The Future of Gasification
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U.S. Energy in the 21St Century: a Primer
U.S. Energy in the 21st Century: A Primer March 16, 2021 Congressional Research Service https://crsreports.congress.gov R46723 SUMMARY R46723 U.S. Energy in the 21st Century: A Primer March 16, 2021 Since the start of the 21st century, the U.S. energy system has changed tremendously. Technological advances in energy production have driven changes in energy consumption, and Melissa N. Diaz, the United States has moved from being a net importer of most forms of energy to a declining Coordinator importer—and a net exporter in 2019. The United States remains the second largest producer and Analyst in Energy Policy consumer of energy in the world, behind China. Overall energy consumption in the United States has held relatively steady since 2000, while the mix of energy sources has changed. Between 2000 and 2019, consumption of natural gas and renewable energy increased, while oil and nuclear power were relatively flat and coal decreased. In the same period, production of oil, natural gas, and renewables increased, while nuclear power was relatively flat and coal decreased. Overall energy production increased by 42% over the same period. Increases in the production of oil and natural gas are due in part to technological improvements in hydraulic fracturing and horizontal drilling that have facilitated access to resources in unconventional formations (e.g., shale). U.S. oil production (including natural gas liquids and crude oil) and natural gas production hit record highs in 2019. The United States is the largest producer of natural gas, a net exporter, and the largest consumer. Oil, natural gas, and other liquid fuels depend on a network of over three million miles of pipeline infrastructure. -
Storing Syngas Lowers the Carbon Price for Profitable Coal Gasification
Carnegie Mellon Electricity Industry Center Working Paper CEIC-07-10 www.cmu.edu/electricity Storing syngas lowers the carbon price for profitable coal gasification ADAM NEWCOMER AND JAY APT Carnegie Mellon Electricity Industry Center, Tepper School of Business, and Department of Engineering and Public Policy, 254 Posner Hall, Carnegie Mellon University, Pittsburgh, Pennsylvania 15213 Integrated gasification combined cycle (IGCC) electric power generation systems with carbon capture and sequestration have desirable environmental qualities, but are not profitable when the carbon dioxide price is less than approximately $50 per metric ton. We examine whether an IGCC facility that operates its gasifier continuously but stores the syngas and produces electricity only when daily prices are high may be profitable at significantly lower CO2 prices. Using a probabilistic analysis, we have calculated the plant-level return on investment (ROI) and the value of syngas storage for IGCC facilities located in the US Midwest using a range of storage configurations. Adding a second turbine to use the stored syngas to generate electricity at peak hours and implementing 12 hours of above ground high pressure syngas storage significantly increases the ROI and net present value. Storage lowers the carbon price at which IGCC enters the US generation mix by approximately 25%. 1 Carnegie Mellon Electricity Industry Center Working Paper CEIC-07-10 www.cmu.edu/electricity Introduction Producing electricity from coal-derived synthesis gas (syngas) in an integrated gasification combined cycle (IGCC) facility can improve criteria pollutant performance over other coal-fueled technologies such as pulverized coal (PC) facilities [1-5] and can be implemented with carbon capture and sequestration. -
Substitute Natural Gas from Biomass Gasification
Rapport SGC 187 Substitute natural gas from biomass gasification ©Svenskt Gastekniskt Center – mars 2008 Haldor Topsoe's methanation process TREMP Per Tunå, Lund Institute of Technology Rapport SGC 187 •1102-7371 • ISRN SGC-R-187-SE SGC:s FÖRORD FUD-projekt inom Svenskt Gastekniskt Center AB avrapporteras normalt i rapporter som är fritt tillgängliga för envar intresserad. SGC svarar för utgivningen av rapporterna medan uppdragstagarna för respek- tive projekt eller rapportförfattarna svarar för rapporternas innehåll. Den som utnyttjar eventuella beskrivningar, resultat eller dylikt i rapporterna gör detta helt på eget ansvar. Delar av rapport får återges med angivande av källan. En förteckning över hittills utgivna SGC-rapporter finns på SGC:s hemsida www.sgc.se. Svenskt Gastekniskt Center AB (SGC) är ett samarbetsorgan för företag verk- samma inom energigasområdet. Dess främsta uppgift är att samordna och effektivisera intressenternas insatser inom områdena forskning, utveckling och demonstration (FUD). SGC har följande delägare: Svenska Gasföreningen, E.ON Gas Sverige AB, E.ON Sverige AB, Göteborg Energi AB, Lunds Energikoncernen AB (publ) och Öresundskraft AB. Följande parter har gjort det möjligt att genomföra detta utvecklingsprojekt: E.ON Gas Sverige AB Göteborg Energi AB SVENSKT GASTEKNISKT CENTER AB Jörgen Held Acknowledgements I would like to thank the following people for their support throughout this thesis work. Professor Hans T. Karlsson at the Department of Chemical Engineering for his dedication to find an interesting thesis work for me. Christian Hulteberg at the Department of Chemical Engineering as he always has a good answer for everything and always had time to help me. Owe Jönsson at E.ON Gas Sverige AB and Lars A Andersson at Göteborg Energi AB for taking their time and to give valuable suggestions and ideas. -
Maximising the Value of Surplus Ethane and Cost-Effective Design to Handle Rich Lng
Poster PO-25 MAXIMISING THE VALUE OF SURPLUS ETHANE AND COST-EFFECTIVE DESIGN TO HANDLE RICH LNG CC Yang Process and Technology Director, LNG Foster Wheeler USA, 2020 Dairy Ashford, Houston, TX 77077, USA [email protected] Geoffrey Bothamley Business Development Manager Oil and Gas Foster Wheeler Energy Limited, Shinfield Park, Reading, Berkshire, RG2 9FW, UK [email protected] ABSTRACT Gas companies have strict requirements for the composition of the natural gas sent out from their LNG receiving terminals in order to satisfy customer requirements in terms of calorific value and quality of the composition. For LNG receiving terminals serving the North American market particularly, the C2+ content and heating value specifications are lower than most natural gases and most existing LNG baseload plants. Cost-effective management of these components enhances the LNG value chain, increasing flexibility in sourcing LNG cargoes. Several alternatives for managing C2+ components in the LNG value chain exist. Generally, extraction can occur at either the receiving terminal or upstream of the liquefaction plant. In many cases it is not cost-effective to reduce the C2 at the baseload plant, as it will reduce the LNG production rate and there may be no local market. Some LNG production plant locations, however, have grown to a size that would meet minimum economic scale for a steam cracker taking C2 and C3 as feedstock for ethylene and propylene production. To accept cargoes of rich LNG, the LNG receiving terminal has to be able to manage the C2+ components in an economically efficient manner. This paper presents a cost- effective C2+ management process design for send-out gas at the LNG receiving terminal. -
Process Technologies and Projects for Biolpg
energies Review Process Technologies and Projects for BioLPG Eric Johnson Atlantic Consulting, 8136 Gattikon, Switzerland; [email protected]; Tel.: +41-44-772-1079 Received: 8 December 2018; Accepted: 9 January 2019; Published: 15 January 2019 Abstract: Liquified petroleum gas (LPG)—currently consumed at some 300 million tonnes per year—consists of propane, butane, or a mixture of the two. Most of the world’s LPG is fossil, but recently, BioLPG has been commercialized as well. This paper reviews all possible synthesis routes to BioLPG: conventional chemical processes, biological processes, advanced chemical processes, and other. Processes are described, and projects are documented as of early 2018. The paper was compiled through an extensive literature review and a series of interviews with participants and stakeholders. Only one process is already commercial: hydrotreatment of bio-oils. Another, fermentation of sugars, has reached demonstration scale. The process with the largest potential for volume is gaseous conversion and synthesis of two feedstocks, cellulosics or organic wastes. In most cases, BioLPG is produced as a byproduct, i.e., a minor output of a multi-product process. BioLPG’s proportion of output varies according to detailed process design: for example, the advanced chemical processes can produce BioLPG at anywhere from 0–10% of output. All these processes and projects will be of interest to researchers, developers and LPG producers/marketers. Keywords: Liquified petroleum gas (LPG); BioLPG; biofuels; process technologies; alternative fuels 1. Introduction Liquified petroleum gas (LPG) is a major fuel for heating and transport, with a current global market of around 300 million tonnes per year. -
Gasification of Woody Biomasses and Forestry Residues
fermentation Article Gasification of Woody Biomasses and Forestry Residues: Simulation, Performance Analysis, and Environmental Impact Sahar Safarian 1,*, Seyed Mohammad Ebrahimi Saryazdi 2, Runar Unnthorsson 1 and Christiaan Richter 1 1 Mechanical Engineering and Computer Science, Faculty of Industrial Engineering, University of Iceland, Hjardarhagi 6, 107 Reykjavik, Iceland; [email protected] (R.U.); [email protected] (C.R.) 2 Department of Energy Systems Engineering, Sharif University of Technologies, Tehran P.O. Box 14597-77611, Iran; [email protected] * Correspondence: [email protected] Abstract: Wood and forestry residues are usually processed as wastes, but they can be recovered to produce electrical and thermal energy through processes of thermochemical conversion of gasification. This study proposes an equilibrium simulation model developed by ASPEN Plus to investigate the performance of 28 woody biomass and forestry residues’ (WB&FR) gasification in a downdraft gasifier linked with a power generation unit. The case study assesses power generation in Iceland from one ton of each feedstock. The results for the WB&FR alternatives show that the net power generated from one ton of input feedstock to the system is in intervals of 0 to 400 kW/ton, that more that 50% of the systems are located in the range of 100 to 200 kW/ton, and that, among them, the gasification system derived by tamarack bark significantly outranks all other systems by producing 363 kW/ton. Moreover, the environmental impact of these systems is assessed based on the impact categories of global warming (GWP), acidification (AP), and eutrophication (EP) potentials and Citation: Safarian, S.; Ebrahimi normalizes the environmental impact. -
The Future Role of Gas in Transport
The Future Role of Gas in Transport Green Gas Transport Pathway 2 Green Gas Transport Pathways Acknowledgements A Network Innovation Allowance project report for Cadent, Gas Networks Ireland, National Grid, Northern Gas Networks, SGN, Wales and West Utilities Green Gas Transport Pathways 3 Executive Summary Project Background, Aims and Objectives This is a Network Innovation Allowance funded project Green gases overseen by a steering group comprising the UK and Ireland gas network operators (Cadent, Gas Networks Ireland, This report discusses the future role of ‘green gases’ which National Grid, Northern Gas Networks, SGN, Wales and West). are biomethane and hydrogen produced from low- and The project follows on from previous studies1 that modelled zero-carbon sources, each produced via two main methods: the role of green gases in decarbonising the GB economy. The Biomethane from Anaerobic Digestion (AD): A role of this study is to understand the transition from the GB mature technology for turning biological material into economy today to a decarbonised economy in 2050, focusing a non-fossil form of natural gas (methane). AD plants on how the transition is achieved and the competing and produce biogas which must then be upgraded to biomethane. complementary nature of different low and zero emission fuels and technologies over time. Biomethane from Bio-Substitute Natural Gas (Bio-SNG): This technology is at an earlier stage of While the project covers the whole economy it focuses on development than AD, but has the potential to unlock transport, especially trucks, as an early adopter of green other feedstocks for biomethane production such as waste gases and as a key enabler of the transition. -
Natural Gas and Propane
Construction Concerns: Natural Gas and Propane Article by Gregory Havel September 28, 2015 For the purposes of this article, I will discuss the use of natural gas and propane [liquefied propane (LP)] gas in buildings under construction, in buildings undergoing renovation, and in the temporary structures that are found on construction job sites including scaffold enclosures. In permanent structures, natural gas is carried by pipe from the utility company meter to the location of the heating appliances. Natural gas from utility companies is lighter than air and is odorized. In temporary structures and in buildings under construction or renovation, the gas may be carried from the utility company meter by pipe or a hose rated for natural gas at the pressure to be used to the location of the heating appliances. These pipes and hoses must be properly supported and must be protected from damage including from foot and wheeled traffic. The hoses, pipes, and connections must be checked regularly for leaks. For permanent and temporary structures, LP gas is usually stored in horizontal tanks outside the structure (photo 1) at a distance from the structure. September 28, 2015 (1) In Photo 1, note the frost on the bottom third of the tank that indicates the approximate amount of LP that is left in the tank. LP gas for fuel is heavier than air and is odorized. It is carried from the tank to the heating appliances by pipe or hose rated for LP gas at the pressure to be used. As it is for natural gas, these pipes and hoses must be properly supported and protected from damage including from foot and wheeled traffic. -
Harmon of Energ THIRD REVIS Onisation of Definitions Rgy
Harmononisation of Definitions of Energrgy Products and Flows THIRD REVISISION OF THE DEFINITIOIONS Part 1: Flows IEA,A, Paris, 21 December 2009 Table of Contents Page Note by Tim Simmons ............................................................................................................................. 5 Flow Structure ......................................................................................................................................... 7 Definition of National Territory (not in flow classification) ................................................................... 9 Supply .................................................................................................................................................... 11 Production .............................................................................................................................................. 13 Receipts from Other Sources ................................................................................................................. 16 Imports and Exports .............................................................................................................................. 18 International Marine Bunkers ................................................................................................................ 21 International Aviation Bunkers ............................................................................................................. 22 Stocks (not in flow classification) ........................................................................................................ -
Review of Technologies for Gasification of Biomass and Wastes
Review of Technologies for Gasification of Biomass and Wastes Final report NNFCC project 09/008 A project funded by DECC, project managed by NNFCC and conducted by E4Tech June 2009 Review of technology for the gasification of biomass and wastes E4tech, June 2009 Contents 1 Introduction ................................................................................................................... 1 1.1 Background ............................................................................................................................... 1 1.2 Approach ................................................................................................................................... 1 1.3 Introduction to gasification and fuel production ...................................................................... 1 1.4 Introduction to gasifier types .................................................................................................... 3 2 Syngas conversion to liquid fuels .................................................................................... 6 2.1 Introduction .............................................................................................................................. 6 2.2 Fischer-Tropsch synthesis ......................................................................................................... 6 2.3 Methanol synthesis ................................................................................................................... 7 2.4 Mixed alcohols synthesis ......................................................................................................... -
Proposal for Development of Dry Coking/Coal
Development of Coking/Coal Gasification Concept to Use Indiana Coal for the Production of Metallurgical Coke, Liquid Transportation Fuels, Fertilizer, and Bulk Electric Power Phase II Final Report September 30, 2007 Submitted by Robert Kramer, Ph.D. Director, Energy Efficiency and Reliability Center Purdue University Calumet Table of Contents Page Executive Summary ………………………………………………..…………… 3 List of Figures …………………………………………………………………… 5 List of Tables ……………………………………………………………………. 6 Introduction ……………………………………………………………………… 7 Process Description ……………………………………………………………. 11 Importance to Indiana Coal Use ……………………………………………… 36 Relevance to Previous Studies ………………………………………………. 40 Policy, Scientific and Technical Barriers …………………………………….. 49 Conclusion ………………………………………………………………………. 50 Appendix ………………………………………………………………………… 52 2 Executive Summary Coke is a solid carbon fuel and carbon source produced from coal that is used to melt and reduce iron ore. Although coke is an absolutely essential part of iron making and foundry processes, currently there is a shortfall of 5.5 million tons of coke per year in the United States. The shortfall has resulted in increased imports and drastic increases in coke prices and market volatility. For example, coke delivered FOB to a Chinese port in January 2004 was priced at $60/ton, but rose to $420/ton in March 2004 and in September 2004 was $220/ton. This makes clear the likelihood that prices will remain high. This effort that is the subject of this report has considered the suitability of and potential processes for using Indiana coal for the production of coke in a mine mouth or local coking/gasification-liquefaction process. Such processes involve multiple value streams that reduce technical and economic risk. Initial results indicate that it is possible to use blended coal with up to 40% Indiana coal in a non recovery coke oven to produce pyrolysis gas that can be selectively extracted and used for various purposes including the production of electricity and liquid transportation fuels and possibly fertilizer and hydrogen. -
Comparison Between Hydrogen and Syngas Fuels in an Integrated Micro Gas Turbine/Solar Field with Storage
energies Article Comparison between Hydrogen and Syngas Fuels in an Integrated Micro Gas Turbine/Solar Field with Storage Maria Cristina Cameretti, Alessandro Cappiello, Roberta De Robbio * and Raffaele Tuccillo Department of Industrial Engineering, University of Naples Federico II, 80125 Naples, Italy; [email protected] (M.C.C.); [email protected] (A.C.); raff[email protected] (R.T.) * Correspondence: [email protected] Received: 9 June 2020; Accepted: 3 September 2020; Published: 12 September 2020 Abstract: In recent years, the use of alternative fuels in thermal engine power plants has gained more and more attention, becoming of paramount importance to overcome the use of fuels from fossil sources and to reduce polluting emissions. The present work deals with the analysis of the response to two different gas fuels—i.e., hydrogen and a syngas from agriculture product—of a 30 kW micro gas turbine integrated with a solar field. The solar field included a thermal storage system to partially cover loading requests during night hours, reducing fuel demand. Additionally, a Heat Recovery Unit was included in the plant considered and the whole plant was simulated by Thermoflex® code. Thermodynamics analysis was performed on hour-to-hour basis, for a given day as well as for 12 months; subsequently, an evaluation of cogeneration efficiency as well as energy saving was made. The results are compared against plant performance achieved with conventional natural gas fueling. After analyzing the performance of the plant through a thermodynamic analysis, the study was complemented with CFD simulations of the combustor, to evaluate the combustion development and pollutant emissions formation, particularly of NOx, with the two fuels considered using Ansys-Fluent code, and a comparison was made.