WO2019091937A1 - Dispositif de distribution d'eau pour dispenser une eau ayant un goût uniforme - Google Patents

Dispositif de distribution d'eau pour dispenser une eau ayant un goût uniforme Download PDF

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Publication number
WO2019091937A1
WO2019091937A1 PCT/EP2018/080227 EP2018080227W WO2019091937A1 WO 2019091937 A1 WO2019091937 A1 WO 2019091937A1 EP 2018080227 W EP2018080227 W EP 2018080227W WO 2019091937 A1 WO2019091937 A1 WO 2019091937A1
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WO
WIPO (PCT)
Prior art keywords
water
line
tds
treatment unit
value
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/EP2018/080227
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English (en)
Inventor
Kirtan Shravan KAMKAR
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Unilever NV
Conopco Inc
Original Assignee
Unilever NV
Conopco Inc
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Filing date
Publication date
Application filed by Unilever NV, Conopco Inc filed Critical Unilever NV
Publication of WO2019091937A1 publication Critical patent/WO2019091937A1/fr
Priority to PH22020550003U priority Critical patent/PH22020550003U1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • 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
    • 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
    • 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
    • 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
    • C02F1/006—Water distributors either inside a treatment tank or directing the water to several treatment tanks; Water treatment plants incorporating these distributors, with or without chemical or biological tanks
    • 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
    • B01D2311/24—Quality control
    • 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
    • B01D2311/25—Recirculation, recycling or bypass, e.g. recirculation of concentrate into the feed
    • 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
    • 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
    • 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
    • C02F2201/004—Seals, connections
    • 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
    • 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
    • C02F2209/003—Downstream control, i.e. outlet monitoring, e.g. to check the treating agents, such as halogens or ozone, leaving the process
    • 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
    • C02F2209/005—Processes using a programmable logic controller [PLC]
    • 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
    • C02F2209/005—Processes using a programmable logic controller [PLC]
    • C02F2209/006—Processes using a programmable logic controller [PLC] comprising a software program or a logic diagram
    • 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
    • C02F2209/10—Solids, e.g. total solids [TS], total suspended solids [TSS] or volatile solids [VS]
    • 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
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2301/00—General aspects of water treatment
    • C02F2301/04—Flow arrangements
    • C02F2301/043—Treatment of partial or bypass streams
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2301/00—General aspects of water treatment
    • C02F2301/04—Flow arrangements
    • C02F2301/046—Recirculation with an external loop

Definitions

  • the present invention relates to a water dispensing device.
  • the present invention more particularly relates to a water dispensing Device which maintains total dissolved solids (TDS) in a given range in the output water which maintains the taste of output water almost constant irrespective of the variation in input TDS levels or any other variation in TDS which occur over a period of time in the dispensing device.
  • TDS total dissolved solids
  • RO devices work on the principle of reduction in dissolved solids from the input water. Water has a particular taste partly because of the dissolved solids. Removal of dissolved solids beyond a certain point may adversely affect the taste. Similarly, if higher amount of dissolved solids remain in the output water (also called permeate), the taste of water may still be unpalatable at least to some consumers. Therefore, in order to adjust the taste of permeate water, remineralization means are used in some RO devices. But that involves adding of minerals from another source and may increase the cost of the water purifier.
  • US7507334 B1 (SIGONA JON-ANDREW VINCENT, 2009) discloses a modular-filter based RO water treatment system that remineralizes purified water twice to ensure the water is alkaline, but uses only one remineralization filter made of calcite. Calcium carbonate causes drastic increase in total dissolved solids (TDS), which may render the water unpalatable at least to some consumers. It also discloses that reverse osmosis filters remove on an average 98% sediments, organics and dissolved salts and reduce the pH to about 6.2 to 6.8 with only 5 to15 ppm of dissolved salts. The remineralisation filter containing mineral calcite raises the pH to about 7.0 and dissolved salts to about 30 on an average and finally the pH to about 7.5 to 8.5 and total solids to 60 ppm.
  • WO 2013/034396 discloses that a cartridge comprising calcium carbonate and magnesium carbonate in a certain combination provides controlled increase in TDS irrespective of the TDS levels in the input water, thereby making the water palatable.
  • the cited prior art does not disclose how to maintain uniform TDS level in the output water that has been purified using a reverse osmosis process where there is significant variation in the TDS levels of the input water. This is important considering the fact that there may be significant variation in the TDS levels from various sources of water and over the lifetime of the water purifier.
  • JP201 1-0251 14A discloses a water purifier having a raw water tank, an RO membrane, a raw water TDS sensor and a pure water TDS sensor.
  • the concentrate is recycled through recirculation line and is returned into the raw water tank through return line.
  • the concentrate may be drained or flushed through drain line by actuating a three-way valve, located upstream of return line. Based on the input from the two TDS sensors, the purifier can select the water source (either 100% tap water or raw water from raw water tank).
  • EP0599281 discloses a process for the treatment of liquids according to the principle of reverse osmosis, in particular for the recovery of substantially pure water from tap water, brackish water or salt water by means of a membrane module having a device. This design of a device providing recirculation of reject water can easily harm the device and the RO membrane as there will be intermittent pressure drop.
  • the disclosure of the application does not disclose a solution to output water in the desired range, it only utilizes the TDS sensor to decide switching between the water source. Therefore, there is a need to provide a device and method capable of achieving any constant TDS range value irrespective of the input/feed water TDS value.
  • the present invention provides a water dispensing device for providing output water in a constant Total Dissolved solids (TDS) range and which also helps in minimizing wastage of water.
  • TDS Total Dissolved solids
  • First aspect of the present invention provides a water dispensing device for providing output water in a constant Total Dissolved solids (TDS) range, the device comprising: a. a feed water inlet in fluid communication with a water storage chamber; b. a water treatment unit positioned downstream of the water storage chamber, the treatment unit having a treated water line and a reject water line;
  • TDS Total Dissolved solids
  • the reject water line is split by a multichannel connector into at least two lines, a recycle line and a drain line; wherein either a multi- way valve is positioned at the multichannel connector or one valve corresponding for every split line, a drain line valve on the drain line and a recycle line valve on the recycle line downstream of the multichannel connector;
  • a TDS sensor positioned on the treated water line, adapted to measure TDS of the water flowing out of the treatment unit;
  • control circuit configured to:
  • Second aspect of the present invention provides a method for providing output water in a constant TDS range by the device according to the first aspect, the method comprising, i. providing an inlet water flow through inlet into the water storage chamber; ii. allowing water to pass from the water storage chamber into the treatment unit; iii. sensing TDS of the water in the treated water line by the TDS sensor;
  • Another aspect of the present invention provides use of the device according to first aspect for minimizing waste water
  • Another aspect of the present invention provides a provides use of the device according to first aspect for maintaining TDS of output water from the device in a constant range.
  • Another aspect of the present invention provides a use of a control circuit configured to drain water from reject water line of a treatment unit through the drain line, when TDS value sensed is higher than the threshold TDS value, and alternately when the sensed value of TDS is less than or equal to the threshold value of TDS, directs water from the reject water line of the treatment unit into the recycle line and into a water storage chamber, in a water dispensing device comprising:
  • a feed water inlet in fluid communication with a water storage chamber
  • the reject water line is split by a multichannel connector into at least two lines, a recycle line and a drain line; wherein either a multi- way valve is positioned at the multichannel connector or one valve corresponding for every split line, a drain line valve on the drain line and a recycle line valve on the recycle line downstream of the multichannel connector;
  • a TDS sensor positioned on the treated water line, adapted to measure TDS of the water flowing out of the treatment unit;
  • Another aspect of the present invention provides a use of a control circuit configured to drain water from reject water line of a treatment unit through the drain line, when TDS value sensed is higher than the threshold TDS value, and alternately when the sensed value of TDS is less than or equal to the threshold value of TDS, directs water from the reject water line of the treatment unit into the recycle line and into a water storage chamber; in a water dispensing device comprising:
  • a feed water inlet in fluid communication with a water storage chamber
  • the reject water line is split by a multichannel connector into at least two lines, a recycle line and a drain line; wherein either a multi- way valve is positioned at the multichannel connector or one valve corresponding for every split line, a drain line valve on the drain line and a recycle line valve on the recycle line downstream of the multichannel connector;
  • a TDS sensor positioned on the treated water line, adapted to measure TDS of the water flowing out of the treatment unit;
  • FIG. 1 and 2 show the water flow diagram of the present invention. Detailed description of the invention
  • any feature of one aspect of the present invention may be utilised in any other aspect of the invention.
  • the word “comprising” is intended to mean “including” but not necessarily “consisting of” or “composed of.” In other words, the listed steps or options need not be exhaustive. It is noted that the examples given in the description below are intended to clarify the invention and are not intended to limit the invention to those examples per se.
  • Numerical ranges expressed in the format “from x to y” are understood to include x and y. When for a specific feature multiple preferred ranges are described in the format “from x to y", it is understood that all ranges combining the different endpoints are also contemplated.
  • the indefinite article “a” or “an” and its corresponding definite article “the” means at least one, or one or more, unless specified otherwise.
  • TDS total dissolved solids
  • RO reverse osmosis
  • other desalination devices are conventionally used at places where the total dissolved solids (TDS) of water are high.
  • TDS total dissolved solids
  • the TDS of surface water e.g., water that comes from lakes and reservoirs ranges from 70 to 120 ppm.
  • TDS of river or stream water ranges from 250 to 500 ppm.
  • underground water e.g. bore-well water is supplied. This water, by far, has very high TDS which may range from 500 to 2000 ppm.
  • RO Reverse osmosis
  • a membrane filtration method that removes many types of large molecules and ions from solutions by applying pressure to the solution when it is on one side of a selective membrane. The result is that the solute is retained on the pressurized side of the membrane and the pure solvent is allowed to pass to the other side.
  • this membrane should not allow large molecules or ions through the pores (holes), but should allow smaller components of the solution (such as water) to pass freely.
  • Reverse osmosis In the normal osmosis process the solvent naturally moves from an area of low solute concentration, through a membrane, to an area of high solute concentration. The movement of a pure solvent to equalize solute concentrations on each side of a membrane generates osmotic pressure. Applying an external pressure to reverse the natural flow of pure solvent, thus, is reverse osmosis. Reverse osmosis, however, involves a diffusive mechanism so that separation efficiency is dependent on solute concentration, pressure, and water flux rate. Reverse osmosis is most commonly known for its use in drinking water purification from seawater, removing the salt and other substances from the water molecules.
  • the output water may have as low as 4 to 5 ppm TDS which may be perceived unacceptably bitter.
  • the TDS of input water is about 2000 ppm; the permeate having TDS more than 200 ppm may be perceived salty.
  • the water dispensing device of the present invention with the given flow path of water and the control circuit configured to drain water from the reject water line of the treatment unit through the drain line, when TDS value sensed is higher than the threshold TDS value, and alternately when the sensed value of TDS is less than or equal to the threshold value of TDS, to direct water from the reject water line of the treatment unit into the recycle line and into the water storage chamber; it was seen that the TDS of the output water of the device was in a constant range and the device of the present invention also contributed to minimizing the wastage of water by allowing recycling of water through the reject water line of the treatment unit.
  • the invention also provides a device that works dynamically to continuously sense the TDS levels of the output water and then take action to ensure that the taste of the output water remains nearly constant and palatable to the consumer throughout the life of the water dispensing Device, the treatment unit and irrespective of the source of water used.
  • the device of the present invention is also beneficial for providing water with desirable TDS levels by the same device in different regions and localities irrespective of the input TDS water levels used as feed water into the device.
  • the device is capable of dispensing water which is even higher than the input/feed water TDS.
  • the preferred constant TDS range of drinking water is desirable between 30 to 250 ppm, more preferably between 50 to 150 ppm and most preferably between 70 to 120 ppm which can be achieved by the device of the present invention by using the threshold TDS value in the range of 30 to 250 ppm, more preferably between 50 to 150 ppm and most preferably between 70 to 120 ppm.
  • the device and method of the present inventions is capable of achieving any constant TDS range value irrespective of the input/feed water TDS value. This can be done by choosing an appropriate threshold value of TDS.
  • Another advantage of the device is that for the same device, the desired TDS of the output water from the device can be varied as per the requirement or taste of the consumer simply by varying the threshold TDS value.
  • the device of the present invention is therefore capable of being employed in any industry where a constant range of TDS of the output water is desired.
  • the present invention is also useful for providing any desired TDS range, which may not be necessarily used for drinking but any other desired purpose, wherein the treatment unit could be any industrial treatment unit. This would ensure that irrespective of the feed water source or the treatment that the feed water undergoes inside a water dispensing device, the TDS of the output water can be in a desired range.
  • the Water Dispensing Device The Water Dispensing Device
  • the present invention provides a water dispensing device for providing output water in a constant Total Dissolved solids (TDS) range, the device comprising: a. a feed water inlet in fluid communication with a water storage chamber;
  • a water treatment unit positioned downstream of the water storage chamber, the treatment unit having a treated water line and a reject water line;
  • the reject water line is split by a multichannel connector into at least two lines, a recycle line and a drain line; wherein either a multi- way valve is positioned at the multichannel connector or one valve corresponding for every split line, a drain line valve on the drain line and a recycle line valve on the recycle line downstream of the multichannel connector;
  • a TDS sensor positioned on the treated water line, adapted to measure TDS of the water flowing out of the treatment unit;
  • control circuit configured to:
  • the threshold value of TDS ranges from 10 to 2000 ppm, more preferably from 15 to 1000 ppm and most preferably from 20 to 500 ppm. It is preferred that upstream of the treatment unit is positioned a mechanical unit for driving water into the treatment unit.
  • the water dispensing device is preferably a water purification device dispensing purified water. It may preferably also have a sediment filter for pre-treatment generally placed before the treatment unit. Such filters may be made of woven or non-woven cloth or a carbon block.
  • the fabric may be made of natural fibers or of synthetic origin. Non-woven cloth made of cotton, polyester, polypropylene, or nylon is preferred.
  • a typical carbon block includes bound activated carbon particles.
  • purification units post the treatment unit such as UV treatment unit and/or a post carbon block and the ones common in the industry of water purification.
  • a feed water inlet is an inlet for providing water to the water dispensing device for purification and/or treatment and may have a varying variety of feed water entering into the device through the inlet.
  • the inlet is in fluid communication with a water storage chamber.
  • the feed water inlet can provide water from various sources which may have any TDS value.
  • a water storage chamber is preferably positioned downstream of the feed water inlet and in fluid communication with the feed water inlet.
  • the water storage chamber is preferably used for storing raw water, that is water before it is treated in the treatment unit.
  • the water storage chamber serves two purposes, one of storing the raw water and another of serving as a chamber to receive the water from the recycle line.
  • the water storage chamber is in fluid communication with the recycle line. It is preferable that the water storage chamber has at least one means to maintain volume of the chamber, preferably a valve and most preferably a float type valve. It is most preferable to have more than one float valves in the water storage chamber.
  • a water treatment as a component of the device of the present invention could be a unit for treating water in any sense, and is used broadly to mean bringing out any change in the composition of water which is dispensed out of the devise for use. It is preferred that the treatment unit in some manner alters the TDS content of the raw water. It is more preferred that the treatment unit is a desalination unit and most preferably a reverse osmosis unit.
  • the treatment unit is positioned downstream of the water storage chamber and has a reject water line; wherein, the reject water line is split by a multichannel connector into at least two lines, a recycle line and a drain line; wherein either a multi-way valve is positioned at the multichannel connector or one valve corresponding for every split line, a drain line valve on the drain line and a recycle line valve on the recycle line downstream of the multichannel connector, such that preferably at a given time water flows through only one split line.
  • the treated water from the treatment unit flows out through the treated water line which may further be treated or processed or may be dispensed through the outlet for dispensing water.
  • the treatment unit therefore has at least two lines for the water to flow out from it, the treated water line and the reject water line.
  • the reject water line is further split by a multichannel connector into at least two lines, a recycle line and a drain line.
  • a multichannel connector preferably serves the purpose to split the reject water line into higher number of lines of which minimum is two.
  • the multichannel connector could be a separate part used for connecting the reject water line with the different lines into which it is split or it may be molded as a single piece splitting into different lines.
  • a multi-way valve could be positioned at the multichannel connector or a separate valve could be present corresponding to each split line emanating from the reject water line of the water treatment unit, such as a drain line valve on the drain line and a recycle line valve on the recycle line downstream of the multichannel connector, such that preferably at a given time water flows through only one split line.
  • the recycle is provided with a flow restrictor downstream of the valve positioned at the multichannel connector or the recycle valve as the case may be.
  • the flow restrictor helps in limiting or restricting the flow of the water flowing through the recycle line, such that at a given time if water simultaneously flows through the drain line and the recycle line, then the amount of water to be recycled could be controlled through the flow restrictor. It is furthermore preferable to have a flow restrictor on the drain line as well.
  • RO membranes are commercially available for industrial and domestic use.
  • the RO membranes may be made in a variety of configurations, with the most preferred configuration being the TFC (thin film composite).
  • a preferred RO membrane is FILMTECTM Membranes Product TW30-1812-50 from The Dow Chemical Company.
  • a Total Dissolved Solids (TDS) sensor The device the present invention includes a 'total dissolved solids' (TDS) measuring means or a Total Dissolved Solids (TDS) sensor positioned on the treated water line, adapted to determine the total dissolved solids adapted to measure TDS of the water flowing out of the treatment unit; and communicating the measured value to the control circuit.
  • the TDS sensor is therefore positioned downstream of the treatment unit and is adapted to measure the TDS of water on the treated water line when the device is in operation.
  • dissolved solids refers generally to any minerals, salts, metals, cations or anions that are dissolved in a water sample. Dissolved solids include many of the substances that impair water color, odor, taste, or overall water quality. Many industries, and the food service industry in particular, require that the water used be held to stringent standards such that the color, odor, or taste of the water does not have any adverse effect on the end product.
  • a TDS sensor may be of any type being capable of sensing or measuring the total dissolved solids.
  • a commonly used TDS meter displays the TDS in parts per million (ppm). For example, a TDS reading of 1 ppm would indicate there is 1 milligram of dissolved solids in 1 kilogram of water.
  • a TDS meter may be an EC meter converting an EC reading to represent the TDS in the sample. Some meters can be selected to display either value.
  • the device of the present invention includes a control circuit preferably configured to control the various components of the device.
  • the control circuit can be either manually or automatically controlled.
  • the control circuit is configured to store a threshold TDS value; and drain water from the reject water line of the treatment unit through the drain line, when TDS value sensed is higher than the threshold TDS value, and alternately when the sensed value of TDS is less than or equal to the threshold value of TDS, directs water from the reject water line of the treatment unit into the recycle line and into the water storage chamber.
  • control circuit is configured to cover a TDS threshold value in a range spanning +/- 10% value of the predetermined TDS value.
  • control circuit comprises a memory. It preferably, includes a simple feedback circuitry or a microprocessor.
  • microprocessor control system is a programmable loop controller (PLC) system capable of monitoring the resistance, impedance, or conductance of the electrodes to enable the adjusting of power output to the electrodes via a connection.
  • PLC programmable loop controller
  • the microprocessor system is associated with software adapted to drive the microprocessor control system.
  • control circuit may be an analogue system utilising comparators or a digital system without a microprocessor.
  • the device of the present invention preferably has a flow rate detection means and/or a pressure detecting means adapted to measure the volume of liquid flowing through the device and/or detect the pressure of water entering the ion-eluting unit and communicating the measured value to the control circuit.
  • a flow rate and/or pressure detecting means adapted to detect the flow or pressure of water entering the device to switch the system on or off in the presence or absence of the flow of water in the device. It is preferred that the flow and/or pressure detecting means can be associated with a timer adapted also to switch the system on and off.
  • the flow control unit may be connected to one or more pumps and/or one or more valves controllable to vary the flow of the water through the device.
  • control circuit includes a constant current circuitry which are well known to a person skilled in the art, any known constant current circuitry may be used for the purpose which measures and/or stores the TDS values and compare the stored threshold TDS values with the real-time sensed TDS values. It is preferred that the control circuit is further configured to include 10% variation of the threshold TDS value in calculation of the threshold TDS value.
  • the control circuit stores a threshold value of TDS and compares with the real-time TDS data sensed by TDS sensor, with the stored threshold TDS value. If the sensed TDS value at a given time is higher than the threshold TDS value, then the water from the treatment unit is drained into the drain line via the reject water line. On the other hand, if the sense value of TDS is lower than the stored threshold TDS value at a given time, then the water from the treatment unit is directed into the recycle line from the reject water line of the water treatment unit and subsequently into the water storage chamber when the device is in operation.
  • the control circuit preferably operably controls the multi-way valve positioned on the multichannel connector when present or the corresponding drain line valve and recycle line valves when present.
  • the flow of water into the recycle line is closed by operably closing the recycle valve or stopping the flow of water into the recycle line, by operably closing the flow of water through the multi-way valve into the recycle line.
  • the flow of water into the drain line is closed by operably closing the drain valve or stopping the flow of water into the drain line, by operably closing the flow of water through the multi-way valve into the drain line.
  • the control circuit may further be configured to allow the permeate line water into the water storage tank.
  • the device of the present invention is also capable of partial recycle by having one or more split lines emanating from the reject water line. It is also possible to have both the recycle line and the drain line open simultaneously but having flow restrictors on at least one and preferably all the lines which distribute the flow of water appropriately between the drain line and the recycle line and any other when that is present. This allows specific percentages of water to flow out from different lines. Such as 30% water flows out from drain line and 70% from recycle line or vice versa.
  • the device of the present invention has a mechanical unit positioned upstream of the water treatment unit to facilitate water into the water treatment unit. It is preferred that the mechanical unit provides pressure to the water flowing into the treatment unit. A pressure of 80 psig or more is preferred of the water that enters into the treatment unit. It is more preferred that the mechanical unit is placed downstream of the water storage chamber. It is highly preferred that the mechanical unit is an electromechanical unit such as a pump. When a pump is used, any type of pump used in the industry of water dispensing devices could be employed which serves the purpose of providing pressure to the water entering treatment unit.
  • the present invention provides a method for providing output water in a constant TDS range by the device according to the first aspect, the method comprising, i. providing an inlet water flow through inlet into the water storage chamber;
  • threshold value of TDS ranges from 100 to 2000.
  • the treatment unit is a reverse osmosis unit.
  • the recycle line is provided with a flow restrictor downstream of the valve positioned at the multichannel connector or the recycle valve.
  • water from the storage chamber is driven into the treatment unit via a mechanical unit.
  • the water from the storage chamber is driven into the treatment unit via a mechanical unit, preferably an electromechanical unit and most preferably a pump.
  • the method further comprises configuring the control circuit to store a threshold TDS value and compare the TDS sensed in step (iii) with the stored threshold TDS value and drain water from the reject water line of the treatment unit through the drain line, when TDS value sensed is higher than the threshold TDS value, and alternately when the sensed value of TDS is less than or equal to the threshold value of TDS, directs water from the reject water line of the treatment unit (4) into the recycle line (5A) and into the water storage chamber.
  • the water dispensing device of the present invention dispenses water.
  • the present invention provides use of the device according to the device of the present invention for minimizing waste water
  • the present invention also provides use of the device according to the device of the present invention for maintaining TDS of output water from the device in a constant range.
  • the present invention provides a use of a control circuit configured to drain water from the reject water line of a treatment unit through the drain line, when TDS value sensed is higher than the threshold TDS value, and alternately when the sensed value of TDS is less than or equal to the threshold value of TDS, directs water from the reject water line of the treatment unit into the recycle line and into a water storage chamber, in a water dispensing device comprising:
  • a feed water inlet in fluid communication with a water storage chamber
  • the reject water line is split by a multichannel connector into at least two lines, a recycle line and a drain line; wherein either a multi- way valve is positioned at the multichannel connector or one valve corresponding for every split line, a drain line valve on the drain line and a recycle line valve on the recycle line downstream of the multichannel connector;
  • an electromechanical unit to facilitate the flow of water from the water storage chamber into the treatment unit.
  • a TDS sensor positioned on the treated water line, adapted to measure TDS of the water flowing out of the treatment unit;
  • e d an outlet positioned downstream of the treated water line for dispensing water; for minimizing waste water.
  • the present invention also provides a use of a control circuit configured to drain water from the reject water line of a treatment unit through the drain line, when TDS value sensed is higher than the threshold TDS value, and alternately when the sensed value of TDS is less than or equal to the threshold value of TDS, directs water from the reject water line of the treatment unit into the recycle line and into a water storage chamber; in a water dispensing device comprising:
  • a feed water inlet in fluid communication with a water storage chamber
  • the reject water line is split by a multichannel connector into at least two lines, a recycle line and a drain line; wherein either a multi- way valve is positioned at the multichannel connector or one valve corresponding for every split line, a drain line valve on the drain line and a recycle line valve on the recycle line downstream of the multichannel connector;
  • a TDS sensor positioned on the treated water line, adapted to measure TDS of the water flowing out of the treatment unit;
  • the constant TDS range is between 30 to 250 ppm, more preferably between 50 to 150 ppm and most preferably between 70 to 120 ppm.
  • the present invention provides use of a control circuit configured to drain water from a treatment unit through the drain line, when TDS value sensed is higher than the threshold TDS value, and alternately when the sensed value of TDS is less than or equal to the threshold value of TDS, directs water from the reject water line of the treatment unit into the recycle line and into a water storage chamber; in a water dispensing device for maintaining TDS of output water from the device in a constant range.
  • the water dispensing device comprises: a. a feed water inlet in fluid communication with a water storage chamber (3);
  • a water treatment unit positioned downstream of the water storage chamber, the treatment unit having a treated water line and a reject water line;
  • the reject water line is split by a multichannel connector into at least two lines, a recycle line and a drain line; wherein either a multi-way valve is positioned at the multichannel connector or one valve corresponding for every split line, a drain line valve on the drain line and a recycle line valve on the recycle line downstream of the multichannel connector;
  • a TDS sensor positioned on the treated water line, adapted to measure TDS of the water flowing out of the treatment unit;
  • FIG. 1 shows a water dispensing device (1 ) for providing output water in a constant Total Dissolved solids (TDS) range, the device (1 ) comprising:
  • a feed water inlet (2) in fluid communication with a water storage chamber (3);
  • a water treatment unit (4) positioned downstream of the water storage chamber (3), the treatment unit (4) having a treated water line (6) and a reject water line (5);
  • the reject water line (5) is split by a multichannel connector (13) into at least two lines, a recycle line (5A) and a drain line (5B); wherein one valve corresponding for every split line, a drain line valve (9) on the drain line (5B) and a recycle line valve (10) on the recycle line (5A) is positioned downstream of the multichannel connector; c. a TDS sensor (7) positioned on the treated water line (6), adapted to measure TDS of the water flowing out of the treatment unit; and d. an outlet (8) positioned downstream of the treated water line (6) for dispensing water.
  • a mechanical unit (12) is shown upstream of the treatment unit (4) for driving water into the treatment unit (4).
  • the water storage chamber (3) is adapted to receive water from the recycle line (5A).
  • Figure 1 also shows the recycle line (5A) is provided with a flow restrictor (1 1 ) downstream of the multichannel connector (13) on the recycle line (5A). Another flow restrictor (14) can also be seen on the drain line
  • FIG 2 shows a version of the device of the present invention as shown in Figure 1 with a difference that a multi-way valve (13A) is positioned at the multichannel connector (13) instead of separate valves for corresponding drain line (5B) and recycle line (5A).
  • a multi-way valve (13A) is positioned at the multichannel connector (13) instead of separate valves for corresponding drain line (5B) and recycle line (5A).
  • the present invention also provides a method for providing output water in a constant TDS range by the device according to the present invention, the method comprising steps of:
  • the device of the present invention is provided and the control circuit of the device is configured to store a threshold TDS of 80ppm.
  • the water will enter the feed water inlet supposing having a TDS of 1000 ppm and into the water storage chamber and then preferably pressurized preferably through a mechanical unit into the treatment unit.
  • the treatment unit in turn will treat the water and the treated water will flow out of the treatment unit into the treated water line which has a TDS sensor positioned on it to sense the TDS of the treated water.
  • the discard water from the treatment unit will flow out of the treatment unit via the reject water line.
  • the reject water line is split into at least two lines, a recycle line and a drain line.
  • a multi-way valve or valves for each corresponding line emanating from the reject water line to ensure that preferably water flows through only one split line at a time.
  • TDS 100 ppm
  • 80 ppm 80 ppm
  • the water from the treatment unit will be drained through the drain line, and this process will continue until the TDS of the water sensed at the treated water line falls to less than the threshold value of 80 ppm.
  • the TDS sensor senses TDS of the treated water to be 75 ppm then preferably no water is allowed to drain and all the water from the reject water line is directed into the recycle line and finally into the water storage chamber.
  • the choice of water flow path into the different lines can is preferably controlled by the control circuit by operably controlling the valves on the drain line and the recycle line, if the TDS of the treated water is sensed to be higher than the threshold TDS value, then the water from the reject water line needs to be directed into the drain line and therefore, the recycle line is closed by operably controlling the recycle line valve and closing it or operably controlling the multi-way valve and stopping the flow of water into the recycle line. Similarly, when the TDS of the treated water is sensed to be lower than the threshold TDS value, the water from the reject water line needs to be directed into the recycle line and therefore, the drain line is closed by operably controlling the drain line valve and closing it or operably controlling the multi-way valve and stopping the flow of water into the drain line.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Water Supply & Treatment (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
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Abstract

La présente invention concerne un dispositif de distribution d'eau pour dispenser une eau de sortie dans une proportion constante de matières dissoutes totales (MTD), le dispositif comprenant : a. une entrée d'eau d'alimentation en communication fluidique avec une chambre de stockage d'eau; b une unité d'osmose inverse positionnée en aval de la chambre de stockage d'eau, l'unité de traitement ayant une conduite d'eau traitée et une conduite d'eau de rejet; la conduite d'eau de rejet étant divisée par un connecteur à canaux multiples en au moins deux conduites, une conduite de recyclage et une conduite d'évacuation; on retrouve soit une vanne à plusieurs voies positionnée au niveau du connecteur à canaux multiples ou bien une vanne correspondant à chaque conduite divisée, une vanne de conduite d'évacuation sur la conduite d'évacuation et une vanne de conduite de recyclage sur la conduite de recyclage en aval du connecteur à canaux multiples; c. un capteur de MTD positionné sur la conduite d'eau traitée, conçu pour mesurer les MTD de l'eau s'écoulant hors de l'unité de traitement; d. une sortie positionnée en aval de la conduite d'eau traitée pour distribuer de l'eau; e. un circuit de commande configuré pour : i stocker une valeur MTD de seuil; et ii. l'eau d'évacuation provenant de la conduite d'eau de rejet de l'unité de traitement par l'intermédiaire de la conduite d'évacuation, lorsque la valeur MTD détectée est supérieure à la valeur MTD de seuil, et inversement, lorsque la valeur détectée de MTD est inférieure ou égale à la valeur MTD de seuil, achemine l'eau de la conduite d'eau de rejet de l'unité de traitement dans la conduite de recyclage et dans la chambre de stockage d'eau; lorsque le dispositif est en fonctionnement. La présente invention concerne également un procédé pour fournir de l'eau de sortie à partir d'un dispositif de distribution d'eau dans une proportion constante de matières dissoutes totales (MTD) et ses utilisations.
PCT/EP2018/080227 2017-11-09 2018-11-06 Dispositif de distribution d'eau pour dispenser une eau ayant un goût uniforme Ceased WO2019091937A1 (fr)

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PH22020550003U PH22020550003U1 (en) 2017-11-09 2020-04-01 A water dispensing device for dispensing water having consistent taste

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EP17200752 2017-11-09

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11660574B2 (en) * 2020-05-28 2023-05-30 University Of Kentucky Research Foundation Devices and methods for removing perfluorinated compounds from contaminated water

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0394777A2 (fr) * 1989-04-27 1990-10-31 Alfred Kärcher GmbH & Co. Installation de lavage pour véhicules
EP0599281A2 (fr) 1992-11-27 1994-06-01 WAT WASSER- UND UMWELTTECHNIK GmbH Procédé et appareil de traitement de liquides par osmose inverse
US7507334B1 (en) 2007-12-03 2009-03-24 Jon-Andrew Vincent Sigona Water treatment system
JP2011025114A (ja) 2009-07-22 2011-02-10 Duskin Co Ltd 切替型ｒｏ浄水器
CN102583808A (zh) * 2012-03-07 2012-07-18 慈溪市附海镇思维工业产品工作设计室 一种具有tds检测传感器的纯净水设备
WO2013034396A1 (fr) 2011-09-07 2013-03-14 Unilever N.V. Système de purification d'eau
CN205151844U (zh) * 2015-10-20 2016-04-13 江门市腾飞科技有限公司 一种通过tds检测值来调节废水排放的纯水机
CN105621535A (zh) * 2015-12-25 2016-06-01 上海浩泽净水科技发展有限公司 一种自动调节回收率的反渗透纯水机系统及其控制方法
CN104291414B (zh) * 2014-09-23 2016-06-15 珠海格力电器股份有限公司 反渗透净水系统、反渗透净水机及控制方法
CN205965523U (zh) * 2016-07-11 2017-02-22 浙江沁园水处理科技有限公司 具有降低纯水tds值功能的净水器

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0394777A2 (fr) * 1989-04-27 1990-10-31 Alfred Kärcher GmbH & Co. Installation de lavage pour véhicules
EP0599281A2 (fr) 1992-11-27 1994-06-01 WAT WASSER- UND UMWELTTECHNIK GmbH Procédé et appareil de traitement de liquides par osmose inverse
US7507334B1 (en) 2007-12-03 2009-03-24 Jon-Andrew Vincent Sigona Water treatment system
JP2011025114A (ja) 2009-07-22 2011-02-10 Duskin Co Ltd 切替型ｒｏ浄水器
WO2013034396A1 (fr) 2011-09-07 2013-03-14 Unilever N.V. Système de purification d'eau
CN102583808A (zh) * 2012-03-07 2012-07-18 慈溪市附海镇思维工业产品工作设计室 一种具有tds检测传感器的纯净水设备
CN104291414B (zh) * 2014-09-23 2016-06-15 珠海格力电器股份有限公司 反渗透净水系统、反渗透净水机及控制方法
CN205151844U (zh) * 2015-10-20 2016-04-13 江门市腾飞科技有限公司 一种通过tds检测值来调节废水排放的纯水机
CN105621535A (zh) * 2015-12-25 2016-06-01 上海浩泽净水科技发展有限公司 一种自动调节回收率的反渗透纯水机系统及其控制方法
CN205965523U (zh) * 2016-07-11 2017-02-22 浙江沁园水处理科技有限公司 具有降低纯水tds值功能的净水器

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11660574B2 (en) * 2020-05-28 2023-05-30 University Of Kentucky Research Foundation Devices and methods for removing perfluorinated compounds from contaminated water

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