Bioasphalt and Biochar from Pyrolysis of Urban Yard Waste by Daniel R

Total Page:16

File Type:pdf, Size:1020Kb

Bioasphalt and Biochar from Pyrolysis of Urban Yard Waste by Daniel R Bioasphalt and Biochar from Pyrolysis of Urban Yard Waste by Daniel R. Hill Submitted in partial fulfillment of the requirements for the degree of Master of Science Department of Civil Engineering Case Western Reserve University January 2012 CASE WESTERN RESERVE UNIVERSITY SCHOOL OF GRADUATE STUDIES We hereby approve the thesis/dissertation of _Daniel R. Hill__________________________________________ candidate for the _Master of Science________________degree*. (signed)_Aaron A. Jennings________________________________ (chair of the committee) _David Zeng_____________________________________ _Xiong “Bill” Yu__________________________________ ________________________________________________ (date) _4 August 2011_________________ *We also certify that written approval has been obtained for any proprietary material contained therein. ii Table of Contents List of Tables……………………………………………………………………………..iii List of Figures……………………………………………………………………………..v Acknowledgements……………………………………………………………………..viii Abstract…………………………………………………………………………………...ix 1. Introduction ......................................................................................................................2 2.1. Recent Interest in Pyrolysis as a Sustainable Technology ....................................... 3 2.2. Desirability of Non-Petroleum-Based Asphalt Binders ......................................... 10 2. Literature Review...........................................................................................................12 2.1. Yard Waste Generation and Management.............................................................. 12 Generation and Current Management……………………………………………….12 Greenhouse Gas Emissions and Carbon Storage……………………………………13 Issues in Yard Waste Composting…………………………………………………..14 2.2. Pyrolysis ................................................................................................................. 16 Slow Pyrolysis………………………………………………………………………17 Fast Pyrolysis………………………………………………………………………..17 Reactor Types……………………………………………………………………….18 2.3. Biochar ................................................................................................................... 23 Properties of Biochar………………………………………………………………..23 Carbon Sequestering Potential of Biochar…………………………………………..25 Added Environmental Benefits of Biochar…………………………………………26 2.4. Bio-Oil .................................................................................................................... 27 Chemical Properties of Bio-Oil……………………………………………………..27 Physical Properties of Bio-Oil………………………………………………………29 Applications of Pyrolysis Liquids…………………………………………………..30 2.5. Asphalt Binder Properties and Testing Procedures ................................................ 35 Rheological Properties of Binders…………………………………………………..35 Pavement Deformations Related to Binder Rheology………………………………37 Testing and Specifications for Binders……………………………………………...38 Specifications for Asphalt Binders in Ohio…………………………………………43 Testing on Bio-Oil…………………………………………………………………..44 3. Materials and Methods ...................................................................................................44 4.1. Sample Collection .................................................................................................. 44 4.2. Sample Preparation ................................................................................................ 47 4.3. Testing Methods ..................................................................................................... 49 Drying……………………………………………………………………………….49 Pyrolysis…………………………………………………………………………….51 Chemical Evaluation of Condensate………………………………………………...59 4. Results and Discussion ..................................................................................................64 5. Summary and Conclusions ............................................................................................75 iii 6. Appendix ........................................................................................................................79 6.1. Appendix A: Methods and Results of Growth Experiments .................................. 79 Experiment 1 - Soybeans……………………………………………………………79 Experiment 2 – Corn………………………………………………………………...82 Experiment 3 – Soybeans…………………………………………………………...84 6.2. Appendix B: Ohio Asphalt Binder Specifications ................................................. 88 7. References ......................................................................................................................90 iv List of Tables Table 1: Example Organizations Promoting Biochar Use .................................................. 6 Table 2: Moisture and Pyrolysis Testing Results for All Samples ................................... 64 Table 3: Moisture and Pyrolysis Testing Results for Branch Samples ............................. 66 Table 4: Moisture and Pyrolysis Testing Results for Leaf Samples ................................. 66 Table 5: Evaluation of Pre-Drying Effect on Yields and Byproduct Collection .............. 68 Table 6: Preliminary Chemical Analysis of Off-Gas Condensate .................................... 74 Table 7: Yield Results from First Biochar Growth Experiment with Soybeans............... 79 Table 8: Yield Results from Second Biochar Growth Experiment with Corn ................. 82 Table 9: Yield Results from Third Biochar Growth Experiment with Beans................... 85 v List of Figures Figure 1: Nutrient Poor Oxisol (left) and Terra Preta Oxisol (right) .................................. 4 Figure 2: Terra Preta Formations Discovered in Brazil ...................................................... 5 Figure 3: Initial Bench Scale Pyrolysis Reactor Setup ....................................................... 7 Figure 4: Soybean Plants in Biochar Growth Experiments ................................................ 8 Figure 5: Corn Plants in Biochar Growth Experiments ...................................................... 9 Figure 6: Schematic of Fluidized Bed Reactor ................................................................. 19 Figure 7: A Rolling Thin Film Oven ................................................................................ 42 Figure 8: Pressure Aging Vessel ....................................................................................... 43 Figure 9: Yard Waste in Biodegradable Bags ................................................................... 46 Figure 10: Yard Waste Brush Pile (Oak Branches) .......................................................... 47 Figure 11: Yard Waste Log Pile ....................................................................................... 47 Figure 12: Rhododendron Leaves Prepared for Pyrolysis ................................................ 48 Figure 13: Oak Branches Prepared for Pyrolysis .............................................................. 49 Figure 14: Dried Willow Branches ................................................................................... 50 Figure 15: Dried Black Locust Leaves ............................................................................. 50 Figure 16: Pyrolysis Reactor Connected to Discharge Piping in Furnace ........................ 52 Figure 17: Heated Piping Directing Off-Gases into Collection Flask .............................. 52 Figure 18: Second Collection Flask and Water-Cooled Condensers ................................ 53 Figure 19: Schematic of Pyrolysis Reactor and Collection System ................................. 53 Figure 20: Second Collection Flask Filled with Dense Off-Gases ................................... 55 Figure 21: Maple Branches Before Pyrolysis ................................................................... 55 Figure 22: Maple Branches After Pyrolysis (Char) .......................................................... 56 Figure 23: Maple Samaras Before Pyrolysis .................................................................... 56 vi Figure 24: Maple Samaras After Pyrolysis (Char) ........................................................... 57 Figure 25: Off-Gases Concentrating in Glass Fittings Above First Collection Flask ...... 58 Figure 26: Setup of Boiling Reflux Flasks Under Condensers for COD Test .................. 61 Figure 27: Comparison of Byproduct Collection and Moisture Content .......................... 68 Figure 28: Byproduct Collection Over Project Duration .................................................. 69 Figure 29: Moisure Contents of Deciduous and Coniferous Samples .............................. 70 Figure 30: Organics Contents of Deciduous and Coniferous Samples ............................. 71 Figure 31: Bottled Pyrolytic Liquids ................................................................................ 73 Figure 32: Dry Soybean Stem Yield versus Char Levels in Soil ...................................... 81 Figure 33: Dry Bean Yield versus Char Levels in Soil .................................................... 81 Figure 34: Dry Plant Yield versus Biochar Levels in Soil ................................................ 83 Figure 35: Dry Plant Yield versus Topsoil Level in Pot ................................................... 84 Figure 36: Dry Bean Yield versus Biochar ....................................................................... 86 Figure 37: Dry Bean Yield versus Topsoil Addition Levels ............................................ 87 Figure 38: Dry Bean Yield versus Sand Addition Levels ................................................
Recommended publications
  • Current Status and Potential of Tire Pyrolysis Oil Production As an Alternative Fuel in Developing Countries
    sustainability Review Current Status and Potential of Tire Pyrolysis Oil Production as an Alternative Fuel in Developing Countries Haseeb Yaqoob 1,2, Yew Heng Teoh 1,* , Farooq Sher 3,4,* , Muhammad Ahmad Jamil 5, Daniyal Murtaza 2, Mansour Al Qubeissi 3,4 , Mehtab UI Hassan 2 and M. A. Mujtaba 6 1 School of Mechanical Engineering, Universiti Sains Malaysia, Engineering Campus, Nibong Tebal, Penang 14300, Malaysia; [email protected] 2 Department of Mechanical Engineering, Khwaja Fareed University of Engineering and Information Technology, Rahim Yar Khan 64200, Pakistan; [email protected] (D.M.); [email protected] (M.U.H.) 3 School of Mechanical, Aerospace and Automotive Engineering, Faculty of Engineering, Environmental and Computing, Coventry University, Coventry CV1 5FB, UK; [email protected] 4 Institute for Future Transport and Cities, Coventry University, Priory Street, Coventry CV1 5FB, UK 5 Department of Mechanical and Construction Engineering, Northumbria University, Newcastle Upon Tyne, NE1 8ST, UK; [email protected] 6 Department of Mechanical Engineering, New Campus Lahore, University of Engineering and Technology, Punjab 39161, Pakistan; [email protected] * Correspondence: [email protected] (Y.H.T.); [email protected] or [email protected] (F.S.) Abstract: Energy is essential for the nature of life and the development of countries. The main demand for the 21st century is to fulfill growing energy needs. Pakistan, through the use of fossil fuels, Citation: Yaqoob, H.; Teoh, Y.H.; meets energy demands. There is pressure on the economy of the country due to the massive reliance Sher, F.; Jamil, M.A.; Murtaza, D.; Al on fossil fuels, and this tendency is influenced by various environmental impacts.
    [Show full text]
  • Bio-Oil Commercialization Plan
    BIO-OIL COMMERCIALIZATION PLAN Bio-Oil Commercialization Plan Prepared for the NH Office of Energy and Planning by Cole Hill Associates 32 Dyke Road PO Box 523 Sugar Hill, NH 03585-5000 (603) 823-5109 July 2004 This material was prepared with financial support from the New Hampshire Governor’s Office of Energy and Community Services (ECS) and the New Hampshire Department of Resources and Economic Development (DRED). However, any opinions, findings, conclusions, or recommendations expressed are those of Cole Hill Associates and do not necessarily reflect the views of ECS (now the NH Office of Energy and Planning) or DRED and do not constitute an endorsement of products or services mentioned. Since this Plan was produced, Cole Hill Associates has relocated: Gerald W. Stewart Cole Hill Associates 4 St. Andrews Lane Bluffton, SC 29909 Telephone/Fax (843) 705-5924 Cell Phone (843) 368-5661 Cole Hill Associates Page 56 July 2004 BIO-OIL COMMERCIALIZATION PLAN Introduction I. Commercialization Plan Summary† A. There is a need for an expanded use of low-grade wood chips in the North Country of New Hampshire.1a,1b,2 B. One alternative is the conversion of wood chips into bio-oil, an environmentally friendly, renewable energy source. C. The objective of this study is to evaluate the economic viability of locating a bio-oil facility in New Hampshire as an alternative use of wood chips, and to inform interested parties as to the current state of bio-oil technology. Contractual requirements for developing this commercialization plan specifically forbid the selection of and /or bias towards any one producer or process.
    [Show full text]
  • 1 Estimating Profitability of Two Biochar Production Scenarios
    Estimating Profitability of Two Biochar Production Scenarios: Slow Pyrolysis vs. Fast Pyrolysis Tristan R. Brown1 *, Mark M. Wright2, 3, and Robert C. Brown2, 3 Iowa State University 1Biobased Industry Center 2Department of Mechanical Engineering 3Center for Sustainable Environmental Technologies * [email protected] Iowa State University Ames, IA 50011 Tel: (515) 460-0183 Fax: (515) 294-6336 ABSTRACT We estimate the profitability of producing biochar from crop residue (corn stover) for two scenarios. The first employs slow pyrolysis to generate biochar and pyrolysis gas and has the advantage of high yields of char (as much as 40 wt-%) but the disadvantage of producing a relatively low-value energy product (pyrolysis gas of modest heating value). The second scenario employs fast pyrolysis to maximize production of bio-oil with biochar and pyrolysis gas as lower-yielding co-products. The fast pyrolysis scenario produces a substantially higher value energy product than slow pyrolysis but at the cost of higher capital investment. We calculate the internal rate of return (IRR) for each scenario as functions of cost of feedstock and projected revenues for the pyrolysis facility. The assumed price range for delivered biomass feedstock is $0 to $83 per metric ton. The assumed carbon offset value for biochar ranges from $20 per metric ton of biochar in 2015 to $60 in 2030. The slow pyrolysis scenario in 2015 is not profitable at an assumed feedstock cost of $83 per metric ton. The fast pyrolysis scenario in 2015 yields 15% IRR with the same feedstock cost because gasoline refined from the bio-oil provides revenues of $2.96 per gallon gasoline equivalent.
    [Show full text]
  • 2013 DOE Bioenergy Technologies Office (BETO) Project Peer Review
    2013 DOE Bioenergy Technologies Office (BETO) Project Peer Review Catalytic Conversion to Liquid Hydrocarbons from Pyrolysis Oil and Syngas May 20, 2013 Bio-Oil Technology Area Review Fei Yu and Philip H. Steele Sustainable Energy Research Center (SERC) Mississippi State University (MSU) *On many slides, the slide notes section has important additional information* This presentation does not contain any proprietary, confidential, or otherwise restricted information Goal/Objective Statement • MSU pyrolysis/syngas program goals: – Develop hydrocarbon and biodiesel fuels from raw bio-oil produced from southern pine and agricultural products and residues; develop auger reactor designs that can provide test quantities of raw bio-oil; test designs at pilot plant scale – Develop technologies for biomass gasification and catalytic conversion of cleaned syngas to hydrocarbon biofuels. This is accomplished through the design and optimization of syngas-to-hydrocarbons pilot plant, including biomass gasification, syngas cleanup, syngas upgrading as well as new catalyst material development. • The MSU pyrolysis/syngas program goals support the development of technologies for conversion of forest resources into cost-competitive liquid fuels, such as renewable gasoline, jet fuel and diesel. Technologies to be tested at laboratory (and pilot scale in FY14). 2 Project Quad Chart Overview Timeline Barriers •Project start date: June 1, 2006 • Barriers addressed •Project end date: June 30, 2014 • Pyrolysis •Percent complete: – Tt-A Feeding dry biomass SERC phase I: 100% – TT-G Fuel synthesis and SERC phase II: 100% upgrading SERC phase III: 90% SERC phase IV: 40% • Syngas – Tt.-F. Syngas Cleanup and Conditioning Budget • Total project funding – Tt-G. Fuels Catalyst Development - DOE share: $15,587,449 - Contractor share: $4,414,254 Partners & Roles • Funding received in FY 2011 (DOE & cost share): Pyrolysis $4,597,536 •Piedmont Bio-Products: licensee • Funding in FY 2012 (DOE & cost share): $4,922,748 Syngas • ARRA Funding: $0 •MS Choctaw Lignite LLC.
    [Show full text]
  • Pyrolysis Oils: Characterization, Stability Analysis, and Catalytic Upgrading to Fuels and Chemicals
    University of Massachusetts Amherst ScholarWorks@UMass Amherst Open Access Dissertations 2-2011 Pyrolysis Oils: Characterization, Stability Analysis, and Catalytic Upgrading to Fuels and Chemicals Tushar Vispute University of Massachusetts Amherst Follow this and additional works at: https://scholarworks.umass.edu/open_access_dissertations Part of the Chemical Engineering Commons Recommended Citation Vispute, Tushar, "Pyrolysis Oils: Characterization, Stability Analysis, and Catalytic Upgrading to Fuels and Chemicals" (2011). Open Access Dissertations. 349. https://scholarworks.umass.edu/open_access_dissertations/349 This Open Access Dissertation is brought to you for free and open access by ScholarWorks@UMass Amherst. It has been accepted for inclusion in Open Access Dissertations by an authorized administrator of ScholarWorks@UMass Amherst. For more information, please contact [email protected]. PYROLYSIS OILS: CHARACTERIZATION, STABILITY ANALYSIS, AND CATALYTIC UPGRADING TO FUELS AND CHEMICALS A Dissertation Presented by TUSHAR P. VISPUTE Submitted to the Graduate School of the University of Massachusetts Amherst in partial fulfillment of the requirements for the degree of DOCTOR OF PHILOSOPHY February 2011 Chemical Engineering © Copyright by Tushar P. Vispute 2011 All Rights Reserved PYROLYSIS OILS: CHARACTERIZATION, STABILITY ANALYSIS, AND CATALYTIC UPGRADING TO FUELS AND CHEMICALS A Dissertation Presented by TUSHAR P. VISPUTE Approved as to style and content by: _______________________________________ George W. Huber, Chair _______________________________________ W. Curt Conner, Member _______________________________________ Scott M. Auerbach, Member ____________________________________ T. J. (Lakis) Mountziaris, Department Head Chemical Engineering ACKNOWLEDGEMENTS I would like to deeply acknowledge the help and support of my advisor Prof. George W. Huber on this fascinating research program. George is an excellent mentor and provides an outstanding research environment in the group for graduate students to work and develop.
    [Show full text]
  • Pyrolysis Oil and Upgrading
    PNNL-22133 Prepared for the U.S. Department of Energy under Contract DE-AC05-76RL01830 Production of Gasoline and Diesel from Biomass via Fast Pyrolysis, Hydrotreating and Hydrocracking: 2011 State of Technology and Projections to 2017 SB Jones JL Male February 2012 PNNL-22133 Production of Gasoline and Diesel from Biomass via Fast Pyrolysis, Hydrotreating and Hydrocracking: 2011 State of Technology and Projections to 2017 SB Jones JL Male February 2012 Prepared for the U.S. Department of Energy under Contract DE-AC05-76RL01830 Pacific Northwest National Laboratory Richland, Washington 99352 Contents 1.0 Introduction ................................................................................................................................ 1 2.0 State of Technology for FY2011 ................................................................................................ 3 2.1 Feedstock and Feedstock Preparation ................................................................................ 3 2.2 Fast Pyrolysis ..................................................................................................................... 5 2.3 Upgrading ........................................................................................................................... 5 2.4 Hydrocracking .................................................................................................................... 7 2.5 Hydrogen Generation ......................................................................................................... 8
    [Show full text]
  • Production of Metallurgical Charcoal from Biomass Pyrolysis: Pilot-Scale Experiment
    22nd International Symposium on Analytical and Applied Pyrolysis Kyoto, 2018 Production of metallurgical charcoal from biomass pyrolysis: pilot-scale experiment a a b b a A. Phounglamcheik *, R. Pitchot , A. Andefors , N. Norberg , and K. Umeki * corresponding author: [email protected] a Division of Energy Science, Luleå University of Technology, SE-971 87 Luleå, Sweden b Future Eco North Sweden AB, SE-961 50 Boden, Sweden Replacement of fossil coal with biomass fuel is a key strategy to decrease CO2 emission in the Nordic industry. Charcoal produced from pyrolysis of forest residue is expected for the application in metallurgical process. Quality of charcoal can reach the requirement, i.e. high carbon content, low volatile, low ash content, and high heating value at high pyrolysis temperature. Nevertheless, to produce charcoal with such high quality, the products distribution may shift toward pyrolysis oil and gas. We have suggested to increase the charcoal yield while keeping its quality by adsorbing large molecule fractions of pyrolysis oil on the pore structure of charcoal produced at relatively high temperature (>600 °C). This study aims at demonstrating the suggested pyrolysis process to produce metallurgical charcoal with high efficiency. The effect of various operation parameters was investigated in batch operations with ca. 130 kg dry wood chips for this purpose. The experiment was conducted in a pilot-scale auger-type pyrolysis reactor. Two cylindrical pipes with screw conveyers and external heating/cooling media are connected for pyrolysis and vapor adsorption. In the pyrolysis reactor, woodchips are heated indirectly with flue gas generated from a propane burner. In the vapor adsorption pipe, charcoal and volatiles are cooled down and part of pyrolysis volatile is condensed and absorbed on the surface of charcoal.
    [Show full text]
  • A Comprehensive Characterization of Pyrolysis Oil from Softwood Barks
    polymers Article A Comprehensive Characterization of Pyrolysis Oil from Softwood Barks Haoxi Ben 1,*, Fengze Wu 1, Zhihong Wu 1 , Guangting Han 2,3, Wei Jiang 2,3 and Arthur J. Ragauskas 4,5 1 Key Laboratory of Energy Thermal Conversion and Control of Ministry of Education, Southeast University, Nanjing 210096, China 2 Qingdao University, Qingdao 266071, China 3 State Key Laboratory of Bio-Fibers and Eco-Textiles, Qingdao University, Qingdao 266071, China 4 Joint Institute for Biological Sciences, Biosciences Division, Oak Ridge National Lab, Oak Ridge, TN 37831, USA 5 Department of Chemical and Biomolecular Engineering, University of Tennessee, Knoxville, TN 37996, USA * Correspondence: [email protected]; Tel.: +86-188-5107-5775 Received: 17 July 2019; Accepted: 19 August 2019; Published: 23 August 2019 Abstract: Pyrolysis of raw pine bark, pine, and Douglas-Fir bark was examined. The pyrolysis oil yields of raw pine bark, pine, and Douglas-Fir bark at 500 ◦C were 29.18%, 26.67%, and 26.65%, respectively. Both energy densification ratios (1.32–1.56) and energy yields (48.40–54.31%) of char are higher than pyrolysis oils (energy densification ratios: 1.13–1.19, energy yields: 30.16–34.42%). The pyrolysis oils have higher heating values (~25 MJ/kg) than bio-oils (~20 MJ/kg) from wood and agricultural residues, and the higher heating values of char (~31 MJ/kg) are comparable to that of many commercial coals. The elemental analysis indicated that the lower O/C value and higher H/C value represent a more valuable source of energy for pyrolysis oils than biomass.
    [Show full text]
  • Study on Phenolic Content in Fast Pyrolysis Oil Obtained from the Model Compounds of Three Major Components in Biomass
    The 2016 International Conference on Advances in Energy, Environment and Chemical Science (AEECS 2016) Study on Phenolic Content in Fast Pyrolysis Oil Obtained from the Model Compounds of Three Major Components in Biomass Liu Ziyun1, 2, a, Wang Lihong1, 2, b, Li Yongjun1, 2, c and Li Zhihe1, 2, d 1School of Agricultural and Food Engineering, Shandong University of Technology, China, 2Shandong Research Center of Engineering and Technology for Clean Energy, Zibo 255049, Shandong Province, China; [email protected] [email protected] [email protected] [email protected] Keywords: cellulose; xylan; lignin; pyrolysis; phenolic compounds Abstract. The aim of this paper is to research variation of phenolic yields in bio-oil and the effect of interactions of three components in biomass, fast pyrolysis experiments were done with cellulose, xylan (as an alternative to hemicellulose) and lignin in tube furnace at different temperatures. Phenolic yields in liquid product analyzed by using Gas chromatography-Mass spectrometry (GC-MS) were divided into four groups: phenols, H-phenols, G-phenols and S-phenols. In single component oil, S-phenols yeild was hardly any. There were trends for phenols, H-phenols and G-phenols that were consistent with temperature increasing from 450 to 550℃. And in cellulose oil, H-phenols was prone to dehydroxylation near 500℃ . The phenolic compounds yields in lignin oil reached 25.98% at 550℃. For two-component oil, the yields of phenols and G-phenols increased due to the interaction of cellulose-lignin, while that of H-phenols decreased. The interaction of xylan-lignin was similar with cellulose-lignin.
    [Show full text]
  • Aging Influence on Rheology Properties of Petroleum-Based Asphalt Modified with Biobinder
    Aging Influence on Rheology Properties of Petroleum-Based Asphalt Modified with Biobinder Julian Mills-Beale, M.ASCE1; Zhanping You, Ph.D., P.E., M.ASCE2; Elham Fini, Ph.D., P.E., M.ASCE3; Boubacar Zada4; Chee Huei Lee5; and Yoke Khin Yap6 Abstract: This paper aims to investigate the viability of using swine waste binder to improve the rheological properties of bituminous asphalt binder. Due to rising bituminous asphalt binder costs, diminishing reserves of crude oil from which asphalt binder is derived, and the gradual paradigm shift toward more environmentally friendly and energy efficient hot-mix asphalt (HMA) mixtures, the asphalt pavement industry is exploring different sustainable alternative binders. Biobinder has the potential to partially or fully replace typical crude-based asphalt. In this paper, biobinder from swine manure is produced by thermochemical liquefaction process at 380°C and 40 MPa (approximately 400 atm) pressure in the absence of oxygen. A Superpave PG 64-22 is then modified with 5% biobinder by total weight of asphalt binder to produce the biobinder. Samples of the base asphalt binder (nonmodified PG 64-22) and samples of asphalt modified with biobinder are characterized by running the Superpave rotational viscosity (RV), dynamic shear rheometer (DSR), and the bending beam rheometer (BBR) tests. Furthermore, Fourier transform infrared (FTIR) spectroscopy investigations were used to validate the chemical bond initiations that caused changes in stiffness and viscosity of the asphalt modified with 5% biobinder from those of base asphalt binder (PG 64-22). The modification resulted in 27% decrease in viscosity of the base binder. The rolling thin film (RTFO)–aged samples of modified binder experienced a 28.9% decrease in average viscosity change when compared with the RTFO-aged samples from the base binder.
    [Show full text]
  • Azarijafari Hessam Phd 2018.Pdf
    UNIVERSITÉ DE SHERBROOKE Faculté de génie Département de génie civil DEVELOPMENT OF A CONSEQUENTIAL DYNAMIC MODEL INCORPORATING VARIABILITY AND UNCERTAINTY ANALYSIS FOR ASSESSING LIFE CYCLE ENVIRONMENTAL IMPACTS OF PAVEMENTS DÉVELOPPEMENT D'UN MODÈLE DYNAMIQUE INCORPORANT L'ANALYSE DE LA VARIABILITÉ ET DE L'INCERTITUDE POUR L'ÉVALUATION DES CONSÉQUENCES ENVIRONNEMENTALES DU CYCLE DE VIE DES CHAUSSÉES Thèse de doctorat Spécialité : génie civil Hessam AZARIJAFARI Sherbrooke (Québec) Canada Juillet 2018 MEMBRES DU JURY Pr. Ben AMOR, Directeur Pr. Ammar YAHIA Codirecteur Pr. Dahai QI Rapporteur Dr. Jeremy GREGORY Évaluateur Dr. Geoffrey GUEST Évaluateur This work is dedicated to my family. ACKNOWLEDGEMENT My journey thus far could never have been such fascinating if it were not because of the following individuals who have made irreplaceable contribution to everything I have achieved. It is why I would like to thank Prof. Ben Amor and Prof. Ammar Yahia for granting me their confidence. I could not have had a better team of directors. You guided me to have a more mature scientific mind, which I am indefinitely grateful and indebted. I would like to thank you for keeping an open door for me all the time, urging me to perfect my research work, as well as filling our collaboration at all levels with pleasure. My special thanks go to Mathieu Courchesne for providing the building energy model and Adam Hayashi and Guillaume Lemieux for the intellectual support from the Canadian cement industry. The statistical data provided by Julie Ruby from the ministry of transportation in Quebec (MTQ) is appreciated. The financial supports of this research project were provided by the Fonds Nature et technologies (FQRNT), the Natural Sciences and Engineering Research Council of Canada (NSERC), the Centre de recherche sur les infrastructures en béton (CRIB), and the Fondation de l’ Université de Sherbrooke.
    [Show full text]
  • Pyrolysis Oil and Upgrading
    PNNL-22684 Prepared for the U.S. Department of Energy under Contract DE-AC05-76RL01830 Production of Gasoline and Diesel from Biomass via Fast Pyrolysis, Hydrotreating and Hydrocracking: 2012 State of Technology and Projections to 2017 SB Jones LL Snowden-Swan February 2013 PNNL-22684 Production of Gasoline and Diesel from Biomass via Fast Pyrolysis, Hydrotreating and Hydrocracking: 2012 State of Technology and Projections to 2017 SB Jones LL Snowden-Swan February 2013 Prepared for the U.S. Department of Energy under Contract DE-AC05-76RL01830 Pacific Northwest National Laboratory Richland, Washington 99352 Contents 1.0 State of Technology for 2012 ..................................................................................................... 1 1.1 Feedstock and Feedstock Preparation ................................................................................ 1 1.2 Fast Pyrolysis ..................................................................................................................... 1 1.3 Upgrading ........................................................................................................................... 1 1.4 Hydrocracking and Balance of Plant .................................................................................. 4 2.0 Progression to 2017 Conversion Target ..................................................................................... 5 3.0 Environmental Sustainability Metrics ........................................................................................ 9 3.1 Greenhouse
    [Show full text]