CN204058043U - A kind of equipment producing high-solubility oxygen in water in cultured product - Google Patents
A kind of equipment producing high-solubility oxygen in water in cultured product Download PDFInfo
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- CN204058043U CN204058043U CN201420556136.6U CN201420556136U CN204058043U CN 204058043 U CN204058043 U CN 204058043U CN 201420556136 U CN201420556136 U CN 201420556136U CN 204058043 U CN204058043 U CN 204058043U
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- water
- nitrogen oxygen
- oxygen separator
- assembly
- separator
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 78
- 239000001301 oxygen Substances 0.000 title claims abstract description 49
- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 49
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims abstract description 44
- DOTMOQHOJINYBL-UHFFFAOYSA-N molecular nitrogen;molecular oxygen Chemical compound N#N.O=O DOTMOQHOJINYBL-UHFFFAOYSA-N 0.000 claims abstract description 99
- 230000003213 activating effect Effects 0.000 claims abstract description 26
- 239000007788 liquid Substances 0.000 claims abstract description 21
- 230000000630 rising effect Effects 0.000 claims description 6
- 238000009360 aquaculture Methods 0.000 abstract description 5
- 244000144974 aquaculture Species 0.000 abstract description 5
- 238000009395 breeding Methods 0.000 abstract description 3
- 230000001488 breeding effect Effects 0.000 abstract description 3
- 238000004064 recycling Methods 0.000 abstract description 3
- 239000012141 concentrate Substances 0.000 abstract description 2
- 230000009467 reduction Effects 0.000 abstract description 2
- 241000251468 Actinopterygii Species 0.000 description 8
- 239000003814 drug Substances 0.000 description 8
- 235000019688 fish Nutrition 0.000 description 8
- 238000000034 method Methods 0.000 description 8
- 241000277275 Oncorhynchus mykiss Species 0.000 description 7
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 7
- 241000252230 Ctenopharyngodon idella Species 0.000 description 6
- 229940079593 drug Drugs 0.000 description 6
- 239000012535 impurity Substances 0.000 description 6
- 238000012360 testing method Methods 0.000 description 6
- OAZWDJGLIYNYMU-UHFFFAOYSA-N Leucocrystal Violet Chemical compound C1=CC(N(C)C)=CC=C1C(C=1C=CC(=CC=1)N(C)C)C1=CC=C(N(C)C)C=C1 OAZWDJGLIYNYMU-UHFFFAOYSA-N 0.000 description 5
- 238000005336 cracking Methods 0.000 description 5
- FDZZZRQASAIRJF-UHFFFAOYSA-M malachite green Chemical compound [Cl-].C1=CC(N(C)C)=CC=C1C(C=1C=CC=CC=1)=C1C=CC(=[N+](C)C)C=C1 FDZZZRQASAIRJF-UHFFFAOYSA-M 0.000 description 5
- 229940107698 malachite green Drugs 0.000 description 5
- 229920006395 saturated elastomer Polymers 0.000 description 5
- 235000013372 meat Nutrition 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 230000001954 sterilising effect Effects 0.000 description 4
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 3
- 206010058490 Hyperoxia Diseases 0.000 description 3
- SDWOCAYOONANHF-UHFFFAOYSA-N [N+](=O)([O-])C=1N=C(OC1)O Chemical class [N+](=O)([O-])C=1N=C(OC1)O SDWOCAYOONANHF-UHFFFAOYSA-N 0.000 description 3
- 229910052785 arsenic Inorganic materials 0.000 description 3
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 description 3
- 229910052793 cadmium Inorganic materials 0.000 description 3
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 3
- WIIZWVCIJKGZOK-RKDXNWHRSA-N chloramphenicol Chemical compound ClC(Cl)C(=O)N[C@H](CO)[C@H](O)C1=CC=C([N+]([O-])=O)C=C1 WIIZWVCIJKGZOK-RKDXNWHRSA-N 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 231100001261 hazardous Toxicity 0.000 description 3
- 230000000222 hyperoxic effect Effects 0.000 description 3
- 230000006872 improvement Effects 0.000 description 3
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 3
- 229910052753 mercury Inorganic materials 0.000 description 3
- 229940049547 paraxin Drugs 0.000 description 3
- 238000001228 spectrum Methods 0.000 description 3
- 238000004659 sterilization and disinfection Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
- PLHJDBGFXBMTGZ-WEVVVXLNSA-N furazolidone Chemical class O1C([N+](=O)[O-])=CC=C1\C=N\N1C(=O)OCC1 PLHJDBGFXBMTGZ-WEVVVXLNSA-N 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000007689 inspection Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 241000881711 Acipenser sturio Species 0.000 description 1
- 241000972773 Aulopiformes Species 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- 241000252233 Cyprinus carpio Species 0.000 description 1
- 241000252234 Hypophthalmichthys nobilis Species 0.000 description 1
- 229910002651 NO3 Inorganic materials 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- IOVCWXUNBOPUCH-UHFFFAOYSA-M Nitrite anion Chemical compound [O-]N=O IOVCWXUNBOPUCH-UHFFFAOYSA-M 0.000 description 1
- 241000700605 Viruses Species 0.000 description 1
- 239000003905 agrochemical Substances 0.000 description 1
- 150000001413 amino acids Chemical class 0.000 description 1
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 210000000988 bone and bone Anatomy 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000003640 drug residue Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 239000003205 fragrance Substances 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 229940088597 hormone Drugs 0.000 description 1
- 239000005556 hormone Substances 0.000 description 1
- 230000004060 metabolic process Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 230000000050 nutritive effect Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 244000045947 parasite Species 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 235000019515 salmon Nutrition 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000010257 thawing Methods 0.000 description 1
- 210000001519 tissue Anatomy 0.000 description 1
- 235000021122 unsaturated fatty acids Nutrition 0.000 description 1
- 150000004670 unsaturated fatty acids Chemical class 0.000 description 1
Landscapes
- Farming Of Fish And Shellfish (AREA)
Abstract
The utility model relates to a kind of equipment producing high-solubility oxygen in water in cultured product, comprise casing, air compressing assembly, heat sink assembly, nitrogen oxygen separator assembly, high-voltage discharge tube, the last the first magnetic water-quality activating pipe, magnetic force resonance pump and gas-liquid separator, described air compressing assembly is arranged on the bottom of described casing, and be connected with described nitrogen oxygen separator assembly, described heat sink assembly is positioned at the top of described air compressing assembly, and be connected with described nitrogen oxygen separator assembly, described nitrogen oxygen separator assembly is connected with described high-voltage discharge tube, described high-voltage discharge tube is connected with described magnetic force resonance pump, described magnetic force resonance pump is connected with the bottom of described gas-liquid separator by described the last the first magnetic water-quality activating pipe.The utility model can carry out all kinds of fishery products of high-density breeding, has reduction aquaculture cost, concentrates stdn cultivation, recycling water resources and saving water resource, saves the advantages such as labor force.
Description
Technical field
The utility model relates to a kind of equipment producing high-solubility oxygen in water in cultured product.
Background technology
In aquaculture, due to O
2and O
3be insoluble in water and can not be saturated for a long time in water, cause O in water
2and O
3comparision contents few, thus the quality of cultured product in water can be affected.
Utility model content
Technical problem to be solved in the utility model is to provide a kind of equipment producing high-solubility oxygen in water in cultured product, this equipment passes through large water molecule cluster very strong for polarity in stagnation point cracking, and dissolve in a large amount of oxygen molecules with negative charge, due to the feature of identical charges, its head and the tail can not be connected, thus ensure that oxygen molecule can be saturated in small water molecule group for a long time, thus reach the object of high-solubility oxygen in water.
The technical scheme that the utility model solves the problems of the technologies described above is as follows: a kind of equipment producing high-solubility oxygen in water in cultured product, comprise casing, air compressing assembly, heat sink assembly, nitrogen oxygen separator assembly, high-voltage discharge tube, the last the first magnetic water-quality activating pipe, magnetic force resonance pump and gas-liquid separator, described air compressing assembly, heat sink assembly, nitrogen oxygen separator assembly, high-voltage discharge tube, the last the first magnetic water-quality activating pipe, magnetic force resonance pump and gas-liquid separator are all positioned at described casing, described air compressing assembly is arranged on the bottom of described casing, and be connected with described nitrogen oxygen separator assembly, described heat sink assembly is positioned at the top of described air compressing assembly, and be connected with described nitrogen oxygen separator assembly, described nitrogen oxygen separator assembly is connected with described high-voltage discharge tube, described high-voltage discharge tube is connected with described magnetic force resonance pump, described magnetic force resonance pump is connected with the bottom of described gas-liquid separator by described the last the first magnetic water-quality activating pipe.
The beneficial effects of the utility model are:
The utility model passes through large water molecule cluster very strong for polarity in stagnation point cracking, and dissolve in a large amount of oxygen molecules with negative charge, due to the feature of identical charges, its head and the tail can not be connected, thus ensure that oxygen molecule can be saturated in small water molecule group for a long time, thus reach the object of high-solubility oxygen in water.
By the utility model for generation of the dissolved oxygen of the water after the device processes of high-dissolved-oxygen water up to more than 35ppm/ premium on currency, to water quality instantaneous sterilization sterilizing, and the objectionable impurities in degradable water, under standard pressure, static state is saturated is more than 60 days, embezzle Deng pressure vessel and reach more than 180 days, all kinds of fishery products of high-density breeding can be carried out, there is reduction aquaculture cost, concentrate stdn cultivation, recycling water resources and saving water resource, save the advantages such as labor force, the water after this device processes is used to carry out cultivating can improve output 10 ~ 13 times compared with common cultural method.
On the basis of technique scheme, the utility model can also do following improvement.
Further, described nitrogen oxygen separator assembly comprises the first nitrogen oxygen separator, the second nitrogen oxygen separator, the 3rd nitrogen oxygen separator and the 4th nitrogen oxygen separator, described first nitrogen oxygen separator, the second nitrogen oxygen separator, the 3rd nitrogen oxygen separator and the 4th nitrogen oxygen separator are disposed side by side in described casing, and are all connected with described high-voltage discharge tube.
Further, described air compressing assembly comprises the first air compressor and the second air compressor, described first air compressor is connected with the second nitrogen oxygen separator with described first nitrogen oxygen separator respectively, and described second air compressor is connected with the 4th nitrogen oxygen separator with described 3rd nitrogen oxygen separator respectively.
Further, described heat sink assembly comprises the first scatterer and the second scatterer, described first scatterer is between described first nitrogen oxygen separator and the second nitrogen oxygen separator, and be connected with the second nitrogen oxygen separator with described first nitrogen oxygen separator respectively, described second scatterer between described 3rd nitrogen oxygen separator and the 4th nitrogen oxygen separator, and is connected with the 4th nitrogen oxygen separator with described 3rd nitrogen oxygen separator respectively.
Further, described gas-liquid separator comprises housing, circular course division board and vent valve, described housing inner top is provided with a solarization air cell, described circular course division board is arranged in described solarization air cell, described vent valve is arranged on the top of described housing, and described the last the first magnetic water-quality activating pipe is connected with described solarization air cell.
Further, described casing is provided with rising pipe, and described water outlet is connected with described solarization air cell.
Further, the described equipment producing high-solubility oxygen in water in cultured product also comprises water inlet pipe and the last the second magnetic water-quality activating pipe, one end of described the last the second magnetic water-quality activating pipe is connected with described water inlet pipe, and the other end is connected with described magnetic force resonance pump through described casing.
Further, the sidewall of described casing is provided with Controlling System, and described Controlling System is electrically connected with described air compressing assembly, heat sink assembly, nitrogen oxygen separator assembly, high-voltage discharge tube, the last the first magnetic water-quality activating pipe, magnetic force resonance pump and gas-liquid separator respectively.
Further, described Controlling System is provided with panel board, start button and pilot lamp.
Further, the sidewall of described casing is also provided with electric switch dish, described electric switch dish is positioned at the bottom of described Controlling System; The bottom of described casing is provided with universal wheel.
Accompanying drawing explanation
Fig. 1 is the utility model produces the equipment of high-solubility oxygen in water structural representation in cultured product;
Fig. 2 is the rear view of Fig. 1;
Fig. 3 is the right view of Fig. 1
In accompanying drawing, the list of parts representated by each label is as follows:
1, casing, 2, first air compressor, 3, second air compressor, 4, first nitrogen oxygen separator, 5, second nitrogen oxygen separator, 6, 3rd nitrogen oxygen separator, 7, 4th nitrogen oxygen separator, 8, first scatterer, 9, second scatterer, 10, high-voltage discharge tube, 11, the last the first magnetic water-quality activating pipe, 12, magnetic force resonance pump, 13, gas-liquid separator, 13-1, housing, 13-2, circular course division board, 13-3, vent valve, 13-4, solarization air cell, 14, rising pipe, 15, water inlet pipe, 16, the last the second magnetic water-quality activating pipe, 17, panel board, 18, start button, 19, pilot lamp, 20, electric switch dish, 21, universal wheel.
Embodiment
Be described principle of the present utility model and feature below in conjunction with accompanying drawing, example, only for explaining the utility model, is not intended to limit scope of the present utility model.
In water, in cultured product, produce an equipment for high-solubility oxygen, as shown in Figure 1 to Figure 3, comprise casing 1, air compressing assembly, heat sink assembly, nitrogen oxygen separator assembly, high-voltage discharge tube 10, the last the first magnetic water-quality activating pipe 11, magnetic force resonance pump 12 and gas-liquid separator 13, described air compressing assembly, heat sink assembly, nitrogen oxygen separator assembly, high-voltage discharge tube 10, the last the first magnetic water-quality activating pipe 11, magnetic force resonance pump 12 and gas-liquid separator 13 are all positioned at described casing 1, described air compressing assembly is arranged on the bottom of described casing 1, and be connected with described nitrogen oxygen separator assembly, described heat sink assembly is positioned at the top of described air compressing assembly, and be connected with described nitrogen oxygen separator assembly, described nitrogen oxygen separator assembly is connected with described high-voltage discharge tube 10, described high-voltage discharge tube 10 is connected with described magnetic force resonance pump 12, and described magnetic force resonance pump 12 is connected with the bottom of described gas-liquid separator 13 by described the last the first magnetic water-quality activating pipe 11.
Described nitrogen oxygen separator assembly comprises the first nitrogen oxygen separator 4, second nitrogen oxygen separator 5, the 3rd nitrogen oxygen separator 6 and the 4th nitrogen oxygen separator 7, described first nitrogen oxygen separator 4, second nitrogen oxygen separator 5, the 3rd nitrogen oxygen separator 6 and the 4th nitrogen oxygen separator 7 are disposed side by side in described casing 1, and are all connected with described high-voltage discharge tube 10.
Described air compressing assembly comprises the first air compressor 2 and the second air compressor 3, described first air compressor 2 is connected with the second nitrogen oxygen separator 5 with described first nitrogen oxygen separator 4 respectively, and described second air compressor 3 is connected with the 4th nitrogen oxygen separator 7 with described 3rd nitrogen oxygen separator 6 respectively.
Described heat sink assembly comprises the first scatterer 8 and the second scatterer 9, described first scatterer 8 is between described first nitrogen oxygen separator 4 and the second nitrogen oxygen separator 5, and be connected with the second nitrogen oxygen separator 5 with described first nitrogen oxygen separator 4 respectively, described second scatterer 9 between described 3rd nitrogen oxygen separator 6 and the 4th nitrogen oxygen separator 7, and is connected with the 4th nitrogen oxygen separator 7 with described 3rd nitrogen oxygen separator 6 respectively.
Described gas-liquid separator 13 comprises housing 13-1, circular course division board 13-2 and vent valve 13-3, a solarization air cell 13-4 is provided with in described housing, described circular course division board 13-2 is arranged in described solarization air cell 13-4 side by side, described vent valve 13-3 is arranged on the top of described housing 13-1, and described the last the first magnetic water-quality activating pipe 11 is connected with described solarization air cell 13-4.
Described casing 1 is provided with rising pipe 14, and described rising pipe 14 is connected with described solarization air cell 13-4.
The described equipment producing high-solubility oxygen in water in cultured product also comprises water inlet pipe 15 and the last the second magnetic water-quality activating pipe 16, one end of described the last the second magnetic water-quality activating pipe 16 is connected with described water inlet pipe 15, and the other end is connected with described magnetic force resonance pump 12 through described casing 1.
The sidewall of described casing 1 is provided with Controlling System, and described Controlling System is electrically connected with described air compressing assembly, heat sink assembly, nitrogen oxygen separator assembly, high-voltage discharge tube 10, magnetic force resonance pump 12 and gas-liquid separator 13 respectively.Described Controlling System is provided with panel board 17, start button 18 and pilot lamp 19.
The sidewall of described casing 1 is also provided with electric switch dish 20, and described electric switch dish 20 is positioned at the bottom of described Controlling System.
The bottom of described casing 1 is provided with universal wheel 21.
The utility model passes through large water molecule cluster very strong for polarity in stagnation point cracking for generation of the equipment of high-dissolved-oxygen water, and dissolve in a large amount of oxygen molecules with negative charge, due to the feature of identical charges, its head and the tail can not be connected, thus ensure that oxygen molecule can be saturated in small water molecule group for a long time, thus reach the object of high-solubility oxygen in water.
Operationally, air becomes pure air after filtering and impurity removing, pure air enters nitrogen oxygen separator assembly (i.e. the first nitrogen oxygen separator 4 by air compressing assembly (i.e. the first air compressor 2 and the second air compressor 3), second nitrogen oxygen separator 5, 3rd nitrogen oxygen separator 6 and the 4th nitrogen oxygen separator 7) carry out nitrogen oxygen separating, wherein, first air compressor 4 and the second air compressor 5 alternation, the timed interval is alternately 15 seconds ~ 20 seconds, described first nitrogen oxygen separator 4 and the second nitrogen oxygen separator 5, 3rd nitrogen oxygen separator 6 and the 4th nitrogen oxygen separator 7 alternation cyclic regeneration produce O
2, the timed interval replaced is 25 seconds ~ 35 seconds, then by pure O
2deliver to high-voltage discharge tube 10 and produce ozone O
3, then, by the ozone O produced
3deliver to magnetic force resonance pump 12, the water molecules in the water entered by water inlet pipe 15, in the last the second magnetic water-quality activating pipe 16, by carry out cracking under the effect of ultrastrong magnetic field and high-pressure rotary and with ozone O
3abundant stirring.When high-voltage discharge tube 10 does not work, pure O
2directly deliver to magnetic force resonance pump 12, the water molecules in the water entered by water inlet pipe 15 under the effect of ultrastrong magnetic field and high-pressure rotary, carry out cracking and with pure O
2abundant stirring, through the abundant mixed water of gas-liquid and ozone O
3mixture or water and pure O
2mixture deliver to gas-liquid separator 13 again and be atomized, unnecessary gas delivery is discharged gas-liquid separation, 13, and the water oxygen mixed solution forming high density after discharging excessive gas discharges the place delivered to for carrying out aquaculture again by rising pipe 14.Described Controlling System, for controlling the working hour of high-voltage discharge tube, namely controls the time of origin of ozone, and arrange the time of ozone generation according to the difference of water quality, with a minute timing, common water quality is generally 20 seconds (O
3) 40 seconds (O
2), water quality is poorer, and the time that ozone is arranged is longer.
The utility model is mainly used in all kinds of aquaculture for generation of the equipment of high-dissolved-oxygen water, by ultrastrong magnetic field and resonance recycling technology, merge with active oxygen under special physical action, and the water molecules of granule state is broken up the micromolecular water become close to monomer, thus the dissolved oxygen factor is produced, in micromolecular water, dissolve in a large amount of active oxygens, thus improve the breeding density of fishery products; This equipment can also circulate efficient quick sterilization, sterilization, by water-quality activating, make fishpond self-assembling formation eucyclic Iarge-scale system of microorganism, and by objectionable impurities as the rapid oxidation such as ammonia nitrogen, nitrate, nitrite, hormone, agricultural chemicals, fish medicine become innoxious substance, and fish body can be penetrated, kill the virus in fish body, bacterium, parasite etc., the objectionable impurities in degraded body.Under this high oxygen condition, the rapid growing of fish, generates in body the very useful amino acid of human body and unsaturated fatty acids, is formed solid to have elastic fleshy fiber.Bone is solid, has powerful vigor.Adult fish taste is splendid.Without appointing and peculiar smell time edible, fragrance is pure strong.During section, meat is snow-white, sparkling and crystal-clear moist, appearance and good.Meat can freeze preservation, steamed after thawing, meat meat flavour and to be fresh and alively as good as.
Dissolved oxygen amount in the utility model water after treatment depends on the size of the hydraulic pressure that equipment water-in enters and the number of times at equipment internal recycle.
The utility model is for generation of the equipment main economic and technical indices of high-dissolved-oxygen water: equipment is per hour produces active water 8 cubic metres, oxygen 6 cubic metres can be produced, peak power 3000W per hour, oxygen in water is as the criterion with the portable oxygen measuring instrument of the U.S., and saturation exponent detects institute's detected result with China spectrum Buddhist nun and is as the criterion.
Embodiment 1
The hydraulic pressure of water-in is 0.3Ma, adopts the dissolved oxygen in water of the portable oxygen measuring instrument test of imported from America after a circular treatment of equipment to be 35ppm/ premium on currency.
Canned under standard pressure (common PVC Plastic Bottle) one week build-in test percentage of oxygen saturation (spectrum Buddhist nun detects institute's electronics dissolved oxygen and detects data, and report number is T11171021605D) is 26.6ppm/ premium on currency.
Embodiment 2
The hydraulic pressure of water-in is 0.4Ma, adopts the dissolved oxygen in water of the portable oxygen measuring instrument test of imported from America after the secondary circulation process of equipment to be 48ppm/ premium on currency.
Canned under standard pressure (common PVC Plastic Bottle) one week build-in test percentage of oxygen saturation (spectrum Buddhist nun detects institute's electronics dissolved oxygen and detects data, and report number is T11301002305D) is 34.8ppm/ premium on currency.
Contaminated fishery products are put into and are concentrated purification through the hyperoxia of 7 ~ 10 days through the utility model again for generation of the water after the device processes of high-dissolved-oxygen water, can reach and the natural quality be as good as, the every objectionable impurities of fishery products after purification remains index and is dispelled completely after testing, and indices all meets GB standard.By the fish of medicine and heavy metal contamination, as: hazardous drugs such as malachite green, leucogentian violet, nitro oxazolone metabolite, sulfa drugs, paraxin, lead, cadmium, mercury, arsenic are degraded, to get rid of fish external in metabolism, make fish body become one aseptic, without the hyalosome cell tissue of any objectionable impurities, and improve its nutritive value.
Since 09 year, with this equipment to freshwater product as (fingerling such as rainbow trout, sturgeon, salmon, grass carp, silver carp, carp has carried out small-scale cultivation and cleaning test, and rainbow trout and grass carp are inspected by random samples in batches, detected result meets fishery products drug residue limit standard completely, contrast with common cultivation side and have very large improvement, the time using in embodiment 2 water cultivation rainbow trout after treatment and grass carp is below 10 days, and the rainbow trout of cultivation and the weight of grass carp are 4 jin.
(state food Inspection Research institute in examining report is cultivated by " rainbow trout " usual way, report number S081227) can see, in rainbow trout body, the content of malachite green is 0.85 μ g/kg, the content of leucogentian violet is 52 μ g/kg, and the content of Furaxone metabolite is 27.20.8 μ g/kg.
But can see by cultivating (state food Inspection Research institute, report number S081226) in examining report to " rainbow trout " hyperoxia cultural method, all not detect containing malachite green, leucogentian violet and Furaxone metabolite.
By cultivating examining report to grass carp usual way, (China passes in and out Quarantine Bureau, report number 211000000144) can see, the hazardous drugs such as malachite green, leucogentian violet, nitro oxazolone metabolite, sulfa drugs, paraxin, lead, cadmium, mercury, arsenic do not reach relative national standards.
But by cultivating examining report to grass carp hyperoxia cultural method, (China passes in and out Quarantine Bureau, report number 211000000145) can see that the hazardous drugs such as malachite green, leucogentian violet, nitro oxazolone metabolite, sulfa drugs, paraxin, lead, cadmium, mercury, arsenic not only reach relative national standards, and also content is all very low.
The foregoing is only preferred embodiment of the present utility model, not in order to limit the utility model, all within spirit of the present utility model and principle, any amendment done, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
Claims (10)
1. one kind produces the equipment of high-solubility oxygen in water in cultured product, it is characterized in that: comprise casing, air compressing assembly, heat sink assembly, nitrogen oxygen separator assembly, high-voltage discharge tube, the last the first magnetic water-quality activating pipe, magnetic force resonance pump and gas-liquid separator, described air compressing assembly, heat sink assembly, nitrogen oxygen separator assembly, high-voltage discharge tube, the last the first magnetic water-quality activating pipe, magnetic force resonance pump and gas-liquid separator are all positioned at described casing, described air compressing assembly is arranged on the bottom of described casing, and be connected with described nitrogen oxygen separator assembly, described heat sink assembly is positioned at the top of described air compressing assembly, and be connected with described nitrogen oxygen separator assembly, described nitrogen oxygen separator assembly is connected with described high-voltage discharge tube, described high-voltage discharge tube is connected with described magnetic force resonance pump, described magnetic force resonance pump is connected with the bottom of described gas-liquid separator by described the last the first magnetic water-quality activating pipe.
2. the equipment producing high-solubility oxygen in water in cultured product according to claim 1, it is characterized in that: described nitrogen oxygen separator assembly comprises the first nitrogen oxygen separator, the second nitrogen oxygen separator, the 3rd nitrogen oxygen separator and the 4th nitrogen oxygen separator, described first nitrogen oxygen separator, the second nitrogen oxygen separator, the 3rd nitrogen oxygen separator and the 4th nitrogen oxygen separator are disposed side by side in described casing, and are all connected with described high-voltage discharge tube.
3. the equipment producing high-solubility oxygen in water in cultured product according to claim 2, it is characterized in that: described air compressing assembly comprises the first air compressor and the second air compressor, described first air compressor is connected with the second nitrogen oxygen separator with described first nitrogen oxygen separator respectively, and described second air compressor is connected with the 4th nitrogen oxygen separator with described 3rd nitrogen oxygen separator respectively.
4. the equipment producing high-solubility oxygen in water in cultured product according to claim 2, it is characterized in that: described heat sink assembly comprises the first scatterer and the second scatterer, described first scatterer is between described first nitrogen oxygen separator and the second nitrogen oxygen separator, and be connected with the second nitrogen oxygen separator with described first nitrogen oxygen separator respectively, described second scatterer between described 3rd nitrogen oxygen separator and the 4th nitrogen oxygen separator, and is connected with the 4th nitrogen oxygen separator with described 3rd nitrogen oxygen separator respectively.
5. the equipment producing high-solubility oxygen in water in cultured product according to any one of Claims 1-4, it is characterized in that: described gas-liquid separator comprises housing, circular course division board and vent valve, described housing inner top is provided with a solarization air cell, described circular course division board is arranged in described solarization air cell, described vent valve is arranged on the top of described housing, and described the last the first magnetic water-quality activating pipe is connected with described solarization air cell.
6. the equipment producing high-solubility oxygen in water in cultured product according to claim 5, it is characterized in that: described casing is provided with rising pipe, described water outlet is connected with described solarization air cell.
7. the equipment producing high-solubility oxygen in water in cultured product according to any one of Claims 1-4, it is characterized in that: the described equipment producing high-solubility oxygen in water in cultured product also comprises water inlet pipe and the last the second magnetic water-quality activating pipe, one end of described the last the second magnetic water-quality activating pipe is connected with described water inlet pipe, and the other end is connected with described magnetic force resonance pump through described casing.
8. the equipment producing high-solubility oxygen in water in cultured product according to any one of Claims 1-4, it is characterized in that: the sidewall of described casing is provided with Controlling System, described Controlling System is electrically connected with described air compressing assembly, heat sink assembly, nitrogen oxygen separator assembly, high-voltage discharge tube, the last the first magnetic water-quality activating pipe, magnetic force resonance pump and gas-liquid separator respectively.
9. the equipment producing high-solubility oxygen in water in cultured product according to claim 8, is characterized in that: described Controlling System is provided with panel board, start button and pilot lamp.
10. the equipment producing high-solubility oxygen in water in cultured product according to claim 8, it is characterized in that: the sidewall of described casing is also provided with electric switch dish, described electric switch dish is positioned at the bottom of described Controlling System; The bottom of described casing is provided with universal wheel.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420556136.6U CN204058043U (en) | 2014-09-25 | 2014-09-25 | A kind of equipment producing high-solubility oxygen in water in cultured product |
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|---|---|---|---|
| CN201420556136.6U CN204058043U (en) | 2014-09-25 | 2014-09-25 | A kind of equipment producing high-solubility oxygen in water in cultured product |
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| CN204058043U true CN204058043U (en) | 2014-12-31 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112028260A (en) * | 2020-09-01 | 2020-12-04 | 谢海亭 | Ecological balance system of inner loop river |
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2014
- 2014-09-25 CN CN201420556136.6U patent/CN204058043U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112028260A (en) * | 2020-09-01 | 2020-12-04 | 谢海亭 | Ecological balance system of inner loop river |
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