part 1: overview of cogeneration and its status in asia - Fire
part 1: overview of cogeneration and its status in asia - Fire
part 1: overview of cogeneration and its status in asia - Fire
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State <strong>of</strong> art review <strong>of</strong> <strong>cogeneration</strong> 17<br />
Recuperators are used to <strong>in</strong>crease the power output <strong>of</strong> gas turb<strong>in</strong>e <strong>cogeneration</strong> systems if<br />
the heat dem<strong>and</strong>s are low. The recuperator is <strong>in</strong> fact only a heat exchanger that is employed<br />
to heat the air leav<strong>in</strong>g the compressor. The exhaust stream from the turb<strong>in</strong>e is passed<br />
through the recuperator before go<strong>in</strong>g <strong>in</strong>to the HRSG so that a <strong>part</strong> <strong>of</strong> the energy conta<strong>in</strong>ed <strong>in</strong><br />
turb<strong>in</strong>e exhaust is utilized <strong>in</strong> the recuperator. The gas turb<strong>in</strong>e <strong>cogeneration</strong> system with<br />
recuperator is sometimes known as the heat exchange cycle.<br />
2.4 Steam Turb<strong>in</strong>es<br />
Steam turb<strong>in</strong>es are the most commonly employed prime movers for <strong>cogeneration</strong><br />
applications, <strong>part</strong>icularly <strong>in</strong> <strong>in</strong>dustries <strong>and</strong> for district heat<strong>in</strong>g. The technology is well proven <strong>in</strong><br />
sugar <strong>and</strong> paper mills hav<strong>in</strong>g dem<strong>and</strong> for both electricity <strong>and</strong> large quantity <strong>of</strong> steam at high<br />
<strong>and</strong> low pressures. Some steam turb<strong>in</strong>e manufacturers are over 100 years old <strong>and</strong> have<br />
products rang<strong>in</strong>g from a few kW to 80 MW. However, turb<strong>in</strong>es below two MW may be<br />
uneconomical except where the fuel has no commercial value.<br />
A <strong>cogeneration</strong> system us<strong>in</strong>g a backpressure steam turb<strong>in</strong>e (see Figure 1.2) consists <strong>of</strong><br />
boiler, turb<strong>in</strong>e, heat exchanger <strong>and</strong> pump. In the steam turb<strong>in</strong>e, the <strong>in</strong>com<strong>in</strong>g high pressure<br />
steam is exp<strong>and</strong>ed to a lower pressure level, convert<strong>in</strong>g the thermal energy <strong>of</strong> high pressure<br />
steam to k<strong>in</strong>etic energy through nozzles <strong>and</strong> then to mechanical power through rotat<strong>in</strong>g<br />
blades. Thermal energy <strong>of</strong> the turb<strong>in</strong>e exhaust steam is then transferred to another fluid,<br />
water, air, etc., <strong>in</strong> a heat exchanger, provid<strong>in</strong>g heat to the processes. For <strong>in</strong>stance, the air<br />
heated by heat exchanger can be used to dry products <strong>in</strong> food process<strong>in</strong>g <strong>in</strong>dustries.<br />
Depend<strong>in</strong>g on the pressure (or temperature) levels at which process steam is required,<br />
backpressure steam turb<strong>in</strong>es can have different configurations. The most common types <strong>of</strong><br />
backpressure steam turb<strong>in</strong>es are shown <strong>in</strong> Figure 2.4. In extraction <strong>and</strong> double extraction<br />
backpressure turb<strong>in</strong>es, some amount <strong>of</strong> steam is extracted from the turb<strong>in</strong>e after be<strong>in</strong>g<br />
exp<strong>and</strong>ed to a certa<strong>in</strong> pressure level. The extracted steam meets the heat dem<strong>and</strong>s at<br />
pressure levels higher than the exhaust pressure <strong>of</strong> the steam turb<strong>in</strong>e.<br />
The backpressure steam turb<strong>in</strong>e has a higher heat to power ratio <strong>and</strong> higher overall<br />
efficiency. Furthermore, back pressure turb<strong>in</strong>e <strong>cogeneration</strong> systems need less auxiliary<br />
equipment than condens<strong>in</strong>g systems, lead<strong>in</strong>g to lower <strong>in</strong>itial <strong>in</strong>vestment costs.<br />
The extraction condens<strong>in</strong>g turb<strong>in</strong>es have higher power to heat ratio <strong>in</strong> comparison with<br />
backpressure turb<strong>in</strong>es. Although condens<strong>in</strong>g systems need more auxiliary equipment such<br />
as the condenser <strong>and</strong> cool<strong>in</strong>g towers, better match<strong>in</strong>g <strong>of</strong> electrical power <strong>and</strong> heat dem<strong>and</strong><br />
can be obta<strong>in</strong>ed where electricity dem<strong>and</strong> is much higher than the steam dem<strong>and</strong> <strong>and</strong> the<br />
load patterns are highly fluctuat<strong>in</strong>g.<br />
In the reheat cycle, steam is extracted from the turb<strong>in</strong>e <strong>and</strong> reheated <strong>in</strong> the boiler dur<strong>in</strong>g the<br />
expansion process. Reheat cycles improve the overall thermal efficiency <strong>and</strong> elim<strong>in</strong>ate any<br />
moisture that may form as the steam pressure <strong>and</strong> temperature are lowered <strong>in</strong> the turb<strong>in</strong>e.<br />
Steam turb<strong>in</strong>es may also <strong>in</strong>clude a regenerative cycle where the steam is extracted from the<br />
turb<strong>in</strong>e <strong>and</strong> used to preheat the boiler feedwater.<br />
The efficiency <strong>of</strong> a backpressure steam turb<strong>in</strong>e <strong>cogeneration</strong> system is the highest. In cases<br />
where 100 per cent backpressure exhaust steam is used, the only <strong>in</strong>efficiencies are gear<br />
drive <strong>and</strong> electric generator losses, <strong>and</strong> the <strong>in</strong>efficiency <strong>of</strong> steam generation. Therefore, with<br />
an efficient boiler, the overall thermal efficiency <strong>of</strong> the system could reach as much as 90 per<br />
cent.