Apparatus and Process for Filtering and Mineralizing a Fluid
20220387934 · 2022-12-08
Inventors
Cpc classification
C02F9/20
CHEMISTRY; METALLURGY
Y02W10/37
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
B01D61/10
PERFORMING OPERATIONS; TRANSPORTING
B01D61/025
PERFORMING OPERATIONS; TRANSPORTING
C02F2201/3222
CHEMISTRY; METALLURGY
B01D2313/60
PERFORMING OPERATIONS; TRANSPORTING
C02F1/68
CHEMISTRY; METALLURGY
C02F2307/10
CHEMISTRY; METALLURGY
C02F1/283
CHEMISTRY; METALLURGY
International classification
B01D61/10
PERFORMING OPERATIONS; TRANSPORTING
B01D61/02
PERFORMING OPERATIONS; TRANSPORTING
Abstract
An apparatus for filtering and mineralizing a fluid. The apparatus includes an amount of contaminated fluid located in a reservoir and a cartridge that is located downstream from the reservoir and in fluid communication with it. A filter is in fluid communication with the reservoir and the cartridge. The contaminated fluid is pumped along a pathway from the reservoir to the cartridge so that the contaminated fluid moves through the filter to generate filtered fluid in the cartridge. A pre-determined amount of an additive is associated with the cartridge for adding to the filtered fluid to generate a final fluid with the amount of the additive material.
Claims
1-39. (canceled)
40. An apparatus for filtering and mineralizing a fluid, the apparatus comprising: an amount of contaminated fluid located in a first reservoir; a cartridge located downstream from the first reservoir and in fluid communication therewith; a filter member in fluid communication with the first reservoir and the cartridge, the contaminated fluid being pumped along a fluid pathway from the first reservoir to the cartridge so that the contaminated fluid contacts the filter member and moves therethrough so as to generate an amount of a filtered fluid in the cartridge; and a pre-determined amount of an additive material associated with the cartridge for adding to the filtered fluid so as to generate an amount of a final fluid having therein the amount of the additive material.
41. The apparatus, according to claim 40, further comprising: i) a pump; ii) a first conduit connected to the first reservoir and the pump; and, iii) a second conduit connected to the pump and the cartridge; wherein the filter member is located between the pump and the cartridge.
42. The apparatus, according to claim 41, wherein the filter member is a reverse osmosis filter.
43. The apparatus, according to claim 40, wherein the filter member is located between the first reservoir and the cartridge.
44. The apparatus, according to claim 40, wherein the additive material includes user specific minerals, vitamins, nutrients, and micro-nutrients.
45. The apparatus, according to claim 40, wherein the additive material is a liquid concentrate solution.
46. The apparatus, according to claim 41, wherein the pump pressurizes the first fluid to a predefined pressure between 80 PSI and 130 PSI pressure.
47. The apparatus, according to claim 40, further comprising a refrigeration unit to cool the filtered fluid and the final fluid exiting the cartridge, or an instant heating module to provide boiling purified or mineralised water.
48. The apparatus, according to claim 40, wherein a peristaltic pump connects the additive material to the cartridge so as to dispense additive material thereinto.
49. The apparatus, according to claim 40, further comprising a flow meter, a flow rate sensor, load cell and/or weight sensor located downstream of the cartridge.
50. The apparatus, according to claim 40, further comprising a UVC LED is located in the water holding tank to ensure that the purified water remains sterile while held in an intermediary tank
51. The apparatus, according to claim 40, wherein the fluid is water.
52. A process for filtering and mineralizing contaminated water, the process comprising: filtering an amount of contaminated water from a first reservoir by pumping the contaminated water from the first reservoir through a filter member into a cartridge, the cartridge being located downstream of the first reservoir so as to generate an amount of filtered water; and adding a predetermined amount of an additive material to the filtered water so as to generated a final water product, the pressure in the cartridge being sufficient to expel the final water product out of the cartridge and into a second reservoir.
53. The process, according to claim 52, wherein the pressure in the cartridge is between 80 PSI and 130 PSI.
54. The process, according to claim 52, wherein the additive material includes user specific minerals, vitamins, nutrients, and micro-nutrients.
Description
BRIEF DESCRIPTION OF FIGURES
[0048] These and other features of that described herein will become more apparent from the following description in which reference is made to the appended drawings wherein:
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DETAILED DESCRIPTION
Definitions
[0063] Unless otherwise specified, the following definitions apply:
[0064] The singular forms “a”, “an” and “the” include corresponding plural references unless the context clearly dictates otherwise.
[0065] As used herein, the term “comprising” is intended to mean that the list of elements following the word “comprising” are required or mandatory but that other elements are optional and may or may not be present.
[0066] As used herein, the term “consisting of” is intended to mean including and limited to whatever follows the phrase “consisting of”. Thus, the phrase “consisting of” indicates that the listed elements are required or mandatory and that no other elements may be present.
[0067] Referring now to
[0068] It should be noted that the description uses the term “fluid”, which a person skilled in the art will recognize is a generic term which covers liquid and gas. In the examples used throughout, the fluid is water.
[0069] Generally speaking, our apparatus combines a Sediment+Carbon and Reverse osmosis membrane into a single filter housing designed to promote a user-centric design. Our cartridge has a lifespan of 6 to 12 months depending on consumption. The sediment and carbon filters are presented as a single module containing the specific elements. Moreover, our apparatus is able to dispense a liquid drop-by-drop by using a peristaltic pump capable of dispensing at a rate as low as 0.5 mL/min. A significant advantage that our apparatus realizes is the combination of the reverse osmosis plus liquid mineralisation plus peristaltic pump which allows us to recreate any currently available water brand. This is done by carefully selecting the correct liquid concentrate and dosage. We are now able to add vitamins to the water produced given the use of the liquid mineralisation system. Conventional water purification devices mostly use “hard remineralisation” using a combination of granules, but these cannot be used with vitamins since hard mineralisation granules cannot currently be enriched with vitamins.
[0070] Generally speaking, reverse osmosis systems “Waste Water” or “Brine Water” as a by-product. This water contains the impurities that are collected by the reverse osmosis membrane. The flushing avoids the reverse osmosis membrane from clogging (commonly referred to as “membrane fouling”). Most conventional systems ask that this water be discarded, when not done automatically. This brine water is very rich in dissolved solids and minerals. In one embodiment, our design collects the brine water in a separate tank that encourages the user to use it to water house plants or their gardens given the nutritional value of this water for plants.
[0071] Our mineral concentrate can be supplied in bottles with a foil seal at the top of the bottle. The bottles would be easily recyclable or ideally made from recycled plastic. This avoids extra cost in having cartridges made and filled with a concentrate, which has a risk of potential contamination and (the more expensive) cartridges would be difficult to recycle (multi-material).
[0072] Broadly speaking, the apparatus 100 includes a first reservoir (a housing for pre-treated or contaminated water) 110 for storing or collecting an amount of contaminated water therein. The reservoir 110 is sized and shaped to define an impure or non-treated water storage space. The reservoir 110 includes a closable opening 115 located on the side of the reservoir 110 which permits the pre-treated water to be poured into the reservoir 110. The closable opening 115 can be of a relatively large diameter or radius in order to allow users to clean the inside of the reservoir 110 when required. The reservoir 110 requires cleaning since the impure water placed into the impure water housing 110 often contains impurities such as limestone that accumulate over time.
[0073] Fluidly connected to the reservoir 110 and downstream therefrom is a pump 125 of specific strength and capacity. A conduit 120 in the form of a first tubing is connected to the pump 125 from a pump inlet to the impure water reservoir 110. A single use water re-mineralization and filter cartridge 500 sized and shaped for connection to the outlet of the pump 125 by means of a second conduit 130 in the form of a second tubing. A collection reservoir 135 sized and shaped to collect a final water product is located beneath the single use re-mineralization and filter cartridge 500 to receive and store the sterile re-mineralized aqueous solution (the final water product). The collection reservoir 135, the first reservoir 110 and the cartridge 500 are located in fluid communication with each other. The collection reservoir 135 is located downstream of the cartridge 500, which in turn is located downstream from the first reservoir 110. The fluid is pumped along a fluid pathway from the first reservoir 110 to the collection reservoir 135. The single use cartridge can be discarded or recycled after each use. It should be noted though that the entirety of the liquid or mineral concentrate (the additive) present is used after each purification cycle.
[0074] In one example, the first and second conduit (tubing) 120, 130 are made from made of polyethylene plastic which is resistant to high pressure as well as being physically flexible.
[0075] The first reservoir 110 is typically a heat resistant hollow construction of rectangular or cylindrical shape, with a capacity of about 500 milliliters to 3.5 liters. The first reservoir 110 is generally manufactured using an injection molding process and using adequate transparent or semi-transparent material such as ABS or Nylon.
[0076] Referring now to
[0077] A housing 105 that is sized and shaped to hold the pump 125, the conduits 120, 130 includes an extruded base on which the reservoir 110 and the collection reservoir 135 rest. The single use re-mineralization and filter cartridge 500 is connected to the extruded housing 105.
[0078] Referring now to
[0079] Referring back to
[0080] Referring back now to
[0081] The sensor 197 is desirably located at the base of the collection reservoir 135, where the collection reservoir 135 rests oil the extruded housing 105. In order to accurately determine the amount of water collected in the collection reservoir 135, the sensor 197 subtracts the weight of the collection reservoir 135 from the total weight measured by the sensor 197, if it is a weight sensor. The apparatus 100 determines the weight of the collection reservoir 135 using a calibration process that is initiated when the user depresses a calibration push button 220, as best seen in
[0082] Referring back to
[0083] Still referring to
[0084] In the example shown in
[0085] Water that does not enter the center tube 520 is not filtered and exits from the filter cartridge 500 via the exit opening 560. This water is known to a person skilled in the art as “back flow”. It is possible to permit this back flow to be reused by this apparatus by allowing it to exit the cartridge at the opening 560 and re-enter the first reservoir 110 and to be filtered later.
[0086] The pre-determined amount of the additive material re-mineralizes the filtered water by using a combination of minerals from a carbon filter, vitamins, minerals, and micro nutrients from a liquid concentrate solution. The additive material may also be a pre-made powder with specific concentrations of nutrients needed by certain users. The additives are not only limited to human consumption but can also be used by plants and animals.
[0087] The reverse osmosis membrane filter 510 used in the examples shown include a pore size that ranges from between 0.0001 micron and 0.001 micron as the filtration unit to filter contaminants that larger than 0.001 microns to produce a purified aqueous solution. The reverse osmosis membrane 510 used removes contaminants including microorganisms, Volatile Organic Compounds (VOCs), and Total Dissolved Solids (TDS) from impure water.
[0088] In one example, the contaminated impure water from the first reservoir 110 first enters a carbon pre-filter (not shown) that removes chlorine and other contaminants before this water enters the reverse osmosis membrane filter 510.
[0089] Water filtered by the reverse osmosis filter membrane 510 is pressurized by the pump 125 so that this water is able to pass through the reverse osmosis filer membrane 510 at the desired rate. The pump 125 ensures that the water is pressurized to a pressure that is greater than 50 PSI. A person skilled in the art will readily recognize that time to purify water increases when the pump 125 pressurizes water to a pressure less than 50 PSI. Water pressurized to less than 50 PSI will result in a slower feed rate of impure water and therefore increase the time required by the invention to purify the impure water. A person skilled in the art will also understand that the useful life span of the reverse osmosis filter membrane 510 is reduced if the pump 125 pressurizes water to a pressure greater than 80 PSI. Experimentation with this apparatus reveals that the feed rate increases by approximately 50 mL/min for every 10 PSI increase of the water pressure. The reverse osmosis filter membrane 510 employed herein is optimized for a single use delivery system rather than for a continuous mass purification process currently on the market. However, water purified using reverse osmosis technologies is difficult to consume unless minerals are added back into the filtered water. As noted above, for a tailor-made use, we have designed our apparatus to ensure a one-time use re-mineralization cartridge can add vitamins and minerals tailored to the individual's health requirements.
[0090] The pump 125 can be centrifugal or a positive displacement pump, having a shape adapted to allow it to be inserted into the extruded housing 105. The pump 125 will be preferably of 110V, 220V, 230V, 240V and 380V with a wattage ranging from around 600 to 5500 watts. In another example, the pump 125 is an RO booster diaphragm pump, which operates at a pressure up to 130 PSI.
[0091] The materiel used to construct the final reservoir 135 is such that the final reservoir 135 can be reused several times to hold the sterilized and re-mineralized aqueous solution produced by apparatus 100.
[0092] In one example, the final reservoir 135 is a two-part detachable water bottle. For example, the final reservoir 135 could be of 2 L capacity with a partition line located inside the final reservoir 135. Once filled, the final reservoir 135 can be separated into two 1 L bottles with individual caps for each opening of the respective bottle. This allows the user to take one of the 1 L bottles to work while leaving the second 1 L at home. In another example, one of the 1 L bottles could also be used as a jug to dispense the purified and re-mineralized aqueous solution directly into the user's glass or another bottle.
[0093] As best illustrated in
[0094] As best illustrated in
[0095] For certain user requirements, especially in hot countries, cool or cold water is very palatable. A refrigeration unit 147 is used to cool the purified and re-mineralized aqueous solution before entering the final reservoir 135. The refrigeration unit 147 is connected to the cartridge inlet 540.
Alternative Embodiments
[0096] As best seen in
[0097] In the case of the apparatus 600, the user places impure water into the first reservoir 110 as illustrated by arrows 610 and 615. Like the previous apparatus 100, the pump 125 draws the contaminated water from the first reservoir 110, through the tubing 120 and into the pump 125 as illustrated by arrows 620 and 625. As illustrated by arrow 635, the pump 125 then causes the contaminated water to exit the pump 125, to pass through first tubing 650, whereupon the contaminated water enters a reverse osmosis filter 1000 for filtration. The purified water exits the reverse osmosis filter 1000 and travels through second tubing 655 where it enters the single use remineralization cartridge 800 as illustrated by arrows 640 and 650. The purified and filtered water is re-mineralized as it passes though the single use remineralization cartridge 800 as illustrated by arrow 660. The now purified and re-mineralized aqueous solution exits the single use re-mineralization cartridge 800 and enters the collection reservoir 135 as illustrated by arrow 665.
[0098] Referring to
[0099] Referring to
[0100] In certain examples that again are based on specific user use, additional sterility may be incorporated into the apparatus. Specifically, additional sterilization of the final water product in the collection reservoirs. To add more sterility to the final solution, the contaminated water is placed in an impure water storage space, and then exposed to an Ultraviolet light source such as a UVC Light Emitting Diode (LED). This LED will be appropriately electrically connected to the pump 125 and the power switch 210 if required. This LED will be a heat resistant light-producing device with a peak wavelength at around 405 nanometers. Certain examples used herein employ the UVC light source in the first reservoir 110. Other examples employ the UVC light source in the water bottle, i.e. the collection reservoir.
[0101] As best seen in
[0102] Referring now to
Operation
[0103] Referring to
[0104] Water that is re-mineralized in the center tube 520 prior to the mineral seal 550 being ruptured is re-mineralized by diluting the re-mineralization material contained within the center tube 520 with the purified water that passing through the center tube holes 530 of the center tube 520. Once the mineral seal 550 is ruptured, purified water passing though the center tube 520 is re-mineralized when it enters the final reservoir 135 and combines with the re-mineralized and purified aqueous solution already contained in the final reservoir 135. The purified and re-mineralized aqueous solution achieves the desired concentration of minerals and vitamins via this method so that this water is consumable. Impure water continues to be pumped into the single use re-mineralization and filter cartridge 500 by the pump 125 until the final reservoir 135 fills to the predefined level and the weight of the final reservoir 135 triggers the load sensor 197 to cause the pump 135 to stop pumping impure water into the single use re-mineralization and filter cartridge 500. Emptying the first reservoir 110 of impure water also stops the flow of contaminated water into the single use re-mineralization and filter cartridge 500.
[0105] Other and further aspects and advantages of the present invention will be obvious upon an understanding of the illustrative embodiments about to be described or will be indicated in the appended claims. Also, various advantages not referred to herein will occur to one skilled in the art upon employment of the invention in practice.