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    Power Generation From Coal Mill Rejection Using Kalina Cycle

    Source: Journal of Energy Resources Technology:;2016:;volume( 138 ):;issue: 005::page 52004
    Author:
    Khankari, Goutam
    ,
    Karmakar, Sujit
    DOI: 10.1115/1.4033425
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: This paper proposes an ammonia–water Kalina cycle driven by lowgrade waste energy released from the combustion reactions of mill's rejection which is coupled with 500 MWe coalfired thermal power plant to quantify the additional electrical power. Energy of combustion for mill rejection is computed by combustion modeling equations. A thermodynamic property calculator for the binary mixture and a computer simulation program have been developed by MSExcel and Visual Basic for Application (VBA) to calculate and optimize the Kalina cycle operating parameters based on thermodynamic modeling equations. Variation of key operating parameters, namely, turbine inlet pressure, mass flow rate of binary mixture, and ammonia mass fraction in mixture is studied and filters the optimum value accordingly to maximize the cycle efficiency. Technocommercial feasibility is also done through economic analysis. The results show that about 562.745 kWe power generation can be added with total plant generation for organization profit. This will enhance the combined plant efficiency from 38.559% to 38.604%. Maximum net Kalina cycle efficiency of 24.74% can be achieved with ammonia mass fraction of 0.4 at condenser back pressure of 1.957 bar and turbine inlet pressure and temperature of 20 bar and 442.40 K, respectively. Ammonia mass fraction of 0.4 is the optimum choice for 20 bar turbine inlet pressure to get maximum output after maintaining minimum 50 K degree of superheat compared to ammonia mass fraction of 0.3. The cycle performance at ammonia mass fraction of 0.4 is better than 0.5 due to less condenser back pressure. Kalina cycle operating with less mass flow rate performs higher cycle efficiency when dryness fraction at turbine exhaust is less than 1 and performance deteriorates at above 1. This deterioration is due to higher condenser energy loss carried away by cooling water (CW) flow. The simple payback period of this system is around 5.5 years if the system is running with 80% plant availability factor and 100% plant load factor.
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      Power Generation From Coal Mill Rejection Using Kalina Cycle

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    https://yetl.yabesh.ir/yetl1/handle/yetl/160941
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    contributor authorKhankari, Goutam
    contributor authorKarmakar, Sujit
    date accessioned2017-05-09T01:27:55Z
    date available2017-05-09T01:27:55Z
    date issued2016
    identifier issn0195-0738
    identifier othermd_138_06_061407.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/160941
    description abstractThis paper proposes an ammonia–water Kalina cycle driven by lowgrade waste energy released from the combustion reactions of mill's rejection which is coupled with 500 MWe coalfired thermal power plant to quantify the additional electrical power. Energy of combustion for mill rejection is computed by combustion modeling equations. A thermodynamic property calculator for the binary mixture and a computer simulation program have been developed by MSExcel and Visual Basic for Application (VBA) to calculate and optimize the Kalina cycle operating parameters based on thermodynamic modeling equations. Variation of key operating parameters, namely, turbine inlet pressure, mass flow rate of binary mixture, and ammonia mass fraction in mixture is studied and filters the optimum value accordingly to maximize the cycle efficiency. Technocommercial feasibility is also done through economic analysis. The results show that about 562.745 kWe power generation can be added with total plant generation for organization profit. This will enhance the combined plant efficiency from 38.559% to 38.604%. Maximum net Kalina cycle efficiency of 24.74% can be achieved with ammonia mass fraction of 0.4 at condenser back pressure of 1.957 bar and turbine inlet pressure and temperature of 20 bar and 442.40 K, respectively. Ammonia mass fraction of 0.4 is the optimum choice for 20 bar turbine inlet pressure to get maximum output after maintaining minimum 50 K degree of superheat compared to ammonia mass fraction of 0.3. The cycle performance at ammonia mass fraction of 0.4 is better than 0.5 due to less condenser back pressure. Kalina cycle operating with less mass flow rate performs higher cycle efficiency when dryness fraction at turbine exhaust is less than 1 and performance deteriorates at above 1. This deterioration is due to higher condenser energy loss carried away by cooling water (CW) flow. The simple payback period of this system is around 5.5 years if the system is running with 80% plant availability factor and 100% plant load factor.
    publisherThe American Society of Mechanical Engineers (ASME)
    titlePower Generation From Coal Mill Rejection Using Kalina Cycle
    typeJournal Paper
    journal volume138
    journal issue5
    journal titleJournal of Energy Resources Technology
    identifier doi10.1115/1.4033425
    journal fristpage52004
    journal lastpage52004
    identifier eissn1528-8994
    treeJournal of Energy Resources Technology:;2016:;volume( 138 ):;issue: 005
    contenttypeFulltext
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    DSpace software copyright © 2002-2015  DuraSpace
    نرم افزار کتابخانه دیجیتال "دی اسپیس" فارسی شده توسط یابش برای کتابخانه های ایرانی | تماس با یابش
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