TW202302469A - Seawater separation system wherein seawater storage tanks are distributed around the separation cavity of the seawater separation system - Google Patents

Abstract

The present invention relates to a seawater separation system. Seawater storage tanks are distributed around a separation cavity of the seawater separation system. The separation cavity is provided with a suspended nozzle of a gasification cavity. Above the gasification cavity is a salt-proof chamber formed by a salt-proof guide ring. The salt-proof chamber is connected with a condensation connection pipe. The seawater storage tanks contain seawater. A pressurized pump is distributed around a seawater delivery device to connect the seawater storage tank and to suck the seawater into a pressurized cavity. A first heater is attached to the exterior of the pressurized cavity. The pressurized cavity is connected to the pressurized chamber. Condensation cavities are distributed around a freshwater collection device. The condensation cavities are provided with a condenser. The condenser communicates with a heat exchanger. The side of the condensation cavities is connected with the condensing pipe, and the lower side of the condensation cavities is connected with a freshwater output pipe. The lower end of the freshwater output pipe is connected with a freshwater collection tank.

Description

Sea water separation system

The present invention is a seawater separation system, wherein, the seawater separation system is provided with a separation cavity, and a nozzle is arranged in the separation cavity, and the nozzle sprays high-temperature and high-pressure seawater in the separation cavity to vaporize the fresh water contained in the seawater. A person in the technical field of salt separation.

The first press refers to the fact that the current climate is becoming more and more extreme, floods and droughts are uncertain, and the area covers a wide range of days, resulting in endangering personal safety and extensive property losses. Among them, droughts are caused by little or no rain for a long time. The situation is: there is no supply of domestic water, which endangers the survival and sanitation of the environment, and the suspension of agricultural planting, resulting in food shortage and famine accompanied by food crisis. Therefore, areas near the sea have begun to turn to seawater desalination to supply people's livelihood and Agricultural, industrial and commercial use.

At present, desalination of seawater is the process of removing salt and minerals from seawater and retaining only fresh water. Among them, the current mainstream is the high-efficiency filtration of seawater desalination using membrane treatment reverse osmosis systems; The thermal cycle system cooperates with the heating of seawater to evaporate and vaporize the fresh water part, and the vaporized fresh water is condensed to become usable fresh water; or the technology of freezing the sea water to freeze the fresh water part, and discharge the salt and minerals out of the ice at the same time as freezing . However, although the above-mentioned membrane treatment reverse osmosis system is efficient, the facilities are huge and expensive, the driving cost of seawater pressurization and the replacement cost of filtration facilities are also high, and the recovery and reuse of salt and minerals in the filtration facilities has limited benefits. However, if the thermal cycle system is to achieve high efficiency and cost control, it has to be attached to thermal power and nuclear power plants and waste incinerators, making it difficult to implement independently under such high heat consumption. Frozen seawater, on the other hand, is The power consumption is too large, and the manufacturing process has a very long time limit, and the actual application effect needs to be evaluated. Therefore, it can be seen that the current seawater desalination has the problem of high cost, which needs to be improved.

In view of the above-mentioned fact that known seawater desalination has the problem of high cost, therefore, the inventor of this case is urged to research and develop in the direction of cost reduction, and after thinking about it in many ways, the inventor of this case thinks, using the method of high temperature spraying and high pressure Sea water is the best.

The seawater separation system of the present invention is distributed with a separation cavity, and the periphery of the separation cavity is distributed with: a seawater storage tank, a seawater delivery device and a freshwater collection device. A gasification chamber is arranged in the separation chamber, and a suspended spray head is distributed in the gasification chamber. The spray head is provided with a downward nozzle, and the spray head is connected with a seawater input pipe penetrating the separation chamber. The separation cavity is provided with an upward and inwardly retracted salt-proof guide ring above the gasification chamber. The salt-proof guide ring forms a salt-proof space above the gasification chamber. The salt-proof space is connected with a transparent Condensation tube out of the separation chamber. At least one salt collection tank is provided under the gasification chamber, and at least one collection tank valve for closing and opening the salt collection tank is provided in the gasification chamber. The seawater storage tank contains seawater, and the surrounding of the seawater conveying device is distributed with: a pressurized pump and a pressurized chamber. The pressurized pump is connected with the seawater storage tank, and the pressurized pump absorbs the seawater contained in the seawater storage tank into the pressurized chamber, and the pressurized chamber has a chamber inside which accommodates the seawater absorbed by the pressurized pump. A first heater is attached to the outside of the pressurized seawater pressurized chamber, and a first solenoid valve is connected to the pressurized chamber to prevent the seawater from backflowing back to the pressurized pump. The pressurized chamber is connected with the seawater input pipe communicating with the pressurized chamber, and the seawater input pipe is provided with a second device between the pressurized chamber and the separation chamber to prevent the seawater from flowing back into the pressurized chamber. Two solenoid valves. Distributed around the fresh water collection device are: a condensation chamber and a heat exchanger. There is a condensation chamber inside the condensation chamber, and a condenser is arranged in the condensation chamber, and the condenser reveals the condensation The heat exchanger is communicated with the outside of the cavity, the side of the condensation cavity is connected with the condensation connecting pipe connected with the condensation chamber, the lower side of the condensation cavity is connected with the fresh water output pipe connected with the condensation chamber, and the lower end of the fresh water output pipe is Connected to a fresh water collection tank.

The seawater separation system of the present invention is distributed with a heat medium heating device, and the heat medium heating device is provided with a medium oil cavity, and a medium oil chamber is arranged inside the medium oil cavity, and the medium oil chamber accommodates the medium oil, the medium oil Distributed outside the cavity are: a first medium oil pump, a second medium oil pump and a third medium oil pump. The first medium oil pump is provided with a first dip tube extending into the medium oil chamber to absorb the medium oil. The first medium oil pump is connected in series with a medium oil heater distributed by the heat medium heating device. The medium oil The heater is additionally equipped with a solar heat collecting umbrella, and the heat medium heating device uses the concentrated light of the solar heat collecting umbrella to heat the heat collector connected with the center of the solar heat collecting umbrella facing upwards. The medium heat collection chamber, the medium oil heater is provided with an oil medium connecting pipe connected in series with the heat collector, and the last oil medium heat collector is connected with the first medium oil return flow that circulates the medium oil back to the oil medium chamber Tube. The second medium oil pump is provided with a second dip tube extending into the medium oil chamber to absorb the medium oil. A second heater attached to the separation chamber is distributed around the separation chamber. The second heater is provided with a second heat medium circulation pipe attached to the separation chamber. The heater is connected to the second heat medium conduit of the second medium oil pump, and the second heat medium circulation pipe leads to a second heat medium return pipe that passes through the second heater and connects with the medium oil chamber. The third medium oil pump is provided with a third dip tube extending into the medium oil chamber to absorb the medium oil. The first heater attached to the outside of the pressurized chamber is provided with a third heat medium circulation pipe surrounding the pressurized chamber, and the third heat medium circulation pipe is connected to the first heater connected to the first The third heat medium conduit of the three-medium oil pump, and the third heat medium circulation pipe leads to a third heat medium return pipe that passes through the first heater and connects to the medium oil chamber.

The first heater of the present invention is provided with a first electric heater that surrounds the pressurized chamber. strip. A third heater attached around the separation chamber is distributed, and the third heater is provided with a second electric heating strip attached to the separation chamber. The seawater separation system is distributed with green energy generators, and the electricity generated by the green energy generators is stored in a storage battery, and the electricity generated by the green energy generators is supplied to the first electric heating strip and the second electric heating strip through the storage battery , and the electricity stored in the storage battery is supplied to the seawater separation system.

The main purpose of the present invention is: the pressurized pump absorbs the seawater contained in the seawater storage tank into the pressurized chamber, the pressurized chamber has the first heater outside, and the pressurized chamber sprays water through the nozzle. The heated seawater enters the separation chamber to be vaporized, and the vaporization is connected to the condensation connection pipe in the salt-proof space. The gasification chamber is hung with a spray head, which is provided with a downward facing nozzle. The spray head is connected with the seawater input pipe to enter the fresh water collection device, and the rest enters the salt particle collection tank.

Another object of the present invention is: the seawater separation system is distributed with the heat medium heating device, the heat medium heating device is provided with the medium oil cavity, the medium oil cavity is provided with the medium oil chamber, and the medium oil chamber accommodates There is medium oil, the first medium oil pump outside the medium oil chamber sucks the medium oil into the heat collector of the medium oil heater, and the solar heat collecting umbrella concentrates light to heat the heat collector, the The medium oil circulating inside the heat collector is circulated back to the oil medium chamber through the first medium oil return pipe, and the medium oil is sucked to the second heater of the separation cavity through the second medium oil pump. The substantial benefit of the first heater outside the pressurized cavity is that the medium oil is sucked by the third medium oil pump.

Another object of the present invention is that: the third heater is provided with the second electric heating bar surrounding the separation cavity, the seawater separation system is distributed with the electricity generated by the green energy generator stored in the battery, and the green energy power generation The electricity generated by the device is supplied to the substantial benefit of the seawater separation system through the storage battery.

〔this invention〕

A: seawater

A1: fresh water

A2: Salt granules

B: kerosene

C: Green energy generator

C1: battery

C2: solar panel

C3: wind turbine

C4: Hydroelectric Generator

1: Sea water separation system

11: Separation cavity

12: Gasification chamber

13: Nozzle

131: Nozzle

132: Seawater input pipe

14: Anti-salt guide ring

141: Anti-salt space

142: Condensation pipe

15: Salt collection tank

151: collection tank valve

16: Second heater

161: Second heat medium circulation pipe

162: Second heat medium conduit

163: Second heat medium return pipe

2: Sea water storage tank

3: Sea water delivery device

31: Booster pump

32: pressurized cavity

33: Pressurized chamber

34: First heater

341: The third heat medium circulation pipe

342: The third heat medium conduit

343: The third heat medium return pipe

35: The first solenoid valve

36: Second solenoid valve

4: Fresh water collection device

41: condensation cavity

411: condensation chamber

412: condenser

42: heat exchanger

43:Fresh water output pipe

44:Fresh water collection tank

5: Heat medium heating device

51: Medium oil cavity

511: Medium Oil Room

512: The first medium oil pump

5121: first dip tube

513:Second medium oil pump

5131: Second dip tube

514: The third medium oil pump

5141: third dip tube

52: Medium Oil Heater

521: Solar umbrella

522: Collector

5221: oil medium heat collector

5222: oil medium connecting pipe

523: The first medium oil return pipe

[Fig. 1] is a schematic diagram of the seawater separation system of the present invention.

[Figure 2] is a schematic diagram of the use of the seawater separation system of the present invention.

[Fig. 3] is another schematic diagram of the seawater separation system of the present invention.

[Fig. 4] is a schematic diagram of a green energy power generation device in the seawater separation system of the present invention.

In order to make your examiners have a further understanding of the present invention, the following examples are hereby described.

The present invention refers to a seawater separation system 1, wherein, the seawater separation system 1 is distributed with a separation cavity 11, and the periphery of the separation cavity 11 is at least distributed with: a seawater storage tank 2, a seawater delivery device 3 and a Fresh water collection device4. The separation chamber 11 is provided with a gasification chamber 12, the gasification chamber 12 is distributed with a suspended nozzle 13, the nozzle 13 is provided with a downward nozzle 131, and the nozzle 13 is connected with a 11 seawater input pipe 132. The separation cavity 11 is provided with an upward and retracted salt-proof guide ring 14 above the gasification chamber 12, and the salt-proof guide ring 14 forms a salt-proof space 141 above the gasification chamber 12. The salt space 141 is connected with a condensation connecting pipe 142 penetrating through the separation cavity 11 . At least one salt collection tank 15 is provided under the gasification chamber 12 , and the gasification chamber 12 is provided with at least one collection tank valve 151 for closing and opening the salt collection tank 15 . The seawater storage tank 2 contains seawater A, and at least around the seawater conveying device 3 are: a pressurization pump 31 and a pressurization cavity 32 . The pressurized pump 31 is connected with the seawater storage tank 2, and the pressurized pump 32 sucks the seawater A contained in the seawater storage tank 2 into the pressurized cavity 32, and the pressurized cavity 32 has a The pressurization chamber 33 of the seawater A sucked and pressurized by the pressurization pump 31, the A first heater 34 is attached to the outside of the pressurized chamber 32 , and the pressurized chamber 32 is connected with a first solenoid valve 35 to prevent the seawater A from flowing back into the pressurized pump 31 . The pressurized chamber 32 is connected with the seawater input pipe 132 communicating with the pressurized chamber 33, and the seawater input pipe 132 is provided with a barrier between the pressurized chamber 32 and the separation chamber 11 to prevent the seawater A from flowing back. The second solenoid valve 36 of the pressurized cavity 32 . The fresh water collecting device 4 is at least distributed around: a condensing chamber 41 and a heat exchanger 42 . The condensing chamber 41 has at least one condensing chamber 411 inside, and a condenser 412 is arranged in the condensing chamber 411, and the condenser 412 communicates with the heat exchanger 42 through the condensing chamber 41, and the condensing chamber The side of 41 is connected with the condensation connection pipe 142 which communicates with the condensation chamber 411. The lower side of the condensation chamber 41 is connected with the fresh water output pipe 43 which communicates with the condensation chamber 411. The lower end of the fresh water output pipe 43 is connected with at least one fresh water collection tank 44. (As shown in Figure 1).

That is, the seawater separation system 1 first draws the seawater A contained in the seawater storage tank 2 into the pressurization chamber 33 of the pressurization chamber 32 according to the pressurization pump 31 to pressurize to a predetermined pressure value, and then Use the first heater 34 to heat the pressurized seawater A inside the pressurized chamber 32, and then open the second solenoid valve 36 to allow the seawater A to enter the seawater input pipe when the seawater A has reached a predetermined temperature 132, spray the high-pressure, high-temperature seawater A into the gasification chamber 12 through the nozzle 13 through the seawater input pipe 132 to vaporize the freshwater A1 part, and separate the salt and minerals into dry salt granules A2 . Part of the vaporized fresh water A1 floats up to the salt-proof space 141 and is cooled and condensed by the condenser 412 of the condensing chamber 41 to form the fresh water A1, and the fresh water A1 is collected into the fresh water collection tank 44 through the fresh water output pipe 43 . And the salt particle body A2 falls into the salt particle collection tank 15, cooperates with the closing and opening of the salt particle collection tank 15 of the collection tank valve 151 to process and discharge the salt particle body A2 (as shown in Figure 2) .

However, the parts of the seawater separation system 1 that can be changed arbitrarily at any time are: the added The number of pressurized chambers 32, the assembly of pressurized chambers 32 with different capacities, the internal pressure of the pressurized chambers 32, and the heating temperature of the first heater 34; so that the separated chambers 11 and The setting of the pressurized chamber 32 is beneficial to:

1. The pressurization pump 31 is used to pressurize the seawater A into the pressurization chamber 32, and can be adjusted arbitrarily in the small volume of the pressurization chamber 32 to maximize the pressurization effect of the seawater A.

2. The pressurized chamber 32 uses the first heater 34 to heat the pressurized seawater A, and the small volume of the pressurized chamber 32 can be adjusted arbitrarily to maximize the high-temperature heating effect of the seawater A.

3. After the seawater A is pressurized and heated at high temperature in the pressurized chamber 32 respectively, the spray head 13 sprays the vaporized fresh water A1 at a high speed in the limited space of the gasification chamber 12 inside the separation chamber 11 , and the pressurized chambers 32 in sequence take turns to continuously generate uninterrupted vaporization pressure in the limited space of the vaporization chamber 12, forcing the vaporized fresh water A1 to spray into the condensing chamber 41, and the condensing chamber 41 The evaporated fresh water A1 is cooled by the condenser 412 at a high speed and condensed into usable fresh water A1 , and the fresh water A1 is continuously collected into the fresh water collection tank 44 through the fresh water output pipe 43 . And the pressurized chamber 32, the separation chamber 11 and the condensation chamber 41 can be connected and laid in a small space to form the seawater separation system 1, and according to the pressurized chamber 32, the separation chamber 11 and the condensation chamber The combination of the cavity 41 enables the seawater separation system 1 to produce the fresh water A1 continuously and rapidly.

4. The number of the separation chambers 11 and the number of matching combinations of the pressurization chambers 32 can be changed according to the demand amount of the fresh water A1.

Afterwards, the conclusions drawn from 1 to 4 at least include: the pressurized chamber 32, the pressurized chamber 32 and the condensing chamber 41 are integrated into a seawater separation system 1 that efficiently and rapidly produces the fresh water A1, and The salt particles separated by the seawater separation system 1 in the gasification chamber 12 A2 can be completely collected and reused, so that the use of the seawater separation system 1 can ensure that the resources contained in the seawater A are not wasted (as shown in FIG. 2 ).

This seawater separation system 1 of the present invention is distributed with heat medium heating device 5 again, and this heat medium heating device 5 is additionally provided with a medium oil cavity 51, and this medium oil cavity 51 is provided with a medium oil chamber 511 again, and this medium oil chamber 511 also contains medium oil B, and the outside of the medium oil chamber 51 is distributed with: a first medium oil pump 512 , a second medium oil pump 513 and a third medium oil pump 514 . The first medium oil pump 512 is additionally equipped with a first dip tube 5121 extending into the medium oil chamber 511 to absorb the medium oil B, and the first medium oil pump 512 is connected in series with the medium distributed by the heat medium heating device 5 Oil heater 52, the medium oil heater 52 is additionally equipped with a solar heat collecting umbrella 521, and the heat medium heating device 5 is heated by the concentrated light of the sun heat collecting umbrella 521 and the heat collector connected upwardly by the center of the sun heat collecting umbrella 521 522, the inside of the heat collector 522 is provided with an oil medium heat collecting chamber 5221 for circulating the medium oil A, and the medium oil heater 52 is also provided with an oil medium connecting pipe 5222 connected in series with the heat collector 522, and the last The oil medium heat collector 52 is also connected with a first medium oil return pipe 523 that circulates the medium oil B back to the oil medium chamber 511 . The second medium oil pump 513 is additionally provided with a second dip tube 5131 extending into the medium oil chamber 511 to suck the medium oil A. The second heater 16 attached to the ring is also distributed around the separation chamber 11, and the second heater 16 is additionally provided with a second heat medium circulation pipe 161 attached to the separation chamber 11. The second heat medium circulation pipe 161 It is also connected to a second heat medium conduit 162 that penetrates the second heater 16 and connects to the second medium oil pump 513. The second heat medium return pipe 163 of the oil chamber 511. The third medium oil pump 514 is additionally provided with a third dipping tube 5141 extending into the medium oil chamber to absorb the medium oil. The first heater 34 attached to the outside of the pressurized chamber 32 is additionally provided with a third heat medium circulation pipe 341 surrounding the pressurized chamber 32. A heater 34 is connected to the third heat medium conduit 342 of the third medium oil pump 514, and the third heat medium circulation pipe 341 is connected to a connection through the first heater 34. The third heat medium return pipe 343 of the medium oil chamber 511 (as shown in FIG. 3 ).

That is, the heat medium heating device 5 first uses the first medium oil pump 512 to transport the medium oil B and continues to pass through the heat collector 522 to absorb the light concentrated by the solar heat collecting umbrella 521 for heating. While heating, heat is also continuously circulated to the medium oil chamber 511, so that the medium oil B continues to accumulate heat in the medium oil chamber 511 to increase the temperature. After the temperature of the medium oil B is thus raised, the The second medium oil pump 513 is delivered to the second heater 16 of the separation chamber 11 to assist the inside of the separation chamber 11 to maintain the stability of the condition in which the seawater A is sprayed and vaporized to produce the fresh water A1. In addition, after the temperature of the medium oil B is thus raised, it can be transported to the pressurized chamber 32 by the third medium oil pump 514 to heat the pressurized seawater A, forcing the pressurized seawater A The heat can be increased, which is beneficial for the seawater A to be rapidly vaporized and separated from the fresh water A1 when sprayed by the nozzle 13 in the vaporization chamber 12, and the separation chamber 11 can stabilize the separation of the seawater according to the second heater 16 The condition of the seawater A vaporized and separated from the fresh water A1 during the initial operation of the system 1, and when the temperature and vaporization pressure of the vaporization chamber 12 reach the sustainable operating conditions, the power of the second heater 16 can be reduced or reduced depending on the situation. Close the operation (such as: shown in Figure 3).

The first heater 34 of the present invention is additionally provided with a first electric heating strip 344 surrounding the pressurized cavity 32 . A third heater 17 attached around the separation cavity 11 is further distributed, and a second electric heating strip 171 attached to the separation cavity 11 is added to the third heater 17 . The seawater separation system 1 is also distributed with a green energy generator C, the power generated by the green energy generator C is stored in the additional storage battery C1, and the power generated by the green energy generator C is supplied to the first battery through the storage battery C1. The electric heating strip 344, the second electric heating strip 171, and the electric power stored in the battery C1 are then supplied to the seawater separation system 1 (as shown in FIG. 4 ).

Yes, the electric energy produced by the green energy generator C is supplied to all the electricity demands of the seawater separation system 1 through the storage battery C1, and the green energy generator C can at least include: Solar panels C2, wind generators C3 and hydroelectric generators C4 (as shown in Figure 4).

It can be seen from the above description that the seawater separation system 1 draws the seawater A into the pressurization chamber 33 according to the pressurization pump 31 to pressurize it to a predetermined pressure value, and then uses the first heater 34 to heat the pressurized seawater A to the predetermined temperature, then open the second solenoid valve 36 to make the seawater A spray into the gasification chamber 12 through the nozzle 13 to vaporize the fresh water A1 part, and the vaporized fresh water A1 part floats to the salt prevention space 141 passes through the condenser 412 of the condensing cavity 41 to cool and condense into the fresh water A1, and the fresh water A1 is collected into the fresh water collection tank 44 through the fresh water output pipe 43, and the separated salt and minerals are simultaneously dried into The salt granules A2 fall into the salt granule collection tank 15, and the first excellent feature of discharging the salt granule body A2 is handled by the closing and opening of the salt granule collection tank 15 of the collection tank valve 151.

Another excellent feature of the present invention is that: the seawater separation system 1 uses the arrangement of the separation chamber 11 and the pressurization chamber 32 to facilitate the pressurization pump 31 to transport the seawater A into the pressurization chamber 32 for pressurization, The effect of the predetermined pressure value of the seawater A inside the pressurized chamber 32 can be adjusted arbitrarily; the seawater A pressurized to a predetermined pressure value is assembled in the pressurized chamber 33 with the first A heater 34 performs heating to a predetermined temperature; after the seawater A is pressurized and heated in the pressurized chamber 32, the spray head 13 is sprayed at a high speed in the limited space of the gasification chamber 12 inside the separation chamber 11. The vaporized fresh water A1, and the pressurized chamber 32 according to the sequence continuously supply the seawater A to the vaporization chamber 12 to vaporize the fresh water A1 continuously, and the vaporized fresh water A1 is sprayed into the condensation chamber 41 to The condenser 412 rapidly cools down the fresh water A1 that can be used, and the fresh water A1 is continuously collected into the fresh water collection tank 44 through the fresh water output pipe 43 , which is a characteristic benefit of the present invention.

Another excellent feature of the present invention is: the heat medium heating device 5 heats the heat collector 522 and the medium oil B with the light concentrated by the solar heat collecting umbrella 521, and the medium oil B continues to circulate heat until the The medium oil chamber 511 raises the temperature of the medium oil B, and the temperature of the medium oil B is raised and sent to the second heater 16 of the separation chamber 11 by the second medium oil pump 513 to assist the separation The inside of the cavity 11 maintains the stability of the condition in which the fresh water A1 is vaporized by the spraying of the sea water A. In addition, the medium oil B can be transported to the pressurized chamber 32 by the third medium oil pump 514 to heat the seawater A that has been pressurized, forcing the seawater A to raise its temperature, and the spray head 13 can be used in the gasification chamber. 12 Spraying rapidly vaporizes and separates the fresh water A1. And according to the second heater 16 can stabilize the vaporization condition of the seawater A in the initial operation of the separation chamber 11, and when the temperature and vaporization pressure of the vaporization chamber 12 reach sustainable operation, the second heater 16 can see the situation Featured benefits for de-powering or shutting down operations.

Another excellent feature of the present invention is that: the electric energy produced by the green energy generator C is supplied to all the electricity demands of the seawater separation system 1 through the storage battery C1.

The technical content and technical characteristics of the present invention have been disclosed above. Accordingly, it can be seen that the present invention does meet the invention patent requirements of novelty, advancement and industrial applicability. Make various replacements and modifications without departing from the spirit of the invention. Therefore, the protection scope of the present invention should not be limited to those disclosed in the embodiments, but should include various replacements and modifications that do not deviate from the present invention, and are covered by the patent scope of the present invention.

A: seawater

1: Sea water separation system

11: Separation cavity

12: Gasification chamber

13: Nozzle

131: Nozzle

132: Seawater input pipe

14: Anti-salt guide ring

141: Anti-salt space

142: Condensation pipe

15: Salt collection tank

151: collection tank valve

2: Sea water storage tank

3: Sea water delivery device

31: Booster pump

32: pressurized cavity

33: Pressurized chamber

34: First heater

35: The first solenoid valve

36: Second solenoid valve

4: Fresh water collection device

41: condensation cavity

411: condensation chamber

412: condenser

42: heat exchanger

43:Fresh water output pipe

44:Fresh water collection tank

Claims (5)

A seawater separation system, wherein, the seawater separation system is provided with a separation cavity, and at least around the separation cavity are: a seawater storage tank, a seawater delivery device and a freshwater collection device; the separation cavity is provided with a A gasification chamber, the gasification chamber is distributed with a suspended nozzle, the nozzle is provided with a nozzle facing downwards, and the nozzle is connected with a seawater input pipe penetrating the separation chamber; the separation chamber is in the gasification chamber An upward and inwardly retracted salt-proof guide ring is provided above the chamber. The salt-proof guide ring forms a salt-proof space above the gasification chamber, and the salt-proof space is connected with a condensation connection pipe that penetrates the separation chamber; There is at least one salt collection tank below the gasification chamber, and at least one collection tank valve for closing and opening the salt collection tank is provided in the gasification chamber; the seawater storage tank contains seawater, and at least There are: a pressurized pump and a pressurized chamber are distributed; the pressurized pump is connected to the seawater storage tank, and the pressurized pump absorbs the seawater contained in the seawater storage tank into the pressurized chamber, Inside the pressurized chamber is a pressurized chamber for containing the seawater sucked and pressurized by the pressurized pump. A first heater is attached to the outside of the pressurized chamber. The seawater flows back to the first electromagnetic valve of the pressurized pump; the pressurized chamber is connected with the seawater input pipe connected to the pressurized chamber, and the seawater input pipe is between the pressurized chamber and the separation chamber A second solenoid valve is provided between them to prevent the seawater from flowing back into the pressurized chamber; the fresh water collection device is at least distributed with: a condensation chamber and a heat exchanger; the condensation chamber has at least one condensation chamber , the condensing chamber is provided with a condenser, and the condenser communicates with the heat exchanger outside the condensing chamber, the side of the condensing chamber is connected with the condensing pipe connected to the condensing chamber, and the condensing chamber is connected to the bottom of the condensing chamber The side is connected with a fresh water output pipe communicating with the condensing chamber, and the lower end of the fresh water output pipe is at least connected with a fresh water collection tank. The seawater separation system as described in Claim 1, wherein, the seawater separation system is further equipped with a heat medium heating device, and the heat medium heating device is additionally provided with a medium oil chamber, and the inside of the medium oil chamber is further provided with a medium oil chamber, The medium oil chamber also contains medium oil, and the outside of the medium oil cavity is distributed with: a first medium oil pump and a second medium oil pump; the first medium oil pump is additionally provided with a The medium oil chamber absorbs the first dipping tube of the medium oil, and the first medium oil pump is connected in series with the medium oil chamber and distributed with a medium oil heater for heating the medium oil. The medium oil heater is additionally equipped with Return the medium oil to the first medium oil return pipe of the medium oil chamber; the second medium oil pump is additionally equipped with a second dipping tube extending into the medium oil chamber to absorb the medium oil; another distribution around the separation chamber There is a second heater attached to the ring, and the second heater is additionally equipped with a second heat medium circulation pipe that is attached to the separation cavity, and the second heat medium circulation pipe is connected to a second heater connected to the second heater. The second heat medium conduit of the second medium oil pump, the second heat medium circulation pipe leads to a second heat medium return pipe that penetrates the second heater and connects with the medium oil chamber. The seawater separation system as described in Claim 1, wherein, the seawater separation system is further equipped with a heat medium heating device, and the heat medium heating device is additionally provided with a medium oil chamber, and the inside of the medium oil chamber is further provided with a medium oil chamber, The medium oil chamber also accommodates medium oil, and the outside of the medium oil chamber is distributed with: a first medium oil pump and a third medium oil pump; chamber to absorb the first dipping tube for the medium oil, the first medium oil pump is connected in series with a medium oil heater for heating the medium oil, and the medium oil heater is additionally provided with a device for returning the medium oil to the medium oil chamber The first medium oil return pipe; the third medium oil pump is additionally equipped with a third dip tube extending into the medium oil chamber to absorb the medium oil; the first heater attached to the outside of the pressurized chamber is additionally equipped with a ring sticker The third heat medium circulation pipe of the pressurized chamber, the third heat medium circulation pipe is connected to a third heat medium conduit that penetrates the first heater and connects to the third medium oil pump, and the third heat medium The media circulation pipe leads to a third heat medium return pipe that penetrates the first heater and connects to the media oil chamber. The seawater separation system as described in Claim 1, wherein, the seawater separation system is further equipped with a heat medium heating device, and the heat medium heating device is additionally provided with a medium oil chamber, and the inside of the medium oil chamber is further provided with a medium oil chamber, The medium oil chamber also contains medium oil, and the outside of the medium oil chamber is distributed with: a first medium oil pump, a second medium oil pump and a third medium oil pump; the first medium oil pump The pump is additionally equipped with a first dipping tube extending into the medium oil chamber to absorb the medium oil. The first medium oil pump is connected in series with a medium oil heater distributed by the heat medium heating device. The medium oil heater is additionally equipped with a sun The heat collecting umbrella, the heat medium heating device is heated by the concentrated light of the solar heat collecting umbrella The center of the heat collector is connected upwards. The heat collector is equipped with an oil-medium heat-collecting chamber through which the medium oil flows. The medium-oil heater is also provided with an oil-medium connecting pipe connected to the heat collector in series, and The last oil medium heat collector is also connected with a first medium oil return pipe that circulates the medium oil back to the oil medium chamber; the second medium oil pump is additionally provided with a second medium oil pump that extends into the medium oil chamber to absorb the medium oil. A dipping tube; a second heater attached to the separation chamber is distributed around the separation chamber, and the second heater is additionally provided with a second heat medium circulation pipe attached to the separation chamber, and the second heat medium circulation pipe is connected to a The second heat medium conduit that passes through the second heater and connects with the second medium oil pump, and the second heat medium circulation pipe leads to a second heat medium return flow that passes through the second heater and connects with the medium oil chamber tube; the third medium oil pump is provided with a third dip tube extending into the medium oil chamber to absorb the medium oil; the first heater attached to the outside of the pressurized chamber is additionally provided with a ring attached to the pressurized chamber The third heat medium circulation pipe, the third heat medium circulation pipe is also connected to a third heat medium conduit that penetrates the first heater and connects to the third medium oil pump, and the third heat medium circulation pipe is also connected to There is a third heat medium return pipe penetrating through the first heater and connected to the medium oil chamber. The seawater separation system as described in Claim 1, wherein the first heater is additionally equipped with a first electric heating strip surrounding the pressurized chamber; a third heater surrounding the separation chamber is additionally distributed, and the The third heater is additionally equipped with a second electric heating strip that surrounds the separation cavity; the seawater separation system is also distributed with a green energy generator, and the electricity generated by the green energy generator is stored in the additional battery, and the green energy generator The generated electric power is supplied to the first electric heating strip and the second electric heating strip through the storage battery, and the electric power stored in the storage battery is supplied to the seawater separation system.

Images