| |
||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
|
||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||||
|
Reciprocating
engines
(5 kW-7 MW) |
|
|
Combustion
turbines
(500 kW-25 MW) |
![]() |
|
Microturbines
(25-500 kW) |
![]() |
Backpressure Steam Turbine (50 kW and up) |
![]() |
|
Fuel
cells
(1 kW-10 MW) |
![]() |
CHP systems should always be able to exceed the total fuel efficiency of even the best central power plants, dividing the energy content of the fuel inputs into the delivered energy content of the total useful output, and taking average transmission and distribution line losses into account. A state-of-the-art central plant (a combined cycle combustion turbine using natural gas) offers a maximum system fuel efficiency for delivered power in the range of 55-60%. At this efficiency level, CHP systems will effectively double the central electric system's average delivered fuel-use efficiency of about 30%. However, under common circumstances, CHP systems will achieve efficiencies exceeding 70%. CHP systems achieving efficiencies exceeding 80% are frequent, and some systems have been shown to reach levels in excess of 90%.
For these reasons, while USCHPA seeks policies to recognize and provide incentive for any CHP systems that can reduce energy waste compared to the current central system power production, USCHPA is willing to accept a requirement that CHP systems qualify for incentives only when they can demonstrate efficiency exceeding the best of the central-station power plants on a delivered power basis; i.e., achieve a useful energy output representing at least 60% of the gross energy input into the CHP system's prime mover.
A Resource Dynamics Corporation report for DOE, Integrated Energy Systems (IES) for Buildings: A Market Assessment, August 2002, gives the following costs and performance data for CHP prime mover technologies. Backpressure steam turbine information was compiled by USCHPA member Turbosteam:
Reciprocating Engine Turbine and Microturbine Size 30kW-8MW 30kW-20MW+ Installed cost
($/kW)*300-1500 350-1500 Electrical efficiency (LHV) 28-42% 14-40% Overall efficiency** ~80-85% ~85-90% Variable O&M costs ($/kWh) 0.0075-0.02 0.004-0.01 Footprint (m2/kW) 0.02-0.03 0.01-0.03 Emissions (g/kWh unless otherwise noted) Diesel: NOx: 9.9-11, CO: 0.45-0.9
Natural gas: NOx: 0.07-1.7, CO: 1.8-2.7NOx: 3-50ppm
CO: 3-50ppmFuels Diesel, natural gas, gasoline, digester gas, biomass and landfill gas; larger units can use dual fuel (gas/diesel) or heavy fuels Natural gas, diesel, kerosene, naphtha, methanol, ethanol, alcohol, flare gas, digester gas, biomass and landfill gas *Cost varies significantly based on siting and interconnection requirements, as well as unit size and configuration.
**Assuming CHP.
Fuel Cell Backpressure Steam Turbine Size 100-3000kW 50 kW and up Installed cost
($/kW)*2000-5000 300-2000 Electrical efficiency (LHV) 40-57% >70% (marginal basis) Overall efficiency** ~80-85% >80% Variable O&M costs ($/kWh) 0.002-0.05 <0.01 Footprint (m2/kW) 0.08 0.004 - 0.03 Emissions (g/kWh unless otherwise noted) NOx:<0.02
CO: <0.01Depends on boiler fuel. However, no need to obtain permits for back-pressure units Fuels Natural gas, propane, digester gas, biomass and landfill gas (potentially) All *Cost varies significantly based on siting and interconnection requirements, as well as unit size and configuration.
**Assuming CHP.
![]()
Heat Recovery Units (HRUs). These units capture heat from the prime mover that can then be used to drive an absorption chiller, run a desiccant dehumidifier, or make hot water or steam for heating.
Absorption Chillers. Chillers transfer recovered heat from prime movers to a heat sink through an absorbent fluid and a refrigerant. The chiller accomplishes its cooling effect by absorbing and then releasing water vapor into and out of a lithium bromide solution.
Desiccant Dehumidifiers. Desiccants use drying agents to remove water from the air being used to condition building space by exposing the desiccant material (such as silica gel, activated alumina, lithium chloride salt, and molecular sieves) to a high relative humidity air stream-allowing it to attract and retain some of the water vapor-and then to a lower relative humidity air stream, which draws the retained moisture from the desiccant.
For more on desiccant technologies, visit NREL's Distributed Thermal Energy Technologies Program site. ORNL's Heating and Cooling Equipment R&D site also has technical details on CHP applications.
![]()
Packaged CHP Systems. According to the DOE, "packaged CHP systems" integrated into commercial buildings can offer up to a 30-40 percent improvement in building efficiency over today's best practices. CHP component manufacturers and DOE are developing pre-engineered, modular CHP systems to make it easier for building owners to connect CHP systems to power, piping, or ducting systems.
Heat Recovery Steam Generator (HRSG). The waste heat generated by a combustion turbine can be used to generate steam in a heat recovery steam generator (HRSG), which can power a steam turbine, heat living space, or generate cooling using steam-driven chillers.
The advantages of these types of systems are inexpensive electrical power and better reliability since the user may be independent from the grid. These systems can be started even if the grid has failed.
According to IDEA, 170 MW Grays Ferry Cogeneration Facility in Philadelphia provides utility district steam service to over 400 buildings downtown
Reduced annual emissions by over 74% (from 2,880 tons to 898 tons in 1998) Fuel efficiency has doubled
![]()
MORE
View the National CHP Project Spotlight
CHP Market Studies page offers opportunities for the various CHP technologies.