CN204267237U - Solar energy ocean thermal energy superposition type electricity generating device - Google Patents
Solar energy ocean thermal energy superposition type electricity generating device Download PDFInfo
- Publication number
- CN204267237U CN204267237U CN201420727749.1U CN201420727749U CN204267237U CN 204267237 U CN204267237 U CN 204267237U CN 201420727749 U CN201420727749 U CN 201420727749U CN 204267237 U CN204267237 U CN 204267237U
- Authority
- CN
- China
- Prior art keywords
- vaporizer
- seawater
- generating device
- superposition type
- electricity generating
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Classifications
-
- 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
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/40—Solar thermal energy, e.g. solar towers
- Y02E10/46—Conversion of thermal power into mechanical power, e.g. Rankine, Stirling or solar thermal engines
Landscapes
- Engine Equipment That Uses Special Cycles (AREA)
Abstract
The utility model provides a kind of solar energy ocean thermal energy superposition type electricity generating device, it includes the solar water heater for heated surface layer seawater, the Multi-stage flash steaming pot be connected is exported with the high temperature seawater of described solar water heater, the deep layer Mare Frigoris water supply pump of cooling water is provided with described multistage flash evaporation tank connected organic Rankine power generation system with for described organic Rankine power generation system, described organic Rankine power generation system includes and connects successively and form the vaporizer in organic Rankine power generation cycle loop, the decompressor of generator is installed, condenser, organic working medium liquid container and organic working medium pump, wherein, described vaporizer is connected with described Multi-stage flash steaming pot.Surface seawater described in solar energy heating to compensate ocean thermal energy and to utilize organic Rankine bottoming cycle generation technology to generate electricity, can also be utilized the condensation fresh water preparing fresh of vaporizer by above-mentioned superposition type generating and sea water desalinating unit simultaneously, comprehensive utilization various energy resources.
Description
Technical field
The utility model relates to solar energy and ocean water thermal gradient energy technical field of comprehensive utilization, is specifically related to one and utilizes solar energy ocean thermal energy superposition type electricity generating device.
Background technique
Along with the develop rapidly of national economy; country is increasing to the demand of the energy, and the deposit of China's mineral fuel is fewer and feweri, and the burning of mineral fuel makes environment go from bad to worse; therefore, tap a new source of energy the effective way becoming China's solution energy crisis and realize sustainable development.And in the coastal of China and Island, have the seriously short of electricity of many places and lack fresh water, the living standard that seriously have impact on local economic development and the people improves.But ocean is a huge energy depot, contains multiple renewable energy sources, and wherein ocean thermal gradients reserves are maximum, be one of energy of the most potentiality to be exploited that international community generally acknowledges.Meanwhile, ocean and periphery thereof also have the resources such as very abundant solar energy.If solar energy and ocean thermal energy are effectively utilized, just can solve the difficulty in above-mentioned area well, change inferior position is advantage, for these areas provide electric energy, and desalinates seawater.So, there is solar energy in prior art and ocean thermal energy equal energy source comprehensive utilization ratio is lower, the shortcomings such as cost compare is high.
Model utility content
In view of this, in order to solve the problems of the technologies described above, the utility model provides a kind of solar energy ocean thermal energy superposition type electricity generating device.
The utility model provides a kind of solar energy ocean thermal energy superposition type electricity generating device, it is characterized in that: it includes the solar water heater for heated surface layer seawater, the Multi-stage flash steaming pot be connected is exported with the high temperature seawater of described solar water heater, the deep layer Mare Frigoris water supply pump of cooling water is provided with described multistage flash evaporation tank connected organic Rankine power generation system with for described organic Rankine power generation system, described organic Rankine power generation system includes and connects successively and form the vaporizer in organic Rankine power generation cycle loop, the decompressor of generator is installed, condenser, organic working medium liquid container and organic working medium pump, wherein, described vaporizer is connected with described Multi-stage flash steaming pot.
Wherein, described Multi-stage flash steaming pot comprise to export with the high temperature seawater of described solar water heater be connected chopped-off head flash drum, export with the concentrated seawater of described chopped-off head flash drum the intergrade flash drum be connected, and export with the concentrated seawater of described intergrade flash drum the final stage flash drum be connected; The concentrated seawater of described final stage flash drum is discharged to seawater, and described intergrade flash drum comprises multiple flash vessel be arranged in series, and the described vaporizer in described organic Rankine power generation system is corresponding with described Multi-stage flash steaming pot and the multi-stage evaporator connected.Wherein, the pressure of the flash drum in described Multi-stage flash steaming pot is different, and from chopped-off head flash drum to final stage flash drum, its pressure reduces gradually; Described Multi-stage flash steaming pot can be six grades of flash drums, seven grades of flash drums, eight grades of flash drums, ten grades of flash drums, ten two-stage flash tanks, ten level Four flash drums, even more than ten level Four flash drums.
Based on above-mentioned superposition type electricity generating device, it comprises the fresh water storage tank be communicated with the condensation water outlet of described vaporizer further.
Based on above-mentioned superposition type electricity generating device, described vaporizer is with described Multi-stage flash steaming pot one_to_one corresponding and the multi-stage evaporator be communicated with.Wherein, the quantity of the vaporizer in described multi-stage evaporator is identical with the quantity of the flash drum in described Multi-stage flash steaming pot, and the vaporizer of same levels is communicated with flash drum.The described Multi-stage flash steaming pot water vapour of discharging provides the thermal source of heating liquid organic working medium wherein for described multi-stage evaporator.
Based on above-mentioned superposition type electricity generating device, it also comprises the pumped vacuum systems be connected with described multi-stage evaporator, for improving the generated energy of described organic Rankine cycle power generation system.
Based on above-mentioned superposition type electricity generating device, the vaporizers at different levels in described multi-stage evaporator are arranged on the outside or inside of the flash drum of described Multi-stage flash steaming pot corresponding level; In described multi-stage evaporator, the organic working medium vapor outlet port of chopped-off head vaporizer is connected with described decompressor, and the liquid organic working medium import of final evaporator is connected with described organic working medium delivery side of pump.
When the vaporizers at different levels in described multi-stage evaporator are arranged on the flash drum of described Multi-stage flash steaming pot corresponding level outside, vaporizer at different levels is connected with the vapor outlet port of the flash drum of same level.Particularly, this multi-stage evaporator comprises the chopped-off head vaporizer be connected with the vapor outlet port of described chopped-off head flash drum, the intergrade vaporizer be connected respectively with the vapor outlet port of described intergrade flash drum and the final evaporator be connected with the vapor outlet port of described final stage flash drum; Described chopped-off head vaporizer, described intergrade vaporizer and described final evaporator are arranged in series successively, and the organic working medium vapor outlet port of described chopped-off head vaporizer is connected with described decompressor, the liquid organic working medium import of described final evaporator is connected with described organic working medium delivery side of pump, described chopped-off head vaporizer, described intergrade vaporizer are connected with described fresh water storage tank respectively with the condensation water outlet of described final evaporator, and described chopped-off head vaporizer, described intergrade vaporizer are connected with pumped vacuum systems respectively with described final evaporator.
When the vaporizers at different levels in described multi-stage evaporator are arranged on the inside of the flash drum of described Multi-stage flash steaming pot corresponding level, vaporizer at different levels is arranged on the top of the inside of the flash drum of same level.Particularly, described multi-stage evaporator comprises the chopped-off head vaporizer be arranged in described chopped-off head flash drum, the final evaporator being arranged on the intergrade vaporizer in described intergrade flash drum and being arranged in described final stage flash drum, described chopped-off head vaporizer, described intergrade vaporizer and described final evaporator are arranged in series successively, and the organic working medium vapor outlet port of described chopped-off head vaporizer is connected with described decompressor, the liquid organic working medium import of described final evaporator is connected with described organic working medium delivery side of pump, described chopped-off head vaporizer, described intergrade vaporizer is connected with described fresh water storage tank with the condensation fresh water of described final evaporator.
Based on above-mentioned superposition type electricity generating device, it also comprises surface seawater supply pump, mixing tank and suction booster, wherein, described mixing tank, described suction booster, described solar water heater and described Multi-stage flash steaming pot connect and compose high temperature seawater circulation loop successively, and described mixing tank is connected with described surface seawater supply pump.The concentrated seawater outlet of described mixing tank and described Multi-stage flash steaming pot.
The using method of above-mentioned superposition type electricity generating device comprises:
Form water vapour: be transported to by surface seawater in described solar water heater, heating of seawater wherein becomes higher than the high temperature seawater equaling 80 DEG C by described solar water heater, and this high temperature seawater is transported to the water vapour being formed in described Multi-stage flash steaming pot and be transported to described vaporizer;
Described organic Rankine power generation system generating: the water vapour that described vaporizer the transfers out liquid organic working medium heated in described vaporizer makes it to become organic working medium steam; This organic working medium steam to be sent in described decompressor and to promote described decompressor acting generating; The exhaust steam that described decompressor is discharged enters in described condenser, by the deep layer Mare Frigoris water condensation be drawn into by deep layer Mare Frigoris water supply pump in described condenser, and liquefy organic working medium; This liquid organic working medium is passed into described organic working medium liquid container and by described organic working medium transport pump in described vaporizer, to carry out organic Rankine power generation cycle.
Wherein, described high temperature seawater is transported in described Multi-stage flash steaming pot and forms the step being transported to the water vapour of described vaporizer and comprise: described high temperature seawater is input in the chopped-off head flash drum in described Multi-stage flash steaming pot that formation temperature is higher than the chopped-off head water vapour and the chopped-off head concentrated seawater that equal 70 DEG C, and described chopped-off head water vapour is transported to the chopped-off head vaporizer in multi-stage evaporator; Described chopped-off head concentrated seawater flows and flow in final stage flash drum and forms final stage concentrated seawater in described Multi-stage flash steaming pot; Described chopped-off head concentrated seawater forms water vapour in the process flowing into described final stage flash drum, and this water vapour is transported in the vaporizer of same level.
When the temperature of described final stage concentrated seawater is lower than surface seawater temperature, be discharged into marine greatly; When the temperature of described final stage concentrated seawater is higher than surface seawater temperature, be passed in mixing tank, and mix with the surface seawater be transported in this mixing tank by surface seawater supply pump, and be transported in described solar water heater by suction booster, and be heated into the high temperature seawater higher than equaling 80 DEG C by described solar water heater, this high temperature seawater to be passed in described Multi-stage flash steaming pot, until form the final stage concentrated seawater higher than surface seawater temperature, complete high temperature seawater circulation.
The step of described organic Rankine power generation system generating comprises: liquid organic working medium to flow out and by described organic working medium transport pump in the final evaporator described multi-stage evaporator from described organic working medium liquid container, this liquid state is organic to flow in described multi-stage evaporator, and heated by the water vapour of discharging from the flash drums at different levels in described Multi-stage flash steaming pot, and flow in described chopped-off head vaporizer, be heated into organic working medium steam by described chopped-off head water vapour, this organic working medium steam is passed into acting generating in described decompressor; Wherein, in the process that described liquid organic working medium flows in described multi-stage evaporator, enter the water vapour at different levels in described multi-stage evaporator and condensation, form the fresh water of being discharged by the condensation water outlet of vaporizer at different levels.
Compared with prior art, the solar energy ocean thermal energy superposition type electricity generating device that the utility model provides has the following advantages: the utility model utilizes described solar water heater that surface seawater is heated to more than 80 DEG C, and the described water vapour utilizing described Multi-stage flash steaming pot the to discharge liquid organic working medium heated in described vaporizer becomes gaseous state organic working medium to do work to drive decompressor, thus drive described organic Rankine systemic circulation to continue generating, and the exhaust steam after utilizing deep sea water to cool acting is to increase the temperature difference of working medium before and after decompressor and enthalpy drop, thus export more merit, simultaneously, described water vapour is condensed formation fresh water in described vaporizer, therefore, the described superposition type electricity generating device that the utility model provides utilizes solar energy compensation ocean thermal energy heat described surface seawater and generate electricity in conjunction with organic Rankine bottoming cycle generation technology, by-product fresh water can also be obtained simultaneously, achieve solar energy, the comprehensive utilization of ocean thermal energy equal energy source, improve energy utilization rate, meanwhile, utilize the fresh water that described Multi-stage flash steaming pot obtains, the energy Ratios of consumption is less, thus reduces desalination of sea water cost.
Further, in the superposition type electricity generating device that the utility model provides, described Multi-stage flash steaming pot is connected one by one respectively with described multi-stage evaporator, utilizes the steam Multi-stage heating organic working medium that this Multi-stage flash steaming pot is formed, reduce heat transfer temperature difference, improve energy utilization rate and generating efficiency.
Further, when the high temperature seawater exported from described solar water heater is after the flash distillation of described Multi-stage flash steaming pot, the concentrated seawater outlet temperature of its final stage flash drum is lower than the temperature of described surface seawater, can directly be discharged in seawater, thus the energy of described high temperature seawater can be made full use of, reduce energy waste, improve desalination of sea water amount simultaneously.
Further, when temperature higher than described surface seawater of the concentrated seawater outlet temperature of described Multi-stage flash steaming pot, the utility model reclaims the concentrated seawater with higher temperature of described Multi-stage flash steaming pot discharge by described mixing tank, and mix with described surface seawater, reduce the temperature difference of the import and export seawater of solar water heater, make full use of the waste heat of described concentrated seawater, reduce the energy consumption of described solar water heater, be conducive to energy saving.
Further, the using method of the superposition type electricity generating device that the utility model provides, conbined usage ocean thermal energy and solar energy, compared with simple solar energy, add using energy source amount, temperature difference from original simple ocean thermal gradients about 20 DEG C, solar energy at least 70 DEG C, at least bring up to about 90 DEG C, increase substantially using energy source scope.
Accompanying drawing explanation
Fig. 1 is the solar energy ocean thermal energy superposition type electricity generating device that provides of the utility model first embodiment and workflow schematic diagram thereof.
Fig. 2 is the solar energy ocean thermal energy superposition type electricity generating device that provides of the utility model second embodiment and workflow schematic diagram thereof.
Wherein, the component symbol 1 in Fig. 1, surface seawater supply pump; 2, mixing tank; 3, suction booster; 4, solar water heater; 5, Multi-stage flash steaming pot; 51, chopped-off head flash drum; 52, intergrade flash drum; 53, final stage flash drum; 6, vaporizer; 61, chopped-off head vaporizer; 62, intergrade vaporizer; 63, final evaporator; 7, condensed water storage tank; 8, compression pump; 9, reverse osmosis membrane filt; 10, sparge water storage tank; 11, fresh water storage tank; 12, decompressor; 13, condenser; 14, organic working medium liquid container; 15, organic working medium pump; 16, deep layer Mare Frigoris water supply pump; 17, pumped vacuum systems.
Embodiment
Below by embodiment, the technical solution of the utility model is described in further detail.
Refer to Fig. 1, the utility model first embodiment provides a kind of solar energy ocean thermal energy superposition type electricity generating device, comprise for heated surface layer seawater solar water heater 4, with the high temperature seawater of described solar water heater 4 export be connected Multi-stage flash steaming pot, provide the deep layer Mare Frigoris water supply pump 16 of cooling water with described multistage flash evaporation tank connected organic Rankine power generation system with for described organic Rankine power generation system.
The suction booster 3 that described superposition type electricity generating device also includes the surface seawater supply pump 1 for extracting surface seawater and is connected with described surface seawater supply pump 1.The surface seawater of extraction is transported in described solar water heater 4 by described suction booster 3.Described surface seawater is heated into the high temperature seawater that temperature is more than 80 DEG C by described solar water heater 4.The high temperature seawater outlet of described solar water heater 4 is connected with described Multi-stage flash steaming pot, and the vapor outlet port of described Multi-stage flash steaming pot is connected with described organic Rankine power generation system.Wherein, when the temperature that the high temperature seawater of described solar water heater 4 exports controls at 100 DEG C ~ 125 DEG C, the optimum rate of utilization of solar energy can be ensured, and seawater fouling can be prevented.In the present embodiment, the temperature of described surface seawater is approximately 26 DEG C, and described surface seawater is heated to about 120 DEG C by described solar water heater.
Described Multi-stage flash steaming pot is ten grades of flash drums, it comprise to export with the high temperature seawater of described solar water heater 4 be connected chopped-off head flash drum 51, export with the concentrated seawater of described chopped-off head flash drum 51 the intergrade flash drum 52 be connected, and export with the concentrated seawater of described intergrade flash drum 52 the final stage flash drum 53 be connected.Described intergrade flash drum 52 comprises eight flash drum (not shown) be arranged in series, and the concentrated seawater outlet of described final stage flash drum 53 is communicated with seawater.
Described have machine power generating system to include vaporizer tank connected with described multistage flash evaporation, the decompressor 12 being provided with motor be connected with the organic working medium vapor outlet port of described vaporizer, the condenser 13 be connected with described decompressor 12, the organic working medium liquid container 14 be connected is exported with the organic working medium of described condenser 13, connect the organic working medium pump 15 of described organic working medium liquid container 14 and described vaporizer, and the deep layer Mare Frigoris water supply pump 16 to be connected with the cooling water intake of described condenser 13.Wherein, described vaporizer, described decompressor 12, described condenser 13, described organic working medium liquid container 14 and described organic working medium pump 15 connect and compose organic Rankine power generation cycle loop successively.
In the present embodiment, vaporizer in described organic Rankine power generation system is that ten grades of vaporizers are arranged on outside described ten grades of flash drums, these ten grades of vaporizers comprise the chopped-off head vaporizer 61 be connected with the vapor outlet port of described chopped-off head flash drum 51, the intergrade vaporizer 62 be connected respectively with the vapor outlet port of described intergrade flash drum 52 and the final evaporator 63 be connected with the vapor outlet port of described final stage flash drum 53; Described chopped-off head vaporizer 61, described intergrade vaporizer 62 and described final evaporator 63 are arranged in series successively, and the organic working medium vapor outlet port of described chopped-off head vaporizer 61 is connected with described decompressor 12, the liquid organic working medium import of described final evaporator 63 is connected with the outlet of described organic working medium 15, described chopped-off head vaporizer 61, described intergrade vaporizer 62 are connected with described fresh water storage tank 7 respectively with the condensation water outlet of described final evaporator 63, and are connected with pumped vacuum systems 17 respectively.Each vaporizer in described multi-stage evaporator is arranged on outside the flash drum of its same level.Described intergrade vaporizer 63 comprises the vaporizer of eight different stages, and with the flash drum one_to_one corresponding in described intergrade flash drum 52.Be appreciated that each vaporizer in described multi-stage evaporator can also be arranged in the flash drum of its same level.
Be appreciated that the electric power that described superposition type electricity generating device that the present embodiment provides can also comprise the wind power generation system that is connected with the generator being arranged on described decompressor 12 and sends to supplement described organic rankine cycle system.Described superposition type electricity generating device also can comprise the electrical energy storage system be connected with the generator being arranged on described decompressor 12, to store the electric power that described organic rankine cycle system sends.Described superposition type electricity generating device can further include the heat reservoir be connected with the high temperature seawater import of described Multi-stage flash steaming pot, operate in order to can maintain the described solar energy ocean thermal energy superposition type electricity generating device that utilizes when bad weather with the heat stored in high temperature seawater, described heat reservoir can be phase-change material heat reservoir.
The utility model embodiment also provides the using method of above-mentioned superposition type electricity generating device to comprise:
Form water vapour: supply 1 pump by surface seawater and extract described surface seawater and be transported in described suction booster 3, described surface seawater is transported in described solar water heater 4 by described suction booster 3; Described surface seawater becomes temperature to be the high temperature seawater of 120 DEG C by described solar water heater 4, and described high temperature seawater is input to formation temperature in described chopped-off head flash drum 51 and is approximately chopped-off head water vapour and the chopped-off head concentrated seawater of 100 DEG C, described chopped-off head water vapour is passed in described chopped-off head vaporizer 61; Described chopped-off head concentrated seawater forms intergrade water vapour and intergrade concentrated seawater in described intergrade flash drum 52, described intergrade water vapour is transported in described intergrade vaporizer 62, and described intergrade concentrated seawater is passed in described final stage flash drum 53; Intergrade concentrated seawater is wherein become final stage water vapour and the final stage concentrated seawater that temperature is approximately 16 DEG C by described final stage flash drum 53, and described final stage water vapour is passed in described final evaporator 63, and described final stage concentrated seawater is discharged in seawater.
Described organic Rankine power generation system generating: start described pumped vacuum systems, described final evaporator 63 is by entering the described liquid organic working medium of described final stage water vapour heating wherein, liquid organic working medium after heating is transported in described intergrade vaporizer 62, meanwhile, described final stage water vapour is condensed into fresh water and is transported in described fresh water storage tank 7 by the condensation water outlet of described final evaporator 63; Liquid organic working medium in described intergrade vaporizer 62 is delivered in described chopped-off head vaporizer 61 after again being heated by the intergrade water vapour entered wherein, and described middle water vapour is then condensed into fresh water and is transported in described fresh water storage tank 7 by the condensation water outlet of described intergrade vaporizer 62; The liquid organic working medium entered wherein is heated into described organic working medium steam by described chopped-off head water vapour by described chopped-off head vaporizer 61, and described organic working medium steam is passed in described decompressor 12, described chopped-off head water vapour is then condensed into fresh water and is transported in described fresh water storage tank 7 by the condensation water outlet of described chopped-off head vaporizer 61; Described organic working medium steam to be delivered in described decompressor 12 by the organic working medium vapor outlet port of described vaporizer 6 and is promoted described decompressor 12 acting generating; Exhaust steam after acting enters in described condenser 14 is extracted less than 200 meters, sea level by described deep layer Mare Frigoris water supply pump 16 and temperature is approximately the deep sea water condensation of 4 DEG C, liquefy organic working medium; Described liquid organic working medium escapes and enter in described organic working medium liquid container 14 by the liquid organic working medium outlet of described condenser 13; The liquid organic working medium flowed out from described organic working medium liquid container 14 is transported in described multi-stage evaporator by described organic working medium pump 15, to proceed organic Rankine power generation cycle.Described organic Rankine power generation system is by utilizing solar energy heating surface seawater, and high temperature seawater is passed in described flash drum 5 and form water vapour, think the energy providing described decompressor 12 to do work generating, also utilize deep sea water to cool acting exhaust steam, make full use of solar energy and ocean thermal energy generating.
Refer to Fig. 2, the utility model second embodiment provides a kind of solar energy ocean thermal energy superposition type electricity generating device, the superposition type electricity generating device that the present embodiment provides is substantially identical with the superposition type electricity generating device that the first embodiment provides, difference is that the superposition type electricity generating device that the present embodiment provides also comprises the high temperature seawater circulatory system, and the seawater desalination system be connected with the condensation water outlet of described vaporizer.
Particularly, the high temperature seawater circulatory system that the present embodiment provides includes the mixing tank 2 connecting described suction booster 3 and described Multi-stage flash steaming pot 5.Described mixing tank 2, described suction booster 3, described solar water heater 4 and described Multi-stage flash steaming pot 5 are in turn connected to form high temperature seawater circulation loop.In the present embodiment, the temperature of surface seawater is approximately 20 DEG C.
The filter 9 that the water transport port that described seawater desalination system includes the condensed water storage tank 7 be connected with the condensation water outlet of described vaporizer 6, the compression pump 8 be connected with described condensed water storage tank 7 and described compression pump 8 connects and the fresh water storage tank 11 be connected with described filter 9 respectively and sparge water storage tank 10.In the present embodiment, described filter 9 is reverse osmosis membrane filt, is mainly used in removing the chlorion that cools from described vaporizer 6 in the condensed water condensed out to provide more highly purified pure water.Desalination water in described fresh water storage tank 11 can as potable water, and the desalination water in described sparge water storage tank 10 can be used as the nonpotable water such as bathing.
The using method of the above-mentioned superposition type electricity generating device that the utility model embodiment provides is substantially identical with the using method of the superposition type electricity generating device that the first embodiment provides, and difference is the process of described formation water vapour and the working procedure of described seawater desalination system.
Form water vapour: the surface seawater by described surface seawater supply pump 1 temperature being approximately 4 DEG C is transported in described mixing tank 2; Described surface seawater is delivered in described solar water heater 4 by described suction booster 3 by described mixing tank 2; The high temperature seawater of heating of seawater to 90 that described suction booster 3 send by described solar water heater 4 DEG C ~ 100 DEG C, and this high temperature seawater is transported to the water vapor and concentrated seawater that become in described Multi-stage flash steaming pot 5 and be approximately 90 DEG C; The vapor outlet port of described Multi-stage flash steaming pot 5 is connected with described vaporizer 6, is delivered to by described water vapour in described vaporizer 6; The seawer outlet of described Multi-stage flash steaming pot 5 is connected with described mixing tank 2, the higher temperature concentrated seawater that has wherein is discharged in described mixing tank 2, mix with described surface seawater, and delivered in described solar water heater 4 by described suction booster 3 together, proceed high temperature seawater circulation.Reclaimed the concentrated seawater with higher temperature of described Multi-stage flash steaming pot 5 discharge by described mixing tank 2, the waste heat of described concentrated seawater can be utilized, reduce the energy consumption of described solar water heater 4, be conducive to energy saving.
Described seawater desalination system: the described water vapour that described Multi-stage flash steaming pot 5 is discharged is passed in described vaporizer 6 and is become condensed water by described liquid organic working medium cooling, described condensed water is discharged by its condensation-water drain by described vaporizer 6, and by condensed water storage tank 7 described in described condensed water; Described condensed water is delivered in described filter 9 by described compression pump 8 after discharging from described condensed water storage tank 7; Described condensed water removes out chlorion wherein in described filter 9, and described condensed water is divided into not chloride ion-containing and can be used for the potable water drunk and containing chlorion and impotable nonpotable water; Described potable water is stored in described fresh water storage tank 11 by the drinking water outlet of described filter 9, and described nonpotable water is stored in described sparge water storage tank 10 by the nonpotable water outlet of described filter 9.Therefore, described seawater desalination system mainly utilize the liquid organic working medium in described vaporizer 6 to cool water vapour that described Multi-stage flash steaming pot 5 discharges and prepare fresh water.
So the above-mentioned superposition type electricity generating device that the utility model embodiment provides utilizes solar energy heating surface seawater and is passed into by high temperature seawater in described Multi-stage flash steaming pot and forms water vapour; Liquid organic working medium in described vaporizer is heated into organic working medium steam by this water vapour; Described organic working medium steam drives described decompressor to do work and generates electricity, and deep sea water is drawn in described condenser, for cooling acting exhaust steam wherein, utilizes solar energy and the generating of ocean thermal energy circulation continuous to complete; The organic working medium simultaneously also utilizing described water vapour to heat in described vaporizer prepares fresh water with condensation.Therefore, the above-mentioned superposition type electricity generating device that the present embodiment provides achieves and makes full use of while solar energy supplements ocean thermal energy generating, can also obtain fresh water, improve energy utilization rate, and reduce desalination of sea water cost.
Finally should be noted that: above embodiment is only in order to illustrate that the technical solution of the utility model is not intended to limit; Although be described in detail the utility model with reference to preferred embodiment, those of ordinary skill in the field have been to be understood that: still can modify to embodiment of the present utility model or carry out equivalent replacement to portion of techniques feature; And not departing from the spirit of technical solutions of the utility model, it all should be encompassed in the middle of the technological scheme scope of the utility model request protection.
Claims (10)
1. a solar energy ocean thermal energy superposition type electricity generating device, it is characterized in that: it includes the solar water heater for heated surface layer seawater, the Multi-stage flash steaming pot be connected is exported with the high temperature seawater of described solar water heater, the deep layer Mare Frigoris water supply pump of cooling water is provided with described multistage flash evaporation tank connected organic Rankine power generation system with for described organic Rankine power generation system, described organic Rankine power generation system includes and connects successively and form the vaporizer in organic Rankine power generation cycle loop, the decompressor of generator is installed, condenser, organic working medium liquid container and organic working medium pump, wherein, described vaporizer is connected with described Multi-stage flash steaming pot.
2. superposition type electricity generating device according to claim 1, is characterized in that: comprise the fresh water storage tank be communicated with the condensation water outlet of described vaporizer further.
3. superposition type electricity generating device according to claim 1 and 2, is characterized in that: described vaporizer is with described Multi-stage flash steaming pot one_to_one corresponding and the multi-stage evaporator be communicated with.
4. superposition type electricity generating device according to claim 3, is characterized in that: comprise the pumped vacuum systems be connected with described multi-stage evaporator further.
5. superposition type electricity generating device according to claim 4, it is characterized in that: the organic working medium vapor outlet port of the chopped-off head vaporizer in described multi-stage evaporator is connected with described decompressor, the liquid organic working medium import of the final evaporator in described multi-stage evaporator is connected with described organic working medium delivery side of pump.
6. superposition type electricity generating device according to claim 5, is characterized in that: the vaporizers at different levels in described multi-stage evaporator are arranged on the outside or inside of the flash drum of described Multi-stage flash steaming pot corresponding level.
7. superposition type electricity generating device according to claim 1, it is characterized in that: comprise surface seawater supply pump, mixing tank and suction booster further, wherein, described mixing tank, described suction booster, described solar water heater and described Multi-stage flash steaming pot connect and compose high temperature seawater circulation loop successively, and described mixing tank is connected with described surface seawater supply pump.
8. superposition type electricity generating device according to claim 1, is characterized in that: comprise the wind power generation system be connected with the generator be arranged on described decompressor further.
9. superposition type electricity generating device according to claim 1, is characterized in that: comprise the electrical energy storage system be connected with the generator be arranged on described decompressor further.
10. superposition type electricity generating device according to claim 1, is characterized in that: comprise the heat reservoir be connected with the high temperature seawater import of described Multi-stage flash steaming pot further.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420727749.1U CN204267237U (en) | 2014-11-28 | 2014-11-28 | Solar energy ocean thermal energy superposition type electricity generating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420727749.1U CN204267237U (en) | 2014-11-28 | 2014-11-28 | Solar energy ocean thermal energy superposition type electricity generating device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204267237U true CN204267237U (en) | 2015-04-15 |
Family
ID=52802108
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420727749.1U Expired - Fee Related CN204267237U (en) | 2014-11-28 | 2014-11-28 | Solar energy ocean thermal energy superposition type electricity generating device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204267237U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104405600A (en) * | 2014-11-28 | 2015-03-11 | 郑州大学 | Solar energy and ocean temperature difference energy cascading type power generation device and utilization method thereof |
| CN106545476A (en) * | 2016-12-26 | 2017-03-29 | 天津大学 | A kind of flash distillation active control system and method for adapting to solar energy organic Rankine bottoming cycle |
-
2014
- 2014-11-28 CN CN201420727749.1U patent/CN204267237U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104405600A (en) * | 2014-11-28 | 2015-03-11 | 郑州大学 | Solar energy and ocean temperature difference energy cascading type power generation device and utilization method thereof |
| CN106545476A (en) * | 2016-12-26 | 2017-03-29 | 天津大学 | A kind of flash distillation active control system and method for adapting to solar energy organic Rankine bottoming cycle |
| CN106545476B (en) * | 2016-12-26 | 2023-03-07 | 天津大学 | Flash evaporation active control system and method adaptive to solar organic Rankine cycle |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104405600A (en) | Solar energy and ocean temperature difference energy cascading type power generation device and utilization method thereof | |
| He et al. | Application of alternative energy integration technology in seawater desalination | |
| CN202924780U (en) | Seawater desalination and power generation comprehensive utilization device | |
| CN102241420B (en) | Solar seawater desalination device and seawater desalination method thereof | |
| CN103613153B (en) | The system of a kind of nuclear power and low-temperature multiple-effect seawater desalination coupled cogeneration | |
| CN104671314B (en) | A kind of lens type solar energy sea water desalinating plant | |
| CN202023706U (en) | Device for carrying out flash evaporation electricity generation and recovering distilled water by using terrestrial heat | |
| CN201737726U (en) | Solar seawater-desalinating device adopting passive flash evaporation technique | |
| CN103663835A (en) | Hybrid MSF (multistage flash)/RO (reverse osmosis) sea water desalination system | |
| CN102336448B (en) | Saline treatment system and method | |
| CN101723476B (en) | Seawater desalination device employing solar energy and vapor compressing distillation | |
| CN103708665A (en) | Renewable energy combined with hot-film coupling seawater desalination and salt manufacturing system | |
| CN201338952Y (en) | Device capable of comprehensively utilizing solar energy to desalinize seawater | |
| CN106745428A (en) | A kind of heat collection type solar multistage flash evaporation seawater desalting device and method | |
| CN201914937U (en) | Seawater desalination system with multilevel heat exchanges | |
| CN103758712A (en) | Seawater desalination system driven by combination of solar energy and ocean thermal energy | |
| CN207943899U (en) | A kind of MVR seawater desalination systems | |
| CN103216283A (en) | Rankine cycling and seawater freshening dual-efficiency waste heat recovery system | |
| CN101205087A (en) | Highly effective sea-water brackish water distillatory using renewable energy | |
| CN204939171U (en) | A kind of portable nuclear desalination system | |
| CN204661346U (en) | Solar cogeneration seawater desalination system | |
| CN108439675A (en) | A kind of solar energy desalination utilization system and method | |
| CN105329962B (en) | Solar energy composite heat pump desalinization and confession domestic water system and method | |
| CN204267237U (en) | Solar energy ocean thermal energy superposition type electricity generating device | |
| CN200995984Y (en) | Efficient multistage cryogenic air-electric seawater desalination plant |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150415 Termination date: 20171128 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |