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    Protection of Boiler Feed Pump Against Transient Suction Pressure Decay

    Source: Journal of Engineering for Gas Turbines and Power:;1974:;volume( 096 ):;issue: 003::page 247
    Author:
    G. S. Liao
    DOI: 10.1115/1.3445801
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: In a previous paper [1], the analysis of pump suction pressure decay utilizing the varying condensate temperature approach was first introduced. Although the paper provided power plant engineers with an accurate analytical method for determining the magnitude of feedwater pump suction pressure decay, no protective method to prevent or alleviate the pressure decay under instant turbine load rejection was mentioned. As unit size has rapidly increased in recent years, the power plant deaerator requires not only a larger storage capacity but also must be elevated higher to protect the boiler feed pumps against suction pressure decay under load rejection. Since this trend is expected to continue, the cost of supporting the power plant deaerator may soon become prohibitive. Several protective methods have been previously introduced. However, the evaluation of the methods was invariably based on the constant-condensate-temperature approach, which is not suitable for central station regenerative cycle units. This paper reevaluates those methods in general and recommends the on-off type deaerator bypass system as the most effective and economical method. The use of this protective method will not only reduce deaerator storage capacity to the absolute minimum as required solely for surge, but will also largely preclude the provision of additional static head for instant load reduction. As a result, enormous savings can be expected both from the deaerator itself and its supporting structures. The magnitude of savings in supporting structures alone may amount to more than a half million dollars for a 750 MW fossile unit. Based on the varying condensate temperature approach, mathematical equations expressing the deaerator pressure decay as well as design parameters required for designing the protective system have been derived. The paper also presents a detailed description of the recommended protective system and discusses some advantages of this system over the others. Finally, a few engineering examples are included to illustrate the application in system design.
    keyword(s): Pressure , Suction , Boilers , Pumps , Design , Power stations , Stress , Condensed matter , Temperature , Storage , Surges , Turbines , Cycles , Equations , Engineers AND Feedwater ,
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      Protection of Boiler Feed Pump Against Transient Suction Pressure Decay

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    http://yetl.yabesh.ir/yetl1/handle/yetl/164748
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    • Journal of Engineering for Gas Turbines and Power

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    contributor authorG. S. Liao
    date accessioned2017-05-09T01:38:07Z
    date available2017-05-09T01:38:07Z
    date copyrightJuly, 1974
    date issued1974
    identifier issn1528-8919
    identifier otherJETPEZ-26711#247_1.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/164748
    description abstractIn a previous paper [1], the analysis of pump suction pressure decay utilizing the varying condensate temperature approach was first introduced. Although the paper provided power plant engineers with an accurate analytical method for determining the magnitude of feedwater pump suction pressure decay, no protective method to prevent or alleviate the pressure decay under instant turbine load rejection was mentioned. As unit size has rapidly increased in recent years, the power plant deaerator requires not only a larger storage capacity but also must be elevated higher to protect the boiler feed pumps against suction pressure decay under load rejection. Since this trend is expected to continue, the cost of supporting the power plant deaerator may soon become prohibitive. Several protective methods have been previously introduced. However, the evaluation of the methods was invariably based on the constant-condensate-temperature approach, which is not suitable for central station regenerative cycle units. This paper reevaluates those methods in general and recommends the on-off type deaerator bypass system as the most effective and economical method. The use of this protective method will not only reduce deaerator storage capacity to the absolute minimum as required solely for surge, but will also largely preclude the provision of additional static head for instant load reduction. As a result, enormous savings can be expected both from the deaerator itself and its supporting structures. The magnitude of savings in supporting structures alone may amount to more than a half million dollars for a 750 MW fossile unit. Based on the varying condensate temperature approach, mathematical equations expressing the deaerator pressure decay as well as design parameters required for designing the protective system have been derived. The paper also presents a detailed description of the recommended protective system and discusses some advantages of this system over the others. Finally, a few engineering examples are included to illustrate the application in system design.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleProtection of Boiler Feed Pump Against Transient Suction Pressure Decay
    typeJournal Paper
    journal volume96
    journal issue3
    journal titleJournal of Engineering for Gas Turbines and Power
    identifier doi10.1115/1.3445801
    journal fristpage247
    journal lastpage254
    identifier eissn0742-4795
    keywordsPressure
    keywordsSuction
    keywordsBoilers
    keywordsPumps
    keywordsDesign
    keywordsPower stations
    keywordsStress
    keywordsCondensed matter
    keywordsTemperature
    keywordsStorage
    keywordsSurges
    keywordsTurbines
    keywordsCycles
    keywordsEquations
    keywordsEngineers AND Feedwater
    treeJournal of Engineering for Gas Turbines and Power:;1974:;volume( 096 ):;issue: 003
    contenttypeFulltext
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