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coal selection criteria for industrial pfbc firing project 3.2 - CCSD

coal selection criteria for industrial pfbc firing project 3.2 - CCSD

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“Coal Selection Criteria <strong>for</strong> Industrial PFBC Firing”<br />

less free SiO2. Also, a maximum of 10% ash contained in the <strong>coal</strong> is needed to obtain an<br />

excellent result. Karita requires the soot and dust concentration at the gas turbine inlet to<br />

be 840 mg/Nm 3 or less.<br />

3.6.2 Gas Turbine Blade Corrosion<br />

Corrosion is due to fine ash particles and corrosive compounds of sulfur, alkali and<br />

alkaline earth elements contained in the <strong>coal</strong>s (Li, Chuming et al. 1991). As mentioned<br />

be<strong>for</strong>e, cyclones are not 100% effective and hence some particulates and corrosive<br />

compounds managed to escape and enter the gas turbine especially when the cyclones<br />

were clogged.<br />

Metal corrosion occurs as a result of complex chemical reactions at high temperature.<br />

Sulfur (SO2 and SO3) and alkali (Na2O and K2O) react to <strong>for</strong>m alkali sulfates with low<br />

melting points (Li, Chuming et al. 1991). Deposition of such sulfates in their molten state<br />

act as an adhesive to stick the micro particles on the blades, promoting complex chemical<br />

reactions <strong>for</strong>ming low melting point complexes impairing the oxide protection on the<br />

blade thereby exfoliating the metal surface by gas and particles flow (Li, Chuming et al.<br />

1991).<br />

To minimize the total alkali release from dolomites, an extremely pure metamorphic<br />

dolomite (e.g. Kaiser Dolowhite) may be used. Alkali removal sorbents, such as<br />

emathlite, have been tested <strong>for</strong> PFBC application. Up to a temperature of 1200 o C, either<br />

a packed bed of emathlite was placed after the cyclone or small emathlite particles were<br />

injected directly into the combustion products prior to the cyclone entrance to control the<br />

alkali to acceptable level (Newby, Keairns et al. 1989). To reduce this type of corrosion,<br />

it is recommended to operate the plant with <strong>coal</strong> that is low in sulfur and alkali, such as<br />

Australian black <strong>coal</strong>s.<br />

3.6.3 In-bed Heat Exchanger Tubes Erosion<br />

This type of erosion was experienced by Wakamatsu plant. The erosion mechanism is<br />

complicated due to the high operating temperature and the following interaction of<br />

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