US20070267357A1 - Method and apparatus for liquid purification - Google Patents
Method and apparatus for liquid purification Download PDFInfo
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- US20070267357A1 US20070267357A1 US11/774,560 US77456007A US2007267357A1 US 20070267357 A1 US20070267357 A1 US 20070267357A1 US 77456007 A US77456007 A US 77456007A US 2007267357 A1 US2007267357 A1 US 2007267357A1
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Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
- B01J19/2405—Stationary reactors without moving elements inside provoking a turbulent flow of the reactants, such as in cyclones, or having a high Reynolds-number
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
- B01J19/248—Reactors comprising multiple separated flow channels
- B01J19/2495—Net-type reactors
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
- C02F1/325—Irradiation devices or lamp constructions
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
- C02F9/20—Portable or detachable small-scale multistage treatment devices, e.g. point of use or laboratory water purification systems
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00164—Controlling or regulating processes controlling the flow
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/32—Details relating to UV-irradiation devices
- C02F2201/322—Lamp arrangement
- C02F2201/3226—Units using UV-light emitting lasers
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/03—Pressure
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/40—Liquid flow rate
Abstract
An apparatus and method for purifying a liquid comprising a photolytic light chamber producing ultraviolet light in the 100 to 300 nanometer range, said light passing through a quartz tube or lens to irradiate the liquid passing through a chamber containing the liquid.
Description
- This application is a division of application Ser. No. 10/9805039, filed on Dec. 13, 2004 in the name of the same inventor.
- Presently, the quality of the global pure drinking water supply is decreasing at a faster rate than the population is expanding. The United Nations International children's Educational Foundation (UNICEF) estimates that 20,000 to 30,000 children die every day from waterborne diseases such as typhoid, malaria, e-coli, cholera and many other contaminants. These contaminants can also include such things as salts, halogens, organic solvents, pesticides, fertilizers, industrial chemicals, bacteria, protozoa, fungi and other foreign matters.
- The extensive use of fertilizers and pesticides by farmers, runoffs from major animal husbandry sites, contamination spills by industries, the dumping of raw sewage into our lakes and streams and the significant number of landfill sites have caused many contaminants to percolate down through the soil and into the underlying water tables throughout the world. The result is that today many more wells and springs are now testing positive for a wide array of toxins and contaminants harmful to human, animal and plant health.
- In many areas of the world, and in the United States of America, public water supply systems are monitored for diseases and toxins on a regular basis to assure the public that the water is safe to drink. However, cases are still reported in the U.S. of contaminated water supply systems. Furthermore the majority of the water piping and distribution systems in the U.S., and internationally, are many decades old and as the water passes from a main purification site to an end user, the water can pickup additional contaminants and toxins from the aging water distribution systems.
- There have been a variety of attempts to provide purified water at a user or business' point of entry and/or point of use site. One such device is known as the Britta. It is a single stage filter utilizing the laws of gravity and a carbon block held in a container. Water is poured into a top holding container and gravity slowly draws the water through the carbon block to a lower container for consumption. Carbon does reduce some toxic chemicals and gases from water however it does not purify the water. This device is also greatly limited by the capacity of water that it can produce in a 24-hour period. It most certainly would not produce enough filtered water to supply a family of four with enough drinking and cooking water for an entire day.
- There are other products available that provide two stage filtering devices consisting of a carbon block filtration and a paper filter surrounding or in line with the carbon block. However, these systems do not address the issue of microorganisms in the water, which can bypass the filtration systems.
- Yet another product available to consumers is a device called the Pur water filter. This system utilizes a small and low wattage ultraviolet (UV) lamp and a carbon block filter. The UV light is known to kill microorganisms in the air and in water. Unfortunately, the UV lamp deteriorates over time to the point that it cannot produce the necessary wavelength to kill microorganisms in the water. Furthermore, the system does not provide a means to know when the UV lamp has deteriorated. As such, the end user may think that the device is adequately killing microorganisms when in fact the UV lamp has become useless as a biocide. The use of a laser for producing UV light for treating water has also been described by Goudy in U.S. Pat. No. 4,661,264
- Another additional means of purifying water has been the use of what is known as KDF 85 and/or KDF 55 as a biocide and is described by Heskett in U.S. Pat. No. 5,951,869. This process utilizes a compound that is basically copper and zinc that creates and ion exchange and chelating (clumping together) producing properties in the water. This material is primarily used in large municipal water treating systems however there have been some attempts to have the KDF 85 or KDF 55 material impregnated onto a paper filter for point of use water treatment systems with limited success.
- While all of the above presented means provide some degree for improving the water supply, none of them fully purify the water in an economical and efficient manner. As such, a technical need still exists to purify water, air or other fluids quickly, efficiently, over a long-term use and do so economically.
- The invention will be better understood by reading the detailed description of the preferred embodiments of the invention along with a review of the drawings, in which:
-
FIG. 1 is an overall view of the various components of the invention; -
FIG. 2 is a cross-sectional view of the first collective filtration unit used in the embodiment ofFIG. 1 ; -
FIG. 3 is a cross-sectional view of the molecular reaction chamber used in the embodiment ofFIG. 1 ; -
FIG. 4 is a planer view of the first and second photolytic light chambers used in the embodiment ofFIG. 1 ; -
FIG. 5 is a cross-sectional view of the second collective filtration unit used in the embodiment ofFIG. 1 ; -
FIG. 6 is a cross-sectional view of the carbon filter used in the embodiment ofFIG. 1 ; -
FIG. 7 is a view of the cover that covers and protects the entire unit show inFIG. 1 ; and -
FIG. 8 is a planer view of the pressure gauge. -
FIG. 9 is a cross sectional planar view of the molecular reaction chamber depicting a plurality of internal mesh screens. - Reference will now be made in detail to the description of the invention as illustrated in the drawings. Although the preferred embodiments of the invention will be described in connection with these drawings, there is no intent to limit the invention to the embodiment or embodiments disclosed therein. On the contrary, the intent is to include all alternatives, modifications and equivalents included within the spirit and scope of the invention as defined by the appended claims.
- Furthermore, the order of the itemized steps in
FIG. 1 are not meant to limit the scope of the invention to the specific itemized order of those steps, but rather to include those steps in any relevant order including any alternatives, modifications and equivalents included within the spirit and scope of the invention as defined by the appended claims. - To aid in the understanding of the invention, examples of some of the specific itemized steps are provided for clarification purposes only. In particular, some of the examples use water for the liquid being purified, however, these examples are not meant to limit the invention to only water, but rather to include any alternative, modification and equivalents included within the spirit and scope of the invention as defined by the appended claims.
- The present invention provides a method and apparatus for treating water or other liquid to assure that the water or liquid is of a high degree of purity. The origin of the water or liquid can be from any source such as municipal water supply systems, independent well systems, tanker truck or rail car, a lake, a river, desalinized sea water, collected rail water or other like source.
-
FIG. 1 depicts an overall view of the liquid treating apparatus 1 without the cover for the apparatus. The cover is shown later inFIG. 7 . The liquid treating apparatus 1 contains a base 2 to which elements of the liquid treating apparatus are connected. The base 2 is constructed with a plurality of mounting holes 3 such that the liquid treating apparatus can be mounted to a wall (not shown) or a frame (not shown). Other equally effective mounting systems are well known in the art. - The water or other liquid (not shown) flows from a pressurized source (not shown) through the inlet pipe 4 through a
pressure regulator 5 through afirst transfer pipe 6 and then through a flow indicator 7. Thepressure regulator 5 assures that the liquid is maintained at or below a predetermined pressure setting for optimal operating efficiency of the liquid treating apparatus 1. The flow meter 7 is connected 8 to the laserlight source generator 9 such that the laserlight source generator 9 only generates a laser light (not shown) in the ultraviolet range when the flow indicator 7 indicates that liquid is flowing through the liquid treating apparatus 1. As the liquid exits the flow indicator the liquid travels through asecond transfer pipe 10 to the first stage of the liquid treatment apparatus 1. - The first stage of the liquid treatment apparatus 1 is the primary
collective filtration unit 11. The primary collective filtration unit 11 (shown in detail inFIG. 2 ) contains a 5.0 micron filter whose primary purpose is to prevent any chemical, particulate matter or other media 5.0 microns or larger from traveling any further than this stage in the liquid treating apparatus 1. - The liquid then exits the primary
collective filtration unit 11 and travels through athird transfer pipe 12 to the second stage of the liquid treatment apparatus 1. The second stage of the liquid treatment apparatus 1 is amolecular reaction unit 13, called the Hydro-Media Reaction Chamber, that functions as an effective biocide. The details and design of themolecular reaction unit 13 is discussed in greater detail in relation toFIG. 3 later in this description of the invention. - The liquid then exits the
molecular reaction unit 13 and flows through afourth transfer pipe 14 to the third stage of the liquid treatment apparatus 1. The third stage of liquid treatment apparatus is a firstphotolytic laser chamber 15 in which the liquid is subjected to ultraviolet light in the 100 to 300 nanometer range produced by a laserlight source generator 9 and received by alaser light receiver 16. This process acts as a biocide by altering the contaminants so that they can be filtered out later and removes volatile organic compounds. The ultraviolet light destroys organic compounds by breaking the covalent bonds in the chemical thereby forming free radicals which react with water and break down into harmless substances. Details of the first and second photolyticlight chambers FIG. 4 . - The liquid then exits the first
photolytic laser chamber 15 through afifth transfer pipe 17 and enters a secondarycollective filtration unit 18. The secondarycollective filtration unit 18 utilizes a 0.5 micron filter which traps or collects all of the destroyed microorganisms that were affected by the firstphotolytic laser chamber 15 and any particulate matter or other media that is 0.5 microns in size or larger. Details of the secondarycollective filtration unit 18 are shown inFIG. 5 . - The liquid then exits the secondary
collective filtration unit 18 and travels through asixth transfer pipe 19 to acarbon filtration unit 20. Thecarbon filtration unit 20 utilizes a pharmaceutical grade granular activated carbon filter. This unit removes odors, chlorine, benzenes and other aromatic ring structures, pesticides and many other volatile organic hydrocarbons that may be found in various combinations in water and/or other liquids. The granular configuration of the activated carbon provides an effective method for maintaining a desired liquid flow rate with maximum beneficial results in eliminating the aforementioned odors and compounds. Details of thecarbon filtration unit 20 are shown inFIG. 6 . - The liquid then exits the
carbon filtration unit 20 through aseventh transfer pipe 21 and enters a secondphotolytic laser chamber 22. The secondphotolytic laser chamber 22 also operates in the 100 to 300 nanometer range. This secondphotolytic laser chamber 22 is the final stage in the liquid treatment apparatus 1 and assures that the liquid and/or water leaving the unit is free from microorganisms by subjecting the liquid or water to a second ultraviolet light process identical to the firstphotolytic laser chamber 15. This provides additional protection to overcome any effects of colonization or of filtration failure. The water or other liquid then exits the unit through aneighth transfer pipe 23. - The
eighth transfer pipe 23 is then connected to apressure gage 24 which is in turn connected to the out goingliquid supply line 25. Thepressure gage 24 is color coded in red, yellow and green zones. When thepressure gage 24 indicates that the liquid pressure in the liquid treatment apparatus 1 is in the green zone, the filters do not have to be replaced. When thepressure gage 24 indicates that the liquid pressure is in the yellow zone, it is time to prepare for changing the filters or to change the filters. When thepressure gage 24 indicates that the liquid pressure is in the red zone, the filters should be replaced. Details of thepressure gage 24 are shown inFIG. 8 . -
FIG. 2 depicts a cross-sectional view of the primarycollection filtration unit 11. This unit consists of acap 26 with aliquid inlet chamber 27 and aliquid outlet chamber 28. Thecap 26 is attached to the removable primarycollection filtration body 29 with an o-ring 30 between thecap 26 and theremovable filtration body 29 to prevent liquid leakage. Inside the primarycollection filtration unit 11 is a 5.0micron filter 31 for the collection of contaminants 5.0 microns in size or larger. In operation, the liquid flows through thesecond transfer pipe 10 into theliquid inlet chamber 27 and into the center of thefilter 32. The liquid then passes through thefilter 31 trapping any objects 5.0 microns in size or larger and exits thecollection filtration body 29 through theoutlet chamber 28 and thethird transfer pipe 12 attached to thecap 26. Thecap 26 also has ableeder valve 33 for bleeding off excess air when the unit is initialized or after replacing thefilter 31. -
FIG. 3 shows a sectional view of themolecular reaction unit 13. Themolecular reaction unit 13 has anupper cap 34 with aliquid inlet chamber 35 and aliquid outlet chamber 36. Thethird transfer pipe 12 is connected to theliquid inlet chamber 35 and thefourth transfer pipe 14 is connected to theliquid outlet chamber 36. Thecap 34 is secured to a removablereaction chamber body 37 with an o-ring 38 between thecap 34 and thereaction chamber body 37. Afilter pad 39, preferably polypropylene or nylon, separates the interior of theupper reaction chamber 40 and theoutlet chamber 36 located in thecap 34. Attached to thecap 34 is aninternal supply tube 41 that extends down to almost the base of thereaction chamber body 37 and within but not touching theconical screen 46 as shown inFIG. 3 . Attached near the center of theinternal supply tube 41 is amiddle mesh screen 42, preferably made of stainless steel that separates theupper reaction chamber 40 from thelower reaction chamber 43. Placed inside of both the upper andlower reaction chambers reaction material 44, preferably a material called KDF 85 and/orKDF 55 as identified and described by Heskett in U.S. Pat. No. 5,951,869. However,other reaction materials 44 are available that could be utilized in place of the KDF 85 and/orKDF 55 and/or in conjunction with theKDF reaction materials 44. Fixedly attached to theinternal supply tube 41 near its base within but not in contact with theconical screen 46 as shown inFIG. 3 is a solid dual funnel shapedobject 45 called the dual funnel. At the base of theinternal supply tube 41 is a conically shapedmesh screen 46 as shown inFIG. 3 , preferably made of stainless steel that covers the internal supply tube opening and wraps up and around the cylindrically shapeddeflector cup 47 shown inFIG. 3 and is fixedly attached to the top of thedeflector cup 47. Themesh screen 46 assures that thereaction material 44 stays above thedeflector cup 47 in thelower reaction chamber 43 in order to assure that thereaction material 44 operates in a turbulent manner with the liquid in thelower reaction chamber 43 when the liquid is flowing through the liquid treatment apparatus 1. Also attached to thedeflector cup 47 is thelower chamber funnel 48. Surrounding thedeflector cup 47 is amedia bed 49 used to fill in the space between thedeflector cup 47, thelower chamber funnel 48 and thereaction chamber body 37. Themedia bed 49 is a man made gravel of consistent size and shape. Thecap 34 also has ableeder valve 50 to release excess air when the unit is initialized or theionization material 44 is replaced. - The operation of the
molecular reaction unit 13 will now be described in detail. Water or other liquid under pressure enters themolecular reaction unit 13 through theliquid inlet chamber 35 and travels down theinternal supply tube 41 where the liquid exits the internal supply tube after passing through amesh screen 46. The liquid is then directed upward by the shape of thedeflector cup 47. As the liquid travels upward it again must pass through themesh screen 46 going between the base of theinternal supply tube 41 and the top of thedeflector cup 47. Themesh screen 46 prevents any reactive material from going into thedeflector cup 47. As the liquid passes between thelower chamber funnel 48 and thedual funnel 45, the liquid gains speed and force due to the restriction of the opening between thelower chamber funnel 48 and thedual funnel 45. The force of the liquid exiting thedual funnel 45 and thelower chamber funnel 48 causes thereaction material 44 to go into turbulent suspension with the liquid. As the liquid rises in themolecular reaction unit 13, the turbulence slows due to the greater opening in the upper andlower reaction chambers middle mesh screen 42 traps thereaction material 44 into thelower reaction chamber 43. Thereaction material 44 in theupper reaction chambers 40 stays in non-turbulent suspension near themiddle mesh screen 42. In use, thereaction material 44 exchanges electrons with contaminants within the liquid thereby causing either an oxidation effect or a reduction effect on the contaminants which causes the contaminants to change into a harmless form that can be filtered out later. The liquid then rises to the top of thereaction unit 13, passes through thefilter pad 39 which keeps all of thereaction material 44 in theupper reaction chamber 40 and the liquid then exits through theoutlet chamber 36 into thefourth transfer pipe 14. - In an alternate embodiment of the
molecular reaction unit 13, there can be a plurality of additional mesh screens 42 between theoriginal mesh screen 42 and thecap 34. This would create additional reaction chambers shown inFIG. 9 in which additionalreactive materials 44 could be placed. The additional reactive chambers and reactive materials can be additional oralternative reaction materials 44 other than KDF 85 and/orKDF 55 that would operate in addition to or as a substitute for thefirst reaction materials 44. Some of the additionalreactive materials 44 may require that themolecular reaction unit 13 be periodically back flushed in order to cleanse themolecular reaction unit 13. -
FIG. 4 depicts the preferred embodiment of the design of the first and second photolyticlight chambers light chamber 22 is the laserlight source generator 9 and on one end of the first photolyticlight chamber 15 is thelaser light receiver 16. In between thegenerator 9 and thereceiver 16 is a continuoushollow quartz tube 51 through which the laser light (not shown) travels in operation. Afirst tube 52 surrounds a first portion of thequartz tube 51 and is sealed around the quartz tube at both ends of thetube space 55 through which the liquid will pass around thequartz tube 51 when the unit is in operation. This creates the first photolyticlight chamber 15. Asecond tube 56 surrounds a second portion of thequartz tube 51 and is sealed 57 and 58 at both ends of thetube 56 around thequartz tube 51. There is aspace 59 between thequartz tube 51 and thetube 56 through which the liquid will pass around thequartz tube 51. Thespaces laser light generator 9 and received by thelaser light receiver 16. - In the first and second photolytic
light chambers first transfer pipe 6, theflow meter 6 sends a signal through theconnection 8 to thelaser light generator 9 which activates the laser light. A laser light, in the 100 to 300 nanometer range, travels through the inside of thequartz tube 51 to thelaser light receiver 16. As the liquid flows through thespaces light chambers - When the liquid or water stops flowing as indicated by the flow meter 7, the
laser light generator 9 shuts off the laser light source so that thelaser light source 9 and the power consumption is only used when there is liquid flowing through the system. In addition, thelaser light generator 9 can be set to operate in a specific range such as 185 or 254 nanometers, or is can be set to oscillate or switch between two or more nanometer ranges for optimum performance. Some of the more obvious advantages to this design is the use of a single source of light for a creating a multitude of exposures and the ability to target a range of ultraviolet light on the liquid to be treated as opposed to a single wavelength. In addition, an ultraviolet light produced by a laser light source will not degenerate over time as does an ultraviolet lamp thus providing a long and economical useful life of the unit. - In an alternative embodiment to the photolytic
light chambers quartz rod 51 or other lens like material that connects the end of the first photolyticlight chamber 15 to the end of the second photolyticlight chamber 22 and allows for the passing of the laser light in the 100 to 300 nanometer range, without inhibiting the laser light spectrum, from the first photolyticlight chamber 15 to the second photolyticlight chamber 22. Usage of a lens or other device attached between the two photolytic chambers allows transfer of the laser beam through both chambers simultaneously and also denies crossover contamination of the liquid. Thus, instead of the liquid being exposed to the ultraviolet light radiating outward from thequartz tube 51, the liquid is exposed directly to the ultraviolet laser light inside of the photolyticlight chambers rod 51 could be placed in front of thelaser light generator 9 and in front of thelaser light receiver 16 which would prevent any direct conductive connection between the liquid and thelaser light generator 9 and/or thelaser light receiver 16. In another alternate embodiment, the inside of the first andsecond tubes light chamber 15 can be placed in a horizontal position and the second photolyticlight chamber 22 placed in a vertical position with a reflective material used to bend the laser light from a horizontal position to a vertical position. - As the liquid exits the first photolytic
light chamber 15, the liquid travels through afifth transfer pipe 17 to the secondarycollective filtration unit 18 shown in the cross-section view inFIG. 5 . The secondarycollective filtration unit 18 has acap 60 with aliquid inlet chamber 61 and aliquid outlet chamber 62. Thecap 60 also has ableeder valve 66 to release excess air when the liquid treatment apparatus 1 is initialized or thefilter 65 is replaced. Between thecap 60 and theremovable filter body 63, there is an o-ring 64 for sealing thecap 60 to thebody 63. Inside of thefilter body 63, there is a 0.5micron filter 65. As a liquid enters thefilter body 63 through thewater inlet chamber 61, the liquid is forced to pass through the 0.5micron filter 65 before passing out through thewater outlet chamber 62 and through thesixth transfer pipe 19. This filtration process deals with the smallest particulates and microorganisms. Due to the aggressiveness of the combination of theionization unit 13 and the first photolyticlight chamber 15, the possibility of colonization of any microorganisms is significantly reduced. - Upon exiting the secondary
collective filtration unit 18, the liquid travels to thecarbon filtration unit 20 shown in a cross-sectional view inFIG. 6 . Thecarbon filtration unit 20 has acap 68 with aliquid inlet chamber 69 and aliquid outlet chamber 70. Thecap 68 also has ableeder valve 74 to release excess air when the liquid treatment apparatus 1 is initialized and/or the activatedcarbon filter 73 is replaced. Between thecap 68 and the removablecarbon filter body 71 there is an o-ring 72 for sealing thefilter assembly 20 from any leakage. Inside of thecarbon filter body 71 there is a pharmaceutical grade granular activatedcarbon filter 73. As the liquid enters thecarbon filter body 71 the liquid is forced to pass through the activatedcarbon filter 73 and exits out of theliquid outlet chamber 70 and through theseventh transfer pipe 21. The activated carbongranular filter 73 removes odors, chlorine, herbicides, benzenes and other aromatic ring structures, pesticides and many other volatile organic hydrocarbons that may be present in various water sources, including municipal water supplies, as the water moves through thecarbon filtration unit 20. - Upon exiting the
carbon filtration unit 20, the liquid travels to the second photolyticlight chamber 22 shown inFIGS. 1 and 4 . This final stage in the liquid purification process is a final ultravioletlight laser chamber 22 that operates in the same manner as described in the first photolyticlight chamber 15 above. This second photolyticlight chamber 22 assures that the liquid is free of any microorganisms by providing a secondary ultraviolet light treatment to overcome any effects of colonization and/or filtration failure that may have occurred in the prior treatment stages. -
FIG. 7 depicts thecover 75 for the liquid treating apparatus 1. The cover is secured to the base 2 with screws or other attachment means (not shown) to keep dust and dirt out and to prevent people or animals from coming in unnecessary contact with the components of the liquid treatment apparatus 1. This cover may be partially or fully clear or transparent and/or have a sight window present in thecover 75 allowing visual opportunity available for people to monitor the liquid treatment apparatus 1 in operation. -
FIG. 8 depicts thepressure gage 24 where in thegage 24 is colored coded into three zones,zone A 77 in which thefilters zone B 78 in which it is time to prepare to change thefilters filters zone C 79 wherein thefilters
Claims (14)
1. A method for killing all life forms in a liquid comprising the steps of:
a. supplying said liquid under pressure to a first tube;
b. exposing said liquid in said first tube to a light source in the 100 to 300 nanometer range from a first end of said tube;
c. receiving said light in a light receiver at a second end of said first tube, wherein the said light is only generated when said liquid is flowing through said first tube; and
d. exiting the light treated liquid from said first tube.
2. The method as defined by claim 1 , wherein said steps comprises controls for exposing said liquid to said light in a specific wavelength that can be preset and/or that can be set by a user.
3. The method as defined by claim 1 , wherein said steps comprises controls for exposing said liquid to oscillating wavelength spectrums of said light within different nanometer ranges at a pre-selected and/or user set wavelength spectrum and/or oscillation speed.
4. The method as defined in any one of claims 1 through 3, wherein said steps comprise:
separating said light source from said liquid in said first tube in a manner that allows said light to pass through said separating medium without diminishing said light wavelength spectrum; and
separating said liquid from said light receiver in a manner that allows said light to pass through to said light receiver and does not diminish said light wavelength spectrum.
5. The method as defined in any one of claims 1 through 3, wherein said steps comprise:
providing an inner tube, made of a material that allows light in the 100 to 300 nanometer range to radiate through the walls of said inner tube without diminishing the wavelength light spectrum that is fixedly connected to both ends of the said first tube such that there is no leakage between said first tube and said inner tube, said inner tube being smaller in diameter than the inner walls of said first tube such that there is a space between said inner and said first tubes for said liquid to pass through; and
exposing said liquid to a said light in the 100 to 300 nanometer spectrums that passes through said inner tube to said receiver without having direct contact with said liquid passing through said space between said inner and said first tubes.
6. The method as defined in any one of claims 1 through 3 wherein said method of generating light is a laser light generator.
7. The method as defined in any one of claims 1 through 3, wherein the inner side of the said outer tube is finished to refract said light back through said liquid.
8. A method for killing all life forms in a liquid comprising the steps of:
a. supplying said liquid under pressure to a first tube;
b. exposing said liquid in said first tube to a light source in the 100 to 300 nanometer range through a lens attached between said first tube and said light source, wherein the said light is only generated when said liquid is flowing through said first tube; and
d. exiting the light treated liquid from said first tube.
9. The method as defined by claim 8 , wherein said steps comprises controls for exposing said liquid to said light in a specific wavelength that can be preset and/or that can be set by a user.
10. The method as defined by claim 8 , wherein said steps comprises controls for exposing said liquid to oscillating wavelength spectrums of said light within different nanometer ranges at a pre-selected and/or user set wavelength spectrum and/or oscillation speed.
11. The method as defined in any one of claims 8 through 10, wherein said steps comprise separating said light source from said liquid in said first tube in a manner that allows said light to pass through said separating medium without diminishing said light wavelength spectrum.
12. The method as defined in any one of claims 8 through 10, wherein said steps comprise:
providing an inner tube, made of a material that allows light in the 100 to 300 nanometer range to radiate through the walls of said inner tube without diminishing the wavelength light spectrum that is fixedly connected to both ends of the said first tube such that there is no leakage between said first tube and said inner tube, said inner tube being smaller in diameter than the inner walls of said first tube such that there is a space between said inner and said first tubes for said liquid to pass through; and
exposing said liquid to a said light in the 100 to 300 nanometer spectrums that passes through said inner tube to said receiver without having direct contact with said liquid passing through said space between said inner and said first tubes.
13. The method as defined in any one of claims 8 through 10 wherein said method of generating light is a laser light generator.
14. The method as defined in any one of claims 8 through 10, wherein the inner side of the said outer tube is finished to refract said light back through said liquid.
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
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US11/774,560 US20070267357A1 (en) | 2004-12-13 | 2007-07-07 | Method and apparatus for liquid purification |
US12/134,739 US7740754B2 (en) | 2004-12-13 | 2008-06-06 | Apparatus for purifying a liquid |
US12/145,278 US20090010812A1 (en) | 2004-12-13 | 2008-06-24 | Apparatus and means for controlling temperature during liquid purification |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/905,039 US7255789B2 (en) | 2004-12-13 | 2004-12-13 | Method and apparatus for liquid purification |
US11/774,560 US20070267357A1 (en) | 2004-12-13 | 2007-07-07 | Method and apparatus for liquid purification |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US10/905,039 Division US7255789B2 (en) | 2004-12-13 | 2004-12-13 | Method and apparatus for liquid purification |
Related Child Applications (2)
Application Number | Title | Priority Date | Filing Date |
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US10/905,039 Division US7255789B2 (en) | 2004-12-13 | 2004-12-13 | Method and apparatus for liquid purification |
US12/145,278 Continuation-In-Part US20090010812A1 (en) | 2004-12-13 | 2008-06-24 | Apparatus and means for controlling temperature during liquid purification |
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US20070267357A1 true US20070267357A1 (en) | 2007-11-22 |
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US11/774,560 Abandoned US20070267357A1 (en) | 2004-12-13 | 2007-07-07 | Method and apparatus for liquid purification |
US12/134,739 Expired - Fee Related US7740754B2 (en) | 2004-12-13 | 2008-06-06 | Apparatus for purifying a liquid |
US12/134,658 Abandoned US20080257833A1 (en) | 2004-12-13 | 2008-06-06 | Method and apparatus for liquid purification |
US12/134,718 Expired - Fee Related US7731858B2 (en) | 2004-12-13 | 2008-06-06 | Method for liquid purification using a molecular reaction unit |
US12/135,407 Abandoned US20090008266A1 (en) | 2004-12-13 | 2008-06-09 | Method and apparatus for liquid purification |
US12/135,396 Abandoned US20090008309A1 (en) | 2004-12-13 | 2008-06-09 | Method and apparatus for liquid purification |
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US10/905,039 Expired - Fee Related US7255789B2 (en) | 2004-12-13 | 2004-12-13 | Method and apparatus for liquid purification |
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US12/134,739 Expired - Fee Related US7740754B2 (en) | 2004-12-13 | 2008-06-06 | Apparatus for purifying a liquid |
US12/134,658 Abandoned US20080257833A1 (en) | 2004-12-13 | 2008-06-06 | Method and apparatus for liquid purification |
US12/134,718 Expired - Fee Related US7731858B2 (en) | 2004-12-13 | 2008-06-06 | Method for liquid purification using a molecular reaction unit |
US12/135,407 Abandoned US20090008266A1 (en) | 2004-12-13 | 2008-06-09 | Method and apparatus for liquid purification |
US12/135,396 Abandoned US20090008309A1 (en) | 2004-12-13 | 2008-06-09 | Method and apparatus for liquid purification |
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US10207936B2 (en) | 2016-02-19 | 2019-02-19 | Silanna UV Technologies Pte Ltd | Ultraviolet reactor with planar light source |
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CN107032552A (en) * | 2017-04-20 | 2017-08-11 | 温州市鹿城区中津先进科技研究院 | Sewage disposal network by node of laser machining device |
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Also Published As
Publication number | Publication date |
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WO2006065697A2 (en) | 2006-06-22 |
US20080308473A1 (en) | 2008-12-18 |
US20080257833A1 (en) | 2008-10-23 |
US7740754B2 (en) | 2010-06-22 |
US20060124556A1 (en) | 2006-06-15 |
WO2006065697A3 (en) | 2006-09-21 |
US20090008266A1 (en) | 2009-01-08 |
US7731858B2 (en) | 2010-06-08 |
US20080230486A1 (en) | 2008-09-25 |
US20090008309A1 (en) | 2009-01-08 |
US7255789B2 (en) | 2007-08-14 |
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