JP2006328977A - Turbine system and its construction method - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a turbine system and its construction method, capable of flexibly producing energy and water in response to respective demands. <P>SOLUTION: This turbine system has a gas turbine facility 10, a steam generating facility 20 for generating steam by using exhaust gas (e) from this gas turbine facility 10 as a heat source, a steam turbine facility 30 for providing rotational motive power by the steam (i) from this steam generating facility 20, and a water manufacturing facility 40 for providing pure water (n) by distilling raw water (m) by using the steam (i) from the steam generating facility 20. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

  The present invention relates to a turbine system including a turbine facility and a water production facility, and a construction method thereof.

  As a turbine system equipped with a turbine facility and a water production facility, pure water is produced in the flash type pure water production facility using the exhaust heat of the gas turbine facility, and superheated steam is again produced from the water produced using the exhaust heat. There is one that generates and injects this superheated steam into a combustor of a gas turbine facility to increase the output of the gas turbine (see Patent Document 1, etc.).

JP 2003-312588 A

  For example, if you install it on a remote island or desert area and try to obtain energy (here, electricity, power, etc.) and water in one plant, water can be stored, so as long as there is stock, it will be supplied regardless of the operation status of the plant. While possible, energy cannot be stored by nature. When the above-mentioned conventional technology is applied to the supply of energy and water, it is necessary to switch the gas turbine equipment to partial load operation as needed when the energy demand fluctuates. Will fluctuate. Water supply and demand imbalance can be dealt with by storing water, but it is also limited by the capacity of the water storage facility. Therefore, in some cases, the energy supply amount may be limited by the water consumption state.

  An object of the present invention is to provide a turbine system that can flexibly produce energy and water in response to respective demands, and a construction method thereof.

  In order to achieve the above object, the present invention provides a steam generation facility for generating steam, a steam turbine facility for obtaining rotational power by the steam from the steam generation facility, and raw water using the steam from the steam generation facility. And a water production facility for obtaining pure water by distillation.

  ADVANTAGE OF THE INVENTION According to this invention, energy and water can be produced corresponding to each demand flexibly.

Embodiments of the present invention will be described below with reference to the drawings.
FIG. 1 is a circuit diagram schematically showing the overall configuration of the turbine system according to the first embodiment of the present invention.
As shown in FIG. 1, this system uses a gas turbine facility 10, an exhaust heat recovery type steam generation facility 20 that generates steam using exhaust gas from the gas turbine facility 10 as a heat source, and steam generated from the steam generation facility 20. A steam turbine facility 30 that obtains rotational power and a water production facility 40 that obtains pure water by distilling raw water (for example, seawater, industrial water, etc.) using steam from the steam generation facility 20 are provided.

  The gas turbine facility 10 is connected to the steam generation facility 20 via an exhaust gas pipe 19. A branch pipe 27 extends from the steam generation facility 20. The branch line 27 includes a steam pipe 26 connected to the steam outlet of the steam generation facility 20, a steam pipe 34 connected to the inlet of the steam turbine facility 30, and a steam pipe 42 connected to the medium inlet of the water production facility 40. These steam pipes 26, 34, 42 are connected by a branch portion 28. The steam turbine facility 30 is connected to the inlet of the steam generation facility 20 via the condensate pipes 36 and 25. A condensate pipe 43 from the water production facility 40 is connected to the condensate pipe 25.

  The gas turbine facility 10 includes a compressor 11, a combustor 12, and a turbine 13. The compressor 11 sucks the air a and compresses it to a predetermined pressure. For example, the suction air flow rate of the compressor 11 is about 88 kg / s, and the pressure ratio is about 15. The compressed air b is guided to the combustor 12 and used to burn the fuel c. The high-temperature and high-pressure combustion gas d thus generated is guided to the turbine 13 disposed downstream and performs expansion work. The temperature of the combustion gas d is, for example, about 1300 ° C. Part of the expansion work of the combustion gas d is consumed as the compression power of the compressor 11 connected to the rotating shaft of the turbine 13, and the remaining work is converted into electric power by the generator 14 connected to the rotating shaft of the turbine 13. The The amount of power generated by the generator 14 is about 27000 kW, for example. After the expansion work is performed, the exhaust gas e discharged from the gas turbine equipment 10 in a state where the temperature and pressure are reduced to about 560 ° C., for example, is guided to the steam generation equipment 20 via the pipe 19 as a heating medium.

  In the present embodiment, the single-shaft turbine 13 is illustrated, but the turbine may be a twin-shaft turbine. Moreover, although the generator 14 is illustrated as a load apparatus of the turbine 13, it replaces with the generator 14 and connecting a pump etc. is also considered.

  The steam generation facility 20 includes a plurality (three in the present embodiment) of heat exchangers in the exhaust gas flow path. These heat exchangers are referred to as a superheater 21, an evaporator 22 and a economizer 23 from upstream along the flow of exhaust gas in the exhaust gas flow path. The exhaust gas e is used as a heat source to heat the feed water f from the condensate pipe 25 by the heat exchangers 21 to 23 to generate superheated steam g. The feed water f supplied into the steam generation facility 20 is about 60 ° C., for example, and the superheated steam g heated by the superheater 21 is about 200 ° C. and the pressure ratio is about 8. As a result of being used as a heating medium in the steam generation facility 20, the exhaust gas h whose thermal energy has been recovered and whose temperature has dropped to about 140 ° C. is released into the atmosphere via the exhaust pipe 24.

  The steam turbine facility 30 includes a steam turbine 31 and a generator 33. The superheated steam i supplied to the steam turbine equipment 30 via the steam pipes 26 and 34 performs expansion work in the steam turbine 31. The shaft power of the steam turbine 31 obtained by the expansion work of the superheated steam i is converted into electric power by the generator 33 connected to the steam turbine 31. In the present embodiment, the superheated steam i becomes wet steam during expansion work in the steam turbine 31. The wet steam j after the expansion work is converted into water k by the condenser 32 and then returned to the steam generation facility 20 through the condenser pipes 36 and 25.

  In the present embodiment, the case where there is one steam turbine 31 is illustrated, but a plurality of steam turbines having different pressures such as high pressure, medium pressure, and low pressure may be employed. Moreover, although the generator 33 is illustrated as a load apparatus of the steam turbine 31, it replaces with the generator 33 depending on the case, and connecting a pump etc. is also considered.

  The water production facility 40 is a reheat type seawater desalination apparatus. In addition, a flash-type seawater desalination apparatus can be used. In this water production facility 40, pure water n is produced by distilling raw water (seawater, industrial water, etc.) m using the superheated steam l guided through the steam pipe 42 as a heating medium. The superheated steam l becomes water p with the production of the pure water n and is returned to the steam generation facility 20.

  As described above, in the present embodiment, the steam from the steam generation facility 20 is diverted at the branch portion 28 and supplied to the steam turbine facility 30 and the water production facility 40, respectively. And in this embodiment, the supply ratio adjustment apparatus 50 which adjusts the supply ratio of the superheated steam g supplied to the steam turbine equipment 30 and the water production equipment 40 is provided. The supply ratio adjusting device 50 includes flow rate adjusting valves 51 and 52 provided respectively on the steam pipe 34 to the steam turbine facility 30 and the steam pipe 42 to the water production facility 40, and the flow rate adjusting valves 51 and 52 are opened. The steam supply ratio to the steam turbine facility 30 and the water production facility 40 is adjusted by adjusting the degree (the flow rate of the superheated steam i, l is adjusted). As a result, when the power demand is greater than the water demand, the steam supply ratio to the steam turbine facility 30 is increased to increase the amount of power generation. Conversely, when the water demand is large relative to the power demand, The amount of water production can be increased by increasing the steam supply rate to the facility 40.

  The flow rate adjusting valves 51 and 52 of the supply rate adjusting device 50 can block the flow paths of the steam pipes 34 and 42 when fully closed, respectively, and the steam supply rate to the steam turbine equipment 30 (flow rate of superheated steam i). It is also possible to set the steam supply ratio (flow rate of superheated steam l) to the water production facility 40 to 0 (zero). When the flow control valve 52 is fully closed and the total amount of superheated steam g is supplied to the steam turbine equipment 30, the power generation amount is, for example, about 8000 kW. The flow control valve 51 is fully closed and the entire amount of superheated steam g is produced in water. The amount of water produced when supplied to the facility 40 is about 120 kg / s.

  As described above, according to the present embodiment, since the superheated steam g from the steam generation facility 20 can be supplied to the steam turbine facility 30 and the water production facility 40, the supply rate adjusting device 50 determines the supply rate of the superheated steam g. By adjusting, in addition to the energy by the gas turbine equipment 10, the production ratio of energy and water obtained by effectively using the exhaust gas e can be arbitrarily adjusted. Therefore, according to this embodiment, energy and water can be produced flexibly corresponding to each demand.

Here, as a comparative example for the present invention, FIG. 2 shows a circuit diagram schematically representing the entire configuration of a conventional turbine system. Note that parts having the same functions as those shown in FIG. 1 are denoted by the same reference numerals as those in FIG.
This comparative example includes a gas turbine facility 10, a steam generation facility 20, and a water production facility 40. The gas turbine facility 10 drives a generator 14 to generate power. Exhaust gas e from the gas turbine facility 10 is guided to a steam generation facility 20 disposed downstream. The steam generation facility 20 generates superheated steam g using the exhaust gas e as a heat source. The generated superheated steam g is guided to the water production facility 40. In the water production facility 40, pure water n is produced from the raw water m using the superheated steam g as a heat source. The superheated steam g used in the water production facility 40 becomes water o and is recovered by the steam generation facility 20. In this comparative example, in order to use all the exhaust heat of the gas turbine equipment 10 for water production, it is necessary to operate in consideration of both power demand and water demand.

  When the power and water production capacities of the comparative example in the case of rated operation all day are as shown in FIG. 3, when the water demand per day is about half of the capacity of the water production facility 40, It is necessary to perform a rated operation for about half a day (see FIG. 4) or a partial load operation of about 50% over the entire day (see FIG. 5). In general, however, the temperature and pressure of the working medium change greatly when the gas turbine equipment is started and stopped. Therefore, stress due to differential pressure change, thermal stress accompanying temperature change, or stress accompanying thermal deformation occurs in the component parts. Therefore, the operation of repeatedly starting and stopping as shown in FIG. 4 is not preferable from the viewpoint of reliability, and further, the fuel in the starting and stopping process is wasted, and is not preferable from the viewpoint of operation efficiency. On the other hand, the partial load operation as shown in FIG. 5 is less efficient than the rated operation and is not preferable in terms of efficiency, and is also not preferable from the viewpoint of reliability and performance because the temperature and pressure of the working medium fluctuate.

  On the other hand, in this embodiment, since the supply ratio of the generated steam of the steam generation facility 20 can be arbitrarily adjusted between the steam turbine facility 30 and the water production facility 40, the operation of the gas turbine facility 10 can be set as the all-day rated operation. Changes in energy and water demand can be accommodated by adjusting the steam supply ratio to the steam turbine facility 30 and the water production facility 40. For example, when the daily water demand is about half of the capacity of the turbine system of the present embodiment, for example, the gas turbine equipment 10 is operated at rated operation all day, while only the steam turbine equipment 30 is operated during the daytime to generate power. It is possible to operate such that the water production is performed by operating only the water production facility 40 at night (see FIG. 6). In general, power demand is greater during the day than at night, but according to the present embodiment, the point of easy operation as shown in FIG. 6 is a great merit. Further, when switching between the operation of only the steam turbine facility 30 and the operation of only the water production facility 40, it is also possible to operate both at a predetermined rate in parallel for a certain period of time according to demand as shown in FIG. .

  As described above, according to the present embodiment, it is possible to flexibly cope with demands for energy and water. Moreover, once activated, it can respond to a wide range of water demand without starting / stopping or partially loading during the operation, and energy production efficiency is high. For example, when water becomes surplus with respect to demand, it is possible to suspend only the water production facility 40 or perform partial load operation without stopping the gas turbine facility 10 or performing partial load operation. In this case, the surplus energy (surplus steam or high-temperature exhaust gas) due to the suspension or partial load operation of the water production facility is used in the steam turbine facility 30, so that the efficiency of the entire plant is hardly lowered. Thus, since the ratio of power generation and water production can be adjusted while keeping the efficiency of the whole plant high, it is possible to cope with various combinations of electric power demand and water demand. Moreover, since the gas turbine equipment 10 can be rated at all day, changes in the pressure and temperature of the working fluid can be minimized, and the reliability is high.

FIG. 8 is a circuit diagram schematically showing the overall configuration of the turbine system according to the second embodiment of the present invention. 8, parts having the same or similar functions as those in FIG.
As shown in FIG. 8, the turbine system according to this embodiment includes a gas turbine facility 10, first and second steam generation facilities 60 and 20, a steam turbine facility 30, and a water production facility 40. The gas turbine facility 10, the second steam generation facility 20, the steam turbine facility 30, and the water production facility 40 are the same as the gas turbine facility 10, the steam generation facility 20, the steam turbine facility 30, and the water production facility 40 of the first embodiment. Each has the same configuration. In the present embodiment, the first steam generation facility 60 generates steam for the water production facility 40, and the second steam generation facility 20 generates steam to the steam turbine facility 30. The first steam generation facility 60 is a steam facility that can be blown.

  The gas turbine facility 10 is connected to the first steam generation facility 60 via the exhaust gas pipe 19. The first and second steam generation facilities 60 and 20 are connected by an exhaust gas pipe 61. The steam pipe 42 from the first steam generation facility 60 is connected to the water production facility 40, and the return pipeline 43 from the water production facility 40 is connected to the first steam generation facility 60. A flow rate adjustment valve 52 is provided in the return line 43. On the other hand, the second steam generation facility 20 is connected to the steam turbine facility 30 via the steam pipe 34, and the steam turbine facility 30 is connected to the second steam generation facility 20 via the condensate pipes 36 and 25. The steam pipe 34 and the condensate pipe 36 are connected via a bypass pipe 35 having an on-off valve 38 and a cooler 39. Further, an on-off valve 37 is provided at a position downstream of the connection portion of the steam pipe 34 with the bypass pipe 35. The condensate pipe 36 is provided with a flow rate adjustment valve 51 on the upstream side and a condenser 32 on the downstream side with respect to the connection portion with the bypass pipe line 35.

  In the first embodiment, the common steam generation facility 20 is connected to the steam turbine facility 30 and the water production facility 40. However, in this embodiment, the steam generation facility dedicated to the water production facility 40 and the steam turbine facility 30, respectively. 60, 20 are provided. Regarding other configurations, the turbine system of the present embodiment has the same configuration as that of the first embodiment.

  In the turbine system according to the present embodiment having the above-described configuration, first, the compressor 11 sucks the atmosphere a in the gas turbine equipment 10 and compresses it to a predetermined pressure. The intake air flow rate is, for example, about 88 kg / s, and the pressure ratio is about 15. The compressed air b is combusted together with the fuel c in the combustor 12, and the generated high-temperature and high-pressure combustion gas d of, for example, about 1300 ° C. is guided to the turbine 13 to perform expansion work. Part of this expansion work is consumed as the compression power of the compressor 11, and the rest is converted into electric power by the generator 14. In the present embodiment, a power generation amount of about 27000 kW is assumed.

  Exhaust gas e of, for example, about 560 ° C. from the gas turbine facility 10 is led to the first steam generation facility 60 via the exhaust gas pipe 19. The first steam generation facility 60 generates superheated steam l from the feed water p using the exhaust gas e as a heat source. This superheated steam l is guided to the water production facility 40 and used to produce pure water n from raw water m. When the maximum flow rate of the superheated steam l is supplied to the water production facility 40, the production amount of the water n is, for example, about 120 kg / s. The superheated steam l used for water production becomes water o and is returned to the first steam generation facility 60 via the return line 43.

  The exhaust gas q leaving the first steam generation facility 60 is guided to the second steam generation facility 20 via the exhaust gas pipe 61. In the first steam generation facility 20, the superheater 21, the evaporator 22, and the economizer 23 use the heat of the exhaust gas q to generate superheated steam g from the feed water f, and the exhaust gas h from which the heat energy is recovered is Released into the atmosphere. The generated superheated steam g is guided to the steam turbine facility 30 to drive the generator 33 by applying shaft power to the steam turbine 31. When the maximum flow rate of the superheated steam g is supplied to the steam turbine equipment 30, the power generation amount is about 8000 kW, for example. The wet steam j discharged from the work by the steam turbine 31 is converted into water k by the condenser 32 and returned to the second steam generation facility 20.

  For example, consider a case where the daily water demand is about half of the capacity. In this case, for example, assuming an operation schedule in which power is generated during the day and water is produced at night, the steam turbine equipment 30 is operated with the flow rate adjustment valve 51 fully opened and the flow rate adjustment valve 52 is fully closed during the daytime to produce water. The facility 40 is stopped. The open / close state of the open / close valves 37 and 38 at this time is open and closed, respectively. Conversely, at night, the flow rate adjusting valve 51 is fully closed to stop the steam turbine facility 30, and the flow rate adjusting valve 52 is fully opened to operate the water production facility 40. At this time, the on-off valve 37 is fully closed and the on-off valve 38 is fully opened, so that the superheated steam g generated in the second steam generation facility 20 flows into the bypass line 35 from the steam pipe 34 and is cooled by the cooler 39. Then, the water is condensed by the condenser 32 and returned to the second steam generation facility 20. Thereby, overheating of the 2nd steam generation equipment 20 is prevented.

  Also in the present embodiment, steam is generated by the steam generation facilities 60 and 20 due to the exhaust heat of the gas turbine facility 10, and the steam generated in the steam generation facilities 60 and 20 by adjusting the opening of the flow rate adjustment valves 52 and 51, etc. Can be arbitrarily used in the water production facility 40 and the steam turbine facility 30. Therefore, the same effect as in the first embodiment can be obtained.

  In the present embodiment, the water production facility 40 and the steam turbine facility 30 need to be designed so that the state quantity of the superheated steam to be used is a steam condition suitable for each. For example, it is preferable that the pressure and temperature of the superheated steam i used in the steam turbine facility 30 be higher than that of the superheated steam l used in the water production facility 40. Although not shown, the output of the steam turbine facility is further increased by using a multi-pressure steam generating facility for generating a plurality of steams having different pressures and a plurality of steam turbine groups having different working steam pressures. .

FIG. 9 simply shows the overall configuration of such a turbine system according to the third embodiment of the present invention. For the purpose of omitting the description, in FIG. 9, the same reference numerals are given to portions that play the same or similar functions as those in the previous drawings.
As shown in FIG. 9, in the present embodiment, the steam generation facility 20 is a multi-pressure steam generation facility having a known configuration, and a high-pressure steam generation unit having a superheater 21H, an evaporator 22H, and a economizer 23H, An intermediate pressure steam generator having a superheater 21M, an evaporator 22M and a economizer 23M, and a low pressure steam generator having a superheater 21L, an evaporator 22L and an economizer 23L are provided. These high-pressure steam generator, medium-pressure steam generator, and low-pressure steam generator are provided in this order from the upstream along the flow of exhaust gas in the exhaust gas flow path. This is almost the same as the generation unit 20. Moreover, the steam turbine equipment 30 in the present embodiment includes a high-pressure steam turbine 31H, an intermediate-pressure steam turbine 31M, and a low-pressure steam turbine 31L. The intermediate-pressure steam turbine 31M is driven mainly by medium-pressure superheated steam generated by the intermediate-pressure steam generator, and the low-pressure steam turbine 31L is driven mainly by low-pressure superheated steam generated by the low-pressure steam generator.

  The low-pressure steam generation unit is connected to the low-pressure steam turbine 31L and the water production facility 40 via the branch pipe 27, and the steam supply ratio to the low-pressure steam turbine 31L and the water production facility 40 is determined by the flow rate adjusting valves 51 and 52. It can be arbitrarily adjusted by adjusting the opening. The steam that has worked in the low-pressure steam turbine 31L and the water production facility 40 is both converted into water and returned to the low-pressure steam generator. Steam that has been preheated through the economizer 23L of the low-pressure steam generator is supplied to the intermediate-pressure steam generator, and superheated steam generated from this steam is supplied to the intermediate-pressure steam turbine 31M. The steam that has worked in the intermediate-pressure steam turbine 31M is joined to the steam pipe 26 from the low-pressure steam generator and supplied to the low-pressure steam turbine 31L or the water production facility 40. Steam that has been preheated through the economizer 23M of the medium pressure steam generator is supplied to the high pressure steam generator, and superheated steam generated from this steam is supplied to the high pressure steam turbine 31H. Then, the steam that has worked in the high-pressure steam turbine 31H is returned to the most upstream portion in the exhaust gas flow direction of the steam generation unit 20, is overheated again, and is supplied to the intermediate-pressure steam turbine 31M.

  That is, the steam generated in the high-pressure steam generator is used to sequentially drive the intermediate-pressure steam turbine M and the low-pressure steam turbine 31L even after driving the high-pressure steam turbine 31H. The steam generated in the intermediate pressure steam generator is used to drive the low pressure steam turbine 31L after driving the intermediate pressure steam turbine 31M. Other configurations are the same as those of the first embodiment.

  According to this embodiment, the steam turbine and the steam generation facility are configured in multiple stages, so that steam having different pressures is used in the corresponding steam turbine, and finally used in the low-pressure turbine 31L or the water production facility 40. By comprising in this way, in addition to the effect similar to 1st Embodiment, energy efficiency can be improved.

  In addition, in each above embodiment, the case where the exhaust heat of gas turbine equipment was utilized was mentioned as an example, and was demonstrated. However, the steam generation method for driving the water production facility and the steam turbine facility is not limited to this, and the heat source need not be the gas turbine facility. For example, as shown in FIG. 10, a boiler 12B may be used as a heat source. The boiler 12 </ b> B may be an extremely general one that burns the fuel c (coal or other fossil fuel) to generate the exhaust gas e, and supplies the generated exhaust gas e to the steam generation facility 20. Other configurations are the same as those of the first embodiment. Of course, the gas turbine equipment 10 of the second and third embodiments can be replaced with a boiler 12B. In addition to the boiler, it is conceivable to use the nuclear reactor 12N as a heat source as shown in FIG. In the configuration example of FIG. 11, the nuclear reaction heat generated in the nuclear reactor 12N is supplied to the steam generation facility 20 (in this case, not a heat exchanger but a water storage tank), and the water in the steam generation facility 20 is changed to superheated steam. It is supplied to steam turbine equipment and water production equipment. Other configurations are the same as those of the first embodiment. Of course, the reactor 12N and the steam generation facility 20 in this example can also be replaced with the gas turbine facility 10 of the second and third embodiments. In these cases, similar effects can be obtained.

  As described above, the method of generating steam for driving the water production facility and the steam turbine facility is not particularly limited, and is generated by burning combustible materials such as dust in addition to those shown in FIGS. 10 and 11. It is conceivable to generate steam using thermal energy.

  Furthermore, since the turbine system of each of the above embodiments can be constructed if there is a steam generation facility, a steam turbine facility, and a water production facility, it can be easily constructed by adding facilities that are insufficient to an existing plant. It is also a great merit to be able to. In other words, when there is an existing plant that includes a steam generation facility and a water production facility that uses steam from the steam generation facility, a steam turbine facility that obtains rotational power from the steam from the steam generation facility (if necessary) The turbine system of the present invention can be constructed by adding another steam generating facility that generates steam to the steam turbine facility. In addition, an existing plant equipped with a steam generation facility and a steam turbine facility that uses steam from this steam generation facility has a water production facility that uses steam from the steam generation facility (to this water production facility if necessary). It is possible to construct the turbine system of the present invention by adding another steam generating facility that generates the steam.

1 is a circuit diagram schematically illustrating an overall configuration of a turbine system according to a first embodiment of the present invention. It is a circuit diagram which represents simply the whole structure of the conventional turbine system which is a comparative example with respect to this invention. It is a graph showing the electric power and water production capacity at the time of carrying out rated operation all day. It is a graph showing the operation schedule in the case of carrying out the rated operation of the conventional turbine system for about half a day when the daily water demand is about half of the capacity of the water production facility. It is a graph showing the operation schedule in the case of carrying out the partial load operation of about 50% of the conventional turbine system over the whole day when the water demand per day is about half of the capacity of the water production facility. It is a graph showing an example of the driving | running schedule of the turbine system of this invention when the water demand per day is about a half of capacity. It is a graph showing the other example of the driving | running schedule of the turbine system of this invention when the water demand per day is about a half of capacity. It is a circuit diagram showing simply the whole composition of the turbine system concerning a 2nd embodiment of the present invention. It is a circuit diagram showing simply the whole composition of the turbine system concerning a 3rd embodiment of the present invention. It is a circuit diagram showing simply the whole composition of other examples of composition of the turbine system of the present invention. It is a circuit diagram showing simply the whole composition of other examples of composition of the turbine system of the present invention.

Explanation of symbols

10 Gas turbine equipment 12B Boiler 12N Reactor 20 Steam generation equipment (second steam generation equipment)
27 Branch Pipe 28 Branch 30 Steam Turbine Equipment 40 Water Production Equipment 50 Supply Ratio Adjuster 60 First Steam Generation Equipment

Claims (13)

A steam generating facility for generating steam;
A steam turbine facility that obtains rotational power by steam from the steam generation facility;
A turbine system comprising: a water production facility that obtains pure water by distilling raw water using steam from the steam generation facility. A steam generating facility for generating steam;
A steam turbine facility that obtains rotational power by steam from the steam generation facility;
A water production facility that obtains pure water by distilling raw water using steam from the steam generation facility;
A turbine system comprising: a supply ratio adjusting means for adjusting a supply ratio of steam supplied to the steam turbine facility and the water production facility.   3. The turbine system according to claim 2, wherein the supply ratio adjusting means is capable of adjusting a steam supply ratio to the steam turbine equipment and a steam supply ratio to the water production equipment to 0 respectively. Turbine system.   2. The turbine system according to claim 1, further comprising a branch pipe that divides the steam from the steam generation facility at a branch portion and supplies the steam to the steam turbine facility and the water production facility, respectively. Turbine system.   The turbine system according to claim 1, comprising: the steam generation facility that generates steam to the steam turbine facility; and the steam generation facility that generates steam for water production facilities. .   The turbine system according to claim 1, further comprising a gas turbine facility that supplies exhaust heat to the steam generation facility as a heat source.   The turbine system according to any one of claims 1 to 5, comprising a boiler that generates steam by using combustion heat of fuel as a heat source.   The turbine system according to any one of claims 1 to 5, further comprising, as a heat source, a nuclear reactor that generates steam using heat generated by nuclear power.   The turbine system according to any one of claims 1 to 8, further comprising the steam turbine facility that converts superheated steam or saturated steam generated by the steam generating facility into wet steam during expansion work. Turbine system. In a plant equipped with a steam generation facility that generates steam and a water production facility that obtains pure water by distilling raw water using the steam from this steam generation facility,
A method for constructing a turbine system, comprising: adding a steam turbine facility for obtaining rotational power by steam from the steam generation facility. In a plant equipped with a steam generation facility that generates steam and a water production facility that obtains pure water by distilling raw water using the steam from this steam generation facility,
A steam turbine facility for obtaining rotational power by steam from the steam generating facility;
A method for constructing a turbine system, comprising adding another steam generation facility for generating steam to the steam turbine facility. In a plant equipped with a steam generation facility for generating steam and a steam turbine facility for obtaining rotational power by the steam from the steam generation facility,
A method for constructing a turbine system, comprising adding a water production facility for obtaining pure water by distilling raw water using steam from the steam generation facility. In a plant equipped with a steam generation facility for generating steam and a steam turbine facility for obtaining rotational power by the steam from the steam generation facility,
A water production facility that obtains pure water by distilling raw water using steam from the steam generation facility;
A turbine system construction method comprising: adding another steam generation facility for generating steam to the water production facility.

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