• Aucun résultat trouvé

OPTIMIZATION OF A DRY LOW NO

N/A
N/A
Protected

Academic year: 2021

Partager "OPTIMIZATION OF A DRY LOW NO"

Copied!
21
0
0

Texte intégral

(1)

Université Libre de Bruxelles Brussels School of Engineering Aero-Thermo-Mechanics

In cooperation with Aachen University of Applied Sciences Department Aerospace Technology

OPTIMIZATION OF A DRY LOW NOX MICROMIX

COMBUSTOR FOR AN INDUSTRIAL GAS TURBINE USING HYDROGEN-RICH SYNGAS FUEL

Dissertation submitted for the degree of Doctor of Engineering Sciences and Technology

by

Jan Keinz

2018

(2)

Abstract I

Abstract

(3)

Résumé II

Résumé

(4)

Acknowledgement III

Acknowledgement

The successful conclusion of the research about DLN Micromix syngas and hydrogen combustion and the completion of this thesis would not have been possible without the support and the assistance of many people.

First, I would like to say thank you to my supervisor Professor Patrick Hendrick for promoting this thesis and for his support during the last years. Furthermore, many thanks go to my committee chair Professor Alessandro Parente for his helpful advice especially in the field of CFD simulations. I gratefully acknowledge their support of the research cooperation between Université Libre de Bruxelles and Aachen University of Applied Sciences.

I owe particular thanks to my co-supervisor Professor Harald Funke for initiating the research activities in the field of hydrogen and syngas fueled gas turbines and for giving me the opportunity to work in this research area. Many thanks for his academic and personal guidance.

Special thanks go to my colleagues from Aachen University of Applied Sciences: Sebastian Börner, Harald Schäfer, Uwe Rönna, Nils Beckmann and Gerhard Hahn. This thesis greatly benefited from their continuous cooperation and advice. The numerical simulations presented in this work have been supported and performed by my colleagues at B&B AGEMA GmbH: Karsten Kusterer, Anis Haj Ayed, Jens Dickhoff and Constantin Striegan. Their support is gratefully acknowledged.

(5)

Table of Contents IV

Table of Contents

Abstract ___________________________________________ I Résumé ___________________________________________ II Acknowledgement ___________________________________ III Table of Contents ____________________________________ IV List of Figures _____________________________________ VIII List of Tables _______________________________________ XI Nomenclature _____________________________________ XII

(6)

Table of Contents V

(7)

Table of Contents VI

(8)

Table of Contents VII

(9)

List of Figures VIII

List of Figures

(10)

List of Figures IX

(11)

List of Figures X

(12)

List of Tables XI

List of Tables

(13)

Nomenclature XII

Nomenclature

Abbreviations

3D three-dimensional

AcUAS Aachen University of Applied Sciences ABB Asea Brown Boveri

AEV Advanced Environmentally-friendly V-shaped burner AGP air guiding panel

APU auxiliary power unit BBC Brown Boveri Company

C carbon

C2H6S dimethyl sulfide C2H6S2 dimethyl disulfide CCP combined cycle plant CCS carbon capture and storage CCU carbon capture and use CFD computational fluid dynamics CH hydrocarbons

CH4 methane

CO carbon monoxide CO2 carbon dioxide COS carbonyl sulfide const. constant CS2 carbon sulfide DLE dry low emissions DLN dry low NOx DP design point EBU Eddy-Break-Up

(14)

Nomenclature XIII

EQHHPP Euro-Québec-Hydro-Hydrogen-Pilot-Project EU European Union

EV Environmentally-friendly V-shaped (burner) FLOX Flameless Oxidation

H-EBU hybrid-EBU H* hydrogen radical H2 hydrogen H2O water

H2S hydrogen sulfide H2SO4 sulfuric acid HO2 hydroperoxyl

IGCC integrated gasification combined cycle IGV inlet guide vane

JICF jet in crossflow LHV lower heating value

MBtu Mega (1∙106) British Thermal Units MES main engine start

MILD Moderate or Intense Low Oxygen Dilution

MMX Micromix

MT multi-tube N2 nitrogen

N2H3 ammonia

(15)

Nomenclature XIV

OH* hydroxyl radical

OH-PLIF hydroxyl planar laser-induced fluorescence PDn normalized power density

ppm parts per million r Arrhenius-formulation

RANS Reynolds-averaged Navier–Stokes equation rpm revolutions per minute

R-SH mercaptans

SAR stoichiometric air requirement SG syngas

SG 90/10 customized SG-mixture for testing SO2 sulfur dioxide

SO3 sulfur trioxide

TBC thermal barrier coating TCD thermal conductivity detector UHC unburned hydrocarbons ULB Université Libre de Bruxelles VECB Versatile Engine Control Box VOC volatile organic compounds

Greek Notations

α alpha – constant [-]

beta – constant [-]

gamma – constant [-]

Δ delta – difference [-]

(16)

Nomenclature XV

DP air fuel equivalence ratio at design point [-] Φ phi – fuel air equivalence ratio [-] ΦDP fuel air equivalence ratio at design point [-] ΨCO psi – substance amount of CO [ppm] ΨH2 psi – substance amount of hydrogen [ppm] Ψj psi – substance amount of component j [ppm] ΨNO psi – substance amount of NO [ppm] ΨNO2 psi – substance amount of NO2 [ppm] ΨNOx psi – substance amount of NOx [ppm]

ρair rho – density of air [ ]

ρfuel rho – density of fuel [ ]

θ theta – air load factor [ ∙ .75∙]

Latin Notations

Aref reference area [m²]

ALF air load factor [ ∙ .75∙]

bref reference width [m]

BR blockage ratio [-]

BRAGP blockage ratio of air guiding panel [-] BRSeg blockage ratio of burner segment [-] BRDR blockage ratio dimension ratio [-]

c velocity [ ]

cair air velocity [ ]

cfuel fuel velocity [ ]

(17)

Nomenclature XVI

CO carbon monoxide [ ], [ppm]

CO2 carbon dioxide [ ], [ppm]

dfuel injector nozzle diameter [m] dAGP inner dimensions of air guiding panel [m] DAGP outer dimensions of air guiding panel [m] dSeg inner dimensions of burner segment [m] DSeg outer dimensions of burner segment [m]

EGT exhaust gas temperature [K]

EI emissions index [ ]

gCO mass related share of carbon monoxide [-] gH2 mass related share of hydrogen [-] H0 relative ambient air humidity [%]

H2 hydrogen [ ],[ppm]

hgate height of air gate [m]

href reference height [m]

J momentum ratio [-]

JDP momentum ratio at design point [-]

Jmax maximum momentum ratio [-]

LHV lower heating value [ ], [ ]

ṁ mass flow [ ]

ṁair mass flow of air [ ]

ṁCO mass flow of carbon monoxide [ ]

ṁfuel mass flow of fuel [ ]

ṁH2 mass flow of hydrogen [ ]

ṁKerosene mass flow of kerosene (Jet A-1) [ ]

(18)

Nomenclature XVII

nfuel number of fuel injector nozzles [-]

N2 nitrogen [%]

NO nitrogen monoxide [ ], [ppm]

NO2 nitrogen dioxide [ ], [ppm]

NOx nitric oxides [ ], [ppm]

O2 oxygen [%]

p0 ambient pressure [bar]

p1 pressure at air inlet [bar]

p2 pressure at compressor inlet [bar] p3 combustor inlet pressure [bar] p5 pressure after last turbine stage [bar]

pfuel fuel pressure [bar]

poil oil pressure [bar]

pref reference pressure [bar]

pst static pressure [bar]

PDn normalized power density [ ]

Q̇ heat flow rate [ ]

Q̇H2 heat flow rate of hydrogen [ ] Q̇Kerosene heat flow rate of kerosene (Jet A-1) [ ] Q̇SG heat flow rate of syngas (SG 90/10) [ ]

r radius [m]

Rair specific gas constant of air [ ], [ ] Rfuel specific gas constant of fuel [ ], [ ]

RM general gas constant [ ], [ ]

Re Reynolds Number [-]

(19)

Nomenclature XVIII

sn normalized distance between injectors [-] SAR stoichiometric air requirement [-]

T temperature [K]

T0 ambient temperature [K]

T1 temperature at air inlet [K]

T3 combustor inlet temperature [K] T4 combustor outlet temperature [K]

Tamb ambient temperature [K]

Tfuel fuel temperature [K]

Tref reference temperature [K]

Tt total temperature [K]

WI Wobbe Index [ ], [ ]

WIi inferior Wobbe Index [ ], [ ]

y injection depth of fuel jet in air cross-flow [m] ycrit critical injection depth [m] yDP injection depth at design point [m]

ymax maximum injection depth [m]

yn normalized injection depth [m]

(Δp/p) pressure loss [-]

(20)

Nomenclature XIX

Subscripts

0 ambient conditions

1 station 1 of the gas turbine: air inlet

2 station 2 of the gas turbine: compressor inlet 3 station 3 of the gas turbine: combustor inlet 4 station 4 of the gas turbine: combustor outlet 5 station 5 of the gas turbine: turbine outlet ad adiabatic

AGP air guiding panel

air air related parameters in general amb ambient conditions

APU related to auxiliary power unit

CO carbon monoxide related parameters in general crit critical

DP design point dyn dynamic

ECS related to ECS-mode eff effective

FMU fuel metering unit

fuel fuel related parameters in general

gate parameters related to the air gate in an air guiding panel H2 hydrogen related parameters in general

i inferior

j general numerical index

Kerosene kerosene (Jet A-1) related parameters in general kg mass related

max maximum

MES related to MES-mode

min minimum

(21)

Nomenclature XX

n normalized

NO nitric oxide related parameters in general NO2 nitrogen dioxide related parameters in general NOx nitrogen oxides related parameters in general oil oil

ref reference

Seg related to the MMX burner segment SG syngas related parameters in general st static

t total

Références

Documents relatifs

Experience Gained from the Space Nuclear Rocket Program (ROVER). Flow Instability Tests for a Particle Bed Reactor Nuclear Thermal Rocket Fuel Element. Thesis, Department of

MIT initiated a research program in the mid 1990's to develop a technology for microscale gas turbine engines. Epstein et al. [7, 8] led this initiative in

As imagens de MET para a liga Pd0,97Ce0,03 oxidada internamente a 1073 K por 24 h figura 4.3.3 mostra a presença de precipitados óxidos aciculares dispersos na matriz cristalina,

The reactor-exchanger design relies on an innovative arrangement of bayonet tubes that allows, at large scale, multiple heat exchanges between hot pressurized flue gas, natural gas

L’archive ouverte pluridisciplinaire HAL, est destinée au dépôt et à la diffusion de documents scientifiques de niveau recherche, publiés ou non, émanant des

The assumption that a solid phase must have been present also within the AHTS is based on the increase in pressure observed within the AHTS during the warm-up period from 1.1K

We will review these results for the determination of the room temperature surface phase diagram for GaAs and for AIAs(100) since these are pertinent to undemanding

- Photoemission yield spectra Y(E) plotted against photon energy for cleaved GaAs after interaction with ionized hydrogen at various exposures. These curves. are a