Energy and the Hydrogen Economy
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Review of Market for Octane Enhancers
May 2000 • NREL/SR-580-28193 Review of Market for Octane Enhancers Final Report J.E. Sinor Consultants, Inc. Niwot, Colorado National Renewable Energy Laboratory 1617 Cole Boulevard Golden, Colorado 80401-3393 NREL is a U.S. Department of Energy Laboratory Operated by Midwest Research Institute • Battelle • Bechtel Contract No. DE-AC36-99-GO10337 May 2000 • NREL/SR-580-28193 Review of Market for Octane Enhancers Final Report J.E. Sinor Consultants, Inc. Niwot, Colorado NREL Technical Monitor: K. Ibsen Prepared under Subcontract No. TXE-0-29113-01 National Renewable Energy Laboratory 1617 Cole Boulevard Golden, Colorado 80401-3393 NREL is a U.S. Department of Energy Laboratory Operated by Midwest Research Institute • Battelle • Bechtel Contract No. DE-AC36-99-GO10337 NOTICE This report was prepared as an account of work sponsored by an agency of the United States government. Neither the United States government nor any agency thereof, nor any of their employees, makes any warranty, express or implied, or assumes any legal liability or responsibility for the accuracy, completeness, or usefulness of any information, apparatus, product, or process disclosed, or represents that its use would not infringe privately owned rights. Reference herein to any specific commercial product, process, or service by trade name, trademark, manufacturer, or otherwise does not necessarily constitute or imply its endorsement, recommendation, or favoring by the United States government or any agency thereof. The views and opinions of authors expressed herein do not necessarily state or reflect those of the United States government or any agency thereof. Available electronically at http://www.doe.gov/bridge Available for a processing fee to U.S. -
Hydrogen Storage Cost Analysis (ST100)
This presentation contains no proprietary, confidential, or otherwise restricted information. 2020 DOE Hydrogen and Fuel Cells Program Review Hydrogen Storage Cost Analysis (ST100) Cassidy Houchins (PI) Brian D. James Strategic Analysis Inc. 31 May 2020 Overview Timeline Barriers Project Start Date: 9/30/16 A: System Weight and Volume Project End Date: 9/29/21 B: System Cost % complete: ~70% (in year 4 of 5) K: System Life-Cycle Assessment Budget Partners Total Project Budget: $999,946 Pacific Northwest National Laboratory (PNNL) Total DOE Funds Spent: ~$615,000 Argonne National Lab (ANL) (through March 2020 , excluding Labs) 2 Relevance • Objective – Conduct rigorous, independent, and transparent, bottoms-up techno- economic analysis of H2 storage systems. • DFMA® Methodology – Process-based, bottoms-up cost analysis methodology which projects material and manufacturing cost of the complete system by modeling specific manufacturing steps. – Predicts the actual cost of components or systems based on a hypothesized design and set of manufacturing & assembly steps – Determines the lowest cost design and manufacturing processes through repeated application of the DFMA® methodology on multiple design/manufacturing potential pathways. • Results and Impact – DFMA® analysis can be used to predict costs based on both mature and nascent components and manufacturing processes depending on what manufacturing processes and materials are hypothesized. – Identify the cost impact of material and manufacturing advances and to identify areas of R&D interest. – Provide insight into which components are critical to reducing the costs of onboard H2 storage and to meeting DOE cost targets 3 Approach: DFMA® methodology used to track annual cost impact of technology advances What is DFMA®? • DFMA® = Design for Manufacture & Assembly = Process-based cost estimation methodology • Registered trademark of Boothroyd-Dewhurst, Inc. -
Net Zero by 2050 a Roadmap for the Global Energy Sector Net Zero by 2050
Net Zero by 2050 A Roadmap for the Global Energy Sector Net Zero by 2050 A Roadmap for the Global Energy Sector Net Zero by 2050 Interactive iea.li/nzeroadmap Net Zero by 2050 Data iea.li/nzedata INTERNATIONAL ENERGY AGENCY The IEA examines the IEA member IEA association full spectrum countries: countries: of energy issues including oil, gas and Australia Brazil coal supply and Austria China demand, renewable Belgium India energy technologies, Canada Indonesia electricity markets, Czech Republic Morocco energy efficiency, Denmark Singapore access to energy, Estonia South Africa demand side Finland Thailand management and France much more. Through Germany its work, the IEA Greece advocates policies Hungary that will enhance the Ireland reliability, affordability Italy and sustainability of Japan energy in its Korea 30 member Luxembourg countries, Mexico 8 association Netherlands countries and New Zealand beyond. Norway Poland Portugal Slovak Republic Spain Sweden Please note that this publication is subject to Switzerland specific restrictions that limit Turkey its use and distribution. The United Kingdom terms and conditions are available online at United States www.iea.org/t&c/ This publication and any The European map included herein are without prejudice to the Commission also status of or sovereignty over participates in the any territory, to the work of the IEA delimitation of international frontiers and boundaries and to the name of any territory, city or area. Source: IEA. All rights reserved. International Energy Agency Website: www.iea.org Foreword We are approaching a decisive moment for international efforts to tackle the climate crisis – a great challenge of our times. -
Hydrogen Station Compression, Storage, and Dispensing Technical Status and Costs
Hydrogen Station Compression, Storage, and Dispensing Technical Status and Costs Independent Review Published for the U.S. Department of Energy Hydrogen and Fuel Cells Program NREL is a national laboratory of the U.S. Department of Energy, Office of Energy NREL is a national laboratory of the U.S. Department of Energy,Efficiency & Renewable Energy, operated by the Alliance for Sustainable Energy, LLC. Office of Energy Efficiency & Renewable Energy, operated by the Alliance for Sustainable Energy, LLC. Technical Report NREL/BK-6A10-58564 May 2014 Contract No. DE -AC36-08GO28308 Hydrogen Station Compression, Storage, and Dispensing Technical Status and Costs G. Parks, R. Boyd, J. Cornish, and R. Remick Independent Peer Review Team NREL Technical Monitor: Neil Popovich NREL is a national laboratory of the U.S. Department of Energy, Office of Energy Efficiency & Renewable Energy, operated by the Alliance for Sustainable Energy, LLC. National Renewable Energy Laboratory Technical Report 15013 Denver West Parkway NREL/BK-6A10-58564 Golden, CO 80401 May 2014 303-275-3000 • www.nrel.gov Contract No. DE-AC36-08GO28308 NOTICE This report was prepared as an account of work sponsored by an agency of the United States government. Neither the United States government nor any agency thereof, nor any of their employees, makes any warranty, express or implied, or assumes any legal liability or responsibility for the accuracy, completeness, or usefulness of any information, apparatus, product, or process disclosed, or represents that its use would not infringe privately owned rights. Reference herein to any specific commercial product, process, or service by trade name, trade- mark, manufacturer, or otherwise does not necessarily constitute or imply its endorsement, recommendation, or favoring by the United States government or any agency thereof. -
Combustion and Heat Release Characteristics of Biogas Under Hydrogen- and Oxygen-Enriched Condition
energies Article Combustion and Heat Release Characteristics of Biogas under Hydrogen- and Oxygen-Enriched Condition Jun Li 1, Hongyu Huang 2,*, Huhetaoli 2, Yugo Osaka 3, Yu Bai 2, Noriyuki Kobayashi 1,* and Yong Chen 2 1 Department of Chemical Engineering, Nagoya University, Nagoya, Aichi 464-8603, Japan; [email protected] 2 Guangzhou Institute of Energy Conversion, Chinese Academy of Sciences, Guangzhou 510640, China; [email protected] (H.); [email protected] (Y.B.); [email protected] (Y.C.) 3 Faculty of Mechanical Engineering, Kanazawa University, Kakuma, Kanazawa, Ishikawa 920-1192, Japan; [email protected] * Correspondence: [email protected] (H.H.); [email protected] (N.K.); Tel.: +86-20-870-48394 (H.H.); +81-52-789-5428 (N.K.) Received: 10 May 2017; Accepted: 20 July 2017; Published: 13 August 2017 Abstract: Combustion and heat release characteristics of biogas non-premixed flames under various hydrogen-enriched and oxygen-enriched conditions were investigated through chemical kinetics simulation using detailed chemical mechanisms. The heat release rates, chemical reaction rates, and molar fraction of all species of biogas at various methane contents (35.3–58.7%, mass fraction), hydrogen addition ratios (10–50%), and oxygen enrichment levels (21–35%) were calculated considering the GRI 3.0 mechanism and P1 radiation model. Results showed that the net reaction rate of biogas increases with increasing hydrogen addition ratio and oxygen levels, leading to a higher net heat release rate of biogas flame. Meanwhile, flame length was shortened with the increase in hydrogen addition ratio and oxygen levels. -
APPENDIX M SUMMARY of MAJOR TYPES of Carfg2 REFINERY
APPENDIX M SUMMARY OF MAJOR TYPES OF CaRFG2 REFINERY MODIFICATIONS Appendix M: Summan/ of Major Types of CaRFG2 Refinery Modifications: Alkylation Units A process unit that combines small-molecule hydrocarbon gases produced in the FCCU with a branched chain hydrocarbon called isobutane, producing a material called alkylate, which is blended into gasoline to raise the octane rating. Alkylate is a high octane, low vapor pressure gasoline blending component that essentially contains no olefins, aromatics, or sulfur. This plant improves the ultimate gasoline-making ability of the FCC plant. Therefore, many California refineries built new or modified existing units to increase alkylate production to blend and to produce greater amounts of CaRFG2. Alkylate is produced by combining C3, C4, and C5 components with isobutane (nC4). The process of alkylation is the reverse of cracking. Olefins (such as butenes and propenes) and isobutane are used as feedstocks and combined to produce alkylate. This process enables refiners to utilize lighter components that otherwise could not be blended into gasoline due to their high vapor pressures. Feed to alkylation unit can include pentanes from light cracked gasoline treaters, isobutanes from butane isomerization unit, and C3/C4 streams from delayed coking units. Isomerization Units - C4/C5/C6 A refinery that has an alkylation plant is not likely to have exactly enough is-butane to match the proplylene and butylene (olefin) feeds. The refiner usually has two choices - buy iso-butane or make it in a butane isomerization (Bl) plant. Isomerization is the rearrangement of straight chain hydrocarbon molecules to form branched chain products or to convert normal paraffins to their isomer. -
The Piedmont Service: Hydrogen Fuel Cell Locomotive Feasibility
The Piedmont Service: Hydrogen Fuel Cell Locomotive Feasibility Andreas Hoffrichter, PhD Nick Little Shanelle Foster, PhD Raphael Isaac, PhD Orwell Madovi Darren Tascillo Center for Railway Research and Education Michigan State University Henry Center for Executive Development 3535 Forest Road, Lansing, MI 48910 NCDOT Project 2019-43 FHWA/NC/2019-43 October 2020 -i- FEASIBILITY REPORT The Piedmont Service: Hydrogen Fuel Cell Locomotive Feasibility October 2020 Prepared by Center for Railway Research and Education Eli Broad College of Business Michigan State University 3535 Forest Road Lansing, MI 48910 USA Prepared for North Carolina Department of Transportation – Rail Division 860 Capital Boulevard Raleigh, NC 27603 -ii- Technical Report Documentation Page 1. Report No. 2. Government Accession No. 3. Recipient’s Catalog No. FHWA/NC/2019-43 4. Title and Subtitle 5. Report Date The Piedmont Service: Hydrogen Fuel Cell Locomotive Feasibility October 2020 6. Performing Organization Code 7. Author(s) 8. Performing Organization Report No. Andreas Hoffrichter, PhD, https://orcid.org/0000-0002-2384-4463 Nick Little Shanelle N. Foster, PhD, https://orcid.org/0000-0001-9630-5500 Raphael Isaac, PhD Orwell Madovi Darren M. Tascillo 9. Performing Organization Name and Address 10. Work Unit No. (TRAIS) Center for Railway Research and Education 11. Contract or Grant No. Michigan State University Henry Center for Executive Development 3535 Forest Road Lansing, MI 48910 12. Sponsoring Agency Name and Address 13. Type of Report and Period Covered Final Report Research and Development Unit 104 Fayetteville Street December 2018 – October 2020 Raleigh, North Carolina 27601 14. Sponsoring Agency Code RP2019-43 Supplementary Notes: 16. -
Hydrogen Storage for Mobility: a Review
materials Review Hydrogen Storage for Mobility: A Review Etienne Rivard * , Michel Trudeau and Karim Zaghib * Centre of Excellence in Transportation Electrification and Energy Storage, Hydro-Quebec, 1806, boul. Lionel-Boulet, Varennes J3X 1S1, Canada; [email protected] * Correspondence: [email protected] (E.R.); [email protected] (K.Z.) Received: 18 April 2019; Accepted: 11 June 2019; Published: 19 June 2019 Abstract: Numerous reviews on hydrogen storage have previously been published. However, most of these reviews deal either exclusively with storage materials or the global hydrogen economy. This paper presents a review of hydrogen storage systems that are relevant for mobility applications. The ideal storage medium should allow high volumetric and gravimetric energy densities, quick uptake and release of fuel, operation at room temperatures and atmospheric pressure, safe use, and balanced cost-effectiveness. All current hydrogen storage technologies have significant drawbacks, including complex thermal management systems, boil-off, poor efficiency, expensive catalysts, stability issues, slow response rates, high operating pressures, low energy densities, and risks of violent and uncontrolled spontaneous reactions. While not perfect, the current leading industry standard of compressed hydrogen offers a functional solution and demonstrates a storage option for mobility compared to other technologies. Keywords: hydrogen mobility; hydrogen storage; storage systems assessment; Kubas-type hydrogen storage; hydrogen economy 1. Introduction According to the Intergovernmental Panel on Climate Change (IPCC), it is almost certain that the unusually fast global warming is a direct result of human activity [1]. The resulting climate change is linked to significant environmental impacts that are connected to the disappearance of animal species [2,3], decreased agricultural yield [4–6], increasingly frequent extreme weather events [7,8], human migration [9–11], and conflicts [12–14]. -
Thermodynamics of Ion Exchange
Chapter 1 Thermodynamics of Ion Exchange Ayben Kilislioğlu Additional information is available at the end of the chapter http://dx.doi.org/10.5772/53558 1. Introduction 1.1. Ion exchange equilibria During an ion exchange process, ions are essentially stepped from the solvent phase to the solid surface. As the binding of an ion takes place at the solid surface, the rotational and translational freedom of the solute are reduced. Therefore, the entropy change (ΔS) during ion exchange is negative. For ion exchange to be convenient, Gibbs free energy change (ΔG) must be negative, which in turn requires the enthalpy change to be negative because ΔG = ΔH - TΔS. Both enthalpic (ΔHo) and entropic (ΔSo) changes help decide the overall selectivity of the ion-exchange process [Marcus Y., SenGupta A. K. 2004]. Thermodynamics have great efficiency on the impulsion of ion exchange. It also sets the equilibrium distribution of ions between the solution and the solid. A discussion about the role of thermodynamics relevant to both of these phenomena was done by researchers [Araujo R., 2004]. As the basic rule of ion exchange, one type of a free mobile ion of a solution become fixed on the solid surface by releasing a different kind of an ion from the solid surface. It is a reversible process which means that there is no permanent change on the solid surface by the process. Ion exchange has many applications in different fields like enviromental, medical, technological,.. etc. To evaluate the properties and efficiency of the ion exchange one must determine the equilibrium conditions. -
A Review of Energy Storage Technologies' Application
sustainability Review A Review of Energy Storage Technologies’ Application Potentials in Renewable Energy Sources Grid Integration Henok Ayele Behabtu 1,2,* , Maarten Messagie 1, Thierry Coosemans 1, Maitane Berecibar 1, Kinde Anlay Fante 2 , Abraham Alem Kebede 1,2 and Joeri Van Mierlo 1 1 Mobility, Logistics, and Automotive Technology Research Centre, Vrije Universiteit Brussels, Pleinlaan 2, 1050 Brussels, Belgium; [email protected] (M.M.); [email protected] (T.C.); [email protected] (M.B.); [email protected] (A.A.K.); [email protected] (J.V.M.) 2 Faculty of Electrical and Computer Engineering, Jimma Institute of Technology, Jimma University, Jimma P.O. Box 378, Ethiopia; [email protected] * Correspondence: [email protected]; Tel.: +32-485659951 or +251-926434658 Received: 12 November 2020; Accepted: 11 December 2020; Published: 15 December 2020 Abstract: Renewable energy sources (RESs) such as wind and solar are frequently hit by fluctuations due to, for example, insufficient wind or sunshine. Energy storage technologies (ESTs) mitigate the problem by storing excess energy generated and then making it accessible on demand. While there are various EST studies, the literature remains isolated and dated. The comparison of the characteristics of ESTs and their potential applications is also short. This paper fills this gap. Using selected criteria, it identifies key ESTs and provides an updated review of the literature on ESTs and their application potential to the renewable energy sector. The critical review shows a high potential application for Li-ion batteries and most fit to mitigate the fluctuation of RESs in utility grid integration sector. -
Innovation Insights Brief 2019
Innovation Insights Brief 2019 NEW HYDROGEN ECONOMY - HOPE OR HYPE? ABOUT THE WORLD ENERGY COUNCIL ABOUT THIS INNOVATION INSIGHTS BRIEF The World Energy Council is the principal impartial This Innovation Insights brief on hydrogen is part of network of energy leaders and practitioners promoting a series of publications by the World Energy Council an affordable, stable and environmentally sensitive focused on Innovation. In a fast-paced era of disruptive energy system for the greatest benefit of all. changes, this brief aims at facilitating strategic sharing of knowledge between the Council’s members and the Formed in 1923, the Council is the UN-accredited global other energy stakeholders and policy shapers. energy body, representing the entire energy spectrum, with over 3,000 member organisations in over 90 countries, drawn from governments, private and state corporations, academia, NGOs and energy stakeholders. We inform global, regional and national energy strategies by hosting high-level events including the World Energy Congress and publishing authoritative studies, and work through our extensive member network to facilitate the world’s energy policy dialogue. Further details at www.worldenergy.org and @WECouncil Published by the World Energy Council 2019 Copyright © 2019 World Energy Council. All rights reserved. All or part of this publication may be used or reproduced as long as the following citation is included on each copy or transmission: ‘Used by permission of the World Energy Council’ World Energy Council Registered in England -
Fuel Properties Comparison
Alternative Fuels Data Center Fuel Properties Comparison Compressed Liquefied Low Sulfur Gasoline/E10 Biodiesel Propane (LPG) Natural Gas Natural Gas Ethanol/E100 Methanol Hydrogen Electricity Diesel (CNG) (LNG) Chemical C4 to C12 and C8 to C25 Methyl esters of C3H8 (majority) CH4 (majority), CH4 same as CNG CH3CH2OH CH3OH H2 N/A Structure [1] Ethanol ≤ to C12 to C22 fatty acids and C4H10 C2H6 and inert with inert gasses 10% (minority) gases <0.5% (a) Fuel Material Crude Oil Crude Oil Fats and oils from A by-product of Underground Underground Corn, grains, or Natural gas, coal, Natural gas, Natural gas, coal, (feedstocks) sources such as petroleum reserves and reserves and agricultural waste or woody biomass methanol, and nuclear, wind, soybeans, waste refining or renewable renewable (cellulose) electrolysis of hydro, solar, and cooking oil, animal natural gas biogas biogas water small percentages fats, and rapeseed processing of geothermal and biomass Gasoline or 1 gal = 1.00 1 gal = 1.12 B100 1 gal = 0.74 GGE 1 lb. = 0.18 GGE 1 lb. = 0.19 GGE 1 gal = 0.67 GGE 1 gal = 0.50 GGE 1 lb. = 0.45 1 kWh = 0.030 Diesel Gallon GGE GGE 1 gal = 1.05 GGE 1 gal = 0.66 DGE 1 lb. = 0.16 DGE 1 lb. = 0.17 DGE 1 gal = 0.59 DGE 1 gal = 0.45 DGE GGE GGE Equivalent 1 gal = 0.88 1 gal = 1.00 1 gal = 0.93 DGE 1 lb. = 0.40 1 kWh = 0.027 (GGE or DGE) DGE DGE B20 DGE DGE 1 gal = 1.11 GGE 1 kg = 1 GGE 1 gal = 0.99 DGE 1 kg = 0.9 DGE Energy 1 gallon of 1 gallon of 1 gallon of B100 1 gallon of 5.66 lb., or 5.37 lb.