CN202811240U - Autoclave technology salinity difference energy generating set - Google Patents
Autoclave technology salinity difference energy generating set Download PDFInfo
- Publication number
- CN202811240U CN202811240U CN2012204869879U CN201220486987U CN202811240U CN 202811240 U CN202811240 U CN 202811240U CN 2012204869879 U CN2012204869879 U CN 2012204869879U CN 201220486987 U CN201220486987 U CN 201220486987U CN 202811240 U CN202811240 U CN 202811240U
- Authority
- CN
- China
- Prior art keywords
- reaction chamber
- fresh water
- solar heater
- pipe
- reaction room
- 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
Images
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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/30—Energy from the sea, e.g. using wave energy or salinity gradient
Landscapes
- Engine Equipment That Uses Special Cycles (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The utility model provides an autoclave technology salinity difference energy generating set and belongs to the technical field of generating plant. The autoclave technology salinity difference energy generating set comprises a reaction room, a motor, a fresh water inlet pipe, a solar heater, a sea water inlet pipe, a water-pouring type condenser, a separator and a turbine. The fresh water inlet pipe is arranged on the lower left portion of the reaction room, the sea water inlet pipe is arranged on the lower right portion of the reaction room, the upper portion of the reaction room is connected with one end of the water pouring type condenser through a pipe, the other end of the water pouring type condenser is connected with one end of the solar heater through a pipe, the other end of the solar heater is connected with the fresh water inlet pipe through a pipe, the separator is installed in the middle of the reaction room, the motor is arranged in the outer side of the reaction room, a shaft of the motor penetrates into reaction room and is installed with the turbine, and the turbine is located between the reaction room and the separator. The autoclave technology salinity difference energy generating set adds the solar heater, manufactures the separator into concavo-convex and bending shape, and the combined action of the solar heater and the separator enables the system to work effectively and circularly for a long time.
Description
Technical field
The utility model relates to a kind of electricity generating device, and particularly a kind of autoclave method salt error energy electricity generating device belongs to the power generating equipment technical field.
Background technique
The poor energy of chemical potential between the seawater that salt error can refer between seawater and the fresh water or two kinds of salt concentrations are different is the ocean energy that occurs with the chemical energy form; The main existence and the He Hai jointing place, simultaneously, salt lake and the underground salt mine in the abundant area of fresh water also can utilize the salt error energy; Salt error can be a kind of renewable energy sources of energy density maximum in the ocean energy.
Ocean salinity energy generating major way has osmometry, vapor pressure method and anti-electrodialysis battery method; Here mainly vapor pressure method is described.
Vapor pressure method is owing to fresh water under same temperature gets soon than evaporation of seawater, therefore seawater saturated vapor pressure on one side is more much lower on one side than fresh water, above the indoor steam of sky can be very fast flows to seawater above the fresh water, just can generate electricity as long as load onto like this steam turbine.
Existing vapor pressure method device has deficiency: the heat that produces when the heat that absorbs during owing to water vapor moves greater than steam, so that the dilute side drop in temperature is faster than seawater side, the transfer of this heat can make system work process slow down finally to stop, and this is a problem that urgent need will solve.
Summary of the invention
In order to solve the deficiency of existing vapor pressure method device: the heat that produces when the heat that absorbs during owing to water vapor moves greater than steam, the problem that causes system work process to slow down finally stopping so that the dilute side drop in temperature is faster than seawater side, the utility model proposes a kind of autoclave method salt error can electricity generating device.
The technological scheme that the utility model adopts is:
Autoclave method salt error energy electricity generating device, comprise reaction chamber, generator, the fresh water inlet tube, solar heater, the seawer inlet pipe, Sprinking condenser, demarcation strip and steam turbine, the reaction chamber lower left quarter is provided with the fresh water inlet tube, the reaction chamber lower right part is provided with the seawer inlet pipe, reaction chamber top is connected to an end of Sprinking condenser by pipe, the other end of Sprinking condenser is connected to an end of solar heater by pipe, the other end of solar heater is connected on the fresh water inlet tube by pipe, demarcation strip is installed in the middle of the reaction chamber, generator is arranged on the reaction chamber outside, axle on the generator is inserted into reaction chamber inside and steam turbine is installed together, and steam turbine is between reaction chamber and demarcation strip.
Demarcation strip is concavo-convex bending, and demarcation strip separates fresh water and seawater in the reaction chamber both sides.
Advantage of the present utility model: this device has increased solar heater in the circulatory system, solar heater can be increased the temperature of condensed water, like this can be so that the temperature of fresh water one side raises, improved the evaporation rate of fresh water, this device also is processed into demarcation strip concavo-convex bending, so that there is an exchange heat between fresh water and seawater, heat energy that can the absorption portion water vapor will absorb from the seawater side, the evaporation of promotion dilute side steam; The acting in conjunction of solar heater and demarcation strip so that system can be permanently effective periodic duty.
Description of drawings
Fig. 1 is the schematic diagram of autoclave method salt error energy electricity generating device;
Among the figure: 1, reaction chamber 2, generator 3, fresh water inlet tube 4, solar heater 5, seawer inlet pipe 6, Sprinking condenser 7, demarcation strip 8, steam turbine.
Embodiment
Below in conjunction with drawings and Examples the utility model is further described.
As shown in the figure, autoclave method salt error energy electricity generating device, comprise reaction chamber 1, generator 2, fresh water inlet tube 3, solar heater 4, seawer inlet pipe 5, Sprinking condenser 6, demarcation strip 7 and steam turbine 8, reaction chamber 1 lower left quarter is provided with fresh water inlet tube 3, reaction chamber 1 lower right part is provided with seawer inlet pipe 5, reaction chamber 1 top is connected to an end of Sprinking condenser 6 by pipe, the other end of Sprinking condenser 6 is connected to an end of solar heater 4 by pipe, the other end of solar heater 4 is connected on the fresh water inlet tube 3 by pipe, demarcation strip 7 is installed in the middle of the reaction chamber 1, generator 2 is arranged on reaction chamber 1 outside, axle on the generator 2 is inserted into reaction chamber 1 inside and steam turbine 8 is installed together, and steam turbine 8 is between reaction chamber 1 and demarcation strip 7.
The effect of solar heater 4 is that condensed water is heated; The effect of Sprinking condenser 6 is water vapor to be cooled down become condensed water.
Working principle: the working principle of this device is similar with the working principle of existing apparatus, major technique has increased solar heater 4 and demarcation strip 7 has been processed into concavo-convex bending in the circulatory system, fresh water enters reaction chamber 1 one sides from fresh water inlet tube 3, seawater enters reaction chamber 1 opposite side from seawer inlet pipe 5, fresh water gets soon than evaporation of seawater under same temperature, therefore seawater saturated vapor pressure on one side is more much lower on one side than fresh water, above the indoor steam of sky can be very fast flows to seawater above the fresh water, steam will be with and allow steam turbine 8 rotate like this, steam turbine 8 can drive generator 2 generatings, steam can flow in the Sprinking condenser 6 and condense into condensed water along with the pipe on top, condensed water can flow to heating in the solar heater 4 along with pipe, fresh water and the new fresh water of heat converge at fresh water inlet tube 3 and enter fresh water one side, reenter the circulatory system; Because solar heater 4 can be increased the temperature of condensed water, like this can be so that the temperature of fresh water one side raises, improved the evaporation rate of fresh water, fragmenting plate 7 is processed into concavo-convex bending simultaneously, so that there is an exchange heat between fresh water and seawater, heat energy that can the absorption portion water vapor will absorb from the seawater side promotes the evaporation of dilute side steam, both actings in conjunction so that system can be permanently effective periodic duty.
Claims (2)
1. the autoclave method salt error can electricity generating device, comprise reaction chamber (1), generator (2), fresh water inlet tube (3), solar heater (4), seawer inlet pipe (5), Sprinking condenser (6), demarcation strip (7) and steam turbine (8), it is characterized in that: reaction chamber (1) lower left quarter is provided with fresh water inlet tube (3), reaction chamber (1) lower right part is provided with seawer inlet pipe (5), reaction chamber (1) top is connected to an end of Sprinking condenser (6) by pipe, the other end of Sprinking condenser (6) is connected to an end of solar heater (4) by pipe, the other end of solar heater (4) is connected on the fresh water inlet tube (3) by pipe, demarcation strip (7) is installed in the middle of the reaction chamber (1), generator (2) is arranged on reaction chamber (1) outside, axle on the generator (2) is inserted into reaction chamber (1) inside and steam turbine (8) is installed together, and steam turbine (8) is positioned between reaction chamber (1) and the demarcation strip (7).
2. can electricity generating device according to the described autoclave method salt error of claims 1, it is characterized in that: demarcation strip (7) is concavo-convex bending, and demarcation strip (7) separates fresh water and seawater in reaction chamber (1) both sides.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012204869879U CN202811240U (en) | 2012-09-24 | 2012-09-24 | Autoclave technology salinity difference energy generating set |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012204869879U CN202811240U (en) | 2012-09-24 | 2012-09-24 | Autoclave technology salinity difference energy generating set |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202811240U true CN202811240U (en) | 2013-03-20 |
Family
ID=47870125
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012204869879U Expired - Fee Related CN202811240U (en) | 2012-09-24 | 2012-09-24 | Autoclave technology salinity difference energy generating set |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202811240U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105736269A (en) * | 2016-05-06 | 2016-07-06 | 中国矿业大学 | Heat pump-reinforced salt-concentration-differential electricity generation device by vapor differential pressure energy method under positive temperature difference |
| CN109426290A (en) * | 2017-09-05 | 2019-03-05 | 韩国能量技术研究院 | Power self-support type intelligence farm system based on salt error power generation |
| US11502323B1 (en) | 2022-05-09 | 2022-11-15 | Rahul S Nana | Reverse electrodialysis cell and methods of use thereof |
| US11502322B1 (en) | 2022-05-09 | 2022-11-15 | Rahul S Nana | Reverse electrodialysis cell with heat pump |
| US11855324B1 (en) | 2022-11-15 | 2023-12-26 | Rahul S. Nana | Reverse electrodialysis or pressure-retarded osmosis cell with heat pump |
-
2012
- 2012-09-24 CN CN2012204869879U patent/CN202811240U/en not_active Expired - Fee Related
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AU2016405486B9 (en) * | 2016-05-06 | 2020-06-11 | China University Of Mining And Technology | Heat pump-reinforced salt-concentration-differential power generation device using vapour differential pressure energy method under positive temperature difference |
| WO2017190505A1 (en) * | 2016-05-06 | 2017-11-09 | 中国矿业大学 | Heat pump-reinforced salt-concentration-differential power generation device using vapour differential pressure energy method under positive temperature difference |
| CN105736269B (en) * | 2016-05-06 | 2018-04-06 | 中国矿业大学 | Steam pressure difference energy method salt error TRT under the positive temperature difference that a kind of heat pump is strengthened |
| CN105736269A (en) * | 2016-05-06 | 2016-07-06 | 中国矿业大学 | Heat pump-reinforced salt-concentration-differential electricity generation device by vapor differential pressure energy method under positive temperature difference |
| AU2016405486B2 (en) * | 2016-05-06 | 2020-01-30 | China University Of Mining And Technology | Heat pump-reinforced salt-concentration-differential power generation device using vapour differential pressure energy method under positive temperature difference |
| CN109426290B (en) * | 2017-09-05 | 2021-12-07 | 韩国能量技术研究院 | Energy self-sufficient type intelligent farm system based on salt difference power generation |
| CN109426290A (en) * | 2017-09-05 | 2019-03-05 | 韩国能量技术研究院 | Power self-support type intelligence farm system based on salt error power generation |
| US11502323B1 (en) | 2022-05-09 | 2022-11-15 | Rahul S Nana | Reverse electrodialysis cell and methods of use thereof |
| US11502322B1 (en) | 2022-05-09 | 2022-11-15 | Rahul S Nana | Reverse electrodialysis cell with heat pump |
| US11563229B1 (en) | 2022-05-09 | 2023-01-24 | Rahul S Nana | Reverse electrodialysis cell with heat pump |
| US11611099B1 (en) | 2022-05-09 | 2023-03-21 | Rahul S Nana | Reverse electrodialysis cell and methods of use thereof |
| US11699803B1 (en) | 2022-05-09 | 2023-07-11 | Rahul S Nana | Reverse electrodialysis cell with heat pump |
| US11855324B1 (en) | 2022-11-15 | 2023-12-26 | Rahul S. Nana | Reverse electrodialysis or pressure-retarded osmosis cell with heat pump |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202811240U (en) | Autoclave technology salinity difference energy generating set | |
| CN103939306B (en) | A kind of two loop-type solar heat power generation systems | |
| CN201706478U (en) | Heat-recovering type demineralized water heating system | |
| CN102583607A (en) | Comprehensive utilization device of renewable energy sources | |
| CN103011473B (en) | Device and method for solar seawater desalination and concentrated seawater resource extraction | |
| CN207404876U (en) | A kind of natural energy resources formula desalination plant | |
| CN203594565U (en) | Steam-driven driving system for solar thermal power generation large power pump | |
| CN103615357B (en) | A kind of wind energy, solar energy, sea wave energy circulation complemental power-generation and seawater desalination system | |
| CN102384048B (en) | Low-temperature-difference solar energy and ocean energy combined power generation system | |
| CN202100286U (en) | Low-pressure heating device of power plant | |
| CN103322551A (en) | Method for recycling energy of high pressure heater in thermal power plant | |
| CN203529968U (en) | Solar wind-power combination seawater desalination device | |
| CN103759237A (en) | Medium-temperature solar steam system | |
| CN204851350U (en) | Utilize living water heating system of power plant's exhaust steam waste heat | |
| CN204554779U (en) | Coal-fired station's bootstrap system | |
| CN203214253U (en) | Heat conducting oil heat storage heat exchanging device for solar photo-thermal power generating | |
| CN201309841Y (en) | Solar sea water desalting device | |
| CN204987552U (en) | Take power generation facility's water resource heat pump | |
| CN201874624U (en) | Seawater steam generator equipment | |
| CN204961185U (en) | Solar energy low temperature steam electric power system | |
| CN204987181U (en) | Utilize heating system of deep geothermol power low temperature electricity generation | |
| CN203024348U (en) | Waste heat utilization system with solution control device | |
| CN203907563U (en) | Medium-temperature solar steam system | |
| CN204227750U (en) | Cooling water of thermoelectric plant heat recovery steam drives compression type heat heat pump heating system | |
| CN203333331U (en) | System capable of carrying out sea water desalination and cooling-heating-power cogeneration at same time |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130320 Termination date: 20130924 |