- •5.3 Test Instructions
- •Table of Allowable Rapid Fluctuations of Certain Key Measurements.
- •5.5.6 Data Verification
- •5.6 Results
- •5.7 Analysis
- •5.7.1 Method of Trending Results
- •5.8 Report
- •HP / IP Turbine Efficiency Test
- •Typical Control Room Data Sheet
- •Point ID
- •Condenser
- •Annexure - I
- •CONDENSER DESIGN DATA
- •Annexure - II
- •TEST READINGS
- •Annexure - III
- •TYPICAL CONTROL ROOM READINGS
- •UNITS
- •kcal/hr
- •3.0 Working And Test Set Up
- •TEST ENGINEER (TE):-----------------------------------------
- •ENGINEERING REVIEW
- •PERSONNEL REQUIRED
- •TEST CREW ORIENTATION
- •REFERENCE DRAWINGS
- •LEAK DETECTOR OPERATION
- •TEST LOG
- •ACCESSIBILITY
- •CONTROL ROOM / UNIT DATA
- •LIST OF INSTRUMENTS & ACCESSORIES REQUIRED FOR AIR-IN-LEAK TEST
- •L. P. Turbine
- •*Total time from leak sensing by instrument to retrieval to zero (0)
- •Unit
- •LOW FEED WATER TEMPERATURE
- •EXCESSIVE MAKEUP
- •HIGH WATER LEVEL
- •EXCESSIVE NUMBER OF TUBES PLUGGED
- •HIGH DRAIN COOLER APPROACH TEMPERATURE (DCA)
- •DRAIN COOLER INLET NOT SUBMERGED
- •IMPROPER SETTING
- •EXCESSIVE TUBE BUNDLE PRESSURE DROP
- •HP Heater Test Data
- •Control Room Readings
- •FAULT TREE
- •LP Heater Test Data
- •Control Room Readings
- •FAULT TREE
- •LOW FEED WATER TEMPERATURE
- •EXCESSIVE MAKEUP
- •WORN VENT
- •HIGH WATER LEVEL
- •TUBE LEAKES
- •HEADER PARTITION LEAKS
- •EXCESSIVE NUMBER OF TUBES PLUGGED
- •HIGH DRAIN COOLER APPROACH TEMPERATURE (DCA)
- •DRAIN COOLER INLET NOT SUBMERGED
- •IMPROPER SETTING
- •EXCESSIVE TUBE BUNDLE PRESSURE DROP
- •EXCESSIVE NUMBER OF TUBES PLUGGED
- •Unit
- •BFP Test Data
- •Typical Control Room Readings
- •Boiler Feed Pump A / B / C
- •Typical DAS Readings
- •Description
- •CONTENTS
- •1.0 Introduction
- •3.1 Process Description
- •4 References
- •4.1 ASME Performance Test Code 4.2 – 1969, Coal Pulverizers
- •5 Prerequisites
- •(A clean air test is performed with the primary air to the mill at full load normal conditions with the mill out of service (normal primary airflow, no fuel flow)).
- •Avg. Velocity
- •6.4 Isokinetic Coal Sampling
- •4.5.2 Unburned in Flyash at Economizer Outlet
- •Summary
- •Dry Gas Loss
- •Gas Temp Leaving AH - Corr. to Design Ambient
- •OBJECTIVE : Determine the amount of Power being consumed by the primary plant equipment.
- •TEST ENGINEER (TE):
- •REFERENCE: ASME PTC 19.6-1955 and TVA Proc. No. TS/PERF/RTST/FOS/16.0
- •BILL OF MATERIALS
- •BILL OF MATERIALS
- •Note: Quantities to be decided as per the requirement
- •2.4 PORTABLE DATA ACQUISITION SYSTEM
- •BILL OF MATERIAL
- •Acquisition
- •EQUIPMENT: Thermocouple wire for flue gas temperature measurement
- •2.9 HIGH VELOCITY THERMOCOUPLE (HVT) PROBE
- •2.11 HIGH VOLUME FLYASH SAMPLER
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Centre For Power Efficiency And Environmental |
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Procedure Number |
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NTPC |
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Protection, NOIDA |
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CENPEEP/EFF/TP/304 |
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TITLE |
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Rev. 1/EMS |
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CENPEEP |
LP Heater Performance Test |
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Issue Date: 20/04/2000 |
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Page: 10 |
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2. |
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Heater Position (Horizontal/Vehicle |
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3. |
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LP Heater No. |
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LPH-1 |
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LPH-2 |
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LPH-3 |
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4. |
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No. of Zones (De-superheating, |
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Condensing, Drain cooling) |
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5. |
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No. of Tubes |
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No. |
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6. |
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Surface Area |
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m2 |
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7. |
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Tube Material |
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8. |
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Tube size (OD x Thickness) |
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mm |
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9. |
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Condensate Inlet Temp. |
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oC |
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10. |
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Condensate Outlet Temp. |
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oC |
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11. |
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Extraction Steam Flow |
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T/hr |
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12. |
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Extraction Steam Pressure |
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kg/cm2 |
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13. |
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Pressure Drop (water side) |
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mwc |
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14. |
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Operating Level (Min/Normal/Max |
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mm |
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15. |
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TTD |
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oC |
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16. |
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DCA |
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oC |
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17. |
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Temperature Rise |
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oC |
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LP Heater Test Data |
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Annexure – II |
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Station: ...................... |
Unit: ................ |
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Test Date: .................. |
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Run No. 1 |
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Run No. 2 |
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Run No. 3 |
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SI.No. |
MEASUREMENT |
Unit |
TIME-------DATA |
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TIME-------DATA |
TIME-------DATA |
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Centre For Power Efficiency And Environmental |
Procedure Number |
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NTPC |
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Protection, NOIDA |
CENPEEP/EFF/TP/304 |
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TITLE |
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Rev. 1/EMS |
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CENPEEP |
LP Heater Performance Test |
Issue Date: 20/04/2000 |
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Page: 11 |
Of 14 |
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Condensate Entering LPH-1 |
0 C |
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1.Temp.
2. |
Condensate Entering LPH-1 |
kg/cm2 |
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Pressure |
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3. |
Condensate Entering LPH-2 |
0 |
C |
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Temp. |
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4. |
Condensate Entering LPH-2 |
kg/cm2 |
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Pressure |
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5. |
Condensate Entering LPH-3 |
0 |
C |
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Temp. |
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6. |
Condensate Entering LPH-3 |
kg/cm2 |
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Pressure |
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7. |
Condensate Leaving LPH-3 |
0 |
C |
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Temp. |
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8. |
Condensate Leaving LPH-3 |
kg/cm2 |
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Pressure |
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9. |
LPH-1 |
Shell Press. |
kg/cm2 |
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10. |
LPH-2 |
Shell Press. |
kg/cm2 |
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11. |
LPH-3 |
Shell Press. |
kg/cm2 |
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12. |
LPH-1 Extraction Temp. |
0 |
C |
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LPH-1 Extraction Press. |
kg/cm2 |
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14. |
LPH-2 Extraction Temp. |
0 |
C |
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LPH-2 Extraction Press. |
kg/cm2 |
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16. |
LPH-3 Extraction Temp. |
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C |
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LPH-3 Extraction Press. |
kg/cm2 |
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18. |
LPH-1 Drain Temp. |
0 |
C |
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LPH-2 Drain Temp. |
0 |
C |
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20. |
LPH-3 Drain Temp. |
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C |
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21. |
Condensate Differential Press. |
kg/cm2 |
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Annexure – III |
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Control Room Readings |
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Station: ...................... |
Unit: ................ |
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Test Date: .................. |
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Sl.No |
Description |
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Test readings |
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Remarks |
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Units |
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Run 1 |
Run 2 |
Run 3 |
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Time |
Time |
Time |
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Centre For Power Efficiency And Environmental |
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Procedure Number |
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NTPC |
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Protection, NOIDA |
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CENPEEP/EFF/TP/304 |
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TITLE |
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Rev. 1/EMS |
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CENPEEP |
LP Heater Performance Test |
Issue Date: 20/04/2000 |
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Page: 12 Of 14 |
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1. |
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Load |
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MW |
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2. |
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Main Steam Temp. |
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0 C |
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3. |
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MS Pressure |
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kg/cm2 |
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4. |
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MS Flow |
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T/Hr. |
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5. |
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Feed Water Flow |
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T/Hr |
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6. |
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SH Attemperation Flow |
T/Hr |
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7. |
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RH Attemperation |
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T/Hr |
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Flow |
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8. |
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LPH –1 Extr. Steam |
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kg/cm2 |
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Pressure |
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9. |
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LPH –1 Extr. Steam |
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0 C |
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Temp. |
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10. |
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LPH-1 Shell Pressure |
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kg/cm2 |
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11. |
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LPH-2 Shell Pressure |
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kg/cm2 |
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12. |
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LPH-3 Shell Pressure |
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kg/cm2 |
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13. |
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Condensate Temp |
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0 C |
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LPH-1 In |
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14. |
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Condensate Temp |
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0 C |
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LPH-1 Out |
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15. |
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Condensate Temp |
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0 C |
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LPH-2 Out |
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16. |
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Condensate Temp |
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0 C |
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LPH-3 Out |
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17. |
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LPH-1 Level |
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mm |
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18. |
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LPH-2 Level |
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mm |
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19. |
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LPH-3 Level |
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mm |
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20. |
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Condenser Vacuum |
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mm Hg |
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21. |
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Barometric Pressure |
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kg/cm2 |
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Annexure - IV
DEFINITIONS
Terminal Temperature Difference (TTD) - The difference between the saturation temperature determined at the heater shell pressure and the temperature of the feedwater leaving heater.
Heater Drain Cooler Approach Temperature Difference (DCA) - The difference between the temperature of the drains leaving the heater and the temperature of the feedwater entering the heater.