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Record of Decision; JEA Circulating Fluidized Bed Combustor Project
76614 Federal Register / Vol. 65, No. 236 / Thursday, December 7, 2000 / Notices Recordkeeping burden. OMB invites would be cost-shared by DOE and JEA specific to the proposals under public comment. (formerly the Jacksonville Electric consideration. Dated: December 1, 2000. Authority) under DOE's Clean Coal The DOE strategy has three principal elements. The first element involved John Tressler, Technology (CCT) Program. The project would demonstrate circulating fluidized preparation of a comprehensive Leader Regulatory Information Management, Programmatic EIS for the CCT Program Office of the Chief Information Officer. bed (CFB) combustion technology at JEA's existing Northside Generating (DOE/EIS±0146, November 1989) to Office of Educational Research and Station in Jacksonville, Florida. After address the potential environmental Improvement careful consideration of the potential consequences of widespread commercialization of each of 22 Type of Review: New. environmental impacts, along with successfully demonstrated clean coal Title: Education Longitudinal Study program goals and objectives, DOE has technologies. of 2002 (ELS 2002). decided that it will provide approximately $73 million in federal The second element involved Frequency: Annually. preparation of a pre-selection, project- Affected Public: Not-for-profit funding support (about 24% of the total cost of approximately $309 million) to specific environmental review of institutions; State, Local, or Tribal proposed CCT projects based on project- Gov't, SEAs or LEAs. design, construct, and demonstrate the CFB technology proposed by JEA. specific environmental data and Reporting and Recordkeeping Hour analyses in accordance with DOE NEPA Burden: Responses: 51,597. Burden FOR FURTHER INFORMATION CONTACT: To regulations (10 CFR 1021.216). For the Hours: 59,497. -
Combustion of Solid Fuel Ina Fluidized Bed Combustor
COMBUSTION OF SOLID FUEL INA FLUIDIZED BED COMBUSTOR A Thesis Presented to The Faculty ofthe Fritz J. and Dolores H. Russ College ofEngineering and Technology Ohio University In Partial Fulfillment Ofthe Requirement for the Degree Master ofScience --,-,*, \ ., by ,m Abu Noman Hossain June, 1998 i ACKNOWLEDGEMENTS I would like to express and extend my heartfelt appreciation and deep gratitude to the many people who have, in one way or other, helped and supported me in my work. To Dr. David J Bayless, my honorable advisor, whom I respect and admire for the excellent advice and guidance he has given me throughout the entire course ofmy study. I will always remember him for his advising, academic, and financial support at Ohio University. To Dr. H. Pasic, who generously served on my thesis committee. His suggestions and hearty attitude made my work easier and enjoyable. To Dr. M. Prudich for his keenness and initiative to serve on my thesis committee. To Len Huffman, for his excellent help and cooperation in the laboratory and mechanical workshop. To Matt Eckels, Ben Reineck and Kyle Wilson for their collaborative help and work in the design and drafting process. To Muhammad Turjo and Shatkat Shah for their endless support and continuous cooperation. To my beloved parents and my family, for their love, support, and encouragement. To Almighty Allah who has blessed me with the opportunity to come to Ohio University and has given this chance to work with these people. ii ABSTRACT The emissions ofpollutants from power plants have become the subject of increasing public concern. -
Fluidized Bed Combustion for Clean Energy
Refereed Proceedings The 12th International Conference on Fluidization - New Horizons in Fluidization Engineering Engineering Conferences International Year 2007 Fluidized Bed Combustion for Clean Energy Filip Johnsson Chalmers University of Technology, Dept. of Energy and Environment, Goteborg, Sweden, fi[email protected] This paper is posted at ECI Digital Archives. http://dc.engconfintl.org/fluidization xii/5 Johnsson: Fluidized Bed Combustion for Clean Energy FLUIDIZATION XII 47 FLUIDIZED BED COMBUSTION FOR CLEAN ENERGY Filip Johnsson Department of Energy and Environment, Energy Technology Chalmers University of Technology SE-41296 Göteborg (Sweden) T: +46-31 772 1449; E: [email protected] ABSTRACT This paper gives a brief overview of the status and prospects for fluidized bed combustion (FBC) for clean energy, with focus on power and heat generation. The paper summarizes recent development trends for the FB technology and makes an outlook into the future with respect to challenges and opportunities for the technology. The paper also identifies areas related to fluidization, which are critical for the technology and, thus, will require research. The main advantage with the FBC technology is the fuel flexibility. A compilation of 715 FB boilers (bubbling and circulating) worldwide illustrates the two main applications for the FBC technology: 1. Small and medium scale heat only or combined heat and power boilers (typically of the order of or less than 100 MW thermal), burning biomass or waste derived fuels, including co-firing with coal and 2. larger (up to 1,000 MWth) power boilers using coal (black coal or lignite) as fuel. Emerging development includes circulating fluidized beds with supercritical steam data (power boilers) with the first project coming on-line in the near future and research on oxy-fuel fired circulating fluidized beds for CO2 capture (O2/CO2 recycle schemes as well as chemical looping combustion). -
Multiphase Oxidation of SO2 by NO2 on Caco3 Particles 2 Defeng Zhao*, Xiaojuan Song*, Tong Zhu, Zefeng Zhang, Yingjun Liu
1 Multiphase Oxidation of SO2 by NO2 on CaCO3 Particles 2 Defeng Zhao*, Xiaojuan Song*, Tong Zhu, Zefeng Zhang, Yingjun Liu 3 BIC-ESAT and SKL-ESPC, College of Environmental Sciences and Engineering, Peking University, Beijing, 100871, China 4 *These authors contributed equally to this work. 5 Correspondence to: Tong Zhu ([email protected]) 6 Abstract. Heterogeneous/multiphase oxidation of SO2 by NO2 on solid or aqueous particles is thought to be a 7 potentially important source of sulfate in the atmosphere, for example, during heavily polluted episodes (haze), 8 but the reaction mechanism and rate are uncertain. In this study, in order to assess the importance of the direct 9 oxidation of SO2 by NO2 we investigated the heterogeneous/multiphase reaction of SO2 with NO2 on individual 10 CaCO3 particles in N2 using Micro-Raman spectroscopy. In the SO2/NO2/H2O/N2 gas mixture, the CaCO3 solid 11 particle was first converted to the Ca(NO3)2 droplet by the reaction with NO2 and the deliquescence of Ca(NO3)2, 12 and then NO2 oxidized SO2 in the Ca(NO3)2 droplet forming CaSO4, which appeared as needle-shaped crystals. 13 Sulfate was mainly formed after the complete conversion of CaCO3 to Ca(NO3)2, that is, during the multiphase 14 oxidation of SO2 by NO2. The precipitation of CaSO4 from the droplet solution promoted sulfate formation. The -8 15 reactive uptake coefficient of SO2 for sulfate formation is on the order of 10 , and RH enhanced the uptake 16 coefficient. We estimate that the direct multiphase oxidation of SO2 by NO2 is not an important source of sulfate 17 in the ambient atmosphere compared with the SO2 oxidation by OH in the gas phase and is not as important as 18 other aqueous phase pathways, such as the reactions of SO2 with H2O2, O3, and O2, with or without transition 19 metals. -
Operation of a Coupled Fluidized Bed System for Chemical Looping
Engineering Conferences International ECI Digital Archives The 14th nI ternational Conference on Fluidization Refereed Proceedings – From Fundamentals to Products 2013 Operation of a Coupled Fluidized Bed System for Chemical Looping Combustion of Solid Fuels with a Synthetic CU-Based Oxygen Carrier Andreas Thon Hamburg University of Technology, Germany Marvin Kramp Hamburg University of Technology, Germany Ernst-Ulrich Hartge Hamburg University of Technology, Germany Stefan Heinrich Hamburg University of Technology, Germany Joachim Werther Hamburg University of Technology, Germany Follow this and additional works at: http://dc.engconfintl.org/fluidization_xiv Part of the Chemical Engineering Commons Recommended Citation Andreas Thon, aM rvin Kramp, Ernst-Ulrich Hartge, Stefan Heinrich, and Joachim Werther, "Operation of a Coupled Fluidized Bed System for Chemical Looping Combustion of Solid Fuels with a Synthetic CU-Based Oxygen Carrier" in "The 14th nI ternational Conference on Fluidization – From Fundamentals to Products", J.A.M. Kuipers, Eindhoven University of Technology R.F. Mudde, Delft nivU ersity of Technology J.R. van Ommen, Delft nivU ersity of Technology N.G. Deen, Eindhoven University of Technology Eds, ECI Symposium Series, (2013). http://dc.engconfintl.org/fluidization_xiv/127 This Article is brought to you for free and open access by the Refereed Proceedings at ECI Digital Archives. It has been accepted for inclusion in The 14th International Conference on Fluidization – From Fundamentals to Products by an authorized administrator of ECI Digital Archives. For more information, please contact [email protected]. OPERATION OF A COUPLED FLUIDIZED BED SYSTEM FOR CHEMICAL LOOPING COMBUSTION OF SOLID FUELS WITH A SYNTHETIC CU-BASED OXYGEN CARRIER Andreas Thon, Marvin Kramp, Ernst-Ulrich Hartge, Stefan Heinrich, Joachim Werther* Institute of Solids Process Engineering and Particle Technology; Hamburg University of Technology Denickestr. -
Flexibility of CFB Combustion: an Investigation of Co-Combustion with Biomass and RDF at Part Load in Pilot Scale
energies Article Flexibility of CFB Combustion: An Investigation of Co-Combustion with Biomass and RDF at Part Load in Pilot Scale Jens Peters * , Jan May, Jochen Ströhle and Bernd Epple Institute for Energy Systems and Technology, Technical University of Darmstadt, Otto-Berndt-Straße 2, 64287 Darmstadt, Germany; [email protected] (J.M.); [email protected] (J.S.); [email protected] (B.E.) * Correspondence: [email protected]; Tel.: +49-(0)-615-1162-2689 Received: 30 July 2020; Accepted: 31 August 2020; Published: 8 September 2020 Abstract: Co-combustion of biomass and solid fuels from wastes in existing highly efficient power plants is a low-cost solution that can be applied quickly and with low effort to mitigate climate change. Circulating fluidized bed combustion has several advantages when it comes to co-combustion, such as high fuel flexibility. The operational flexibility of circulating fluidized bed (CFB) co-combustion is investigated in a 1 MWth pilot plant. Straw pellets and refuse-derived fuel (RDF) are co-combusted with lignite at full load and part loads. This study focusses on the impact on the hydrodynamic conditions in the fluidized bed, on the heat transfer to the water/steam side of the boiler, and on the flue gas composition. The study demonstrates the flexibility of CFB combustion for three low-rank fuels that differ greatly in their properties. The co-combustion of RDF and straw does not have a negative effect on hydrodynamic stability. How the hydrodynamic conditions determine the temperature and pressure development along the furnace height is shown. -
Fgd) By-Products
CHARACTERIZATION OF TRACE ELEMENTS IN DRY FLUE GAS DESULFURIZATION (FGD) BY-PRODUCTS DISSERTATION Presented in Partial Fulfillment of the Requirements for the Degree Doctor of Philosophy in the Graduate School of The Ohio State University By Panuwat Taerakul, B.ENG., M.B.A., M.S. ***** The Ohio State University 2005 Dissertation Committee: Approved by Professor Harold Walker, Adviser Professor Linda Weavers Dr. Tarunjit Butalia Adviser Professor Yu-Ping Chin Civil Engineering Graduate Program ABSTRACT This study investigates the amount, distribution, variation and fate of trace elements in FGD by-product. Dry FGD by-product including lime spray dryer (LSD) ash have possible uses in agricultural and construction applications. However, the variability in the chemical properties, especially levels of trace elements, of LSD ash is a concern due to the possible release to the environment. Changes in levels of inorganic constituents in LSD ash collected from the McCracken Power Plant were measured. Variability of elemental composition in leachate and bulk chemical properties (i.e. available lime index (ALI), calcium carbonate equivalent (CCE), and total neutralization potential (TNP)) were also examined. Little variability over different time periods (e.g., daily to yearly) and little variability between samples collected from different particle collection hoppers were observed. Trace elements including As, Se, and Hg in LSD ash and in the leachate did not surpass limits for land application (EPA 503 Rule) or RCRA. Therefore, LSD ash is a consistent material which can be beneficially re-used in an environmentally sound manner. ii Further study of LSD ash samples was conducted to examine the distribution of trace elements in different fractions. -
Oxidation of FGD-Caso3 and Effect on Soil Chemical Properties When Applied to the Soil Surface
2007 World of Coal Ash (WOCA), May 7-10, 2007, Covington, Kentucky, USA Home Oxidation of FGD-CaSO3 and Effect on Soil Chemical Properties When Applied to the Soil Surface Liming Chen1, Cliff Ramsier2, Jerry Bigham3, Brian Slater3, David Kost1, Yong Bok Lee3, and Warren A. Dick1 1School of Natural Resources, The Ohio State University/The Ohio Agricultural Research and Development Center, Wooster, OH, USA. 2Ag Spectrum Company, Dewitt, IA, USA. 3School of Natural Resources, The Ohio State University, Columbus, OH, USA. KEYWORDS: FGD-sulfite, FGD-sulfate, soil quality, gypsum, coal combustion products ABSTRACT The use of high-sulfur coal for power generation in the United States requires the removal of sulfur dioxide (SO2) produced during burning in order to meet clean air regulations. If SO2 is removed from the flue gas using a wet scrubber without forced air 2- oxidation, much of the S product created will be sulfite (SO3 ). Plants only take up S in 2- 2- the form of sulfate (SO4 ), and SO3 is toxic to plants and may cause damage to plant 2- roots. For agricultural uses, SO3 in flue gas desulfurization (FGD) products must 2- oxidize to SO4 in soils before crops are planted. However, there is little information 2- 2- about the oxidation of SO3 in FGD product to SO4 under field conditions. An FGD- CaSO3 obtained from American Electric Power Company was applied at rates of 0, 1.12 and 3.36 Mg ha-1 to the surface of an agricultural soil (Wooster silt loam, Oxyaquic 2- Fragiudalf). The SO4 in the surface soil (0-10 cm) was analyzed on days 3, 7, 17, 45, 2- and 61. -
Biomass Gasification in Rotating Fluidized Bed
Refereed Proceedings The 13th International Conference on Fluidization - New Paradigm in Fluidization Engineering Engineering Conferences International Year 2010 BIOMASS GASIFICATION IN ROTATING FLUIDIZED BED Mania Abdollahi∗ Christophe Guyy Jamal Chaoukiz ∗Ecole Polytecnique Montreal, [email protected] yEcole´ Polytechnique zEcole´ Polytechnique This paper is posted at ECI Digital Archives. http://dc.engconfintl.org/fluidization xiii/89 Abdollahi et al.: BIOMASS GASIFICATION IN ROTATING FLUIDIZED BED BIOMASS GASIFICATION IN ROTATING FLUIDIZED BED Mania Abdollahi-Neisiani, Christophe Guy and Jamal Chaouki Chemical Engineering Department, É cole Polytechnique, Montréal H3C 3A7, Canada Abstract A steady-state mathematical model is developed for a rotating fluidized bed gasifier. Integrating reactor hydrodynamics with devolatilization kinetics, char gasification and combustion of both char and gas species; the model is used to present the gas-solid phenomena in novel reactor and investigates the reactor application in gasification processes. Model outputs are compared with experimental and simulation results of existing fluidized bed gasifier. It is observed that for the same equivalence ratio, the gasification process in RFB-SG is improved as a result of improved heat and mass transfer and gas-solid contact. 1. Introduction The conversion of biomass into useful forms of energy and chemicals can be achieved in a number of ways. However the conversion of biomass to combustible gas through gasification is considered as one of the promising options for biomass conversion and utilization [1]. Due to the presence of numerous endothermic and exothermic reactions in the gasification mechanism, it is necessary to maintain a high heat transfer throughout the reactor. This requirement makes fluidized bed reactors favorable for gasification process. -
A Great Tool for Flue Gas Desulfurization Solids Analysis
Thermogravimetry: A Great Tool for Flue Gas Desulfurization Solids Analysis Brad Buecker Kansas City Power & Light Company, La Cygne, KS, USA and Roger Blaine*, Ph.D. TA Instruments, 109 Lukens Drive, New Castle, DE 19720, USA INTRODUCTION Over 50 percent of the electricity generated in the United States comes from coal- fired power plants. Perhaps a hundred or so utility boilers are already equipped with flue gas scrubbers. Anticipated tightening of sulfur dioxide (SO2) emissions regulations will require other existing and new plants to also install scrubbers. A popular design has been and will be the wet-limestone type, where finely ground, slurried limestone is sprayed onto the flue gas to remove SO2. Reliable monitoring of scrubber solids chemistry is critical for proper operation of scrubbing systems. Thermogravimetry is an excellent tool for these analyses. A Brief Overview of Scrubber Chemistry Flue-gas scrubbing is a step-wise chemistry process, where the overall reaction is a classic example of aqueous acid-base chemistry applied on an industrial scale. Alkaline limestone slurry (composed primarily of calcium carbonate, CaCO3) reacts with acidic sulfur dioxide, as represented in Equation 1. + -2 +2 -2 CaCO3 + 2H + SO3 → Ca + SO3 + H2O + CO2↑ (1) In the absence of any other reactants, calcium and sulfite ions will precipitate as a hemihydrate, where water is actually included in the crystal lattice of the scrubber byproduct. +2 -2 Ca + SO3 + ½H2O → CaSO3·½H2O↓ (2) Proper operation of a scrubber is dependent upon the efficiency of the above- listed reactions. Control of pH via reagent feed is very important. Many wet-limestone scrubbers operate at a solution pH of around 5.6 to 5.8. -
Calcium Bisulfite Oxidation Rate in the Wet Limestone-Gypsum Flue Gas
Environ. Sci. Technol. 1999, 33, 1931-1935 results. It has been shown that liquid-phase composition Calcium Bisulfite Oxidation Rate in (sulfite concentration, dissolved oxygen, pH), temperature, - and the presence, even in traces, of catalysts (Co2+,Cu2+, the Wet Limestone Gypsum Flue Mn2+) and inhibitors (alcohols, phenols, hydroquinone) Gas Desulfurization Process strongly affect the reaction rate. Sulfite oxidation was studied both in homogeneous ,² conditions, obtained by contacting a sulfite solution with an AMEDEO LANCIA* AND oxygen saturated solution, and in heterogeneous conditions, DINO MUSMARRA³ obtained by contacting a sulfurous solution with an oxygen Dipartimento di Ingegneria Chimica, containing gas phase. Results for homogeneous conditions UniversitaÁ di Napoli ªFederico IIº, p.le Tecchio 80, 80125 are relatively consistent. Working with high sulfite concen- Napoli, Italy, and Istituto di Ricerche sulla Combustione, trations Yagi and Inoue (2) and Srivastva et al. (3) found a CNR, p.le Tecchio 80, 80125 Napoli, Italy first-order kinetic equation with respect to both oxygen and sulfite. On the other hand, results obtained with lower 3 concentrations, indicate a /2-order dependence from sulfite In this paper oxidation of calcium bisulfite in aqueous and a zero-order dependence from oxygen, both in the absence and in the presence of such catalysts as copper, solutions was studied, in connection with the limestone- manganese, and cobalt (4-9). The dependence of the reaction gypsum flue gas desulfurization process. Experimental rate on the catalyst concentration is more uncertain; while measurements of the oxidation rate were carried out in a the reaction rate is proportional to the square root of the laboratory scale stirred reactor with continuous feeding concentration of Co2+ or Mn2+, the description of the catalytic of both gas and liquid phase. -
AP-42, Vol. I, CH1.1 Bituminous and Subbituminous Coal Combustion
1.1 Bituminous And Subbituminous Coal Combustion 1.1.1 General Coal is a complex combination of organic matter and inorganic mineral matter formed over eons from successive layers of fallen vegetation. Coals are classified by rank according to their progressive alteration in the natural metamorphosis from lignite to anthracite. Coal rank depends on the volatile matter, fixed carbon, inherent moisture, and oxygen, although no single parameter defines a rank. Typically, coal rank increases as the amount of fixed carbon increases and the amount of volatile matter and moisture decreases. Bituminous coals are by far the largest group and are characterized as having lower fixed carbon and higher volatile matter than anthracite. The key distinguishing characteristics of bituminous coal are its relative volatile matter and sulfur content as well as its slagging and agglomerating characteristics. Subbituminous coals have higher moisture and volatile matter and lower sulfur content than bituminous coals and may be used as an alternative fuel in some boilers originally designed to burn bituminous coals.1 Generally, bituminous coals have heating values of 10,500 to 14,000 British thermal units per pound (Btu/lb) on a wet, mineral-matter-free basis.2 As mined, the heating values of typical U.S. bituminous coals range from 10,720 to 14,730 Btu/lb.3 The heating values of subbituminous coals range from 8,300 to 11,500 Btu/lb on a wet, mineral-matter-free basis2, and from 9,420 to 10,130 Btu/lb on an as-mined basis.3 Formulae and tables for classifying coals are given in Reference 2.