Chemical kinetics study of combustion characteristics of ammonia-air mixtures under high pressure lean conditions

Similar documents
Ammonia Based Fuels For Environmentally Friendly Power Generation

Simulation of Low-Btu Syngas Combustion in Trapped Vortex Combustor

Changes in combustion properties of Natural gas when mixed with Hydrogen

EFEECT OF HYDROGEN ADDITION ON METHANE COMBUSTION IN A CAN TYPE COMBUSTOR

The International Gas Research Conference IGRC-2014 September 17-19, 2014, Copenhagen, Denmark

Experimental Results of Laminar Burning Velocities of Adiabatic Syngas/H 2 -Rich Fuel Flames Second Set

DESIGN AND SIMULATION OF A TRAPPED-VORTEX COMBUSTION CHAMBER FOR GAS TURBINE FED BY SYNGAS

CHAPTER 1 FUNDAMENTAL OF COMBUSTION

Measurement of key values in combustion: The heat flux burner method to determine laminar burning velocities

ADVANCED STEAM GENERATORS

Numerical Modeling of Biomass and Solid Waste-Based Syngas Fuels Combustion

STUDY OF HYDROGEN ENRICHED PREMIXED FLAMES

An Improved Reaction Mechanism for Combustion of Core (C 0 -C 4 ) Fuels

DESCRIPTIONS OF HYDROGEN-OXYGEN CHEMICAL KINETICS FOR CHEMICAL PROPULSION

Dry Low-NOx Combustion Technology for Novel Clean Coal Power Generation Aiming at the Realization of a Low Carbon Society

CO 2 and NO x Emissions Reduction in Combustion Systems

Reforming landfill gas to syngas

Development of Micro Combustion Systems: Insights through Computations and Experiments

CEE 452/652. Week 14, Lecture 1 NOx control. Dr. Dave DuBois Division of Atmospheric Sciences, Desert Research Institute

Nitrogen oxide chemistry in combustion processes. Based on material originally by Prof. Mikko Hupa

Large Eddy Simulation of Syngas and Biogas Explosions Accounting for High Temperature and Pressure Effects

Theory Comparison between Propane and Methane Combustion inside the Furnace

Properties of laminar premixed hydrogen- added ammonia/air flames

FUEL- OXYDANT FLEXIBLE COMBUSTION

sco 2 Research & Development at NETL

Oxy-Combustion Flame Fundamentals for Supercritical CO2 Power Cycles Pete Strakey, NETL

Experimental and kinetic modeling study of CO and NO formation under oxy-fuel conditions. Manuel Barbas. Supervisor: Mário Manuel Gonçalves da Costa

Studying the Effect of H 2, O 2 and CO 2 /N 2 Addition on the Laminar Flame Speed of CH 4 /LPG-Air Mixtures

Simulation of Dual Firing of Hydrogen and JP-8 in a Swirling Combustor

MSW Processing- Gasifier Section

Carpet Waste Gasification:

Flameless Combustion of H 2 - Enriched Fuels: a CFD Aided Experimental Investigation

R&D on Hydrogen Energy Carriers toward Low Carbon Society

Reactive CFD model for the simulation of glass furnace combustion

A reduced chemical kinetics mechanism for NOx emission prediction in biomass combustion

Development of Technologies to Utilize Green Ammonia in Energy Market

DISCLAIMER. Portions of this document may be illegible electronic image products. Images are produced from the best available original document.

Ammonia Combus,on in spark igni,on engine condi,ons

Clean Energy Utilisation from Biogas and Biomass Gasification (Kinetic step)

Electrochemistry is fundamentally different from combustion. What if we treated fuel cells differently from a heat engines?

EXERGY DESTRUCTION AND CHEMICAL IRREVERSIBILITIES DURING COMBUSTION IN SPARK IGNITION ENGINE USING OXYGENATED AND HYDROCARBON FUELS

Laminar Burning Velocity under Quenching Conditions for Propane-Air and Ethylene-Air Flames

CHAPTER 2 COMBUSTION PROPERTIES

Modelling Ethylene-Hydrogen Jet Flames in the MILD Combustion Regime

Environment Protection Engineering. ON CO AND NOx EMISSION IN THE KINETIC COMBUSTION OF PROPANE/NATURAL GAS MIXTURES

NOx Reduction: Flue Gas Recirculation vs Selective Catalytic Reduction. Presented by Jason Jacobi October 28, 2015

Experimental Campaign on a Hydrogen Fuelled Combustor for a 10 MW Class Gas Turbine with Reduced NOx Emissions

SYNERGI MELLEM BIOGAS- OPGRADERING OG SOEC

SIP Energy Carriers Updates and Establishment of Green Ammonia Consortium

SUCCEEDING IN THE VCE 2017 UNIT 3 CHEMISTRY STUDENT SOLUTIONS

Enabling technologies for precombustion

Numerical Analysis of the Combustible Properties of Sewage Sludge Gasification Gas

Analysis of numerical models for the formation of NOX for combustion of gases in the strong swirl flow

FUEL PROCESSING FOR PEM FUEL CELLS


NOx in Cement Clinker Production - Experiences Reducing NOx-Emissions

MODELLING COMBUSTION AND THERMAL NO X FORMATION IN ELECTRIC ARC FURNACES FOR THE PRODUCTION OF FERRO-SILICON AND SILICON-METAL

Influence of Steam Dilution on the Combustion of Natural Gas and Hydrogen in Premixed and Rich-Quench-Lean Combustors

CHAPTER 1 INTRODUCTION

Fundamental Kinetics Database Utilizing Shock Tube Measurements

Dr. L. Axelsson, Chief Engineer, Development

NON THERMAL PLASMA CONVERSION OF PYROGAS INTO SYNTHESIS GAS

Further Development of Low Pressure Drop Duct Burners

An Optimization-Based Approach for the Development of a Combustion Chamber for Residential Micro Gas-Turbine Applications

Problems in chapter 9 CB Thermodynamics

Stability and Combustion Efficiency of a Meso-Scale Combustor Burning Different Hydrocarbon Fuels

COMBUSTION CHARACTERIZATION OF PRODUCER GAS FROM BIOMASS GASIFICATION

Effect of Choke Ring Position on Thermal and Fluid Flow in a SRU Thermal Reactor

State of the Art (SOTA) Manual for Stationary Gas Turbines

Plasma-assisted combustion: applications and fundamental mechanisms

Main Technology Policy Messages/Recommendations

Reforming and burning of ammonia in micro hydrogen and power generation systems

Ammonia Fuel Network Ted Hollinger September 28, 2010

Henning Bockhorn et al. / Energy Procedia 120 (2017)

Low Temperature Hydrocarbon Oxidation and Explosion Safety

The effect of hydrogen addition on flammability limit and NO x emission in ultra-lean counterflow CH 4 /air premixed flames

ADVANCED CATALYTIC STUDIES FOR POWER ENGINEERING AND ENVIRONMENTAL PROTECTION

Effect of Natural Gas Fuel Addition on the Oxidation of Fuel Cell Anode Gas

Validation studies of CFD codes on hydrogen combustion

The effect of hydrogen containing fuel blends upon flashback in swirl burners. Nick Syred Cardiff School of Engineering Wales, U.K.

Fluid dynamics of a post-combustion chamber in electric arc steelmaking plants

EFFECT ON PERFORMANCE OF ENGINE BY INJECTING HYDROGEN

Furnace. 1. (10 points) mol/s 53.5% H2O CO2

Burner Config. #3 The Oxy-Fuel Burner

An Innovative Volatile Organic Compound Incinerator

NOx in Cement Clinker Production - Formation and Measures to minimize NOx-Emission

Project Background (long term goals)

Applications of the constrained Gibbs energy method in modelling thermal biomass conversion.

Selection of technology for the low calorific synthetic gas combustion in the gas turbine combustion chamber

Chemical Looping Reforming with Packed Bed Technology: Experimental Study and Modelling

NUMERICAL STUDY OF LAMINAR PREMIXED METHANE/AIR FLAMES WITH CARBON DIOXIDE DILUTION

Energy Flows and Carbon Emissions: Anaerobic Digestion

Hydrogen fuel supply system and re-heat gas turbine combustion

Investigation of Vitiated Species on the Effect of Scramjet Combustion Using Fuel of Hydrogen or Ethylene

Effects of Small-Scale Turbulence on NOx Formation in Premixed Flame Fronts

The Stability of Turbulent Hydrogen Diffusion Jet Flames

Experimental Investigation of Plasma Assisted Reforming of Propane

R&D on Hydrogen and Energy Carriers in Japan

Chapter 10 Material Balances for Processes Involving Reaction 10.1 Species Material Balances Processes Involving a Single Reaction

GREMI NON-THERMAL PLASMAS AND HYDROGEN PRODUCTION

Transcription:

Chemical kinetics study of combustion characteristics of ammonia-air mixtures under high pressure lean conditions Hadi Nozari and Arif Karabeyoğlu Department of Mechanical Engineering Koç University İstanbul, Turkey 2014 NH 3 Fuel Conference

Low-cost storage (like propane storage conditions) Higher volumetric energy density Ref: «Ammonia and related chemicals as potential indirect hydrogen storage materials», By R. Lan et al., 2012

Power generation capacity Ref: «Fuel Conditioning System for Ammonia-Fired Power Plants» By Arif Karabeyoğlu, Brian Evans, 2012

Drawbacks also exist!

Low flame temperature and slow kinetics 2500 2000 1500 1000 500 Methane H2 Kerosene NH3 0 Adiabatic Flame Temperature (K) 1 atm and 20 C «Ammonia It s Transformation and Effective Utilization» AIAA 2008

Flame Speed (cm/sec) Low flame speed 160 140 145 120 100 80 60 40 20 0 40 14 H2 CH4 NH3 Standard Temperature and Pressure Air as oxidizer

NH3, A SOURCE OF NOx IN FLAMES Fuel NOx A simplified reaction mechanism Ref: Miller, J. A. et al., Combust. Sci. Tech., 34:149 176 (1983)

Objective Approach To burn NH3 in a power generation system in efficient and environmentally friendly way: Low NOx emission Low NH3 slip Chemical kinetics study of NH3/H2/Air under practical combustion conditions Developing a reduced mechanism capable of predicting combustion characteristics with an acceptable accuracy CFD simulation of combustion by applying the reduced mechanism Experimental study to examine the validity of results

Studied Cases Reactants Composition NH3/H2/Air xnh 3 + yh 2 + a stoi O 2 + 3.76 N 2 b H 2 O + c N 2 % E of NH 3 NH 3 H 2 O 2 N 2 100 0.1228 0 0.1843 0.6929 80 0.0958 0.0382 0.1819 0.6840 P=17 atm ɸ=0.5 (gas turbine condition) 60 0.0701 0.0745 0.1797 0.6757 40 0.0456 0.1091 0.1776 0.6677 20 0.0223 0.1421 0.1755 0.6600 0 0 0.1736 0.1736 0.6528 %E NH3 = X NH3 LHV NH3 X NH3 LHV NH3 + X H2 LHV H2 100

Laminar flame speed sensitivity analysis Autoignition process NOx formation sensitivity analysis Impact of variation of main parameters on total NOx level REACTION MECHANISM Konnov Mechanism* Elements: N/H/O Species: 30 Reactions: 240 * A.A.Konnov, Combust. Flame 156 (2009) 2093 2105

Laminar flame speed sensitivity analysis Aim: To identify the most influential reactions to the laminar flame speed 100% NH 3 80%NH 3 R9: H+O 2 OH+O R10: H+O 2 HO 2 ɸ = 0.5, P=17 bar, T= 673 K S i = (A i /S u ) ( S u / A i ) S i : Normalized sensitivity coefficient of the i th reaction A i : Pre-exponential rate constant of the i th reaction S u : Laminar flame speed

Ammonia decomposition analysis Aim: To identify the contribution of each reaction in molar conversion of NH 3 100% NH 3 80%NH 3 60%NH 3 Study Cases The most important reactions and their contribution (%) ɸ = 0.5, P=17 bar, T= 673 K Fuel mixture NH 3 +OH NH 2 +H 2 O NH 3 +O NH 2 +OH NH 3 +NH 2 N 2 H 3 +H 2 Pure NH 3 95% 4.64% 0.23% 80%NH 3 94.8% 5.04% 0.11% 60%NH 3 94.5% 5.45% ignorable

Importance of OH radical in flame speed Correlation ɸ = 0.5, P=17 bar, T= 673 K

Autoignition Importance of radicals in autoignition and ignition initiation 100%NH 3 80%NH 3 ɸ=0.5, T=1300 K, P=17 bar Accumulation of influential radicals close to the ignition time

Autoignition - Effect of initial mixture T - Effect of NH3 content ɸ=0.5, P=17 bar

NOx Formation Effect of H2 addition to the mixture Addition up to 80% Increase in total NOx ɸ=0.5 Higher than 80% H2 Thermal NOx increase>fuel NOx decrease Decrease in total NOx Fuel NOx decrease>thermal NOx increase

NOx Formation Effect of equivalence ratio variation Increasing / Decreasing trend Two opposite effects: 1) Increase in thermal NOx by increase in adiabatic flame T 2) Decreasing fuel NOx by decreasing O/F ratio NH i + OX NO + H i X OX: Oxygenated species Noticeable reduction in NO x emission under the rich conditions P=17 bar, T=673 K

Under the studied conditions Controlling role of radicals in laminar flame speed and autoignition process with OH as the most influential radical Adding H2 to the fuel mixture improved laminar flame speed and autoignition process Adding H2 does not necessarily decrease the NOx level Total NOx formation is highly dependent on the competition between fuel NO x and thermal NO x levels NOx level is very sensitive to equivalence ratio in all the mixture compositions Localized rich combustion seems to minimize NOx. Ammonia slip may be the compromise

Obtaining a reduced mechanism applicable to CFD codes CFD simulation of the combustion process using the resulted reduced mechanism Experimental investigation of NH3 combustion in combustor of a power generation unit

Thank You