Main Feed Pumps Parts

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Filter By: Corrosion Preventive Anodes
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Part Number
NSN
NIIN
A15-3416 Corrosion Preventive Anode
007253999
MIL-A-18001 Corrosion Preventive Anode
005822011
MIL-A-18001 Corrosion Preventive Anode
007253999
MIL-A-18001 Corrosion Preventive Anode
008136053
MIL-A-18001 Corrosion Preventive Anode
008136054
MIL-A-18001 Corrosion Preventive Anode
008136055
MIL-A-18001KCLASS1TYPEZDM0.825 Corrosion Preventive Anode
007253999
MIL-A-18001KCLASS1TYPEZEPB4.0 Corrosion Preventive Anode
005822011
MIL-A-18001LCLASS1TYPEZEP4.0 Corrosion Preventive Anode
005822011
MIL-A-18001ZEP4B Corrosion Preventive Anode
005822011
MILA18001CLASS2TYPEZRN0.675-6FT Corrosion Preventive Anode
008136054
MILA18001KCLASS2TYPEZRN0.405-6FT Corrosion Preventive Anode
008136053
MILA18001KCLASS2TYPEZRN0.675-6FT Corrosion Preventive Anode
008136054
MILA18001KCLASS2TYPEZRN0.840-6FT Corrosion Preventive Anode
008136055
MILA18001LCLASS2TYPEZRN0.840-6FT Corrosion Preventive Anode
008136055
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Main Feed Pumps

Picture of Main Feed Pumps

A deaerating feed tank (DFT), often found in steam plants that propel ships, is located after the main condensate pump and before the main feed booster pump. It has these three purposes:

Based on the relevant theoretical Rankine cycle diagram, there are four main processes, or steps:

In the practical implementation of a Rankine cycle, it is common to break the single pump (process 1 to 2) into three pumps: (in water flow order: condensate pump, feed booster pump and then feedwater pump).

A surge volume allows the plant to change bells (power output level) without running the feed pump dry or flooding the turbines. Consider the plant running in a steady state condition.

The bell is increased, more power output demanded, the rate of feed is increased. This draws more water from the condenser, perhaps to the point of being dry and starving the boiler resulting in a loss of propulsion. This is until the water, converted to steam, provides its energy to the turbine and then is condensed in the condenser.

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