KR20110068589A - Deep sea water distillation apparatus - Google Patents

Deep sea water distillation apparatus Download PDF

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Publication number
KR20110068589A
KR20110068589A KR1020090125616A KR20090125616A KR20110068589A KR 20110068589 A KR20110068589 A KR 20110068589A KR 1020090125616 A KR1020090125616 A KR 1020090125616A KR 20090125616 A KR20090125616 A KR 20090125616A KR 20110068589 A KR20110068589 A KR 20110068589A
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KR
South Korea
Prior art keywords
water
treated
ozone
treatment
mixing
Prior art date
Application number
KR1020090125616A
Other languages
Korean (ko)
Inventor
민하 안
Original Assignee
주식회사 위넥스글로벌
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Publication date
Application filed by 주식회사 위넥스글로벌 filed Critical 주식회사 위넥스글로벌
Priority to KR1020090125616A priority Critical patent/KR20110068589A/en
Publication of KR20110068589A publication Critical patent/KR20110068589A/en

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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/48Treatment of water, waste water, or sewage with magnetic or electric fields
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/725Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/78Treatment of water, waste water, or sewage by oxidation with ozone
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/08Seawater, e.g. for desalination
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination
    • Y02A20/131Reverse-osmosis

Abstract

PURPOSE: Seawater desalination method and facility are provided to remove fine particle materials contained in water by coagulating without adding a coagulant during a filtering process. CONSTITUTION: A seawater desalination method comprises the following steps: inserting ozone into deep seawater to be processed, for purifying the deep seawater and improving the magnetic force of the deep seawater; removing coagulated materials from the deep seawater by filtering with a first filter(6)ting materials to be oxidized by injecting the ozone and applying the magnetic force into the deep seawater, to pass the deep seawater through an activated carbon catalyst layer; and secondly removing the coagulated materials by filtering with a second filter(10).

Description

 Deep sea water distillation apparatus

The present invention relates to a method for producing mineral water containing mineral components beneficial to the human body from deep sea water by applying a magnetic force simultaneously with ozone injection to deep sea water (raw water).

The conventional treatment method using ozone is a method of dissolving ozone in water once and reacting the dissolved ozone with the oxidized substance in water. Specifically, ozone is dissipated in water as fine bubbles in an acid substrate provided at a lower portion of a large water tank. In order to dissolve as much ozone as possible, the depth of the water is deepened and the bubble is made small. However, for practical use, the water depth is 5 to 6 m and the size (particle size) of the bubble is limited to about 20 μm. In addition, a residence time of about 8 to 10 minutes is required before the reaction, and an ozone melting tank or the like is required, and the equipment itself is enlarged.

However, even when using such a facility, the utilization rate of ozone is about 60 to 80%. On the other hand, in the case of water containing both of the representative inorganic oxides and organic substances such as soluble iron and manganese, the relatively well oxidized minerals are preferentially oxidized when ozone is injected, and the oxidative decomposition of organic matters does not proceed very much. For this reason, colloidal substances are produced when the inorganic material is oxidized, which consumes ozone, and the amount of ozone necessary for oxidatively decomposing organic matter becomes several times as necessary for the original treatment.

In order to solve the above-mentioned problem, ozone may be injected again after removing the colloidal substance. However, this colloidal substance has a submicron particle size, and thus it is difficult to remove it as it is. do. Therefore, this treatment method requires equipment such as a flocculant addition facility and a reaction tank, and there is a problem that waste is increased by adding a flocculant. Accordingly, an object of the present invention is to provide a compact treatment method and treatment facility capable of purifying water without adding a flocculant and improving ozone utilization efficiency.

In order to solve the above-mentioned problems, the treatment method of the present invention, by applying a magnetic force to the water to be treated, injecting ozone to oxidize and agglomerate the blood oxide, and then remove the aggregated material by filtration, and once again A magnetic force is applied to the water to be treated and ozone is injected, and then a catalyst layer made of activated carbon is passed through to filter and remove the flocculant. In addition, the treatment facility of the present invention injects ozone generated by the first ozone generator into the water to be treated by the magnetic treatment unit and the magnetic treatment unit which draws the first and second ozone generators and the water to be treated. A first magnetic treatment reactor composed of an ozone injection mixing unit for mixing, a first filter for removing agglomerated substances in the water to be treated in the first magnetic treatment reactor, and a water treatment from the first filter to draw a predetermined magnetic force. A second magnetic treatment reactor composed of an ozone injection mixing unit which injects and mixes ozone generated from the second ozone generator to the water to be treated in the magnetic treatment unit, and draws the treated water from the second magnetic treatment reactor. It is composed of a reaction tank for oxidizing and decomposing with a catalyst layer made of activated carbon and a second filter for removing aggregates in the water to be treated.

According to the configuration of the treatment equipment described above, suspending substances generated by oxidizing colloidal substances and organic substances generated by oxidation of inorganic substances by applying a magnetic force when oxidizing the water to be treated with ozone. Can be aggregated without using a chemical such as a flocculant.

In addition, the wing body provided in the ozone injection mixing portion of the magnetic treatment reactor is composed of a pair of semicircular wing plates, and the two wing plates are inclined at a predetermined angle with respect to the flow direction of the water to be treated and twisted in opposite directions. It is arranged so that it is arranged so as to separate the front space part of the intersection of these two wing plates to the left and right. The projection body is composed of a columnar portion fixed to the inner wall surface of the mixing cylindrical body and a mushroom-shaped portion formed at the tip of the columnar portion, and a plurality of protrusions are arranged in a zigzag shape on the inner wall surface of the mixing cylindrical body.

According to the configuration of the ozone injection mixing portion, the pair of blades arranged in the mixing cylindrical body divides the water to be treated and twists in the opposite direction to each other. The downstream projections change the flow in the radial direction of the mixing cylindrical body while further dividing the flow. As a result, a severe collision effect occurs in the water flow, and ozone reacts with the treated water quickly.

According to the present invention, it is possible to improve the utilization efficiency of ozone in the seawater desalination process using ozone to produce high purity mineral water at low cost energy, and to provide a compact treatment method and treatment facility.

This water treatment facility draws in the storage tank 1 which stores the to-be-processed water, and the to-be-processed water in this storage tank 1 through the conveyance piping 3 which has the pump 2, and acts a predetermined magnetic force. And a first magnetic treatment reactor (5) for injecting (aspirating) ozone (ozone gas) generated by the first ozone generator (4) into the water to be treated and mixing and agglomerating the first magnetic treatment reactor (5). The first filter (6) for removing the aggregated reactant, that is, the aggregated material in the c) and the treated water from which the aggregated material has been removed from the first filter (6), draw a predetermined magnetic force and at the same time the second ozone The second magnetic treatment reaction tank 8 for injecting (aspirating) ozone (ozone gas) generated by the generator 7 into the treated water again, mixing and condensing it, and the treated water from the second magnetic treatment reaction tank 8. Reactor 9 for catalyzing granular activated carbon (catalyst layer) as a catalyst, and decomposition products (reactants) oxidized and decomposed in the reactor 9 It consists of a second filter 10 for removing the water and a treated water tank for storing the water to be treated, that is, the treated water from which the decomposition products are removed in the second filter (10).

1 is a diagram showing the overall configuration of the deep seawater desalination plant of the invention.

Claims (1)

Seawater desalination treatment method characterized by injecting ozone into water to be treated Claim 2 The method for treating seawater desalination according to claim 1, characterized in that after the magnetic force is applied, the aggregated substance in the water to be treated is removed by filtration. Claim 3 . After applying magnetic force to the water to be treated and injecting ozone to oxidize and agglomerate the oxidation substance, the coagulant is removed by filtration, and magnetic force is applied to the water to be treated and ozone is injected. , Seawater desalination treatment method characterized by passing the activated carbon catalyst layer Claim 4 . The seawater desalination treatment method according to claim 3, wherein the aggregated material is removed by filtration after passing through the catalyst layer. Claim 5 . A magnetic treatment reactor comprising an ozone generator and a magnetic treatment unit which draws in the water to be subjected to a predetermined magnetic force, and an ozone injection mixing unit which injects and mixes the water to be treated by the ozone generator described above. Seawater desalination treatment facility, characterized in that it consists of a filter that removes aggregates in the water to be treated from the reactor Claim 6 . A first and second ozone generators, a magnetic processing unit which draws the water to be treated to apply a predetermined magnetic force, and an ozone injection mixing unit which mixes and injects ozone generated from the first ozone generator into the water to be treated in the magnetic processing unit; A magnetic treatment reactor, a first filter for removing agglomerated matter in the water to be treated in the first magnetic treatment reactor, and a magnetic treatment unit for drawing a treated water from the first filter and applying a predetermined magnetic force. A second magnetic treatment reactor comprising an ozone injection mixing unit for injecting and mixing ozone generated by the second ozone generator into the treated water, and oxidizing the treated water from the second magnetic treatment reactor by using a catalyst layer composed of activated carbon. Seawater freshwater, characterized in that it consists of a reactor to decompose and a second filter to remove aggregates in the water to be treated from the reactor. Treatment plant Claim 7 . The ozone injection mixing part of the self-treatment reactor is called a mixing cylinder, an ozone injection tube inserted upstream of the mixing cylinder body, and a wing body which mixes and mixes the water to be treated in the mixing cylinder body near the ozone injection tube. Water treatment equipment according to claim 5 or 6, characterized in that it is composed of a plurality of protrusions disposed downstream of the wing body in the mixing cylindrical body. Claim 8 . The wing body is made of a pair of semi-circular wing plates, and the two wing plates are arranged to be twisted in opposite directions to each other by inclining at a predetermined angle with respect to the direction in which the water to be treated flows. Water treatment equipment according to claim 7 characterized in that a divider divider is provided Claim 9 . The projection body is composed of a columnar portion fixed to the inner wall surface of the mixing cylindrical body and a mushroom-shaped portion formed at the tip of the columnar portion, and a plurality of protrusions are arranged in a zigzag shape on the inner wall surface of the mixing cylindrical body. Water treatment equipment according to claim 7 characterized in that Claim 10 . The wing body is composed of a pair of semicircular wing plates, and the two wing plates are arranged to be twisted in opposite directions to each other by inclining at a predetermined angle with respect to the flow direction of the water to be treated. Install a divider that divides wealth from side to side. In addition, the projection body is composed of a columnar portion fixed to the inner wall surface of the mixing cylindrical body and a mushroom-shaped portion formed at the tip of the columnar portion, and a plurality of projection bodies are arranged in a zigzag shape on the inner wall surface of the mixing cylindrical body. Water treatment equipment according to claim 7
KR1020090125616A 2009-12-16 2009-12-16 Deep sea water distillation apparatus KR20110068589A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1020090125616A KR20110068589A (en) 2009-12-16 2009-12-16 Deep sea water distillation apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1020090125616A KR20110068589A (en) 2009-12-16 2009-12-16 Deep sea water distillation apparatus

Publications (1)

Publication Number Publication Date
KR20110068589A true KR20110068589A (en) 2011-06-22

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103159270A (en) * 2011-12-19 2013-06-19 松下电器产业株式会社 Water purifier
KR20150080194A (en) 2013-12-31 2015-07-09 한국해양과학기술원 The manufacturing process of high hardness drinking water using NF/RO/ED membrane connection system
KR20150143062A (en) 2014-06-13 2015-12-23 한국해양과학기술원 Removal of anions and conversion technology of carbonate ions from seawater
CN106007265A (en) * 2016-07-29 2016-10-12 台州学院 Advanced treatment method of chemical industry pharmaceutical wastewater biochemical tail water

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103159270A (en) * 2011-12-19 2013-06-19 松下电器产业株式会社 Water purifier
KR20150080194A (en) 2013-12-31 2015-07-09 한국해양과학기술원 The manufacturing process of high hardness drinking water using NF/RO/ED membrane connection system
KR20150143062A (en) 2014-06-13 2015-12-23 한국해양과학기술원 Removal of anions and conversion technology of carbonate ions from seawater
CN106007265A (en) * 2016-07-29 2016-10-12 台州学院 Advanced treatment method of chemical industry pharmaceutical wastewater biochemical tail water
CN106007265B (en) * 2016-07-29 2019-02-01 台州学院 A kind of deep treatment method of pharmaceutical waste water biochemical tail water

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