logging in or signing up CFBC Boiler MukeshKJha Download Post to : URL : Related Presentations : Let's Connect Share Add to Flag Embed Email Send to Blogs and Networks Add to Channel Copy embed code: Embed: Flash iPad Dynamic Copy Does not support media & animations Automatically changes to Flash or non-Flash embed WordPress Embed Customize Embed URL: Copy Thumbnail: Copy The presentation is successfully added In Your Favorites. Views: 12967 Category: Science & Tech.. License: All Rights Reserved Like it (8) Dislike it (0) Added: December 01, 2010 This Presentation is Public Favorites: 11 Presentation Description No description available. Comments Posting comment... By: kolapallipadmaka (19 month(s) ago) Dear mukesh, nice power pt. presentation. Please send this to my mail id- firstname.lastname@example.org Thanks. Saving..... Post Reply Close Saving..... Edit Comment Close By: joshipower (31 month(s) ago) Dear Mukesh, Pl allow me to download PPt or u can send it my mail id.- (email@example.com) Rgds, Dilip Joshi Saving..... Post Reply Close Saving..... Edit Comment Close By: er_anandsoni (37 month(s) ago) iam happy because share your views & knowledge thanks Saving..... Post Reply Close Saving..... Edit Comment Close By: darshitupadhyay (39 month(s) ago) very very impressive presentation. If possible,send it to firstname.lastname@example.org Saving..... Post Reply Close Saving..... Edit Comment Close By: kukmenon (39 month(s) ago) Good presentation. Please send this to email@example.com Saving..... Post Reply Close Saving..... Edit Comment Close loading.... See all Premium member Presentation Transcript An Overview of CFBC Boiler : An Overview of CFBC Boiler By- Mukesh Jha Sr.Engineer -Projects, a2z Powercom Pvt.Ltd. INTRODUCTION : INTRODUCTION Boiler- As per “THE INDIAN BOILERS(AMENDMENT ) ACT2007 A ‘Boiler’ means a pressure vessel in which steam is generated for use external to itself by application of heat which is wholly or partly under pressure when steam is shut off but does not include a pressure vessel With Capacity less than 25 ltrs (such capacity being measured from the feed check valve to the main steam stop valve); With less than 1 kilogram per centimeter square design gauge pressure & working gauge pressure; or In which water is heated below one hundred degree centigrade . Boiler Component : Boiler Component ‘Boiler component’ means Steam piping , Feed water piping, Economizer ,Super heater, any mounting or other fitting and any other external or internal part of a Boiler which is subjected to pressure exceeding one kilogram per centimeter square gauge. STEAM PIPING : STEAM PIPING “Steam Pipe "means any pipe through which steam passes if- (1)The pressure at which the steam passes through such pipe exceeds 3.5kg/cm^2 above atmospheric pressure, or (2)Such pipe exceeds 254 mm in internal diameter and pressure of steam exceeds 1kg/cm^2.above the atmospheric pressure. and includes in either case any connected fitting of a steam pipe. Slide 5: At atmospheric pressure water volume increases 1,600 times BURNER WATER SOURCE SOFTENERS CHEMICAL FEED FUEL BLOW DOWN SEPARATOR VENT STACK DEAERATOR PUMPS BOILER ECO-NOMI-ZER VENT EXHAUST GAS STEAM TO PROCESS Figure: Schematic overview of a boiler room Boiler Systems : Boiler Systems Flue gas system Water treatment system Feed water system Steam System Blow down system Fuel supply system Air Supply system Fuels used in Boiler : Fuels used in Boiler Types of Boilers : Types of Boilers Fire Tube Boiler Water Tube Boiler Packaged Boiler Stoker Fired Boiler Pulverized Fuel Boiler Waste Heat Boiler Fluidized Bed (FBC) Boiler Slide 9: Type of Boilers (Light Rail Transit Association) 1. Fire Tube Boiler Relatively small steam capacities (12,000 kg/hour) Low to medium steam pressures (18 kg/cm2) Operates with oil, gas or solid fuels Slide 10: Type of Boilers 2. Water Tube Boiler (Your Dictionary.com) Used for high steam demand and pressure requirements Capacity range of 4,500 – 120,000 kg/hour Combustion efficiency enhanced by induced draft provisions Lower tolerance for water quality and needs water treatment plant Slide 11: Type of Boilers (BIB Cochran, 2003) 3. Packaged Boiler Comes in complete package Features High heat transfer Faster evaporation Good convective heat transfer Good combustion efficiency High thermal efficiency Classified based on number of passes Slide 12: Type of Boilers 4. Stoke Fired Boilers Spreader stokers Uses both suspension and grate burning Coal fed continuously over burning coal bed Coal fines burn in suspension and larger coal pieces burn on grate Good flexibility to meet changing load requirements Preferred over other type of stokers in industrial application Slide 13: Type of Boilers 4. Stoke Fired Boilers b) Chain-grate or traveling-grate stoker (University of Missouri, 2004) Uses both suspension and grate burning Coal fed continuously over burning coal bed Coal fines burn in suspension and larger coal pieces burn on grate Good flexibility to meet changing load requirements Preferred over other type of stokers in industrial application Slide 14: Type of Boilers Tangential firing 5. Pulverized Fuel Boiler Pulverized coal powder blown with combustion air into boiler through burner nozzles Combustion temperature at 1300 -1700 °C Benefits: varying coal quality coal, quick response to load changes and high pre-heat air temperatures Coal is pulverized to a fine powder, so that less than 2% is +300 microns, and 70-75% is below 75 microns. Coal is blown with part of the combustion air into the boiler plant through a series of burner nozzles. Slide 15: Advantages Its ability to burn all ranks of coal from anthracitic to lignitic, and it permits combination firing (i.e., can use coal, oil and gas in same burner). Because of these advantages, there is widespread use of pulverized coal furnaces. Disadvantages High power demand for pulverizing Requires more maintenance, flyash erosion and pollution complicate unit operation Pulverized Fuel Boiler (Contd..) Slide 16: Type of Boilers Agriculture and Agri-Food Canada, 2001 6. Waste Heat Boiler Used when waste heat available at medium/high temp Auxiliary fuel burners used if steam demand is more than the waste heat can generate Used in heat recovery from exhaust gases from gas turbines and diesel engines Slide 17: 7.Fluidized Bed (FBC) Boiler An Overview- Fluidized bed combustion has emerged as a viable alternative and has significant advantages over conventional firing system and offers multiple benefits – compact boiler design, fuel flexibility, higher combustion efficiency and reduced emission of noxious pollutants such as SOx and NOx. The fuels burnt in these boilers include coal, washery rejects, rice husk, bagasse & other agricultural wastes. The fluidized bed boilers have a wide capacity range. Slide 18: Mechanism of Fluidised Bed Combustion When an evenly distributed air or gas is passed upward through a finely divided bed of solid particles such as sand supported on a fine mesh, the particles are undisturbed at low velocity. As air velocity is gradually increased, a stage is reached when the individual particles are suspended in the air stream – the bed is called “fluidized”. With further increase in air velocity, there is bubble formation, vigorous turbulence, rapid mixing and formation of dense defined bed surface. The bed of solid particles exhibits the properties of a boiling liquid and assumes the appearance of a fluid – “bubbling fluidized bed”. Slide 19: At higher velocities, bubbles disappear, and particles are blown out of the bed. Therefore, some amounts of particles have to be recirculated to maintain a stable system – “circulating fluidised bed”. Fluidization depends largely on the particle size and the air velocity. If sand particles in a fluidized state is heated to the ignition temperatures of coal, and coal is injected continuously into the bed, the coal will burn rapidly and bed attains a uniform temperature. The fluidized bed combustion (FBC) takes place at about 840OC to 950OC. Slide 20: Since this temperature is much below the ash fusion temperature, melting of ash and associated problems are avoided. The lower combustion temperature is achieved because of high coefficient of heat transfer due to rapid mixing in the fluidized bed and effective extraction of heat from the bed through in-bed heat transfer tubes and walls of the bed. The gas velocity is maintained between minimum fluidisation velocity and particle entrainment velocity. This ensures stable operation of the bed and avoids particle entrainment in the gas stream. Combustion process requires the three “T”s that is Time, Temperature and Turbulence. In FBC, turbulence is promoted by fluidisation. Improved mixing generates evenly distributed heat at lower temperature. Residence time is many times greater than conventional grate firing. Thus an FBC system releases heat more efficiently at lower temperatures. Slide 21: Fixing, bubbling and fast fluidized beds As the velocity of a gas flowing through a bed of particles increases, a value is reaches when the bed fluidises and bubbles form as in a boiling liquid. At higher velocities the bubbles disappear; and the solids are rapidly blown out of the bed and must be recycled to maintain a stable system. principle of fluidisation Slide 22: Since limestone is used as particle bed, control of sulfur dioxide and nitrogen oxide emissions in the combustion chamber is achieved without any additional control equipment. This is one of the major advantages over conventional boilers. Types of Fluidised Bed Combustion Boilers There are three basic types of fluidised bed combustion boilers: 1. Atmospheric classic Fluidised Bed Combustion System (AFBC) 2. Pressurised Fluidised Bed Combustion System (PFBC). 3. Circulating (fast) Fluidised Bed Combustion system(CFBC) Slide 23: AFBC / Bubbling Bed In AFBC, coal is crushed to a size of 1 – 10 mm depending on the rank of coal, type of fuel feed and fed into the combustion chamber. The atmospheric air, which acts as both the fluidization air and combustion air, is delivered at a pressure and flows through the bed after being preheated by the exhaust flue gases. The velocity of fluidising air is in the range of 1.2 to 3.7 m /sec. The rate at which air is blown through the bed determines the amount of fuel that can be reacted. Almost all AFBC/ bubbling bed boilers use in-bed evaporator tubes in the bed of limestone, sand and fuel for extracting the heat from the bed to maintain the bed temperature. The bed depth is usually 0.9 m to 1.5 m deep and the pressure drop averages about 1 inch of water per inch of bed depth. Very little material leaves the bubbling bed – only about 2 to 4 kg of solids are recycled per ton of fuel burned. Slide 24: Bubbling Bed Boilers In the bubbling bed type boiler, a layer of solid particles (mostly limestone, sand, ash and calcium sulfate) is contained on a grid near the bottom of the boiler. This layer is maintained in a turbulent state as low velocity air is forced into the bed from a plenum chamber beneath the grid. Fuel is added to this bed and combustion takes place. Normally, raw fuel in the bed does not exceed 2% of the total bed inventory. Velocity of the combustion air is kept at a minimum, yet high enough to maintain turbulence in the bed. Velocity is not high enough to carry significant quantities of solid particles out of the furnace. Slide 25: This turbulent mixing of air and fuel results in a residence time of up to five seconds. The combination of turbulent mixing and residence time permits bubbling bed boilers to operate at a furnace temperature below 1650°F. At this temperature, the presence of limestone mixed with fuel in the furnace achieves greater than 90% sulfur removal. Boiler efficiency is the percentage of total energy in the fuel that is used to produce steam. Combustion efficiency is the percentage of complete combustion of carbon in the fuel. Incomplete combustion results in the formation of carbon monoxide (CO) plus unburned carbon in the solid particles leaving the furnace. In a typical bubbling bed fluidized boiler, combustion efficiency can be as high as 92%. This is a good figure, but is lower than that achieved by pulverized coal or cyclone-fired boilers. In addition, some fuels that are very low in volatile matter cannot be completely burned within the available residence time in bubbling bed-type boilers. Slide 26: Features of bubbling bed boiler Fluidised bed boiler can operate at near atmospheric or elevated pressure and have these essential features: • Distribution plate through which air is blown for fluidizing. • Immersed steam-raising or water heating tubes which extract heat directly from the bed. • Tubes above the bed which extract heat from hot combustion gas before it enters the flue duct. Slide 27: Bubbling Bed Boiler-1 Slide 28: Bubbling Bed Boiler-2 Slide 32: 2. Pressurised Fluidised Bed Combustion System (PFBC). Pressurised Fluidised Bed Combustion (PFBC) is a variation of fluid bed technology that is meant for large-scale coal burning applications. In PFBC, the bed vessel is operated at pressure up to 16 ata ( 16 kg/cm2). The off-gas from the fluidized bed combustor drives the gas turbine. The steam turbine is driven by steam raised in tubes immersed in the fluidized bed. The condensate from the steam turbine is pre-heated using waste heat from gas turbine exhaust and is then taken as feed water for steam generation. The PFBC system can be used for cogeneration or combined cycle power generation. By combining the gas and steam turbines in this way, electricity is generated more efficiently than in conventional system. The overall conversion efficiency is higher by 5% to 8%. . At elevated pressure, the potential reduction in boiler size is considerable due to increased amount of combustion in pressurized mode and high heat flux through in-bed tubes. Slide 33: PFBC Boiler for Cogeneration Slide 34: 3. Circulating (fast) Fluidised Bed Combustion system(CFBC) The need to improve combustion efficiency (which also increases overall boiler efficiency and reduces operating costs) and the desire to burn a much wider range of fuels has led to the development and application of the CFB boiler. Through the years, boiler suppliers have been increasing the size of these high-efficiency steam generators. This CFBC technology utilizes the fluidized bed principle in which crushed (6 –12 mm size) fuel and limestone are injected into the furnace or combustor. The particles are suspended in a stream of upwardly flowing air (60-70% of the total air), which enters the bottom of the furnace through air distribution nozzles. The fluidising velocity in circulating beds ranges from 3.7 to 9 m/sec. The balance of combustion air is admitted above the bottom of the furnace as secondary air. Slide 35: The combustion takes place at 840-900oC, and the fine particles (<450 microns) are elutriated out of the furnace with flue gas velocity of 4-6 m/s. The particles are then collected by the solids separators and circulated back into the furnace. Solid recycle is about 50 to 100 kg per kg of fuel burnt. There are no steam generation tubes immersed in the bed. The circulating bed is designed to move a lot more solids out of the furnace area and to achieve most of the heat transfer outside the combustion zone - convection section, water walls, and at the exit of the riser. Some circulating bed units even have external heat exchanges. The particles circulation provides efficient heat transfer to the furnace walls and longer residence time for carbon and limestone utilization. Similar to Pulverized Coal (PC) firing, the controlling parameters in the CFB combustion process are temperature, residence time and turbulence. Slide 36: For large units, the taller furnace characteristics of CFBC boiler offers better space utilization, greater fuel particle and sorbent residence time for efficient combustion and SO2 capture, and easier application of staged combustion techniques for NOx control than AFBC generators. CFBC boilers are said to achieve better calcium to sulphur utilization – 1.5 to 1 vs. 3.2 to 1 for the AFBC boilers, although the furnace temperatures are almost the same. CFBC boilers are generally claimed to be more economical than AFBC boilers for industrial application requiring more than 75 – 100 T/hr of steam CFBC requires huge mechanical cyclones to capture and recycle the large amount of bed material, which requires a tall boiler. A CFBC could be good choice if the following conditions are met. 1. Capacity of boiler is large to medium 2.Sulphur emission and NOx control is important 3.The boiler is required to fire low-grade fuel or fuel with highly fluctuating fuel quality. Slide 39: Circulating bed boiler (At a Glance)- At high fluidizing gas velocities in which a fast recycling bed of fine material is superimposed on a bubbling bed of larger particles. The combustion temperature is controlled by rate of recycling of fine material. Hot fine material is separated from the flue gas by a cyclone and is partially cooled in a separate low velocity fluidized bed heat exchanger, where the heat is given up to the steam. The cooler fine material is then recycled to the dense bed. Slide 40: Advantages of Fluidised Bed Combustion Boilers 1. High Efficiency FBC boilers can burn fuel with a combustion efficiency of over 95% irrespective of ash content. FBC boilers can operate with overall efficiency of 84% (plus or minus 2%). 2. Reduction in Boiler Size High heat transfer rate over a small heat transfer area immersed in the bed result in overall size reduction of the boiler. 3. Fuel Flexibility FBC boilers can be operated efficiently with a variety of fuels. Even fuels like flotation slimes, washer rejects, agro waste can be burnt efficiently. These can be fed either independently or in combination with coal into the same furnace. 4. Ability to Burn Low Grade Fuel FBC boilers would give the rated output even with inferior quality fuel. The boilers can fire coals with ash content as high as 62% and having calorific value as low as 2,500 kcal/kg. Even carbon content of only 1% by weight can sustain the fluidised bed combustion. Slide 41: 5. Ability to Burn Fines Coal containing fines below 6 mm can be burnt efficiently in FBC boiler, which is very difficult to achieve in conventional firing system. 6. Pollution Control SO2 formation can be greatly minimised by addition of limestone or dolomite for high sulphur coals. 3% limestone is required for every 1% sulphur in the coal feed. Low combustion temperature eliminates NOx formation. 7. Low Corrosion and Erosion The corrosion and erosion effects are less due to lower combustion temperature, softness of ash and low particle velocity (of the order of 1 m/sec). 8. Easier Ash Removal – No Clinker Formation Since the temperature of the furnace is in the range of 750 – 900o C in FBC boilers, even coal of low ash fusion temperature can be burnt without clinker formation. Ash removal is easier as the ash flows like liquid from the combustion chamber. Hence less manpower is required for ash handling. Slide 42: 9. Less Excess Air – Higher CO2 in Flue Gas The CO2 in the flue gases will be of the order of 14 – 15% at full load. Hence, the FBC boiler can operate at low excess air - only 20 – 25%. 10. Simple Operation, Quick Start-Up High turbulence of the bed facilitates quick start up and shut down. Full automation of start up and operation using reliable equipment is possible. 11. Fast Response to Load Fluctuations Inherent high thermal storage characteristics can easily absorb fluctuation in fuel feed rates. Response to changing load is comparable to that of oil fired boilers. 12. No Slagging in the Furnace-No Soot Blowing In FBC boilers, volatilisation of alkali components in ash does not take place and the ash is non sticky. This means that there is no slagging or soot blowing. 13 Provisions of Automatic Coal and Ash Handling System Automatic systems for coal and ash handling can be incorporated, making the plant easy to operate comparable to oil or gas fired installation. Slide 43: 14 Provision of Automatic Ignition System Control systems using micro-processors and automatic ignition equipment give excellent control with minimum manual supervision. 15 High Reliability The absence of moving parts in the combustion zone results in a high degree of reliability and low maintenance costs. 16 Reduced Maintenance Routine overhauls are infrequent and high efficiency is maintained for long periods. 17 Quick Responses to Changing Demand A fluidized bed combustor can respond to changing heat demands more easily than stoker fired systems. This makes it very suitable for applications such as thermal fluid heaters, which require rapid responses. 18 High Efficiency of Power Generation By operating the fluidized bed at elevated pressure, it can be used to generate hot pressurized gases to power a gas turbine. This can be combined with a conventional steam turbine to improve the efficiency of electricity generation and give a potential fuel savings of at least 4%. Slide 46: General Arrangements of FBC Boiler FBC boilers comprise of following systems: i) Fuel feeding system ii) Air Distributor iii) Bed & In-bed heat transfer surface iv) Ash handling system Many of these are common to all types of FBC boilers 1. Fuel Feeding system For feeding fuel, sorbents like limestone or dolomite, usually two methods are followed: under bed pneumatic feeding and over-bed feeding. Under Bed Pneumatic Feeding If the fuel is coal, it is crushed to 1-6 mm size and pneumatically transported from feed hopper to the combustor through a feed pipe piercing the distributor. Based on the capacity of the boiler, the number of feed points is increased, as it is necessary to distribute the fuel into the bed uniformly. Slide 47: Over-Bed Feeding The crushed coal, 6-10 mm size is conveyed from coal bunker to a spreader by a screw conveyor. The spreader distributes the coal over the surface of the bed uniformly. This type of fuel feeding system accepts over size fuel also and eliminates transport lines, when compared to under-bed feeding system. 2. Air Distributor The purpose of the distributor is to introduce the fluidizing air evenly through the bed cross section thereby keeping the solid particles in constant motion, and preventing the formation of defluidization zones within the bed. The distributor, which forms the furnace floor, is normally constructed from metal plate with a number of perforations in a definite geometric pattern. The perforations may be located in simple nozzles or nozzles with bubble caps, which serve to prevent solid particles from flowing back into the space below the distributor. The distributor plate is protected from high temperature of the furnace by: i) Refractory Lining ii) A Static Layer of the Bed Material or iii) Water Cooled Tubes. Slide 48: 3. Bed & In-Bed Heat Transfer Surface: a) Bed The bed material can be sand, ash, crushed refractory or limestone, with an average size of about 1 mm. Depending on the bed height these are of two types: shallow bed and deep bed. At the same fluidizing velocity, the two ends fluidise differently, thus affecting the heat transfer to an immersed heat transfer surfaces. A shallow bed offers a lower bed resistance and hence a lower pressure drop and lower fan power consumption. In the case of deep bed, the pressure drop is more and this increases the effective gas velocity and also the fan power. b) In-Bed Heat Transfer Surface In a fluidized in-bed heat transfer process, it is necessary to transfer heat between the bed material and an immersed surface, which could be that of a tube bundle, or a coil. The heat exchanger orientation can be horizontal, vertical or inclined. From a pressure drop point of view, a horizontal bundle in a shallow bed is more attractive than a vertical bundle in a deep bed. Also, the heat transfer in the bed depends on number of parameters like (i) bed pressure (ii) bed temperature (iii) superficial gas velocity (iv) particle size (v) Heat exchanger design and (vi) gas distributor plate design. Slide 49: 4. Ash Handling System a) Bottom ash removal In the FBC boilers, the bottom ash constitutes roughly 30 - 40 % of the total ash, the rest being the fly ash. The bed ash is removed by continuous over flow to maintain bed height and also by intermittent flow from the bottom to remove over size particles, avoid accumulation and consequent defluidization. While firing high ash coal such as washery rejects, the bed ash overflow drain quantity is considerable so special care has to be taken. b) Fly ash removal The amount of fly ash to be handled in FBC boiler is relatively very high, when compared to conventional boilers. This is due to elutriation of particles at high velocities. Fly ash carried away by the flue gas is removed in number of stages; firstly in convection section, then from the bottom of air preheater/economizer and finally a major portion is removed in dust collectors. The types of dust collectors used are cyclone, bagfilters, electrostatic precipitators (ESP’s) or some combination of all of these. To increase the combustion efficiency, recycling of fly ash is practiced in some of the units. Slide 50: General Features of our Project(3nos) Installed Capacity : 1 X 15 MW Proposed Fuels : 85 % of Bagasse / Biomass, 15 % of Coal, Pet Coke. Boiler Type : Circulating Fluidized Bed Combustion (CFBC) Boiler parameters : Flow – 75 TPH Pressure – 87 Kg/cm^2 Temperature - 515 ± 5 oC Turbine Type : Two Nos. of uncontrolled extraction type and one no. of controlled extraction cum condensing type Turbine parameters : Pressure – 84 Kg/cm^2 Temperature - 510 ± 5 oC Plant load Factor : 0.85 No. of Days of power : 335 plant operation in a year Slide 51: General Features of our Project(1nos) Installed Capacity : 1 X 15 MW Proposed Fuels : 85 % of Bagasse / Biomass, 15 % of Coal, Pet Coke. Boiler Type : Circulating Fluidized Bed Combustion (CFBC) Boiler parameters : Flow – 100 TPH Pressure – 87 Kg/cm^2 Temperature - 515 ± 5 oC Turbine Type : Two Nos. of uncontrolled extraction type and one no. of controlled extraction cum condensing type Turbine parameters : Pressure – 84 Kg/cm^2 Temperature - 510 ± 5 oC Plant load Factor : 0.85 No. of Days of power : 335 plant operation in a year Slide 52: 600 MWe OTU CFB. Using the BENSON Vertical technology, Foster Wheeler has developed a design for a 600 MWe supercritical CFB boiler Future of CFBC Boiler Slide 54: FOSTER WHEELER AWARDED CONTRACT FOR WORLD’S LARGEST 100% BIOMASS BOILER ZUG, SWITZERLAND, April 7, 2010 - Foster Wheeler AG (Nasdaq: FWLT) announced today that its Global Power Group has been awarded a contract by GDF SUEZ, one of the leading energy providers in the world, for the design, supply and erection of a 190 MWe (gross megawatt electric) 100% biomass-fired circulating fluidized-bed (CFB) boiler island for the Polaniec Power Station in Poland. Foster Wheeler has received a full notice to proceed on this contract which will be executed jointly by its subsidiaries in Finland and Poland. The terms of the agreement were not disclosed and the contract value will be included in the company’s bookings for the first quarter of 2010. Construction completion and start of operation of the new steam generator is scheduled for fourth-quarter 2012. Foster Wheeler will design and supply the steam generator and auxiliary equipment, including biomass yard, and will carry out the civil works, erection and commissioning of the boiler island. Once complete, this will be the world’s largest biomass boiler burning wood residues and up to 20% agro biomass. Slide 55: Boiler Boiler blow down Boiler feed water treatment Performance of a boiler Slide 56: Performance of a Boiler 1. Boiler performance Causes of poor boiler performance Poor combustion Heat transfer surface fouling Poor operation and maintenance Deteriorating fuel and water quality Heat balance: identify heat losses Boiler efficiency: determine deviation from best efficiency Slide 57: Performance of a Boiler Heat Balance An energy flow diagram describes geographically how energy is transformed from fuel into useful energy, heat and losses Slide 58: Performance of a Boiler Heat Balance Balancing total energy entering a boiler against the energy that leaves the boiler in different forms Heat in Steam BOILER Heat loss due to dry flue gas Heat loss due to steam in fuel gas Heat loss due to moisture in fuel Heat loss due to unburnts in residue Heat loss due to moisture in air Heat loss due to radiation & other unaccounted loss % % % % 2% % % 100.0 % Fuel Slide 59: Performance of a Boiler Heat Balance Goal: improve energy efficiency by reducing avoidable losses Avoidable losses include: Stack gas losses (excess air, stack gas temperature) Losses by unburnt fuel Blow down losses Condensate losses Convection and radiation Slide 60: Performance of a Boiler Boiler Efficiency Thermal efficiency: % of (heat) energy input that is effectively useful in the generated steam The efficiency is the different between losses and energy input The energy gain of the working fluid (water and steam) is compared with the energy content of the boiler fuel. Slide 61: Performance of a Boiler hg -the enthalpy of saturated steam in kcal/kg of steam hf -the enthalpy of feed water in kcal/kg of water Boiler Efficiency: Direct Method Parameters to be monitored: Quantity of steam generated per hour (Q) in kg/hr Quantity of fuel used per hour (q) in kg/hr The working pressure (in kg/cm2(g)) and superheat temperature (oC), if any The temperature of feed water (oC) Type of fuel and gross calorific value of the fuel (GCV) in kcal/kg of fuel Slide 62: Performance of a Boiler Advantages Quick evaluation Few parameters for computation Few monitoring instruments Easy to compare evaporation ratios with benchmark figures Disadvantages No explanation of low efficiency Various losses not calculated Boiler Efficiency: Direct Method Slide 63: Performance of a Boiler Boiler Efficiency: Indirect Method Principle losses: i) Dry flue gas ii) Evaporation of water formed due to H2 in fuel iii) Evaporation of moisture in fuel iv) Moisture present in combustion air v) Unburnt fuel in fly ash vi) Unburnt fuel in bottom ash vii) Radiation and other unaccounted losses Slide 64: Performance of a Boiler Boiler Efficiency: Indirect Method Required calculation data Ultimate analysis of fuel (H2, O2, S, C, moisture content, ash content) % oxygen or CO2 in the flue gas Fuel gas temperature in ◦C (Tf) Ambient temperature in ◦C (Ta) and humidity of air in kg/kg of dry air GCV of fuel in kcal/kg % combustible in ash (in case of solid fuels) GCV of ash in kcal/kg (in case of solid fuels) Slide 65: Performance of a Boiler Boiler Efficiency: Indirect Method Advantages Complete mass and energy balance for each individual stream Makes it easier to identify options to improve boiler efficiency Disadvantages Time consuming Requires lab facilities for analysis Slide 66: Performance of a Boiler Controls ‘total dissolved solids’ (TDS) in the water that is boiled Blows off water and replaces it with feed water Conductivity measured as indication of TDS levels Calculation of quantity blow down required: 2. Boiler Blow Down Slide 67: Performance of a Boiler Two types of blow down Intermittent Manually operated valve reduces TDS Large short-term increases in feed water Substantial heat loss Continuous Ensures constant TDS and steam purity Heat lost can be recovered Common in high-pressure boilers Boiler Blow Down Slide 68: Performance of a Boiler Benefits Lower pretreatment costs Less make-up water consumption Reduced maintenance downtime Increased boiler life Lower consumption of treatment chemicals Boiler Blow Down Slide 69: Performance of a Boiler Quality of steam depend on water treatment to control Steam purity Deposits Corrosion Efficient heat transfer only if boiler water is free from deposit-forming solids 3. Boiler Feed Water Treatment Slide 70: Performance of a Boiler Deposit control To avoid efficiency losses and reduced heat transfer Hardness salts of calcium and magnesium Alkaline hardness: removed by boiling Non-alkaline: difficult to remove Silica forms hard silica scales Boiler Feed Water Treatment Slide 71: Performance of a Boiler Internal water treatment Chemicals added to boiler to prevent scale Different chemicals for different water types Conditions: Feed water is low in hardness salts Low pressure, high TDS content is tolerated Small water quantities treated Internal treatment alone not recommended Boiler Feed Water Treatment Slide 72: Performance of a Boiler External water treatment: Removal of suspended/dissolved solids and dissolved gases Pre-treatment: sedimentation and settling First treatment stage: removal of salts Processes Ion exchange Demineralization De-aeration Reverse osmoses Boiler Feed Water Treatment Slide 73: Performance of a Boiler a) Ion-exchange process (softener plant) Water passes through bed of natural zeolite of synthetic resin to remove hardness Base exchange: calcium (Ca) and magnesium (Mg) replaced with sodium (Na) ions Does not reduce TDS, blow down quantity and alkalinity b) Demineralization Complete removal of salts Cations in raw water replaced with hydrogen ions External Water Treatment Slide 74: Performance of a Boiler c) De-aeration Dissolved corrosive gases (O2, CO2) expelled by preheating the feed water Two types: Mechanical de-aeration: used prior to addition of chemical oxygen scavangers Chemical de-aeration: removes trace oxygen External Water Treatment Slide 75: Performance of a Boiler External Water Treatment ( National Productivity Council) Mechanical de-aeration O2 and CO2 removed by heating feed water Economical treatment process Vacuum type can reduce O2 to 0.02 mg/l Pressure type can reduce O2 to 0.005 mg/l Slide 76: Performance of a Boiler External Water Treatment Chemical de-aeration Removal of trace oxygen with scavenger Sodium sulphite: Reacts with oxygen: sodium sulphate Increases TDS: increased blow down Hydrazine Reacts with oxygen: nitrogen + water Does not increase TDS: used in high pressure boilers Slide 77: Performance of a Boiler d) Reverse osmosis Osmosis Solutions of differing concentrations Separated by a semi-permeable membrane Water moves to the higher concentration Reversed osmosis Higher concentrated liquid pressurized Water moves in reversed direction External Water Treatment Slide 78: Performance of a Boiler d) Reverse osmosis External water treatment Slide 79: Introduction Type of boilers Performance of a boiler Energy efficiency opportunities Slide 80: Stack temperature control Feed water preheating using economizers Combustion air pre-heating Incomplete combustion minimization Excess air control Avoid radiation and convection heat loss Automatic blow down control Reduction of scaling and soot losses Reduction of boiler steam pressure Variable speed control Controlling boiler loading Proper boiler scheduling Boiler replacement Energy Efficiency Opportunities Slide 81: 1. Stack Temperature Control Keep as low as possible If >200°C then recover waste heat Energy Efficiency Opportunities 2. Feed Water Preheating Economizers Potential to recover heat from 200 – 300 oC flue gases leaving a modern 3-pass shell boiler 3. Combustion Air Preheating If combustion air raised by 20°C = 1% improve thermal efficiency Slide 82: 4. Minimize Incomplete Combustion Symptoms: Smoke, high CO levels in exit flue gas Causes: Air shortage, fuel surplus, poor fuel distribution Poor mixing of fuel and air Oil-fired boiler: Improper viscosity, worn tops, cabonization on dips, deterioration of diffusers or spinner plates Coal-fired boiler: non-uniform coal size Energy Efficiency Opportunities Slide 83: 83 Energy Efficiency Opportunities 5. Excess Air Control Excess air required for complete combustion Optimum excess air levels varies 1% excess air reduction = 0.6% efficiency rise Portable or continuous oxygen analyzers Slide 84: Energy Efficiency Opportunities 7. Automatic Blow Down Control 6. Radiation and Convection Heat Loss Minimization Fixed heat loss from boiler shell, regardless of boiler output Repairing insulation can reduce loss Sense and respond to boiler water conductivity and pH Slide 85: Energy Efficiency Opportunities 9. Reduced Boiler Steam Pressure 8. Scaling and Soot Loss Reduction Every 22oC increase in stack temperature = 1% efficiency loss 3 mm of soot = 2.5% fuel increase Lower steam pressure = lower saturated steam temperature = lower flue gas temperature Steam generation pressure dictated by process Slide 86: Energy Efficiency Opportunities 11. Control Boiler Loading 10. Variable Speed Control for Fans, Blowers and Pumps Suited for fans, blowers, pumps Should be considered if boiler loads are variable Maximum boiler efficiency: 65-85% of rated load Significant efficiency loss: < 25% of rated load Slide 87: Energy Efficiency Opportunities 13. Boiler Replacement 12. Proper Boiler Scheduling Optimum efficiency: 65-85% of full load Few boilers at high loads is more efficient than large number at low loads Financially attractive if existing boiler is Old and inefficient Not capable of firing cheaper substitution fuel Over or under-sized for present requirements Not designed for ideal loading conditions Slide 88: Boilers THANK YOU FOR YOUR ATTENTION You do not have the permission to view this presentation. In order to view it, please contact the author of the presentation.