| Typical operating role | Maximizes electricity production by expanding steam to a condenser. | Produces electricity while allowing controlled steam extraction for district heating or industrial use. | Discharges useful process or heating steam at a controlled pressure instead of condensing it fully. | Choose according to the project’s electricity demand, heat-offtake requirements, and seasonal load profile. |
| Typical electrical capacity | Approximately 5–40 MW for many municipal waste-to-energy plants. | Approximately 5–40 MW, depending on steam production and heat demand. | Approximately 1–30 MW, commonly selected for combined heat and power applications. | The generator rating should reflect normal, minimum, and maximum steam flows rather than boiler nameplate capacity alone. |
| Typical net electrical efficiency | About 18–30% of the waste feedstock’s lower heating value, depending on steam conditions and plant auxiliaries. | About 15–27% when substantial steam is extracted for heat use. | About 10–25% when optimized for useful heat delivery rather than electricity alone. | Use net efficiency after deducting fans, pumps, flue-gas treatment, conveyors, and other plant loads. |
| Overall CHP energy utilization | Usually lower when no useful heat market exists; excess condenser heat is rejected. | Typically about 55–85% when extracted steam has a stable heat customer. | Typically about 60–85% when the useful heat load is continuous and properly matched. | CHP performance depends more on heat utilization than on turbine design alone. |
| Indicative turbine-generator island cost | Approximately USD 1,000–2,500 per kW for equipment and installation allowance, excluding boiler, flue-gas treatment, buildings, and civil works. | Approximately USD 1,200–2,800 per kW because of extraction controls, valves, and additional steam-system equipment. | Approximately USD 900–2,200 per kW, depending on steam pressure, controls, and heat-delivery equipment. | Use these as early-stage planning ranges only; site conditions, currency, capacity, and contract scope can materially change costs. |
| Recommended steam conditions | Commonly about 40–65 bar(a) and 380–450°C for modern waste-to-energy service, subject to corrosion and deposit limits. | Commonly about 40–65 bar(a) and 380–450°C, with extraction pressures designed around the heat network. | Inlet conditions may be similar, while outlet steam pressure is often about 2–15 bar(a), depending on the process or heating system. | Higher pressure and temperature can improve efficiency but may increase corrosion, materials, inspection, and maintenance requirements. |
| Expected annual availability | Approximately 90–95% for a well-maintained plant with planned outage management. | Approximately 90–95%, with additional attention required for extraction valves and control systems. | Approximately 90–96% when steam demand is stable and the system is not frequently operated outside its design range. | Availability targets must include boiler outages, condenser limitations, grid restrictions, and waste-feed interruptions. |
| Design service life | Typically 25–30 years with periodic inspections, rotor assessment, and major overhauls. | Typically 25–30 years, subject to extraction-system integrity and control-system upgrades. | Typically 25–30 years, provided exhaust-pressure conditions and heat loads remain within design limits. | Require documented lifecycle support, spare-parts availability, and a planned modernization path for controls and electrical systems. |
| Major overhaul interval | Usually every 5–8 years, depending on operating hours, starts, vibration, and steam quality. | Usually every 5–8 years, with additional inspection of extraction stages and valves. | Usually every 5–8 years, depending on load cycling and exhaust-steam conditions. | Budget for outage labor, rotor inspection, seals, bearings, valve testing, generator testing, and control-system updates. |
| Primary operational risk | Condenser fouling, cooling-water restrictions, wet-steam erosion, and low-load efficiency loss. | Steam-demand fluctuations, extraction-valve failure, and unstable heat-network pressure. | Loss of the heat customer, excessive exhaust pressure, and inability to maintain the required process-steam conditions. | Complete a failure-mode review covering steam quality, condenser performance, grid connection, and heat-offtake reliability. |
| Key safety and design standards | Common references include IEC 60045-1 for steam turbines, IEC 60034 for rotating electrical machines, ASME B31.1 for power piping, ASME Boiler and Pressure Vessel Code for pressure equipment, EN 12952 for water-tube boilers where applicable, and NFPA 850 or equivalent fire-protection requirements. | The applicable legal requirements depend on the project country, pressure category, grid code, fire authority, and environmental permit. |
| Minimum performance guarantees to request | Net power output, steam rate, heat rate, generator efficiency, vibration limits, condenser back pressure, ramp rate, noise level, emissions-related auxiliary power, and guaranteed availability. | Guarantees should be measured using agreed test codes, defined ambient conditions, and clearly stated waste composition and steam-quality assumptions. |
| Best-fit project profile | Projects prioritizing electricity export and having limited or unreliable heat demand. | Projects with both electricity sales and a dependable district-heating or industrial heat customer. | Projects where useful heat has a high value and a stable year-round customer is available. | Select the configuration that maximizes risk-adjusted lifecycle revenue, not simply the highest rated electrical output. |