Improvement of the performance of thermal power systems through energy and exergy analysis
Table Of Contents
- Title page i
Approval Page ii
Certification iii
Dedication iv
Acknowledgements v
Nomenclature vii
Table of Contents xi
List of Tables xiv
List of Figures xix
Abstract xxiii
Chapter ONE
INTRODUCTION
- 1.0Background 1
- 1.1Energy Sources in Nigeria 3
- 1.2Electricity Generation in Nigeria 4
- 1.3Statement of Problem 7
- 1.4Aims and Objectives of the Study 8
- 1.5Scope of the Study 9
- 1.6Significance of the Study 9
- 1.7Study Area 10
Chapter TWO
LITERATURE REVIEW
- 2.0Energy Demand and Supply 11
- 2.1Overview of Thermal Power Plants 12
- 2.2Theoretical Review of Similar Works 15
Chapter THREE
SYSTEM DESIGN AND IMPLEMENTATION
- 3.0Conceptual Framework 19
- 3.1General Approach 19
- 3.2Sources of Data 20
- 3.3System Description 21
x
3.
- 3.1Case I- Egbin Steam Power Plant 21
3.
- 3.2Case II- Geregu I Gas Turbine Power Plant 24
- 3.4Assumptions for Power Plants Analysis 27
- 3.5Combustion Equation 28
- 3.6Air-Fuel Ratio 29
- 3.7Adiabatic Flame or Combustion Temperature 29
- 3.8Specific gravity, Volumetric and Mass Flow rate of Fuel 30
- 3.9Mass Balance 30
- 3.10Energy Balance Equation 31
3.
- 10.1Boiler/Steam Generator 31
3.
- 10.2Turbine Sub-system 32
3.
- 10.3Condenser Sub-system 33
3.
- 10.4Pump Sub – system 34
3.
- 10.5Feedwater Heater Sub-system 34
3.
- 10.6Deaerator 36
3.
- 10.7Drain Cooler 37
3.
- 10.8Cooling Water 37
3.
- 10.9Energy Analysis of the Plant 37
- 3.11Exergy Analysis 37
3.
- 11.1Exergy Balance Equation 38
3.
- 11.2Exergy destruction factor or efficiency defect 40
3.11.3Fuel Depletion Ratio 40
3.11.4Irreversibility Factor of a Component 40
3.
- 11.5Boiler/Steam Generator 40
3.
- 11.6Turbine Sub-system 41
3.
- 11.7Condenser Sub-system 42
3.
- 11.8Pump Sub-system 43
3.11.9Feedwater Heater Sub-system 44
3.11.10Deaerator 46
3.
- 11.11Cooling Water 46
3.11.12Drain Cooler 46
xi
3.11.13Exergy Efficiency of the Plant 48
3.11.14Exergetic Performance Coefficient of the Plant 48
3.11.15Exergetic Sustainability Indicators 48
- 3.12Air-standard Cycle for Geregu I Power plant 49
3.
- 12.1Energy Analysis of Compressor Sub-system 51
3.
- 12.2Energy Analysis of Combustion Chamber Sub-system 51
3.
- 12.3Energy Analysis of Turbine Sub-system 52
3.
- 12.4Thermal Efficiency of Gas Turbine Plant 53
- 3.13Exergy Analysis of Gas Turbine Plant 53
3.
- 13.1Exergy Analysis of Compressor Sub –system 53
3.
- 13.2Exergy Analysis of Combustion Chamber Sub-system 55
3.
- 13.3Exergy Analysis of Turbine Sub-system 56
3.
- 13.4Exergy Loss of Exhaust Sub-system 57
3.
- 13.5Gas Turbine Cycle Exergy Efficiency 57
Chapter FOUR
SYSTEM TESTING AND EVALUATION
- AND ANALYSIS
4.0Combustion Equation of Fuel used for Egbin Steam Power Plant 58
- 4.1Energy Analysis of Boiler/Steam generator 61
4.
- 1.1Exergy or Second Law Analysis of Boiler/Steam Generator 62
- 4.2Calculating ThermomechanicalExergy of Egbin Steam Power Plant 62
4.2.1Standard Chemical Exergy of the Hydrocarbons used in Egbin Steam 66
Power Plant
4.
- 2.2Calculating Chemical Exergy of Fuel used in Egbin Steam Power Plant 67
4.2.3Calculating Total Fuel Exergy of Egbin Steam Power Plant 68
4.
- 2.4Adiabatic Combustion Temperature for Egbin Steam Power Plant 68
4.3Energy and Exergy Analysis of Turbine Sub-system 71
4.
- 3.1Energy Analysis of High Pressure Turbine (HPT) 72
4.3.2Exergy Analysis of High Pressure Turbine (HPT) 74
4.
- 3.3Energy Analysis of Intermediate Pressure Turbine (IPT) 74
4.
- 3.4Exergy Analysis of Intermediate Pressure Turbine (IPT) 77
4.
- 3.5Energy Analysis of the Low Pressure Turbine(LPT) 78
4.
- 3.6Exergy Analysis of Low Pressure Turbine (LPT) 81
xii
- 4.4Energy Analysis of the Condenser Sub-system 82
4.
- 4.1Exergy Analysis of the Condenser Sub-system 83
- 4.5Energy Analysis of the Condenser Effective Pump (CEP) 83
4.
- 5.1Exergy Analysis of the Condenser Effective Pump(CEP) 85
4.
- 5.2Energy Analysis of the Boiler Feed Pump (BFP) 86
4.
- 5.3Exergy Analysis of the Boiler Feed Pump (BFP) 87
- 4.6Energy Analysis of High Pressure Feedwater Heater 6 88
4.
- 6.1Exergy Analysis of the High Pressure Feedwater Heater 6 89
4.
- 6.2Energy Analysis of High Pressure Feedwater Heater 5(HPH5) 90
4.
- 6.3Exergy Analysis of High Pressure Feedwater Heater 5(HPH5) 91
4.
- 6.4Energy Analysis of Low Pressure Feedwater Heater 3(LPH3) 92
4.
- 6.5Exergy Analysis of Low pressure Feedwater Heater 3(LPH3) 93
4.
- 6.6Energy Analysis of Low pressure Feedwater Heater 2(LPH2) 94
4.
- 6.7ExergyAnalysis of Low Pressure Feedwater Heater 2(LPH2) 95
4.
- 6.8Energy Analysis of Low pressure Feedwater Heater 1(LPH1) 96
4.
- 6.9Exergy Analysis of Low Pressure Feedwater Heater 1(LPH1) 97
4.
- 6.10Energy Analysis of the Deaerator 99
4.
- 6.11Exergy Analysis of the Deaerator 99
4.
- 6.12Energy Analysis of the Drain cooler 100
4.
- 6.13Exergy analysis of the Drain Cooler 101
4.6.14Energy and Exergy Analysis of the Cooling Water 101
4.6.15Energy and Exergy Analysis of the Power Plant 102
- 4.7Analysis of Air-Standard Cycle of Geregu I Power Plant 103
- 4.8Energy Analysis of Compressor Sub-system 104
4.
- 8.1Exergy Analysis of the Compressor Sub-system 106
4.
- 8.2Combustion Equation of Fuel used in Geregu I Gas Turbine Plant 108
4.
- 8.3Energy Analysis of Combustion Chamber Sub-system 111
4.
- 8.4Specific Heat of Combustion Products 112
4.
- 8.5Calculating the thermomechanicalExergy of fuel used in Geregu I gas
power plant 114
4.
- 8.6Standard Chemical Exergyof Hydrocarbons used in GereguI gas
power plant 117
xiii
4.
- 8.7Calculating Chemical Exergy of fuel used in Geregu I power plant 118
4.8.8Calculating Exergy destruction at the Combustion Chamber119
4.
- 8.9Calculating Fuel Exergy of Geregu I gas Turbine Power Plant 120
4.8.10Exergy Analysis of the Combustion Chamber Sub-system 120
4.8.11Adiabatic Flame or Combustion Temperature of Geregu I Power Plant 121
4.
- 8.12Energy Analysis of Turbine Sub-system 123
4.
- 8.13Exergy Analysis of Turbine Sub- system 132
4.
- 8.14Exergy Loss in the Exhaust Sub-system 134
4.8.15Thermal Efficiency of the Gas Turbine Cycle 134
4.
- 8.16Exergy Analysis of the Gas Turbine Cycle 135
Chapter FIVE
SUMMARY, CONCLUSION AND RECOMMENDATIONS
- RESULTS AND DISCUSSIONS
- 5.0Presentation of result of Egbin Steam Power Plant 136
- 5.1Improvements on Boiler/Steam Generator Performance of Egbin Power Plant 147
- 5.2Plant Performance indicators of Egbin steam power plant 167
- 5.3Presentation of result of Geregu I Gas Turbine Power Plant 173
5.4Improvement of the performance of the combustion chamber of Geregu I gas
turbine power plant 180
5.5Plant performance indicators of Geregu gas turbine plant 204
5.6Presentation of result of Air standard cycle analysis of GereguI gas
turbine plant 209
- 5.7Improvement on Power Output from Egbin and Geregu I Power Plants 210
5.8Comparison of the Efficienciesof Egbin and Geregu I Power Plants 212
Recommendation 215
Conclusion 215
REFERENCES
APPENDICES
Thesis Abstract
This research work is aimed at using the energy and exergy analysis with thermodynamic
data to suggest improvements in the performance of steam and gas turbine power plants. In
this regard, specific data from Egbin steam power plant and Geregu I gas turbine power plant
were used for the analysis. In the analysis, scientific tools such as Engineering Equation
Solver (EES) programme with built-in functions for most thermodynamic and transport
properties was used to calculate the enthalpy and entropy at various nodal points, while
EXCEL spreadsheet and SCILAB software code were used to analyze both the energetic and
exergetic efficiencies of the individual components, thermal efficiencies, gross station heat
rate etc. These software were also used to calculate the exegetic performance coefficient and
exegetic sustainability indicators of the power plants. The results of the analysis at both
design and operating conditions show that exergy destruction occur more in the boiler/steam
generator of Egbin steam power plant and combustion chamber of Geregu I gas turbine
power plant than in other major components of each plant. The normal operating conditions
of the steam boiler exit pressure and temperature are 125.70/540.72 and condenser pressure
and temperature are 0.0872bar and 42.950Crespectively for Egbin steam power plant in the
year 2009. From the study, the maximum exergy loss was found in the boiler/steam generator
with a value of 55.32% in the year. Changing the boiler exit pressure and temperature from
the normal operating conditions to 165.70/560.72 (ie, in step of 10 bar and 50C), the exergy
loss reduced to 53.99%.The cycle thermal energy and exergy efficiencies at the normal
operating conditions were 41.03% and 39.94 % respectively. Improvement in the cycle
thermal energy and exergy efficiencies with the same steps from normal operating conditions
to 165.70/560.72 were 41.23% and 40.12% respectively. The improvement increased the
power output from 197593.8KW to 199358.57kW showing power increase of 1764.77kW or
1.765MW. The gross station heat rate decreased from 8775kJ/kWh to 8732kJ/kWh which is
good for the life of the plant. Also, the improvement increased the exergetic performance
coefficient from 0.6133 to 0.6188. The exergy sustainability indicators such as
environmental effect factor decreased from the value 1.0412 to 1.0230 showing about 1.75%
reduction in hazardous gaseous emissions to the environment. Another exergy indicator, the
sustainability index factor increased from the value 0.9604 to 0.9775 indicating 1.78%
resource utilization and sustainability. For Geregu I gas turbine plant, the operating condition
Thesis Overview
<p>
</p><p>INTRODUCTION<br>1.0 Background<br>Thermal power plants are widely utilized throughout the world for electricity generation.<br>They include steam power plants, gas turbine power plants, nuclear power plants, internal<br>combustion engines. There are numerous aged and new thermal power plants that are in<br>service throughout the world today, for example, about 1,300 steam power plants have been in<br>service for more than 30 years in the USA, [1]. In recent years, global warming has been a<br>major issue due to continuous growth of greenhouse gas emissions from different sources.<br>The contributors to greenhouse effects are carbon dioxide (CO2), nitrogen dioxide (NO2) and<br>sulphur dioxide (SO2). Carbon dioxide is a major greenhouse gas which is mainly blamed for<br>global warming.<br>Different industrial processes such as power plants, oil refineries, fertilizer plants, cement and<br>steel plants are the main contributors of CO2 emission. Fossil fuels such as coal, oil and<br>natural gas are the main energy sources for power generation and will continue to generate<br>power due to large reserves and affordability. Demirbas, [2] reported that about 98% of CO2<br>emission results from fossil fuel combustion. Many power companies have investigated and<br>undertaken measures to improve the efficiencies of such power plants in order to minimize<br>their environmental impacts(e.g. by reducing emissions of CO2, NO2 and SO2), and to make<br>them more competitive, as deregulation of the power industry proceeds. Such investigations<br>have been based on energy consideration. It has also sparked interest in the scientific<br>community to take a closer look at the energy conversion devices and to develop new<br>techniques to better utilize the existing transfer and energy change.<br>The most commonly used method for analysis of an energy conversion system is the first law<br>of thermodynamics. Engineers and scientist have been traditionally applying the first law of<br>thermodynamics to calculate the enthalpy balances for more than a century to quantify the<br>loss of efficiency in a process due to loss of energy. However, the first law of<br>thermodynamics deals with the quantity of energy and asserts that energy cannot be created or<br>destroyed, [3]. This law serves as a necessary tool for accounting for energy during a process<br>and offers no challenges to the engineer. However, in recent years the second law analysis,<br>2<br>also known as exergy analysis of energy systems has more and more drawn the interest of<br>energy engineers and scientific community. Exergy analysis provides an effective technique<br>for measuring and optimizing performance of a thermal system by accounting for energy<br>quality. It can also be used to assess the sustainability level of energy systems. Sustainability<br>means a supply of energy resources that is sustainably available at reasonable cost and causes<br>no minimal negative effects. Sustainability is necessary to overcome current ecological,<br>economic, and developmental problems. The exergy sustainability indicators include exergy<br>efficiency, waste exergy ratio, recoverable exergy rate, exergy destruction factor,<br>environmental effect factor and exergetic sustainability index, [4].<br>For power plants, exergy analysis allows one to determine the maximum potential for<br>electricity production associated with the incoming fuel or any flow in the plant. This<br>maximum is achieved if the fuel or flow is utilized in processes that ultimately bring it to<br>complete thermodynamic equilibrium with the environment, while generating electricity<br>reversibly. Thus, exergy analysis provides the theoretical efficiency limitations upon any<br>power plant. Losses in the potential for electricity generation occur due to irreversibilities and<br>determined directly with exergy analysis. The exergy concept has gained considerable interest<br>in the thermodynamic analysis of thermal processes and plant systems since it has been seen<br>that the first law analysis has been insufficient from an energy performance point of view.<br>Based on the second law of thermodynamics, the exergy analysis represents the third step in<br>the plant system analysis, following the mass and the energy balances. The aim of the exergy<br>analysis is to identify the magnitudes and the locations of exergy losses, in order to improve<br>the existing systems, processes or components, or to develop new processes or systems, [5].<br>The method of exergy analysis is particularly suited for furthering the goal of more efficient<br>resource utilization, since it enables the location, and time magnitudes of wastes and losses to<br>be determined. Improved resource utilization can be realized by reducing exergy destruction<br>within a system. The objective in exergy analysis is to identify sites where exergy destructions<br>and losses occur and rank them for significance. Exergy losses include the exergy flowing to<br>the surroundings, whereas exergy destruction indicates the loss of exergy within the system<br>boundary due to irreversibility. This allows attention to be centered on the aspects of system<br>operation thatoffer the greatest opportunities for improvement, [6]. Exergy analysis which is<br>the combined first and second law analysis gives much more meaningful evaluation indicating<br>the association of irreversibilities or exergy destruction with combustion and heat transfer<br>3<br>processes. This allows thermodynamic evaluation of energy conservation option in power<br>and refrigeration cycles, thereby provides an indicator that points the direction in which<br>engineers should concentrate their efforts to improve the performance of thermal systems. The<br>second law of thermodynamics has proved to be a very powerful tool in the optimization of<br>complex thermodynamic systems, [7],[8],[9].<br>1.1 EnergySources in Nigeria<br>The country is endowed with both the conventional and the non-conventional energy<br>resources. The conventional comprises mostly of the non-renewable resources such as crude<br>petroleum oil, natural gas, coal, tar sand and uranium, [10]. The country has the tenth largest<br>oil and gas reserves in the world. The various non-conventional energy resources available in<br>the country that can be harnessed for power generation are nuclear, solar, wind power,<br>biomass energy, wave and tidal energy and geothermal energy. Nigeria’s near equatorial<br>location, extensive and diverge vegetation, prevailing trade winds and many rivers endow her<br>with large quantities and quality of renewable energy sources,[11].These include solar<br>radiation, hydro power, wind and biomass energy. Nigeria’s coal reserves are large and<br>estimated at 2.7 billion metric tonnes of which 650 million tonnes are proven reserves. About<br>95% of the Nigerian coal production in late 1950s and early 1960s was consumed locally,<br>mainly for railway transportation, electricity production and industrial heating in cement<br>production. Nigeria has abundant reserves of natural gas. The quantity of natural gas is at<br>least twice as much as the oil, and the horizon for the availability of natural gas is definitely<br>longer than that of oil. In energy terms, the quantity of natural gas used for electricity<br>generation is very significant. The known reserves of natural gas have been estimated at about<br>187.44 trillion standard cubic feet or 5.30 x 1012 standard cubic meters as at the year<br>2007,[12].<br>The third major source of energy, oil, is Nigeria’s major source of revenue used for<br>development. As at January 2005, Nigeria’s proven crude reserve stood at 35.2 billion barrels.<br>The majority of the reserves are found along the country’s coastal Niger Delta. As at 2007,<br>Nigeria’s energy resource availability expressed in barrels (bbls) and standard cubic feet (scf)<br>and other units showed that crude oil availability in Nigeria stood at 36.5 billion barrels. Other<br>energy resources include natural gas whose availability is 187.44 trillion standard cubic feet,<br>coal and lignite estimated at 2.7 billion tonnes as shown in Table 1.1<br>4<br>Table 1.1: Energy Resource Availability in Nigeria<br>RESOURCES AVAILABILITY<br>Crude oil 36.5 billion bbl<br>Natural gas 187.44 trillion scf<br>Coal and lignite 2.7 billion tones<br>Tar sands 31 billion bbl oil equivalent<br>Hydropower (large scale) 11,250mw<br>Hydropower (small scale) 3,500mw (estimate)<br>Solar radiation 3.5 – 7.0kwh/m2-day<br>Wind 2 – 4m/s annual average<br>Fuel wood 13.1 million ha of forest/wood land<br>Animal waste<br>Very significant<br>Quantity not available<br>Crop residue<br>Tidal energy<br>Uranium<br>Source: Energy Commission of Nigeria, 2007<br>Solar radiation intensity varies in a quasi-predictable way. It varies with day and night,<br>location, weather and climate. It increases with altitude and solar altitude angle. For instance,<br>at an altitude of 3,000m and solar altitude angle of 900 (i.e. overhead) it gets as high as<br>1.18KW/m2, while at sea levels it is < 1.0 KW/m2. It is reduced by cloudiness, atmospheric<br>gases, atmospheric particles (aerosols) and obstructions.<br>1.2 Electricity Generation in Nigeria<br>Generation of electricity is a very complex process involving many sub-processes and has<br>multiple critical parameters. A decline in thermal efficiency leads to a higher cost of<br>electricity generation due to more fuel usage and also will result in much higher carbon<br>deposits. Therefore, it is very important to stress on the performance of power plants.<br>Electricity generation is the conversion of other kinds of energy, mainly primary energy into<br>electrical energy. Generally, the process of generating electricity goes through several<br>5<br>transformations from primary energy directly into electricity. For instance, in a thermal power<br>station, the primary energy is converted to a high temperature steam, as an intermediate heat<br>source, then into mechanical energy in the turbine physically connected with the generators<br>where the electrical energy is produced.<br>Power generation in Nigeria is mainly from three technologies only which include hydroelectric<br>power stations, steam and gas thermal stations. Most of these facilities are being<br>managed by the Power Holding Company of Nigeria (PHCN); a government owned utility<br>company that coordinates all activities of the power sector such as generation, transmission,<br>distribution and marketing before they were privatized. Since inception of PHCN, the<br>authority expands annually in order to meet the ever increasing demand. Unfortunately, the<br>majority of Nigerians have no access to electricity and the supply to those provided is not<br>regular. In a bid to make the power sector more functional, the PHCN was unbundled into 18<br>successor companies (1 Transmission, 11 Distribution and 6 Generation companies). This was<br>done due to current privatization in the sector [13].<br>Prior to 1960s, energy supply and consumption consisted predominantly of non-commercial<br>energy, viz-fuel wood, charcoal, solar radiation, agricultural waste and residues. Major<br>commercial fuel was coal used in railway engines and for power generation. Contributions to<br>commercial energy came frompetroleum products (petrol and diesel) for road vehicles and<br>from electricity (from coal and diesel generators). Up till 2005, the grid electricity supply<br>industry was predominantly the vertically integrated public utility-National Electric Power<br>Authority (NEPA), which owned about 98% generating capacity and 100% of transmission<br>and distribution capacity. In consequence and in particular through former President<br>OlusegunObasanjo’s power project and President Goodluck Jonathan’s power road map for<br>power sector reform of August 2010, actual maximum peak generation has now more than<br>doubled (4300MW) since the start of the reform in 2000 and installed generation is now<br>above 10109.5MW, [13].<br>At present, the installed capacities in power stations in Nigeria are shown in Tables 1.2, 1.3<br>and 1.4 for pre-1999 power stations and other power stations as contained in a document<br>prepared by Energy Commission of Nigeriain 2007.<br>6<br>Table 1 .2: Pre- 1999 Power Stations<br>Station Capacity (MW)<br>Kainji Hydro 760<br>JebbaHydro 578<br>Shiroro Hydro 600<br>Egbin Thermal 1320<br>Sapale Thermal 1020<br>Ijora Thermal 60<br>Delta Thermal 912<br>Afam Thermal 711<br>Orji River Thermal 30<br>NESCO 30<br>Total 6,021MW<br>Source: Energy Commission of Nigeia,2007<br>Other power generating stations include eight National Integrated Power Project (NIPP)<br>which were built in some states of the country. These are Gbarain Integrated Power Project in<br>Bayelsa State, Egbema Integrated Power Project located in Imo State, Ibom Integrated Power<br>Project in AkwaIbom State.<br>Table1.3: National Integrated Power Project (NIPP)<br>Station Capacity(MW)<br>Gbarain, Bayelsa 225<br>Ihubor, Edo 451<br>Omoku, Rivers 230<br>Sapela,Delta 451<br>Egbema, Imo 338<br>Calabar, Cross Rivers 561<br>IkotAbasi, AkwaIbom 300<br>Ibom Power, AkwaIbom 188<br>Total 2,744MW<br>Source: Energy Commission of Nigeria, 2007<br>7<br>Another milestone in the power sector for electricity generation is the establishment of<br>Independent Power Producer (IPP) in different parts of the country. These include the AES<br>power station in Lagos State, Alaoji power station in Abia State, Papalanto power station in<br>Ogun State and others.<br>Table 1.4: Independent Power Producers (IPP)<br>Station Capacity(MW)<br>Geregu, Kogi 414<br>Omotosho, Ondo 335<br>Papalanto,Ogun 335<br>Alaoji, Abia 346<br>AES, Lagos 270<br>Geometric, Aba 140<br>Agip JV, Okpai/Kwale, Delta 480<br>Chevron JV, Agura,Igbin, Lagos 750<br>Total Fina, Obite, Rivers 500<br>Exxon Mobil Bonny, Rivers 500<br>Total 4070MW<br>Source: Energy Commission of Nigeria,2007<br>These National Integrated Power Projects (NIPPs) and Independent Power Producers (IPPs)<br>will augment the power generated by these power generating stations to meet the electricity<br>demand of the country.<br>1.3 Statement ofProblem<br>The global power sector is facing a number of issues, but the most fundamental challenge is<br>meeting the rapidly growing demand for energy services in a sustainable way. This challenge<br>is further compounded by the today’s volatile market-rising fuel costs, increased<br>environmental regulations etc. Thermal power plants are one of the most important elements<br>of energy sector and they are masterworks that enable production of electrical energy which<br>can be thought as one of the basic needs after food and water. Preference of the thermal power<br>8<br>plant type in electricity production is a big dilemma and prior discussion subject to related<br>parties in recent years. For instance, environmentalist act against fossil-fuelled thermal power<br>plants or nuclear power plants and they try to warn decision makers about environmental<br>pollution, global warming, carbon emission etc. The primary energy source possibilities of<br>countries are one of the basic factors that determine the preferences of a thermal power plant.<br>Namely, USA, Germany, India and China produce more than 50% of their electrical energy<br>by coal-fired thermal power plant, while most of the thermal power plants, in countries that<br>have abundance of natural gas such as Qatar, are gas fired. The choice is directly related to the<br>reserve capabilities of the primary energy sources which are one of the main issues for<br>government policies and preferences.<br>Today, many generating utilities are striving to improve the efficiency of their existing power<br>generating stations. The problem of low power generation output from these plants is as a<br>result of defective plant components and improper fuel utilization in the systems.<br>1.4 Aims and Objectives of the Study<br>The aim of this research is to<br>(i) Carry out energetic and exergetic performance analysis, at the design and actual<br>operating conditions for the existing unit 5 (220MW) of the 1320MW Egbin steam<br>power plant and unit 11(138MW) of the 414MW Geregu I gas turbine power plant in<br>order to identify the components that needs improvement.<br>The objectives of the study are to determine:<br>(i) the quantity of energy and exergy flows and location of losses.<br>(ii) the energy efficiency of the plant and its components.<br>(iii) plant performance parameters such as heat rate, specific fuel consumption and<br>thermal discharge index.<br>(iv) theexergy efficiency of the plant and its components.<br>(v) theexergy destructionswithin the system components.<br>(vi) exergetic performance coefficient.<br>(vii) exergetic sustainability indicators- exergy destruction ratio, waste exergy ratio,<br>environmental effect factor and exergetic sustainability index and<br>(viii) systems that have potential for significant performance improvement.<br>9<br>To achieve these objectives, we summarize thermodynamic models for the considered power<br>plants on mass, energy and exergy balance equations.<br>1.5 Scope of the Study<br>The scope of this work involves<br>Ø analysis of thermal power systems.<br>Ø determining the irreversibility rates in the plant components.<br>Ø comparative performance of the power plants at both design and operating<br>conditions,and<br>Ø performing sensitivity analysis on the variation of thermodynamic intensive properties<br>like temperature and pressure in improving the plants performance.<br>1.6 Significance of the Study<br>The growth, prosperity and national security of any country are critically dependent upon the<br>adequacy of its electricity supply industry. Over the past two decades, the stalled expansion<br>of Nigeria’s grid capacity, combined with the high cost of diesel and petrol has crippled the<br>growth of the country’s productive and commercial industries. It has stifled the creation of<br>jobs which are urgently needed in a country with a large and rapidly growing population; and<br>the erratic and unpredictable nature of electricity supply has engendered a deep and bitter<br>sense of frustration that is felt across the country as a whole and in its urban centers in<br>particular. Electricity consumers and the citizenry as a whole demand a fundamental reversal<br>of the long and debilitating malaise which has blighted the industry and, in doing so, bridled<br>the tremendous energy and creativity of this great and populous nation. More particularly they<br>demand real and immediate improvements in service levels, [14].<br>Nigeria needs over 10,000 MW of electricity for her domestic and industrial demands of<br>which about 4000MW is currently being generated from power plant locations across the<br>country. The quantity generated are transmitted and distributed through the national grid to<br>primary energy consumers. As a result of inefficient operation of some of these plants owing<br>to long age in service, the need to identify the location of the inefficiency in the plant becomes<br>imperative. Generally, the performance of thermal power plants is evaluated through energetic<br>performance criteria based on first law of thermodynamics, including electrical power and<br>thermal efficiency. In recent decades, the exergetic performance based on the second law of<br>10<br>thermodynamics has been found to be a useful method in the design, evaluation, optimization<br>and improvement of thermal power plants. The exergetic performance analysis can not only<br>determine magnitudes, location and causes of irreversibilities in the plants, but also provides<br>more meaningful assessment of plant individual components efficiency, [15]. The use of<br>exergy analysis becomes the answer as a tool for pin-pointing inefficiencies. The features of<br>this technique make it valuable in the thermodynamic analysis aiming at the improvement of<br>the efficiency of existing thermal plants through an adjustment of their operating parameters<br>or in the design of efficient new thermal plants.<br>1.7 Study Area<br>Nigeria is the most populous African country with the total population estimate of over 152<br>million people. She has over ten power generating stations (both thermal and hydro power<br>stations) established before the year 1999.<br>Besides having these power stations, there are eight National Integrated Power Projects<br>(NIPPs) established after the year 1999 and many Independent Power Producers (IPPs). For<br>the purpose of this study, the Egbinpower station and the Geregu power station will be<br>considered because the former uses steam and water as working fluid and the later uses air<br>and combustion products as working fluid where the boiler/steam generator and combustion<br>chamber are fired by natural gas. These power plants contribute good percentages of over 15.9<br>million MW of electricity consumed for both domestic and industrial use by the populace<br>annually.<br>Egbin thermal plant is located atIjede area of Ikorodu, a suburb of Lagos State. The plant was<br>commissioned in 1985 and consists of 6 units of 220 (6X220) MW (Reheat – Regenerative).<br>They are dual fired (gas and heavy oil) system with modern control equipment, single reheat;<br>six stages of regenerative feed heating. Natural gas is supplied to the plant directly from the<br>Nigerian Gas Company (NGC) Lagos operations department, which is annexed to the thermal<br>plant. Since Egbin thermal plant is located on the shores of the lagoon, cooling water for the<br>plant’s condensers is pumped from the lagoon into the water treatment plant en route to the<br>condensers.<br>The Geregu I gas thermal power station located in Ajaokuta, Kogi State of Nigeria was<br>commissionedin 2006 and it consists of three independent units, each being rated</p><p> </p>
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