(70) Therefore, the risk of sulphuric acid dew point attack ... - DTI Home
(70) Therefore, the risk of sulphuric acid dew point attack ... - DTI Home
(70) Therefore, the risk of sulphuric acid dew point attack ... - DTI Home
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HRSG, <strong>the</strong> steam itself is originally raised within <strong>the</strong> gasifier). The cooled<br />
gases are <strong>the</strong>n exhausted via <strong>the</strong> stack to atmosphere.<br />
The condensate from <strong>the</strong> low pressure LP steam turbine is passed through a<br />
condensate preheater prior to entry to <strong>the</strong> deaerator. Here <strong>the</strong> incoming water<br />
is heated by direct contact with steam. From <strong>the</strong> deaerator, <strong>the</strong>re are three<br />
supply lines to <strong>the</strong> HRSG, namely <strong>the</strong> HP, IP and LP lines.<br />
The LP pump supplies feedwater directly to an LP evaporator within <strong>the</strong><br />
HRSG. Following evaporation, some saturated steam is extracted after <strong>the</strong> LP<br />
evaporator and used in <strong>the</strong> dryer to remove moisture from <strong>the</strong> incoming<br />
pulverised fuel (PF). The remaining saturated steam from <strong>the</strong> evaporator feeds<br />
into <strong>the</strong> LP superheater. After being superheated, <strong>the</strong> LP steam is split into two<br />
lines. One line supplies <strong>the</strong> superheated LP steam to <strong>the</strong> LP turbine ano<strong>the</strong>r<br />
recirculates <strong>the</strong> LP superheated steam back to <strong>the</strong> deareator.<br />
The IP pump supplies feed water to <strong>the</strong> syngas cooler and gasifier membrane<br />
wall where <strong>the</strong> heat from <strong>the</strong> gasification process is utilised to generate IP<br />
steam as previously described. Some steam is also bled <strong>of</strong>f and fed to <strong>the</strong><br />
gasifier itself as part <strong>of</strong> <strong>the</strong> gasification process. The IP steam from <strong>the</strong> gasifier<br />
is <strong>the</strong>n fed into <strong>the</strong> HRSG for superheating. Following superheating, <strong>the</strong> IP<br />
steam is added to <strong>the</strong> exit line from <strong>the</strong> HP turbine. These lines combine and<br />
are reheated in <strong>the</strong> HRSG before entering <strong>the</strong> IP turbine.<br />
The HP pump supplies feedwater to <strong>the</strong> high-pressure, low-temperature<br />
(HP/LT) economiser and <strong>the</strong>n on to <strong>the</strong> HP/HT economiser. Upon leaving <strong>the</strong><br />
HP/HT economiser, feedwater is extracted to supply <strong>the</strong> waste heat boiler<br />
within <strong>the</strong> gasifier (see above) as well as supplying a source <strong>of</strong> heat for <strong>the</strong><br />
clean fuel gas line. Saturated steam is <strong>the</strong>refore produced from both <strong>the</strong> HP<br />
evaporator within <strong>the</strong> HRSG and <strong>the</strong> waste heat boiler within <strong>the</strong> gasifier. The<br />
two steam lines <strong>the</strong>n recombine to be superheated within <strong>the</strong> HRSG. The<br />
superheated HP steam is <strong>the</strong>n fed to <strong>the</strong> HP turbine for power generation.<br />
The IP turbine steam supply consists <strong>of</strong> <strong>the</strong> HP turbine exit flow combined<br />
with <strong>the</strong> HRSG IP line. The LP turbine steam supply consists <strong>of</strong> <strong>the</strong> IP turbine<br />
exit flow combined with <strong>the</strong> HRSG LP line.<br />
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