KR20190138004A - a system for clean water on the sea - Google Patents

Abstract

The present invention relates to a water treatment system used at sea. The water treatment system used at sea is configured to eliminate microorganisms in introduced seawater in a seawater supply pipe and reduce binding force of the seawater by means of light energy, wavelength energy and a microwave. Seawater supplied through the seawater supply pipe passes through a water purification system installed on a ship (A) on the sea so that organic substances, contaminants, and microorganisms contained in the seawater are separated and removed, and a part of seawater having a self-purification ability is discharged to the sea. The remaining seawater passes through water purification processes of a floatation separation chamber, a decomposition chamber, a coagulating reaction chamber, a settling chamber, and a filter so that organic substances, contaminants, and microorganisms contained in the seawater are separated to facilitate separation of salts. The seawater purified thereby is supplied to a seawater heating chamber, a first heat exchange pipe, and a second heat exchange pipe, and heated by a heat exchange method and a thermodilution method in which a heat exchange unit, a re-combustion unit, a focused combustion unit, a light concentration plate, a magnetization contact piece, an ultrasonic generator, and a high frequency generator are used. Accordingly, steam from which salts are removed is discharged and then, the seawater is turned into pure water with relatively low energy by an ion-exchange method. If necessary, it is possible to obtain drinking water while the seawater passes through a desalination layer on which pumice stone, elvan, zeolite, tourmaline, and red clay are stacked.

Description

System for clean water on the sea

The present invention relates to a water treatment system in the sea, and in particular, a portion of the seawater purified by separating the organic matter, pollutants and microorganisms contained in the seawater while undergoing water purification process for the incoming seawater is self-cleaning water purification The discharged seawater is discharged back to the sea, and organic matter, pollutants and microorganisms separated from the seawater are used as solid fuel materials, while the remainder of the purified seawater is heated by heat exchange and thermal dilution. While applying ultrasonic wave and microwave while using ion exchange method, it converts seawater to pure water using less energy, and can drink while passing through desalination layer of pumice, ganban stone, zeolite, tourmaline and ocher as needed. The present invention relates to a water treatment system at sea in which drinking water can be obtained.

In general, the seawater is being polluted day by day due to the pollutants and rivers thrown away from rivers and lakes.

Nevertheless, there is little effort to directly clean up the seawater, and only a part of the seawater is dehydrated to use drinking water or drinking water.

In addition, seawater desalination is a series of water treatment processes that removes dissolved substances, including salts, from seawater, which cannot be directly used for domestic or industrial water, to obtain high-purity drinking water, domestic water, and industrial water. Also known as, the device used to produce seawater as freshwater is called a seawater desalination device.

The seawater desalination device is a device that makes salt water by removing salt in an economical way so that 98% of seawater or brackish water on earth can be useful for human life.

When rain falls on the ground, it flows into the sea through several paths, while salts and other substances dissolve as water flows on and into the ground, increasing salinity.

Water arriving at sea or in lowlands is evaporated by solar energy, leaving salts in the evaporation process, and only pure water forms clouds and rains.

This shows the evaporation process where physical separation takes place and the condensation process where water vapor meets cold air and turns into rainwater, which is a representative desalination seen in natural phenomena.

The seawater desalination method is largely based on the principle of heating seawater using a heat source and condensing the generated steam to obtain fresh water by using evaporation and osmosis in reverse, and passing the seawater through a semi-permeable membrane. Reverse osmosis (hereinafter referred to as RO) of membrane separation to produce fresh water is a representative method of seawater desalination.

The evaporation method using a heat source is classified into a multi-stage evaporation method (hereinafter referred to as MSF) and a multi-effect method (hereinafter referred to as MED) according to the flow of the fluid.

The membrane separation method can be divided into reverse osmosis and forward osmosis.

The reverse osmosis process (RO) is a method of separating ionic substances and pure water from a seawater using a reverse osmosis membrane, and in order to separate ionic substances and pure water from seawater, The above high pressure is required and the pressure at this time is called reverse osmosis. In general, since the use of a high-pressure pump that consumes most of the power as the seawater supply means as described above, there is a disadvantage that a considerable amount of energy is consumed for desalination of seawater.

In addition, the large-scale desalination treatment by the membrane separation method is composed of a plurality of stages 111, as shown in Figure 1, the evaporator 110 divided into a heat recovery section 110a and the heat shield section (110b) is The stage 111 includes a condenser 112, a water separator 113, and a flashing chamber 114.

In addition, one side of the evaporator 110 is a brine heater (Brine Heater) for heating the preheated circulating brine (Recycling Brine) preheated to the operating temperature using the heat energy of the low-pressure steam supplied through the steam supply pipe ( 120 is provided, the other side of the evaporator 110 is provided with a deaerator (130) for removing carbon dioxide and oxygen contained in the feed-up (Make-up) flowing into the last stage of the evaporator.

Then, the condensate recovery pump 140 is connected to the brine heater 120 so that the condensed water in the brine heater 120 to the power generation facility for reuse, the concentrated brine so that the circulating brine can circulate inside the evaporator Brine Recirculation Pump (150) is provided, the fresh water pump 160 for sending the fresh water condensed by the evaporator to the post-treatment process and the concentrated brine discharge pump 170 for discharging the concentrated brine reaching the last stage of the evaporator (170). ) Is provided.

A vacuum system 180 is provided as a means for removing non-condensable gases such as carbon dioxide and air that are not condensed in the evaporator 110, and the vacuum system 180 is supplied through the steam supply pipe 181. A first pre-ejector 182 and a second pre-ejector 183 are provided, which eject the middle pressure steam to the internal nozzle to drastically reduce the pressure, and are sucked from the evaporator by the difference in pressure. First, second, and third condensers (184, 185, 186) for condensing non-condensable gas with cold concentrated water introduced through the concentrated brine inlet (189) are provided, and a third condenser ( 186) the condensed water is discharged to the atmosphere through the concentrated brine discharge pipe 187, the non-condensable gas in the third condenser 186 is discharged to the atmosphere through the gas discharge pipe (188).

However, the large-scale desalination treatment using the conventional membrane separation method as described above requires a separate large-capacity transfer pump 303 and temporary piping for circulation of the acidic liquid, and thus requires manpower and equipment for washing. In addition to excessively necessary, it takes a lot of time to connect the temporary piping, there was a problem that the overall downtime of the desalination plant is long.

In addition, when the capacity of the desalination plant is increased, the size of the mobile acid washing apparatus must also be increased, so that there is a problem of having to manufacture a separate mobile acid washing apparatus again.

Accordingly, the present invention is to solve the conventional problems as described above, the part of the seawater purified by separating the organic matter and pollutants and microorganisms contained in the seawater while undergoing the water purification process for the incoming seawater is self-cleaning water and midnight The seawater with the ability to be discharged back to the sea, and the organic matter, pollutants and microorganisms separated from the seawater to be used as a solid fuel material, while the remainder of the purified seawater by heat exchange method and thermal dilution method Ultrasonic waves and microwaves are applied while heating to change the seawater to pure water using less energy, and drinking water while passing through the desalination layer of pumice, elvan, zeolite, tourmaline and ocher as needed. Providing a water treatment system at sea to get this possible drinking water For that purpose.

Water treatment system at sea of the present invention for achieving the above object,

The seawater is discharged through the seawater supply pipe to remove the organics, pollutants and microorganisms contained in the seawater through the water purification device installed in the vessel (A) on the sea, and then to remove salts through the heating device to discharge the pure water. If necessary, the pure water is discharged through the desalination layer to discharge the drinking water containing mineral components,

Install high frequency generators at regular intervals on the outer surface of the seawater supply pipe to generate high frequency to kill microorganisms causing green algae or red tide,

Install a plurality of light emitting elements at regular intervals in the transparent layer of the sea water supply pipe to receive light energy by radiant heat in the form of electromagnetic spectrum,

Install a plurality of ultrasonic generators at predetermined intervals in the sea water supply pipe to receive the wavelength energy by the ultrasonic waves,

By installing a plurality of microwave generators at regular intervals in the sea water supply pipe to generate and supply microwaves, the coupling force of the sea water is weakened by the light energy, the wavelength energy, and the microwave, thereby facilitating the next purification process.

It is supplied to the flotation tank to separate the organic matter and pollutants that are lighter than seawater by the ultrasonic waves generated by the ultrasonic generator and the vibration generated by the vibration generator, and the anion oxygen generated by the negative ion oxygen generator.

The seawater passing through the floating separation tank is supplied to the decomposition tank so that the floating of the seawater is actively progressed by the ultrasonic wave generated by the ultrasonic generator and the vibration generated by the vibration generator and the anion oxygen generated by the negative ion oxygen generator.

The sea water is supplied to the coagulation reaction tank so that the organic matter and contaminants that are heavier than the sea water are stable while vortexing by the fan,

The organic and contaminants that are heavier than seawater and seawater are supplied to the sedimentation tank so that organic matter and contaminants that are heavier than the seawater that has settled on the inclined bottom surface through the strainer are collected and discharged to the outside.

The seawater passing through the settling tank is to allow the microorganisms that are dead while passing through the filter having a filter therein to be filtered,

The organic and contaminated components and dead microorganisms to be provided as a raw material for producing a separate solid fuel,

Part of the seawater removed by separating the organic and contaminants and dead microorganisms is magnetized and purified by a magnet attached to the outer surface of the seawater discharge pipe to discharge seawater having self-cleaning ability back to the sea,

The remainder of the seawater removed by separating the organic and contaminants and dead microorganisms is to be concentrated into the seawater heating chamber of the heating apparatus through a supply pipe having a check valve for preventing backflow.

When the fuel supplied into the combustion chamber is combusted in the combustion chamber of the heating apparatus ignited by the ignition means, the seawater heating chamber formed in the interior of the seawater chamber formed by the heat exchanger of the small grains of alumina, molybdenum, ceramic, tourmaline, and ganbanite The sea water is heated to produce and discharge steam through a discharge pipe having a check valve for preventing backflow.

A plurality of first heat exchange tubes and a second heat exchange tube at an upper end thereof are installed in the upper portion of the combustion chamber so that a portion of the sea water supplied to the seawater heating chamber is heated.

A recombustion unit and a focus combustion unit are installed at an upper end of the first heat exchange tube of the combustion chamber to recombust the combustion gas in an incomplete combustion state that rises,

Light in the form of electromagnetic spectrum generated when burning the fuel is transmitted to the light collecting plate installed on the outer surface of the first and second heat exchanger tube to transmit heat by radiant heat to the surface,

A plurality of magnetization contact pieces are formed to protrude in the lower portion of the first and second heat exchange tubes to generate thermal energy by kinetic energy such as rising combustion gas,

On the outer wall of the seawater heating chamber, a plurality of ultrasonic wave generators and high frequency generators are installed on the seawater where ultrasonic waves and high frequency waves are heated to activate molecular movement so that vaporization of water is promoted to discharge steam from which salts are removed from the seawater. ,

The salt is removed steam is to discharge the pure water through the ion exchange chamber,

If necessary, the pure water is passed through the desalination layer of pumice, elvan, zeolite, tourmaline, and ocher, to contain minerals.

In the water treatment system at sea according to the present invention, the binding force of seawater is weakened by light energy, wavelength energy, and microwave while killing microorganisms by the high frequency generator of the seawater supply pipe to the incoming seawater. To facilitate

The seawater supplied through the seawater supply pipe is used to separate the organics, pollutants and microorganisms contained in the seawater through the purification process of the flotation tank, the decomposition tank, the flocculation tank, the settling tank and the filter to facilitate the separation of salts. ,

The long life treated seawater is supplied to the seawater heating chamber, the first heat exchanger tube and the second heat exchanger tube of the heating apparatus, and is provided with a heat exchanger, a reburner, a focus combustion unit, a light collecting plate, a magnetization contact piece, an ultrasonic generator, and a high frequency generator. By heating the seawater using the super-dilution method to promote vaporization to discharge the salt-free steam, and to use the ion exchange method to convert the seawater into pure water using less energy,

If necessary, there is an effect of obtaining drinking water available for drinking while passing through the desalination layer of pumice, elvan, zeolite, tourmaline, and ocher.

Figure 1 is a schematic diagram showing a large scale desalination treatment apparatus of a conventional membrane separation method.
2 is a schematic diagram showing a schematic configuration of the present invention.
3 is a schematic view showing the structure of the present invention.
Figure 4 is a schematic diagram showing the configuration of the heating apparatus of the present invention.

Hereinafter, exemplary embodiments of the present invention will be described with reference to the accompanying drawings.

1 kg of typical seawater contains water (96.5%) in sodium chloride (NaCl) 27.213%, magnesium chloride (MgCl 2) 3.807%, magnesium sulfate (MgSO 4) 1.658%, calcium sulfate (CaSO 4) 1.260% potassium sulfate (K 2 SO 4) 0.863%, carbonic acid It is known to contain 0.123% of calcium (CaCO3) and 0.076% of magnesium bromide (MgBr2).

However, due to environmental pollution such as inflow of polluted rivers or throwing waste, the seawater contains a large amount of organic matter, pollutants and microorganisms in addition to salts. The salts can be removed by evaporation or membrane separation. Organics, contaminants and microorganisms are not removed and must be treated separately.

Therefore, the water treatment system at sea according to the present invention separates organic matters, pollutants and microorganisms contained in seawater through seawater supply pipe (B) via seawater purification device (C) installed on the vessel (A) on the sea. Part of the seawater is removed by self-cleaning from the seawater discharge pipe (D) to be discharged back to the sea, while the rest of the seawater is removed through the heating device (E) to remove the pure water. Accordingly, the pure water is to discharge the drinking water containing the mineral component via the desalination layer (F),

Install a large number of high frequency generators (1) at regular intervals on the outer surface of the sea water supply pipe (B) to generate high frequency to kill microorganisms causing green algae or red tide,

By installing a plurality of light emitting heating elements (3) at regular intervals in the transparent layer (2) of the sea water supply pipe (B) to receive light energy by radiant heat in the form of electromagnetic spectrum,

In the sea water supply pipe (B) to install a plurality of ultrasonic generators at a predetermined interval to receive the wavelength energy by the ultrasonic waves,

A plurality of microwave generators 5 are installed in the seawater supply pipe B at regular intervals to generate and supply microwaves, so that the binding force of seawater is weakened by the light energy, wavelength energy, and microwaves, thereby facilitating the following water treatment. Let's do it,

When the seawater through the seawater supply pipe (B) is supplied to the floating separation tank (10) of the water purification device (C), the combined state of the molecular structure of the seawater by the ultrasonic waves generated in the ultrasonic generator 11 installed on the inner wall Cut it off.

Vibration generators 12 to which permanent magnets 15 are respectively attached to magnetizing plates 14 coupled to four sides of alternating magnets 13 repeatedly having N polarity and S polarity in the floating separation tank 10. Install a number of vibrations in the sea water,

Anion oxygen generated in the anion oxygen generator 16 installed in the outside is mixed into the sea water circulating through the circulation pipe 18 by the pump 17 and aerated through the aeration mechanism 19 so as to be aerated by ultrasonic and vibration inside. Seawater in which the separation of the molecular bonds proceeds is separated and collected by organic matter and contaminants lighter than seawater by flotation in the floating separation tank 10,

The seawater passing through the floating separation tank 10 is supplied to the decomposition tank 20 so as to break the bonding state of the molecular structure of the seawater by ultrasonic waves generated by the ultrasonic generator 21 on one inner wall.

In order to generate vibrations in the seawater by installing a plurality of vibration generators 22 each having permanent magnets 25 attached to the magnetization plates 24 coupled to all four sides of the alternating magnets 23 repeatedly having N polarities and S polarities. and,

Anion oxygen generated in the anion oxygen generator 26 installed in the outside is mixed in the sea water circulated by the pump 27 to be aerated through the aeration mechanism 28 so that the rise of sea water actively proceeds inside,

The electromagnetic wave generator 29 installed at the top sends ultrasonic electrons and anion oxygen out of the seawater back into the water by the magnetic field and the electromagnetic waves to maintain the decomposition efficiency,

The seawater from which the organic matter and the contaminant contained in the decomposition tank 20 are separated is supplied to the agglomeration reaction tank 30 and coupled to the shafts 32 and 32a of the reduction motors 31 and 31a to slowly rotate the fan. (33, 34) (33a, 34a) to make the organics and contaminants that are heavier than seawater separated from seawater in vortex stable

Seawater and organic components that are heavier than seawater and contaminants that remain stable in the agglomeration reaction tank 30 are supplied to the settling tank 40 and are coupled to the shaft 42 of the reduction motor 41 to gradually rotate the strainer 43. ) To collect organic substances and pollutants that are heavier than seawater that has sunk on the inclined bottom surface and discharge them to the outside.

The seawater passing through the settling tank 40 allows the microorganisms that are dead while passing through the filter 50 having the filter 51 therein to be filtered,

The organic and contaminated components and dead microorganisms to be provided as a raw material for producing a separate solid fuel,

Part of the seawater removed by separating the organic and contaminants and dead microorganisms is magnetized and purified by the magnet 6 attached to the outer surface of the seawater discharge pipe D to discharge the seawater having the self-cleaning ability back to the sea,

The seawater removed by separating the organic and contaminants and microorganisms is to be concentrated in the seawater heating chamber 60 of the heating device E through the supply pipe 62 having the check valve 61 for preventing the backflow,

And to combust the fuel supplied to the inside from the combustion chamber 70 of the heating device E to be ignited by a separate ignition means,

The seawater heating chamber 60 is formed inside the combustion chamber 70 to form a heat exchanger 71 in which small grains of alumina, molybdenum, ceramic, tourmaline, and agglomerate are formed. To produce and discharge steam through a discharge pipe (64) having a check valve (63) for preventing a backflow,

A plurality of first heat exchange tubes 65 are installed in the upper portion of the combustion chamber 70 so that a portion of the seawater supplied to the seawater heating chamber 60 is heated.

The reburn unit 72 located at the upper end of the first heat exchange tube 65 of the combustion chamber 70 is formed of a plurality of reburn nets 73 rolled iron wire mesh in a cochlear shape to replay iron iron material. The desired 73 causes the combustion gas in an incomplete combustion state to be burned while temporarily regenerating combustion heat of 600 ° C. or higher,

In the focal combustion section 75 formed on the reburning network 73 of the reburn section 72 one by one, the combustion gas passing through the spaces inside the small cylinders 76 made of a plurality of iron chromium is formed in the hemispherical body 77. While the gas is collected inside and ascended through the discharge pipe 78 in the upper center, the combustion gas in an incomplete combustion state is burned again.

A plurality of second heat exchange tubes 66 are installed at an upper portion of the focus combustion unit 75 of the combustion chamber 70 so that a part of the seawater supplied to the seawater heating chamber 60 is heated.

Light in the form of an electromagnetic spectrum generated when burning the fuel is transmitted to the light collecting plate 79 installed on the outer surfaces of the first and second heat exchange tubes 65 and 66 to transmit heat by radiant heat to the surface. By doing so, radiant heat is added to the direct combustion heat and the heat storage of the first heat exchange chamber 10,

A plurality of magnetization contact pieces 80 are formed to protrude from the lower portions of the first and second heat exchange tubes 65 and 66 to collide with the kinetic energy of the combustion gas, which rises during combustion, thereby causing thermal energy due to resistance. To occur,

The magnetization connecting piece 80 is composed of a metal piece 81 coated on the outer surface of the tourmaline powder 82 of the magnetic when subjected to heat to receive the kinetic energy that is a movement by the rising combustion gas, etc. To transfer heat to the first and second heat exchange tubes (65, 66),

On the outer wall of the seawater heating chamber 60, a plurality of ultrasonic generators 83 and high frequency generators 84 are provided to the seawater where ultrasonic waves from the ultrasonic generator 83 and high frequency from the high frequency generator 84 are heated. Molecular motion is activated to promote the vaporization of water, and at the same time, the first and second heat exchange tubes 65 and 66 have direct combustion heat, heat storage of the heat exchanger 71, and radiant heat and magnetization connecting pieces through the light collecting plate 22. 23 is added to the heat energy due to the resistance and the second heat exchange tube 66 is added to the combustion heat of the reburn unit 72 and the focus combustion unit 75, the heat inside the combustion chamber 70 is completely applied To vaporize the water and discharge the salt-free steam through the discharge pipe 64 having the check valve 63 for preventing the backflow,

The salt is removed from the steam to discharge the pure water through the ion exchange chamber (85),

If necessary, the pure water is composed of a desalination layer in which pumice, elvan, zeolite, tourmaline, and ocher are laminated (to pass minerals, so that minerals are contained so that drinking water is available for drinking.

In the water treatment system according to the embodiment of the present invention configured as described above, the organic matter contained in the seawater while the seawater passes through the water purification device (C) installed on the vessel (A) on the sea through the seawater supply pipe (B). After separating and removing the contaminants and microorganisms, the salts are removed through the heating device (E) to discharge the pure water, and if necessary, the pure water contains the mineral component via the desalination layer (F). To drain drinking water,

The high frequency generator 1 is installed on the outer surface of the sea water supply pipe B at regular intervals to generate high frequency to kill microorganisms causing green algae or red tide.

A plurality of light emitting heating elements 3 are installed in the transparent layer 2 of the seawater supply pipe B at regular intervals to receive light energy by radiant heat in the form of an electromagnetic spectrum.

A plurality of ultrasonic generators 4 are installed in the sea water supply pipe B at predetermined intervals to receive the wavelength energy by ultrasonic waves.

A plurality of microwave generators 5 are installed in the seawater supply pipe B at regular intervals to generate and supply microwaves, so that the binding force of seawater is weakened by the light energy, wavelength energy, and microwaves, thereby facilitating the following water treatment. Do it.

When the seawater through the seawater supply pipe (B) is supplied to the floating separation tank 10 of the water purification device (C), the combined state of the molecular structure of the seawater by the ultrasonic waves generated by the ultrasonic generator 11 installed on the inner wall Try to cut it off.

Vibration generators 12 to which permanent magnets 15 are respectively attached to magnetizing plates 14 coupled to four sides of alternating magnets 13 repeatedly having N polarity and S polarity in the floating separation tank 10. Install a number of vibrations to occur in the sea water.

Anion oxygen generated in the anion oxygen generator 16 installed in the outside is mixed into the sea water circulating through the circulation pipe 18 by the pump 17 and aerated through the aeration mechanism 19 so as to be aerated by ultrasonic and vibration inside. Seawater in which the separation of the molecular bonds proceeds is separated from the organic matter and pollutants, which are lighter than seawater, by the flotation force in the flotation separation tank 10.

The seawater passing through the floating separation tank 10 is supplied to the decomposition tank 20 so as to break the bonding state of the molecular structure of the seawater by ultrasonic waves generated by the ultrasonic generator 21 of one inner wall.

In order to generate vibrations in the seawater by installing a plurality of vibration generators 22 each having permanent magnets 25 attached to the magnetization plates 24 coupled to all four sides of the alternating magnets 23 repeatedly having N polarities and S polarities. do.

Anion oxygen generated in the anion oxygen generator 26 installed in the outside is mixed in the sea water circulated by the pump 27 to be aerated through the aeration mechanism 28 so that the rise of sea water is actively progressed inside.

The electromagnetic wave generator 29 installed at the top sends ultrasonic electrons and anion oxygen out of the seawater back into the water by the magnetic field and the electromagnetic waves to maintain the decomposition efficiency,

The seawater from which the organic matter and the contaminant contained in the decomposition tank 20 are separated is supplied to the agglomeration reaction tank 30 and coupled to the shafts 32 and 32a of the reduction motors 31 and 31a to slowly rotate the fan. (33, 34) (33a, 34a) ensures that organics and contaminants that are heavier than seawater separated from seawater are in a stable state during vortexing.

Seawater and organic components that are heavier than seawater and contaminants that remain stable in the agglomeration reaction tank 30 are supplied to the settling tank 40 and are coupled to the shaft 42 of the reduction motor 41 to gradually rotate the strainer 43. ), The organic matter and pollutants, which are heavier than the seawater sinking on the inclined bottom, are collected and discharged to the outside.

The seawater passing through the settling tank 40 allows the microorganisms that are dead while passing through the filter 50 having the filter 51 therein to be filtered.

The organic and contaminants and dead microorganisms are to be provided as raw materials for preparing a separate solid fuel.

A portion of the seawater removed by separating the organic and contaminants and dead microorganisms is magnetized and purified by a magnet 6 attached to the outer surface of the seawater discharge pipe D to discharge the seawater having the self-cleaning ability back to the sea.

The seawater removed by separating the organic and contaminants and microorganisms is urged to the seawater heating chamber 60 of the heating apparatus E through the supply pipe 62 having the check valve 61 for preventing the backflow.

The fuel supplied to the inside is combusted in the combustion chamber 70 of the heating apparatus E which is ignited by a separate ignition means.

The seawater heating chamber 60 is formed inside the combustion chamber 70 to form a heat exchanger 71 in which small grains of alumina, molybdenum, ceramic, tourmaline, and agglomerate are formed. The steam is produced and discharged through the discharge pipe 64 having the non-return check valve 63.

A plurality of first heat exchange tubes 65 are installed in the upper portion of the combustion chamber 70 so that a portion of the seawater supplied to the seawater heating chamber 60 is heated.

The reburn unit 72 located at the upper end of the first heat exchange tube 65 of the combustion chamber 70 is formed of a plurality of reburn nets 73 rolled iron wire mesh in a cochlear shape to replay iron iron material. The desired 73 causes the combustion gas in an incomplete combustion state to be burned while temporarily storing heat of combustion at 600 ° C or higher.

In the focal combustion section 75 formed on the reburning network 73 of the reburn section 72 one by one, the combustion gas passing through the spaces inside the small cylinders 76 made of a plurality of iron chromium is formed in the hemispherical body 77. The gas is collected in the interior and ascends through the discharge pipe 78 in the upper center to burn the combustion gas in an incomplete combustion state again.

A plurality of second heat exchange tubes 66 are installed at an upper portion of the focus combustion unit 75 of the combustion chamber 70 so that a portion of the seawater supplied to the seawater heating chamber 60 is heated.

Light in the form of an electromagnetic spectrum generated when burning the fuel is transmitted to the light collecting plate 79 installed on the outer surfaces of the first and second heat exchange tubes 65 and 66 to transmit heat by radiant heat to the surface. By doing so, radiant heat is added to the direct combustion heat and the heat storage of the first heat exchange chamber 10.

A plurality of magnetization contact pieces 80 are formed to protrude from the lower portions of the first and second heat exchange tubes 65 and 66 to collide with the kinetic energy of the combustion gas, which rises during combustion, thereby causing thermal energy due to resistance. To occur.

The magnetization connecting piece 80 is composed of a metal piece 81 coated on the outer surface of the tourmaline powder 82 of the magnetic when subjected to heat to receive the kinetic energy that is a movement by the rising combustion gas, etc. To transfer heat to the first and second heat exchange tubes (65, 66).

On the outer wall of the seawater heating chamber 60, a plurality of ultrasonic generators 83 and high frequency generators 84 are provided to the seawater where ultrasonic waves from the ultrasonic generator 83 and high frequency from the high frequency generator 84 are heated. Molecular motion is activated to promote the vaporization of water, and at the same time, the first and second heat exchange tubes 65 and 66 have direct combustion heat, heat storage of the heat exchanger 71, and radiant heat and magnetization connecting pieces through the light collecting plate 22. 23 is added to the heat energy due to the resistance and the second heat exchange tube 66 is added to the combustion heat of the reburn unit 72 and the focus combustion unit 75, the heat inside the combustion chamber 70 is completely applied While vaporizing the water, the salt is removed from the steam through the discharge pipe 64 having the check valve 63 for preventing the backflow.

The steam from which the salts are removed allows the pure water to be discharged while passing through the ion exchange chamber 85.

If necessary, the pure water is allowed to contain minerals while passing through the desalination layer F in which pumice, elvan, zeolite, tourmaline, and ocher are stacked to obtain drinking water that is drinkable.

Although the preferred embodiments of the present invention have been illustrated and described above, the present invention is not limited to the above-described embodiments, and the present invention is not limited to the above-described embodiments without departing from the spirit of the present invention as claimed in the claims. Various modifications may be made by those skilled in the art, and such modifications are intended to fall within the scope of the appended claims.

A: Sea water supply pipe B: Water purifier
C: Seawater discharge pipe D: Heating device
E: desalination layer 10: flotation tank
20: decomposition tank 30: flocculation reaction tank
30: sedimentation tank 50: filter
60: seawater heating chamber 70: combustion chamber
80: magnetization contact piece 83: ultrasonic generator
84: high frequency generator 85: ion exchange chamber

Claims (5)

To weaken the binding force by killing microorganisms in the seawater supplied through the seawater supply pipe (B),
Through the seawater supply pipe (B), the seawater is to remove and remove the organic and pollutant and microorganisms contained in the seawater through the water purification device (C) installed in the vessel (A) above the sea to discharge a part to the sea and,
The remainder of the sea water from which the organic and polluted impurities and microorganisms are separated is discharged of pure water by removing salts through the heating device E installed in the vessel A,
Part of the pure water is to discharge the drinking water containing the mineral component via the desalination layer (F) installed in the vessel (A),
The remainder of the pure water is a water treatment system at sea, characterized in that configured to discharge the drinking water containing mineral components via the midnight magnetization layer (4) installed in the vessel (A). The method according to claim 1,
Install a plurality of high frequency generator (1) at regular intervals on the outer surface of the sea water supply pipe (B) to generate high frequency to kill microorganisms causing green algae or red tide,
By installing a plurality of light emitting heating elements (3) at regular intervals in the transparent layer (2) of the sea water supply pipe (B) to receive light energy by radiant heat in the form of electromagnetic spectrum,
In the sea water supply pipe (B) to install a plurality of ultrasonic generators at a predetermined interval to receive the wavelength energy by the ultrasonic waves,
A plurality of microwave generators 5 are installed in the seawater supply pipe B at regular intervals to generate and supply microwaves, so that the binding force of seawater is weakened by the light energy, wavelength energy, and microwaves, thereby facilitating the following water treatment. Water treatment system at sea, characterized in that configured to. The method according to claim 1,
The water purifier (C) above,
When the seawater is supplied to the flotation separation tank 10 through the seawater supply pipe (B) to break the bonding state of the molecular structure of the seawater by the ultrasonic waves generated in the ultrasonic generator 11 installed on the inner wall.
Vibration generators 12 to which permanent magnets 15 are respectively attached to magnetizing plates 14 coupled to four sides of alternating magnets 13 repeatedly having N polarity and S polarity in the floating separation tank 10. Install a number of vibrations in the sea water,
Anion oxygen generated in the anion oxygen generator 16 installed in the outside is mixed into the sea water circulating through the circulation pipe 18 by the pump 17 and aerated through the aeration mechanism 19 so as to be aerated by ultrasonic and vibration inside. Seawater in which the separation of the molecular bonds proceeds is separated and collected by organic matter and contaminants lighter than seawater by flotation in the floating separation tank 10,
The seawater passing through the floating separation tank 10 is supplied to the decomposition tank 20 so as to break the bonding state of the molecular structure of the seawater by ultrasonic waves generated by the ultrasonic generator 21 on one inner wall.
In order to generate vibrations in the seawater by installing a plurality of vibration generators 22 each having permanent magnets 25 attached to the magnetization plates 24 coupled to all four sides of the alternating magnets 23 repeatedly having N polarities and S polarities. and,
Anion oxygen generated in the anion oxygen generator 26 installed in the outside is mixed in the sea water circulated by the pump 27 to be aerated through the aeration mechanism 28 so that the rise of sea water actively proceeds inside,
The electromagnetic wave generator 29 installed at the top sends ultrasonic electrons and anion oxygen out of the seawater back into the water by the magnetic field and the electromagnetic waves to maintain the decomposition efficiency,
The seawater from which the organic matter and the contaminant contained in the decomposition tank 20 are separated is supplied to the agglomeration reaction tank 30 and coupled to the shafts 32 and 32a of the reduction motors 31 and 31a to slowly rotate the fan. (33, 34) (33a, 34a) to make the organics and contaminants that are heavier than seawater separated from seawater in vortex stable
Seawater and organic components that are heavier than seawater and contaminants that remain stable in the agglomeration reaction tank 30 are supplied to the settling tank 40 and are coupled to the shaft 42 of the reduction motor 41 to gradually rotate the strainer 43. ) To collect organic substances and pollutants that are heavier than seawater that has sunk on the inclined bottom surface and discharge them to the outside.
The seawater passing through the settling tank 40 allows the microorganisms that are dead while passing through the filter 50 having the filter 51 therein to be filtered,
The organic and contaminated components and dead microorganisms to be provided as a raw material for producing a separate solid fuel,
Part of the seawater removed by separating the organic and contaminants and dead microorganisms is magnetized by a magnet (6) attached to the outer surface of the seawater discharge pipe (D) to be discharged back to the sea, characterized in that the water treatment system. The method according to claim 1,
The above heating device (E),
The seawater removed by separating the organic and contaminants and microorganisms is to be concentrated in the seawater heating chamber 60 through a supply pipe 62 having a check valve 61 for preventing backflow.
And to combust the fuel supplied to the inside from the combustion chamber 70 of the heating device E to be ignited by a separate ignition means,
The seawater heating chamber 60 is formed inside the combustion chamber 70 to form a heat exchanger 71 in which small grains of alumina, molybdenum, ceramic, tourmaline, and agglomerate are formed. To produce and discharge steam through a discharge pipe (64) having a check valve (63) for preventing a backflow,
A plurality of first heat exchange tubes 65 are installed in the upper portion of the combustion chamber 70 so that a portion of the seawater supplied to the seawater heating chamber 60 is heated.
The reburn unit 72 located at the upper end of the first heat exchange tube 65 of the combustion chamber 70 is formed of a plurality of reburn nets 73 rolled iron wire mesh in a cochlear shape to replay iron iron material. The desired 73 causes the combustion gas in an incomplete combustion state to be burned while temporarily regenerating combustion heat of 600 ° C. or higher,
In the focal combustion section 75 formed on the reburning network 73 of the reburn section 72 one by one, the combustion gas passing through the spaces inside the small cylinders 76 made of a plurality of iron chromium is formed in the hemispherical body 77. While the gas is collected inside and ascended through the discharge pipe 78 in the upper center, the combustion gas in an incomplete combustion state is burned again.
A plurality of second heat exchange tubes 66 are installed at an upper portion of the focus combustion unit 75 of the combustion chamber 70 so that a part of the seawater supplied to the seawater heating chamber 60 is heated.
Light in the form of an electromagnetic spectrum generated when burning the fuel is transmitted to the light collecting plate 79 installed on the outer surfaces of the first and second heat exchange tubes 65 and 66 to transmit heat by radiant heat to the surface. By doing so, radiant heat is added to the direct combustion heat and the heat storage of the first heat exchange chamber 10,
A plurality of magnetization contact pieces 80 are formed to protrude from the lower portions of the first and second heat exchange tubes 65 and 66 to collide with the kinetic energy of the combustion gas, which rises during combustion, thereby causing thermal energy due to resistance. To occur,
The magnetization connecting piece 80 is composed of a metal piece 81 coated on the outer surface of the tourmaline powder 82 of the magnetic when subjected to heat to receive the kinetic energy that is a movement by the rising combustion gas, etc. To transfer heat to the first and second heat exchange tubes (65, 66),
On the outer wall of the seawater heating chamber 60, a plurality of ultrasonic generators 83 and high frequency generators 84 are provided to the seawater to which the ultrasonic waves from the ultrasonic generator 83 and the high frequency from the high frequency generator 84 are heated. Molecular motion is activated to promote the vaporization of water, and at the same time, the first and second heat exchange tubes 65 and 66 have direct combustion heat, heat storage of the heat exchanger 71, and radiant heat and magnetization connecting pieces through the light collecting plate 22. 23 is added to the heat energy due to the resistance and the second heat exchange tube 66 is added to the combustion heat of the reburn unit 72 and the focus combustion unit 75, the heat inside the combustion chamber 70 is completely applied To vaporize the water and discharge the salt-free steam through the discharge pipe 64 having the check valve 63 for preventing the backflow,
The salt-free steam is configured to discharge pure water while passing through the ion exchange chamber (85). The method according to claim 4,
The water treatment system at sea, characterized in that the pure water is passed through the desalination layer (F) of pumice, elvan, zeolite, tourmaline, and ocher to contain minerals so as to obtain drinking water available for drinking.

Images