CN203855433U - Built-in jet flow oxygenation protein separator - Google Patents
Built-in jet flow oxygenation protein separator Download PDFInfo
- Publication number
- CN203855433U CN203855433U CN201420164470.7U CN201420164470U CN203855433U CN 203855433 U CN203855433 U CN 203855433U CN 201420164470 U CN201420164470 U CN 201420164470U CN 203855433 U CN203855433 U CN 203855433U
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- Prior art keywords
- separator
- jet
- pipe
- staving
- oxygen increasing
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Abstract
The utility model provides a built-in jet flow oxygenation protein separator which comprises a separator barrel, and is characterized in that a fixing rack with an inclined surface is arranged at the bottom in the separator barrel; a jet flow oxygenation device is fixed on the inclined surface of the fixing rack; a water outlet pipe is arranged on the separator barrel; the water outlet pipe is connected with a water outlet flow buffer pipe; a water inlet and an oxygenation air inlet are formed in the separator barrel; an oxygenation air inlet pipe is connected between the oxygenation air inlet and the jet flow oxygenation device; an anti-vortex baffle with a round hole is arranged on the upper part in the separator barrel; a foam collection chamber is formed above the top end of the separator barrel; a foam overflow pipe communicated with the separator barrel is arranged in the foam collection chamber; a foam discharging pipe is arranged on the lower part of a side wall of the foam collection chamber; a drain outlet is formed in the bottom of the separator barrel. The built-in jet flow oxygenation protein separator has the characteristics of high water treatment capacity, obvious separation effect, good gas-liquid mixing effect, low equipment cost and operating cost, simplicity in installation and maintenance and the like.
Description
Technical field
The utility model relates to the instrument field of sea farming, a kind ofly specifically for aquaculture water treatment system, albumen is carried out to separated equipment.
Background technology
The protein separator using on present society, is all to have the jet Liqiud-gas mixing device of a set of split to carry out work, and its shortcoming is complex structure, and volume is large, current consumption is large, and gas-liquid mixed efficiency is lower, and it is little to process the water yield.
Utility model content
The utility model provides a kind of built-in Jet-flow oxygen increasing protein separator, its objective is that the volume of existing split Jet-flow oxygen increasing formula protein separator is large in order to solve, efficiency compared with low, to process the water yield little, and the problem that current consumption is large, the volume of Jet-flow oxygen increasing protein separator is reduced, efficiency raises, the processing water yield is large, reduces energy consumption.
The technical solution of the utility model is:
A built-in Jet-flow oxygen increasing protein separator, comprises separator staving, it is characterized in that: the bottom in described separator staving is provided with the anchor with inclined-plane, on the inclined-plane of this anchor, is fixed with jet-flow oxygen increasing device; Described separator staving is provided with rising pipe, and this rising pipe is connected with water outlet current buffer tube; Described separator staving is provided with water-in and oxygenation inlet mouth, between described oxygenation inlet mouth and described jet-flow oxygen increasing device, is connected with oxygenation inlet pipe; Top in described separator staving is provided with out round-meshed anti-swirl baffle; Foam collecting chamber is equipped with in the top on the top of described separator staving, is provided with the foam communicating with described separator staving and overflows except pipe in described foam collecting chamber, and the bottom of described foam collecting chamber sidewall is provided with foam vent pipe; Described separator staving bottom is provided with sewage draining exit.
The transparent water level pipe that is provided with sign inner bucket water position outside described separator staving, water level pipe is communicated with separator staving.To observe the water level of separator staving.
Jet-flow oxygen increasing device in described separator staving comprises submersible machine, and the output shaft of submersible machine is connected with hollow impellers, and the cavity of hollow impellers has suction opening, between suction opening and oxygenation inlet mouth on separator staving, with oxygenation inlet pipe, is connected.
The angle that is fixed on jet-flow oxygen increasing device on anchor and separator staving bottom is 0 degree-90 degree, and jet-flow oxygen increasing device jet water course direction is toward at the bottom of bucket.
Anti-swirl baffle is: be cross spread and open round-meshed anti-swirl baffle, anti-swirl baffle vertically arranges, and the top of anti-swirl baffle extends to the top of the inwall of separator staving.
The lower sidewall of separator staving is provided with rising pipe, in separator staving inside, is connected with the mouth of pipe straight up with rising pipe, and caliber is greater than the water outlet current buffer tube of rising pipe caliber.
Compared with prior art, the utlity model has following beneficial effect:
1, the utility model utilizes built-in jet-flow oxygen increasing device, and a large amount of air intakes is inner to separator, and jet-flow oxygen increasing device drives a large amount of water simultaneously, air and water is fully mixed into vaporific, and air is initiatively sucked by jet-flow oxygen increasing device.Have advantages of that equipment volume is little, process that the water yield is large, separating effect significantly, equipment cost and low, the easy installation and maintenance of running cost.
2, in bucket, upper part is provided with vertical baffle, can place while preventing because of fluidic device gas-liquid mixed and make the water in bucket form whirlpool, and the foam that script has been stacked into more than the water surface sucks in water again, thereby has reduced effect and the efficiency of albumen sepn.
3, fluidic device injection direction is at the bottom of bucket, with form an angle at the bottom of bucket (0 degree-90 degree), then this design is dispersed into the current of two strands of different directions at the bottom of impelling the current of injection first to hit barrel, and drive bubble to rise along spiral path, not only increased the duration of contact of bubble and water, allow bubble absorption take more objectionable impurities out of, and reduced the surging force of current, make the water surface in bucket there will not be rolling effect and these two kinds of effects of cyclonic effect all the foam on the water surface can be brought in backwater again, reduce albumen sepn effect.
4, on the sidewall of separator staving, be provided with 2 rising pipes, rising pipe at the pipeline mouth of pipe of bucket inside straight up, and extend to staving middle part highly, more than caliber amplifies twice simultaneously, to prevent because going out water suction force crosses the too much bubble of good general and is discharged to outside bucket, thereby have influence on the effect of other equipment that are connected with protein segregating unit and the separating effect of protein segregating unit itself.
Accompanying drawing explanation
Fig. 1 is structure iron of the present utility model;
Fig. 2 is jet-flow oxygen increasing device structural representation of the present utility model.
In the drawings, 1: foam collecting chamber, 2: foam vent pipe, 3: oxygenation inlet mouth, 4: anti-swirl baffle, 5: oxygenation inlet pipe, 6: jet-flow oxygen increasing device, 7: with the anchor, 8 on inclined-plane: separator staving, 9: sewage draining exit, 10: rising pipe, 11: water outlet current buffer tube, 12: water-in, 13: gauging line, 14: transparent water level pipe, 15: foam collecting region, 16: foam overflows except pipe, 17: submersible machine, 18: suction opening, 19: hollow impellers, 20: cavity.
Embodiment
Below in conjunction with accompanying drawing embodiment, the utility model is further illustrated.Following examples will contribute to those skilled in the art further to understand the utility model, but not limit in any form the utility model.It should be pointed out that to those skilled in the art, without departing from the concept of the premise utility, can also make some distortion and improvement.These all belong to protection domain of the present utility model.
As shown in Figure 1, built-in Jet-flow oxygen increasing protein separator, comprise separator staving 8, the bucket end at described separator staving 8 is provided with sewage draining exit 9, bottom in described separator staving 8 is provided with the anchor 7 with inclined-plane, on the inclined-plane of this anchor 7, be fixed with the jet-flow oxygen increasing device 6 of installing with angled at the bottom of bucket (0-90 degree), the side wall upper part of described separator staving 8 is provided with water-in 12 and oxygenation inlet mouth 3, between described oxygenation inlet mouth 3 and described jet-flow oxygen increasing device 6, be provided with oxygenation inlet pipe 5, the inside on described separator staving 8 tops is provided with and is cross spread and opens round-meshed anti-swirl baffle 4, the lower end of anti-swirl baffle 4 is positioned under gauging line 13, upper end extends to the top of the inwall of separator staving 8.The lower sidewall of described separator staving 8 is provided with rising pipe 10, what in described separator staving 8 inside, be connected with rising pipe 10 has the mouth of pipe straight up, caliber is water outlet current the buffer tube 11 more than twice of rising pipe 10, the outside of 8 barrels of walls of described separator staving is communicated with the transparent water level pipe 14 of sign inner bucket water position, foam collecting chamber 1 is equipped with at the place, top on the top of described separator staving 8, in described foam collecting chamber 1, being provided with the foam communicating with described separator staving 8 overflows except pipe 16, the bottom of described foam collecting chamber 1 sidewall is provided with foam vent pipe 2, described separator staving 7 is ampuliform.
As shown in Figure 2, jet-flow oxygen increasing device 6 comprises submersible machine 17, on described submersible machine 17 shafts, is fixed with hollow impellers 19, and the cavity 20 of hollow impellers 19 is connected with suction opening 18.
Principle of work of the present utility model is as follows: during work, sewage enters in separator staving 8 from water-in 12, air enters from oxygenation inlet mouth 3, by oxygenation inlet pipe 5, for the suction opening 18 of jet-flow oxygen increasing device 6 provides air, jet-flow oxygen increasing device 6 utilizes submersible machine 17 to drive the fixing with it hollow impellers with jet function 19 by output shaft, the negative pressure producing at cavity 20 places at impeller center during 19 rotation of rotation hollow impellers, this negative pressure by air successively by oxygenation inlet mouth 3, oxygenation inlet pipe 5, the air-breathing mouth of pipe 18 and cavity 20 are initiatively drawn into separator staving 8 inside, by air intake in water and break into atomic little bubble, and be fully mixed into vaporific with the water in separator staving 8, downward-sloping jet-flow oxygen increasing device 6 ejects the flow impact that nebulizes with air mixed to a bucket wall, forms the current of two groups of different directions, and bubble is being driven with spiral path and rising to the water surface by these current, small gas ducks in drink and rises to gradually in the process of the water surface, utilize surface tension that the protein in water, grease and tiny particle (residue of bait or ight soil) etc. are adsorbed on to surface, and the foam collecting region that these materials are taken on gauging line 13 form foam, in this process, the anti-swirl baffle 4 in separator staving 8 stops that the water of barrel interior upper part forms whirlpool and foam is brought back in water again, along with foam is being on the increase and constantly piling up of foam collecting region, foam spills in foam collecting chamber 1 except pipe 16 through overflowing from foam, foam is at foam collecting chamber 1 slowly after fragmentation, and its a small amount of water of taking out of, protein, grease and tiny particle are got rid of through foam vent pipe 2, treated water is being carried bubble flow velocity when by large diameter water outlet current buffer tube 11 secretly and is being slowed down, and most of bubble from the 11 interior escapes of water outlet current buffer tube out, only has and a small amount of bubble is discharged to bucket from rising pipe 10 together with treated water.The mouth of pipe height of water outlet current buffer tube 11 is arranged on higher than jet-flow oxygen increasing device 6, can make protein separator in water inlet not enough or while there is no water access arrangement jet-flow oxygen increasing device 6 be buried in water always, the submersible machine 17 that prevents in running order jet-flow oxygen increasing device 6 is exposed in air and overheated burning; The mouth of pipe height of the current of water outlet simultaneously buffer tube 11, lower than water-in 12, can prevent that the sewage that newly enters separator staving 8 is directly discharged to bucket from water outlet current buffer tube 11.Because heterogeneity and the dirty degree of sewage are different, therefore this albumen sepn device need regulate the elevation of water surface in bucket to reach optimal separation effect, inner bucket water position height carrys out textual research and explain by transparent water level pipe 14, by regulating water-in 12 flooding quantity sizes to realize, by foam, overflow and determine except 16 speed of overflowing foam of pipe.
Claims (6)
1. a built-in Jet-flow oxygen increasing protein separator, comprises separator staving, it is characterized in that: the bottom in described separator staving is provided with the anchor with inclined-plane, on the inclined-plane of this anchor, is fixed with jet-flow oxygen increasing device; Described separator staving is provided with rising pipe, and this rising pipe is connected with water outlet current buffer tube; Described separator staving is provided with water-in and oxygenation inlet mouth, between described oxygenation inlet mouth and described jet-flow oxygen increasing device, is connected with oxygenation inlet pipe; Top in described separator staving is provided with out round-meshed anti-swirl baffle; Foam collecting chamber is equipped with in the top on the top of described separator staving, is provided with the foam communicating with described separator staving and overflows except pipe in described foam collecting chamber, and the bottom of described foam collecting chamber sidewall is provided with foam vent pipe; Described separator staving bottom is provided with sewage draining exit.
2. built-in Jet-flow oxygen increasing protein separator according to claim 1, is characterized in that: outside described separator staving, be provided with the transparent water level pipe of sign inner bucket water position, water level pipe is communicated with separator staving.
3. built-in Jet-flow oxygen increasing protein separator according to claim 1, it is characterized in that: the jet-flow oxygen increasing device in separator staving comprises submersible machine, the output shaft of submersible machine is connected with hollow impellers, the cavity of hollow impellers has suction opening, between suction opening and oxygenation inlet mouth on separator staving, with oxygenation inlet pipe, is connected.
4. built-in Jet-flow oxygen increasing protein separator according to claim 1, is characterized in that: be fixed on jet-flow oxygen increasing device on anchor and the angle of separator staving bottom and be 0 degree-90 degree, and jet-flow oxygen increasing device jet water course direction is toward at the bottom of bucket.
5. built-in Jet-flow oxygen increasing protein separator according to claim 1, it is characterized in that: the inside on separator staving top is provided with and is cross spread and opens round-meshed anti-swirl baffle, anti-swirl baffle vertically arranges, and the top of anti-swirl baffle extends to the top of the inwall of separator staving.
6. built-in Jet-flow oxygen increasing protein separator according to claim 1, is characterized in that: the lower sidewall of separator staving is provided with rising pipe, in separator staving inside, is connected with the mouth of pipe straight up with rising pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420164470.7U CN203855433U (en) | 2014-04-04 | 2014-04-04 | Built-in jet flow oxygenation protein separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420164470.7U CN203855433U (en) | 2014-04-04 | 2014-04-04 | Built-in jet flow oxygenation protein separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203855433U true CN203855433U (en) | 2014-10-01 |
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ID=51605300
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420164470.7U Expired - Fee Related CN203855433U (en) | 2014-04-04 | 2014-04-04 | Built-in jet flow oxygenation protein separator |
Country Status (1)
| Country | Link |
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| CN (1) | CN203855433U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106186181A (en) * | 2016-08-30 | 2016-12-07 | 嘉善金亿精密铸件有限公司 | A kind of eddy flow water-distributing protein separator |
| CN107617269A (en) * | 2017-11-06 | 2018-01-23 | 江苏嘉宇特种装备股份有限公司 | A kind of high-efficiency gas-liquid separator |
| CN108689445A (en) * | 2018-08-01 | 2018-10-23 | 青岛越洋水产科技有限公司 | Efficient kinetic energy purifies protein separator |
| CN110292019A (en) * | 2018-03-22 | 2019-10-01 | 顾向前 | Pure oxygen dissolution used for aquiculture and foam fraction factor double-duty plant |
-
2014
- 2014-04-04 CN CN201420164470.7U patent/CN203855433U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106186181A (en) * | 2016-08-30 | 2016-12-07 | 嘉善金亿精密铸件有限公司 | A kind of eddy flow water-distributing protein separator |
| CN107617269A (en) * | 2017-11-06 | 2018-01-23 | 江苏嘉宇特种装备股份有限公司 | A kind of high-efficiency gas-liquid separator |
| CN110292019A (en) * | 2018-03-22 | 2019-10-01 | 顾向前 | Pure oxygen dissolution used for aquiculture and foam fraction factor double-duty plant |
| CN108689445A (en) * | 2018-08-01 | 2018-10-23 | 青岛越洋水产科技有限公司 | Efficient kinetic energy purifies protein separator |
| CN108689445B (en) * | 2018-08-01 | 2023-12-08 | 青岛越洋水产科技有限公司 | High-efficiency kinetic energy purifying protein separator |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141001 |