This document provides information on instrumentation and control of material handling for an FGD plant. It discusses the process and instrumentation diagrams for limestone and gypsum handling systems. It describes various sensors used such as zero speed switches, chute block switches, belt sway switches, pull chord switches, vibration monitoring, temperature monitoring, and silo level monitoring. It outlines the control philosophy including operating modes, interlocks, and start up and shutdown sequences. Path selection, emergency stops, and alarm indications are also covered.
Oxygen treatment for super critical power plantsSantosh Pardhi
Oxygen treatment improves water quality in supercritical power plants by reducing flow-assisted corrosion and impurities that cause turbine blade deposits. It works by dosing oxygen gas at the deaerator and condensate polishing unit outlet to produce stable iron oxide layers that minimize corrosion. The advantages of oxygen treatment include virtually no iron transport, reduced flow-assisted corrosion, less frequent regeneration of condensate polishers, and a broad effective pH range.
A boiler is a device that generates steam by transferring heat from burning fuel to water. There are two main types: fire-tube boilers where hot gases pass through tubes surrounded by water, and water-tube boilers where water passes through tubes surrounded by hot gases. Boilers have many applications including power generation, heating, and industrial processes. Key factors in boiler selection include required steam properties, size, cost, and fuel/water availability. Boilers are also classified based on design features such as tube layout, firing method, pressure, and circulation.
Hello,
I am trying to explain about Steam Generator (Boiler) in this session, due to length of said presentation, I am deciding to divide it in three parts.
Part 1 cover the “Introduction & Types of Steam Generator”
Part 2 cover about the “Parts of Steam Generator and Its Accessories & Auxiliaries” and
Part 3 cover the “Efficiency & Performance”
This document summarizes the design of a water gas shift reactor system. It includes sections on the design objectives, specifications for the feed composition, catalyst properties, and dimensions of the high- and low-temperature shift reactors. It also describes the governing equations, assumptions, and methodology for simulating the reactor system performance. The simulation results show the conversion levels achieved in each reactor, their volumes, and the predicted pressure drops across the reactors. Features of the design are also discussed, along with overall conclusions.
This document summarizes different processes for removing carbon dioxide from ammonia plant streams. It discusses why CO2 removal is important, and describes common processes like MEA and MDEA absorption. The Benfield process uses hot potassium carbonate solution promoted by diethanolamine to physically absorb CO2. Issues with the Benfield process include foaming, corrosion, and vanadation problems. Retrofitting with a new amine promoter called LRS 10 can improve CO2 removal efficiency and reduce energy costs for the Benfield process.
This document summarizes the annual catalyst unloading and reloading process for the primary reformer at a chemical plant. It describes removing the spent catalyst from 224 tubes using vacuum pumps over 48 hours. Samples were taken and tubes were cleaned. New catalyst was then loaded in two layers - a bottom layer of nickel catalyst in 5 buckets per tube and a top layer of nickel-potassium catalyst in 7 buckets per tube. Dip heights and pressure drops were measured to ensure proper loading. The process was completed over 11 days during the annual turnaround.
The document discusses the turbine vacuum system, which is required to increase the enthalpy drop across the steam turbine and improve its efficiency. The key components of a vacuum system include the condenser, cooling water system, ejectors or vacuum pumps, and gland sealing system. The condenser uses cooling water to condense exhaust steam from the turbine, lowering the pressure and allowing more heat to be extracted from the steam. Ejectors or liquid ring vacuum pumps are then used to evacuate non-condensable gases from the condenser and achieve the desired vacuum level.
Oxygen treatment for super critical power plantsSantosh Pardhi
Oxygen treatment improves water quality in supercritical power plants by reducing flow-assisted corrosion and impurities that cause turbine blade deposits. It works by dosing oxygen gas at the deaerator and condensate polishing unit outlet to produce stable iron oxide layers that minimize corrosion. The advantages of oxygen treatment include virtually no iron transport, reduced flow-assisted corrosion, less frequent regeneration of condensate polishers, and a broad effective pH range.
A boiler is a device that generates steam by transferring heat from burning fuel to water. There are two main types: fire-tube boilers where hot gases pass through tubes surrounded by water, and water-tube boilers where water passes through tubes surrounded by hot gases. Boilers have many applications including power generation, heating, and industrial processes. Key factors in boiler selection include required steam properties, size, cost, and fuel/water availability. Boilers are also classified based on design features such as tube layout, firing method, pressure, and circulation.
Hello,
I am trying to explain about Steam Generator (Boiler) in this session, due to length of said presentation, I am deciding to divide it in three parts.
Part 1 cover the “Introduction & Types of Steam Generator”
Part 2 cover about the “Parts of Steam Generator and Its Accessories & Auxiliaries” and
Part 3 cover the “Efficiency & Performance”
This document summarizes the design of a water gas shift reactor system. It includes sections on the design objectives, specifications for the feed composition, catalyst properties, and dimensions of the high- and low-temperature shift reactors. It also describes the governing equations, assumptions, and methodology for simulating the reactor system performance. The simulation results show the conversion levels achieved in each reactor, their volumes, and the predicted pressure drops across the reactors. Features of the design are also discussed, along with overall conclusions.
This document summarizes different processes for removing carbon dioxide from ammonia plant streams. It discusses why CO2 removal is important, and describes common processes like MEA and MDEA absorption. The Benfield process uses hot potassium carbonate solution promoted by diethanolamine to physically absorb CO2. Issues with the Benfield process include foaming, corrosion, and vanadation problems. Retrofitting with a new amine promoter called LRS 10 can improve CO2 removal efficiency and reduce energy costs for the Benfield process.
This document summarizes the annual catalyst unloading and reloading process for the primary reformer at a chemical plant. It describes removing the spent catalyst from 224 tubes using vacuum pumps over 48 hours. Samples were taken and tubes were cleaned. New catalyst was then loaded in two layers - a bottom layer of nickel catalyst in 5 buckets per tube and a top layer of nickel-potassium catalyst in 7 buckets per tube. Dip heights and pressure drops were measured to ensure proper loading. The process was completed over 11 days during the annual turnaround.
The document discusses the turbine vacuum system, which is required to increase the enthalpy drop across the steam turbine and improve its efficiency. The key components of a vacuum system include the condenser, cooling water system, ejectors or vacuum pumps, and gland sealing system. The condenser uses cooling water to condense exhaust steam from the turbine, lowering the pressure and allowing more heat to be extracted from the steam. Ejectors or liquid ring vacuum pumps are then used to evacuate non-condensable gases from the condenser and achieve the desired vacuum level.
Power plant chemistry ( External Water Treatment )umar farooq
The document provides an overview of power plant chemistry and related topics. It discusses basic chemistry concepts, heat transfer, water chemistry, types of hardness in water, and marine ecology surveys. The document is presented in multiple parts that cover fundamental concepts, water treatment processes, steam water cycle systems, boiler operations, and course objectives for participants.
This document summarizes a new process for converting coal to ammonia using Kellogg Brown & Root's (KBR) Transport Reactor Integrated Gasifier (TRIG) technology. The process involves:
1. Gasifying coal using KBR's TRIG technology to produce syngas. The syngas is then purified through steps like acid gas removal.
2. Compressing the purified syngas and feeding it into an ammonia synthesis loop to produce ammonia using a conventional KBR ammonia process.
3. Recovering the ammonia produced and refrigerating it for storage or transport.
The paper provides details on the major unit operations in the coal gasification and ammonia
Refinery process, Refinery unit, catalyst, CDU, VDU, hydro cracker, residue up gradation unit.It is a part of Refinary Management. Interested people can gather knowledge from this PPT
This document provides information about boilers, including their definition, principle of operation, types, parts, and auxiliaries. It defines a boiler as a closed vessel that converts water into steam using heat energy from fuel. The key points are:
- Boilers work by transferring heat from hot flue gases to water via convection, converting the water to high-pressure steam.
- Boilers are classified based on whether tubes contain water or fire (fire tube or water tube), number of tubes, furnace position, shell axis orientation, and circulation method.
- Boiler parts include mountings like the water level indicator, pressure gauge, and safety valve, as well as accessories like the feed pump
High level introduction
Mainstream syngas = steam reforming processes
Ammonia; methanol; hydrogen/HyCO
Town gas
Steam reforming; low pressure cyclic
Direct reduction iron (DRI)
HYL type processes; Midrex type processes
This document provides an overview of the Butterworth-Heinemann Series in Chemical Engineering. It lists the series editor and advisory editors, as well as several example book titles in the series related to topics like chemical process equipment, gas separation processes, heterogeneous reactor design, and more. It also provides brief descriptions of some related titles on topics such as catalyst supports, particulate solids processing, mixing in process industries, and process control workshops.
Este documento discute la importancia de determinar la biodisponibilidad de metales pesados en sedimentos para evaluar el verdadero impacto ambiental. Explica que solo las formas solubles e intercambiables son biodisponibles. Describe el método de especiación química secuencial de Tessier para identificar las fases de los metales. Aplica este método a una cuenca y encuentra que los metales estudiados no presentan niveles de biodisponibilidad que representen un riesgo. Concluye que la mayoría de los metales
The document discusses hydrogen production via steam reforming of natural gas. Steam reforming involves four steps: reforming, shift conversion, gas purification, and methanation. It produces hydrogen at high efficiency and is the lowest cost production method currently available. However, it also produces carbon dioxide as a byproduct. Newer steam reforming plants use pressure swing absorption to produce 99.99% pure hydrogen. While steam reforming is an efficient process, it contributes to carbon dioxide emissions, so methods to capture and store the CO2 are being investigated.
This document provides information about water treatment processes and ion exchange resins used in water purification. It discusses the sources and types of water impurities and how treatment methods like coagulation with polyaluminum chloride, filtration through activated carbon filters, and ion exchange with resins like strong acid cation and weak acid cation can remove various contaminants. It also provides specifications for the ion exchange resins and details their chemical properties and manufacturing processes.
1. The document provides a detailed overview of cement chemistry and manufacturing processes. It covers the history of cement and key developments.
2. The main manufacturing processes - wet, dry suspension, and dry preheater processes - are described. The preheater system used to preheat raw materials is explained in detail.
3. The key cement minerals C3S, C2S, C3A, and C4AF are defined in terms of their chemical formulas and roles in cement hydration and strength development. Their properties and crystal structures are also summarized.
Cooling water is used to remove heat from machines and can be recycled or used once. Recirculating systems use cooling towers or ponds to remove heat. Industrial cooling towers use water sources like rivers as makeup water to replace evaporated water. They continuously circulate water through heat exchangers where heat is absorbed and rejected to the atmosphere through partial water evaporation. Different types of cooling towers exist like natural draft, induced draft, and forced draft towers which vary based on design and how air is moved through the tower. Key components, performance parameters, and maintenance factors of cooling towers are discussed.
(LTS) Low Temperature Shift Catalyst - Comprehensive OverviewGerard B. Hawkins
The document discusses low temperature shift catalysts used in hydrogen production plants. It describes the purpose of low temperature shift catalysts in further converting carbon monoxide to carbon dioxide to improve hydrogen yield and remove impurities. It then covers the chemistry, typical operating conditions, factors influencing catalyst activity like temperature profile and poisons, and byproduct formation issues. The document promotes the VSG-C111/112 series as superior catalysts, highlighting their resistance to poisons like sulfur and chloride, low methanol byproduct formation, high activity, and strength properties.
The document discusses how steam is used extensively in dairy processing for heating, sterilization, and maintaining hygienic conditions. Some key applications of steam mentioned include pasteurization, homogenization, UHT processing, heating water and air, evaporation, and cleaning and sterilization of equipment. The document also emphasizes the importance of high quality steam delivered at the proper pressure and temperature for efficient and precise process control.
PRESENTATION-Commissioning Experiences on Ammonia and Urea projects- Independ...Mumin HACIMUSALAR
This document provides an overview of the author's experience commissioning six ammonia and urea plants between 2002-2014 in various countries. It summarizes the key milestones and timelines for pre-commissioning and commissioning each plant. The time from start of pre-commissioning to first urea production ranged from 8 to 19 months. Most projects experienced delays, with the delay period ranging from 2 to 17 months compared to original targets. Factors contributing to delays included issues providing natural gas and obtaining necessary permits.
A boiler is a closed vessel that heats water or another fluid using combustion of fuels like wood, coal, oil, or gas. The heated fluid exits the boiler for use in processes or heating applications. There are different types of boilers including fire-tube boilers where hot gases pass through tubes in the boiler, water-tube boilers where water circulates in externally heated tubes, and flash boilers which rapidly vaporize water into steam. Boilers can be made of materials like steel, iron, or copper and come in configurations such as pot, fire-tube, water-tube, and sectional designs.
This document presents a case study and methods to re-establish a condemned boiler. It includes an introduction, contents listing, acknowledgements, abstract on the Hindustan Storage & Distribution Company where the boiler is located, specifications and diagrams of the boiler, scope of dismantling and repair work, results of dismantling, scope of work after renovation including flue gas analysis and boiler tuning.
(HTS) High Temperature Shift Catalyst (VSG-F101) - Comprehensiev OverviewGerard B. Hawkins
The document discusses improvements in high temperature shift catalysts. It describes the characteristics and operational issues of traditional HTS catalysts and how the new VULCAN Series VSG-F101 catalyst has addressed these issues through modifications to its microstructure and composition. The VSG-F101 has shown improved activity, strength, and resistance to thermal and mechanical stresses during plant upsets compared to previous catalysts.
The document discusses efficient operation and maintenance of boilers at NTPC Simhadri. It provides an overview of NTPC's journey and capacity, describes the types of boilers used, and outlines best practices adopted to reduce boiler tube leakages. These include improved startup procedures, monitoring of chemical parameters, thorough inspections and testing, and implementation of new technologies like acoustic leak detectors and process instrumentation systems. The presentation aims to share experiences in achieving zero boiler tube failures through preventative maintenance practices.
Boilers produce steam using thermal energy released from fuel combustion. Steam is used for power generation, heating buildings, and industrial processes. Boilers are classified based on orientation, tube configuration, firing method, circulation type, pressure, and number of tubes. Fire tube boilers have hot gases passing inside tubes surrounded by water, while water tube boilers have water inside tubes surrounded by hot gases. Common fire tube boilers include the Cochran, Cornish, and Lancashire designs. Water tube boilers are classified as horizontal or bent tube designs with multiple drums. Proper boiler selection depends on steam needs, space, costs, and other factors.
The document discusses steam turbine control and instrumentation. It describes various types of steam turbines including conventional cycle, combined cycle, and nuclear turbines ranging from 210MW to 800MW. It then discusses the aims of automation in steam turbines, including improved control quality, increased plant availability and efficiency. The document outlines the main subsystems of steam turbine control including control systems, monitoring and measurement systems, and protection systems. It provides details on an Automatic Turbine Run-Up System (ATRS) which automatically controls the start-up process. The ATRS utilizes functional group control philosophy and consists of sub-group controls, sub-loop controls, and drive interface controls. It also describes the turbine protection system and various tripping criteria to
The presentation will give you brief idea about the operation of hydro power plant which includes pre-check conditions, starting and stopping sequences, loading of unit, emergency stopping, parameter monitoring and control.
Power plant chemistry ( External Water Treatment )umar farooq
The document provides an overview of power plant chemistry and related topics. It discusses basic chemistry concepts, heat transfer, water chemistry, types of hardness in water, and marine ecology surveys. The document is presented in multiple parts that cover fundamental concepts, water treatment processes, steam water cycle systems, boiler operations, and course objectives for participants.
This document summarizes a new process for converting coal to ammonia using Kellogg Brown & Root's (KBR) Transport Reactor Integrated Gasifier (TRIG) technology. The process involves:
1. Gasifying coal using KBR's TRIG technology to produce syngas. The syngas is then purified through steps like acid gas removal.
2. Compressing the purified syngas and feeding it into an ammonia synthesis loop to produce ammonia using a conventional KBR ammonia process.
3. Recovering the ammonia produced and refrigerating it for storage or transport.
The paper provides details on the major unit operations in the coal gasification and ammonia
Refinery process, Refinery unit, catalyst, CDU, VDU, hydro cracker, residue up gradation unit.It is a part of Refinary Management. Interested people can gather knowledge from this PPT
This document provides information about boilers, including their definition, principle of operation, types, parts, and auxiliaries. It defines a boiler as a closed vessel that converts water into steam using heat energy from fuel. The key points are:
- Boilers work by transferring heat from hot flue gases to water via convection, converting the water to high-pressure steam.
- Boilers are classified based on whether tubes contain water or fire (fire tube or water tube), number of tubes, furnace position, shell axis orientation, and circulation method.
- Boiler parts include mountings like the water level indicator, pressure gauge, and safety valve, as well as accessories like the feed pump
High level introduction
Mainstream syngas = steam reforming processes
Ammonia; methanol; hydrogen/HyCO
Town gas
Steam reforming; low pressure cyclic
Direct reduction iron (DRI)
HYL type processes; Midrex type processes
This document provides an overview of the Butterworth-Heinemann Series in Chemical Engineering. It lists the series editor and advisory editors, as well as several example book titles in the series related to topics like chemical process equipment, gas separation processes, heterogeneous reactor design, and more. It also provides brief descriptions of some related titles on topics such as catalyst supports, particulate solids processing, mixing in process industries, and process control workshops.
Este documento discute la importancia de determinar la biodisponibilidad de metales pesados en sedimentos para evaluar el verdadero impacto ambiental. Explica que solo las formas solubles e intercambiables son biodisponibles. Describe el método de especiación química secuencial de Tessier para identificar las fases de los metales. Aplica este método a una cuenca y encuentra que los metales estudiados no presentan niveles de biodisponibilidad que representen un riesgo. Concluye que la mayoría de los metales
The document discusses hydrogen production via steam reforming of natural gas. Steam reforming involves four steps: reforming, shift conversion, gas purification, and methanation. It produces hydrogen at high efficiency and is the lowest cost production method currently available. However, it also produces carbon dioxide as a byproduct. Newer steam reforming plants use pressure swing absorption to produce 99.99% pure hydrogen. While steam reforming is an efficient process, it contributes to carbon dioxide emissions, so methods to capture and store the CO2 are being investigated.
This document provides information about water treatment processes and ion exchange resins used in water purification. It discusses the sources and types of water impurities and how treatment methods like coagulation with polyaluminum chloride, filtration through activated carbon filters, and ion exchange with resins like strong acid cation and weak acid cation can remove various contaminants. It also provides specifications for the ion exchange resins and details their chemical properties and manufacturing processes.
1. The document provides a detailed overview of cement chemistry and manufacturing processes. It covers the history of cement and key developments.
2. The main manufacturing processes - wet, dry suspension, and dry preheater processes - are described. The preheater system used to preheat raw materials is explained in detail.
3. The key cement minerals C3S, C2S, C3A, and C4AF are defined in terms of their chemical formulas and roles in cement hydration and strength development. Their properties and crystal structures are also summarized.
Cooling water is used to remove heat from machines and can be recycled or used once. Recirculating systems use cooling towers or ponds to remove heat. Industrial cooling towers use water sources like rivers as makeup water to replace evaporated water. They continuously circulate water through heat exchangers where heat is absorbed and rejected to the atmosphere through partial water evaporation. Different types of cooling towers exist like natural draft, induced draft, and forced draft towers which vary based on design and how air is moved through the tower. Key components, performance parameters, and maintenance factors of cooling towers are discussed.
(LTS) Low Temperature Shift Catalyst - Comprehensive OverviewGerard B. Hawkins
The document discusses low temperature shift catalysts used in hydrogen production plants. It describes the purpose of low temperature shift catalysts in further converting carbon monoxide to carbon dioxide to improve hydrogen yield and remove impurities. It then covers the chemistry, typical operating conditions, factors influencing catalyst activity like temperature profile and poisons, and byproduct formation issues. The document promotes the VSG-C111/112 series as superior catalysts, highlighting their resistance to poisons like sulfur and chloride, low methanol byproduct formation, high activity, and strength properties.
The document discusses how steam is used extensively in dairy processing for heating, sterilization, and maintaining hygienic conditions. Some key applications of steam mentioned include pasteurization, homogenization, UHT processing, heating water and air, evaporation, and cleaning and sterilization of equipment. The document also emphasizes the importance of high quality steam delivered at the proper pressure and temperature for efficient and precise process control.
PRESENTATION-Commissioning Experiences on Ammonia and Urea projects- Independ...Mumin HACIMUSALAR
This document provides an overview of the author's experience commissioning six ammonia and urea plants between 2002-2014 in various countries. It summarizes the key milestones and timelines for pre-commissioning and commissioning each plant. The time from start of pre-commissioning to first urea production ranged from 8 to 19 months. Most projects experienced delays, with the delay period ranging from 2 to 17 months compared to original targets. Factors contributing to delays included issues providing natural gas and obtaining necessary permits.
A boiler is a closed vessel that heats water or another fluid using combustion of fuels like wood, coal, oil, or gas. The heated fluid exits the boiler for use in processes or heating applications. There are different types of boilers including fire-tube boilers where hot gases pass through tubes in the boiler, water-tube boilers where water circulates in externally heated tubes, and flash boilers which rapidly vaporize water into steam. Boilers can be made of materials like steel, iron, or copper and come in configurations such as pot, fire-tube, water-tube, and sectional designs.
This document presents a case study and methods to re-establish a condemned boiler. It includes an introduction, contents listing, acknowledgements, abstract on the Hindustan Storage & Distribution Company where the boiler is located, specifications and diagrams of the boiler, scope of dismantling and repair work, results of dismantling, scope of work after renovation including flue gas analysis and boiler tuning.
(HTS) High Temperature Shift Catalyst (VSG-F101) - Comprehensiev OverviewGerard B. Hawkins
The document discusses improvements in high temperature shift catalysts. It describes the characteristics and operational issues of traditional HTS catalysts and how the new VULCAN Series VSG-F101 catalyst has addressed these issues through modifications to its microstructure and composition. The VSG-F101 has shown improved activity, strength, and resistance to thermal and mechanical stresses during plant upsets compared to previous catalysts.
The document discusses efficient operation and maintenance of boilers at NTPC Simhadri. It provides an overview of NTPC's journey and capacity, describes the types of boilers used, and outlines best practices adopted to reduce boiler tube leakages. These include improved startup procedures, monitoring of chemical parameters, thorough inspections and testing, and implementation of new technologies like acoustic leak detectors and process instrumentation systems. The presentation aims to share experiences in achieving zero boiler tube failures through preventative maintenance practices.
Boilers produce steam using thermal energy released from fuel combustion. Steam is used for power generation, heating buildings, and industrial processes. Boilers are classified based on orientation, tube configuration, firing method, circulation type, pressure, and number of tubes. Fire tube boilers have hot gases passing inside tubes surrounded by water, while water tube boilers have water inside tubes surrounded by hot gases. Common fire tube boilers include the Cochran, Cornish, and Lancashire designs. Water tube boilers are classified as horizontal or bent tube designs with multiple drums. Proper boiler selection depends on steam needs, space, costs, and other factors.
The document discusses steam turbine control and instrumentation. It describes various types of steam turbines including conventional cycle, combined cycle, and nuclear turbines ranging from 210MW to 800MW. It then discusses the aims of automation in steam turbines, including improved control quality, increased plant availability and efficiency. The document outlines the main subsystems of steam turbine control including control systems, monitoring and measurement systems, and protection systems. It provides details on an Automatic Turbine Run-Up System (ATRS) which automatically controls the start-up process. The ATRS utilizes functional group control philosophy and consists of sub-group controls, sub-loop controls, and drive interface controls. It also describes the turbine protection system and various tripping criteria to
The presentation will give you brief idea about the operation of hydro power plant which includes pre-check conditions, starting and stopping sequences, loading of unit, emergency stopping, parameter monitoring and control.
This document discusses instrument maintenance practices at National Fertilizers Limited, a chemical process industry. It outlines the importance of instrumentation in process industries and describes various types of control loops used. It then discusses different types of maintenance practices including day-to-day, preventative, shutdown, and breakdown maintenance. Finally, it outlines upgrades made to instrumentation systems, including implementing a distributed control system and programmable logic controllers, to improve reliability, efficiency, and use of latest technologies.
This document discusses instrument maintenance practices at National Fertilizers Limited, a chemical process industry. It outlines the importance of instrumentation in process industries and describes various types of control loops used. It then discusses different types of maintenance practices including day-to-day, preventative, shutdown, and breakdown maintenance. Finally, it outlines upgrades made to instrumentation systems, including replacing old pneumatic and single loop controllers with a distributed control system and programmable logic controllers to improve reliability, efficiency, and optimization.
RIG INTEGRATED APPS FOR DRILLING & COMPLETIONS OPERATIONSiQHub
The document discusses Rig Integrated Apps for automating Managed Pressure Drilling (MPD) operations. It describes apps that can integrate with rig control systems to automate MPD sequences like connections, tripping, and testing. This allows MPD operations to be conducted without constant human operation or oversight, improving safety, efficiency and reducing costs by requiring fewer on-site personnel. The apps analyze rig data in real-time to monitor pressures, detect kicks and other downhole events, and automatically adjust MPD equipment to maintain well control.
This document discusses cascade control systems. It defines cascade control as using two closed loop controllers where the output of the first controller is the set point of the second. The first loop is called the master controller and the second the slave controller. Cascade control provides more precise control of processes with multiple stages. It allows compensation for load changes and helps maintain desired values. The document outlines applications in steam power plants including drum level control and steam temperature control. It notes both advantages like improved dynamics but also drawbacks like increased complexity and cost.
The document provides information on an advanced soft starter product line including its range of models, voltage ranges, protection levels, control voltages, approvals, accessories, and key features. The soft starters have models ranging from 23A to 1600A and 7.5kW to 800kW with voltage ranges from 380V to 690V AC. Accessories include fingerguards, communication modules, remote operators, control panels, and software tools. Key features highlighted are the intuitive interface, adjustable busbars, monitoring capabilities, logs, parameter sets, and premium motor protection functions.
In this presentation , I have covered WM-PP interface. The presentation gives an overview of the concept as well as the process flow with and without the interface.It also talks about the master data and the various parameters that play a key role in the WM-PP processes
This document provides standard operating procedures for safely operating the 6.6kV switchboard at NMDC. It outlines safety precautions, roles and responsibilities, and step-by-step procedures for switching various feeders on and off, including incomer, bus coupler, and outgoing feeders. The procedures describe checking equipment status, obtaining clearances, verifying voltages and breaker positions before executing switch operations either locally or remotely via SCADA. Emergency conditions and general instructions are also covered.
Thermo scientific pro line overview - sales trainingTechno Service
Pro-Line Products provides bulk material handling products including conveyor accessories, motion monitors, flow switches, and point level switches. Some key products are belt misalignment switches, safety cable pull switches, tripper position switches, tilt switches, and capacitance level switches. These devices detect conditions like conveyor belt misalignment, emergency stops on conveyors, tripper car positions, and material levels in bins and silos to automate processes and provide alarms. The devices use technologies like mechanical switches, Doppler microwave sensing, and capacitance sensing to monitor bulk materials in various applications.
MR not building up due to issues with angle cocks, body bogie hoses, or air dryer bypass needing adjustment. BP not charging due to potential issues with cab setup, emergency brake handle position, TPWS cocks, or leaks from emergency exhaust or pneumatic panel. Check relevant isolating cocks, air pressures, cab modes, and fault codes to diagnose and resolve air pressure drops.
The document outlines goals for loop control, basic control systems, control strategies, instrumentation, and calibration. It discusses open and closed loop examples, basic control system components like circuit breakers and contactors, and control strategies for motors and valves. It also covers various types of instrumentation like proximity switches, speed sensors, level switches, pressure gauges and switches, temperature gauges and switches, and how to test, draw diagrams for, install, and calibrate them.
Interlocking System in Jaipur Metro.pptxAshish585772
The document discusses interlocking systems used in Jaipur Metro. It describes the basic components and functions of interlocking systems including point machines, signals, track circuits, route setting and locking. It covers primary safety considerations like safe behavior in normal and faulty conditions through fail-safe design. It also discusses interlocking interfaces, environmental factors, and key functions such as routes, points, signals and their control.
This document discusses switch-on-to-fault (SOTF) protection schemes. It describes the purpose of SOTF schemes, which is to trip a transmission line breaker when closed onto a faulted line. It outlines three common SOTF scheme applications and details the internal logic and settings of SOTF schemes in numerical relays. The document compares internal dead line detection logic to external trigger methods and discusses merits and limitations of different SOTF implementation methods. It also provides examples of SOTF logic for different breaker arrangements like one and a half breaker, double bus, and double bus transfer schemes.
The document describes the functions and design of a Burner Management System (BMS). The key purposes of a BMS are to safely start up and shut down fuel firing equipment, continuously monitor safety interlocks, and execute automatic shutdown if unacceptable conditions occur. It provides details on purge cycles, fuel selection permissives, trip conditions, alarms, and implementation including field devices, control electronics, and the human interface.
The document provides an overview of the Relion 670 series bay control REC670 product. It includes over 20 protection, control, monitoring and communication functions. Example functions include differential protection, overcurrent protection, voltage protection, frequency protection, autoreclosing, control functions like synchronism check and apparatus control. The product comes pre-configured in packages for single breaker, double breaker and 1.5 breaker applications with different interlocking and apparatus control capabilities. It has communication capabilities including horizontal GOOSE communication.
PROJECT ON WATER CONTROL IN AMUSEMENT PARK USINGPrashant Shekhar
This document presents a project to design a water control system for an amusement park ride using a programmable logic controller (PLC). The project is being conducted through an internship program in association with Mitsubishi Electric. The water ride involves detecting carts, filling and emptying a water tank using solenoid valves, and triggering a water jet. The PLC will sense the ride status and control the inlet and outlet valves to automate the water flow process.
1) The document describes several automation projects completed by MCM including assembly lines for ballast production, pipe bending, foam cutting, and exhaust pipe assembly with insulation.
2) Key features of the automation projects include use of pallets, pneumatic control systems, simultaneous operations at multiple stations, and modular designs allowing for increased productivity.
3) One project includes an 8-station transfer line that performs three successive operations to assemble insulated exhaust pipes at a rate of 6 pieces per minute. Another project utilizes a 10-station line to build core-coil subassemblies for ballasts.
The document describes DEIF's hydro control technology and products for hydro power plants. It discusses DEIF's headquarters in Skive, Denmark where they centralize production, R&D, testing, training and shipping. It then outlines their global sales and support network. The document proceeds to describe DEIF's controller solutions for hydro projects, including the DM-400 integrated controller. It provides an example application of the DM-400 controlling a Pelton turbine and discusses its functions. Finally, it summarizes DEIF products for mini, small and large hydro applications, including the GPC-3 controller for valve control in mini hydro plants.
Similar to Instrumentation & control of typical material handling of FGD Plant (20)
DEEP LEARNING FOR SMART GRID INTRUSION DETECTION: A HYBRID CNN-LSTM-BASED MODELgerogepatton
As digital technology becomes more deeply embedded in power systems, protecting the communication
networks of Smart Grids (SG) has emerged as a critical concern. Distributed Network Protocol 3 (DNP3)
represents a multi-tiered application layer protocol extensively utilized in Supervisory Control and Data
Acquisition (SCADA)-based smart grids to facilitate real-time data gathering and control functionalities.
Robust Intrusion Detection Systems (IDS) are necessary for early threat detection and mitigation because
of the interconnection of these networks, which makes them vulnerable to a variety of cyberattacks. To
solve this issue, this paper develops a hybrid Deep Learning (DL) model specifically designed for intrusion
detection in smart grids. The proposed approach is a combination of the Convolutional Neural Network
(CNN) and the Long-Short-Term Memory algorithms (LSTM). We employed a recent intrusion detection
dataset (DNP3), which focuses on unauthorized commands and Denial of Service (DoS) cyberattacks, to
train and test our model. The results of our experiments show that our CNN-LSTM method is much better
at finding smart grid intrusions than other deep learning algorithms used for classification. In addition,
our proposed approach improves accuracy, precision, recall, and F1 score, achieving a high detection
accuracy rate of 99.50%.
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Car accident rates have increased in recent years, resulting in losses in human lives, properties, and other financial costs. An embedded machine learning-based system is developed to address this critical issue. The system can monitor road conditions, detect driving patterns, and identify aggressive driving behaviors. The system is based on neural networks trained on a comprehensive dataset of driving events, driving styles, and road conditions. The system effectively detects potential risks and helps mitigate the frequency and impact of accidents. The primary goal is to ensure the safety of drivers and vehicles. Collecting data involved gathering information on three key road events: normal street and normal drive, speed bumps, circular yellow speed bumps, and three aggressive driving actions: sudden start, sudden stop, and sudden entry. The gathered data is processed and analyzed using a machine learning system designed for limited power and memory devices. The developed system resulted in 91.9% accuracy, 93.6% precision, and 92% recall. The achieved inference time on an Arduino Nano 33 BLE Sense with a 32-bit CPU running at 64 MHz is 34 ms and requires 2.6 kB peak RAM and 139.9 kB program flash memory, making it suitable for resource-constrained embedded systems.
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image analysis and enhance healthcare outcomes. This research paves the way
for future exploration and optimization of advanced CNN models in medical
imaging, emphasizing addressing false positives and resource efficiency.
2. • Process and Instrumentation
• Control Philosophy
• Frequency of switching between Operating and Standby
• Shutdown Sequence
• Annunciation and Alarm List
• Start Up Sequence
Topic
• Changeover Sequence
5. Process and Instrumentation
• Mounted on Tail Pulley /Snub Pulley
• Application: This device actuates relay contacts
at preset speed. Using these contacts desired
control action such as zero speed protection/
under speed protection can be achieved.
• Installed in Conveyor, Crusher, Bucket Elevator
and other rotating equipment.
• Mounted in Chute
• Application: This device actuates relay
contacts where chute is blocked due to
material Jamming
Zero Speed Switch
Chute Block Switch
6. Process and Instrumentation
• Mounted on Both Side of Conveyor
• Application: protective switch for detecting
the meandering (sway or deviation) of belt
conveyors, and sends out an alarm signal
• Detection & Monitoring Through Belt
Watch Panel
• Mounted on Both Side of Conveyor
• Application: Pull cord switch is used as
a safety switch to stop the conveyor
belt in case of an emergency
• Detection & Monitoring Through Belt
Watch Panel
Belt Sway Switch:
Pull Chord Switch:
7. • Belt Watch Panel1 for Lime Stone Handling System for
11 Nos. Belt conveyor & Belt Watch Panel2 for Lime
Stone Handling System for 3 Nos. Belt Watch Panel
• Each Belt Watch Panel having nos. of Belt Watch Controller
and each module connected to corresponding conveyor’s Belt
Sway Switch and Pull Chord Switch.
• 1) Master Cum Display Unit
• 2) Signal Module
• 3)Termination Module
• 4) Control Panel:
Process and Instrumentation
• Key Component of Belt Watch Panel.
9. Vibration Monitoring for Crusher 1 & 2
to determine the problem
• Unbalance
• Misalignment
• Mechanical Looseness
• Antifriction / Sleeve Bearing Defects
• Gear Defects
• Belt Defects
• Hammer Defects
• Bent Shaft
• Electrical Problems
• Resonance
Process and Instrumentation
Permissible Vibration Level:4.5mm/sec
10. Digital Vibration Indicator
Forbes Marshal 901P
PLC
4-20mA
PLC OUTPUT
Vibration Monitoring System
Process and Instrumentation
time waveform
DE-X & Y AXIS
NDE-X & Y AXIS
Shinkawa- CBT-420
11. Temperature Monitoring for Crusher Bearing(DE/NDE):
Process and Instrumentation
RTD –PT-100
Transmitter: E&H: TM-
112
PLC
4-20mA/Hart
• For Bearing Temperature Monitoring .
• Key Indicator of Bearing Health.
• Installed at Driving & Non Driving End – Bearing of Crusher 1 & 2
12. Silo Level Monitoring (Ultrasonic Level Measurement):
Process and Instrumentation
• For Silo Level Monitoring .
• Installed at Bin Top (SB1)
PLC
4-20mA/Hart
Level Sensor–Siemens:
Ecomax -XPS
Transmitter: LUT400
13. Belt Scale:
Process and Instrumentation
• Material Flow Measurement(t/h) & Totalized Output.
• Installed on BC-1 & BC-2
PLC
4-20mA (Flow Rate)
Totalized PulseOutput
KG/M
4 Nos.
IPA
14. The whole Limestone Handling System can be divided in two
independent handling systems as listed below. Each
system can operate either independently or as both.
Control Philosophy-Lime Stone Handling
• Path – IA through BF-1, BF-2, BC-1, CR-1, BF-5, BE-1A and BF-7
• Path – IB through BF-1, BF-2, BC-1, CR-1, BF-6, BE-1B and BF-7
• Path – IIA through BF-3, BF-4, BC-2, CR-2, BF-5, BE-1A and BF-
• Path – IIB through BF-3, BF-4, BC-2, CR-2, BF-6, BE-1B and BF-7
System-2- Handling systemfromLSStorageBin SB-1up toDayBin Silos DBS-1/2througheitherof
the followingpaths–
• Path – III through RF-1, BF-8 and BE-2A
• Path – IV through RF-2, BF-9 and BE-2B
System-1 - Handling system from Underground Tunnel up to LS Storage Bin SB-1 through
either of the following paths –
15. The Limestone & Gypsum Handling System will be
controlled and monitored from WFGD PLC
Three position Mode Selector Switch (MSS) on OWS -
Mode – I – Operation at automatic sequentially interlocked condition
Off
Mode – II- Operation at manual sequentially interlocked condition
Control Philosophy-Lime Stone & Gypsum Handling
System
Maintenance Bypass Selector Switch (MSS) on OWS
ON – Operation at Manual De-interlocked Condition during
Maintenance
Off
16. One Emergency Stop Button to stop the operation of the system in case of Emergency,
irrespective of positions Path Selector Switch and Mode Selector Switch .
HMI On Screen Image with Running / Position / On (Red) Indication, as applicable, for
each Motors / ILMS-1 / ILMS-2/ MD-1/ MD-2/ SM-1/ SM-2/ BW-1/ BW-2/ LSU/ FG-1/
FG-2/LSU.
HMI of Gypsum Handling System On Screen Image with Running / Position / On (Red)
Indication, as applicable, for each drives / Tripper-1/ Tripper-2/ FG-1/ FG-2
One no. Position (Green) Indication for the following items –
Control Philosophy-Lime Stone & Gypsum Handling
System
All positions for Path Selector Switch
All positions for Mode Selector Switch
All positions for Maintenance Bypass Switch
Provision tin OWS / HMI
17. Local Panels for SM-1, SM-2, BW-1, BW-2, ILMS-1, ILMS-2, MD-1, MD-2 shall
have Local/ Remote Mode Selector for Operation. All Operations of such
panels shall be done and monitored from either Locally or WFGD PLC as per
mode selected.
Local Control Panels for DE-1, DE-2 shall be controlled locally. Remote
feedback regarding trip and on status shall be taken to WFGD PLC, and run
permissive shall be obtained from WFGD PLC.
VS, FS shall be have all Motor and the system will be controlled from PLC.
Motors, Flap Gates, Rack & Pinion Gate, Motorised Butterfly Valves shall be
operated through WFGD PLC.
Control Philosophy-Lime Stone Handling
Local Panels
18. Local Push Button station.
Local push Button station with One Emergency Stop
Push Button for drive for Emergency operation
Control Philosophy-Lime Stone Handling
Hooter
One common Hooter will be located in suitable location of the
plant area. This hooter will be activated before starting of the
operation under any path.
19. This system is an Individual System and it operates separately.
It is operated from the Local Control Panel
The LSU can be started, if the conveyor BC-1 or BC-2 is running and the running permissive received from WFGD
PLC.
On starting of the system knife gate position is decided as per running status of BF-5 & BF-6.The
Knife Gate is closed in event of BF-05 in running mode, where the material will be fed to the
conveyor. The Knife Gate is energized and charged in event of BF-06 in running mode, where the
material will then be fed to BF-06.
Consequently the Screw Conveyor starts after the preset time and conveys the material.
At the system will check whether bottle sample collector is in proper position for sample collection. If it is not in
the position then it will rotate for proper position. After one hour it will rotate next bottle position for sample
filling.
After the preset time the Sample divider will start to rotate and which feed sample material to bottle collector
and also feed reject material to screw conveyor as per requirement..
Control Philosophy-Lime Stone Handling
Lime Sampling Unit
20. Damper
Damper Operation – As per selected path
S
VD
P
LocalControlPanel.
Sequential
Timer Panel
WFGDPLC
Dust
Extraction
System
1 for Under
Ground
Hopper area
2 for
Crusher House
Area
Control Philosophy-Lime Stone Handling
21. • The DE system shall be controlled from LCP through start command
and feedback from WFGD PLC.
• In local mode the there also have provision for manual operation
through start/stop button from local starter panel where as motorized
actuator will be operated from in-built starter panel.
• Selected Path Feedback to be obtained from WFGD PLC
• System ON command shall be given to the DE Panel from WFGD PLC.
• The motorized valves for different paths shall be energized according
to the path selection from PLC
Control Philosophy-Lime Stone Handling
Dust Extraction System
22. Damper Operation of Dust Extraction Crusher House area
BC01 MBV101 PATH-IA/IB
BC02 MBV102 PATH-IIA/IIB
BF05 MBV103 PATH-IA/IIA
BF06 MBV104 PATH-IB/IIB
BE1A INLET MBV105A PATH-IA/IIA
BE1B INLET MBV105B PATH-IB/IIB
BF-08 MBV106A PATH-III
BF-09 MBV106B PATH-IV
BE-2A(OUTLET) MBV108A PATH-III
BE-2B(OUTLET) MBV108B PATH-IV
BE-1A MBV109A PATH-IA/IIA
BE-1B MBV109B PATH-IB/IIB
BE-2A-INLET MBV111A PATH-III
BE-2B-INLET MBV111B PATH-IV
Control Philosophy-Lime Stone Handling
Damper Operation of Under Ground Hopper Area
BC01-BF-01-BF-02 MBV101B PATH-IA/IB
BC02-BF-03- BF04 MBV101A PATH-IIA/IIB
24. Silo Fluidization System
• Fluidising system consist compressor and
Sequential Timer Panel for Bin aeration.
• Each compressor having inbuilt starter and
local operation facility.
• The Fluidising System can be controlled from
the LHP Control Room.
Control Philosophy-Lime Stone Handling
25. Flap Gate (FG):
All Flap Gates shall be motorized actuator type, with power supply feeder in respective Panels. It shall be operated
From WFGD PLC.
• Feedback (F/b) & Output from WFGD PLC
• Indication on Local Panel
Rack and Pinion Gate (RPG):
Feedback (F/b) & Output from WFGD PLC
Indication on Local Panel
All Rack and Pinion Gates shall be motorized actuator type, with power supply feeder
in respective Panels. It shall be operated From WFGD PLC.
Control Philosophy-Lime Stone Handling
26. The whole Gypsum Handling System can be operated through
either of the following paths –
Control Philosophy-Gypsum Handling System
• Path – I through FG-01, BC-1A and Tripper-1
• Path – II through FG-01, BC-1B and Tripper-2
• Path – III through FG-02, BC-1B and Tripper-2
• Path – IV through FG-02, BC-1B and Tripper-1
27. Provision to be kept in OWS for Gypsum Handling System (contd)
a) One Emergency Stop (Red) Button to stop the operation of the system in case of
Emergency, irrespective of positions Path Selector Switch and Mode Selector Switch .
b) HMI On Screen Image with Running / Position / On (Red) Indication, as applicable, for
each drives / Tripper-1/ Tripper-2/ FG-1/ FG-2
c) One no. Position (Green) Indication for the following items –
All positions for Path Selector Switch
All positions for Mode Selector Switch
All positions for Maintenance Bypass Switch
28. Operation Philosophy –Gypsum
Handling System
Local Push Button station.
Local push Button station for all drives have One Emergency Stop Push Button
Local Panel:
• All Motor of local Panels shall have a Local /Remote Mode Selector.
• Motors shall be in Remote mode for operation through WFGD PLC and in Local mode for
operation from Local Panels. However, there are some panels which will have only
Operation Permissive in Remote Mode, but Operation shall be done locally.
• Local Emergency Stop from LPBS can be operated provided beside each local drive
irrespective of Local / Remote Mode Selection
Hooter
One common Hooter will be located in suitable location of the plant area. This hooter will
be activated before starting of the operation under any path
29. Control Philosophy for Tripper panel
• Tripper Panel will be mounted on Tripper car. In Local mode same can be operated
from local panel.
• Two nos. emergency stop button is considered. One will be provided on Tripper Panel
and another will be provided fixed platform to stop the machine at any position from
Tripper panel and also from fixed platform.
• The tripper brakes and rail clamps shall be energised (and released) when the tripper
motors are ON and the brakes will be applied when the travel motors are OFF.
• Two travel limit switches (TLS & OTLS) shall be provided at either end of tripper
carriage for limiting the travel drive between two ends of the track. The first one shall
be normal limit and the second one for over travel limit.
• In addition to above, 2 Nos. position indication Limit switch for position of tripper will
be provided in Main control room.
Operation Philosophy –Gypsum
Handling System
30. Tripper Control Panel
Operation Philosophy –Gypsum
Handling System
Following individual indications shall be provided on local control panel
1) Motor ON/OFF/TRIP
2) Brakes applied
3) Rail clamps applied
4) Flap gate position
Indication of tripper flap gate positions shall be given in the main LHP control room.
Chute blockage switch shall be provided at each leg of chute and shall trip the tripper
conveyor in case of blockage.
31. Operation Philosophy –Gypsum
Handling System
Belt Watch Panel (BWP):
Feedback (F/b) & Output from WFGD PLC
• PCS Operated for Each Conveyors & Belt Feeders
• BSS Operated for Each Conveyors & Belt Feeders
Indication on Local Panel
• Identification of PCS and BSS Operated.
• Mode of communication with WFGD PLC through Analog Signal Cable and
Digital Signal Cable
Flap Gates (FG-1, FG-2, 3WFG-1, 3WFG-2, 3WFG-3, 3WFG-4)
• Feedback (F/b) & Output from WFGD PLC
• All Flap Gates shall be motorized actuator type, with power supply feeder in
respective Panels. It shall be operated From WFGD PLC.
32. Operation Philosophy –Gypsum
Handling System
Dust Suppression System.
• The dust suppression system mainly consists of a solenoid valve, with water pipe line
throughout the gypsum storage shade.
• The Water Pipe lines are equipped with nozzles at different strategic positions.
• The water will be available from customer’s end up to the solenoid valve at desired
pressure.
• The Solenoid Valve shall be operated from the WFGD PLC Control Room and are
included within the System operation sequence.
33. Control Philosophy – Start Up, Shut down &
Interlocking – Lime Stone Handling System
PATH-Selector
Switch (PSS)
PATH-IA PATH-IB PATH-IIA PATH-IIB
Operation at Automatic Sequentially Interlocked Condition
Mode Selector Switch: MSS in Mode-I (Automatic Sequentially Operation)
Maintenance Bypass Switch (MBS) on HMI Screen is kept ‘Off’ position
All respective Flap Gates (FG) on HMI Screen are kept in required position.
Level of LS Storage Bin SB-1(LI) is not high.
Start Ventilation System (VS)
All Drives and Local Panels shall be in remote mode Selected Position
PCS – not operated for the selected Path
BSS – not operated for the selected Path
Emergency Stop– not operated for the selected Path
VMS for Crusher – Not High
Temperature for Crusher – not high.
Chute Block switch not operated
Motor Protection for respective Feeders not tripped
Interlocking.
34. Additional
Interlocking for
Magnetic
Separators,
Suspended
Magnets, and
Metal detector
and Flap Gate
O/L Fault Relay – Not Tripped.
All Stop PB – Reset.
Metal Detector – Reset
FG – End of Travel Limit Switch – Reset
FG – Thrust Limit Switch – Reset.
Control Philosophy – Start Up, Shut down &
Interlocking – Lime Stone Handling System
35. Path – IA – START UP
STOP
Button
RPG1&2
Belt
Feeder1&2
Other drive Opposite
to Start Seq.
Ventilation
Fan
Path – IA – STOP
System will trip if Interlocking condition fail
Control Philosophy – Start Up, Shut down &
Interlocking – Lime Stone Handling System
36. Path – IB – START UP
STOP
Button
RPG1&2
Belt
Feeder1&2
Other drive Opposite
to Start Seq.
Ventilation
Fan
Path – IB – STOP
System will trip if Interlocking condition fail
Control Philosophy – Start Up, Shut down &
Interlocking – Lime Stone Handling System
37. Path – IIA – START UP
STOP
Button
RPG3&4
Belt
Feeder3&4
Other drive Opposite
to Start Seq.
Ventilation
Fan
Path – IIA – STOP
System will trip if Interlocking condition fail
Control Philosophy – Start Up, Shut down &
Interlocking – Lime Stone Handling System
38. Path – IIB – START UP
STOP
Button
RPG3&4
Belt
Feeder3&4
Other drive Opposite
to Start Seq.
Ventilation
Fan
Path – IIB – STOP
System will trip if Interlocking condition fail
Control Philosophy – Start Up, Shut down &
Interlocking – Lime Stone Handling System
39. PATH-Selector Switch
(PSS)
PATH-III PATH-IV
Operation at Automatic Sequentially Interlocked Condition
Mode Selector Switch: MSS in Mode-I (Automatic Sequentially Operation)
Maintenance Bypass Switch (MBS) on HMI Screen is kept ‘Off’ position
Fluidizing System shall be in ‘ON’ condition.
Level of LS Storage Bin SB-1(LI) is not LOW.
All Drives and Local Panels shall be in remote mode Selected Position
PCS – not operated for the selected Path
BSS – not operated for the selected Path
Emergency Stop– not operated for the selected Path
Chute Block switch not operated
Motor Protection for respective Feeders not tripped
Interlocking.
Control Philosophy – Start Up, Shut down &
Interlocking – Lime Stone Handling System
40. START
Button
DE-2 BE-2A BF-8 RF-1
Path – III – START UP
STOP Button RF-1 BF-8 BE-2A DE-2
Path – III – STOP
System will trip if Interlocking condition fail
Control Philosophy – Start Up, Shut down &
Interlocking – Lime Stone Handling System
41. START
Button
DE-2 BE-2A BF-8 RF-1
Path – III – START UP
STOP Button RF-1 BF-8 BE-2A DE-2
Path – III – STOP
System will trip if Interlocking condition fail
Control Philosophy – Start Up, Shut down &
Interlocking – Lime Stone Handling System
42. PATH-Selector
Switch (PSS)
PATH-I PATH-II PATH-III PATH-IV
Operation at Automatic Sequentially Interlocked Condition
Mode Selector Switch: MSS in Mode-I (Automatic Sequentially Operation)
Maintenance Bypass Switch (MBS) on HMI Screen is kept ‘Off’ position
Flap Gate in proper position.
All Drives and Local Panels shall be in remote mode Selected Position
PCS – not operated for the selected Path
BSS – not operated for the selected Path
Emergency Stop– not operated for the selected Path
Under speed switch – closed at 90% speed of the conveyor within designed accelerated time.
Chute Block switch not operated
Motor Protection for respective Feeders not tripped
Interlocking.
Control Philosophy – Start Up, Shut down &
Interlocking – Gypsum Handling System
43. START
Button
3WFG-1
& 2 -
OPEN
BC-1A DS-SV BF-1
Path – I – START UP
STOP Button
VACCUM
FILTER
DS-SV BC-1A
3WG-1&2
CLOSE
Path – I – STOP
System will trip if Interlocking condition fail
Control Philosophy – Start Up, Shut down &
Interlocking – Lime Stone Handling System
44. START
Button
3WFG-3
& 4 -
OPEN
BC-1B DS-SV BF-2
Path – II – START UP
STOP Button
VACCUM
FILTER
DS-SV BC-1B
3WG-3&4
CLOSE
Path – II – STOP
System will trip if Interlocking condition fail
Control Philosophy – Start Up, Shut down &
Interlocking – Lime Stone Handling System
45. START
Button
3WFG-3
& 4 -
OPEN
BC-1B DS-SV BF-2
Path – III – START UP
STOP Button
VACCUM
FILTER
DS-SV BC-1b
3WG-3&4
CLOSE
Path – III – STOP
System will trip if Interlocking condition fail
Control Philosophy – Start Up, Shut down &
Interlocking – Lime Stone Handling System
46. START
Button
3WFG-
1 & 2
OPEN
BC-1A DS-SV RBF-1
Vaccum
Filter-2
Path – IV – START UP
STOP Button
VACCUM
FILTER-2
DS-SV BC-1A
3WG-1&2
CLOSE
Path – IV – STOP
System will trip if Interlocking condition fail
Control Philosophy – Start Up, Shut down &
Interlocking – Lime Stone Handling System
47. Condition Status : Normal
Control Philosophy: Annunciation & Alarm
Annunciation System on HMI/OWS will be as follows:-
Annunciation Window on OWS Screens : Off
Status indication of Equipments/ Signals : Steady Glow.
Buzzer : Off
Condition Status : Fault
Annunciation Window on OWS Screens : Blinking
Status indication of Equipments/ Signals : Fast Blinking
Buzzer : Sounding
48. Press Accept Button
Control Philosophy: Annunciation & Alarm
Annunciation Window on OWS Screens : Steady Glow
Status indication of Equipments/ Signals : Fast Blinking.
Buzzer : Off
Press Reset after Fault Clearance
Annunciation Window on OWS Screens : OFF
Status indication of Equipments/ Signals : Steady Blinking
Buzzer : Off
Press Reset Before Fault Clearance
Annunciation Window on OWS Screens : Steady Glow
Status indication of Equipments/ Signals : Fast Blinking
Buzzer : Off
49. • Overload Relay operated for all Motor Drives
• Pull Chord Switch operated for all Belt Conveyors & Belt Feeders, as applicable
• Belt Sway Switch operated for all Belt Conveyors & Belt Feeders, as applicable
• Zero Speed Switch operated for all Belt Conveyors & Belt Feeders, as applicable
• Level High of LS Storage Bin SB-1
• Level High of Sump in Underground Hopper Area.
• Chute Blocked as applicable.
Annunciation & Alarm: Limestone Handling System
Annunciation in HMI:-
50. Magnetic separator fault and cleaning belt trip.
Metal detector fault.
Metal Detected.
Metal detector Not Reset.
Belt weigher fault.
Sampling System fault.
Dust Extraction system fault and trips.
Emergency Stop Push Button operated.
Annunciation & Alarm: Limestone Handling System
Annunciation in HMI:-
51. Overload Relay operated for all Motor Drives
Pull Chord Switch operated for all Belt Conveyors & Reversible Belt Feeder, as applicable
Belt Sway Switch operated for all Belt Conveyors & Reversible Belt Feeder, as applicable
Zero Speed Switch operated for all Belt Conveyors & Reversible Belt Feeders, as applicable
Chute Plugged as applicable.
Dust Suppression Pressure Switch Low.
Emergency Stop Push Button operated.
Annunciation & Alarm: Gypsum Handling System
Annunciation in HMI:-