Effects of operational parameters on the thermodynamic performance of FBCC steam power plant

Abstract In this study, the effects of operational parameters on the thermodynamic performance of a FBCC steam power plant with a rated output of 7.7 MW are investigated by the developed model such as excess air, coal type and steam pressure based on the first and second laws of thermodynamics. The plant consists of a FBCC, a WHB and an economizer as subsystems and fans, pumps, cyclone and chimney as auxiliary systems. The model results are shown to agree well with plant operational data. As a result of this study, it is observed that the first and the second law efficiencies of the system decrease 5.1% and 5.2%, respectively, as the excess air increases from 10% to 70%. As the steam pressure increases from 4 to 12 bar, the energy efficiency of the system decreases to 2.1% but the exergy efficiency of the system increases to 19.9%. The amount of irreversibility occurring in the system is also calculated at each location through the developed model. The FBCC has the largest irreversibility, of about 80.4% of the total irreversibilities in the plant, mostly due to the irreversible combustion process. It is also observed that the coal type does not affect the first and the second law efficiencies considerably.

[1]  Chuguang Zheng,et al.  Exergy cost analysis of a coal fired power plant based on structural theory of thermoeconomics , 2006 .

[2]  M. J. Moran,et al.  Exergy Analysis: Principles and Practice , 1994 .

[3]  Gemma Grasa,et al.  Circulating fluidized bed combustion in the turbulent regime: modelling of carbon combustion efficiency and sulphur retention , 2001 .

[4]  Mircea Cârdu,et al.  Application of the methodology to estimate the energy-ecologic efficiency of fluidized bed boilers , 2001 .

[5]  G. Barigozzi,et al.  Description, applications and numerical modelling of bubbling fluidized bed combustion in waste-to-energy plants , 2008 .

[6]  A. Gungor,et al.  Effects of Immersed Surfaces on the Combustor Efficiency of Small-Scale Fluidized Beds , 2005 .

[7]  I. Dincer The role of exergy in energy policy making , 2002 .

[8]  A. Gungor Analysis of combustion efficiency in CFB coal combustors , 2008 .

[9]  M. J. Moran,et al.  Thermal design and optimization , 1995 .

[10]  Noam Lior,et al.  Energy, exergy, and Second Law performance criteria , 2007 .

[11]  Amitava Datta,et al.  Exergy analysis of a coal‐based 210 MW thermal power plant , 2007 .

[12]  M. Puncochár,et al.  Entropy of fluidized bed—a measure of particles mixing , 2003 .

[13]  Marc A. Rosen,et al.  Second‐law analysis: approaches and implications , 1999 .

[14]  Joris Koornneef,et al.  Development of fluidized bed combustion—An overview of trends, performance and cost , 2007 .

[15]  Frank P. Incropera,et al.  Fundamentals of Heat and Mass Transfer , 1981 .

[16]  Chia-Chin Chuang,et al.  Engineering design and exergy analyses for combustion gas turbine based power generation system , 2004 .

[17]  D.-J. Kim,et al.  Exergetic and thermoeconomic analyses of power plants , 2003 .

[18]  S. K. Som,et al.  Thermodynamic irreversibilities and exergy balance in combustion processes , 2008 .

[19]  C. Y. Wen,et al.  A comprehensive model for fluidized bed coal combustors , 1980 .

[20]  Kunihiko Mouri,et al.  Exergy analysis on combustion and energy conversion processes , 2005 .

[21]  C. Wen Mechanics of Fluidization , 1966 .

[22]  Cen Ke-fa,et al.  Boilers and burners , 1999 .

[23]  Ibrahim Dincer,et al.  On exergy and environmental impact , 1997 .