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Appendix E-2.c.i Energy Plan 2004-2013 Follow-up Studies and ...

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Re-powering Study for the Northport <strong>and</strong> Port Jefferson Power Stations<br />

<strong>Appendix</strong> II Northport System Descriptions<br />

A constant differential pressure is maintained across the HP drum level control valves by varying the<br />

speed of the feedwater pump.<br />

A motor operated on-off tight shutoff valve is provided downstream of the HP drum level control valve to<br />

prevent water leakage into the drum during start<strong>up</strong>.<br />

2.8.2 Intermediate Pressure Feedwater<br />

Each feedwater pump has an interstage bleed connection for IP feedwater s<strong>up</strong>ply to the HRSG IP<br />

economizer inlet. The connection is piped to a line containing a pressure gage, a check valve, <strong>and</strong> a gate<br />

valve. A branch line from the condensate system connects to the line to provide water to fill the IP drum.<br />

A branch from the line provides water for the HRSG reheater attemperator. This line has a gate valve <strong>and</strong><br />

a flow element <strong>and</strong> transmitter for DCS indication.<br />

Downstream of the branch connections there is a pressure transmitter. The IP feedwater line connects to<br />

the HRSG IP feedwater inlet connection. Downstream of the inlet connection, within the HRSG's<br />

vendors scope, there is a check valve, a manual gate valve, the IP economizer, a flow element with a flow<br />

transmitter, a temperature element, a drum level control valve with manual block <strong>and</strong> bypass valves, <strong>and</strong><br />

an air operated on-off tight shutoff valve. The flow signal, along with the drum level <strong>and</strong> steam flow<br />

signals, is used to position the drum level control valve.<br />

A branch line immediately downstream of the economizer <strong>and</strong> <strong>up</strong>stream of the drum level control valve<br />

provides the heating medium for the fuel gas heater.<br />

2.9 Fuel Gas<br />

Refer to PID-8-7A through 7D in <strong>Appendix</strong> III.<br />

The fuel gas delivered to Northport is AGA pipeline quality gas. No gas compressors are required.<br />

The fuel gas system (FGS) is designed to meet the requirements of the CTs including flow, pressure,<br />

temperature, moisture content, <strong>and</strong> cleanliness. To provide these requirements the FGS will include a<br />

pressure-reducing station, metering, filtration, gas heating, flow control, <strong>and</strong> scrubber with vent stack <strong>and</strong><br />

CH4 monitors to detect gas leakage.<br />

The FGS piping begins at the outlet of the gas s<strong>up</strong>pliers metering station. A single line is routed from the<br />

metering station, through a knockout drum <strong>and</strong> filter/separator to meet the CT cleanliness requirements.<br />

Liquids separated from the gas stream are automatically drained into a fuel gas drains tank. A<br />

containment area is provided under the drain for capturing spills. A knockout drum, designed to remove<br />

any liquids from the pipeline gas, will be installed at the interface with the gas s<strong>up</strong>plier <strong>up</strong>stream of the<br />

filter/separator.<br />

For The Backyard Option at Northport, a 100% capacity shell <strong>and</strong> tube fuel gas heat exchanger is<br />

provided for each gas turbine to raise the fuel temperature to the gas turbine manufacturer’s requirements.<br />

The source of heat for these is cycle steam. The fuel gas s<strong>up</strong>ply lines leaving the heaters are routed to<br />

their respective CT enclosures. The CT enclosures include the gas shutoff, vent, <strong>and</strong> control valves that<br />

control the flow of gas to the CTs.<br />

2.10 Aqueous Ammonia<br />

Refer to PID-08-17A in <strong>Appendix</strong> III.<br />

March 30, 2009 163

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