PERFORMANCE EVALUATION AND RECURRING JAMMING PROBLEM ANALYSIS OF AIR PREHEATER IN COAL-FIRED POWER PLANTS

Similar documents
HEAT EXCHANGERS. Heat exchangers are broadly classified based on the following considerations.

Design of Air Pre-Heater for Blast Furnace Gas Fired Boiler

Boiler Draft Equipment

Heat Exchanger. The purpose may be either to remove heat from a fluid or to add heat to a fluid.

Fig.: macroscopic kinetic energy is an organized form of energy and is much more useful

Heat Recovery Units. Heat Recovery 1

Problem Cause Remedial action. Gauge glass There was excess chemical dosage The normal ph recommended was 9.5 to See photo 3 & 4.

CENTRIFUGAL PUMPS. STATE the purposes of the following centrifugal pump components:

THE GATE COACH All Rights Reserved 28, Jia Sarai N.Delhi-16, ,-9998

Torad Rotary Spool Compressor

Seyedeh Sepideh Ghaffari 1 & Seyed Ali Jazayeri 2

CL4001 HEAT TRANSFER OPERATIONS

Solution of I Mid Term Steam Engineering 6ME5A

Introduction to Heat Exchangers

Analysis of Evaporative Cooler and Tube in Tube Heat Exchanger in Intercooling of Gas Turbine

The Condensate Water Systems

PESIT-Bangalore South Campus

2x58 MW Coal Fired Power Plant at Mauritius

WHAT IS A BOILER? BOILER IS AN EQUIPMENT WHICH PRODUCES STEAM AT THE REQUIRED PRESSURE AND TEMPERATURE. BOILER DESIGN, MANUFACTURE & INSTALLATION ARE

OPTIMISATION OF SOOT BLOWER OPERATION IN BOILER TO IMPROVE EFFICIENCNY

B.Tech. First Semester Examination Basics of Mechanical Engineering (ME-101F)

Amec Foster Wheeler- Fired Heater Division

Heat pump and energy recovery systems

Brown Hills College of Engineering & Technology

Compression of Fins pipe and simple Heat pipe Using CFD

There are two devices used together for heating crude oil in petroleum refinery as in figure (1), and these devices are:

Review on Waste Heat Recovery Techniques in Air Conditioning Application

Boiler. Fire tube Boiler:

FAN PERFORMANCE AND UTILIZATION OF COMPRESSED AIR IN THERMALPOWERPLANT

Analysis to speed up of the start-up of steam boiler OP-380

PACKAGED COMMERCIAL WATERTUBE BOILERS

CFD Analysis of temperature dissipation from a hollow metallic pipe through circular fins using Ansys 14.5

Electric Power Conference, 2011 Section 6D: Innovations of Maintenance Technologies and Practice 1

Bryan Flexible Water Tube. Ultra-High Efficiency Condensing Hot Water Boilers. 3,000,000 BTUH Natural Gas Fired

Design and Construction Standards SECTION PLUMBING EQUIPMENT

Experimental investigation of Hybrid Nanofluid on wickless heat pipe heat exchanger thermal performance

A chimney system Re-designing to increase boiler efficiency against fouling.

Sootblowers. Learning Outcome. Learning Objectives. When you complete this module you will be able to: Discuss sootblowers.

CHAPTER 3 BASIC STEAM CYCLE

Influence of Feed Water Heaters on the Performance of Coal Fired Power Plants

COOPERATIVE PATENT CLASSIFICATION

Heat Transfer Enhancement using Herringbone wavy & Smooth Wavy fin Heat Exchanger for Hydraulic Oil Cooling

Energy recovery from exhaust gases using Heat Pipe technology

NOx REDUCTION EXPERIENCE ON NATURAL GAS FIRED TURBO FURNACES

AUTOMATION OF BOILERS USING LABVIEW

When you complete this module you will be able to: Describe various watertube boiler designs, including large generating units.

Study and Design Considerations of HRSG Evaporators in Fast Start Combined Cycle Plants. Govind Rengarajan, P.E.CEM, Dan Taylor

How is the heat transfer?

As we discussed early in the first chapter that heat can transfer through materials and the surrounding medium whenever temperature gradient exists

Jurnal UMP Social Sciences and Technology Management Vol. 3, Issue. 3,2015

Enhanced Temperature Control Logic for Electro Static Precipitator (ESP) Hopper Heaters

HOT AIR AIR HEATER. (888) Copyright 2010 Paragon Airheater Technologies, All Right Reserved

JÄSPI Solid Fuel Boiler

Steam Power Cycles Part II

ETA ACCU 90% HIGHEST EFFICIENCY AIR HANDLING UNIT

PIPING SYSTEM EQUIPMENTS

ASH MEASUREMENT AT NRG HUNTLEY USING HIGH TEMPERATURE STRAIN GAUGES

Experience In Motion. WXH and WXM Utility-Grade Multistage Ring Section Pumps

SECTION PLUMBING EQUIPMENT

RHC GAS FIRED HEATING COILS

Department of Mechanical and Production Engineering Ahsanullah University of Science and Technology (AUST) Lab Manual on ME 4202

Trends for Radiant Tube Heated Strip Lines

MODEL ANSWER FOR ELEMENTS OF MECH.ENGG.(17413) 1) steam boiler- It is a closed vessel in which steam is produced from water by combustion of fuel.

Thermal Fluid Heaters

CHAPTER 6. HEATING PRODUCTION EQUIPMENT AND SYSTEMS

Division III Process Gas Treatment Equipment

New generation heat exchanger improves industrial energy efficiency

CHAPTER 2: PROPERTIES OF STEAM AND STEAM POWER

Numerical Stability Analysis of a Natural Circulation Steam Generator with a Non-uniform Heating Profile over the tube length

Access Energy Thermapower Organic Rankine Cycle (ORC) Systems

Trade of Plumbing. Module 2: Domestic Hot and Cold Water Service Unit 10: Hot Water Supply Phase 2

ANALYSING THE EFFECTIVENESS OF THE HEAT EXCHANGER BY INCREASING OVERALL HEAT TRANSFER COEFFICIENT

Pulse Jet Baghouse ASTEC PULSE JET BAGHOUSE. for Asphalt Facilities

HOW TO BOOST THE PERFORMANCE OF FIRED HEATERS

IV SEMESTER DIPLOMA EXAMINATION, JANUARY-2013 THERMODYNAMICS

Multifunction pump for handling gaseous liquids in process engineering

Small size, big energy savings

Development of Boiler Design

The pump. A pump is a device that moves fluids (liquids or gases), or sometimes slurries, by mechanical action.

Draft and Venting. Chapter 6

Prepared by Technical Team

ICONE DRAFT Proceedings of the 16th International Conference on Nuclear Engineering ICONE16 May 11-15, 2008, Orlando, Florida, USA

Energy-Efficiency Measures List

Performance analysis of ejector refrigeration system with environment friendly refrigerant driven by exhaust emission of automobile

CFD ANALYSIS OF DOUBLE PIPE PARALLEL FLOW HEAT EXCHANGER

ENERGY UTILIZATION IN CERAMIC TILES INDUSTRIES

Importance of a Draught Regulator

MECHANICAL SCIENCE Module 2 Heat Exchangers

Coarse Coal Centrifuges. VM1650 is the world s largest capacity Coarse Coal Centrifuge

PRESENTATION ON PAT TARGET & HEAT RATE IMPROVEMENT

The equipment and materials shall be designed and constructed in accordance with the ASME code section I 2001 ED A02 and Chinese Standards.

DESIGN AND MANUFACTURING OF CHEMICAL AGITATOR

FLUIDIZED BED BOILERS

Hebei Datang International Wangtan Power Company, China

PREVIEW COPY. Compressors. Table of Contents. Introduction to Compressors...3. Lesson Two Reciprocating Compressors...21

Vacuum System Troubleshooting Author: Keith Webb, P.E. Application Engineering Manager

Efficiency of Application the Condensing Heat Utilizers in the Existing Boiler's Unit in Heat Power Station

HIGH PRESSURE DOUBLE CASE PUMPS

Union County Vocational - Technical Schools Scotch Plains, New Jersey

Module 3: Liquid Fossil Fuel (Petroleum) Lecture 25: Refinery Equipments

Transcription:

PERFORMANCE EVALUATION AND RECURRING JAMMING PROBLEM ANALYSIS OF AIR PREHEATER IN COAL-FIRED POWER PLANTS M.Srinivasa Rao M.Tech Student, Department of Mechanical Engineering, GMRIT, Srikakulam, AP, India. ---------------------------------------------------------------------***--------------------------------------------------------------------- Abstract - Air preheaters make a considerable contribution to the improved overall efficiency of fossilfuel-fired power plants. It is a heat exchanger that absorbs waste heat from exit flue gas in boiler and transfers the heat to the incoming cold air. In utility boilers it is used to heat the air required for combustion purpose as well as dry and transport coal. Thermal stress deformation is an inherent disadvantage of operating rotary air-preheaters, resulting in the leakage of fluids and a decrease in the efficiency of the preheated system. Leakage can negatively impact mill performance by limiting the amount of available hot primary air. This paper focuses on the recurring jamming problem of a Regenerative type air pre heater (model TZ-NFQI-3-2.2). Based on the results a method for online monitoring of the tightness of the radial seals is proposed. seal leakage, deterioration of heat absorption characteristics of basket elements due to fouling or plugging. When the rotor rotates, air leakages may exist, e.g., entrained leakage. Air leakage consumes extra energy from the fan in the boiler system and decreases the heat exchange efficiency of the air preheater [2]. B.J. Drobnic [3] analyzed the leakage flow through different leak paths; he showed that the leak path from the cool air to the hot flue gas exerted the most significant effect on the heat transfer efficiency. A method for calculating the mass flows of gas through the seals was also introduced [4], and an adjusting method to reduce the seal clearances in radial seals was further presented [5]. Gromovyk and Ivanik [6] determined the thermal stresses and displacements that occur in an elastic hollow ceramic circular cylinder when convective heat exchange occurs. Key Words: Air pre heater, Air leakage, Gas side efficiency, Seals, X-ratio. 1. INTRODUCTION: Rotary air preheater is one of the important energy recovery systems in the steam power plant which was first introduced in 1920 by Ljungstrom [1]. The main function is to primarily preheat the combustion air for rapid and efficient combustion in the furnace serving as the last heat trap for the boiler system, a regenerative air preheater typically accounts for over 10% of a plants thermal efficiency on a typical steam generator. Considering this, when evaluating the performance of an air preheater one should take into account all of the process variables. A very good method to improve the overall efficiency of a thermal power plant is to preheat the air. If the incoming air for combustion is not preheated, then some energy must be supplied to heat the air to a temperature required to facilitate combustion. As a result, more fuel will be consumed which increases the overall cost and decreases the efficiency. There are many factors, which contribute to the deterioration of air preheater performance like high 2. MODE OF HEAT TRANSFER IN APH The process of heat transfer takes place in APH is Convection, it involves energy exchange between a bulk fluid and a surface or interface. Two kinds of Convective processes exist : (a) Forced Convection in which motion past a surface is caused by an external agency such as a pump or fan, and (b) Natural or Free convection in which density changes in the fluid resulting from the energy exchange cause a natural fluid motion to occur. The Air Preheater is a regenerative type Rotary heat exchanger uses forced convection in which flue gases and air passes through a rotating cylinder filled with heat transfer surfaces (heating elements).the flue gas heat the rotating elements, which in turn preheat the air before it is re-circulated to the boiler. In the air heater, there is a heat recovery process.as the rotor revolves, the waste heat is absorbed from the flue gas streams and fresh air is heated by the accumulated heat. 2015, IRJET ISO 9001:2008 Certified Journal Page 1257

3. WORKING PRINCIPLE OF REGENERATIVE AIR PREHEATER The Regenerative Air Preheater absorbs waste heat from flue gas and transfers this heat to the incoming cold air by means of continuously rotating Heat Transfer Elements of specially formed metal plates. Thousands of these high 3.1 Leakages in rotary heat exchangers: The basic element of a rotary heat exchanger s operation is a rotating matrix in a compact casing that transfers the heat from the hot flue gas to the cold combustion air. The rotation of the matrix requires an appropriate sealing system to prevent mixing of the flue gas and the air, commonly referred to as leakage. efficiency elements are spaced and compactly arranged within 24 sector shaped compartments of a radially divided cylindrical shell called the rotor. The housing surrounding the rotor is provided with duct connections at both the ends, and is adequately sealed by Radial & Axial Sealing members forming an Air Passage through one half of the Preheater and Gas Passage through the other. As the rotor rotates, it slowly rotates the mass of heating elements alternatively through the air and gas passages. The heat is absorbed by the element surfaces while passing through the hot gas stream, and then as the same surfaces are carried through the air stream, they release the stored up heat to the air, thus increasing the temperature of the incoming air. Fig-2: arrangement of seals around the rotor The above figure shows the schematically shows a typical arrangement of seals around the rotor of a rotary heat exchanger. The seals in Fig. 2 prevent leakage due to pressure differences between certain locations in the heat exchanger. The Radial seals are located along the edges of the radial division plates and bear against the Sector plates. The Axial seals are located axially along the outer edges of the radial division plates and bear against the axial seal plates. The Circumferential (or Bypass) seals are located in the housing around the periphery of the rotor and bear against the T bar attached to the periphery of the rotor. The Axial seal Plate to Sector plate seals is attached to the Axial seal plates and bear against the Sector plates. The Rotor post seals are attached to the ends of the Rotor Post and bear against the Sector plates. 3.2 Advantages of Seals: a. Reducing and maintaining low air preheater leakage is vital to minimize the fan horsepower required to move the air and gas flows through Fig-1: Typical tri-sector RAPH view the air preheater. b. It also serves to reduce the dilution effect and corrosion potential of the leaving gas stream due 2015, IRJET ISO 9001:2008 Certified Journal Page 1258

to mixing with colder air at the air inlet temperature. c. Seals can wear due to soot blowing, corrosion, erosion, and contact with the static sealing surfaces on start up and/or shutdown. d. Seal wear and seal settings should be checked at least once per year so that seals can be reset to proper clearances or replaced should they exhibit excessive wear. e. Sealing plate surfaces may also wear due to contact with the seals and erosion, and they may also become out of level and out of plane. 4.1 Effects of leakage : Air leakage has the largest single drawback on APH performance. Increased auxiliary power consumption, and higher-pressure differentials that can limit combustion air fan operation. Air heater leakage % can be determined using this procedure, which is defined as the weight of air passing from the airside to the gas side of the air heater. This index is an indicator of the condition of the air heater s seals. As air heater seals wear, air heater leakage increases. The increase in air heater leakage increases the station service power requirements of the forced draft and induced draft fans, increasing unit net heat rate and at times limiting unit capacity. ) *100 f. Seal plate wear should also be repaired as soon as detected, and plate alignments should be verified every 3-5 years and reset as soon as the need is detected. 4. AIR HEATER PERFORMANCE: Table -1: The rotary preheater technical characteristics AIR PREHEATER UNITS @350MW Flue gas inlet 0 C 301 4.2 Gas Side Efficiency: = 3.81% Gas side efficiency is an indicator of the internal condition of the air heater. As conditions inside the air heater worsen (baskets wear, ash pluggage, etc), the air heater gas side efficiency decreases. This is generally accompanied by an increase in exit gas temperature and a decrease in air heater air outlet temperature, resulting in an increase in unit heat rate. temperature Flue gas outlet 0 C 134 temperature Flue gas quantity t/hr 1063 Temperature of air entering air heater Temperature of air leaving air heater 0 C 46 0 C 291 = 136.74 Calorific value of coal Kcal/Kg 3300 *100 = 64.41 2015, IRJET ISO 9001:2008 Certified Journal Page 1259

Collected Data: Tgnl Gas outlet temperature corrected for no leakage. Tae Temperature of air entering air heater = 46 o c Tge Temperature of gas entering air heater = 301 0 c Tgl Temperature of gas leaving air heater = 134 0 c 5. RECURRING JAMMING PROBLEM IN APH 4.3 X-Ratio: X-Ratio depends on the moisture in coal, air infiltration, air & gas mass flow rates, leakage from the setting and specific heats of air & flue gas. X-ratio does not provide a measure of thermal performance of the air heater, but is a measure of the operating conditions. *100 Failure analysis: During unit is running at elevated loads the =96.07 heating elements called modules will gain high amount of heat and causes thermal expansion whereas casing at flue gas side and air side will differentially elongate because of =0.668 Collected Data: Tae Temperature of air entering air heater = 46 0c Tal Temperature of air leaving air heater = 291 0c Tge Temperature of gas entering air heater = 301 0c 4.4 Energy saved by APH in a 350 mw Boiler: Heat energy by flue gas Q f= M f*c f *(T2-T1) f = (1063x103) x 0.28 (301-134) Kcal/hr 48.93 x 106 Kcal/hr [let us assume Q f= Q c for calculating the coal consumption] Heat energy by burning coal Q c = Mass of coal used * calorific value = 48.93 x 106 Kcal/hr= (Mc) x 3300 Kcal/hr Therefore Mc 14.524 T/hr So by using APH in boiler approx. 15T/hr coal is saving. temperature difference. Thus the clearance maintaining between the casing and module outer diameter is high at flue gas flow path comparatively air flow path. At this juncture there may be problem of jamming at air side. Due to this current dragging by the Electric motor is comparatively high from normal operation. Abnormal sounds coming from the APH. Remedial measures to avoid recurrence of the problem: Adjust the Axial seal at the air flow section so the clearance can be increased to the desire level and also adjust the radial seals to accommodate the thermal expansion taken place in the rotor as the allowable expansion of APH rotor is given in vertical direction. If rotor comes into stand still condition go for manual turning and try for taking air motor into service. 2015, IRJET ISO 9001:2008 Certified Journal Page 1260

6. OPERATION AND MAINTENANCE a) Check whether the bearing lubricating oil pressure is between 0.33 and 1.6 MPa, the oil level is normal and there is no leak in system. Adjust the water outlet valve of air cooler to make the oil temperature between 30 ~40 and the differential pressure of oil filter is lower than 1.3 MPa. b) Check and make sure that there is no abnormal sound in the air pre-heater and gear device. c) Change oil of guide bearing oil system at least once a year. d) The reducer box cannot leak in the operation. In continuous working, the working oil temperature shouldn't be higher than 80. Make working oil test after it is running for 3000 hours and change oil when necessary Leakage in the preheater can be checked during operation by analyzing flue gas for CO, drop across the air preheater. e) Make frequent inspection and analysis on the oxygen quantity, flue gas and air temperature, air differential pressure and flue gas temperature difference at inlet and outlet of air pre-heater to determine the leak or dust block of air pre-heater and judge whether re-combustion occurs. Make inspection on air pre-heater if the temperature of any point rises by 10 abnormally. expansion taken place in the rotor as the allowable expansion of APH rotor is given in vertical direction. This reduces the air leakage and max efficiency can be obtained. REFERENCES: [1] T. Museet, The Ljungstrom Air Preheater 192, ASME History, 1995. [2] T.J. Lambertson, Performance factors of a periodic-flow heat exchanger, Transactions of the ASME 80 (1958) p586-592. [3] B.J. Drobnic, A numerical model for the analyses of heat transfer and leakage in a rotary air preheater, International Journal of Heat and Mass Transfer 49 (2006) 5001-5009. [4] T. Skiepko, Method of monitoring and measurement of seal clearances in a rotary heat exchanger, Heat Recovery System 8 (1998) 469 473. [5] T. Skiepko, Some essential principles for adjustment of seal clearances in rotary regenerators, Heat Transfer Engineering 14 (1993) 27 43. [6] V.I. Gromovyk, Y.G. Ivanik, The thermal-stress state of heat-sensitive ceramic tubular systems in the case of convective heat exchange, Journal of Applied Mathematics and Mechanics 59 (1995) 159 163. ACKNOWLEDGEMENT The authors would like to thank GMR KAMALANGA ENERGY LIMITED, DHENKANAL (dist), ODISHA, INDIA for the technical support of this work. BIOGRAPHIES Mr. M. Srinivasarao received his B.Tech degree from GMR institute of Technology in 2011 and M.Tech from GMR institute of Technology in 2015. 7. CONCLUSION Due to the differential thermal expansions between the casings and the heating elements, the clearances maintaining between the casing and module outer diameter is vary at different sections of APH. At this juncture there may be problem of jamming at air side. Adjust the Axial seal at the air flow section so the clearance can be increased to the desire level and also adjust the radial seals to accommodate the thermal 2015, IRJET ISO 9001:2008 Certified Journal Page 1261