Structure of atmospheric pressure premixed hydrogen-oxygen flame doped with iron pentacarbonyl
|
|
- Conrad Baker
- 6 years ago
- Views:
Transcription
1 Structure of atmospheric pressure premixed hydrogen-oxygen flame doped with iron pentacarbonyl I.E. Gerasimov, D.A. Knyazkov, A.G. Shmakov, A.A. Paletsky, V.M. Shvartsberg, T.A. Bolshova, O.P. Korobeinichev Institute of Chemical Kinetics & Combustion, Novosibirsk, Russia 7 th International Seminar on Flame Structure, Novosibirsk, Russia, July 11-15, 2011
2 Background Combustion chemistry of iron-containing compounds, including iron pentacarbonyl Fe(CO) 5, is of considerable interest. Fe(CO) 5 is known to be an effective flame inhibitor (due to formation from Fe(CO) 5 in flames FeO and FeOH species, which catalyze the recombination of H and OH radicals). Additive of Fe(CO) 5 (or other ICS) reduces soot concentration in the post-flame zone under certain conditions. Synthesis of iron-containing nanoparticles in flames is a promising line of research. These issues are interrelated because they deal with chemical transformations of ICS in flames. Dr. Linteris, et al proposed a detailed chemical kinetic mechanism for flame inhibition by Fe(CO) 5. Atakan et al made a major experimental contribution to study of ICS transformation in flames.
3 Motivation Earlier developed mechanism of Fe(CO) 5 transformation in flames (Babushok, Linteris et al.) was validated by comparing measured and simulated burning velocities of premixed flames and extinction strain rates of opposed-jet diffusion flames. Atakan and coworkers validated it against measured concentration profiles of atomic iron. Therefore, an urgent need emerged to validate the mechanism by comparing measured and predicted flame structure, especially concentration profiles of iron-containing products of Fe(CO) 5 combustion.
4 Objective to validate the mechanism for iron pentacarbonyl transformation in flames by comparison of chemical kinetic model predictions with new experimental data on spatial variations of mole fractions of Fe-containing products of Fe(CO) 5 oxidation in atmospheric-pressure H 2 /O 2 /N 2 flame
5 Premixed, near-stoichiometric (f=1.1) H 2 /O 2 /N 2 flame stabilized on a flat burner at P=1 bar and T 0 =60 0 C was studied. The gas velocity near the burner was 107 cm/s (75% of the flame speed). Perforated plate Experimental approach Fresh mixture Steel beads Bubbler with Fe(CO) 5 Flame temperature ~ 1600 K Thermostat 60 0 С Flame reactants Component H 2 O 2 N 2 Fe(CO) 5 Content, %
6 Ion pump, 400 L/s Turbomolecular pump, 500 L/s Turbomolecular pump, 500 L/s Diffusion pump, 1100 L/s Experimental approach Molecular beam mass spectrometric setup for measuring ICS mole fraction profiles Flame 5x10 torr -8 3x10 torr torr -5 6,7 мм MS-7302 Liquid-nitrogen trap Sonic probe Disk chopper Skimmer Burner with burner positioning mechanism The quartz probe was clogged by Fecontaining particles for 5 minutes of experiment and underwent irreversible changes. Mean-square error ±50% as a result of low concentration of Fe species
7 Modeling Flame structure was simulated using PREMIX code. Chemical kinetic mechanism for Fe(CO) 5 transformation in flames proposed by Babushok, Linteris et al. (59 reactions involving 12 ICS) and mechanism GRI 3.0 were used for the simulation. Calculation and visualization of Fe-element fluxes from species to species was performed using the KINALC and the Flux Viewer codes
8 Results and Discussion Simulated spatial variations of major ICS concentration in H 2 /O 2 /N 2 flame doped with 100 ppm Fe(CO) 5 stabilized on a flat burner at 1 bar.
9 Results and Discussion Spatial variations of Fe mole fraction in H 2 /O 2 /N 2 flame doped with 100 ppm Fe(CO) 5 stabilized on a flat burner at 1 bar; symbols experiment, curves modeling.
10 Results and Discussion Spatial variations of FeOH mole fraction in H 2 /O 2 /N 2 flame doped with 100 ppm Fe(CO) 5 stabilized on a flat burner at 1 bar; symbols experiment, curves modeling.
11 Results and Discussion Spatial variations of FeO 2 mole fraction in H 2 /O 2 /N 2 flame doped with 100 ppm Fe(CO) 5 stabilized on a flat burner at 1 bar; symbols experiment, curves modeling.
12 Results and Discussion Spatial variations of Fe(OH) 2 mole fraction in H 2 /O 2 /N 2 flame doped with 100 ppm Fe(CO) 5 stabilized on a flat burner at 1 bar; symbols experiment, curves modeling.
13 Results and Discussion Where is FeO? The intensity of peak at 72 AMU (FeO) was very low and we failed to measure it along the flame zone. It may be explained by 2 reasons: 1. a low FeO concentration in the flame (contrary to the model prediction). 2. a low sensitivity of mass spectrometer to FeO. In our practice we met examples when two parent compounds have essentially different calibration coefficients, e.g. k(po2)/k(po)=0.77/0.02=38.5. By the same argument we failed to measure FeH and FeOOH.
14 Results and Discussion Spatial variations of total ICS concentration in H 2 /O 2 /N 2 flame doped with 100 ppm Fe(CO) 5 stabilized on a flat burner at 1 bar; symbols experiment, curves modeling. Fe + FeO 2 + FeOH + Fe(OH) 2 50%-deficit of iron is observed at mm above burner. Possible explanation: Fe 2 O 3, Fe 3 O 4 and other species, which were not measured, are present in the flame.
15 Results and Discussion Schematic diagram of ICS reaction pathways in H 2 /O 2 /N 2 flame doped with 100 ppm Fe(CO) 5 at 0.3 mm from the burner. Fe(CO) 5 -CO Fe(CO) 4 +H/ -H 2 O FeOH Fe(OH) 2 -CO Fe(CO) 3 +H/ -H 2 +H 2 O -CO Fe(CO) 2 -CO +O/ -O 2 +H/ -OH +H 2 / -H 2 O FeO +O/ -O 2 Fe(CO) Fe FeO 2 +O/ -CO 2 +O 2
16 Conclusions 1. Concentrations of iron-containing products of Fe(CO) 5 combustion (Fe, FeO 2, FeOH, and Fe(OH) 2 ) in a H 2 /O 2 /N 2 flame at atmospheric pressure using the MBMS method were measured. 2. A kinetic model for flame inhibition by Fe(CO) 5 proposed earlier by Rumminger, Reinelt, Babushok, Linteris was validated basing on the experimental data. 3. The kinetic model satisfactorily predicts FeO 2 and Fe(OH) 2 in the flame. FeOH and Fe(OH) 2 were shown to be the main iron-containing products of Fe(CO) 5 oxidation in the flame studied. In the flame reaction zone, atomic iron was shown to be the main iron-containing compound produced by the reduction of iron oxides via interaction with H, O, and H 2.
17 Thank you!
18 H 2 O a) Major stable species Neat flame and flame doped with 230 ppm of Fe(CO) H Neat H2 flame мольная доля O 2 H H 2 O б) Doped flame O расстояние от горелки, мм
19 Reactions responsible for flame inhibition by Fe(CO) 5 FeOH + H FeO + H 2 FeO + H 2 O Fe(OH) 2 Fe(OH) 2 + H FeOH + H 2 O Total: H + H H 2 Fe + O 2 + M FeO 2 + M FeO 2 + O FeO + O 2 FeO + O Fe + O 2 Total: O + O O 2
Ammonia Combus,on in spark igni,on engine condi,ons
Ammonia Combus,on in spark igni,on engine condi,ons Catherine Duynslaegher, Hervé Jeanmart, Jacques Vandooren, Université catholique de Louvain, Belgium Introduc,on Search for alternatives to fossil fuels
More informationConversion of Hydrocarbons into Syn-Gas Stimulated by Non-thermal Atmospheric Pressure Plasma
Conversion of Hydrocarbons into Syn-Gas Stimulated by Non-thermal Atmospheric Pressure Plasma Alexander Fridman, Alexander Gutsol Young I Cho, Chiranjeev Kalra Plasma Catalysis Vs. Plasma Processing Methane
More informationTheory Comparison between Propane and Methane Combustion inside the Furnace
International Journal of Current Engineering and Technology E-ISSN 2277 4106, P-ISSN 2347 5161 2015 INPRESSCO, All Rights Reserved Available at http://inpressco.com/category/ijcet Research Article Theory
More informationThe Influence of Chemical Inhibitor Addition on Reverse-Jet Flame Stabilization
68 -GT-39 The Society shall not be responsible for statements or opinions advanced in papers or in discussion at meetings of the Society or of its Divisions or Sections, or printed in its publications.
More informationAn Improved Reaction Mechanism for Combustion of Core (C 0 -C 4 ) Fuels
An Improved Reaction Mechanism for Combustion of Core (C 0 -C 4 ) Fuels Chitralkumar V. Naik*, Karthik V. Puduppakkam, Ellen Meeks July 13, 2011 The 7th International Conference on Chemical Kinetics Outline
More informationExperimental investigation of the effect of nitrogen dilution on NO x emission in propane-air non-premixed flame
MCS 7 Chia Laguna, Cagliari, Sardinia, Italy, September 11-15, 2011 Experimental investigation of the effect of nitrogen dilution on NO x emission in propane-air non-premixed flame Abdolrasoul Rangrazi*
More informationCopyright 2006 Igor V. Novosselov
Copyright 2006 Igor V. Novosselov Chemical Reactor Networks for Combustion Systems Modeling Igor V. Novosselov A dissertation submitted in partial fulfillment of the requirement for the degree of Doctor
More informationAnalysis of numerical models for the formation of NOX for combustion of gases in the strong swirl flow
Analysis of numerical models for the formation of NOX for combustion of gases in the strong swirl flow P. Grzymislawski* 1, R. Slefarski 1, M. Golebiewski 1 1 Poznan University of Technology, Poland Abstract
More informationSelective Oxidation of Advanced High Strength Steels (AHSS) and Ultra High Strength Steel (UHSS) Utilizing Direct Fired Burners
Selective Oxidation of Advanced High Strength Steels (AHSS) and Ultra High Strength Steel (UHSS) Utilizing Direct Fired Burners Scott Brown 1, David Schalles 2, Frank Beichner 3 1 Director of Sales and
More informationHigh temperature sulfidation of pack-tantalized iron
JOURNAL DE PHYSIQUE IV Colloque C9, suppltment au Journal de Physique 111, Volume 3, dccembre 1993 High temperature sulfidation of pack-tantalized iron A. Galerie, F. Passier, X. Nguyen Khac and M. Caillet
More informationChemical kinetics study of combustion characteristics of ammonia-air mixtures under high pressure lean conditions
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,
More informationCharacterization of Coal and Biomass Conversion Behaviors in Advanced Energy Systems
Characterization of Coal and Biomass Conversion Behaviors in Advanced Energy Systems Investigators Reginald E., Associate Professor, Mechanical Engineering; Paul A. Campbell and Liqiang Ma, Graduate Researchers
More informationThe effect of temperature on the rate of an enzyme catalyzed reaction. Subtitle
The effect of temperature on the rate of an enzyme catalyzed reaction Subtitle In this experiment, we will continue to study acid phosphatase kinetics. Acid phosphatase kinetics Time Enzyme concentration
More informationSwirl chamber for vitrification of fly ashes
WTiUE 016 13, 05004 (017) DOI: 10.1051/ e3sconf/0171305004 Swirl chamber for vitrification of fly ashes Robert Zarzycki 1,* 1 Czestochowa University of Technology, Department of Energy Engineering, ul.
More informationCharacterization of Coal and Biomass. Conversion Behaviors in Advanced Energy Systems
Characterization of Coal and Biomass Conversion Behaviors in Advanced Energy Systems Reginald Mitchell, Paul Campbell and Liqiang Ma High Temperature Gasdynamics Laboratory Group Mechanical Engineering
More informationPrediction of Pollutant Emissions from Industrial Furnaces Using Large Eddy Simulation
Paper # B03 Topic: Turbulent Flames 5 th US Combustion Meeting Organized by the Western States Section of the Combustion Institute and Hosted by the University of California at San Diego March 25-28, 2007.
More informationThe effect of hydrogen addition on flammability limit and NO x emission in ultra-lean counterflow CH 4 /air premixed flames
Proceedings of the Combustion Institute 30 (2005) 303 311 Proceedings of the Combustion Institute www.elsevier.com/locate/proci The effect of hydrogen addition on flammability limit and NO x emission in
More informationEMPIRICAL FORMULA DETERMINATION
Name Date Class Chapter 10 Chemical Quantities EXPERIMENT EMPIRICAL FORMULA DETERMINATION Text Reference Section 10.3 PURPOSE To determine the empirical formula of magnesium oxide. BACKGROUND Carbon dioxide
More informationRECENT COST REDUCTION DEVELOPMENTS IN THE HEATING OF STEEL
RECENT COST REDUCTION DEVELOPMENTS IN THE HEATING OF STEEL Steven J. O'Connor, Senior Applications Engineer, Bloom Engineering Company Anthony G. Fennell, Western Regional Manager, Bloom Engineering Company
More informationANSYS Combustion Analysis Solutions - Overview and Update
ANSYS Combustion Analysis Solutions - Overview and Update Gilles Eggenspieler ANSYS, Inc. 1 Agenda Overview of Combustion Analysis Solution Reduced Order Models Finite Rate Models Pollutant Models Examples
More informationCOMBUSTION CHARACTERIZATION OF PRODUCER GAS FROM BIOMASS GASIFICATION
Global NEST Journal, Vol 14, No 2, pp 125-132, 2012 Copyright 2012 Global NEST Printed in Greece. All rights reserved COMBUSTION CHARACTERIZATION OF PRODUCER GAS FROM BIOMASS GASIFICATION J.J. HERNÁNDEZ
More informationEffect of Flue Gas Recirculation on the Formation of Fine Particulate Matter in a Domestic Pellet-Fired Boiler
Effect of Flue Gas Recirculation on the Formation of Fine Particulate Matter in a Domestic Pellet-Fired Boiler U. Fernandes, M. Henriques and M. Costa Mechanical Engineering Department, Instituto Superior
More informationLow-mass PM analyzer MEXA-1370PM Improvement of the Performance for PM Composition Analysis
F e a t u r e A r t i c l e Feature Article Low-mass PM analyzer MEXA-1370PM Improvement of the Performance for PM Composition Analysis Masayoshi Shinohara, Tomoshi Yoshimura Particulate matter (PM) emitted
More informationPOLTTOPROSESSIEN LASKENNALLINEN JA KOKEELLINEN TUTKIMUS:
1 POLTTOPROSESSIEN LASKENNALLINEN JA KOKEELLINEN TUTKIMUS: Application of HTAC Technique in Combustion of Liquid Fuels Janne Wahlman and Antti Oksanen Energy and Process Engineering Tampere University
More informationInvestigators: R. E. Mitchell, Associate Professor, Mechanical Engineering Department; P. A. Campbell and L. Ma, Graduate Researchers
Coal and Biomass Char Reactivity Investigators: R. E. Mitchell, Associate Professor, Mechanical Engineering Department; P. A. Campbell and L. Ma, Graduate Researchers Project Overview: There is considerable
More informationCOMBUSTION OF LIQUID FUELS COMBUSTION AND FUELS
COMBUSTION OF LIQUID FUELS PHASES OF LIQUID FUEL BURNING Two phases of liquid fuel burning: a) phase of liquid evaporation, b) phase of vapour burning. Cloud of vapour Droplet of fuel DOMINATING FACTORS
More informationTable of Contents. Preface...
Preface... xi Chapter 1. Metallurgical Thermochemistry... 1 1.1. Introduction... 1 1.2. Quantities characterizing the state of a system and its evolution... 3 1.2.1. The types of operations... 3 1.2.2.
More informationDetermination of the Empirical Formula of Magnesium Oxide
Determination of the Empirical Formula of Magnesium Oxide The quantitative stoichiometric relationships governing mass and amount will be studied using the combustion reaction of magnesium metal. Magnesium
More informationMeasurements and analysis of CO and O 2 emissions in CH 4 /CO 2 /O 2 flames
Available online at www.sciencedirect.com Proceedings of the Combustion Institute 33 (2011) 3399 3405 Proceedings of the Combustion Institute www.elsevier.com/locate/proci Measurements and analysis of
More informationThe Formation of Carbon Monoxide from Diffusion Flames
The Formation of Carbon Monoxide from Diffusion Flames S. LOMAX and R. F. SIMMONS Department of Chemistry The University of Manchester Institute of Science and Technology Manchester M6 1D, England ABSTRACT
More informationThe empirical formula of a compound
The empirical formula of a compound Reference: Chapter 1, Section 1.2, pages 21 24 Please note Aim A full risk assessment should be carried out prior to commencing this experiment. Personal safety equipment
More informationReforming and burning of ammonia in micro hydrogen and power generation systems
8 th Annual Ammonia Fuel Conference Portland, OR, USA, 18-21 September 2011 Reforming and burning of ammonia in micro hydrogen and power generation systems O.C. Kwon *, J.M. Joo, S.I. Lee and D.H. Um School
More informationChemistry 145 Exam number 4 name 11/19/98 # Faraday s constant is 96,500 c/mole of electrons.
Chemistry 145 Exam number 4 name 11/19/98 # Faraday s constant is 96,500 c/mole of electrons. A.(16) An electrochemical cell is prepared with a strip of manganese metal dipping in to a 1.0 M MnSO 4 solution
More informationObservation of Impurity Accumulation After Hydrogen Multi-Pellet Injection in Large Helical Device
Plasma Science and Technology, Vol.15, No.3, Mar. 2013 Observation of Impurity Accumulation After Hydrogen Multi-Pellet Injection in Large Helical Device DONG Chunfeng ( ) 1, Shigeru MORITA 1,2, Motoshi
More informationTechnological Aspects of Metal Nanopowders
PHYSICS and CHEMISTRY of NANOMATERIALS, lecture 6 Alexander A. Gromov gromov@tpu.ru Chair of Silicates and Nanomaterials, Faculty of Chemical Technology, Tomsk Polytechnic University, RUSSIA Technological
More informationCFD Study of Flare Operating Parameters
CFD Study of Flare Operating Parameters By Daniel Chen, Helen Lou, & Peyton C. Richmond Dan. F. Smith Chemical Engineering Department Xianchang Li Mechanical Engineering Department Lamar University, Beaumont,
More informationICAC MARAMA Portable Emission Analyzers
ICAC MARAMA Portable Emission Analyzers Drew Wilson ECOM America www.ecomusa.com May 19, 2011 Portable Analyzers A quick history Originally developed for combustion efficiency applications. Measured O2,
More informationCO 2 Capture and Storage: Options and Challenges for the Cement Industry
CO 2 Capture and Storage: Options and Challenges for the Cement Industry Martin Schneider, Düsseldorf, Germany CSI Workshop Beijing, 16 17 November 2008 CO 2 abatement costs will tremendously increase
More informationAutomated Methanol dosage using Liquid Flow Controllers: How Nitrogen-Methanol processes for the heat treatment of steel can get more transparent and
: How Nitrogen-Methanol processes for the heat treatment of steel can get more transparent and efficient White Paper Juni 2010 Automated Methanol dosage using Liquid Flow Controllers: How Nitrogen-Methanol
More informationScreening, Definition: The unit involved is called a screen.
Screening, Definition: Screening is a unit operation that separates materials in and/or on water (found in different sizes) from water and from entering water treatment facilities and mains. The unit involved
More informationImpact of Selective Oxygen Injection on NO, LOI, and Flame Luminosity in a Fine Particle, Swirl-Stabilized Wood Flame
Paper # 7CO-63 Topic: Coal and Biomass Combustion and Gasification 8 th U. S. National Combustion Meeting Organized by the Western States Section of the Combustion Institute and hosted by the University
More informationa) The self-diffusion coefficient of a metal with cubic structure can be expressed as
EXERCISES KJM5120 Chapter 5; Diffusion 1. Random (self) diffusion a) The self-diffusion coefficient of a metal with cubic structure can be expressed as 1 n D = s 6 t 2 where n/t represents the jump frequency
More informationNUMERICAL SIMULATIONS OF OXY-COMBUSTION OF PULVERIZED COAL IN SWIRL BURNERS. P. Warzecha, A. Bogusławski
Częstochowa University of Technology INSTITUTE OF THERMAL MACHINERY NUMERICAL SIMULATIONS OF OXY-COMBUSTION OF PULVERIZED COAL IN SWIRL BURNERS P. Warzecha, A. Bogusławski Institute of Thermal Machinery
More informationCalculating energy changes from burning fuels
Calculating energy changes from burning fuels TEACHERS AND TECHNICIANS NOTES Specification reference: C3.3.1 Energy from reactions (a) The relative amounts of energy released when substances burn can be
More information44. Sim Reactions Example
14022-ORC-J 1 (15) 44. Sim Reactions Example 44.1. General This example contains instructions on how to create a simple leaching reactor model where 10 t/h of FeS is leached with acid (H 2 SO 4 ) and air
More informationANSWERS: Combustion. 2C3H8(g) + 7O2(g) 6CO(g) + 8H2O(g)
ANSWERS: Combustion organic molecule methane equation for complete combustion CH4(g) + 2O2(g) CO2(g) + 2H2O(g) equation for incomplete combustion 4CH4(g) + 5O2(g) 2CO(g) + 2C(s) + 8H2O(g) methanol 2CH3OH(l)
More informationSteamate* technology. superior protection against condensate system corrosion. Water Technologies & Solutions technical bulletin
Water Technologies & Solutions technical bulletin Steamate* technology superior protection against condensate system corrosion problems in steam distribution systems The steam distribution system can be
More informationIRON CARBONATE SCALE GROWTH AND THE EFFECT OF INHIBITION IN CO 2 CORROSION OF MILD STEEL
IRON CARBONATE SCALE GROWTH AND THE EFFECT OF INHIBITION IN CO 2 CORROSION OF MILD STEEL Kunal Chokshi, Wei Sun, Srdjan Nesic Institute for Corrosion and Multiphase Technology, Ohio University 342 West
More informationEffect of CO Gas Concentration on Reduction Rate of Major Mineral Phase in Sintered Iron Ore
, pp. 570 575 Effect of CO Gas Concentration on Reduction Rate of Major Mineral Phase in Sintered Iron Ore Daisuke NOGUCHI, 1) * Ko-ichiro OHNO, 2) Takayuki MAEDA, 2) Kouki NISHIOKA 3) and Masakata SHIMIZU
More informationA New Theranostic System Based on Gold Nanocages and Phase-Change Materials with Unique Features for Photoacoustic Imaging and Controlled Release
1/2011 Supporting Information A New Theranostic System Based on Gold Nanocages and Phase-Change Materials with Unique Features for Photoacoustic Imaging and Controlled Release Geon Dae Moon,, Sung-Wook
More informationAngle-resolved XPS study of carbon steel passivity and chloride-induced depassivation in simulated concrete pore solution
Angle-resolved XPS study of carbon steel passivity and chloride-induced depassivation in simulated concrete pore solution Authors: P. Ghods et al Year: 2012 Introduction Carbon steel rebar is generally
More informationEXPERIMENT 5. Molecular Absorption Spectroscopy: Determination of Iron with 1,10-Phenanthroline
EXPERIMENT 5 Molecular Absorption Spectroscopy: Determination of Iron with 1,10-Phenanthroline UNKNOWN Submit a clean, labeled 100-mL volumetric flask to the instructor so that your unknown iron solution
More informationStudies on Alloys and Composites that Undergo Anomalous Codeposition
Studies on Alloys and Composites that Undergo Anomalous Codeposition Electrochemical of of South Columbia, SC908 09, 1998 Electrochemical Systems Studied FeNi alloys and FeNiSiO composites Electrodeposition
More informationAbout AMETEK/Thermox Worldwide Availability and Support Fuel Savings Calculator
About AMETEK/Thermox AMETEK/Thermox has been a pioneer in the use of zirconium oxide to measure oxygen since 1967. We introduced combined oxygen and combustibles measurement in 1974 and have continued
More information(3) The compound boron nitride (BN) has a high melting point (2967 ºC), high density, and is very hard. What is the best classification of this solid?
Solids and Liquids Name: Period: (1) Identify the type of solid formed by each compound. (a) Ag (b) CO 2 (c) SiO 2 (d) wax (e) MgCl 2 (f) Fe (g) graphite (h) SO 2 (i) CaCO 3 (j) I 2 (k) rubber (l) SiC
More informationTHE DEVELOPMENT OF THE POTENTIAL AND ACADEMIC PROGRAMMES OF WROCŁAW UNIVERSITY OF TECHNOLOGY
THE DEVELOPMENT OF THE POTENTIAL AND ACADEMIC PROGRAMMES OF WROCŁAW UNIVERSITY OF TECHNOLOGY Mining and Power Engineering dr inż. Tomasz Hardy (PhD Eng.) Combustion and fuels - laboratory Project co-financed
More informationChemistry CH1HP. (Jan13CH1Hp01) General Certificate of Secondary Education Higher Tier January Unit Chemistry C1. Unit Chemistry C1 TOTAL
Centre Number Surname Candidate Number For Examiner s Use Other Names Candidate Signature Examiner s Initials Science A Unit Chemistry C1 Chemistry Unit Chemistry C1 Monday 14 January 2013 For this paper
More informationWhich of these is the formula for disulfur heptoxide? A. S 2 O 7 B. S 7 O 2 C. SO 2 D. N 2 O
Which of these is the formula for disulfur heptoxide? A. S 2 O 7 B. S 7 O 2 C. SO 2 D. N 2 O Which of these is the correct chemical formula for a molecule of oxygen? A. O B. O -2 C. O +2 D. O 2 Which of
More informationCondensate System Troubleshooting andoptimization
Condensate System Troubleshooting andoptimization One of the prime considerations in the operation of a boiler is feedwater quality. The better the feedwater, the less likely that water-related problems
More informationES Hydrogen Production via the Iron/Iron Oxide Looping Cycle. Copyright 2011 by ASME
Proceedings of the ASME 2011 5th International Conference on Energy Sustainability ES2011 August 7-10, 2011, Washington, DC, USA ES2011-54 Abstract Hydrogen Production via the Iron/Iron Oxide Looping Cycle
More informationGrowth of oxide thin films on 4H- silicon carbide in an afterglow reactor
University of South Florida Scholar Commons Graduate Theses and Dissertations Graduate School 2006 Growth of oxide thin films on 4H- silicon carbide in an afterglow reactor Eugene L. Short University of
More informationHydrogen oxygen steam generator integrating with renewable energy resource for electricity generation
Available online at www.sciencedirect.com Energy Procedia 29 (2012 ) 12 20 World Hydrogen Energy Conference 2012 Hydrogen oxygen steam generator integrating with renewable energy resource for electricity
More informationCombustion of low-volatile coal with an advanced oxy-fuel burner concept including direct oxygen injection
Institute of Combustion and Power Plant Technology Prof. Dr. techn. G. Scheffknecht Combustion of low-volatile coal with an advanced oxy-fuel burner concept including direct oxygen injection Simon Grathwohl,
More informationImpacts of oxy-fuel combustion on coal ash and deposits
Impacts of oxy-fuel combustion on coal ash and deposits Jost O. L. Wendt, Dunxi Yu, William J. Morris, Zhonghua Zhan, Michael Newton, Andrew Fry University of Utah and Reaction Engineering International
More informationAccelerated phosphorous poisoning of automotive SCR-catalyst
Accelerated phosphorous poisoning of automotive SCR-catalyst Karl Henrik Bergquist Department of Chemical Engineering, Lund Institute of Technology, Lund, Sweden Abstract A study of an accelerated phosphorus
More informationImpacts of a Zero Valent Iron PRB on Downgradient Biodegradation Processes. John E. Vidumsky DuPont Corporate Remediation Group
Impacts of a Zero Valent Iron PRB on Downgradient Biodegradation Processes John E. Vidumsky DuPont Corporate Remediation Group Why is Downgradient Biodegradation Important? Significant contaminant mass
More informationSupplementary Information:
Supplementary Information: A low-energy Forward Osmosis Process to Produce Drinking Water Zhaoyang Liu* a, Hongwei Bai a, Jonathan Lee b and Darren Delai Sun* a a. School of Civil & Environmental Engineering,
More informationPrima PRO process mass spectrometer
APPLICATION NOTE Prima PRO process mass spectrometer Accurate multi-component blast furnace gas analysis maximizes iron production and minimizes coke consumption No.?????? Author: Graham Lewis, Thermo
More informationPTAC PROCESS TECHNOLOGY II - SYSTEMS. Last Reviewed: Page 1 of 10
Systems Overview Water Systems: Potable Water Fire Water Water Systems: Service/Utility Waste Water Storm Water 1. Describe how process industry facilities are divided into systems. Identify the types
More information1. Use the Ellingham Diagram (reproduced here as Figure 0.1) to answer the following.
315 Problems 1. Use the Ellingham Diagram (reproduced here as Figure 0.1) to answer the following. (a) Find the temperature and partial pressure of O 2 where Ni(s), Ni(l), and NiO(s) are in equilibrium.
More informationCompounds & Reactions Week 1. Writing Formulas & Balancing Equations. Write the chemical formula for each molecular (covalent) compound.
Compounds & Reactions Week 1 Name Writing Formulas & Balancing Equations Write the chemical formula for each ionic compound. 1. Lithium fluoride 2. Copper (II) chloride 3. Manganese (II) oxide 4. Potassium
More informationThermal Evaporation. Theory
Thermal Evaporation Theory 1. Introduction Procedures for depositing films are a very important set of processes since all of the layers above the surface of the wafer must be deposited. We can classify
More informationgreen B 1 ) into a single unit to model the substrate in this reaction. enzyme
Teacher Key Objectives You will use the model pieces in the kit to: Simulate enzymatic actions. Explain enzymatic specificity. Investigate two types of enzyme inhibitors used in regulating enzymatic activity.
More informationSurface Characterization of Laser Polished Indirect-SLS Parts
Surface Characterization of Laser Polished Indirect-SLS Parts Jorge A. Ramos, David L. Bourell, Joseph J. Beaman Laboratory for Freeform Fabrication The University of Texas at Austin, Austin, Texas 78712
More informationClick to edit Master title style
Click to edit Master title style Zhili Feng, Xinghua Yu, Jeff Bunn, Andrew Payzant- ORNL Demetrios Tzelepis, TARDEC Click to edit Outline Master title style Background Hydrogen Inducted Cracking (HIC)
More informationChallenges in Processing of P/M Chromium Manganese Low-Alloy Steels
Challenges in Processing of P/M Chromium Manganese Low-Alloy Steels Robert J. Causton 1 and Bruce A. Lindsley 2 1 Hoeganaes Corporation, Buzau, Romania 2 Hoeganaes Corporation, Cinnaminson, NJ 08077, USA
More informationA Single Analyzer Solution for Refinery Flare Emissions Monitoring (40 CFR 60 Subpart Ja) Using Mass Spectrometry
A Single Analyzer Solution for Refinery Flare Emissions Monitoring (40 CFR 60 Subpart Ja) Using Mass Spectrometry Introduction New environmental regulations have recently prompted many oil refineries and
More informationEffect of Volatile Matter Content of Coal on Carbothermic Reduction of Ore / Coal Composite Pellets Packed in a Tall Bed
China Steel Technical Report, No. 27, pp.11-19, Lung-Jen (2014) Chiang, Kuo-Cheng Yang and I-Ching Hsiao 11 Effect of Volatile Matter Content of Coal on Carbothermic Reduction of Ore / Coal Composite Pellets
More informationChemistry CH1FP. (Jun15CH1FP01) General Certificate of Secondary Education Foundation Tier June Unit Chemistry C1. Unit Chemistry C1 TOTAL
Centre Number Surname Candidate Number For Examiner s Use Other Names Candidate Signature Examiner s Initials Question Mark Science A Unit Chemistry C1 Chemistry Unit Chemistry C1 Tuesday 9 June 2015 General
More informationFLAME AERODYNAMICS COMBUSTION AND FUELS
FLAME AERODYNAMICS IMPORTANCE OF AERODYNAMICS IN COMBUSTION Fuel Heat Combustion chamber, furnace Flue gas Air Heat Flow reactor Oxidizer: Fuel: Flue gas: MEDIA - air: primary, secondary sometimes tetriary
More informationOxy-fuel combustion integrated with a CO 2 processing unit
POLISH STRATEGIC PROGRAM ADVANCED TECHNOLOGIES FOR ENERGY GENERATION Oxy-fuel combustion integrated with a CO 2 processing unit coordinator: Wojciech Nowak AGH University of Science and Technology Kraków,
More informationPotentials and Limitations with respect to NO x -Reduction of Coke Plants
Potentials and Limitations with respect to NO x -Reduction of Coke Plants NEUWIRTH, Ralf 1, HUHN, Friedrich 1, KIM, Ronald 1, GORSKI, Arkadius 1 (1. ThyssenKrupp Industrial Solution AG, BU Process Technologies,
More informationToday! Demonstrations of Redox Chemistry! Electrochemistry! electrons moving about! equilibrium with a control knob! The disappearing Aluminum Rod!
Today! Electrochemistry! electrons moving about! equilibrium with a control knob! Redox chemistry! oxidation and reduction! Demonstrations of Redox Chemistry! The disappearing Aluminum Rod! Alkali Metals
More informationBURNER FLAME TEMPERATURE DURING WARM UP AND HOT STANDBY. Alan D. Mosher KPS Technology & Engineering LLC
BURNER FLAME TEMPERATURE DURING WARM UP AND HOT STANDBY Alan D. Mosher KPS Technology & Engineering LLC Presented at the Brimstone Sulfur Symposium Facilitated by Brimstone STS Limited Vail Colorado September
More informationExplosion Hazard Evaluation and Determination of the Explosion Parameters for Selected Hydrocarbons C6 C8
Explosion Hazard Evaluation and Determination of the Explosion Parameters... 399 Central European Journal of Energetic Materials, 2012, 9(4), 399-409 ISSN 1733-7178 Explosion Hazard Evaluation and Determination
More informationCoal char oxidation kinetics in air medium
Coal char oxidation kinetics in air medium Alexander G. Korotkikh 1, Konstantin V. Slyusarskiy 1,*, and Ivan V. Sorokin 1 1 National ResearchTomsk polytechnic university, 634050 Tomsk, Russia Abstract.
More informationVLSI Technology. By: Ajay Kumar Gautam
By: Ajay Kumar Gautam Introduction to VLSI Technology, Crystal Growth, Oxidation, Epitaxial Process, Diffusion Process, Ion Implantation, Lithography, Etching, Metallization, VLSI Process Integration,
More informationExperiment Twelve Empirical Formula of Magnesium Oxide
Experiment Twelve Empirical Formula of Magnesium Oxide Objective The purpose of this experiment is to determine the stoichiometric ratio of magnesium and oxygen following the combustion of magnesium metal.
More informationGASOLINE FROM NATURAL GAS BY SULFUR PROCESSING
GASOLINE FROM NATURAL GAS BY SULFUR PROCESSING BY Erek J. Erekson R. Gopalakrishnan January 1996 Work Performed Under Contract No.: DE-AC22-93PC92114 For U.S. Department of Energy Pittsburgh Energy Technology
More information*20GSD5201* Double Award Science: Chemistry. Unit C2 Higher Tier TUESDAY 9 JUNE 2015, AFTERNOON [GSD52] *GSD52* *G5802* TIME 1 hour 15 minutes.
Centre Number Candidate Number General Certificate of Secondary Education 2015 Double Award Science: Chemistry Unit C2 Higher Tier [GSD52] *GSD52* *G5802* *GSD52* TUESDAY 9 JUNE 2015, AFTERNOON TIME 1
More informationEnergy From Electron Transfer. Chemistry in Context
Energy From Electron Transfer Chemistry in Context Energy Types Batteries Hybrid Cars (Electrical) H 2 (and Other) Fuel Cells Solar Fuel Cell Car Demo H 2 Fuel Cell Reactions Step 1: H 2 (g) 2H + (aq)
More informationAtmosphere Effect on Soldering of Flip Chip Assemblies. C. C. Dong Air Products and Chemicals, Inc. U.S.A.
Atmosphere Effect on Soldering of Flip Chip Assemblies C. C. Dong Air Products and Chemicals, Inc. U.S.A. Atmosphere Effect on Soldering of Flip Chip Assemblies Abstract An experimental study was conducted
More informationHYDROGEN AS A CARRIER GAS. Gas Chromatography new frontiers: can Hydrogen substitute Helium?
HYDROGEN AS A CARRIER GAS Gas Chromatography new frontiers: can Hydrogen substitute Helium? Manufacturing UHP gas generators for lab analysis since 1979, CLAIND is seating in Lenno, on Como Lake, where
More informationEVALUATION OF A CHEMICAL CLEANING FORMULATION FOR THE STEAM GENERATOR OF NUCLEAR POWER PLANTS
EVALUATION OF A CHEMICAL CLEANING FORMULATION FOR THE STEAM GENERATOR OF NUCLEAR POWER PLANTS A.L.Rufus, H.Subramanian, V.S.Sathyaseelan, Padma S.Kumar, S.Veena B.Anupkumar, M.P.Srinivasan, S.Velmurugan
More informationThe Nernst-Einstein equation indicates that the ratio β /D for a given material varies only with temperature. Calculate β/d for oxygen ions in Zr 0.
The Nernst-Einstein equation indicates that the ratio β /D for a given material varies only with temperature. Calculate β/d for oxygen ions in 0.8 Y 0.2 1.9 at 800 C. 1 The Nernst-Einstein equation indicates
More informationUniversity of Concepcion, Department of Metallurgical Engineering, Concepcion, Chile
J Min Metall Sect B-Metall 50 (2) B (2014) 127-132 Journal of Mining and Metallurgy, Section B: Metallurgy KINETICS OF STIBNITE ( ) OXIDATION AT ROASTING TEMPERATURES R Padilla a,*, A Aracena b, MC Ruiz
More informationSAIOH Interpretation of Elemental Analyses Results. By: Jaco van Rensburg
SAIOH 2013 Interpretation of Elemental Analyses Results By: Jaco van Rensburg WHY AEROSOL SAMPLING? Air sampling for aerosols, to determine the airborne concentrations of particulate matter, forms a major
More informationSeparations and Reactors. Acrylic Acid Production via the Catalytic Partial Oxidation of Propylene
Separations and Reactors Acrylic Acid Production via the Catalytic Partial Oxidation of Propylene Process Information Background Acrylic acid (AA) is used as a precursor for a wide variety of chemicals
More informationTo hold a large reserve of metal ions in the soluble form.
I 1. I + 3 ' z CHROME REDUCTION AND REMOVAL OF HEAVY METALS IN THE PRESENCE OF CHELATING AGENTS In the electroplating industry the use of electroless solutions has increased tremendously over the past
More information