Ventilation and Leak Dispersion in CCGT Enclosures Patrick Phelps ( Flowsolve ) and Douglas Wylie (GEC Energy Services) IPUC 7 - Luxembourg - May 2000.

Slides:



Advertisements
Similar presentations
Air Flow Analysis in Pharmaceutical “Clean Rooms”
Advertisements

CFD Modelling of Gas Freeing of VLCCs K. Chow University of Hertfordshire Fluid Mechanics Research Group 2006 European PHOENICS User Meeting.
Phoenics User Conference on CFD May 2004 Vipac Engineers & Scientists Ltd COMPUTATIONAL FLUID DYNAMICS Simulation of Turbulent Flows and Pollutant Dispersion.
1 According to PETROSAFE safety policy, the company is keen that: Introduction All Egyptian Petroleum companies and foreign companies working in A.R.E.
OFF DESIGN PERFORMANCE PREDICTION OF STEAM TURBINES
The Care and Feeding of Silane Art Garcia FM Global March 23, 2006.
Fired And Unfired Pressure Vessels
ROGER SANTON, HEALTH & SAFETY LABORATORY, BUXTON
Open-Path Gas Detection - Philosophy of Use or The Story of Clouds.
1 Application of for Predicting Indoor Airflow and Thermal Comfort.
Energy Saving in Hospitals: Hong Kong Initiatives
1 | WEATHERIZATION ASSISTANCE PROGRAM STANDARDIZED CURRICULUM – July 2012eere.energy.gov Building Science Basics WEATHERIZATION INSTALLER/TECHNICAN FUNDAMENTALS.
Improving and Trouble Shooting Cleanroom HVAC System Designs By George Ting-Kwo Lei, Ph.D. Fluid Dynamics Solutions, Inc. Clackamas, Oregon.
University of Western Ontario
Cogeneration. Is the simultaneous production of electrical and thermal energy from a single fuel source.
1 Validation of CFD Calculations Against Impinging Jet Experiments Prankul Middha and Olav R. Hansen, GexCon, Norway Joachim Grune, ProScience, Karlsruhe,
Power Plant Construction and QA/QC Section 2.4– Boiler Auxiliaries
Buildings and Structures 2 Natural and Mechanical Ventilation.
Study of potential leakage on several stressed fittings for hydrogen pressures up to 700 bar D Houssin-Agbomson 1, D Jamois 2, Ch Proust 2, J Daubech 2,
1 EERMC Public Meeting on Combined Heat and Power September 17, 2013.
“Energy Efficiency Guide for Industry in Asia”
Combined Heat and Power and Air Quality - Guidance for Local Authorities Ed Dearnley Policy Officer.
Defining Hazardous Zones – Electrical Classification Distances Gary Howard,Andrei Tchouvelev, Vlad Agranat and Zhong Cheng Defining Hazardous Zones – Electrical.
Toxic Release and Dispersion Models
Evaluation of Safety Distances Related to Unconfined Hydrogen Explosions Sergey Dorofeev FM Global 1 st ICHS, Pisa, Italy, September 8-10, 2005.
POWER GENERATION TECHNOLOGIES
Combined_Cycle_Power_Plant Prepared by: Nimesh Gajjar.
Exergy Analysis of STHE P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Formalization of Thermo-economics…..
Gas Turbine Power Plant
Patrick Thornton, SNS/FPE June 9, 2008
Operation and Maintenance
Vapor and Combined Power Cycles (2)
Pro-Science 4 th International Conference of Hydrogen Safety, September 12-14, 2011, SAN FRANCISCO, USA EXPERIMENTAL STUDY OF IGNITED UNSTEADY HYDROGEN.
Plant Utility System (TKK-2210) 14/15 Semester 4 Instructor: Rama Oktavian Office Hr.: M-F
Activity A5-CI due by 4 pm Friday 02/29 Chapter 4 Mallard HW quiz – new due date: end of the day next Monday 03/03 Chapter 4 quiz in class next Tuesday.
Page 1 SIMULATIONS OF HYDROGEN RELEASES FROM STORAGE TANKS: DISPERSION AND CONSEQUENCES OF IGNITION By Benjamin Angers 1, Ahmed Hourri 1 and Pierre Bénard.
Explosion An explosion is a rapid expansion of gases resulting in a rapid moving pressure or shock wave. The expansion can be mechanical or it can be.
2nd International Hydrogen Conference on Hydrogen Safety. San Sebastián, Spain – Sept Hydrogen Safety. New Challenges based on BMW Hydrogen.
Unit 2 -Gas And Diesel Power Plants
Air Movement and Natural Ventilation
IAEA Meeting on INPRO Collaborative Project “Performance Assessment of Passive Gaseous Provisions (PGAP)” December, 2011, Vienna A.K. Nayak, PhD.
Objective of the investigation: Determine the number and arrangement of jet fans to be installed in the Acapulco Tunnel that will ensure an air quality.
Wu. Y., International Conference on Hydrogen Safety, September Initial Assessment of the Impact of Jet Flame Hazard From Hydrogen Cars In.
International Conference on Hydrogen Safety 2011 – San Francisco, 12 Sept 2011 Risk informed separation distances for hydrogen refuelling stations Frederic.
SUBJECT CODE NAME OF SUBJECT TOPIC :::::: FLUID POWER ENGINEERING CENTRIFUGAL PUMP Parul Institute of Engineering & Technology.
Heat pumps Effectiveness measured by the Coefficient of Performance C.O.P. = T h /(T h -T c ) This comes from the Carnot Efficiency As the outside air.
Jet With No Cross Flow RANS Simulations of Unstart Due to Mass Injection J. Fike, K. Duraisamy, J. Alonso Acknowledgments This work was supported by the.
Experimental and numerical studies on the bonfire test of high- pressure hydrogen storage vessels Prof. Jinyang Zheng Institute of Process Equipment, Zhejiang.
Acetylene Storage in Enclosed Vehicle Compartments Thomas Kamm, P.Eng. Safety Engineering Specialist.
Heat Pumps In a heat engine, heat is converted to mechanical energy by taking advantage of the fact that heat flows from hot to cold. The heat is taken.
ENERGY CONVERSION MME 9617A Eric Savory Lecture 10 – Analyzing a complete plant: Energy conversion cycles Department.
Heat Pumps In a heat engine, heat is converted to mechanical energy by taking advantage of the fact that heat flows from hot to cold. The heat is taken.
THERMAL POWER PLANT. INTRODUCTION : THERMAL POWER PLANTS CONVERT THE HEAT ENERGY OF COAL INTO ELECTRICAL ENERGY. COAL IS BURNT IN A BOILER WHICH CONVERTS.
Prepared by : Nishant .A. Raval
I ntroduction.. 1 Energy Conversion  Energy Conversion  Energy Conversion is when energy changes into another form. In physics, the term energy describes.
WORK Work = Force x Distance POWER power = work done ÷ time taken ENERGY 1-POTENTIAL ENERGY (Potential Energy = Force x Distance ) 2-KINETIC ENERGY Energy.
Gas Turbine Power Plant
S.G. Giannissi1,2, I.C.Tolias1,2, A.G. Venetsanos1
ICHS 2015 – Yokohama, Japan | ID195
HOMOGENEOUS HYDROGEN DEFLAGRATIONS IN SMALL SCALE ENCLOSURE
M. Tabarra, R.D. Matthews, B. Kenrick South Bank University, London
Content Development of the second generation Power2 Case studies
Risk Reduction Potential of Accident Mitigation Features
Sandia National Laboratories
Risk informed separation distances for hydrogen refuelling stations
Risk informed separation distances for hydrogen refuelling stations
Rajan Bhandari Senior Lecturer
Smokes extraction principle
Combined Cycle Power Plants
Rui Wang, Gequn Shu, Hua Tian, Xuan Wang*
Presentation transcript:

Ventilation and Leak Dispersion in CCGT Enclosures Patrick Phelps ( Flowsolve ) and Douglas Wylie (GEC Energy Services) IPUC 7 - Luxembourg - May 2000

Ventilation and Leak Dispersion in CCGT Enclosures b Industrial Context b Health and Safety Issues b Application to an Existing Power Station b Application to New Enclosure Designs b Conclusions b Experimental Verification

Industrial Context - 1 Combined Cycle Gas Turbine (CCGT) Plants b Gas turbines drive an electricity generator b Engine exhaust waste heat recovered by a boiler to produce steam. b Steam turbine generates further output.

Industrial Context - 2 b Turbines are fuelled by gas at very high pressures b Liquid fuel system as back-up b Turbines are contained within acoustic enclosures. b Enclosures tend to be installation- specific designs

Frame 6 Turbine Generator Frame 6 Turbine Generator

Industrial Context - 3 Each enclosure is divided into a number of compartments containing b Auxiliary equipment b Gas turbine and exhaust plenum b Reduction gearing and the generation equipment. Auxiliary/GT/exhaust compartment is usually self- contained, with a dedicated ventilation system

Ventilation and Leak Dispersion in CCGT Enclosures

Health and Safety Issues - 1 b Enclosure ventilation system removes some heat from the turbine casing b Enables operatives to carry out readings and routine maintenance under operating conditions. b However, enclosures remain a thermally hostile and noisome environment.

Health and Safety Issues - 2 b Gas from leakages can accumulate to flammable proportions in poorly ventilated regions of the enclosures - dead zones b OUTCOME - Big Bang b REMEDY - Use the ventilating air to safely dilute and disperse any gas leakage. b MOTIVATION - Legislation

UK Safety Assessment of CCGT Enclosures - 1 Identify nature and potential sources of hazardous material releases Identify nature and potential sources of hazardous material releases Determine leak frequency and inventory of releases Determine leak frequency and inventory of releases Investigate airflow characteristics Investigate airflow characteristics identify "dead zones" identify "dead zones" Predict dispersion consequences safety-critical release scenarios Predict dispersion consequences safety-critical release scenarios Implement remedial measures Implement remedial measures

UK Safety Assessment of CCGT Enclosures - 2 b Experimental investigation of airflow characteristics is difficult within the confines of a turbine generator enclosure, especially under operational conditions. b HSE promote computer simulation as the most appropriate technology in this case.

UK Safety Assessment of CCGT Enclosures - 3 CFD models can b simulate the dispersion consequences of releases under a variety of operating conditions b compare the efficiency of alternative ventilation strategies, to achieve the desired dilution / dispersion result

Safe Dispersion Criteria - 1 Santon Criterion The ventilation arrangements within the turbine enclosure must be such as to ensure the safe dilution/dispersion of gas releases prior to activation of mitigation/shutdown systems by the gas detection system. The criteria to be applied are that the envelope of the 50% LEL concentration contour should not occupy more than 0.1% of the free volume of the enclosure, for a gas leak of sufficient magnitude to trigger the gas detection system.

Safe Dispersion Criteria - 2 G = V * (0.01 * E) * (0.01 * S). b Gas concentration level (S) detected by sensors for activating emergency response systems (typically 10%) b Lower Explosive Limit (E) for the turbine fuel gas is around 5%. b Maximum undetected leak is thus of magnitude 10% of LEL For compliance, ensuing flammable envelope (of the 50% LEL surface) must not exceed 0.1% of the compartment free volume. For compliance, ensuing flammable envelope (of the 50% LEL surface) must not exceed 0.1% of the compartment free volume.

Safe Dispersion Criteria - 3 Compartment free volume

Reference Leak Scenario Zero momentum leak source b corresponds to jet release impinging immediately on an obstruction (casing, flange body} b No net directionality imparted to release. b A directional release would require additional assumptions….. b A directional release would require additional assumptions …..

Application to an Existing Power Station - 1 A CFD-based simulation study commissioned by IVO Generation Systems and Regional Power Generators Ltd

Application to an Existing Power Station - 2

Application to an Existing Power Station - 3 Over 100 simulations performed Studies to determine b air flow distribution b worst case operating condition (hot,cold); b worst case leak location; b efficiency of alternative retrofit ventilation strategies, to achieve HSE compliance

Air flow Distribution at inlet to Turbine Compartment

Application to an Existing Power Station

Application to an Existing Power Station - Parameter Studies Over 100 simulations performed Studies to determine b air flow distribution b worst case operating condition (hot,cold); b worst case leak location; b efficiency of alternative retrofit ventilation strategies, to achieve HSE compliance

Hot Operating Conditions: Envelope volume %

Cold Operating Conditions: Envelope volume %

Application to an Existing Power Station - Parameter Studies Over 100 simulations performed Studies to determine b air flow distribution b worst case operating condition (hot,cold); b worst case leak location; b efficiency of alternative retrofit ventilation strategies, to achieve HSE compliance

Worst Case Leak Location b Under both hot and cold conditions, the worst case leak location was found to be in the pit region, in front of the lowest combustor flanges

Application to an Existing Power Station - Parameter Studies Over 100 simulations performed Studies to determine b air flow distribution b worst case operating condition (hot,cold); b worst case leak location; b efficiency of alternative retrofit ventilation strategies, to achieve HSE compliance

Alternative Ventilation Strategies : 1 - Abject failures b Increasing ventilation rate b overhead pendant baffles b twin outlets b blowing air into the pit region b sucking air from the pit region b EGT wavewall idea

Alternative Ventilation Strategies : 2 - Heroic failures b Reversed flow system air supply through existing outletair supply through existing outlet air extract to TG inlet plenumair extract to TG inlet plenum b Lateral side-gust system air supply through side doorair supply through side door air extract through existing outletair extract through existing outlet other inlets blocked offother inlets blocked off

Alternative Ventilation Strategies : 3 - Final Success ! The Corkscrew Strategy b Close all existing inlets b plate over grated walkway tops b Single non-symmetric outlet b Two inlet slots, one high, one low, cut in connecting doors b 30-degree deflector plates create corkscrew effect

Corkscrew Ventilation Scheme

And so This led on to

Application to New Enclosure Designs A CFD-based simulation study commissioned by the Thermal Power Division of Kvaerner Energy Ltd

Application to New Enclosure Designs

Enclosure Geometry - Elevation

Enclosure Geometry - End View

Application to New Enclosure Designs

Turbine combustor flanges and associated pipework

Geometry Representation - 1

Geometry Representation - 2

Application to New Enclosure Designs - Workscope Over 25 different simulations performed Studies to determine sensitivity to: b nodalisation level & distribution; b leak location; b ventilating flowrate; b presence of internal geometric features; b inlet flow manipulation.

Findings - 1 b The worst case leakage scenario, under cold start-up conditions, was a zero-momentum leakage from the flanges in front of the lowest can combustor b The flammable gas cloud with the reference ventilation arrangement was twenty five times larger than the target value (11 times larger if the accessory compartment volume was included)

Reference Configuration {Flammable volume: 2.8% TC}

Application to New Enclosure Designs - Workscope Over 25 different simulations performed Studies to determine sensitivity to: b nodalisation level & distribution; b leak location; b ventilating flowrate; b presence of internal geometric features; b inlet flow manipulation.

Findings - 2 b Increasing the ventilating air flow by 25% had little effect on ventilation efficiency ( gas leak size increased proportionately ).

Application to New Enclosure Designs - Workscope Over 25 different simulations performed Studies to determine sensitivity to: b nodalisation level & distribution; b leak location; b ventilating flowrate; b presence of internal geometric features; b inlet flow manipulation.

Atomising Air System {Flammable volume: 1.9% TC}

Application to New Enclosure Designs - Workscope Over 25 different simulations performed Studies to determine sensitivity to: b nodalisation level & distribution; b leak location; b ventilating flowrate; b presence of internal geometric features; b inlet flow manipulation.

Findings - 3 : Inlet Flow Manipulation Improved results (decrease in flammable cloud size) obtained by : b adding a scoop diverter at inlet ; b throttling - increasing the inlet velocity ; b concentrating the incoming flow towards the axial centreline; b blocking off the outermost inlet hole(s) on each side; and b biasing the massflow distribution.

Final Configuration {Flammable Volume: 0.2% TC}

Conclusions b Flammable cloud volumes of less than 0.1% of the free volume of the combined compartments are attainable (at least conceptually). b This would satisfy the current UK dispersion criterion. b Compliance achieved without major structural changes to enclosure or to air delivery system.

Future Efforts b Confirm high velocities do not provoke thermal shock problems in hot operation b Confirm required manipulation of inlet air supply is technically feasible (!) b Use model to predict likely over-pressures arising from deflagration of the confined gas plume.

Experimental Verification b No quantitative data available. b Qualitative comparison - video footage of smoke tests on installations with similar internal geometries. b Smoke trails confirm magnitude and direction of airflow in the region in front of the can flanges and around the front upper part of the turbine barrel

Ventilation and Leak Dispersion in CCGT Enclosures Thank you for your attention. When I count to three, When I count to three, you will awake and remember nothing …..

Ventilation and Leak Dispersion in CCGT Enclosures Patrick Phelps (Flowsolve Ltd) and Douglas Wylie (GEC Energy Services) IPUC 7 - Luxembourg - May 2000