CN203625073U - Seawater desalination system - Google Patents
Seawater desalination system Download PDFInfo
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- CN203625073U CN203625073U CN201320854215.0U CN201320854215U CN203625073U CN 203625073 U CN203625073 U CN 203625073U CN 201320854215 U CN201320854215 U CN 201320854215U CN 203625073 U CN203625073 U CN 203625073U
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- seawater
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- desalination system
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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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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model relates to a seawater desalination system, and particularly relates to the seawater desalination system capable of increasing seawater distillation efficiency. The seawater desalination system comprises a seawater inlet for introducing seawater, a concentrated seawater outlet and a heating device and is characterized in that seawater enters from the seawater inlet, the seawater inlet is connected to a heating side of the heating device, the heating side is communicated with an evaporator which is also connected to a steam discharge port and a concentrated seawater discharge port, a porous medium material in contact with the seawater is arranged in the evaporator, and a part of seawater is evaporated into steam which is discharged from the steam discharge port; and the other part of concentrated seawater is discharged from the concentrated seawater discharge port. The seawater desalination system has the beneficial effects that as the porous medium material with super-large specific surface area is arranged in the evaporator, when the porous medium material is in contact with the seawater, an air layer is formed on the surface, which is in contact with the seawater, of the porous medium material, the distillation area of the seawater is enlarged through the porous medium material, and the distillation amount of the seawater in unit time is also increased.
Description
Technical field
The utility model relates to a kind of seawater desalination system, specifically a kind of seawater desalination system that improves sea water by distillation efficiency.
Background technology
On the earth, about 97% water resources is seawater, and other 2% from glacier, the day by day written global strategic resource problem of the shortage of water resources, and in order to solve water resources growing tension, countries in the world turn to ocean sight, carry out the research of sea water desaltination.And the stock number of desalination water per capita of China is only world occupancy volume per person's 1/4, come the 121st, the world, united state classifies one of 13 Ge poor-water states as.Utilizing seawater is one of important measures that solve China's water resources crisis.Wanting water to sea is to solve coastal (coastal waters) and island, and the Freshwater resources such as ship lack the reality of field lack of water and select.The main method of sea water desaltination at present has distillation method, embrane method, cold method etc.Wherein distillation method mainly contains multistage flash evaporation method, multiple-effect distillation, the distillation method of calming the anger, solar distilling method etc.; Embrane method mainly comprises reverse osmosis, electroosmose process etc.Although method for desalting seawater is a lot, at present real form industry size only have multistage flash evaporation method, multiple-effect distillation, vapour compression method and reverse osmosis method.Every kind of method has deficiency, exist complex process, energy consumption large, produce that water water quality inferiority, inconvenient operation, easily fouling, operation cost are high, unstable etc. the problem of producing water ratio.Need one to realize easy, effectively improve the seawater desalination system of evaporation of seawater efficiency and heat utilization rate.
Summary of the invention
The deficiency existing for traditional method for desalting seawater, realize efficient distillation seawater desalination, invest little, operation cost is low, water rate is stable, unharmful substance discharge, less energy-consumption, without consuming a large amount of electric energy texts, the utility model provides a kind of sea water desalinating plant, comprise the seawater entrance of introducing seawater, concentrated seawater outlet and heating unit, it is characterized in that: described seawater enters from described seawater entrance, described seawater entrance is connected to the hot side that obtains of heating unit, described that hot side is communicated to vaporizer, this vaporizer is also connected with steam outlet and concentrated seawater relief outlet, in described vaporizer, be provided with the porous media material with contact with sea water, part evaporation of seawater becomes water vapour to discharge from described steam outlet, another part concentrated seawater is discharged from described concentrated seawater outlet.
The vapor exhaust outlet of described vaporizer is connected with vacuum unit, and this vacuum unit makes vaporizer and water vapour drain passageway keep vacuum.
Described vaporizer comprises jet valve, and described seawater, through squirt pump pressurised driving, is injected in described porous media material from described jet valve; Or described vaporizer comprises jet valve, described seawater, through squirt pump pressurised driving, sprays in reallocation orifice plate from described jet valve, drops onto on described porous media material through reallocation orifice plate.
Between described vacuum unit and the outlet of the vapor exhaust of vaporizer, be also provided with condenser, described seawater entrance is connected to the hot side that obtains of condenser, is somebody's turn to do to such an extent that hot side seawater relief outlet is connected to described heating unit; The heat radiation side of described condenser contacts with water vapour and forms condensation fresh water, and this condensation fresh water drains into fresh-water tank through fresh water pump.
Described seawater entrance and heating unit obtain between hot side and are also connected with preheater, and described seawater entrance is connected to the hot side that obtains of preheater, are somebody's turn to do to such an extent that hot side seawater relief outlet is connected to described heating unit; The heat radiation side of described preheater is communicated with the outlet of vaporizer concentrated seawater and concentrated seawater outlet.
Described seawater entry sequence connection condenser obtains hot side, preheater obtains hot side and described heating unit obtains hot side, to vaporizer seawater entrance, and water vapor condensation heat radiation in described condenser; The heat radiation side of described preheater is communicated with the outlet of vaporizer concentrated seawater and concentrated seawater outlet.
The heated side of described heating unit is the hot-fluid that hot-fluid pump drives; Or the heated side of described heating unit is solar energy collector.Between described condenser and seawater entrance, be connected with strainer.
Vaporizer of the present utility model is connected with condenser, and the top of condenser connects vacuum unit by pipeline, makes to obtain certain vacuum tightness in condenser and vaporizer by vacuum unit, forms negative pressure.In vaporizer, adopting lower pressure is for reducing the saturated vapor pressure of seawater, thereby under lower temperature and lower pressure, seawater just can evaporate rapidly, reduces the energy expenditure of whole process, increase steam output, the fresh water yield of raising system.
Brief description of the drawings
Fig. 1 is the seawater desalination system system diagram of a kind of embodiment of the utility model;
Fig. 2 is the system diagram of the seawater desalination system of the another kind of embodiment of the utility model.
In figure: 1-vaporizer, 2-condenser, 3-heating unit, 4-preheater, 5-fresh-water tank, 6-strainer, 7-vacuum unit, 8-hot-fluid pump, 9-brinepump, 10-fresh water pump, 11-seawater entrance, the outlet of 12-strong brine, 13-hot-fluid entrance, the outlet of 14-hot-fluid, 15-porous media material material, 16-spray jet, 17-reallocation orifice plate, 18-squirt pump, 19-solar energy collector, 20-steam outlet.
Specific embodiment
Below in conjunction with embodiment and accompanying drawing thereof, the utility model is described in further detail; but embodiment of the present utility model is only the description that embodiment of the present utility model is carried out; not scope of the present utility model is defined; do not departing under the prerequisite of the utility model design spirit; various distortion or improvement that the common engineering technical personnel in this area make the technical solution of the utility model, within all should falling into the definite protection domain of claims of the present utility model.
As shown in Figure 1, the utility model provides a kind of seawater desalination system, comprise the seawater entrance 11 of introducing seawater, concentrated seawater outlet 12 and heating unit 3, described seawater enters from described seawater entrance 11, described seawater entrance 11 is connected to the hot side that obtains of heating unit 3, described that hot side is communicated to vaporizer 1, this vaporizer 1 is also connected with steam outlet 20 and concentrated seawater relief outlet 12, in described vaporizer 1, be provided with and the porous media material 15 of contact with sea water, a part of evaporation of seawater becomes water vapour to discharge from described steam outlet 20; Another part concentrated seawater is discharged from described concentrated seawater outlet 12.Concentrated seawater is by the concentrated seawater pump 9 discharge system of pressurizeing, and seawater squirt pump 18 sucks seawater from seawater entrance 11, absorb heat, and pressurization is injected in vaporizer 1 through heating unit 3.In the present embodiment, heating unit 3 adopts solar energy collector 19 as thermal source, and the thermal medium after solar energy collector 19 heating enters heating unit 3 from hot-fluid entrance 13, and the thermal medium after heat radiation returns to solar energy collector 19 from hot-fluid outlet 14.It will be understood by those skilled in the art that, the effect of heating unit 3 is that the seawater to entering heats, and reaching suitable temperature, concrete type of heating can have various ways, such as adopting electrically heated or directly heating with the heating part of solar energy collector.Adopt in the present embodiment thermal medium as middle heat transferring medium, and adopt hot-fluid pump 8 to drive, make heating efficiency can not be subject to the position influence of heating unit 3, solar energy collector 19 can adopt a lot of groups, thereby is applied to larger seawater desalination system.
Further, in vaporizer 1, be provided with porous media material 15 adsorbing seawaters of super large specific surface area, the surface of itself and contact with sea water forms one deck gas-bearing formation, increases the distillation area of seawater by porous media material, has also just increased the distillation amount of seawater unit time.For whole system, also reduce the start-up temperature of system operation, favourable for the scope of application that improves system.
Further, vaporizer 1 comprises jet valve 16, and seawater, through squirt pump 18 pressurised driving, is injected in described porous media material from above-mentioned jet valve 16.Adopt this kind of form can strengthen the granulation degree of seawater, the surface-area of increase seawater, for contacting preparatory condition with porous media material, improves the distillation efficiency while contact with porous media material.
Another kind of embodiment of the present utility model, the vapor exhaust outlet 20 of vaporizer 1 is connected with vacuum unit 7, and this vacuum unit 7 makes vaporizer 1 and water vapour drain passageway keep vacuum.In vaporizer 1, be airtight with water vapour path, vacuum unit 7 can be vacuum pump or fan etc., can in vaporizer 1, form lasting vacuum tightness, when seawater evaporates after water vapour in vaporizer, water vapour can push original air and is discharged to outside system by vacuum unit 7.Adopt vacuum unit 7 can effectively reduce the steam partial pressure in vaporizer 1, improve the efficiency that evaporation of seawater becomes water vapour, reduce the vaporization temperature of seawater, seawater is evaporated under low-temperature reduced-pressure state, particularly be combined with the super large surface-area of porous media material, water molecules desorption and evaporating on porous media material material, thus the steam output of unit time increased, can significantly improve fresh water productive rate.Concrete vacuum unit 7 is connected to vaporizer 1 as shown in Figure 2, and the gas in vaporizer 1 aspirates through vacuum unit 7, is discharged to outside system.
Another kind of embodiment of the present utility model, shown in Fig. 2, is also provided with condenser 2 between the vapor exhaust of vacuum unit 7 and vaporizer 1 outlet 20, seawater entrance 11 be connected to condenser 2 hot side, be somebody's turn to do to such an extent that the seawater relief outlet of hot side is connected to heating unit 3; The heat radiation side of condenser 2 contacts with water vapour and forms condensation fresh water, and this condensation fresh water drains into fresh-water tank 5 through fresh water pump 10.Between condenser 1 and seawater entrance 11, be connected with strainer 6.The pollutent that adopts this strainer 6 can reduce in seawater enters into system.Can improve the temperature of seawater by condenser 1 is set, reduce the energy expenditure at heating unit place, can improve the efficiency of whole system simultaneously.In addition, seawater temperature is lower, and necessarily the variation throughout the year of the seawater temperature below the depth of water is less, can condensation form stable condensation fresh water.Can reduce the steam partial pressure in the vacuum area that vaporizer 1 is communicated with condenser heat radiation side by the heat radiation side of condenser, and the temperature of seawater has determined the steam partial pressure size that condenser heat radiation side can form, the heat-sinking capability of condenser has determined the size of fresh water generative capacity.The fresh water of gained is transported to fresh-water tank 5 by fresh water pump 10 herein.Adopt condenser that seawater minimum temperature in system is heated, water vapour goes out fresh water to seawater heat radiation condensation simultaneously, realizes the object of sea water desaltination.
Another one object of the present utility model is to provide a kind of seawater desalination system control method, seawater desalination system comprises the seawater entrance of introducing seawater, concentrated seawater outlet and heating unit, wherein, seawater enters from described seawater entrance, seawater entrance is connected to the hot side that obtains of heating unit, be somebody's turn to do to such an extent that hot side is communicated to vaporizer, this vaporizer is also connected with steam outlet and concentrated seawater relief outlet, in vaporizer, be provided with and the porous media material of contact with sea water, a part of evaporation of seawater becomes water vapour to discharge from described steam outlet; Another part concentrated seawater is discharged from described concentrated seawater outlet.Also comprise the vacuum mechanism of the vapor exhaust outlet that is connected to vaporizer, this vacuum mechanism makes vaporizer and water vapour drain passageway keep vacuum.And be also provided with condenser between the outlet of the vapor exhaust of this vacuum mechanism and vaporizer, vaporizer and condenser form the space of relative sealing, the space of the relative sealing here refers to not have outside air to enter in this space, once after vacuumizing, only have the water vapour in vaporizer to result from this space, seawater entrance is connected to the hot side that obtains of condenser, is somebody's turn to do to such an extent that hot side seawater relief outlet is connected to heating unit; The heat radiation side of condenser forms condensation fresh water and drains into fresh-water tank through fresh water pump.And form the space of relative sealing at vaporizer and condenser, control method order comprises following steps:
A, unlatching vacuum mechanism form vacuum in vaporizer and condenser;
B, form after fresh water when continuing in condenser, close vacuum pump.
Step a, air in the space of the relative sealing that vaporizer and condenser form is constantly discharged to outside system by vacuum unit, along with the lasting generation of water vapour, the main gas in space is water vapour, and the meeting that affects of the condensation of air on water vapour significantly reduces;
Step b, when the air in the space of relative closure be reduced to very low, the generation fresh water that can be easy to continue, at this time, condenser becomes the parts of main reduction steam partial pressure, can close vacuum pump, because the main gas that at this moment vacuum pump is discharged is water vapour, it can be a kind of waste.
Understandable, if vacuum deficiency situation while occurring, still can open again vacuum unit and meet the needs of fresh water processing.
Another embodiment of the present utility model, as shown in Figure 2, obtaining between hot side of seawater entrance 11 and heating unit 3 is also connected with preheater 4, and seawater entrance 11 is connected to the hot side that obtains of preheater 4, is somebody's turn to do to such an extent that hot side seawater relief outlet is connected to described heating unit 3; The heat radiation side of this preheater is communicated with concentrated seawater outlet and the concentrated seawater outlet 12 of vaporizer 1.The concentrated seawater temperature of vaporizer 1 is higher, and directly the system of discharging can form larger thermal waste, also can form thermal pollution, by carrying out heat exchange with seawater, can improve on the one hand seawater and enter heating unit 3 temperature before, also reduce in addition outside discharges heat, reduce thermal pollution.Further, preheater 4 the hot side relief outlet that can obtain hot side with condenser is connected, can improve like this seawater temperature that obtains hot side that enters preheater 4, also improved preheater 4 the seawater temperature of hot side relief outlet, can further improve the seawater temperature that enters heating unit 3, improve the thermo-efficiency of system.
Another embodiment of the present utility model, as shown in Figure 2, vaporizer 1 comprises jet valve 16, seawater, through squirt pump 18 pressurised driving, sprays in reallocation orifice plate 17 from above-mentioned jet valve 16, drops onto on described porous media material 15 through reallocation orifice plate.Adopt this kind of form can strengthen the granulation degree of seawater; increase the surface-area of seawater; reallocation orifice plate 17 can be designed to be suitable for the form that porous media material coordinates; reallocate through orifice plate; it is scattered in above porous media material material below more equably, increases wet distillation efficiency.
Make as a whole scheme with Fig. 2 and see, seawater entrance 11 is linked in sequence, and condenser 2 obtains hot side, preheater 4 obtains hot side and heating unit 3 obtains hot side, to the seawater entrance of vaporizer 1, and water vapor condensation heat radiation in condenser 1; Be communicated with the outlet of vaporizer concentrated seawater and concentrated seawater outlet 12 in the heat radiation side of preheater 4.Can realize like this seawater by gradient-heated, thereby improve the thermo-efficiency of system, meanwhile, make water vapour obtain condensation, the discharge thermal pollution of concentrated seawater reduces, and the comprehensive utilization ratio of system is promoted.
Claims (8)
1. a seawater desalination system, comprise the seawater entrance of introducing seawater, concentrated seawater outlet and heating unit, it is characterized in that: described seawater enters from described seawater entrance, described seawater entrance is connected to the hot side that obtains of heating unit, and described that hot side is communicated to vaporizer, this vaporizer is also connected with steam outlet and concentrated seawater relief outlet, in described vaporizer, be provided with and the porous media material of contact with sea water, a part of evaporation of seawater becomes water vapour to discharge from described steam outlet; Another part concentrated seawater is discharged from described concentrated seawater outlet.
2. seawater desalination system according to claim 1, is characterized in that: the vapor exhaust outlet of described vaporizer is connected with vacuum unit, and this vacuum unit makes vaporizer and water vapour drain passageway keep vacuum.
3. seawater desalination system according to claim 1, is characterized in that: described vaporizer comprises jet valve, and described seawater, through squirt pump pressurised driving, is injected in described porous media material from described jet valve; Or described vaporizer comprises jet valve, described seawater, through squirt pump pressurised driving, sprays in reallocation orifice plate from described jet valve, drops onto on described porous media material through reallocation orifice plate.
4. seawater desalination system according to claim 2, it is characterized in that: between described vacuum unit and the outlet of the vapor exhaust of vaporizer, be also provided with condenser, described seawater entrance is connected to the hot side that obtains of condenser, is somebody's turn to do to such an extent that hot side seawater relief outlet is connected to described heating unit; The heat radiation side of described condenser contacts with water vapour and forms condensation fresh water, and this condensation fresh water drains into fresh-water tank through fresh water pump.
5. seawater desalination system according to claim 1, it is characterized in that: described seawater entrance and heating unit obtain and between hot side, be also connected with preheater, described seawater entrance is connected to the hot side that obtains of preheater, is somebody's turn to do to such an extent that hot side seawater relief outlet is connected to described heating unit; The heat radiation side of described preheater is communicated with the outlet of vaporizer concentrated seawater and concentrated seawater outlet.
6. seawater desalination system according to claim 2, it is characterized in that: described seawater entry sequence connection condenser obtains hot side, preheater obtains hot side and described heating unit obtains hot side, to vaporizer seawater entrance, water vapor condensation heat radiation in described condenser; The heat radiation side of described preheater is communicated with the outlet of vaporizer concentrated seawater and concentrated seawater outlet.
7. according to the seawater desalination system described in any one in claim 1-6, it is characterized in that: the heated side of described heating unit is the hot-fluid that hot-fluid pump drives; Or the heated side of described heating unit is solar energy collector.
8. seawater desalination system according to claim 7, is characterized in that: between described condenser and seawater entrance, be connected with strainer.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201320854215.0U CN203625073U (en) | 2013-12-24 | 2013-12-24 | Seawater desalination system |
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| CN201320854215.0U CN203625073U (en) | 2013-12-24 | 2013-12-24 | Seawater desalination system |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104150548A (en) * | 2013-12-24 | 2014-11-19 | 北京大学工学院包头研究院 | Sea water desalination system |
| CN104628067A (en) * | 2014-12-26 | 2015-05-20 | 皇明太阳能股份有限公司 | Solar-powered seawater desalination device, stove combined device and using method thereof |
| CN114604921A (en) * | 2022-02-22 | 2022-06-10 | 广东南大机器人有限公司 | Seawater desalination system |
-
2013
- 2013-12-24 CN CN201320854215.0U patent/CN203625073U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104150548A (en) * | 2013-12-24 | 2014-11-19 | 北京大学工学院包头研究院 | Sea water desalination system |
| CN104150548B (en) * | 2013-12-24 | 2016-06-22 | 北京大学包头创新研究院 | A kind of seawater desalination system |
| CN104628067A (en) * | 2014-12-26 | 2015-05-20 | 皇明太阳能股份有限公司 | Solar-powered seawater desalination device, stove combined device and using method thereof |
| CN114604921A (en) * | 2022-02-22 | 2022-06-10 | 广东南大机器人有限公司 | Seawater desalination system |
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| 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: 20140604 Termination date: 20201224 |