Utilisation of waste heat from the power plant by use of the ORC aided with bleed steam and extra source of heat

Utilization of waste heat recovered from the exhaust gases of the power generation unit by means of ORC (organic Rankine cycles) installation is considered. The waste heat is available in the form of a stream of hot water having temperature of 90 °C in the amount of 200 MWt. To increase evaporation temperature of ORC working fluid the heat of steam from the extraction points from the low-pressure part of steam turbine is used. Subsequently additional heat from compressor cooling of the carbon dioxide capture and storage installation is also considered as a way to provide extra heat to the ORC. Thermodynamic analysis of the supercritical plant with and without incorporation of ORC was accomplished using a commercial code Aspen Plus. For ORC considered were four working fluids such as n-pentane, ethanol, R236ea and R245fa. Determined were major parameter describing the operational features of the hybrid power plant such as the change of the unit power, efficiency and increase of electricity production of the hybrid installation consisting of the reference plant and the ORC. The highest thermal efficiency of the ORC is obtained in the case ethanol as working fluid, whereas the highest amount of electricity is produced in the case of R236ea.

[1]  Dariusz Mikielewicz,et al.  A thermodynamic criterion for selection of working fluid for subcritical and supercritical domestic micro CHP , 2010 .

[2]  Yiping Dai,et al.  Thermodynamic analysis and optimization of an (organic Rankine cycle) ORC using low grade heat source , 2013 .

[3]  Aleksandra Borsukiewicz-Gozdur Influence of heat recuperation in ORC power plant on efficiency of waste heat utilization , 2010 .

[4]  Costante Mario Invernizzi,et al.  The potential role of organic bottoming Rankine cycles in steam power stations , 1999 .

[5]  N. Lai,et al.  Working fluids for high-temperature organic Rankine cycles , 2007 .

[6]  Michel Feidt,et al.  Performance optimization of low-temperature power generation by supercritical ORCs (organic Rankine cycles) using low GWP (global warming potential) working fluids , 2014 .

[7]  Anna Skorek-Osikowska,et al.  Economic analysis of a supercritical coal-fired CHP plant integrated with an absorption carbon capture installation , 2014 .

[9]  Janusz Badur,et al.  Exergy Losses in the Szewalski Binary Vapor Cycle , 2015, Entropy.

[10]  T. Hung Waste heat recovery of organic Rankine cycle using dry fluids , 2001 .

[11]  Bertrand F. Tchanche,et al.  Fluid selection for a low-temperature solar organic Rankine cycle , 2009 .

[12]  Tomasz Kowalczyk,et al.  The thermodynamic analysis of the Szewalski hierarchic vapour cycle cooperating with a system of waste heat recovery , 2015 .

[13]  W. Stanek,et al.  Exergetic cost of steam power plant operation , 2011 .

[14]  Andrzej Ziębik,et al.  Thermoecological analysis of an oxy-fuel combustion power plant integrated with a CO2 processing unit , 2015 .

[15]  Luis M. Romeo,et al.  Optimization of boiler cold-end and integration with the steam cycle in supercritical units , 2010 .

[16]  Chi-Chuan Wang,et al.  Effect of working fluids on organic Rankine cycle for waste heat recovery , 2004 .

[17]  Yan Li,et al.  Thermodynamic analysis and performance optimization of an ORC (Organic Rankine Cycle) system for multi-strand waste heat sources in petroleum refining industry , 2014 .

[18]  V. Maizza,et al.  Unconventional working fluids in organic Rankine-cycles for waste energy recovery systems , 2001 .

[19]  Jay H. Lee,et al.  Carbon capture from stationary power generation sources: A review of the current status of the technologies , 2013, Korean Journal of Chemical Engineering.

[20]  P. Markewitz,et al.  How clean is clean? Incremental versus radical technological change in coal-fired power plants , 2013 .