quantification of a second target ion, T', the monitor base unit has a third cartridge having a third sensor with a third layer doped with a marker ion, M'. In order to quantify the second ion, T', the value for the number of target ions, T, becomes R.sub.A, the number of reference ions, R', in the calculation required to quantify the second target ion, T'. The marker ion, M, on the second layer of the second sensor becomes the target ion, T', for detection of the second target ion, T'. Thus, the computation for the second target ion, T', is as follows:

where: R'.sub.A is T.sub.A, the number of target ions, T.

T'.sub.A is the number of target ions in the analyte, and

W.sub.M' is the atomic weight of the marker ions, M'.

Thus, the number of target ions in the analyte is expressed as follows: ##EQU4##

As is apparent from the above description, monitors of the present invention may be employed to detect and quantify multiple ions. For example, a monitor may be configured to detect mercury and copper. In such a monitor, the container of ion exchange resin is doped with lead. The analyte passes into the container and the ions heavier than lead exchange with the lead. The analyte passes over the first sensor layer which has an ion exchange resin doped with mercury. The lead exchanges with the mercury. The water passes through a resin bed doped with mercury to capture any lead ions that failed to exchange with the mercury on the first sensor layer. Thus the water now has the mercury that was displaced, the mercury in the analyte and cations lighter than mercury. The water passes over the second sensor, which is doped with copper. The mercury, and only the mercury, exchanges with the copper. The layer of the third sensor is doped with calcium. The copper from the second sensor displaces the calcium ions on the third sensor, and so on.

The weight change on the first sensor layer is the weight of lead less the weight of the mercury displaced by the lead. Since the unit weight of the lead and mercury are known, the number of lead ions is calculated. The exchange of mercury with lead is a one-for-one exchange. Thus, the number of mercury ions displaced is known. The weight change on the second layer is (1) the weight of the mercury which was displaced by the lead, (2) the weight of the mercury in the analyte and (3) less the weight of the copper ions displaced. The unit weights of mercury and copper are known and, thus, the total weight of the mercury, and the total number of mercury ions, on the layer is known. Subtracting the number of displaced mercury ions from the total mercury ions on the layer yields the number of mercury ions in the analyte. The calculations for the copper detection are the same as that for mercury.

It should be appreciated that the monitor will detect and quantify multiple ions so long as the ions being detected have ions with adjacent selectivity coefficients. If there is a break in the succession for selectivity, the sensor cartridge for the ion having the highest selectivity in a contiguous group must be preceded with a container of ion exchange resin having the next higher selectivity coefficient on the exchange sites of the resin.

Referring now to FIG. 3, one embodiment of the apparatus of the present invention, adapted to monitor two ions, is shown. The monitor 54 has a monitor base unit 56, connected to a microprocessor 58. The monitor base unit 56 has a base unit water inlet 60, a base unit water outlet 62, a first sensor cartridge 64, and a second sensor cartridge 66.

As viewed in FIG. 4, the sensor cartridges 64 and 66 engage cartridge engaging slots 70 when seated on the monitor base unit 56. When seated, the first sensor cartridge, 64 engages a first water inlet nipple 72 located in a first water inlet 74, a first water outlet nipple 76, located in a first water outlet 78 and a pair of electrical connector pins 80 located on a rear surface 82 of the monitor base unit 56. The second sensor cartridge 66 engages a second water inlet nipple 84 located in a second water inlet 86, a second water outlet nipple 88, located in a second water outlet 90 and a pair of electrical connector pins 92 located on the rear surface 82 of the monitor base unit 56. The water inlet nipples and water outlet nipples 72, 76, 84, 88 have circumferentially mounted O-rings 94 located in O-ring grooves 95 (shown in FIG. 6). Pairs of indicator lights 96, are located in a top region 98 of the rear surface 82 for each sensor cartridge 64 and 66. The pairs of indicator lights, 96 flash green when the sensor cartridges 64 and 66 are operational and flash red when the sensor cartridges 64 and 66 need replacement.

As viewed in FIG. 5, the analyte water enters the base unit water inlet 60, passes into a container 100, which contains a bed of ion exchange resin doped with the reference ion, R, where the ions heavier than the reference ion exchange for the reference ion. The water exiting the container 100 passes into the first water inlet 74. Water exiting the first sensor cartridge 64 passes through the first water outlet 78, and flows through a tube 104 into the second water inlet 86. Water exiting the second sensor cartridge 66 passes through the second water outlet 90 and on through the base unit water outlet 62.

FIG. 6 shows the first sensor cartridge 64. When in its seated position, as shown in FIG. 3, the first water inlet nipple 72 engages a water inlet recess 110, the first water outlet nipple 76 engages a water outlet recess 112 and the electrical connector pins 80 engage an electrical pin recess 116.

The analyte water, shown in a flow path 120, enters the first sensor cartridge 64 through the water inlet recess 110, passes across a top surface 130 of a first BAW device 132, passes a water exit passage 134, and flows through a first bed of ion resin exchange resin 136. The first BAW device, 132, has a layer of ion exchange resin 137 doped with a target ion, T, a top electrode 138, a layer of piezoelectric crystal 140, a bottom electrode 142 and an insulator 144. Though quartz crystals, such as those commercially available from Sawtek, Inc., Orlando, Fla. and Motorola, Inc. Phoenix, Ariz., are the preferred piezoelectric crystals, other crystals exhibiting piezoelectric properties may also be used to achieve similar results. It is also preferred that the insulator 144 encapsulate the bottom electrode 142 to isolate the bottom electrode 142 from the analyte water.

The analyte water then passes through the first water outlet 78 and into the second sensor cartridge 66, shown in FIG. 7. The analyte water, shown in a flow path 120, enters the second sensor cartridge 66 through the water inlet recess 150, passes across a top surface 152 of a second BAW device 154, having a layer of ion exchange resin 156 doped with a marker ion, M, passes a water exit passage 157, and flows through a second bed of ion resin exchange resin 158, which is doped with the marker ion, M.

In these embodiments, the flow rate of the analyte water will be determined by a flow meter (not shown) with the rate in ml/sec being inputted to the microprocessor 20. It is preferred that the flow rate be less than 0.125 gpm and that the temperature range of the analyte water be between 45 and 75 degrees F. Thus, any type of flow meter capable of measuring fluids having these ranges of flow and temperature, and capable of sending a signal to the microprocessor, may be used. For example, magnetic flowmeters, coriolis mass flowmeters, vortex shedders, differential pressure meters or variable area flowmeters are all well known in the art and all may be adapted to measure the desired flows and produce the desired outputs.

The microprocessor converts the mass m, computed in Sauerbrey's equation to the number of ions of the target ions, T and T' by accessing a conversion table embedded in the microprocessor 20. The number of ions is adjusted by the capture ratio of the ion exchange resin. The microprocessor 20 then divides the number of ions accumulated in time t, and divides by the analyte water flow during time t. The result is the concentration of Tand T' in the analyte. The concentration, in parts per billion, is transmitted to an output device, such as a PC, not shown. In the preferred embodiment, a microprocessor 20, such as the Motorola 68HC11, is be employed to perform frequency counting, linearization, computational functions, converting frequency to mass, table look-up functions including converting mass to number of ions and outputting MCL's for each ion being detected, arithmetic functions computing ppm (parts-per-million) or ppb (parts-per billion) and data conversion to output devices. However, in other embodiments a series of microprocessors adapted to perform different portions of the required calculations, and to provide the necessary outputs, may be used to achieve similar results.

As described above, the method of the present invention may be used to detect concentration levels of certain contaminants in an aqueous flow. However, the BAW system may be substituted for the conductivity system of the preferred embodiment to provide a failure detector for a filter cartridge. For example, if there was a need to detect Hg, Pb, and Ba, then detection of Cu, the ion that precedes those on the selectivity chart, would provide indication that the ion exchange resin was at a stage to break through for any of those elements. If the threshold ion is at the copper level, then when the ion exchange resin has reached a saturation stage in which copper is breaking through the resin, the filter cartridge needs replacement before heavier, more toxic metals elute into the filtered water. In this embodiment, the water passing from a water filter passes into a water inlet of a monitor base unit having a sensor cartridge. The sensor has a layer of ion exchange resin incorporated on a top electrode of the BAW device. The layer is doped with a marker ion, which in this case is calcium. Any ions having a selectivity coefficient higher than calcium will affix to the layer and displace calcium ions. Ions having selectivity coefficients lower than calcium will not affix to the resin layer. The exchange of heavier than calcium ions with calcium on the layer will increase the mass of the layer to the extent that heavier than calcium ions are present in the water less the mass of the calcium ions displaced. When a frequency drop of the BAW device indicates that the mass, m, of the layer has increased above a certain level, the microprocessor transmits an electronic output device, such as, a red light, which alerts the user that the water filter requires a change of the filtration cartridge.

In another embodiment for detecting and quantifying ions, the BAW device is replaced with the sensor substrate having conductive pads and the reference ions and target ions are detected and quantified by measuring changes in voltage rather than by changes in mass. This embodiment is identical to the monitors described with reference to FIGS. 1 and 2, except that a flowmeter and microprocessor are added to convert the changes in voltage into contamination levels, measured in parts per million, parts per billion, etc., of the desired contaminant.

In another embodiment, an ion selective polymer is employed in place of the calcium doped ion exchange resin to detect levels of copper. A polymer such as polyvinyl pyridine, PVP, is incorporated on a top electrode of a BAW device. Polyvinyl pyridine is selective for copper, i.e., if ions heavier or lower than PVP pass by a PVP incorporated layer, the ions will not affix to the surface. Thus, by measuring the mass loading of the PVP layer, the sensor containing the PVP layer will quantify the number of copper ions in the analyte. The embodiment can be used as a copper monitor, a threshold monitor for an ion exchange resin column or as a provider of R.sub.A, the number of copper ions used as reference ions in an ion quantifying monitor.

Although the present invention has been described in considerable detail with reference to certain preferred versions thereof, other versions would be readily apparent to those of ordinary skill in the art. Therefore, the spirit and scope of the appended claims should not be limited to the description of the preferred versions contained herein.