CN104445761A - Energy-saving seawater purification equipment - Google Patents
Energy-saving seawater purification equipment Download PDFInfo
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- CN104445761A CN104445761A CN201410561952.0A CN201410561952A CN104445761A CN 104445761 A CN104445761 A CN 104445761A CN 201410561952 A CN201410561952 A CN 201410561952A CN 104445761 A CN104445761 A CN 104445761A
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- seawater
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- 239000013535 sea water Substances 0.000 title claims abstract description 83
- 238000000746 purification Methods 0.000 title abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 41
- 238000004062 sedimentation Methods 0.000 claims abstract description 10
- 238000001914 filtration Methods 0.000 claims description 18
- 230000001112 coagulating effect Effects 0.000 claims description 9
- 230000001954 sterilising effect Effects 0.000 claims description 9
- 239000004952 Polyamide Substances 0.000 claims description 7
- 229920002647 polyamide Polymers 0.000 claims description 7
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 5
- 230000000694 effects Effects 0.000 abstract description 11
- 238000005868 electrolysis reaction Methods 0.000 abstract description 6
- 239000010865 sewage Substances 0.000 abstract description 5
- 238000004659 sterilization and disinfection Methods 0.000 abstract description 4
- 238000011033 desalting Methods 0.000 abstract description 2
- 230000015271 coagulation Effects 0.000 abstract 1
- 238000005345 coagulation Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 21
- 238000010612 desalination reaction Methods 0.000 description 12
- 238000001223 reverse osmosis Methods 0.000 description 12
- 239000012528 membrane Substances 0.000 description 10
- 238000005516 engineering process Methods 0.000 description 8
- 238000005562 fading Methods 0.000 description 6
- 238000004821 distillation Methods 0.000 description 5
- 239000013505 freshwater Substances 0.000 description 5
- 238000004140 cleaning Methods 0.000 description 4
- 238000001704 evaporation Methods 0.000 description 4
- 230000008020 evaporation Effects 0.000 description 4
- 241000894006 Bacteria Species 0.000 description 3
- 241000195493 Cryptophyta Species 0.000 description 3
- 150000002500 ions Chemical class 0.000 description 3
- 235000019600 saltiness Nutrition 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 239000003651 drinking water Substances 0.000 description 2
- 235000020188 drinking water Nutrition 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 238000007781 pre-processing Methods 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000008399 tap water Substances 0.000 description 2
- 235000020679 tap water Nutrition 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical compound [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 241000003864 Umbilicaria pertusa Species 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 230000001488 breeding effect Effects 0.000 description 1
- 239000012267 brine Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 229910001431 copper ion Inorganic materials 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- BHEPBYXIRTUNPN-UHFFFAOYSA-N hydridophosphorus(.) (triplet) Chemical compound [PH] BHEPBYXIRTUNPN-UHFFFAOYSA-N 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000001471 micro-filtration Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000001728 nano-filtration Methods 0.000 description 1
- 230000002572 peristaltic effect Effects 0.000 description 1
- 230000035790 physiological processes and functions Effects 0.000 description 1
- 231100000572 poisoning Toxicity 0.000 description 1
- 230000000607 poisoning effect Effects 0.000 description 1
- 229920003229 poly(methyl methacrylate) Polymers 0.000 description 1
- 239000004926 polymethyl methacrylate Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 238000001256 steam distillation Methods 0.000 description 1
- 230000004083 survival effect Effects 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
-
- 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
- C02F2103/08—Seawater, e.g. for desalination
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/33—Wastewater or sewage treatment systems using renewable energies using wind energy
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The invention relates to energy-saving seawater purification equipment comprising a water inlet pipe (1) and a purification container (2), wherein a coagulation sedimentation layer (3), a filter layer (4) and a disinfection layer (5) are sequentially arranged in the purification container (2) from top to bottom, the lower end of the purification container (2) is connected with an electrolysis chamber (11) by a connecting pipe (6), a first valve (9) is arranged at the joint of the connecting pipe (6) and the electrolysis chamber (11), the electrolysis chamber (11) is connected with a drainage pipe (12), the connecting pipe (6) is communicated with a circulating pipe (7), the other end of the circulating pipe (7) is communicated with the upper end of the purification container (2), and the electrolysis chamber (11) is sequentially connected with a storage battery pack (13) and a solar assembly (14). The energy-saving seawater purification equipment can be used for effectively and conveniently treating sewage, so that the sewage treatment effect is greatly improved, and the seawater purification and desalting cost is reduced.
Description
Technical field
The present invention relates to a kind of energy-saving seawater treating plant, belong to water-treatment technology field.
Background technology
Seawater is flowing, and for the mankind, water volume that can be utilized is unrestricted.Seawater is liquid mineral reserve worthy of the name, and on average have the mineral substance of 3,570 ten thousand tons in the seawater of every cubic kilometer, in 100 known in the world multiple elements, 80% can find in the seawater.The source of seawater or land fresh water and the setter of weather, the fresh water that world ocean evaporates every year has 4,500,000 cubic kilometers, wherein 90% returns to ocean by rainfall, and 10% becomes sleet drops on large ground, then returns to ocean again along river.Desalination technology develops into industry.It was expected, along with the deterioration of ecotope, the last approach that the mankind solve water shortage is likely the desalination to seawater.
Seawater is a kind of very complicated polycomponent aqueous solution.In seawater, various element all exists with certain physical chemistry form.The existence form of copper is comparatively complicated in the seawater, and major part is that organic complex form exists.In free ion, only have sub-fraction to there is major part with bivalent positive ion form is all occur with negative ion complex compound.So free copper ion only accounts for the sub-fraction of whole dissolved copper.Have the sodium that content very enriches in seawater, but its chemical conduct is very simple, it almost all exists with Na+ ionic species.
Containing a large amount of salt and multiple element in seawater, wherein many elements are that needed by human body is wanted.But various material concentration is too high in seawater, considerably beyond sanitary standard for drinking water, if drunk in a large number, can cause that some element is excessive enters human body, affect the physiological function of human normal, human body also can be caused to dewater, serious also causing is poisoning.
Shortage of fresh water in the world, a lot of country is in the state of serious water shortage, in order to production, the life of the mankind, by sea water desaltination, purification, for the mankind, provides existence water source, is the needs of human survival.And when people go to sea, after the fresh water on ship is used up, people will be in the predicament not having fresh water supply and demand, the excessive lack of water of people will produce life danger, and seawater can not directly be drunk, and just can drink after needing purification, desalination.Sea water desaltination is mainly in order to supply drinking water and agricultural water, and edible salt also can be produced as byproduct sometimes.Sea water desaltination is very popular in Middle East, and some island and ship are also used.Therefore seawater cleaning desalination techniques is more and more extensive in the application of society.Because tellurian sewage, waste residue, waste oil and chemical substance constantly flow into the sea in a steady stream, also purifying treatment to be carried out to seawater to before sea water desaltination.
A large amount of microorganism, bacterium and algae is there is in seawater.In seawater, the breeding of bacterium, algae and microbial growth not only can bring many troubles to water intake facilities, and directly can affect the normal operation of sea water desalting equipment and process pipe.Periodically flood tide, ebb, carry a large amount of silt in seawater secretly, turbidity changes greatly, and easily causes seawater pretreatment system to operate unstable.Seawater has larger corrodibility, will do certain screening to the material of the equipment adopted in system, valve, pipeline member, and corrosion resistant performance will be got well.
Sea water desaltination treatment technology refers to the sea water desaltination of 35000mg/L to the tap water of below 500mg/L.At present, the beautiful sea water desaltination membrane method in east applied of installing in the world mainly contains multistage flash evaporation (MSF), multiple-effect evaporation (MED) and reverse osmosis method (RO), since half a century, oneself has supported the population in the world more than 100,000,000, facilitates Arid desert region and developed country's coastal economy and social development.
Seawater is very high due to its saltiness, and can not be used directly, and mainly adopts two kinds of methods to desalinize seawater, i.e. distillation method and reverse osmosis method.The place that distillation method is mainly used in super-huge sea water desaltination process and heat energy is abundant.Reverse osmosis membrane applicable surface very wide, and ratio of desalinization is very high, is therefore widely used.First reverse osmosis membrane is extracted by seawater, carry out preliminary treatment, reduce turbidity of sea water, prevent the microbial growth such as bacterium, algae, then the supercharging of Special high-voltage pump is used, make seawater enter reverse osmosis membrane, because seawater saltiness is high, therefore seawater reverse osmosis membrane must have equipment with high desalinization, the features such as corrosion-resistant, high pressure resistant, antipollution, seawater after reverse osmosis membrane processing, its saltiness reduces greatly, about TDS content is down to 200 mg/litre from 36000 mg/litre.Water quality after desalination is even better than tap water, so just can for industry, business, resident and boats and ships, naval vessels.
Current Global Seawater desalination techniques is planted more than more than 20, comprise reverse osmosis method, low multiple-effect, multistage flash evaporation, electroosmose process, pressure steam distillation, dew point method of evaporation, water-electricity cogeneration, hotting mask coproduction and utilize nuclear energy, sun power, wind energy, tidal energy seawater desalination technology etc., and multinomial pre-treatment and the aftertreatment technology such as micro-filtration, ultrafiltration, nanofiltration.
From large classification, be mainly divided into distillation method (hot method) and the large class of embrane method two, wherein low multiple-effect distillation, multistage flash vaporization and reverse osmosis membrane are global mainstream technologys.Generally speaking, low multiple-effect has energy-conservation, low, the desalination water quality advantages of higher of sea water preprocessing requirement; Reverse osmosis membrane has low, the low power consumption and other advantages of investment, but sea water preprocessing requires high; Multistage flash vaporization possesses skills ripe, reliable, the advantage such as device output is large, but energy consumption is higher.It is generally acknowledged, low multiple-effect distillation and reverse osmosis membrane are future directions.
Chinese utility model patent specification sheets CN 202144462 U openly so a kind of sea water purifier.This sea water purifier comprises containment housing, described containment housing top is provided with water-in, described containment housing sidewall bottom is provided with water outlet, described containment housing is provided with force (forcing) pump, force (forcing) pump has two air pressure mouths, two described air pressure mouths are connected with containment housing respectively, double-layer polyamide osmosis filtration film is provided with in containment housing, the edge seal of double-layer polyamide osmosis filtration film is fixed on the sidewall of containment housing, this utility model can effective save energy, without the need to often changing reverse osmosis membrane, effectively reduce job costs.But this high-efficiency water purifying treatment device structure is comparatively simple, seawater cleaning, fading effect are bad.
Chinese invention patent specification sheets CN 102515342 U openly so a kind of sea water purifier.This sea water purifier comprises peristaltic pump, prosopyle, water inlet pipe, biological filter body, poly (methyl methacrylate) plate, posticum and rising pipe; Principle of biological nitrogen removal is utilized to choose U. pertusa tamping unit by carrying out purifying treatment to water quality under different control condition, compared with traditional biological denitrification phosphorous removal technique, brine waste can be processed, do not need additional carbon, cost for wastewater treatment is low, achieve the resource utilization of N, P pollutent in waste water, there are very wide market outlook.But this high-efficiency water purifying treatment device structure is comparatively simple, seawater cleaning, fading effect are bad.
Summary of the invention
The technical problem to be solved in the present invention is to provide a kind of energy-saving seawater treating plant, and this energy-saving seawater treating plant can be effective, disposes of sewage easily, the effect of the sewage disposal greatly improved, and the cost having saved seawater cleaning, desalination.
In order to solve the problems of the technologies described above, energy-saving seawater treating plant of the present invention comprises water inlet pipe, purifying vessel, coagulating sedimentation layer, filtering layer, sterilizing layer is set gradually from top to bottom in purifying vessel, purifying vessel lower end connects tank room by pipe connecting, pipe connecting and tank room junction are provided with the first valve, separate room and connect water shoot, through connection circulation tube on pipe connecting, the circulation tube the other end is connected with purifying vessel upper end is through, and tank room connects secondary battery, solar components successively.
Described energy-saving seawater treating plant also comprises water pump, and water pump is arranged on the junction of purifying vessel and pipe connecting, and water pump is connected with secondary battery.
Described energy-saving seawater treating plant also comprises the second valve, and the second valve is arranged on circulation tube.
Described purifying vessel lower end arranges ultraviolet tube.
Described ultraviolet tube is at least one, and ultraviolet tube is evenly arranged in purifying vessel lower end.
Described coagulating sedimentation layer forms component and contains polymerize aluminum chloride.
Described filtering layer is double-layer polyamide osmosis filtration layer.
Described solar components is photovoltaic module.
Described purifying vessel is made up of stainless material.
Adopt this energy-saving seawater treating plant, owing to setting gradually coagulating sedimentation layer, filtering layer, sterilizing layer from top to bottom in purifying vessel, purifying vessel lower end connects tank room by pipe connecting, such seawater can effectively filter, sterilize, carry out desalination process again, and this structure purifies, fading effect is relatively good; Due to connection circulation tube through on pipe connecting, the circulation tube the other end is connected with purifying vessel upper end is through, can carry out repeatedly circular treatment to reach better effect to seawater; Because tank room connects secondary battery, solar components successively, can sun power be utilized like this, economize on resources, reduce the cost of purification; Because purifying vessel lower end arranges ultraviolet tube, ultra-violet sterilization process can be carried out to seawater; Again because filtering layer is double-layer polyamide osmosis filtration layer, adopt this structure, extra large water purification, fading effect are fine.
Accompanying drawing explanation
Below in conjunction with the drawings and specific embodiments, the present invention is further detailed explanation.
Fig. 1 is the structural representation of energy-saving seawater treating plant of the present invention.
Wherein have: 1. water inlet pipe; 2. purifying vessel; 3. coagulating sedimentation layer; 4. filtering layer; 5. sterilizing layer; 6. pipe connecting; 7. circulation tube; 8. water pump; 9. the first valve; 10. the second valve; 11. tank rooms; 12. water shoots; 13. secondary battery; 14. solar components.
Embodiment
The treating plant of energy-saving seawater shown in Fig. 1, comprise water inlet pipe 1, purifying vessel 2, coagulating sedimentation layer 3, filtering layer 4, sterilizing layer 5 is set gradually from top to bottom in purifying vessel 2, purifying vessel 2 lower end connects tank room 11 by pipe connecting 6, pipe connecting 6 and tank room 11 junction are provided with the first valve 9, separate room 11 and connect water shoot 12, through connection circulation tube 7 on pipe connecting 6, circulation tube 7 the other end is connected with purifying vessel 2 upper end is through, and tank room 11 connects secondary battery 13, solar components 14 successively.
Described energy-saving seawater treating plant also comprises water pump 8, and water pump 8 is arranged on the junction of purifying vessel 2 and pipe connecting 6, and water pump 8 is connected with secondary battery 13.
Described energy-saving seawater treating plant also comprises the second valve 10, second valve 10 and is arranged on circulation tube 7.
Described purifying vessel 2 lower end arranges ultraviolet tube.
Described ultraviolet tube is at least one, and ultraviolet tube is evenly arranged in purifying vessel 2 lower end.
Described coagulating sedimentation layer 3 forms component and contains polymerize aluminum chloride.
Described filtering layer 4 is double-layer polyamide osmosis filtration layer.
Described solar components 14 is photovoltaic module.
Described purifying vessel 2 is made up of stainless material.
Owing to setting gradually coagulating sedimentation layer 3, filtering layer 4, sterilizing layer 5 in purifying vessel 2 from top to bottom, purifying vessel 2 lower end connects tank room 11 by pipe connecting 6, such seawater can effectively filter, sterilize, carry out desalination process again, and this structure purifies, fading effect is relatively good; Due to connection circulation tube 7 through on pipe connecting 6, circulation tube 7 the other end is connected with purifying vessel 2 upper end is through, can carry out repeatedly circular treatment to reach better effect to seawater; Because tank room 11 connects secondary battery 13, solar components 14 successively, can sun power be utilized like this, economize on resources, reduce the cost of purification; Because purifying vessel 2 lower end arranges ultraviolet tube, ultra-violet sterilization process can be carried out to seawater; Again because filtering layer 4 is double-layer polyamide osmosis filtration layer, adopt this structure, extra large water purification, fading effect are fine.
Seawater enters in purifying vessel 2 from water inlet pipe 1, precipitate successively, filter, disinfect, carry out ultra-violet sterilization process again, seawater after process, by pipe connecting 6, circulation tube 7 repeats above-mentioned work, when repeating, only need close the first valve 9, open the second valve 10, open water pump 8 again, seawater just can be made to repeat purifying treatment, seawater after purifying treatment, enter into tank room 11 electrolysis again, water after electrolysis from rising pipe 12 out, can be purified, water after desalination, before water enters tank room 11, open the first valve 9.
The technical characteristic described in detail is not had to be prior art in the application.Above-described embodiment is the principle of illustrative the application and effect thereof only, but not for limiting the application.Any person skilled in the art scholar all under the spirit and category of the application, can modify above-described embodiment or changes.Therefore, have in art and usually know that the knowledgeable modifies or changes not departing from all equivalences completed under the spirit and technological thought that the application discloses, must be contained by the claim of the application.
Claims (9)
1. an energy-saving seawater treating plant, it is characterized in that: comprise water inlet pipe (1), purifying vessel (2), coagulating sedimentation layer (3) is set gradually from top to bottom in purifying vessel (2), filtering layer (4), sterilizing layer (5), purifying vessel (2) lower end connects tank room (11) by pipe connecting (6), pipe connecting (6) and tank room (11) junction are provided with the first valve (9), separate room (11) and connect water shoot (12), the upper through connection circulation tube (7) of pipe connecting (6), circulation tube (7) the other end is connected with purifying vessel (2) upper end is through, tank room (11) connects secondary battery (13) successively, solar components (14).
2. according to energy-saving seawater treating plant according to claim 1, it is characterized in that: also comprise water pump (8), water pump (8) is arranged on the junction of purifying vessel (2) and pipe connecting (6), and water pump (8) is connected with secondary battery (13).
3. according to energy-saving seawater treating plant according to claim 1, it is characterized in that: also comprise the second valve (10), the second valve (10) is arranged on circulation tube (7).
4. according to energy-saving seawater treating plant according to claim 1, it is characterized in that: described purifying vessel (2) lower end arranges ultraviolet tube.
5. according to energy-saving seawater treating plant according to claim 4, it is characterized in that: described ultraviolet tube is at least one, and ultraviolet tube is evenly arranged in purifying vessel (2) lower end.
6. according to energy-saving seawater treating plant according to claim 1, it is characterized in that: described coagulating sedimentation layer (3) forms component and contains polymerize aluminum chloride.
7. according to energy-saving seawater treating plant according to claim 1, it is characterized in that: described filtering layer (4) is double-layer polyamide osmosis filtration layer.
8. according to energy-saving seawater treating plant according to claim 1, it is characterized in that: described solar components (14) is photovoltaic module.
9. according to energy-saving seawater treating plant according to claim 1, it is characterized in that: described purifying vessel (2) is made up of stainless material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410561952.0A CN104445761A (en) | 2014-10-21 | 2014-10-21 | Energy-saving seawater purification equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410561952.0A CN104445761A (en) | 2014-10-21 | 2014-10-21 | Energy-saving seawater purification equipment |
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| Publication Number | Publication Date |
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| CN104445761A true CN104445761A (en) | 2015-03-25 |
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| CN201410561952.0A Withdrawn CN104445761A (en) | 2014-10-21 | 2014-10-21 | Energy-saving seawater purification equipment |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106242128A (en) * | 2016-08-01 | 2016-12-21 | 武汉中舟环保设备股份有限公司 | A kind of boats and ships fresh-water tank purifies Preservation Treatment system |
| CN106915852A (en) * | 2016-11-03 | 2017-07-04 | 蔡顺豪 | A kind of light system of seawaterization |
| WO2017157053A1 (en) * | 2016-03-18 | 2017-09-21 | 深圳市易特科信息技术有限公司 | Portable seawater purification device |
| CN108314120A (en) * | 2018-02-08 | 2018-07-24 | 新昌县海格赛斯贸易有限公司 | A kind of novel brackish water desalination device |
| CN113429027A (en) * | 2021-07-22 | 2021-09-24 | 刘祖煌 | Novel seawater desalination pretreatment device |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5949892A (en) * | 1982-09-07 | 1984-03-22 | レニングラドスキイ・テクノロジチエスキイ・インステイテユ−ト・ホロデイルノイ・プロミスレンノステイ | Electrochemical disposal method and device for sewage |
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| CN202144462U (en) * | 2011-04-26 | 2012-02-15 | 傅娜 | Seawater purifier |
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| CN102642960A (en) * | 2012-05-07 | 2012-08-22 | 广州金川环保设备有限公司 | Device and method for ship ballast water processing and applied to seawater/freshwater |
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| JPS5949892A (en) * | 1982-09-07 | 1984-03-22 | レニングラドスキイ・テクノロジチエスキイ・インステイテユ−ト・ホロデイルノイ・プロミスレンノステイ | Electrochemical disposal method and device for sewage |
| CN2458288Y (en) * | 2000-12-19 | 2001-11-07 | 贺佳国 | Electronic treater for fresh water |
| CN201447393U (en) * | 2009-06-30 | 2010-05-05 | 河海大学 | Outdoor drinking water purification device |
| CN201762189U (en) * | 2010-05-26 | 2011-03-16 | 刘正明 | Solar scenery water circulating and utilizing device |
| CN202144462U (en) * | 2011-04-26 | 2012-02-15 | 傅娜 | Seawater purifier |
| CN102515342A (en) * | 2012-01-31 | 2012-06-27 | 沈阳创达技术交易市场有限公司 | Seawater purifying equipment and method |
| CN102642960A (en) * | 2012-05-07 | 2012-08-22 | 广州金川环保设备有限公司 | Device and method for ship ballast water processing and applied to seawater/freshwater |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2017157053A1 (en) * | 2016-03-18 | 2017-09-21 | 深圳市易特科信息技术有限公司 | Portable seawater purification device |
| CN106242128A (en) * | 2016-08-01 | 2016-12-21 | 武汉中舟环保设备股份有限公司 | A kind of boats and ships fresh-water tank purifies Preservation Treatment system |
| CN106915852A (en) * | 2016-11-03 | 2017-07-04 | 蔡顺豪 | A kind of light system of seawaterization |
| CN108314120A (en) * | 2018-02-08 | 2018-07-24 | 新昌县海格赛斯贸易有限公司 | A kind of novel brackish water desalination device |
| CN113429027A (en) * | 2021-07-22 | 2021-09-24 | 刘祖煌 | Novel seawater desalination pretreatment device |
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Application publication date: 20150325 |