Bio-Oil Commercialization Plan
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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. -
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. -
For Immediate Release Via the Canadian Custom Disclosure Network Magellan Aerospace Announces Report on Voting Results for Dire
FOR IMMEDIATE RELEASE VIA THE CANADIAN CUSTOM DISCLOSURE NETWORK MAGELLAN AEROSPACE ANNOUNCES REPORT ON VOTING RESULTS FOR DIRECTORS Mississauga, Ontario – May 7, 2019 - Magellan Aerospace Corporation (the "Corporation") announces that today at the annual meeting of shareholders of the Corporation (the “Meeting”) the proposed nominees for directors of the Corporation received the following votes: Percentage Percentage Name of Proposed of Votes Votes of Votes Nominee Votes For For Withheld Withheld N. Murray Edwards 52,039,044 99.24% 396,775 0.76% Phillip C. Underwood 52,140,305 99.44% 295,514 0.56% Beth M. Budd Bandler 52,397,269 99.93% 38,550 0.07% William G. Davis 51,769,034 98.73% 666,785 1.27% Bruce W. Gowan 51,830,249 98.85% 605,570 1.15% Larry G. Moeller 51,749,149 98.69% 686,670 1.31% Steven Somerville 52,075,254 99.31% 360,565 0.69% As a result, all of the above named nominees have been elected to hold office for the ensuing year, or until their successors are duly elected or appointed, subject to the provisions of the Business Corporations Act (Ontario) and by-laws of the Corporation. About Magellan Aerospace: Magellan Aerospace is one of the world's most integrated aerospace industry suppliers. Magellan designs, engineers, and manufactures aeroengine and aerostructure assemblies and components for aerospace markets, advanced products for military and space markets, and complementary specialty products. Magellan is a public company whose shares trade on the Toronto Stock Exchange (TSX: MAL), with operating units throughout Canada, the United States, the United Kingdom, India, Northern Ireland, and Poland. -
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. -
Sustainable Growth Strategies in the Canadian Space Sector
Sustainable Growth Strategies in the Canadian Space Sector Sustainable Growth Strategies in the Canadian Space Sector Submitted by: Ian Christison Applied Project (APRJ-699) Word Count 20,187 Academic Coach: Conor VibertCarroll Submission Date: March 31, 2008 Assignment Number: 3 Sustainable Growth Strategies in the Canadian Space Sector 2 Table of Contents 1 Introduction....................................................................................................4 1.1 Defining the Problem ..............................................................................7 1.2 Problem Issues.......................................................................................7 1.3 Topic Definition.......................................................................................8 1.4 Project Definition Literature Search ........................................................8 1.5 Research Effective Reading Method and Literature Review...................8 1.6 Project Challenges and Focus Strategy..................................................9 2 Literature Review.........................................................................................10 2.1 Research Questions .............................................................................10 2.2 Research Boundaries ...........................................................................10 2.3 Alternative Courses of Action to be Evaluated......................................10 2.4 Research users ....................................................................................11 -
2021 First Quarter Report
QUARTERLY REPORT MARCH 31, 2021 This Management’s Discussion and Analysis (“MD&A”) of the financial condition and results of operations of Magellan Aerospace Corporation (“Magellan” or the “Corporation”) should be read in conjunction with the unaudited condensed consolidated interim financial statements and the notes thereto for the three month period ended March 31, 2021, and the audited annual consolidated financial statements for the year ended December 31, 2020 (available on SEDAR at www.sedar.com). Unless otherwise noted, all financial information has been prepared in accordance with Canadian Generally Accepted Accounting Principles (“GAAP”), specifically International Accounting Standard (“IAS”) 34, Interim Financial Reporting as issued by the International Accounting Standards Board (“IASB”), which is within the framework of International Financial Reporting Standards (“IFRS”). This MD&A provides a review of the significant developments that have impacted the Corporation’s performance during the three month period ended March 31, 2021 relative to the three month period ended March 31, 2020. The information contained in this report is as at May 4, 2021. All financial references are in Canadian dollars unless otherwise noted. The MD&A contains forward-looking information that represents the Corporation’s internal projections, expectations, estimates or beliefs concerning, among other things, future operating results and various components thereof or the Corporation’s future economic performance. These statements relate to future events or future performance. In particular and without limitation there are forward looking statements under the heading “Overview”, “Results of Operations”, “Liquidity and Capital Resources”, “Risk Factors”, “Future Changes in Accounting Policies” and “Outlook”. In some cases, forward-looking statements can be identified by terminology such as “may”, “will”, “should”, “expects”, “projects”, “plans”, “anticipates”, and similar expressions. -
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. -
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 -
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. -
110307 Nr Wsps
FOR IMMEDIATE RELEASE VIA THE CANADIAN CUSTOM DISCLOSURE NETWORK AND THE TOP US FINANCIAL MARKETS NEWS RELEASE New Bell Helicopter Wire Strike Protection System Development Winnipeg, Manitoba – March 8, 2011 – Magellan Aerospace announced today a new agreement with Bell Helicopter for a Wire Strike Protection System (WSPS®) kit development. The helicopter to be fitted with WSPS will be the Bell UH-1Y. The design and production of the WSPS will be carried out at Magellan’s Bristol Aerospace operating division in Winnipeg, Manitoba, for delivery of the prototype kits in 2011. Bristol is the global expert for this unique system, offering a proven design and acknowledged technological expertise. In January of this year, the company also announced a new agreement with Hindustan Aeronautics Limited (HAL), headquartered in Bangalore, India for the design and development of a new WSPS kit for the HAL Advanced Light Helicopter (ALH). Bell Helicopters is a long time customer and supporter of WSPS. Bristol's initial WSPS development and testing was for the Bell CH-136 Kiowa in 1977. Bristol has previously adapted the design to several variants of Bell's UH-1 helicopters. Mr. Don Boitson, Vice President and General Manger, Bristol Aerospace, commented, “Our WSPS continues to lead the way with helicopter OEMs, and we are proud of our long-lasting and ongoing relationship with Bell Helicopter.” In 1977 Bristol, with the Canadian Forces, designed the WSPS to provide a measure of protection for helicopters to the potentially devastating consequences of inadvertent encounters with horizontally strung wires and cables. In 2009, Bristol reached the milestone of delivering its 20,000 th WSPS kit. -
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. -
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.