CN219460262U - System for producing liquid brine concentrate - Google Patents

System for producing liquid brine concentrate Download PDF

Info

Publication number
CN219460262U
CN219460262U CN202190000357.3U CN202190000357U CN219460262U CN 219460262 U CN219460262 U CN 219460262U CN 202190000357 U CN202190000357 U CN 202190000357U CN 219460262 U CN219460262 U CN 219460262U
Authority
CN
China
Prior art keywords
salt
calcium
mixing tank
liquid brine
sodium
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.)
Active
Application number
CN202190000357.3U
Other languages
Chinese (zh)
Inventor
西蒙娜·博格
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.)
Xi MengnaBoge
Original Assignee
Xi MengnaBoge
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Xi MengnaBoge filed Critical Xi MengnaBoge
Application granted granted Critical
Publication of CN219460262U publication Critical patent/CN219460262U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • 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
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/385—Concentrates of non-alcoholic beverages
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/42—Preservation of non-alcoholic beverages
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/52—Adding ingredients
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L3/00—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs
    • A23L3/26—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by irradiation without heating
    • A23L3/28—Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by irradiation without heating with ultraviolet light
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L5/00—Preparation or treatment of foods or foodstuffs, in general; Food or foodstuffs obtained thereby; Materials therefor
    • A23L5/55—Rehydration or dissolving of foodstuffs
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/52—Adding ingredients
    • A23L2/54—Mixing with gases
    • 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
    • C02F1/008—Control or steering systems not provided for elsewhere in subclass C02F
    • 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
    • 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
    • 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
    • C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
    • 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
    • C02F1/68—Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable water
    • 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
    • Y02A20/124—Water desalination
    • Y02A20/131—Reverse-osmosis

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Polymers & Plastics (AREA)
  • Nutrition Science (AREA)
  • Food Science & Technology (AREA)
  • Health & Medical Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
  • Medicines Containing Plant Substances (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The utility model relates to a system for producing a liquid brine concentrate which can be diluted to obtain water for human consumption, comprising a reverse osmosis demineralizer (2) for preparing demineralized water, a sterilization device (3) for sterilizing the demineralized water, CO 2 -a source (4), -a carbonator (5) for carbonating the sterilized demineralised water, -a mixing tank (6) connected to the carbonator (5), -a supply circuit for supplying salt to the mixing tank (6), -an adjusting device (7) for adjusting the pH of the liquid brine concentrate (10) present in the mixing tank (6) to a range between 4 and 9, -a mechanical stirring device (8) for stirring the liquid brine concentrate (10) present in the mixing tank (6).

Description

System for producing liquid brine concentrate
Technical Field
The present utility model relates to a system for preparing a liquid concentrate, the liquid concentrate thus obtained and water for human consumption produced with the liquid concentrate thus obtained, which can be diluted to obtain water for human consumption and which has the characteristics of natural mineral water or water not present in nature.
Background
The preparation of water for human consumption obtained by remineralisation of water containing little ions is a complex problem from a chemical point of view, especially when liquid concentrates produced on an industrial scale are chosen for convenience and then sold in on-site dilutable doses according to the requirements of the final product production.
It should be noted first that the most common and most widely occurring ions in natural water are essentially calcium, magnesium and bicarbonate ions, and second sodium, potassium, chloride and sulfate ions. Furthermore, the chemical composition of natural mineral water shows that the most abundant substance is calcium bicarbonate (Calcium Bicarbonate).
Thus, a first problem in obtaining a liquid concentrate that can be diluted for the production of "synthetic" mineral water featuring a reasonable calcium carbonate balance is that the calcium bicarbonate (unlike carbonate) is not present in solid form, but only in aqueous solution.
A second problem is that it must also take into account the possible precise precipitation of salts in the liquid concentrate at the time of preparation or over time, due to temperature variations, exposure to uv light, etc. Indeed, the most critical aspect is the possible precipitation of calcium carbonate.
The technical task of the present utility model is therefore to provide a system for preparing a liquid concentrate which is able to eliminate the above-mentioned technical drawbacks of the prior art, said liquid concentrate being able to be diluted to obtain water intended for human consumption and having the characteristics of natural mineral water or water not present in nature.
Within the scope of this technical task, one object of the present utility model is to provide a system for preparing a liquid concentrate of water that can be diluted to obtain water for human consumption and that has the characteristics of natural mineral water or water not present in nature, wherein the liquid concentrate produced has a reasonable calcium carbonate balance and negligible or zero amounts of precipitated salts, in particular calcium carbonate.
Disclosure of Invention
The technical task according to the present utility model and these and other objects are achieved by providing a system for producing a liquid brine concentrate that can be diluted to obtain water for human consumption, characterized in that it comprises a reverse osmosis demineralizer for preparing demineralized water, a sterilizing device for sterilizing said demineralized water, CO 2 A source, a carbonator for carbonating the sterilized demineralized water, a mixing tank connected to the carbonator, a supply circuit for supplying salt to the mixing tank, a regulating device for regulating the pH of the liquid brine concentrate present in the mixing tank to a range between 4 and 9, a stirring device for stirring the liquid brine present in the mixing tankA mechanical stirring device of concentrate, said supply circuit comprising a plurality of storage tanks connected to said demineralizer for storing salt in crystalline or liquid form, and for each storage tank there is a corresponding metering pump, said storage tanks comprising a tank for storing potassium bicarbonate salt and/or a tank for storing sodium bicarbonate salt, at least one tank for storing calcium salt and at least one tank for storing salt other than calcium salt, there being also provided a controller for feeding the salt present in the storage tanks into the mixing tank in sequence, said controller being programmed to feed said potassium bicarbonate salt and/or said sodium bicarbonate salt first or last.
In general, it has been found convenient to use a salt selected from the group consisting of calcium ascorbate, calcium carbonate, calcium sulfate dihydrate, calcium citrate, calcium fluoride, calcium chloride dihydrate, calcium gluconate, potassium dihydrogen phosphate, potassium gluconate, potassium citrate, potassium fluoride, potassium chloride, potassium iodide, potassium aspartate, manganese ascorbate, manganese aspartate, manganese carbonate, manganese citrate, manganese chloride, manganese gluconate, magnesium hydroxide, magnesium citrate, magnesium ascorbate, magnesium succinate, magnesium chloride hexahydrate, magnesium sulfate heptahydrate, sodium ascorbate, sodium dihydrogen phosphate, sodium carbonate, sodium gluconate, sodium fluoride, sodium chloride, zinc gluconate, zinc ascorbate, zinc sulfate heptahydrate, sodium selenite, sodium selenate, and selenomethionine in an appropriate amount based on the formulation.
A controller equipped with suitable software manages the necessary doses according to the set recipe, all controlled by metering pumps dedicated to each salt tank.
If the salt is stored in crystalline form, further advantages are obtained compared to the case where the salt is stored in a concentrated liquid solution.
The time and cost of obtaining the required amount of crystalline salt is greatly reduced because they do not require the use of dedicated labor or water resources.
Furthermore, the storage of the crystalline salt does not require any particular attention, unlike liquid brine concentrates, which require continuous and continual monitoring to assess quality and the presence of precipitates.
Drawings
Further features and advantages of the utility model will become more apparent from the description of one embodiment of a system for preparing a liquid concentrate (water that can be diluted to obtain a characteristic of natural mineral water or water not present in nature) according to the utility model, illustrated by way of example in the accompanying drawings, in which:
fig. 1 schematically illustrates one of the possible configurations of a system for producing a liquid brine concentrate.
Detailed Description
The system 1 for producing a liquid brine concentrate 10 that can be diluted to obtain water for human consumption comprises a reverse osmosis demineralizer 2 for preparing demineralized water, a sterilization means 3 for sterilizing the demineralized water, CO 2 A source 4, a carbonator 5 for carbonating the sterilized demineralized water, a mixing tank 6 connected to said carbonator 5, a supply circuit for supplying salt to said mixing tank 6, a regulating device 7 for regulating the pH of the liquid brine concentrate 10 present in the mixing tank 6 to a range between 4 and 9, and a mechanical stirring device 8 for stirring the liquid brine concentrate 10 present in the mixing tank 6.
A feed pump 16 is provided to demineralize CO from the carbonator 5 2 The saturated water is supplied to the mixing tank 6.
The demineralizer 2 may be supplied with tap water.
The sterilizing device 3 is positioned along the water circuit fed to the mixing tank 6 and may comprise one or more UV lamps.
For example, but not necessarily, a UV lamp is located downstream of the carbonator and upstream of the 0.2 micron filter; in the mixing tank, there is one additional UV lamp near the water inlet, and at the mixing tank outlet there is another 0.2 micron filter and in turn one UV lamp.
The salt supply circuit includes a plurality of storage tanks for storing salt in crystalline form.
The storage tank comprises a first tank 9a for storing potassium bicarbonate salt and/or a first tank 9a for storing sodium bicarbonate salt, at least one second tank 9b for storing calcium salt and at least one third tank 9c for storing salts other than calcium salt. In some system solutions a first tank 9a for storing potassium bicarbonate salt and a first tank 9a for storing sodium bicarbonate salt are provided, in other system solutions only one of them is provided.
For example, but not necessarily, the calcium salt may be selected from one or more calcium salts including calcium ascorbate, calcium carbonate, calcium sulfate dihydrate, calcium citrate, calcium fluoride, calcium chloride dihydrate, and calcium gluconate.
The at least one salt other than the calcium salt may for example comprise a magnesium salt.
For example, but not necessarily, the magnesium salt may be selected from one or more magnesium salts including magnesium hydroxide, magnesium citrate, magnesium ascorbate, magnesium succinate, magnesium chloride hexahydrate, and magnesium sulfate heptahydrate.
For example, but not necessarily, salts other than the magnesium salt, may include potassium dihydrogen phosphate, potassium gluconate, potassium citrate, potassium fluoride, potassium chloride, potassium iodide, potassium aspartate, manganese ascorbate, manganese aspartate, manganese carbonate, manganese citrate, manganese chloride, manganese gluconate, sodium ascorbate, sodium dihydrogen phosphate, sodium carbonate, sodium gluconate, sodium fluoride, sodium chloride, zinc gluconate, zinc ascorbate, zinc sulfate heptahydrate, sodium selenite, sodium selenate, and selenomethionine.
The reservoir can be connected to a corresponding dispenser (not shown) for weighed doses of salt in crystalline or liquid form.
The salt supply circuit may include one or more feed pumps (first feed pump 14a, second feed pump 14b, third feed pump 14 c), preferably one feed pump for each salt stored in each storage tank.
The system 1 is provided with a controller 11, which controller 11 is configured to control the sequential feeding of the salt present in the storage tanks to the mixing tank 6.
The controller 11 is programmed to control the first or last feeding of bicarbonate, i.e. potassium bicarbonate salt or sodium bicarbonate salt (if only one of them is provided), in any order or together (if both are provided).
The storage tank contains the salt in crystalline or liquid form.
The controller 11 is programmed to extract precise amounts from the storage tanks based on the individual formulations.
The controller 11 may control the activation of the feed pump with the delay required to feed bicarbonate first or last.
CO 2 The source 4 is connected to the bottom of the mixing tank 6 by means of a bubbler 12, which bubbler 12 is used for the CO 2 Bubbling into the liquid brine concentrate present in the mixing tank 6.
The mixing tank 6 is connected to a device for portioned packaging of the liquid brine concentrate.
Finally, the mixing tank 6 comprises an openable lid.
The cover may optionally have a gas-tight sealing system.
In a preferred embodiment, the system 1 coordinated by the controller 11 operates in the following manner.
The reverse osmosis demineralizer 2 obtains a first batch of demineralized water from tap water.
The demineralized water is first sterilized and then passed through carbonator 5 with CO 2 And (5) saturation.
The pump 16 is started and then after the second sterilization step, the first batch of CO is removed 2 Saturated demineralised water is introduced into the mixing tank 6.
At this point, the metering pump is started and the soluble salts present in the storage tank are extracted in programmed amounts and in sequence according to the formulation and introduced into the mixing tank 6.
The mixing tank 6 is then fed by a bubbler 12 to keep the liquid brine solution CO 2 Saturated, but only when the pH does not reach the desired value. The first or preferably last addition of sodium bicarbonate and/or potassium bicarbonate allows to avoid the formation of Ca in carbonate environments 2+ Local concentration of ions, which may trigger CaCO 3 Is a precipitate of (a) and (b).
The method of producing the liquid concentrate makes it possible to obtain satisfactory calcium concentrations without the concentration of chlorides and sulphates being too high (chlorides and in particular sulphates giving bitterness to the water) and to obtain sufficient levels of bicarbonate while maintaining the sodium and potassium concentrations at acceptable levels.
After further sterilization, the liquid saline concentrate produced in the mixing tank 6 is packaged into doses, in particular capsules or bags, for direct use by special equipment at the production and consumption sites of mineral water. Mineral water is produced and dispensed by the apparatus by diluting a liquid concentrate with demineralised sterile water.
The dilution ratio is from 1:10 to 1:60, in particular it is equal to about 1:20 for the dose in the capsule and about 1:50 for the dose in the bag.
The materials used, as well as the dimensions, may in fact be any according to requirements and to the state of the art.

Claims (7)

1. A system (1) for producing a liquid brine concentrate (10), which liquid brine concentrate (10) can be diluted to obtain water for human consumption, characterized in that it comprises a reverse osmosis demineralizer (2) for preparing demineralized water, a sterilization means (3) for sterilizing the demineralized water, CO 2 A source (4), a carbonator (5) for carbonating the sterilized demineralized water, a mixing tank (6) connected to the carbonator (5), a supply circuit for supplying salt to the mixing tank (6), a regulating device (7) for regulating the pH of the liquid brine concentrate (10) present in the mixing tank (6) to a range between 4 and 9, a mechanical stirring device (8) for stirring the liquid brine concentrate (10) present in the mixing tank (6), the supply circuit comprising a plurality of storage tanks connected to the demineralizer (2) for storing salt in crystalline or liquid form, and for each storage tank one corresponding metering pump, the storage tanks comprising a first tank (9 a) for storing potassium bicarbonate salt and/or a first tank (9 a) for storing sodium bicarbonate salt, a second tank (9 b) for at least one calcium salt storage and at least one third tank (9 c) for storing salt other than calcium salt, a controller (11) for sequentially feeding the salt present in the storage tanks into the mixing tank (6) being programmed at the end is providedFeeding the potassium bicarbonate salt and/or the sodium bicarbonate salt.
2. System (1) for producing a liquid brine concentrate (10) according to claim 1, characterized in that the calcium salt is selected from one of the following salts: calcium ascorbate, calcium carbonate, calcium sulfate dihydrate, calcium citrate, calcium fluoride, calcium chloride dihydrate, and calcium gluconate.
3. System (1) for producing a liquid brine concentrate (10) according to claim 1, characterized in that it comprises one or more storage tanks for storing magnesium salts, which can be selected from one of the following salts: magnesium hydroxide, magnesium citrate, magnesium ascorbate, magnesium succinate, magnesium chloride hexahydrate and magnesium sulfate heptahydrate.
4. System (1) for producing a liquid brine concentrate (10) according to claim 1, characterized in that the salt other than calcium salt may be selected from one of the following salts: potassium dihydrogen phosphate, potassium gluconate, potassium citrate, potassium fluoride, potassium chloride, potassium iodide, potassium aspartate, manganese ascorbate, manganese aspartate, manganese carbonate, manganese citrate, manganese chloride, manganese gluconate, sodium ascorbate, sodium dihydrogen phosphate, sodium carbonate, sodium gluconate, sodium fluoride, sodium chloride, zinc gluconate, zinc ascorbate, zinc sulfate heptahydrate, sodium selenite, sodium selenate, and selenomethionine.
5. System (1) for producing a liquid brine concentrate (10) according to claim 1, characterized in that the CO 2 The source (4) is connected to the bottom of the mixing tank (6) by means of a bubbler (12), the bubbler (12) being used for introducing CO 2 Bubbling into the liquid brine concentrate present in the mixing tank (6).
6. System (1) for producing a liquid brine concentrate (10) according to claim 1, characterized in that the mixing tank (6) is connected to a device for portioned packaging of the liquid brine concentrate.
7. System (1) for producing a liquid brine concentrate (10) according to claim 1, characterized in that the mixing tank (6) comprises an openable closure.
CN202190000357.3U 2020-03-18 2021-03-18 System for producing liquid brine concentrate Active CN219460262U (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
IT202020000001216U IT202000001216U1 (en) 2020-03-18 2020-03-18 PLANT FOR THE PRODUCTION OF A DILUTABLE LIQUID SALINE CONCENTRATE FOR OBTAINING WATER INTENDED FOR HUMAN CONSUMPTION
IT202020000001216 2020-03-18
PCT/IT2021/000013 WO2021186482A1 (en) 2020-03-18 2021-03-18 Production plant of a dilutable liquid saline concentrate for obtaining water intended for human consumption

Publications (1)

Publication Number Publication Date
CN219460262U true CN219460262U (en) 2023-08-04

Family

ID=75825818

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202190000357.3U Active CN219460262U (en) 2020-03-18 2021-03-18 System for producing liquid brine concentrate

Country Status (4)

Country Link
EP (1) EP4106549A1 (en)
CN (1) CN219460262U (en)
IT (1) IT202000001216U1 (en)
WO (1) WO2021186482A1 (en)

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL1023522C2 (en) * 2003-05-23 2004-11-24 Sara Lee De Nv Mineral concentrate.
IT1401899B1 (en) * 2010-06-16 2013-08-28 Berger Johann PROCESS AND PLANT FOR THE PREPARATION OF A DILUIBLE LIQUID CONCENTRATE FOR THE ACHIEVEMENT OF WATER INTENDED FOR HUMAN CONSUMPTION AND PRESENTING THE CHARACTERISTICS OF A MINERAL WATER, LIQUID CONCENTRATE AND WATER INTENDED FOR HUMAN CONSUMPTION SO FINE
EP3091862B1 (en) * 2013-12-18 2020-12-02 Société des Produits Nestlé S.A. Process for supplying magnesium and/or calcium enriched water based beverage

Also Published As

Publication number Publication date
EP4106549A1 (en) 2022-12-28
IT202000001216U1 (en) 2021-09-18
WO2021186482A1 (en) 2021-09-23

Similar Documents

Publication Publication Date Title
CA2098839C (en) Dialysate production system with dialysate pellets
CN108367952A (en) Purified and remineralization water
US11191290B2 (en) Process for supplying magnesium and/or calcium enriched water based beverage and associated manufacturing apparatus
JP2004530424A (en) Methods, apparatus and compositions for enhancing calcium in beverages
US8277848B2 (en) Method for preparing aqueous solution of high-concentration calcium phosphate stable in neutral pH range
JPH04259469A (en) Method and apparatus for preparing medicine solution such as dialysis liquid
WO2011136091A1 (en) Weakly acidic hypochlorous acid, and apparatus and method for production thereof
CA2377076C (en) Preparation and metering of components mixed with co2
CN219460262U (en) System for producing liquid brine concentrate
EP2582635B1 (en) Process for the preparation of a dilutable liquid concentrate to obtain water destined for human consumption and having the characteristics of a natural mineral water
US11638439B2 (en) Vitamin D-fortified water and method of manufacturing thereof
RU2568846C2 (en) Acid dialysis concentrate
JP2001327975A (en) Residual chlorine correction apparatus for dental tap water
US20190045823A1 (en) A process for making a liquid low sodium food-grade salt
CZ2003198A3 (en) Process for preparing potable water and potable water prepared in such a manner
JP3991296B2 (en) Method for producing residual chlorine-containing water and apparatus therefor
JP2001137854A (en) Production method of sterilizing water containing hypochlorous acid, production device of high concentration salt water used therein, and device for sterilizing water containing hypochlorous acid using this device
WO2012053942A1 (en) Solutions for bicarbonate hemodialysis
US20230406703A1 (en) Hypochlorite water production method and production apparatus
KR20240140785A (en) Method for producing mineral ionic liquid
CN110621300A (en) Device for the temporary generation of a physiological or isotonic aqueous solution based on water
JP5853275B2 (en) Weakly acidic hypochlorous acid, and production apparatus and production method thereof
CN117303681A (en) Seawater desalination water quality adjusting and storing device and adjusting process thereof
JP5692657B2 (en) Weakly acidic hypochlorous acid, and production apparatus and production method thereof
JPH0461865A (en) Solid agent dissolution type dialyzing fluid feed device and method therefor

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant