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Gas Turbine Handbook : Principles and Practices

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<strong>Gas</strong> <strong>Turbine</strong> Exhaust Treatment 139<br />

same amount of NO x<br />

reduction. Steam flow requirements are nominally<br />

1.5-2.0 times those required for water injection. The steam<br />

injection rate for a typical aeroderivative gas turbine operating at<br />

25 megawatts is 3.3% of the compressor inlet air flow. As a function<br />

of mass flow (steam to fuel), ratios of up to 2.4 by weight have been<br />

used 10 .<br />

However, there is also a limit to the amount of steam that may<br />

be injected into the gas turbine in general, <strong>and</strong> into the primary combustor<br />

zone in particular. The maximum total steam injection into the<br />

gas turbine is between 5% <strong>and</strong> 20% of existing air flow. The allowable<br />

amount of steam to be injected into the combustor primary zone is<br />

limited by the flameout characteristics of the combustor. Also the allowable<br />

amount of steam injected for power augmentation is set by<br />

mechanical considerations <strong>and</strong> compressor pressure ratio limitations.<br />

On a per-pound basis, steam contains more expansion energy<br />

than air; the Cp of steam is approximately twice the Cp of air. The<br />

power output gain from steam injection is about 4% for each 1% of<br />

steam injected (where % of steam injected refers to main turbine<br />

flow). The following graph (Figure 9-5) shows the effect of a constant<br />

5% steam injection on the load carrying ability of a typical gas turbine.<br />

For comparative purposes, the output variation with ambient<br />

temperature is shown for the same turbine without steam injection.<br />

SELECTIVE CATALYTIC REDUCTION<br />

Selective catalytic reduction (SCR) is a process in which NO x<br />

is removed from the exhaust gas stream by the injection of ammonia<br />

(NH 3<br />

) into the stream <strong>and</strong> the subsequent chemical reaction in<br />

the presence of a catalyst. For a given gas condition (temperature,<br />

gas composition, etc.) the performance of the SCR is a function of<br />

the catalyst type <strong>and</strong> geometry, the residence time of the gas in the<br />

reactor, <strong>and</strong> the amount of ammonia injected upstream of the reactor.<br />

Selection of the catalyst is specific to the temperature in which<br />

it is expected to operate. The ammonia utilized in the process may<br />

be either anhydrous or aqueous. The injection systems differ slightly<br />

depending on the type of ammonia injected. The basic chemical reactions<br />

11 are:

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