WO2022160367A1 - 一种用于海水温差发电装置的星合循环系统 - Google Patents

一种用于海水温差发电装置的星合循环系统 Download PDF

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Publication number
WO2022160367A1
WO2022160367A1 PCT/CN2021/075219 CN2021075219W WO2022160367A1 WO 2022160367 A1 WO2022160367 A1 WO 2022160367A1 CN 2021075219 W CN2021075219 W CN 2021075219W WO 2022160367 A1 WO2022160367 A1 WO 2022160367A1
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Prior art keywords
water pipe
condenser
seawater
pipe
distiller
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PCT/CN2021/075219
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English (en)
French (fr)
Inventor
房盼盼
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房盼盼
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Priority to AU2021424943A priority Critical patent/AU2021424943A1/en
Publication of WO2022160367A1 publication Critical patent/WO2022160367A1/zh

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K25/00—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for
    • F01K25/08—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using special vapours
    • F01K25/10—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using special vapours the vapours being cold, e.g. ammonia, carbon dioxide, ether
    • F01K25/106—Ammonia
    • 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
    • C02F1/02—Treatment of water, waste water, or sewage by heating
    • C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01D—NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
    • F01D15/00—Adaptations of machines or engines for special use; Combinations of engines with devices driven thereby
    • F01D15/10—Adaptations for driving, or combinations with, electric generators
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K27/00—Plants for converting heat or fluid energy into mechanical energy, not otherwise provided for
    • F01K27/02—Plants modified to use their waste heat, other than that of exhaust, e.g. engine-friction heat
    • 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
    • F03G—SPRING, WEIGHT, INERTIA OR LIKE MOTORS; MECHANICAL-POWER PRODUCING DEVICES OR MECHANISMS, NOT OTHERWISE PROVIDED FOR OR USING ENERGY SOURCES NOT OTHERWISE PROVIDED FOR
    • F03G7/00—Mechanical-power-producing mechanisms, not otherwise provided for or using energy sources not otherwise provided for
    • F03G7/04—Mechanical-power-producing mechanisms, not otherwise provided for or using energy sources not otherwise provided for using pressure differences or thermal differences occurring in nature
    • F03G7/05—Ocean thermal energy conversion, i.e. OTEC
    • H—ELECTRICITY
    • H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
    • H05K—PRINTED CIRCUITS; CASINGS OR CONSTRUCTIONAL DETAILS OF ELECTRIC APPARATUS; MANUFACTURE OF ASSEMBLAGES OF ELECTRICAL COMPONENTS
    • H05K7/00—Constructional details common to different types of electric apparatus
    • H05K7/20—Modifications to facilitate cooling, ventilating, or heating
    • H05K7/20709—Modifications to facilitate cooling, ventilating, or heating for server racks or cabinets; for data centers, e.g. 19-inch computer racks
    • H05K7/20763—Liquid cooling without phase change
    • 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
    • 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
    • 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
    • Y02E20/00—Combustion technologies with mitigation potential
    • Y02E20/16—Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]

Definitions

  • the invention relates to the technical field of seawater thermoelectric power generation and the technical field of seawater desalination, in particular to a star combined cycle system for a seawater thermoelectric power generation device.
  • Hybrid cycle, Uehara cycle, Karina cycle, Rankine cycle, etc. in ocean thermoelectric devices now all have the problem of high energy consumption in the world. Its energy consumption is almost the same as its own production capacity or even higher than its output, which is also the reason why even the power generation device with zero energy consumption has not been widely promoted and applied in the past 140 years, but has been kept in storage. in the laboratory;
  • the existing ocean thermoelectric device needs to consume a lot of power to extract the warm seawater on the surface and the cold seawater 1000 meters below the water, which wastes a lot of power resources, and the traditional seawater thermoelectric power generation cannot effectively carry out the distillation of water vapor. transport, resulting in a lot of waste of resources.
  • the purpose of the present invention is to provide a star combined cycle system for a seawater thermoelectric power generation device, so as to solve the problems raised in the above background technology.
  • a star-joint cycle system for a seawater thermoelectric power generation device comprising an IDC server, a No. 1 condenser, an evaporator, a turbine, a generator, a distiller and a No. 2 condenser
  • One side of the IDC server is provided with a server cooling pipe, one end of the server cooling pipe is provided with a No. 2 water pipe, the top of the IDC server is provided with a No. 1 water pipe, and one end of the No. 1 water pipe is provided Connected to the evaporator, one end of the cooling pipe of the server is provided with the No. 5 water pipe, the No. 5 water pipe is connected with the No.
  • valves are provided on the outer sides of the No. 2 water pipe and the No. 4 water pipe.
  • the top of the distiller is provided with a vacuum pump.
  • the IDC server is located at a position fifty to sixty meters below the sea level.
  • the No. 1 condenser, the turbine, the generator and the evaporator are all located twenty meters below the sea level.
  • the No. 2 condenser is located on land.
  • the distiller is located one to ten meters below the sea level.
  • the steam in the distiller is naturally transported to the No. 2 condenser on land in a gaseous manner for fresh water extraction.
  • a sea salt conveyor is provided at the bottom of the distiller, and one end of the sea salt conveyor extends to the land.
  • the No. 1 condenser, the evaporator and the No. 2 condenser are all of the coil type.
  • the beneficial effects of the present invention are as follows: the present invention has a simple structure, is novel and has strong practicability, and by adding a valve, the current limitation of the No. Two water pumps for cold and hot sea water are used, which reduces the energy consumption of the device by 90%. By adding a distributor, the mixed treatment between high temperature sea water and normal temperature sea water is realized. By adding an IDC server, the server is cooled. The tube makes full use of the waste heat of the IDC and preheats the seawater to about 70 degrees. By adding an evaporator, the hot water can heat up and re-vaporize the liquefied ammonia in the evaporator. By adding a turbine, The power generation of the generator is realized.
  • a condenser By adding a condenser, the condensation and liquefaction of ammonia gas is realized.
  • a distiller By adding a distiller, the distillation treatment of seawater is realized.
  • a sea salt conveyor By adding a sea salt conveyor, the transportation of distilled sea salt is realized.
  • the distiller and the No. 2 condenser are added. There is a height difference between the distiller and the No. 2 condenser, so that the distilled water vapor is transported to the No. 2 condenser in a gaseous state.
  • the No. 2 condenser By adding the No. 2 condenser, it is realized With the help of the No. 2 condenser of the condensing equipment, the cold and heat exchange is carried out in an air-cooled manner to produce water vapor liquefaction.
  • Fig. 1 is the internal structure schematic diagram of the present invention
  • FIG. 2 is a distribution diagram of some components of the present invention.
  • a star-conjunction cycle system for a seawater thermoelectric power generation device including an IDC server 1, a No. 1 condenser 7, an evaporator 14, a turbine 15, and a generator 16.
  • Distiller 18 and No. 2 condenser 20 one side of the IDC server 1 is provided with a server cooling pipe 2, one end of the server cooling pipe 2 is provided with a No. 2 water pipe 3, and the top of the IDC server 1 is provided with a No. 1 water pipe 23.
  • One end of the No. 1 water pipe 23 is connected to the evaporator 14, one end of the server cooling pipe 2 is provided with the No. 5 water pipe 12, the No. 5 water pipe 12 is connected with the No.
  • the outside of the No. 2 water pipe 3 and the No. 4 water pipe 6 are provided with valves, which are convenient for the valves to control the water flow of the No. 2 water pipe 3 and the No. 4 water pipe 6.
  • the top of the distiller 18 is provided with a vacuum pump 17, which is convenient for the vacuum pump 17 Vacuuming the distiller 18 to improve the distillation efficiency, the IDC server 1 is located at a position fifty to sixty meters below the sea level, which is convenient for the IDC server 1 to fully utilize its waste heat to generate electricity, and does not discharge the waste heat into the ocean, thereby reducing hot air Pollution, reduce carbon emissions, reduce energy consumption of IDC server 1, save land space, No.
  • the No. 2 condenser 20 is located on land, which is convenient for the collection of fresh water.
  • the transportation of seawater desalination in the form of gasification will greatly reduce the cost of seawater desalination and solve the current situation of the lack of freshwater resources in the country.
  • the distiller 18 is located one to ten times below sea level. The position of the meter is convenient for the distiller 18 to better desalinize the seawater, which improves the desalination efficiency of seawater.
  • the bottom of the distiller 18 is provided with a sea salt conveyor 21, and one end of the sea salt conveyor 21 extends to the land, so that the sea salt conveyor 21 can transport the distilled sea salt, the No. 1 condenser 7, the evaporator 14 and the The No. 2 condenser 20 is all of the spiral tube type, which realizes the sufficient reaction.
  • the high-temperature ammonia gas in the No. 1 steam pipe 8 enters the No. 1 condenser 7, and the seawater enters the No. 1 condenser 7 through the No. 4 water pipe 6, and the high-temperature ammonia gas affects the No.
  • the seawater in 7 is heated, the temperature of the heated seawater is 75 degrees, and the ammonia gas becomes an ammonia gas solution after cooling down, and the seawater heated in the No. 1 condenser 7 enters the distributor 4 through the No.
  • the No. 3 water pipe 3 enters, the No. 2 water pipe 3 is mixed with the seawater of 75 degrees in the No.
  • the mixed seawater temperature reaches the water temperature required by the IDC server 1, and the mixed water enters the IDC server 1 through the server cooling pipe 2
  • the IDC server 1 is cooled and cooled, and the seawater after cooling the IDC server 1 becomes high-temperature seawater. Due to the pressure, after the seawater is heated, it will naturally pass through the No. 6 water pipe 22 Enter the evaporator 14, so that the device that originally needs to extract seawater from the water surface no longer needs to extract seawater, but naturally obtains high-temperature seawater through the pressure and the waste heat of the IDC server 1 to perform natural work on the evaporator 14.
  • the ammonia in the No. 1 condenser 7 The gas solution enters the No.
  • the distillation process Since the distiller 18 is located below the sea level, it forms a height difference with the No. 2 condenser 20 on the shore, and the heated steam will rise from the sea level with the No. 3 steam pipe 19 to the No. 2 condenser on the shore.
  • the condenser 20 is condensed, the sea breeze on the seaside refrigerates the No. 2 condenser 20, and the water vapor is condensed into fresh water, and the distilled sea salt crystals are transported to the land through the sea salt conveyor 21.
  • first”, “second”, “third”, “fourth” are only used for descriptive purposes and should not be understood as indicating or implying relative importance or implying the number of technical features indicated, Thus, features defined as “first”, “second”, “third”, “fourth” may expressly or implicitly include at least one of such features.

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  • Engineering & Computer Science (AREA)
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  • General Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Computer Hardware Design (AREA)
  • Microelectronics & Electronic Packaging (AREA)
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  • Sustainable Development (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Physics & Mathematics (AREA)
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  • General Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)

Abstract

一种用于海水温差发电装置的星合循环系统，通过阀门实现了二号通水管和四号通水管的限流，利用海水压强取代两个冷热海水的抽水泵，让装置的能耗减低了90％，通过分配器实现了对高温海水与常温海水之间的混合处理，通过IDC服务器实现了服务器冷却管充分利用IDC的废热并对海水进行了提前加热温度升至70度左右，通过蒸馏器和二号冷凝器实现了蒸馏完的水蒸气是以气态的方式输送到二号冷凝器，通过二号冷凝器实现了借助冷凝设备二号冷凝器以风冷的方式进行冷热交换产生水汽液化。

Description

一种用于海水温差发电装置的星合循环系统 技术领域
本发明涉及海水温差发电技术领域与海水淡化技术领域，具体为一种用于海水温差发电装置的星合循环系统。
 背景技术
海洋温差能装置中的混合循环，上原循环，卡琳娜循环，朗肯循环等现在世界上所有的循环都存在能耗大的问题。其能量消耗与自身产能几乎持平甚至高于产出，这也是了导致海洋温差能发电即使是0能耗的发电装置却在以往140多年来都没有得到广泛的推广与应用而是一直被封存于实验室里；
现有的海洋温差能装置需要消耗大量的电力去抽取水面温海水以及水下1000米的冷海水，浪费了大量的电力资源，且传统的海水温差发电中不能对蒸馏后的水蒸气进行有效的输送，造成了大量的资源浪费。
 技术解决方案
本发明的目的在于提供一种用于海水温差发电装置的星合循环系统，以解决上述背景技术中提出的问题。
为实现上述目的，本发明提供如下技术方案：一种用于海水温差发电装置的星合循环系统，包括IDC服务器、一号冷凝器、蒸发器、透平机、发电机、蒸馏器和二号冷凝器，所述IDC服务器的一侧设有服务器冷却管，所述服务器冷却管的一端设有二号通水管，所述IDC服务器的顶部设有一号通水管，所述一号通水管的一端连接与蒸发器，所述服务器冷却管的一端设有五号通水管，所述五号通水管与二号通水管连接，所述五号通水管的一端设有分配器，所述分配器的一侧设有三号通水管，所述三号通水管的一端连接有一号冷凝器，所述一号冷凝器的一侧设有四号通水管，所述一号冷凝器的一侧设有七号通水管，所述七号通水管的内部设有氨气，所述七号通水管的一端设有工质泵，所述工质泵的一侧设有八号通水管，且八号通水管的一端与蒸发器连接，所述蒸发器的顶部设有二号通汽管，所述二号通汽管的一端连接有透平机，所述透平机的一侧安装有发电机，所述透平机的一侧设有一号通汽管，且一号通汽管的一端与一号冷凝器连接，所述蒸发器的一侧通过通气管连接有蒸馏器，所述蒸馏器的一侧设有三号通汽管，所述分配器的顶部设有六号通水管，所述六号通水管的一端设有蒸馏器，所述三号通汽管的一端设有二号冷凝器。
作为本发明的一种优选方案：所述二号通水管和四号通水管的外侧均设有阀门。
作为本发明的一种优选方案：所述蒸馏器的顶部设有真空泵。
作为本发明的一种优选方案：所述IDC服务器位于海平面以下五十至六十米的位置。
作为本发明的一种优选方案：所述一号冷凝器、透平机、发电机和蒸发器均位于海平面以下二十米的位置。
作为本发明的一种优选方案：所述二号冷凝器位于陆地上。
作为本发明的一种优选方案：所述蒸馏器位于海平面以下一至十米的位置。
作为本发明的一种优选方案：所述蒸馏器内的蒸气以气态方式自然输送至陆地上的二号冷凝器进行淡水提取。
作为本发明的一种优选方案：所述蒸馏器的底部设有海盐输送机，所述海盐输送机的一端延伸至陆地上。
作为本发明的一种优选方案：所述一号冷凝器、蒸发器和二号冷凝器均与螺旋管式。
 有益效果
与现有技术相比，本发明的有益效果是：本发明的结构简单，新颖且实用性强，通过加入了阀门，实现了二号通水管和四号通水管的限流，利用海水压强取代了两个冷热海水的抽水泵，让装置的能耗减低了90%，通过加入了分配器，实现了对高温海水与常温海水之间的混合处理，通过加入了IDC服务器，实现了服务器冷却管充分利用IDC的废热并对海水进行了提前加热温度升至70度左右，通过加入了蒸发器，实现了热水对蒸发器内液化氨气的升温并重新汽化，通过加入了透平机，实现了发电机的发电，通过加入了冷凝器，实现了氨气的冷凝液化，通过加入了蒸馏器，实现了海水的蒸馏处理，通过加入了海盐输送机，实现了蒸馏出海盐的输送，通过加入了蒸馏器和二号冷凝器，蒸馏器和二号冷凝器有高低落差，实现了蒸馏完的水蒸气是以气态的方式输送到二号冷凝器，通过加入了二号冷凝器，实现了借助冷凝设备二号冷凝器以风冷的方式进行冷热交换产生水汽液化。
 附图说明
图1为本发明内部结构示意图；
图2为本发明部分组件分布图。
图中：1、IDC服务器；2、服务器冷却管；3、二号通水管；4、分配器；5、三号通水管；6、四号通水管；7、一号冷凝器；8、一号通汽管；9、七号通水管；10、工质泵；11、八号通水管；12、五号通水管；13、二号通汽管；14、蒸发器；15、透平机；16、发电机；17、真空泵；18、蒸馏器；19、三号通汽管；20、二号冷凝器；21、海盐输送机；22、六号通水管；23、一号通水管。
 本发明的实施方式
下面将结合本发明实施例中的附图，对本发明实施例中的技术方案进行清楚、完整地描述，显然，所描述的实施例仅仅是本发明一部分实施例，而不是全部的实施例。基于本发明中的实施例，本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例，都属于本发明保护的范围。
请参阅图1-2，本发明提供一种技术方案：一种用于海水温差发电装置的星合循环系统，包括IDC服务器1、一号冷凝器7、蒸发器14、透平机15、发电机16、蒸馏器18和二号冷凝器20，IDC服务器1的一侧设有服务器冷却管2，服务器冷却管2的一端设有二号通水管3，IDC服务器1的顶部设有一号通水管23，一号通水管23的一端连接与蒸发器14，服务器冷却管2的一端设有五号通水管12，五号通水管12与二号通水管3连接，五号通水管12的一端设有分配器4，分配器4的一侧设有三号通水管5，三号通水管5的一端连接有一号冷凝器7，一号冷凝器7的一侧设有四号通水管6，一号冷凝器7的一侧设有七号通水管9，七号通水管9的内部设有氨气，七号通水管9的一端设有工质泵10，工质泵10的一侧设有八号通水管11，且八号通水管11的一端与蒸发器14连接，蒸发器14的顶部设有二号通汽管13，二号通汽管13的一端连接有透平机15，透平机15的一侧安装有发电机16，透平机15的一侧设有一号通汽管8，且一号通汽管8的一端与一号冷凝器7连接，蒸发器14的一侧通过通气管连接有蒸馏器18，蒸馏器18的一侧设有三号通汽管19，分配器4的顶部设有六号通水管22，六号通水管22的一端设有蒸馏器18，三号通汽管19的一端设有二号冷凝器20，便于一号冷凝器7对氨气进行液化处理，提高了循环效率。
二号通水管3和四号通水管6的外侧均设有阀门，便于阀门对二号通水管3和四号通水管6的水流进行控制，蒸馏器18的顶部设有真空泵17，便于真空泵17对蒸馏器18进行抽真空处理，提高了蒸馏效率，IDC服务器1位于海平面以下五十至六十米的位置，便于IDC服务器1完全利用其废热发电，不把废热排入海洋，从而降低热气污染，降低碳排放量，减少IDC服务器1的能耗，节省陆地空间，一号冷凝器7、透平机15、发电机16和蒸发器14均位于海平面以下二十米的位置，提高了工作效率，二号冷凝器20位于陆地上，便于对淡水进行收集，海水淡化以气化形态输送将大幅度降低海水淡化成本，解决国家淡水资源缺乏的现状，蒸馏器18位于海平面以下一至十米的位置，便于蒸馏器18对海水更好的淡化处理，提高了海水淡化效率，蒸馏器18内的蒸气以气态方式自然输送至陆地上的二号冷凝器20进行淡水提取，提高了淡水的提取的效率，蒸馏器18的底部设有海盐输送机21，海盐输送机21的一端延伸至陆地上，便于海盐输送机21对蒸馏出的海盐进行输送，一号冷凝器7、蒸发器14和二号冷凝器20均与螺旋管式，实现了反应的充分。
具体的，在使用时，一号通汽管8内高温的氨气进入一号冷凝器7内，海水通过四号通水管6进入一号冷凝器7内，高温的氨气对一号冷凝器7内的海水进行加热，加热后的海水温度为75度，氨气降温后变为氨气溶液，一号冷凝器7内加热的海水通过三号通水管5进入分配器4内，海水从二号通水管3进入，二号通水管3与三号通水管5内75度的海水混合，混合的海水温度达到IDC服务器1所需的水温，混合后的水通过服务器冷却管2进入IDC服务器1内并对其进行废热回收处理，并对IDC服务器1进行降温冷却，对IDC服务器1进行冷却处理后的海水变成高温海水，由于压强的缘故在海水受热后它会自然通过六号通水管22进入蒸发器14，让原本需要抽取水面海水的装置不再需要抽取海水了，而是通过压强和IDC服务器1的废热自然得到高温海水对蒸发器14进行自然做工，一号冷凝器7内的氨气溶液进入七号通水管9，七号通水管9内的氨气溶液通过工质泵10进入八号通水管11，八号通水管11内的氨气溶液进入蒸发器14，蒸发器14内的高温海水对氨气溶液进行蒸发处理，氨气溶液蒸发变为氨气，氨气通过二号通汽管13进入透平机15，透平机15带动发电机16进行发电，蒸发器14内的海水进入蒸馏器18内，未混合的75度海水直接通过六号通水管22进入蒸馏器18内，真空泵17对蒸馏器18的内部进行真空处理，对75度的海水进行蒸馏处理，蒸馏过程中由于蒸馏器18位于海平面下，所以它与在岸上的二号冷凝器20形成了一个高低落差，受热的蒸气会随着三号通汽管19从海平面下上升到岸上的二号冷凝器20进行冷凝，海边的海风对二号冷凝器20进行制冷，水汽冷凝后变为淡水，蒸馏后的海盐结晶通过海盐输送机21输送到陆地。
在本发明的描述中，需要理解的是，术语“同轴”、“底部”、“一端”、“顶部”、“中部”、“另一端”、“上”、“一侧”、“顶部”、“内”、“前部”、“中央”、“两端”等指示的方位或位置关系为基于附图所示的方位或位置关系，仅是为了便于描述本发明和简化描述，而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作，因此不能理解为对本发明的限制。
此外，术语“第一”、“第二”、“第三”、“第四”仅用于描述目的，而不能理解为指示或暗示相对重要性或者隐含指明所指示的技术特征的数量，由此，限定有“第一”、“第二”、“第三”、“第四”的特征可以明示或者隐含地包括至少一个该特征。
在本发明中，除非另有明确的规定和限定，术语“安装”、“设置”、“连接”、“固定”、“旋接”等术语应做广义理解，例如，可以是固定连接，也可以是可拆卸连接，或成一体；可以是机械连接，也可以是电连接；可以是直接相连，也可以通过中间媒介间接相连，可以是两个元件内部的连通或两个元件的相互作用关系，除非另有明确的限定，对于本领域的普通技术人员而言，可以根据具体情况理解上述术语在本发明中的具体含义。
尽管已经示出和描述了本发明的实施例，对于本领域的普通技术人员而言，可以理解在不脱离本发明的原理和精神的情况下可以对这些实施例进行多种变化、修改、替换和变型，本发明的范围由所附权利要求及其等同物限定。

Claims (10)

  1. 一种用于海水温差发电装置的星合循环系统，包括IDC服务器（1）、一号冷凝器（7）、蒸发器（14）、透平机（15）、发电机（16）、蒸馏器（18）和二号冷凝器（20），其特征在于，所述IDC服务器（1）的一侧设有服务器冷却管（2），所述服务器冷却管（2）的一端设有二号通水管（3），所述IDC服务器（1）的顶部设有一号通水管（23），所述一号通水管（23）的一端连接与蒸发器（14），所述服务器冷却管（2）的一端设有五号通水管（12），所述五号通水管（12）与二号通水管（3）连接，所述五号通水管（12）的一端设有分配器（4），所述分配器（4）的一侧设有三号通水管（5），所述三号通水管（5）的一端连接有一号冷凝器（7），所述一号冷凝器（7）的一侧设有四号通水管（6），所述一号冷凝器（7）的一侧设有七号通水管（9），所述七号通水管（9）的内部设有氨气，所述七号通水管（9）的一端设有工质泵（10），所述工质泵（10）的一侧设有八号通水管（11），且八号通水管（11）的一端与蒸发器（14）连接，所述蒸发器（14）的顶部设有二号通汽管（13），所述二号通汽管（13）的一端连接有透平机（15），所述透平机（15）的一侧安装有发电机（16），所述透平机（15）的一侧设有一号通汽管（8），且一号通汽管（8）的一端与一号冷凝器（7）连接，所述蒸发器（14）的一侧通过通气管连接有蒸馏器（18），所述蒸馏器（18）的一侧设有三号通汽管（19），所述分配器（4）的顶部设有六号通水管（22），所述六号通水管（22）的一端设有蒸馏器（18），所述三号通汽管（19）的一端设有二号冷凝器（20）。
  2. 根据权利要求1所述的一种用于海水温差发电装置的星合循环系统，其特征在于：所述二号通水管（3）和四号通水管（6）的外侧均设有阀门。
  3. 根据权利要求1所述的一种用于海水温差发电装置的星合循环系统，其特征在于：所述蒸馏器（18）的顶部设有真空泵（17）。
  4. 根据权利要求1所述的一种用于海水温差发电装置的星合循环系统，其特征在于：所述IDC服务器（1）位于海平面以下五十至六十米的位置。
  5. 根据权利要求1所述的一种用于海水温差发电装置的星合循环系统，其特征在于：所述一号冷凝器（7）、透平机（15）、发电机（16）和蒸发器（14）均位于海平面以下二十米的位置。
  6. 根据权利要求1所述的一种用于海水温差发电装置的星合循环系统，其特征在于：所述二号冷凝器（20）位于陆地上。
  7. 根据权利要求1所述的一种用于海水温差发电装置的星合循环系统，其特征在于：所述蒸馏器（18）位于海平面以下一至十米的位置。
  8. 根据权利要求1所述的一种用于海水温差发电装置的星合循环系统，其特征在于：所述蒸馏器（18）内的蒸气以气态方式自然输送至陆地上的二号冷凝器（20）进行淡水提取。
  9. 根据权利要求1所述的一种用于海水温差发电装置的星合循环系统，其特征在于：所述蒸馏器（18）的底部设有海盐输送机（21），所述海盐输送机（21）的一端延伸至陆地上。
  10. 根据权利要求1所述的一种用于海水温差发电装置的星合循环系统，其特征在于：所述一号冷凝器（7）、蒸发器（14）和二号冷凝器（20）均与螺旋管式。
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