TWM619154U - Seawater separating system - Google Patents

Abstract

This creation refers to a seawater separation system, in which seawater storage tanks are distributed around the separation chamber of the seawater separation system, the separation chamber is provided with a gasification chamber with suspended nozzles, and the gasification chamber is provided with salt prevention above The salt-proof chamber formed by the guide ring is connected with a condensing nozzle. The sea water storage tank contains sea water. A pressurizing pump is distributed around the seawater conveying device and connected to the seawater storage tank to suck the seawater into the pressurizing cavity. A first heater is attached to the outside of the pressurizing cavity, and the pressurizing cavity is connected to the pressurizing cavity. room. A condensing cavity is distributed around the fresh water collecting device, the condensing cavity is provided with a condenser, the condenser is connected with a heat exchanger, the side of the condensing cavity is connected with the condensing nozzle, the lower side is connected with a fresh water outlet pipe, and the lower end of the fresh water outlet pipe A fresh water collection tank is connected.

Description

Sea water separation system

This creation refers to a seawater separation system, wherein the seawater separation system is provided with a separation chamber, and the separation chamber is provided with a spray nozzle. The spray nozzle sprays high-pressure seawater at high temperature in the separation chamber to vaporize the fresh water contained in the seawater. Those in the technical field of salt separation.

The first press means that the current climate is becoming extreme, floods and droughts are uncertain, and the area covers a wide area, which leads to personal safety and extensive property losses. Among them, especially droughts are caused by little rain or long-term no rain. The situation is as follows: the lack of domestic water, which endangers survival and the destruction of the sanitary environment, coupled with the suspension of agricultural planting, resulting in food shortages and food crises accompanied by famines, therefore, areas near the sea began to drastically turn to desalination to provide people's livelihood and Agricultural, industrial and commercial use.

At present, seawater desalination is the process of removing seawater salts and minerals, and only retaining fresh water. Among them, the current mainstream is the use of membrane treatment reverse osmosis systems for high-efficiency filtration seawater desalination; in addition, it is the combination of thermal and nuclear power plants and garbage incinerators. The thermal cycle system cooperates with heating the sea water to evaporate and vaporize the fresh water part, and the vaporized fresh water is then condensed into usable fresh water; or freezing makes the sea water freeze the fresh water part, and at the same time it freezes, the technology to discharge the salt and minerals out of the ice . 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 are limited. However, if the thermal cycle system is to achieve high efficiency and cost control, it has to be attached to thermal and nuclear power plants and waste incinerators, making it difficult to implement independently under this high heat energy consumption. Frozen seawater consumes too much electricity, and the process time is extremely long, and the actual application effect needs to be evaluated. Therefore, it can be seen that the current desalination of seawater has the problem of high cost, and it needs to be improved.

In view of the above-mentioned facts that the conventional seawater desalination has the problem of high cost, therefore, the creators of this case are encouraged to research and develop in the direction of reducing costs, and through the creators of this case Think about it all the way, and then think about it, it is best to use high temperature to spray high pressure sea water.

The seawater separation system of this creation is distributed with separation chambers, and the periphery of the separation chamber is distributed with seawater storage tanks, seawater transportation devices and freshwater collection devices. A gasification chamber is arranged in the separation cavity, and suspended spray heads are distributed in the gasification chamber, and the spray head is provided with a nozzle facing downward, and the spray head is connected with a seawater input pipe that penetrates the separation cavity. The separation chamber is provided with an upward and inwardly shrinking anti-salt guide ring above the gasification chamber. The anti-salt guide ring forms a anti-salt space above the gasification chamber. The condensing pipe that exits the separation cavity. At least one salt particle collection tank is arranged below the gasification chamber, and the gasification chamber is at least provided with a collection tank valve for closing and opening the salt particle collection tank. The seawater storage tank contains seawater, and the seawater conveying device is distributed around a pressurizing pump and a pressurizing cavity. The pressurizing pump is connected to the seawater storage tank, and the pressurizing pump sucks the seawater contained in the seawater storage tank into the pressurizing cavity, and the pressurizing cavity has an inside of the pressurizing cavity to accommodate the suction of the pressurizing pump A first heater is attached to the outside of the pressurized chamber with the pressurized seawater, and the pressurized chamber is connected with a first solenoid valve that prevents the seawater from flowing back to the pressurizing pump. The pressure chamber is connected with the seawater inlet pipe communicating with the pressure chamber, and the seawater inlet pipe is provided between the pressure chamber and the separation chamber with a first preventing the seawater from flowing back to the pressure chamber. Two solenoid valve. Distributed around the fresh water collecting device are: a condensing cavity and a heat exchanger. The condensing cavity has a condensing chamber inside the condensing chamber, and a condenser is provided in the condensing chamber. The condenser is exposed to the condensing cavity and is connected to the heat exchanger. The side of the condensing cavity is connected to the condensing chamber. For the condensing connection pipe, the lower side of the condensing cavity body is connected with a fresh water outlet pipe communicating with the condensing chamber, and the lower end of the fresh water outlet pipe is connected with a fresh water collecting tank.

The seawater separation system of this creation is distributed with heat medium heating devices, 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 is contained in the medium oil. Distributed on the outside of 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 suck the medium oil, and the first medium oil pump is connected in series with the medium oil heater distributed by the heat medium heating device, and the medium oil The heater is additionally equipped with a solar heat collecting umbrella. The heat medium heating device uses the solar heat collecting umbrella to concentrate the light to heat the solar heat collecting umbrella’s central and upwardly connected heat collector. The heat collector is provided with an oil circulating the medium oil. In the medium heat collection chamber, the medium oil heater is provided with an oil medium communication pipe connected in series with the heat collector, and the last heat collector is connected with a first medium oil return pipe that circulates the medium oil back to the medium oil chamber. The second medium oil pump is provided with A second dip tube extending into the medium oil chamber to suck the medium oil. A ring-attached second heater is distributed around the separation cavity. The second heater is provided with a second heat medium circulation tube attached to the separation cavity. The heater is connected to the second heat medium pipe of the second medium oil pump, and the second heat medium circulation pipe is connected to a second heat medium return pipe through which the second heater is connected to the medium oil chamber. The third medium oil pump is provided with a third dip tube extending into the medium oil chamber to suck the medium oil. The first heater attached to the outside of the pressurizing cavity is provided with a third heat medium circulating tube that is attached to the pressurizing cavity. The third heat medium pipe of the three-medium oil pump, and the third heat medium circulation pipe leads through a third heat medium return pipe that penetrates the first heater and is connected to the medium oil chamber.

The first heater of the invention is provided with a first electric heating strip which is attached to the pressurized cavity. A ring-attached third heater is distributed around the separation cavity, and the third heater is provided with a second electric heating strip attached to the separation cavity. The seawater separation system is distributed with green energy generators, the electricity generated by the green energy generators is stored in the installed battery, and the electricity generated by the green energy generator is supplied to the first electric heating bar and the second electric heating bar through the battery , And the electricity stored in the battery is supplied to the seawater separation system.

The main purpose of this creation is: the pressurized pump sucks the seawater contained in the seawater storage tank into the pressurized cavity, the first heater is provided outside the pressurized cavity, and the pressurized cavity sprays through the nozzle The heated seawater enters the separation chamber and vaporizes, and vaporizes in the condensing pipe connected to the anti-salt space. The gasification chamber is suspended with a spray nozzle, and is provided with a downward nozzle. The spray nozzle is connected with the seawater input pipe to enter the fresh water collection device, and the rest enters the salt particle collection tank.

Another purpose of this creation is: the seawater separation system is provided 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 on the outside of the medium oil cavity sucks the medium oil into the collector of the medium oil heater, and the solar heat-collecting umbrella concentrates the light to heat the collector, the The medium oil circulating in the heat collector is circulated back to the oil medium chamber by 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 medium oil is sucked to the first heater outside the pressurizing cavity through the third medium oil pump.

Another purpose of this creation is: the third heater is provided with a ring attached to the separation cavity In the second electric heating bar, the seawater separation system is distributed with the electricity generated by the green energy generator and stored in the storage battery, and the electricity generated by the green energy generating device is supplied to the seawater separation system through the storage battery.

[This creation]

A: sea water

A1: Fresh water

A2: Salt granules

B: Medium oil

C: Green Energy Generator

C1: battery

C2: Solar panel

C3: Wind turbine

C4: Hydroelectric generator

1: Seawater separation system

11: Separate the cavity

12: Vaporization chamber

13: Nozzle

131: Nozzle

132: Sea water input pipe

14: Anti-salt guide ring

141: Salt-proof space

142: Condensation Takeover

15: Salt collection tank

151: Collection tank valve

16: second heater

161: The second heat medium circulation pipe

162: The second heat medium pipe

163: The second heat medium return pipe

17: The third heater

2: Seawater storage tank

3: Sea water conveying device

31: Pressure pump

32: Pressurized chamber

33: pressurized chamber

34: The first heater

341: The third heat medium circulation pipe

342: Third Heat Medium Pipe

343: The third heat medium return pipe

35: The first solenoid valve

36: The second solenoid valve

4: Fresh water collection device

41: Condensation chamber

411: Condensation Chamber

412: Condenser

42: heat exchanger

43: Fresh water outlet pipe

44: Fresh water collection tank

5: Heat medium heating device

51: Medium oil cavity

511: Medium Oil Room

512: The first oil pump

5121: The first dip tube

513: The second medium oil pump

5131: second dip tube

514: Third Medium Oil Pump

5141: Third Dip Tube

52: Medium oil heater

521: Solar Collecting Umbrella

522: Collector

5221: Oil-medium heat collection chamber

5222: oil medium connecting pipe

523: First medium oil return pipe

[Figure 1] is a schematic diagram of the seawater separation system created for this creation.

[Figure 2] is a schematic diagram of the seawater separation system used for this creation.

[Figure 3] is another schematic diagram of the seawater separation system of this creation.

[Figure 4] This is a schematic diagram of the seawater separation system with green energy power generation device created for this creation.

In order to enable your reviewer to have a better understanding of this creation, the following examples are used to illustrate it.

This creation refers to a seawater separation system 1, in which the seawater separation system 1 is distributed with a separation cavity 11, and at least around the separation cavity 11 are distributed: a seawater storage tank 2, a seawater conveying device 3, and a distributed Fresh water collection device 4. The separation cavity 11 is provided with a vaporization chamber 12, the vaporization chamber 12 is distributed with suspended spray heads 13, and the spray head 13 is provided with a nozzle 131 facing downwards, and the spray head 13 is connected to the separation chamber. 11 of the 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. 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 condensing connection pipe 142 that penetrates the separation cavity 11. At least one salt particle collection tank 15 is provided below the gasification chamber 12, and the gasification chamber 12 is provided with at least a collection tank valve 151 for closing and opening the salt particle collection tank 15. The seawater storage tank 2 contains seawater A, and the seawater conveying device 3 has at least distributed around it: a pressurized pump 31 and a pressurized cavity 32 are distributed. The pressure pump 31 is connected to the seawater storage tank 2, and the pressure pump 31 sucks the seawater A contained in the seawater storage tank 2 into the pressure chamber 32, and the pressure chamber 32 has a housing inside. The pressurizing chamber 33 of the seawater A sucked and pressurized by the pressurizing pump 31, the first heater 34 is attached to the outside of the pressurizing chamber 32, and the pressurizing chamber 32 is connected to prevent the seawater A Reverse flow back to the first solenoid valve of the booster pump 31 35. The pressure chamber 32 is connected with the seawater inlet pipe 132 communicating with the pressure chamber 33, and the seawater inlet pipe 132 is provided between the pressure 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. At least distributed around the fresh water collecting device 4: a condensation cavity 41 and a heat exchanger 42 are distributed. The condensation chamber 41 has at least one condensation chamber 411 inside. The condensation chamber 411 is provided with a condenser 412. The condenser 412 passes through the condensation chamber 41 and communicates with the heat exchanger 42. The side of 41 is connected with the condensing pipe 142 communicating with the condensing chamber 411, the lower side of the condensing cavity 41 is connected with a fresh water outlet pipe 43 communicating with the condensing chamber 411, and the lower end of the fresh water outlet pipe 43 is connected with at least a fresh water collecting tank 44 (As shown in Figure 1).

Yes, the seawater separation system 1 first sucks the seawater A contained in the seawater storage tank 2 into the pressure chamber 33 of the pressure chamber 32 according to the pressure pump 31 to pressurize to a predetermined pressure value, and then The first heater 34 is used to heat the pressurized seawater A inside the pressurized cavity 32, and when the seawater A has reached a predetermined temperature, the second solenoid valve 36 is opened to allow the seawater A to enter the seawater inlet pipe 132. The seawater input pipe 132 sprays the high-pressure, high-temperature seawater A into the gasification chamber 12 through the nozzle 13 to vaporize the fresh water A1, and separate the salt and minerals into dry salt particles A2 . The vaporized fresh water A1 partly floats up to the salt-proof space 141 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 to the fresh water collection tank 44 through the fresh water outlet pipe 43 . The salt particles A2 fall into the salt particle collection tank 15, and the salt particle collection tank 15 is closed and opened with the collection tank valve 151 to process and discharge the salt particles A2 (as shown in Figure 2) .

However, the parts of the seawater separation system 1 that can be arbitrarily changed are: the number of the pressurizing chambers 32, the assembly of the pressurizing chambers 32 of different capacities, the internal pressure of the pressurizing chamber 32, the first The heater 34 heats the temperature; for this, the arrangement of the separation cavity 11 and the pressurization cavity 32 accompanied by a small individual is beneficial to:

1. The pressurizing pump 31 delivers the seawater A into the pressurizing cavity 32 for pressurization, and can be adjusted arbitrarily to maximize the pressurizing benefit of the seawater A in a small volume of the pressurizing cavity 32.

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

3. After the seawater A is pressurized and heated at a high temperature in the pressurized chamber 32, the nozzle 13 sequentially sprays the vaporized fresh water A1 in the limited space of the vaporization chamber 12 inside the separation chamber 11 at a high speed. , And in sequence, the pressurized cavity 32 takes turns to continuously generate an uninterrupted vaporization pressure in the limited space of the vaporization chamber 12, forcing the vaporized fresh water A1 to be sprayed into the condensation cavity 41, the condensation cavity 41 The condenser 412 cools and vaporizes the fresh water A1 at a high speed and condenses into the usable fresh water A1. The fresh water A1 is continuously collected into the fresh water collecting tank 44 through the fresh water outlet pipe 43. And the pressurized cavity 32, the separation cavity 11 and the condensation cavity 41 can be connected and laid in a small space to form the seawater separation system 1, and according to the pressurization cavity 32, the separation cavity 11 and the condensation The combination of the cavity 41 enables the seawater separation system 1 to continuously and rapidly produce the fresh water A1.

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

After this, the conclusions sorted out from one to four at least have: the pressurized cavity 32, the pressurized cavity 32, and the condensing cavity 41 converge to form the seawater separation system 1 that efficiently and rapidly produces the fresh water A1, and The salt particles A2 separated by the seawater separation system 1 in the gasification chamber 12 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 Figure 2 Show).

The seawater separation system 1 of the present invention is further provided with a heat medium heating device 5, and the heat medium heating device 5 is additionally provided with a medium oil cavity 51. The medium oil cavity 51 is further provided with a medium oil chamber 511 inside. 511 further contains medium oil B, and outside the medium oil cavity 51 are distributed 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 provided with a first dip tube 5121 extending into the medium oil chamber 511 to suck the medium oil B, and the first medium oil pump 512 is connected in series with a medium distributed by the heat medium heating device 5 Oil heater 52, the medium oil heater 52 is additionally provided with a solar heat collecting umbrella 521, and the heat medium heating device 5 is heated by the solar heat collecting umbrella 521 concentrated light to heat the solar heat collecting umbrella 521 centrally and upwardly connected to the heat collector 522, the heat collector 522 is provided with an oil medium heat collecting chamber 5221 that circulates the medium oil A. The medium oil heater 52 is additionally provided with an oil medium connecting pipe 5222 connected in series to the heat collector 522, and the last The heat collector 522 is further connected with a first medium oil return pipe 523 that circulates the medium oil B back to the medium oil 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. There is a second heater 16 attached around the separation cavity 11, and the second heater 16 is additionally provided with a ring attached to the separation cavity. The second heat medium circulation pipe 161 of the body 11, the second heat medium circulation pipe 161 is in turn connected to a second heat medium pipe 162 that penetrates the second heater 16 and is connected to the second medium oil pump 513, the second The heat medium circulation pipe 161 further conducts a second heat medium return pipe 163 through which the second heater 16 is connected to the medium oil chamber 511. The third medium oil pump 514 is additionally provided with a third dip tube 5141 extending into the medium oil chamber to suck the medium oil. The first heater 34 attached to the outside of the pressurizing cavity 32 is additionally provided with a third heat medium circulating pipe 341 that surrounds the pressurizing cavity 32, and the third heat medium circulating pipe 341 is also connected to a third heat medium circulating pipe 341 which is connected to the outside of the pressurizing cavity 32. A heater 34 is connected to the third heat medium pipe 342 of the third medium oil pump 514, and the third heat medium circulation pipe 341 is in turn connected to a third heat medium pipe 341 that penetrates the first heater 34 to connect to the medium oil chamber 511 The heat medium return pipe 343 (as shown in Fig. 3).

Yes, the heat medium heating device 5 first uses the first medium oil pump 512 to transport the medium oil B and continuously passes through the heat collector 522 to absorb the concentrated light of the solar heat-collecting umbrella 521 for heating, and the medium oil B is heated in the light While heating, it continues to circulate the heat to the medium oil chamber 511, so that the medium oil B continues to gather heat in the medium oil chamber 511 to increase the temperature. After the temperature of the medium oil B is raised, the The second medium oil pump 513 is delivered to the second heater 16 of the separation cavity 11 to assist the interior of the separation cavity 11 to maintain the stability of the conditions in which the seawater A sprays and vaporizes the fresh water A1. In addition, after the temperature of the medium oil B is increased, the third medium oil pump 514 can be used to transport the pressurized seawater A to the pressurized cavity 32 to force the pressurized seawater A. The heat can be increased, which is advantageous for the seawater A to be quickly vaporized and separated when the spray head 13 is sprayed into a mist in the vaporization chamber 12 to separate the fresh water A1, and the separation chamber 11 can stabilize the seawater separation according to the second heater 16 When the system 1 initially operates, the seawater A is vaporized and separated from the fresh water A1. When the temperature and vaporization pressure of the vaporization chamber 12 reach the sustainable operating conditions, the second heater 16 can reduce the power or Close operation (as shown in Figure 3).

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

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

From the above description, it can be known that the seawater separation system 1 sucks the seawater A into the pressure chamber 33 according to the pressure pump 31 to be pressurized to a predetermined pressure value, and then heats the pressurized seawater by the first heater 34 A reaches a predetermined temperature, and then open the second solenoid valve 36 so that the sea water A is sprayed into the vaporization chamber 12 through the nozzle 13 to vaporize the fresh water A1 part, and the vaporized fresh water A1 part floats up to the salt-proof space 141 is cooled and condensed into the fresh water A1 through the condenser 412 of the condensing cavity 41, and the fresh water A1 is collected to the fresh water collection tank 44 through the fresh water outlet pipe 43, and the separated salt and minerals are dried into the fresh water at the same time. The salt granule A2 falls into the salt granule collection tank 15, and the salt granule collection tank 15 is closed and opened in conjunction with the collection tank valve 151 to process and discharge the salt granule A2.

Another outstanding feature of this creation is that the seawater separation system 1 is arranged with the separation cavity 11 and the pressurizing cavity 32 to facilitate the pressurizing pump 31 to transport the seawater A into the pressurizing cavity 32 for pressurization. The predetermined pressure value of the sea water A inside the pressurizing cavity 32 can be adjusted arbitrarily; the sea water A pressurized to the predetermined pressure value is assembled in the pressurizing chamber 33 outside the pressurizing cavity 32. 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 sequentially sprays out at high speed in the limited space of the vaporization chamber 12 inside the separation chamber 11 The fresh water A1 is vaporized, and the pressurized chamber 32 in order takes turns to continuously supply the sea water A to the vaporization chamber 12 to continuously vaporize the fresh water A1, and the vaporized fresh water A1 is sprayed into the condensing chamber 41. The condenser 412 is cooled at a high speed into the usable fresh water A1, and the fresh water A1 is continuously collected into the fresh water collecting tank 44 through the fresh water outlet pipe 43, which becomes the characteristic benefit of this creation.

Another outstanding feature of this creation is that the heat medium heating device 5 heats the heat collector 522 and the medium oil B with the light concentrated by the solar collector umbrella 521, and the medium oil B continues to circulate the heat to the medium oil chamber 511 liters Increase the temperature of the medium oil B. After the temperature of the medium oil B is increased, the second medium oil pump 513 is used to deliver to the second heater 16 of the separation chamber 11 to assist the internal maintenance of the separation chamber 11 The condition stability of the fresh water A1 when the sea water A is sprayed and vaporized. In addition, the medium oil B can be delivered to the pressurizing cavity 32 by the third medium oil pump 514 to heat the pressurized seawater A, forcing the sea water A to increase its heat, and the spray head 13 sprays and vaporizes the fresh water A1 in the vaporization chamber 12 quickly. And according to the second heater 16 can stabilize the vaporization conditions of the seawater A at the initial operation of the separation chamber 11, and when the temperature and vaporization pressure of the vaporization chamber 12 reach continuous operation, the second heater 16 can be visualized. The characteristic benefit of reducing power or shutting down operation.

Another outstanding feature of this creation is that the electric energy produced by the green energy generator C is supplied to the seawater separation system 1 through the battery C1 with a characteristic benefit.

The technical content and technical characteristics of this creation have been disclosed as above. It can be seen that this creation does have the new patent requirements for novelty, advancement and industrial applicability. However, those familiar with this technology may still make various kinds of work based on the disclosure of this creation. Replacement and modification without departing from the creative spirit of this case. Therefore, the scope of protection of this creation should not be limited to those disclosed in the embodiments, but should include various replacements and modifications that do not deviate from this creation, and be covered by the scope of patent applications for new models.

A: sea water

1: Seawater separation system

11: Separate the cavity

12: Vaporization chamber

13: Nozzle

131: Nozzle

132: Sea water input pipe

14: Anti-salt guide ring

141: Salt-proof space

142: Condensation Takeover

15: Salt collection tank

151: Collection tank valve

2: Seawater storage tank

3: Sea water conveying device

31: Pressure pump

32: Pressurized chamber

33: pressurized chamber

34: The first heater

35: The first solenoid valve

36: The second solenoid valve

4: Fresh water collection device

41: Condensation chamber

411: Condensation Chamber

412: Condenser

42: heat exchanger

43: Fresh water outlet pipe

44: Fresh water collection tank

Claims (5)

A seawater separation system, wherein separation cavities are distributed in the seawater separation system, and at least distributed around the separation cavity: seawater storage tanks, seawater transportation devices, and freshwater collection devices are distributed; and a fresh water collection device is distributed in the separation cavity. A gasification chamber, the gasification chamber is distributed with suspended spray heads, the spray head is provided with a downward nozzle, and the spray head is connected with a seawater input pipe that penetrates the separation chamber; the separation chamber is in the gasification chamber The upper part of the chamber is provided with an upward and retracted anti-salt guide ring, the anti-salt guide ring forms a anti-salt space above the gasification chamber, and the anti-salt space is connected with a condensation connection pipe that penetrates the separation chamber; At least one salt collection tank is provided below the gasification chamber, and the gasification chamber is provided with at least one collection tank valve that closes and opens the salt collection tank; the seawater storage tank contains seawater, and the seawater transportation device is at least distributed around the periphery There are: a pressure pump and a pressure chamber are distributed; the pressure pump is connected to the seawater storage tank, and the pressure pump sucks the seawater contained in the seawater storage tank into the pressure chamber, The pressurizing cavity has a pressurizing chamber that contains the seawater sucked and pressurized by the pressurizing pump. A first heater is attached to the outside of the pressurizing cavity. The seawater flows back to the first solenoid valve of the pressurizing pump; the pressurizing cavity is connected with the seawater input pipe communicating with the pressurizing chamber, and the seawater input pipe is between the pressurizing cavity and the separation cavity There is a second solenoid valve to prevent the seawater from flowing back to the pressurized cavity; at least distributed around the fresh water collecting device: a condensation cavity and a heat exchanger are distributed; the condensation cavity has at least one condensation cavity inside , The condensing chamber is provided with a condenser, the condenser is communicated with the heat exchanger outside the condensing cavity, the side of the condensing cavity is connected with the condensing nozzle that communicates with the condensing cavity, and the condensing cavity is lowered The side is connected with a fresh water outlet pipe communicating with the condensing chamber, and the lower end of the fresh water outlet pipe is connected with at least a fresh water collection tank. The seawater separation system according to claim 1, wherein the seawater separation system is further provided with a heat medium heating device, the heat medium heating device is additionally provided with a medium oil cavity, and a medium oil chamber is provided inside the medium oil cavity, The medium oil chamber further contains medium oil, and on the outside of the medium oil cavity are distributed: a first medium oil pump and a second medium oil pump; The medium oil chamber sucks the first dip tube of the medium oil, the first medium oil pump is connected in series with the medium oil cavity, and a medium oil heater for heating the medium oil is additionally provided with the medium oil heater The first medium oil return pipe that returns the medium oil to the medium oil chamber; the second medium oil pump is additionally provided with a second dip tube that extends into the medium oil chamber to suck the medium oil; and is distributed around the separation cavity There is a second heater attached to the second heater, the second heater is additionally provided with a second heat medium circulation pipe attached to the separation cavity, and the second heat medium circulation pipe is in turn connected to the second heater through which the second heater is connected. The second heat medium pipe of the two medium oil pumps, and the second heat medium circulation pipe is also connected with a second heat medium return pipe which penetrates the second heater to connect with the medium oil chamber. The seawater separation system according to claim 1, wherein the seawater separation system is further provided with a heat medium heating device, the heat medium heating device is additionally provided with a medium oil cavity, and a medium oil chamber is provided inside the medium oil cavity, The medium oil chamber further contains medium oil, and on the outside of the medium oil cavity are distributed: a first medium oil pump and a third medium oil pump; the first medium oil pump is additionally provided with the medium oil The first dip tube for sucking the medium oil in the chamber, 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 medium oil that returns the medium oil to the medium oil chamber. The first medium oil return pipe; the third medium oil pump is additionally provided with a third dip tube extending into the medium oil chamber to suck the medium oil; the first heater attached to the outside of the pressurizing cavity is additionally provided with a ring sticker The third heat medium circulation pipe of the pressurized cavity, and the third heat medium circulation pipe is also connected with a third heat medium pipe which penetrates the first heater and is connected to the third medium oil pump, and the third heat medium The medium circulation pipe is also connected to a third heat medium return pipe which penetrates the first heater and connects to the medium oil chamber. The seawater separation system according to claim 1, wherein the seawater separation system is further provided with a heat medium heating device, the heat medium heating device is additionally provided with a medium oil cavity, and a medium oil chamber is provided inside the medium oil cavity, The medium oil chamber further contains medium oil, and the outside of the medium oil cavity is further distributed with: a first medium oil pump, a second medium oil pump and a third medium oil pump; the first medium oil pump The Pu Zeng is provided with a first dip tube extending into the medium oil chamber to suck the medium oil, the first medium oil pump is connected in series with the medium oil heater distributed by the heat medium heating device, and the medium oil heater is additionally provided with a solar A heat-collecting umbrella, the heat-medium heating device is heated by the solar heat-collecting umbrella and concentrated light rays in the solar heat-collecting umbrella A heat collector connected to the upper side of the center, an oil medium heat collecting chamber for circulating the medium oil is arranged inside the heat collector, and the medium oil heater is additionally provided with an oil medium connecting pipe connected in series with the heat collector, and The last collector is further connected with a first medium oil return pipe that circulates the medium oil back to the medium oil chamber; the second medium oil pump is additionally provided with a second dip tube extending into the medium oil chamber to suck the medium oil ; The separation cavity is additionally distributed around the second heater ring attached, the second heater is additionally provided with a second heat medium circulation tube attached to the separation cavity, and the second heat medium circulation tube is connected with a permeable The second heater is connected to the second heat medium pipe of the second medium oil pump, and the second heat medium circulation pipe is further connected with a second heat medium return pipe through which the second heater is connected to the medium oil chamber; The third medium oil pump is additionally provided with a third dip tube extending into the medium oil chamber to suck the medium oil; the first heater attached to the outside of the pressurizing cavity is additionally provided with a Three heat medium circulation pipes, the third heat medium circulation pipe is also connected to a third heat medium pipe that penetrates the first heater and is connected to the third medium oil pump, and the third heat medium circulation pipe is also connected to a third heat medium pipe The first heater is connected to the third heat medium return pipe of the medium oil chamber. The seawater separation system according to claim 1, wherein the first heater is additionally provided with a first electric heating strip that is attached to the pressurized cavity; a third heater attached to the pressurized cavity is additionally distributed around the separation cavity, the The third heater is additionally provided with a second electric heating strip that surrounds the separation cavity; the seawater separation system is also equipped with green energy generators, and the electricity generated by the green energy generators is stored in an additional battery, and the green energy generators The generated electric power is supplied to the first electric heating bar and the second electric heating bar through the battery, and the electric power stored in the battery is supplied to the seawater separation system.

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