THE ART of the POSSIBLE the Fuel Flexibility of GE Power's
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Investigation of Waste Biogas Flame Stability Under Oxygen Or Hydrogen-Enriched Conditions
energies Article Investigation of Waste Biogas Flame Stability Under Oxygen or Hydrogen-Enriched Conditions Nerijus Striugas,¯ Rolandas Paulauskas *, Raminta Skvorˇcinskiene˙ and Aurimas Lisauskas Laboratory of Combustion Processes, Lithuanian Energy Institute, Breslaujos str. 3, LT-44403 Kaunas, Lithuania; [email protected] (N.S.); [email protected] (R.S.); [email protected] (A.L.) * Correspondence: [email protected]; Tel.: +370-37-401830 Received: 18 August 2020; Accepted: 9 September 2020; Published: 11 September 2020 Abstract: Increasing production rates of the biomethane lead to increased generation of waste biogases. These gases should be utilized on-site to avoid pollutant emissions to the atmosphere. This study presents a flexible swirl burner (~100 kW) with an adiabatic chamber capable of burning unstable composition waste biogases. The main combustion parameters and chemiluminescence emission spectrums were examined by burning waste biogases containing from 5 to 30 vol% of CH4 in CO2 under air, O2-enriched atmosphere, or with the addition of hydrogen. The tested burner ensured stable combustion of waste biogases with CH4 content not less than 20 vol%. The addition of up to 5 vol% of H2 expanded flammability limits, and stable combustion of the mixtures with CH4 content of 15 vol% was achieved. The burner flexibility to work under O2-enriched air conditions showed more promising results, and the flammability limit was expanded up to 5 vol% of CH4 in CO2. However, the combustion under O2-enriched conditions led to increased NOx emissions (up to 1100 ppm). Besides, based on chemiluminescence emission spectrums, a linear correlation between the spectral intensity ratio of OH* and CH* (IOH*/ICH*) and CH4 content in CO2 was presented, which predicts blow-off limits burning waste biogases under different H2 or O2 enrichments. -
FACT SHEET 7: Liquid Hydrogen As a Potential Low- Carbon Fuel for Aviation
FACT SHEET 7: Liquid hydrogen as a potential low- carbon fuel for aviation This fact sheet aims to explain how current aviation fuels operate before providing descriptions of how alternative fuel options, like sustainable aviation fuels (SAF) and liquid hydrogen, could help meet the rigorous climate targets set by the aviation industry. Secondly, this document explores the limitations and opportunities of liquid hydrogen when it comes to the manufacturing, safety, current uses and outlooks. This document concludes with a discussion on policy, mandates and incentives on the topic of hydrogen as a potential fuel for aviation. Introduction – Why hydrogen? Aircraft fly thanks to a combination of air and a combustion process that occurs in the aircraft engines. The primary source of energy is the fuel. Each kilogram of fuel, which would occupy less than 1 litre of volume, contains a significant amount of energy, 42.8 MJ [1]. If we could convert the energy of a 1L bottle of fuel into electric energy to power a cell phone, the battery would last for over 2 months. This energy is extracted in the combustion chamber of the engine in the form of heat; Compressed air enters the combustion chamber and gets heated up to temperatures nearing 1,500°C. This hot high- pressure air is what ultimately moves the aircraft forward. Kerosene is composed of carbon and hydrogen (hence it’s a hydrocarbon fuel). When the fuel is completely burned, these carbon and hydrogen molecules recombine with oxygen to create water vapor (H2O) and carbon dioxide (CO2) (Fig.1). August 2019 Emissions: From Combustion: H2O + CO2 Other: NOx, nvPM SOx, soot Fuel in (C + H) Figure 1 Schematic of a turbofan engine adapted from: [2] Carbon dioxide will always be created as a by-product of burning a carbon-based fuel. -
The Future of Liquid Biofuels for APEC Economies
NREL/TP-6A2-43709. Posted with permission. The Future of Liquid Biofuels for APEC Economies Energy Working Group May 2008 Report prepared for the APEC Energy Working Group under EWG 01/2006A by: Anelia Milbrandt National Renewable Energy Laboratory (NREL) Golden, Colorado, USA Web site: www.nrel.gov Dr. Ralph P. Overend NREL Research Fellow (Retired) Ottawa, Ontario, Canada APEC#208-RE-01.8 Acknowledgments The authors would like to acknowledge and thank the project overseer Mr. Rangsan Sarochawikasit (Department of Alternative Energy Development and Efficiency, Thailand) for his leadership of this project. We also would like to thank Dr. Helena Chum (National Renewable Energy Laboratory, USA) for contributing materials, and providing review and feedback; and the chair of APEC Biofuels Task Force, Mr. Jeffrey Skeer, (Department of Energy, USA) for his support and guidance. The authors also greatly appreciate the time and valuable contributions of the following individuals: Ms. Naomi Ashurst and Ms. Marie Taylor, Department of Industry, Tourism and Resources, Australia Ms. Siti Hafsah, Office of the Minister of Energy, Brunei Darussalam Mr. Mark Stumborg, Agriculture and Agri-Food, Canada Ms. Corissa Petro, National Energy Commission, Chile Mr. Song Yanqin and Mr. Zhao Yongqiang, National Development and Reform Commission, China Mr. K.C. Lo, Electrical and Mechanical Service Department, Hong Kong, China Dr. Hom-Ti Lee, Industrial Technology Research Institute, Chinese Taipei Mr. Hendi Kariawan, Indonesia Biofuels Team, Indonesia Dr. Jeong-Hwan Bae, Korea Energy Economics Institute, Republic of Korea Mr. Diego Arjona-Arguelles, Secretariat for Energy (SENER), Mexico Mr. Angel Irazola and Mr. Diego de la Puente Consigliere, Agricola Del Chira S.A., Peru Mr. -
Nebraska Liquid Fuel Carriers Information Guide
Information Guide March 2021 Nebraska Liquid Fuel Carriers Overview Any person transporting motor fuels or aircraft fuels in a transport vehicle into, within, or out of Nebraska must obtain a liquid fuel carriers license. A copy of the license must be carried in the transport vehicle whenever motor fuels or aircraft fuels are carried in this state. In addition, a copy of the bill of lading, manifest, bill of sale, purchase order, sales invoice, delivery ticket, or similar documentation must be carried in the transport vehicle at all times when transporting motor fuels or aircraft fuels in Nebraska. This documentation must include the following information: v Date; v Type of fuel; v Amount of fuel; v Where and from whom the fuel was obtained; v Destination state or delivery location; v Name and address of the owner of the fuel; and v Name and address of the consignee or purchaser. A license is not required for persons transporting motor fuels or aircraft fuels within Nebraska for their own agricultural, quarrying, industrial, or other nonhighway use; nor is it required for the transportation of leaded racing fuels, propane, or compressed natural gas, regardless of its ownership or use. This guidance document is advisory in nature but is binding on the Nebraska Department of Revenue (DOR) until amended. A guidance document does not include internal procedural documents that only affect the internal operations of DOR and does not impose additional requirements or penalties on regulated parties or include confidential information or rules and regulations made in accordance with the Administrative Procedure Act. -
Development of a Liquid Injection Propane System for Spark-Ignited Engines Via Fuel Temperature Control" (2007)
Scholars' Mine Masters Theses Student Theses and Dissertations Summer 2007 Development of a liquid injection propane system for spark- ignited engines via fuel temperature control Brian Charles Applegate Follow this and additional works at: https://scholarsmine.mst.edu/masters_theses Part of the Mechanical Engineering Commons Department: Recommended Citation Applegate, Brian Charles, "Development of a liquid injection propane system for spark-ignited engines via fuel temperature control" (2007). Masters Theses. 4555. https://scholarsmine.mst.edu/masters_theses/4555 This thesis is brought to you by Scholars' Mine, a service of the Missouri S&T Library and Learning Resources. This work is protected by U. S. Copyright Law. Unauthorized use including reproduction for redistribution requires the permission of the copyright holder. For more information, please contact [email protected]. DEVELOPMENT OF A LIQUID INJECTION PROPANE SYSTEM FOR SPARK- IGNITED ENGINES VIA FUEL TEMPERATURE CONTROL by BRIAN CHARLES APPLEGATE A THESIS Presented to the Faculty of the Graduate School of the UNIVERSITY OF MISSOURI-ROLLA In Partial Fulfillment of the Requirements for the Degree MASTER OF SCIENCE IN MECHANICAL ENGINEERING 2007 Approved by _______________________________ _______________________________ James A. Drallmeier, Advisor Virgil Flanigan _______________________________ Chris Ramsay © 2007 Brian Charles Applegate All Rights Reserved iii ABSTRACT This thesis entails the development of a liquid injected propane fuel system. Propane fuel offers opportunities in emissions reductions and lower carbon dioxide production per kilogram of fuel. However, drawbacks to the fuel include current storage in a saturated state. The storage method allows higher fuel volume density storage to minimize storage size. This method of storing the fuel presents fuel metering challenges resultant from the variable density of the two-phase flow. -
Fire Dynamics and Forensic Analysis of Liquid Fuel Fires
The author(s) shown below used Federal funds provided by the U.S. Department of Justice and prepared the following final report: Document Title: Fire Dynamics and Forensic Analysis of Liquid Fuel Fires Author: Christopher L. Mealy, Matthew E. Benfer, Daniel T. Gottuk Document No.: 238704 Date Received: May 2012 Award Number: 2008-DN-BX-K168 This report has not been published by the U.S. Department of Justice. To provide better customer service, NCJRS has made this Federally- funded grant final report available electronically in addition to traditional paper copies. Opinions or points of view expressed are those of the author(s) and do not necessarily reflect the official position or policies of the U.S. Department of Justice. This document is a research report submitted to the U.S. Department of Justice. This report has not been published by the Department. Opinions or points of view expressed are those of the author(s) and do not necessarily reflect the official position or policies of the U.S. Department of Justice. FIRE DYNAMICS AND FORENSIC ANALYSIS OF LIQUID FUEL FIRES Final Report Grant No. 2008-DN-BX-K168 Prepared by: Christopher L. Mealy, Matthew E. Benfer, and Daniel T. Gottuk Hughes Associates, Inc. 3610 Commerce Drive, Suite 817 Baltimore, MD 21227 Ph. 410-737-8677 FAX 410-737-8688 February 18, 2011 This document is a research report submitted to the U.S. Department of Justice. This report has not been published by the Department. Opinions or points of view expressed are those of the author(s) and do not necessarily reflect the official position or policies of the U.S. -
Prima PRO Process Mass Spectrometer No
APPLICATION NOTE Prima PRO process mass spectrometer No. ?????? Accurate multi-component blast furnace gas analysis maximizes iron production and minimizes coke consumption Author: Graham Lewis, Thermo Fisher Scientific, Winsford, Cheshire, United Kingdom Key words • Top gas analysis • Below burden probe • Gas efficiency • Coke rate • Mass balance • Calorific value • Heat balance • Magnetic sector • Above burden probe Introduction Over a billion tonnes of iron a year are produced in These reduction zones are shown in Figure 1. blast furnaces, representing around 94% of global iron production1. The blast furnace consists of a large steel stack, lined with refractory brick. Iron ore, coke and limestone are dropped into the top of the furnace and preheated air blown into the bottom through nozzles called ‘Tuyeres’. Iron oxides are reduced in the melting zone, or ‘Bosh’, forming liquid iron (called ‘hot metal’) and liquid slag. These liquid products are drained from the furnace at regular intervals, and the blast furnace will run continuously for several years, until the refractory lining needs replacing. A wide variety of chemical reactions take place in the blast furnace. At the elevated temperatures towards the bottom Figure 1 of the furnace, a series of direct reduction reactions take Reduction place; these can be simplified to: profile in the blast furnace FeO + C = Fe + CO At lower temperatures higher up in the furnace, a series of indirect reduction reactions take place, simplified to: FeO + CO = Fe + CO2 Analysis of carbon monoxide (CO) and carbon dioxide Process control requirements (CO2) give vital information on the efficiency of the reduction The advantages of process MS over conventional analysis processes. -
Potential Impacts on the Energy System at the Integrated Steelwork by Changing Injection Coal Types to the Blast
A publication of CHEMICAL ENGINEERING TRANSACTIONS The Italian Association VOL. 35, 2013 of Chemical Engineering www.aidic.it/cet Guest Editors: Petar Varbanov, Jiří Klemeš, Panos Seferlis, Athanasios I. Papadopoulos, Spyros Voutetakis Copyright © 2013, AIDIC Servizi S.r.l., ISBN 978-88-95608-26-6; ISSN 1974-9791 DOI: 10.3303/CET1335162 Potential Impacts on the Energy System at the Integrated Steelwork by Changing Injection Coal Types to the Blast Furnace Joel Orre*,a, Chuan Wanga, Johannes Larssonb, Erik Olssonb a 97512, Luleå, Sweden Swerea Mefos, Box 812, SE- b SSAB EMEA Oxelösund, SSAB SE-613 80, Oxelösund, Sweden [email protected] Pulverized coal is often injected into the blast furnaces (BFs) at the integrated steelworks as reducing agent for the hot metal production. The BF process will behave different depending on the injection coal used. The objective of this study is to investigate how different types of coal will influence the BF, and the total energy system at an integrated steel plant. The major process units covered in the model are coking plant, BF, reheating furnace at the rolling mill and a power plant. They are all linked to each other via the main products as well as process gases (i.e. blast furnace gas (BFG) and coke oven gas (COG)) and oxygen network. At the studied plant, the mixed gas of BFG and COG is used within the coking batteries at the coking plant and hot stoves at the BF. The fuel used at the reheating furnace is COG and oil with high heating values. In total, 13 different types of coal and one biomass charcoal are included in the study. -
Liquid Electric Automobile Fuels
Bridging Renewable Electricity with Transportation Fuels Grigorii Soloveichik ARPA-E workshop August 27, Denver, CO Imperative: reducing green house gases emission while preserving energy security • Fossil fuels used for power generation emit CO2 and other GHG that leads to dramatic climate change • Burning fossil fuels in internal combustion engines for transportation is responsible for about 1/3 of GHG emission • Replacement coal for natural gas reduced GHG emissions for grid scale power generation but replacement of liquid transportation fuels with NG is currently not viable due to low energy density of methane • Market penetration of electric vehicles is lower than anticipated due to high cost of batteries, long charge time and range anxiety Solution: replace fossil fuels with zero- emission regenerable fuels • More than 95% vehicles use liquid fuels, infrastructure in place • ICEs emit CO2 and other GHGs (hard to capture) • Electricity from renewable sources is clean and can be used directly (batteries) or to generate hydrogen to power fuel cells • Batteries are expensive; recharging time and range anxiety lead to low public acceptance • Hydrogen fuel cell vehicles are considered to be ultimate solution for long range transportation and dense urban areas Vehicle energy consumption and emissions (full energy cycle) Vehicle type Energy consumption, kWh/mile CO2 emissions, g/mile Average gasoline car 1.55 411 Gasoline car (Honda Accord) 1.08 286 Diesel car (FW Jetta) 1.11 299 Hybrid car (Prius) 0.79 212 BEV (Tesla) 1.09 (0.40 battery) -
The Future Role of Forest-Based Biofuels: Industrial Impacts in the Nordic Countries
energies Article The Future Role of Forest-Based Biofuels: Industrial Impacts in the Nordic Countries Eirik Ogner Jåstad 1 , Torjus Folsland Bolkesjø 1, Per Kristian Rørstad 1, Atle Midttun 2, Judit Sandquist 3 and Erik Trømborg 1,* 1 Faculty of Environmental Sciences and Natural Resource Management, Norwegian University of Life Sciences, P.O. Box 5003, NO-1432 Ås, Norway; [email protected] (E.O.J.); [email protected] (T.F.B.); [email protected] (P.K.R.) 2 BI Norwegian Business School, Nydalsveien 37, 0484 Oslo, Norway; [email protected] 3 SINTEF Energy Research, 7465 Trondheim, Norway; [email protected] * Correspondence: [email protected]; Tel.: +47-90-041-478 Abstract: This study applies a partial equilibrium forest sector model to analyse the impacts of biofuel deployment for road transport in the Nordic countries, when alternative use of the biomass resources and transport sector electrification are considered. We foresee a strong electrification of the transport sector, resulting in a demand for biofuels of approximately 2.5 billion L in 2035 and 1 billion L in 2050 in a 100% fossil-free base scenario. The simultaneous increase in demand from pulping industries and biofuel will cause an overall increase in wood use, of which the biofuels share will constitute approximately 20–25%. The utilization of harvest residues will increase more than 300% compared to the current level, since biofuel production will reallocate some of the current raw material used in district heating. Biofuel consumption in road transport will likely reduce after 2040 due to increasing electrification, but it is plausible that the declining domestic demand will be replaced by increasing demand from international biofuel markets in aviation and shipping. -
Liquid Fuel Treatment Systems
GER-3481C GE Power Generation Liquid Fuel Treatment Systems Howard J. Kaplan Technical Leader, Fluid Systems Engineering Kenneth E. Majchrzak Principal Engineer, Power Plant Engineering GE Power Systems GE Company Schenectady, NY GER-3481C GE Power Generation Liquid Fuel Treatment Systems Howard J. Kaplan Technical Leader, Fluid Systems Engineering Kenneth E. Majchrzak Principal Engineer, Power Plant Engineering GE Power Systems GE Company Schenectady, NY Howard J. Kaplan Howard Kaplan is Technical Leader of Gas Turbine Power Plant Fluid Systems. He has over 25 years’ experience in design and develop- ment of gas turbine auxiliary systems, serving three years as principal engineer for fuels-related systems. Current responsibilities include fuel oil, fuel gas, fuel purge, Dry Low NOx, atomizing air, water injection and lube oil. Kenneth E. Majchrzak Kenneth E. Majchrzak is a Principal Mechanical Engineer in the Power Plant Engineering Department. He is Technical Leader for the department on fuel systems, power plant pumps, and provides primary support for HRSGs. Ken joined GE in 1982 as Manager – Compressor Application Engineering in Fitchburg, Massachusetts. He has nearly 25 years’ experience with rotating equipment in the areas of application and systems design for aircraft gas turbines, process centrifugal compres- sors, radial inflow steam turbines and pumps. A lists of figures and tables appears at the end of this paper GER-3481C LIQUID FUEL TREATMENT SYSTEMS H. J. Kaplan and K. E. Majchrzak GE Power Systems Schenectady, NY INTRODUCTION The degree of the fuel treatment equipment GE heavy-duty gas turbines are capable of burn- sophistication, plant equipment investment, and ing a variety of liquid fuels, from petroleum naph- operating costs required for this equipment are thas to residuals. -
Combustion of Coal Combustion Is a Rapid Chemical Reaction Between Fuel and Oxygen
Combustion of Coal Combustion is a rapid chemical reaction between fuel and oxygen. When combustible elements of fuel combine with O2, heat energy comes out. During combustion combustible elements like Carbon, Sulfur, Hydrogen etc combine with oxygen and produce respective oxides. The source of oxygen in fuel combustion is air. By volume there is 21% of Oxygen presents in air and by weight it is 23.2%. Although there is 79% (by volume) nitrogen in air but it plays no role in combustion. Actually Nitrogen carries heat produced during combustion to steam boiler stack. As per combustion theory the quantity of air required for combustion is that which provides sufficient O2 to completely oxidize combustible elements of fuel. This quantity of air is normally known as STOICHIOMETRIC AIR requirement. Different types of coal combustion techniques Combustion of Coal Combustion may be defined as the rapid high temperature complicated chemical reaction of oxygen with carbon, hydrogen and sulphur of coal. These reactions follow mainly four steps 1. Formation of coal-oxygen complexes with evolution of heat. 2. Decomposition of these complexes with the generation of CO2 and H2O molecules and formation of carboxyl (COOH), carbonyl (C=O) and phenolic -OH groups along with more heat generation. 3. Decomposition of these groups to produce CO, CO2, H2, H2O and hydrocarbons such as ethane, ethylene, propylene etc. 4. Decomposition of aliphatic structure (relating to or denoting organic compounds in which carbon atoms form open chains (as in the alkanes), not aromatic rings.) with the formation of CO, CO2 and H2O. In low temperatures, the first step is developed faster than others.