CN108328848A - The return-to-zero method of cultivation water - Google Patents
The return-to-zero method of cultivation water Download PDFInfo
- Publication number
- CN108328848A CN108328848A CN201710042437.5A CN201710042437A CN108328848A CN 108328848 A CN108328848 A CN 108328848A CN 201710042437 A CN201710042437 A CN 201710042437A CN 108328848 A CN108328848 A CN 108328848A
- Authority
- CN
- China
- Prior art keywords
- water
- cultivation
- pond
- cultivation water
- ozone
- 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
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 243
- 238000000034 method Methods 0.000 title claims abstract description 30
- 238000012545 processing Methods 0.000 claims abstract description 61
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 46
- 241000195493 Cryptophyta Species 0.000 claims abstract description 45
- 238000009360 aquaculture Methods 0.000 claims abstract description 40
- 244000144974 aquaculture Species 0.000 claims abstract description 39
- 241000894006 Bacteria Species 0.000 claims abstract description 20
- 238000001914 filtration Methods 0.000 claims abstract description 12
- 229910052500 inorganic mineral Inorganic materials 0.000 claims abstract description 10
- 239000011707 mineral Substances 0.000 claims abstract description 10
- 239000006041 probiotic Substances 0.000 claims description 42
- 235000018291 probiotics Nutrition 0.000 claims description 42
- 239000010453 quartz Substances 0.000 claims description 14
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 14
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 12
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical group [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 10
- 239000001301 oxygen Substances 0.000 claims description 10
- 229910052760 oxygen Inorganic materials 0.000 claims description 10
- 230000009286 beneficial effect Effects 0.000 claims description 9
- 229910002651 NO3 Inorganic materials 0.000 claims description 6
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 claims description 6
- 241001148470 aerobic bacillus Species 0.000 claims description 6
- 229910021529 ammonia Inorganic materials 0.000 claims description 6
- IOVCWXUNBOPUCH-UHFFFAOYSA-M Nitrite anion Chemical compound [O-]N=O IOVCWXUNBOPUCH-UHFFFAOYSA-M 0.000 claims description 5
- 230000003647 oxidation Effects 0.000 claims description 5
- 238000007254 oxidation reaction Methods 0.000 claims description 5
- 239000013589 supplement Substances 0.000 claims description 4
- 235000007164 Oryza sativa Nutrition 0.000 claims description 3
- 239000007864 aqueous solution Substances 0.000 claims description 3
- 230000005611 electricity Effects 0.000 claims description 3
- 238000000605 extraction Methods 0.000 claims description 3
- 239000012535 impurity Substances 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 3
- 235000013379 molasses Nutrition 0.000 claims description 3
- 235000009566 rice Nutrition 0.000 claims description 3
- 239000000284 extract Substances 0.000 claims description 2
- 240000007594 Oryza sativa Species 0.000 claims 1
- 230000005923 long-lasting effect Effects 0.000 abstract description 2
- 241000251468 Actinopterygii Species 0.000 description 30
- 238000009395 breeding Methods 0.000 description 21
- 230000001488 breeding effect Effects 0.000 description 21
- 210000003608 fece Anatomy 0.000 description 17
- 230000012010 growth Effects 0.000 description 15
- 230000001954 sterilising effect Effects 0.000 description 10
- 230000008569 process Effects 0.000 description 9
- 230000000694 effects Effects 0.000 description 7
- 238000004659 sterilization and disinfection Methods 0.000 description 7
- 238000003672 processing method Methods 0.000 description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 230000004913 activation Effects 0.000 description 4
- 238000011067 equilibration Methods 0.000 description 4
- 230000001932 seasonal effect Effects 0.000 description 4
- 238000000354 decomposition reaction Methods 0.000 description 3
- 230000000249 desinfective effect Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 230000008030 elimination Effects 0.000 description 3
- 238000003379 elimination reaction Methods 0.000 description 3
- 230000007774 longterm Effects 0.000 description 3
- 239000003643 water by type Substances 0.000 description 3
- 241000209094 Oryza Species 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000029142 excretion Effects 0.000 description 2
- 230000005415 magnetization Effects 0.000 description 2
- 230000003472 neutralizing effect Effects 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000003442 weekly effect Effects 0.000 description 2
- 241000143060 Americamysis bahia Species 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 206010029412 Nightmare Diseases 0.000 description 1
- 241000108664 Nitrobacteria Species 0.000 description 1
- IOVCWXUNBOPUCH-UHFFFAOYSA-N Nitrous acid Chemical compound ON=O IOVCWXUNBOPUCH-UHFFFAOYSA-N 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- MMDJDBSEMBIJBB-UHFFFAOYSA-N [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[NH6+3] Chemical compound [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[NH6+3] MMDJDBSEMBIJBB-UHFFFAOYSA-N 0.000 description 1
- 230000002159 abnormal effect Effects 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000005276 aerator Methods 0.000 description 1
- 230000005791 algae growth Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 210000000476 body water Anatomy 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000003139 buffering effect Effects 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 235000013339 cereals Nutrition 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 230000009849 deactivation Effects 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 239000005446 dissolved organic matter Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 210000003127 knee Anatomy 0.000 description 1
- 230000002045 lasting effect Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- GQPLMRYTRLFLPF-UHFFFAOYSA-N nitrous oxide Inorganic materials [O-][N+]#N GQPLMRYTRLFLPF-UHFFFAOYSA-N 0.000 description 1
- 238000006213 oxygenation reaction Methods 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 238000012552 review Methods 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 230000004083 survival effect Effects 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 239000010457 zeolite 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
- C02F1/30—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
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
-
- 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
- C02F1/68—Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable water
-
- 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
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/20—Nature of the water, waste water, sewage or sludge to be treated from animal husbandry
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
- C02F3/348—Biological treatment of water, waste water, or sewage characterised by the microorganisms used characterised by the way or the form in which the microorganisms are added or dosed
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)
- Farming Of Fish And Shellfish (AREA)
Abstract
The invention discloses a kind of return-to-zero methods of cultivation water, comprise the steps of：Cultivation water in one aquaculture pond is guided into a processing pond, imposes an ozone treatment, and processing is irradiated with a ultraviolet, so as to eliminating harmful bacterium and algae in the cultivation water, and becomes a clear water.It is guided into again to a foster pond, by drip filtration treatment, and adds some special strains and algae in the cultivation water, and minerals are supplemented in the cultivation water.It separately supports pond in this and has been built into a pelelith, so as to adjusting the pH value of the cultivation water, the clear water is enable to become a new cultivation water, and be returned to original or " zero " state.The new cultivation water is guided again again and is back to the aquaculture pond, and can be long lasting for same loop water is used, without separately adding new water.
Description
Technical field
The present invention relates to a kind of return-to-zero methods of cultivation water.
Background technology
The cultivating systems such as general common farm, aquarium or fishpond of fresh water or seawater at present, due to aquatic-organism
Daily residual bait or excreta can then generate largely in water and have the harmful substances such as dangerous ammonia and nitrous acid.Therefore it needs
To be general coarse, bulky grain and other residual baits that may filter that or excretion preliminary filtering in advance via physical filtering.Then
Again via biofiltration, Nitrosomas is converted ammonia into nitrite；Nitrite transformation is harmless by recycling Nitromonas
Nitrate.Finally, in addition nitrate excessive in cultivation water then must more renew water and could remove.In addition to this, when long
Under cultivation long-term Jian, it will cultivating system is caused to generate " turning one's coat " phenomenon, the reason of " turning one's coat " phenomenon causes, even often
It, which continues, carries out above general common physical filtering and biofiltration, still can be accumulated in cultivation water it is other can be voluntarily autonomous
The harmful bacteria of growth and algae.Once gradually occupying the life of the probiotics such as original probiotics, nitrifier or microalgae
After depositing space, nitrifier and microalgae will mortality, and make entire cultivating system disequilibrium, and cause water quality violent
Variation, so that the crash of entire cultivating system, and the survival of entail dangers to water fish only.The problem of confrontation above " turning one's coat ",
For now, still must by weekly more renew water, could remove these harmful bacterias and algae, and can maintain
Timeliness will be comparable of short duration.Only after changing water each time, it is necessary to a large amount of addition supplements beneficial strain and algae,
To keep the quantity of probiotics and algae, cultivating system to be possible to maintain longer time without collapsing, such way,
A large amount of water, probiotics and algae will be expended, the cost spent is then comparable huge, and general cultivation dealer is basic
It is to be difficult to bear.
To solve above-mentioned disadvantage, thus have invention I 273889 that on 2 21st, 2007 TaiWan, Chinas are announced "
Indoor high-density aquaculture water circle device " Patent Case discloses：One can purify the clean unit of a breeding water body, one can
The green ray light-wave energy of oxygen is released so as to the resonant activation unit of breeding water body resonant activation, one can allow supporting after resonant activation
It grows water body and further magnetizes stable magnetization and stablize unit and one can drive breeding water body can be in aquaculture pond, clean unit, resonance
The cycle driving unit circulated between unit is stablized in activation unit and the magnetization.The clean unit have a physical filter,
One biological processor, a denitration process device and one and disinfecting and sterilizing device.It is filtered out using the physical filter outstanding in breeding water body
Floating solid (such as：Feed residual bait and fishes and shrimps excrement)；It is continuous and, using in the biological processor, by microorganism (such as nitrobacteria)
Adhere to form " biomembrane " in surface of filter medium, with decompose remove breeding water body in organic suspension/dissolved solid (such as：Compared with tool
The ammoniacal nitrogen and phosphate of toxicity)；Then, using the denitration process device, the nitrate nitrogen in breeding water body is reduced into nitrogen
And it removes；Finally, it is gone out except the bacterium in breeding water body, and oxidation removal remnants organic matters using the disinfecting and sterilizing device.So as to inciting somebody to action
The dirty breeding water body purified treatment being discharged from aquaculture pond is at legal breeding water body water standard is met, similar to sterile free from admixture
Clear water state.
Although the patent case has dirty cultivation purifying water process into clean cultivation water, it is similar to sterile, nothing
The function of the clear water state of impurity, processing equipment is excessive, and can occupy excessive space and it is necessary to often a large amount of to replace
New water, so that forming waste.Moreover, sterile, free from admixture clear water after processed, the probiotics in water and algae one
Denier has little time flourish, or when original progress water process, it is contemplated that the harmful bacteria that can be eliminated is again quick once again with algae
Growth, and again occupy original probiotics and the living space of algae, then can be easy to cause fish only inadaptable, seriously
Person will large quantities of death, in turn result in great loss.Therefore, the cyclic processing device of the patent case can only at most make cultivation
System multidimensional holds one section of of short duration equilibration time, such as one month.Once cultivating system is in probiotics and carries out denitration
When the stage of processing, it is still desirable to it is large batch of to carry out changing water, so as to extending the time of cultivating system balance, but be more than once
After this of short duration equilibration time, the crash of cultivating system is still resulted in.
Have again invention I 320304 that on 2 11st, 2010 TaiWan, Chinas are announced " automatic circulating-water life-supporting with support
Grow system " Patent Case, it discloses：It is somebody's turn to do including at least dismountable group type cultivation groove body, the circulating purifier connection of an automation
Groove body and an automatic real time monitoring, early warning and feedback equipment are cultivated, it is described to monitor the water quality in the breeding trough body
It includes mechanical and microbial deactivation apparatus, a disinfecting device and a life support system to automate circulating purifier,
To extract, water is after physical and biofiltration processing in cultivation groove body, after carry out disinfection sterilization and raising dissolved oxygen in water rate,
It imports in cultivation groove body to recycle and reuse, whereby, it is ensured that the water quality in cultivation groove body is abnormal in optimum state, and in water quality
When, warning message can be sent out in time, is excluded by operator, and the system is allow to provide the cultivation ring of one almost " constant "
Border.
The processing equipment that the patent case equally has is excessive, the shortcomings that occupying excessive space and largely renew water often,
Therefore in using upper still ideal not to the utmost.Moreover, in the same manner, sterile, free from admixture clear water after processed, such as probiotics and algae
When the growth of class is incomplete or when original water process, it is contemplated that the harmful bacteria that is eliminated and algae once again fast-growth and
Replace probiotics and when algae, although have early warning mechanism, that is, after waiting until that cultivation water flashes the redlight, it is so-called to carry out
" take stopgap measures " reactive mode.However, as cultivation time gets over more remote, such " constant " mode, it is inevitable
It is to be increasingly difficult to maintain, also only extends the equilibration time for remaining of short duration, such as two months at most.Namely it is in alarm
Water large batch of will be changed when the stage, finally, be unable to escape entire cultivation water eventually and ruined and the destiny of crash, gently then cause fish
Group's is not suitable with, then large quantities of death when serious, and cultivation dealer can be caused greatly to lose.Therefore above-mentioned two patent cases,
Whether it is disposed at denitration stage or warning stage, can only all maintain one section of of short duration equilibration time, such as one
The moon or two months.Even if at this stage, progress largely changes water, such as fails to add beneficial strain and algae, Er Qiewei
When removing the harmful bacteria of a large amount of fast-growths and algae in water removal, cultivating system not may long sustaining, be unable to escape eventually
The destiny of system crash, therefore be all a nightmare that can't get rid of forever for cultivating dealer.
It is another have Chinese disclosed invention the 201410104746.7th on July 9th, 2014 " a kind of aquiculture waste water
Processing method " discloses：Include the following steps：1. level-one sedimentation filtration, 2. algae purifications, 3. oxidation removal solubilised states are organic
Object, the filtering of 4. two-stage precipitations, 5. are pumped into dissolved oxygen and 6. sterilizings, ultimately form available recirculated water.With operation letter
Just, easy to implement, have treating capacity big, the advantages that low energy consumption, continuous operation；Recirculated water after processing is rich in dissolving
Oxygen is free of dissolved organic matter, inorganic matter and germ, securely and reliably.
Last one of program of the water treatment method of the patent case is " sterilizing ", at this time via " sterilizing "
In water after processed, without any probiotics and for the algae of feeding.With the master of " zero " processing method of the invention
It is to be to want technical characteristic：" first eliminating harmful bacteria and algae, then cultivate probiotics and algae ", that is, supporting after processing
It grows and is rich in probiotics and algae in water, therefore the technical characteristic of the present invention and the patent case are significantly different.Again before the patent
The processing routine of case needs aquaculture pond ,-grade settling tank, sludge filter press, zeolite filter, algae purification pond, solubilised state organic
The processing unit of object digestion chamber, ozonator-pump, two level settling tank, oxygenation pond, aerator and liquid storage tank etc. up to 11, therefore
Need very large accommodating space and processing time.Review that present invention only requires 2, a processing pond and a foster ponds etc.
Processing unit, you can be carried out at the same time for the cultivation water in aquaculture pond and " handle, sterilization, remove algae, filtering, foster water, bacteria, foster algae
And feeding " the effects that, therefore best water treatment effect and breeding function can be reached.
Invention content
The purpose of the present invention is to provide a kind of return-to-zero methods of cultivation water, can be by the cultivation in aquaculture pond
Water is removed harmful bacterium and algae, then is implanted into preselected beneficial strain and microalgae, make its be returned to it is original or
Person " zero " state, " zero " processing method without separately dosing new water.
A kind of return-to-zero method of cultivation water, comprises the steps of：By the cultivation water in the aquaculture pond guide into
Enter to a processing pond；An ozone is imposed for the cultivation water to handle, and processing, institute are irradiated with a ultraviolet
Ozone is stated under the ultraviolet light irradiation, using oxidation, so as to eliminating harmful bacterium and algae in the cultivation water,
Become a clear water；The clear water after will be processed is guided into again to a foster pond, makes the clear water via drip
Filtration treatment, and a beneficial strain and an algae are added in the clear water, using the algae as aquatic-organism feeding
Bait, be built into a pelelith in the foster pond, so as to adjusting the pH value of the cultivation water, separately add in the foster pond
Add a minerals, to supplement the minerals in water, so as to a new cultivation water can be cleaned into；The new cultivation water is guided again again
It is back in the aquaculture pond.
Further, it is in the forniciform water-supply-pipe of wave that one is equipped in the processing pond, and the water-supply-pipe connection one first is taken out
Water pump is able to extract the cultivation water in the processing pond using first suction pump and enters the water-supply-pipe, described
Water-supply-pipe is connected with an ozone delivery pipe, the external ozone generators of ozone delivery pipe, so that one ozone of conveying enters to
The water-supply-pipe is fused with the cultivation water.
Further, the water-supply-pipe is close to a control valve is equipped at the position of the ozone delivery pipe, so as to rotating institute
Control valve is stated, the flow velocity of the cultivation water is conveyed to control the water-supply-pipe, and is controlled ozone delivery pipe conveying institute
The concentration in ozone to the water-supply-pipe is stated, the supply of the ozone is to input 25 to 50 g per hour, and make described support
The concentration for growing the ozone in water maintains 5 to 10PPM.
Further, the water outlet end of the water-supply-pipe connects at least one or more the quartz burner, to generate
Ultraviolet is stated, so as to the irradiation for alloing the cultivation water fused with the ozone to pass through the quartz burner.
Further, the length of the quartz burner is 120 centimeters, wattage 55W, and electricity consumption is then 1/3 horsepower.
Further, by the continual cultivation water extracted in the processing pond of first suction pump, by described
The treatment with irradiation of the ozone treatment and the quartz burner in water-supply-pipe, then the cultivation water flow back into the place again
It manages in pond, processing time is 5 to 12 hours.
Further, at least one or more Dropping filter is provided in the foster pond, each Dropping filter is then
Multiple layers of drip box is set, different filter materials is set in each drip box, it is remaining so as to institute in cultivation water described in layering
Impurity, the Dropping filter by one second suction pump, continue 24 hours for the cultivation in the foster pond
Water carries out cycle extraction, makes the cultivation water is continual to be filtered by the Dropping filter.
Further, the strain is an aerobic bacteria, including probiotics, Nitrosomas and nitrifier, the strain tune
The ratio matched with 100 g of strain, then coordinates 1 kilogram of molasses, 20 liters of aqueous solution and 100 g of rice bran, through adjusting
After dissolving, the primary extremely foster pond was poured into every 12 hours, so as to turning out the aerobic bacteria in the clear water,
To remove the ammonia in clear water, nitrite and nitrate.
Further, a tank is connected between the processing pond and the foster pond, so as to the clear water can be stored, utilized
The tank and the adjusting that water can be carried out with the foster pond respectively for the processing pond.
So-called " zero " processing mode, that is, in original cultivation water, be processed by disinfection clean
Clear water doses appropriate minerals, after neutralizing pH value, is implanted into previously selected probiotics strain with algae in fish culture pond
In, allow its breeding of growing up again.And can be long lasting for using identical recirculated water, and it is cleaned into clean cultivation water, it is not required to
Will other than recirculated water water source, separately replace and new water be added.Substantially, signified " zero " processing method of the present invention is special with this
Before profit " constant " alleged by case, maximum difference is that " constant " mode is reaction equation, that is, to wait until that cultivation water lights red
After lamp, the reactive mode of so-called " take stopgap measures " is carried out, so as to reinforcement and safeguards water quality.But with cultivation
Time is more remote, and such " constant " mode is increasingly difficult to maintain.Finally, be unable to escape eventually entire cultivation water ruin, system crash
Destiny.However, " zero " mode of the present invention is in cultivation water, i.e., before sending out a warning, begin to carry out at " zero "
Reason, is both that will process, and clean clear water doses appropriate minerals, after neutralizing pH value, then with previously selected strain
It is refilled in breeding pool with algae, the strains such as its probiotics or nitrifier and algae is enable to grow up again breeding.
After the return-to-zero method of cultivation water of the present invention uses above-mentioned technological means, have the advantages that following：
1, a large amount of processing cultivation waters that can continuously recycle by harmful bacterium and algae in elimination cultivation water, then are implanted into
Scheduled strain and algae make the cultivation water be returned to a clean state, and for long-time free-changing water, to save water resource.
2, water temperature variation when can be according to Various Seasonal, and the cycle times of processing cultivation water process are selected, and
Can according to processing cost number, selection every time only processing total Water 1/4 to 1/5 or 1/2 to 1/3 between, be
One of enforceable mode of the present invention, so as to can reach the processing method of most economical cultivation water.
3, one processing pond and foster pond are only needed, you can place is carried out at the same time for cultivation water caused by aquaculture pond
Reason, sterilization remove algae, filtering, support the effects that water and feeding, therefore can reach best cultivation water treatment efficiency and breeding function.
4, it by all relevant treatment filter plants, is established in processing pond and foster pond, therefore will not occupy excessive
Space, so as to breeding spaces can be saved.
5, aerobic bacteria is cultivated using foster pond, to decompose the nuisances such as ammonia in cultivation water, nitrite and nitrate
Matter.
6, beneficial algae is cultivated using foster pond, it is possible to provide the bait as aquatic-organism feeding.
Description of the drawings
Fig. 1 is the filtration treatment flow chart of the present invention.
Fig. 2 is the configuration schematic diagram of the present invention.
Fig. 3 uses schematic diagram for processing pond of the present invention.
Fig. 4 uses schematic diagram for the foster pond of the present invention.
Table one is the reference table for the interval time that the present invention executes return-to-zero.
【Symbol description】
1 aquaculture pond, 2 processing pond
21 water-supply-pipe, 211 control valve
22 first suction pump, 23 ozone delivery pipe
24 ozone generators, 25 quartz burner
3 foster pond, 31 Dropping filter
311 drip box, 32 second suction pump
33 peleliths.
Specific implementation mode
The frequency and processing water of the return-to-zero of the embodiment of the present invention, can be previously according to the current shape in the aquaculture pond
State, then determined with the asynchronous water temperature of seasonableness, it may include：As fed, fish are only at long status, pH value, water in water
Temperature, temperature bacterium, at influence factors such as long status, after first passing through assessment, then, can make one at long status and microalgae
Cover the frequency and processing water of return-to-zero.In other words, season asynchronous water temperature variation is bigger, and the frequency of return-to-zero is got over
It is high.Following table one is the reference table for the interval time for executing return-to-zero.
Table one
Described in above-mentioned table one, still can because the difference of fingerling, fish body it is of different sizes, the number of fish school number etc. conditions it is different,
And have different processing frequencies and processing water, the return-to-zero interval time in the table one water per treatment, then be one
The reference value of general orientation when processing, although being not an absolute value, but still the great value for having reference and acting on.
As shown in Figs.1 and 2, the embodiment of the present invention includes following steps：
A. the cultivation water in an aquaculture pond is guided into a processing pond.It, can when starting to execute return-to-zero method
Generated cultivation water in an aquaculture pond 1 will be come from, concentrated and be guided into a processing pond 2.The appearance of the processing pond 2
Between water is about 55 tons to 60 tons, and the treatment temperature thermostatic control of cultivation water is between 20 DEG C to 25 DEG C.
B. clear water is become with ozone treatment and ultraviolet treatment with irradiation for the cultivation water.As shown in figure 3, at this
It is in the forniciform water-supply-pipe 21 of wave that one is equipped in reason pond 2, which connects one first suction pump 22, utilizes first pumping
The cycle that water pump 22 is able to extracts the cultivation water in the processing pond 2.The water-supply-pipe 21 connects an ozone delivery pipe 23 again, and the ozone is defeated
It send pipe a 23 external ozone generators 24, so that one ozone of conveying enters to the water-supply-pipe 21, is fused with the cultivation water.It should
Close to a control valve 211 is equipped at the position of the ozone delivery pipe 23 on water-supply-pipe 21, so as to rotating the control valve 211, with
It controls the water-supply-pipe 21 and conveys the flow velocity of the cultivation water, and be controlled the ozone delivery pipe 23 and be delivered in the water-supply-pipe 21
Concentration, that is, the flow velocity of cultivation water is fast, then ozone be dissolved in that the concentration in cultivation water is low but quantity is more, conversely, when the stream of cultivation water
When speed is slow, then ozone is dissolved in the height of the concentration in cultivation water but quantity is few.And it sets by the water-supply-pipe 21 and is bent in as a wave
Shape can make cultivation water when the water-supply-pipe 21 flows, and impulse is generated in each knee, and the ozone in cultivation water is made to obtain
Uniformly to stir and fuse.The supply of the ozone is to input 25 to 50 g per hour, and make the cultivation ozone in water
Concentration is maintained at 5 to 10PPM, so as to for harmful bacteria in elimination cultivation water and the harmful algae of removing.The water-supply-pipe 21 again
Water outlet end be connected to the quartz burners 25 of multiple concatenations, it is multiple so as to enabling the cultivation water fused by ozone to pass through
Quartz burner 25.The length of each quartz burner 25 is 120 centimeters, wattage 55W, and electricity consumption is then 1/3 horsepower.It borrows
So that the fused cultivation water for having ozone can be made when by the quartz burner 25 via the interaction of ultraviolet and ozone
With, make the ozone under ultraviolet light irradiation, generate fierce oxidation, with enhance cultivation water is sterilized and except algae work
With.In this way, extracting the cultivation water in the processing pond 2 by the continual cycle of first suction pump 22, water delivery is iterated through
The treatment with irradiation of the ozone treatment of pipe 21 and multiple quartz burners 25 makes the cultivation water become a clean clear water, then clearly
Water is flow back into again in the processing pond 2, and the circular treatment time is 5 to 12 hours.
C. the clear water after will be processed is guided into again to a foster pond, and filters and add beneficial bacterium by drip
Kind, algae and minerals, and it is cleaned into a new cultivation water.As shown in figure 4, ozone and ultraviolet will be passed through in the processing pond 2
Sterilization and except algae after clear water, then be guided into a foster pond 3.This supports the drop of setting at least one or more in pond 3
Flow filter 31, each Dropping filter 31 are then arranged the drip box 311 of multilayer, difference are respectively provided in each drip box 311
A filter material, so as to the layering clear water.The Dropping filter 31 by one second suction pump 32, continue 24 hours for
The clear water supported in pond 3 carries out cycle extraction, and the continual Dropping filter 31 that iterates through of clear water is made to be dripped
Filter is flowed through, which is about 120 tons, and the treatment temperature of the clear water is controlled between 20 DEG C to 25 DEG C, simultaneously
More Dropping filters 31 can be started to be used cooperatively, to handle different waters.Then in this support added in pond 3 it is beneficial
Strain.The strain can be the aerobic bacterias such as probiotics, Nitrosomas and nitrifier, the ratio of allotment, with 100 g
Strain, then coordinate 1 kilogram of molasses, 20 liters of aqueous solution and 100 g of rice bran, after formulated dissolving, with every 12 hours
It pours into and is once supported in pond 3 to this, so as to turning out aerobic bacterium in the clear water, to remove the ammonia in clear water, nitrous
The harmful substances such as hydrochlorate and nitrate.And suitable beneficial algae is added in the clear water, it can be used as aquatic-organism for generating
The bait of feeding.Again in the clear water add boiling water powder, to supplement the minerals in water, the minerals may include calcium, magnesium etc. at
Point.The bottom that pond 3 is separately supported in this is placed in suitable pelelith 33, and the pH of the cultivation water can be adjusted using the pelelith 33
Value.So as to the processing method using above-mentioned foster water, and the clear water is enable to be cleaned into the new cultivation water that a suitable aquatic-organism is survived.
Therefore, the present embodiment is by harmful bacterium and algae in elimination cultivation water, then is implanted into scheduled probiotics and algae, makes this
New cultivation water is returned to a clean state, and for long-term free-changing water.
D. the new cultivation water is guided again and is back in the aquaculture pond.Cultivation water after cleaned is total by step B and C
After having 36 hours processing and foster water, then it can guide and be back in original aquaculture pond 1 again, be made again as new cultivation water
With in this way, can further coordinate more processing ponds 2 and foster pond 3 while start, for lasting unbroken carry out cultivation water
Processing.And the aquatic-organism raised in aquaculture pond 1, then in the foster pond 3 that can ingest the cultured algae of institute as food,
And growth can be promoted.Minimum processing pond 2 and the foster pond 3 for only needing one of the present invention again, you can carry out cultivation water processing,
Sterilization removes algae, filtering, supports the effects that water and feeding, therefore will not occupy excessive space, and can reach best cultivation water
Treatment effect and breeding function.
The present embodiment by cultivation water via circular treatment after, can especially make cultivation water zero become a new cultivation water
It is continuing with, and can long-time cultivation water free of replacement.Only need more to exchange treaties every half a year later 15% water, and every 3 to 5 years about more
50% water is changed, in this way, the effect of can then reaching 10 to 15 years free-changing waters.
The present invention can also reconnect a tank between the processing pond and the foster pond again, clear so as to that can store this
Water, and have the function of water buffering using the tank, and the water storage in the processing pond and the foster pond can be adjusted respectively
Amount, so as to reaching with a processing pond and foster pond, you can the effect of being handled for the cultivation water of more aquaculture ponds.
The above-mentioned return-to-zero method of the present invention, which focuses on, maintains both an aquaculture pond and foster pond probiotics permanent
The breeding environment of the ecological balance；And the most important condition of both aquaculture pond and foster pond the probiotics ecological balance how is maintained,
It please refers to described in one content of above-mentioned table.To be to control excreta quantity/speed of cultivation pond fish type, every fish in the shoal of fish
Size only, with the factors such as the change of temperature/dissolved oxygen amount of seasonal variations cultivation water.Once the quantity of fish type excreta/
Speed, the size of fish only in the shoal of fish obtain after stablizing and controlling, then greatly with factors such as cultivation water temperature/dissolved oxygen amounts of seasonal variations
Aquaculture pond can about be calculated and decompose the required total amount of probiotics amount of shoal of fish excreta.As long as supporting the sum of probiotics in pond
Amount/growth rate can obtain balance with total amount of probiotics amount/growth rate needed for decomposition shoal of fish excreta in aquaculture pond, i.e.,
Can the entire breeding environment of long sustaining the ecological balance, without causing the collapse of entire cultivating system (also referred to as " to turn one's coat existing
As ").
Variety classes fish has different excretion object amount/speed again, when the more excretas of fish quantity are more, and with the time,
Fish grows up, and volume is bigger to drain fish as fed differences that are also more, or using more/few daily, and causes fish excrement total
Amount/speed can also change.In addition, summer cultivation water temperature is improved compared with winter, (temperature is high in water, and bacterium growth is quick；It is molten in water
Oxygen amount reduces, and pH value can also decline), aerobic bacteria is bigger to cultivation dissolved oxygen in water demand etc., synthesis and all of above phase of integration
After the factor of pass, the probiotics demand total quantity that aquaculture pond decomposes shoal of fish excreta can be about calculated.Again via above-mentioned table
One content can be seen that the major control factors for the different ecological balances, due to having to calculate aquaculture pond decomposition fish
The probiotics demand total quantity of group's excreta, it is necessary to which grasping as fed, (feeding is more, and excreta is more, and probiotics demand increases
Add, and dissolved oxygen in water demand can also increase), pH value (pH value reduce when probiotics growth can decline), water temperature (temperature increase,
Probiotics growth rate is speeded), individual probiotics quantity/type/growth rate, the frequency and water per treatment etc. for handling water
All factors.And the return-to-zero method of cultivation water of the present invention essentially consists in while controlling the growth speed of aquaculture pond probiotics
Degree/quantity and the decomposition required total amount of probiotics amount/speed of shoal of fish excreta in aquaculture pond.Make aquaculture pond and foster pond this two
In the state that person probiotics maintains always with most preferably efficiency is decomposed, that is, probiotics is held at " growth golden period " most
Good state.And the speed of growth/quantity of the two probiotics is controlled simultaneously, to allow foster pond probiotics to obtain fully growth
Afterwards, it then is added into aquaculture pond, and reaches the total amount of probiotics amount/objective speed for decomposing aquaculture pond shoal of fish excreta enough.Such as
This aquaculture pond just can be with minimal number of probiotics, to the excreta of most quantity in resolution process aquaculture pond.And it is cultivating
When probiotics in pond i.e. will be weak, you can by the return-to-zero method of the present invention, once again, and cultivated from foster pond
Go out new, strong probiotics to be added into aquaculture pond, with its excreta of resolution process.Therefore, the probiotics in aquaculture pond is all
It is to be chronically at " growth golden period ", there can be the best efficiency for decomposing excreta, so can be only achieved long-term free of replacement new
Cultivation water, and maintain most economical cultivation efficiency.
Specifically, how use above-mentioned table one, for example, with the time by the fish cultivated can only grow up and volume increase
Greatly, opposite that the quantity of excreta can be caused excessive, and destroy the balance of entire breeding ecological.But general cultivation dealer works as can
It is directly learnt by above-mentioned one revealed content of table, is such as intended to control total quantity/speed of aquaculture pond shoal of fish excreta processed, it must
The total quantity of the shoal of fish must be reduced and/or lower the daily feeding amount of the shoal of fish, could so be controlled in stable probiotics quantity/speed
Under, and the efficient total quantity for decomposing shoal of fish excreta of energy, so as to the balance of the permanent entire breeding ecological of maintenance.Furthermore
In response to (25 ~ 35 DEG C) variations of pH value (7.0 ~ 8.0) and water temperature under Various Seasonal (spring, summer, autumn, winter) environment, then it is aided with again
Each governing factor in table one is such as intended to control aquaculture pond probiotics processed and is maintained at " growth golden period " and its quantity/speed, then
After the feeding total amount that the aquaculture pond shoal of fish must be controlled, finally just with processing water frequency appropriate (weekly 1 ~ 3 time) and processing water
(a large amount of, middle amount or a small amount of), so as to can revealed " return-to-zero " technical characteristic through the invention, supported with reaching most perfect
Grow the ecological balance.
The foregoing is merely a present invention embodiments therein, when the patent protection model that cannot limit the present invention with this
Enclose, such as simple equivalence changes made by claims under this invention and description with replace, should all still fall within
In the range of the covered protection of claims of the present invention.
Claims (9)
1. a kind of return-to-zero method of cultivation water, which is characterized in that comprise the steps of：
Cultivation water in the aquaculture pond is guided into a processing pond；
An ozone is imposed for the cultivation water to handle, and processing is irradiated with a ultraviolet, and the ozone is in institute
It states under ultraviolet light irradiation, one is become so as to eliminating harmful bacterium and algae in the cultivation water using oxidation
Clear water；
The clear water after will be processed is guided into again to a foster pond, makes the clear water via drip filtration treatment, and
A beneficial strain and an algae are added in the clear water, using the algae as the bait of aquatic-organism feeding, in institute
It states foster pond and is built into a pelelith, so as to adjusting the pH value of the cultivation water, separately in adding a minerals in the foster pond,
To supplement the minerals in water, so as to a new cultivation water can be cleaned into；
By the new cultivation water, guiding is back in the aquaculture pond again again.
2. the return-to-zero method of cultivation water as described in claim 1, it is characterised in that：It is in wave that one is equipped in the processing pond
The forniciform water-supply-pipe of wave, the water-supply-pipe connect one first suction pump, are able to extract the place using first suction pump
The cultivation water in reason pond enters the water-supply-pipe, and the water-supply-pipe is connected with an ozone delivery pipe, the ozone conveying
An external ozone generators are managed, so that one ozone of conveying enters to the water-supply-pipe, are fused with the cultivation water.
3. the return-to-zero method of cultivation water as claimed in claim 2, it is characterised in that：The water-supply-pipe is close to described smelly
It is equipped with a control valve at the position of oxygen delivery pipe, so as to rotating the control valve, the cultivation is conveyed to control the water-supply-pipe
The flow velocity of water, and be controlled the ozone delivery pipe and convey concentration in the ozone to the water-supply-pipe, the ozone
Supply is to input 25 to 50 g per hour, and the concentration of the ozone in the cultivation water is made to maintain 5 to 10PPM.
4. the return-to-zero method of cultivation water as claimed in claim 2, it is characterised in that：The water outlet end of the water-supply-pipe connects
Be connected to few one or more the quartz burner, to generate the ultraviolet, so as to make with the ozone it is fused described in
Cultivation water can pass through the irradiation of the quartz burner.
5. the return-to-zero method of cultivation water as claimed in claim 4, it is characterised in that：The length of the quartz burner is
120 centimeters, wattage 55W, electricity consumption is then 1/3 horsepower.
6. the return-to-zero method of cultivation water as claimed in claim 4, it is characterised in that：Continue by first suction pump
Constantly extract the cultivation water in the processing pond, by the water-supply-pipe the ozone treatment and the quartz burner
Treatment with irradiation, then the cultivation water flow back into again in the processing pond, processing time be 5 to 12 hours.
7. the return-to-zero method of cultivation water as described in claim 1, it is characterised in that：It is provided at least in the foster pond
One or more Dropping filter, each Dropping filter are then arranged multiple layers of drip box, are arranged not in each drip box
With filter material, so as to impurity remaining in cultivation water described in layering, the Dropping filter by one second suction pump,
Continue for the cultivation water in the foster pond to carry out cycle extraction in 24 hours, keeps the cultivation water continual logical
The Dropping filter is crossed to be filtered.
8. the return-to-zero method of cultivation water as described in claim 1, it is characterised in that：The strain is that an aerobic is thin
Bacterium, including probiotics, Nitrosomas and nitrifier, the ratio of the strain allotment, with 100 g of strain, then coordinate 1 kilogram
Molasses, 20 liters of aqueous solution and 100 g of rice bran, after formulated dissolving, primary supported to described with pouring within every 12 hours
Pond, so as to turning out the aerobic bacteria in the clear water, to remove the ammonia in clear water, nitrite and nitrate.
9. the return-to-zero method of cultivation water as described in claim 1, it is characterised in that：The processing pond and the foster pond
Between connect a tank, can be respectively for the processing pond and institute using the tank so as to the clear water can be stored
State the adjusting that foster pond carries out water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710042437.5A CN108328848A (en) | 2017-01-20 | 2017-01-20 | The return-to-zero method of cultivation water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710042437.5A CN108328848A (en) | 2017-01-20 | 2017-01-20 | The return-to-zero method of cultivation water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108328848A true CN108328848A (en) | 2018-07-27 |
Family
ID=62922075
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710042437.5A Pending CN108328848A (en) | 2017-01-20 | 2017-01-20 | The return-to-zero method of cultivation water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108328848A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110272168A (en) * | 2019-07-23 | 2019-09-24 | 湖州弘鑫生态农业科技有限公司 | A kind of three-dimensional intelligent water treatment system |
| CN111204876A (en) * | 2020-01-20 | 2020-05-29 | 中国科学院南海海洋研究所 | Method for efficiently purifying and utilizing aquaculture tail water |
| CN113929246A (en) * | 2021-09-23 | 2022-01-14 | 上海握蓝物联科技(集团)有限公司 | Efficient disinfection equipment applied to drinking water |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1248398A (en) * | 1998-09-23 | 2000-03-29 | 王秉心 | Closed circulation cultivation system |
| CN101336621A (en) * | 2007-07-05 | 2009-01-07 | 飞寰实业有限公司 | Automatic circulating-water life-supporting and breeding system |
| CN201317710Y (en) * | 2008-12-23 | 2009-09-30 | 中国水产科学研究院珠江水产研究所 | Aquacultural water purifying and recycling system |
| CN102167455A (en) * | 2011-03-08 | 2011-08-31 | 北京科净源科技股份有限公司 | Water treatment technology building method of circulating water system |
| CN202218569U (en) * | 2011-07-20 | 2012-05-16 | 宁波大学 | Zero-emission circulatory water breeding system |
| CN103663871A (en) * | 2013-12-10 | 2014-03-26 | 苏州市相城区新时代特种水产养殖场 | Method used for processing and recycling of aquacultural waste water |
| CN205527914U (en) * | 2016-03-28 | 2016-08-31 | 贵州北极熊实业有限公司 | Feeder apparatus is thrown to no vapour soda water ozone |
-
2017
- 2017-01-20 CN CN201710042437.5A patent/CN108328848A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1248398A (en) * | 1998-09-23 | 2000-03-29 | 王秉心 | Closed circulation cultivation system |
| CN101336621A (en) * | 2007-07-05 | 2009-01-07 | 飞寰实业有限公司 | Automatic circulating-water life-supporting and breeding system |
| CN201317710Y (en) * | 2008-12-23 | 2009-09-30 | 中国水产科学研究院珠江水产研究所 | Aquacultural water purifying and recycling system |
| CN102167455A (en) * | 2011-03-08 | 2011-08-31 | 北京科净源科技股份有限公司 | Water treatment technology building method of circulating water system |
| CN202218569U (en) * | 2011-07-20 | 2012-05-16 | 宁波大学 | Zero-emission circulatory water breeding system |
| CN103663871A (en) * | 2013-12-10 | 2014-03-26 | 苏州市相城区新时代特种水产养殖场 | Method used for processing and recycling of aquacultural waste water |
| CN205527914U (en) * | 2016-03-28 | 2016-08-31 | 贵州北极熊实业有限公司 | Feeder apparatus is thrown to no vapour soda water ozone |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110272168A (en) * | 2019-07-23 | 2019-09-24 | 湖州弘鑫生态农业科技有限公司 | A kind of three-dimensional intelligent water treatment system |
| CN111204876A (en) * | 2020-01-20 | 2020-05-29 | 中国科学院南海海洋研究所 | Method for efficiently purifying and utilizing aquaculture tail water |
| CN113929246A (en) * | 2021-09-23 | 2022-01-14 | 上海握蓝物联科技(集团)有限公司 | Efficient disinfection equipment applied to drinking water |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107251830B (en) | Circulating aquaculture process and system | |
| CN104521832B (en) | Cultivation method for fish fries and adult fishes | |
| Sandifer et al. | Conceptual design of a sustainable pond-based shrimp culture system | |
| CN108439711A (en) | A kind of marine culture waste water integrated treatment purification system and method | |
| CN109548720B (en) | Compound prawn farming systems based on heterotopic biological flocculation is cultivated and normal position is nitrified | |
| CN211241202U (en) | Three-dimensional co-culture device for seawater-resistant vegetables and aquatic animals | |
| JP2017148007A (en) | Cultivation system of fish seedling | |
| CN108432685A (en) | The water environment of high load capacity aquaculture regulates and controls and circulating water culture system | |
| CN101305702A (en) | Industrial Tilapia seedling-raising method | |
| JP2000245297A (en) | Device for culturing fish or shellfish | |
| CN110122399B (en) | Simple circulating water culture system and method for large spiny loaches | |
| CN103999814B (en) | A kind of fish shellfish algae cyclic coexistence water treatment system | |
| Brune et al. | Partitioned aquaculture systems | |
| CN108328848A (en) | The return-to-zero method of cultivation water | |
| CN102415345A (en) | Method for cultivating macrobrachium rosenbergii offspring seed by using aquatic ozone culture system | |
| JP2013042678A (en) | Corbicula leana rearing kit | |
| CN113087199B (en) | Water quality control method for artificially breeding Changjiang river finless porpoise | |
| JP2020074761A (en) | Breeding water quality management system for circulation type on-land culture and operation method | |
| CN205455446U (en) | Fresh water wheel animalcule system that cultivates | |
| CN107473386A (en) | A kind of method of water plant functional group combined treatment fishing breeding pond sewage | |
| JP2539295B2 (en) | Circulation purification method and device for water for aquaculture | |
| CN105613433B (en) | Freshwater rotifer breeding method and system | |
| CN109315339A (en) | A kind of intermittent industrial circulating water cultivating method | |
| CN108633802A (en) | A kind of method of biological breeding Penaeus Vannmei parent shrimp | |
| TWI572566B (en) | Water treatment method for use in aquaculture system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20180727 |