CN104221989A - High-speed water body oxygenation device - Google Patents
High-speed water body oxygenation device Download PDFInfo
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- CN104221989A CN104221989A CN201410456793.8A CN201410456793A CN104221989A CN 104221989 A CN104221989 A CN 104221989A CN 201410456793 A CN201410456793 A CN 201410456793A CN 104221989 A CN104221989 A CN 104221989A
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Abstract
The invention discloses a high-speed water body oxygenation device. The high-speed water body oxygenation device comprises boosting equipment, a water inlet pipeline, a water outlet pipeline, a valve, a gas pipeline, a valve and a bubble crushing device arranged on the water outlet pipeline, wherein the bubble crushing device consists of two discontinuous flow blocking parts which are arranged on the water outlet pipeline along a water flow direction; the flow blocking part close to a water coming direction is provided with at least one through hole along the water flow direction, and the area of the flow blocking part firstly keeps constant, decreases gradually, and keeps constant; the flow blocking part far away from the water coming direction is provided with a plurality of groups of circular through holes along the water flow direction; the number of through holes in each group of through holes is greater than or equal to 3. Ultrahigh-density fine bubbles are generated by a large quantity of cavitation nucleuses formed on a tension surface through which high-speed turbulent current flows; the high-speed water body oxygenation device is simple in structure, is compact in layout, and is very suitable for the processes of intensive aquaculture, highly-aerobic aquatic product transportation and the like.
Description
Technical field
The present invention relates to aquaculture field, be specially a kind of two-forty water body oxygenate apparatus.
Background technology
High speed oxygenation is the problem perplexing many aquaculture families always, as madai etc. needs the fish of high dissolved oxygen environment to be difficult to find good oxygenation way in breeding process, need a large amount of oxygen replenishing equipments to run simultaneously, and the growth of fish of noise extreme influence.In addition, the fish such as duckbilled fish need great dissolved oxygen to meet living necessities in transportation, because anoxic causes a large amount of fish body dead more than traditional air pump and airbag transport, also limit transportation range.
Tradition bubble diameter is at 0.5mm-2mm, rise rapidly in water, vanishing immediately after the arrival water surface disappears, and slow for the microbubble rate of climb in water of diameter below 50 μm, specific surface area is large, and therefore the speed of gas-liquid mass transfer is far above traditional large-size bubbles.In recent years, micron bubble is not only widely used in the industrial circles such as air supporting, oxygenation aeration, beverage deoxidation, is also more and more applied to the civil areas such as medical treatment, beauty treatment, bathing.
Due to the various advantages of micron bubble, increasing people begin one's study micron bubble produce mechanism and micron bubble generate equipment.Existing micron bubble generating means mainly contains supersonic oscillations formula, mechanical shearing type and hydraulic shear formula etc.Wherein, because sonic oscillation formula and mechanical shearing type need the machinery of addition ultrasound wave generating device or complexity to form, therefore apply less, current micron bubble generating means adopts hydraulic shear formula mostly, by special design, realize unique flow field, by the hydraulic shear effect in flow field, the large-size bubbles in fluid is broken for micron bubble.As patent CN 101565230 B, describe micron bubble generating means and cyclone thereof, the bubble breaking discharged by low-pressure area by the hydraulic shear effect of rotating flow becomes micron bubble, and the equipment close with it also has patent JP JP 2003-126665.
Existing hydraulic shear declines a meter bubble generator, the negative pressure of the low-pressure area all relying on rotational flow field or Venturi tube structure to be formed introduces gas (or directly passing into compressed air), be discharged in fluid by molten gas with the form of bubble by higher-pressure region again, the hydraulic shear effect finally by rotational flow field carries out fragmentation to large-size bubbles.The said equipment can produce the microbubble of some, but number of bubbles in unit volume is less, generally 10
5individual/below L, is difficult to meet the keeping demand under the higher environment of unit oxygen demand.
Summary of the invention
In order to solve the less problem of number of bubbles in unit volume, the invention provides a kind of two-forty water body oxygenate apparatus, it utilizes high velocity turbulent flow to flow through the tiny bubble of a large amount of cavitation nucleus generation VHD that low surface tension surface, local is formed, bubble diameter that this process produces is minimum, is about 5-50 μm.
For achieving the above object, technical scheme of the present invention is:
A kind of two-forty water body oxygenate apparatus, it comprises supercharging equipment, inlet and outlet pipe and valve, gas piping and valve, and is arranged on the bubble breaking device on outlet pipeline;
Wherein, this bubble breaking device is be arranged on outlet pipeline two along the discontinuous choked flow piece of water (flow) direction; Wherein, near inflow direction choked flow piece along water (flow) direction there being at least one through hole, this through hole cross section is circular, and its area first remains unchanged along water (flow) direction, then diminishes gradually, then remains unchanged; Away from inflow direction choked flow piece along water (flow) direction being also provided with several group manholes, often organize through hole number and be more than or equal to 3, perpendicular to the projection in water (flow) direction plane, distance of center circle is from identical each other, and often organizes the close inflow direction choked flow piece corresponding through hole of circular projection distance at the distance of center circle perpendicular to circular projection in water (flow) direction plane from identical;
Wherein, if be d1 near the cylindrical hole internal diameter away from water (flow) direction of inflow direction choked flow piece, number of openings is n1, cylindrical hole internal diameter away from inflow direction choked flow piece is d2, often organizing number of openings is n2, outlet pipeline internal diameter is D, and the distance of two assembly opposite faces is h, then parameter should meet d1n1
1/2=0.2D-0.5D, d2n2
1/2=0.2d1-0.5d1, h are at 0.5n1d1
2/ D to 2n1d1
2between/D;
Wherein, the through hole bus of two choked flow piece opposing through-bores opening parts becomes circular arc line from straight line; If be d1 near the cylindrical hole internal diameter away from water (flow) direction of inflow direction choked flow piece, this circular arc type bus along the tangent line at choked flow piece through hole main body generatrix direction distance 0.5d1 place and the angle of choked flow piece through hole main body bus at 15 °-75 °.If the cylindrical hole internal diameter away from the close water (flow) direction of inflow direction choked flow piece is 0.5d2, this circular arc type bus along the tangent line at choked flow piece through hole main body generatrix direction distance d2 place and the angle of choked flow piece through hole main body bus at 30 °-75 °; Circular arc type bus near the cylindrical hole away from water (flow) direction of inflow direction choked flow piece is less than 1/2h in the length of water (flow) direction, and the circular arc type bus away from the cylindrical hole of the close water (flow) direction of inflow direction choked flow piece is less than 1/4h in the length of water (flow) direction;
Wherein, gas piping is connected on inlet pipeline, by negative pressure self-priming or the mode such as compressor gas supplied, gas and vapor permeation is entered inlet pipeline;
Wherein, described supercharging equipment is the water pump that peripheral pump, jet pump, measuring pump, peristaltic pump or plunger pump etc. can increase fluid pressure.
The present invention adopts the beneficial effect of technique scheme to be: this apparatus structure is simple, compact in design, is very applicable to the process such as intensive aquaculture and high aerobic aquatic product transportation.
Accompanying drawing explanation
Fig. 1 is assembly connection diagram of the present invention;
Fig. 2 is the STRUCTURE DECOMPOSITION schematic diagram of bubble breaking device of the present invention;
Fig. 3 is the generalized section of bubble breaking device of the present invention;
Fig. 4 is away from the schematic cross-section of inflow direction choked flow piece in through hole;
Fig. 5 is near the schematic cross-section of inflow direction choked flow piece in through hole.
Embodiment
Present pre-ferred embodiments is provided, to describe technical scheme of the present invention in detail below in conjunction with accompanying drawing.
As shown in Figure 1, it is the common eel cultivation oxygenation pool being provided with this device, it consists of: common eel aquaculture water mire 9, water feeding one-way valve 7(is containing screen pack), inlet pipeline 2, Venturi tube 3 form inlet and outlet pipe and valve, air inlet pipeline 5 and check valve 4 form gas piping and valve, jet pump 1 is supercharging equipment, and valve 10 and outlet pipeline 6 form outlet pipeline and valve, bubble breaking device 8, when needs carry out oxygenation to the common eel pool 9, open outlet pipeline valve 10, open jet pump 1, aquaculture water in the common eel pool 9 through water feeding one-way valve 7(containing screen pack) filter bulky grain after enter inlet pipeline 2, high-velocity flow is by forming negative pressure at trunnion place during Venturi tube 3, air passes through air inlet pipeline 5 under the effect of this negative pressure, enter Venturi tube 3 through check valve 4 to mix with water inlet, above-mentioned gas-liquid mixture carries out entering outlet pipeline 6 after dissolving mixing through jet pump 1, the heavy-oxygen-enriched water containing high concentration micron bubble formed after bubble breaking device 8 fragmentation enters the common eel pool 9, for its high speed oxygenation.
As shown in Figure 2,3, described bubble breaking device 8 is for being arranged on outlet pipeline two along the discontinuous choked flow piece of water (flow) direction; Wherein, near inflow direction choked flow piece 81 along water (flow) direction there being at least one through hole 811, this through hole cross section is circular, and its area first remains unchanged along water (flow) direction, then diminishes gradually, then remains unchanged; Away from inflow direction choked flow piece 82 along water (flow) direction being also provided with several group manholes 821, often organize through hole number and be more than or equal to 3, perpendicular to the projection in water (flow) direction plane, distance of center circle is from identical each other, and often organizes the close inflow direction choked flow piece corresponding through hole of circular projection distance at the distance of center circle perpendicular to circular projection in water (flow) direction plane from identical.
In described two discontinuous choked flow pieces, if be d1 near the cylindrical hole internal diameter away from water (flow) direction of inflow direction choked flow piece, number of openings is n1, cylindrical hole internal diameter away from inflow direction choked flow piece is d2, often organizing number of openings is n2, outlet pipeline internal diameter is D, and the distance of two assembly opposite faces is h, then parameter should meet d1n1
1/2=0.2D-0.5D, d2n2
1/2=0.2d1-0.5d1, h are at 0.5n1d1
2/ D to 2n1d1
2between/D; As shown in Figure 4,5, wherein the through hole bus of two choked flow piece opposing through-bores opening parts is circular arc line, if be d1 near cylindrical hole 811 internal diameter away from water (flow) direction of inflow direction choked flow piece 81, described circular arc type bus 8111 along the tangent line at choked flow piece through hole main body generatrix direction distance 0.5d1 place and the angle of choked flow piece through hole main body bus at 15 °-75 °; If be 0.5d2 away from cylindrical hole 821 internal diameter of the close water (flow) direction of inflow direction choked flow piece 82, this circular arc type bus 8211 along the tangent line at choked flow piece through hole main body generatrix direction distance d2 place and the angle of choked flow piece through hole main body bus at 30 °-75 °, and being less than 1/2h near the circular arc type bus 8111 of the cylindrical hole 811 away from water (flow) direction of inflow direction choked flow piece 81 in the length of water (flow) direction, the circular arc type bus 8211 away from the cylindrical hole 821 of the close water (flow) direction of inflow direction choked flow piece 82 is less than 1/4h in the length of water (flow) direction.
Above-mentioned embodiment is exemplary, is to better enable those skilled in the art understand this patent, can not be interpreted as it is restriction this patent being comprised to scope; As long as any change that the technology contents essence that technical scheme is made disclosed in this patent is identical or equivalent or modification, all fall into the scope that this patent comprises.
Claims (7)
1. a two-forty water body oxygenate apparatus, it comprises supercharging equipment, inlet and outlet pipe and valve, gas piping and valve, and is arranged on the bubble breaking device on outlet pipeline; It is characterized in that, this bubble breaking device is be arranged on outlet pipeline two along the discontinuous choked flow piece of water (flow) direction; Wherein, near inflow direction choked flow piece along water (flow) direction there being at least one through hole, this through hole cross section is circular, and its area first remains unchanged along water (flow) direction, then diminishes gradually, then remains unchanged; Away from inflow direction choked flow piece along water (flow) direction being also provided with several group manholes, often organize through hole number and be more than or equal to 3, perpendicular to the projection in water (flow) direction plane, distance of center circle is from identical each other, and often organizes the close inflow direction choked flow piece corresponding through hole of circular projection distance at the distance of center circle perpendicular to circular projection in water (flow) direction plane from identical.
2. two-forty water body oxygenate apparatus as claimed in claim 1, it is characterized in that, in described two discontinuous choked flow pieces, if be d1 near the cylindrical hole internal diameter away from water (flow) direction of inflow direction choked flow piece, number of openings is n1, and the cylindrical hole internal diameter away from inflow direction choked flow piece is d2, often organizing number of openings is n2, outlet pipeline internal diameter is D, and the distance of two assembly opposite faces is h, then parameter should meet d1n1
1/2=0.2D-0.5D, d2n2
1/2=0.2d1-0.5d1, h are at 0.5n1d1
2/ D to 2n1d1
2between/D.
3. two-forty water body oxygenate apparatus as claimed in claim 1, it is characterized in that, the through hole bus of two choked flow piece opposing through-bores opening parts becomes circular arc line from straight line.
4. two-forty water body oxygenate apparatus as claimed in claim 3, it is characterized in that: set the cylindrical hole internal diameter away from water (flow) direction near inflow direction choked flow piece as d1, described circular arc type bus along the tangent line of choked flow piece through hole main body generatrix direction distance 0.5d1 and the angle of choked flow piece through hole main body bus at 15 °-75 °; If the cylindrical hole internal diameter away from the close water (flow) direction of inflow direction choked flow piece is 0.5d2, this circular arc type bus along the tangent line at choked flow piece through hole main body generatrix direction distance d2 place and the angle of choked flow piece through hole main body bus at 30 °-75 °.
5. two-forty water body oxygenate apparatus as claimed in claim 3, it is characterized in that: the circular arc type bus near the cylindrical hole away from water (flow) direction of inflow direction choked flow piece is less than 1/2h in the length of water (flow) direction, and the circular arc type bus away from the cylindrical hole of the close water (flow) direction of inflow direction choked flow piece is less than 1/4h in the length of water (flow) direction.
6. two-forty water body oxygenate apparatus as claimed in claim 1, is characterized in that: described gas piping is connected on inlet pipeline, by negative pressure self-priming or the mode such as compressor gas supplied, gas and vapor permeation is entered inlet pipeline.
7. two-forty water body oxygenate apparatus as claimed in claim 1, is characterized in that: described supercharging equipment is arbitrary water pump that peripheral pump, jet pump, measuring pump, peristaltic pump or plunger pump etc. can increase fluid pressure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410456793.8A CN104221989A (en) | 2014-09-10 | 2014-09-10 | High-speed water body oxygenation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410456793.8A CN104221989A (en) | 2014-09-10 | 2014-09-10 | High-speed water body oxygenation device |
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| CN104221989A true CN104221989A (en) | 2014-12-24 |
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ID=52211611
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410456793.8A Pending CN104221989A (en) | 2014-09-10 | 2014-09-10 | High-speed water body oxygenation device |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2019144532A1 (en) * | 2018-01-26 | 2019-08-01 | Linde Aktiengesellschaft | Oxygen dissolving apparatus for ponds |
| CN110558273A (en) * | 2019-10-15 | 2019-12-13 | 上海海洋大学 | Pond river crab aqueous vapor integrated auxiliary breeding device with microbubbles carried by water |
| CN112956445A (en) * | 2021-04-09 | 2021-06-15 | 江皓 | System and method for transporting live fish by adopting nano bubble water |
| CN113854232A (en) * | 2021-10-18 | 2021-12-31 | 中国人民解放军空军勤务学院 | Water oxygenation device |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101869799A (en) * | 2009-06-17 | 2010-10-27 | 株式会社山口工业 | Micron bubble device |
| CN201690904U (en) * | 2010-02-05 | 2011-01-05 | 侯旭光 | Dissolved oxygen device for aquaculture |
| JP2013103205A (en) * | 2011-11-16 | 2013-05-30 | Icst:Kk | High concentration oxygen water production apparatus, high concentration oxygen water watering apparatus, and high concentration oxygen water production method |
| CN103785311A (en) * | 2014-03-05 | 2014-05-14 | 上海纯元环保科技有限公司 | Micro-nano bubble generating device |
| CN203635365U (en) * | 2013-11-19 | 2014-06-11 | 金青松 | Micron bubble shower |
-
2014
- 2014-09-10 CN CN201410456793.8A patent/CN104221989A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101869799A (en) * | 2009-06-17 | 2010-10-27 | 株式会社山口工业 | Micron bubble device |
| CN201690904U (en) * | 2010-02-05 | 2011-01-05 | 侯旭光 | Dissolved oxygen device for aquaculture |
| JP2013103205A (en) * | 2011-11-16 | 2013-05-30 | Icst:Kk | High concentration oxygen water production apparatus, high concentration oxygen water watering apparatus, and high concentration oxygen water production method |
| CN203635365U (en) * | 2013-11-19 | 2014-06-11 | 金青松 | Micron bubble shower |
| CN103785311A (en) * | 2014-03-05 | 2014-05-14 | 上海纯元环保科技有限公司 | Micro-nano bubble generating device |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2019144532A1 (en) * | 2018-01-26 | 2019-08-01 | Linde Aktiengesellschaft | Oxygen dissolving apparatus for ponds |
| CN110558273A (en) * | 2019-10-15 | 2019-12-13 | 上海海洋大学 | Pond river crab aqueous vapor integrated auxiliary breeding device with microbubbles carried by water |
| CN112956445A (en) * | 2021-04-09 | 2021-06-15 | 江皓 | System and method for transporting live fish by adopting nano bubble water |
| CN112956445B (en) * | 2021-04-09 | 2024-03-26 | 江皓 | System and method for transporting live fish by using nano bubble water |
| CN113854232A (en) * | 2021-10-18 | 2021-12-31 | 中国人民解放军空军勤务学院 | Water oxygenation device |
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