POWERENERGY

Similar documents
CONSIDERATIONS IN CONVERTING A DUAL SHELL OR A DUAL PRESSURE COAL FIRED PLANT CONDENSER INTO A COMBINED CYCLE PLANT CONDENSER

POWERENERGY

Innovate & Implement

Steam Power Cycles Part II

PV Newsletter Monthly Publication from CoDesign Engineering Skills Academy

9707 Key West Avenue, Suite 100 Rockville, MD Phone: Fax:

Boiler Basics. Design and operation

POWER Selecting Shell Side Design Temperature for Feedwater Heaters

Chapter 10 VAPOR AND COMBINED POWER CYCLES

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

2017 FSRUG Thermal Performance Feedwater Heater Troubleshooting FSRUG FWH Troubleshooting 1

CHAPTER 3 BASIC STEAM CYCLE

Raising the Efficiency of Gas-Fired Power Plants and CCPP. GEA Heat Exchangers

Yarway Narvik Steam Desuperheater Series 4300 TempLow

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

Attention is drawn to the following places, which may be of interest for search:

TEPZZ 87_ 6A_T EP A1 (19) (11) EP A1 (12) EUROPEAN PATENT APPLICATION

MECHANICAL SCIENCE Module 2 Heat Exchangers

HEAT GENERATION 1.01 RELATED CORNELL DESIGN AND CONSTRUCTION STANDARDS. B. Section HVAC Basic Materials and Methods

Foster Wheeler Condensers and Feedwater Heaters. High Quality Steam Components

YARWAY NON-REPAIRABLE DRIP AND TRACER STEAM TRAPS SERIES PB, 29, 129Y AND 29S

Economical and simplified solutions that offer quality and optimum steam trap service.

Open System Condensate receiver tank of cylindrical. design type SDR A with highpressure

Your Concentrated Solar Power Generation Partner

Week 13 Chapter 10 Vapor & Combined Power Cycles

Watts Bar Unit 1 A2 Feedwater Heater Partition Plate Weld Failure

Power Boiler Design, Inspection, and Repair

United States Patent (19) Hoizumi et al.

Steam Generator (Boiler) & Steam Turbine. Steam Generator (Boiler) ME 268. Model Lab

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

Boiler Condensate Return Basics. Presented by Steve Connor February 24, 2016

Beneficial Use of Landfill Gas for Leachate Evaporation and Power Generation

SPRAY COOLING BOF HOODS by David A. Lehr, Senior Engineer UCAR Carbon Company Inc., Parma, OH

Silhouette. Feedwater Heater. Boiler Feedwater

What to Expect from Your EtaPRO Investment

GPPS-2017-Put 4 digit paper number here

BORSIG WASTE HEAT BOILERS FOR NITRIC ACID, CAPROLACTAM AND FORMALDEHYDE PLANTS PROCESS HEAT EXCHANGER. A Member of KNM Group Berhad

Insty-Pac Steam Humidifiers

By: Prof K. M. Joshi,

HEAT EXCHANGE INSTITUTE, INC.

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

Custom Design TYPE CS

Thermodynamics: Homework A Set 7 Jennifer West (2004)

Solution of I Mid Term Steam Engineering 6ME5A

CHAPTER 6. HEATING PRODUCTION EQUIPMENT AND SYSTEMS

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

Products Solutions Services. Energy Solutions. Food & Beverage industry. Slide 2

So far 2010 is proving to be

2 Newsletter 1/2014. Bosch Industriekessel GmbH Illustrations are only examples Subject to change without notice 1/2014 TT/SLI_de/en_Newsletter_1/14

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

Element D Services Heating, Ventilating, and Air Conditioning

CONDENSER TUBE COMPARISON WINYAH 2. Leif Svensen P.E. Santee Cooper One Riverwood Drive Moncks Corner, SC 29461

A Review on Analysis of Vapour Compression Refrigeration System Using Matrix Heat Exchanger

A Newsletter published by ESI. The Steam and Power SPECIAL FORCES

PT15 MATERIAL : DIMENSIONS - Nominal in inches. AVAILABLE SPARES: Disc (Packet of 5) ORDERING INFORMATION: Refer to "HOW TO ORDER" page.

100 years of boiler technology leadership.

HEAT TRANSPORT SHUTDOWN COOLING

ASH MEASUREMENT AT NRG HUNTLEY USING HIGH TEMPERATURE STRAIN GAUGES

Speransa 2008: Round table: Nuclear and sustainable development Universitad Politecnica de Valencia \UPV - Passive safety systems -

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

Chapter 11. Design of Other BOP

FEEDWATER TANK WITH DEAERATOR DATASHEET. Capacity 1000 to lt Operating Pressure 0,5 bar

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

Healthy Buildings 2017 Europe July 2-5, 2017, Lublin, Poland. Mold Infestation in Buildings of Warm Humid Climate Case Studies

Figure 1. Ejector cross-sectional drawing. Figure 2. Precondenser to left of vacuum flasher. pressure.

Complete solution for your applications and requirements

LIFE MANAGEMENT OF FEEDWATER HEATERS AT KCPL

OPERATING AND MAINTENANCE MANUAL FOR VERTICAL IMMERSION HEATED STEAM BOILERS. Technical Control Systems Limited MODELS "VIHS"

/ / Take the technological step into MODERN Condensate Handling Equipment for steam systems MANUFACTURED IN AMERICA with craftsmanship and quality.

Moss MOSS TRAY DEAERATOR ECONOMICAL INDUSTRIAL DEAERATOR SYSTEMS

ON VERY RARE OCCASIONS, AN EVOLUTION TAKES PLACE THAT MAKES EVERYONE STOP AND NOTICE.

Miniature Hobby Boiler Inspection and Certification Requirements

Steam Contamination - Causes & Cures

Solution builder. in energy management.

BuildingName The Description of the Project P DOCUMENTS

Complete solution for your applications and requirements

Feed Water Heaters Performance Indicators and Characteristics on the 405MW Coal-Thermal Power Plant

Condensate Recovery and Return System SDR A

Why steam trap survey?

Deaerator. Specifications

Steam Ancillary Equipment. Primary Steam System, Water Treatment and Auxiliary Steam System Equipment

OPERATING AND MAINTENANCE MANUAL FOR PLATE HEAT EXCHANGER INDIRECT FIRED WATER HEATER. Electric Heater Company Base Model "BWXP"

Off Design Operation of Hybrid Noncondensable Gas Removal Systems for Flash Steam Cycle Geothermal Power Plants

Efficient Steam System Design

WKS 2200 SERIES (USA only) --INSTALLATION INSTRUCTIONS--

Unfired Steam Generators (Series RB) Installation, Operation and Maintenance

APPLICATION NOTE. Applying pressure sensing in arc flash protection applications with air magnetic circuit breakers

TYPE.005 DA-STP TYPE.005 DA-STP-2T. Spray Tray Deaerating Pressurized Boiler Feed Pumps. and. when separate surge tank is utilized

Steam and Power Conversion System

Effects of Ultra-High Turndown in Hydronic Boilers By Sean Lobdell and Brian Huibregtse January 2014

Case 15 Refrigeration System for Chemical Fertilizer Plant Ammonia Storage

tech-info Sugar drying and cooling plants BMA plants are employed at beet and cane sugar factories and sugar refineries worldwide

WHU WATER HEATING UNITS. GENERAL MANUAL MODEL KEY. June 2007 WHU WATER HEATING UNITS


Annex A-8 CONCENTRATED SOLAR POWER UNITS INDEX TO SYSTEM/COMPONENT CAUSE CODES

Secondary Systems: Condensate/Feedwater Cycle

FIFTH CLASS POWER ENGINEER S

PUMPS & PUMPING SYSTEMS FOR THE CHEMICAL PROCESSING & HEATING & AIR CONDITIONING INDUSTRY

INFINITY FLUIDS CORPORATION

SULPHUR RECOVERY UNIT

Transcription:

Proceedings of the ASME 2015 Power & Energy Conversion Conference POWER2015 June 28-July 2, 2015, San Diego, CA, USA POWERENERGY2015-49418 IMPROVEMENTS IN THE PERFORMANCE OF A SUBCOOLING ZONE IN A FEEDWATER HEATER WITH DUAL END PLATE DESIGN WITH WATER SEAL IN BETWEEN Ranga Nadig, Ph.D. Maarky Thermal Systems Inc. 1415, Route 70 East, Suite 604, Cherry Hill, NJ, 08034, USA ABSTRACT In a horizontal feedwater heater with a partial length subcooling zone the end plate located at the entrance to the subcooling zone is the only non-welded barrier that prevents the condensing zone steam from entering the subcooling zone. The end plate is usually two or three inches thick and the tube holes in the end plate are drilled to tolerances similar to that of the tubesheet. As the steam from condensing zone tries to enter the subcooling zone it condenses in the tight spaces between the active tube and the tube hole in the end plate forming a liquid barrier that prevents further ingress of steam into the subcooling zone. With usage and wear the gap between the active tube and the tube hole in the end plate increases thereby weakening the liquid barrier. The liquid barrier is completely lost when the tubes are plugged. Steam from condensing zone enters the subcooling zone and disrupts the performance of the subcooling zone, the performance of the feedwater heater and the efficiency of the power plant. This problem is faced by all horizontal feedwater heaters with subcooling zones that are in operation in power plants worldwide.. This loss of performance can be eliminated by employing the patent pending Maarky concept of dual end plate subcooling zone with a water seal. The dual end plate subcooling zone with water seal concept comprises of two end plates separated by a short distance. The gap between the two end plates is filled with condensate thereby forming a triple barrier to ingress of condensing zone steam into the subcooling zone. The performance of the subcooling zone and the longevity of the heater are preserved, This paper discusses the design of subcooling zone in present day feedwater heaters, degradation of performance of subcooling zone and the improvements brought about by the patent pending Maarky concept of dual end plate subcooling zone with water seal. INTRODUCTION In a steam power plant feedwater heaters are used to gradually increase the temperature of the feedwater in stages up to the boiler operating conditions. Preheating the feedwater improves the thermodynamic efficiency of the cycle, reduces the plant operating costs and minimizes thermal shock to the boiler metal. A steam power plant may be equipped with a number of feedwater heaters. The energy used to heat the feedwater is usually derived from steam extracted from the steam turbine. Feedwater heaters can be open or closed heat exchangers. In an open feedwater heater such as deaerator the extraction steam is directly allowed to mix with the feedwater heater thereby heating it. A closed feedwater heater, topic of present discussion, is a shell and tube heat exchanger wherein the feedwater passes through the tubes and is heated by turbine extraction flowing on the outside of the tubes. 1

In a steam power plant the feedwater heaters located upstream of the boiler feed pump are termed as high pressure feedwater heaters and those located downstream of the boiler feed pump are referred to as low pressure feedwater heaters. In high pressure heaters the turbine extraction steam has a sizeable amount of superheat. Feedwater in high pressure feedwater heaters is typically heated in three stages in three separate compartments: a desuperheating zone, a condensing zone and a subcooling zone. Initial heating of the feedwater is carried out in the subcooling zone by subcooling the condensed turbine extraction steam. The feedwater is then further heated in the condensing zone by the condensing turbine extraction steam. The final heating of the feedwater occurs in the desuperheating zone by the superheat in the turbine extraction steam. In low pressure heaters the turbine extraction steam has minimal amount of superheat or no superheat. Therefore feedwater in low pressure feedwater heaters is typically heated in one or two stages in one or two separate compartments: a condensing zone only or a combination of condensing and subcooling zone. In a two zone low pressure feedwater heater the initial heating of the feedwater heater is carried out in the subcooling zone by subcooling the condensed turbine extraction steam. The second and final heating of the feedwater heater occurs in the condensing zone from the condensing turbine extraction steam. PROBLEMS WITH SUBCOOLING ZONE IN EXISTING FEEDWATER HEATERS In low as well as high pressure feedwater heaters the subcooling zone is surrounded by turbine extraction steam. Leakage of extraction steam into the subcooling zone leads to condensate reheating, flashing and subsequent degradation in heater performance. In the present day heater design the extraction steam is prevented from entering the subcooling zone by (a) proper welding of the subcooling zone components (b) of the maintaining the water level above the entrance to the subcooling zone and (c) employing an end plate to separate the subcooling zone from the condensing zone. The end plate is usually 2-3 thick and the tube holes in the end plate are drilled to a tolerance similar to that of the tubesheet. When the extraction steam enters the tight spaces between the active tube outer diameter and the end plate tube hole it condenses and forms water seal that prevents further ingress of steam into the subcooling zone. Improper tube hole drilling tolerances, inactive tube because of tube plugging, extended usage or a combination thereof leads to widening of the gap between the outer diameter of the tube and the tube hole in the end plate. In such a scenario, extraction steam enters the subcooling zone and heats the condensate thereby compromising the performance of the subcooling zone and the entire heater. With each passing year the problem escalates with substantial decrease in the heater efficiency. When the degradation in performance is unsustainable the heater is replaced. Steam ingress into subcooling zone through the end plate holes is a major problem affecting the performance and reliability of present day feedwater heaters operating in power plants worldwide. REMEDY FOR THE PROBLEMS AFFLICTING SUBCOOLING ZONE The ingress of steam into the subcooling zone can be eliminated by using two end plates with a water seal in between. The dual end plate with water seal eliminate the problems associated with leakage of condensing zone steam into the subcooling zone. If required multiple end plates can be used. The patent pending Maarky innovation includes the following design features: Employ two end plates instead of one. Close the gap between the end plates at the bottom and side so as to create a water compartment. Leave the top open so that condensate can enter the water compartment. Install a small drain hole in the bottom of the compartment so as to prevent water stagnation and facilitate marginal flow of condensate. The dual end plate with a water seal offers the following advantages: There is a triple layer of separation between the condensing and the subcooling zone. The present day technology offers a single layer of separation. Condensate collected in the enclosure between the end plates will fill the space between the tube outer diameter and the end plate tube hole on the inner and outer end plate. As the condensate in the annular space is close to the shellside saturation temperature condensing zone steam cannot condense on the condensate. The absence of a heat sink voids the incentive for the condensing zone steam to enter the annular space. The outer end plate constitutes the first barrier, the condensate in the annular space forms the second barrier and the inner end plate forms the third barrier. Widening of the gap between the tube outer diameter and the tube hole in the outer end plate and subsequent ingress of steam into the gap between the end plate will not impact the performance of the subcooling zone. 2

The dual end plate with an in-between water seal offers a triple seal that prevents leakage of steam into the subcooling zone. The performance of subcooling zone is secured and the life of the feedwater heater is prolonged. CONCLUSION Degradation in the performance of the subcooling zone is impacting the longevity of the horizontal feedwater heaters and efficiency of power plants worldwide. The loss of performance and subsequent failure of subcooling zone is attributed to ingress of condensing zone steam into the subcooling zone due to widening of the annular space between the active tube and the tube hole in the end plate due to wear and tear during normal usage and in the event the tubes are plugged. The patent pending Maarky concept of dual end plate design with water seal in between provides a triple barrier against the ingress of condensing zone steam into the subcooling zone. Steam leakage into the subcooling zone is eliminated. The performance of the subcooling zone, the reliability and the longevity of the feedwater heater and the efficiency of the power plant is preserved. REFERENCES [1] Heat Exchange Institute Standards for Feedwater Heaters, 9 th Edition. 3

4

5

6

7