This application is based upon and claims the benefit of priority from the prior Japanese Patent Application No. 2003-63723 filed on Mar. 10, 2003;
the entire contents of which are incorporated herein by reference.
The present invention relates to steam turbine plant.
More specifically, the invention relates to steam turbine plant for power generation, which is provided with a feedwater heater in a steam condenser.
A steam turbine plant includes steam generator, high pressure turbine, a plurality of low pressure turbines. The steam turbine plant further includes a plurality of steam condensers which condense steam from the plurality of low pressure turbines and a plurality of low pressure feedwater heaters which are provided within the steam condensers as the structural elements respectively. A feedwater heater which is provided within a steam condenser is also called as a neck heater, since the feedwater heater is installed at an upper (neck) portion of the steam condenser. The low pressure feedwater heaters constitute a plurality of feedwater heating lines which are arranged and connected in parallel. The steam turbine plant has a plurality of high pressure feedwater heaters which heat a feedwater from the low pressure feedwater heaters by steam bled from the high pressure turbine. Each of the steam condensers are connected to each of adjacent steam condensers by a connection shell. The steam condensers, the feedwater heating lines which are provided with the low pressure feedwater heaters arranged and connected in parallel, the high pressure feedwater heaters and steam generator are connected in series by feedwater line.
The low pressure feedwater heaters use bled steam from low pressure turbines as a heating source of the feedwater.
Generally, tiers of low pressure feedwater heaters arranged in series in the feedwater heating lines increase, the amount of heat exchanged in the low pressure feedwater heater also increases, which may contribute to high efficiency in view of thermal or plant efficiency. Moreover, when the low pressure feedwater heaters are installed inside of the steam condensers to save space of the steam turbine plant, it is desirable to reduce pressure drop of the steam discharged from the low pressure turbines and flowing around the low pressure feedwater heaters. For this reason, a neck heater type of structure is adopted for the steam condensers of conventional steam turbine plant. The neck heater type of structure is that the low pressure feedwater heaters are installed and arranged inside of the steam condensers at neck portions, which are a space above a portion where the steam discharged from the low pressure turbines condenses in the steam condensers.
Therefore, in conventional steam turbine plant, which includes n units of casings, n units of low pressure turbines and n units of steam condensers, constitute n pieces of the feedwater heating lines inserted in series to the feedwater line respectively. Each of the feedwater heating lines has a same number of the low pressure feedwater heaters, which are connected in series, inside of the steam condensers. The same numbers of the low pressure feedwater heaters are arranged in each of the steam condensers. Additionally, since each of the steam condensers are connected to the adjacent steam condenser by connection shell, differences of pressure distribution among the steam condensers are mitigated.
Nevertheless, since each of the low pressure feedwater heaters are connected with the bleeding lines, which extend from the casings of the low pressure turbines as a heating source, space of the neck portion of the steam condensers is relatively small. Especially, the bleeding lines have a large diameter for the low pressure feedwater heaters, which are provided at an upstream side of the feedwater heating lines, because the feedwater heaters at an upstream side of the feedwater heating lines employs the steam bled from a downstream side of the low pressure turbines as the heating source. This causes difficulty in planning such a steam turbine plant, especially in designing an arrangement of bleeding lines, feedwater heating lines or supports of these bleeding lines or low pressure feedwater heater at the neck portions. And it may result in necessity of further internal structure inside the steam condensers. This may cause necessity of enlarging space for the plant itself. And it may cause not only increase of costs but also pressure drop of the steam flowing inside of the steam condensers, which may effects reduction of the plant efficiency.
From a viewpoint of the feedwater, the feedwater line has feedwater heating lines whose number is the same as the steam condensers and which are arranged in parallel in conventional steam turbine plant. However, in order to avoid unbalance of the feedwater among the feedwater heating lines, it is desirable to provide less numbers of feedwater heating lines, which may contribute to increasing redundancies of controls of the steam turbine plant, especially for nuclear power plant.
Accordingly, an advantage of an aspect of the present invention is to provide a steam turbine plant which has less internal structure, e.g. The low pressure feedwater heaters, bleeding lines or so on, inside the steam condensers.
To achieve the above advantage, one aspect of the present invention is to provide a steam turbine plant that comprises a steam generator, a plurality of low pressure turbines being driven by steam from the steam generator, a plurality of steam condensers to condense the steam from the low pressure turbines into condensed water, a feedwater line which supplies the condensed water to the steam generator as feedwater, the feedwater line including a plurality of feedwater heating lines connected in parallel, a number of feedwater heating lines being less than a number of steam condensers, and a plurality of low pressure feedwater heaters, wherein each of the feedwater heating lines includes at least one low pressure feedwater heater provided in at least one of the steam condensers to heat the condensed water by steam bled from the low pressure turbines.
Another aspect of the present invention is to provide a steam turbine plant that comprises a steam generator, a plurality of low pressure turbines being driven by steam from the steam generator, a plurality of steam condensers to condense the steam from the low pressure turbines into condensed water, a feedwater line which supplies the condensed water to the steam generator as feedwater, the feedwater line including a plurality of first feedwater heating lines connected in parallel and a plurality of second feedwater heating lines connected in parallel and coupled to the downstream side of the first feedwater heating lines, a first number of first feedwater heating lines being different than a second number of second feedwater heating lines, and a plurality of low pressure feedwater heaters, wherein each of the first and second feedwater heating lines includes at least one low pressure feedwater heater provided in at least one of the steam condensers to heat the condensed water by steam bled from the low pressure turbines.
Another aspect of the present invention is to provide a steam turbine plant that comprises a steam generator, a plurality of low pressure turbines being driven by steam from the steam generator, a plurality of steam condensers to condense the steam from the low pressure turbines into condensed water, a feedwater line which supplies the condensed water to the steam generator as feedwater, the feedwater line including a plurality of feedwater heating lines connected in parallel and a plurality of low pressure feedwater heaters, wherein each of the feedwater heating lines includes at least one low pressure feedwater heater provided in at least one of the steam condensers to heat the condensed water by steam bled from the low pressure turbines, and wherein a first number of low pressure feedwater heaters provided in a first steam condenser is different than a second number of low pressure feedwater heaters provided in a second steam condenser.
In accordance with the aspect of the present invention, feedwater heating lines provided inside of the steam condensers are reduced so that space efficiency inside the steam condensers are improved and that the costs for a construction of the steam turbine plant are also reduced.
First embodiment in accordance with the present invention will be explained with reference to
Steam generator 1, which is connected with a heating source (not shown), for example nuclear reactor or boiler, generates steam. The steam passes through high pressure turbine 2 and steam line 9, then lead to a plurality of casings 12a, 12b, 12c, . . . and 12n of low pressure turbines 3a, 3b, 3c, . . . and 3n. Generally, the number of low pressure turbines 3a, 3b, 3c, . . . and 3n are more than or equal to three (3). Each of low pressure turbines 3a, 3b, 3c, . . . and 3n are installed in casings 12a, 12b, 12c, . . . and 12n, whose number is also the same as the number of low pressure turbines 3a, 3b, 3c, . . . and 3n. The steam led to each of the casings 12a, 12b, 12c, . . . and 12n drives each of low pressure turbines 3a, 3b, 3c, . . . and 3n. The steam is then discharged from low pressure turbines 3a, 3b, 3c, . . . and 3n to each of steam condensers 4a, 4b, 4c, . . . and 4n as discharged steam. Each of steam condensers 4a, 4b, 4c, . . . and 4n are placed beneath each of low pressure turbines 3a, 3b, 3c, . . . and 3n and are connected with each of the casings 12a, 12b, 12c, . . . and 12n. Each of the steam condensers 4a, 4b, 4c, . . . and 4n are connected to each of adjacent steam condensers 4a, 4b, 4c, . . . and 4n by a connection shell 11. In steam condensers 4a, 4b, 4c, . . . and 4n, the discharged steam is cooled down and condenses into water as a condensed water (condensate). The condensed water (condensate) is gathered and led to feedwater line 8. In feedwater line 8, condensate pump 5 (pressurizer) give pressure to the condensed water (condensate) as a feedwater. The feedwater is led to low pressure feedwater heaters 6a, 6b, 6c, . . . and 6(n-1) and is heated up. The feedwater, after heated up in low pressure feedwater heaters 6a, 6b, 6c, . . . and 6(n-1), is further pumped up by feedwater pump 20 (pressurizer) as a high pressure feedwater pump. The feedwater pumped up to high pressure by feedwater pump 20 (pressurizer) then led to high pressure feedwater heaters 7a and 7b in feedwater line 8. In high pressure feedwater heaters 7a and 7b, the feedwater is further heated up and then supply to steam generator 1 from feedwater line 8. In this manner, the steam turbine plant constitutes closed-loop as a Rankine Cycle.
Bled steam for low pressure feedwater heaters 6a, 6b, 6c, . . . and 6(n-1) is taken out from the middle of low pressure turbines 3a, 3b, 3c, . . . and 3n. The bled steam is led to bleeding lines 10a, 10b, 10c, . . . and 10(n-1) as bleeding steam lines from an opening provided in the casings 12a, 12b, 12c, . . . and 12(n-1) of low pressure turbines 3a, 3b, 3c, . . . and 3(n-1). Each of bleeding lines 10a, 10b, 10c, . . . and 10(n-1) are connected to each of feedwater heaters 6a, 6b, 6c, . . . and 6(n-1) High pressure feedwater heaters 7a and 7b are employ bled steam from high pressure turbine 2 or from steam line 9 as a heating source (not shown).
Low pressure feedwater heaters 6a, 6b, 6c, . . . and 6(n-1) are shell and tube type heat exchangers. The shell and tube type heat exchangers are constituted by a shell and a plurality of tubes arranged inside the shell. Feedwater is passed through the tubes and exchanging heat, while the steam for heating is led to a shell side of the shell and tube type heat exchanger.
Low pressure feedwater heaters 6a, 6b, 6c, . . . and 6(n-1) are installed inside a neck portion of steam condensers 4a, 4b, 4c, . . . and 4(n-1) to improve a space efficiency. The neck portion is a space above a portion where the steam that passed through low pressure turbines 3a, 3b, 3c, . . . and 3n condenses in each of steam condensers 4a, 4b, 4c, . . . and 4n. Thus, low pressure feedwater heaters 6a, 6b, 6c, . . . and 6(n-1) are arranged inside the space of steam condensers 4a, 4b, 4c, . . . and 4(n-1).
Steam condensers 4a, 4b, 4c, and 4n are closely arranged each other. (n-1) units of low pressure feedwater heaters 6a, 6b, 6c, . . . and 6(n-1) are provided inside steam condensers 4a, 4b, 4c, . . . and 4(n-1). Feedwater line 8 includes a plurality of feedwater heating lines 6A, 6B, 6C, . . . and 6(N-1). Each of the feedwater heating lines 6A, 6B, 6C, . . . and 6(N-1) has one of low pressure feedwater heaters 6a, 6b, 6c, . . . 6(n-1) respectively. Low pressure feedwater heaters 6a, 6b, 6c, . . . 6(n-1) are arranged and connected in parallel inside of steam condensers 4a, 4b, 4c, . . . and 4n. Feedwater heating lines 6A, 6B, 6C, . . . and 6(N-1) are provided between condensate pump 5 (pressurizer) and high pressure feedwater pump 20 (pressurizer) in feedwater line 8. Feedwater lines 8 includes feed water heating lines 6A, 6B, 6C, . . . and 6(N-1) as a constituent elements. Feedwater heating lines 6A, 6B, 6C and 6N are seriesly inserted in feedwater line 8 as a whole.
Each of feedwater heating lines 6A, 6B, 6C, . . . and 6(N-1) may have a plurality of low pressure feedwater heaters arranged and connected in series. In this case, all of steam condensers 4a, 4b, 4c, . . . and 4n may have at least one of low pressure feedwater heaters, and the number of the low pressure feedwater heaters may be greater than the number of steam condensers 4a, 4b, 4c, . . . and 4n. There is a less number of the feedwater heating lines, which are connected in parallel and inserted in series in feedwater line 8, than the number of steam condensers 4a, 4b, 4c, . . . and 4n. The number of the feedwater heating lines may be one (1) or more, but is less than the number of steam condensers 4a, 4b, 4c, . . . and 4n. Bleeding steam lines 10a, 10b, 10c, and 10(n-1) may be connected to any of casings 12a, 12b, 12c, and 12n of low pressure turbines 3a, 3b, 3c, . . . and 3n.
According to this embodiment, the number of the low pressure feedwater heaters disposed inside of steam condenser 4a, 4b, 4c, . . . and 4n are lessened compared with a conventional steam turbine plant. In order to keep the amount of heat exchanged in the low pressure feedwater heaters at a preferable level, each of low pressure feedwater heaters 6a, 6b, 6c, . . . and 6(n-1) may be enlarged in size to increase the amount of heat. However, internal structures, such as bleeding lines, of steam condensers 4a, 4b, 4c, . . . and 4n maybe lessened to improve pressure drop of the steam inside steam condensers 4a, 4b, 4c, . . . and 4n. And the size of steam condensers 4a, 4b, 4c, . . . and 4n may be reduced.
Some detailed configurations of the first embodiment having three (3) units of the low pressure turbines, the casings and the steam condensers are explained below with reference of
As described in
Steam condenser 4a accommodates low pressure feedwater heaters 6a1, 6a2 and 6a3 as neck heaters. Steam condenser 4b accommodates low pressure feedwater heaters 6a4 and 6b4 as neck heaters. Steam condenser 4c accommodates low pressure feedwater heaters 6b1, 6b2 and 6b3 as neck heaters. Feedwater heating lines 6A and 6b are merged into one at an upstream side of high pressure feedwater pump 20 in feedwater line 8.
The feedwater, from steam condensers 4a, 4b and 4c, is divided into two flows and is led to each of feedwater heating lines 6A and 6B. In feedwater heating line 6A, The temperature of the feedwater rises as the feedwater flow through low pressure feedwater heaters 6a1, 6a2, 6a3 and 6a4 in this order. In the same manner, the temperature of the feedwater rises as the feedwater flows through low pressure feedwater heaters 6b1, 6b2, 6b3 and 6b4 in this order in feedwater heating line 6B. As a heating source, steam bled from low pressure steam turbine 3a, 3b and 3c are introduced to low pressure feedwater heater 6a1 to 6a4 and 6b1 to 6b4. Connections of bleeding lines are explained with reference to
Since four (4) low pressure feedwater heaters 6a1 to 6a4 and 6b1 to 6b4 are connected in series respectively in each of feedwater heating lines 6A and 6B, four (4) different conditions of bled steam is used for each of tiers of low pressure feedwater heaters 6a1 and 6b1, 6a2 and 6b2, 6a3 and 6b3, 6a4 and 6b4 as the heating source. As mentioned above, bled steam, as the heating source, is taken out (bled) from low pressure turbines 3a, 3b and 3c. As shown in
Bleeding lines 10a1 to 10a4 and 10b1 to 10b4 are connected to low pressure feedwater heater 6a1 to 6a4 and 6b1 to 6b4 respectively. More precisely, openings 13a are connected to low pressure feedwater heaters 6a1 and 6b1 by bleeding lines 10a1, openings 13b are connected to low pressure feedwater heaters 6a2 and 6b2 by bleeding lines 10a2, openings 13c are connected to low pressure feedwater heaters 6a3 and 6b3 by bleeding lines 10a3, and openings 13d are connected to low pressure feedwater heaters 6a4 and 6b4 by bleeding lines 10a4. Bleeding lines 10a1 to 10a4 and 10b1 to 10b4 may pass through connection shells 11. The connections of bleeding lines 10a1 to 10a4 may be determined suitably provided that the conditions, such as the temperature or the pressure, of bled steam supplied to each of low pressure feedwater heater 6a1 to 6a4 and 6b1 to 6b4 are determined appropriately.
As shown in
In
As shown in
The number of the casings of steam turbine 3a, 3b and 3c is also three (3). Each of the casings is connected with each of steam condensers 4a, 4b and 4c respectively. As is the same manner with
Steam condenser 4a accommodates low pressure feedwater heaters 6a2, 6a3 and 6a4 as neck heaters. Steam condenser 4b accommodates low pressure feedwater heaters 6a1 and 6b4 as neck heaters. Steam condenser 4c accommodates low pressure feedwater heaters 6b1, 6b2 and 6b3 as neck heaters. Feedwater heating lines 6A and 6b are merged into one line at an upstream side of high pressure feedwater pump 20 in feedwater line 8.
According to this configuration, total amount of the low pressure feedwater heaters may be also lessened compared to the conventional steam turbine plant. It may contribute to improve pressure drop inside the steam condensers 4a, 4b and 4c, to reduce internal constructions or the size of steam condensers 4a, 4b and 4c itself.
The number of the casings of steam turbine 3a, 3b and 3c is also three (3). Each of the casings is connected with each of steam condensers 4a, 4b and 4c respectively. As is the same manner with
Steam condenser 4a accommodates low pressure feedwater heaters 6a1, 6a2, 6a3 and 6a4 as neck heaters. Steam condenser 4b accommodates low pressure feedwater heaters 6b1, 6b2, 6b3 and 6b4 as neck heaters. Steam condenser 4c is free of any low pressure feedwater heater 6a1 to 6a4 and 6b1 to 6b4. Feedwater heating lines 6A and 6b are merged into one at an upstream side of high pressure feedwater pump 20 in feedwater line 8.
According to this configuration, total amount of the low pressure feedwater heaters may be also lessened compared to the conventional steam turbine plant. It may contribute to improve pressure drop inside the steam condensers 4a, 4b and 4c, to reduce internal constructions or the size of steam condensers 4a, 4b and 4c itself. Furthermore, an arrangement of low pressure feedwater heaters 6a1 to 6a4 and 6b1 to 6b4 inside of steam condenser 4a and 4b may be substantially the same.
This configuration is a modification of the configuration shown in
This configuration is a modification of the configuration shown in
According to this configuration, the dual heater itself may be larger than a single low pressure feedwater heater, such as low pressure feedwater heater 6b1 or 6b4, still the dual heater is smaller size when compared to two (2) of the low pressure feedwater heaters arranged and connected separately. Therefore, it may improve a space efficiency inside steam condensers 4a, 4b and 4c or it may reduce a size or inner structures of steam condensers 4a, 4b and 4c. And it may also improve the pressure drop inside the steam condensers 4a, 4b and 4c. As the dual heater, two of low pressure feedwater heaters 6a1 to 6a4 and 6b1 to 6b4 may be selected in suitable way. The steam condenser which is provided with the dual heater may also be determined suitably.
This configuration is a modification of the example shown in
According to configuration, since arrangements of low pressure feedwater heater 6a1 to 6a4 and 6b1 to 6b4 are the same, pressure drop of inside steam condensers 4a and 4b are almost the same. This may improve simplicity of designing the insides of steam condensers 4a and 4b.
This configuration is a modification of the configuration shown in
According to configuration, the space efficiency inside of steam condensers 4a, 4b and 4c are improved because of use of the dual heater. Furthermore, since arrangements of low pressure feedwater heater 6a1 to 6a3 and 6b1 to 6b3 may be the same in each of steam condensers 4a and 4c, pressure drop of inside steam condensers 4a and 4c are almost the same. This may improve simplicity of designing inside of steam condensers 4a and 4c.
This configuration is a modification of the example shown in
According to this configuration, one of steam condensers 4a, 4b and 4c has high pressure feedwater heaters 7a1, 7a2 and 7b1, 7b2 instead of the low pressure feedwater heaters 6a1 to 6a4 or 6b1 to 6b4. This configuration may reduce a size of the steam turbine plant itself, since it is not usual for a conventional steam turbine plant to arrange high pressure feedwater heaters 7a and 7b inside steam condensers 4a, 4b and 4c as neck heaters. Steam condenser 4a, which is provided with the high pressure feedwater heater may be determined in suitable way. In other words, it may be steam condenser 4b or 4c.
Second embodiment in accordance with the present invention will be explained with reference to
As is the same manner with the first embodiment shown in
Bled steam for low pressure feedwater heaters 6a1, 6b1, 6c1, . . . 6n1 and 6a2, 6b2, 6c2, . . . 6(n-1)2 is taken out from the middle of low pressure turbines 3a, 3b, 3c, . . . and 3n as the same manner with the first embodiment. The bled steam is led to the bleeding lines (not shown) and is supplied to low pressure feedwater heaters 6a1, 6b1, 6c1, . . . 6n1 and 6a2, 6b2, 6c2, . . . 6(n-1)2.
Low pressure feedwater heaters 6a1, 6b1, 6c1, . . . 6n1 and 6a2, 6b2, 6c2, . . . 6(n-1)2 are installed inside of neck portions of steam condensers 4a, 4b, 4c, . . . and 4n to improve a space efficiency.
Steam condensers 4a, 4b, 4c, and 4n are closely arranged each other. N units of low pressure feedwater heaters 6a1, 6b1, 6c1, . . . and 6n1 are provided inside steam condensers 4a, 4b, 4c, . . . and 4n. (n-1) units of low pressure feedwater heaters 6a2, 6b2, 6c2, . . . and 6(n-1)2 are provided inside steam condensers 4a, 4b, 4c, . . . and 4(n-1). Feedwater line 8 includes a plurality of first feed water heating lines 61A, 61B, 61C, . . . and 61N. Each of first feed water heating lines 61A, 61B, 61C, . . . and 61N has one of low pressure feedwater heaters 6a1, 6b1, 6c1, . . . 6n1 respectively. Low pressure feedwater heaters 6a1, 6b1, 6c1, . . . 6n1 are arranged and connected in parallel inside of steam condensers 4a, 4b, 4c, . . . and 4n. First feedwater heating lines 61A, 61B, 61C, . . . and 61N are provided between condensate pump 5 (pressurizer) and high pressure feedwater pump 20 (pressurizer) in feedwater line 8.
Feedwater line 8 further includes a plurality of second feed water heating lines 62A, 62B, 62C, . . . and 62(N-1) at a downstream side of first feedwater heating lines 61A, 61B, 61C, . . . and 61N. Each of second feed water heating lines 62A, 62B, 62C, . . . and 62(N-1) has one of low pressure feedwater heaters 6a2, 6b2, 6c2, . . . 6(n-1)2 respectively. Low pressure feedwater heaters 6a2, 6b2, 6c2, . . . 6(n-1)2 are arranged and connected in parallel inside of steam condensers 4a, 4b, 4c, and 4(n-1). Second feedwater heating lines 62A, 62B, 62C, . . . and 62(N-1) are connected in parallel and inserted in series at a downstream side of first feedwater heating lines 61A, 61B, 61C, . . . and 61N in feedwater line 8.
Thus, feedwater lines 8 includes first feed water heating lines 61A, 61B, 61C, . . . and 61N and second feed water heating lines 62A, 62B, 62C, . . . and 62(N-1) as a constituent elements. First feedwater heating lines 61A, 61B, 61C and 61N as a whole are seriesly inserted in feedwater line 8. Second feedwater heating lines 62A, 62B, 62C, . . . and 62(N-1), whose number is less than the number of first feedwater heating lines 61A, 61B, 61C, . . . and 61N, are coupled to a downstream side of first feedwater heating lines 61A, 61B, 61C, . . . and 61N and are seriesly inserted in feedwater line 8 as a whole.
Each of second feedwater heating lines 62A, 62B, 62C, . . . and 62(N-1) may have a plurality of low pressure feedwater heaters arranged and connected in series. In this case, all of steam condensers 4a, 4b, 4c, . . . and 4n may have at least one of low pressure feedwater heaters, and the number of the low pressure feedwater heaters may be greater than the number of steam condensers 4a, 4b, 4c, . . . and 4n. Still there is a less number of the second feedwater heating lines than the number of steam condensers 4a, 4b, 4c, . . . and 4n. The number of the feedwater heating lines may be one (1) or more, but is less than the number of steam condensers 4a, 4b, 4c, . . . and 4n. The bleeding steam lines may be connected to any of casings 12a, 12b, 12c, and 12n of low pressure turbines 3a, 3b, 3c, . . . and 3n as the same manner with the first embodiment.
According to this embodiment, the number of the low pressure feedwater heaters disposed inside of steam condenser 4a, 4b, 4c, . . . and 4n are lessened compared with a conventional steam turbine plant. In order to keep the amount of heat exchanged in the low pressure feedwater heaters at a preferable level, each of low pressure feedwater heaters 6a, 6b, 6c, . . . and 6(n-1) may be enlarged in size to increase the amount of heat. However, internal structures, such as the bleeding lines, of steam condensers 4a, 4b, 4c, . . . and 4n may be lessened to improve pressure drop of the steam inside steam condensers 4a, 4b, 4c, . . . and 4n. And the size of steam condensers 4a, 4b, 4c, . . . and 4n may be reduced.
Some detailed configurations of the second embodiment having three (3) units of the low pressure turbines, the casings and the steam condensers are explained below with reference of
As described in
Low pressure feedwater heaters 6a1, 6b1 and 6c1 are connected in series in each of first feedwater heating lines 6A, 6B and 6C respectively. Low pressure feedwater heater 6a2 to 6a4 are connected in series in second feedwater heating line 62A, while low pressure feedwater heaters 6b2 to 6b4 are connected in series in second feedwater heating line 62B. Low pressure feedwater heaters 6a1 to 6a4 and 6b1 to 6b4 are neck heaters, which are disposed inside of steam condensers 4a, 4b and 4c. Each three (3) of low pressure feedwater heaters 6a2 to 6a4 and 6b2 to 6b4, which are connected in series in either of second feedwater heating lines 62A or 62B, are dispersed in two (2) of steam condensers 4a, 4b and 4c.
Steam condenser 4a accommodates low pressure feedwater heaters 6a1, 6a2 and 6a3 as neck heaters. Steam condenser 4b accommodates low pressure feedwater heaters 6a4, 6b1 and 6b4 as neck heaters. Steam condenser 4c accommodates low pressure feedwater heaters 6c1, 6b2 and 6b3 as neck heaters. Feedwater heating lines 6A and 6b are merged into one at an upstream side of high pressure feedwater pump 20 in feedwater line 8.
The feedwater, from first feedwater heating lines 61A, 61B and 61C, is divided into two flows and is led to each of feedwater heating lines 62A and 62B. In feedwater heating line 62A, The temperature of the feedwater rises as the feedwater flow through low pressure feedwater heaters 6a2, 6a3 and 6a4 in this order. In the same manner, the temperature of the feedwater rises as the feedwater flows through low pressure feedwater heaters 6b2, 6b3 and 6b4 in this order in feedwater heating line 62B. As a heating source, steam bled from low pressure steam turbine 3a, 3b and 3c may be introduced to low pressure feedwater heater 6a1 to 6a4 and 6b1 to 6b4 as the same manner shown in
This configuration is a modification of the configuration shown in
According to this configuration, the space efficiency inside of steam condensers 4a, 4b and 4c are improved because of use of the dual heater. Furthermore, since arrangements of low pressure feedwater heater 6a1 to 6a3 and 6b1 to 6b3 may be the same in each of steam condensers 4a and 4c, pressure drop of inside steam condensers 4a and 4c are almost the same. This may improve simplicity of designing the insides of steam condensers 4a and 4c.
Other embodiments of the present invention will be apparent to those skilled in the art from consideration of the specification and practice of the invention disclosed herein. It is intended that the specification and example embodiments be considered as exemplary only, with a true scope and spirit of the invention being indicated by the following.
Number | Date | Country | Kind |
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2003-063723 | Mar 2003 | JP | national |
Number | Name | Date | Kind |
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3878273 | Anderson | Apr 1975 | A |
4417446 | Nakamoto et al. | Nov 1983 | A |
4421068 | Aral | Dec 1983 | A |
4489563 | Kalina | Dec 1984 | A |
5860279 | Bronicki et al. | Jan 1999 | A |
6644030 | Moss et al. | Nov 2003 | B1 |
Number | Date | Country | |
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20040177614 A1 | Sep 2004 | US |