CN204999641U - Way of distillation sea water desalination - Google Patents
Way of distillation sea water desalination Download PDFInfo
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- CN204999641U CN204999641U CN201520501743.7U CN201520501743U CN204999641U CN 204999641 U CN204999641 U CN 204999641U CN 201520501743 U CN201520501743 U CN 201520501743U CN 204999641 U CN204999641 U CN 204999641U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
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Abstract
The utility model provides a way of distillation sea water desalination has reduced the equipment investment betterly, improves operating efficiency, practices thrift the energy consumption, has reduced the scale deposit of working medium operation side, corruption, has reduced equipment trouble simultaneously and has rateed, has solved the poor and short -lived problem of system's result of use, and it includes working medium circulation system and sea water vapor cooling system, working medium circulation system includes the force (forcing) pump, the force (forcing) pump passes through the sprayer and connects the evaporimeter, the evaporimeter passes through steam water heat exchanger and connects the force (forcing) pump, steam water heat exchanger connects the sprayer forms working medium circulation system, sea water vapor cooling system includes the sea water pump, the sea water pump passes through heat exchanger and connects the evaporimeter, the evaporimeter is connected steam water heat exchanger, steam water heat exchanger passes through heat exchanger and connects the fresh -water tank.
Description
Technical field
The utility model relates to the technical field of environmental treatment, particularly a kind of distillation sea water desalting system and desalination method thereof.
Background technology
Current distillation sea water desalting technique mainly contains vapour compression distillation method, multistage flash evaporation distillation method, low-temperature multiple-effect distillation.Vapour compression sea water desaltination is by the seawater through preheating, and send into vaporizer and part evaporation in vaporizer, the steam produced is incorporated into the heated side of vaporizer after compressor compression improves pressure, draws after vapor condensation as product water.Multistage flash evaporation seawater desalting through the seawater of heating, will evaporate, vapor condensation is obtained fresh water in the flashing chamber reduced gradually at multiple pressure successively.Desalting seawater through multi-effect evaporation allows the seawater after heating, and evaporate in the vaporizer of multiple series connection, previous evaporator evaporation steam is out as the thermal source of next vaporizer, and condensation becomes fresh water.Front a kind of steam evaporated in vaporizer must carry out Overheating Treatment before entering compressor, and compressor easily produces fault, facility investment is large, power consumption is high; Latter two needs to run under certain vacuum tightness, and complex process, equipment is huge, and steam consumption is many.The easy fouling of aforesaid method equipment, corrosion, affect result of use and the life-span of equipment, econmics comparison is poor.
Summary of the invention
For existing the problems referred to above, the utility model provides a kind of distillation sea water desalting system, reduce facility investment preferably, improve operational efficiency, energy efficient, reduce working medium and run side fouling, corrosion, decrease equipment failure rate simultaneously, solve the problem that system result of use is poor and the life-span is short.
The technical solution of the utility model is as follows:
A kind of distillation sea water desalting system, it comprises duplex matter system and evaporation of seawater cooling system, described duplex matter system comprises force (forcing) pump, described force (forcing) pump connects vaporizer by injector, described vaporizer connects described force (forcing) pump by vapor-water heat exchanger, described vapor-water heat exchanger connects described injector, form duplex matter system, described evaporation of seawater cooling system comprises sea-water pump, described sea-water pump connects described vaporizer by heat exchanger, described vaporizer connects described vapor-water heat exchanger, and described vapor-water heat exchanger connects fresh-water tank by heat exchanger.
It is further characterized in that: described vaporizer connects described force (forcing) pump by lime set case, and described lime set case connects described vapor-water heat exchanger by throttling valve; Described force (forcing) pump connects described injector by auxiliary heater.
In said system of the present utility model, owing to have employed duplex matter system and evaporation of seawater cooling system, worker quality liquid provides high temperature refrigerant steam by working medium circulation, high temperature refrigerant steam makes the water in evaporation of seawater cooling system in vaporizer, realize evaporation, the steam formed after evaporation passes to worker quality liquid heat in vapor-water heat exchanger, worker quality liquid is heated up, worker quality liquid after intensification enters in injector, achieve the recycle of heat, fresh water is formed after self condensing into liquid, achieve the separation of seawater, seawater is in a heat exchanger to carrying out preheating simultaneously, achieve the circle transmission of heat, operational efficiency can be improved, energy efficient, simultaneously owing to adopting the alone cycle of clean working medium to transmit, reduce working medium and run side fouling, corrosion, decrease equipment failure rate simultaneously, improve system result of use and work-ing life.
Accompanying drawing explanation
Fig. 1 is the utility model embodiment one distillation sea water desalting system schematic;
Fig. 2 is the utility model embodiment two distillation sea water desalting system schematic.
Embodiment
See Fig. 1, embodiment one,
A kind of distillation sea water desalting system, it comprises duplex matter system 1 and evaporation of seawater cooling system 2, duplex matter system 1 comprises force (forcing) pump 3, force (forcing) pump 3 connects injector 5 by auxiliary heater 4, injector 5 connects vaporizer 6, vaporizer 6 connects vapor-water heat exchanger 7 by throttling valve 13, vapor-water heat exchanger 7 connects force (forcing) pump 3 and injector 5 respectively, form duplex matter system, evaporation of seawater cooling system 2 comprises sea-water pump 8, sea-water pump 8 connects sea water tank 9, sea-water pump 8 connects vaporizer 6 by heat exchanger 10, vaporizer 6 connects vapor-water heat exchanger 7, vapor-water heat exchanger 7 connects fresh-water tank 11 by heat exchanger 10.
In the utility model distillation sea water desalting system:
Vaporizer 6 is seawater heat absorption evaporators: Absorption by Sea Water working medium heat of vaporization produces water vapor, and working medium releases heat condensation.Vaporizer 6 sea intake is connected with heat exchanger 10 seawer outlet by pipeline, steam outlet is connected with vapor-water heat exchanger 7 steam inlet by pipeline, seawater concentrated solution outlet is discharged by pipeline, refrigerant vapor import to be exported with injector 5 by pipeline and is connected, and the outlet of working fluid condenses liquid is connected with throttling valve 13 import by pipeline;
Injector 5 has steam in suction vapor-water heat exchanger and promotes the function of its pressure and temperature, maintenance vapor-water heat exchanger internal pressure: injector 5 import to be exported with auxiliary heater 4 by pipeline and is connected, outlet is connected with the import of vaporizer 6 refrigerant vapor by pipeline, and suction port is connected with vapor-water heat exchanger 7 vapour outlet by pipeline;
Throttling valve 13 is throttling devices: throttling valve 13 import is exported by pipeline and vaporizer 6 working fluid condenses liquid, exports and is connected with the import of vapor-water heat exchanger 7 working medium by pipeline;
Vapor-water heat exchanger 7 is working medium and water vapour heat exchanger: working medium is absorbed heat and evaporated, seawater steam exothermic condensation.The import of vapor-water heat exchanger 7 working medium to be exported with throttling valve 13 by pipeline and is connected, and sender property outlet is connected with injector 5 suction port by pipeline, and steam inlet is connected with vaporizer 6 seawater vapour outlet, and solidifying water out is connected with the import of heat exchanger 10 fresh water;
Auxiliary heater 5 is ancillary heating equipment of sea water desaltination novel process and device.Auxiliary heater 5 import to be exported with force (forcing) pump 8 by pipeline and is connected, and exports and is connected with injector 2 import by pipeline;
Heat exchanger 10 is fresh water and sea water heat exchange device: fresh water exothermic temperature declines, and seawater endothermic temperature rises.Heat exchanger 10 sea intake to be exported with sea-water pump 8 by pipeline and is connected, seawer outlet is connected with vaporizer 6 sea intake by pipeline, fresh water import is coagulated water out by pipeline with vapor-water heat exchanger 7 and is connected, and water outlet is connected with fresh-water tank 11 import by pipeline;
Force (forcing) pump 3 provides power for working medium circulation: force (forcing) pump 3 import to be exported with vapor-water heat exchanger 7 by pipeline and is connected, and exports and is connected with auxiliary heater 4 import by pipeline;
Sea water tank 9 is the containers depositing seawater: sea water tank 9 is exported and is connected with sea-water pump 8 import by pipeline, and its import is connected with external device (ED);
Sea-water pump 8 provides power for marine stream: sea-water pump 10 import to be exported with sea water tank 9 by pipeline and is connected, and exports and is connected with heat exchanger 6 sea intake by pipeline;
The fresh water container of discharging from heat exchanger 10 deposited by fresh-water tank 11: fresh-water tank 11 import is connected with heat exchanger 10 water outlet by pipeline, exports and is connected with external device (ED) by pipeline.
See Fig. 2, embodiment two,
A kind of distillation sea water desalting system, it comprises duplex matter system 1 and evaporation of seawater cooling system 2, duplex matter system 1 comprises force (forcing) pump 2, force (forcing) pump 3 connects injector 5 by auxiliary heater 4, injector 5 connects vaporizer 6, vaporizer 6 connects force (forcing) pump 3 by lime set case 12, lime set case 12 connects vapor-water heat exchanger 7 by throttling valve 13, vapor-water heat exchanger 7 connects injector 5, form duplex matter system, evaporation of seawater cooling system 2 comprises sea-water pump 8, sea-water pump 8 connects sea water tank 9, sea-water pump 9 connects vaporizer 6 by heat exchanger 10, vaporizer 6 connects vapor-water heat exchanger 7, vapor-water heat exchanger 7 connects fresh-water tank 11 by heat exchanger 10.
In the utility model distillation sea water desalting system:
Vaporizer 6 is seawater heat absorption evaporators: Absorption by Sea Water working medium heat of vaporization produces water vapor, and working medium releases heat condensation.Vaporizer 6 sea intake is connected with heat exchanger 10 seawer outlet by pipeline, steam outlet is connected with vapor-water heat exchanger 7 steam inlet by pipeline, seawater concentrated solution outlet is discharged by pipeline, refrigerant vapor import to be exported with injector 5 by pipeline and is connected, and the outlet of working fluid condenses liquid is connected with lime set case 12 import, throttling valve 13 import respectively by pipeline;
Injector 5 has steam in suction vapor-water heat exchanger and promotes the function of its pressure and temperature, maintenance vapor-water heat exchanger internal pressure: injector 5 import to be exported with auxiliary heater 4 by pipeline and is connected, outlet is connected with the import of vaporizer 6 refrigerant vapor by pipeline, and suction port is connected with vapor-water heat exchanger 7 vapour outlet by pipeline;
Throttling valve 13 is throttling devices: throttling valve 13 import is exported with vaporizer 6 working fluid condenses liquid respectively by pipeline, lime set case 12 import is connected, and exports and is connected with the import of vapor-water heat exchanger 7 working medium by pipeline;
Vapor-water heat exchanger 7 is working medium and seawater heat of steam switch: working medium is absorbed heat and evaporated, seawater steam exothermic condensation.The import of vapor-water heat exchanger 7 working medium to be exported with throttling valve 13 by pipeline and is connected, and sender property outlet is connected with injector 5 suction port by pipeline, and steam inlet is connected with vaporizer 6 seawater vapour outlet, and solidifying water out is connected with the import of heat exchanger 10 fresh water;
Auxiliary heater 5 is ancillary heating equipment of sea water desaltination novel process and device.Auxiliary heater 5 import to be exported with force (forcing) pump 8 by pipeline and is connected, and exports and is connected with injector 2 import by pipeline;
Heat exchanger 10 is fresh water and sea water heat exchange device: fresh water exothermic temperature declines, and seawater endothermic temperature rises.Heat exchanger 10 sea intake to be exported with sea-water pump 8 by pipeline and is connected, seawer outlet is connected with vaporizer 6 sea intake by pipeline, fresh water import is coagulated water out by pipeline with vapor-water heat exchanger 7 and is connected, and water outlet is connected with fresh-water tank 11 import by pipeline;
The worker quality liquid container of discharging from vaporizer 6 deposited by lime set case 12: lime set case 12 import is exported with vaporizer 6 working fluid condenses liquid respectively by pipeline, throttling valve 13 import is connected, and exports and is connected with force (forcing) pump 3 import by pipeline;
Force (forcing) pump 3 provides power for working medium circulation: force (forcing) pump 3 import to be exported with lime set case 12 by pipeline and is connected, and exports and is connected with auxiliary heater 4 import by pipeline;
Sea water tank 9 is the containers depositing seawater: sea water tank 9 is exported and is connected with sea-water pump 8 import by pipeline, and its import is connected with external device (ED);
Sea-water pump 8 provides power for marine stream: sea-water pump 10 import to be exported with sea water tank 9 by pipeline and is connected, and exports and is connected with heat exchanger 6 sea intake by pipeline;
The fresh water container of discharging from heat exchanger 10 deposited by fresh-water tank 11: fresh-water tank 11 import is connected with heat exchanger 10 water outlet by pipeline, exports and is connected with external device (ED) by pipeline.
In above-described embodiment, injector 5 comprises nozzle, mixing section and diffuser-.
Distillation sea water desalting method,
(1), force (forcing) pump 3 enters in injector after being heated by auxiliary heater 4 after being pressurizeed by worker quality liquid;
(2), working medium enters in vaporizer 6 by injector 5, seawater is by after heat exchanger 10 preheating simultaneously, enter in vaporizer 6, indirect heat exchange is carried out at vaporizer 6 maritime interior waters and working medium, evaporate after Absorption by Sea Water working medium heat, water becomes steam and separates from seawater and enter in vapor-water heat exchanger 3, seawater is concentrated, simultaneously working medium in vaporizer 6 release of heat rear section or all enter in vapor-water heat exchanger 7 with evaporation of seawater after the fresh water steam that produces carry out heat exchange, the steam that part worker quality liquid absorbs heat generation is inhaled in injector 5, pressurized pump 3 pressurization of worker quality liquid in the worker quality liquid of lime set case 12 or vapor-water heat exchanger enters in vaporizer 6 by injector 5 after entering and mixing with the working substance steam sucked from vapor-water heat exchanger 7 in injector 5, form working medium circulation,
(3) fresh water formed that condenses after the fresh water steam that, seawater is separated carries out heat exchange with worker quality liquid in vapor-water heat exchanger 7 enters in heat exchanger 10, the seawater be pressed into sea-water pump carries out heat exchange, complete seawater to be separated, to concentrate and preheating, form the circle transmission of heat.
The task of duplex matter system absorbs heat exactly from seawater steam, and then these heats are passed to seawater makes it evaporate, and completes the recycle of heat energy.According to heat conduction principle, the temperature of working medium must lower than seawater vapor temperature, and working medium could absorb heat from seawater steam.Adopt the nozzle of injector to spray working medium, the working substance steam in suction vapor-water heat exchanger, the Temperature of Working in maintenance vapor-water heat exchanger, lower than the temperature of seawater steam, makes the working medium in vapor-water heat exchanger can absorb seawater heat of vaporization.Then aspirate working substance steam to mix in injector with injection working medium, entered vaporizer by compression boosting intensification thereafter.In vaporizer, working medium heating seawater, is condensed into liquid after releasing heat.Be divided into two portions from vaporizer worker quality liquid out, enter vapor-water heat exchanger after a part of throttling, enter injector after absorbing heat of vaporization, another part enters injector nozzle after being pressurizeed by force (forcing) pump and sprays, and two portions mix boosting again and heat up.So far, working medium completes a closed circulation.
The task of evaporation of seawater cooling system is that Absorption by Sea Water heat is evaporated, and then steam is carried out cooling becomes fresh water, completes the desalination of seawater.Sea evaporation of water has mainly come by vaporizer, carries out indirect heat exchange at vaporizer maritime interior waters and working medium, and evaporate after absorbing working medium heat, water is just separated from seawater, and seawater is concentrated.Then discharge concentrated seawater, water vapor then enters vapor-water heat exchanger and cools.In vapor-water heat exchanger, the water vapor separated from seawater still carries out indirect heat exchange with working medium, and heat is passed to working medium, condenses into liquid, so far, complete the main process of sea water desaltination after releasing heat.
Heat required for above-mentioned evaporation of seawater is mainly taken from seawater itself.Seawater evaporates under pressure, steam after evaporation transfers heat to cycle fluid by vapor-water heat exchanger, then cycle fluid transfers heat to seawater again by vaporizer, evaporates again after Absorption by Sea Water heat, completes the transmission circulation of heat.Because seawater concentration device has calorific loss in operational process, therefore, in the utility model, be provided with auxiliary heater, system is heated, can the heat of replenish loss.
The principle of work of the utility model distillation sea water desalting system is described below more with reference to the accompanying drawings:
1. duplex matter system:
First force (forcing) pump 3 extracts the worker quality liquid in lime set case 12 and pressurizes to it, improves the pressure of working medium.Working medium after boosting enters auxiliary heater 4 and heats, and enters the nozzle of injector 5 after heat temperature raising, increases sharply at nozzle kinetic energy, and reaches very high-speed at nozzle exit, pressure drop.Due to the ejector action of high velocity air, thus the steam of the vapor-water heat exchanger 7 be connected with injector 5 has been attracted, in respective sustain vapor-water heat exchanger 7, the saturation pressure of working medium side is less than the saturation pressure of seawater side, ensure that the temperature of working medium is less than the temperature of seawater steam all the time, working medium can absorb the evaporation of seawater steam heat.The working substance steam be attracted and jet exit working medium enter in injector 2 diffuser-and fully mix, and are then entered vaporizer 6 by compression boosting intensification together.In vaporizer 6, working substance steam indirect heating seawater, self is condensed into liquid after releasing heat.Be divided into two portions from vaporizer 6 worker quality liquid out, a part, by entering vapor-water heat exchanger 7 after throttling valve 13 throttling, absorbs seawater steam heat, enters injector 5 after evaporation; Another part enters lime set case 12 and pressurizes via force (forcing) pump 3, and enter injector 5 after being heated by auxiliary heater 4 after pressurization, so far, working medium completes a closed circulation process.
2. evaporation of seawater cooling system:
First seawater enters sea water tank 9, the seawater then in sea-water pump 8 extracting seawater case 9, and seawater is sent into heat exchanger 10 preheating.In heat exchanger 10, seawater carries out heat exchange with the fresh water of coming from vapor-water heat exchanger 7, and seawater endothermic temperature rises, and then enters vaporizer 6.Carry out indirect heat exchange at vaporizer 6 maritime interior waters and working medium, evaporate after Absorption by Sea Water working medium heat, fresh water is separated from seawater, and seawater is concentrated.The water vapor generated in vaporizer 6 enters vapor-water heat exchanger 7 subsequently, and carry out indirect heat exchange with working medium, heat is passed to working medium, self is condensed into water of condensation.Then water of condensation enters heat exchanger 10, carries out indirect heat exchange with seawater, releases thermal temperature and declines, enter thereafter fresh-water tank 11, finally discharge use.
The seawater be concentrated in vaporizer 6, is discharged by pipeline and is further processed.
Effective effect of the present utility model is:
The utility model uses clean working medium alone cycle, improves equipment operating efficiency, extension device work-ing life.Seawater heat can be made full use of, reduce external heat input, save energy consumption.
Claims (3)
1. a distillation sea water desalting system, it is characterized in that: it comprises duplex matter system and evaporation of seawater cooling system, described duplex matter system comprises force (forcing) pump, described force (forcing) pump connects vaporizer by injector, described vaporizer connects described force (forcing) pump by vapor-water heat exchanger, described vapor-water heat exchanger connects described injector, form duplex matter system, described evaporation of seawater cooling system comprises sea-water pump, described sea-water pump connects described vaporizer by heat exchanger, described vaporizer connects described vapor-water heat exchanger, described vapor-water heat exchanger connects fresh-water tank by heat exchanger.
2. a kind of distillation sea water desalting system according to claim 1, is characterized in that: described vaporizer connects described force (forcing) pump by lime set case, and described lime set case connects described vapor-water heat exchanger by throttling valve.
3. a kind of distillation sea water desalting system according to claims 1 or 2, is characterized in that: described force (forcing) pump connects described injector by auxiliary heater.
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| CN201520501743.7U CN204999641U (en) | 2015-07-13 | 2015-07-13 | Way of distillation sea water desalination |
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| CN201520501743.7U CN204999641U (en) | 2015-07-13 | 2015-07-13 | Way of distillation sea water desalination |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104944485A (en) * | 2015-07-13 | 2015-09-30 | 无锡雪浪环境科技股份有限公司 | Distillation method seawater desalination system and method |
| CN112759011A (en) * | 2020-12-31 | 2021-05-07 | 中谷宏(海南)实业有限公司 | Low-temperature evaporation seawater desalination device without vacuum pump |
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2015
- 2015-07-13 CN CN201520501743.7U patent/CN204999641U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104944485A (en) * | 2015-07-13 | 2015-09-30 | 无锡雪浪环境科技股份有限公司 | Distillation method seawater desalination system and method |
| CN112759011A (en) * | 2020-12-31 | 2021-05-07 | 中谷宏(海南)实业有限公司 | Low-temperature evaporation seawater desalination device without vacuum pump |
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Address after: 214000 no.2020 Lihu Avenue, Binhu District, Wuxi City, Jiangsu Province Patentee after: WUXI XUELANG ENVIRONMENTAL TECHNOLOGY Co.,Ltd. Address before: 214128 Shuangxin economic Park, Taihu street, Binhu District, Wuxi City, Jiangsu Province Patentee before: WUXI XUELANG ENVIRONMENTAL TECHNOLOGY Co.,Ltd. |