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CO 2 Capture Study<br />

For <strong>800</strong> <strong>MW</strong> <strong>Power</strong> <strong>Plant</strong> – Tjeldbergodden<br />

1. The alternative of using an auxiliary boiler to provide <strong>the</strong> steam <strong>for</strong> <strong>the</strong><br />

CO2 capture plant has been demonstrated to be of lesser <strong>the</strong>rmal<br />

efficiency<br />

If <strong>the</strong> rules of integration are to be followed <strong>the</strong>n <strong>the</strong> alternatives are:<br />

2. Install <strong>the</strong> optimum steam turbine <strong>for</strong> <strong>the</strong> capture case and accept <strong>the</strong><br />

inefficiency resulting while <strong>the</strong> capture plant is not present.<br />

3. Install <strong>the</strong> optimum steam turbine <strong>for</strong> <strong>the</strong> capture case and add a small<br />

steam turbine to accept <strong>the</strong> steam which will be used by <strong>the</strong> capture plant<br />

when it is eventually commissioned<br />

4. Install <strong>the</strong> optimum steam turbine <strong>for</strong> <strong>the</strong> non-capture case and accept <strong>the</strong><br />

inefficiency resulting after <strong>the</strong> capture plant is commissioned and <strong>the</strong><br />

plant will be configured as shown below<br />

HP Steam<br />

Source<br />

Reheat<br />

Coils<br />

IP Steam<br />

Source<br />

LP Steam<br />

Source<br />

Condenser<br />

Steam to CO 2<br />

capture plant<br />

Steam Circuit <strong>for</strong> CCGT <strong>Power</strong> <strong>Plant</strong> with steam extraction <strong>for</strong> CO 2<br />

capture plant<br />

GT-Master versions of <strong>the</strong> abated and non-abated cases were made and<br />

used to demonstrate each case in <strong>the</strong> off design <strong>for</strong>m. The net <strong>the</strong>rmal<br />

efficiencies obtained are:<br />

With Extract Without Extract<br />

Small LP Turbine (Abated case) 51.71% 55.31%<br />

Large LP Turbine (Non-abated case) 51.50% 56.63%<br />

In reality <strong>the</strong>se results show so little difference between ei<strong>the</strong>r configuration of<br />

turbine that <strong>the</strong>re is no point in considering <strong>the</strong> addition of a small temporary<br />

turbine (alternative 3 above). Alternative 4 will give a marginally greater<br />

output until <strong>the</strong> Carbon dioxide capture plant is commissioned but <strong>the</strong> capital<br />

cost of <strong>the</strong> turbine is likely to be higher. It is suggested that options 2 & 4<br />

should be developed during detailed design with a turbine supplier when <strong>the</strong><br />

costs can be developed in greater detail and when <strong>the</strong> minor per<strong>for</strong>mance<br />

differences can be quantified with assurance.<br />

CB2005-0022_Final Report.Doc

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