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Questions and Answers
What is the primary focus of the document RIHAND-LMI-OD-OPS-SYST-009?
What is the primary focus of the document RIHAND-LMI-OD-OPS-SYST-009?
- The safe operation and maintenance of pulverised fuel plants (correct)
- The financial analysis of pulverised fuel operations
- The environmental impact assessment of pulverised fuel usage
- The installation process of pulverised fuel plants
Which of the following is mentioned as an important aspect of the pulverised fuel operation?
Which of the following is mentioned as an important aspect of the pulverised fuel operation?
- The development of an explosive mixture (correct)
- Cost reduction strategies
- Supplier relationship management
- Energy consumption management
What type of document is RIHAND-LMI-OD-OPS-SYST-009 classified as?
What type of document is RIHAND-LMI-OD-OPS-SYST-009 classified as?
- A procedure document
- A safety guideline (correct)
- A training manual
- A maintenance checklist
What is one of the key elements to be included in the instruction and training regarding pulverised fuel?
What is one of the key elements to be included in the instruction and training regarding pulverised fuel?
Which of the following is NOT listed in the index of the document?
Which of the following is NOT listed in the index of the document?
What is the design capacity of the PF Mill with the given specifications?
What is the design capacity of the PF Mill with the given specifications?
What type of feeder is mentioned for the PF Mill?
What type of feeder is mentioned for the PF Mill?
What criterion is NOT mentioned as a potential cause for pulverized fuel explosions?
What criterion is NOT mentioned as a potential cause for pulverized fuel explosions?
What is the maximum capacity range of the gravimetric feeder mentioned?
What is the maximum capacity range of the gravimetric feeder mentioned?
Which specific aspect concerning safety is highlighted in relation to P.F. handling?
Which specific aspect concerning safety is highlighted in relation to P.F. handling?
What is the HGI value of the raw coal for the minimum design capacity in the PF Mill?
What is the HGI value of the raw coal for the minimum design capacity in the PF Mill?
Which manufacturer's equipment is referenced in the PF Mill and RC Feeders?
Which manufacturer's equipment is referenced in the PF Mill and RC Feeders?
What air to fuel ratio indicates that an explosion cannot be sustained?
What air to fuel ratio indicates that an explosion cannot be sustained?
What is one cause of explosive mixtures in milling systems?
What is one cause of explosive mixtures in milling systems?
Where is it most likely for coal to ignite and produce coal gas leading to an explosion?
Where is it most likely for coal to ignite and produce coal gas leading to an explosion?
Which situation can lead to an accumulation of an explosive mixture in the boiler furnace?
Which situation can lead to an accumulation of an explosive mixture in the boiler furnace?
What typically precedes a complete loss of ignition?
What typically precedes a complete loss of ignition?
What is a potential consequence of partial loss of ignition during operation?
What is a potential consequence of partial loss of ignition during operation?
What limits the mill outlet temperature in a pulverized fuel system?
What limits the mill outlet temperature in a pulverized fuel system?
What happens if uncooled deposits of coal are allowed to remain in a mill system?
What happens if uncooled deposits of coal are allowed to remain in a mill system?
What element is crucial for an explosive mixture to form?
What element is crucial for an explosive mixture to form?
What condition might prevent the milling system from being put into service?
What condition might prevent the milling system from being put into service?
What is the minimum velocity in the P.F. pipes on a running mill required to minimize fuel deposition?
What is the minimum velocity in the P.F. pipes on a running mill required to minimize fuel deposition?
When are personnel allowed in the vicinity of the P.F. plant?
When are personnel allowed in the vicinity of the P.F. plant?
What should be established to ensure abnormalities in the milling system are communicated promptly?
What should be established to ensure abnormalities in the milling system are communicated promptly?
What action should be taken following an indication of over pressurization in a P.F. system?
What action should be taken following an indication of over pressurization in a P.F. system?
What temperature management guideline applies to a running mill's outlet temperature?
What temperature management guideline applies to a running mill's outlet temperature?
What is the purpose of maintaining design features like mill fire detectors in a P.F. plant?
What is the purpose of maintaining design features like mill fire detectors in a P.F. plant?
What is crucial to note during the operation of a standing mill?
What is crucial to note during the operation of a standing mill?
What should happen during a partial or complete loss of ignition in the milling process?
What should happen during a partial or complete loss of ignition in the milling process?
Flashcards
RIHAND-LMI-OD-OPS-SYST-009
RIHAND-LMI-OD-OPS-SYST-009
A document outlining instructions for safe operation and maintenance of a pulverized fuel plant at the Rihand Thermal Power Station.
Explosive Mixture
Explosive Mixture
A flammable mixture of combustible materials, often dust or fuel particles, and air. This mixture, when ignited, can lead to rapid combustion and an explosion within the PF plant.
Sources of Ignition
Sources of Ignition
Sources of ignition can be anything that provides the energy to start a fire or explosion within a PF plant. Examples include sparks, hot surfaces, static electricity, and even friction.
Instructions and Training
Instructions and Training
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Pulverized Fuel (PF)
Pulverized Fuel (PF)
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Design Capacity of a PF Mill
Design Capacity of a PF Mill
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Pulverized Fuel Fineness (70% through 200 mesh)
Pulverized Fuel Fineness (70% through 200 mesh)
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Grindability Index (HGI)
Grindability Index (HGI)
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Pulverized Fuel Explosion
Pulverized Fuel Explosion
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Leakage of Pulverized Fuel
Leakage of Pulverized Fuel
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Factors that Cause a PF Explosion
Factors that Cause a PF Explosion
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Ideal Air-to-Fuel Ratio in Milling Systems
Ideal Air-to-Fuel Ratio in Milling Systems
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Explosions in Milling Systems
Explosions in Milling Systems
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Causes of Explosive Mixtures in Milling Systems
Causes of Explosive Mixtures in Milling Systems
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Static Coal Ignition
Static Coal Ignition
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Explosive Mixtures in Boiler Furnaces
Explosive Mixtures in Boiler Furnaces
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Complete Loss of Ignition
Complete Loss of Ignition
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Partial Loss of Ignition
Partial Loss of Ignition
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Fuel Quality and Combustion
Fuel Quality and Combustion
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Ignition in PF Systems
Ignition in PF Systems
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Fuel/Gas Accumulation
Fuel/Gas Accumulation
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Pressure Relief Vents
Pressure Relief Vents
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Minimum Fuel Velocity
Minimum Fuel Velocity
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Over-Pressurization
Over-Pressurization
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Acceptable Mill Outlet Temperature
Acceptable Mill Outlet Temperature
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Maintaining Design Features
Maintaining Design Features
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PF Station Evacuation Procedure
PF Station Evacuation Procedure
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Line of Command and Communication
Line of Command and Communication
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Controlled Access to PF Plant
Controlled Access to PF Plant
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Study Notes
Location Management Instructions for Pulverized Fuel Plant
- Document title: The Safe Operation and Maintenance of Pulverised Fuel Plant
- Document name: RIHAND-LMI-OD-OPS-SYST-009
- Revision: 04, August 2022
- Review date: 02.12.2024
- Approved for implementation by: HOP (Rihand)
Index
- Document includes an index with page numbers for each topic
- Topics include introduction, superseded documents, reference documents, records of revision, scope, discussion and background information, the development of an explosive mixture, sources of ignition, instructions and training of plant staff, principles involved in safe operation and maintenance, operational procedures, fires in milling systems, actions in a mill system containing a fire, putting a mill system into service, taking a mill system out of service, coal flow failure, furnace precautions, burner management system (BMS)/FSSS, bunkers, boiler ash and dust hoppers, responsibility, review, distribution list, LMI checklist, and annexure
Introduction
- Ignition of finely divided combustible materials in suspension can cause significant explosions and emissions of flame, classified as dangerous
- All dusts, whether hot or cold, are considered dangerous
- Essential for personnel awareness of risks involved in pulverized fuel (PF) and hot fly ash explosions and fires
- Document provides information, defines acceptable practices, and outlines procedures to prevent accidents and deal with any accidental fires
Superseded Documents
- RIHAND-LMI-OD-OPS-SYST-009 Rev.03 (November 2021) listed as a superseded document
Reference Documents
- COS-ISO-00-OD/OPS/SYST/009Rev. no.: 0 (August 2022) referenced
Records of Revision
- LMI format adjusted according to RIHAND-LMI-OD-GEN-002 Rev 04, July 2021
- Clause 2.2.1.4 revised, featuring mill outlet temperatures for imported coal/pellet firing
- Clause 2.6.6 elaborated
Scope
- Document outlines operational and maintenance practices for minimizing explosions and fires in pulverised fuel (PF) plants
- Applicable to 6 x 500 MW units of NTPC Rihand, with specific technical specifications for PF mills, raw coal feeders, and associated PF piping and auxiliaries.
Discussion and Background Information
- Possible locations of PF explosions are detailed throughout milling systems, boiler furnaces.
- Focus on flammable dust/fuel suspensions in the air within explosive ranges and ignition sources.
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