The present invention relates to water treatment systems and more particularly to point-of-use water treatment systems.
A variety of filter technologies have been developed for treating fluid streams, such as water intended for human consumption. For example, activate carbon filters have long been used to remove particulate and organic contaminants from water and other fluid streams. It is not uncommon for a water treatment system (“WTS”) to combine a carbon block filter with a source of radiant energy, such as an ultraviolet (“UV”) light source, to kill microorganisms in the filtered water. One such WTS is disclosed in U.S. Pat. No. 5,698,091 to Kuennen et al, which is incorporated herein by reference in its entirety. UV treatment devices typically include a UV bulb and associated ballast circuitry that add cost and complexity to the WTS.
Microbiological interception (“MI”) filters have been developed to reduce/trap/inactivate microorganisms in a fluid stream. For example, various MI filter-related technologies have been developed by Koslow Technologies Corp. and are disclosed in U.S. Pat. Nos. 6,835,311; 6,660,172; 6,872,311; 7,144,533; 6,953,604; 6,998,058; 7,008,537; 6,959,820; 7,011,752; 6,913,154; 6,866,704; 6,630,016; 6,550,622 and 6,770,204 (collectively, “the Koslow patents”). MI filters are typically less expensive than UV treatment devices because they are not electrically powered and do not require complex electrical circuitry. In general, MI filters have an inherent fail-safe mechanism that helps to protect the end user from consumption of water and other fluids treated after the MI filter has exceeded its operating life. More specifically, the flow rate of a typical MI filter will decrease over time in correspondence with the operating life of the MI filter. In other words, a conventional MI filter is designed so that its flow rate will continually decrease to a point where it essentially prevents use of the filter beyond its effective life. For example, conventional MI filters clog as a result of natural organic matter in the fluid stream. As organic matter accumulates within the microporous structure of the MI filter, the overall flow rate of the filter is decreased. Although this inherent clogging provides certain benefits, it also causes the MI filter to undergo increasingly lower flow rates, which causes the system to treat fluid more slowly and is undesirable in most applications. MI filters have sometimes been used with simple filter life monitors. For example, one known WTS with MI filter technology uses a filter life monitor that operates based on the “on time” of the system. This type of system records the amount of time that the system has been operated after the installation of a new MI filter, and signals for the replacement of the filter after a predetermined time period. This type of filter life monitor can provide a significantly inaccurate estimate of filter life when the pressure of the raw fluid varies. For example, when water pressure exceeds the expected pressure, the flow rate will increase and the filter life monitor will underestimate its usage. On the other hand, when water pressure is below the expected pressure the flow rate will decrease and the filter life monitor will overestimate its usage. Further, the MI filter is susceptible to premature clogging when the total organic carbon (“TOC”) present in the raw fluid is relatively high. For example, testing of a commercially available WTS with MI filter has shown that a MI filter rated for 2,000 gallons or six months may clog in as little as 50 gallons when subject to influent having a TOC level of as low as two parts per million.
The present invention provides a water treatment system (“WTS”) having a prefilter, a carbon block filter and a microbiological interception (“MI”) filter that operate in combination to treat a fluid stream, such as water. In one embodiment, the prefilter is a multi-layer nonwoven prefilter. In another embodiment, the prefilter is a pleated fabric prefilter. If desired, the WTS may include two prefilters, for example, both a multi-layer nonwoven prefilter and a pleated fabric prefilter.
In one embodiment, the water treatment system further includes a volumetric end-of-life filter monitor that monitors the life of the MI filter. In this embodiment, the MI filter may be configured to provide at least a predetermined flow rate throughout its rated life.
In one embodiment, the MI filter may include carbon particles and a binder. The MI filter may include a carbon particle distribution that with a mean particle diameter ranging from about 60 microns to about 80 microns and with a particle size distribution in which no more than about 10% by weight of the particles are larger than about 140 mesh and no more than about 10% by weight are smaller than about 500 mesh.
These and other objects, advantages, and features of the invention will be readily understood and appreciated by reference to the detailed description of the current embodiment and the drawings.
a-f are perspective views showing installation of the pleated prefilter on the filter assembly.
A water treatment system (“WTS”) according to an embodiment of the present invention is shown in
As noted above, the filter assembly 14 of the present invention includes multiple filters. The illustrated embodiment includes an arrangement of filters 16, 18, 20 and 22 that provide removal of particulate, VOC and microbiological contaminants. In the illustrated embodiment, the filters 16, 18, 20 and 22 are arranged in a coaxial configuration with the MI filter 16 located at the center, the carbon block filter 18 surrounding the MI filter 16, the nonwoven prefilter 20 wrapped about the carbon block filter 18 and the pleated fabric prefilter 22 disposed about the nonwoven prefilter 20. In this configuration, the fluid flows radially inwardly through the outermost filter (i.e. pleated fabric prefilter 22) and then sequentially radially inwardly through each successive filter (i.e. nonwoven prefilter 20 and carbon block filter 18) until it reaches and passes through the innermost filter (e.g. MI filter 16). The filters 16, 18, 20 and 22 may be arranged in other configurations, for example, by positioning the filters one adjacent to the next in a serial arrangement. The flow rate and capacity of the filter assembly (and the individual filters) may vary from application to application. However, in the illustrated embodiment, the filter assembly 14 may have a flow rate in the range of 0.7 to 0.9 gallons per minute with a capacity of 1,000 to 2,000 gallons with NSFI claims for Standard 53 VOC reduction. The dimensions of the filter assembly 14 and various filters may vary from application to application, but in the illustrated embodiment, the filter assembly 14 may be roughly 5″ in diameter and 7½″ long. The MI filter 16 may have an outer diameter of approximately 2.6″ and a length of approximately 6½″. The carbon block filter 18 may have an inner diameter of sufficient size to be fitted around the MI filter and have an outer diameter of approximately 4.2″.
The WTS 10 includes one or more filter housings to enclose the various filters and prefilters, and to provide a flow path for the raw fluid through the filters. The filter housing(s) may be easily opened and closed to facilitate filter maintenance, such as by retaining ring 300. As noted above, the WTS 10 of the illustrated embodiment includes a filter housing that is essentially identical to the filter housing of U.S. Pat. No. 6,984,320 to Bartkus et al. In the illustrated embodiment, the base housing 202, filter bracket 500 and retaining ring 300 cooperatively define and selectively close the filter chamber 208. More specifically, the filter bracket 500 is fitted over the open upper end of the base housing 202 to hold the filters within the filter chamber 208. The retaining ring 300 secures the filter bracket 500 to the base housing 202. The base housing 202 includes a threaded region 206 adjacent its open end to threadedly receive the retaining ring 300. The filter bracket 500 may include separate inlet and outlet ports 502 and 504 to allow untreated fluid to enter and treated fluid to exit the filter chamber 208. Flow control can be accomplished either by incorporation of a flexible orifice or limiting the size of the exit port on the system or one of the filters. The various components of the filter housing may be manufactured from a thermoplastic polymer, such as glass filled polypropylene, or metal. In this embodiment, the filter housing is a generally cylindrical housing with an open upper end, but its size, shape and configuration may vary from application to application. The use of a single housing, as shown in the illustrated embodiment, provides a number of advantages over multiple housing systems. For instance, the single housing system is simpler to manufacture and install, and reduces the size of the WTS.
Referring now to
The MI filter 16 may be a conventional microbiological interception filter. For example, the MI filter 16 may be manufactured in accordance with the microbiological interception filter technology disclosed in one or more of the following patents issued to Koslow Technologies Corporation: U.S. Pat. Nos. 6,835,311; 6,660,172; 6,872,311; 7,144,533; 6,953,604; 6,998,058; 7,008,537; 6,959,820; 7,011,752; 6,913,154; 6,866,704; 6,630,016; 6,550,622 and 6,770,204 (collectively, “the Koslow patents”), all of which are incorporated herein by reference in their entirety. The MI filter 16 may include a microporous structure made of an array of active particles. The active particles may be joined by a binder. A microbiological interception enhancing agent is formed on the microporous structure. The microbiological interception enhancing agent may include cationic material in combination with a biologically active metal. Although the active particles of the microporous structure may be any of variety of active particles, such as any of the various active particles disclosed in the Koslow patents, the active particles in the illustrated embodiment are activated carbon particles. Similarly, the biologically active metal may be essentially any suitable biologically active metal, such as the biologically active metals disclosed in the Koslow patents, including, but not limited to, silver, copper, zinc, cadmium, mercury, antimony, gold, aluminum, platinum, palladium, and combinations thereof.
In the illustrated embodiment, the MI filter 16 is manufactured in accordance with the teachings of one or more of the Koslow patents, except that the MI filter 16 may be modified to overcome the tendency of the MI filter 16 to undergo significant flow rate reduction over its useful life. To this end, the MI filter 16 of the present invention may include an active particle distribution with a larger mean particle size than disclosed in the Koslow patents. In the illustrated embodiment, the active particles of the MI filter 16 are activated carbon particles having a mean particle size distribution that corresponds with the disclosure of U.S. Pat. No. 6,368,504 to Kuennen et al, which is incorporated herein by reference in its entirety. For example, in the illustrated embodiment, the MI filter 16 may include a carbon mixture in which the mean particle diameter ranges between approximately 60 microns and 80 microns, and in which the +140 mesh particles and the −500 mesh particles are each less than approximately 10% of the particle size distribution. The mean particle diameter is, however, more preferably about 65 to about 75 microns, and most preferably about 70 microns. The +140 mesh particles and the −500 mesh particles are more preferably each less than approximately 8% of the particle size distribution, and most preferably each less than approximately 7% and 7.5%, respectively, of the particle size distribution. In another effort to address the tendency of the MI filter 16 to undergo significant flow rate reduction over its useful life, the MI filter 16 may include a different cationic polymer than disclosed in the Koslow patents. In this embodiment, the cationic polymer may be selected to provide the desired charge density and selectivity of the media. For example, a cationic polymer with a smaller charge may result in less clogging and hence greater flow rates through the life of the MI filter 16.
The carbon block filter 18 may be a conventional carbon block filter, such as the carbon block water filter disclosed in U.S. Pat. No. 6,368,504 to Kuennen et al, which as noted above is incorporated herein by reference in its entirety. As shown in
As noted above, the WTS 10 may include one or more prefilters. In the illustrated embodiment, shown in
A pleated fabric prefilter 22 may be disposed coaxially about the carbon block filter 18. The pleated fabric prefilter 22 may be a nonwoven polypropylene, such as a melt blow polypropylene. As shown in
The illustrated WTS 10 may also include a highly accurate volumetric flow meter (not shown) to measure flow rate through the WTS 10. The flow meter tracks the volume of fluid through the systems and is not susceptible to some of the inaccuracies inherent in meters that estimate flow rate based on WTS “on” time. The WTS 10 may also track the amount of time that has passed since the filter was installed to provide a second mechanism for tracking filter life. This second mechanism is not used to estimate the volume of fluid that has passed through the system, but rather to track time-based rather than use-based filter life. In the illustrated embodiment, the flow meter includes a flow turbine with electronic sensing (not shown) and a microprocessor. The flow turbine spins in direct proportion to the volume of water passing through the system. The electronic sensing device (not shown) senses rotation of the flow turbine, for example, by generating an electronic pulse for each rotation of the turbine. For example, the flow turbine may include magnetic material and the electronic sensing device may include a sensor capable of generating signals in response to the magnetic material in the rotation flow turbine. The WTS 10 includes a control system incorporated into electronics module 400 that is capable of receiving signals from the electronic sensing device and calculating water volume based on the signals. The WTS is programmed with a preset volume and/or time depending on the filter used. For example, in one application the WTS may include a filter rated for 1,000 gallons of flow or one year of installed time, whichever comes first. The WTS may include one or more indicators to notify the user when a filter needs to be replaced. For example, the WTS 10 may include light-emitting diodes (“LEDs”) that are illuminated to provide a visual indication when a filter needs to be replaced. The control system can also be programmed to provide a visual indication when the filter status is acceptable. For example, the control system may provide a flashing light when the treated water is being dispensed while the filter status is acceptable. The flashing light may change color to show that a filter needs to be replaced. For example, a green flashing light may be presented when the filter status is acceptable and a red flashing light may be presented when a filter needs to be replaced. In addition or in the alternative, the WTS 10 can incorporate a noise generator, such as a speaker, to provide an audible indication when a filter needs to be replaced. If desired, the control system can be programmed to prevent water from flowing through the WTS 10 when a filter needs to be replaced. The WTS 10 can be programmed to provide a warning when a filter is nearing the end of its operating life. For example, the WTS 10 may illuminate a warning light when a filter is at approximately 90 percent of its life. The user may use this advance warning to obtain a new filter before the life of the existing filter expires.
As an alternative, the filter assembly 14 (or an individual filter) may include one or more RFID smart chips (not shown) that retain all preset and usage information for the filter. An RFID smart chip can convey this information to the WTS 10 so that the WTS can convey the appropriate signals to the user regarding filter status. The RFID smart chip helps to protect the user from utilizing a filter beyond its useful life because it will have accurate information regarding the filter even if the filter is accidentally reinstalled after its useful life has expired. For example, an RFID smart chip can be programmed with the capacity of the filter, such as 600 gallon or one year whichever. When installed in the WTS 10, this information can be passed to the control system so that the WTS 10 can provide the appropriate information to the user. An RFID smart chip may also maintain a record of filter use and installed time in nonvolatile memory. Usage information can be collected by the WTS 10 and sent to an RFID smart chip for storage in memory. The WTS 10 may obtain usage information from an RFID smart chip when appropriate to allow accurate filter status information to be conveyed to the user. The RFID smart chip may also include a password that allows the WTS 10 to recognize whether or not the filter is “genuine.” The one or more RFID smart chips and relating electronic controls may be manufactured in accordance with the teaching of U.S. Pat. No. 6,673,250 to Kuennen et al, which is incorporated herein by reference in its entirety.
The above description is that of the current embodiment of the invention. Various alterations and changes can be made without departing from the spirit and broader aspects of the invention as defined in the appended claims, which are to be interpreted in accordance with the principles of patent law including the doctrine of equivalents. Any reference to claim elements in the singular, for example, using the articles “a,” “an,” “the” or “said,” is not to be construed as limiting the element to the singular.
Number | Date | Country | |
---|---|---|---|
60955937 | Aug 2007 | US |