CN108069552A - A kind of seawater treatment system - Google Patents
A kind of seawater treatment system Download PDFInfo
- Publication number
- CN108069552A CN108069552A CN201711332576.8A CN201711332576A CN108069552A CN 108069552 A CN108069552 A CN 108069552A CN 201711332576 A CN201711332576 A CN 201711332576A CN 108069552 A CN108069552 A CN 108069552A
- Authority
- CN
- China
- Prior art keywords
- water
- ozone
- organic matter
- blending tank
- water outlet
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000013535 sea water Substances 0.000 title claims abstract description 36
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 109
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 55
- 238000002156 mixing Methods 0.000 claims abstract description 33
- 239000005416 organic matter Substances 0.000 claims abstract description 32
- 230000001954 sterilising effect Effects 0.000 claims abstract description 30
- 102000004169 proteins and genes Human genes 0.000 claims abstract description 29
- 108090000623 proteins and genes Proteins 0.000 claims abstract description 29
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 25
- 229910001385 heavy metal Inorganic materials 0.000 claims abstract description 22
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 7
- 238000001914 filtration Methods 0.000 claims description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 6
- 239000006004 Quartz sand Substances 0.000 claims description 5
- 239000010419 fine particle Substances 0.000 claims description 5
- 238000000926 separation method Methods 0.000 claims description 5
- 229910052799 carbon Inorganic materials 0.000 claims description 4
- 239000000706 filtrate Substances 0.000 claims description 4
- 238000002386 leaching Methods 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims description 4
- 241000894006 Bacteria Species 0.000 claims description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims 1
- 239000003344 environmental pollutant Substances 0.000 claims 1
- 229910052760 oxygen Inorganic materials 0.000 claims 1
- 239000001301 oxygen Substances 0.000 claims 1
- 231100000719 pollutant Toxicity 0.000 claims 1
- 241000238634 Libellulidae Species 0.000 description 13
- 238000011109 contamination Methods 0.000 description 5
- 230000006378 damage Effects 0.000 description 5
- 238000009360 aquaculture Methods 0.000 description 4
- 244000144974 aquaculture Species 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 241000305776 Rynchops Species 0.000 description 3
- 239000000356 contaminant Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 241000607598 Vibrio Species 0.000 description 2
- 206010047400 Vibrio infections Diseases 0.000 description 2
- 239000000090 biomarker Substances 0.000 description 2
- 244000052769 pathogen Species 0.000 description 2
- 230000001717 pathogenic effect Effects 0.000 description 2
- 239000010453 quartz Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003653 coastal water Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000009432 framing Methods 0.000 description 1
- 238000003306 harvesting Methods 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 239000002699 waste material Substances 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
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- 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
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
-
- 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
- C02F1/325—Irradiation devices or lamp constructions
-
- 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
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/20—Heavy metals or heavy metal compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
Abstract
A kind of seawater treatment system, the system are made of heavy metals removal device, organic matter separator and ultraviolet sterilization apparatus；The heavy metals removal device is made of water pump, water inlet, more medium filter and water outlet；The organic matter separator is made of ozone blending tank, jet pump, ejector, ozone generator, Protein Skimmer, jet pump and ejector；The ultraviolet sterilization apparatus carries out sterilization processing to the water handled well through organic matter separator.
Description
Technical field
The invention belongs to water treatment field more particularly to a kind of seawater treatment systems.
Background technology
With the development of human being's production, the continuous growth of population, every year to the waste of ocean dumping up to tens tons, largely
Polluter have no temperately to arrange to ocean, the nearly maritime environment pollution that coastal estuary bay and coastal big and medium-sized cities are adjoined adds
Play, marine environmental quality decline year by year, and offshore pollution scope expands.
The pollution of seawater has seriously constrained the sustainable development of aquaculture, and cultivation risk greatly improves, some places
Even often there is situation about having no harvest.
To ensure the normal production of culture fishery, production could be entered by all having to pass through processing from the seawater of coastal waters extraction
Link, but the method that each cultivation unit uses at present is still that simple filtering and sterilization process carry out Seawater Treatment, these sides
Method treated seawater often occurs heavy metal, organic matter and the exceeded situation of Biological indicators, can not adapt to current seawater ring
The requirement in border.
The content of the invention
In view of the deficiencies of the prior art, the object of the present invention is to provide a kind of seawater treatment system, the system is for current
Existing heavy metal, organic matter and Biological indicators excessive problem carry out process optimization, make the seawater handled through the system and each
Item index is better than aquatic fry growing and the requirement of cultivation.
The technical solution adopted by the present invention is as follows：
A kind of seawater treatment system, the system is by heavy metals removal device A, organic matter separator B and ultraviolet sterilization
Device C is formed,
The heavy metals removal device A is made of water pump, water inlet, more medium filter and water outlet, pending water
Entering more medium filter 3 through water inlet after water pump pressurizes, the water after filtering flows out heavy metals removal device A from water outlet,
Into organic matter separator B；
The organic matter separator B is by ozone blending tank, jet pump, ejector, ozone generator, Separation of Proteins
Device, jet pump and ejector composition, enter from the water that heavy metals removal device A water outlets flow out through ozone blending tank water inlet
Ozone blending tank enters protein by ozone blending tank water outlet with the mixed water of ozone through Protein Skimmer water inlet
Separator carries out the organic matter in water separation removal, and the jet pump of ozone blending tank draws water from jet stream intake, through jet stream
Device from efflux backwater mouth enters ozone blending tank after being mixed with ozone, and the air inlet of ejector is connected with ozone generator.Albumen
The jet pump of matter separator draws water from jet stream intake, enters protein from efflux backwater mouth after ejector is mixed with air
Separator, the air inlet of ejector are connected with air entry, through the water that organic matter separator B is handled well by water outlet flow out into
Enter ultraviolet sterilization apparatus C.Ozone blending tank before Protein Skimmer is set, contact of the seawater with ozone can be effectively increased
Ozone concentration in time and raising seawater, can effectively kill vibrios in seawater etc. has aquaculture the disease of serious harm
Bacterium.
The ultraviolet sterilization apparatus C carries out sterilization processing to the water handled well through organic matter separator (B).
The ultraviolet sterilization apparatus (C) carries out described in sterilization processing the water handled well through organic matter separator (B)
Ultraviolet sterilization apparatus C is made of water inlet, irradiation chamber and water outlet, and the water handled well through organic matter separator B is by water outlet
Mouth outflow enters irradiation chamber from water inlet and carries out sterilizing processing, and treated, and water is flowed out through water outlet from system water outlet.
In one preferred embodiment, irradiation intracavitary is provided with the quartz burner of different capacity, in water inlet 20
It is equipped between water outlet 21 across pipe, to facilitate the maintaining of ultraviolet sterilization apparatus C.
Multilayer quartz sand and carbon leaching material are filled in another preferred embodiment, in more medium filter,
By the filtering and suction-operated of multilayer filtrate, the fine particle and heavy metal contaminants in seawater can be effectively removed.
In another preferred embodiment, the ozone blending tank carries pressure, so that water is from ozone blending tank
Substantial amounts of micro-bubble can be released when out entering Protein Skimmer, improves Protein Skimmer 14 to organic contamination
Treatment effeciency.
Beneficial technique effect：
Multilayer quartz sand and carbon leaching material are filled in more medium filter in the system of the present invention, can be effectively removed
Fine particle and heavy metal contaminants in seawater, organic matter separator B set ozone to mix before Protein Skimmer
Tank can be effectively increased the time of contact of seawater and ozone and improve the ozone concentration in seawater, can effectively kill the arc in seawater
Bacterium etc. has aquaculture the germ of serious harm, and in organic matter separator, since ozone blending tank carries pressure,
Water can release substantial amounts of micro-bubble when out entering Protein Skimmer from ozone blending tank, improve Separation of Proteins
Device is to the treatment effeciency of organic contamination；Further, ultraviolet sterilization apparatus is set in systems, it is remaining that destruction can be played
The effect of ozone, and can rapidly kill the germ in seawater.The system can effectively remove heavy metal pollution in seawater, have
Machine object pollutes and pathogen contamination, cost of investment are low, easy to operate, reliable.
Description of the drawings
Fig. 1 is the structural framing figure of the present invention；
Fig. 2 is the structure chart of the equipment of the present invention；
Reference sign：A heavy metals removal devices, B organic matter separators, C ultraviolet sterilization apparatus, 1 water pump, 2
Water inlet, 3 more medium filters, 4 water outlets, 5 ozone blending tank water inlets, 6 ozone blending tanks, 7 ozone blending tank water outlets
Mouthful, 8 jet stream intakes, 9 jet pumps, 10 ejectors, 11 efflux backwater mouths, 12 ozone generators, the water inlet of 13 Protein Skimmers
Mouth, 14 Protein Skimmers, 15 water outlets, 16 jet stream intakes, 17 jet pumps, 18 ejectors, 19 air inlets and air entry,
20 water inlets, 21 water outlets, 22 irradiation chambers, 23 system water outlets
Specific embodiment：
As shown in Figure 1, the present invention provides a kind of seawater treatment systems, the system is by heavy metals removal device A, organic matter
Separator B and ultraviolet sterilization apparatus C compositions,
As shown in Fig. 2, the heavy metals removal device A is by water pump 1, water inlet 2, more medium filter 3 and water outlet 4
Composition, pending water enter more medium filter 3 after the pressurization of water pump 1 through water inlet 2, and the water after filtering is flowed from water outlet 4
Go out heavy metals removal device A, into organic matter separator B；
The organic matter separator B is by ozone blending tank 6, jet pump 9, ejector 10, ozone generator 12, protein
Separator 14, jet pump 17 and ejector 18 form, and the water flowed out from heavy metals removal device A water outlets 4 is through ozone blending tank
Water inlet 5 is intake with the mixed water of ozone into ozone blending tank 6 by ozone blending tank water outlet 7 through Protein Skimmer
Mouthfuls 13 enter Protein Skimmers 14, carry out separation removal to the organic matter in water, and the jet pump 9 of ozone blending tank 6 is from jet stream
Intake 8 draws water, from efflux backwater mouth 11 into ozone blending tank 6 after ejector 10 is mixed with ozone, ejector 10 into
Gas port is connected with ozone generator 12.The jet pump 17 of Protein Skimmer 14 draws water from jet stream intake 16, through ejector 18
Entering Protein Skimmer 14 from efflux backwater mouth 20 after being mixed with air, the air inlet of ejector 18 is connected with air entry 19,
The water handled well through organic matter separator B exits into ultraviolet sterilization apparatus C by water outlet 15.
The ultraviolet sterilization apparatus C carries out sterilization processing to the water handled well through organic matter separator B.It is described ultraviolet
Line sterilizing unit C is made of water inlet 20, irradiation chamber 22 and water outlet 21, and the water handled well through organic matter separator B is by going out
The mouth of a river 15, which is flowed out from water inlet 20 into irradiation chamber 22, carries out sterilizing processing, and treated water is through water outlet 21 from system
Water outlet 23 flows out.
In one preferred embodiment, the quartz burner that different capacity is provided in chamber 22 is irradiated, in water inlet
It is equipped between 20 and water outlet 21 across pipe, to facilitate the maintaining of ultraviolet sterilization apparatus C.
In another preferred embodiment, multilayer quartz sand and activated carbon are filled in the more medium filter 3
Filtrate by the filtering and suction-operated of multilayer filtrate, can effectively remove the fine particle in seawater and heavy metal pollution
Object.
In another preferred embodiment, the ozone blending tank 6 carries pressure, so that water is from ozone blending tank
6 can release substantial amounts of micro-bubble when out entering Protein Skimmer 14, improve Protein Skimmer 14 to organic dirt
The treatment effeciency of dye.
Multilayer quartz sand and carbon leaching material are filled in more medium filter 3 in the system of the present invention, can effectively be gone
Except the fine particle and heavy metal contaminants in seawater, organic matter separator B sets ozone to mix before Protein Skimmer
Tank is closed, the time of contact of seawater and ozone can be effectively increased and improves the ozone concentration in seawater, can effectively be killed in seawater
Vibrios etc. has aquaculture the germ of serious harm, and in organic matter separator B, since ozone blending tank is with pressure
Power, water can release substantial amounts of micro-bubble when out entering Protein Skimmer from ozone blending tank, improve protein point
From device to the treatment effeciency of organic contamination；Further, ultraviolet sterilization apparatus 22 is set in systems, destruction can be played
The effect of residual ozone, and can rapidly kill the germ in seawater.The system can effectively remove heavy metal-polluted in seawater
Dye, organic pollution and pathogen contamination, cost of investment are low, easy to operate, reliable.
Above-mentioned detailed description is illustrating for one of the present invention practicable embodiment, which is not to limit
The scope of the claims of the present invention is made, all equivalence enforcements or change without departing from carried out by the present invention are intended to be limited solely by the patent model of this case
In enclosing.
Claims (5)
1. a kind of seawater treatment system, which is killed by heavy metals removal device (A), organic matter separator (B) and ultraviolet light
Bacterium device (C) forms；
The heavy metals removal device (A) is made of water pump (1), water inlet (2), more medium filter (3) and water outlet (4),
Pending water after water pump (1) pressurization through water inlet (2) into more medium filter (3), water after filtering is from water outlet (4)
Heavy metals removal device (A) is flowed out, into organic matter separator (B)；
The organic matter separator (B) by ozone blending tank (6), jet pump (9), ejector (10), ozone generator (12),
Protein Skimmer (14), jet pump (17) and ejector (18) composition, flow out from heavy metals removal device (A) water outlet (4)
Water through ozone blending tank water inlet (5) into ozone blending tank (6), with the mixed water of ozone by ozone blending tank water outlet
(7) enter Protein Skimmer (14) through Protein Skimmer water inlet (13), separation removal is carried out to the organic matter in water, it is smelly
The jet pump (9) of oxygen blending tank (6) draws water from jet stream intake (8), from efflux backwater after ejector (10) is mixed with ozone
Mouth (11) is connected into ozone blending tank (6), the air inlet of ejector (10) with ozone generator (12), Protein Skimmer
(14) jet pump (17) draws water from jet stream intake (16), from efflux backwater mouth (20) after ejector (18) is mixed with air
Into Protein Skimmer (14), the air inlet of ejector (18) is connected with air entry (19), through organic matter separator B processing
Good water exits into ultraviolet sterilization apparatus (C) by water outlet (15)；
The ultraviolet sterilization apparatus (C) carries out sterilization processing to the water handled well through organic matter separator (B).
2. a kind of seawater treatment system as described in claim 1, the ultraviolet sterilization apparatus (C) is by water inlet (20), spoke
It forms according to chamber (22) and water outlet (21), is flowed out through the water that organic matter separator (B) is handled well by water outlet (15) from water inlet
Mouth (20) carries out sterilizing processing into irradiation chamber (22), and treated, and water is flowed through water outlet (21) from system water outlet (23)
Go out.
3. seawater treatment system as claimed in claim 2, the interior ultraviolet radiator for being provided with different capacity of irradiation chamber (22)
Pipe is equipped between the water inlet (20) of the ultraviolet sterilization apparatus (C) and water outlet (21) across pipe, to facilitate ultraviolet light
The maintaining of sterilizing unit (C).
4. a kind of seawater treatment system as described in claim 1, the more medium filter (3) is interior to be filled with multilayer quartz sand
And carbon leaching material, by the filtering and suction-operated of multilayer filtrate, the fine particle and a huge sum of money in seawater can be effectively removed
Belong to pollutant.
5. a kind of seawater treatment system as described in any one of foregoing claim, the ozone blending tank (6) carry pressure, with
So that water can release substantial amounts of micro-bubble when out entering Protein Skimmer (14) from ozone blending tank (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711332576.8A CN108069552A (en) | 2017-12-13 | 2017-12-13 | A kind of seawater treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711332576.8A CN108069552A (en) | 2017-12-13 | 2017-12-13 | A kind of seawater treatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108069552A true CN108069552A (en) | 2018-05-25 |
Family
ID=62158563
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711332576.8A Pending CN108069552A (en) | 2017-12-13 | 2017-12-13 | A kind of seawater treatment system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108069552A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110089697A (en) * | 2019-05-21 | 2019-08-06 | 华南理工大学 | A kind of preparation method of instant clean shellfish |
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|---|---|---|---|---|
| JPH02207882A (en) * | 1989-02-06 | 1990-08-17 | Takashi Mae | Device for treating sewage or the like |
| CN103112996A (en) * | 2013-02-06 | 2013-05-22 | 姜汉平 | Aquaculture water circulation purification method and device |
| CN104642248A (en) * | 2014-12-11 | 2015-05-27 | 赵亦兵 | Seawater recirculating aquaculture system |
| CN206375783U (en) * | 2016-12-15 | 2017-08-04 | 郑州浪鲸泳池设备制造有限公司 | Aquarium hydraulic automatic water treatment system |
| JP2017201935A (en) * | 2016-05-12 | 2017-11-16 | タイワン ウォーター リサイクル テクノロジー カンパニー リミテッドＴａｉｗａｎ Ｗａｔｅｒ Ｒｅｃｙｃｌｅ Ｔｅｃｈｎｏｌｏｇｙ Ｃｏ．， Ｌｔｄ． | Method and system for combining aquaculture with plant cultivation |
| EP3246292A1 (en) * | 2016-05-16 | 2017-11-22 | Taiwan Water Recycle Technology Co., Ltd. | Method and system of cultivating aquatic product and plant |
| CN107459209A (en) * | 2017-08-24 | 2017-12-12 | 广州翔曦能源科技有限公司 | A kind of circular water treating system and a kind of cultivation water circulation purifying method |
| CN208394956U (en) * | 2017-12-13 | 2019-01-18 | 广州畅驰机电设备有限公司 | A kind of seawater treatment system |
-
2017
- 2017-12-13 CN CN201711332576.8A patent/CN108069552A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02207882A (en) * | 1989-02-06 | 1990-08-17 | Takashi Mae | Device for treating sewage or the like |
| CN103112996A (en) * | 2013-02-06 | 2013-05-22 | 姜汉平 | Aquaculture water circulation purification method and device |
| CN104642248A (en) * | 2014-12-11 | 2015-05-27 | 赵亦兵 | Seawater recirculating aquaculture system |
| JP2017201935A (en) * | 2016-05-12 | 2017-11-16 | タイワン ウォーター リサイクル テクノロジー カンパニー リミテッドＴａｉｗａｎ Ｗａｔｅｒ Ｒｅｃｙｃｌｅ Ｔｅｃｈｎｏｌｏｇｙ Ｃｏ．， Ｌｔｄ． | Method and system for combining aquaculture with plant cultivation |
| EP3246292A1 (en) * | 2016-05-16 | 2017-11-22 | Taiwan Water Recycle Technology Co., Ltd. | Method and system of cultivating aquatic product and plant |
| CN206375783U (en) * | 2016-12-15 | 2017-08-04 | 郑州浪鲸泳池设备制造有限公司 | Aquarium hydraulic automatic water treatment system |
| CN107459209A (en) * | 2017-08-24 | 2017-12-12 | 广州翔曦能源科技有限公司 | A kind of circular water treating system and a kind of cultivation water circulation purifying method |
| CN208394956U (en) * | 2017-12-13 | 2019-01-18 | 广州畅驰机电设备有限公司 | A kind of seawater treatment system |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110089697A (en) * | 2019-05-21 | 2019-08-06 | 华南理工大学 | A kind of preparation method of instant clean shellfish |
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Application publication date: 20180525 |
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