Abstract: A dual flow filter provides meaningful flow through the base of a monolithic carbon composite filter, creating axial flow, while concurrently providing radial flow through the side walls of the monolithic carbon composite filter element. The filter provides consumers with a more rapidly flowing product offering less pressure drop, i.e., resistance to flow, than other portable filters that have been offered to the consumer, while enhancing the simplicity, utility and esthetics of the product.

Abstract: A portable filtration assembly includes a housing containing a water inlet port and a water outlet port and a sub-micron filter disposed in the housing having hydrophilic sub-micron rated membrane filter elements. The sub-micron filter is configured to effect a six log reduction of bacteria (99.9999%) and a four log reduction of protozoa (99.99%) at a flow rate between 10-30 mL/sec requiring a pressure of 1.5-10 psi. The assembly also includes structure for venting air through the hydrophilic sub-micron rated membrane filter elements. The assembly may additionally include a monolithic radial flow carbon composite filter also disposed in the housing. The monolithic radial flow carbon composite filter is configured for removing at least 80% of chlorine and at least 90% of lead over a minimum of forty gallons at a flow rate of 10 mL/sec at a pressure drop of 10 psi or less.

Abstract: A pitcher or carafe housing is provided that has a raw water reservoir. A high performance filter receives raw water from a lower portion of the reservoir. The water is preferably received at or travels through a water entry tube to the back and bottom of the filter. In about 1-3 minutes the water percolates through the filter element, until it reaches a water exit port. A pouring chamber may be provided at the side of the pitcher for receiving the water from the water exit port, so that the water will continue to be treated and flow up into the pouring chamber until the water level equalizes in height in the reservoir and the pouring chamber. The filter and its housing may be placed into and removed from the inside of the raw water reservoir, or the filer housing may be side loaded. The filter media may be a polyester non-woven mat with a weight of 4-7 oz./yd.2 impregnated with carbon or zeolite and subject to compression between about 25-75% (e.g. about 50%).

Abstract: A pitcher or carafe housing is provided that has a raw water reservoir. A high performance filter receives raw water from a lower portion of the reservoir. The water is preferably received at or travels through a water entry tube to the back and bottom of the filter. In about 1-3 minutes the water percolates through the filter element, until it reaches a water exit port. A pouring chamber may be provided at the side of the pitcher for receiving the water from the water exit port, so that the water will continue to be treated and flow up into the pouring chamber until the water level equalizes in height in the reservoir and the pouring chamber. The filter and its housing may be placed into and removed from the inside of the raw water reservoir, or the filer housing may be side loaded. The filter media may be a polyester non-woven mat with a weight of 4-7 oz./yd.2 impregnated with carbon or zeolite and subject to compression between about 25-75% (e.g. about 50%).

Abstract: A simple yet effective method and apparatus produce a web suitable for treatment of water as a static filtration media, e. g. to remove chlorine and lead from water in contact with the media. A web is coated with a coating composition that facilitates treatment of water and includes a binder, and the web is compressed in one dimension about 25-75% (e. g. 40-60%) so as to make the void size distribution substantially more uniform. The compression is substantially maintained until the binder substantially cures so that the coated final web produced has a second void size distribution more uniform than the first void size distribution, e. g. the coated final web having void volumes with a mean value of about 6-7×10−8 liters and/or an RDV/BV ratio of at least 0.4, and a porosity of greater than 90%.

Abstract: An enhanced static filtration media may comprise a mat body comprising a non-woven of fibers that comply with 21 CFR 177.2260, and having a weight of about 4-7 oz./sq. ft.; a coating on the mat comprising about 100%-200% of the weight of the mat, and including, by weight, about 60-85% activated carbon, about 10-20% binder, and about 0-25% zeolite; and the media mat having an RDV/BV ratio of greater than about 0.4, and a porosity of greater than 90%. Various pitcher constructions make optimal use of the media. In some pitchers, the level of filtered water is easily viewed from the outside while the media is not visible from the outside.

Abstract: A pitcher or carafe housing is provided that has a raw water reservoir. A high performance filter receives raw water from a lower portion of the reservoir. The water is preferably received at or travels through a water entry tube to the back and bottom of the filter. In about 1-3 minutes the water percolates through the filter element, until it reaches a water exit port. A pouring chamber may be provided at the side of the pitcher for receiving the water from the water exit port, so that the water will continue to be treated and flow up into the pouring chamber until the water level equalizes in height in the reservoir and the pouring chamber. The filter and its housing may be placed into and removed from the inside of the raw water reservoir, or the filer housing may be side loaded. The filter media may be a polyester non-woven mat with a weight of 4-7 oz./yd.2 impregnated with carbon or zeolite and subject to compression between about 25-75% (e.g. about 50%).

Abstract: A water treatment system including a bottle with a neck, a tube for disposition within the bottle and having water treatment material (such as activated carbon for removing a significant portion of the chlorine in tap water) associated with it, and a cap. The bottle is filled by causing water to flow through the tube, through the water treatment material, into the bottle. When filled, the bottle neck is closed off by screwing the cap into contact with the neck, the cap closing off the tube so that water does not flow through the tube out of the bottle, but rather exteriorly of the tube through openings in a cap first element and between the tube and the neck. A second element of the cap releasably closes off the water flow openings.

Abstract: A filter assembly for use with a bottle having a circular cross-section neck or open end includes a fine filtration media having a mean pore size of about 1-3 microns and capable of removing contaminants of 3-4 micron size and larger, and an inner filtration media disposed radially inward of the fine filtration media. The inner filtration media includes activated carbon, preferably a porous activated carbon/plastic matrix having a porosity of between about 10-150 microns. The outer housing contains the fine filtration media and the inner filtration media, and is dimensioned to pass through the neck or open end of the bottle. The fine filtration media preferably comprises sheets on opposite faces of a microfiber filter media formed of glass microfibers of varying cross-sectional diameters, with the fine filtration media in a pleated or accordion configuration. A filter assembly may also be provided having a spring pressed straw.