CN113697898B - Sea water desalination and ice cold accumulation coupling system - Google Patents
Sea water desalination and ice cold accumulation coupling system Download PDFInfo
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- CN113697898B CN113697898B CN202111120496.2A CN202111120496A CN113697898B CN 113697898 B CN113697898 B CN 113697898B CN 202111120496 A CN202111120496 A CN 202111120496A CN 113697898 B CN113697898 B CN 113697898B
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- 238000010612 desalination reaction Methods 0.000 title claims abstract description 30
- 239000013535 sea water Substances 0.000 title claims abstract description 29
- 230000008878 coupling Effects 0.000 title claims abstract description 10
- 238000010168 coupling process Methods 0.000 title claims abstract description 10
- 238000005859 coupling reaction Methods 0.000 title claims abstract description 10
- 238000009825 accumulation Methods 0.000 title description 6
- 239000013078 crystal Substances 0.000 claims abstract description 29
- 238000003860 storage Methods 0.000 claims abstract description 20
- 239000007788 liquid Substances 0.000 claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 43
- 239000003507 refrigerant Substances 0.000 claims description 22
- 238000003756 stirring Methods 0.000 claims description 17
- 238000001816 cooling Methods 0.000 claims description 12
- 238000005119 centrifugation Methods 0.000 claims description 10
- 238000007790 scraping Methods 0.000 claims description 5
- 238000004891 communication Methods 0.000 claims description 4
- 239000007921 spray Substances 0.000 claims description 3
- 238000007599 discharging Methods 0.000 abstract description 6
- 230000005611 electricity Effects 0.000 abstract description 5
- 230000007246 mechanism Effects 0.000 abstract description 5
- 238000000605 extraction Methods 0.000 abstract description 3
- 238000012546 transfer Methods 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 17
- 150000003839 salts Chemical class 0.000 description 7
- 238000007710 freezing Methods 0.000 description 6
- 230000008014 freezing Effects 0.000 description 6
- 238000000926 separation method Methods 0.000 description 6
- 238000011161 development Methods 0.000 description 4
- 239000013505 freshwater Substances 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 239000002002 slurry Substances 0.000 description 4
- 238000011033 desalting Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 230000006872 improvement Effects 0.000 description 3
- 238000010248 power generation Methods 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 2
- 239000012267 brine Substances 0.000 description 2
- 238000004146 energy storage Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000005457 ice water Substances 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000013011 mating Effects 0.000 description 1
- 238000010309 melting process Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 230000001932 seasonal effect Effects 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/38—Treatment of water, waste water, or sewage by centrifugal separation
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/22—Treatment of water, waste water, or sewage by freezing
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25C—PRODUCING, WORKING OR HANDLING ICE
- F25C1/00—Producing ice
- F25C1/12—Producing ice by freezing water on cooled surfaces, e.g. to form slabs
- F25C1/14—Producing ice by freezing water on cooled surfaces, e.g. to form slabs to form thin sheets which are removed by scraping or wedging, e.g. in the form of flakes
- F25C1/145—Producing ice by freezing water on cooled surfaces, e.g. to form slabs to form thin sheets which are removed by scraping or wedging, e.g. in the form of flakes from the inner walls of cooled bodies
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25C—PRODUCING, WORKING OR HANDLING ICE
- F25C5/00—Working or handling ice
- F25C5/18—Storing ice
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/08—Seawater, e.g. for desalination
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/10—Energy recovery
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25C—PRODUCING, WORKING OR HANDLING ICE
- F25C2301/00—Special arrangements or features for producing ice
- F25C2301/002—Producing ice slurries
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25C—PRODUCING, WORKING OR HANDLING ICE
- F25C2400/00—Auxiliary features or devices for producing, working or handling ice
- F25C2400/10—Refrigerator units
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Physics & Mathematics (AREA)
- Organic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Physical Water Treatments (AREA)
Abstract
The invention provides a seawater desalination and ice storage coupling system, which comprises a centrifugal machine, wherein the centrifugal machine comprises a box body, a cover body, a rotary drum, a centrifugal motor, a spiral scraper and an operating mechanism, a centrifugal liquid inlet hole is formed in the cover body, a plurality of through holes are formed in the side wall of the rotary drum, a discharging rod is fixedly connected or integrally connected with the upper end of the spiral scraper, the cross sections of the discharging rod and the spiral scraper are in a V shape or a U shape, a centrifugal discharging hole connected with the discharging rod is formed in the upper portion of the box body, and a drain hole communicated with an inner cavity of the box body is formed in the lower portion of the box body. Through setting up helical piping and discharge rod, can be at the extraction of complete ice crystal under the condition that centrifuge does not stop work, efficiency is relatively higher, through storing the ice after the centrifugal desalination, realizes cold energy transfer in time and space, can effectually take down the electricity that can produce at the energy, can also carry out the arbitrage according to the difference of peak low valley electricity.
Description
Technical Field
The invention relates to a water treatment and energy cascade utilization system, in particular to a sea water desalination and ice storage coupling system.
Background
The sea water desalination is an open source increment technology for realizing water resource utilization, and the development of the technology is necessary in the future, and common sea water desalination methods mainly comprise a distillation method, a reverse osmosis method and a freezing method, wherein the conventional freezing method mainly comprises the steps of cooling sea water to freeze at a low temperature, separating, washing and melting ice crystals to obtain fresh water, the separation of the ice crystals mainly adopts a gravity method for desalination, the separation efficiency is relatively low, and the desalination efficiency is also influenced by the fact that the fresh water is used for removing salt-containing water on the surface of the ice crystals after the desalination. In addition, with the development of renewable energy power generation systems, energy storage is an important method for improving random power generation and absorption, wherein ice storage plays an important role in building energy conservation, and is one of the main trends of future development, however, the existing sea water desalination system does not have an energy storage function, the development is restricted by desalination cost, and the product competitiveness is relatively low.
The chinese patent application publication No. CN112299521a discloses a centrifugal apparatus for seawater desalination, which can improve the separation speed of salt and ice crystals to some extent, however, it requires shutdown to take out ice crystals after the separation process is completed, and the taken out ice crystals also require fresh water to remove salt-containing water on the ice crystal surface, affecting the efficiency, and the cold energy of the ice crystals is not fully utilized.
In addition, the traditional freezing method mainly takes a block shape as a research object, and the heat conductivity coefficient of ice is low, and the preparation efficiency of the block ice is low and the energy consumption is high along with the increase of the thickness of the ice layer, so that the sea water desalination system adopting the traditional freezing method has relatively low efficiency and relatively high energy consumption.
In view of the above, the present inventors have conducted intensive studies on the above problems and have made the present application.
Disclosure of Invention
The invention aims to provide a seawater desalination and ice storage coupling system with relatively high efficiency.
In order to achieve the above purpose, the present invention adopts the following technical scheme:
The utility model provides a sea water desalination and ice cold-storage coupled system, includes ice maker and centrifuge that connects gradually, centrifuge includes that the upper end has the open-ended box, lid, the vertical arrangement of lid that closes on the box just rotate the rotary drum of being connected in the inner chamber of box, be used for driving rotary drum pivoted centrifugal motor, set up spiral scraper in the rotary drum and be used for driving the spiral scraper hugs closely or keeps away from the operating device of the inside wall of rotary drum, set up on the lid with the centrifugation feed liquor hole of the inner chamber intercommunication of box, the centrifugation feed liquor hole with ice maker is connected, a plurality of perforation of seting up on the lateral wall of rotary drum, the upper end fixed connection of spiral scraper or an organic whole are connected with and are located the discharge rod of rotary drum upper end, the cross section of discharge rod and spiral scraper is V-shaped or U-shaped, the upper portion of box seted up with the centrifugal discharge hole of discharge rod engagement, the lower part of box is seted up with the drain hole of the inner chamber intercommunication of box,
As an improvement of the invention, the ice maker uses a suspension ice crystal method to make ice efficiently, the ice maker comprises an outer cylinder, an inner cylinder arranged in the outer cylinder, a stirring rod inserted in the inner cylinder and coaxially arranged with the inner cylinder, a stirring motor for driving the stirring rod to rotate, and a scraping plate fixedly connected with the stirring rod and used for scraping ice crystals adhered on the inner wall of the inner cylinder, a closed refrigerant channel is arranged between the outer cylinder and the inner cylinder, a refrigerant input joint communicated with the refrigerant channel and an ice making liquid joint communicated with the inner cylinder are arranged at the upper part of the outer cylinder, and a refrigerant output joint communicated with the refrigerant channel and an ice making liquid inlet joint communicated with the inner cylinder are arranged at the lower part of the outer cylinder.
As an improvement of the invention, the centrifugal discharge hole is connected with a salinity meter, and the salinity meter is directly or indirectly connected with the centrifugal motor in a communication way.
The invention further comprises a precooling heat exchanger, wherein a cold medium inlet of the precooling heat exchanger is communicated with the drain hole, and a water outlet of the precooling heat exchanger is connected with the ice maker.
The invention further comprises a refrigerator, wherein the upper end of the refrigerator is provided with an ice storage inlet communicated with the centrifugal discharge hole, and the lower part of the side wall of the refrigerator is provided with a chilled water outlet.
As an improvement of the invention, the chilled water outlet is connected with water equipment, a return pipe is arranged on the water equipment, and a spray pipe connected with the return pipe is arranged at the upper part of the inner cavity of the refrigerator.
By adopting the technical scheme, the invention has the following beneficial effects:
1. Through setting up helical piping and discharge rod, can be at the extraction of complete ice crystal under the condition that centrifuge does not stop working, efficiency is higher relatively, simultaneously because centrifuge does not stop working, ice crystal surface does not have the brine, need not to use fresh water to get rid of the brine on ice crystal surface, has further improved sea water desalination efficiency.
2. The ice maker adopted by the invention is not easy to agglomerate because the ice maker is continuously stirred in the ice making process, so that the obtained ice is fluid ice, the thermal resistance of the ice water mixing end is almost zero, the ice maker can quickly exchange heat with refrigeration working media, the heat exchange efficiency is high, and the ice making time is short; in addition, since the ice crystals have a small volume, the desalting process corresponds to the separation of salt on the surface, and thus the desalting effect is better under the same rotation speed and centrifugation time.
3. According to the ice maker, water flows from bottom to top, the refrigerating working medium flows from top to bottom, the generated ice crystals automatically gather to the top by the principle that the ice crystal density is smaller than that of water, layering of ice slurry with high ice content and ice slurry with low ice content can be effectively achieved, and continuous output of ice slurry can be achieved by discharging the ice slurry from the upper part.
4. The refrigerator adopted by the invention utilizes the principle that ice floats on the water surface, sprays return water at the upper part, discharges chilled water at the lower part, so that the water flushes the ice crystals, and the heat conduction and heat exchange are replaced by the heat convection, thereby realizing rapid heat exchange.
5. The invention combines the ice melting process of the freezing method with cold accumulation, and the ice maker has dual purposes, so that the system is more compact and has more application value.
6. Through storing the ice after centrifugal desalination, the transfer of cold energy in time and space is realized, the electricity generated by the generated energy can be effectively consumed, and the arbitrage can be carried out according to the difference of peak electricity and valley electricity.
7. The energy cascade utilization of the desalination process is beneficial to improving the energy utilization rate of the system, reducing the comprehensive cost of the system and improving the competitiveness of the product.
Drawings
FIG. 1 is a schematic diagram of a seawater desalination and ice storage coupling system;
FIG. 2 is a schematic view of a cut-away structure of an ice maker according to the present invention;
FIG. 3 is a schematic view of a centrifuge in a cut-away configuration of the present invention, with parts omitted;
FIG. 4 is a schematic view of the structure of the transfer drum and its mating parts according to the present invention;
fig. 5 is a schematic view of a structure of a refrigerator according to the present invention.
The labels correspond to the following:
10-an ice maker; 11-an outer cylinder;
12-an inner cylinder; 13-stirring rod;
14-a stirring motor; 15-scraping plates;
16-refrigerant channels; 17-refrigerant input connection;
18-an ice making liquid outlet joint; 19-refrigerant outlet connection;
20-a centrifuge; 21-a box body;
22-cover; 23-a rotating drum;
24-spiral scraper; 25-an operating mechanism;
26-centrifuging the liquid inlet; 27-salinity meter;
28-a discharging rod; 29 centrifuging the discharge hole;
30-precooling a heat exchanger; 40-a refrigerator;
41-ice storage liquid inlet holes; 42-chilled water outlet;
43-spraying pipes; 50-water using equipment;
61-an ice making liquid inlet joint; 62-drainage holes;
63-a controller; 64-melter.
Detailed Description
The invention will be further described with reference to the accompanying drawings and specific examples.
As shown in fig. 1 to 5, the present embodiment provides a coupling system for sea water desalination and ice storage, which includes an ice maker 10 and a centrifuge 20 connected in sequence, and further includes a pre-cooling heat exchanger 30 and a refrigerator 40 connected to the centrifuge 20, respectively.
The ice maker 10 includes an outer cylinder 11, an inner cylinder 12 provided in the outer cylinder 11, a stirring rod 13 inserted in the inner cylinder 12 and coaxially arranged with the inner cylinder 12, a stirring motor 14 for driving the stirring rod 13 to rotate, and a scraper 15 fixedly connected to the stirring rod 13 for scraping ice crystals adhering to an inner wall of the inner cylinder 12, wherein a specific transmission connection structure between the stirring motor 14 and the stirring rod 13 is a conventional structure, such as a coupling connection or the like. A closed refrigerant channel 16 is arranged between the outer cylinder 11 and the inner cylinder 12, and the refrigerant channel 16 is preferably a spiral channel; the upper part of the outer cylinder 11 is provided with a refrigerant input joint 17 communicated with the upper end of the refrigerant channel 16 and an ice making liquid joint 18 communicated with the inner cylinder 12, the lower part of the outer cylinder 11 is provided with a refrigerant output joint 19 communicated with the lower end of the refrigerant channel 16 and an ice making liquid inlet joint 61 communicated with the inner cylinder 12, and preferably, the ice making liquid inlet joint 61 is positioned at the bottom of the outer cylinder 11. In use, liquid refrigerant flows in from the refrigerant inlet joint 17 positioned relatively above and flows out from the refrigerant outlet joint 19 positioned relatively below in a gaseous state, so that heat in the seawater is taken away, and part of the seawater is frozen. Of course, ice maker 10 may also include heat exchange tubes and the like, which are configured and connected in the same manner as conventional ice maker 10, and are not critical to this embodiment and will not be described in detail herein. By continuously stirring during the ice making process, caking can be avoided and fluid ice can be obtained.
The centrifuge 20 comprises a box body 21 with an opening at the upper end, a cover body 22 covered on the box body 21, a rotary drum 23 which is vertically arranged and is rotatably connected in the inner cavity of the box body 21, a centrifugal motor (not shown in the figure) for driving the rotary drum 23 to rotate, a spiral scraper 24 arranged in the rotary drum 23 and an operating mechanism 25 for driving the spiral scraper 24 to cling to or keep away from the inner side wall of the rotary drum 23, wherein the specific transmission connection structure between the centrifugal motor and the rotary drum 23 is the same as that of a conventional centrifuge, a plurality of perforations are formed on the side wall of the rotary drum 23, and the width or the diameter of the perforations cannot be too large, so that water can be thrown out of the rotary drum 23 under the centrifugal force, and ice crystals are filtered on the inner side wall of the rotary drum 23; the operating mechanism 25 may be a conventional mechanism such as an electric telescopic rod fixedly connected to the screw blade 24. The cover 22 is provided with a centrifugal liquid inlet hole 26 communicated with the inner cavity of the box 21, and the centrifugal liquid inlet hole 26 is connected with the ice making liquid joint 18 of the ice maker 10 through a conduit; the bolt direction of spiral scraper 24 is the same with the rotation direction of rotary drum 23, and spiral scraper 24's projected chord length on the horizontal plane should be matched with the radius of rotary drum in order to closely laminate, spiral scraper 24's upper end fixed connection or integrated connection have the discharge pole 28 that is located rotary drum 23 upper end, and the cross section of discharge pole 28 and spiral scraper 24 is V-arrangement or U-arrangement, i.e. its upside is formed with V-arrangement groove or U-arrangement groove, and V-arrangement groove or U-arrangement groove intercommunication between them, the upper portion of box 21 has offered the centrifugal discharge port 29 that links up with discharge pole 28, the lower part of box 21 has offered the wash port 62 that communicates with the inner chamber of box 21, in this way, when need not go to ice crystal, spiral scraper 24 keeps away from the lateral wall of rotary drum 23, when spiral scraper 24 is hugged closely on the inside wall of rotary drum 23, along with the rotation of rotary drum 23, the ice crystal that adhesion on its inside wall can be hung down by spiral scraper 24 and fall in V-arrangement groove or U-arrangement groove, simultaneously on the discharge pole 28 under the effect that rotary drum 23 rotates the whirl that forms, last centrifugal discharge port 29 that flows, finally, from the centrifugal discharge port 29 that links up to discharge port 29, the high temperature salt is realized, and the continuous operation is realized in the high temperature of the centrifuge is stopped in order to take off, and the high temperature of the sea water 20 is realized.
The ice water can be effectively separated by introducing the fluid ice into the centrifugal machine 20, and the separation of salt packets in the ice crystals can be accelerated by acceleration provided by centrifugal force, similar to a gravity method, so that the effect of rapid desalination is realized, and the seawater with the salinity of 3 percent can be desalted to the salinity of less than 0.1 percent by rotating for 2 minutes under the condition of 5000 r/min.
Considering that the seawater has different salinity in seasonal rainy season and dry season and ice making working condition changes, preferably, in the embodiment, the salinity meter 27 is connected to the centrifugal discharge hole 29, and the salinity meter 27 is directly connected with the centrifugal motor or indirectly connected with the centrifugal motor through the controller 63 in a communication way, so when the salinity meter 27 detects that the salinity is higher than a preset highest threshold value, the controller 63 increases the centrifugation time or accelerates the centrifugation speed, otherwise, when the salinity meter 27 detects that the salinity is lower than a preset minimum threshold value, the centrifugation time or the centrifugation speed is reduced, thereby realizing the real-time control of the working state of the centrifugal machine 20 and effectively reducing the energy consumption. In addition, if necessary, a melter 64 may be provided between the salinity meter 27 and the centrifugal discharge hole 29 to fuse the ice crystals, avoiding direct entry of the ice crystals into the salinity meter 27 affecting metering accuracy.
The structure of the pre-cooling heat exchanger 30 is the same as that of a conventional heat exchanger, and the pre-cooling heat exchanger 30 can be directly purchased from the market, and the pre-cooling heat exchanger 30 is provided with a cold medium inlet and a hot medium outlet which are communicated with each other, and a water inlet hole and a water outlet hole which are communicated with each other, the cold medium inlet of the pre-cooling heat exchanger 30 is communicated with a water outlet hole 62, and the water outlet of the pre-cooling heat exchanger 30 is connected with an ice making liquid inlet joint 61 of the ice maker 10. Thus, when seawater enters the ice maker 10 through the pre-cooling heat exchanger 30, it can be pre-cooled, thereby improving the working efficiency of the ice maker 10, making full use of the cold energy in the water discharged from the centrifuge 20, and the water discharged from the heat medium outlet is directly discharged or collected for further extraction of salt.
The ice storage box 40 is a conventional heat insulation box body, the upper end of the ice storage box body is provided with an ice storage liquid inlet hole 41 communicated with the centrifugal discharge hole 29, and the lower part of the side wall of the ice storage box 40 is provided with a chilled water outlet 42 so as to provide cold water for equipment needing cold water. Preferably, the chilled water outlet 42 is connected with a conventional water using apparatus 50, a return pipe is provided to the water using apparatus 50, and a shower pipe 43 connected to the return pipe is provided to an upper portion of an inner chamber of the refrigerator 40. Since the ice crystals have a density less than that of water, the ice crystals may be suspended at the upper portion of the inner cavity of the refrigerator 40 after entering the refrigerator 40; when cold energy is needed, the temperature of the water flowing back is higher, the cold energy is absorbed after the water is fully contacted with the ice crystals through upper spraying, and finally the water is discharged out of the refrigerator 40 in a form of frozen water, so that a heat exchanger is not needed, and the refrigerator is economical and reliable, and the heat exchange efficiency is high due to the large contact surface. After the chilled water is supplied with cooling energy, it is determined whether the return flow is required according to the water level in the refrigerator 40.
According to the seawater desalination and ice cold accumulation coupling system provided by the embodiment, the process of condensing and melting seawater desalination water by a decoupling freezing method is performed, desalted ice is used as a cold accumulation medium, and a refrigerating unit can be used for desalting and cold accumulation at the same time, so that the utilization rate of each part of the system can be effectively improved, and the production benefit is improved; the system can be used in combination with renewable energy sources for power generation, and can also be used in the scenes of island, ships, energy micro-nets and the like.
The present invention has been described in detail with reference to the accompanying drawings, but the embodiments of the present invention are not limited to the above embodiments, and those skilled in the art can make various modifications to the present invention according to the prior art, which are all within the scope of the present invention.
Claims (6)
1. The utility model provides a sea water desalination and ice cold-storage coupled system, its characterized in that, includes ice machine and the centrifuge that connects gradually, the centrifuge includes that the upper end has the open-ended box, lid, the vertical arrangement of closing on the box just rotates the rotary drum of connecting in the inner chamber of box, be used for driving rotary drum pivoted centrifugal motor, set up spiral scraper in the rotary drum and be used for driving the spiral scraper hugs closely or keeps away from operating device of the inside wall of rotary drum, set up on the lid with the centrifugation feed liquor hole of the inner chamber intercommunication of box, the centrifugation feed liquor hole with the ice machine is connected, a plurality of perforation have been seted up on the lateral wall of rotary drum, the upper end fixed connection of spiral scraper or an organic whole are located the discharge rod of rotary drum upper end, the discharge rod with the cross section of spiral scraper all is V-shaped or U-shaped, the upper portion of box seted up with the centrifugation discharge hole that the discharge rod links up, the drain hole of the inner chamber intercommunication of box is seted up to the lower part of box.
2. The seawater desalination and ice storage coupling system of claim 1, wherein the ice maker comprises an outer cylinder, an inner cylinder arranged in the outer cylinder, a stirring rod inserted in the inner cylinder and coaxially arranged with the inner cylinder, a stirring motor for driving the stirring rod to rotate, and a scraper fixedly connected with the stirring rod and used for scraping ice crystals adhered on the inner wall of the inner cylinder, a closed refrigerant channel is arranged between the outer cylinder and the inner cylinder, a refrigerant input joint communicated with the refrigerant channel and an ice making liquid joint communicated with the inner cylinder are arranged at the upper part of the outer cylinder, and a refrigerant output joint communicated with the refrigerant channel and an ice making liquid joint communicated with the inner cylinder are arranged at the lower part of the outer cylinder.
3. The coupled seawater desalination and ice thermal storage system of claim 1, wherein the centrifugal discharge hole is connected with a salinity meter, and the salinity meter is directly or indirectly connected with the centrifugal motor in a communication manner.
4. The coupled seawater desalination and ice storage system of any one of claims 1-3, further comprising a pre-cooling heat exchanger, wherein a cold medium inlet of the pre-cooling heat exchanger is in communication with the drain hole, and a water outlet of the pre-cooling heat exchanger is connected to the ice maker.
5. A seawater desalination and ice storage coupled system as claimed in any one of claims 1 to 3, further comprising a refrigerator, wherein an ice storage liquid inlet communicated with the centrifugal discharge hole is formed at the upper end of the refrigerator, and a chilled water outlet is formed at the lower part of the side wall of the refrigerator.
6. The coupled seawater desalination and ice storage system of claim 5, wherein the chilled water outlet is connected with a water device, a return pipe is arranged on the water device, and a spray pipe connected with the return pipe is arranged at the upper part of the inner cavity of the refrigerator.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202111120496.2A CN113697898B (en) | 2021-09-24 | 2021-09-24 | Sea water desalination and ice cold accumulation coupling system |
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