Development of clean coal technology by using the feature of oxy-fuel combustion
|
|
- Howard Patterson
- 6 years ago
- Views:
Transcription
1 Development of clean coal technology by using the feature of oxy-fuel combustion Hirotatsu Watanabe Department of mechanical and control engineering, graduate school of science and engineering, Tokyo Institute of Technology 4th oxy-fuel capacity building course, 2/3 September, 2012 Tokyo Institute of Technology, Japan
2 Introduction 2 CO 2 has attracted unfavorable attention as one of the greenhouse gases, which is the main cause of global warming. O 2 /CO 2 combustion (oxy-fuel combustoin) is seen as one of the major options for CO 2 capture for future clean technologies. Caprock CO 2 transport Coal firing plant Saline aquifer CO 2 Fig. Schematic diagram of CCS
3 Introduction 3 Air Coal O 2 ASU (Air Separation Unit) Over 95% of CO 2 Boiler Flue gas treatment Recycled gas Fig. Exhaust gas concentration Fig. Oxy-fuel combustion and CCS system CO 2 capture Direct CO 2 recovery becomes possible without additional energy consumption. Another approach for reducing CO 2 emission is the use of renewable fuels such as biomass CO 2 N 2 O 2
4 Introduction 4 CO 2 Coal/Biomass or Biomass Air ASU (Air Separation Unit) O 2 Over 95% of CO 2 Boiler Recycled gas Fig. Exhaust gas concentration Flue gas treatment Fig. Oxy-fuel combustion and CCS system CO 2 capture O 2 /CO 2 biomass combustion with CCS can be used as a sink for CO 2. O 2 /CO 2 coal or biomass combustion is a promising technology for reducing CO 2 emission N 2 O 2
5 5 Introduction Small scale facilities are useful for fundamental mechanism clarification of O 2 /CO 2 combustion Demonstration plant Small experimental facilities Scaledown Cylinder of CO 2 Cylinder of Ar Vacuum pump Flow meter Reaction tube Infrared furnace Valve Valve Valve PC To tar trap Biomass sample Thermometric point P Pressure gauge
6 6 Introduction What are differences between O 2 /N 2 and O 2 /CO 2 combustion? Recycling process High CO 2 concentration Heat transfer characteristics (Thermophysical Properties of CO 2 ) CO 2 chemical reactivity CO 2 is not inert but participates in chemical reactions primarily through the reaction (CO 2 + H = CO + OH)
7 Introduction 7 By using CO 2 chemical reactivity, clean coal technology for oxy-fuel combustion is potentially developed Mechanism clarification through fundamental research is required High CO 2 concentration Minerals (Na,,) Coal or biomass CO 2 chemical reactivity affects gas/solid phase reaction Gas phase reaction Volatile-N NO or N 2 Solid phase reaction Carbonate formation (Na 2 CO 3 )
8 8 Introduction Our laboratory has used different experimental facilities and calculation for mechanism clarification of O 2 /CO 2 coal and biomass combustion Flat flame reactor, Drop tube furnace, TGA Detailed chemical reaction kinetics Flat flame Cylinder of CO 2 Flow meter Reaction tube Infrared furnace Valve To tar trap Biomass sample Valve Cylinder of Ar Thermometric point Primary gas (CH 4, O 2, CO 2, NH 3 /Ar) Vacuum pump Valve PC P Pressure gauge Fig. Flat flame reactor Fig. Drop tube furnace Fig. Thermobalance
9 9 Table of contents Effect of CO 2 on gas phase reactions Ultra-low NO x emission by using CO 2 chemical reactivity Effect of CO 2 on solid phase reaction Salt formation during biomass pyrolysis Summary
10 10 Table of contents Effect of CO 2 on gas phase reactions Ultra-low NO x emission by using CO 2 chemical reactivity Effect of CO 2 on solid phase reaction Salt formation during biomass pyrolysis Summary
11 11 Ultra-low NO x emission Uniform field Low NO x emission Recycles gas (Mainly CO 2 including NO x ) Fig. NO x conversion ratio in O 2 /CO 2 combustion [1] NO x emission decreased to 1/7 owing to recycling process when equivalent ratio is assumed to be uniform O 2 /CO 2 combustion has potential for reducing further NO x emission by combined with staged combustion [1] Liu and Okazaki, Fuel 2003
12 Ultra-low NO x emission 12 NO x, HCN and NH 3 formation are inhibited in fuel-rich region Primary gases Coal with gases Secondary gases Fuelrich Fuellean Air ratio (excess O 2 ratio) High Low High conc. of CO 2 Fig. Staged combustion (without recycling NO x ) The effect of high CO 2 concentration on NO x formation and reduction mechanisms under staged combustion is discussed
13 13 Contents This research NO x formation and reduction mechanism in staged O 2 /CO 2 combustion and air combustion were investigated. A flat CH 4 flame doped with NH 3 for fuel-n was used, and measurements were performed. CHEMKIN-PRO was used to investigate a detailed NO x reduction mechanism
14 Flat flame reactor 14 A large part of the fuel conversion in the combustion process occurs in the gas phase Flat flame Honeycomb Quartz tube Primary gas (CH 4, O 2, CO 2, NH 3 /Ar) Fig. Flat flame reactor Flat flame is very useful for one-dimensional analysis and mechanism clarification of gas phase reactions
15 Exhaust Flow Meter Chemiluminescent NO x detector Primary combustion GC Pump Silica-gel Cold Trap Exhaust Insulator Quarts Tube Flow Controllers Flat flame Primary gas (Air, CH 4, NH 3 or O 2, CO 2, CH 4, NH 3 ) Air CH 4 CO 2 O 2 comp- NH 3 ressor (Ar) Fig. Schematic diagram of experimental apparatus Pre-heater Ceramic honeycomb NO x, HCN, NH 3 emissions in air or O 2 /CO 2 combustion were investigated under primary combustion
16 Primary combustion 16 Flat flame Table 1 Experimental conditions (primary combustion) Initial O 2 conc. [vol. %] Initial NH 3 conc. [vol. %-CH 4 ] primary Primary gas (CH 4, Air, NH 3 /Ar.or. CH 4, O 2, CO 2, NH 3 /Ar) Air Oxy-fuel Primary combustion characteristics are important to discuss NO x emission in staged combustion. HCN, NH 3 (gas detector) and NO x emission of primary combustion were measured.
17 OH radical measurement 17 OH radicals are relevant with NH 3 and HCN formation and decompositon. OH* chemiluminescence images of flat flame was acquired by ICCD camera Interference filter (306.3 nm) 26 p = 0.70 CCD camera Lens Flat flame SUS mesh (a) CCD camera with (b) Flat flame interference filter Fig. Schematic diagram of OH * measurement system Primary gas (CH 4, O 2, CO 2, NH 3 /Ar)
18 Exhaust Flow Meter Chemiluminescent NO x detector Flow Controllers Staged combustion GC Pump Silica-gel Cold Trap Secondary gas (Air or O 2 +CO 2 ) Exhaust Insulator Flat flame Primary gas (Air, CH 4, NH 3 or O 2, CO 2, CH 4, NH 3 ) Air CH 4 CO 2 O 2 comp- NH 3 ressor (Ar) Fig. Schematic diagram of experimental apparatus 26 Quarts Tube Pre-heater Ceramic honeycomb NO x reduction by staged combustion was investigated 18
19 Staged combustion 19 a Air ratio (excess O 2 ratio) F FO O 2 2 F F CH CH 4 4 st F : flow rate [l min -1 ] Secondary gas (Air or O 2, CO 2 ) 26 secondary a Secondary gas Flat flame primary 30 mm SUS mesh Ceramic honeycomb Primary gas (CH 4, O 2, CO 2, NH 3 /Ar) Fig. Mixing part Primary gas (CH 4, O 2, NH 3 /Ar) Fig. Flame photograph
20 Experiment conditions 20 Table 1 Experimental conditions (staged combustion) Air Oxy-fuel Initial O 2 conc. [vol. %] Initial NH 3 conc. [vol. %-CH 4 ] s = 1.2 s = 1.2 s = 1.2 p = 0.60 Secondary gas (Air or O 2, CO 2 ) Primary gas (CH 4, Air, NH 3 /Ar, or CH 4, O 2, CO 2, NH 3 /Ar) Nomenclature : : Air ratio or O 2 /CH 4 stoic. ratio Flat flame p = 0.65 Primary gas Flat flame p = 0.70 Primary gas Staged combustion experiments were performed by changing primary air ratio (excess O 2 ratio)
21 21 Results (staged combustion) s = 1.2 Secondary gas (Air or O 2, CO 2 ) primary 40 % decreased due to CO 2 reactivity Primary gas Fig. Experimental apparatus Primary O 2 /CH 4 stoic. ratio [-] Fig. NO x CR (Conversion Ratio) [2] [2] H. Watanabe et al. Combustion and Flame 2011 The lowest NO x CR of O 2 /CO 2 combustion is lower than that of air combustion by 40 %
22 Results (primary combustion) N-min = 0.7 N-min = O 2 /CH 4 stoic. ratio [-] Fig. 1 Air-fuel combustion O 2 /CH 4 stoic. ratio [-] Fig. 2 O 2 /CO 2 combustion HCN and NH 3 concentrations in O 2 /CO 2 combustion are quite low compared with those of air combustion [2] H. Watanabe et al. Combustion and Flame 2011
23 23 Results x 10 0 (a) Air combustion (b) O 2 /CO 2 combustion Fig. Measured OH * images at O 2 /CH 4 stoich. ratio stoich. of 0.7 OH* concentration is higher in O 2 /CO 2 combustion than in air combustion Fig. Measured profiles of OH * chemiluminescence at O 2 /CH 4 ratio of 0.7 The following reaction is progressed in O 2 /CO 2 combustion CO 2 + H CO + OH
24 Reactions related with OH 24 Reaction paths relevant with NH 3 and OH NH 3 + OH NH 2 + H 2 O NH 2 + OH NH + H 2 O NH + NO N 2 + OH Reaction paths relevant with HCN and OH HCN + OH HNCO + H HNCO + H NH 2 + CO OH radicals progress the decomposition of NH 3 and HCN
25 CHEMKIN-PRO calculation 25 Primary gas Mesh Flat flame One-dimensional plug flow reactor Temperature [K] [mm] Air Oxy Air Oxy Distance from mesh [mm] Fig. Temperature distribution NO x formation mechanisms in primary combustion were investigated with detailed chemical reaction kinetics (GRI-Mech 3.0) Table Calculation conditions O 2 /CH 4 stoich. ratio [-] 0.7 NH 3 conc. [vol. %-CH 4 ] 1.0
26 Fig. Predicted OH concentration distribution in O 2 /CO 2 combustion Calculation results (OH) 26 Mesh Flat flame Primary gas [mm] Calculation also shows that OH radicals in O 2 /CO 2 combustion is higher than in air combustion because of the reaction: CO 2 +H CO + OH
27 Results (primary combustion) 27 (a) Experiment (b) Calculation Fig. Exhaust NH 3, HCN, NO concentration ( = 0.7) [2] NH 3 and HCN are decomposed in O 2 /CO 2 combustion due to OH radical [2] H. Watanabe et al. Combustion and Flame 2011
28 Results (primary combustion) 28 (NO+HCN+NH 3 ) exhaust / NH 3,inlet [-] Exp. Total nitrogen-compounds emission (NO, HCN, NH 3 ) of O 2 /CO 2 combustion is lower than that of air combustion (NO+HCN+NH 3 ) exhaust / NH 3,inlet [-] Calc. 0 Air Oxy 0 Air Oxy Fig. The sum of exhaust NO, HCN and NH 3 concentration N 2 is easily formed during O 2 /CO 2 combustion
29 Reaction pathways 29 Calculation shows reaction pathways from NH 3 to N 2. NH formation by OH radical is important in N 2 formation Fig. Reaction pathways at primary = 0.6, total = 0.8 (X CO2,inlet = 0.70) [3] [3] H. Watanabe et al. Energy and Fuels 2012
30 Effect of OH radical 30 +OH HNO +O +OH +H NH 3 NH 2 NH +OH +H +NO +O +OH +NO N 2 O +H NO +OH N +NO N 2 Fig. Reaction paths related with N 2 formation Under fuel-rich condition HNO +OH +OH +O NO +OH +H NH 3 NH 2 NH N +OH +H +NO +NO +NO +O +OH N 2 O N +H 2 Fig. Reaction paths related with N 2 formation OH radical oxidizes NH, and converts to HNO OH radical contributes to NO formation when NH 3 does not remain OH radical produces NH, which is NO reduction agency OH radical contributes to N 2 formation when an amount of NH 3 remains
31 31 Conclusion (ultra-low NO x ) NO x formation mechanism in O 2 /CO 2 and air combustion was investigated experimentally and numerically. CO 2 chemical reactivity produced OH radical through (CO 2 + H CO + OH) The lowest NO x conversion ratio in O 2 /CO 2 staged combustion was lower than it in air staged combustion by 40 % due to CO 2 reactivity Reaction pathways from NH 3 to N 2 were revealed, and it was shown that OH radical contributed to N 2 formation when an amount of NH 3 remains
32 32 Table of contents Effect of CO 2 on gas phase reactions Ultra-low NO x emission by using CO 2 chemical reactivity Effect of CO 2 on solid phase reaction Salt formation during biomass pyrolysis Summary
33 33 Introduction Pyrolysis of solid fuel Pyrolysis occurs as the first step in solid combustion. Pyrolysis has been generally investigated under an inert gas such as N 2, Ar, He. Understanding pyrolysis under CO 2 is important for the design of O 2 /CO 2 biomass combustors Gas Solid fuel Tar Char Fig. Pyrolysis
34 34 Introduction What is pyrolysis difference between under inert gas and CO 2? Heat transfer characteristics (Themophysical properties of CO 2 ) Reaction of CO 2 with minerals (Ca, K, Na, Mg) Salt (carbonate) formation is expected. Heat CO 2 atomosphere Na, K,Ca Solid fuel Gas Tar Biomass ex.) Na 2 CO 3 Fig. Pyrolysis Char
35 35 Introduction This work Effect of CO 2 on pyrolysis process through mineral reactions is studied. Cellulose and lignin which are the main components of biomass are heated under CO 2, or Argon atmosphere Metal-depleted lignin is also used to investigate the effect of CO 2 on minerals in lignin The chemical composition of char is characterized by FT-IR (Fourier Transform Infrared Spectroscopy).
36 Experiment 36 Table 1 Ultimate analysis of sample (wt%) Sample C H N S Ash Cellulose Lignin (Alkali lignin) Metal depleted lignin When the metal-depleted lignin was prepared, metal was removed from the lignin by stirring a mixture of lignin, water, and ion-exchange resin Lignin stirring Separate, dry process Ion-exchange resin Metal depleted lignin
37 Experiment 37 Table 2 Ash composition [mg/g] Sample Na K Lignin (Alkali lignin) Metal depleted lignin Ash is removed by 80 % by ionexchange Lignin and metal depleted lignin were analyzed by using FT-IR No significant difference was observed between both samples except for -OH: -ONa Ion exchange -OH The difference is mineral content
38 Experiment 38 Cylinder of CO 2 Cylinder of Ar Vacuum pump Flow meter Reaction tube Infrared furnace Valve Valve Valve PC To tar trap Biomass sample Thermometric point P Pressure gauge Fig. Schematic diagram of thermobalance Table Experiment Surrounding conditions gas CO 2 or Ar Gas flow rate [l min -1 ] Heating rate [K s -1 ] 0.8 1, 10, 60 Thermogravimetric curve is measured. The surface chemistry of the char was investigated by FTIR
39 Results 39 [4] H. Watanabe et al. Proc. Combust. Inst. 2012, in press Weight fraction [mg/mg d.a.f.] Cellulose (Ash: 0 wt%) Weight fraction [mg/mg d.a.f.] Lignin (Ash: 18.2 wt%) Char-CO 2 reaction (> 1100 K) Temperature [K] Fig. Pyrolysis curves of cellulose (Ash: 0 wt%, Heating rate : 1 Ks -1 ) Temperature [K] Fig. Pyrolysis curves of lignin (Ash: 18.2 wt%, Heating rate : 1 Ks -1 ) Contrary to expectations, the weight of the lignin chars formed under CO 2 increased by about 10 % above 873 K
40 40 Results Weight fraction [mg/mg d.a.f.] Why increased? Lignin (Ash: 18.2 wt%) Temperature [K] Fig. Pyrolysis curves of lignin (Ash: 18.2 wt%, Heating rate : 1 Ks -1 ) CO 2 physical adsorption Carbonate formation have the potential to cause an increase in the weight fraction due to CO 2 Char weight does not change by a degassing procedure (5 kpa for 1 h). CO 2 physical adsorption is insignificant Carbonate is expected to be formed during pyrolysis
41 Results Weight fraction = Sample weight Initial weight of CaO 41 Minerals can react with CO 2, and salt form. (Ⅰ) CaO + CO 2 CaO CO 2 (Ⅱ) CaO CO 2 CaCO 3 (Ⅲ) CaCO 3 CaO + CO 2 Weight fraction [-] CaO heating under CO 2 (Ⅰ) (Ⅰ+Ⅱ) (Ⅲ) There is a possibility that Na or K in lignin reacts with CO 2, and Na 2 CO 3 and K 2 CO 3 are formed Temperature [K] Fig. Thermogravimetric curves of CaO (Heating rate : 1 Ks -1 )
42 Results 42 [4] H. Watanabe et al. Proc. Combust. Inst. 2012, in press Weight fraction [mg/mg d.a.f.] Lignin (Ash: 18.2 wt%) Metal-depleted Lignin (Ash: 3.2 wt%) Temperature [K] Temperature [K] Fig. Pyrolysis curves (Heating rate : 1 Ks -1 ) Mineral components in lignin react with CO 2, and carbonate is expected to be formed
43 FT-IR analysis 43 Weight fraction [mg/mg d.a.f.] Lignin (Ash: 18.2 wt%) Temperature [K] Fig. Pyrolysis curves of lignin (Ash: 18.2 wt%, Heating rate : 1 Ks -1 ) Surface chemistry of chars derived under CO 2 or Ar at 1073 K were investigated by FTIR to investigate carbonate formation. Na 2 CO 3 was also characterized by FTIR as reference
44 FT-IR 1450 cm -1 Aromatic C-C Carbonate 880 cm -1 Carbonate 44.] ụ [a ity s n te In Na 2 CO 3.] ụ [a ity s n te In Char derived from lignin (at 1073 K) Ar CO2 CO 2 Ar Wave number [cm -1 ] Fig. FTIR spectra of Na 2 CO 3 and char derived from lignin
45 FT-IR [4] H. Watanabe et al. Proc. Combust. Inst. 2012, in press 45.] ụ [a ity s n te In Ar CO cm -1 Table The atomic group and structures Ar CO 2 Wave number (cm -1 ) 1450 Atomic group and structures Aromatic C-C Carbonate Peak area corresponding to carbonate under CO 2 is almost twice of that under Ar Wave number [cm -1 ] Fig. FTIR spectra of chars focusing on 1450 cm -1 A salt such as Na 2 CO 3 or K 2 CO 3 is formed during lignin pyrolysis under CO 2
46 FT-IR 1730 cm -1 The difference of peaks for C=O appeared (1730 cm -1 ). 840 cm ] ụ [a ity s n te In Na 2 CO 3.] ụ [a ity s n te In Char derived from lignin (1073 K) Ar CO2 CO 2 Ar Wave number [cm -1 ] Fig. FTIR spectra of char derived from lignin and Na 2 CO
47 .] ụ [a s ity n te In Ar CO2 Results Ar CO Wave number [cm -1 ] Fig. FTIR of spectra focusing on C=O group (Char, 1073 K) Table The atomic structures Wave number (cm -1 ) Atomic group and structures C=O Over 1700 Below 1700 C=O groups which are not in conjunction with aromatic ring are only found in chars formed under CO 2 [4] H. Watanabe et al. Proc. Combust. Inst. 2012, in press C C O C O 47
48 Heating rate 48 Char yield [mg/mg d.a.f.] % 8 % Ar CO 2 7 % 1 Ks Ks Ks -1 Fig. Char yield derived from lignin of 1073 K Although, an increase in char yield under CO 2 declines with increasing heating rate, carbonate is formed at various heating rate
49 49 Mechanism Alkaline compounds highly favor the carbonization, dehydration, decarboxylation, and demethoxylation reactions, leading to a modified carboneous structures. Sodium ion is very small and it can penetrate into the biomass textures and break intermolecular hydrogen bridges under heating. Breaking the hydrogen bridges by carbonate compound seems to form C=O group not associated with an aromatic ring. Futher investigations are required to clarify more detailed catalytic mechanisms
50 Conclusion (carbonate) 50 In this study, the effect of CO 2 on pyrolysis was investigated. Cellulose, lignin, and metal-depleted lignin pyrolysis experiment were performed. Pyrolysis of lignin, but not that of cellulose and metaldepleted lignin, was affected by CO 2. The salts such as Na 2 CO 3 or K 2 CO 3 were formed during lignin pyrolysis under CO 2 It was suggested that these salts affected the char formation reaction, in that, char formed during lignin pyrolysis under CO 2 had unique chemical bands
51 51 Table of contents Effect of CO 2 on gas phase reactions Ultra-low NO x emission by using CO 2 chemical reactivity Effect of CO 2 on solid phase reaction Salt formation during biomass pyrolysis Summary
52 52 Summary In this presentation, unique CO 2 characteristics such as OH radical and carbonate formation were presented. Under specific condition, OH radical formed by CO 2 reactivity can be used for low-no x emission. Carbonate was found during lignin pyrolysis under CO 2, while it was not found in air combustion.
53 Thank you very much for your kind attention
Clarification of gasification behavior of solid fuel char prepared under CO 2 atmosphere
3rd Oxyfuel Combustion Conference Ponferrada, Spain Technical session 3c Clarification of gasification behavior of solid fuel char prepared under CO 2 atmosphere Tokyo Institute of Techonology Kiyomi SHIMOMURA*
More informationEffect of gasifying agents and their partial pressure on the gasification rate of Shengli brown coal
Effect of gasifying agents and their partial pressure on the gasification rate of Shengli brown coal Shu Zhang, Xujun Chen, Xueying Zhang, Yonggang Wang*, Deping Xu School of Chemical and Environmental
More informationStudy on catalytic pyrolysis and efficient gasification of cellulose as biomass samples
Energy and Sustainability VI 27 Study on catalytic pyrolysis and efficient gasification of cellulose as biomass samples Q. Wang 1, T. Watanabe 1, R. Ogawa 1, P. Aparu 1 & K. Sugiyama 2 1 Graduate School
More informationElemental Analysis (EA)
Elemental Analysis Elemental Analysis (EA) - Weight percentages of C, H, N, S done by combustion in O 2 - Gas chromatographic analysis of CO 2, H 2 O and N 2, SO 2 - Oxygen as CO - Other elements such
More informationN 2 O Decomposition by CaO under Conditions of Carbonator of Calcium Looping Cycle
1 71 st IEA-FBC, Seoul, Korea, Nov.4-6, 2015 N 2 O Decomposition by CaO under Conditions of Carbonator of Calcium Looping Cycle T. Shimizu,, S. Sizuno, K. Ito, R. Houshito, H.j. Kim, L.y. Li Niigata 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 informationPulverised Coal Pyrolysis and Char Combustion Characteristics in Simulated Air (O 2 /N 2 ) and Oxy-fuel (O 2 /CO 2 ) Conditions
1 st Oxy-fuel Combustion Conference, Cottbus, Germany - 9 September 29 Pulverised Coal Pyrolysis and Char Combustion Characteristics in Simulated Air (O 2 /N 2 ) and Oxy-fuel (O 2 /CO 2 ) Conditions Renu
More informationDevelopment and optimization of a two-stage gasifier for heat and power production
Journal of Physics: Conference Series PAPER OPEN ACCESS Development and optimization of a two-stage gasifier for heat and power production Related content - Design and implementation of a laserbased absorption
More informationCatalytic gasification of biomass for hydrogen production with in-situ CO 2 absorption using novel bi-functional Ni-Mg-Al-CaO catalyst
School Energy of Research something Institute OTHER Catalytic gasification of biomass for hydrogen production with in-situ CO 2 absorption using novel bi-functional CaO catalyst Mohamad Anas Nahil, Chunfei
More informationAsian Journal on Energy and Environment ISSN Available online at
As. J. Energy Env. 2006, 7(03), 347-355 Asian Journal on Energy and Environment ISSN 1513-4121 Available online at www.asian-energy-journal.info Pyrolysis Characteristics of Blends of Agricultural Residues
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 informationCZESTOCHOWA UNIVERSITY OF TECHNOLOGY
CZESTOCHOWA UNIVERSITY OF TECHNOLOGY Faculty of Environmental Engineering and Biotechnology Institute of Advanced Energy Technologies 3rd Oxyfuel Combustion Conference September 9-13 th 2013 Ponferrada,
More informationFINAL REPORT. Participants in the reported tasks 1. Ravi Subramanian 2. Manoranjan Misra 3. Kent Hoekman
FINAL REPORT Subtask 2.2.1: Solar thermal hydrogen production Duration of the Project: October 01 2009 - Dec 31, 2010 Date of Final Report Submission: January 24, 2011 Primary Lead contact Vaidyanathan
More informationLICONOX Linde s new technology for removal of NOx and SOx integrated in the CO 2 processing unit
2 nd Oxyfuel Combustion Conference LICONOX Linde s new technology for removal of NOx and SOx integrated in the CO 2 processing unit Roland Ritter a *, Nicole Schödel b, Florian Winkler b a LINDE-KCA Dresden
More informationThree-dimensional modelling of steam-oxygen gasification in a circulating fluidized bed
Lappeenranta University of Technology From the SelectedWorks of Kari Myöhänen June, 2012 Three-dimensional modelling of steam-oxygen gasification in a circulating fluidized bed Kari Myöhänen, Lappeenranta
More informationSynthesis of silicon carbide from coal fly ash and activated carbon powder
Material Science Research India Vol. 6(2), 251-256 (2009) Synthesis of silicon carbide from coal fly ash and activated carbon powder SULARDJAKA¹, JAMASRI¹, M.W. WILDAN¹ and KUSNANTO² ¹Department of Mechanical
More informationPower-Cost Alternative De-NOx Solutions for Coal-Fired Power Plants
Power-Cost Alternative De-NOx Solutions for Coal-Fired Power Plants 12/21/2015 Power Engineering By Bin Xu, David Wilson, and Rob Broglio Traditionally, large coal-fired generating units have complied
More informationEffect of Pressure and Heating Rates on Biomass Pyrolysis and Gasification
Effect of Pressure and Heating Rates on Biomass Pyrolysis and Gasification Pradeep K. Agrawal School of Chemical and Biomolecular Engineering Georgia Institute of Technology June 15, 2012 Auburn University
More informationNOx processing experiences for removal in the CO 2 plant for the Oxyfuel combustion process
NOx processing experiences for removal in the CO 2 plant for the Oxyfuel combustion process Roland Ritter, Torsten Stoffregen, Linde Engineering Dresden GmbH Nicole Schödel, Florian Winkler, Linde Engineering
More informationGasification Research at OSU
Gasification Research at OSU Ajay Kumar, Assistant Professor Biobased Products and Energy Center (BioPEC), Biosystems and Agricultural Engineering, Oklahoma State University OK EPSCoR Annual State Conference
More informationMikko Hupa Åbo Akademi Turku, Finland
Åbo Akademi Chemical Engineering Department Course The Forest based Biorefinery Chemical and Engineering Challenges and Opportunities May 3-7, 2010 Thermal conversion of biomass Mikko Hupa Åbo Akademi
More informationATTRITION OF LIGNITE CHAR DURING FLUIDIZED BED GASIFICATION: EXPERIMENTAL AND MODELING STUDIES. Paola Ammendola and Fabrizio Scala
ATTRITION OF LIGNITE CHAR DURING FLUIDIZED BED GASIFICATION: EXPERIMENTAL AND MODELING STUDIES Paola Ammendola and Fabrizio Scala Introduction The The urgent need need to to capture and and sequester CO
More informationSteam Gasification of Low Rank Fuel Biomass, Coal, and Sludge Mixture in A Small Scale Fluidized Bed
Steam Gasification of Low Rank Fuel Biomass, Coal, and Sludge Mixture in A Small Scale Fluidized Bed K.H. Ji 1, B.H. Song *1, Y.J. Kim 1, B.S. Kim 1, W. Yang 2, Y.T. Choi 2, S.D. Kim 3 1 Department of
More informationA reduced chemical kinetics mechanism for NOx emission prediction in biomass combustion
A reduced chemical kinetics mechanism for NOx emission prediction in biomass combustion Ehsan Houshfar 1 Øyvind Skreiberg 2 Peter Glarborg 3 Terese Løvås 1 1 Norwegian University of Science and Technology
More informationThe Novel Design of an IGCC System with Zero Carbon Emissions
1621 A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 61, 2017 Guest Editors: Petar S Varbanov, Rongxin Su, Hon Loong Lam, Xia Liu, Jiří J Klemeš Copyright 2017, AIDIC Servizi S.r.l. ISBN 978-88-95608-51-8;
More informationFuel Analysis and Burning Characteristics
Fuel Analysis and Burning Characteristics Fuel Analysis and Burning Characteristics - Terms and Concepts Particle burning stages: drying - devolatilization char Proximate & ultimate analysis Heating value
More informationCOMPARATIVE BEHAVIOUR OF AGRICULTURAL BIOMASS RESIDUES DURING THERMOCHEMICAL PROCESSING
Global NEST Journal, Vol 14, No 2, pp 111-117, 2012 Copyright 2012 Global NEST Printed in Greece. All rights reserved COMPARATIVE BEHAVIOUR OF AGRICULTURAL BIOMASS RESIDUES DURING THERMOCHEMICAL PROCESSING
More informationSTUDIES ON NUCLEAR COAL GASIFICATION IN ARGENTINA
STUDIES ON NUCLEAR COAL GASIFICATION IN ARGENTINA D. Nassini (1), G.G. Fouga (1,2), G. De Micco (1,2) H.E. Nassini (2) and A.E. Bohé (1,2) (1) Consejo Nacional de Investigaciones Científicas y Técnicas
More informationExperience of Operating a Small Pilot-Scale Oxy-Fuel CFB Test Rig
2 nd International Oxyfuel Combustion Conference September 12-16, 2011 Yeppoon, Queensland, Australia Experience of Operating a Small Pilot-Scale Oxy-Fuel CFB Test Rig Tomasz CZAKIERT, Marcin Klajny, Waldemar
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 informationStructure of atmospheric pressure premixed hydrogen-oxygen flame doped with iron pentacarbonyl
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
More informationChanges in combustion properties of Natural gas when mixed with Hydrogen
Changes in combustion properties of Natural gas when mixed with Hydrogen PARISA SAYAD, ALESSANDRO SCHÖNBORN AND JENS KLINGMANN DEPARTMENT OF ENERGY SCIENCES, LUND UNIVERSITY PARISA.SAYAD@ENERGY.LTH.SE
More informationMini converter carbons and wastes for Biogas production and Energy Cogeneration model «ПТК-52»
Mini converter carbons and wastes for Biogas production and Energy Cogeneration model «ПТК-52» Team: System processing of raw materials, thermochemical conversion reactor. Features: the team is a model
More informationGasification of Non-Coking Coals
International Conference of Advance Research and Innovation (-2014) Gasification of Non-Coking Coals Akanksha Mishra a,*, Shalini Gautum b, Tripurari Sharma a a Department of Mechanical & Automobile Engineering,
More informationDevelopment of a novel reformer for tar-free syngas production
Available online at www.sciencedirect.com ScienceDirect Energy Procedia 75 (2015 ) 246 251 The 7 th International Conference on Applied Energy ICAE2015 Development of a novel reformer for tar-free syngas
More informationMETHOD 3 - GAS ANALYSIS FOR THE DETERMINATION OF DRY MOLECULAR WEIGHT. NOTE: This method does not include all of the
312 METHOD 3 - GAS ANALYSIS FOR THE DETERMINATION OF DRY MOLECULAR WEIGHT NOTE: This method does not include all of the specifications (e.g., equipment and supplies) and procedures (e.g., sampling) essential
More informationCo-combustion of Lignite with Biochar
Co-combustion of Lignite with Jale Yanik, Asli Toptas, Yeliz Yildirim Department of Chemistry, Faculty of Science, Ege University, 351 Izmir,Turkey General Aspects Aim Materials and Methods Results Conclusion
More informationThe Effects of Increased Pressure on the Reaction Kinetics of Biomass Pyrolysis and Combustion
The Effects of Increased Pressure on the Reaction Kinetics of Biomass Pyrolysis and Combustion Charles Churchman, P.E. Stephanie England, E.I.T. International Applied Engineering, Inc. Marietta, Georgia
More informationCOGENERATION POSIBILITIES WITH THE ARGENTINEAN MODULAR NUCLEAR POWER REACTOR CAREM
Technical Meeting to Examine the Techno- Economics Opportunities for Non-Electric Applications of Small and Medium Sized or Modular Reactors COGENERATION POSIBILITIES WITH THE ARGENTINEAN MODULAR NUCLEAR
More informationTrace Moisture Contamination in Ultra-High Purity Phosphine: Techniques for Measurement and Control
Trace Moisture Contamination in Ultra-High Purity Phosphine: Techniques for Measurement and Control M. Raynor, H. Funke, J. Yao, T. Watanabe and R. Torres, Matheson Tri-Gas, Advanced Technology Center,
More informationSTEAM GASIFICATION OF LOW RANK COAL CHARS IN A THERMOBALANCE REACTOR AND A FLUIDIZED BED REACTOR
Refereed Proceedings The 13th International Conference on Fluidization - New Paradigm in Fluidization Engineering Engineering Conferences International Year 2010 STEAM GASIFICATION OF LOW RANK COAL CHARS
More informationCleaning biomass generated syngas: is biochar a cheaper alternative to expensive catalysts? Ajay Kumar Oklahoma State University
Cleaning biomass generated syngas: is biochar a cheaper alternative to expensive catalysts? Ajay Kumar Oklahoma State University Biomass Feedstocks Biofuels through Thermochemical Conversions Characterization
More informationMIT Carbon Sequestration Forum VII Pathways to Lower Capture Costs
MIT Carbon Sequestration Forum VII Pathways to Lower Capture Costs 1 October 1 November 2006 Royal Sonesta Hotel, Cambridge, MA Oxyfuel Pathways Rodney Allam Consultant Air Products PLC, UK Oxyfuel Technology
More informationREDUCTION OF NITRIC OXIDE ON THE CHAR SURFACE AT PULVERIZED COMBUSTION CONDITIONS
Proceedings of the Combustion Institute, Volume 29, 2002/pp. 2275 2281 REDUCTION OF NITRIC OXIDE ON THE CHAR SURFACE AT PULVERIZED COMBUSTION CONDITIONS ALEJANDRO MOLINA, ERIC G. EDDINGS, DAVID W. PERSHING
More informationPlastic to Fuel Technologies
Plastic to Fuel Technologies Author: Mauro Capocelli, Researcher, University UCBM Rome (Italy) 1. Theme description The growth of economy and consumes, combined with the modern models of production, have
More informationKinetic Study of Oil Shale Conversion
Kinetic Study of Oil Shale Conversion Pankaj Tiwari Dr. Milind Deo Dr. Eric Eddings Chemical Engineering Dept, University of Utah Table of contents Background Previous studies Surface retorting Shell s
More informationUS-DOE Patent Clearance is not required prior to the publication of this document.
Technical Progress Report Rate nhibition of Steam Gasification by Adsorbed Hydrogen DOE Grant ifde-fg22-93pc93213 Reporting Period: 1/1/95-12/31/95 Dennis J. Miller, Principal nvestigator US-DOE Patent
More informationGASIFICATION OF BIOMASS CHAR OBTAINED VIA PYROLYSIS
GASIFICATION OF BIOMASS CHAR OBTAINED VIA PYROLYSIS D. López-González, M. Fernández-López, J.L. Valverde and L. Sánchez-Silva 1 * Department of Chemical Engineering. University of Castilla-La Mancha. Spain
More informationExperimental Investigation of the Entrained Flow Gasification of a Bituminous Coal and a Lignite
Experimental Investigation of the Entrained Flow Gasification of a Bituminous Coal and a Lignite M.Sc. Andreas Geißler, M.Sc. Markus Steibel, M.Sc. Federico Botteghi, Prof. Hartmut Spliethoff Institute
More informationSMS 100 MERCURY ANALYZER SMS 100. Mercury analysis directly on solid samples from the undisputed leader in Atomic Spectroscopy
SMS 100 MERCURY ANALYZER SMS 100 Mercury analysis directly on solid samples from the undisputed leader in Atomic Spectroscopy SMS 100 Overview The SMS 100 is a dedicated mercury analyzer for the determination
More informationCatalytic Activated Ceramic Dust Filter a new technology for combined removal of dust, NOx, dioxin, VOCs and acids from off gases.
Catalytic Activated Ceramic Dust Filter a new technology for combined removal of dust, NOx, dioxin, VOCs and acids from off gases. * Presenting author Peter Schoubye and Joakim Reimer Jensen *, Haldor
More informationAbout Praxair. Air Separation. Applications. our purpose. 1 Where your talent makes an impact
About Praxair Air Separation Applications our purpose 1 Where your talent makes an impact who we are 2 Where your talent makes an impact Energy Metals Chemicals Manufacturing Electronics Food Healthcare
More informationSTUDIES ON NUCLEAR HYDROGEN PRODUCTION BY STEAM COAL GASIFICATION IN ARGENTINA
Technical Meeting to Examine the Role of Nuclear Hydrogen Production in the Context of Hydrogen Economy STUDIES ON NUCLEAR HYDROGEN PRODUCTION BY STEAM COAL GASIFICATION IN ARGENTINA G.G. Fouga, D. Nassini,
More informationCatalytic Pyrolysis of Lignin for Bio oils
Catalytic Pyrolysis of Lignin for Bio oils Haoxi Ben and Arthur Ragauskas Georgia Institute of Technology Institute of Paper Science and Technology http://www.eia.doe.gov http://www.nrel.gov 2 Kraft Pulp
More informationSensors and Instrumentation Systems for Oxy-Coal Combustion Diagnosis -- Updates for the EPSRC-EON OxyCAP Project in Kent
Sensors and Instrumentation Systems for Oxy-Coal Combustion Diagnosis -- Updates for the EPSRC-EON OxyCAP Project in Kent Y. Yan, G. Lu, M. M. Hossain, D. Sun and L. Gao Instrumentation, Control and Embedded
More informationName of Process: Vendor: Applicable Pesticides and related POPs wastes: Technology description:
Name of Process: Vacuum Heating Decomposition Vendor: Hoei-Shokai Co.Ltd Web site: http:// www.hoei-shokai.co.jp Applicable Pesticides and related POPs wastes: Applicable chemicals: DXNs, PCBs, BHC, Chlordane,
More informationWRI S PRE GASIFICATION TREATMENT OF PRB COALS FOR IMPROVED ADVANCED CLEAN COAL GASIFIER DESIGN
WRI S PRE GASIFICATION TREATMENT OF PRB COALS FOR IMPROVED ADVANCED CLEAN COAL GASIFIER DESIGN SER Contract No. WY49975WRI Dr. Al Bland Western Research Institute FINAL EXECUTIVE SUMMARY REPORT WRI S PRE
More informationDETERMINATION OF THE FORMS OF NITROGEN RELEASED IN COAL TAR DURING RAPID DEVOLATILIZATION. Draft Semi-Annual Report
DETERMINATION OF THE FORMS OF NITROGEN RELEASED IN COAL TAR DURING RAPID DEVOLATILIZATION Draft Semi-Annual Report Principal Investigator: Thomas H. Fletcher Grant No. DE-FG22-95PC95215-06 Chemical Engineering
More informationFuels. N4 & N5 Homework Questions
St Peter the Apostle High school Chemistry Department Fuels N4 & N5 Homework Questions Answer questions as directed by your teacher. National 4 level questions are first followed by National 5 level questions.
More informationControl of pollutants in flue gases and fuel gases
Control of pollutants in flue gases and fuel gases Ron Zevenhoven Helsinki University of Technology, Espoo, Finland Pia Kilpinen Åbo Akademi University, Turku, Finland sponsored / funded by The Nordic
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 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 informationOptimal Design and Operation of SNCR System for a 150t/h CFB Boiler and Discussion on the Measurement of Flue Gas Components
Optimal Design and Operation of SNCR System for a 150t/h CFB Boiler and Discussion on the Measurement of Flue Gas Components Yang Hairui Tsinghua University 66 th IEA-FBC meeting 18-20, March, 2013 Brno,
More informationNumerical Modeling of Urea Injection and NO Emission in a Stoker Boiler
Paper # 070CO-0196 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 informationLow volatile coal combustion under oxy-fuel atmosphere
Low volatile coal combustion under oxy-fuel atmosphere A. G. Borrego 1, D. Alvarez 1, I. Fernández-Dominguez 1, J.C. Ballesteros 2, R. Menéndez 1 1 Instituto Nacional del Carbón, CSIC. P.O. Box 73, 33080
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 informationExperimental study assessment of mitigation of carbon formation on Ni/YSZ and Ni/CGO SOFC anodes operating on gasification syngas and tars
Experimental study assessment of mitigation of carbon formation on Ni/YSZ and Ni/CGO SOFC anodes operating on gasification syngas and tars Clean Coal Technologies Conference 2009 19 May 2009 Joshua Mermelstein
More informationDEVELOPMENT OF WET-OXIDATION TREATMENT SYSTEM FOR FILTER BACKWASH SLUDGE AND ION EXCHANGE RESINS
DEVELOPMENT OF WET-OXIDATION TREATMENT SYSTEM FOR FILTER BACKWASH SLUDGE AND ION EXCHANGE RESINS T. Miyamoto, M. Motoyama, M. Shibuya JGC Corporation 2-3-1, Minato Mirai, Nishi-ku, Yokohama, 220-6001,
More informationIntroduction: Thermal treatment
Thermal Treatment 2 Introduction: Thermal treatment Technologies using high temperatures to treat waste (or RDF) Commonly involves thermal combustion (oxidation) Reduces waste to ash (MSW c. 30% of input)
More informationSimulation of Flameless Combustion of Natural Gas in a Laboratory Scale Furnace
Turkish J. Eng. Env. Sci. 30 (2006), 135 143. c TÜBİTAK Simulation of Flameless Combustion of Natural Gas in a Laboratory Scale Furnace Sébastien MURER, Barbara PESENTI and Paul LYBAERT Thermal Engineering
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 informationTGA testing of biomass char gasification Antero Moilanen
TGA testing of biomass char gasification Antero Moilanen Finnish-Swedish Flame Days 2013 Gasification Workshop Paviljonki, Jyväskylä, 17th 18th of April 2013 2 Biomass fuel as feedstock Fuel is fed to
More informationLaser measurement of KCl vapor in 4 MW CFB boiler during straw combustion and ferric sulfate injection
Laser measurement of KCl vapor in 4 MW CFB boiler during straw combustion and ferric sulfate injection Juha Toivonen, Tapio Sorvajärvi Department of Physics, Tampere University of Technology, P.O. Box
More informationTA INSTRUMENTS THERMOGRAVIMETRIC ANALYZERS
TA INSTRUMENTS THERMOGRAVIMETRIC ANALYZERS TA INSTRUMENTS Q SERIES THERMOGRAVIMETRIC ANALYZERS Sensitive, Precise, Rugged and Automated are words that describe a TA Instruments Thermogravimetric Analyzer.
More informationDimitra Zaharaki 1, Kostas Komnitsas 1 and Georgios Bartzas 2
Dimitra Zaharaki 1, Kostas Komnitsas 1 and Georgios Bartzas 2 1 School of Mineral Resources Engineering, Technical University of Crete, Chania, 73100, Greece 2 School of Mining and Metallurgical Engineering,
More informationEXPERIENCE WITH ATMOSPHERIC FLUIDIZED BED GASIFICATION OF SWITCHGRASS. Jerod Smeenk and Robert C. Brown
EXPERIENCE WITH ATMOSPHERIC FLUIDIZED BED GASIFICATION OF SWITCHGRASS Jerod Smeenk and Robert C. Brown Center for Coal and the Environment Iowa State University 286 Metals Development Building Ames, IA
More informationBiomass Pyrolysis and Gasification of Different Biomass Fuels
8 th U.S. National Combustion Meeting Organized by the Western States Section of the Combustion Institute And hosted by the University of Utah May 19-22, 213 Biomass Pyrolysis and Gasification of Different
More informationField-test at Betonstal Sp. z.o.o. Szczecin/ Poland
Field-test at Betonstal Sp. z.o.o. Szczecin/ Poland M. Schmidt, R. Brandenburg, A. Schwock Executive Summary Field experiments were performed in order to investigate the feasibility of the removal of gaseous
More informationFully Extractive Vs. Dilution Extractive CEMS
Fully Extractive Vs. Dilution Extractive CEMS Cemtek Environmental Emissions Seminar & Training Session Santa Ana, CA a technical solution to meet every need CEMTEK Environmental Inc. 3041 S. Orange Ave.
More informationHigh-efficiency low LCOE combined cycles for sour gas oxy-combustion with CO[subscript 2] capture
High-efficiency low LCOE combined cycles for sour gas oxy-combustion with CO[subscript 2] capture The MIT Faculty has made this article openly available. Please share how this access benefits you. Your
More informationThe Role of Structure and Composition in Gasification Reactivity of Biomass Char
The Role of Structure and Composition in Gasification Reactivity of Biomass Char Gautami Newalkar 1, Kristiina Iisa 2, Carsten Sievers 1 and Pradeep K. Agrawal 1 1 School of Chemical & Biomolecular Engineering,
More informationProduction of synthesis gas from liquid or gaseous hydrocarbons, and the synthesis gas per se, are covered by group C01B 3/00.
C10J PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES (synthesis gas from liquid or gaseous hydrocarbons C01B; underground gasification
More informationS.E. (Chemical) (First Semester) EXAMINATION, 2012 PROCESS CALCULATIONS (2008 PATTERN) Time : Three Hours Maximum Marks : 100
Total No. of Questions 12] [Total No. of Printed Pages 8 Seat No. [4162]-185 S.E. (Chemical) (First Semester) EXAMINATION, 2012 PROCESS CALCULATIONS (2008 PATTERN) Time : Three Hours Maximum Marks : 100
More informationRole of Gasification in a Bio-Based Future
Role of Gasification in a Bio-Based Future A. van der Drift June 2015 ECN-L--15-063 ROLE of GASIFICATION in a BIO-BASED FUTURE Bram van der Drift 2 June 2015 European Biomass Conference, Vienna www.ecn.nl
More informationThe Role of Solid Fuel Conversion in Future Power Generation
The Role of Solid Fuel Conversion in Future Power Generation Hartmut Spliethoff FINNISH-SWEDISH FLAME DAYS 2013 Focus on Combustion and Gasification Research Jyväskylä, April, 17th and 18th 2013 Content
More informationLignite oxidative desulphurization. Notice 2: effects of process parameters
Int J Coal Sci Technol (2015) 2(3):196 201 DOI 10.1007/s40789-015-0056-3 Lignite oxidative desulphurization. Notice 2: effects of process parameters Volodymyr Gunka 1 Serhiy Pyshyev 1 Received: 18 July
More informationMethods for determination of mercury in LP gas
(JLPGA-S-07) Methods for determination of mercury in LP gas 1. Scope This standard specifies the methods for determination of gaseous mercury in vaporized liquid liquefied petroleum (LP) gas. Remarks 1
More informationTreatment Technologies
Treatment Technologies Precipitation Softening INTRODUCTION CHEMISTRY OF PRECIPITATION SOFTENING COLD LIME SOFTENING WARM LIME SOFTENING HOT PROCESS SOFTENING SILICA REDUCTION REDUCTION OF OTHER CONTAMINANTS
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. Mitchell, Associate Professor, Mechanical Engineering; Paul A. Campbell and Liqiang Ma, Graduate
More informationDiode laser analyser LS4000 Ammonia slip measurement for DeNOx process
ABB MEASUREMENT & ANALYTICS APPLICATION NOTE Diode laser analyser LS4000 Ammonia slip measurement for DeNOx process Optimize efficiency of denitrification process in DeNOx unit. Reduce downstream problems,
More informationThermogravimetry Study on Pyrolysis of Various Lignocellulosic Biomass for Potential Hydrogen Production
Thermogravimetry Study on Pyrolysis of Various Lignocellulosic Biomass for Potential Hydrogen Production S.S. Abdullah, S. Yusup, M.M. Ahmad, A. Ramli, L. Ismail Abstract This paper aims to study decomposition
More informationWORLD CONGRESS ON INDUSTRIAL BIOTECHNOLOGY
WORLD CONGRESS ON INDUSTRIAL BIOTECHNOLOGY CONCORD BLUE REFORMER Deriving a Synthetic Gas Building Block from Waste Scott A. Noll, Ph.D. Vice President-Project Management Concord Blue USA, Inc. 12424 Wilshire
More informationOnline Gas Analyzer / Monitor
Sheet No. 1 of 9 CH4 H2 SOX NOX NH3 CO2 HF HCL HCN CO O2 Providing the latest in Combustion Gas & Emission Analyzers for Boiler, Engine, Furnace, and other applications. Sheet No. 2 of 9 Vasthi OMGA 8000
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 informationMolten Salt Reactors in Gasification and Gas Purification
Molten Salt Reactors in Gasification and Gas Purification Presenting author: Ville Nikkanen Place: 6 th International Freiberg Conference on IGCC & XtL Technologies Dresden, Germany Time: 19 th of May
More informationFormation of Fine Particulate Matter in a Domestic Pellet-Fired Boiler. José Madeira
Formation of Fine Particulate Matter in a Domestic Pellet-Fired Boiler José Madeira Abstract This article concentrates on the formation of fine particulate matter (PM) in a domestic pellet-fired boiler.
More informationHow do I make a basic combustion characterisation of biofuel?
Combustion File No: 24 Version No: 1 How do I make a basic combustion characterisation of biofuel? Date: Author(s): Source(s): Referee(s): Status: Sponsor: 5-Nov-1 Johan Hustad/Maria Barrio Authors Peter
More informationTwo-stage Gasification of Untreated and Torrefied Wood
133 A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 50, 2016 Guest Editors: Katharina Kohse-Höinghaus, Eliseo Ranzi Copyright 2016, AIDIC Servizi S.r.l., ISBN 978-88-95608-41-9; ISSN 2283-9216
More informationVisualization and Control of Particulate Contamination Phenomena in a Plasma Enhanced CVD Reactor
Visualization and Control of Particulate Contamination Phenomena in a Plasma Enhanced CVD Reactor Manabu Shimada, 1 Kikuo Okuyama, 1 Yutaka Hayashi, 1 Heru Setyawan, 2 and Nobuki Kashihara 2 1 Department
More informationCOMBUSTION AND GASIFICATION RATES OF LIGNOCELLULOSIC CHARS (submitted for publication in Progress in Energy and Combustion Science
COMBUSTION AND GASIFICATION RATES OF LIGNOCELLULOSIC CHARS (submitted for publication in Progress in Energy and Combustion Science Colomba Di Blasi Dipartimento di Ingegneria Chimica, Università degli
More information