JP2005248826A - Power generation/distillation compound plant and method for operating same - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a power generation/distillation compound plant capable of widely coping with changes in power generation demand and distillation demand with the minimum facility capacity, and a method for operating the same. <P>SOLUTION: In the power generation distillation compound plant provided with a steam turbine 1 supplied with steam from steam supply facilities 21 and driving a generator, distillation facilities 2 manufacturing fresh water from sea water by exhaust gas from the steam turbine 1, an emergency damp condenser 3 acquiring surplus steam from the steam turbine 1, and a condensed water header 4 collecting condensed water created in the distillation facilities 2 and condensed water created in the emergency damp condenser 3, and supplying water to a water supply tank 5 of a deaerator provided on the steam supply facilities 21 from the condensed water header 4, the emergency damp condenser 3 is provided with a make up water system 9, a hot well level meter 8 and a hot well level regulator 6, the water supply tank 5 of the deaerator is provided with a level meter 10 and a level regulator 7, and the condensed water header 4 is provided with a pressure gage 11 and a blow line 12. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

  The present invention relates to a power generation / desalination complex plant that produces fresh water together with electric power and an operation method thereof.

  A power generation / desalination complex plant is installed as a facility for supplying fresh water together with electric power in remote islands. In the power generation / desalination complex plant, the exhaust steam after being used for power generation by the steam turbine is used as a heat source for evaporating seawater in the desalination facility, and the steam after being used as a heat source in the desalination is condensate. Then, it is supplied again to the boiler of the steam turbine (see Patent Document 1 below).

  The amount of exhaust steam from the steam turbine is substantially proportional to the power generation output of the steam turbine determined by the power generation demand (power generation requirement), while the amount of steam consumed on the water production side is substantially proportional to the water production demand (water production requirement). Since each demand (required amount) is independent from each other, it is possible to deal with a wide range of operating conditions by installing a buffer such as a dump condenser that can adjust the difference in the required amount of steam.

  For example, when the fresh water demand is lower than the power generation demand, surplus steam is generated, and the surplus steam is sent to the dump condenser. On the other hand, when the desalination demand is higher, the amount of steam flowing into the dump condenser decreases, and when both coincide, the steam flow rate flowing into the dump condenser becomes zero. Furthermore, in a plant in which a bypass system for supplying steam without going through a steam turbine is installed, operation corresponding to a higher fresh water generation demand is possible as compared with a power generation demand.

The operation of such a power generation / desalination plant will be described below.
Condensate flow control of the power generation desalination plant controls the hot well level of the desalination facility, while the dump condenser also performs hot well level control in the same way, condensate from the desalination facility and condensate from the dump capacitor. Are combined at the condensate header and led to a boiler deaerator water supply tank that supplies steam to the steam turbine.

Since fresh water generation facilities always have system leaks, make-up (new water injection) is always required for the system. In the deaerator water supply tank, level control is performed by balancing this make-up (water injection) flow rate and blow flow rate. When the level drops, make-up is performed, and when the level rises, blow-off is performed. Control makeup flow throughout the plant. The inlet valve of the deaerator is used for pressure control of the condensate header.
Japanese Patent Laid-Open No. 10-47015

  In the conventional power generation / desalination complex plant described above, when the operating state changes and the system leak flow rate changes, the condensate header pressure fluctuates. The controllability is particularly bad when the plant is large because the time constant until the makeup water made up by the deaerator and made up by the deaerator returns to the condensate header is large.

  In addition, when an ejector is used to make the dump condenser negative pressure, condensate is usually used as a cooling source for the ejector steam, but the condensate temperature of the freshwater generation facility is high in the power generation and desalination complex plant. Therefore, the temperature of the condensate header becomes 100 ° C. or higher, whereas, both for dump condenser outlet condensate flow that varies greatly depending on the operating condition is not suitable as a cooling source.

  Furthermore, in a plant where multiple boilers are installed and a system that bypasses the steam turbine and feeds steam to the desalination facility, the power generation demand is small compared to the desalination demand. Therefore, it is possible to operate the plant with higher thermal efficiency by reducing the number of boilers used, while using a bypass system to secure the steam flow required for fresh water generation. It can be operated by supplying steam to the freshwater production facility.

  At this time, the cooling water must have a flow rate proportional to the bypass steam flow rate. However, when this cooling water is discharged from the boiler feed pump or extracted from the middle stage, the number of boiler operations is temporarily reduced from five to three. When the number of operating boiler feed pumps decreases, the amount of cooling water that needs to be pumped out per pump increases 5/3 times, and the capacity of the boiler feed pump needs to be increased.

  The present invention has been made to solve the above-described problems, and provides a power generation / desalination complex plant capable of widely responding to changes in power generation demand and water generation demand with a minimum facility capacity and an operation method thereof. For the purpose.

  In order to achieve the above-mentioned object, the invention of claim 1 is a fresh water production system for producing fresh water by evaporating seawater by exhaust gas from a steam turbine that is supplied with steam from a steam supply facility to drive a generator, and exhausted from the steam turbine. Equipment, a dump condenser that takes in surplus steam from the steam turbine, a condensate generated in the desalination equipment, and a condensate header that collects condensate generated in the dump condenser, from the condensate header In the power generation / desalination complex plant configured to supply water to a water supply tank of a deaerator provided in the steam supply facility, the dump condenser includes a makeup water system, a hot well level meter, and a hot well level control valve, The deaerator water tank has a level meter and a level control valve, and the condensate header has a pressure gauge and a blow line.

  According to a second aspect of the present invention, in the power generation / desalination complex plant according to the first aspect, when the hot well level of the dump capacitor is different from a set value, the hot well level is set by opening and closing the hot well level control valve. When the pressure of the condensate header is reduced, make-up is performed from the make-up water system to the hot well of the dump condenser, and when the pressure of the condensate header is higher than a specified value, the system is connected to the blow line. The header pressure is lowered to a specified value by blowing condensate outside, and the inlet valve of the deaerator water tank is connected to the tank of the water tank regardless of the hot well level of the dump condenser and the pressure of the condensate header. A method of controlling so as to keep the level constant.

  The invention of claim 3 includes a steam turbine that is supplied with steam from a steam supply facility to drive a generator, a fresh water production facility that produces fresh water by evaporating seawater by exhaust of the steam turbine, A dump condenser that takes in surplus steam, a condensate generated in the fresh water generation facility, and a condensate header that collects condensate generated in the dump condenser, and is provided from the condensate header to the steam supply facility. In a power generation / desalination complex plant configured to supply water to a water tank of a deaerator, the power generation / desalination complex plant includes an ejector that negatively sets the internal pressure of the dump condenser, and serves as a cooling source of working steam of the ejector at an outlet of the dump condenser The minimum flow system of the connected condensate pump is used.

  According to a fourth aspect of the present invention, there is provided a steam turbine that is supplied with steam from a steam supply facility to drive a generator, a fresh water production facility that produces fresh water by evaporating seawater by exhaust of the steam turbine, A dump condenser that takes in surplus steam, a condensate generated in the fresh water generation facility, and a condensate header that collects condensate generated in the dump condenser, and is provided from the condensate header to the steam supply facility. In a power generation / desalination complex plant that supplies water to a water supply tank of a deaerator, a bypass system that supplies steam from the steam supply facility to the freshwater generation facility without passing through the steam turbine, and provided in the bypass system And a medium for cooling the steam in the temperature reducing device is supplied from the condensate header. .

  According to the present invention, it is possible to provide a power generation / desalination complex plant and a method for operating the power generation / desalination complex plant that can widely respond to changes in power generation demand and water generation demand with a minimum facility capacity.

  Hereinafter, first to third embodiments of the power generation / desalination complex plant of the present invention will be described with reference to the drawings.

  First, a first embodiment will be described with reference to FIG. In the power generation / desalination complex plant of this embodiment, the water generation facility 2 and the dump condenser 3 are connected in parallel to the exhaust system of the steam turbine 1 to which steam is supplied from the exhaust heat recovery boiler 21 of the gas turbine power generation facility 20. Yes. The condensate of the fresh water generator 2 and the condensate of the dump condenser 3 are connected to the condensate header 4, and the condensate from the condensate header 4 is connected to the deaerator water supply tank 5 of the exhaust heat recovery boiler 21. ing. A dump condenser hot well level adjusting valve 6 is provided at the outlet of the dump condenser 3, and a deaerator water tank level adjusting valve 7 is provided at the inlet of the deaerator water tank 5. Further, a hot well level meter 8 and a makeup water system 9 are connected to the dump condenser 3, and a level meter 10 is connected to the deaerator water tank 5. The condensate header 4 is provided with a pressure gauge 11 and a blow line 12. Although not shown, a generator is connected to the steam turbine 1.

  In the power generation / desalination complex plant of this embodiment configured as above, when the hot well level of the dump condenser 3 is high, the dump condenser hot well level control valve 6 is opened, and the hot well level can be kept constant. it can. Further, when the pressure of the condensate header 4 is lowered, the hot well level can be recovered to a predetermined value by performing makeup from the makeup water system 9 to the hot well of the dump condenser 3.

  On the other hand, when the pressure of the condensate header 4 is high, the condensate header pressure can be lowered to a specified value by opening the blow line 12. Furthermore, the inlet valve of the deaerator water supply tank 5 can be operated while continuously controlling the tank level regardless of the hot well level of the dump condenser 3 and the pressure of the condensate header 4.

  Thus, in the power generation / desalination complex plant of this embodiment, the system leak water can be appropriately supplied regardless of the operation state of the water generation facility 2 and the power generation facility, and the pressure of the condensate header 4 Since compensation for the system leak can be performed by make-up to the dump capacitor 3 immediately upstream of the condensate header 4, stable control can be performed with a short time constant.

  Next, a second embodiment of the present invention will be described with reference to FIG. In the power generation / desalination complex plant of the present embodiment, the water generation facility 2 and the dump condenser 3 are connected to the exhaust of the steam turbine 1 to which steam is supplied from the exhaust heat recovery boiler 21 of the gas turbine power generation facility 20. Condensate from the fresh water generator 2 and the dump condenser 3 is connected to the condensate header 4, and the condensate from the condensate header 4 is connected to the deaerator water supply tank 5 of the exhaust heat recovery boiler 21. . The dump condenser 3 is connected to an ejector 22 that makes the internal pressure negative. Cooling of the steam supplied to the ejector 22 using the minimum flow line 13 of the condensate pump 23 connected to the outlet of the dump condenser 3. It is the system configuration which performs. Although not shown, a generator is connected to the steam turbine 1.

  In the power generation / desalination complex plant of the present embodiment configured as described above, the ejector 22 can be operated using the minimum flow of the condensate pump 23. Therefore, the ejector 22 can be operated stably regardless of the steam flow rate to the dump condenser 3, and a wide range of changes in power generation demand and fresh water demand can be accommodated.

  Next, a third embodiment of the present invention will be described with reference to FIG. The power generation / desalination complex plant of this embodiment includes a plurality of boilers A, B, C, D, and E that supply steam to the steam turbine 1. The boiler A is an exhaust heat recovery boiler 21 of the gas turbine power generation facility 20. The outputs of the plurality of boilers A, B, C, D, E are also connected to the inlet side of the fresh water generation facility 2 and the dump condenser 3 via the bypass system 14 and the temperature reducing device 24. Further, a spray water system 15 is provided from the condensate header 4 for collecting the condensate generated in the fresh water generation facility 2 and the condensate generated in the dump condenser 3 to the temperature reducing device 24, and the temperature reducing device 24 cools the steam To supply spray water.

  Normally, the cooling water of the steam turbine bypass system is discharged from the boiler feed pump or extracted from the middle stage in order to take out the degassed system, but in the power generation / desalination complex plant of this embodiment, the makeup water deaerated to some extent is used. Therefore, it is not necessary to take out the spray water from the downstream side of the deaerator, so that the spray water system 15 for supplying the spray water to the bypass system 14 is connected from the condensate header 4.

  In the power generation / desalination complex plant of this embodiment configured as described above, since the cooling water for cooling the steam of the bypass system 14 is supplied without using the boiler feed pump, the number of boiler feed pumps depends on the number of boilers operated. The plant can be operated without changing the ratio of the spray water amount to the passing flow rate.

  For example, in a certain planning example, when five boilers are operated with respect to 100% power generation demand and 100% water production demand as rated points, the feed water flow rate passing through the boiler feed pump is 150 kg / s. In this plant, when the generation demand is 30% and the desalination demand is 100%, three boilers are sufficient, but it is necessary to supply backup steam to the desalination facility. At this time, when spray water is extracted from the boiler feed pump, the flow rate through the boiler feed pump is 210 kg / s, whereas when the configuration of this embodiment is adopted, it is 170 kg / s. Therefore, the capacity of the boiler feed pump can be reduced from 210kg / s to 170kg / s by taking spray from the condensate header, and the boiler feed pump can be selected near the rated point. The pump can be operated efficiently in the range, and since the heat recovery of the boiler can be used more effectively, the plant can be operated efficiently.

1 is a system diagram showing a power generation / desalination complex plant according to a first embodiment of the present invention. The systematic diagram which shows the electric power generation desalination complex plant of the 2nd Example of this invention. The systematic diagram which shows the electric power generation desalination complex plant of the 3rd Example of this invention.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 ... Steam turbine, 2 ... Fresh water generation equipment, 3 ... Dump condenser, 4 ... Condensate header, 5 ... Deaerator water supply tank, 6 ... Dump condenser hot well level control valve, 7 ... Deaerator water tank level control valve , 8 ... Dump condenser hot well level meter, 9 ... Supply water system, 10 ... Deaerator water tank level meter, 11 ... Condensate header pressure gauge, 12 ... Condensate header blow line, 13 ... Condensate pump minimum flow line , 14 ... Bypass system, 15 ... Spray water system, 20 ... Gas turbine power generation equipment, 21 ... Waste heat recovery boiler, 22 ... Ejector, 23 ... Condensate pump, 24 ... Temperature reducing device.

Claims (4)

  A steam turbine that is supplied with steam from a steam supply facility and drives a generator; a desalination facility that produces fresh water by evaporating seawater by the exhaust of the steam turbine; and a dump condenser that takes in surplus steam from the steam turbine; A condensate header that collects the condensate generated in the freshwater generation facility and the condensate generated in the dump condenser, and from the condensate header to a water supply tank of a deaerator provided in the steam supply facility In a power generation / desalination complex plant that supplies water, the dump condenser includes a makeup water system, a hot well level meter, and a hot well level control valve, and the water tank of the deaerator includes a level meter and a level control valve. And the condensate header is provided with a pressure gauge and a blow line.   The power generation / desalination complex plant according to claim 1, wherein when the hot well level of the dump condenser is different from a set value, the hot well level is maintained at a set value by opening and closing the hot well level control valve, and the condensate When the header pressure drops, makeup is performed from the makeup water system to the hot well of the dump condenser, and when the condensate header pressure is higher than a specified value, condensate is blown out of the system from the blow line. The header pressure is lowered to a specified value, and the inlet valve of the water tank of the deaerator keeps the tank level of the water tank constant regardless of the hot well level of the dump condenser and the pressure of the condensate header. An operation method of a power generation / desalination complex plant, characterized by controlling.   A steam turbine that is supplied with steam from a steam supply facility and drives a generator; a desalination facility that produces fresh water by evaporating seawater by the exhaust of the steam turbine; and a dump condenser that takes in surplus steam from the steam turbine; A condensate header that collects the condensate generated in the freshwater generation facility and the condensate generated in the dump condenser, and from the condensate header to a water supply tank of a deaerator provided in the steam supply facility In a power generation / desalination complex plant that supplies water, an ejector for negatively setting the internal pressure of the dump condenser is provided, and a condensate pump connected to an outlet of the dump condenser as a cooling source for working steam of the ejector A power generation and desalination complex plant characterized by utilizing a minimum flow system. A steam turbine that is supplied with steam from a steam supply facility and drives a generator; a desalination facility that produces fresh water by evaporating seawater by the exhaust of the steam turbine; and a dump condenser that takes in surplus steam from the steam turbine; And a condensate header that collects the condensate generated in the freshwater generation facility and the condensate generated in the dump condenser, and from the condensate header to a water supply tank of a deaerator provided in the steam supply facility In a power generation / desalination complex plant that supplies water, a bypass system that supplies steam from the steam supply facility to the freshwater generation facility without passing through the steam turbine, and a temperature reduction device provided in the bypass system, And a medium for cooling the steam in the temperature reducing device is supplied from the condensate header. Plant.

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