1-During cold start up turbine inlet steam minimum temperature should be saturation
temperature at the particular pressure + 50 Deg C.
Example: Turbine operating at 67 kg/cm2 pressure, its
inlet steam temperature should be285+50 =335 deg C
2-Distinguishing the Turbine starts up types.
- Cold start
up-
when HP and IP inner casing temperature is lower or equal 170oC
- Warm
start up-
when HP and IP inner casing temperature is lower or equal 430oC
- Hot start
up –
when HP and IP inner casing temperature is greater than 430oC.
3-To open ESV the vacuum should be at
least 0.3 Kg/cm2A (-0.73 kg/cm2)
4-In turbine rotors, over speed trip
bolt is always fitted at the DE side only. This is because, not weaken the Turbine
NDE side shaft, as NDE side shaft size is already made small & drilled for
key ways
5-Expansion bellows for lube oil lines
are fitted at the Turbine front bearings, as Turbine expansion occurs towards
front end
6-In oil cooler heat exchangers,oil
pressure is always kept at higher side than water pressure. This is to avoid
entry oil water in lube oil system.
7-In many Turbine, control oil (oil used for HP, LP valves actuators & ESV) is used at higher
temperature 55-60 deg C.This is because “Actuators & ESV components are
operating at very less clearance need low oil viscosity.
8-Control oil filters are of lesser filter size as compared
to lube oil filters.
Generally
filters are designed based on the minimum clearance through which the oil flow,
hence lube oil filters are of higher openings (25 to 40 microns) as bearings clearance will be in the
range of 200 microns to 500 microns. Control oil filters are of lesser size
openings (10 to 25 microns) , as discussed earlier Actuators & ESV components are operating at
very less clearance up to 50 microns.
9-Positive displacement
Lube oil pumps have in built as well as external PRVs (Fitted at the discharge
line).Lube oil pumps (Positive displacement pumps) are always started with discharge valve open unlike centrifugal pumps
10-Emergency oil pump do
not have PRVs
11-Emergency oil pumps flow capacity = Main/Auxiliary oil pump X 25%
12-Emergency oil pump
pressure = Main oil pump pressure X 30%
13-Control oil pumps flow capacity = Main/Auxiliary oil pump X 10%
14-For lube oil coolers:
Cooling water flow = Oil flow X 2
15-For lube oil coolers
, Heat load in KW = Cooler surface area X 5.3
16-Turbine lube oil
consumes 30 to 35% of total cooling water required for plant auxiliary
17-Generator air cooler
consumes 20 to 25% of total cooling water required for plant auxiliary
18-Bearing inlet oil pressure during high rotor speed (Normal
operation) is lesser than that of low speed (During barring gear operation)
19-There is always off set
alignment between Turbine rotor & Gear box pinion shaft. This is for accommodating
the misalignment during operation, as Gear box is operating at higher oil
temperature than Turbine.
Generally Gear box pinion
shaft is kept at lower level (0.15 to 0.3 mm) & offset side depends on the
direction of rotation of Turbine shaft viewed from turbine front end. If
Turbine rotor is rotating clockwise then offset is towards RHS.
20-Low oil temperature can
damage the Turbine bearings: Because;
When temperature
decreases too much, oil in the bearing becomes so viscous that it clings to the
shaft surface which drags it around the bearing. This makes the oil wedge in
the bearing lose. its stability. The pulsating wedge excites high rotor
vibration referred to as oil whip or oil whirl.
Too low temperature - and hence, too large
viscosity - of the bearing inlet oil causes the bearing oil flow to decrease
due to increased friction in the oil supply piping. The reduced oil flow may be
too small for adequate cooling, causing bearing overheating and possible
damage.
21-Slight sub atmospheric
pressure is maintained inside the bearing housing and its drain line by the
vapour extraction fans installed on the lube oil tank cover. Why is this
pressure maintained?
First.
To prevent oil mist
from escaping past the bearing oil seals into the turbine hall.
Second.
To prevent accumulation of hydrogen and oil
vapour in the lube oil tank atmosphere, which could create an explosion hazard
·
22-For lube oil:
During normal
operation, water is removed from the oil by the oil purifier and the vapour extraction
fans. During a long outage, water can also be drained from the bottom of the
lube oil tank.
23-Main oil tank level:
The major adverse
consequence/operating concern caused by too low tank level is impaired pump
performance due to cavitation and possibly vapour locking or gas locking. The
lower the oil level, the smaller the suction head of the pumps in the tank. Pump
cavitation and eventually vapour locking can result. The lowered level can also
lead to ingress of gases from the tank atmosphere into the pump suction piping,
and then the pump itself. An excessive accumulation of gases in the pump can
decrease its capacity, and finally result in pump gas locking. Too high tank
level increases the risk of tank overfill. The resultant oil spill has its own adverse consequences
such as an environmental hazard.
24-Rotor lift
due to jacking oil pressure
Drive end :0.1
mm & NDE :0.05 mm
The jacking oil pressure at the bearing inlet is not
controlled. As the oil is supplied by a positive displacement pump,
its pressure rises until the bearing resistance to the
oil flow is overcome. This happens when the turbine generator rotor is lifted off
the bearings.
25-Wheel
chamber pressure = (Turbine inlet pressure X Turbine load in MW X 0.6)/Turbine
Capacity in MW
26-Steam
condensers has fixed support at cooling water inlet side & sliding support
at the opposite side
27-Surface condensers installed at higher elevation are always producing lower vacuum.Power plants installed at or near the sea produce high vacuum
28-At steam condensers Vacuum breaker valves are provided to bring down the rotor speed to zero as early as possible
29-Closing time of ESV & HP control valves are 0.3 to 0.4 seconds and 0.4 to 0.6 seconds respectively
30-Pressure of N2 gas in control oil accumulator is 2 to 3 kg/cm2 lesser than control oil line pressure
29-Closing time of ESV & HP control valves are 0.3 to 0.4 seconds and 0.4 to 0.6 seconds respectively
30-Pressure of N2 gas in control oil accumulator is 2 to 3 kg/cm2 lesser than control oil line pressure
31-For STG: Bearing temperature trend goes on decreasing from Turbine front to Generator rear end
32-For STG: Bearing Vibrations trend goes on increasing from Turbine front to Generator rear end
33-Velocity of condensate water at ejector & gland steam condenser is 0.5 to 0.7 m/sec & 1 to 1.5 m/sec respectively
33-Velocity of condensate water at ejector & gland steam condenser is 0.5 to 0.7 m/sec & 1 to 1.5 m/sec respectively
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