- •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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Protection, NOIDA |
CENPEEP/EFF/TP/201 |
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TITLE |
Rev. 1 |
Date: 01/20/00 |
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CENPEEP |
Routine Pulverizer Performance Test |
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requires accurate estimation of parameters such as moisture in coal, HGI of raw coal and mill output fineness.
Collection of a representative coal sample from pressurized gravimetric feeder had been a major constraint in characterizing the mill performance because of unrepresentative sampling location and inappropriate equipment for sample collection. The performance of the mill is governed by the following operating parameters that need to be set accurately if a reliable database is required to be generated.
a)Mill outlet temperature
b)Mill air flow
c)Accuracy of gravimetric feeder
d)Raw coal size
3Pulverizer Testing
Pulverizers are selected to provide a required grinding capacity, based upon a set of design criteria that include the required coal particle fineness and coal characteristics. The required pulverizer capacity is determined by the boiler heat input requirement, with some additional allowance added to account for wear of the mechanical parts. The required fineness is a function of specific coal properties such as the volatiles in coal and the rank of the coal. It is also a function of the type of burners, firing system and furnace size. Coal characteristics that determine the mill performance are the grindability and the moisture in the coal.
Pulverizer capacity shall vary according to the current operating conditions. There is a defined relationship between mill mechanical capacity, coal grindability and coal particle fineness. Higher grindability means that mill can grind more coal to same fineness or the same amount of coal to a greater fineness.
Pulverizer capacity is affected by such factors as moisture in coal, and the available primary air inlet temperature and flow. To a lesser extent, the ambient temperature and raw coal temperature will also affect the mill performance.
High ash content in coal results in greater loading on pulverizers and subsequent erosion causes performance degradation. Internal wear parts life varies from 2500 hrs for erosive coals to 5000 hrs for softer coals, and within the same pulverizer, the life of different components can differ by as much as 100%.
3.1 Process Description
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Centre For Power Efficiency And Environmental |
Procedure Number |
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NTPC |
Protection, NOIDA |
CENPEEP/EFF/TP/201 |
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TITLE |
Rev. 1 |
Date: 01/20/00 |
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CENPEEP |
Routine Pulverizer Performance Test |
Issue Date: |
Draft |
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Page: |
5 |
Of 18 |
This procedure provides guidelines for conducting the performance checks on pulverizers. Implementation of this procedure in conjunction with associated prerequisites shall result in identification of pulverizer system deficiencies and possible improvement of the coal pulverizer systems.
Performance guarantee tests conducted on the pulverizers for their acceptance stipulate most of these tests and base line data are available with most of the stations. However, the testing techniques have improved due to availability of modern instruments, which are capable of giving a better insight into pulverizer system performance. This procedure describes in detail the methodology of pulverizer testing using the dirty pitot testing kit.
3.2Objective
The objective of this procedure is to establish a standard method for the following performance tests related to the pulverizer system.
(1)Clean air balancing between coal transport pipes.
(2)Dirty air balancing between coal transport pipes.
(3)Fuel balancing between coal transport pipes.
(4)Fineness testing of pulverized coal using isokinetic sampling.
(5)Fineness testing of pulverized coal using non isokinetic sampling.
(6)Calibration of feeders.
This methodology is suitable for the following conditions only.
•For pulverized fuel sampling from vertical circular pipes.
•Maximum particle size to be sampled should be less than one-third diameter of the sampler tip aperture.
•Sampling to be done in pipes with an internal diameter between 250mm and 700mm.
•The air/coal ratio in the pipe is with in the normal range of direct fired pulverized system.
The numbers of sampling ports are determined based on the available straight lengths of coal pipes, upstream or downstream of the nearest bends. The guidelines for locating testing cross sections are described in ASME PTC 4.2.