The invention relates to tank-based water heating systems that include a sacrificial anode to limit the amount of corrosion of the tank.
Because water heater tanks are typically made of metal, the material can react with the water stored in the tank resulting in corrosion of the metal and, eventually, failure of the tank. Mechanisms for limiting this type of corrosion include lining the tank with a non-corrosive material such as glass. Some water heating systems also include a sacrificial anode to limit corrosion of the tank material. The sacrificial anode reacts with the water to cause a current to flow through the anode and the tank. This chemical reaction causes the sacrificial anode to degrade instead of corroding the metal material of the water tank walls.
The level of protection provided by the sacrificial anode increases with the current of the sacrificial anode relative to the tank walls. However, an increased current also causes the sacrificial anode to degrade more rapidly. The current of the sacrificial anode, the rate of anode degradation, and the ability of the anode to protect the tank material is dependent upon multiple variable conditions including the conductivity of the water in the tank.
In one embodiment, the invention provides a method for controlling the current of a sacrificial anode based on the conductivity state of the water. An unregulated current of the sacrificial anode relative to the water tank is measured and a conductivity state of the water is identified based on the measured unregulated current. A maximum current limit for the sacrificial anode is determined based on the conductivity state of the water and the current of the sacrificial anode is limited such that the current does not exceed the determined maximum current limit.
In some embodiments, the conductivity state is determined by identifying a first current threshold and a second current threshold in a look-up table stored on a memory that correspond to a temperature of the water in the tank. The measured unregulated current of the anode is compared to the first and second current thresholds. If the measured unregulated current is less than both thresholds, the conductivity state of the water is determined to be low. If the measured unregulated current is between the two thresholds, the conductivity state is determined to be moderate. If the measured unregulated current is greater than both thresholds, the conductivity state is determined to be high.
In some embodiments, the first and second current thresholds are selected from the look-up table based on water temperature, the geometry of the water tank (as identified by a product model number), and the geometry/chemistry of the anode (as identified by a product model number).
In some embodiments, the determined maximum current limit corresponds to a minimum current required to protect the water tank from corrosion multiplied by a safety factor. In some embodiments, it is determined whether an odor reduction mode of the water heater is activated and, when the odor reduction mode is activated, the determined maximum current limit is reduced to a value less than the original determined maximum current limit, but greater than or equal to the minimum current required to protect the water tank from corrosion.
In some embodiments, degradation of the water tank is periodically evaluated. A subsequent unregulated current of the anode is measured and compared to the original unregulated current value. The determined maximum current limit is increased when the difference between the initial unregulated current value and the subsequent unregulated current value exceeds a degradation threshold.
In another embodiment, the invention provides a water heating system including a water tank, a sacrificial anode, and a water heater controller. The water heater controller measures an unregulated current of the sacrificial anode relative to the water tank and identifies a conductivity state of the water in the water tank based on the measured unregulated current. A maximum current limit for the sacrificial anode is determined based on the conductivity state and the current of the sacrificial anode is limited so that the current does not exceed the determined maximum current limit.
Other aspects of the invention will become apparent by consideration of the detailed description and accompanying drawings.
Before any embodiments of the invention are explained in detail, it is to be understood that the invention is not limited in its application to the details of construction and the arrangement of components set forth in the following description or illustrated in the following drawings. The invention is capable of other embodiments and of being practiced or of being carried out in various ways.
Software included in the implementation of the water heating system 100 is stored in the memory 203 of the controller 105. The software includes, for example, firmware, one or more applications, program data, one or more program modules, and other executable instructions. The controller 105 is configured to retrieve from memory and execute, among other things, instructions related to the control processes and methods described herein.
The PCB of the controller 105 also includes, among other things, a plurality of additional passive and active components such as resistors, capacitors, inductors, integrated circuits, converters, and amplifiers. These components are arranged and connected to provide a plurality of electrical functions to the PCB including, among other things, filtering, signal conditioning, signal converter, and voltage regulation. For descriptive purposes, the PCB and the electrical components populated on the PCB are collectively referred to herein as the controller 105.
The controller also includes an anode current circuit 209. As described in detail below, the anode current circuit 209 interacts with the processor 201 to measure a current of the sacrificial anode 107 relative to the water tank 101 and to regulate the current such that the current is limited to a determined maximum current limit.
Furthermore, to allow the same controller 105 and look-up table to be included in multiple different water heating system configurations, the look-up table can include additional dimensions. For example, the ranges of currents corresponding to a low, moderate, and high conductivity are defined based, not only on the temperature of the water, but also based on the geometry and composition of the water tank 101 and the sacrificial anode 107. However, instead of requiring measurements and analysis of the water tank 101 and the sacrificial anode, the controller 105 is configured to identify the water tank 101 and the sacrificial anode 107 in the look-up table based on a product model number assigned to the specific component. As such, the portion of the look-up table illustrated in
Returning now to
If the measured unadjusted current is less than both thresholds, the controller 105 determines that the water in the tank 101 has low conductivity. In low conductivity water, a higher current is required to adequately protect the water tank 101 from corrosion. As such, the controller 105 defines the “maximum current limit” for the water heating system as a high current limit value (step 307). In some constructions, the controller 105 may even artificial apply a current to the anode from a power source to ensure that the current of the anode 107 is sufficient to protect the tank 101 from corrosion.
If the measured unadjusted current is greater than the first threshold, but lower than the second threshold, the controller 105 determines that the water in the tank 101 has moderate conductivity. The controller then defines the “maximum current limit” for the water heating system as a medium current limit value (i.e., a current value that is less than the current limit value for low conductivity water) (step 309). Similarly, if the measured unadjusted current is greater than both the first threshold and the second threshold, then the controller 105 determines that the water in the tank 101 has high conductivity and defines the “maximum current limit” for the water heating system 100 as a low current limit value (i.e., a current value that is less than the current limit value for both low conductivity and moderate conductivity water) (step 311).
Once the conductivity state of the water has been determined and the maximum current limit has been defined, the controller 105 regulates the current of the anode 107 using a current limiting circuit 209.
In the examples described above, the controller 105 determines a conductivity state of the water in the tank 101 and controls the current of the anode based on the conductivity state. However, the system described above also implements additional functionality to adjust the value of the determined maximum current limit for the water heating system 100 based on other variables such as, for example, the condition of the water and the tank 101.
A negative side effect of using a sacrificial anode 107 to protection the tank 101 from corrosion is that, in some water conditions, excessive current can cause the water in the tank to have an unpleasant odor.
As illustrated in
If the odor reduction mode is not activate (step 603), then the controller 105 continues to regulate the current of the anode based on the original maximum current limit (including the safety factor). However, if the odor reduction mode is activated, the controller 105 reduces the value of the current limit (step 605). For example, the controller 105 can remove the safety factor and regulate the current of the anode based only on the minimum current level required to protect the tank. Alternatively, the controller 105 can adjust the maximum current limit value such that the adjusted maximum current level falls between the original current limit value and the minimum required current.
Over time, the glass lining of the water tank 101 will wear away and, as noted above, the anode 107 itself will begin to degrade. As such, the anode current required to protect the tank from corrosion will generally increase over the life of the water heating system 100.
The controller 105 begins by determining whether a degradation evaluation time period has elapsed (step 701). The controller 105 can be programmed to perform this evaluation periodically (e.g., once a month or once a year). If the degradation evaluation time period has not yet elapsed, the controller 105 continues regulating the current of the anode based on the determined maximum current limit (step 703). However, when the controller 105 determines that it is again time to evaluate the condition of the water heating system 100, the controller 105 removes the current limit applied to the anode 107 by the anode current circuit 209 and measures an unregulated current of the anode 107 (step 705).
Water heating systems are typically not relocated during the life of the water heating system 100 and the conductivity of water at a location will generally not change significantly over the same time period. Therefore, after the degradation evaluation time period has elapsed, any change in the measured unregulated current will be predominantly due to degradation of the water heating system 100. In the example of
When the degradation threshold is exceeded, the controller 105 can increase the current limit in a variety of ways. For example, the controller 105 can apply a higher safety factor to the maximum current limit. Alternatively, the controller 105 can adjust the maximum current limit based on the magnitude of the deviation between the original measured unadjusted current and the subsequent measured unadjusted current. Furthermore, in other constructions, the controller 105 increases the current limit based on changes to the measured unadjusted current regardless of whether a degradation threshold has been exceeded. In some such constructions, the value of the safety factor described above is directly related to the magnitude of the deviation between the original unadjusted current of the anode and a present value of the unadjusted current of the anode.
As noted above, although increasing the value of the maximum current limit increases the level of protection provided to the tank, it will also increase the rate of degradation of the sacrificial anode. Therefore, in some constructions, a maximum current limit set-point is defined for the anode 107 of the water heating system 100. The maximum current limit set-point can be defined as a current value that will cause the anode to degrade to the point of failure after a defined period of time. The maximum current limit set-point can be defined such that the defined period of time until failure of the anode correlates to the expected life of the water heater tank or, alternatively, a warranty period for the water heating system 100. Preventing the controller 105 from increasing the maximum current limit beyond the maximum current limit set-point ensures that the anode 107 remains operational for at least a known, defined period of time.
Thus, the invention provides, among other things, a system and method for regulating the current of a sacrificial anode based on a conductivity state of the water in a water heater tank to ensure adequate protection and reduce the rate of degradation of the sacrificial anode. Various features and advantages of the invention are set forth in the following claims.
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Corr-Rad (Cathodic Protection Systems Design, 2011, http://web.archive.org/web/20110606180556/http://www.corr-rad.com/design.html). |
Australian Government Department of Education, Employment and Workplace Relations (referred to as a DEEWR, Cathodic Protection, 2008 https://nationalvetcontent.edu.au/alfresco/d/d/workspace/SpacesStore/50f126e2-c01a-472f-b07b-4c52fa0025f3/ims/typeAappliances/storage—water—heaters/cathodic.html). |
Number | Date | Country | |
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20140262822 A1 | Sep 2014 | US |