WO2020202590A1 - Moving body - Google Patents
Moving body Download PDFInfo
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- WO2020202590A1 WO2020202590A1 PCT/JP2019/022900 JP2019022900W WO2020202590A1 WO 2020202590 A1 WO2020202590 A1 WO 2020202590A1 JP 2019022900 W JP2019022900 W JP 2019022900W WO 2020202590 A1 WO2020202590 A1 WO 2020202590A1
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- WIPO (PCT)
- Prior art keywords
- cooling
- unit
- cooling unit
- gas turbine
- seawater
- Prior art date
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Classifications
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- 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
- F01K23/00—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids
- F01K23/02—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled
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- 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
- F01K11/00—Plants characterised by the engines being structurally combined with boilers or condensers
- F01K11/02—Plants characterised by the engines being structurally combined with boilers or condensers the engines being turbines
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- 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
- F02C7/00—Features, components parts, details or accessories, not provided for in, or of interest apart form groups F02C1/00 - F02C6/00; Air intakes for jet-propulsion plants
- F02C7/04—Air intakes for gas-turbine plants or jet-propulsion plants
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- 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
- F02C7/00—Features, components parts, details or accessories, not provided for in, or of interest apart form groups F02C1/00 - F02C6/00; Air intakes for jet-propulsion plants
- F02C7/12—Cooling of plants
Definitions
- the combined cycle power generation system supplies the combustion gas generated by the combustion means to the gas turbine to rotate the gas turbine, and the generator generates electricity by the rotational force and exhausts the heat remaining in the exhaust gas from the gas turbine.
- This is a system in which a heat recovery boiler recovers steam to generate steam, the steam turbine is rotated by the generated steam, and a generator generates electricity by the rotational force.
- This type of combined cycle power generation system is not only used in onshore power plants, but in recent years it is a system that can demonstrate high power generation efficiency, so its use outside of land is also being considered.
- Patent Document 1 discloses a ship power generation system mounted on a ship for the purpose of power generation on board.
- This ship power generation system is a power generation system installed on a ship such as an LNG ship, and like the above-mentioned combined cycle power generation system, generates rotational power by supplying combustion gas to a gas turbine to generate rotational power of the gas turbine.
- steam is generated by recovering heat from the exhaust gas discharged from the gas turbine, and the generated steam is supplied to the steam turbine to generate rotational power, which is the rotational force of the steam turbine.
- the generator generates electricity.
- the air is sucked and compressed, mixed with the fuel gas by the combustion means and burned, and the gas turbine is rotationally driven by the generated combustion gas, so that the generator generates power by this rotational force.
- the temperature of the air supplied to the combustion means rises, the air density decreases, so that the mass of the air sent to the combustion means decreases, and as a result, the output decreases (in other words, the amount of power generation decreases).
- a method for lowering the temperature of the air supplied to the combustion means has been conventionally proposed.
- a method for example there is a method in which mist is generated in the intake chamber where the air is sucked, and the air sucked into the intake chamber cools the air supplied to the combustion means by taking away the latent heat of vaporization of the mist. ..
- the method using mist can evaporate only the amount of mist up to the saturated steam pressure corresponding to the atmospheric temperature, so if the power generation system is installed in a hot and humid tropical region, or in a hot and humid environment in summer, the power generation system In the case of using the above, there is a problem that the air supplied to the combustion means cannot be sufficiently cooled, and it is difficult to obtain the effect of recovering the output.
- a refrigerator is provided to produce cold water using the heat of combustion of fuel, and the heat using the cold water (cold heat source) produced by the refrigerator is provided.
- a exchanger is installed in the intake chamber to cool the air supplied to the combustion means by this cold water.
- the gas turbine unit has a heat input to the refrigerator and an input power amount.
- the effect of output recovery is small and the energy efficiency of the entire power generation system is reduced.
- the size of the refrigerator is inevitably increased and the cost burden is large.
- the power generation system installed on the mobile body has a problem. Since space saving is required as described above, expansion of the installation space of the refrigerator is also a big problem.
- the above method alone can save power generation systems while suppressing the problem that the effect of output recovery depends on the environment in which the power generation system is located and the decrease in energy efficiency of the entire power generation system. There is a problem that it is difficult to suppress a decrease in the output of the gas turbine unit while realizing space.
- the present invention has been made in view of the above circumstances, and provides a moving body provided with a cooling device capable of efficiently cooling the air supplied to the combustion means and suppressing a decrease in the output of the gas turbine unit. Is the purpose.
- the characteristic configuration of the moving body according to the present invention for achieving the above object is to generate a combustion gas by burning a mixture of fuel gas and air in which liquid fuel is vaporized by a combustion means, and generate the combustion gas by the combustion means. It is used in a power generation system including a gas turbine unit in which a gas turbine is rotationally driven by the generated combustion gas and a first power generation means for generating power by utilizing the rotational force of the gas turbine, and cooling of air supplied to the combustion means.
- the first cooling unit that uses the heat medium used to vaporize the liquid fuel as a cold heat source, the second cooling unit that uses the heat medium from the refrigerator as a cold heat source, and seawater as a heat medium are used as cold heat sources.
- the point is that at least two of the third cooling units are provided.
- a first cooling unit using a heat medium used for vaporizing liquid fuel as a cold heat source a second cooling unit using a heat medium from a refrigerator as a cold heat source, and seawater as a heat medium.
- the air supplied to the combustion means is cooled in at least two cooling units of the third cooling unit using the above as a cooling heat source.
- the present invention is a moving body provided with the above-mentioned cooling device, for example, by moving the moving body to a place where a combined cycle power generation system without a cooling device is installed, the moving body can be moved.
- a cooling device can be attached to this combined cycle power generation system, which makes it possible to suppress a decrease in the output of the gas turbine unit.
- a further characteristic configuration of the moving body according to the present invention is that the cooling device includes the first cooling unit and the second cooling unit.
- the air supplied to the combustion means is cooled by using the heat medium used for vaporizing the liquid fuel as a cooling heat source, and the air is supplied to the second cooling unit.
- the heat medium from the refrigerator is used as a cooling heat source for cooling.
- a heat medium that has taken cold heat from the liquid fuel is inevitably generated when the liquid fuel is vaporized. Therefore, the heat medium that has taken cold heat from the liquid fuel is burned.
- the cold heat of the liquid fuel can be effectively utilized.
- not only the cooling by the cold heat source from the refrigerator but also the cold heat of the liquid fuel is used. By using the same cooling together, it is not necessary to cool the air only by cooling with the cold heat of the cold water from the refrigerator.
- the cold heat of the liquid fuel can be effectively utilized to cool the air supplied to the combustion means, and the decrease in energy efficiency of the entire power generation system can be suppressed.
- a further characteristic configuration of the moving body according to the present invention is that the cooling device is such that the air supplied to the combustion means flows in the order of the second cooling unit and the first cooling unit. The point is that the second cooling unit is arranged.
- the heat medium used as a cold heat source in the first cooling unit is used for vaporizing the liquid fuel, and the temperature is extremely low by obtaining a considerable amount of cold heat.
- the heat medium used as a cold heat source in the second cooling unit is cold water produced by a refrigerator, and the temperature is relatively higher than that of the heat medium used in the first cooling unit. There is a tendency. Therefore, according to the above characteristic configuration, the air supplied to the combustion means is cooled in the second cooling unit where the temperature of the heat medium used is relatively high, and then the temperature of the heat medium used is relatively low. Since cooling is performed in the cooling unit, the air can be cooled without wasting the cold heat of each heat medium used in the two cooling units as much as possible.
- a further characteristic configuration of the moving body according to the present invention is that the cooling device includes the first cooling unit and the third cooling unit.
- the air supplied to the combustion means is cooled by using the heat medium used for vaporizing the liquid fuel as a cooling source, and the air is supplied to the third cooling unit.
- Seawater as a heat medium is cooled as a cold heat source.
- the cold heat of the liquid fuel is effectively utilized by using a heat medium that has taken away the cold heat that is inevitably generated in the system that generates electricity using the liquid fuel as a cold heat source. It can be used.
- the third cooling In the unit the temperature can be lowered by cooling the air supplied to the combustion means with the cold heat of seawater. This makes it easier to suppress a decrease in the output of the power generation system.
- the refrigerator since the refrigerator is not required in this feature configuration, the problem of increasing the size of the refrigerator does not occur, the burden on the cost can be reduced, and the space of the power generation system can be saved.
- a further characteristic configuration of the moving body according to the present invention is that the cooling device is such that the air supplied to the combustion means flows in the order of the third cooling unit and the first cooling unit. The point is that the third cooling unit is arranged.
- the heat medium used as a cold heat source in the first cooling unit obtains a considerable amount of cold heat from the liquid fuel, and its temperature is extremely low.
- the temperature of seawater used as a cold heat source in the third cooling section is relatively higher than that of the heat medium used as a cold heat source in the first cooling section, although it depends on the sampling depth. There is a tendency. Therefore, according to the above characteristic configuration, the air supplied to the fuel means is cooled in the third cooling unit where the temperature of the heat medium used is relatively high, and then the temperature of the heat medium used is relatively low. Since cooling is performed in the cooling unit, the air can be cooled without wasting the cold heat of each heat medium used in the two cooling units as much as possible.
- a further characteristic configuration of the moving body according to the present invention is that the cooling device includes the second cooling unit and the third cooling unit.
- the air supplied to the combustion means is cooled by using the heat medium from the refrigerator as a cooling heat source in the second cooling unit, and the air is used as a heat medium in the third cooling unit. It is cooled using seawater as a cold heat source.
- the combustion is performed after suppressing the decrease in the energy efficiency of the entire power generation system, reducing the burden on the cost, and saving the space of the power generation system.
- the air supplied to the means can be cooled, which can suppress a decrease in the output of the gas turbine unit.
- a further characteristic configuration of the moving body according to the present invention is that the cooling device has the second and second cooling devices so that the air supplied to the combustion means flows in the order of the third cooling section and the second cooling section.
- the third cooling unit is arranged.
- the temperature of the seawater used as the cold heat source in the third cooling section tends to be relatively higher than that of the cold water from the refrigerator used as the cold heat source in the second cooling section, although it depends on the sampling depth. .. Therefore, according to the above characteristic configuration, the air supplied to the combustion means is cooled in the third cooling unit where the temperature of the heat medium used is relatively high, and then the temperature of the heat medium used is relatively low. Since cooling is performed in the cooling unit, the air can be cooled without wasting the cold heat of each heat medium used in the two cooling units as much as possible.
- a further characteristic configuration of the moving body according to the present invention is that the cooling device includes the first cooling unit, the second cooling unit, and the third cooling unit.
- the first cooling unit that uses the heat medium used to vaporize the liquid fuel as a cold heat source
- the second cooling unit that uses the heat medium from the refrigerator as a cold heat source
- seawater The air supplied to the combustion means is cooled in the third cooling unit used as a cold heat source.
- the cold heat obtained by vaporizing the liquid fuel consumed by the power generation system during power generation can be obtained.
- the temperature of the air supplied to the combustion means can be suppressed from the decrease in the output of the power generation system only by the cold heat of each heat medium used in any two of the three cooling units due to insufficient reasons. Even in cases where the temperature cannot be lowered to such a temperature, by providing three cooling units, the air supplied to the combustion means is cooled by the cold heat of each heat medium used in these three cooling units. The temperature can be lowered. As a result, the decrease in the output of the power generation system can be further suppressed.
- a further characteristic configuration of the moving body according to the present invention is that in the cooling device, the air supplied to the combustion means circulates in the order of the third cooling unit, the second cooling unit, and the first cooling unit. The point is that the first, second and third cooling units are arranged.
- the temperature of seawater used as a cold heat source in the third cooling section is higher than that of the heat medium used as a cold heat source in the first cooling section and the second cooling section, although it depends on the sampling depth.
- the temperature tends to be relatively high, and the heat medium used as a cold heat source in the second cooling section tends to have a relatively high temperature as compared with the heat medium used in the first cooling section. .. Therefore, according to the above-mentioned characteristic configuration, the air supplied to the combustion means is cooled in the order of the cooling unit having the highest relative temperature of the heat medium to be used, that is, after cooling in the third cooling unit, the second cooling unit. Since the cooling is performed in the first cooling unit and then cooled in the first cooling unit, the air can be cooled without wasting the cooling heat of each of the heat media used in the three cooling units as much as possible.
- a further characteristic configuration of the moving body according to the present invention is a fuel tank in which the liquid fuel is stored and a fuel tank.
- a vaporization unit that vaporizes the liquid fuel by using the heat medium used in the first cooling unit as a heat source. With the gas turbine unit The point is that the first power generation means is provided.
- the moving body is a moving body including a cooling device, a fuel tank, a vaporization unit, a gas turbine unit, and a first power generation means.
- the gas turbine unit The first power generation means generates electricity by the rotational force of the gas turbine.
- the air supplied to the combustion means is cooled by the above cooling device, and mist is generated as in the conventional case. Since it is not used, the effect of recovering the output of the power generation system can be obtained.
- a further characteristic configuration of the moving body according to the present invention is an exhaust heat recovery boiler unit that vaporizes water by exhaust gas from the gas turbine unit.
- a steam turbine unit in which the steam turbine is rotationally driven by steam vaporized in the exhaust heat recovery boiler unit, and A second power generation means for generating power by utilizing the rotational force of the steam turbine is provided. It is a ship.
- the moving body becomes a ship further provided with the exhaust heat recovery boiler unit, the above-mentioned turbine unit, and the second power generation means (in other words, a ship equipped with a combined cycle power generation system), and this movement
- the steam turbine is rotationally driven by utilizing the heat of the exhaust gas from the gas turbine unit, and the rotational force of the steam turbine also generates electricity by the second power generation means. Therefore, it is possible to efficiently generate electricity by effectively utilizing the heat of the exhaust gas from the gas turbine unit.
- the moving body according to the present invention even if the area where the moving ship is navigating or anchoring is often in the tropics, the air supplied to the combustion means is cooled by the above cooling device. Since the mist is not used as in the above, the effect of recovering the output of the power generation system can be obtained.
- the cooling device includes a third cooling unit that uses seawater as a heat medium as a cold heat source.
- the steam turbine unit includes a condenser that recovers steam used for rotationally driving the steam turbine as condensate. The point is that the seawater used in the third cooling unit is used as a cold heat source, and a condensate cooling unit for cooling the inside of the condenser is provided.
- the seawater used in the third cooling unit is used as a cooling heat source, the inside of the condenser is cooled in the condensate cooling unit, and the steam discharged from the steam turbine is used in the condenser. It can be cooled inside and recovered as condensate. Therefore, it is possible to share a part of the seawater pipes for supplying seawater to the third cooling part and the condensate cooling part and recovering seawater from these cooling parts, so that the arrangement of the pipes can be simplified. , The number of pumps required to distribute seawater in the pipe can be reduced.
- a further characteristic configuration of the moving body according to the present invention is a first seawater flow path through which the seawater supplied to the third cooling unit flows.
- the air is cooled even if the amount of seawater supplied to the third cooling unit is small. It is difficult to make a difference in the effect, but even in such a case, it is an unnecessary increase in pump output to always distribute the entire amount of seawater pumped by the pump to the condensate cooling section via the third cooling section. Connect. Further, when the temperature of the seawater is higher than the temperature of the outside air, the air may be heated by supplying the seawater to the third cooling unit.
- a bypass flow path connecting the first seawater flow path and the second seawater flow path is provided, and the amount of seawater flowing through the bypass flow path is adjusted by the adjusting means to adjust the third cooling unit.
- the amount of seawater flowing to the condensate cooling section via the above and the amount of seawater flowing to the condensate cooling section through the bypass flow path without passing through the third cooling section can be adjusted. Therefore, by adjusting the amount of seawater flowing through the bypass flow path according to the amount of seawater required by the third cooling unit, it is possible to suppress an unnecessary increase in pump output.
- the total amount of seawater pumped up by the pump is adjusted so that it flows through the bypass flow path so that seawater is not supplied to the third cooling unit. It is also possible to prevent the situation where the air is heated.
- a further characteristic configuration of the moving body according to the present invention is to determine the number of operating gas turbine units based on the power demand and the operating state of the cooling device.
- the operating state of the cooling device changes depending on the degree of cooling of the air supplied to the combustion means in each of the first cooling part, the second cooling part, and the third cooling part, and the degree of cooling of the air by each cooling part is determined. By changing it, the operating state of the cooling device can be changed as appropriate. Further, the degree of cooling of air by each cooling unit can be changed by changing the temperature of the heat medium supplied to the cooling unit or by starting or stopping the supply of the heat medium to the cooling unit. Further, the electric power demand in the present application means the electric power required by the mobile body, the electric power required by one or more facilities to which the electric power is supplied from the mobile body, and the power generation system for the purpose of storing electricity. It is a concept that includes electric power to be generated.
- a further characteristic configuration of the moving body according to the present invention is to determine the operating state of the cooling device based on the electric power demand and the output characteristics of the gas turbine unit.
- the cooling device can be operated in an appropriate operating state that meets the power demand, and it is possible to prevent the cooling device from being loaded more than necessary.
- a further characteristic configuration of the moving body according to the present invention is that the cooling device includes the first cooling unit and at least one of the second cooling unit and the third cooling unit. With the air supplied to the combustion means cooled by the first cooling unit, at least one of the second cooling unit and the third cooling unit is used based on the power demand and the output characteristics of the gas turbine unit. The point is that the operating state of the cooling device is determined by determining the degree of cooling of the air supplied to the combustion means.
- the air by at least one of the second cooling unit and the third cooling unit is based on the power demand and the output characteristics of the gas turbine unit.
- the degree of cooling can be determined, and the operating state of the cooling device can be determined. Therefore, the operating state of the cooling device determined in this way is an operating state in which the cold heat of the liquid fuel is effectively utilized.
- the air supplied to the combustion means is cooled by the first cooling unit, and the combustion is performed by the second cooling unit and the third cooling unit based on the power demand and the output characteristics of the gas turbine unit.
- the degree of cooling of the air supplied to the means the operating state of the cooling device is determined, and with the air supplied to the combustion means cooled by the first cooling unit, the power demand and the output characteristics of the gas turbine unit.
- the degree of cooling of the air supplied to the combustion means by the second cooling unit based on the above, the operating state of the cooling device is determined, and the air supplied to the combustion means is cooled by the first cooling unit. This includes determining the operating state of the cooling device by determining the degree of cooling of the air supplied to the combustion means by the third cooling unit based on the power demand and the output characteristics of the gas turbine unit. ..
- a further characteristic configuration of the moving body according to the present invention is that the cooling device includes the first cooling unit, the second cooling unit, and the third cooling unit.
- the combustion means by the second cooling unit is based on the power demand and the output characteristics of the gas turbine unit.
- the degree of cooling of the air supplied to the cooling device is determined.
- the degree of cooling of the air by the second cooling unit is determined based on the power demand and the output characteristics of the gas turbine.
- the operating state of the cooling device can be determined. Therefore, the operating state of the cooling device determined in this way is an operating state in which the cold heat of the liquid fuel is effectively utilized.
- a further characteristic configuration of the moving body according to the present invention determines the operating state of the cooling device according to at least one of the air condition and the cooling device condition, and the first cooling unit. The point is to determine the degree of cooling of the air supplied to the combustion means by at least one of the second cooling unit and the third cooling unit.
- the degree of cooling of air by each cooling unit after determining the operating state of the cooling device according to the atmospheric condition. Therefore, for example, after determining the state in which the air is not cooled by any one of the first to third cooling units as the operating state of the cooling device, the degree of cooling of the air by the other cooling units is determined. You can decide and operate the cooling system.
- the atmospheric condition is the atmospheric temperature, atmospheric pressure, humidity, etc.
- the condition of the cooling device is the presence or absence of a failure, the temperature of the seawater used, the amount of LNG used, and the like.
- FIG. 1 is a diagram showing a schematic configuration of a power generation system E mounted on a ship (LNG carrier).
- the power generation system E uses a fuel tank 1 in which liquefied natural gas (LNG) as a liquid fuel is stored and water as a heat medium to vaporize the LNG into a fuel gas.
- LNG liquefied natural gas
- a mixture of the vessel 2 (vaporizer) and fuel gas and air is burned by the combustor 6 (combustion means) to generate combustion gas, and the combustion gas generated by the combustor 6 rotates the gas turbine 7.
- the exhaust heat recovery boiler unit 25 that vaporizes water to generate steam
- It includes a first generator 35 (first power generation means) that uses it to generate electricity, and a second generator 36 (second power generation means) that uses the rotational force of the steam turbine 30 to generate power.
- the fuel tank 1 is connected to the other end of the fuel supply path L1 whose one end is connected to the combustor 6 in the gas turbine unit G, and the vaporizer 2 is arranged in the fuel supply path L1. .. Further, the vaporizer 2 is a heat exchanger in which a vaporization medium supply path L2 through which water as a heat source flows and a first cooling medium supply path L3 through which water obtained with cold heat from LNG flows are connected.
- the LNG supplied from the inside of the fuel tank 1 is heated and vaporized by the heat of the water supplied through the vaporization medium supply path L2 in the vaporizer 2, and is supplied to the combustor 6 as a fuel gas. ..
- the gas turbine unit G has a compressor 5, a combustor 6, and a gas turbine 7.
- the compressor 5 is rotationally driven by the gas turbine 7, and the air cooled by the cooling device 20 described later is supplied through the first air supply path L10, and the supplied air is compressed and sent out to the combustor 6. It is configured. Further, the combustor 6 burns a mixture of fuel gas supplied through the fuel supply path L1 and compressed air supplied from the compressor 5 through the second air supply path L11 to generate combustion.
- the gas is sent to the gas turbine 7 through the combustion gas supply path L12.
- the gas turbine 7 is rotationally driven by the combustion gas sent from the combustor 6, and the rotational force is transmitted to the compressor 5 and the first generator 35. Further, the combustion gas used to drive the rotation of the gas turbine 7 is sent out as exhaust gas to the exhaust heat recovery boiler unit 25, which will be described later, through the exhaust gas supply path L13.
- the refrigerator 10 in the present embodiment is a so-called absorption chiller, and as shown in FIG. 2, includes an evaporator 11, a absorber 13, a regenerator 15 and a condenser 17.
- the evaporator 11 is provided inside the second cooling medium supply path L4 through which water supplied as a cooling heat source to the second cooling section 22 of the cooling device 20 described later flows, and the second cooling medium supply path L4.
- a cooling medium recovery path L5 through which water that has been connected and has been deprived of cold heat flows is arranged in the second cooling unit 22, and water stored in the evaporator 11 is pumped up by a pump (not shown).
- a first spraying means 12 for spraying is provided in the evaporator 11. Further, the evaporator 11 is in a state of communicating with the absorber 13 via a passage, and the inside of the evaporator 11 and the absorber 13 is depressurized by a vacuum pump (not shown).
- the water sprayed by the first spraying means 12 is evaporated at a low temperature of about 5 ° C. under reduced pressure to cool the water flowing through the cooling medium recovery path L5, thereby cooling the water.
- Water having cold heat used as a cold heat source is produced in the cooling unit 22. The water evaporated at low temperature (that is, water vapor) moves to the absorber 13 through the passage.
- the absorber 13 stores an absorbing liquid (for example, an aqueous solution of lithium bromide) inside the absorber 13 and sprays a high-concentration absorbing liquid heated in the regenerator 15 described later into the absorber 13.
- the second spraying means 14 is arranged. In the absorber 13, the high-concentration absorption liquid sprayed by the second spraying means 14 is cooled by the refrigerant, and the water vapor generated in the evaporator 11 is absorbed by the cooled absorption liquid.
- the absorbent liquid stored in the absorber 13 is pumped up by a pump (not shown) and supplied, so that the supplied absorbent liquid is heated by the heating means 16. It has become.
- the heating means 16 is not particularly limited as long as it can heat the absorbing liquid, and examples thereof include those using the heat of combustion of fuel gas and the heat of an electric heater.
- the water vapor absorbed by the absorbent liquid in the absorber 13 is separated by heating the absorbent liquid supplied from the absorber 13. The separated water vapor moves to the condenser 17 which is in a state of being communicated with the regenerator 15 via the passage.
- the water vapor separated by the regenerator 15 is cooled by the refrigerant, and the condensed water is supplied to the evaporator 11.
- the cold heat of the refrigerant for example, water supplied from the outside as appropriate is used to cool the absorber 13 and the condenser.
- a refrigerant flow path La through which this refrigerant flows passes through the inside of the 17.
- the water as a cold heat source produced in the evaporator 11 of the refrigerator 10 may be used only by the second cooling unit 22, but is used for the air conditioner provided on the ship. Is also good. That is, the flow paths branched from the second cooling medium supply path L4 and the cooling medium recovery path L5 connected to the evaporator 11 are appropriately connected to the air conditioner, and serve as a cooling heat source through the second cooling medium supply path L4. The water may be supplied to the air conditioner, and the water from which the cold heat has been deprived in the air conditioner may be recovered through the cooling medium recovery path L5.
- the cooling device 20 is configured to cool the air flowing through the first air supply path L10 (air supplied to the combustor 6). Specifically, in the present embodiment, the cooling device 20 uses the first cooling unit 21 that uses water as a heat medium used for vaporizing LNG as a cold heat source, and the water produced by the refrigerator 10. A second cooling unit 22 used as a cold heat source and a third cooling unit 23 using seawater as a heat medium as a cold heat source are provided.
- the first cooling unit 21 is a heat exchanger to which the vaporization medium supply path L2 and the first cooling medium supply path L3 are connected, and water as a heat medium is a heat exchanger between the vaporizer 2 and the first cooling unit 21. It circulates between them through the vaporization medium supply path L2 and the first cooling medium supply path L3.
- the first cooling unit 21 cools the air supplied to the combustor 6 by the cold heat of the water supplied through the first cooling medium supply path L3 (that is, the water obtained from the LNG).
- the second cooling unit 22 is a heat exchanger to which the second cooling medium supply path L4 and the cooling medium recovery path L5 are connected, and the water as the heat medium is the evaporator 11 of the refrigerator 10 and the second cooling. It circulates with the unit 22 through the second cooling medium supply path L4 and the cooling medium recovery path L5.
- the second cooling unit 22 cools the air supplied to the combustor 6 by the cold heat of the water supplied through the second cooling medium supply path L4 (that is, the water produced by the refrigerator 10 and obtained cold heat). To do.
- the third cooling unit 23 supplies seawater to which the seawater supplied from the condensate cooling unit 32, which will be described later, flows through the first seawater supply channel L6 (first seawater channel) through which the seawater pumped from the sea by the pump P1 flows. It is a heat exchanger connected to the passage L7 (second seawater flow path).
- the third cooling unit 23 cools the air supplied to the combustor 6 by the cold heat of seawater as a cold heat source supplied through the first seawater supply path L6.
- a bypass flow path L8 connecting the first seawater supply path L6 and the second seawater supply path L7 is connected between the pump P1 and the third cooling unit 23 in the first seawater supply path L6.
- an adjusting device 24 (adjusting means) is provided at a connection point of the bypass flow path L8 in the first seawater supply path L6, and the adjusting device 24 adjusts the amount of seawater flowing through the bypass flow path L8. You can do it.
- the cooling units 21, 22, and 23 are the third cooling unit 23, the second cooling unit 22, and the first cooling unit 21 from the upstream side in the flow direction of the air flowing to the combustor 6.
- the air is arranged in this order, and the air sucked into the first air supply passage L10 is cooled in the order of the third cooling unit 23, the second cooling unit 22, and the first cooling unit 21.
- the exhaust heat recovery boiler unit 25 is used to rotate and drive the gas turbine 7, and is configured to recover the heat of the exhaust gas discharged from the gas turbine 7. Specifically, in the present embodiment, the exhaust heat recovery boiler unit 25 heats and vaporizes the water in the plurality of drums 26 by the heat of the exhaust gas from the gas turbine 7 to produce steam. Then, this steam is sent to the steam turbine 30 of the steam turbine unit S through the steam supply path L14. The exhaust gas from which the heat has been recovered is appropriately discharged to the outside.
- the steam turbine unit S includes a steam turbine 30, a condenser 31, and a condenser cooling unit 32.
- the steam turbine 30 is rotationally driven by the steam sent from the exhaust heat recovery boiler unit 25, and the rotational force is transmitted to the second generator 36.
- the condenser 31 is provided with a condenser cooling unit 32 inside, and the steam used to drive the rotation of the steam turbine 30 is returned to water in the condenser 31 to supply water. It is supplied to the drum 26 through the road L15.
- the condensate cooling unit 32 is a heat exchanger in which the second seawater supply path L7 and the seawater discharge path L9 for discharging seawater to the sea are connected, and the cold heat of the seawater supplied through the second seawater supply path L7.
- the inside of the condenser 31 is cooled by, and the seawater used for cooling the inside of the condenser 31 is discharged to the sea through the seawater discharge path L9.
- the temperature of the seawater supplied through the second seawater supply path L7 is about 32 ° C.
- the temperature of the seawater used for cooling the inside of the condenser 31 is It will be about 42 ° C.
- the first generator 35 is driven by the gas turbine 7 to generate electricity
- the second generator 36 is driven by the steam turbine 30 to generate electricity.
- the fuel gas vaporized in the vaporizer 2 is supplied to the combustor 6, and the air cooled in the cooling device 20 is supplied to the combustor 6 in the combustor 6.
- a mixture of fuel gas and air is burned, and the generated combustion gas is sent to the gas turbine 7, so that the gas turbine 7 is rotationally driven, and the rotational force drives the first generator 35. And power is generated.
- the combustion gas used to drive the rotation of the gas turbine 7 is sent to the exhaust heat recovery boiler unit 25 as exhaust gas, and the steam is generated in the exhaust heat recovery boiler unit 25 by utilizing the heat of the exhaust gas.
- the steam turbine 30 is rotationally driven, and the rotational force drives the second generator 36 to generate power.
- the output of the power generation system E is reduced (in other words, the amount of power generation is reduced). Can be suppressed. Further, in the case where a plurality of gas turbine units G are installed on a ship, since the decrease in the output of the power generation system E can be suppressed by providing the cooling device 20, the gas turbine unit G required to obtain the same electric power It is possible to reduce the number of installed turbines, and it is possible to reduce equipment costs, maintenance costs, and installation space.
- cooling device 20 in the present embodiment is used as a cooling heat source for cooling the air that supplies the combustor 6 with the heat medium that has taken the cold heat from the LNG, which is inevitably generated when the LNG is vaporized.
- the cold heat of LNG can be effectively utilized.
- the air supplied to the combustor 6 is cooled in the three cooling units 21, 22, 23, there is a problem that the energy efficiency of the entire power generation system E is lowered, and the size of the refrigerator 10 is increased.
- the combustor solves the problem that the output of the power generation system E decreases due to the inevitable problem and the lack of cooling heat obtained by vaporizing the LNG consumed by the power generation system E during power generation.
- the air supplied to No. 6 can be sufficiently cooled to suppress a decrease in the output of the power generation system E.
- the water used as a cold heat source in the first cooling unit 21 is used for vaporizing LNG.
- the temperature of LNG is about ⁇ 160 ° C.
- LNG when LNG is vaporized by the water used in the first cooling unit 21 to make a fuel gas of about 10 ° C., heat is generated.
- Water as a medium obtains a considerable amount of cold heat, and if the temperature before obtaining the cold heat is about 13 ° C., the temperature after obtaining the cold heat is about 5 ° C.
- the water used as the cold heat source in the second cooling unit 22 is produced by the refrigerator 10, and the temperature is relatively higher than the water used in the first cooling unit 21.
- the temperature at the time of supplying to the second cooling unit 22 is about 7 ° C., and after the second cooling unit 22 is deprived of cold heat by the air.
- the temperature at is about 15 ° C.
- the seawater used as a cold heat source in the third cooling unit 23 depends on the sampling depth, but if it is pumped from a depth of 30 m to 70 m, it is about 20 to 30 ° C., as shown in FIG. As shown, in the present embodiment, the temperature is about 25 ° C., and the temperature after the cold heat is taken away by the air in the third cooling unit 23 is about 32 ° C.
- the third cooling unit 23, the second cooling unit 22, and the first cooling unit 21 are arranged in this order from the upstream side in the flow direction of the air flowing to the combustor 6, so that the first air is supplied.
- the air sucked into the passage L10 (35 ° C. in this embodiment) is cooled in the order of the cooling units 21, 22, 23 in which the temperature of the heat medium to be used is relatively high, that is, the third cooling unit 23 first.
- the temperature becomes about 30 ° C.
- the second cooling unit 22 the temperature becomes about 20 ° C.
- the first cooling unit 21 the air supplied to the combustor 6 is supplied.
- it can be cooled to about 15 ° C., and the air can be efficiently cooled without wasting the cold heat of each heat medium used by the three cooling units 21, 22, 23 as much as possible.
- a part of the seawater piping (that is, for supplying seawater to the third cooling unit 23 and the condensate cooling unit 32 and collecting seawater from these cooling units 23 and 32 (that is,).
- the first seawater supply route L6, the second seawater supply route L7, and the seawater discharge route L9) are shared, which simplifies the arrangement of pipes and increases the number of pumps P1 for distributing seawater. Only one unit is needed.
- a bypass flow path L8 connecting the first seawater supply path L6 and the second seawater supply path L7 is provided so that the amount of seawater flowing through the bypass flow path L8 can be adjusted by the adjusting device 24.
- the air can be supplied even if the amount of seawater supplied to the third cooling unit 23 is small. Although it is difficult to make a difference in the cooling effect, flowing seawater to the condensate cooling unit 32 via the third cooling unit 23 leads to an unnecessary increase in the pump output even in such a case. Further, when the temperature of the sucked air is higher than the temperature of the seawater, the air may be heated by supplying the seawater to the third cooling unit 23.
- an unnecessary increase in the output of the pump P1 can be suppressed by adjusting the amount of seawater flowing through the bypass flow path L8 by the adjusting device 24 as needed. ..
- the temperature of the seawater is higher than the temperature of the air by adjusting the total amount of the seawater pumped by the pump P1 so as to flow through the bypass flow path L8 by the adjusting device 24. Even in such a case, it is possible to prevent a situation in which the air is heated by seawater.
- FIG. 3 is a diagram showing a schematic configuration of a power generation system E1 mounted on a ship (LNG carrier).
- the power generation system E1 includes a vaporizer 2, a plurality of gas turbine units Ga and Gb, a refrigerator 10, a plurality of cooling devices 20a and 20b, and a plurality of exhaust heat recovery boiler units 25a. It includes 25b and a steam turbine unit S.
- the power generation system E1 includes a control device 40 and a temperature sensor Tb for detecting the atmospheric temperature.
- the mobile power generation system E1 according to the second embodiment also includes a fuel tank in which liquefied natural gas is stored and the rotational force of the gas turbines 7a and 7b of the gas turbine units Ga and Gb.
- a first power generation means for generating power by utilizing the above, and a second power generation means for generating power by utilizing the rotational force of the steam turbine 30 are provided.
- FIG. 3 a configuration in which two of each of a plurality of gas turbine units, a plurality of cooling devices, and a plurality of exhaust heat recovery boiler units are provided is shown.
- a fuel regulating valve V1 is provided between the fuel tank and the vaporizer 2 in the fuel supply path L1, and the opening / closing operation of the fuel regulating valve V1 is the operation of the electric power demand and the gas turbine unit. It is controlled by the control device 40 based on the state and the like.
- the vaporization medium supply path L2 connected to the vaporizer 2 is branched into the vaporization medium supply paths L2a and L2b on the upstream side thereof, and the first cooling is also connected to the vaporizer 2.
- the media supply path L3 is branched into the first cooling medium supply paths L3a and L3b on the downstream side thereof.
- the cooling medium supply path L3 is provided with a heat exchanger 37 and a buffer tank 38 in this order from the upstream side.
- the heat exchanger 37 is for exchanging heat between the water obtained from LNG in the vaporizer 2 and the seawater appropriately pumped from the sea, and the buffer tank 38 is used at the time of starting the power generation system E1. This is for temporarily storing the water supplied to the first cooling units 21a and 21b.
- the two gas turbine units Ga and Gb have the same configuration as the gas turbine unit G in the first embodiment, and include compressors 5a and 5b and gas turbines 7a and 7b. That is, in the present embodiment, the air cooled by the cooling devices 20a and 20b is supplied to the compressors 5a and 5b through the first air supply paths L10a and L10b, respectively. Further, the air supplied to the compressors 5a and 5b is mixed with the fuel gas and burned in a combustor (not shown).
- the combustion gas generated in the combustor is sent to the gas turbines 7a and 7b to be used for rotational driving of the gas turbines 7a and 7b, and then as exhaust gas through the exhaust gas supply paths L13a and L13b, the exhaust heat recovery boiler unit 25a, It is sent to 25b.
- the second cooling medium supply path L4 connected to the refrigerator 10 is branched into the second cooling medium supply paths L4a and L4b on the downstream side of the refrigerator 10 and is also frozen.
- the cooling medium recovery path L5 connected to the machine 10 branches into the cooling medium recovery paths L5a and L5b on the upstream side of the refrigerator 10.
- a seawater temperature sensor Ta that measures the temperature of seawater is provided in the refrigerant flow path La that passes through the inside of the absorber 13 and the condenser 17 of the refrigerator 10.
- the vaporization medium supply paths L2a and L2b and the first cooling medium supply paths L3a and L3b are connected to the first cooling units 21a and 21b of the cooling devices 20a and 20b in the second embodiment, respectively. Further, the second cooling medium supply paths L4a and L4b and the cooling medium recovery paths L5a and L5b are connected to the second cooling units 22a and 22b, respectively.
- the first seawater supply passage L6 branches into the first seawater supply passages L6a and L6b on the downstream side of the pump P1, and the third cooling unit 23a of the cooling devices 20a and 20b,
- the first seawater supply channels L6a and L6b are connected to the 23b, and the seawater drainage channels L9a and L9b are connected to the 23b, and the first seawater supply channels L6a and L6b are connected to the third cooling units 23a and 23b.
- the supplied seawater is discarded into the sea through the seawater drainage channels L9a and L9b.
- the cooling units 21a, 21b, 22a, 22b, 23a and 23b are the third cooling units 23a, 23b and the second from the upstream side of the first air supply passages L10a and L10b.
- the cooling units 22a and 22b and the first cooling units 21a and 21b are arranged in this order.
- the exhaust heat recovery boiler units 25a and 25b in the second embodiment vaporize the water in the drums 26a and 26b by the exhaust gas sent from the gas turbines 7a and 7b through the exhaust gas supply paths L13a and L13b, respectively, to produce steam. Then, this steam is sent to the steam turbine 30 through the supply paths L14a and L14b.
- the condensate cooling unit 32 of the steam turbine unit S is connected to the second seawater supply line L7 branched from the first seawater supply line L6b and is connected to the seawater discharge line L9c.
- the seawater supplied through the seawater supply channel L7 is discarded into the sea through the seawater discharge channel L9c.
- the steam produced by the exhaust heat recovery boiler units 25a and 25b is returned to water in the condenser 31 and supplied to the drums 26a and 26b through the water supply passages L15a and L15b.
- the control device 40 is a device responsible for various controls related to the operation of the power generation system E1.
- the control device 40 can determine the number of operating gas turbine units Ga and Gb based on the power demand and the operating states of the cooling devices 20a and 20b.
- the operating states of the cooling devices 20a and 20b can be predetermined, or can be appropriately determined based on the power demand and the output characteristics of the gas turbine units Ga and Gb. Further, the output characteristics of the gas turbine units Ga and Gb are predetermined according to the atmospheric temperature, atmospheric pressure, humidity, seawater temperature and the like.
- FIG. 4 is a graph showing the output characteristics of the gas turbine unit determined in advance according to the atmospheric temperature.
- the one-point chain line X1 in the figure shows the first output characteristic when one gas turbine unit is operated while the cooling device is operated so that the air supplied to the combustor becomes 15 ° C.
- X2 shows the second output characteristic when two gas turbine units are operated in a state where the cooling device is operated so that the air supplied to the combustor becomes 15 ° C.
- the two-point chain wire Y1 in the figure shows the third output characteristic when one gas turbine unit is operated while the cooling device is operated so that the air supplied to the combustor becomes 10 ° C.
- the two-point chain wire Y2 shows the fourth output characteristic when two gas turbine units are operated in a state where the cooling device is operated so that the air supplied to the combustor becomes 10 ° C.
- control device 40 can meet the power demand of 49.2 MW at an atmospheric temperature of 20 ° C. in a predetermined operating state of the cooling devices 20a and 20b (an operating state in which the air supplied to the combustor is 15 ° C.).
- the number of operating gas turbine units Ga and Gb is determined to be two, and the two gas turbine units Ga and Gb are operated (the state of the black circle (1) in FIG. 4).
- the temperature of the cold water supplied from the refrigerator 10 to the second cooling unit is lowered (that is, the degree of cooling of the air by the second cooling unit is increased), and the cooling devices 20a and 20b are used.
- the operating state is changed to an operating state in which the air supplied to the combustor is 10 ° C., and one of the two operating gas turbine units Ga and Gb is stopped.
- the operating state of the cooling devices 20a and 20b and the number of operating gas turbine units Ga and Gb can be determined according to the power demand, which meets the power demand.
- the cooling device can be operated in an appropriate operating state, and the number of gas turbine units that meets the power demand can be operated without unnecessarily increasing the number of operating gas turbine units.
- control device 40 when the gas turbine units Ga and Gb are rapidly started or when the trips of the gas turbines 7a and 7b are stopped, the flow rate of LNG suddenly increases and the heat retained in the water supplied to the vaporizer 2 suddenly decreases. Even when the operation is performed properly, the buffer tank 38 provided in the cooling medium supply path L3 is provided with a sufficient amount of water, and control is performed so that water can be supplied quickly. As a result, it is possible to prevent the vaporizer 2 from being damaged by freezing due to insufficient heat.
- the cooling devices 20, 20a, 20b include first cooling units 21,21a, 21b, second cooling units 22, 22a, 22b, and third cooling units 23, 23a, 23b.
- the configuration is set, a configuration in which the cooling device includes at least any two of the above three cooling units may be adopted.
- the air supplied to the combustor 6 is cooled by the first cooling units 21, 21a, 21b and the second cooling units 22, 22a, 22b. Therefore, it is possible to suppress a decrease in the output of the power generation systems E and E1 in the same manner as described above.
- the air supplied to the combustor 6 is the second cooling unit 22, 22a, 22b, and the first cooling unit from the viewpoint of cooling the air without wasting the cold heat of the heat medium as much as possible. It is preferable to arrange these two cooling units 21,21a, 21b, 22, 22a, 22b so that they are distributed in the order of 21,21a, 21b.
- the cold heat of the LNG is effectively utilized and the energy efficiency of the entire power generation system is lowered.
- the air supplied to the combustor 6 is supplied to the first cooling units 21 and 21a and 21b and the third cooling units 23, 23a and 23b, while suppressing the problem of the chiller and the inevitable increase in size of the refrigerator. Since it can be cooled by the above, it is possible to suppress a decrease in the output of the power generation systems E and E1 in the same manner as described above.
- these two cooling units 21 and 21a so that the air supplied to the combustor 6 circulates in the order of the third cooling units 23, 23a and 23b and the first cooling units 21 and 21a and 21b. It is preferable to arrange 21b, 23, 23a, 23b, and in this way, the air can be cooled without wasting the cold heat of the heat medium as much as possible.
- the configuration including the second cooling units 22, 22a, 22b and the third cooling units 23, 23a, 23b is adopted, there is a problem that the energy efficiency of the entire power generation system is lowered and the size of the refrigerator is increased.
- the air supplied to the combustor 6 can be cooled by the second cooling units 22, 22a, 22b and the third cooling units 23, 23a, 23b, while suppressing the occurrence of the problem that the above is unavoidable.
- the two cooling units 22, 22a so that the air supplied to the combustor 6 flows in the order of the third cooling units 23, 23a, 23b and the second cooling units 22, 22a, 22b. It is preferable to arrange 22b, 23, 23a, 23b, and in this way, the air can be cooled without wasting the cold heat of the heat medium as much as possible.
- the first cooling units 21,21a, 21b, the second cooling units 22, 22a, 22b and the third cooling units 23, 23a, 23b constituting the cooling devices 20, 20a, 20b burn.
- the configuration was such that the third cooling units 23, 23a, 23b, the second cooling units 22, 22a, 22b, and the first cooling units 21, 21, 21a, 21b were arranged in this order from the upstream side in the flow direction of the air flowing to the vessel 6.
- the arrangement of these cooling units is not limited to this, and can be appropriately set.
- the moving body is a ship including a fuel tank 1, a vaporizer 2, a gas turbine unit G, an exhaust heat recovery boiler unit 25, a steam turbine unit S, and generators 35 and 36, respectively.
- a moving body equipped with a cooling device may be used, and in addition to the cooling device, the configuration required for gas turbine power generation (fuel tank, vaporizer, gas turbine unit and It may be a moving body equipped with a first generator).
- the cooling device provided by the moving body can be used in this power generation system.
- moving objects include, but are not limited to, LPG carriers, ethylene ships, ammonia ships, liquefied hydrogen carriers, large tuna ships, refrigerated container ships, floating ships, etc. It also includes floating structures that have been built or modified and towed to the site of use and moored during the trial period or almost permanently, and other various land transportation facilities (trucks, dolly vehicles).
- a part of the seawater piping for supplying seawater to the third cooling unit 23 and the condensate cooling unit 32 and collecting seawater from these cooling units 23 and 32 is not limited to this.
- a pipe for supplying seawater and collecting seawater to the third cooling unit 23 and a pipe for supplying seawater and collecting seawater to the condensate cooling unit 32 are provided, respectively, for third cooling.
- the condensate cooling unit 32 may use seawater supplied from a pipe different from the seawater used in the unit 23.
- a bypass flow path L8 connecting the first seawater supply path L6 and the second seawater supply path L7 is provided, and an adjusting device for adjusting the amount of seawater flowing through the bypass flow path L8.
- the configuration is provided with 24, the configuration is not limited to this, and a bypass flow path and an adjusting device may be provided as necessary.
- the mode of adjusting the amount of seawater flowing through the second seawater supply channel L7 is not adopted, but as in the first embodiment, an appropriate adjusting device is provided to provide a second. The amount of seawater flowing through the seawater supply channel L7 may be adjusted.
- water is used as the heat medium used in the vaporizer 2 and the first cooling units 21, 21, 21a, 21b, but an antifreeze solution such as ethylene glycol is used instead of water. Is also good. If an antifreeze solution is used, the temperature of the antifreeze solution is lower than that of water (for example, to 0 ° C.) by vaporizing LNG into fuel gas by heat exchange with the antifreeze solution in the vaporizer 2. By using the antifreeze liquid obtained from the LNG in the first cooling unit 21 and cooling the air supplied to the combustor 6, the air can be cooled to, for example, about 10 ° C.
- the cold heat of the refrigerant supplied from the outside is appropriately used for cooling the high-concentration absorbent liquid in the absorber 13 of the refrigerator 10 and cooling the water vapor in the condenser 17.
- the refrigerant flow path La is branched from the first seawater supply passages L6 and L6a, flows through the absorber 13 and the condenser 17, and is connected to the second seawater supply passage L7, seawater is provided.
- the piping can be shared.
- the arrangement of can be simplified.
- the flow path of the cooling water used in the condenser of the electric turbo refrigerator is branched from the first seawater supply passages L6 and L6a. If it is provided so as to circulate in the condenser and connect to the second seawater supply path L7, a part of the seawater pipe can be shared and the arrangement of the pipe can be further simplified as described above.
- the pipe through which seawater flows is preferably made of stainless steel or titanium in consideration of the occurrence of rust and the like.
- seawater used as a cold heat source is pumped up from a depth of 30 m to 70 m as an example, but the present invention is not limited to this.
- deep seawater can be used as a cold heat source.
- FIG. 1 does not show the configuration corresponding to the heat exchanger 37 and the buffer tank 38 in the second embodiment, also in the power generation system E mounted on the ship according to the first embodiment. It is preferable to provide a heat exchanger and a buffer tank in the first cooling medium supply path L3.
- the output characteristics of the gas turbine units Ga and Gb for determining the operating state of the cooling devices 20a and 20b those predetermined in accordance with the atmospheric temperature are used. Predetermined ones may be used according to the atmospheric pressure, humidity, and seawater temperature.
- the gas turbine units Ga and Gb are provided so as to be able to meet a predetermined power demand under a predetermined atmospheric temperature in a predetermined operating state of the cooling devices 20a and 20b. After determining the number of operating units, the gas turbine units Ga and Gb are operated, and then the operating state of the cooling devices 20a and 20b and the number of operating units of the gas turbine units Ga and Gb are appropriately adjusted according to the power demand and changes in the atmospheric temperature. The mode is changed, but the present invention is not limited to this.
- the operating states of the cooling devices 20a and 20b are determined based on the power demand and the output characteristics of the gas turbine units Ga and Gb, and further, the gas turbine units Ga and Gb are determined based on the determined operating state and the power demand.
- the gas turbine units Ga and Gb may be operated after determining the number of operating units.
- the cooling devices 20a and 20b are operated in advance according to the state where the atmospheric temperature is the highest and the electric power demand is the highest. The state and the number of operating gas turbine units Ga and Gb may be determined.
- the present invention is not limited to this.
- the operating state of the cooling devices 20a and 20b changes the degree of cooling of air by at least one of the first cooling units 21a and 21b, the second cooling units 22a and 22b and the third cooling unit 23a and 23b.
- the temperature of seawater measured by the seawater temperature sensor Ta may be high, and it may be considered that the cooling of air by the third cooling units 23a and 23b is not effective.
- the regulating valves appropriately provided in the first seawater supply paths L6a and L6b are closed to change the operating state of the cooling devices 20a and 20b to the three cooling units 21a, 21b, 22a, 22b, 23a and 23b.
- the air is cooled by the first cooling units 21a and 21b and the second cooling units 22a and 22b, and the air is not cooled by the third cooling units 23a and 23b (in other words, the first cooling). It is also possible to change to an operating state in which the cooling degree of air by the third cooling portions 23a and 23b is lowered without changing the cooling degree of air by the portions 21a and 21b and the second cooling portions 22a and 22b).
- the air produced by the first cooling units 21a and 21b, the second cooling units 22a and 22b, and the third cooling units 23a and 23b is based on the power demand and the output characteristics of the gas turbine unit.
- the operating state of the cooling devices 20a and 20b is determined by determining the degree of cooling, but the present invention is not limited to this.
- the operating states of the cooling devices 20a and 20b are determined according to the atmospheric conditions (atmospheric temperature, atmospheric pressure, humidity, etc.), and the first cooling units 21a and 21b, the second cooling units 22a and 22b, and the third cooling unit 23a, The degree of cooling of the air by 23b may be determined.
- the operating state of the cooling devices 20a and 20b is determined to be a state in which the air having a low temperature is operated with a cooling capacity capable of cooling to a predetermined temperature.
- the degree of cooling of air by each of the cooling units 21a, 21b, 22a, 22b, 23a, and 23b may be determined so as to obtain such an operating state.
- the output characteristics of the gas turbine units Ga and Gb are taken into consideration when determining the operating state of the cooling devices 20a and 20b and the number of operating gas turbine units Ga and Gb.
- the operation is not limited to this, and the operation of the power generation system may be controlled in consideration of the efficiency characteristics of the gas turbine units Ga and Gb.
- An example of operation control of the power generation system in consideration of the efficiency characteristics of the gas turbine units Ga and Gb will be described with reference to FIG.
- FIG. 5 is a graph showing the efficiency characteristics of the gas turbine unit, and the one-point chain line Z1 in the figure shows a load factor of 60 in a state where the cooling device is operated so that the air supplied to the combustor is 15 ° C.
- the efficiency characteristic per gas turbine unit (first efficiency characteristic) when it is% is shown, and the one-point chain wire Z2 shows the load factor in a state where the cooling device is operated so that the air supplied to the combustor becomes 15 ° C.
- the efficiency characteristic per gas turbine unit (second efficiency characteristic) when it is 100% is shown, and the two-point chain wire Z3 is in a state where the cooling device is operated so that the air supplied to the combustor becomes 10 ° C.
- the efficiency characteristics (third efficiency characteristics) per gas turbine unit when the load factor is 100% are shown.
- the cooling device was operated at a load factor of 60% so that the air supplied to the combustor was 15 ° C., and two gas turbine units were operated (black circles (1) in FIG.
- the cooling device On condition that the power demand can be met, the cooling device is operated so that the air supplied to the combustor becomes 10 ° C. by a method such as lowering the temperature of the cold water supplied from the refrigerator, and the gas turbine unit is operated.
- the number of operating units is reduced to one (the state of the black circle (5) in FIG. 5).
- the efficiency per gas turbine unit will be slightly reduced from the viewpoint of increasing the cooling capacity of the cooling device, but by reducing the number of operating gas turbine units to one, the gas turbine unit The efficiency per unit will eventually improve. In this way, by controlling the operation of the power generation system in consideration of the efficiency characteristics of the gas turbine unit, the gas turbine unit can be operated efficiently.
- the present invention can be used for a moving body provided with a cooling device capable of efficiently cooling the air supplied to the combustion means and suppressing a decrease in the output of the gas turbine unit.
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Abstract
Description
前記冷却装置は、
前記液体燃料を気化するために利用した熱媒体を冷熱源として利用する第一冷却部、冷凍機からの熱媒体を冷熱源として利用する第二冷却部及び熱媒体としての海水を冷熱源として利用する第三冷却部のうち、少なくともいずれか二つを備える点にある。 The characteristic configuration of the moving body according to the present invention for achieving the above object is to generate a combustion gas by burning a mixture of fuel gas and air in which liquid fuel is vaporized by a combustion means, and generate the combustion gas by the combustion means. It is used in a power generation system including a gas turbine unit in which a gas turbine is rotationally driven by the generated combustion gas and a first power generation means for generating power by utilizing the rotational force of the gas turbine, and cooling of air supplied to the combustion means. It is a moving body equipped with a cooling device, which is used for
The cooling device
The first cooling unit that uses the heat medium used to vaporize the liquid fuel as a cold heat source, the second cooling unit that uses the heat medium from the refrigerator as a cold heat source, and seawater as a heat medium are used as cold heat sources. The point is that at least two of the third cooling units are provided.
また、上記のように、冷凍機からの冷熱源がもつ冷熱だけを利用するような場合と異なり、上記特徴構成においては、冷凍機からの冷熱源による冷却だけでなく、液体燃料がもつ冷熱を利用した冷却を併用していることで、冷凍機からの冷水が持つ冷熱による冷却だけで空気を冷却する必要がなくなる。したがって、燃焼手段に供給する空気を十分に冷却して、発電システムの出力回復の効果を得られるようにしても、発電システム全体でのエネルギー効率の低下を抑えられ、冷凍機の大型化も避けられるため、コスト面での負担の軽減や、発電システムの省スペース化を図ることができる。 In a power generation system that generates power using a liquid fuel, a heat medium that has taken cold heat from the liquid fuel is inevitably generated when the liquid fuel is vaporized. Therefore, the heat medium that has taken cold heat from the liquid fuel is burned. By using it as a cold heat source for cooling the air supplied to the means, the cold heat of the liquid fuel can be effectively utilized.
Further, unlike the case where only the cold heat of the cold heat source from the refrigerator is used as described above, in the above characteristic configuration, not only the cooling by the cold heat source from the refrigerator but also the cold heat of the liquid fuel is used. By using the same cooling together, it is not necessary to cool the air only by cooling with the cold heat of the cold water from the refrigerator. Therefore, even if the air supplied to the combustion means is sufficiently cooled to obtain the effect of recovering the output of the power generation system, the decrease in energy efficiency of the entire power generation system can be suppressed and the size of the refrigerator can be avoided. Therefore, it is possible to reduce the burden on the cost and save the space of the power generation system.
これに対して、第二冷却部において冷熱源として利用する熱媒体は、冷凍機で製造された冷水などであり、第一冷却部において利用する熱媒体と比較して、相対的に温度が高い傾向にある。
したがって、上記特徴構成によれば、燃焼手段に供給する空気を、利用する熱媒体の温度が相対的に高い第二冷却部において冷却した後、利用する熱媒体の温度が相対的に低い第一冷却部において冷却するため、2つの冷却部で利用する各熱媒体がもつ冷熱を極力無駄にすることなく、空気を冷却することができる。 The heat medium used as a cold heat source in the first cooling unit is used for vaporizing the liquid fuel, and the temperature is extremely low by obtaining a considerable amount of cold heat.
On the other hand, the heat medium used as a cold heat source in the second cooling unit is cold water produced by a refrigerator, and the temperature is relatively higher than that of the heat medium used in the first cooling unit. There is a tendency.
Therefore, according to the above characteristic configuration, the air supplied to the combustion means is cooled in the second cooling unit where the temperature of the heat medium used is relatively high, and then the temperature of the heat medium used is relatively low. Since cooling is performed in the cooling unit, the air can be cooled without wasting the cold heat of each heat medium used in the two cooling units as much as possible.
また、発電システムが発電時に消費する液体燃料を気化して得られる冷熱だけでは空気の温度を発電システムの出力低下を抑えられるような温度にまで下げることができない場合であっても、第三冷却部において、燃焼手段に供給する空気を海水のもつ冷熱でも冷却して温度を下げることができる。これにより、発電システムの出力低下を抑え易くなる。
更に、この特徴構成においては、冷凍機を必要としないため、冷凍機の大型化という問題も発生せず、コスト面での負担の軽減や、発電システムの省スペース化を図ることもできる。 Similar to the above, in the first cooling section, the cold heat of the liquid fuel is effectively utilized by using a heat medium that has taken away the cold heat that is inevitably generated in the system that generates electricity using the liquid fuel as a cold heat source. It can be used.
In addition, even if the temperature of the air cannot be lowered to a temperature that can suppress the decrease in the output of the power generation system only by the cold heat obtained by vaporizing the liquid fuel consumed by the power generation system during power generation, the third cooling In the unit, the temperature can be lowered by cooling the air supplied to the combustion means with the cold heat of seawater. This makes it easier to suppress a decrease in the output of the power generation system.
Further, since the refrigerator is not required in this feature configuration, the problem of increasing the size of the refrigerator does not occur, the burden on the cost can be reduced, and the space of the power generation system can be saved.
これに対して、第三冷却部において冷熱源として利用する海水は、採取する深さにもよるが、その温度は第一冷却部において冷熱源として利用する熱媒体と比較して相対的に高い傾向にある。
したがって、上記特徴構成によれば、燃料手段に供給する空気を、利用する熱媒体の温度が相対的に高い第三冷却部において冷却した後、利用する熱媒体の温度が相対的に低い第一冷却部において冷却するため、2つの冷却部で利用する各熱媒体がもつ冷熱を極力無駄にすることなく、空気を冷却できる。 As described above, the heat medium used as a cold heat source in the first cooling unit obtains a considerable amount of cold heat from the liquid fuel, and its temperature is extremely low.
On the other hand, the temperature of seawater used as a cold heat source in the third cooling section is relatively higher than that of the heat medium used as a cold heat source in the first cooling section, although it depends on the sampling depth. There is a tendency.
Therefore, according to the above characteristic configuration, the air supplied to the fuel means is cooled in the third cooling unit where the temperature of the heat medium used is relatively high, and then the temperature of the heat medium used is relatively low. Since cooling is performed in the cooling unit, the air can be cooled without wasting the cold heat of each heat medium used in the two cooling units as much as possible.
したがって、上記特徴構成によれば、燃焼手段に供給する空気を、利用する熱媒体の温度が相対的に高い第三冷却部において冷却した後、利用する熱媒体の温度が相対的に低い第二冷却部において冷却するため、2つの冷却部で利用する各熱媒体がもつ冷熱を極力無駄にすることなく、空気を冷却できる。 The temperature of the seawater used as the cold heat source in the third cooling section tends to be relatively higher than that of the cold water from the refrigerator used as the cold heat source in the second cooling section, although it depends on the sampling depth. ..
Therefore, according to the above characteristic configuration, the air supplied to the combustion means is cooled in the third cooling unit where the temperature of the heat medium used is relatively high, and then the temperature of the heat medium used is relatively low. Since cooling is performed in the cooling unit, the air can be cooled without wasting the cold heat of each heat medium used in the two cooling units as much as possible.
したがって、上記特徴構成によれば、燃焼手段に供給する空気を、利用する熱媒体の相対的な温度が高い冷却部の順に冷却する、即ち、第三冷却部において冷却した後、第二冷却部において冷却し、その後、第一冷却部において冷却するため、3つの冷却部で利用する各熱媒体がもつ冷熱を極力無駄にすることなく、空気を冷却することができる。 As described above, the temperature of seawater used as a cold heat source in the third cooling section is higher than that of the heat medium used as a cold heat source in the first cooling section and the second cooling section, although it depends on the sampling depth. The temperature tends to be relatively high, and the heat medium used as a cold heat source in the second cooling section tends to have a relatively high temperature as compared with the heat medium used in the first cooling section. ..
Therefore, according to the above-mentioned characteristic configuration, the air supplied to the combustion means is cooled in the order of the cooling unit having the highest relative temperature of the heat medium to be used, that is, after cooling in the third cooling unit, the second cooling unit. Since the cooling is performed in the first cooling unit and then cooled in the first cooling unit, the air can be cooled without wasting the cooling heat of each of the heat media used in the three cooling units as much as possible.
前記第一冷却部で利用する前記熱媒体を温熱源として利用して前記液体燃料を気化する気化部と、
前記ガスタービンユニットと、
前記第一発電手段と、を備える点にある。 Further, a further characteristic configuration of the moving body according to the present invention is a fuel tank in which the liquid fuel is stored and a fuel tank.
A vaporization unit that vaporizes the liquid fuel by using the heat medium used in the first cooling unit as a heat source.
With the gas turbine unit
The point is that the first power generation means is provided.
また、本発明に係る移動体においては、移動体が移動又は停止している地域が熱帯地方であっても、燃焼手段に供給する空気の冷却を上記冷却装置によって行い、従来のようにミストを利用して行うようにしていないため、発電システムの出力回復の効果を得ることができる。 According to the above characteristic configuration, the moving body is a moving body including a cooling device, a fuel tank, a vaporization unit, a gas turbine unit, and a first power generation means. In this moving body, the gas turbine unit The first power generation means generates electricity by the rotational force of the gas turbine. By providing the above-mentioned cooling device, the moving body having such a configuration suppresses the decrease in energy efficiency of the entire power generation system, reduces the burden on the cost, and saves the space of the power generation system. On top of that, the air supplied to the combustion means can be cooled, whereby a decrease in the output of the gas turbine unit can be suppressed, and power generation can be efficiently performed.
Further, in the moving body according to the present invention, even if the area where the moving body is moving or stopped is a tropical region, the air supplied to the combustion means is cooled by the above cooling device, and mist is generated as in the conventional case. Since it is not used, the effect of recovering the output of the power generation system can be obtained.
前記排熱回収ボイラーユニットで気化された蒸気により蒸気タービンが回転駆動する蒸気タービンユニットと、
前記蒸気タービンの回転力を利用して発電する第二発電手段と、を備え、
船舶である点にある。 Further, a further characteristic configuration of the moving body according to the present invention is an exhaust heat recovery boiler unit that vaporizes water by exhaust gas from the gas turbine unit.
A steam turbine unit in which the steam turbine is rotationally driven by steam vaporized in the exhaust heat recovery boiler unit, and
A second power generation means for generating power by utilizing the rotational force of the steam turbine is provided.
It is a ship.
また、本発明に係る移動体においては、移動体たる船舶が航行又は停泊している地域が熱帯地方である場合が多くても、燃焼手段に供給する空気の冷却を上記冷却装置によって行い、従来のようにミストを利用して行うようにしていないため、発電システムの出力回復の効果を得ることができる。 According to the above-mentioned characteristic configuration, the moving body becomes a ship further provided with the exhaust heat recovery boiler unit, the above-mentioned turbine unit, and the second power generation means (in other words, a ship equipped with a combined cycle power generation system), and this movement In the body ship, the steam turbine is rotationally driven by utilizing the heat of the exhaust gas from the gas turbine unit, and the rotational force of the steam turbine also generates electricity by the second power generation means. Therefore, it is possible to efficiently generate electricity by effectively utilizing the heat of the exhaust gas from the gas turbine unit.
Further, in the moving body according to the present invention, even if the area where the moving ship is navigating or anchoring is often in the tropics, the air supplied to the combustion means is cooled by the above cooling device. Since the mist is not used as in the above, the effect of recovering the output of the power generation system can be obtained.
前記蒸気タービンユニットは、前記蒸気タービンの回転駆動に利用した蒸気を復水として回収する復水器と、
前記第三冷却部において利用する前記海水を冷熱源として利用し、前記復水器の内部を冷却する復水冷却部とを備える点にある。 Further, a further characteristic configuration of the moving body according to the present invention is that the cooling device includes a third cooling unit that uses seawater as a heat medium as a cold heat source.
The steam turbine unit includes a condenser that recovers steam used for rotationally driving the steam turbine as condensate.
The point is that the seawater used in the third cooling unit is used as a cold heat source, and a condensate cooling unit for cooling the inside of the condenser is provided.
したがって、第三冷却部及び復水冷却部に海水を供給したり、これらの冷却部から海水を回収したりするための海水用配管の一部を共用化できるため、配管の配置をシンプル化したり、配管内に海水を流通させるために必要なポンプの台数を削減したりできる。 According to the above characteristic configuration, the seawater used in the third cooling unit is used as a cooling heat source, the inside of the condenser is cooled in the condensate cooling unit, and the steam discharged from the steam turbine is used in the condenser. It can be cooled inside and recovered as condensate.
Therefore, it is possible to share a part of the seawater pipes for supplying seawater to the third cooling part and the condensate cooling part and recovering seawater from these cooling parts, so that the arrangement of the pipes can be simplified. , The number of pumps required to distribute seawater in the pipe can be reduced.
前記第三冷却部から前記復水冷却部へと供給される前記海水が流通する第二海水流路と、
前記第一海水流路と前記第二海水流路とを繋ぐバイパス流路と、
前記バイパス流路を流通する前記海水の量を調節する調節手段とを備える点にある。 Further, a further characteristic configuration of the moving body according to the present invention is a first seawater flow path through which the seawater supplied to the third cooling unit flows.
A second seawater flow path through which the seawater supplied from the third cooling unit to the condensate cooling unit flows,
A bypass flow path connecting the first seawater flow path and the second seawater flow path,
The point is that it is provided with an adjusting means for adjusting the amount of the seawater flowing through the bypass flow path.
上記特徴構成によれば、第一海水流路と第二海水流路とを繋ぐバイパス流路を設け、このバイパス流路に流通する海水の量を調節手段によって調節することで、第三冷却部を経由して復水冷却部へと流れる海水の量と、第三冷却部を経由することなくバイパス流路を通って復水冷却部へと流れる海水の量とを調節することができる。
したがって、第三冷却部が必要とする海水の量に応じて、バイパス流路に流通する海水の量を調節することにより、ポンプ出力の不必要な増加を抑えることができる。また、外気の温度よりも海水の温度が高いような場合に、ポンプで汲み上げた海水の全量をバイパス流路に流通するように調節し、第三冷却部へ海水を供給しないようにすることで、空気を加熱してしまうような事態を防止することもできる。 When the temperature difference between the seawater supplied to the third cooling unit and the outside air sucked in to supply the combustion means is small, the air is cooled even if the amount of seawater supplied to the third cooling unit is small. It is difficult to make a difference in the effect, but even in such a case, it is an unnecessary increase in pump output to always distribute the entire amount of seawater pumped by the pump to the condensate cooling section via the third cooling section. Connect. Further, when the temperature of the seawater is higher than the temperature of the outside air, the air may be heated by supplying the seawater to the third cooling unit.
According to the above characteristic configuration, a bypass flow path connecting the first seawater flow path and the second seawater flow path is provided, and the amount of seawater flowing through the bypass flow path is adjusted by the adjusting means to adjust the third cooling unit. The amount of seawater flowing to the condensate cooling section via the above and the amount of seawater flowing to the condensate cooling section through the bypass flow path without passing through the third cooling section can be adjusted.
Therefore, by adjusting the amount of seawater flowing through the bypass flow path according to the amount of seawater required by the third cooling unit, it is possible to suppress an unnecessary increase in pump output. In addition, when the temperature of seawater is higher than the temperature of the outside air, the total amount of seawater pumped up by the pump is adjusted so that it flows through the bypass flow path so that seawater is not supplied to the third cooling unit. , It is also possible to prevent the situation where the air is heated.
また、本願における電力需要とは、移動体が必要とする電力や、移動体から電力が供給される一又は複数の設備が必要とする電力の他、蓄電などを目的として発電システムにより発電しようとする電力などを含む概念である。 The operating state of the cooling device changes depending on the degree of cooling of the air supplied to the combustion means in each of the first cooling part, the second cooling part, and the third cooling part, and the degree of cooling of the air by each cooling part is determined. By changing it, the operating state of the cooling device can be changed as appropriate. Further, the degree of cooling of air by each cooling unit can be changed by changing the temperature of the heat medium supplied to the cooling unit or by starting or stopping the supply of the heat medium to the cooling unit.
Further, the electric power demand in the present application means the electric power required by the mobile body, the electric power required by one or more facilities to which the electric power is supplied from the mobile body, and the power generation system for the purpose of storing electricity. It is a concept that includes electric power to be generated.
前記第一冷却部により前記燃焼手段に供給する空気を冷却した状態で、前記電力需要と前記ガスタービンユニットの出力特性とに基づいて、前記第二冷却部及び前記第三冷却部の少なくとも一方による前記燃焼手段に供給する空気の冷却度合を決定することで、前記冷却装置の運転状態を決定する点にある。 Further, a further characteristic configuration of the moving body according to the present invention is that the cooling device includes the first cooling unit and at least one of the second cooling unit and the third cooling unit.
With the air supplied to the combustion means cooled by the first cooling unit, at least one of the second cooling unit and the third cooling unit is used based on the power demand and the output characteristics of the gas turbine unit. The point is that the operating state of the cooling device is determined by determining the degree of cooling of the air supplied to the combustion means.
前記燃焼手段に供給する空気を前記第一冷却部及び前記第三冷却部によって冷却する状態で、前記電力需要と前記ガスタービンユニットの出力特性とに基づいて、前記第二冷却部による前記燃焼手段に供給する空気の冷却度合を決定することで、前記冷却装置の運転状態を決定する点にある。 Further, a further characteristic configuration of the moving body according to the present invention is that the cooling device includes the first cooling unit, the second cooling unit, and the third cooling unit.
With the air supplied to the combustion means cooled by the first cooling unit and the third cooling unit, the combustion means by the second cooling unit is based on the power demand and the output characteristics of the gas turbine unit. By determining the degree of cooling of the air supplied to the cooling device, the operating state of the cooling device is determined.
以下、図面を参照して本発明の第1実施形態に係る移動体について説明する。尚、本実施形態では、移動体が船舶である場合を例示して説明する。 [First Embodiment]
Hereinafter, the moving body according to the first embodiment of the present invention will be described with reference to the drawings. In this embodiment, a case where the moving body is a ship will be described as an example.
次に、本発明の第2実施形態に係る移動体について説明する。尚、本実施形態においても、移動体が船舶である場合を例示して説明する。また、第1実施形態と同様の構成については同一の符号を付し、詳細な説明は省略する。 [Second Embodiment]
Next, the moving body according to the second embodiment of the present invention will be described. In this embodiment as well, the case where the moving body is a ship will be described as an example. Further, the same components as those in the first embodiment are designated by the same reference numerals, and detailed description thereof will be omitted.
〔1〕上記各実施形態においては、冷却装置20,20a,20bが、第一冷却部21,21a,21b、第二冷却部22,22a,22b及び第三冷却部23,23a,23bを備える構成としたが、冷却装置が上記3つの冷却部のうち、少なくともいずれか二つを備える構成を採用しても良い。 [Another Embodiment]
[1] In each of the above embodiments, the
尚、この場合には、熱媒体がもつ冷熱を極力無駄にすることなく、空気を冷却するという観点から、燃焼器6に供給する空気が第二冷却部22,22a,22b、第一冷却部21,21a,21bの順に流通するように、これら2つの冷却部21,21a,21b,22,22a,22bを配置することが好ましい。 When a configuration including the
In this case, the air supplied to the combustor 6 is the
尚、この場合には、燃焼器6に供給する空気が第三冷却部23,23a,23b、第一冷却部21,21a,21bの順に流通するように、これら2つの冷却部21,21a,21b,23,23a,23bを配置することが好ましく、このようにすれば、熱媒体がもつ冷熱を極力無駄にすることなく、空気を冷却できる。 Further, even when a configuration including the
In this case, these two cooling
尚、この場合には、燃焼器6に供給する空気が第三冷却部23,23a,23b、第二冷却部22,22a,22bの順に流通するように、これら2つの冷却部22,22a,22b,23,23a,23bを配置することが好ましく、このようにすれば、熱媒体がもつ冷熱を極力無駄にすることなく、空気を冷却できる。 Further, when the configuration including the
In this case, the two cooling
冷却装置を備えた移動体であれば、例えば、冷却装置を備えていないコンバインドサイクル発電システムを備えた施設等に移動体を移動させることで、移動体が備えた冷却装置によって、この発電システムにおける燃焼器に供給する空気を冷却することが可能となり、ガスタービンユニットの出力低下を抑えられるようになる。
また、冷却装置とガスタービン発電に必要な構成とを搭載するのであれば、比較的小型の移動体にも適用して実用化できる。
尚、移動体としては、LNG船の他、LPG船、エチレン船、アンモニア船、液化水素運搬船、大型マグロ船、冷凍コンテナ船、浮船等が挙げられるが、これらに限定されず、造船所にて建造又は改造して使用地に曳航され、試用期間中又はほぼ恒久的に係留される浮体構造物、その他の陸上各種輸送機関(トラック、ドーリー車)なども含まれる。 [3] In the above embodiment, the moving body is a ship including a
In the case of a moving body equipped with a cooling device, for example, by moving the moving body to a facility equipped with a combined cycle power generation system without a cooling device, the cooling device provided by the moving body can be used in this power generation system. It becomes possible to cool the air supplied to the combustor, and it becomes possible to suppress a decrease in the output of the gas turbine unit.
Further, if a cooling device and a configuration required for gas turbine power generation are installed, it can be applied to a relatively small mobile body and put into practical use.
In addition to LNG carriers, moving objects include, but are not limited to, LPG carriers, ethylene ships, ammonia ships, liquefied hydrogen carriers, large tuna ships, refrigerated container ships, floating ships, etc. It also includes floating structures that have been built or modified and towed to the site of use and moored during the trial period or almost permanently, and other various land transportation facilities (trucks, dolly vehicles).
また、上記第2実施形態では、第二海水供給路L7に流通する海水の量を調節する態様を採用していないが、上記第1実施形態と同様に、適宜調節装置を設けて、第二海水供給路L7に流通する海水の量を調節するようにしても良い。 [5] In the first embodiment, a bypass flow path L8 connecting the first seawater supply path L6 and the second seawater supply path L7 is provided, and an adjusting device for adjusting the amount of seawater flowing through the bypass flow path L8. Although the configuration is provided with 24, the configuration is not limited to this, and a bypass flow path and an adjusting device may be provided as necessary.
Further, in the second embodiment, the mode of adjusting the amount of seawater flowing through the second seawater supply channel L7 is not adopted, but as in the first embodiment, an appropriate adjusting device is provided to provide a second. The amount of seawater flowing through the seawater supply channel L7 may be adjusted.
まず、電力需要とガスタービンユニットGa,Gbの出力特性とに基づいて冷却装置20a,20bの運転状態を決定し、更に、この決定した運転状態と電力需要とに基づいてガスタービンユニットGa,Gbの運転台数を決定した上で、ガスタービンユニットGa,Gbを稼働させるようにしても良い。
また、一日における大気温度の変化や電力需要の変化が予め分かっているような場合には、最も大気温度が高い状態や最も電力需要が多い状態に合わせて、予め冷却装置20a,20bの運転状態やガスタービンユニットGa,Gbの運転台数を決定するようにしても良い。 [13] In the second embodiment, the gas turbine units Ga and Gb are provided so as to be able to meet a predetermined power demand under a predetermined atmospheric temperature in a predetermined operating state of the
First, the operating states of the
Further, when the change in the atmospheric temperature and the change in the electric power demand in one day are known in advance, the
冷却装置20a,20bの運転状態は、第一冷却部21a,21b、第二冷却部22a,22b及び第三冷却部23a,23bのうちの少なくともいずれかの冷却部による空気の冷却度合を変えることで変更できる。
例えば、海水温度センサTaで計測された海水の温度が高く、第三冷却部23a,23bによる空気の冷却が有効でないと考えられる場合がある。この場合には、第一海水供給路L6a,L6bに適宜設けられる調整弁を閉弁して、冷却装置20a,20bの運転状態を、3つの冷却部21a,21b,22a,22b,23a,23bで空気を冷却する運転状態から第一冷却部21a,21b及び第二冷却部22a,22bで空気を冷却し、第三冷却部23a,23bで空気を冷却しない運転状態(言い換えれば、第一冷却部21a,21b及び第二冷却部22a,22bによる空気の冷却度合を変えずに、第三冷却部23a,23bによる空気の冷却度合を下げた運転状態)に変えることもできる。 [14] In the second embodiment, as a case of changing the operating state of the
The operating state of the
For example, the temperature of seawater measured by the seawater temperature sensor Ta may be high, and it may be considered that the cooling of air by the
大気の状態(大気温度や気圧、湿度など)に応じて、冷却装置20a,20bの運転状態を決定し、第一冷却部21a,21b、第二冷却部22a,22b及び第三冷却部23a,23bによる空気の冷却度合を決定しても良い。
例えば、大気温度が低い場合(20~30℃程度)には、冷却装置20a,20bの運転状態をこの温度が低い空気を所定の温度まで冷却できるような冷却能力で運転する状態と決定し、このような運転状態となるように、各冷却部21a,21b,22a,22b,23a,23bによる空気の冷却度合を決定するようにしても良い。 [15] In the second embodiment, the air produced by the
The operating states of the
For example, when the atmospheric temperature is low (about 20 to 30 ° C.), the operating state of the
尚、図5は、ガスタービンユニットの効率特性を示すグラフであり、同図中の一点鎖線Z1は、燃焼器に供給する空気が15℃となるように冷却装置を運転した状態で負荷率60%である場合のガスタービンユニット1台あたりの効率特性(第一効率特性)を示し、一点鎖線Z2は、燃焼器に供給する空気が15℃となるように冷却装置を運転した状態で負荷率100%である場合のガスタービンユニット1台当たりの効率特性(第二効率特性)を示し、二点鎖線Z3は、燃焼器に供給する空気が10℃となるように冷却装置を運転した状態で負荷率100%である場合のガスタービンユニット1台当たりの効率特性(第三効率特性)を示す。
大気温度20℃において、燃焼器に供給する空気が15℃となるように冷却装置を負荷率60%で運転し、ガスタービンユニットを2台稼働させた状態(図5中の黒丸(1)の状態)から、ガスタービンユニットの運転台数及び空気の冷却度合を変えずに大気温度が35℃に上昇した状態(図5中の黒丸(2)の状態)になると、ガスタービンユニット1台当たりの効率は低下する。この状態(図5中の黒丸(2)の状態)から、燃焼器に供給する空気が15℃となるようにガスタービン出力と冷却装置とが負荷率100%で運転した状態(図5中の黒丸(3)の状態)にすることで、ガスタービンユニット1台当たりの効率を向上させることができる。その後、大気温度が27℃まで低下し、同時に電力需要も低下してガスタービンユニット1台当たりの効率が低下したような状態(図5中の黒丸(4)の状態)となった際に、電力需要を賄うことができることを条件に、冷凍機から供給する冷水の温度を下げるなどの方法によって、燃焼器に供給する空気が10℃となるように冷却装置を運転して、ガスタービンユニットの運転台数を1台に減らした状態(図5中の黒丸(5)の状態)にする。そうすることで、冷却装置による冷却能力を上げるという点からすればガスタービンユニット1台当たりの効率は若干低下するが、ガスタービンユニットの運転台数を1台に減らしていることで、ガスタービンユニット1台当たりの効率は最終的に向上する。
このように、ガスタービンユニットの効率特性を考慮して発電システムの運転制御を行うことで、ガスタービンユニットを効率良く稼働させることができる。 [16] In the second embodiment, the output characteristics of the gas turbine units Ga and Gb are taken into consideration when determining the operating state of the
FIG. 5 is a graph showing the efficiency characteristics of the gas turbine unit, and the one-point chain line Z1 in the figure shows a load factor of 60 in a state where the cooling device is operated so that the air supplied to the combustor is 15 ° C. The efficiency characteristic per gas turbine unit (first efficiency characteristic) when it is% is shown, and the one-point chain wire Z2 shows the load factor in a state where the cooling device is operated so that the air supplied to the combustor becomes 15 ° C. The efficiency characteristic per gas turbine unit (second efficiency characteristic) when it is 100% is shown, and the two-point chain wire Z3 is in a state where the cooling device is operated so that the air supplied to the combustor becomes 10 ° C. The efficiency characteristics (third efficiency characteristics) per gas turbine unit when the load factor is 100% are shown.
At an air temperature of 20 ° C., the cooling device was operated at a load factor of 60% so that the air supplied to the combustor was 15 ° C., and two gas turbine units were operated (black circles (1) in FIG. 5). From the state), when the atmospheric temperature rises to 35 ° C. (the state of the black circle (2) in FIG. 5) without changing the number of operating gas turbine units and the degree of air cooling, one gas turbine unit per unit. Efficiency is reduced. From this state (the state of the black circle (2) in FIG. 5), the gas turbine output and the cooling device are operated at a load factor of 100% so that the air supplied to the combustor becomes 15 ° C. (in FIG. 5). By setting the black circle (3)), the efficiency per gas turbine unit can be improved. After that, when the air temperature dropped to 27 ° C., and at the same time, the power demand also dropped and the efficiency per gas turbine unit decreased (the state of the black circle (4) in FIG. 5). On condition that the power demand can be met, the cooling device is operated so that the air supplied to the combustor becomes 10 ° C. by a method such as lowering the temperature of the cold water supplied from the refrigerator, and the gas turbine unit is operated. The number of operating units is reduced to one (the state of the black circle (5) in FIG. 5). By doing so, the efficiency per gas turbine unit will be slightly reduced from the viewpoint of increasing the cooling capacity of the cooling device, but by reducing the number of operating gas turbine units to one, the gas turbine unit The efficiency per unit will eventually improve.
In this way, by controlling the operation of the power generation system in consideration of the efficiency characteristics of the gas turbine unit, the gas turbine unit can be operated efficiently.
2 気化器(気化部)
6 燃焼器(燃焼手段)
7,7a,7b ガスタービン
10 冷凍機
20,20a,20b 冷却装置
21,21a,21b 第一冷却部
22,22a,22b 第二冷却部
23,23a,23b 第三冷却部
24 調節装置(調節手段)
25,25a,25b 排熱回収ボイラーユニット
30 蒸気タービン
31 復水器
32 復水冷却部
35 第一発電機(第一発電手段)
36 第二発電機(第二発電手段)
L6,L6a,L6b 第一海水供給路(第一海水流路)
L7 第二海水供給路(第二海水流路)
L8 バイパス流路
G,Ga,Gb ガスタービンユニット
S 蒸気タービンユニット
E,E1 発電システム 1
6 Combustor (combustion means)
7,7a,
25, 25a, 25b Exhaust heat
36 Second generator (second power generation means)
L6, L6a, L6b 1st seawater supply channel (1st seawater channel)
L7 Second seawater supply channel (second seawater channel)
L8 Bypass flow path G, Ga, Gb Gas turbine unit S Steam turbine unit E, E1 Power generation system
Claims (18)
- 液体燃料が気化した燃料ガス及び空気との混合気を燃焼手段で燃焼して燃焼ガスを発生させて、当該燃焼手段で発生した燃焼ガスによってガスタービンが回転駆動するガスタービンユニットと、前記ガスタービンの回転力を利用して発電する第一発電手段とを備えた発電システムに用いられ、前記燃焼手段に供給する空気の冷却に供される冷却装置、を備えた移動体であって、
前記冷却装置は、
前記液体燃料を気化するために利用した熱媒体を冷熱源として利用する第一冷却部、冷凍機からの熱媒体を冷熱源として利用する第二冷却部及び熱媒体としての海水を冷熱源として利用する第三冷却部のうち、少なくともいずれか二つを備える移動体。 A gas turbine unit in which a mixture of fuel gas vaporized from liquid fuel and air is burned by a combustion means to generate a combustion gas, and the gas turbine is rotationally driven by the combustion gas generated by the combustion means, and the gas turbine. It is a moving body provided with a cooling device, which is used in a power generation system provided with a first power generation means for generating power by utilizing the rotational force of the above combustion means and is used for cooling the air supplied to the combustion means.
The cooling device
The first cooling unit that uses the heat medium used to vaporize the liquid fuel as a cold heat source, the second cooling unit that uses the heat medium from the refrigerator as a cold heat source, and seawater as a heat medium are used as cold heat sources. A moving body including at least two of the third cooling units. - 前記冷却装置は、前記第一冷却部と前記第二冷却部とを備える請求項1に記載の移動体。 The moving body according to claim 1, wherein the cooling device includes the first cooling unit and the second cooling unit.
- 前記冷却装置は、前記燃焼手段に供給する空気が前記第二冷却部、前記第一冷却部の順に流通するように、前記第一及び第二冷却部が配置されている請求項2に記載の移動体。 The second aspect of the present invention, wherein the first and second cooling units are arranged so that the air supplied to the combustion means flows in the order of the second cooling unit and the first cooling unit. Mobile body.
- 前記冷却装置は、前記第一冷却部と前記第三冷却部とを備える請求項1に記載の移動体。 The moving body according to claim 1, wherein the cooling device includes the first cooling unit and the third cooling unit.
- 前記冷却装置は、前記燃焼手段に供給する空気が前記第三冷却部、前記第一冷却部の順に流通するように、前記第一及び第三冷却部が配置されている請求項4に記載の移動体。 The fourth aspect of the present invention, wherein the first and third cooling units are arranged in the cooling device so that the air supplied to the combustion means flows in the order of the third cooling unit and the first cooling unit. Mobile body.
- 前記冷却装置は、前記第二冷却部と前記第三冷却部とを備える請求項1に記載の移動体。 The moving body according to claim 1, wherein the cooling device includes the second cooling unit and the third cooling unit.
- 前記冷却装置は、前記燃焼手段に供給する空気が前記第三冷却部、前記第二冷却部の順に流通するように、前記第二及び第三冷却部が配置されている請求項6に記載の移動体。 The sixth aspect of claim 6 in which the second and third cooling units are arranged so that the air supplied to the combustion means flows in the order of the third cooling unit and the second cooling unit. Mobile body.
- 前記冷却装置は、前記第一冷却部と前記第二冷却部と前記第三冷却部とを備える請求項1に記載の移動体。 The moving body according to claim 1, wherein the cooling device includes the first cooling unit, the second cooling unit, and the third cooling unit.
- 前記冷却装置は、前記燃焼手段に供給する空気が前記第三冷却部、前記第二冷却部、前記第一冷却部の順に流通するように、前記第一、第二及び第三冷却部が配置されている請求項8に記載の移動体。 In the cooling device, the first, second and third cooling units are arranged so that the air supplied to the combustion means flows in the order of the third cooling unit, the second cooling unit, and the first cooling unit. The moving body according to claim 8.
- 前記液体燃料が貯蔵された燃料タンクと、
前記第一冷却部で利用する前記熱媒体を温熱源として利用して前記液体燃料を気化する気化部と、
前記ガスタービンユニットと、
前記第一発電手段と、を備える請求項1~9のいずれか一項に記載の移動体。 The fuel tank in which the liquid fuel is stored and
A vaporization unit that vaporizes the liquid fuel by using the heat medium used in the first cooling unit as a heat source.
With the gas turbine unit
The mobile body according to any one of claims 1 to 9, further comprising the first power generation means. - 前記ガスタービンユニットからの排ガスによって水を気化する排熱回収ボイラーユニットと、
前記排熱回収ボイラーユニットで気化された蒸気により蒸気タービンが回転駆動する蒸気タービンユニットと、
前記蒸気タービンの回転力を利用して発電する第二発電手段と、を備え、
船舶である請求項10に記載の移動体。 An exhaust heat recovery boiler unit that vaporizes water with exhaust gas from the gas turbine unit,
A steam turbine unit in which the steam turbine is rotationally driven by steam vaporized in the exhaust heat recovery boiler unit, and
A second power generation means for generating power by utilizing the rotational force of the steam turbine is provided.
The moving body according to claim 10, which is a ship. - 前記冷却装置は、前記第三冷却部を備え、
前記蒸気タービンユニットは、前記蒸気タービンの回転駆動に利用した蒸気を復水として回収する復水器と、
前記第三冷却部において利用する前記海水を冷熱源として利用し、前記復水器の内部を冷却する復水冷却部とを備える請求項11に記載の移動体。 The cooling device includes the third cooling unit.
The steam turbine unit includes a condenser that recovers steam used for rotationally driving the steam turbine as condensate.
The mobile body according to claim 11, further comprising a condensate cooling unit that cools the inside of the condenser by using the seawater used in the third cooling unit as a cooling heat source. - 前記第三冷却部に供給される前記海水が流通する第一海水流路と、
前記第三冷却部から前記復水冷却部へと供給される前記海水が流通する第二海水流路と、
前記第一海水流路と前記第二海水流路とを繋ぐバイパス流路と、
前記バイパス流路を流通する前記海水の量を調節する調節手段とを備える請求項12に記載の移動体。 The first seawater flow path through which the seawater supplied to the third cooling unit flows, and
A second seawater flow path through which the seawater supplied from the third cooling unit to the condensate cooling unit flows,
A bypass flow path connecting the first seawater flow path and the second seawater flow path,
The moving body according to claim 12, further comprising an adjusting means for adjusting the amount of seawater flowing through the bypass flow path. - 電力需要と前記冷却装置の運転状態とに基づいて、前記ガスタービンユニットの運転台数を決定する請求項1~13のいずれか一項に記載の移動体。 The moving body according to any one of claims 1 to 13, which determines the number of operating gas turbine units based on the power demand and the operating state of the cooling device.
- 電力需要と前記ガスタービンユニットの出力特性とに基づいて、前記冷却装置の運転状態を決定する請求項1~14のいずれか一項に記載の移動体。 The moving body according to any one of claims 1 to 14, which determines the operating state of the cooling device based on the electric power demand and the output characteristics of the gas turbine unit.
- 前記冷却装置は、前記第一冷却部と、前記第二冷却部及び前記第三冷却部のうちの少なくともいずれか一方とを備え、
前記燃焼手段に供給する空気を前記第一冷却部によって冷却する状態で、前記電力需要と前記ガスタービンユニットの出力特性とに基づいて、前記第二冷却部及び前記第三冷却部の少なくとも一方による前記燃焼手段に供給する空気の冷却度合を決定することで、前記冷却装置の運転状態を決定する請求項15に記載の移動体。 The cooling device includes the first cooling unit and at least one of the second cooling unit and the third cooling unit.
With the air supplied to the combustion means cooled by the first cooling unit, at least one of the second cooling unit and the third cooling unit is used based on the power demand and the output characteristics of the gas turbine unit. The moving body according to claim 15, wherein the operating state of the cooling device is determined by determining the degree of cooling of the air supplied to the combustion means. - 前記冷却装置は、前記第一冷却部、前記第二冷却部及び前記第三冷却部を備え、
前記燃焼手段に供給する空気を前記第一冷却部及び前記第三冷却部によって冷却する状態で、前記電力需要と前記ガスタービンユニットの出力特性とに基づいて、前記第二冷却部による前記燃焼手段に供給する空気の冷却度合を決定することで、前記冷却装置の運転状態を決定する請求項15に記載の移動体。 The cooling device includes the first cooling unit, the second cooling unit, and the third cooling unit.
With the air supplied to the combustion means cooled by the first cooling unit and the third cooling unit, the combustion means by the second cooling unit is based on the power demand and the output characteristics of the gas turbine unit. The moving body according to claim 15, wherein the operating state of the cooling device is determined by determining the degree of cooling of the air supplied to the cooling device. - 大気の状態及び前記冷却装置の状況のうちの少なくともいずれか一方に応じて、前記冷却装置の運転状態を決定し、前記第一冷却部、前記第二冷却部及び前記第三冷却部のうちの少なくともいずれかによる前記燃焼手段に供給する空気の冷却度合を決定する請求項1~14のいずれか一項に記載の移動体。 The operating state of the cooling device is determined according to at least one of the air condition and the state of the cooling device, and the operating state of the first cooling unit, the second cooling unit, and the third cooling unit is determined. The moving body according to any one of claims 1 to 14, which determines the degree of cooling of the air supplied to the combustion means by at least one of them.
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Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0797933A (en) * | 1993-09-29 | 1995-04-11 | Toshiba Corp | Intake air cooling device of gas turbine |
KR20100047716A (en) * | 2008-10-29 | 2010-05-10 | (주)엑서지엔지니어링 | Air cooling apparustus for gas turbine |
JP2015155689A (en) * | 2014-01-20 | 2015-08-27 | 三菱重工業株式会社 | Liquefied gas cold utilization system and liquefied gas cold utilization method |
WO2016078790A1 (en) * | 2014-11-20 | 2016-05-26 | Siemens Aktiengesellschaft | Apparatus and method for cooling or heating the air inlet of a gas turbine |
KR20180046625A (en) * | 2016-10-28 | 2018-05-09 | 삼성중공업 주식회사 | Gas turbine generating apparatus and startup operating method of the same |
JP2018141381A (en) * | 2017-02-27 | 2018-09-13 | 三菱重工業株式会社 | Marine power generating system and power generation method of marine power generating system |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1112505C (en) * | 1995-06-01 | 2003-06-25 | 特雷克特贝尔Lng北美公司 | Liquefied natural gas (LNG) fueled combined cycle power plant and LNG fueled gas turbine plant |
JPH10238368A (en) * | 1996-10-12 | 1998-09-08 | Yoshihide Nakamura | Combined cycle system |
JP2000204909A (en) | 1999-01-11 | 2000-07-25 | Osaka Gas Co Ltd | Lng cryogenic power generation system |
-
2019
- 2019-06-10 WO PCT/JP2019/022900 patent/WO2020202590A1/en active Application Filing
- 2019-06-10 SG SG11202110787TA patent/SG11202110787TA/en unknown
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- 2019-06-10 KR KR1020217031901A patent/KR20210143209A/en active IP Right Grant
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Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0797933A (en) * | 1993-09-29 | 1995-04-11 | Toshiba Corp | Intake air cooling device of gas turbine |
KR20100047716A (en) * | 2008-10-29 | 2010-05-10 | (주)엑서지엔지니어링 | Air cooling apparustus for gas turbine |
JP2015155689A (en) * | 2014-01-20 | 2015-08-27 | 三菱重工業株式会社 | Liquefied gas cold utilization system and liquefied gas cold utilization method |
WO2016078790A1 (en) * | 2014-11-20 | 2016-05-26 | Siemens Aktiengesellschaft | Apparatus and method for cooling or heating the air inlet of a gas turbine |
KR20180046625A (en) * | 2016-10-28 | 2018-05-09 | 삼성중공업 주식회사 | Gas turbine generating apparatus and startup operating method of the same |
JP2018141381A (en) * | 2017-02-27 | 2018-09-13 | 三菱重工業株式会社 | Marine power generating system and power generation method of marine power generating system |
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