CN109205736A - A kind of hot driven free piston reverse osmosis seawater desalting dynamical system based on Stirling cycle - Google Patents

A kind of hot driven free piston reverse osmosis seawater desalting dynamical system based on Stirling cycle Download PDF

Info

Publication number
CN109205736A
CN109205736A CN201811059208.5A CN201811059208A CN109205736A CN 109205736 A CN109205736 A CN 109205736A CN 201811059208 A CN201811059208 A CN 201811059208A CN 109205736 A CN109205736 A CN 109205736A
Authority
CN
China
Prior art keywords
free piston
reverse osmosis
engine
dynamical system
seawater
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN201811059208.5A
Other languages
Chinese (zh)
Other versions
CN109205736B (en
Inventor
耿冬寒
李秀兵
金龙
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tianjin Polytechnic University
Original Assignee
Tianjin Polytechnic University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Tianjin Polytechnic University filed Critical Tianjin Polytechnic University
Priority to CN201811059208.5A priority Critical patent/CN109205736B/en
Publication of CN109205736A publication Critical patent/CN109205736A/en
Application granted granted Critical
Publication of CN109205736B publication Critical patent/CN109205736B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/441Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/025Reverse osmosis; Hyperfiltration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/08Apparatus therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/10Accessories; Auxiliary operations
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2311/00Details relating to membrane separation process operations and control
    • B01D2311/20Power consumption
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/08Seawater, e.g. for desalination
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/002Construction details of the apparatus
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/10Energy recovery
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination
    • Y02A20/131Reverse-osmosis
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination
    • Y02A20/138Water desalination using renewable energy
    • Y02A20/144Wave energy

Abstract

The hot driven free piston reverse osmosis seawater desalting dynamical system based on Stirling cycle that the invention discloses a kind of, the system comprises: the cold chamber of type Stirling engine with free piston (1), engine cooling apparatus (2), engine regenerator (3), engine heater (4), the hot chamber of type Stirling engine with free piston (5), free piston assembly (6), compression accumulator (7), 2/2-way solenoid valve (8) and load accumulator (9), seawater desalination reverse osmosis membrane module (10);The engine cooling apparatus (2), engine regenerator (3), engine heater (4) join end to end;By realizing the reciprocating motion of free piston assembly under the cooperation of compression accumulator using Stirling cycle function, the intracavitary seawater of driving pump overcomes osmotic pressure to enter reverse osmosis membrane assembly, is desalinated system of the invention;System proposed by the present invention is to reduce energy conversion and transmission link by simplifying transmission chain, can be further improved the Energy economy quality for improving desalination by reverse osmosis.

Description

A kind of hot driven free piston reverse osmosis seawater desalting power based on Stirling cycle System
Technical field
The present invention relates to heat-driven desalination by reverse osmosis field more particularly to a kind of hot driven frees based on Stirling cycle Piston reverse osmosis seawater desalting dynamical system.
Background technique
Freshwater resources are the important material bases of mankind's existence, economic development and social progress.Nowadays, due to Greatly develop industry, the discharge of sanitary sewage, water pollution is increasingly severe caused by rubbish huddles etc..The big portion in the whole world now Point country belongs to water shortage country, and the earth is there are a large amount of seawater, and sea water desalination is to solve coastal area shortage of fresh water Effective way.While alleviating freshwater resources anxiety, sea water desalination also brings new pressure to the energy and environment.With energy Source is becoming tight with environmental problem day, and the energy needed for sea water desalination will become research emphasis.
In the technical field of sea water desalination, hyperfiltration has worldwide quite been widely applied, at present One of the three big main stream approach of sea water desalination are listed as with multistage flash distillation, multi-effect distilling.Principle of reverse osmosis is pushed away with outside energy Dynamic seawater realizes the separation of salinity and water in solution by macromolecule membrane.Although phase transformation, technique intrinsic energy is not present in the process Consume less, and the hydraulic energy of concentrated seawater can also be achieved energy regenerating after desalinating, but the power source of desalination by reverse osmosis is high-pressure pump, Operating pressure generally increases with increasing for seawater salinity, in order to maintain the higher water yield of equipment, high-pressure pump also need be again Seawater provides additional motive force to overcome process resistance, and work power consumption will generally occupy system energy consumption about 35%
Scotsman's Stirling (Robert Stirling) proposition in 1816 one is by two constant temperature process and two equal appearances The thermodynamic cycle of process composition, referred to as Stirling cycle.Stirling cycle is swollen by two constant volume endothermic processes and two fixed temperature The Reversible Cycle of swollen process composition, and the heat of constant volume exothermic process releasing is exactly constant volume endothermic process and is absorbed.Heat engine It absorbs heat in fixed temperature (T1) expansion process from high temperature heat source, and to low-temperature heat source heat release in fixed temperature (T2) compression process.This is followed Ring is used primarily for Thermal Motor, and the working medium in system is compressed continuously and expands under different potential temperature, last output work.
Conventional reverse osmosis process flow is: raw water → pretreatment system → high-pressure hydraulic pump → reverse osmosis membrane assembly → purification Water.For desalination by reverse osmosis dynamical system, only needs that seawater can be pushed to overcome osmotic pressure by reverse osmosis membrane, push the shape of function Formula may be either the shaft work of rotary pump, can also do work for the straight line of reciprocating pump (such as piston type).
Stirling engine can to the extremely well-adapted of heat source as a kind of external piston engine tool heated To utilize the renewable energy such as solar energy, biomass energy and industrial exhaust heat, exhaust gas etc..Develop on the basis of conventional engines from The rigid bodies transmission mechanisms such as crank connecting link are cancelled by piston engine, using non-rigid medium as the receiving of piston translation mechanical energy Body keeps the periodicity of movement.
Summary of the invention
It is an object of the invention to overcome dynamical problem present in current seawater desalination system, provide a kind of based on this The hot driven free piston reverse osmosis seawater desalting dynamical system of Te Lin circulation has compact-sized, efficient energy conversion height, component Few, power density is high, energy
Utilization efficiency is high, and reliability is higher, the advantages of using clean energy resource;And it can be using low-grade heat source as heating Heat source, utilization efficiency of heat energy are higher.A kind of hot reverse osmosis seawater of driven free piston based on Stirling cycle provided by the invention Desalination dynamical system has wide development in heat-driven desalination by reverse osmosis field and should prospect.
To achieve the goals above, the present invention provides a kind of hot reverse osmosis sea of driven free piston based on Stirling cycle Water desalinates dynamical system, the system comprises: the cold chamber of α type Stirling engine with free piston (1), engine cooling apparatus (2), Engine regenerator (3), engine heater (4), the hot chamber of α type Stirling engine with free piston (5), free piston assembly (6), compression accumulator (7), 2/2-way solenoid valve (8) and load accumulator (9), seawater desalination reverse osmosis membrane module (10); The engine cooling apparatus (2), engine regenerator (3), engine heater (4) join end to end.
As a kind of Novel power system, the origin of heat that the engine heater (4) absorbs is abundant, can be chemistry Energy burning, electric energy heating, nuclear energy etc., can also be Novel clean solar energy, geothermal energy etc..
As a kind of Novel power system, gas working medium in the system be helium, argon gas, nitrogen, air or they Mixed gas.
As a kind of Novel power system, the engine uses α type Stirling engine with free piston, and structure is simple It is compact.
As a kind of Novel power system, the engine is using compression accumulator (7) cooperation 2/2-way solenoid valve (8) Realize the operating of Stirling engine.
As a kind of Novel power system, the engine cooling apparatus (2) of the system is cooling using seawater, and cooling hydrodynamic(al) Power derives from Stirling engine part output pressure.
As a kind of Novel power system, the load accumulator (9) and seawater desalination reverse osmosis membrane module of the system (10) it is connected, stable output pressure can be provided.
A kind of hot driven free piston reverse osmosis seawater desalting dynamical system based on Stirling cycle of the invention, advantage It is:
1, the origin of heat that system of the invention absorbs is inhaled than wide, and heat source adaptability is stronger, is suitable for various energy Source, such as solar energy, bio-fuel, industrial exhaust heat, nuclear energy etc.;
2, system of the invention uses the environmentally friendly gas working medium such as helium, argon gas, nitrogen, air or their mixed gas, There is no greenhouse effects, environmentally friendly;
3, the knot of system of the invention using Stirling engine with free piston compared to traditional Stirling engine Structure reduces the free-piston intermediate transfer component in an engine, to reduce the mechanical oscillation of system, improve and be The reliability and service life of system have higher power density, more compact structure and less material consumption;
4, system of the invention uses free-piston desalination by reverse osmosis dynamical system, is further simplified transmission chain, reduces energy Amount conversion and transmission link are conducive to improve efficiency of energy utilization, reduce the energy cost of desalination;
5, system of the invention, which can effectively utilize clean energy resource and provide, stablizes power, realizes sea water desalination, has weight Big effects of energy saving and emission reduction and wide application prospect.
Detailed description of the invention
A kind of hot driven free piston reverse osmosis seawater desalting dynamical system schematic diagram based on Stirling cycle of Fig. 1.
Appended drawing reference:
1, the cold chamber of α type Stirling engine with free piston
2, engine cooling apparatus
3, engine regenerator
4, engine heater
5, the hot chamber of α type Stirling engine with free piston
6, free piston assembly
7, compression accumulator
8,2/2-way solenoid valve
9, accumulator is loaded
10, seawater desalination reverse osmosis membrane module
Specific embodiment
To make the object, technical solutions and advantages of the present invention clearer, below in conjunction with attached in the embodiment of the present invention Figure, is clearly and completely described technical solution of the present invention, it is clear that described embodiment is that a part of the invention is real Example is applied, instead of all the embodiments.Based on the embodiments of the present invention, those of ordinary skill in the art are not making creation Property labour under the premise of every other embodiment obtained, shall fall within the protection scope of the present invention.
The present invention efficiently utilizes various heat sources, and adaptability is stronger, using α type Stirling engine with free piston, reduces Intermediate transmission part, may be implemented the densification of higher power density and structure and the low cost of processing and fabricating, and operating is reliable Property greatly improves, it is easy to accomplish industrial production and practical application.
As shown in Figure 1, the present invention is a kind of hot driven free piston reverse osmosis seawater desalting power based on Stirling cycle System, the system comprises: the cold chamber of α type Stirling engine with free piston (1), engine cooling apparatus (2), engine backheat Device (3), engine heater (4), the hot chamber of α type Stirling engine with free piston (5), free piston assembly (6), compression store Energy device (7), 2/2-way solenoid valve (8) and load accumulator (9), seawater desalination reverse osmosis membrane module (10);The engine Cooler (2), engine regenerator (3), engine heater (4) join end to end.
A kind of hot driven free piston reverse osmosis seawater desalting dynamical system based on Stirling cycle, at work, Gas working medium absorbs heat from heat source by engine heater 4, and hot chamber working medium expansion work pushes free-piston (6) Movement, the intracorporal seawater of other end chamber of compression piston, a part of seawater enter compression accumulator (7) storage unit by check valve Divide energy;A part is entered engine cooling apparatus (2) by check valve, and last part enters seawater desalination reverse osmosis film group Part (10) provides pressure for reverse osmosis membrane.When free-piston (6) moves to outer dead point, speed zero, 2/2-way is electric at this time Magnet valve (8) is connected, and the seawater in accumulator enters plunger shaft by three-way electromagnetic valve (8), and piston is pushed to move to inner dead point, stores Energy device serves as engine backhaul startup power.
Working medium in engine cooling apparatus (2) cooling acting, transports free-piston (6) to the left by engine regenerator (3) The intracavitary seawater acting of dynamic (as shown in Figure 1) compression piston, a part of seawater enter compression accumulator (7) by check valve and store Portion of energy;A part enters engine cooling apparatus (2) by check valve, and last part enters seawater desalination reverse osmosis film Component (10) provides pressure for reverse osmosis membrane.When free-piston (6) moves to inner dead point, speed zero, 2/2-way at this time Solenoid valve (8) is connected, and the seawater in accumulator enters plunger shaft by three-way electromagnetic valve (8), and piston is pushed to move to outer dead point, It moves repeatedly.All concatenating accumulator with engine cooling apparatus (2) in seawater desalination reverse osmosis membrane module (10) is that seawater is light Change reverse osmosis membrane assembly (10) and engine cooling apparatus (2) and source of consistent pressure is provided.
It should be noted last that the above material is only used to illustrate the technical scheme of the present invention and not to limit it.Although reference Embodiment describes the invention in detail, those skilled in the art should understand that, to technical solution of the present invention It is modified or replaced equivalently, without departure from the spirit and scope of technical solution of the present invention, should all cover of the invention In scope of the claims.

Claims (10)

1. a kind of hot driven free piston reverse osmosis seawater desalting dynamical system based on Stirling cycle, which is characterized in that described System includes: the cold chamber of α type Stirling engine with free piston (1), engine cooling apparatus (2), engine regenerator (3), hair Motivation heater (4), the hot chamber of α type Stirling engine with free piston (5), free piston assembly (6), compression accumulator (7), 2/2-way solenoid valve (8) and load accumulator (9), seawater desalination reverse osmosis membrane module (10);The engine cooling apparatus (2), engine regenerator (3), engine heater (4) join end to end.
2. the hot driven free piston reverse osmosis seawater desalting dynamical system according to claim 1 based on Stirling cycle, It is characterized in that, the origin of heat that the engine heater (4) absorbs is inhaled than wide, heat source adaptability is stronger, is applicable in In various energy, such as solar energy, bio-fuel, industrial exhaust heat, nuclear energy etc..
3. the hot driven free piston reverse osmosis seawater desalting dynamical system according to claim 1 based on Stirling cycle, It is characterized in that, the gas working medium in the system is hydrogen, helium, argon gas, nitrogen, air or their mixed gas.
4. the hot driven free piston reverse osmosis seawater desalting dynamical system according to claim 1 based on Stirling cycle, It is characterized in that, the power resources use α type Stirling engine with free piston.
5. the hot driven free piston reverse osmosis seawater desalting dynamical system according to claim 1 based on Stirling cycle, It is characterized in that, the engine cooling apparatus (2) is cooling using seawater, power resources are produced by free-piston reciprocating motion Part seawater pressure energy.
6. the hot driven free piston reverse osmosis seawater desalting dynamical system according to claim 1 based on Stirling cycle, It is characterized in that, the free piston assembly (6) under the cooperation of compression accumulator (7) and 2/2-way solenoid valve (8), is realized Reciprocating motion, the intracavitary seawater of driving pump overcomes osmotic pressure to enter reverse osmosis membrane assembly, desalinated.
7. the hot driven free piston reverse osmosis seawater desalting dynamical system according to claim 4 based on Stirling cycle, It is characterized in that, described use α type Stirling engine with free piston.
8. the hot driven free piston reverse osmosis seawater desalting dynamical system according to claim 1 based on Stirling cycle, It is characterized in that, described connect in free-piston pump chamber with each pipeline adds check valve, as shown in Figure of description (1).
9. the hot driven free piston reverse osmosis seawater desalting dynamical system according to claim 1 based on Stirling cycle, It is characterized in that, the load accumulator (9), seawater desalination reverse osmosis membrane module (10) are connected.
10. the hot driven free piston reverse osmosis seawater desalting dynamical system according to claim 1 based on Stirling cycle, It is characterized in that, described all water sources used are all seawater.
CN201811059208.5A 2018-09-12 2018-09-12 Stirling cycle-based thermal drive free piston reverse osmosis sea water desalination power system Active CN109205736B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201811059208.5A CN109205736B (en) 2018-09-12 2018-09-12 Stirling cycle-based thermal drive free piston reverse osmosis sea water desalination power system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811059208.5A CN109205736B (en) 2018-09-12 2018-09-12 Stirling cycle-based thermal drive free piston reverse osmosis sea water desalination power system

Publications (2)

Publication Number Publication Date
CN109205736A true CN109205736A (en) 2019-01-15
CN109205736B CN109205736B (en) 2023-05-23

Family

ID=64983727

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201811059208.5A Active CN109205736B (en) 2018-09-12 2018-09-12 Stirling cycle-based thermal drive free piston reverse osmosis sea water desalination power system

Country Status (1)

Country Link
CN (1) CN109205736B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2021067397A1 (en) * 2019-10-01 2021-04-08 Purdue Research Foundation Double-acting piston batch reverse osmosis desalination assembly and method

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1733615A (en) * 2005-07-01 2006-02-15 天津大学 Energy-saving reverse osmosis desalting process and device for seawater/brackish water
CN101782095A (en) * 2010-03-12 2010-07-21 国家海洋局天津海水淡化与综合利用研究所 Differential energy recovery device and method for seawater desalination system
CN204342494U (en) * 2015-03-20 2015-05-20 中国人民解放军总后勤部建筑工程研究所 A kind of double-piston sea water desalinating plant
CN107560212A (en) * 2017-09-30 2018-01-09 中国科学院理化技术研究所 A kind of economic benefits and social benefits free-piston type Stirling thermal drivers refrigeration machine/heat pump
CN207435108U (en) * 2017-11-01 2018-06-01 吉林大学 A kind of energy recycle device of small-sized seawater desalination reverse osmosis system
CN207468239U (en) * 2017-11-15 2018-06-08 北京天诚同创电气有限公司 Seawater desalination system
CN108285192A (en) * 2018-03-28 2018-07-17 天津融渌众乐科技有限公司 A kind of desalination plant and its hybrid system using temperature difference driving
CN108506178A (en) * 2018-03-28 2018-09-07 天津融渌众乐科技有限公司 A kind of energy recycle device and its hybrid system of the driving of combination temperature difference

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1733615A (en) * 2005-07-01 2006-02-15 天津大学 Energy-saving reverse osmosis desalting process and device for seawater/brackish water
CN101782095A (en) * 2010-03-12 2010-07-21 国家海洋局天津海水淡化与综合利用研究所 Differential energy recovery device and method for seawater desalination system
CN204342494U (en) * 2015-03-20 2015-05-20 中国人民解放军总后勤部建筑工程研究所 A kind of double-piston sea water desalinating plant
CN107560212A (en) * 2017-09-30 2018-01-09 中国科学院理化技术研究所 A kind of economic benefits and social benefits free-piston type Stirling thermal drivers refrigeration machine/heat pump
CN207435108U (en) * 2017-11-01 2018-06-01 吉林大学 A kind of energy recycle device of small-sized seawater desalination reverse osmosis system
CN207468239U (en) * 2017-11-15 2018-06-08 北京天诚同创电气有限公司 Seawater desalination system
CN108285192A (en) * 2018-03-28 2018-07-17 天津融渌众乐科技有限公司 A kind of desalination plant and its hybrid system using temperature difference driving
CN108506178A (en) * 2018-03-28 2018-09-07 天津融渌众乐科技有限公司 A kind of energy recycle device and its hybrid system of the driving of combination temperature difference

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2021067397A1 (en) * 2019-10-01 2021-04-08 Purdue Research Foundation Double-acting piston batch reverse osmosis desalination assembly and method

Also Published As

Publication number Publication date
CN109205736B (en) 2023-05-23

Similar Documents

Publication Publication Date Title
CN106286170A (en) Solar energy, sea water source heat pump, combustion gas and supercritical carbon dioxide combined marine electricity generation system
Wong et al. Solar thermal water pumping systems: a review
CN102435000A (en) Solar energy system combined cooling and electricity based on ammonia water mixed refrigerant
CN101737282A (en) High-efficiency hybrid ocean temperature difference power generating system
US11859494B2 (en) Combined circulating system of micro gas turbine, transportation means and charging system
CN101915147A (en) Combustion motor and stirling compound engine
CN103982383A (en) Solar energy-ocean thermal energy combined power generation system
CN104929709B (en) Solar energy humid air cycle electricity-water cogeneration system
CN112648106A (en) Beta type stirling drive free piston seawater desalination pressurization system
CN109205736A (en) A kind of hot driven free piston reverse osmosis seawater desalting dynamical system based on Stirling cycle
CN210505692U (en) Distributed tower type solar-driven supercritical carbon dioxide seawater desalination system
CN202501677U (en) Steam compression refrigeration device driven by organic Rankine cycle
CN206942822U (en) The device externally to be done work using environment thermal energy
CN210135009U (en) Stirling compressed gas energy storage device
CN210559478U (en) Wind-solar complementary two-stage flash evaporation seawater desalination system based on vortex tube
CN113294307A (en) Wave energy assisted temperature difference energy power generation system
CN203515854U (en) Thermo-acoustic-driven Stirling engine
CN112576328A (en) Power cycle water and electricity cogeneration system and method thereof
CN113833619B (en) Recyclable osmotic pressure power generation system
CN217712707U (en) Energy conversion device for recovering power generation by using natural gas excess pressure
CN219220535U (en) Four-combined supply system for cold, hot and electric power and sea water desalination
CN217055318U (en) Carbon dioxide brayton and organic Rankine cycle power generation system
CN215176145U (en) Combined cooling and power supply circulating system
CN112145313B (en) Stirling compressed gas energy storage device and use method thereof
CN212838197U (en) Based on CO2Mixed working medium supercharging heat absorption transcritical circulation dry and hot rock geothermal power generation system

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant