RU2555330C2 - Drinking water production method and installation for drinking water production - Google Patents

Abstract

FIELD: food industry.

SUBSTANCE: inventions group relates to food industry and may be used for drinking water production. For the said purpose water is drawn from a natural source, settled with access of atmospheric oxygen in 20-40 m³ vessels during 10-15 h and treated by way of passing through a device having an external and an internal cylinders. Water passes through the central cavity of the device from the dropping pipe and is whirled by counterflows spiralwise in the magnetic pipe. Then one proceeds with treatment with fullerenes by way of passing water through a cylindrical device containing an internal cylinder with holes whereto one periodically adds preliminarily prepared source water with hydrated fullerenes C₆₀HyFn, such water produced as follows: into a 2 l flask one pours 2 l of source water and adds hydrated fullerene in a concentration of 14.4mg/l; the flask is rotated during 1 min counter-clockwise at a rate corresponding to a funnel formation. Then the water is settled during 2 min and repeatedly rotated during 30 sec and then again settled during 2 min; one takes 1 ml of the resultant solution and pours it into 1 l of source water; the procedure is repeated until production of a solution of fullerenes C₆₀HyFn with concentration equal to 10^-20 mol/l. the produced drinking water is bottled. A device for drinking water production is additionally produced.

EFFECT: inventions group ensures production of water suitable for regular consumption by man and having improved taste and organoleptic properties.

2 cl, 1 dwg, 1 tbl, 2 ex

Description

The invention relates to a method and apparatus for treating water using fullerenes and can be used in the food industry to improve the properties of drinking water.

A known method of restoring water to its original properties, the processing is carried out on the next device, which contains a housing 10 with inlet and outlet openings 46, 48. The flow path is limited to containers 30, 32, which contain the medium acting on water. The housing is double-walled with an outer 24 and inner wall 16, which limit the first closed tank 30 for the environment. The inner wall extends coaxially forming a closed container 32 of the second tubular vessel in the form of a first inner pipe 14, which extends from the perimeter and from the bottom at a distance from the inner wall. Flat separation elements 54, 56 extend from the first inner pipe in a radial direction, the lower end edges of which end at the level of the lower wall 18 of the first inner pipe and which divide the intermediate space between the first and second inner pipes into two partial spaces 58, 60. One of the spaces connected to the inlet, and the other to the outlet. The inlet and outlet openings are limited by a sleeve or pipe section 50, 52 that are sealed relative to the intermediate space. Partial spaces are connected in the lower zone of the housing, located at a distance from the inlet and outlet openings. From the first inner pipe, protrusions 62, 64, 66, 68 extend into a partial space, forming a swirling device (RU 2450975 C2, 05.20.2012).

The disadvantage of this method is that the processing method is carried out on a structurally complex device and does not provide the desired properties for water.

A known method of producing drinking water, including the evaporation of water and the conversion of steam into a condensed liquid state, the condensate is additionally treated with natural mineral schungite dispersion of 0.5-10 mm with a volume ratio of T: W = 0.5-2.0 for 12- 24 hours, and the resulting drinking water is cooled to a temperature of 0 - (- 18) ° C. The treatment of condensate with shungite under the conditions of the claimed parameters provides an additional effect of natural marcial healing waters. This is due to the fact that during processing, as well as under natural conditions (marcial sources are located in Karelia on massive outcrops of schungite plates), globular carbon is extracted - fullerene of grade C ₆₀ , the content of which in shungite is in the range 0.001-0, 1% (RU 2253630 C2, 06/10/2005).

The disadvantage of this method is the storage of water only in frozen form, and the water obtained by this method cannot be used for a long time.

A known method of electrochemical water treatment, including electrochemical treatment in a multi-membrane electrolyzer, in this case, after passing through the coarse cleaning step, water is supplied only to the middle chamber of the electrolyzer, separated by semi-permeable membranes from the anode and cathode chambers, where water is divided into three streams through semi-permeable membranes, the last of which fill the lateral anode and cathode chambers equipped with nozzles for the exit of anolyte and catholyte, while using the elements installed in the middle chamber, forms They twist a winding stream of purified water, which alternately approaches either the anode or cathode mebran, after leaving the cell, the stream of purified water from the middle chamber enters the magnetizing device, passes through a swirler located in the pyramidal casing, and enters the container, where together with the crystal is exposed to light and electromagnetic radiation with a wavelength of 100,000 m to 1 mm. Semi-permeable membranes contain shungite, silicon and silver in their structure to saturate the purified water with fullerenes and silicon and silver ions (RU 2388702 C2, 05/10/2010).

The disadvantage of this method is the silver content in the membranes, since in a high concentration in water silver kills the microflora of the body, both harmful and beneficial - causing dysbiosis, and in small quantities it kills far from all pathogenic bacteria, but only some.

The closest analogue is a method for producing water containing fullerenes, which include water molecules and float in water when burning a mixed gas of oxygen and hydrogen in water at high pressure and when burning graphite using the produced combustion gas, and a device for implementing the method, which is resistant to pressure container, jet nozzle for a mixed gas of oxygen, hydrogen and graphite, an ignition system, a combustion chamber and a filtration device (US 6833145 B1, 12/21/2004).

The disadvantage of the closest analogue is that the known method and device for its implementation are not environmentally friendly, the resulting water cannot be used for continuous use by humans, since they contain chemical elements released during combustion, which can accumulate in the human body, which can provoke or other diseases, increased energy costs.

The objective of the invention is to improve the quality of water, which can be used for constant human consumption without harm to health, as well as reducing energy consumption in the production of water, increasing reliability and environmental friendliness, as well as improving the taste and organoleptic properties of water.

The problem is solved in that the method of producing drinking water, according to the invention, provides for successive stages of the process: water intake from a natural source, sedimentation of water with the access of oxygen in the tank with a volume of 20-40 m ³ for 10-15 hours, water treatment, which is carried out by passing water through a device having an external and internal cylinder, water passes from a supply pipe through a central cavity of the device, is twisted by counter flows in a spiral device and into pipe, and then processing with fullerenes, which is carried out by passing water through a cylindrical device containing an inner cylinder with holes, into which periodically added pre-prepared source water with hydrated C ₆₀ HyFn fullerenes is added and which is obtained as follows: pour 2 into a 2-liter flask l of the source water and hydrated fullerene at a concentration of 14.4 mg / l is added to it, the flask is rotated counterclockwise for 1 minute at a speed conducive to the formation of a funnel, then water is defended for 2 minutes, rotated again for 30 seconds, again defended for 2 minutes, 1 ml is taken from the resulting solution and poured into 1 liter of feed water, the procedure is repeated until a solution of C ₆₀ HyFn fullerenes with a concentration of 10 ^-20 mol is obtained / l, bottling the resulting drinking water.

Also, the problem is solved in that the installation for producing drinking water, according to the invention, contains at least one device for water intake, a stainless steel tank with a volume of 20-40 m ³ , a device having an external and internal cylinder, through a central cavity The device passes water from a supply pipe, which is twisted by oncoming flows in a spiral and in a magnetic pipe, a device for treating water with fullerenes, which is a cylindrical device containing an inner cylinder with an opening s, which are periodically added a previously prepared raw water with hydrated fullerene C ₆₀ HyFn, wherein the inner cylinder has a hole size of 1-100 nm, and a filling system.

The technical result of the claimed invention is the production of drinking water with improved taste and organoleptic properties, with the combined use of all these types of processing, namely oxygen saturation and treatment with fullerenes under the stated modes due to the action of the above types of processing.

Fullerenes are not a drug. The main effect of fullerenes in our body is the collection and neutralization of free radicals (oxidants). Free radicals have a destructive effect on the cells of our body. Fullerenes do not have a targeted therapeutic effect on a specific disease or organ. They act as a powerful long-term antioxidant. Free radicals occur during oxidation. A small percentage of their presence in the body is even necessary, but excess is fatal.

It is the claimed sequence, modes of the process and the claimed device that allows you to get drinking water collected from a natural source with the following properties:

- surface tension of water from a natural source of 59-76 dyne / cm ² , and the resulting water - 55-49 dyne / cm ² ;

- the pH of the water from a natural source is 5.5-6.5, and the resulting water is 7.2-8.5;

- ORP of water from a natural source +250 - +350, and the resulting water - (+150) - (- 40).

The water obtained in the declared modes, allows you to get water with the above properties. Saturation of water with oxygen for less than 10 hours can lead to low oxygen saturation of the treated water and insufficiently high level of time-stable oxygenated state of treated water. At the same time, an increase in the time of oxygen saturation for more than 15 hours does not improve the quality of the produced drinking water, but increases the energy consumption, which affects the cost of production. The passage of water from the supply pipe along the spiral of the device and through the magnetic pipe allows you to get water with the declared parameters of the redox potential and pH. Treatment with fullerenes under the stated conditions allows to obtain water with certain properties, with a decrease in the concentration of fullerene solutions, the resulting water will not have the declared properties, and with an increase in the concentration of fullerene solutions, the water will not be suitable for drinking. Reducing the size of the holes of the inner cylinder, a device for processing fullerenes, will not allow the necessary treatment with fullerenes, and increasing the size of the holes can lead to an increased content of fullerenes in the finished water, which will also adversely affect the quality of the resulting water.

The technical result will be achieved only when using the declared modes.

In FIG. 1 is a structural block diagram of an apparatus for producing drinking water.

Installation for producing drinking water, at least one device for water intake 1, a stainless steel container 2, with a volume of 20-40 m ³ , a device 3 having an external and internal cylinder, water passes from the supply pipe through the central cavity of the device, which twisted by counter flows in a spiral and in a magnetic tube, a device for treating water with fullerenes 4, which is a cylindrical device containing an inner cylinder with holes, into which a previously prepared and similar water with hydrated fullerenes C ₆₀ HyFn, while the inner cylinder has holes 1-100 nm in size, and a filling system 5.

The method is as follows.

Water, at least one of the devices 1 is taken from a natural source and sent to a container 2, which is a stainless steel tank with a volume of 20-40 m ³ . In the aforementioned container, water settles with oxygen for 10-15 hours. After infusion, water is supplied to the device 3. Processing is carried out by passing water through a device having an external and internal cylinder. Through the central cavity of the device, water passes from the supply pipe, is twisted by counter flows in a spiral and in a magnetic pipe. Next, the treated water enters the device for processing fullerenes 4. The device 4 is a cylindrical device containing an inner cylinder with holes. In this case, pre-prepared source water with hydrated C ₆₀ HyFn fullerenes is periodically added to the inner cylinder. Water with hydrated C ₆₀ HyFn fullerenes was prepared as follows: pour 2 L of feed water into a 2-liter flask and add hydrated fullerene at a concentration of 14.4 mg / L, rotate the flask counterclockwise for 1 minute at a speed that promotes the formation of funnels, then water is defended for 2 minutes, rotated again for 30 seconds, again defended for 2 minutes, 1 ml is taken from the resulting solution and poured into 1 liter of source water, the procedure is repeated until a solution of C ₆₀ HyFn fullerenes with a concentration of 10 is obtained ^-20 mol / l. And in the outer cylinder of device 4, water enters from device 3, which is enriched in C ₆₀ HyFn fullerenes. After complete processing, the water is sent for bottling.

The term “energy saturation of water” refers to the intensity (amplitude) and duration of a flash of radiation observed when “Reagent” (a solution of ferrous salt and a luminescence sensitizer — luminol) is added to the water, recorded by a single-photon multiplier detector. To measure the energy saturation of water, 1 ml of test water was poured into a disposable Eppendorf tube and 10 μl of Reagent were added. A reagent was used which, after adding to water, the final concentrations of FeSO4 and luminol were 10 μM and 10 μM, respectively. After adding the reagent to water and mixing, the tube was placed in a single photon counter “Biotoke 7” and radiation from the sample was recorded for a period of at least 60 seconds with a time resolution of 1 second. Each measurement was carried out in three parallels. According to the measurement results, the average value of the amplitudes of the radiation waves and the sum of the pulses in 50 seconds were calculated. The experiment was subjected to water taken from the source, and water obtained by the claimed method. After 24 hours of keeping the source and finished water in contact with air, the activity of the finished water is several times higher than the activity of the source water, while the pH values of these waters did not differ.

Example 1

The organoleptic properties of the resulting water were tested on volunteers. The test involved 15 people who took the water processed by the claimed method and water from the same source, prepared according to the prototype. A softer taste of water processed by the claimed method was noted by 14 people.

Example 2

For water treatment, the claimed installation was applied. Water for processing was taken from a natural source in Slovenia (Ljubljana). Table 1 presents the indicators of water before and after treatment. 5 experiments were carried out.

From the table. 1 it follows that with the claimed processing method, the claimed device has the effect of decreasing the ORP and the surface tension of water with increasing pH.

Going beyond the stated parameters of the process will not allow you to get drinking water that has exactly the above properties.

Using the resulting drinking water will expand the range of drinking water.

Claims (2)

1. A method of producing drinking water, characterized in that it provides for successive stages of the process: water intake from a natural source, sedimentation of water with the access of oxygen in air in a volume of 20-40 m ³ for 10-15 hours, processing, which is carried out by passing water, through a device having an external and internal cylinder, water passes from the supply pipe through the central cavity of the device, is twisted by counter flows in a spiral and in a magnetic pipe, and then processing by fullerenes, which is carried out by passing water through a cylindrical device containing an inner cylinder with holes into which pre-prepared feed water with hydrated C ₆₀ HyFn fullerenes is periodically added, which is prepared as follows: 2 L of feed water is poured into a 2-liter flask and hydrated fullerene is added to it at a concentration of 14.4 mg / l, the flask is rotated for 1 minute counterclockwise at a speed conducive to the formation of a funnel, then the water is defended for 2 minutes, repeatedly ayut for 30 seconds, again assert 2 minutes from the resulting solution, take 1 mL and poured into 1 liter of initial water, the procedure is repeated until a solution C ₆₀ fullerenes HyFn a concentration of 10 ^-20 mol / l, bottled drinking water. 2. Installation for producing drinking water according to claim 1, characterized in that it contains at least one device for water intake, a stainless steel tank with a volume of 20-40 m ³ , a device having an external and internal cylinder, through a central cavity The device passes water from a supply pipe, which is twisted by oncoming flows in a spiral and in a magnetic pipe, a device for treating water with fullerenes, which is a cylindrical device containing an inner cylinder with holes, into which it is periodically added Pre-prepared feed water with hydrated C ₆₀ HyFn fullerenes is added, while the inner cylinder has openings of 1-100 nm in size and a filling system.

Images