Thermodynamic analysis of reheat cycle steam power plants (original) (raw)

Effect of key parameters on thermodynamic and thermoeconomic performance of steam power plant

The first law of thermodynamics is a useful tool for thermodynamics processes analysis. The exergy analysis of a conventional steam power plant was done. This analysis is based on first and second law of thermodynamics. In the present paper, a conventional steam power plant was investigated using a thermoeconomic analysis. Having done this analysis the inefficient components of a steam power plant cycle was identified. In this analysis, it was assumed that the cycle components are adiabatic and the potential and kinetic terms of exergy were negligible. The exergy analysis combined with the economical aspects. These aspects include capital investment cost, fuel cost and operating and maintenance cost for evaluation of final cost of product. According to this calculation exergy destruction cost of each component in the cycle and their role were evaluated. Based on these results the effect of the component efficiency on the final cost of the product and performance revealed. Effect of main steam temperature, reheated temperature, condenser pressure and number of the feed water heaters on cycle performance and final electrical power cost were also determined.

THERMOECONOMIC ANALYSIS OF ALKHOMS STEAM POWER PLANT AT DIFFERENT OPERATING LOADS

Journal of Engineering Research, 2021

Exergoeconomic (thermoeconomic) analysis is performed on Alkhoms steam power plant. The nominal power of the plant is 120 MW. The analysis is based on real-time data and performed for three different loads. The main factor of load variation is the variation of the steam mass flow rate. These loads are 120 MW (full load), 60 MW (part load), and 100 MW (real-time operation). It is worth to mention that high-pressure heaters are out of service these days. A systematic and general methodology for defining and calculating exergetic efficiencies, exergy destruction, and exergy related to costs in thermal systems is presented. The methodology is based on the Specific Exergy Costing (SPECO) method. Results of the exergy analysis showed the exergetic efficiency (effectiveness) increases from 34.74% at the real-time operation to 40.96% at full operating load, and hence the ratio of the total exergy destruction to fuel input exergy decreases from 64.46% at a real-time operation to 59.6 at part load up to 57.88% at full operating load. The exergoeconomic analysis results the average specific cost is 0.177 /kWhatreal−timeoperationand0.113/kWh at real-time operation and 0.113 /kWhatrealtimeoperationand0.113/kWh at part load, and 0.102 /kWhatfulloperatingloadtakingintoconsiderationtheescalationoffuelprice(levelizedfuelcost).Itisfoundthatthecostofexergydestructioninthesteamgeneratorpresentsthemaincontributiontothetotalcostofexergyloss;itsvaluevariesinthesteamgeneratorfrom8296/kWh at full operating load taking into consideration the escalation of fuel price (levelized fuel cost). It is found that the cost of exergy destruction in the steam generator presents the main contribution to the total cost of exergy loss; its value varies in the steam generator from 8296 /kWhatfulloperatingloadtakingintoconsiderationtheescalationoffuelprice(levelizedfuelcost).Itisfoundthatthecostofexergydestructioninthesteamgeneratorpresentsthemaincontributiontothetotalcostofexergyloss;itsvaluevariesinthesteamgeneratorfrom8296/h at the real-time operation to 6560 /hatfulloperatingload,whileexergydestructioncostatpartloadisatanotablevalueof3495/h at full operating load, while exergy destruction cost at part load is at a notable value of 3495 /hatfulloperatingload,whileexergydestructioncostatpartloadisatanotablevalueof3495/h due to low fuel consumption. The contributions and the variation of exergy destruction cost with load are lower for the other components.

Energy and Exergy Analysis of a 348.5 MW Steam Power Plant

Energy Sources, Part A: Recovery, Utilization, And Environmental Effects, 2010

In the present work, the energy and exergy analysis of Kostolac power plant in Serbia is presented. The primary objectives of this article are to analyze the system components separately and to identify and quantify the sites having the largest energy and exergy losses. The energy and exergy efficiency is calculated using the plant operating data from the plant at different loads. The load variation is studied with the data at 100% and 60% of full load. Moreover, the effects of the load variations are calculated in order to obtain a good insight into this analysis. The performance of the plant is estimated by a component-wise modeling, and a detailed break-up of energy and exergy losses for the considered plant has been presented. The results show that energy losses have mainly occurred in the condenser where 421 MW is lost to the environment while only 105.78 MW has been lost from the boiler. Nevertheless, the irreversibility rate of the boiler is higher than the irreversibility rates of the other components. The percentage ratio of the exergy destruction to the total exergy destruction was found to be maximum in the boiler system (88.2%) followed by the turbines (9.5%), and then the forced draft fan condenser (0.5%). In addition, the calculated thermal efficiency based on the lower heating value of fuel was 39% while the exergy efficiency of the power cycle was 35.77%.

Thermo-Economic Analysis of Simple Cycle Steam Power Plant

Basrah journal for engineering science

Thermal steam power plants represent the most important and dependable type for supplying the base load of electricity around the world. The thermos-economic analysis is an important tool for improving the performance of thermal steam power plants. In the present study, a thermo-economic analysis of a simple steam power plant for different boiler pressure was performed. The analysis comprises the energy, exergy, entropy, economics, and exergy-economic of a simple cycle steam power plant for different boiler pressure. The analysis was performed for a simple steam power plant with the constant output power of 10 MW and the boiler pressure is varied from 10 bar to 100 bar by a step of 10 bar. For each boiler pressure and constant output power, firstly, the fuel mass flow rate, steam flow rate, energy and exergy efficiency, and cost of electricity were calculated. Secondly, entropy generation, exergy destruction, and exergy efficiency for each component were calculated. Finally, exergy ...

Fundamentals of Thermodynamics Applied to Thermal Power Plants

In this chapter it is reviewed the fundamental principles of Thermodynamics aiming at its application to power plants cycle analysis. The three most common thermodynamic cycles are studied starting with the Brayton cycle, the Diesel Cycle, and the Rankine cycle. These ideal cycles are thermodynamic operating models for gas turbines, diesel engines, and steam turbines, respectively. Thermal efficiencies, operating conditions and cycle variations are also analyzed. The last issue studied is the combined Brayton-Rankine cycle, which is a trend in industry due to its higher overall efficiency.

Investigation of the thermodynamic performance of an existing steam power plant via energy and exergy analyses to restrain the environmental repercussions: A simulation study

Environmental Engineering Research, 2021

Exergy analysis is an important tool to identify the improvements in various industrial processes. In this study, the existing steam power plant is examined based on energy and exergy analyses. The steam network in the power plant is comprised of two sections, one of them is used for paddy drying, while other portion is used to operate the turbine for in-house electricity production. Mass, energy, and exergy balances are applied to individual equipment of the plant. The power plant is modeled and simulated using Aspen HYSYS® V10. The calculated thermodynamic values are used for in-depth analysis of the power plant. Case-studies are included in this study to show the effect of various operational parameters on the process efficiency. The analysis shows that the boiler is the major source of exergy destruction, because of the incomplete combustion process, and inappropriate insulations. The remedial actions are also suggested in the study.

IJERT-Second Law Based Thermodynamic Analysis of Cogeneration Plant

International Journal of Engineering Research and Technology (IJERT), 2014

https://www.ijert.org/second-law-based-thermodynamic-analysis-of-cogeneration-plant https://www.ijert.org/research/second-law-based-thermodynamic-analysis-of-cogeneration-plant-IJERTV3IS10149.pdf The first law of Thermodynamics is used to analyze the energy utilization, but it is unable to account quality aspect of energy. The second law based thermodynamic analysis or exergy analysis assesses the energy on quantity as well as the quality and enables us to identify the magnitude and locations of real energy losses, to improve the existing systems or processes. The present paper deals with exergy analysis performed on an operating 23MW e unit of lignite and Indonesian coal fired cogeneration power plant at Nirma Limited, Bhavnagar. The exergy losses occurred in CFBC boiler combustor, heat recovery system and back pressure turbine have been calculated and distribution of the exergy losses during the real time plant running conditions has been assessed. The First law efficiency and the Second law efficiency of the components have also been calculated. The major exergy losses were found within the heat recovery system of the boiler.

Thermal Analysis of Steam Turbine Power Plants

Steam are a major energy consumer. Optimising process operating conditions can considerably improve turbine water rate, which in turn will significantly reduce energy requirement. Various operating parameters affect condensing and back pressure turbine steam consumption and efficiency. The industrial sector is the largest energy consumer, accounting for about 30 % of total energy used. Fuel and energy prices are continuously rising. With the present trend of energy prices and scarcity of hydrocarbon resources lowering energy requirement is a top priority. Energy conservation benefits depend on the adopting minor or major modifications and using the latest technology. Turbines are designed for a particular operating conditions like steam inlet pressure, steam inlet temperature and turbine exhaust pressure/ exhaust vacuum, which affects the performance of the turbines in a significant way. Variations in these parameters affects the steam consumption in the turbines and also the turbine efficiency. The present study was done to improve the power output of the turbine, thermal efficiency and specific steam consumption in conventional steam power plants. Three cycles i.e regenerative cycle, superheater cycle and cogeneration cycle are considered to formulate the data and obtain a better result in steam turbine power plants.