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CHAPTER 2
TYPES & ASSESSMENT PARAMETERS
Combined heat and power (CHP, also known as cogeneration) can provide thermal
energy for buildings or processes, while simultaneously generating part of the
electricity needed at the site.
2.1 CLASSIFICATION OF COGENERATION SYSTEMS
Cogeneration systems are normally classified according to the sequence of energy use
and the operating schemes adopted.
A cogeneration system can be classified as either a topping or a bottoming cycle on
the basis of the sequence of energy use. In a topping cycle, the fuel supplied is used to
first produce power and then thermal energy, which is the by-product of the cycle and
is used to satisfy process heat or other thermal requirements. Topping cycle
cogeneration is widely used and is the most popular method of cogeneration.
2.1.1 BOTTOMING CYCLE
In a bottoming cycle, the primary fuel produces high temperature thermal energy and
the heat rejected from the process is used to generate power through a recovery boiler
and a turbine generator. Bottoming cycles are suitable for manufacturing processes
that require heat at high temperature in furnaces and kilns, and reject heat at
significantly high temperatures. Typical areas of application include cement, steel,
ceramic, gas and petrochemical industries.
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FIG 2.1 Bottoming Cycle
2.1.2 TOPPING CYCLE
The four types of topping cycle cogeneration systems are briefly explained infollowing table
Table 2.1 Types of topping Cycles
A gas turbine or diesel
engine producing electrical
or mechanical power
followed by a heat recovery
boiler to create steam to
drive a secondary steam
turbine. This is called acombined-cycle topping
system.
The second type of system
burns fuel (any type) to
produce high-pressure
steam that then passes
through a steam turbine to
produce power with the
exhaust provides lowpressure process steam.
This is a steam-turbine
topping system.
A third type employs heat
recovery from an engine
exhaust and/or jacket
cooling system flowing to a
heat recovery boiler, where
it is converted to process
steam / hot water for furtheruse.
The fourth type is a gas
turbine topping system. A
natural gas turbine drives a
generator. The exhaust gas
goes to a heat recovery
boiler that makes process
steam and process heat
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2.2 ASSESSMENT PARAMETERS OF COGENERATION
SYSTEMS
Before proceeding with the description of cogeneration technologies, it is necessary to
define certain indices, which reveal the thermodynamic performance of a
cogeneration system and facilitate the comparison of alternative solutions (systems).
Numerous indices have appeared in the literature. The most important of those are
defined in this chapter:
Efficiency of the prime mover (e.g. of gas turbine, Diesel engine, steam turbine):
where
shaft power of the prime mover,
fuel power (flux of the fuel energy) consumed by the system.
fuel mass flow rate,
lower heating value of fuel.
Electrical efficiency:
Where is the net electric power output of the system, i.e. the electric power
consumed by auxiliary equipment has been subtracted from the electric power of the
generator.
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Thermal efficiency:
where
is the useful thermal power output of the cogeneration system.
Total energy efficiency of the cogeneration system:
The quality of heat is lower than the quality of electricity and it is decreasing with the
temperature at which it is available. For example the quality of heat in the form of hot
water is lower than the quality of heat in the form of steam. Consequently, one may
say that it is not very proper to add electricity and heat, as it appears in Eq. (2.5).
Therefore following relations are also used:
Power to heat ratio:
Table Heat-to-power ratios and other parameters of cogeneration systems
CogenerationSystem Heat-to-powerratio (kWth/
kWe)
Power output(asper cent of fuelinput)
Overallefficiency(percent)
Back-pressure steamturbine
4.0-14.3 14-28 84-92
Extraction-condensingsteam turbine
2.0-10.0 22-40 60-80
Gas turbine 1.3-2.0 24-35 70-85
Combined cycle 1.0-1.7 34-40 69-83
Reciprocating engine 1.1-2.5 33-53 75-85
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Fuel energy savings ratio:
where
total fuel power for separate production of and ,
fuel power of the cogeneration system producing the same amounts of and
In order for a cogeneration system to be a rational choice from the point of view of
energy savings, it must be FESR > 0.
Equations (2.3)-(2.6) lead to the following relations:
It should be mentioned that the power to heat ratio is one of the main characteristics
for selecting a cogeneration system for a particular application.
2.4 COGENERATION IS MOST ATTRACTIVE WHEN
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The demand for both steam and power is balanced i.e. consistent with the
range of steam: power output ratios that can be obtained from a suitable
cogeneration plant.
A single plant or group of plants has sufficient demand for steam and power to
permit economies of scale to be achieved.
Peaks and troughs in demand can be managed or, in the case of electricity,
adequate backup supplies can be obtained from the utility company.
Table 7.3: Typical Heat: Power Ratios for Certain Energy Intensive Industries
Industry Minimum Maximum Average
Breweries 1.1 4.5 3.1
Pharmaceuticals 1.5 2.5 2.0
Fertilizer 0.8 3.0 2.0
Food 0.8 2.5 1.2
Paper 1.5 2.5 1.9
The ratio of heat to power required by a site may vary during different times of theday and seasons of the year. Importing power from the grid can make up a shortfall in
electrical output from the cogeneration unit and firing standby boilers can satisfy
additional heat demand. Many large cogeneration units utilize supplementary or boost
firing of the exhaust gases in order to modify the heat: power ratio of the system to
match site loads.
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