CN107246352B - Seawater wave energy desalination system - Google Patents
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- CN107246352B CN107246352B CN201710466762.4A CN201710466762A CN107246352B CN 107246352 B CN107246352 B CN 107246352B CN 201710466762 A CN201710466762 A CN 201710466762A CN 107246352 B CN107246352 B CN 107246352B
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- 238000010612 desalination reaction Methods 0.000 title claims abstract description 229
- 239000013535 sea water Substances 0.000 title claims abstract description 160
- 238000007906 compression Methods 0.000 claims abstract description 95
- 230000006835 compression Effects 0.000 claims abstract description 94
- 239000013505 freshwater Substances 0.000 claims abstract description 87
- 239000012267 brine Substances 0.000 claims abstract description 61
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 claims abstract description 61
- 230000033001 locomotion Effects 0.000 claims abstract description 33
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 32
- 239000012528 membrane Substances 0.000 claims abstract description 29
- 238000001223 reverse osmosis Methods 0.000 claims abstract description 25
- 238000007667 floating Methods 0.000 claims abstract description 24
- 238000004146 energy storage Methods 0.000 claims abstract description 22
- 239000002699 waste material Substances 0.000 claims abstract description 18
- 238000006243 chemical reaction Methods 0.000 claims abstract description 5
- 230000009471 action Effects 0.000 claims description 22
- 238000005381 potential energy Methods 0.000 claims description 14
- 230000008878 coupling Effects 0.000 claims description 10
- 238000010168 coupling process Methods 0.000 claims description 10
- 238000005859 coupling reaction Methods 0.000 claims description 10
- 230000009916 joint effect Effects 0.000 claims description 6
- GELKBWJHTRAYNV-UHFFFAOYSA-K lithium iron phosphate Chemical compound [Li+].[Fe+2].[O-]P([O-])([O-])=O GELKBWJHTRAYNV-UHFFFAOYSA-K 0.000 claims description 2
- 238000013019 agitation Methods 0.000 claims 1
- 238000011161 development Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 238000013461 design Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 241000251468 Actinopterygii Species 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000009499 grossing Methods 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000000452 restraining effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F03—MACHINES OR ENGINES FOR LIQUIDS; WIND, SPRING, OR WEIGHT MOTORS; PRODUCING MECHANICAL POWER OR A REACTIVE PROPULSIVE THRUST, NOT OTHERWISE PROVIDED FOR
- F03B—MACHINES OR ENGINES FOR LIQUIDS
- F03B13/00—Adaptations of machines or engines for special use; Combinations of machines or engines with driving or driven apparatus; Power stations or aggregates
- F03B13/12—Adaptations of machines or engines for special use; Combinations of machines or engines with driving or driven apparatus; Power stations or aggregates characterised by using wave or tide energy
- F03B13/14—Adaptations of machines or engines for special use; Combinations of machines or engines with driving or driven apparatus; Power stations or aggregates characterised by using wave or tide energy using wave energy
- F03B13/16—Adaptations of machines or engines for special use; Combinations of machines or engines with driving or driven apparatus; Power stations or aggregates characterised by using wave or tide energy using wave energy using the relative movement between a wave-operated member, i.e. a "wom" and another member, i.e. a reaction member or "rem"
- F03B13/20—Adaptations of machines or engines for special use; Combinations of machines or engines with driving or driven apparatus; Power stations or aggregates characterised by using wave or tide energy using wave energy using the relative movement between a wave-operated member, i.e. a "wom" and another member, i.e. a reaction member or "rem" wherein both members, i.e. wom and rem are movable relative to the sea bed or shore
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/08—Seawater, e.g. for desalination
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F05—INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
- F05B—INDEXING SCHEME RELATING TO WIND, SPRING, WEIGHT, INERTIA OR LIKE MOTORS, TO MACHINES OR ENGINES FOR LIQUIDS COVERED BY SUBCLASSES F03B, F03D AND F03G
- F05B2220/00—Application
- F05B2220/62—Application for desalination
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- 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
- Y02A20/131—Reverse-osmosis
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- 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
- Y02A20/138—Water desalination using renewable energy
- Y02A20/144—Wave energy
-
- 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
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Other Liquid Machine Or Engine Such As Wave Power Use (AREA)
Abstract
本发明公开了一种海水波浪能淡化系统,包括两正交浮子组、曲柄联杆结构、海水淡化、压缩空气储能以及水气存储单元;两正交浮子组根据波浪方向全方位捕获波浪能,电磁离合器、锥形齿轮以及牵引齿轮协同耦合两浮子组捕获能量,并由曲柄联杆结构将牵引齿轮旋转运动转化为淡化活塞和压缩活塞的上下运动,中心浮球经电磁阀调节膨胀腔和压缩腔气压,平抑波浪能的波动功率,确保海水淡化的恒压转化。浓盐水废压能通过压缩活塞下移,转化成高压气体内能;水气存储单元存储淡水和压缩空气,调控中心浮球气压,提升压缩储能效率;本发明极大提升波浪能转化效率、反渗透膜淡化效率和使用寿命,必将推动波浪能海水淡化的真正实用化。
The invention discloses a seawater wave energy desalination system, which comprises two orthogonal float groups, a crank link structure, seawater desalination, compressed air energy storage and a water vapor storage unit; the two orthogonal float groups capture wave energy in all directions according to the wave direction, an electromagnetic clutch, a bevel gear and a traction gear cooperatively couple the two float groups to capture energy, and the crank link structure converts the rotational motion of the traction gear into the up and down movement of the desalination piston and the compression piston. Ensure constant pressure conversion of seawater desalination. The waste pressure energy of concentrated brine is converted into high-pressure gas internal energy through the downward movement of the compression piston; the water-gas storage unit stores fresh water and compressed air, adjusts the air pressure of the central floating ball, and improves the compression energy storage efficiency; the invention greatly improves the wave energy conversion efficiency, reverse osmosis membrane desalination efficiency and service life, and will definitely promote the real practical application of wave energy seawater desalination.
Description
技术领域technical field
本发明公开了一种海水波浪能淡化系统,是一种应用于广阔海洋、电能及淡水缺乏区域,利用海洋波浪能和压缩空气协同实现海水的反渗透膜式淡化的淡化系统。The invention discloses a seawater wave energy desalination system, which is a desalination system that is applied to vast oceans, areas lacking electric energy and fresh water, and utilizes ocean wave energy and compressed air to realize reverse osmosis membrane desalination of seawater.
背景技术Background technique
随着世界能源危机和近海资源逐步开发,远洋鱼类及深海石油资源的开发日益受到各国关注,我国先后出台了“一带一路”、以及《全国海洋经济规划发展纲要》,旨在加速我国远洋资源的开发利用。然而,海上淡水缺乏和电力供给困难等问题,极大制约了远洋资源的开发利用,海水波浪能作为一种新兴的清洁能源,蕴含容量大,且与海水淡化天然耦合,已成为世界各国科研人员的重要研究方向。With the world's energy crisis and the gradual development of offshore resources, the development of pelagic fish and deep-sea oil resources has attracted increasing attention from all countries. my country has successively issued the "Belt and Road" and the "National Marine Economic Planning and Development Outline", aiming to accelerate the development and utilization of my country's pelagic resources. However, the lack of fresh water at sea and the difficulty of power supply have greatly restricted the development and utilization of offshore resources. Seawater wave energy, as an emerging clean energy, has a large capacity and is naturally coupled with seawater desalination. It has become an important research direction for researchers all over the world.
目前,海水淡化主要采用反渗透膜淡化工艺,利用电能驱动提水泵完成淡化膜供水压力恒定,以提高海水淡化效率和反渗透膜使用寿命,但海水淡化是高耗能产业,传统电力供给必将加剧环境污染和能源危机。同时,反渗透膜式海水淡化效率和使用寿命都与淡化压力密切相关,但波浪能的间歇性和波动性极易导致膜淡化压力变化,严重影响其使用寿命,储能是有效解决波动功率平抑的有效方法,但常用的蓄电池和液压等储能方式,极易导致环境污染。压缩空气储能是一种严格无污染的新型储能方式,如何与波浪能以及海水淡化能量耦合,提升波浪能利用率、海水淡化效率是必须要解决的关键问题。At present, seawater desalination mainly adopts the reverse osmosis membrane desalination process, which uses electric energy to drive the water pump to complete the constant water supply pressure of the desalination membrane to improve the efficiency of seawater desalination and the service life of the reverse osmosis membrane. However, seawater desalination is a high energy-consuming industry, and traditional power supply will definitely aggravate environmental pollution and energy crisis. At the same time, the efficiency and service life of reverse osmosis membrane seawater desalination are closely related to the desalination pressure, but the intermittency and volatility of wave energy can easily lead to changes in membrane desalination pressure, which seriously affects its service life. Energy storage is an effective way to effectively solve fluctuating power. However, commonly used energy storage methods such as batteries and hydraulic pressure can easily lead to environmental pollution. Compressed air energy storage is a new type of energy storage that is strictly pollution-free. How to couple with wave energy and seawater desalination energy to improve wave energy utilization and seawater desalination efficiency is a key issue that must be solved.
发明内容Contents of the invention
本发明的技术任务是针对上述技术上的不足,提出的一种新型海水波浪能淡化系统。The technical task of the present invention is to propose a novel seawater wave energy desalination system aimed at the above-mentioned technical deficiencies.
本发明解决上述技术问题采用的技术方案为:海水波浪能淡化系统包括两正交浮子组、曲柄联杆结构、海水淡化、压缩空气储能以及水气存储单元。两正交浮子组根据波浪方向全方位捕获波浪能,并经曲柄联杆结构驱动淡化活塞上下运动,完成海水吸入、海水淡化以及淡水和高压浓盐水排出,压缩空气储能平抑波浪能波动性和间歇性问题,确保海水淡化恒压高效转化,提升反渗透膜淡化效率和使用寿命。The technical solution adopted by the present invention to solve the above-mentioned technical problems is: the seawater wave energy desalination system includes two orthogonal float groups, a crank linkage structure, seawater desalination, compressed air energy storage and water vapor storage unit. The two orthogonal float groups capture wave energy in all directions according to the wave direction, and drive the desalination piston to move up and down through the crank-link structure to complete seawater intake, seawater desalination, and discharge of fresh water and high-pressure concentrated brine. Compressed air energy storage stabilizes wave energy fluctuations and intermittent problems, ensures constant pressure and efficient conversion of seawater desalination, and improves desalination efficiency and service life of reverse osmosis membranes.
两正交浮子组为两组正交设置的捕获装置Ⅰ和捕获装置Ⅱ,捕获装置包括两圆柱体浮子、浮子联杆、俯仰中轴、俯仰齿轮、锥形齿轮Ⅰ、水平联轴以及调向结构。所述圆柱体浮子在海浪浮力和激荡力共同作用下,上下运动捕获波浪能,驱动浮子联杆作俯仰运动,并由俯仰中轴、俯仰齿轮以及锥形齿轮Ⅰ协同转化成水平联轴的旋转运动,水平联轴旋转运动经调向结构与曲柄联杆结构机械耦合,驱动淡化活塞运动完成海水淡化。所述调向结构包括内嵌电磁离合器Ⅱ的锥形齿轮Ⅱ以及内嵌电磁离合器Ⅰ的牵引齿轮,锥形齿轮Ⅱ经电磁离合器Ⅱ与捕获装置Ⅰ的水平联轴耦合,将捕获装置Ⅰ捕获能量传递至牵引齿轮;所述牵引齿轮内嵌电磁离合器Ⅰ与捕获装置Ⅱ水平联轴同轴耦合,将捕获装置Ⅱ捕获能量传递至牵引齿轮,牵引齿轮外齿为锥形结构,与锥形齿轮Ⅱ机械耦合,所述电磁离合器根据波浪方向改变耦合至牵引齿轮的捕获装置数量;所述曲柄联杆结构上端和牵引齿轮刚性联接,下部经约束轴承和淡化活塞刚性联接,完成牵引齿轮旋转运动到淡化活塞上下运动的转化。The two orthogonal float groups are two sets of catch device I and catch device II set up orthogonally. The catch device includes two cylindrical floats, float linkage, pitch center shaft, pitch gear, bevel gear I, horizontal coupling and direction adjustment structure. Under the joint action of ocean buoyancy and turbulent force, the cylindrical buoy moves up and down to capture wave energy, drives the buoy linkage to perform pitching motion, and is converted into horizontal coupling rotation by the pitching central axis, pitching gear and bevel gear I. The horizontal coupling rotation is mechanically coupled with the crank linkage structure through the steering structure, and drives the desalination piston to complete seawater desalination. The direction adjustment structure includes a bevel gear II with an embedded electromagnetic clutch II and a traction gear with an embedded electromagnetic clutch I. The bevel gear II is coupled with the horizontal coupling of the capture device I through the electromagnetic clutch II, and transmits the energy captured by the capture device I to the traction gear; The upper end of the link structure is rigidly connected with the traction gear, and the lower part is rigidly connected with the desalination piston through the constraining bearing, so as to complete the transformation from the rotation motion of the traction gear to the up and down motion of the desalination piston.
海水淡化包括淡化活塞、淡水腔以及淡化腔,所述淡化活塞为内嵌反渗透膜的圆柱体活塞,在曲柄联杆推动下分离淡水和浓盐水,纵向设置多个空心圆柱型淡化通道,将淡水送入淡水腔;所述淡水腔包括淡化活塞以及淡水腔内壁,用于存储淡化活塞下移产生的淡水;淡水腔上端设置淡水排出阀,在淡化活塞上移过程中将淡化后的淡水送入淡水存储室存储。所述淡化腔是海水淡化主要场所,由淡化活塞、淡化腔内壁、海水进入通道以及淡化腔底板构成,淡化活塞由曲柄联杆以及压缩空气储能共同作用,完成海水吸入、海水淡化以及淡水排出;所述海水进入通道为圆环式柱状结构,内嵌圆环式柱状大气进出通道,海水进入通道上端设置海水进入阀Ⅰ,下端设置海水进入阀Ⅱ,控制海水进入淡化腔的流量;所述淡化腔底板为外套在大气进出通道的圆盘式固定端板,用于支撑淡化海水质量以及反渗透膜淡化压力;淡化腔底板设置圆盘式端盖,由内嵌在端板上的电磁铁控制,用于开关圆环式浓盐水排出通道Ⅰ。Seawater desalination includes a desalination piston, a fresh water chamber and a desalination chamber. The desalination piston is a cylindrical piston embedded with a reverse osmosis membrane, which separates fresh water and concentrated brine under the push of a crank link. A plurality of hollow cylindrical desalination channels are arranged longitudinally to send fresh water into the fresh water chamber. Water storage room for storage. The desalination chamber is the main place for seawater desalination, which is composed of a desalination piston, an inner wall of the desalination chamber, a seawater inlet channel and a desalination chamber bottom plate. The desalination piston is jointly operated by a crank linkage and compressed air energy storage to complete seawater intake, seawater desalination and freshwater discharge; the seawater inlet channel is a circular columnar structure, embedded with a circular columnar air inlet and outlet channel. The disc-type fixed end plate in the air inlet and outlet channels is used to support the quality of desalinated seawater and the desalination pressure of the reverse osmosis membrane; the bottom plate of the desalination chamber is equipped with a disc-type end cover, which is controlled by an electromagnet embedded in the end plate, and is used to switch the circular concentrated brine discharge channel I.
压缩空气储能包括大气进出通道、压缩活塞、压缩腔、膨胀腔以及中心浮球。所述大气进出通道为圆环式柱状结构,设置在两活塞联杆运动通道的外侧,上端与大气相连,下端经大气进出阀Ⅰ和压缩腔相联,控制吸入气体流量;所述压缩活塞为耐盐腐蚀的扁平圆柱体活塞,与淡化活塞刚性联接,内嵌浓盐水排出通道Ⅱ,浓盐水排出阀Ⅰ控制浓盐水排出流量,压缩活塞上侧为膨胀腔室,下侧为压缩腔室,调控膨胀腔室和压缩腔室气体压力,确保反渗透膜淡化压力恒定;所述压缩腔由压缩活塞、压缩腔内壁以及压缩腔底板共同构成,压缩活塞下移,将多余波浪能转化为气体内能,气压逐步升高,直至超过中心浮球气压,单向阀Ⅰ开启,压缩空气储存至中心浮球;所述膨胀腔由淡化腔底板、压缩活塞、膨胀腔内壁以及大气进出通道外侧共同构成,中心浮球内压缩气体经电磁流量阀Ⅱ进入膨胀腔做功,助推淡化活塞下移,确保反渗透膜淡化压力恒定,海水淡化结束,高压浓盐水经淡化腔底板进入膨胀腔,助推压缩活塞下移,进一步压缩空气储能;所述中心浮球用于存储压缩空气,同时为海水淡化设备提供浮力支撑,确保波浪能捕获装置水平基准稳定。Compressed air energy storage includes air inlet and outlet passages, compression pistons, compression chambers, expansion chambers and center floats. The air inlet and outlet channel is a circular columnar structure, which is arranged outside the movement channel of the two piston linkages. The upper end is connected to the atmosphere, and the lower end is connected to the compression chamber through the air inlet and outlet valve I to control the inhalation gas flow; the compression piston is a flat cylindrical piston resistant to salt corrosion, which is rigidly connected to the desalination piston. The desalination pressure is constant; the compression chamber is composed of the compression piston, the inner wall of the compression chamber and the bottom plate of the compression chamber. The compression piston moves down to convert excess wave energy into gas internal energy, and the air pressure gradually increases until it exceeds the air pressure of the central floating ball. The one-way valve I opens and the compressed air is stored in the central floating ball. constant, the seawater desalination is completed, and the high-pressure concentrated brine enters the expansion chamber through the bottom plate of the desalination chamber, which helps the compression piston to move down and further compresses the air to store energy; the central floating ball is used to store compressed air, and at the same time provide buoyancy support for the seawater desalination equipment to ensure the stability of the horizontal reference of the wave energy capture device.
水气存储单元包括压储气室、淡水存储室以及光伏电池。所述压储气室固定在淡水存储室下方,存储压缩气体,并为淡水存储室提供浮力支撑,经压缩气体通道和中心浮球相联,压缩气体通道上设置气体双向流动的涡旋机,用于调控中心浮球气压,有效提升压缩空气储能效率。所述淡水存储室位于压储气室上侧,由压储气室提供的浮力支撑,并经淡水通道和淡水排出阀与淡水腔相连,淡水通道上设置单向阀Ⅱ;淡水存储室上侧设置直流抽水泵,负责为远洋轮船等用户提取淡水。所述光伏电池设置在淡水存储室上端,内设磷酸铁锂蓄电池,为海水波浪能淡化系统的电磁阀、电磁铁、电磁离合器、直流抽水泵以及涡旋机提供电源支持。The water vapor storage unit includes a pressurized air storage chamber, a fresh water storage chamber and photovoltaic cells. The compressed gas storage chamber is fixed below the fresh water storage chamber, stores compressed gas, and provides buoyancy support for the fresh water storage chamber. The compressed gas channel is connected to the central floating ball. The compressed gas channel is provided with a vortex machine with two-way flow of gas, which is used to control the air pressure of the central floating ball, effectively improving the energy storage efficiency of compressed air. The fresh water storage room is located on the upper side of the pressure storage room, supported by the buoyancy provided by the pressure storage room, and connected to the fresh water cavity through the fresh water channel and the fresh water discharge valve. The fresh water channel is provided with a one-way valve II; the upper side of the fresh water storage room is provided with a DC pump, which is responsible for extracting fresh water for users such as ocean-going ships. The photovoltaic cell is arranged on the upper end of the fresh water storage room, and a lithium iron phosphate battery is installed inside to provide power support for the solenoid valve, electromagnet, electromagnetic clutch, DC pump and scroll machine of the seawater wave energy desalination system.
本发明带来的有益效果是:The beneficial effects brought by the present invention are:
1)将反渗透膜式海水淡化和波浪能捕获一体化设计,海水吸入和淡水排出一体化完成,引入了基于海水势能的自吸入机制,省却了传统海水淡化重要耗能设备——提水泵的使用,极大降低海水淡化功率消耗。1) The integrated design of reverse osmosis membrane seawater desalination and wave energy capture, the integration of seawater suction and freshwater discharge, the introduction of a self-suction mechanism based on seawater potential energy, saves the use of pumps, an important energy-consuming equipment for traditional seawater desalination, and greatly reduces the power consumption of seawater desalination.
2)内置反渗透膜的多孔淡化活塞,下移运动实现浓盐水和淡水自动分离,极大简化了海水淡化环节;特别是浓盐废水的排出机制,浓盐水废压能助推空气压缩,提供了一种新型高压浓盐水能量回收途径,极大提高了海水淡化效率以及波浪能利用效率。2) The porous desalination piston with built-in reverse osmosis membrane moves down to realize the automatic separation of concentrated brine and fresh water, which greatly simplifies the seawater desalination process; especially for the discharge mechanism of concentrated brine wastewater, the waste pressure of concentrated brine can boost air compression, providing a new energy recovery method for high-pressure concentrated brine, which greatly improves the efficiency of desalination of seawater and the efficiency of wave energy utilization.
3)将淡化活塞和压缩活塞一体化设计,动态调控膨胀腔和压缩腔内气体压力,有效平抑波浪能的波动性和间歇性问题对膜淡化性能影响,极大提高了海水淡化效率和反渗透膜使用寿命。3) The integrated design of the desalination piston and the compression piston can dynamically control the gas pressure in the expansion chamber and the compression chamber, effectively smoothing the impact of wave energy fluctuations and intermittent problems on the membrane desalination performance, and greatly improving the desalination efficiency of seawater and the service life of the reverse osmosis membrane.
4)本发明具有结构紧凑、可移动、易维护、抗海浪冲击性强,海水淡化效率高并具有稳定淡水供给等优点,必将大幅推动海水波浪能淡化系统的实用化。4) The present invention has the advantages of compact structure, mobility, easy maintenance, strong resistance to sea wave impact, high seawater desalination efficiency and stable fresh water supply, and will greatly promote the practical application of seawater wave energy desalination systems.
附图说明Description of drawings
图1海水波浪能淡化系统结构图。Fig. 1 Structural diagram of seawater wave energy desalination system.
图2两正交浮子组俯视图。Fig. 2 Top view of two orthogonal float groups.
图3两正交浮子组和曲柄联杆结构剖面图。Fig. 3 is a sectional view of two orthogonal float groups and a crank link structure.
图4淡化活塞结构图。Figure 4. Structural diagram of the desalination piston.
图5淡化腔底板剖面图。Figure 5 Sectional view of the bottom plate of the desalination chamber.
图6海水进入通道和大气进出通道剖面图。Figure 6 is a sectional view of the seawater inlet channel and the atmosphere inlet and outlet channel.
图7淡化系统多种模式选择流程图。Fig. 7 Flow chart of multiple mode selection of desalination system.
图中标号说明:1.海水进入阀Ⅰ,2.海水进入阀Ⅱ,3.电磁铁,4.浓盐水排出阀Ⅰ,5.浓盐水排出阀Ⅱ,6.电磁流量阀Ⅱ,7.大气进出阀Ⅰ,8.电磁流量阀Ⅰ,9.大气进出阀Ⅱ,10.单向阀Ⅰ,11.淡化活塞,12.压缩活塞,13.淡水腔,14.淡化腔,15.膨胀腔,16.压缩腔,17.曲柄联杆结构,18.光伏电池,19.保护罩,20.淡水排出阀,21.圆柱体浮子,22.中心浮球,23.固定地锚,24.压储气室,25.淡水存储室,26.直流抽水泵,27.圆盘式端盖,28.单向阀Ⅱ,29.涡旋机,30.浮子联杆,31.俯仰中轴,32.俯仰齿轮,33.锥形齿轮Ⅰ,34.锥形齿轮Ⅱ,35.水平联轴,36.淡水通道,37.牵引齿轮,38.约束轴承,39.电磁离合器Ⅰ,40.电磁离合器Ⅱ,41.淡化通道,42.反渗透膜,43.大气进出通道,44.海水进入通道,45.浓盐水排出通道Ⅰ,46.淡化腔底板,47.浓盐水排出通道Ⅱ,48.压缩腔底板,49.压缩气体通道,50.活塞联杆运动通道;A-A’.淡化腔底板剖面,B-B’.海水进入通道和大气进出通道剖面。Explanation of symbols in the figure: 1. Seawater inlet valve Ⅰ, 2. Seawater inlet valve Ⅱ, 3. Electromagnet, 4. Concentrated salt water discharge valve Ⅰ, 5. Concentrated brine discharge valve Ⅱ, 6. Electromagnetic flow valve Ⅱ, 7. Atmospheric inlet and outlet valve Ⅰ, 8. Electromagnetic flow valve Ⅰ, 9. Atmospheric inlet and outlet valve Ⅱ, 10. One-way valve Ⅰ, 11. Desalination piston, 12. Compression piston, 13. Fresh water chamber, 14. Desalination chamber, 15. Expansion chamber, 16. Compression chamber, 17. Curve Handle link structure, 18. Photovoltaic cell, 19. Protective cover, 20. Fresh water discharge valve, 21. Cylindrical float, 22. Center floating ball, 23. Fixed ground anchor, 24. Pressure storage chamber, 25. Fresh water storage chamber, 26. DC pump, 27. Disc type end cover, 28. One-way valve II, 29. Vortex machine, 30. Float linkage, 31. Pitching axis, 32. Pitching gear, 33. Conical Gear Ⅰ, 34. Bevel gear Ⅱ, 35. Horizontal coupling, 36. Fresh water channel, 37. Traction gear, 38. Constrained bearing, 39. Electromagnetic clutch Ⅰ, 40. Electromagnetic clutch Ⅱ, 41. Desalination channel, 42. Reverse osmosis membrane, 43. Air inlet and outlet channel, 44. Seawater inlet channel, 45. Concentrated brine discharge channel Ⅰ, 46. Desalination chamber bottom plate, 47. Concentrated brine discharge channel II, 48. Compression chamber bottom plate, 49. Compressed gas channel, 5 0. Piston linkage movement channel; A-A'. Desalination chamber bottom plate section, B-B'. Seawater inlet channel and atmosphere inlet and outlet channel section.
变量说明:H海浪波高,hmin启动波浪高度,Pw.波浪能捕获功率,Pd淡化功率,Pe膨胀功率,Pc.压缩功率。Variable description: H sea wave height, h min start wave height, P w. wave energy capture power, P d desalination power, P e expansion power, P c . compression power.
注:H<hmin时海浪蕴含能量少,无捕获价值。Note: When H<h min, the wave contains less energy and has no capture value.
具体实施方式Detailed ways
下面结合附图和实例对本发明进一步说明。The present invention will be further described below in conjunction with accompanying drawings and examples.
本发明所公布的海水波浪能淡化系统(如图1)包括两正交浮子组(包括圆柱体浮子21、浮子联杆30、俯仰中轴31、俯仰齿轮32、锥形齿轮Ⅰ33、水平联轴35、锥形齿轮Ⅱ34、电磁离合器Ⅰ39、电磁离合器Ⅱ40、牵引齿轮37)、曲柄联杆结构17、海水淡化(淡化活塞11、淡水腔13、淡化腔14、海水进入阀Ⅰ1、海水进入阀Ⅱ2、海水进入通道44、淡化通道41、反渗透膜42、淡水排出阀20、电磁铁3、圆盘式端盖27、浓盐水排出通道Ⅰ45)、压缩空气储能(压缩活塞12、压缩腔16、膨胀腔15、中心浮球22、大气进出阀Ⅰ7、大气进出阀Ⅱ9、大气进出通道43、单向阀Ⅰ10、电磁流量阀Ⅰ8、电磁流量阀Ⅱ6)、水气存储单元(压储气室24、涡旋机29、压缩气体通道49、淡水存储室25、单向阀Ⅱ28、淡水通道36、直流抽水泵26、光伏电池18)。The seawater wave energy desalination system announced by the present invention (as shown in Figure 1) includes two orthogonal float groups (comprising cylindrical float 21, float linkage 30, pitching center shaft 31, pitch gear 32, bevel gear I33, horizontal coupling shaft 35, bevel gear II34, electromagnetic clutch I39, electromagnetic clutch II40, traction gear 37), crank link structure 17, seawater desalination (desalination piston 11, freshwater chamber 13, desalination chamber 14, seawater entering Valve Ⅰ1, seawater inlet valve Ⅱ2, seawater inlet channel 44, desalination channel 41, reverse osmosis membrane 42, fresh water outlet valve 20, electromagnet 3, disc-type end cover 27, concentrated brine outlet channel I45), compressed air energy storage (compression piston 12, compression chamber 16, expansion chamber 15, center float 22, air inlet and outlet valve I7, air inlet and outlet valve II9, atmosphere inlet and outlet channel 43, one-way valve I10, electromagnetic flow valve I8, electromagnetic flow valve II6), Water and gas storage unit (pressurized gas storage chamber 24, scroll machine 29, compressed gas passage 49, fresh water storage chamber 25, check valve II 28, fresh water passage 36, DC water pump 26, photovoltaic cell 18).
所述两正交浮子组中圆柱体浮子21在海浪浮力和激荡力共同作用下,上下运动捕获波浪能,驱动浮子联杆30俯仰,经俯仰中轴31、俯仰齿轮32以及锥形齿轮Ⅰ33,将俯仰运动转化为水平联轴35的旋转运动;水平联轴35的旋转运动经锥形齿轮Ⅱ34、电磁离合器Ⅰ39以及电磁离合器Ⅱ40转化为牵引齿轮37的旋转运动。曲柄联杆结构17上端和牵引齿轮37刚性联接,下部经约束轴承38和淡化活塞11刚性联接,将牵引齿轮37的旋转运动转化至淡化活塞11上下运动,驱动海水淡化。The cylindrical float 21 in the two orthogonal float groups moves up and down to capture the wave energy under the joint action of the buoyancy of the sea waves and the turbulent force, and drives the float link 30 to pitch, through the pitch center shaft 31, the pitch gear 32 and the bevel gear I33, the pitch motion is converted into the rotation motion of the horizontal coupling shaft 35; the rotation motion of the horizontal coupling shaft 35 is converted into the rotation motion of the traction gear 37 through the bevel gear II34, the electromagnetic clutch I39 and the electromagnetic clutch II40. The upper end of the crank link structure 17 is rigidly connected to the traction gear 37, and the lower part is rigidly connected to the desalination piston 11 through the restraining bearing 38, which converts the rotation motion of the traction gear 37 into the up and down motion of the desalination piston 11, driving seawater desalination.
所述海水淡化由淡化活塞11上下运动,完成海水吸入、海水淡化以及淡水排出。外界海水经海水进入阀Ⅰ1、海水进入阀Ⅱ2以及海水进入通道44进入淡化腔14,助推淡化活塞11上移;淡化腔14内的海水在淡化压力作用下,经淡化通道41以及反渗透膜42淡化为淡水,进入淡水腔13,并随淡化活塞11的上移,经淡水排出阀20排出;淡化腔14内的浓盐水,在电磁铁3开启圆盘式端盖27的作用下,经浓盐水排出通道Ⅰ45排入膨胀腔15,助推压缩活塞12下移,直至压缩活塞12下移到压缩腔底板48,膨胀腔15内浓盐水再经浓盐水排出阀Ⅰ4、浓盐水排出通道Ⅱ47以及浓盐水排出阀Ⅱ5排出至大海。The seawater desalination is moved up and down by the desalination piston 11 to complete seawater inhalation, seawater desalination and freshwater discharge. External seawater enters the desalination chamber 14 through the seawater inlet valve I1, seawater inlet valve II2 and seawater inlet channel 44, and pushes the desalination piston 11 to move upward; under the desalination pressure, the seawater in the desalination chamber 14 is desalinated into fresh water through the desalination channel 41 and the reverse osmosis membrane 42, enters the fresh water chamber 13, and is discharged through the fresh water discharge valve 20 with the upward movement of the desalination piston 11; Next, the concentrated brine is discharged into the expansion chamber 15 through the concentrated brine discharge channel I45, and the compression piston 12 is pushed down until the compression piston 12 moves down to the bottom plate 48 of the compression chamber.
所述压缩空气储能由压缩活塞12的上下运动,完成压缩储能和膨胀助推,平抑波浪的波动功率,确保海水恒压淡化。外界大气经大气进出阀Ⅰ7以及大气进出通道43进入压缩腔16,随压缩活塞12下移,将多余波浪能以压缩空气形式进行存储,随着压缩气体压力升高,单向阀Ⅰ10打开,高压气体存储至中心浮球22;中心浮球22内高压气体,分别电磁流量阀Ⅰ8和电磁流量阀Ⅱ6进入压缩腔16和膨胀腔15,压缩气体膨胀释能,调控淡化腔14内压力,膨胀助推压缩活塞12和淡化活塞11运动,确保淡化腔14内气压恒定。The compressed air energy storage is completed by the up and down movement of the compression piston 12, which completes the compression energy storage and expansion boost, stabilizes the fluctuating power of waves, and ensures constant pressure desalination of seawater. The external air enters the compression chamber 16 through the air inlet and outlet valve I7 and the air inlet and outlet channel 43, and as the compression piston 12 moves down, the excess wave energy is stored in the form of compressed air. As the pressure of the compressed gas rises, the one-way valve I10 opens, and the high-pressure gas is stored in the center float 22; the high-pressure gas in the center float 22 enters the compression chamber 16 and the expansion chamber 15 through the electromagnetic flow valve I8 and the electromagnetic flow valve II6 respectively. The movement of the desalination piston 11 ensures constant air pressure in the desalination chamber 14 .
所述水气存储单元用于存储淡水和压缩空气,同时压缩空气为淡水提供浮力支持。压储气室24经涡旋机29、压缩气体通道49与中心浮球22联通,涡旋机29用于调控中心浮球22内气压,确保压缩储能和膨胀释能无过欠压缩和膨胀损耗;淡水存储室25经单向阀Ⅱ28和淡水通道36,汇总收集淡水,并经直流抽水泵26供给外界需求;光伏电池18内设磷酸铁锂蓄电池,为海水波浪能淡化系统的电磁阀、电磁铁、电磁离合器、直流抽水泵以及涡旋机提供电源支持。The water vapor storage unit is used to store fresh water and compressed air, and the compressed air provides buoyancy support for the fresh water. The pressure storage chamber 24 communicates with the central floating ball 22 through the vortex machine 29 and the compressed gas passage 49. The vortex machine 29 is used to regulate the air pressure in the central floating ball 22 to ensure that the compression energy storage and expansion release energy have no over-compression and expansion loss; Electromagnetic clutch, DC water pump and scroll machine provide power support.
波浪的间歇性和波动性极易导致海水淡化压力波动,严重影响海水淡化效率以及膜使用寿命,为此调控压缩空气储能状态,平抑波动功率对海水淡化压力影响,系统存在波浪海水淡化、波浪压缩海水淡化、波浪膨胀海水淡化以及水压膨胀海水淡化四种工作模式,如图7所示,工作模式判定是基于波浪工况、中心浮球气压、以及实时计算获取的Pw、Pc、Pe以及Pd进行的。The intermittency and volatility of waves can easily lead to pressure fluctuations in seawater desalination, which seriously affects the efficiency of seawater desalination and the service life of the membrane. To control the energy storage state of compressed air and stabilize the impact of fluctuating power on seawater desalination pressure, the system has four operating modes: wave seawater desalination, wave compression seawater desalination, wave expansion seawater desalination, and water pressure expansion seawater desalination .
当Pw=Pd时,系统运行在独立波浪海水淡化模式;When P w =P d , the system operates in the independent wave seawater desalination mode;
当Pw>Pd,调控压缩功率Pc,波浪能的多余功率以压缩空气形式存储,使Pw-Pc=Pd,系统运行在波浪压缩海水淡化模式;When P w >P d , adjust the compression power P c , the excess power of the wave energy is stored in the form of compressed air, so that P w -P c =P d , the system operates in the wave compression seawater desalination mode;
当Pw<Pd,调控膨胀功率Pe,使Pw+Pe=Pd,波浪能差额功率由高压气体膨胀补充,系统运行在波浪膨胀海水淡化;When P w < P d , adjust the expansion power P e so that P w + P e = P d , the wave energy balance power is supplemented by high-pressure gas expansion, and the system operates in wave expansion seawater desalination;
当H<hmin时,波浪蕴含能量较小,海水淡化所需能量完全有压缩空气储能提供,系统运行在水压膨胀海水淡化。When H<h min , the energy contained in the wave is small, and the energy required for seawater desalination is completely provided by compressed air energy storage, and the system operates under water pressure expansion for seawater desalination.
1、独立波浪海水淡化1. Independent wave seawater desalination
当海况良好时,系统捕获波浪能基本满足海水淡化要求,圆柱体浮子21上仰主要进行海水吸入、大气吸入以及淡水排出;下俯主要进行海水淡化、浓盐水废压利用及排出。When the sea conditions are good, the wave energy captured by the system basically meets the requirements of seawater desalination. The cylindrical float 21 is mainly used for seawater suction, atmospheric suction and freshwater discharge when it is raised up; it is mainly used for seawater desalination, concentrated brine waste pressure utilization and discharge when it is lowered.
圆柱体浮子21在波浪作用下上仰,波浪机械能、水势能和大气动能,共同驱动淡化活塞11和压缩活塞12上移。海水在水势能作用下,经海水进入阀Ⅰ1、海水进入阀Ⅱ2进入淡化腔14,外界大气经大气进出阀Ⅰ7进入压缩腔16,淡水腔14内的淡水随淡化活塞11上移,经淡水排出阀20逐步排出,并在淡化活塞11上移至淡水腔13顶部时,海水进入阀Ⅰ1、海水进入阀Ⅱ2以及淡水排出阀20关闭。圆柱体浮子21上仰至上限,上仰结束。The cylindrical buoy 21 rises up under the action of waves, and the wave mechanical energy, water potential energy and atmospheric kinetic energy jointly drive the desalination piston 11 and the compression piston 12 to move upward. Under the action of water potential energy, seawater enters the desalination chamber 14 through the seawater inlet valve I1 and seawater inlet valve II2, and the outside air enters the compression chamber 16 through the atmosphere inlet and outlet valve I7. The fresh water in the freshwater chamber 14 moves up with the desalination piston 11 and is gradually discharged through the freshwater discharge valve 20. When the desalination piston 11 moves up to the top of the freshwater chamber 13, the seawater inlet valve I1, seawater inlet valve II2 and freshwater outlet valve 20 are closed. Cylinder float 21 raises up to upper limit, raises up and ends.
圆柱体浮子21在波浪作用下下俯,波浪机械能驱动淡化活塞11和压缩活塞12下移,进行海水淡化。海水通过淡化活塞11内嵌的淡化通道41和反渗透膜42将淡水送入淡水腔13,随着淡化活塞12逐步下移至淡化下限位置,海水淡化完成,此时电磁铁3启动,圆盘式端盖27上移,淡化腔13内残留的高压浓盐水,经浓盐水排出通道Ⅰ45自动进入膨胀腔15,此时海水淡化完成,系统进入浓盐水废压利用阶段,大气进出阀Ⅰ7、大气进入阀Ⅱ9关闭,压缩活塞12在波浪机械能和浓盐水废压能共同作用下开始压缩气体,随着压缩气体气压升高,高压气体经单向阀Ⅰ10进入中心浮球22进行存储,压缩活塞12下移至压缩腔16底部,浓盐水在自身废压作用下,经浓盐水排出阀Ⅰ4、浓盐水排除通道Ⅱ47以及浓盐水排出阀Ⅱ5排出,直至浓盐水全部排出,浓盐水排出阀Ⅰ4和浓盐水排出阀Ⅱ5关闭,圆柱体浮子21下俯至下限,下俯结束。The cylindrical buoy 21 sinks under the action of waves, and the mechanical energy of the waves drives the desalination piston 11 and the compression piston 12 to move down to desalinate seawater. Seawater sends fresh water into the freshwater chamber 13 through the desalination channel 41 embedded in the desalination piston 11 and the reverse osmosis membrane 42. As the desalination piston 12 gradually moves down to the desalination lower limit position, seawater desalination is completed. At this time, the electromagnet 3 is activated, the disc-shaped end cover 27 moves up, and the high-pressure concentrated brine remaining in the desalination chamber 13 automatically enters the expansion chamber 15 through the concentrated brine discharge channel I45. Ⅱ9 is closed, and the compression piston 12 starts to compress the gas under the joint action of the wave mechanical energy and the concentrated brine waste pressure energy. As the pressure of the compressed gas rises, the high-pressure gas enters the central floating ball 22 through the one-way valve Ⅰ10 for storage, and the compression piston 12 moves down to the bottom of the compression chamber 16. Dive down to the lower limit, and the dive ends.
2、波浪压缩海水淡化2. Wave compression seawater desalination
当波浪较大,系统捕获波浪能超过海水淡化所需能量时,多余能量以压缩空气形式储存在中心浮球22。圆柱体浮子21上仰主要进行海水和大气的吸入以及淡水排出;下俯主要进行海水淡化、浓盐水废压利用、浓盐水排出以及压缩空气储能。When the waves are large and the wave energy captured by the system exceeds the energy required for seawater desalination, the excess energy is stored in the central floating ball 22 in the form of compressed air. The cylindrical float 21 is mainly used for seawater and air intake and fresh water discharge when it is raised up; it is mainly used for desalination of seawater, waste pressure utilization of concentrated brine, discharge of concentrated brine and compressed air energy storage when it is lowered.
圆柱体浮子21在波浪作用下上仰,波浪机械能、水势能和大气动能,共同驱动淡化活塞11和压缩活塞12上移。海水在水势能作用下,经海水进入阀Ⅰ1、海水进入阀Ⅱ2进入淡化腔14,外界大气经大气进出阀Ⅰ7进入压缩腔16,淡水腔13内的淡水随淡化活塞11上移,经淡水排出阀20逐步排出,并在淡化活塞11上移至淡水腔13顶部时,海水进入阀Ⅰ1、海水进入阀Ⅱ2、大气进出阀Ⅰ7、大气进入阀Ⅱ9以及淡水排出阀20关闭,圆柱体浮子21上仰至上限,上仰结束。The cylindrical buoy 21 rises up under the action of waves, and the wave mechanical energy, water potential energy and atmospheric kinetic energy jointly drive the desalination piston 11 and the compression piston 12 to move upward. Under the action of water potential energy, seawater enters the desalination chamber 14 through the seawater inlet valve I1 and seawater inlet valve II2, and the outside air enters the compression chamber 16 through the atmosphere inlet and outlet valve I7. The fresh water in the freshwater chamber 13 moves up with the desalination piston 11 and is gradually discharged through the freshwater discharge valve 20. When the desalination piston 11 moves up to the top of the freshwater chamber 13, the seawater inlet valve I1, seawater inlet valve II2, atmosphere inlet and outlet valve I7, atmosphere inlet valve II9 and freshwater outlet valve 20 are closed. Cylinder float 21 raises up to upper limit, raises up and ends.
圆柱体浮子21在波浪作用下下俯,波浪机械能驱动淡化活塞11和压缩活塞12下移,多余波浪能以压缩空气形式储存,消纳多余功率确保淡化压力恒定。海水通过淡化活塞11内嵌的淡化通道41和反渗透膜42,将淡水送入淡水腔13;随着淡化活塞12逐步下移至淡化下限位置,海水淡化完成,此时电磁铁3开启,圆盘式端盖27上移,淡化腔14内残留的高压浓盐水,经浓盐水排出通道Ⅰ45自动进入膨胀腔15,压缩活塞12在波浪机械能和浓盐水的废压能共同作用下压缩气体,气体气压逐步升高,经单向阀Ⅰ10存储至中心浮球22,压缩活塞12最终下移至压缩腔16底部,浓盐水在自身废压作用下,经浓盐水排出阀Ⅰ4、浓盐水排出通道Ⅱ47以及浓盐水排出阀Ⅱ5排出,当圆柱体浮子21下俯至下限,下俯结束。The cylindrical buoy 21 sinks under the action of waves, the mechanical energy of the waves drives the desalination piston 11 and the compression piston 12 to move down, and the excess wave energy is stored in the form of compressed air to absorb excess power to ensure constant desalination pressure. Seawater passes through the desalination channel 41 embedded in the desalination piston 11 and the reverse osmosis membrane 42, and sends fresh water into the fresh water chamber 13; as the desalination piston 12 gradually moves down to the lower limit position of desalination, seawater desalination is completed, at this time the electromagnet 3 is turned on, the disc-type end cover 27 moves up, and the high-pressure concentrated brine remaining in the desalination chamber 14 automatically enters the expansion chamber 15 through the concentrated brine discharge channel I45, and the compression piston 12 compresses the gas under the combined action of wave mechanical energy and waste pressure energy of the concentrated brine. It rises gradually and is stored in the central floating ball 22 through the one-way valve I10. The compression piston 12 finally moves down to the bottom of the compression chamber 16. Under the action of its own waste pressure, the concentrated brine is discharged through the concentrated brine discharge valve I4, the concentrated brine discharge channel II47 and the concentrated brine discharge valve II5. When the cylindrical float 21 descends to the lower limit, the descent ends.
3、波浪膨胀海水淡化3. Sea water desalination by wave expansion
当波浪较小,系统捕获的波浪能低于海水淡化所需能量时,不足的能量由中心浮球22内高压气体,膨胀助力补充。圆柱体浮子21上仰主要进行海水和大气的吸入、淡水排出以及膨胀气体的排出,下俯主要进行海水淡化、膨胀助力、浓盐水废压利用及排出。When the wave is small and the wave energy captured by the system is lower than the energy required for seawater desalination, the insufficient energy is supplemented by the high-pressure gas in the central floating ball 22 and the expansion assist. The cylindrical float 21 is mainly used for seawater and air intake, fresh water discharge and expansion gas discharge when it is raised up, and seawater desalination, expansion boosting, and waste pressure utilization and discharge of concentrated brine are mainly performed when it is lowered.
圆柱体浮子21在波浪作用下上仰,波浪机械能、水势能和大气进入的动能,共同驱动淡化活塞11和压缩活塞12上移。海水在水势能作用下,经海水进入阀Ⅰ1、海水进入阀Ⅱ2进入淡化腔14,外界大气经大气进出阀Ⅰ7进入压缩腔16,淡水腔13内的淡水随淡化活塞11上移,经淡水排出阀20逐步排出,同时膨胀腔15内压缩气体也在压缩活塞12的推动下,经大气进入阀Ⅱ9排出,并在淡化活塞11上移至淡水腔13顶部时,海水进入阀Ⅰ1、海水进入阀Ⅱ2以及淡水排出阀20关闭,圆柱体浮子21上仰至上限,上仰结束。The cylindrical buoy 21 rises up under the action of the waves, and the mechanical energy of the waves, the potential energy of the water and the kinetic energy entering the atmosphere jointly drive the desalination piston 11 and the compression piston 12 to move upward. Under the action of water potential energy, seawater enters desalination chamber 14 through seawater inlet valve I1 and seawater inlet valve II2, and external air enters compression chamber 16 through atmosphere inlet and outlet valve I7. The valve II2 and the fresh water discharge valve 20 are closed, and the cylinder float 21 lifts up to the upper limit, and the lift ends.
圆柱体浮子21在波浪作用下下俯,波浪机械能以及气体膨胀能共同驱动淡化活塞11和压缩活塞12下移,进行海水淡化。海水通过淡化活塞11内嵌的淡化通道41和反渗透膜42将淡水送入淡水腔13,同时,中心浮球22内气体经电磁流量阀Ⅱ6进入膨胀腔15,膨胀助推活塞下移,压缩腔内气体无阻经大气进出阀Ⅰ7、大气进入阀Ⅱ9自动排出,淡化活塞12逐步下移至淡化下限位置,海水淡化完成,此时进入至浓盐水废压利用阶段,此时大气进出阀Ⅰ7、大气进入阀Ⅱ9关闭,电磁铁3开启,圆盘式端盖27上移,淡化腔13内残留的高压浓盐水经浓盐水排出通道Ⅰ45自动进入膨胀腔15,压缩活塞12在波浪机械能和浓盐水的废压能共同作用下,压缩气体气压升高,并经单相阀Ⅰ10进入中心浮球22存储,直至压缩活塞12下移至压缩腔16底部,浓盐水在自身废压的作用下,通过浓盐水排出阀Ⅰ4、浓盐水排除通道Ⅱ47以及浓盐水排出阀Ⅱ5排出。圆柱体浮子21下俯至下限,下俯结束。The cylindrical buoy 21 sinks under the action of waves, and the mechanical energy of the waves and the expansion energy of the gas jointly drive the desalination piston 11 and the compression piston 12 to move down to desalinate seawater. The sea water is sent into the fresh water chamber 13 through the desalination channel 41 embedded in the desalination piston 11 and the reverse osmosis membrane 42. At the same time, the gas in the center floating ball 22 enters the expansion chamber 15 through the electromagnetic flow valve II6, and the expansion assists the piston to move downward. The inlet valve II9 is closed, the electromagnet 3 is opened, the disc-type end cover 27 moves upward, the high-pressure concentrated brine remaining in the desalination chamber 13 automatically enters the expansion chamber 15 through the concentrated brine discharge channel I45, and the compression piston 12 is under the joint action of the wave mechanical energy and the waste pressure energy of the concentrated brine, the pressure of the compressed gas rises, and enters the central floating ball 22 through the single-phase valve I10 for storage until the compression piston 12 moves down to the bottom of the compression chamber 16. Passage II47 and concentrated brine discharge valve II5 are discharged. Cylindrical float 21 descends to the lower limit, and descends to the end.
4、水压膨胀海水淡化4. Water pressure expansion seawater desalination
当波浪极小,波浪能没有捕获价值时,活塞11上移所需的能量由水势能、大气动能以及气体膨胀能共同提供,下俯过程所需能量完全由气体膨胀能提供。活塞上移主要进行海水吸入、淡水排出、膨胀助推以及膨胀气体的排出,下移主要进行海水淡化、膨胀助推以及浓盐水废压利用及排出。When the wave is extremely small and the wave energy has no capture value, the energy required for the upward movement of the piston 11 is provided jointly by water potential energy, atmospheric kinetic energy and gas expansion energy, and the energy required for the downward process is completely provided by the gas expansion energy. The upward movement of the piston is mainly for seawater suction, fresh water discharge, expansion boost and discharge of expansion gas, and the downward movement is mainly for seawater desalination, expansion boost and concentrated brine waste pressure utilization and discharge.
淡化活塞上移过程,水势能、大气进入动能以及压缩气体膨胀能共同驱动淡化活塞11和压缩活塞12上移。海水在水势能作用下,经海水进入阀Ⅰ1、海水进入阀Ⅱ2进入淡化腔14,中心浮球22内压缩气体经电磁流量阀Ⅰ8进入压缩腔16,膨胀做功助推压缩活塞12和淡化活塞11上移,淡水腔13内的淡水随淡化活塞11的上移,经淡水排出阀20排出,膨胀腔15内气体在压缩活塞12推动下,经大气进入阀Ⅱ9排出,直至淡化活塞11上移至淡水腔13顶部,海水进入阀Ⅰ1、海水进入阀Ⅱ2、电磁流量阀Ⅰ8以及淡水排出阀20关闭,淡化活塞11上移至上限,上移结束。During the upward movement of the desalination piston, the water potential energy, the atmospheric entry kinetic energy and the expansion energy of the compressed gas jointly drive the desalination piston 11 and the compression piston 12 to move upward. Under the action of water potential energy, seawater enters the desalination chamber 14 through the seawater inlet valve I1 and seawater inlet valve II2, and the compressed gas in the center floating ball 22 enters the compression chamber 16 through the electromagnetic flow valve I8, and the expansion works to push the compression piston 12 and the desalination piston 11 to move upward. Move up to the top of the fresh water chamber 13, seawater inlet valve I1, seawater inlet valve II2, electromagnetic flow valve I8 and freshwater discharge valve 20 are closed, the desalination piston 11 moves up to the upper limit, and the upward movement ends.
淡化活塞下移过程,气体膨胀能驱动淡化活塞11和压缩活塞12下移,进行海水淡化。中心浮球22内气体经电磁流量阀Ⅱ6进入膨胀腔15,推动压缩活塞12下移,带动淡化活塞11下移,海水在淡化活塞11的压力下,通过淡化活塞11内嵌的淡化通道41和反渗透膜42,将淡水送入淡水腔13,压缩腔16内气体无阻经大气进出阀Ⅰ7、大气进入阀Ⅱ9自由排出,淡化活塞11逐步下移至淡化下限位置,海水淡化完成,此时进入浓盐水废压利用阶段,大气进出阀Ⅰ7、大气进入阀Ⅱ9关闭,此时电磁铁3开启,圆盘式端盖27上移,淡化腔13内残留的高压浓盐水经浓盐水排出通道Ⅰ45自动进入膨胀腔15,压缩腔16内气体在浓盐水的废压能作用下进行压缩,高压气体经单向阀Ⅰ10进入中心浮球22,直至压缩活塞12下移至压缩腔16底部,浓盐水在自身废压的作用下经浓盐水排出阀Ⅰ4、浓盐水排出通道Ⅱ47以及浓盐水排出阀Ⅱ5排出,淡化活塞11下移至下限,下移结束。During the downward movement of the desalination piston, the gas expansion can drive the desalination piston 11 and the compression piston 12 to move downward to desalinate seawater. The gas in the center float 22 enters the expansion chamber 15 through the electromagnetic flow valve II6, pushes the compression piston 12 to move down, and drives the desalination piston 11 to move down. Under the pressure of the desalination piston 11, the seawater passes through the desalination channel 41 embedded in the desalination piston 11 and the reverse osmosis membrane 42, and sends fresh water into the fresh water chamber 13. Completed, enter the waste pressure utilization stage of concentrated brine at this time, the air inlet and outlet valve I7 and the air inlet valve II9 are closed, at this time the electromagnet 3 is turned on, the disc-type end cover 27 moves up, the high-pressure concentrated brine remaining in the desalination chamber 13 automatically enters the expansion chamber 15 through the concentrated brine discharge channel I45, the gas in the compression chamber 16 is compressed under the action of the waste pressure energy of the brine, and the high-pressure gas enters the central floating ball 22 through the one-way valve I10 until the compression piston 12 moves down to the bottom of the compression chamber 16. Down through the concentrated brine discharge valve I4, the concentrated brine discharge channel II47 and the concentrated brine discharge valve II5, the desalination piston 11 moves down to the lower limit, and the downward movement ends.
Claims (1)
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