CN107725191A - Power and water joint supply device - Google Patents
Power and water joint supply device Download PDFInfo
- Publication number
- CN107725191A CN107725191A CN201710981453.0A CN201710981453A CN107725191A CN 107725191 A CN107725191 A CN 107725191A CN 201710981453 A CN201710981453 A CN 201710981453A CN 107725191 A CN107725191 A CN 107725191A
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- China
- Prior art keywords
- ammonia
- combustion chamber
- water
- supply device
- power
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- 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.)
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Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02C—GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
- F02C3/00—Gas-turbine plants characterised by the use of combustion products as the working fluid
- F02C3/20—Gas-turbine plants characterised by the use of combustion products as the working fluid using a special fuel, oxidant, or dilution fluid to generate the combustion products
- F02C3/22—Gas-turbine plants characterised by the use of combustion products as the working fluid using a special fuel, oxidant, or dilution fluid to generate the combustion products the fuel or oxidant being gaseous at standard temperature and pressure
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/04—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of inorganic compounds, e.g. ammonia
- C01B3/047—Decomposition of ammonia
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B5/00—Water
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02G—HOT GAS OR COMBUSTION-PRODUCT POSITIVE-DISPLACEMENT ENGINE PLANTS; USE OF WASTE HEAT OF COMBUSTION ENGINES; NOT OTHERWISE PROVIDED FOR
- F02G3/00—Combustion-product positive-displacement engine plants
- F02G3/02—Combustion-product positive-displacement engine plants with reciprocating-piston engines
-
- 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
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
Abstract
The present invention discloses a kind of power and water joint supply device, the device includes ammonia feedway, combustion chamber, force piece and water collecting device, the ammonia feedway can connect combustion chamber so that ammonia is supplied into combustion chamber, the combustion chamber also receives air supply, the combustion chamber connects force piece with by being vented the activity of propulsion power part caused by combustion chambers burn, the combustion chamber has exhaust channel, and the water collecting device is located on exhaust channel and collects the water in exhaust.The device can produce pure water while power is produced, and be particluarly suitable for applying under the environmental conditions such as island, offshore platform, naval vessel.
Description
Technical field
The present invention relates to energy source and power supply system, more particularly to the device of power and water joint supply can be realized.
Background technology
Island, offshore platform, naval vessel etc. due to being limited by conditions such as natural locations, result in can not realize energy source and power and
Drinking water is self-supporting.Fed by the Shipping energy and fresh water, there is the problems such as transporting high cost, supply is unstable.Sea
The development of water desalination technology and commercial Application, existing semicentennial history, are formd with multistage flash evaporation, counter-infiltration during this period
With the industrial technology that multiple-effect evaporation is main representative.Expert it is believed that three, 40 years from now in commercial Application, Reng Jiangshi
Based on this three technology.
External most of seawater desalting plant is built in together with power plant, and this is current large-scale Seawater Desalination Project
Main construction mode.Water-electricity cogeneration is primarily referred to as desalinization water and electric power co alliance.Because desalinization cost is very big
Consumption electric power and the cost of steam are depended in degree, water-electricity cogeneration can utilize steam and the electric power of power plant to be filled for desalinization
Offer power is put, so as to realize that high efficiency of energy utilizes and reduced desalinization cost.But water-electricity cogeneration is extremely complex to be
System engineering, for main processes, including sea water preprocessing, desalination (desalination), desalination water post processing etc., there is energy
Optimum utilization need to solve with a series of problems, such as recovery, equipment antiscale and correct discharge of anti-corrosion and strong brine.
The content of the invention
It is an object of the invention to provide power and water joint supply device, with overcome in the prior art energy source and power with it is light
Above mentioned problem existing for water supply system.
The present invention solves one of used technical scheme of its technical problem：
Power and water joint supply device, including ammonia feedway, combustion chamber, force piece and water collecting device, the ammonia supply
Combustion chamber can be connected so that ammonia is supplied into combustion chamber to device, and the combustion chamber also receives air supply, combustion chamber connection force piece
So that by being vented the activity of propulsion power part caused by combustion chambers burn, the combustion chamber has exhaust channel, and the water collecting device is set
On exhaust channel and collect exhaust in water.
China is hydrazine yield and the most country of dosage in the world at present, accounts for 1/3 of Gross World Product or so, thus China
There is excellent condition to be done step-by-step from existing fossil energy and turn to the reproducible ammonia energy.
Power and water joint supply device are using ammonia as fuel, and the device can supply water while power is exported.By
Burnt in carbon-based fuel is not present in combustion chamber, turn into N after ammonia burning2And H2O, therefore the system is without CO2 emission.Control
Ammonia completely burned in a combustion chamber, pure water is can obtain in water collecting device.The water of ammonia burning generation is with water in exhaust channel
The form of steam is present, and vapor is condensate in exhaust channel via Temperature fall, then via water collecting device centralized collection.
Among one embodiment：The water collecting device includes condensing mechanism.Condensing mechanism can accelerate the condensation speed of vapor
Rate, improve the generation efficiency of liquid pure water.
Among one embodiment：The ammonia of ammonia feedway supply be liquid ammonia, the liquid ammonia pass through the condensing mechanism and from
Liquid ammonia, which becomes, turns to gaseous ammonia, and is aqueous water by the water vapor condensation in exhaust channel.Because the gasification latent heat of liquefied ammonia is higher
(under -33.41 DEG C and 101.325kPa, gasification latent heat reaches 1371.18kJ/kg), can significantly reduce steam temperature, even
It is reduced to below freezing, the higher ice of coproduction purity.
Among one embodiment：The ammonia of ammonia feedway supply be liquid ammonia, the liquid ammonia pass through the condensing mechanism and from
Liquid ammonia, which becomes, turns to gaseous ammonia, and is solid water by the water vapor condensation in exhaust channel.
The gasification latent heat of liquefied ammonia is higher, and under -33.41 DEG C and 101.325kPa, gasification latent heat reaches 1371.18kJ/kg, because
This present invention is using ammonia as fuel, can there is gasification latent heat (or cold) in technical solution of the present invention caused by liquid ammonia gasification
The recovery of effect ground utilizes.
Among one embodiment：The power also includes cold collection device with water joint supply device, and the ammonia feedway supplies
The ammonia given is liquid ammonia, and the cold collection device is connected between ammonia feedway and combustion chamber using while the liquefied ammonia that gasifies is ammonia
And cold is collected with outside cooling using the gasification latent heat of liquefied ammonia.Outside cooling is directed to power and water joint supply apparatus system
Outside cooling.The cold collection device includes at least one of air-conditioning equipment, refrigerating equipment or freezing equipment.The power with
Water joint supply device can also include refrigeration plant, and the cold collection device is connected with refrigeration plant by heat exchanger, should
Cold collection device cools down the refrigeration plant by heat exchanger.The embodiment be to gasification latent heat caused by liquid ammonia gasification (or
Cold) technical scheme that further utilizes.
Among one embodiment：The power also includes nitrogen collection device, the nitrogen collection device with water joint supply device
Exhaust channel is connected to collect nitrogen.Because the product of ammonia combustion reaction in atmosphere is water and nitrogen, water collecting device is located at
The water in exhaust is collected on exhaust channel, nitrogen is received by nitrogen collection device in the lump in the nitrogen and air of combustion reaction generation
Integrate as High Purity Nitrogen.The device and traditional device structure compared by separating air acquisition high-purity ammon are simple, and can significantly drop
Low energy expenditure.
Among one embodiment：The power and water joint supply device also include generator, force piece connection generator with
The generator is driven to export electric energy.Further realize the Joint Production of electric energy and pure water.
Among one embodiment：The power and water joint supply device, in addition to ammonia cracker, ammonia feedway connection
Ammonia cracker for ammonia cracker to provide ammonia, and the ammonia cracker, which decomposes ammonia and generated, hydrogen, and the ammonia cracker connects
Connect combustion chamber and include the fuel of hydrogen to be provided for combustion chamber.
The ammonia cracker energy decomposition unit liquid separation ammonia and generate have hydrogen, the ammonia cracker connection combustion chamber think burning
Room provides the fuel for including hydrogen and ammonia.Wherein：The burning-point of the hydrogen is less than the burning-point of ammonia, therefore hydrogen in combustion chamber first put by burning
Heat is to light the ammonia of combustion chamber, Hydrogen Energy accelerated combustion process, so as to improve the combustibility of ammonia fuel.Without increasing in the present embodiment
Carburation class A fuel A, because increased HC fuel needs extra fuel storage, conveying and control system, system is set to tend to be complicated.
Among one embodiment：The power and water joint supply device, in addition to heat exchanger, the heat exchanger match somebody with somebody combination burning
The exhaust of room, so that heat caused by the exhaust of combustion chamber imports ammonia cracker to be provided for ammonia cracking reaction via heat exchanger
Reaction heat.
Ammonia cracking reaction is the endothermic reaction, and ammonia cracker heat as caused by the exhaust of combustion chamber provides cracking reaction temperature
Degree, and extra heating energy source need not be increased, improve the efficiency of energy utilization of the power and water joint supply device.
Power and the water joint supply device of the present invention is by ammonia and air mixed combustion in a combustion chamber, caused by burning
The activity of propulsion power part is vented, and collects the water in exhaust combustion chamber.Among one embodiment：Mixed in a combustion chamber with air in ammonia
The step of before combination burning also including being gaseous ammonia by liquid ammonia gasification, the liquid ammonia gasification are that cold caused by gaseous ammonia is used for combustion
The water condensation burnt in the exhaust of room is aqueous water or solid water.Among another embodiment：Mixed in a combustion chamber with air in ammonia
Also include before burning, amino moiety is decomposed into the step of generating hydrogen, heat caused by the burning provides for amino moiety decomposition reaction
Reaction heat.
Compared with background technology, it has the following advantages that the technical program：
The power produces pure water or ice with water joint supply device while power is produced.Wherein, the ammonia cracks
Device energy decomposition unit liquid separation ammonia simultaneously generates and has hydrogen, Hydrogen Energy accelerated combustion process, so as to improve the combustibility of ammonia fuel, and
Other impurity will not be introduced in pure water or ice.Also, ammonia cracker heat can carry as caused by the exhaust of combustion chamber
For cracking reaction temperature, without increasing extra heating energy source.
Brief description of the drawings
The invention will be further described with reference to the accompanying drawings and detailed description.
Fig. 1 is system diagram of the power with water joint supply device of embodiment one；
Fig. 2 is system diagram of the power with water joint supply device of embodiment two；
Fig. 3 is system diagram of the power with water joint supply device of embodiment three；
Fig. 4 is system diagram of the power with water joint supply device of example IV.
Embodiment
Embodiment 1：
Power as shown in Figure 1 and water joint supply device, including combustion chamber 1, ammonia feedway 2, force piece 3 and water are received
Acquisition means 5, the ammonia feedway 2 can connect combustion chamber 1 so that ammonia is supplied into combustion chamber 1, and the combustion chamber 1 also receives air supply,
The combustion chamber 1 connects force piece 3, and to be burnt by combustion chamber 1, caused exhaust propulsion power part 3 is movable, and the combustion chamber 1 has
Exhaust channel 4, the water collecting device 5 are located on exhaust channel 4 and collect the water in exhaust.
With water joint supply device by ammonia and air mixed combustion in combustion chamber 1, caused exhaust of burning pushes away the power
The dynamic activity of force piece 3.Force piece 3 can be toggle or turbine mechanism, and force piece 3 drives generator 9 to export electric energy.
The water during combustion chamber 1 is vented is collected simultaneously, it is possible to achieve supplies water while output power.The device be especially suitable for island,
Electric power and drinking water joint supply under the environmental conditions such as offshore platform, naval vessel.Fired due to carbon-based fuel being not present in combustion chamber 1
Burn, turn into N after ammonia burning2And H2O, therefore the system is without CO2 emission.Ammonia completely burned in combustion chamber 1 is controlled, water is received
Pure water is can obtain in acquisition means 5.The water of ammonia burning generation exists as water vapor in exhaust channel 4, vapor warp
It is condensate in by Temperature fall in exhaust channel, then via the centralized collection of water collecting device 5.
In order to accelerate the condensing rate of vapor, the generation efficiency of liquid pure water is improved, may include in water collecting device 5
Condensing mechanism.Condensing mechanism can be heat pipe waste-heat recoverer, dividing wall type heat exchanger, heat regenerator, ceramic heat exchanger or
Jet model mixing heating unit.Heat pipe waste-heat recoverer is changed using what the efficient heat transfer characteristic and its environmental suitability of heat pipe manufactured
Thermal, its structure type are：Monoblock type, separate type or combined type.Dividing wall type heat exchanger heat exchanger can be：Cooling tower (or
Claim cooling column), gas scrubbing tower (or scrubbing tower), injecting type heat exchanger, mixing condenser.
Embodiment 2：
Power as shown in Figure 2 and water joint supply device, including combustion chamber 1, ammonia feedway 2, force piece 3 and water are received
Acquisition means 5, the ammonia feedway 2 can connect combustion chamber 1 so that ammonia is supplied into combustion chamber 1, and the combustion chamber 1 also receives air supply,
The combustion chamber 1 connects force piece 3, and to be burnt by combustion chamber 1, caused exhaust propulsion power part 3 is movable, and the combustion chamber 1 has
Exhaust channel 4, the water collecting device 5 are located on exhaust channel 4 and collect the water in exhaust.Force piece 3 can be crank connecting link
Mechanism or turbine mechanism.If force piece 3 selects turbine mechanism, gas turbine can be formed with compressor coaxial cooperation.This implementation
In example, the ammonia of the ammonia feedway 2 supply is liquid ammonia, and the liquid ammonia becomes from liquid ammonia by the condensing mechanism 5 and turns to gas
State ammonia, because the gasification latent heat of liquefied ammonia is higher (under -33.41 DEG C and 101.325kPa, gasification latent heat reaches 1371.18kJ/kg),
Steam temperature can be significantly reduced,
And it is aqueous water by the water vapor condensation in exhaust channel 4.The heat exchange amount of liquefied ammonia, the temperature of water can further be increased
Be reduced to it is below freezing, with the higher ice of coproduction purity.
Embodiment 3：
Power as shown in Figure 3 and water joint supply device, including combustion chamber 1, ammonia feedway 2,
Force piece 3, water collecting device 5 and ammonia cracker 6, the ammonia feedway 2 connection ammonia cracker 6 think that ammonia splits
Solve device 6 and ammonia is provided, the ammonia cracker 6, which decomposes ammonia and generated, hydrogen, and burning is thought in the ammonia cracker 6 connection combustion chamber
Room 1 provides the fuel for including hydrogen.The combustion chamber 1 also receives air supply, and the combustion chamber 1 connects force piece 3 to pass through combustion
Burning room 1 is vented the activity of propulsion power part 3 caused by burning, and force piece 3 drives the output electric energy of generator 9.The combustion chamber 1 has row
Gas path 4, the water collecting device 5 are located on exhaust channel 4 and collect the water in exhaust.
The ammonia cracker 6 decomposition unit liquid separation ammonia and can generate and have hydrogen, and the ammonia cracker 6 connection combustion chamber 1 is thought
Combustion chamber 1 provides the fuel for including hydrogen and ammonia.Wherein：The burning-point of the hydrogen is less than the burning-point of ammonia, therefore hydrogen is first in combustion chamber
Combustion heat release is to light the ammonia of combustion chamber 1, Hydrogen Energy accelerated combustion process, so as to improve the combustibility of ammonia fuel.The present embodiment
In need not increase HC fuel, because increased HC fuel needs extra fuel storage, conveying and control system, system is become
In complexity.
Among the present embodiment：The power also includes nitrogen collection device 7, the nitrogen collection device with water joint supply device
7 connect exhaust channels 4 to collect nitrogen.Because the product of ammonia combustion reaction in atmosphere is water and nitrogen, water collecting device 5 is set
The water in exhaust is collected on exhaust channel 4, nitrogen collects dress by nitrogen in the lump in the nitrogen and air of combustion reaction generation
Put 7 and be collected as High Purity Nitrogen.
Embodiment 4：
Power as shown in Figure 4 and water joint supply device, including combustion chamber 1, ammonia feedway 2, force piece 3, exhaust
Path 4, water collecting device 5, ammonia cracker 6 and heat exchanger 7.The ammonia feedway 2 connection ammonia cracker 6 thinks that ammonia splits
Solve device 6 and ammonia is provided, the ammonia cracker 6, which decomposes ammonia and generated, hydrogen, and burning is thought in the ammonia cracker 6 connection combustion chamber
Room 1 provides the fuel for including hydrogen.The combustion chamber 1 also receives air supply, and the combustion chamber 1 connects force piece 3 to pass through combustion
Burning room 1 is vented the activity of propulsion power part 3 caused by burning, and force piece 3 drives the output electric energy of generator 9.The combustion chamber 1 has row
Gas path 4, the water collecting device 5 are located on exhaust channel 4 and collect the water in exhaust.
The heat exchanger 7 coordinates the exhaust of combustion chamber, so that heat is via heat exchanger 7 caused by the exhaust of combustion chamber 1
Import ammonia 6 reaction heat to be provided for ammonia cracking reaction of cracker.Ammonia cracking reaction is the endothermic reaction, ammonia cracker 6 by
Heat caused by the exhaust of combustion chamber 1 provides cracking reaction temperature, and need not increase extra heating energy source, and improving this should
The efficiency of energy utilization of power and water joint supply device.
Under the catalytic action of ammonia catalyst for cracking, ammonia splits reaction temperature and is also required to remain more than 200 DEG C.Wherein, ammonia
Catalyst for cracking can be the catalyst for being loaded with ruthenium, rhodium, nickel and/or iron.After the exhaust propulsion power part 3 of combustion chamber 1, enter
Exhaust heat temperature in exhaust channel 4 still can reach 300-400 DEG C, can provide heat for ammonia cracking reaction, and need not
Increase extra heating energy source.Due to being cracked by ammonia and hydrogen mixed combustion, ammonia cracker 6 in combustion chamber 1 by amino moiety
For hydrogen, the temperature control in preferable ammonia cracker is at 200 DEG C -400 DEG C.
Embodiment described above only expresses the several embodiments of the present invention, and its description is more specific and detailed, but simultaneously
Therefore the limitation of the scope of the claims of the present invention can not be interpreted as.It should be pointed out that come for one of ordinary skill in the art
Say, without departing from the inventive concept of the premise, various modifications and improvements can be made, these belong to the protection of the present invention
Scope.Therefore, the protection domain of patent of the present invention should be determined by the appended claims.
Claims (10)
1. power and water joint supply device, including ammonia feedway, combustion chamber, force piece and water collecting device, ammonia supply
Device connects combustion chamber so that ammonia is supplied into combustion chamber, and the combustion chamber also receives air supply, and the combustion chamber connects force piece with logical
Cross exhaust propulsion power part activity caused by combustion chambers burn, it is characterised in that：The combustion chamber has exhaust channel, and the water is collected
Device is located on exhaust channel and collects the water in exhaust.
2. power according to claim 1 and water joint supply device, it is characterised in that：The water collecting device includes cold
Solidifying mechanism.
3. power according to claim 2 and water joint supply device, it is characterised in that：The ammonia of ammonia feedway supply
For liquid ammonia, the liquid ammonia becomes by the condensing mechanism and from liquid ammonia turns to gaseous ammonia, and by the vapor in exhaust channel
It is condensed into aqueous water or solid water.
4. power according to claim 1 and water joint supply device, it is characterised in that：Also include cold collection device,
The ammonia of ammonia feedway supply is liquid ammonia, and the cold collection device is connected between ammonia feedway and combustion chamber with simultaneously
The liquefied ammonia that gasifies is ammonia and collects cold using the gasification latent heat of liquefied ammonia with outside cooling.
5. power according to claim 4 and water joint supply device, it is characterised in that：The cold collection device includes
At least one of air-conditioning equipment, refrigerating equipment or freezing equipment.
6. power according to claim 4 and water joint supply device, it is characterised in that：Also include refrigeration plant, this is cold
Amount collection device is connected with refrigeration plant by heat exchanger, and the cold collection device cools down the refrigeration by heat exchanger and set
It is standby.
7. power according to claim 1 and water joint supply device, it is characterised in that：Also include nitrogen collection device,
The nitrogen collection device connects exhaust channel to collect nitrogen.
8. power according to claim 1 and water joint supply device, it is characterised in that：Also include generator, the power
Part connects generator to drive the generator to export electric energy.
9. the power according at least one in claim 1 to 8 and water joint supply device, it is characterised in that：Also include
Ammonia cracker, the fuel supply system connect ammonia cracker to provide ammonia for ammonia cracker, and the ammonia cracker decomposes
Ammonia simultaneously generates and has hydrogen, and the ammonia cracker connects combustion chamber and includes the fuel of hydrogen to be provided for combustion chamber.
10. power according to claim 9 and water joint supply device, it is characterised in that：Also include heat exchanger, the heat
Exchanger coordinates the exhaust of combustion chamber, thinks so that heat caused by the exhaust of combustion chamber imports ammonia cracker via heat exchanger
The reaction heat that ammonia cracking reaction provides.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710981453.0A CN107725191A (en) | 2017-10-20 | 2017-10-20 | Power and water joint supply device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710981453.0A CN107725191A (en) | 2017-10-20 | 2017-10-20 | Power and water joint supply device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107725191A true CN107725191A (en) | 2018-02-23 |
Family
ID=61212254
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710981453.0A Pending CN107725191A (en) | 2017-10-20 | 2017-10-20 | Power and water joint supply device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107725191A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2019204857A1 (en) * | 2018-04-26 | 2019-10-31 | Renam Properties Pty Ltd | Offshore energy generation system |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102505990A (en) * | 2011-11-08 | 2012-06-20 | 上海交通大学 | Power generation method of condensing double-working medium gas turbine circulation system |
| CN107100736A (en) * | 2017-06-09 | 2017-08-29 | 厦门大学 | Combustion turbine combined system |
-
2017
- 2017-10-20 CN CN201710981453.0A patent/CN107725191A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102505990A (en) * | 2011-11-08 | 2012-06-20 | 上海交通大学 | Power generation method of condensing double-working medium gas turbine circulation system |
| CN107100736A (en) * | 2017-06-09 | 2017-08-29 | 厦门大学 | Combustion turbine combined system |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2019204857A1 (en) * | 2018-04-26 | 2019-10-31 | Renam Properties Pty Ltd | Offshore energy generation system |
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Application publication date: 20180223 |