WO2016100491A1 - On-demand system for drawing and purifying well water - Google Patents
On-demand system for drawing and purifying well water Download PDFInfo
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- WO2016100491A1 WO2016100491A1 PCT/US2015/066058 US2015066058W WO2016100491A1 WO 2016100491 A1 WO2016100491 A1 WO 2016100491A1 US 2015066058 W US2015066058 W US 2015066058W WO 2016100491 A1 WO2016100491 A1 WO 2016100491A1
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- water
- source
- filtration system
- chlorine
- tank
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
- B01D61/025—Reverse osmosis; Hyperfiltration
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- 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
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
- B01D61/08—Apparatus therefor
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
- B01D61/12—Controlling or regulating
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2311/00—Details relating to membrane separation process operations and control
- B01D2311/04—Specific process operations in the feed stream; Feed pretreatment
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2311/00—Details relating to membrane separation process operations and control
- B01D2311/26—Further operations combined with membrane separation processes
- B01D2311/2649—Filtration
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- 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
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- 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
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- 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
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
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- 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
- C02F1/50—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
-
- 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
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/76—Treatment of water, waste water, or sewage by oxidation with halogens or compounds of halogens
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/12—Halogens or halogen-containing compounds
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/20—Heavy metals or heavy metal compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/306—Pesticides
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/32—Hydrocarbons, e.g. oil
- C02F2101/322—Volatile compounds, e.g. benzene
-
- 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
- C02F2201/002—Construction details of the apparatus
- C02F2201/005—Valves
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- 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
- C02F2201/009—Apparatus with independent power supply, e.g. solar cells, windpower or fuel cells
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- 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
- C02F2209/04—Oxidation reduction potential [ORP]
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- 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
- C02F2209/29—Chlorine compounds
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- 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
- C02F2209/42—Liquid level
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
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- Y—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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/20—Controlling water pollution; Waste water treatment
- Y02A20/208—Off-grid powered water treatment
- Y02A20/211—Solar-powered water purification
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- Y—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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/20—Controlling water pollution; Waste water treatment
- Y02A20/208—Off-grid powered water treatment
- Y02A20/212—Solar-powered wastewater sewage treatment, e.g. spray evaporation
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- Y—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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
Definitions
- This disclosure relates to methods and systems for generating potable water from impure or contaminated water, such as crude well water (groundwater).
- a ready supply of pure water is generally regarded as the single most important factor affecting human health. Millions of individuals become ill each year from drinking water that is contaminated with dangerously high levels of chemical and/or biological impurities. Pollutants often occur in well water (groundwater) as well as in surface water, particularly in developing countries. Moreover, developing countries often lack the resources to sufficiently and systematically treat water to remove organic compounds such as volatile organic compounds (VOCs), pesticides and their breakdown products, heavy metals, parasites, viruses, and bacteria that pose such risks. Infants and young children are at much greater risk than adults from drinking impure water.
- VOCs volatile organic compounds
- Desirable systems should be capable of operating from a variety of different electrical power sources, with a minimum of maintenance and for extended periods of time. Systems that can operate in harsh environments with little or no technical expertise required for their upkeep would be useful. For example, such systems should eliminate expensive, complex maintenance procedures such as cleaning, should avoid long wait times between activating the system to deliver pure water and the actual time water is provided, and should be safe and simple to use so that children can fill containers from the water so-supplied.
- the disclosure provides an on-demand water treatment system and method that is designed to provide potable drinking water from various source (wells, municipal, and some ground sources), which do not require product storage tank for the system and which can be operated on direct current (DC) power (such as solar cells) for remote operation.
- a system and method can include, for example, automatic chlorinated disinfection with permeate or concentrate stream, and incorporates a pre- filtration stage for removing suspended solid contaminants.
- the system can include a chlorination feature that provides protection against microorganisms inside the storage tank and prevents bio-film growth.
- Carbon block filters can be used to remove VOCs, cysts and the like, as well as any remaining free chlorine to prevent damage to a Reverse Osmosis (RO) system membrane that provides a final downstream purification or filtration stage to generate the potable drinking water.
- RO Reverse Osmosis
- this system does not require a product tank requiring any additional post treatments for water storage.
- a pressure regulated or flow controlled pump that can be operated on DC power (for example, 24VDC) provides water for users on demand.
- a source of impure water a source tank, and a first filtration stage between the source of impure water and the source tank;
- a pump in communication with an actuator, which supplies impure water from the source through the first filtration stage and into the storage tank, when a low pressure or low level condition drops below a predetermined value.
- a method for providing potable water on-demand comprising providing a water filtration system as disclosed above, and activating the permeate dispense valve to provide the potable water.
- a water filtration system for providing potable water on-demand as described immediately above by elements a) through e), and comprising the disclosed elements a) through e) in fluid communication, the water filtration system further comprising:
- a chlorine doser valve in communication with the ORP meter that actuates a chlorine doser to add chlorine to the source tank, when the chlorine level drops below a first predetermined level.
- Yet a further aspect of this disclosure provides a water filtration system for providing potable water on-demand as described immediately above by elements a) through g), and comprising the disclosed elements a) through g) in fluid communication, the water filtration system further comprising:
- a method for providing potable water on-demand comprising providing a water filtration system as disclosed immediately above with the additional features, actuating the chlorine doser valve of element g) to add chlorine to the source tank if the chlorine level drops below the first predetermined level.
- the method can further comprise actuating the feedback loop valve of element h) to return water to the source tank if the chlorine level rises above the second predetermined level, and activating the permeate dispense valve to provide the potable water.
- FIG. 1 provides an illustration of one aspect of the present disclosure, showing a schematic of a one embodiment of the system for illustration purposes.
- FIG. 2 also illustrates an aspect of the present disclosure, showing a schematic of an alternatively embodiment of the system for illustration purposes.
- an on-demand water treatment system and method that provides potable drinking water from any ground water source, particularly wells, which does not require any product storage tank, and which can be operated on DC power for remote operation.
- the present system and method can include, for example, an automatic chlorinated disinfection feature and can incorporate a pre-filtration stage for removing suspended solid contaminants.
- FIG. 1 One aspect of the present disclosure is provided at FIG. 1.
- the system illustrated in FIG. 1 draws water from bore wells with a well pump, coarsely strains, and then pre-filters the source water to remove suspended solids.
- a pleated cartridge filter can be used in this pre-filtration stage, and such cartridges can be readily replaced without requiring any special technical expertise.
- the pleated cartridge filter can be tailored according to the specific chemical and biological contaminants in the well water. For example, high iron content water can be ameliorated using a specific prefilter for iron or other metal contaminants.
- Pre-filtered water is then stored in a source tank as shown in FIG. 1.
- the source tank could also receive water from a pressurized water source or other water source.
- the stored water is passed from the source tank, through a source pump, through multiple carbon filters, and into a reverse osmosis water treatment system in sequence.
- the carbon filter block pre-filters the water to remove VOCs, cysts, and chlorine from the source tank.
- the reverse osmosis (RO) system removes the remaining contaminants according to the membrane design capacity.
- the filtration sequence ends with a water dispense faucet that facilitates the on- demand feature of the present system.
- a pressure switch is triggered which activates the source pump and provides potable drinking water to users.
- the discharge line pressure increases to a pre-set condition, thereby triggering the pressure switch to shut off the source pump.
- This combination of features makes the disclosed water treatment system configuration a completely "on-demand" system. Because the system has sufficient on-demand water flow and pressure, this configuration allows the system to keep pace with user demand, and therefore a permeate storage tank is not required.
- a low water level indicator can be used to monitor the water level of the source tank, which can activate the well pump to force additional water into the source tank when the level drops below a predetermined level or volume.
- the source tank can be chlorine disinfected with food grade chlorination tablets or other food grade chlorination product.
- this chlorination feature can be accomplished with an inline chlorinator, that utilizes a partial stream from either the permeate or the concentrate flow.
- an ORP (oxidation-reduction potential) meter that measures the chlorine level in the source tank discharge, and which turns on a solenoid valve on the permeate side stream to provide chlorination with the inline chlorinator.
- the same ORP meter feedback can turn on a solenoid valve on the concentrate side stream to provide chlorination through the inline chlorinator.
- the present system is capable of direct current operation, including 24VDC operation from solar photovoltaic panel power.
- FIG. 2 illustrates a schematic of other aspects and embodiments of the system and method of the disclosure.
- the intake water for the disclosed treatment system can be drawn from multiple sources, such as uninfluenced wells, municipal water, and other sources.
- water typically can be pumped from the source to a storage tank, such as a 1000 or 2000 L storage tank. Tank size can depend on, for example, the local water and power supply, as well as the local consumption needs.
- the source water can be piped to the tank with stainless steel piping or National Sanitation Foundation (NSF)-approved pipe and fittings.
- NSF National Sanitation Foundation
- FIG. 2 depicts one water system configuration, in which source water is pre-filtered with pleated cartridge filters and then run through an inline chlorinator (chlorine doser) before being stored in the source tank.
- Chlorination level can be adjusted based on source water conditions.
- the free chlorine level in the source tank is generally maintained between about 1 to about 2 ppm.
- Following chlorination there may be mineral deposit at the conical bottom of the tank, and such deposits can be removed regularly, for example by simply draining or rinsing out. This regular procedure would prevent deposit buildups that could harbor microorganisms that may be difficult to access and treat with chlorination.
- the carbon blocks remove free chlorine, volatile organics and other organic compounds, and harmful cysts.
- the RO membranes remove the remainder of the contaminants and provide safe drinking water. Through this filtration process a concentrate stream is generated with the filtered contaminants, and this stream then can be disposed of according to any local regulations. Further, this concentrate stream could be used for other purposes if desired, for example, for sanitary needs.
- the disclosed water treatment system can be installed at sites that have a source of water that is available at all times of the day and all year round.
- the source water is typically a freshwater source from a sealed uninfluenced well or from a pre-treated municipal source. That is, the source water generally is not a surface source or an influenced well, and the source water is not brackish or salt water. Further, the source water is typically not influenced by runoffs, flooding, or other means of adulteration.
- the following Table illustrates typical minimum water quality requirements to work well with the disclosed Table 1. Typical Minimum Source Water Quality
- incoming water supplies that do not meet these requirements may be advantageously subjected to additional pre-treatment prior to exposing, for example the carbon filters and the RO filtration unit to the water.
- System performance may be affected if requirements are far outside these typical specifications, including system output production and cartridge change-out frequency.
- the disclosed system can be operated by trained operators who can operate the system daily and independently and could perform regular maintenance and quality monitoring requirements. Such operators can provide maintenance support, replacement of parts as needed, and monitor water quality typically with kits that are easy to use. If wireless coverage is available, wireless monitors that report water and filter quality can be used for remote data reporting. It is expected that such units can supply sufficient water for 300 or more users daily and be capable of, for example, 400 L (liter) per hour capacity. This is particularly achievable as the source tank is typically 1000 L to 2000 L in capacity. Usage above tank capacity would require regular water supply from the source.
- the source of impure water can be a well or municipal water source, and can particularly be a sealed well.
- surface contamination of wells is typically controlled by the use of a surface seal.
- Providing a seal involves drilling a relatively large hole to a predetermined depth or to a confining formation (clay or bedrock, for example), and then further drilling a smaller hole for completing the well from that point forward.
- the well is typically cased from the surface down into the smaller hole, with a casing that is the same diameter as that hole.
- the annular space between the large bore hole and the smaller casing can be filled with, for example, bentonite clay, concrete, or other sealant materials.
- Such a procedure creates an impermeable seal from the surface to the next confining layer that keeps contaminants from migrating down the outer sidewalls of the casing or borehole and into the aquifer.
- wells typically are capped with either an engineered well cap or seal that vents air through a screen into the well, but also keeps insects, small animals, and unauthorized persons from accessing the well.
- the filtration system disclosed herein can constitute part of a water distribution center or kiosk, where the filtration system is particularly designed to meet requirements of low power consumption, high reliability, low maintenance, and versatile applicability for well waters and pre-treated municipal water.
- the treatment system can typically consists of a 1000 L source water storage tank that is filled from fresh water wells or from pre-treated municipal systems.
- An inline chlorination system to the source tank can provide microbiological disinfection.
- the water can be pushed through a carbon block filter to removes cysts, organics, pesticides, heavy metals and free chlorine from the source water tank. Downstream of the carbon block is the reverse osmosis unit in series, to clean and purify the water further.
- the RO unit completes the fine filtration process to eliminate remainder contaminants to dispense safe drinking water.
- the RO system includes a filtration membrane, so that any contaminants left in the water will be filtered through the membrane into a pipe separate from the safe drinking water, and will subsequently be recycled back to the source tank.
- the water system can include a valve (not shown in the Figures) downstream of the carbon filter, for example, prior to any water entering the RO system, that is used to measure the amount of chlorine that goes into the tank.
- the amount of chlorine will be measured daily using, for example, paper strip indicator.
- the chlorine entering the approach to measuring the chlorine going into the tank is by a DPD test kit that uses a colorimetric method.
- the water distribution center or kiosk configuration is particularly useful for deploying the disclosed system in remote areas, where the lack of sufficient and reliable power to operate a purification system can present serious problems.
- the disclosed system can be operated very simply using two toggle switches to operate two pumps, namely a feed pump and a recirculation pump.
- a control panel can be powered up to operate the unit with a start push button, which is separate from the stop switch to power down the unit.
- Such a unit operates as a true on-demand dispense unit, because there is no delay in start-up and dispense, which is immediate after start up.
- the disclosed system can produce at least about 10,000 liters of water per day if run continuously. While the full unit can be operated and adapted for AC or DC power configurations, the disclosed unit has the advantage of operating highly efficiently with solar photovoltaic panel power, with well below IkW power needed when in operation. In standby the disclosed unit can use very small amounts of power. Further, the system can incorporate simple controls for basic unit functionality and can measure inlet and dispense water conductivity for monitoring quality.
- Additional features that can be provided by the disclosed system are simple regular maintenance service plans, which typically use an operator to clean pre-filters on an as-needed basis. This pre-filter cleaning is estimated to be about monthly in frequency.
- maintenance can include the operator checking source tank free chlorine level daily and adding chlorination for disinfection as required.
- the pre-filters are expected to be replaced approximately once every three to six months, the RO membranes approximately once a year, and the pumps approximately once every three years or more.
- startup follows good engineering practice. For example, on initial filling of the source tank with unpurified water, the system is chlorinated for a minimum of 3 hours to allow the antimicrobial action to take effect. Free chlorine level is checked in the source tank, and the process of adding more chlorination and/or waiting for the full contact time can be used. If chlorine levels are too high, for example, over 4ppm, then additional raw (unpurified) can be added to the source tank and the maintained for an additional contact time. Water samples can be taken and measured as required. Typically, the RO membranes can be run for 8 or more hours during startup. It may be desirable to run more than one quantity of water equivalent to one source tank through the system during startup.
- chlorine and chlorination refer to the use of conventional chlorine-containing antimicrobial, antibacterial, and disinfectant products such as hypochlorite-containing compounds and components, that are suitable for use in a water purification system that produces water for consumption.
- VOC volatile organic compound
- sanitary well seal is used to refer to a manufactured seal installed at the top of the well casing which, when installed, creates a watertight seal to prevent contaminated or polluted water from gaining access to the ground water supply.
- various publications may be referenced. The disclosures of these publications are hereby incorporated by reference in pertinent part, in order to more fully describe the state of the art to which the disclosed subject matter pertains. The references disclosed are also individually and specifically incorporated by reference herein for the material contained in them that is discussed in the sentence in which the reference is relied upon. To the extent that any definition or usage provided by any document incorporated herein by reference conflicts with the definition or usage applied herein, the definition or usage applied herein controls.
- a projectile includes a single projectile such as a slug, as well as any combination of more than one projectile, such as multiple pellets of shot of any size or combination of sizes.
- reference to “a projectile” includes multiple particles of a chemical composition or mixture of compositions that constitutes a projectile, and the like.
- compositions and methods are described in terms of “comprising” various components or steps, the compositions and methods can also “consist essentially of or “consist of the various components or steps.
- Applicants reserve the right to proviso out or exclude any individual members of any such group, including any sub-ranges or combinations of sub-ranges within the group, if for any reason Applicants choose to claim less than the full measure of the disclosure, for example, to account for a reference that Applicants are unaware of at the time of the filing of the application.
- Values or ranges may be expressed herein as “about”, from “about” one particular value, and/or to “about” another particular value. When such values or ranges are expressed, other embodiments disclosed include the specific value recited, from the one particular value, and/or to the other particular value. Similarly, when values are expressed as approximations, by use of the antecedent "about,” it will be understood that the particular value forms another embodiment. It will be further understood that there are a number of values disclosed therein, and that each value is also herein disclosed as
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Abstract
Description
Claims
Priority Applications (6)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AU2015364736A AU2015364736B2 (en) | 2014-12-19 | 2015-12-16 | On-demand system for drawing and purifying well water |
| CN201580075855.3A CN107206319B (en) | 2014-12-19 | 2015-12-16 | On-demand system for pumping and purifying well water |
| US15/536,927 US10494284B2 (en) | 2014-12-19 | 2015-12-16 | On-demand system for drawing and purifying well water |
| BR112017013072-6A BR112017013072B1 (en) | 2014-12-19 | 2015-12-16 | SYSTEM ON DEMAND TO EXTRACT AND PURIFY WELL WATER |
| MX2017007886A MX390610B (en) | 2014-12-19 | 2015-12-16 | ON-DEMAND SYSTEM TO EXTRACT AND PURIFY WELL WATER. |
| ZA2017/04867A ZA201704867B (en) | 2014-12-19 | 2017-07-18 | On-demand system for drawing and purifying well water |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US201462094319P | 2014-12-19 | 2014-12-19 | |
| US62/094,319 | 2014-12-19 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2016100491A1 true WO2016100491A1 (en) | 2016-06-23 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/US2015/066058 Ceased WO2016100491A1 (en) | 2014-12-19 | 2015-12-16 | On-demand system for drawing and purifying well water |
Country Status (7)
| Country | Link |
|---|---|
| US (1) | US10494284B2 (en) |
| CN (1) | CN107206319B (en) |
| AU (1) | AU2015364736B2 (en) |
| BR (1) | BR112017013072B1 (en) |
| MX (1) | MX390610B (en) |
| WO (1) | WO2016100491A1 (en) |
| ZA (1) | ZA201704867B (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20030019764A1 (en) * | 2000-08-11 | 2003-01-30 | H20 Technologies, Ltd. | Under the counter water treatment system |
| US20040168989A1 (en) * | 2003-02-28 | 2004-09-02 | Tempest Gerard F. | System and method for water purification |
| US20110186529A1 (en) * | 2010-01-29 | 2011-08-04 | Wright A Vernon | Solar-powered water purification system |
| US20120024796A1 (en) * | 2011-03-30 | 2012-02-02 | Crystal Lagoons Corporation Llc | Sustainable method and system for treating water bodies affected by bacteria and microalgae at low cost |
| US20140021126A1 (en) * | 2012-07-18 | 2014-01-23 | Dan Lin | Reversible backwashing self-cleaning filter |
Family Cites Families (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20020036162A1 (en) * | 1996-08-08 | 2002-03-28 | Magnusson Jan H. | Appliance with iodinated water source |
| JP2003018429A (en) * | 2001-07-02 | 2003-01-17 | Matsushita Electric Ind Co Ltd | Pedestal level control circuit and pedestal level control method |
| US7632410B2 (en) * | 2003-08-21 | 2009-12-15 | Christopher Heiss | Universal water purification system |
| CN1699202A (en) * | 2004-05-19 | 2005-11-23 | 周建吾 | Direct drinking water device |
| US20110018652A1 (en) * | 2009-07-22 | 2011-01-27 | Chun-Hsien Pan | Multimedia network splitter |
| MY170712A (en) * | 2010-04-26 | 2019-08-27 | Ryozo Irie | Wastewater treatment method and system |
| IT1400751B1 (en) * | 2010-06-30 | 2013-07-02 | St Microelectronics Srl | CIRCUIT FOR OPTIMIZING THE PROGRAMMING OF A FLASH MEMORY |
| CN101935111B (en) * | 2010-08-26 | 2012-12-19 | 宝钢工程技术集团有限公司 | Wastewater recycling preparation system with low energy consumption |
| CN102328980A (en) * | 2011-06-23 | 2012-01-25 | 张家港市创新化学石膏制品有限公司 | Water purification material and preparation method thereof |
| CN104108809B (en) * | 2014-06-05 | 2016-06-01 | 深圳市翰唐环保科技有限公司 | The purification process of waste water |
-
2015
- 2015-12-16 WO PCT/US2015/066058 patent/WO2016100491A1/en not_active Ceased
- 2015-12-16 US US15/536,927 patent/US10494284B2/en active Active
- 2015-12-16 CN CN201580075855.3A patent/CN107206319B/en active Active
- 2015-12-16 BR BR112017013072-6A patent/BR112017013072B1/en active IP Right Grant
- 2015-12-16 AU AU2015364736A patent/AU2015364736B2/en active Active
- 2015-12-16 MX MX2017007886A patent/MX390610B/en unknown
-
2017
- 2017-07-18 ZA ZA2017/04867A patent/ZA201704867B/en unknown
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20030019764A1 (en) * | 2000-08-11 | 2003-01-30 | H20 Technologies, Ltd. | Under the counter water treatment system |
| US20040168989A1 (en) * | 2003-02-28 | 2004-09-02 | Tempest Gerard F. | System and method for water purification |
| US20110186529A1 (en) * | 2010-01-29 | 2011-08-04 | Wright A Vernon | Solar-powered water purification system |
| US20120024796A1 (en) * | 2011-03-30 | 2012-02-02 | Crystal Lagoons Corporation Llc | Sustainable method and system for treating water bodies affected by bacteria and microalgae at low cost |
| US20140021126A1 (en) * | 2012-07-18 | 2014-01-23 | Dan Lin | Reversible backwashing self-cleaning filter |
Also Published As
| Publication number | Publication date |
|---|---|
| CN107206319B (en) | 2021-06-18 |
| AU2015364736B2 (en) | 2020-11-19 |
| CN107206319A (en) | 2017-09-26 |
| BR112017013072A2 (en) | 2018-02-20 |
| ZA201704867B (en) | 2021-06-30 |
| BR112017013072B1 (en) | 2022-08-02 |
| MX390610B (en) | 2025-03-20 |
| US20190092668A1 (en) | 2019-03-28 |
| MX2017007886A (en) | 2017-09-05 |
| US10494284B2 (en) | 2019-12-03 |
| AU2015364736A1 (en) | 2017-06-29 |
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