CN2895406Y - Sewater desalting system utilizing jet technology - Google Patents
Sewater desalting system utilizing jet technology Download PDFInfo
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- CN2895406Y CN2895406Y CNU2006201154154U CN200620115415U CN2895406Y CN 2895406 Y CN2895406 Y CN 2895406Y CN U2006201154154 U CNU2006201154154 U CN U2006201154154U CN 200620115415 U CN200620115415 U CN 200620115415U CN 2895406 Y CN2895406 Y CN 2895406Y
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- treatment system
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- desalination
- desalination treatment
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/131—Reverse-osmosis
Abstract
The utility model relates to a sea water desalination system with fluidics, which comprises filter equipment, a sound energy handling equipment and a desalination equipment. The sea water after rough filtration and fine filtration enters the sound energy handling equipment, then becomes small micelle sea water to be stored in the tank, and are transferred by a pump to the reverse osmosis membrane. The water after filtration becomes fresh water and is stored in the fresh water tank. The reverse osmosis membrane can be changed to a distillation apparatus. The utility model has advantages of simple structure of the desalination devices, low investment and cost, stable performance. The sea water is not only desalinated but also changed into small micelle sea water which is easy to be absorbed by human body.
Description
Technical field
The utility model relates to the sea water desaltination treatment unit, is specifically related to a kind of desalination treatment system that utilizes fluidics, belongs to International Classification of Patents C02F1/00 " processing of water, waste water, sewage " technical field.
Background technology
At present, the method for the sea water desaltination of adopting is many both at home and abroad, as covert method, method of evaporation, distillation method, method of cooling, membrane separation process, reverse osmosis method, electroosmose process, chemical equilibrium method, ion exchange method, hydration method, solvent extration etc.What maintain the leading position at present is to dodge anxious distillation method, accounts for 70% of current sea water desaltination ultimate production.Its shortcoming is: facility investment is many, and the seawater internal circulating load is big, and the system water yield is little, and the system water speed is slow, and enrichment factor is lower, the process cost height.
Summary of the invention
The purpose of this utility model is to overcome the deficiency of aforesaid method, and a kind of novel sea water desalinization treatment system that adopts fluidics is provided.
The purpose of this utility model is realized by following technical scheme.
Utilize the desalination treatment system of fluidics, comprise filtration unit, the acoustic energy treatment unit, desalting equipment three parts are formed.Filtration unit comprises the seawater acquisition port, connects sea-water pump, connects the coarse filtration device, connects fine filtering apparatus again.Seawater after the smart filter enters the acoustic energy treatment unit, and according to actual needs, this acoustic energy treatment unit can be extremely multistage for secondary.Seawater through the acoustic energy treatment unit was handled has become the subset seawater, is stored in the tank, and through being pumped to reverse osmosis membrane, the water after the infiltration becomes fresh water, is stored in the fresh-water pool.
Another kind of scheme of the present utility model is: change the reverse osmosis membrane in the such scheme into distiller, the fresh water through distiller distills out is stored in the fresh-water pool.
Described acoustic energy treatment unit is mainly a fluid sound energy generator, is a metallic cavity, comprises that cavity and upper and lower axocoel are formed in one; The axle center of the upper/lower terminal face of upper and lower axocoel is provided with co-axial two outlets, is evenly distributed with inlet on the middle cavity.The inlet that distributes on the middle cavity is 4-40.This inlet is the inclined hole of following current body trend, and the angle of this inlet axis and cylindrical tangent line is 30 °-90 °.The ratio of this inlet aperture and outlet aperture is 100: 1-20.The diameter ratio of the root diameter of axocoel and middle cavity is 1 on the described liquid sonic-energy producer inner chamber: 1-5.
The invention has the advantages that: simple in structure, facility investment is few, and cost is low, stable performance.Not only with sea water desaltination, but also be small-micelle water, be easy to the absorption by human body utilization the seawater short chain.
Description of drawings
Fig. 1 is the equipment combination synoptic diagram of invention desalination treatment system;
Fig. 2,3 is the inner-cavity structure synoptic diagram of sound energy generator in the acoustic energy treatment unit.
Among the figure: 1, seawater acquisition port, 2, sea-water pump, 3, rough filtering device, 4, fine filtering device, 5, air compressor machine, 6, the acoustic energy treatment unit, 7, small molecules seawater tank, 8, pump, 9, reverse osmosis membrane, 10, fresh-water pool, 11, the liquid sonic-energy producer.
Embodiment
As shown in Figure 1, prepare the seawater of desalination,, deliver to rough filtering device 3, tentatively filter the filtering plurality of impurities by sea-water pump 2 by seawater acquisition port 1.After the coarse filtration, enter fine filtering device 4, processing such as sterilize.Smart filter is laggard goes into acoustic energy treatment unit 6, by air compressor machine 5 send airs to liquid sonic-energy producer 11, through secondary (can be multistage) jet vibration treatment, become purified small molecules seawater, deposit in the small molecules seawater tank 7, deliver to reverse osmosis membrane 9 through pump 8 again, after reverse-osmosis treated, remove salinity, become fresh water, deposit in the fresh-water pool 10, available.(above-mentioned rough filtering device and fine filtering device are the device of using in the prior art.)
As shown in Figure 2, liquid sonic-energy producer 1 is a metallic cavity, comprises that cavity and upper and lower axocoel are formed in one; The axle center of the upper/lower terminal face of upper and lower axocoel is provided with co-axial two outlets, is evenly distributed with inlet on the middle cavity.The inlet that distributes on the middle cavity is 4-40.This inlet is the inclined hole of following current body trend, and the angle of this inlet axis and cylindrical tangent line is 30 °-90 °.The ratio of inlet aperture and outlet aperture is 100: 1-20.The diameter ratio of the root diameter of axocoel and middle cavity is 1 on described liquid sonic-energy producer 1 inner chamber: 1-5.The frequency of producer is 100HZ-30 ten thousand HZ, and the sound intensity of producer is greater than 100dB.The pressure of liquid pressure pump is 0.2Mpa-80Mpa; The power of liquid pressure pump is 2KW-500KW.
The fluidics that the utility model is alleged, it is the liquid sonic-energy processing technology, its principle is as follows: the process of liquid sonic-energy processing can be sketched and be: according to solid-state, liquid, the different qualities of the processed material that gaseous state etc. are different and processing purpose, select specific hydrodynamic force medium, specific audio frequency, the specific sound intensity, specific sound field distributes and other processing condition, under these conditions processed material is carried out the acoustic energy processing treatment, make processed material generation corresponding mechanics effect, or calorifics effect, or chemical effect, or biological effect, or the caused variation of above multiple effect, reach the purpose that acoustic energy is processed.
" the fluid dynamic type sound energy producer is to be propulsion source with the fluid, utilizes adjustment liquid or high-speed gas to produce audible sound and ultransonic producer.Distinct advantages be simple in structure, cost is low, treatment capacity is big, and is easy to operate, durable in use, 7. " and the more important thing is it " it is little to consume energy, and propulsion source is convenient, thereby is well suited for industrial application.8. " though in theory the fluid dynamic type sound energy rattler have above-mentioned 7 kinds of advantages, develop must cross over from the possibility of theory and reach distance between the technology feasibility as fluid dynamic type sound energy coal slurry industry of the present invention.
" the fluid dynamic type sound energy rattler has demonstrated its distinct advantages aspect industrial application at present, shows its huge vitality.Yet, because ... the mathematics manipulation that wherein relates to is difficulty very, thereby so far ... sound generating mechanism does not also obtain comparatively gratifying explanation, and most research only limits to analysis of experimental phenomena.In a series of application, mainly result and the characteristic trend that provides based on the empirical curve of experimental formula and concrete different situation considers a problem.Require for reality, the acoustic characteristic that theoretic accurate indication is relevant with calculating distributes or the like as frequency, intensity, sound field, can more help its application and control undoubtedly.Thereby the generation of convection cell power rattler sound wave and the further research of feature are to be worth the deeply research direction of discussion from now on.⑨”
Above-mentioned " about acoustic energy " notes content partly draws from answering Chong Fu to show " ultrasonics " book: 7. ... draw from the 495th page of chapter 7 the 7.3rd joint; 8. ... draw from the 506th page of chapter 7 7.3.6 joint; 9. ... draw from the 506th page of chapter 7 7.3.6 joint." ultrasonics " publish for Chinese science press; No. 092, [capital] Xindeng word; The second impression in December, 1993 of first version in December nineteen ninety.
Claims (7)
1, a kind of desalination treatment system that utilizes fluidics, it is characterized in that: it comprises filtration unit, the acoustic energy treatment unit, desalting equipment three parts, consisting of of filtration unit: seawater acquisition port (1), connect sea-water pump (2), sea-water pump (2) connects coarse filtration device (3), and the outlet of coarse filtration device (3) connects the inlet of fine filtering apparatus (4); The outlet of fine filtering apparatus (4) connects acoustic energy treatment unit (6), and last step acoustic energy treatment unit connects subset seawater tank (7), and tank (7) connects reverse osmosis membrane (9) by pump (8), connects fresh-water pool (10) by pipeline.
2, the desalination treatment system that utilizes fluidics according to claim 1 is characterized in that: described reverse osmosis membrane (9) can be substituted by distiller.
3, the desalination treatment system that utilizes fluidics according to claim 1 is characterized in that: described acoustic energy treatment unit (6) is the combination of one-level to multistage liquid sonic-energy producer (11); Liquid sonic-energy producer (11) is a metallic cavity, comprises that cavity and upper and lower axocoel are formed in one; The axle center of the upper/lower terminal face of upper and lower axocoel is provided with co-axial two outlets, is evenly distributed with inlet on the middle cavity.
4, the desalination treatment system that utilizes fluidics according to claim 1 is characterized in that: the inlet that distributes on the cavity in described is 4-40.
5, the desalination treatment system that utilizes fluidics according to claim 1 is characterized in that: described inlet is the inclined hole of following current body trend, and the angle of this inlet axis and cylindrical tangent line is 30 °-90 °.
6, the desalination treatment system that utilizes fluidics according to claim 1 is characterized in that: the ratio of described inlet aperture and outlet aperture is 100: 1-20.
7, the desalination treatment system that utilizes fluidics according to claim 1 is characterized in that: the diameter ratio of the root diameter of axocoel and middle cavity is 1 on described liquid sonic-energy producer (11) inner chamber: 1-5.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2006201154154U CN2895406Y (en) | 2006-05-16 | 2006-05-16 | Sewater desalting system utilizing jet technology |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2006201154154U CN2895406Y (en) | 2006-05-16 | 2006-05-16 | Sewater desalting system utilizing jet technology |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2895406Y true CN2895406Y (en) | 2007-05-02 |
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| Application Number | Title | Priority Date | Filing Date |
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| CNU2006201154154U Expired - Fee Related CN2895406Y (en) | 2006-05-16 | 2006-05-16 | Sewater desalting system utilizing jet technology |
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| Country | Link |
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| CN (1) | CN2895406Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2009062364A1 (en) * | 2007-11-13 | 2009-05-22 | Xiaohua Xu | A seawater desalination system using cavitating jet technique |
| WO2016161862A1 (en) * | 2015-04-08 | 2016-10-13 | 李岳桓 | Ore composition, and water generator and seawater desalination equipment made therefrom, and method for generating small molecule water |
-
2006
- 2006-05-16 CN CNU2006201154154U patent/CN2895406Y/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2009062364A1 (en) * | 2007-11-13 | 2009-05-22 | Xiaohua Xu | A seawater desalination system using cavitating jet technique |
| WO2016161862A1 (en) * | 2015-04-08 | 2016-10-13 | 李岳桓 | Ore composition, and water generator and seawater desalination equipment made therefrom, and method for generating small molecule water |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: BEIJING GUANGHUI XIAOMING SOUND ENERGY TECHNOLOGY Free format text: FORMER OWNER: XU XIAONING Effective date: 20071109 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20071109 Address after: 100097, Haidian District building, No. 1, building 1, Jin Zhuang hospital, Beijing, Patentee after: Beijing Guanghui Xiaoming Sound Energy Technology Institute Address before: 100089 Beijing city Haidian District landianchang Century City fine snow Park No. 6 Building 3 unit 1D Patentee before: Xu Xiaoning |
|
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20070502 Termination date: 20120516 |