WO2011120068A1 - Procédé d'optimisation d'eau potable - Google Patents

Procédé d'optimisation d'eau potable Download PDF

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Publication number
WO2011120068A1
WO2011120068A1 PCT/AT2011/000161 AT2011000161W WO2011120068A1 WO 2011120068 A1 WO2011120068 A1 WO 2011120068A1 AT 2011000161 W AT2011000161 W AT 2011000161W WO 2011120068 A1 WO2011120068 A1 WO 2011120068A1
Authority
WO
WIPO (PCT)
Prior art keywords
water
mineral
column
ingredients
tank
Prior art date
Application number
PCT/AT2011/000161
Other languages
German (de)
English (en)
Inventor
Christoph Rudolf Dietrichsteiner
Manfred Dietrichsteiner
Original Assignee
Christoph Rudolf Dietrichsteiner
Manfred Dietrichsteiner
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 Christoph Rudolf Dietrichsteiner, Manfred Dietrichsteiner filed Critical Christoph Rudolf Dietrichsteiner
Publication of WO2011120068A1 publication Critical patent/WO2011120068A1/fr

Links

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
    • C02F1/68—Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable water
    • C02F1/685—Devices for dosing the additives
    • C02F1/688—Devices in which the water progressively dissolves a solid compound
    • 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
    • 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
    • C02F1/20—Treatment of water, waste water, or sewage by degassing, i.e. liberation of dissolved 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
    • C02F1/66—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
    • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/02—Non-contaminated water, e.g. for industrial water supply
    • C02F2103/026—Treating water for medical or cosmetic purposes
    • 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]
    • 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
    • C02F2209/06—Controlling or monitoring parameters in water treatment pH
    • 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
    • C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
    • 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

Definitions

  • the invention relates to a method for optimizing drinking water, preferably low-ion, raw water and a plant for carrying out the method according to the invention.
  • the occurrence of over-, under- and malnutrition is not only dependent on the topographical situation and the presence or availability of the food supply, but also on the capacity of the metabolism to utilize and be able to use the supplied nutrients and active ingredients.
  • the undersupply of essential nutrients and active ingredients can best be compensated by increased intake.
  • the consequences of poor food quality and low food quantity can be compensated by the direct supply of high-quality nutrients and active ingredients that are easily accessible to the body.
  • US 5,910,233 A describes a process for the production of mineralized drinking water.
  • the water is first distilled and then mixed with various materials by flowing the water through different layers of soil material in a device.
  • Object of the present invention is for technically produced drinking water
  • the object of the invention is in each case independent by a method for optimizing drinking water from raw water comprising the steps of a) feeding the raw water into a tank, b) degassing the raw water, c) flowing the degassed water through at least three mineral columns and by a system for Carrying out the method, wherein at least one tank and at least three mineral columns, and optionally in each case at least one interface for hygiene, the metered addition of ingredients and aftertreatment are arranged.
  • the advantage here is that even recycled or originally demineralized water has an appealing taste.
  • the pH of the water in particular after the feed, can be adjusted to a value selected from a range with a lower limit of 5.5 and an upper limit of 7, optionally with sulfuric acid or sodium bicarbonate solution, whereby a physiologically compatible pH value is obtained. Value is achieved, and yet no health impairment caused by the acid or base, because they are used in such small quantities.
  • the redox potential of the water in particular after the pH adjustment, can be optimized by adding a hydrogen peroxide solution, and thereby the water to be treated act as an oxidizing agent.
  • the water is preferably degassed by a baffle plate column with Raschig rings, whereby dissolved gases and other volatile components that interfere with the process of the invention can be removed.
  • the water flows through a first mineral column with trickled zeolite with the properties of clinoptilolite with a grain size of a range with a lower limit of 6 mm and an upper limit of 10 mm, the high content of Si0 2 certifies this natural mineral healing properties becomes.
  • the second mineral column is filled with feldspar material, preferably of the Bissteinerwald, having a grain size of a range with a lower limit of 3 mm and an upper limit of 10 mm, whereby rock material with numerous minerals and trace elements is used and the necessity of these materials for conservation the health of science has been proven many times.
  • feldspar material preferably of the Bissteinerwald
  • a marble column is used, preferably from the Untersberg, with an average grain size of 5 mm to 25 mm, preferably 12 mm, whereby a further enrichment of minerals and trace elements of the water to be treated can be achieved.
  • At least one interface for hygiene-securing measures and / or for the metered addition of different ingredients and / or the aftertreatment of the water is arranged, whereby the drinking water produced by the method according to the invention can be further optimized.
  • ingredients are understood as meaning nutrients, minerals, trace elements, vitamins, provitamins, proteins, amino acids and derivatives of amino acids, flavors, colorants, etc.
  • the inventive method for producing a sensory optimized drinking fluid base is a supply of minerals and optionally trace elements and / or other active components selected from a group comprising vitamins or provitamins, proteins, amino acids and derivatives of Amino acids, etc. possible.
  • the ingredients and their concentrations can each be adjusted according to the needs of the respective target group. Furthermore, it is thereby possible to compensate for diet-related deficiency symptoms, for example by an increased content of nutrients in the drinking liquid. Also, the addition of nutrients preceding and subsequent technical steps of the invention support these advantages.
  • the inventive production of drinking water is due to the use of the technical system described in more detail below.
  • a content of poor or free, in particular ion-poor or demineralized water is used.
  • the degree of purity of the water used depends on the method of purification used, for example distillation, pressure filtration through a semipermeable membrane, removal of ralization, methods using ion exchangers, ultrafiltration, osmosis, reverse osmosis, evaporation, double reverse osmosis, etc. It can also be used in a technical process occurring water that meets the conditions mentioned.
  • the process according to the invention not only provides an improvement in the drinking attractiveness of water, but also provides an improved basis for the production of drinking liquids in general.
  • the process steps mentioned below define the manufacturing process. On those steps, which are necessary for the sterility and hygiene of the manufacturing process and depending on the nature of the end product to be achieved and the equipment used for manufacturing, which may vary for each end product is not explicitly discussed, but are known in the art , The process steps can be subdivided as follows: 1. feed of the purified base water or raw water, 2. pH optimization (optional), 3. optimization of the redox potential (optional), 4th degassing column, 5. first mineral column, 6th interface hygiene (optional ), 7. Second mineral column, 8th interface for metered additions (optional), 9th third mineral column, 10th interface post-treatment (optional), 11th product removal or filling station.
  • the feed and raw water used is an ion-poor water produced by distillation, condensation, reverse osmosis or similar processes.
  • a water produced during a technical process that fulfills the stated criteria can also be used.
  • the process according to the invention is described for demineralized waters, it is also possible to use it on moderately to heavily mineralized drinking waters with low enjoyment attractiveness.
  • the pH may be unfavorable.
  • the adjustment of the pH value is carried out with 10% sulfuric acid, or 10% sodium bicarbonate solution. Since the raw water is a low-mineral unbuffered water, requires only very small amounts that do not play a role in terms of food compatibility.
  • the content of dissolved gases and other volatile components may affect the effect of the method according to the invention.
  • a baffle plate column or another, comparable in effect process step for degassing is provided.
  • the column is filled with Raschig rings, these short tube pieces made of glass or ceramic serve to increase the surface area.
  • the liquid medium is introduced into the column in the head region and from below a countercurrent with a neutral gas, such as nitrogen or helium, is applied and blown.
  • Filter candles are known to those skilled in the field of drinking water treatment from the prior art devices. Examples of this are activated carbon filters for the separation of organic substances in drinking water, or ion exchangers for the reduction of water hardness.
  • the filter cartridges used for water treatment purposes have a diameter of 4 - 8 inches and a length of 10 - 30 inches and can be adapted to the flow rate. These are suitable to be filled even with suitable material and easily used or changed. Filter cartridges prove to be low maintenance and particularly practical in the test facilities.
  • the filling height of the mineral columns must be selected such that the uniform distribution of the water flowing through is ensured. This is certainly true if at the top of the column at least 1cm free height remains and the grain size of the mineral granules has a dimension of 3.0 mm to 15 mm. These dimensions can also be mixed in a filter candle, which counteracts rapid blocking.
  • the first mineral column is filled with zeolite.
  • the properties of the zeolite in effect, are similar to those of clinoptilolite.
  • Various tested artificially prepared zeolites are not or barely usable for the purpose. Because of the physical properties of zeolite, trickling is necessary. Inappropriate application of the water to the column leads to increased material abrasion and blockage.
  • the grain size and the column length must be adapted to the desired throughput. In the test facilities, a particle size of 6 mm to 10 mm proved itself.
  • the local hygiene requirements imposed by food legislation must be complied with, so an interface should be provided for hygiene measures.
  • Hygienic interfaces can be arranged between the mineral columns. These may be arranged after the first, second and third mineral columns as well as after only one of the three mineral columns. Separation of mineral abrasion, eg by filtration or centrifugation, can also be carried out at these hygiene interfaces. A physical degerming process ensures the sterility of the drinking liquid. In any case, the water used must comply with the relevant national food regulations.
  • the second mineral column is filled with a feldspar mineral. Optimization has shown that choosing the right material is crucial.
  • the mineral mined in the Bissteinerwald by Schindele has proved to be optimal.
  • the grain size and the column length must be adapted to the desired throughput and, as with the first mineral column, most suitably accomplished with the "filter candles" described above limited to 10 mm diameter.
  • the previously described grain sizes of the minerals used in the mineral columns are for mineral columns with 4 to 8 inch diameter filter cartridges and 10 to 30 inches in diameter.
  • the rock deposit of "Schindele's Minerals TM" is a volcanic cone of metamorphic para-gneiss of amphibolite facies formed by a fracture of the Earth's crust.
  • the respective quantities of nutrients and active substances such as minerals, trace elements and / or further active components, selected from a group comprising vitamins or provitamins, proteins, amino acids and derivatives of amino acids, etc.
  • nutrients and active substances such as minerals, trace elements and / or further active components, selected from a group comprising vitamins or provitamins, proteins, amino acids and derivatives of amino acids, etc.
  • the homogeneity of the product is achieved by buffering in a homogenizing tank. If necessary, an additional hygiene interface is added to the dosing, such as a degermination process.
  • ⁇ -carotene a suitable active substance, such as ⁇ -carotene.
  • flavors can eg: cocoa, tea, fruit, spice u. Coffee flavors are used.
  • Fruit juice concentrates may be eg orange juice, lemon juice, etc. Usable additives must comply with food law.
  • the third mineral column contains marble as in the previously described steps in a preferably self-filling filter cartridge. It has also been shown here that, depending on the degree of crystallization, there is an activity maximum. Interestingly, a Mamor with comparatively low degree of crystallization, such as e.g. Untersberger marble opposite high-crystalline marble the best effect.
  • the Untersberger marble occurs on the northern slope of the Untersberg (Northern Limestone Alps) near Mariestenbrunn (Salzburg).
  • the rock formed in the Upper Cretaceous about 85 million years ago is a surf breccia from the older rocks of the Untersberg (predominantly Dachstein limestone and Piassenkalk).
  • the very dense and weather-resistant rock is composed of fine to rare coarse-grained fragments and rolls, cemented with calcite. It varies in color from light beige (with red spots) to pink and reddish, rarely yellow. All types of Untersberger marble are fine and coarse conglomerates, consisting of limestone rubble and fragments of older rocks of the Untersberg (mainly Piassenkalk). In addition, there are small dark red laterite balls and fragments of snails, mussels, etc., but only the thick-skinned hipurites and oysters have escaped smashing in the surf. However, the conglomerate stone nature is rarely recognizable because during consolidation the boundaries were blurred by recrystallization.
  • the filter cartridges described above are used as mineral columns.
  • End areas it may be useful to increase the number of mineral columns and fill with suitable rock granules.
  • the process steps are chosen so that they build on each other and result in toothing that harmonic whole that distinguishes the uniqueness of Trinkakzeptanzverêtung invention.

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  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Non-Alcoholic Beverages (AREA)
  • Physical Water Treatments (AREA)
  • Water Treatment By Sorption (AREA)

Abstract

L'invention concerne un procédé d'optimisation d'eau potable à partir d'eau brute, de préférence pauvre en ions, comprenant : a) l'amenée de l'eau brute dans un réservoir, b) le dégazage de l'eau brute dans le réservoir, c) le passage de l'eau dégazée dans au moins trois colonnes à garnissage minéral. L'invention concerne en outre une installation permettant de mettre en œuvre le procédé selon l'invention, dans laquelle sont disposés au moins un réservoir et au moins trois colonnes à garnissage minéral, et facultativement au moins une interface respective pour l'hygiène, l'addition dosée de constituants et le retraitement.
PCT/AT2011/000161 2010-04-02 2011-04-01 Procédé d'optimisation d'eau potable WO2011120068A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
ATA539/2010 2010-04-02
ATA539/2010A AT509658B1 (de) 2010-04-02 2010-04-02 Verfahren zur optimierung von trinkwasser

Publications (1)

Publication Number Publication Date
WO2011120068A1 true WO2011120068A1 (fr) 2011-10-06

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PCT/AT2011/000161 WO2011120068A1 (fr) 2010-04-02 2011-04-01 Procédé d'optimisation d'eau potable

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AT (1) AT509658B1 (fr)
WO (1) WO2011120068A1 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2499992A (en) * 2012-03-05 2013-09-11 Ide Technologies Ltd Water mineralization

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111239266B (zh) * 2018-11-29 2021-10-22 中国科学院大连化学物理研究所 一种细内径毛细管液相色谱柱填充方法及匀浆罐

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0421563A1 (fr) * 1989-09-18 1991-04-10 Shinki Sangyo Co., Ltd. Procédé et dispositif pour la production d'eau minérale activée
US5910233A (en) 1997-08-08 1999-06-08 Berg; Gary Method of and device for producing mineralized drinking water
EP0928565A1 (fr) * 1997-12-17 1999-07-14 Meta Handelsgesellschaft m.b.H. Liquide potable
WO2002096225A2 (fr) * 2001-05-31 2002-12-05 The Procter & Gamble Company Eau potable enrichie
WO2009066151A2 (fr) * 2007-11-20 2009-05-28 Suk, Diana, Hyun, Choon Dispositif pour activer des liquides

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19926752A1 (de) * 1999-06-11 2000-12-14 Dynamics Umweltschutz Verfahren zur Erzielung eines biologisch hochwertigen Wassers, z. B. Fischwassers
DE19933204A1 (de) * 1999-07-15 2001-01-18 Dieter Meyer Wasseraufbereitungsvorrichtung

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0421563A1 (fr) * 1989-09-18 1991-04-10 Shinki Sangyo Co., Ltd. Procédé et dispositif pour la production d'eau minérale activée
US5910233A (en) 1997-08-08 1999-06-08 Berg; Gary Method of and device for producing mineralized drinking water
EP0928565A1 (fr) * 1997-12-17 1999-07-14 Meta Handelsgesellschaft m.b.H. Liquide potable
WO2002096225A2 (fr) * 2001-05-31 2002-12-05 The Procter & Gamble Company Eau potable enrichie
WO2009066151A2 (fr) * 2007-11-20 2009-05-28 Suk, Diana, Hyun, Choon Dispositif pour activer des liquides

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2499992A (en) * 2012-03-05 2013-09-11 Ide Technologies Ltd Water mineralization
GB2499992B (en) * 2012-03-05 2014-12-10 Ide Technologies Ltd Water mineralization

Also Published As

Publication number Publication date
AT509658B1 (de) 2016-01-15
AT509658A1 (de) 2011-10-15

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