Training Session on Energy Equipment Cogeneration Presentation from the “Energy Efficiency Guide for Industry in Asia” www.energyefficiency.asia.org 1 © UNEP 2006 Training Agenda: Cogeneration Introduction Types of cogeneration systems Assessment of cogeneration systems Energy efficiency opportunities 2 © UNEP 2006 Introduction What’s a Cogeneration/CHP System? • Generation of multiple forms of energy in one system: heat and power • Defined by its “prime movers” • • • • • Reciprocating engines Combustion or gas turbines, Steam turbines Microturbines Fuel cells 3 © UNEP 2006 Introduction Efficiency Advantage of CHP Conventional Generation (58% Overall Efficiency) 36 Units (Losses) Combined Heat & Power (85% Overall Efficiency) 60 24 Uni ts = 40% 68 100 40 34 Uni ts = 85% 6 Units (Losses) (UNESCAP, 2004) 10 Units (Losses) 4 © UNEP 2006 Introduction Benefits of Cogeneration / CHP) • Increased efficiency of energy conversion and use • Lower emissions, especially CO2 • Ability to use waste materials • Large cost savings • Opportunity to decentralize the electricity generation • Promoting liberalization in energy markets 5 © UNEP 2006 Training Agenda: Cogeneration Introduction Types of cogeneration systems Assessment of cogeneration systems Energy efficiency opportunities 6 © UNEP 2006 Type of Cogeneration Systems • Steam turbine • Gas turbine • Reciprocating engine • Other classifications: - Topping cycle - Bottoming cycle 7 © UNEP 2006 Type of Cogeneration Systems Steam Turbine Cogeneration System • Widely used in CHP applications • Oldest prime mover technology • Capacities: 50 kW to hundreds of MWs • Thermodynamic cycle is the “Rankin cycle” that uses a boiler • Most common types • Back pressure steam turbine • Extraction condensing steam turbine 8 © UNEP 2006 Type of Cogeneration Systems Back Pressure Steam Turbine • Steam exits the turbine at a higher pressure that the atmospheric HP Steam Boiler Advantages: -Simple configuration -Low capital cost -Low need of cooling water -High total efficiency Turbine Fuel Condensate Process LP Steam Figure: Back pressure steam turbine Disadvantages: -Larger steam turbine -Electrical load and output can not be matched 9 © UNEP 2006 Type of Cogeneration Systems Extraction Condensing Steam Turbine HP Steam • Steam obtained by extraction from an intermediate stage • Remaining steam is exhausted • Relatively high capital cost, lower total efficiency • Control of electrical power independent of thermal load Boiler Turbine Fuel LP Steam Condensate Process Condenser Figure: Extraction condensing steam turbine 10 © UNEP 2006 Type of Cogeneration Systems Gas Turbine Cogeneration System • Operate on thermodynamic “Brayton cycle” • atmospheric air compressed, heated, expanded • excess power used to produce power • Natural gas is most common fuel • 1MW to 100 MW range • Rapid developments in recent years • Two types: open and closed cycle 11 © UNEP 2006 Type of Cogeneration Systems Open Cycle Gas Turbine Exhaust Gases • Open Brayton cycle: atmospheric air at increased pressure to combustor • Old/small units: 15:1 New/large units: 30:1 Condensate from Process HRSG Steam to Process Combustor Fuel • Exhaust gas at 450600 oC • High pressure steam produced: can drive steam turbine G Generator Compressor Turbine Air Figure: Open cycle gas turbine cogeneration 12 © UNEP 2006 Type of Cogeneration Systems Closed Cycle Gas Turbine Heat Source • Working fluid circulates in a closed circuit and does not cause corrosion or erosion Heat Exchanger G Generator • Any fuel, nuclear or solar energy can be used Compressor Turbine Condensate from Process Steam to Process Figure: Closed Cycle Gas Turbine Cogeneration System 13 © UNEP 2006 Type of Cogeneration Systems Reciprocating Engine Cogeneration Systems • Used as direct mechanical drives • Many advantages: operation, efficiency, fuel costs • Used as direct mechanical drives • Four sources of usable waste heat Figure: Reciprocating engine cogeneration system 14 (UNESCAP, 2000) © UNEP 2006 Type of Cogeneration Systems Topping Cycle • Supplied fuel first produces power followed by thermal energy • Thermal energy is a by product used for process heat or other • Most popular method of cogeneration 15 © UNEP 2006 Type of Cogeneration Systems Bottoming Cycle • Primary fuel produces high temperature thermal energy • Rejected heat is used to generate power • Suitable for manufacturing processes 16 © UNEP 2006 Training Agenda: Cogeneration Introduction Types of cogeneration systems Assessment of cogeneration systems Energy efficiency opportunities 17 © UNEP 2006 Assessment of Cogeneration Systems Performance Terms & Definitions • Overall Plant Heat Rate (kCal/kWh): Ms x (hs hw) Power Output (kW ) Ms = Mass Flow Rate of Steam (kg/hr) hs = Enthalpy of Steam (kCal/kg) hw = Enthalpy of Feed Water (kCal/kg) • Overall Plant Fuel Rate (kg/kWh) Fuel Consumption * (kg / hr ) Power Output (kW ) 18 © UNEP 2006 Assessment of Cogeneration Systems Steam Turbine Performance • Steam turbine efficiency (%): Actual Enthalpy Drop across the Turbine (kCal / kg) x 100 Isentropic Enthalpy drop across the Turbine (kCal / kg) Gas Turbine Performance • Overall gas turbine efficiency (%) (turbine compressor): Power Output (kW ) x 860 x 100 Fuel Input for Gas Turbine (kg / hr ) x GCV of Fuel (kCal / kg) 19 © UNEP 2006 Assessment of Cogeneration Systems Heat Recovery Steam Generator (HRSG) Performance • Heat recovery steam generator efficiency (%): M s x ( hs hw ) [ M f x Cp (t in t out )] [ M aux x GCV of Fuel (kCal / kg)] Ms = Steam Generated (kg/hr) hs = Enthalpy of Steam (kCal/kg) hw = Enthalpy of Feed Water (kCal/kg) Mf = Mass flow of Flue Gas (kg/hr) t-in = Inlet Temperature of Flue Gas (0C) t-out = Outlet Temperature of Flue Gas (0C) Maux = Auxiliary Fuel Consumption (kg/hr) x 100 20 © UNEP 2006 Training Agenda: Cogeneration Introduction Types of cogeneration systems Assessment of cogeneration systems Energy efficiency opportunities 21 © UNEP 2006 Energy Efficiency Opportunities Steam Turbine Cogeneration System Steam turbine: • Keep condenser vacuum at optimum value • Keep steam temperature and pressure at optimum value • Avoid part load operation and starting & stopping Boiler & steam – see other chapters 22 © UNEP 2006 Energy Efficiency Opportunities Gas Turbine Cogeneration System Gas turbine – manage the following parameters: • • • • • Gas temperature and pressure Part load operation and starting & stopping Temperature of hot gas and exhaust gas Mass flow through gas turbine Air pressure Air compressors – see compressors chapter Heat recovery system generator – see waste heat recovery chapter 23 © UNEP 2006 Training Session on Energy Equipment Cogeneration THANK YOU FOR YOUR ATTENTION 24 © UNEP GERIAP Disclaimer and References • This PowerPoint training session was prepared as part of the project “Greenhouse Gas Emission Reduction from Industry in Asia and the Pacific” (GERIAP). While reasonable efforts have been made to ensure that the contents of this publication are factually correct and properly referenced, UNEP does not accept responsibility for the accuracy or completeness of the contents, and shall not be liable for any loss or damage that may be occasioned directly or indirectly through the use of, or reliance on, the contents of this publication. © UNEP, 2006. • The GERIAP project was funded by the Swedish International Development Cooperation Agency (Sida) • Full references are included in the textbook chapter that is available on www.energyefficiencyasia.org 25 © UNEP 2006