FIELD OF THE INVENTIONThis invention relates to filter cartridges for use in gravity-fed water treatment systems. In particular, this invention relates to a filter cartridge having novel filter media.[0001]
BACKGROUND OF THE INVENTIONDomestic water treatment devices are known in the art. Among these devices are self-contained systems which process water in batches. Examples of batch devices are pitchers/carafes and larger reservoirs where treated water is poured, for example, from a spigot. These self-contained systems typically have upper and lower chambers separated by a filter cartridge. They rely on gravity to force water from the upper chamber, through the cartridge, and into the lower chamber, thereby producing treated water.[0002]
The presence of unwanted and potentially harmful contaminants in water, especially drinking water, is of concern to many people. This concern creates a desire for water treatment devices in the home and elsewhere. Many water treatment devices and methods have been developed to remove or neutralize chemical and particulate contaminants. Some of these devices and methods incorporate chemically active materials to treat the water. For example, activated carbon is capable of removing the bad taste and odor from water as well as chlorine and other reactive chemicals. Ion exchange resins are useful for removing metal and other ions from water. However, no single material or chemical has been found that will remove all contaminants.[0003]
In addition to chemical and particulate contaminants, water often contains biological contaminants. These contaminants often can not be entirely removed by activated carbon, ion exchange resins, or other chemically active water purifiers. The biological contaminants may be susceptible to harsher chemical treatment, but such chemicals are, typically, themselves contaminants or can not be easily incorporated in gravity-fed treatment devices, especially those for household use. In addition to being resistant to removal by standard chemical means, many of these biological contaminants, such as protozoan cysts like cryptosporidium, are only a few microns in size.[0004]
Because of their small size and the relative unavailability of suitable chemical removal methods for these biological contaminants, a gravity-fed water treatment device which can remove protozoan cysts and still retain satisfactory flow rate has been very difficult to develop. Present devices which filter cysts out of water require pressurization, either from the tap or by manual pumping, to achieve a satisfactory flow rate. However, such devices are relatively complex and expensive, and in the case of manual pressurization systems, harder to operate. Thus, there is a need for a gravity-fed water treatment device that is capable of removing biological contaminants, including cysts like cryptosporidium, while providing an acceptable flow rate.[0005]
SUMMARY OF THE INVENTIONAccording to the present invention, a filter cartridge for a gravity-fed water treatment is provided. In one aspect of the invention, the filter cartridge includes a porous particulate filter that has an open upper end, a closed lower end, and sidewalls between the two ends. The porous particulate filter is sealed to a portion of the filter cartridge by a connecting member. Water is treated as the water flows into the open upper end and through the sidewalls of the porous particulate filter. Air within the filter, that is displaced by incoming water, flows out of the open upper end of the filter.[0006]
In another aspect of invention, the filter cartridge includes a porous particulate filter with sidewalls and an inlet. Granular media is contained within the sidewalls of the filter. Water is treated as it flows through the inlet of the filter, through the granular media, and radially outward through the sidewalls of the filter.[0007]
In a further aspect of the invention, the filter cartridge includes a porous particulate filter which includes glass fibers and a hydrophilic binder. The porous particulate filter is sealed to a portion of the filter cartridge by a connecting member. Water that is treated by the filter cartridge has greater than 99.95% of 3-5 micron cysts particles removed.[0008]
These and other advantages and features of novelty which characterize the invention are pointed out with particularity in the claims annexed hereto. However, for a better understanding of the invention and its advantages, reference should be made to the drawings which form a further part hereof, and to the accompanying descriptive matter in which there is illustrated and described a preferred embodiment of the invention.[0009]
BRIEF DESCRIPTION OF THE DRAWINGSA preferred embodiment of the present invention will be described with reference to the accompanying drawings, wherein like reference numerals identify corresponding parts:[0010]
FIG. 1 is an exploded perspective view of an embodiment of a filter cartridge according to the present invention; and[0011]
FIG. 2 is a partial cross-sectional view of the filter cartridge shown in FIG. 1.[0012]
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTThe[0013]filter cartridge20 described herein can be used in a variety of gravity-fed water treatment devices. Referring to FIGS. 1 and 2, this preferred embodiment of thefilter cartridge20 contains aporous particulate filter24 withgranular media26 disposed withinparticulate filter24.Filter cartridge20 also has ashell22 which surroundsporous particulate filter24 to provide mechanical support for the particulate filter.Shell22 has acollar36 which seals porousparticulate filter24 tocartridge20 so that water flowing through the cartridge must pass throughporous particulate filter24 and is, thereby, treated.
[0014]Porous particulate filter24 mechanically filters particles and biological contaminants, such as protozoan cysts, out of the water. To effectively filter biological contaminants, porousparticulate filter24 should have pores smaller than the size of the contaminants that are to be filtered. Biological cysts, such as cryptosporidium, are only a few microns in size. An effective cryptosporidium filter must have pores that are less than about 5 microns, and preferably less than about 2 microns, in diameter. Thus, porousparticulate filter24 is, preferably, microporous, which means that the particulate filter has pores which are approximately 1-3 microns or smaller in size.
Preferably[0015]porous particulate filter24 removes greater than 99.95% of 3-4 micron cysts particles from water treated with the filter cartridge. The level of cyst filtration is determined using the protocols of NSF 53 §6.5 and 6.12, incorporated herein by reference.
Porous[0016]particulate filter24 is preferably formed in ashape having sidewalls25 and an open upper end.Sidewalls25 of porousparticulate filter24 are substantially cylindrical. However, other shapes of the sidewalls are also included within the scope of the invention. Moreover,sidewalls25 ofparticulate filter24 may be flat or pleated, as shown in FIG. 1. Pleated sidewalls provide greater filter surface area than do flat sidewalls for an otherwise identical filter configuration. However, the pleats should not be closely spaced or the flow rate through the pleats will be decreased.
The upper end of[0017]particulate filter24 is at least partially open so that water can flow intoparticulate filter24 and air withinparticulate filter24 can escape as it is displaced by the water. The bottom end of porous particulate filter may be closed (not shown) or open (see FIGS. 1 and 2). If the bottom end is open thenporous particulate filter24 should be attached to an object, such as abottom cap29 ofshell22, which will prevent the flow of water out of the open bottom end ofparticulate filter24.
[0018]Porous particulate filter24 can be formed from a wide variety of materials. Preferably,sidewalls25 ofporous particulate filter24 are made from a hydrophilic, microporous filter media. Optionally, if the bottom end of porousparticulate filter24 is closed, then the bottom can also be made from the hydrophilic, microporous filter media. One example of a suitable hydrophilic, microporous filter media is a carbon block which has been hollowed out to create sidewalls and a open upper end.
The preferred hydrophilic, microporous filter media for the construction of porous[0019]particulate filter24 is fibrous sheet filter media. The fibers of this sheet filter media can be either natural, such as fiber made of cellulose or cellulose derivatives, or synthetic, such as fibers made from polymers or glass. Preferably, the fibers are synthetic fibers, and more preferably, the fibers are glass microfibers. Often natural fibers, such as cellulose fibers, are thicker than synthetic fibers resulting in fewer pores and a correspondingly slower flow rate.
The flow rate of water through a given porous particulate filter is of critical importance in determining the acceptability of porous[0020]particulate filter24 for a gravity-fed water treatment device. Flow rate is typically determined by the size of the pores, the pressure applied to the water to push it through the pores, and the composition of the filter. In gravity-fed devices, such as carafes or household water storage containers, the pressure exerted on water to push it throughfilter cartridge20 is due only to a gravitational force on the water itself. For household gravity-fed water treatment devices, such as carafes, the pressure exerted on the water is typically less than about 0.5 lb/in2. Consequently, the gravity-induced flow rate through a typical microporous particulate filter is very slow and not practical for a gravity-fed water treatment device.
To overcome this limitation, the preferred porous[0021]particulate filters24 of the invention contain hydrophilic material. Hydrophilic materials, as defined for purposes of the present invention, are those materials, which when dry, are quickly wetted (i.e., they absorb droplets of water quickly). The hydrophilicity of these materials is due to an attractive force between the hydrophilic material and water which is greater than the surface tension of the water at the water/filter interface (i.e. the attractive force between the individual water molecules at the interface).
The hydrophilicity of porous[0022]particulate filter24 may be a result of the hydrophilic nature of the fibers or other material of the porous particulate filter. Alternatively, the hydrophilicity of the filter may be due to an additive to the material of the filter. Such an additive may be capable of creating a hydrophilic particulate filter even if the filter contains non-hydrophilic or hydrophobic fibers.
A hydrophilic additive to the filter may also serve other functions within the filter material. One example of such an additive is a hydrophilic binder which is added to the media, not only to impart hydrophilicity to the binder, but also to bind the microfibers of the media together to form a sheet. Hydrophilic sheet filter media having these properties is available from Alhstrom, Mt. Holly Springs, Pa. (Grade 2194-235). Suitable hydrophilic binder for use in binding glass microfibers is available from Goodrich (Part No. 26450).[0023]
Sheet filter media was obtained from the above-named source. The sheet filter media had an average pore size of about 1.2 μm and a thickness of about 0.024 in. The porous particulate filter was about 3 in. tall and had a 1.75 in. outer diameter. The porous particulate filter was pleated to give[0024]40 pleats uniformly spaced around the filter with a pleat depth of about 0.25 in., giving the filter an inner diameter of 1.25 in.
To protect porous[0025]particulate filter24 from damage, ashell22 may be disposed aroundfilter24.Shell22 has three connectable pieces, atop cap28, abottom cap29, and abody30, as shown in FIGS. 1 and 2. This configuration allows for easy placement ofparticulate filter24 infilter cartridge20. Other shell configurations may be used and are included within the scope of the invention.
[0026]Shell22 also has one ormore inlet apertures32 and one ormore outlet apertures34 through which water enters and exits filtercartridge20, respectively.Inlet apertures32 are positioned in an upper portion ofshell22 in either top cap28 (see FIGS. 1 and 2) or an upper portion of body30 (not shown).
[0027]Outlet apertures34 are typically located in thebottom cap29, but could also be on the side ofbody30.Inlet apertures32 andoutlet apertures34 are positioned withinshell22 so that water flowing intoinlet apertures32 goes throughgranular media26 and porousparticulate filter24 prior to exiting outoutlet apertures34.
Porous[0028]particulate filter24 is adhesively connected tobottom cap29 to provide a seal to prevent water from flowing around the bottom offilter24.Bottom cap29 also contains one or moreridged columns31 which, whenbottom cap29 is slid intobody30, will contact a lip of anindentation35 in the interior portion ofbody30 to firmly holdcap29 in place. There are spaces betweenridged columns31 ofcap29 to allow water to flow out offilter cartridge20 throughoutlet apertures34 inbottom cap29.
[0029]Shell22 also has acollar36 acting as a connecting member, which provides a seal between porousparticulate filter24 andfilter cartridge20 so that water flowing throughinlet apertures32 must pass through porousparticulate filter24 before exiting throughoutlet apertures34.Collar36 has an annular cup formed by acylinder37 and abase39. Porousparticulate filter24 is adhesively attached within the annular cup formed bycylinder37 andbase39 to provide a water-tight connection tocollar36. Other methods of sealing porousparticulate filter24 tocartridge20 are also included within the scope of the invention.
[0030]Shell22 is typically constructed of a plastic or polymeric material.Shell22 is preferably made from a molded plastic.
The flow rate of water through porous[0031]particulate filter24 is often diminished by the presence of air adjacent to porousparticulate filter24. Air trapped nearparticulate filter24 forms an interface with the water inparticulate filter24. There will be a surface tension associated with this interface. Unless there is enough pressure to break this surface tension, the water will not flow. Thus, it is desirable that there be a path for the escape of air as it is displaced by water flowing intofilter cartridge20. One advantage of the filter configuration depicted in FIGS. 1 and 2 is that air in the interior of the shape formed by porousparticulate filter24 can flow out the open upper end of porousparticulate filter24 andexit filter cartridge20 throughinlet apertures32.
When[0032]shell22 is provided around porousparticulate filter24, air may also be trapped ingap38 betweenshell22 andparticulate filter24. The presence of trapped air may reduce the flow rate throughfilter24 as the water level withingap38 rises.
[0033]Air outlet apertures40 are provided inshell22 so that the air can escape fromgap38, especially when outlet apertures34 are below the water level of the water treatment device.Air outlet apertures40 are often provided near the upper end ofgap38 which is proximate the sealed connection betweenshell22 and porousparticulate filter24. This configuration will allow most or all of the air to escape the cartridge as air will naturally rise to the highest possible level due to the buoyancy of air in water. In addition to providing an escape path for air,air outlet apertures38 may also function as water outlet apertures.
[0034]Granular media26 is typically disposed withinshell22 to provide additional water purification. As shown in FIG. 2,granular media26 is preferably disposed within porousparticulate filter24. This configuration is advantageous becauseparticulate filter24 will preventgranular media26 from coming out offilter cartridge20. In addition, granular media can be disposed within a separate granularmedia containment region41 of shell22 (see FIG. 2).
[0035]Granular media26 comprises chemicals or materials that are suitable for treating water.Granular media26 typically includes chemicals or other materials that are capable of removing, reducing, or deactivating one or more of the following elements: bad odor, bad taste, organic contaminants, chemical contaminants, and metal or other unwanted ions, such as chlorine. Suitablegranular media26 includes carbon, zeolites, an ion exchange resin, or a combination thereof. A preferred form of carbon for use as granular media is granular activated carbon. A preferred granular media for use in the filter cartridges of the invention is a mixture of a weak-acid cation exchange resin and granular activated carbon.
In one embodiment of the invention, at least a portion of[0036]granular media26 is hydrophilic. Hydrophilic granular media includes granular activated carbon. A hydrophilic granular media disposed within porousparticulate filter24 may facilitate the flow of water through porousparticulate filter24. Hydrophilic granular media in contact with porousparticulate filter24 may provide a less resistive flow path for water into and through the (preferably hydrophilic) sidewalls25 of porousparticulate filter24.
It should be understood that the present invention is not limited to the preferred embodiment described above, which is illustrative only. Changes may be made in detail, especially matters of shape, size, arrangement of parts, or materials of components within the principles of the invention to the full extent indicated by the broad general meanings of the terms in which the appended claims are expressed.[0037]