CN201148357Y - Circulation cultivation water air-float purifying equipment - Google Patents
Circulation cultivation water air-float purifying equipment Download PDFInfo
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- CN201148357Y CN201148357Y CNU2007200159140U CN200720015914U CN201148357Y CN 201148357 Y CN201148357 Y CN 201148357Y CN U2007200159140 U CNU2007200159140 U CN U2007200159140U CN 200720015914 U CN200720015914 U CN 200720015914U CN 201148357 Y CN201148357 Y CN 201148357Y
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Abstract
The utility model discloses a gas floating purification device of cycling aquaculture water. In the device, a water intake pipe (1) is connected with the inlet of a gas-liquid mixing pump (11) through a valve (2), a flow meter (5) and a vacuum gauge (10); an air intake pipe (12) is also connected with the inlet of the gas-liquid mixing pump (11), and is provided with a gas flow meter (13) and a valve (14); the outlet of the gas-liquid mixing pump (11) is connected with a dissolving air container (15); the dissolving air container (15) is connected with an outgassing column (22) in a gas floating tank (23) through a pressure gauge (18) and a valve (19); the upper end of the gas floating tank (23) is also connected with a foam removing pipeline (21); the lower end of the foam removing pipeline (21) is arranged in a foam collecting groove (20); the lower end of the gas floating tank (23) is connected with a rising pipe (25); the rising pipe (25) is connected with a valve (24). The purification device has excellent purifying effects on micro particles in the aquaculture water; the removal efficiency of the micro particles (based on the turbidity) reaches above 75 percent. In addition, as a result of the dissolution of air, the concentration of dissolved oxygen in the aquaculture water can be increased by 30 percent to 60 percent.
Description
Technical field:
The utility model relates to a kind of cyclic culture water treating plant, especially a kind ofly can effectively remove microparticle (below 20 microns) in the aquaculture water, improves water pH value and help the cyclic culture water body air-float purification equipment of oxygenation.
Background technology:
In circulating water culture system, propagate the bait that fish are thrown in artificially, except that being eaten up, all the other all remain in cultures in the water; And institute's bait material also has only 20~30% nutritive ingredient to be absorbed by fish, and major part is then arranged in the breed water with the form of ight soil.In the circulating water cultivation process, the miniature solid particle of generation accounts for the total solids particulate more than 90%, and its main component is protein and organic acid.The accumulation of microparticle not only can be stopped up the fish gill, causes the death by suffocation of fish, decomposes in water because of it simultaneously, the dissolved oxygen in also can consume water, increases ammonia nitrogen and organic content, causes water quality deterioration.Owing to adopting common sand, net filtration to be difficult to effective microparticle of removing in the aquaculture water, therefore, the removal of miniature solid particulate is the emphasis and the difficult point of aquaculture technology research always in the aquaculture water.
Summary of the invention:
The utility model is in order to solve the existing the problems referred to above of prior art, a kind of miniature solid particle that can effectively remove in the aquaculture water to be provided, and improves cultivation water pH value and helps the cyclic culture water body air-float purification equipment of oxygenation.
Technical solution of the present utility model is: a kind of cyclic culture water body air-float purification equipment, it is characterized in that: water inlet pipe 1 is arranged, water inlet pipe 1 is by valve 2, under meter 5, vacuum meter 10 joins with the inlet of gas-liquid mixing pump 11, also be connected to inlet pipe 12 with the inlet of gas-liquid mixing pump 11, inlet pipe 12 is provided with gas meter 13, valve 14, the outlet of gas-liquid mixing pump 11 and dissolving 15 join, dissolving 15 is by tensimeter 18, outgas post 22 in valve 19 and the air flotation tank 23 joins, be connected to foam removal pipeline 21 with the upper end of air flotation tank 23, the lower end of foam removal pipeline 21 places in the foam receiving tank 20, the lower end of air flotation tank 23 and rising pipe 25 join, and are connected to valve 24 on the rising pipe 25.
Be provided with vapor pipe 17 in the upper end of described dissolving 15, vent valve 16 is arranged on the vapor pipe 17.
Be connected to intercepting sewer 3 with the inlet end of described valve 2, intercepting sewer 3 is connected on the water inlet pipe 8 between under meter 5, the vacuum meter 10 by valve 4, water inlet pipe 8 between intercepting sewer 3 and the under meter 5 joins with water shoot 7, water discharge valve 6 is arranged on the water shoot 7, valve (9) is arranged on the water inlet pipe 8 between intercepting sewer 3 and the vacuum meter 10.
The utility model is that gas-liquid mixing pump and dissolving and air-flotation column are in series, microparticle in the aquaculture water there is very strong decontamination effect improving, the clearance of microparticle (with turbidometer) is more than 75%, simultaneously because effective removal of microparticle, reduced organic content, cultivation water pH value is improved.Because the dissolving in of air, dissolved oxygen concentration can increase by 30%~60% in the aquaculture water in addition.The utility model has also made full use of waterhead, and the foam concentrate matter of air-flotation column top is collected in the foam collection device by the overflow effect, has reduced energy consumption, has reduced purification cost and labor intensity of operating personnel.
Description of drawings:
Fig. 1 is the structural representation of the utility model embodiment.
Embodiment:
Below in conjunction with description of drawings embodiment of the present utility model.As shown in Figure 1: water inlet pipe 1 is arranged, water inlet pipe 1 is by valve 2, under meter 5, vacuum meter 10 joins with the inlet of gas-liquid mixing pump 11, also be connected to inlet pipe 12 with the inlet of gas-liquid mixing pump 11, inlet pipe 12 is provided with gas meter 13, valve 14, the outlet of gas-liquid mixing pump 11 and dissolving 15 join, dissolving 15 is by tensimeter 18, outgas post 22 in valve 19 and the air flotation tank 23 joins, be connected to foam removal pipeline 21 with the upper end of air flotation tank 23, the lower end of foam removal pipeline 21 places in the foam receiving tank 20, the lower end of air flotation tank 23 and rising pipe 25 join, and are connected to valve 24 on the rising pipe 25.Air flotation tank 23, foam receiving tank 20 can place on the operator's console 26, and air flotation tank 23 bottoms join by ring flange 27 and operator's console 26.
Too much for preventing the liquid in the dissolving 15, pressure is excessive, is provided with vapor pipe 17 in the upper end of described dissolving 15, and vent valve 16 is arranged on the vapor pipe 17, remaining gas can be discharged by vent valve.Pressure for buffer traffic meter 3, also for 6 in case of necessity as discharge pipe line, be connected to intercepting sewer 3 with the inlet end of described valve 2, intercepting sewer 3 is connected on the water inlet pipe 8 between under meter 5, the vacuum meter 10 by valve 4, water inlet pipe 8 between intercepting sewer 3 and the under meter 5 joins with water shoot 7, water discharge valve 6 is arranged on the water shoot 7, and the water inlet pipe 8 between intercepting sewer 3 and the vacuum meter 5 joins with valve 9.
Working process:
Water inlet pipe 1 is communicated with the water shoot of culturing the pond, and valve-off 4,6 is observed under meter 5, vacuum meter 10, and adjusts valve 2,9, with the flow and the vacuum tightness of control water inlet (culturing the sewage that discharge in the pond); Simultaneously, observe gas meter 13, adjust valve 14, with the control air air input.Water and gas pump into dissolving 15 after entering gas-liquid mixing pump 11 simultaneously, observe tensimeter 18, and regulated valve 19 is with the pressure of control dissolved air water.Dissolved air water discharges micro bubble, water by outgas post 13, micro bubble will adhere to the miniature solid particle, float to liquid level, form a large amount of foams, the foam of come-up enters in the foam receiving tank 20 by foam removal pipeline 21, and the clear water after the purification sinks and rising pipe 25, valve 24 by being arranged on air flotation tank 23 lower ends, enter and culture in the pond, finish a working cycle.
In the scavenging process, the gas in the dissolving 15 is too much, when pressure is excessive, can unnecessary gas be discharged by valve 16.
And for the pressure of buffer traffic meter 5, but valve-off 2, valve 6, Open valve 4,9, sewage then pass through intercepting sewer 3, valve 4,9, purify; And sewage is when need not to purify, but valve-off 2,9 then, Open valve 4,6, then sewage is directly discharged.
Claims (3)
1. cyclic culture water body air-float purification equipment, it is characterized in that: water inlet pipe (1) is arranged, water inlet pipe (1) is by valve (2), under meter (5), vacuum meter (10) joins with the inlet of gas-liquid mixing pump (11), also be connected to inlet pipe (12) with the inlet of gas-liquid mixing pump (11), inlet pipe (12) is provided with gas meter (13), valve (14), the outlet of gas-liquid mixing pump (11) and dissolving (15) join, dissolving (15) is by tensimeter (18), outgas post (22) in valve (19) and the air flotation tank (23) joins, be connected to foam removal pipeline (21) with the upper end of air flotation tank (23), the lower end of foam removal pipeline (21) places in the foam receiving tank (20), the lower end of air flotation tank (23) and rising pipe (25) join, and are connected to valve (24) on the rising pipe (25).
2. cyclic culture water body air-float purification equipment according to claim 1 is characterized in that: be provided with vapor pipe (17) in the upper end of described dissolving (15), vent valve (16) is arranged on the vapor pipe (17).
3. cyclic culture water body air-float purification equipment according to claim 1 and 2, it is characterized in that: be connected to intercepting sewer (3) with the inlet end of described valve (2), intercepting sewer (3) is connected on the water inlet pipe (8) between under meter (5), the vacuum meter (10) by valve (4), water inlet pipe (8) between intercepting sewer (3) and the under meter (5) joins with water shoot (7), water discharge valve (6) is arranged on the water shoot (7), on the water inlet pipe (8) between intercepting sewer (3) and the vacuum meter (10) valve (9) is arranged.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNU2007200159140U CN201148357Y (en) | 2007-11-16 | 2007-11-16 | Circulation cultivation water air-float purifying equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNU2007200159140U CN201148357Y (en) | 2007-11-16 | 2007-11-16 | Circulation cultivation water air-float purifying equipment |
Publications (1)
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CN201148357Y true CN201148357Y (en) | 2008-11-12 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CNU2007200159140U Expired - Fee Related CN201148357Y (en) | 2007-11-16 | 2007-11-16 | Circulation cultivation water air-float purifying equipment |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101955241A (en) * | 2010-10-11 | 2011-01-26 | 无锡鼎天环保设备有限公司 | Intermittent type air-floating system |
CN102657134A (en) * | 2012-05-31 | 2012-09-12 | 山东省海洋水产研究所 | Industrial circulating seawater aquiculture system |
WO2016110043A1 (en) * | 2015-01-09 | 2016-07-14 | 深圳泓亚海洋科技集团有限公司 | Suspension apparatus capable of separating soluble organic waste in mariculture |
CN108502959A (en) * | 2018-06-22 | 2018-09-07 | 南京中衡元环保科技有限公司 | Intensive air-floating apparatus and system |
-
2007
- 2007-11-16 CN CNU2007200159140U patent/CN201148357Y/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101955241A (en) * | 2010-10-11 | 2011-01-26 | 无锡鼎天环保设备有限公司 | Intermittent type air-floating system |
CN102657134A (en) * | 2012-05-31 | 2012-09-12 | 山东省海洋水产研究所 | Industrial circulating seawater aquiculture system |
CN102657134B (en) * | 2012-05-31 | 2014-10-22 | 山东省海洋水产研究所 | Industrial circulating seawater aquiculture system |
WO2016110043A1 (en) * | 2015-01-09 | 2016-07-14 | 深圳泓亚海洋科技集团有限公司 | Suspension apparatus capable of separating soluble organic waste in mariculture |
CN108502959A (en) * | 2018-06-22 | 2018-09-07 | 南京中衡元环保科技有限公司 | Intensive air-floating apparatus and system |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20081112 Termination date: 20141116 |
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EXPY | Termination of patent right or utility model |