1. A PRESENTATION ON 660MW TURBO-GENERATOR ,ITS AUXILIARIES
AND ASSOCIATED SYSTEMS OF
STAGE – I OF SIPAT SUPER THERMAL PROJECT

2. STEAM TURBINE K

3. LMZ (LENINGRADSKY METALLICHESKY ZAVOD)
K STANDS FOR KLAPAN LTD.,BULGARIA WHICH SUPPLIES TURBINE,NOZZLES,DIAPHRAGMS, SEALS,BLADES ETC.

4. GENERAL INFORMATION
TG DECK IS VIS SUPPORTED AND HAS 26 CONCRETE COLUMNS (T1 – T26).
TG HALL IS CONSTITUTED OF 3 MAINS ROWS OF COLUMNS – A,B ,C ROW AND TWO BAYS – AB BAY AND BC BAY. THE WIDTH OF AB BAY IS 36m AND BC BAY IS 12m
CONDENSER TUBE BANKS (CW PATH) HAS AN INCLINATION OF 40.
THERE ARE TWO MAIN EOT CRANES FOR TG HALL.EACH EOT CRANE IS HAVING A CAPACITY OF 200t FOR MAIN HOIST AND 20t FOR AUXILIARY HOIST. 35.5m IS THE MAXIMUM VERTCAL DISTANCE A HOIST CAN TRAVEL.TANDEM OPERATION OF TWO EOT CRANES ARE ALLOWED.

10. RATED CONDITIONS FINAL FEED WATER TEMP. : 286.350C LOAD : 660MW
BEFORE HP STOP VALVE
STEAM PRESSURE : 247KSC
STEAM TEMPERATURE : 5370C
STEAM FLOW : T/HR
AFTER HPC
STEAM PRESSURE : 48KSC
STEAM PRESSURE : C
BEFORE IP STOP VALVE
STEAM PRESSURE : 43.2KSC
STEAM TEMPERATURE : 5650C
STEAM FLOW TO REHEATER : T/HR.
DESIGN CONDENSER PRESSURE : 0.105KSC (abs.)
COOLING WATER FLOW : 64000M3/HR
FINAL FEED WATER TEMP. : C
FREQUENCY RANGE : 47.5 – 51.5 Hz

11. STEAM TURBINE Generator rated speed 3000 rpm
SIPAT
STEAM TURBINE
Generator rated speed rpm
Generator manufacturer Electrosila
No. of bleedings 8
Length of the turbine m
No. of stages
HPT 17
IPT 11x2
LPT-1 5x2
LPT-2 5x2
Total 59

12. STEAM TURBINE Parameters Pr. Before HPC SV 247.0 Ksc
SIPAT
STEAM TURBINE
Parameters
Pr. Before HPC SV Ksc
Temp. before HPC SV C
Steam flow TPH
Pr. After HPC Ksc
Temp. after HPC C
Pr. Before IP SV Ksc
Temp. before IP SV C
Steam flow to reheat TPH
Design Cond pr Ksc
CW flow TPH
Final FW Temp C

13. STEAM TURBINE Turbine Governing system Normal Operating Pr. 50 Ksc
SIPAT
STEAM TURBINE
Turbine Governing system
Mode of Governing Nozzle
Type E/H
Control fluid Firequel-L make
Supresta-USA
Normal Operating Pr. 50 Ksc
Capacity lpm
Fluid pump motor rating 200 KW
Filter material Ultipor
Mesh size 25 µ

14. STEAM TURBINE Lube oil system SIPAT
Lube oil Tn-22C Russia Mobil DTE Oil light Teresso 32
In accordance with ISO VG 32
Absolute viscosity Centipoise
Kinematic viscosity -32 Centistokes
Specific gravity 0.89
Flash point C
Fire point C
Oil requirement per bearing
N lpm
N lpm
N lpm
N lpm
N lpm
N lpm
N lpm
N lpm
N lpm
N lpm

15. STEAM TURBINE Lube oil system Seal steam system
SIPAT
STEAM TURBINE
Lube oil system
Total oil system capacity lit
Full volume of oil tank lit
Material of tank SS
Normal lube oil pressure 1.2 Ksc
Oil temp at inlet of bearings
Normal C
Maximum C
Piping SS
Seal steam system
Source of gland sealing system
During normal operation End glands of HPC & IPC
During low load operation End glands of HPC & IPC + AS
Quantity of seal steam required TPH
Seal steam pressure at turbine glands Ksc
Seal steam temperature at turbine glands 160 0C

16. TURBINE SEAL STEAM TWO HEADERS OR COLLECTORS ARE THERE i.e. HOT
COLLECTOR AND COLD COLLECTOR.
INITIAL SOURCE OF STEAM SUPPLY IS APRDS (UNIT HT,16KSC,310OC).
PRESSURE AND TEMPERATURE OF COLD HEADER OR COLLERTOR ARE 1.1TO1.15 KSC ABSOLUTE AND 140TO 180OC RESPECTIVELY.
PRESSURE AND TEMPERATURE OF HOT HEADER OR COLLERTOR ARE 1.1TO1.15 KSC ABSOLUTE AND RESPECTIVELY.

17. STEAM TURBINE Turbine Protection Over speed trip 110-112 %
SIPAT
STEAM TURBINE
Turbine Protection
Over speed trip %
Low lube oi pressure (g) Ksc
Low vacuum trip (abs) Ksc
Thrust bearing excessive wear trip +1.2/-2.0 mm
Pressure relief diaphragm setting 1.2 (abs) Ksc

18. STEAM TURBINE Materials of construction HP Outer casing 15Cr1Mo1V
SIPAT
STEAM TURBINE
Materials of construction
HP Outer casing 15Cr1Mo1V
HP blade/carrier casings 15Cr1Mo1V
IP Outer casing 15Cr1Mo1V
LP inner casing Steel 3
LP Outer casing Steel 3
HP Shaft 25Cr1Mo1V
IP Shaft 25Cr1Mo1V
LP Shaft 26CrNi3Mo2V
Moving blades
HPT first stage blades 18Cr11MoNiVNb (1-5)
HPT other stages 15Cr11MoV (6-17)
IPT first stage 18Cr11MoNiVNb (1-3)
IPT other stages 15Cr11MoV (4-11)
LPT last stage 13Cr11Ni2W2MoV
LPT other stages 20Cr13 (1-2)
LPT other stages 15Cr11MoV (3-4)

19. STEAM TURBINE HPT first stage 18Cr11MoNiVNb (1-5)
SIPAT
STEAM TURBINE
Fixed blades
HPT first stage 18Cr11MoNiVNb (1-5)
HPT other stages 15Cr11MoV (6-17)
IPT first stage 18Cr11MoNiVNb
IPT other stages 15Cr11MoV
LPT first stage 12Cr13 (1-4)
LPT Other stages 08 Cr13 (5)
Number of stages
HPT
Impulse stages 1
Reaction stages 16
IPT
Impulse stages 22
Reaction stages 0
LPT
Impulse stages 20
All rows of blades are integrally shrouded

20. STEAM TURBINE No. of HP Stop valves 2 No. of HP Control valves 4
SIPAT
STEAM TURBINE
No. of HP Stop valves 2
No. of HP Control valves 4
Type of control valve unit Block united
No. of IP Stop valves 2
No. of IP Control valves 4
Type of control valves Separate
No. of Journal bearings for turbine 8
No. of Journal bearings for Gen 4
No. of thrust cum journal bearing 1
Type of thrust bearing Tilting
Type of journal bearing 6-Fixed & 2-Tilting pad
Material of bearing shell Alloy steel
Type of lining Babbit
LPT diaphrams 4

21. STEAM TURBINE Turbine model No K-660-247
SIPAT
STEAM TURBINE
Turbine model No K
Generator model No TBB-660-2T3
Strainers are installed in the steam chests of the stop valves
In HPT, having passed the control stage and 8 stages which generate left jet of steam (from generator towards front bearing) steam changes its direction 180° and flows between internal and external cylinders to 8 stages of right jet (towards generator)
In CRH lines, NRV has a bypass with electric valve and control valve to enable counter flow mode of HPT with the aim of warming up of cylinder and high pressure cross over pipes at turbine start up and cold condition
HPT has nozzle steam distribution system
IPT has throttle steam distribution system
On each upper half (cover) of low pressure cylinder four membrane type relief valves are installed which are activated when the absolute pressure in exhaust nozzles rises up to 1.35 – 1.4 Ksc absolute

22. TG SEAL STEAM SYSTEM
SIPAT

23. HPT SEAL STEAM CONNECTION
TO BLED STEAM TO LPH # 4
1ST CHAMBER
2ND CHAMBER
HPT
TO 2nd CHAMBER EXHAUST
TO HOT SEAL STEAM HEADER
TO BLED STEAM TO D/A
TO GSC

24. IPT SEAL STEAM CONNECTION
TO COLD SEAL STEAM HEADER
TO GSC

25. LPT SEAL STEAM CONNECTION
FROM COLD SEAL STEAM HEADER
TO GSC

26. IN HIGH PRESSURE DRAINAGE EXPANSION TANK A VALVES IN DRAINAGE COLLECTORS FROM EXTRACTION STEAM PIPES TO HPHs (10MAL20AA110, 10MAL20AA120, 10MAL20AA140) AND IN LOW PRESSURE DRAINAGE EXPANSION TANK VALVES IN DRAINAGE COLLECTORS FROM EXTRACTION STEAM PIPES TO LPHs(10MAL30AA110, 10MAL30AA120) CLOSE AUTOMATICALLY IF TURBINE LOAD INCREASES OVER 200MW AND AT THE SAME TIME ALL VALVES ARE OPEN IN THE CORRESPONDING STEAM EXTRACTION FROM THE TURBINE TO HPHs AND LPHs.
VALVES IN DRAINAGE PIPES OF HPBP AND LPBP (10MAL30AA107, 10MAL30AA108) CLOSE AUTOMATICALLY IF TURBINE LOAD INCREASES OVER 30MW.

27. CONTROL FLUID SYSTEM
FIRE RESISTANT SYNTHETIC HYDRAULIC FLUID FYRQUEL – L MANUFACTURED BY “SUPRESTA” IS USED AS OPERATING FLUID.ITS SELF IGNITION TEMPERATURE IS ABOUT 740OC.
OPERATING PRESSURE IS APPROXIMATELY 50KSC.
OPERATING TEMPERATURE IS 45-55OC.
CONTROL OIL SUPPLY UNIT CNSISTS OF A RESERVOIR (10MAX10BB001)OF CAPACITY 7.0m3 ,2NOS.OIL COOLERS(10MAX10AC001,10MAX10AC002),DE-AERATOR,MESH FILTER,FINE FILTER(10MAX18AT001),DUPLEX FILTER(10MAX14AT001) AND 2 NOS. OF VERTICALLY MOUNTED CENTRIFUGAL PUMPS(10MAX11AP001,10MAX12AP001) DRIVEN BY AC MOTOR (1W+1S).EACH PUMP IS HAVING A CAPACITY OF 36m3/h AND DISCHARGE PRESSURE IS 50KSC.
CONTROL FLUID RESERVOIR IS SEPERATED BY TWO NUMBERS OF TANDEM MESHES OF CELL SIZE 0.25mm INTO TWO SECTIONS ,DIRTY AND CLEAN. DE- AERATOR IS INSTALLED INSIDE THE RESERVOIR INFRONT OF MESHES AND IT CONSISTS OF SLOPING PLATE ASSEMBLY.
CF FINE FILTER FOR REMOVING MECHANICAL IMPURITIES IS INSTALLED IN RESERVOIR. DURING NORMAL OPERATION CF IS SUPPLIED TO THE FINE FILTER THROUGH AN ORIFICE OF DIAMETER 4mm FROM UNSTABILIZED PRESSURE LINE VIA VALVE 10MAX18AA501 . AFTER THAT IT IS DISCHARGED IN THE DIRTY CHAMBER OF THE RESERVOIR. WHEN TURBINE IS STOPPED CF IS SUPPLIED TO THE FINE FILTER WITH THE HELP OF ANOTHER PUMP (CF TRANSFER PUMP,10MAX19AP001,CAPACITY 4m3/hr, AND DISCHARGE PRESSURE 25KSC) VIA VALVES 10MAX19AA503 AND10MAX19AA504 FOR FILTERING PURPOSE KEEPING MAIN PUMPS IN OFF CONDITION.

28. OIL PURIFICATION IS CONTINUOUS DUE TO FILTERING OF ITS PART VIA CONCURRENTLY MOUNTED WORKING FILTER CARTRIDGES INSTALLED INSIDE THE FINE FILTER HOUSING.
FILTER CARTRIDGES DESIGN ALLOWS USAGE OF DIFFERENT FILTERING MATERIAL.
METAL SEMI-PINCEBECK MESH WITH FILTERING DEGREE OF 70 MICRONS TO FLUSH SYSTEM AFTER INSTALLATION OR MAINTENANCE.
FILTER BELTING FABRIC WITH FILTERING DEGREE 30 – 40 MICRONS FOR PRIMARY REFINING DURING TURBINE OPERATION.
FILTERING ELEMENTS MANUFACTURED BY ”PALL” WITH FILTERING DEGREE 12 MICRONS FOR CONTINUOUS OIL FILTERING DURING TURBINE OPERATION.
OCCURRENCE OF PRESSURE OF 0.1 TO 0.3KSC IN FILTER HOUSING WITHIN 1-3 HOURS SHOWS CORRECT ASSEMBLY OF FILTER AND ITS PROPER OPERATION.
IT IS NECESSARY TO SWITCH OFF THE FINE FILTER AND REPLACE FILTERING ELEMENTS IF PRESSURE IN FILTER HOUSING RISES UPTO 2KSC.WHICH SHOWS CONTAMINATION OF FILTER FABRIC.
INSIDE FILTER HOUSING THERE IS A RELIEF VALVE BYPASSING FLUID BESIDES FILTER CARTRIDGES WHEN THEY ARE CONTAMINATED AND PRESSURE RISES UPTO 5KSC.
AN OIL LEVEL GAUGE WITH ALARM SYSTEM WHISKERS (10MAX10CL001,10MAX 10CL002) IS PROVIDED IN THE CLEAN SIDE OF THE RESERVOIR.
NORMAL OPERATING LEVEL IS 700mm FROM THE UPPER COVER (30 GRADUATION OF L.G.) AND THE AMOUNT OF CF IS 2.5m3

29. MAXIMUM ALLOWALABLE UPPER LIMIT (WITH CF PUMPS IN STOPPED CONDITION) IS 150mm FROM THE UPPER COVER (85 GRADUATION OF L.G.) AND MINIMUM OPERATING LEVEL IS 800mm (20 GRADUATON OF L.G.) FROM THE UPPER COVER.
CF PUMP STOPS AUTOMATICALLY INCASE OF RESERVOIR OIL LEVEL LOW-LOW.
FOR VISUAL OVSERVATION OF OIL LEVEL ,LEVELGLASSES HAVE BEEN PROVIDED IN THE BOTH SIDES (DIRTY AS WELL AS CLEAN).
DIFFERENTIAL PRESSURE SWITCH (10MAX10CP001) HAS BEEN PROVIDED TO WARN ABOUT INCREASE IN PRESSURE DIFFERENCE IN SIDE THE MESH FILTER. ALLOWABLE DIFFERENCE IN MESHES DOESNOT EXCEED 150mm.
THE STANDBY CF PUMP STARTS WHEN THE RUNNING ONE TRIPS OR SYSTEM PRESSURE DROPS TO 36KSC.
IT TAKES 2 MINS FOR THE SYSTEM TO GET PRESSURIZED.
IF SYSTEM PRESSURE DROPS TO 20KSC (10MAX14CP001) AND STOP VALVES START CLOSING ,THE OPEARTING PUMP WILL STOP AND NO SIGNAL WILL BE GENERATED TO START THE STAND BY PUMP (SENSING OIL LEAKAGE).
CF PUMP ALSO TRIPS ON FIRE PROTECTION.
DUPLEX FULL PASSAGE FILTER WITH FILTERING DEGREE 20-25MICRONS IS INSTALLED IN GENERAL PRESSURE COLLECTOR OF CONTROL SYSTEM.IF PRESSURE DIFFERENCE (10MAX14CP301,10MAX15CP301) ACROSS THE RUNNING FILTER REACHES 0.8KSC,THE STANDBY FILTER HAS TO BE TAKEN INTO SERVICE.

30. 2 NOS.OF CF COOLERS (A&B) ARE INSTALLED IN THE CF SUPPLY LINE BEHIND THE DUPLEX FILTER. THESE COOLERS ARE DOUBLE PASS (BY WATER) SURFACE HEAT EXCHANGERS WITH TUBULAR DESIGN ,WATER STREAM FLOWS INSIDE THE TUBES AND CONSIST OF 148 TUBES OF SIZE 16X1500mm AND HEAT EXCHANGE AREA 25m2.CF FLOWS FROM TO DOWNARD.
COOLERS ARE DESIGNED FOR A MAXIMUM COOLING WATER PRESSURE OF 10 ± 0.5KSC AND CF PRESSURE OF ± 0.5KSC.CF FLOW RATE TO EACH COOLER IS 50m3/hr AND PRESSURE DROP IS 0.2KSC. CW FLOW RATE TO EACH COOLER IS 80m3/hr AND PRESSURE DROP IS 0.194KSC.
FOR HYDRODYNAMIC FLUSHING OF PIPELINES DURING MAINTENANCE,THERE IS A BYPASS VALVE (10MAX14AA501)TO THE COOLERS WHICH SHOULD BE CLOSED AND SEALED DURING ROUTINE OPERATION.
IN THE INPUT AND OUTPUT TO THE COOLERS CF LINE IS PROVIDED WITH TRIPLE-PASS SWITCHING OVER VALVES WHICH PREVENT FALSE ACTIVATION OF BOTH COOLERS.
CF TEMPERATURE IS MAINTAINED (48-52OC)BY COOLING WATER FLOW VARIATION WITH THE HELP OF A FLOW CONTROL STATION CONSISTING OF A PNEUMATIC CONTROL VALVE (10PGM20AA001) AND A BYPASS MOTORIZED CONTROL VALVE(10PGM20AA002).IN CASE TEMPERATURE RISES TO 55OC (10MAX14CT001,10MAX14CT002),MOTORIZED BYPASS VALVE OPENS TO MAINTAIN THE CF TEMPERATURE. THE MAXIMUM LIMIT OF CW TEMPERATURE AT COOLER INLET IS 37OC.IF CW TEMPERATURE IS BELOW 36OC ONE COOLER CAN BE PUT OUT OF OPERATION.

31. CF SUPPLY TO CONTROL UNITS IS CARRIED OUT BY TWO PRESSURE COLLECTORS OF STABILIZED AND UNSTABILIZED PRESSURE.
CF IS SUPPLIED TO UNSTABILIZED PRESSURE COLLECTOR THROUGH AN ORIFICE OF SIZE 22mm. STOP AND CONTROL VALVE ACTUATORS ARE FED FROM THIS COLLECTOR.
INTO STABILIZED PRESSURE COLLECTOR WHICH FEEDS OIL TO ALL CONTROL DEVICES,CF IS SUPPLIED FROM THE SECTION BETWEEN PUMPS AND THE ORIFICE.
DUE TO THE ARRANGEMENT MENTIONED ABOVE ,THE PRESSURE VARIATION IN UNSTABILIZED PRESSURE COLLEECTOR CAUSED BY INCREASE IN CF CONSUMPTION WITH OPEN ACTUATORS AFFECTS IN A LESS DEGREE PRESSURE VARIATION IN STABILIZED PRESSURE COLLECTOR.
SPRING-WEIGHT ACCUMULATOR (10MAX20BB001) IS CONNECTED TO UNSTABILIZED PRESSURE COLLECTOR TO PREVENT DECREASE IN FORWARD PRESSURE IN CASE OF LOSS AC SUPPLY TO THE PUMPS FOR 5-7SECS OR DURING PUMP CHANGE-OVER.
THE SETTING OF FLUID PRESSURE LEVEL (45KSC) TO BE ENSURED BY THE ACCUMULATOR IS DETERMINED BY A WEIGHT WHICH IS CONCRETE FILLED IN THE SITE.
ONE NRV IS INSTALLED IN THE LINE CONNECTING THE ACCUMULATOR TO THE UNSTABILIZED PRESSURE COLLECTOR. ACCUMULATOR IS FILLED WITH THE CF THROUGH AN ORIFICE OF SIZE 5mm INSTALLED IN THE BYPASS LINE OF THE NRV.
TWO EXHAUST FANS (1W+1S) ,10MAX21AN001,10MAX21AN002 (CAPACITY OF 3200m3/hr AT A HEAD OF 5- 20mm OF WATER COLUMN) ARE ALSO INSTALLED TO REMOVE CF VAPOUR FROM CF RESERVOIR AND SYSTEM.
THE EXHAUSTER SWITCHES ON AUTOMATICALLY WHEN CF PUMP STARTS AND SWITCHES OFF AUTOMATICALLY WITH 15mins TIME DELAY AFTER THE STOPPING OF CF PUMP AND CF SYSTEM PRESSURE DROPS BELOW 2.0KSC.

32. HYDRAULIC TEST OF PIPE LINES CARRIED OUT AT A PRESSURE OF 90KSC
HYDRAULIC TEST OF PIPE LINES CARRIED OUT AT A PRESSURE OF 90KSC.HYDRAULIC TEST SHOULD BE CARRIED OUT AFTER ASSEMBLING,OVERHAUL AND INSPECTION.

33. SIPAT
CONTROL FLUID SYSTEM

34. CONTROL FLUID SYSTEM Isolation valves on pump suction & discharge side
SIPAT
CONTROL FLUID SYSTEM
Isolation valves on pump suction & discharge side
Pump discharge pressure 50 Ksc
Capacity 41 TPH
Stabilized pressure header supply oil to servo motors of SV & CV
Un stabilized pressure header with 22 mm orifice
Accumulator in unstabilized pressure header
CF tank capacity m3
Duplex filter
Control fluid transfer pump to empty the CF tank
CF Temperature control by control station in the ECW line

35. COMPONENT OF GOVERNING SYSTEM
ELECTRO-HYDRAULIC CONVERTER – SUMMER – 8 NOS.
SUMMER – 8NOS.
ELECTRO-MECHANICAL CONVERTER – 8NOS.
GOVERNING BLOCK
CONTROLGEAR(AE001) – 1NO.
EMERGENCY GOVERNOR OR OVERSPEED GOVERNOR– 1NO.
TRIP SOLENOID (AA213,AA214)-2NOS.
TEST ELECTROMAGNETS(AA211,AA212) – 2NOS.
ROTATIONAL SPEED DETECTOR -3 NOS.
LIMITER OF PRESSURE (AA502) – 1NO.
SPEED TRANSDUCER – 1NO.
LEVER OF OVER SPEED GOVERNOR (AX201)– 1NO.
PILOT VALVE FOR SUPPLY (AX202) – 1NO.
ACCUMULATOR – 1NO.
OIL SUPPLY AND PURIFIER UNIT
SERVOMOTOR OF HPSV – 2NOS.
SERVOMOTOR OF HPCV – 4NOS.
SERVOMOTOR OF IPSV – 2NOS.
SERVOMOTOR OF IPCV – 4NOS.
SERVOMOTOR OF CRH NRV – 2NOS.
LOCKING PILOT VALVE (AA001,AA002,AB001,AB002)- 4NOS.
EX.STOP VALVE SERVOMOTOR OR ESV (10LBQ10AA101)– 1NO.

36. DIFFERENT TYPES OF OIL HEAD PRESSURE LINE (STABILIZED,50KSC,10MAX15)
HEAD PRESSURE LINE ( NON-STABILIZED,50KSC,10MAX15)
LINE OF PROTECTION (50KSC,10MAX51)
LINE TO COCK THE OVERSPEED GOVERNOR SLIDE VALVE (50KSC)
CONTROL OIL LINE TO STOP VALVE SERVOMOTORS (50KSC,10MAX16)
CONTROL LNE TO SUMMATORS (35KSC,10MAX17)

38. TURBINE PROTRCTIONS
OUT OF TOLERANCE ROTOR OVERSPEED : ALARM AT 3300RPM AND TRIPPING AT 3360RPM
OUT OF TOLERANCE AXIAL DISPLACEMENT OF ROTOR:
TOWARDS FRONT BEARING BY 0.6mm (-0.6mm) -ALARM.
TOWARDS FRONT BEARING BY 1.2mm (-1.2mm) - TRIPPING.
TOWARDS GENERATOR BY 1.4mm (+1.4mm)A- ALARM.
TOWARDS GENERATOR BY 2.0mm (+2.0mm) - TRIPPING.
LUBRICATING OIL PRESSURE DROP: ALARM AT 0.70KSC AND TRIPPING AT 0.30KSC WITH 3SECS TIME DELAY.
PRESSURE RISE IN CONDENSER:ALARM AT 0.15KSC abs. AND TRIPPING AT 0.20KSC abs. PROTECTION IS INTRODUCED AUTOMETICALLY AT UNIT START-UP AFTER PRESSURE DROP IN CONDENSER LOWER THAN 0.15KSC abs. OR AT TURBINE SPEED INCREASE OVER 1500RPM. PROTECTION IS IN OPERATION UNTIL STOP VALVES ARE OPEN
INCREASE OF BEARING VIBRATION: ALARM SOUNDS AT INCREASE OF VERTICAL OR TRANSVERSE OR AXIAL COMPONENT OF VIBRATION ON ANY BEARING OF TG SET REACHES 4.5mm/s .TRIPPING OCCURS WITH 2 SECS TIME DELAY AT INCREASE OF VERTICAL OR TRANSVERSE COMPONENT OF VIBRATION OVER 11.2mm/s ON ANY TWO BEARINGS OF TG SET.

39. RISE IN STEAM TEMPERATURE AT HPT OUTLET:
LIVE STEAM TEMPERATURE BEFORE TURBINE FALLS BELOW 470OC:
LIVE STEAM TEMPERATURE BEFORE TURBINE RISES ABOVE 565OC:
STEAM TEMPERATURE BEFORE IV FALLS BELOW 500OC:
STEAM TEMPERATURE BEFORE IV RISES ABOVE 593OC:
MOT LEVEL LOW-LOW:
DRIP LEVEL HIGH-HIGH IN ANY HPH:
ANY FAILURE IN TURBNE CONTROL SYSTEM ELECTRONICS:
GENETERATOR PROTECTION:
FIRE PROTECTION OPERATED:
EPB PRESED.

40. TURBINE LUBE OILSYSTEM
LUBRICATION OIL SYSTEM IS DESIGNED TO SUPPLY OIL TO TURBINE AND GENERATOR BEARINGS IN ALL TURBINE PLANT OPERATION MODES AND ALSO TO PROVIDE ROTOR JACKING OIL SYSTEM AND GENERATOR SEAL OIL SYSTEM WITH OIL.
LUBRICATION OIL IS ISO VG 32 TYPE WITH FOLLOWING PROPERTIES:
ABSOLUTE VISCOCITY : 16.7CENTIPOISE
KINEMATIC VISCOSITY : 32CENTISTOKE
SPECIFIC GRAVITY : 0.89
SPECIFIC HEAT : 0.459Kcal/Kg Deg.C
FLASH POINT : 180OC
FIRE POINT : 240OC
DEGREE OF CLEANLINESS : 16/13 ISO 4406
PERMISSIBLE SUSPENDED PARTICLE SIZE : 25 MICRON
WATER CONTENT : <10PPM
LUBE OILTANK IS MADE OF STAINLESS STEEL AND HAVING A CAPACITY OF 58m3 . PROVISION IS MADE FOR OIL TREATMENT INSIDE THE TANK BY PROVIDING TWO ROWS OF FLAT GRIDS WITH MESH DIMENSIONS 0.25mm LOCATED INSIDE THE TANK WHICH DIVIDES THE TANK INTO DIRTY AND CEAN COMPARTMENTS. THE AIR SEPARATOR CONSISTING OF TILTED METAL PLATES SET IS INSTALLED TO SEPARATE THE AIR DISSOLVED IN OIL.
THE OIL TANK HAS ATTACHMENTS FOR OIL DRAINING TO OIL TREATMENT PLANT FOR SLUDGE DRAIN AND TO EMERGENCY TANK INCASE OF FIRE.

41. NORMAL OPERATING LEVEL IS 600mm FROM TANK TOP COVER
NORMAL OPERATING LEVEL IS 600mm FROM TANK TOP COVER.ALARM IS AT 500mm AND TURBINE TRIP IS THERE AT 400mm.
4 NOS OF LUBE OIL PUMPS (SINGLE STAGE CENTRIFUGAL) ARE INSTALLED VERTICALLY ABOVE THE TANK .2 PUMPS (AUXILLIARY OIL PUMP) ARE ac MOTOR DRIVEN AND 2 PUMPS ARE dc (EMERGENCY OIL PUMP) MOTOR DRIVEN.
ONE PUMP WITH ac MOTOR IS CONTINUOUS RUNNING AND OTHER IS KEPT STANDBY.
EACH ac PUMP IS HAVING A DISCHARGE CAPACITY OF 300m3/hr A DISCHARGE PRESSURE OF 4.3KSC.
EOP WLL START IN CASE OF LOSS OF AC.EACH EOP IS HAVING A DISCHARGE CAPACITY OF 250m3/hr AND A DISCHARGE PRESSURE OF 2 KSC.FOR HIGHIER RELIABILITY EOP DELIVERS OIL DIRECTLY TO THE BEARING BYPASSING COOLER AND THROTTLE VALVE.

42. TG LUBE OIL SUPPLY SYSTEM
SIPAT
TG LUBE OIL SUPPLY SYSTEM

43. SIPAT
TG LUBE OIL SYSTEM

44. TG LUBE OIL SYSTEM Turbine oil is ISO VG 32 Bearings SIPAT
KV CST at 500C
Acidity Number < 0.05 mg KOH/r
Viscosity index > 90
Bearings
HPT Front N1
HPT Rear N2
IPT Front (TB) N3
IPT Rear N4
LPT-1 Front N5
LPT-1 Rear N6
LPT-2 Front N7
LPT-2 Rear N8
Generator Front N9
Generator Rear N10
Exciter Front N11
Exciter Rear N12

45. TG LUBE OIL SYSTEM DC Lube oil pump 1 No.
SIPAT
TG LUBE OIL SYSTEM
DC Lube oil pump 1 No.
Equipment
Capacity (m3/hr)
Head (Ksc)
AC Lube oil pump
300
4.3
DC Lube oil pump
250
2.0
NRV & Isolation valve in each Lube oil pump discharge line
Oil first goes to duplex filter instead of cooler
Coolers Bypass line with isolating valve
Hydraulic Pressure control valve maintains the pressure at the center shaft level at 1.2 Ksc
PCV Bypass with throttling orifice which provides lubrication even at fully closed control valve

46. SIPAT
TG LUBE OIL SYSTEM
Oil is first delivered to bearing brasses through emergency tanks located on bearing cap
Emergency tanks capacity in m3 N N N N N N N N
N9 0.5 N N N

47. SIPAT
TG LUBE OIL SYSTEM
Lube oil temperature control by control station in the ECW inlet line to Lube oil coolers
View glasses in the oil return line from each bearing
MOT Capacity 58 m3
Duplex filters fineness 25 µm
Provision is made for oil cleaning by delivering a portion of oil from the oil pressure pipe to the oil tank through the fine cleaning filter with fineness of µm
Fresh oil is filled through the above filter only
Oil recirculation pump to purify the oil
Electrical oil heater of 152 KW capacity is provided for the preliminary oil warming in the lubrication oil tank before turbine start up by running the oil recirculation pump
Oil draining to Emergency lube oil tank in case of emergency with MOV

48. TG LUBE OIL SYSTEM Oil trap at the suction of the vapor extractor fans
SIPAT
TG LUBE OIL SYSTEM
Oil trap at the suction of the vapor extractor fans
Oil trap drain to lubrication oil tank
Jacking oil pumps suction also given from lube oil discharge header after coolers & before control valve

49. TG JACKING OIL AND BARRING GEAR SYSTEM
SIPAT
TG JACKING OIL AND BARRING GEAR SYSTEM

50. Barring gear & Jacking oil system
SIPAT
Barring gear & Jacking oil system
Automatic barring gear engagement at the rotor stop and barring gear disengaging at the start-up
High pressure oil supply for bearing inserts oil jacking
Barring speed 1.05 rpm
Motorized barring gear
Torque transfer from the barring gear motor to the turbine shaft is carried out via three stage reducer and free wheel clutch
Reduction gear first stage shaft end mounts special handle for hand barring
Normal source for jacking oil pumps suction is from lube oil pumps discharge header after coolers
JOP discharge pressure: 120 Ksc

51. Barring Gear & Jacking oil system
SIPAT
Barring Gear & Jacking oil system
Dozing devices at each bearing of the Turbine & Generator which contain strainer, NRV, orifice & isolation valve
Bearing jacking oil is supplied via separate lines for oil jacking of inserts of bearing no: 4-9
Stand-by bearing insert oil jacking pump is not provided as the system is designed to realize auxiliary functions at turbine start-up. If this pump does not start when it is required then also the turbine can be operated normally without any bearing damage and disturbance of turbine operation
Each bearing insert jacking oil line is equipped with orifice only
Both pumps cut in/cut out is 1500/1500
Barring gear cut in/cut out is 1500/1500

52. Barring Gear & Jacking oil system
SIPAT
Barring Gear & Jacking oil system
Bearing Insert Oil Jacking Pump is started automatically, if the rotor neck displacement becomes more than 0.1 mm relative to the insert of any of bearings No. 4,…9 provided that the oil pressure to rotor jacking is higher than 45 kg/cm2 or the turbine rotor rotational speed is higher than 1500 rpm
Pump is stopped automatically, with time delay of 30 seconds, if the rotor neck displacement is less than 0.1 mm relative to the insert of bearings No. 4-9

53. GENERATOR SEAL OIL SYSTEM
SIPAT
GENERATOR SEAL OIL SYSTEM

54. GENERATOR SEAL OIL SYSTEM
SIPAT
GENERATOR SEAL OIL SYSTEM
Seal oil pumps suction from MOT
No Hydrogen side seal oil pump
Pumps re-circulation line directly to MOT
Coolers bypass valve
Magnetic filters 2 No. (1W+1SB)
NRV in the seal oil line after filters
DPR
DPR bypass manual control valve

55. GENERATOR SEAL OIL SYSTEM
SIPAT
GENERATOR SEAL OIL SYSTEM
Damper tanks 2 No.: 1 for TE & 2 for EE, designed for oil supply to front and back generator shaft seals with drop, specified by the height of damper tank installation, and also to seal at short-time interruption in oil supply, at the moment of automatic transfer from working pump to standby and at generator runback with generator shaft seal pumps switched off
View glasses in return oil lines
Float hydraulic seal functions as SOT
Hydraulic seal overflows in to return oil header
No SOST
Provision of trap upstream of fans
Fans suction is from return oil header

56. GENERATOR STATOR WATER COOLING SYSTEM
SIPAT
GENERATOR STATOR WATER COOLING SYSTEM

57. STATOR WATER COOLING SYSTEM
SIPAT
STATOR WATER COOLING SYSTEM
Water tank not on the generator
Ejector to make vacuum over the water tank to prevent air ingress
Ejector cooling by auxiliary cooling water
Air venting of Generator through Gas trap connected from winding inlet and outlet headers
Gas trap to determine hydrogen present which will be extracted from trap cap to gas analyzer
Coolers bypass valve
Ion exchanger-1 contains anion & cat ion in H-OH form to maintain conductivity
Ion exchanger-2 contains anion & cat ion in Na-OH form to maintain Ph if it decreases below 8
Ion exchanger-1 first will be put in to service for reducing dissolved oxygen below 5.0 µs/cm and then it will be put out of service. Then Ion exchanger-2 will be put in to service to increase the Ph value. If conductivity increases above µs/cm, Ion exchanger-2 to be stopped

58. STATOR WATER COOLING SYSTEM
SIPAT
STATOR WATER COOLING SYSTEM
Control valves at the inlet of individual Ion exchanger circuits
DM water flow through ion exchanger is 1.5 to 2.0 m
No NAOH dozing system
Ion exchangers separate bypass lines
Mechanical filter at the inlet of Ion exchanger circuit
Dissolved oxygen analyzer & Ph analyzer
Winding inlet valve for flow adjustment
Winding outlet valve for pressure adjustment
Normal make up from DM make up line & emergency make up line from CST
Filter in the common make up line
Control station in the common make up line

59. GENERATOR GAS SUPPLY SYSTEM
SIPAT
GENERATOR GAS SUPPLY SYSTEM

60. GENERATOR GAS SUPPLY SYSTEM
SIPAT
GENERATOR GAS SUPPLY SYSTEM
Two Hydrogen manifolds to connect 16 cylinders each
Direct acting Pressure regulator installed on cylinder connecting line to Manifold header to reduce the Hydrogen pressure from 175 Ksc to 10 Ksc
Total Pressure regulators 32
Safety valve on each manifold header which operates when the Hydrogen pressure in the manifold exceeds 10.5 Ksc
MOV & NRV in each manifold header
Three CO2 manifolds to connect 17 cylinders each
Each manifold header contains MOV, NRV & Isolation valve
MOV with manual bypass valve at the inlet of CO2 heater
CO2 heater is steam heated
Steam source is from auxiliary steam system
Steam parameters: 15 Ksc & 210 0C
MOV in the steam inlet line
Steam exhaust will go to FWSV Dish flash tank
Manifold header pressure is Ksc
Control station with Pressure regulator provided D/S of heater to maintain a pressure of Ksc with manual bypass valve
SV installed D/S of pressure regulator operates if the pr > 5.0 Ksc
Capacity of one cylinder 50 lit

61. GENERATOR GAS SUPPLY SYSTEM
SIPAT
GENERATOR GAS SUPPLY SYSTEM
One Hydrogen manifold is in operation under normal operating conditions
If the pr decreases below < 10 Ksc, an alarm will come and operator connects the standby manifold and disconnects the first manifold
Two CO2 manifolds are in operation under normal operating conditions
If the pr decreases below < 20 Ksc, an alarm will come and operator connects the standby manifold and disconnects the first manifold
Provision is given for emergency removal of hydrogen from generator itself by providing a line with one manual isolating valve & 2 No. MOV

62. FLASH TANKS
DRAINS FROM THE TURBINE AND STEAM LINES ARE REMOVED TO TWO HP DRAIN FLASH TANKS - A (10MAL10BB001) AND B (10MAL20BB001) AND ONE LP DRAIN FLASH TANK (10MAL30BB001)
BOTH THE HP FLASH TANKS ARE HAVING A CAPACITY OF 2.6m3. LP DRAIN FLASH TANK IS ALSO HAVING A CAPACITY OF 2.6m3.

63. CONDENSER Design LMZ Design CW Flow 64000 m3/hr
SIPAT
CONDENSER
Design LMZ
Design CW Flow m3/hr
Vacuum 77 mm Hg (abs) at 33 0C
89 mm Hg (abs) at 36 0C
No. of passes 1
Total no. of tubes (OD)x0.71 (t)
(OD)x1.00 (t)
Tube material ASTM A-249 TP 304
Rated TTD 3.40C
DT of CW 100C

64. CONDENSATE EXTRACTION PUMP
SIPAT
CONDENSATE EXTRACTION PUMP
Design flow rate Kg/s
Discharge pressure Ksc
Shut off head m
Pump speed rpm
Power input KW
No. of stages 6
Type of first stage impeller double entry
Depth m

65. DE-AERATOR Design Pressure 13 Ksc No. of trays 896 Spray valves 132
SIPAT
DE-AERATOR
Design Pressure 13 Ksc
No. of trays 896
Spray valves 132
Design temp for D/A C
Design temp for FST C

66. DRIP PUMP Design flow rate 324.509 TPH Discharge pressure 43 ata
SIPAT
DRIP PUMP
Design flow rate TPH
Discharge pressure ata
Shut off head m
Pump speed rpm
Power input KW
No. of stages 5
Type of first stage impeller centrifugal, single entry
Depth mm

67. MDBFP Pump flow 769.950 TPH Suction temp 186.2 0C
SIPAT
MDBFP
Pump flow TPH
Suction temp C
BP Suction pr ata
BFP Suction pr ata
BFP Discharge pr ata
BFP Discharge temp C
BP Discharge pr ata
Shut off head m
BFP Speed rpm
BP Speed rpm
Normal R/C flow 220 TPH
HC Rated O/P Speed 6505 rpm
Outer casing type barrel
No. of stages 7
BFP warm up flow 15 TPH

68. TDBFP Pump flow 1283.14 TPH Suction temp 186.2 0C
SIPAT
TDBFP
Pump flow TPH
Suction temp C
BP Suction pr ata
BFP Suction pr ata
BFP Discharge pr ata
BFP Discharge temp C
BP Discharge pr ata
Shut off head m
BFP Speed rpm
BP Speed rpm
Normal R/C flow 365 TPH
HC Rated O/P Speed 6505 rpm
Outer casing type barrel
No. of stages 7
BFP warm up flow 20 TPH

69. TDBFP GOVERNING SYSTEM
SIPAT

70. GOVERNING SYSTEM PARTS OF GOVERNING SYSTEM Hydraulic Accumulator (HA)
SIPAT
GOVERNING SYSTEM
PARTS OF GOVERNING SYSTEM
Hydraulic Accumulator (HA)
Remote switch (RS)
Lubrication system pressure relay (LSPR)
Trip Gear (TG)
Stop valve (SV)
Governor valve 1 (GV1)
Governor valve 2 (GV2)
Cut off pilot valve (COPV)
Electro mechanical converter (EMC)
Electro mechanical converter position transducer (ECPT)
Electronic control part (ECP)
Servo motor (S)
Governor valves position transducer (GVPT)

71. TDBFP TURBINE Number of stages 9 Casing Split Steam admission Dual
SIPAT
TDBFP TURBINE
Number of stages 9
Casing Split
Steam admission Dual
Steam pressure at inlet ata
Steam temperature at inlet C
Turbine operating speed rpm
Steam consumption TPH
Steam pressure at exhaust ata
Turning gear speed 15 rpm
Type of governing system Electro-Hydraulic
Over speed type trip Centrifugal + electrical
JOP Not required
Lube oil tank capacity m3
Lube oil Same as main turbine

72. TDBFP CONDENSER CW flow 3000 TPH
SIPAT
TDBFP CONDENSER
CW flow TPH
Vacuum in the condenser Ksc (abs)
Total no. of tubes 3312
Tube OD and thickness x1.06 mm
No. of water passes 2
Tube material ASTM A-249 TP321

73. SIPAT
TDBFP LUBE OIL SYSTEM

74. TDBFP EXTRACTION SYSTEM
SIPAT
TDBFP EXTRACTION SYSTEM

75. TDBFP CONDENSATE SYSTEM
SIPAT
TDBFP CONDENSATE SYSTEM

76. SIPAT
ACW SYSTEM

77. SIPAT
ACW SYSTEM
Suction header is from all the 4 CW inlet lines to condensers
MOV at Suction header from CW line
MOV at SCS inlet
MOV at PHE inlet & outlet
Supply to
Ejector of Stator water cooling system
TDBFP vacuum pumps (4 No.)
Main turbine vacuum pumps (1 No. extra)
MOV at return header to CW line

78. SIPAT
TURBINE VACUUM SYSTEM

79. TURBINE HEATING FLANGES SYSTEM
SIPAT

80. AUXILIARY STEAM SYSTEM
SIPAT
AUXILIARY STEAM SYSTEM

81. CONDENSATE SUPPLY SYSTEM TO EXT NRVS
SIPAT
CONDENSATE SUPPLY SYSTEM TO EXT NRVS

82. SIPAT
EXHAUST HOOD SPRAY

83. SIPAT
FEED WATER SYSTEM

84. TDBFP-A FEED WATER SYSTEM
SIPAT

85. MDBFP FEED WATER SYSTEM
SIPAT
MDBFP FEED WATER SYSTEM

86. LP DOZING & OXY TREATMENT SYSTEM
SIPAT
LP DOZING & OXY TREATMENT SYSTEM

87. SIPAT
HP BYPASS SYSTEM

88. SIPAT
LP BYPASS SYSTEM

89. SIPAT
Thank you