Plant control apparatus and combined cycle power plant
원문보기
IPC분류정보
국가/구분
United States(US) Patent
등록
국제특허분류(IPC7판)
F01K-023/10
F01K-007/24
F01K-007/16
F01K-011/02
출원번호
US-0843388
(2015-09-02)
등록번호
US-10087786
(2018-10-02)
우선권정보
JP-2014-186181 (2014-09-12)
발명자
/ 주소
Kiga, Hikaru
Tobo, Masayuki
Akebi, Toyohiro
Nakamura, Keiichi
출원인 / 주소
KABUSHIKI KAISHA TOSHIBA
대리인 / 주소
Oblon, McClelland, Maier & Neustadt, L.L.P.
인용정보
피인용 횟수 :
0인용 특허 :
10
초록▼
In one embodiment, a combined cycle power plant includes first and second superheaters to generate first and second main steams, first and second reheaters to heat first and second discharge steams to generate first and second reheat steams, and a steam turbine to be supplied with the merged first a
In one embodiment, a combined cycle power plant includes first and second superheaters to generate first and second main steams, first and second reheaters to heat first and second discharge steams to generate first and second reheat steams, and a steam turbine to be supplied with the merged first and second reheat steams. The plant further includes a first valve to adjust a flow rate of the first discharge or reheat steam, and a second valve to adjust a flow rate of the second discharge or reheat steam. A plant control apparatus includes a determination module to determine a target opening degree of the second valve by using flow rates of the first and second main steams, and a controller to compare the determined target opening degree with a valve opening degree of the second valve and to control the second valve based on a comparison result.
대표청구항▼
1. A plant control apparatus configured to control a combined cycle power plant comprising: a first superheater configured to recover heat of exhaust gas of a first gas turbine to generate first main steam;a second superheater configured to recover heat of exhaust gas of a second gas turbine to gene
1. A plant control apparatus configured to control a combined cycle power plant comprising: a first superheater configured to recover heat of exhaust gas of a first gas turbine to generate first main steam;a second superheater configured to recover heat of exhaust gas of a second gas turbine to generate second main steam;a first steam turbine configured to be supplied with the first main steam and the second main steam;a first reheater configured to heat first discharge steam obtained by dividing discharge steam of the first steam turbine to generate first reheat steam;a second reheater configured to heat second discharge steam obtained by dividing the discharge steam of the first steam turbine to generate second reheat steam;a second steam turbine configured to be supplied with the first reheat steam and the second reheat steam after the first reheat steam and the second reheat steam are merged;a first valve as a motor-operated valve, configured to adjust a flow rate of the first discharge steam supplied to the first reheater or the first reheat stream discharged from the first reheater; anda second valve as the motor-operated valve, configured to adjust a flow rate of the second discharge steam supplied to the second reheater or the second reheat stream discharged from the second reheater,the plant control apparatus comprising:a determination module configured to obtain a flow rate ratio of a flow rate of the first main steam and a flow rate of the second main steam, obtain a flow coefficient corresponding to a valve opening degree of the first valve by using correspondence between a valve opening degree and a flow coefficient of the motor-operated valve, determine a target flow coefficient of the second valve by using the obtained flow coefficient of the first valve and the obtained flow rate ratio, and determine, as a target opening degree of the second valve, a valve opening degree of the second valve corresponding to the target flow coefficient of the second valve in the correspondence; anda controller configured to compare the determined target opening degree with a valve opening degree of the second valve and to perform one of an opening operation and a closing operation of the second valve in accordance with a state whether the determined target opening degree is larger or smaller than the valve opening degree of the second valve. 2. The apparatus of claim 1, wherein the determination module calculates, as a main steam average flow rate ratio, a moving time average of the flow rate ratio of the first main steam and the second main steam, and determines the target opening degree of the second valve by using the calculated main steam average flow rate ratio and the correspondence between the valve opening degree and the flow coefficient of the second valve. 3. The apparatus of claim 2, wherein the determination module determines a target flow coefficient of the second valve by using the main steam average flow rate ratio, and determines, as the target opening degree of the second valve, the valve opening degree of the second valve corresponding to the target flow coefficient of the second valve in the correspondence. 4. The apparatus of claim 1, wherein the combined cycle power plant further comprises a third valve provided between the second superheater and the first steam turbine and configured to adjust the flow rate of the second main steam, andthe determination module is configured, in a case where the third valve is to be opened to supply the second main steam to the first steam turbine from a state that only the first main steam is supplied to the first steam turbine, to determine the target opening degree of the second valve by using the flow rate ratio when the third valve is opened and the correspondence between the valve opening degree and the flow coefficient of the second valve, before the third valve is opened to a stipulated rate, and to determine the target opening degree of the second valve by using the flow rate ratio at determination time and the correspondence between the valve opening degree and the flow coefficient of the second valve, after the third valve is opened to the stipulated rate. 5. A combined cycle power plant comprising: a first superheater configured to recover heat of exhaust gas of a first gas turbine to generate first main steam;a second superheater configured to recover heat of exhaust gas of a second gas turbine to generate second main steam;a first steam turbine configured to be supplied with the first main steam and the second main steam;a first reheater configured to heat first discharge steam obtained by dividing discharge steam of the first steam turbine to generate first reheat steam;a second reheater configured to heat second discharge steam obtained by dividing the discharge steam of the first steam turbine to generate second reheat steam;a second steam turbine configured to be supplied with the first reheat steam and the second reheat steam after the first reheat steam and the second reheat steam are merged;a first valve as a motor-operated valve, configured to adjust a flow rate of the first discharge steam supplied to the first reheater or the first reheat stream discharged from the first reheater;a second valve as the motor-operated valve, configured to adjust a flow rate of the second discharge steam supplied to the second reheater or the second reheat stream discharged from the second reheater;a first measuring instrument configured to measure a flow rate of the first main steam;a second measuring instrument configured to measure a flow rate of the second main steam;an opening degree meter configured to measure a valve opening degree of the second valve;a determination module configured to obtain a flow rate ratio of the flow rate of the first main steam measured by the first measuring instrument and the flow rate of the second main steam measured by the second measuring instrument, obtain a flow coefficient corresponding to a valve opening degree of the first valve by using correspondence between a valve opening degree and a flow coefficient of the motor-operated valve, determine a target flow coefficient of the second valve by using the obtained flow coefficient of the first valve and the obtained flow rate ratio, and determine, as a target opening degree of the second valve, a valve opening degree of the second valve corresponding to the target flow coefficient of the second valve in the correspondence; anda controller configured to compare the determined target opening degree with the measured valve opening degree of the second valve and to perform one of an operating operation and a closing operation of the second valve in accordance with a state whether the determined target opening degree is larger or smaller than the measured valve opening degree of the second valve.
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이 특허에 인용된 특허 (10)
Inaba Yoshiaki (Hitachi JPX) Tokunaga Kenji (Tokyo JPX) Shimizu Akihiro (Hitachi JPX) Kuribayashi Tetsuzo (Hitachi JPX), Apparatus for heat recovery and method for operating the apparatus.
Gounder Ponnusami K. (San Diego CA) Raskin Neil R. (Carlsbad CA) Kauranen Timo M. (San Diego CA), System and method for reheat steam temperature control in circulating fluidized bed boilers.
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