Combustion of Coal Combustion Is a Rapid Chemical Reaction Between Fuel and Oxygen
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New Federal Law Addresses Excise Tax on LNG, LPG, And
Multistate Tax EXTERNAL ALERT New federal law addresses excise tax on LNG, LPG, and CNG August 13, 2015 Overview President Obama recently signed into law the Surface Transportation and Veterans Health Care Choice Improvement Act of 2015 (H.R. 3236).1 Effective January 1, 2016, the new law equalizes the federal excise tax treatment of liquefied natural gas (LNG) and liquefied petroleum gas (LPG) and provides further guidance applicable to the taxation of compressed natural gas (CNG). This Tax Alert summarizes these federal excise tax law changes. The federal excise tax on alternative fuels Currently, under Internal Revenue Code (I.R.C.) §4041, the federal excise tax on “alternative fuels” is imposed when such fuels are sold for use or used as a fuel in a motor vehicle or motorboat.2 The term “alternative fuels” includes, but is not limited to, LNG, CNG, and LPG.3 LNG is currently subject to tax at the federal diesel fuel tax rate of 24.3 cents per gallon.4 However, LNG contains a lower energy content than diesel. According to the Oak Ridge National Laboratory, LNG has an energy content of 74,700 Btu per gallon (lower heating value), while diesel has an energy content of 128,450 Btu per gallon (lower heating value).5 Therefore, one gallon of LNG has the energy equivalency of 58 percent of one gallon of diesel fuel, although LNG is currently taxed as having the energy equivalency of 100 percent of one gallon of diesel fuel.6 Similarly, LPG is currently subject to tax at the federal gasoline tax rate of 18.3 cents per gallon.7 However, LPG contains a lower energy content than gasoline. -
Final Report Study on the Potential of Increased Use of LPG for Cooking in Developing Countries
Final Report Study on the Potential of Increased Use of LPG for Cooking in Developing Countries September 2020 TABLE OF CONTENTS Executive Summary ....................................................................................................................................................................... 2 List of Abbreviations ...................................................................................................................................................................... 6 Preface .......................................................................................................................................................................................... 7 1 Introduction.......................................................................................................................................................................... 8 1.1 General ................................................................................................................................................................................. 8 1.2 Background ........................................................................................................................................................................... 8 2 Purpose and Scope of the Study ............................................................................................................................................ 9 2.1 Purpose of the Study ........................................................................................................................................................... -
Liquefied Petroleum Gas (LPG)
Liquefied Petroleum Gas (LPG) Demand, Supply and Future Perspectives for Sudan Synthesis report of a workshop held in Khartoum, 12-13 December 2010 The workshop was funded by UKaid from the Department for International Development Cover image: © UNAMID / Albert Gonzalez Farran This report is available online at: www.unep.org/sudan Disclaimer The material in this report does not necessarily represent the views of any of the organisations involved in the preparation and hosting of the workshop. It must be noted that some time has passed between the workshop and the dissemination of this report, during which some important changes have taken place, not least of which is the independence of South Sudan, a fact which greatly affects the national energy context. Critically, following the independence, the rate of deforestation in the Republic of Sudan has risen from 0.7% per year to 2.2% per year, making many of the discussions within this document all the more relevant. Whilst not directly affecting the production of LPG, which is largely derived from oil supplies north of the border with South Sudan, the wider context of the economics of the energy sector, and the economy as a whole, have changed. These changes are not reflected in this document. This being said, it is strongly asserted that this document still represents a useful contribution to the energy sector, particularly given its contribution to charting the breadth of perspectives on LPG in the Republic of Sudan. Liquefied Petroleum Gas (LPG) Demand, Supply and Future Perspectives for Sudan Synthesis report of a workshop held in Khartoum, 12-13 December 2010 A joint publication by: Ministry of Environment, Forestry and Physical Development – Sudan, Ministry of Petroleum – Sudan, United Kingdom Department for International Development, United Nations Development Programme and United Nations Environment Programme Table of contents Acronyms and abbreviations . -
Influence of the Use of Liquefied Petroleum Gas (LPG) Systems In
energies Article Influence of the Use of Liquefied Petroleum Gas (LPG) Systems in Woodchippers Powered by Small Engines on Exhaust Emissions and Operating Costs Łukasz Warguła 1,* , Mateusz Kukla 1 , Piotr Lijewski 2, Michał Dobrzy ´nski 2 and Filip Markiewicz 2 1 Institute of Machine Design, Faculty of Mechanical Engineering, Poznan University of Technology, Piotrowo 3, PL-60965 Poznan, Poland; [email protected] 2 Institute of Internal Combustion Engines and Drives, Faculty of Civil Engineering and Transport, Poznan University of Technology, Piotrowo 3, PL-60965 Poznan, Poland; [email protected] (P.L.); [email protected] (M.D.); fi[email protected] (F.M.) * Correspondence: [email protected]; Tel.: +48-(61)-665-20-42 Received: 12 August 2020; Accepted: 3 November 2020; Published: 4 November 2020 Abstract: The use of alternative fuels is a contemporary trend in science aimed at the protection of non-renewable resources, reducing the negative impact on people and reducing the negative impact on the natural environment. Liquefied petroleum gas (LPG) is an alternative fuel within the meaning of the European Union Directive (2014/94/UE), as it is an alternative for energy sources derived from crude oil. The use of LPG fuel in low-power internal combustion engines is one of the currently developed scientific research directions. It results from the possibility of limiting air pollutant emissions compared to the commonly used gasoline and the lower cost of this fuel in many countries. By “gasoline 95” the Authors mean non-lead petrol as a flammable liquid that is used primarily as a fuel in most spark-ignited internal combustion engines, whereas 95 is an octane rating (octane number). -
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. -
Prediction of Producer Gas Composition for Small Scale Commercial Downdraft Gasifiers
PREDICTION OF PRODUCER GAS COMPOSITION FOR SMALL SCALE COMMERCIAL DOWNDRAFT GASIFIERS H Roesch*, J Dascomb, B Greska, A Krothapalli *Corresponding Author email: [email protected] *Corresponding Author phone: +18504967682 Energy and Sustainability Center, Florida State University 2525 Pottsdamer St, #229A, Tallahassee, Fl 32310 ABSTRACT: The goal of this study was to produce a model predicting the composition and heating value of producer gas made from a small scale (20-250 kWth), down-draft gasifier. Due the non-ideal conditions in this type of gasifier, classical thermodynamic equilibrium models are inaccurate. A more reliable prediction model for gas produced in a system of this size and type is needed. Eight biomass feedstocks were gasified and analyzed for this study. The pelletized feedstocks chosen were; alfalfa, algae, field grass, hemp, miscanthus, peanut shells, pine, and municipal solid waste. The feedstocks were chosen for their wide ranging availability and low costs. The commercial downdraft gasifier used was an Ankur Scientific WBG-20. This air-fed gasifier is capable of producing synthesis gas at a rate of up to 60 Nm3/hr (50 kWth). Each feedstock was first characterized by proximate and ultimate analysis, and then the synthesis gas was analyzed by gas chromatography. The large variation of reaction temperatures and equivalence ratios occurring in the economic downdraft gasifier reduced the accuracy of the conventional thermodynamic equilibrium simulation. The synthesis gas produced in these tests was used to create a more applicable model for estimating composition and heating value for this type of system. The model developed from these tests estimates the heating value of the synthesis gas produced from the ultimate and proximate analysis of the feedstock with an average error of 5% over all feedstocks tested. -
2002-00201-01-E.Pdf (Pdf)
report no. 2/95 alternative fuels in the automotive market Prepared for the CONCAWE Automotive Emissions Management Group by its Technical Coordinator, R.C. Hutcheson Reproduction permitted with due acknowledgement Ó CONCAWE Brussels October 1995 I report no. 2/95 ABSTRACT A review of the advantages and disadvantages of alternative fuels for road transport has been conducted. Based on numerous literature sources and in-house data, CONCAWE concludes that: · Alternatives to conventional automotive transport fuels are unlikely to make a significant impact in the foreseeable future for either economic or environmental reasons. · Gaseous fuels have some advantages and some growth can be expected. More specifically, compressed natural gas (CNG) and liquefied petroleum gas (LPG) may be employed as an alternative to diesel fuel in urban fleet applications. · Bio-fuels remain marginal products and their use can only be justified if societal and/or agricultural policy outweigh market forces. · Methanol has a number of disadvantages in terms of its acute toxicity and the emissions of “air toxics”, notably formaldehyde. In addition, recent estimates suggest that methanol will remain uneconomic when compared with conventional fuels. KEYWORDS Gasoline, diesel fuel, natural gas, liquefied petroleum gas, CNG, LNG, Methanol, LPG, bio-fuels, ethanol, rape seed methyl ester, RSME, carbon dioxide, CO2, emissions. ACKNOWLEDGEMENTS This literature review is fully referenced (see Section 12). However, CONCAWE is grateful to the following for their permission to quote in detail from their publications: · SAE Paper No. 932778 ã1993 - reprinted with permission from the Society of Automotive Engineers, Inc. (15) · “Road vehicles - Efficiency and emissions” - Dr. Walter Ospelt, AVL LIST GmbH. -
Cleaning Ucg Synthesis
Underground Coal Gasification (UCG), its Potential Prospects and its Challenges Dr. Duncan Seddon, FRACI, CChem, MSPE, Duncan Seddon & Associates Pty Ltd Email: [email protected] Dr. Mike Clarke, FIEAust, CPEng, FAusIMM, RPEQ, M.E.T.T.S. Pty Ltd Email: [email protected] Abstract: Coal is widely available in most parts of the world. Underground Coal Gasification (UCG) gives the promise of turning many poor quality coal resources into exploitable reserves by delivering energy in the form of synthesis gas, potentially at very low cost. The synthesis gas can be used for generation of electricity and the production of fuels and chemicals by commercially proven technology. Furthermore, any carbon present in the synthesis gas not used for downstream products could be easily separated and geo-sequestrated. This could extend the Fossil Fuel Age by providing low cost energy for developing and developed countries alike. Unfortunately, as Australian experience has shown, UCG also comes with technical and environmental challenges that are still not fully resolved. The paper outlines key developments in UCG and issues raised by Australian experience, particularly in regard to the contamination of acquifers. The paper discusses the quality of UCG synthesis gas and its potential use in downstream applications. The clean-up steps required for various downstream applications are described. A key hurdle to up-take of UCG is the overall cost of clean-up which has to be added to the cost of UCG production. This cost is discussed and the potential of UCG as a major new feedstock described. 1.0 Introduction Underground Coal Gasification (UCG) as a source of synthesis gas (syn-gas) for power generation, liquid fuels production and/or chemicals and fertiliser manufacture has been made to look beguilingly simple and straightforward by many of it proponents. -
Scale Gas-‐To-‐Methanol Conversion by Engine Reformers
System Model of Small-Scale Gas-to-Methanol Conversion by Engine Reformers By Angela J. Acocella B.S., Mechanical Engineering Rensselaer Polytechnic Institute, 2012 Submitted to the Engineering Systems Division in partial fulfillment of the requirements for the degree of Master of Science in Technology & Policy at the Massachusetts Institute of Technology June 2015 © 2015 Massachusetts Institute of Technology, All rights reserved Signature of Author............................................................................................................. Technology & Policy Program; Engineering Systems Division May 8, 2015 Certified by.............................................................................................................................. Daniel R. Cohn Research Scientist, MIT Energy Initiative Thesis Supervisor Accepted by............................................................................................................................. Dava J. Newman Professor of Aeronautics and Astronautics and Engineering Systems Director, Technology and Policy Program 2 System Model of Small-Scale Gas-to-Methanol Conversion by Engine Reformers by Angela J. Acocella Submitted to the Engineering Systems Division On May 8, 2015 in partial fulfillment of the requirements for the degree of Master of Science in Technology & Policy ABSTRACT As global energy demands grow and environmental concerns over resource extraction methods intensify, high impact solutions are becoming increasingly essential. Venting and flaring of associated -
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. -
Challenges and Opportunities of Biomethane for Pipeline Injection In
CHALLENGES & OPPORTUNITIES OF BIOMETHANE FOR PIPELINE INJECTION IN CALIFORNIA Valentino Tiangco, Ph.D. ER&D Department 15th Annual LMOP Conference and Project Expo Hilton Baltimore Hotel Baltimore, MD January 17-19, 2012 Powering forward. Together. Overview: • SMUD • Benefits • Challenges • Overcoming Challenges • SMUD’s Renewable Energy Mix • Strategic Approach www.smud.org • Opportunities • Summary SMUD – Owned By Customers • Not for Profit, Publicly Owned Utility • Sacramento County (small part of Placer County) • Almost 600,000 Customers; 1.4 Million Population • 6th Largest in U.S. • 7 Member Board of Directors • Elected by Ratepayers • Not a Part of City or County • Manage Balancing Authority in Northern California (BANC) • Low Rates, Innovative & Green! 3 Benefits of Biomethane • Unlike wind and solar, generation from biomethane is not intermittent and can be dispatched to fill-in the gaps and promote system reliability. • Reduces GHG emissions by displacing natural gas and reducing release of methane to the atmosphere. • Increases productive development and use of renewable resources from organic wastes. • Biomethane from renewable sources like dairy digesters and landfills can be a reliable source of renewable fuel that can power the cleanest and most efficient electricity generation facilities in the California. • Biomethane flexibility of use because of transportation and storage capabilities, • The opportunity to use a low cost renewable fuel (biomethane) when firing combined cycle generators thus producing renewable electrons at highest efficiencies, and • Biogas has very low carbon footprint, rated as the lowest carbon producing fuel through the CEC’s proceedings for the Low Carbon Fuel Standard. • Creates local jobs by keeping local power plants operating and keeping electricity costs lower, which helps local businesses to prosper and add jobs. -
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.