CN212504406U - Saline and alkaline water desalination circulation system based on micro-grid power supply - Google Patents
Saline and alkaline water desalination circulation system based on micro-grid power supply Download PDFInfo
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- CN212504406U CN212504406U CN202020237061.0U CN202020237061U CN212504406U CN 212504406 U CN212504406 U CN 212504406U CN 202020237061 U CN202020237061 U CN 202020237061U CN 212504406 U CN212504406 U CN 212504406U
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Abstract
The utility model discloses a saline and alkaline water desalination circulation system based on little electric wire netting power supply. The system comprises a water taking subsystem, a filtering subsystem, a thermal evaporation subsystem, a salt sunning system and a micro-grid system, and salt and transpiration condensate in saline-alkali soil are effectively separated by utilizing solar photo-thermal, so that water resource conversion and salt transfer are realized, and comprehensive utilization is realized. Wherein the water taking subsystem mainly takes water from a field side water pool; the filtering subsystem carries out primary separation of salt and water through a nanofiltration membrane system and a reverse osmosis membrane system; the thermal evaporation subsystem heats concentrated brine and alkaline water by solar energy; the salt drying system dries the heated strong brine in the sun to separate out crystal salt; the micro-grid system is responsible for providing power energy supply for the whole system through photovoltaic power generation. The utility model discloses can regard as one of the important ways of alleviating the water resource shortage and improving saline and alkaline land, have the significance to improving arid area people quality of life, improving desert arid area ecological environment.
Description
Technical Field
The utility model relates to a little electric wire netting engineering application and ecological saltwater desalination field especially relate to a saltwater desalination circulation system based on little electric wire netting power supply.
Background
The shortage of fresh water resources in arid regions has become a serious problem in many countries, and even wars may be caused. The rainfall of western and northern parts of China is extremely limited every year, the climate is extremely arid, the annual rainfall of the regions is even less than 100mm, and the water resource shortage, the soil salinization and the land desertification are three prominent problems threatening the survival of local residents. At present, the agricultural water supply department in China turns to and considers the cyclic utilization of saline-alkali water in desertification areas to relieve the drought pressure and the increasingly intensified contradiction of water supply, but the saline-alkali water is lack of effective treatment technology, so that the benefit and the disadvantage of the irrigation and utilization of saline-alkali water resources are not well known, the saline-alkali water discharged from irrigation areas causes more serious secondary pollution to soil after being irrigated again, and the influence on the yield and the quality of crops is great. A large amount of untreated saline water discharged from farmlands in arid regions not only wastes limited water resources, but also brings threats to agricultural production and environment. The water discharged from the alkali discharge ditch of the irrigation area enters the river, and the mineralization degree of the river water body is continuously increased, so that the further ecological environment problem in the range of the drainage basin is caused. In view of the fact that sunlight is relatively sufficient in arid areas, the use of solar heat to separate salt from water is an effective means to solve the above problems. The method utilizes solar photo-thermal to effectively separate salt and transpiration condensate in saline-alkali water, realizes water resource conversion and salt transfer and comprehensively utilizes the salt and the solar photo-thermal to serve as one of important ways for relieving water resource shortage and effectively improving the saline-alkali water, is not only a major research topic facing water conservancy and agricultural science, but also has important strategic significance for improving the living quality of local people and improving the ecological environment of a drainage basin.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to prior art not enough, provide a saline and alkaline water desalination circulation system based on little electric wire netting power supply to alleviate arid pressure and the water supply contradiction that aggravates day by day, solve the problem that arid and land salinization area fresh water resources are not enough. The utility model discloses the technical scheme who adopts as follows:
saline and alkaline water desalination circulation system based on little grid power supply, its characterized in that, the system includes: the system comprises a water taking subsystem, a filtering subsystem, a thermal evaporation subsystem, a solar salt system and a micro-grid system; the water taking subsystem is provided with a water inlet tank of the filtering subsystem, and the filtering subsystem is connected with the water inlet tank through a pipeline; a fresh water outlet of the filtering subsystem is connected with a fresh water tank, a concentrated water outlet of the filtering subsystem is connected with a strong brine tank, the strong brine tank is connected with the thermal evaporation subsystem through a pipeline, and concentrated strong brine water is heated through solar energy; the salt drying system dries the heated strong brine in the sun to separate out crystal salt; the micro-grid system is responsible for providing power energy supply for the whole set of saline-alkali water desalination circulation system through photovoltaic power generation. The water intaking subsystem includes: a water taking pump; a sand filtration tank; a water inlet tank. The main function is to take water from the field through a water taking pump and store the water into a sand filtration tank, preliminarily precipitate large impurities such as sand, stone, mud and grass in water quality, store salt and alkali water after sand filtration into a water inlet tank and enter a nanofiltration subsystem.
The water taking subsystem comprises a water taking pump, a sand filter tank and a water inlet tank; the water taking pump, the sand filter tank and the water inlet tank are sequentially connected through a pipeline.
The filtering subsystem comprises a nanofiltration membrane system, a concentrated water tank and a reverse osmosis membrane system; the nanofiltration membrane system is arranged for primarily separating chloride ions, water molecules and other divalent and high-valent ions; the saline-alkali water containing bivalent and high-valent ions enters a concentrated water tank and is discharged; further separating by a strong brine reverse osmosis system containing chloride ions; the unit system is a high-pressure concentration system, 90% of weak solution is recycled, so that the water amount entering a subsequent thermal evaporation subsystem is reduced, and the heat required by thermal evaporation is reduced;
the inlet of the nanofiltration membrane system is connected with the water inlet tank of the water taking subsystem through a pipeline, the light salt water outlet of the nanofiltration membrane system is connected with the reverse osmosis membrane system, and the concentrated water outlet of the nanofiltration membrane system is connected with the concentrated water tank;
the fresh water outlet of the reverse osmosis membrane system is connected with the fresh water tank, and the strong brine outlet is connected with the strong brine tank.
The thermal evaporation subsystem includes: a condenser; a photovoltaic heating system; an evaporator; the cold saline-alkali water is heated in the condenser by the steam generated by the evaporator and then enters the photovoltaic heating system, the saline-alkali water heated by the foundation enters the photovoltaic heating system for heating, the heating efficiency is improved, the generated steam condensate water can be used as distilled water, and the steam is obtained by evaporating the saline-alkali water; the structure includes:
the brine-alkali water inlet of the condenser is connected with the concentrated water tank of the filtering subsystem through a pipeline, the brine-alkali water outlet of the condenser is connected with the photovoltaic heating system, the condenser is provided with a heating medium inlet and a condensed water outlet, and the heating medium inlet is connected with the steam outlet of the evaporator through a pipeline;
the outlet of the heated saline water of the photovoltaic heating system is connected with the inlet of the evaporator;
still connect the pipeline between the saline and alkaline water export of evaporimeter and the import of photovoltaic heating system, the saline and alkaline water temperature after the evaporation descends and does not reach and shone salt concentration, then utilizes the circulating pump to pump into photovoltaic heating system and continue heating cycle.
The evaporator adopts a flash evaporator, and can be further provided with an electric heating device, the electric heating device is connected with the microgrid system, and the microgrid system can supply power to heat and evaporate saline water in the evaporator. When the weather is hot, the photovoltaic generated energy is large, and the generated energy of the microgrid system is larger than the power consumption, the redundant electric energy is used for heating, and the evaporation of the evaporator is accelerated.
The evaporator is provided with a vacuum pump, so that the whole thermal evaporation subsystem can be in vacuum, and the concentrated saline water reaching the standard is guided to the collection tank.
The microgrid subsystem comprises: a photovoltaic power generation system; a support structure; a sink system; an inverter system; an energy storage battery system. The system adopts a 'power generation-charging' integrated design, and uses the electric energy generated by a solar panel for the production electricity of the saline-alkali water desalination system (mainly supplying electricity for instruments and meters in the system, electricity for a control system, electricity for a motor, electricity for a water pump, electricity for a filtering subsystem and electricity for a heating pipe in an evaporator); meanwhile, redundant electric energy is stored in the energy storage system, so that on one hand, the electricity of the system is supplemented when the sunlight is insufficient; and on the other hand, the system power subsystem is provided with stable power supply so as to maintain the balance and stability of the whole system power supply load. The whole system is uniformly managed and dispatched by the communication and control system to use the electricity of each subsystem, and the stable operation of the whole system is kept.
The utility model discloses a saltwater alkaline desalination circulation system accessible process control system (communication and control system) control based on little power grid power supply, include: PLC, data communication system (MODBUSRTU), human-machine interface unit (HMI), rack, Uninterrupted Power Supply (UPS). The communication and control system takes a PLC as a core, monitors and controls the equipment state through DI, DO, AI and AO, and simultaneously communicates with a photovoltaic energy storage control unit (mPPT), an Inverter (INV) and a power distribution system EPM meter through an MODBUSRTU. There are 3 types of Human Machine Interfaces (HMI) including: the system comprises a local workstation, a touch screen and a system for remote monitoring through a 4G gateway VPN.
The utility model discloses a saline and alkaline water desalination circulation system based on little electric wire netting power supply can be used for improving desert arid region ecological environment to gain and showing the effect, it uses this area saline and alkaline water to handle it as irrigation that provides to this region with fresh water, distilled water as the object, and retrieve sodium ion and make it can be utilized, and utilize the regional abundant solar energy of desert arid to supply power for saline and alkaline water desalination circulation system.
The utility model discloses a characteristics mainly embody in following several aspects:
(1) the system can fully utilize local resources and climatic characteristics of arid regions, namely saline-alkali water, sufficient illumination heat and other resources and characteristics, and carry out salt and water separation according to local conditions;
(2) the system considers the characteristics of local geographical distribution limitation and abundant solar energy resources, adopts a micro-grid power supply technology, adopts photovoltaic green energy as all energy sources, and realizes self-sufficiency of electric power;
(3) the system adopts a pure physical separation technology, does not add additional separation agents and chemicals, avoids secondary pollution to local soil and rivers, and has extremely high environmental protection popularization value;
(4) compared with the traditional seawater desalination system, the system has the advantages of lower cost, low equipment price and higher popularization;
(5) compared with the traditional seawater desalination system, the system can reduce the salinity of saline-alkali water, and can also recover sodium ions, sulfate radicals (sulfur elements) and the like through the nanofiltration membrane of the filtration subsystem, wherein the elements are important chemical raw materials, on one hand, the raw materials can reduce the operation cost of the system, and on the other hand, the raw materials have important values for production and life; in addition, some fresh water resources generated by the system have higher water resource purity (such as condensed water of a thermal evaporation subsystem), can be directly drunk or even used as distilled water, and have higher added value and better economic value.
Drawings
FIG. 1 is a schematic diagram of a desalination circulation system based on a microgrid for supplying power;
FIG. 2 is a detailed schematic diagram of portions of the water intake subsystem and the filtration subsystem;
FIG. 3 is a flow diagram of an evaporation subsystem;
FIG. 4 is a schematic diagram of a microgrid subsystem;
FIG. 5 is a process control system (communication and control system) architecture diagram;
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention more clearly understood, the present invention is further described in detail below with reference to the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are for purposes of illustration only and are not intended to limit the invention. Furthermore, the technical features mentioned in the embodiments of the present invention described below can be combined with each other as long as they do not conflict with each other.
The utility model relates to a brine and alkaline water desalination circulation system based on little electric wire netting power supply. The system comprises: the system comprises a water taking subsystem, a filtering subsystem, a thermal evaporation subsystem, a salt sunning system, a micro-grid system and the like, and salt and transpiration condensate in the salt water are effectively separated by utilizing solar photo-thermal, so that water resource conversion and salt transfer are realized, and comprehensive utilization is realized. The water taking subsystem mainly takes water from a field side water pool and performs primary precipitation on large impurities such as sand, stone, mud and grass in water; the filtering subsystem carries out primary separation of salt and water through a nanofiltration membrane system and a reverse osmosis membrane system; the thermal evaporation subsystem heats concentrated brine and alkaline water by solar energy; the salt drying system dries the heated strong brine in the sun to separate out crystal salt; the micro-grid system is responsible for providing power energy supply for the whole system through photovoltaic power generation; the process control system is based on the PLC and carries out process control on the whole system. As one of the important ways of relieving water resource shortage and effectively improving saline-alkali soil, the utility model not only solves the important research subject faced by water conservancy and agricultural science, but also has important strategic significance in improving the life quality of people in arid regions and improving the ecological environment in arid regions of deserts. For explaining the effect of the utility model, the following is to explain the utility model discloses the method carries out the detailed description:
the system comprises: 1) a water intake subsystem; 2) a filtration subsystem; 3) a thermal evaporation subsystem; 4) a salt sun drying system; 5) a microgrid system.
The water taking subsystem comprises: the water taking pump, the sand filter tank and the water inlet tank are sequentially connected through a pipeline. The main function is to take water from the field through a water taking pump and store the water into a sand filtration tank, preliminarily precipitate large impurities such as sand, stone, mud and grass in water quality, store salt and alkali water after sand filtration into a water inlet tank and enter a nanofiltration subsystem.
The filtering subsystem comprises: receive filter membrane system, dense water case, reverse osmosis membrane system, the import of receiving filter membrane system passes through the pipeline and links to each other with the case of intaking of water subsystem, and the light salt water export of receiving filter membrane system links to each other with reverse osmosis membrane system, and the dense water export of receiving filter membrane system links to each other with the dense water case.
A nanofiltration membrane system: the unit system is arranged for primarily separating chloride ions, water molecules and other divalent and high-valent ions; the saline-alkali water containing bivalent and high-valent ions enters a concentrated water tank and is discharged; the dilute brine containing chloride ions is further separated by a reverse osmosis system;
reverse osmosis membrane system: the unit system is a high-pressure concentration system, 90% of weak solution is recovered, so that the water quantity entering a subsequent thermal evaporation subsystem is reduced, and the heat required by thermal evaporation is reduced. Wherein, the fresh water export of reverse osmosis membrane system links to each other with fresh water tank, and the strong brine export links to each other with strong brine tank. The water in the fresh water tank is finally sent to the fresh water tank for irrigation.
Thirdly, the thermal evaporation subsystem comprises: a condenser (heat exchanger), a photovoltaic heating system (solar heating plate), an evaporator; wherein, the strong brine tank of the reverse osmosis membrane system is connected with the lower inlet of the condenser (heat exchanger) through a pipeline. The thermal evaporation subsystem is also equipped with associated instrumentation and piping.
Condenser (heat exchanger): cold saline-alkali water enters the condenser from the inlet and flows out of the condenser from the outlet, and the cold saline-alkali water is used as a continuous cold source and used for cooling hot steam into fresh water; hot steam enters from the steam inlet and is used as a continuous heat source for preheating cold saline-alkali water; finally, the fresh water is collected and taken away from the lower outlet. The cold saline-alkali water passes through the tube bundle (tubule) inside the device, and the tube bundle is divided into an upper part and a lower part, and the lower part tube bundle water flow direction is from the right to the left, and the upper part tube bundle water flow direction is from the left to the right. The water in the lower part flows to the upper part. The hot steam passes through the outer pipe of the device, and the hot steam is filled in the inner space of the whole device after entering and contacts with the pipe bundle to generate heat exchange.
The photovoltaic heating system (solar heating plate) is formed by connecting a plurality of vacuum airing pipes which are horizontally arranged in parallel in series, and the vacuum airing principle is similar to that of a solar hot water pipe. The solar heating device is divided into an upper layer and a lower layer, and the upper layer pipe is arranged in the gap between the lower layer pipes, so that the space is utilized to the maximum, and more vacuum glass pipes can be irradiated by sunlight. The brine-alkali water outlet of the condenser (heat exchanger) is connected with the water inlet (positioned at the lower end) of the photovoltaic heating system (solar heating plate), the preheated brine enters the sun drying pipe to be continuously heated, the water outlet (positioned at the upper end) of the photovoltaic heating system (solar heating plate) is connected with the inlet of the flash tank (evaporator), and the brine-alkali water is discharged into the flash tank (evaporator) to be subjected to gas-liquid separation when the boiling temperature is reached, so that the brine-alkali water outlet and the water inlet (positioned at the lower end) of the photovoltaic heating system. Wherein, the flash tank (evaporimeter) still can link to each other through circulation pipeline and photovoltaic heating system (solar energy hot plate) water inlet (being located the lower extreme), and the salt water temperature after the evaporation descends and does not reach and shine salt concentration, then utilizes the circulating pump suction to shine the pipe and continue heating cycle.
An evaporator: the high-temperature salt water meeting the heat requirement enters an evaporator, the evaporator is subjected to vacuum treatment, the gas-liquid separation speed is higher, and the generated high-temperature steam is rapidly pumped out. And the saline water which does not meet the concentration requirement is pumped out and enters the sun tube to be heated continuously, and the control is needed according to the situation. Once reaching the concentration of the solar salt, the salt water in the evaporator is immediately and completely led out. The evaporator is internally provided with a vacuum pump and is arranged right above the evaporator, and the pumped water vapor can be condensed into distilled water for utilization; meanwhile, the whole thermal evaporation subsystem is in vacuum through the steam pumping process. The fresh water condensed by the steam enters from the upper part of the collecting tank, and is discharged, packaged and transported away after the tank body is fully collected with the fresh water. The lower part of the evaporator is provided with a heating pipe which is connected with a photovoltaic power generation system in the microgrid system, when the weather is hot, the photovoltaic power generation amount is larger, and when the power generation amount of the microgrid system is larger than the power consumption amount, the redundant electric energy is used for heating, so that the evaporation of the evaporator is accelerated.
Fourthly, the micro-grid subsystem comprises: a photovoltaic power generation system; a support structure; a sink system; an inverter system; an energy storage battery system. The supporting structure mainly supports the photovoltaic panel power generation panel and is used as a battery bracket; the photovoltaic power generation panel is connected with the confluence system; the confluence system is connected with the inverter system; the inverter system is connected with the energy storage battery system and the power grid bus, and controls current to enter the bus or be stored by the battery system according to the instruction of the control system; the system adopts a 'power generation-charging' integrated design, and uses the electric energy generated by a solar panel for the production electricity of the saline-alkali water desalination system (mainly supplying electricity for instruments and meters in the system, electricity for a control system, electricity for a motor, electricity for a water pump, electricity for a filtering subsystem and electricity for a heating pipe in an evaporator); meanwhile, redundant electric energy is stored in the energy storage system, so that on one hand, the electricity of the system is supplemented when the sunlight is insufficient; and on the other hand, the system power subsystem is provided with stable power supply so as to maintain the balance and stability of the whole system power supply load. The whole system is uniformly managed and dispatched by the communication and control system to use the electricity of each subsystem, and the stable operation of the whole system is kept.
The utility model discloses accessible process control system (communication and control system) control, include: PLC, data communication system (MODBUSRTU), human-machine interface unit (HMI), rack, Uninterrupted Power Supply (UPS). The communication and control system takes a PLC as a core, monitors and controls the equipment state through DI, DO, AI and AO, and simultaneously communicates with a photovoltaic energy storage control unit (mPPT), an Inverter (INV) and a power distribution system EPM meter through an MODBUSRTU. In addition, the control system is also connected with various sensors, instruments, electric valves, pumps and other equipment in the water taking subsystem, the filtering subsystem, the thermal evaporation subsystem, the solar salt system and other systems through a wired network so as to realize the acquisition of the operation data of the whole system and the realization of real-time control. There are 3 types of Human Machine Interfaces (HMI) including: the system comprises a local workstation, a touch screen and a system for remote monitoring through a 4G gateway VPN.
It will be understood by those skilled in the art that the foregoing is merely a preferred embodiment of the present invention, and is not intended to limit the invention to the particular forms disclosed, but on the contrary, the intention is to cover all modifications, equivalents, and alternatives falling within the spirit and scope of the invention as defined by the appended claims.
Claims (7)
1. Saline and alkaline water desalination circulation system based on little grid power supply, its characterized in that, the system includes: the system comprises a water taking subsystem, a filtering subsystem, a thermal evaporation subsystem, a solar salt system and a micro-grid system; the water taking subsystem is provided with a water inlet tank of the filtering subsystem, and the filtering subsystem is connected with the water inlet tank through a pipeline; a fresh water outlet of the filtering subsystem is connected with a fresh water tank, a concentrated water outlet of the filtering subsystem is connected with a strong brine tank, the strong brine tank is connected with the thermal evaporation subsystem through a pipeline, and concentrated strong brine water is heated through solar energy; the salt drying system dries the heated strong brine in the sun to separate out crystal salt; the micro-grid system is responsible for providing power energy supply for the whole set of saline-alkali water desalination circulation system through photovoltaic power generation.
2. The microgrid-based powered saltwater desalination circulation system of claim 1 wherein the water intake subsystem comprises a water intake pump, a sand filter tank, a water intake tank; the water taking pump, the sand filter tank and the water inlet tank are sequentially connected through a pipeline.
3. The microgrid power based brine water desalination circulation system of claim 1, wherein the filtration subsystem comprises a nanofiltration membrane system, a concentrated water tank, a reverse osmosis membrane system;
the inlet of the nanofiltration membrane system is connected with the water inlet tank of the water taking subsystem through a pipeline, the light salt water outlet of the nanofiltration membrane system is connected with the reverse osmosis membrane system, and the concentrated water outlet of the nanofiltration membrane system is connected with the concentrated water tank;
the fresh water outlet of the reverse osmosis membrane system is connected with the fresh water tank, and the strong brine outlet is connected with the strong brine tank.
4. The microgrid-powered saltwater desalination cycle system of claim 1 wherein the thermal evaporation subsystem comprises: a condenser; a photovoltaic heating system; an evaporator;
the brine-alkali water inlet of the condenser is connected with the concentrated water tank of the filtering subsystem through a pipeline, the brine-alkali water outlet of the condenser is connected with the photovoltaic heating system, the condenser is provided with a heating medium inlet and a condensed water outlet, and the heating medium inlet is connected with the steam outlet of the evaporator through a pipeline;
the outlet of the heated saline water of the photovoltaic heating system is connected with the inlet of the evaporator;
still connect the pipeline between the saline and alkaline water export of evaporimeter and the import of photovoltaic heating system, the saline and alkaline water temperature after the evaporation descends and does not reach and shone salt concentration, then utilizes the circulating pump to pump into photovoltaic heating system and continue heating cycle.
5. The brine desalination circulation system based on micro-grid power supply as claimed in claim 4, wherein the evaporator is provided with an electric heating device, and the electric heating device is connected with the micro-grid system and can be powered by the micro-grid system to generate heat so as to heat and evaporate the brine in the evaporator.
6. The microgrid-based powered saltwater desalination circulation system of claim 1, wherein the microgrid system comprises: photovoltaic power generation system, bearing structure, system of converging, inverter system, energy storage battery system.
7. The microgrid power based saltwater desalination circulation system of claim 4 wherein the evaporator is provided with a vacuum pump so that the entire thermal evaporation subsystem can be under vacuum and the concentrated saltwater up to standard is directed to a collection tank.
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114651546A (en) * | 2022-03-07 | 2022-06-24 | 南京林业大学 | Selective permeable semi-open type washing and sunning integrated saline-alkali soil improvement system |
| CN114794001A (en) * | 2022-05-06 | 2022-07-29 | 中国水产科学研究院渔业机械仪器研究所 | Saline and alkaline pond quality of water improvement equipment |
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2020
- 2020-03-02 CN CN202020237061.0U patent/CN212504406U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114651546A (en) * | 2022-03-07 | 2022-06-24 | 南京林业大学 | Selective permeable semi-open type washing and sunning integrated saline-alkali soil improvement system |
| CN114651546B (en) * | 2022-03-07 | 2024-02-27 | 南京林业大学 | Selective semi-open type washing and sun-drying integrated saline-alkali soil improvement system |
| CN114794001A (en) * | 2022-05-06 | 2022-07-29 | 中国水产科学研究院渔业机械仪器研究所 | Saline and alkaline pond quality of water improvement equipment |
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