CN1647623A - High oxygen resolving aerator - Google Patents

High oxygen resolving aerator Download PDF

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Publication number
CN1647623A
CN1647623A CN 200510056752 CN200510056752A CN1647623A CN 1647623 A CN1647623 A CN 1647623A CN 200510056752 CN200510056752 CN 200510056752 CN 200510056752 A CN200510056752 A CN 200510056752A CN 1647623 A CN1647623 A CN 1647623A
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CN
China
Prior art keywords
water
oxygen
oxygen release
aerator
high oxygen
Prior art date
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Pending
Application number
CN 200510056752
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Chinese (zh)
Inventor
靳巨军
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Individual
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Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN 200510056752 priority Critical patent/CN1647623A/en
Publication of CN1647623A publication Critical patent/CN1647623A/en
Priority to CN 200520118505 priority patent/CN2800754Y/en
Priority to CNA2005100979982A priority patent/CN1762859A/en
Priority to PCT/CN2005/001396 priority patent/WO2006099780A1/en
Pending legal-status Critical Current

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    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01KANIMAL HUSBANDRY; AVICULTURE; APICULTURE; PISCICULTURE; FISHING; REARING OR BREEDING ANIMALS, NOT OTHERWISE PROVIDED FOR; NEW BREEDS OF ANIMALS
    • A01K63/00Receptacles for live fish, e.g. aquaria; Terraria
    • A01K63/04Arrangements for treating water specially adapted to receptacles for live fish
    • A01K63/042Introducing gases into the water, e.g. aerators, air pumps
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/727Treatment of water, waste water, or sewage by oxidation using pure oxygen or oxygen rich gas
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/74Treatment of water, waste water, or sewage by oxidation with air
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/78Treatment of water, waste water, or sewage by oxidation with ozone

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  • Life Sciences & Earth Sciences (AREA)
  • Environmental Sciences (AREA)
  • Marine Sciences & Fisheries (AREA)
  • Animal Husbandry (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)

Abstract

The high oxygen resolving aerator includes main body as one water passing cavity with water inlet and water outlet; oxygen releaser set inside the water outlet of the water passing cavity, connected via pipe with oxygen source; and water conveyer set in the water inlet of the water passing cavity to output pressurized water flow. The oxygen releaser is made of micron level oxygen releasing material and the oxygen releasing material is air permeating and water permeating core of ceramic or airstone. The high oxygen resolving aerator may be set in any depth inside water, and during operation, the water conveyer with submerged pump pumps in water flow, and the water flow after passing through water passing cavity exchanges with the oxygen releaser. The present invention is suitable for use in aquatic cultivation, aquarium, live fish transportation, etc.

Description

A kind of high oxygen dissolution aerator
Technical field
The invention belongs to aquatic group breed, transporting equipment, be specifically related to dissolved oxygen, oxygenation device that a kind of aquatic group is cultured, transported.
Background technology
In the known technology, dissolved oxygen in aquatic group breed, the transporting equipment, the most employing at the water layer interface of oxygenation device spray or dark, shoaling layer convection current stirring, need power bigger, and streaming potential forms than thump Shui nationality fish, Shui nationality fish were impacted and injured, also consume the physical efficiency of Shui nationality fish, have a strong impact on the survival rate of Shui nationality fish.The source of the gas that uses mostly is the extensive style single-point and injects, and the little dissolved oxygen water that then makes of bleed pressure is limited to the local finite waters, and bleed pressure greatly then makes the valuable source of the gas effusion water surface, the waste source of the gas.ZL90203950.4 Chinese patent disclosed a kind of " multi-functional live fish transport case " technical scheme, though the problems referred to above have been done necessarily to overcome, its structure is very complicated, and it adopts nature spray substantially, extensively advances oxygen, mixes oxygen, and the dissolved oxygen effect is extremely limited.And its mixed gas filling core material easily stops up by dirt, influences the oxygen release effect.ZL92200294.0 Chinese patent disclosed a kind of " live fish storage and transportation apparatus " technical scheme, it adopts venturi type oxygenation hybrid nozzle, forces to mix oxygen, though certain effect is arranged, it still belongs to liquid, the direct extensive mixing of gas, the dissolved oxygen effect is limited.In addition, along with the development of up-to-date Shui nationality plantation technology, the variation of very big understanding and practice takes place in people at the suitable molecular oxygen content of sea, fresh water to aquatic group.Measure according to comparative trial, fresh water Cyprinidae class and seawater Bothidae class are when water oxygen level is 2.5~4 mg/litre, and respiratory rate is 60~120 a times/per minute, and when water oxygen level reached 25 mg/litre, respiratory rate was 10~15 a times/per minute.Can reduce the autophage of aquatic group being this moment greatly, significantly reduces excreta, correspondingly reduces the pollution to water quality.On the other hand, under the environment of high oxygen enrichment, the algae in the water multiplied play stronger inhibitory action, and can directly kill harmful anaerobic bacteria in the water.Above-mentioned two class technical schemes, its dissolved oxygen effect can reach 10 mg/litre at most, can not adapt to the needs of modern farming far away.The ZL02269987.2 " a kind of high oxygen dissolution aerator " of applicant's power of formerly patenting have stronger dissolved oxygen effect, but heavy-oxygen-enriched water adheres to the aspect that is trapped in the oxygen release body easily, is difficult for and hypoxemia water convective exchange.
Summary of the invention
The objective of the invention is provides a kind of simple in structure for solving the technical problem of liquid, gas dissolved oxygen weak effect in the known technology, and self-cleaning is good, and the dissolved oxygen effect is remarkable, and gas-liquid dissolves the high oxygen dissolution aerator of transformation efficiency mutually.
The present invention takes following technical scheme.
High oxygen dissolution aerator, include the oxygen release device, the high oxygen dissolution aerator body is the water flowing cavity, the water flowing cavity is provided with water inlet, delivery port, delivery port one side is provided with the oxygen release device in the water flowing cavity, oxygen release device and source of the gas link, and water inlet one side is provided with the water delivery device of exportable pressure flow in the water flowing cavity.The oxygen release device is installed ceramic core oxygen release piece or oxygen release materials such as airstone core, tracheae core is installed.Ceramic core oxygen release piece, airstone core, tracheae core oxygen release material are permeation, seepage material, and its material structure is a micron dimension, and its grainiess is 0.01~10 micron (μ m).The oxygen release device can be set to link with source of the gas in groups in the serial or parallel connection mode more than several.Source of the gas can be oxygen, ozone source or atmosphere.The water delivery device of pressure flow is the axial-flow type immersible pump, circulates in the bottom waters bottom water being forced.The water delivery device of pressure flow also can be external penstocks, makes the convection circulation of levels current.The spacing of top layer is the 5-30 millimeter in oxygen release device outgas aspect and the water flowing cavity.
The present invention has tangible technique effect compared to existing technology.
The oxygen release material that the oxygen release device is installed all is contained in water flowing cavity inner chamber, itself and the interior top layer of water flowing cavity are provided with a determining deviation, make the water delivery device current of axial-flow type immersible pump output for example of output pressure current, the oxygen enrichment atomized water exchange fusion that the oxygen release material is discharged on the one hand, reach dissolved oxygen effect preferably, can with up to 98% gas atomization in water.It is suitable to dispose, and can make the molecular oxygen content of heavy-oxygen-enriched water can reach 5~40 mg/litre.Current can wash away the oxygen release material surface on the other hand, make its surface that keeps clean, and prevent that dirt from stopping up and algae multiplies, and influence oxygen and discharge.The sample practical probation, the Shui nationality time-to-live prolongs greatly, even reaches 3 years.Get volume size according to on-the-spot fish pond, fishpond or fish transportation vehicle, can design the many assembly covers of the many groups of a device or many devices and use, little of viewing and admiring fish jar, all can adjust use to the fish farm of the square meter waters surface up to ten thousand greatly.
Description of drawings
Accompanying drawing 1 is the high oxygen dissolution aerator vertical view.
Accompanying drawing 2 is the high oxygen dissolution aerator front view.
Accompanying drawing 3 is a high oxygen dissolution aerator B-B view.
Accompanying drawing 4 is a high oxygen dissolution aerator D portion zoomed-in view.
Accompanying drawing 5 is high oxygen dissolution aerator user mode figure.
Among the figure, 1-delivery port, 2-oxygen release device, 3-tracheae, 4-oxygen release material, 5-water flowing chamber water stream channel, 6-water flowing cavity, 7-force decreasing plate, 8-water delivery device, 9-water inlet, d-oxygen release laminar flow water spacing.
Embodiment
It below is the specific embodiment of invention.Embodiment is used for illustrating of the present invention, rather than the present invention is imposed any restrictions.
High oxygen dissolution aerator includes oxygen release device (2), the high oxygen dissolution aerator body is water flowing cavity (6), water flowing cavity (6) is provided with water inlet (9), delivery port (1), delivery port (1) one side is provided with oxygen release device (2) in water flowing cavity (6), oxygen release device (2) links through tracheae (3) and source of the gas, and water inlet (9) one sides are provided with the water delivery device (8) of exportable pressure flow in water flowing cavity (6).Oxygen release device (2) is installed oxygen release material (4).Oxygen release material (4) ceramic core or airstone core or tracheae core are permeation, infiltration material, and its material structure is a micron dimension, and its grainiess is 0.1~10 micron (μ m).The oxygen release device (2) that is arranged on interior delivery port (1) one side of water flowing cavity (6) is set to link through tracheae (3) and source of the gas in groups in the serial or parallel connection mode more than several according to handling the big I in waters.Oxygen release device (2) links through tracheae (3) and oxygen or sources of the gas such as ozone source or atmosphere.The water delivery device of pressure flow (8) is the axial-flow type immersible pump.Also can external penstocks to the water flowing chamber of water flowing cavity (6) water stream channel (5) water delivery.The spacing d ≈ 5-30 millimeter of oxygen release device (2) outgas aspect and the interior top layer of water flowing cavity (6).Between water delivery device (8) and oxygen release device (2), force decreasing plate (7) is installed, is slowed down the certain potential energy of current.Water inlet (9) as the water periphery grid mouth is set, stop that foreign matter enters the water flowing cavity.
High oxygen dissolution aerator can be placed on any aspect in the water, water delivery device during work (8) axial-flow type immersible pump pumps into current through water inlet (9), current, current feed water flowing chamber water stream channel (5) through force decreasing plate (7), and dissolved oxygen is finished exchange after delivery port (1) is discharged cavity in the spacing of top layer 5-30 millimeter in oxygen release device (2) outgas aspect and water flowing cavity (6).

Claims (9)

1, a kind of high oxygen dissolution aerator, include oxygen release device (2), it is characterized in that, the high oxygen dissolution aerator body is water flowing cavity (6), water flowing cavity (6) is provided with water inlet (9), delivery port (1), delivery port (1) one side is provided with oxygen release device (2) in water flowing cavity (6), and oxygen release device (2) links through tracheae (3) and source of the gas, and water inlet (9) one sides are provided with the water delivery device (8) of exportable pressure flow in water flowing cavity (6).
2, high oxygen dissolution aerator according to claim 1 is characterized in that, oxygen release device (2) is installed oxygen release material (4).
3, high oxygen dissolution aerator according to claim 1 is characterized in that, the oxygen release material of installing in the oxygen release device (2) (4) is ceramic core or airstone core or tracheae core matter.
4, according to claim 2 or 3 described high oxygen dissolution aerators, it is characterized in that, ceramic core oxygen release piece that oxygen release device (2) is installed or airstone core or tracheae core oxygen release material (4) are permeation, seepage material, and its material structure is a micron dimension, and its grainiess is 0.1~10 micron (μ m).
5, high oxygen dissolution aerator according to claim 1 is characterized in that, the oxygen release device (2) that is arranged on interior delivery port (1) one side of water flowing cavity (6) can be set to link through tracheae (3) and source of the gas in groups with string or parallel way more than two.
6, high oxygen dissolution aerator according to claim 1 is characterized in that, oxygen release device (2) links through tracheae (3) and oxygen or sources of the gas such as ozone source or atmosphere.
7, high oxygen dissolution aerator according to claim 1 is characterized in that, the water delivery device of pressure flow (8) is the axial-flow type immersible pump.
8, high oxygen dissolution aerator according to claim 7 is characterized in that, the water delivery device of pressure flow (8) is external penstocks.
9, high oxygen dissolution aerator according to claim 1 is characterized in that, the spacing d ≈ 5-30 millimeter of oxygen release device (2) outgas aspect and the interior top layer of water flowing cavity (6).
CN 200510056752 2005-03-25 2005-03-25 High oxygen resolving aerator Pending CN1647623A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
CN 200510056752 CN1647623A (en) 2005-03-25 2005-03-25 High oxygen resolving aerator
CN 200520118505 CN2800754Y (en) 2005-03-25 2005-09-05 Interaction type aerator with high oxygen dissolution
CNA2005100979982A CN1762859A (en) 2005-03-25 2005-09-05 Interactive high oxygen dissolution aerator
PCT/CN2005/001396 WO2006099780A1 (en) 2005-03-25 2005-09-05 An interactive high-dissolved oxygen device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200510056752 CN1647623A (en) 2005-03-25 2005-03-25 High oxygen resolving aerator

Publications (1)

Publication Number Publication Date
CN1647623A true CN1647623A (en) 2005-08-03

Family

ID=34876784

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 200510056752 Pending CN1647623A (en) 2005-03-25 2005-03-25 High oxygen resolving aerator

Country Status (2)

Country Link
CN (1) CN1647623A (en)
WO (1) WO2006099780A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112997934A (en) * 2021-03-18 2021-06-22 大连海洋大学 Method for promoting reproductive capacity of parent stichopus japonicus

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6155794A (en) * 1998-09-09 2000-12-05 Fangchenggang Ocean Science And Technology Development Center Aspirating aerator
JP2003144003A (en) * 2001-11-15 2003-05-20 Mishimaya Kaisanten:Kk Oxygen feeder for fishery
CN2577574Y (en) * 2002-10-10 2003-10-08 靳巨军 Highly soluble oxygen supplier

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112997934A (en) * 2021-03-18 2021-06-22 大连海洋大学 Method for promoting reproductive capacity of parent stichopus japonicus

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WO2006099780A1 (en) 2006-09-28

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