Ethane Storage and Distribution Hub in the United States
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Blending Hydrogen Into Natural Gas Pipeline Networks: a Review of Key Issues
Blending Hydrogen into Natural Gas Pipeline Networks: A Review of Key Issues M. W. Melaina, O. Antonia, and M. Penev 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. Technical Report NREL/TP-5600-51995 March 2013 Contract No. DE-AC36-08GO28308 Blending Hydrogen into Natural Gas Pipeline Networks: A Review of Key Issues M. W. Melaina, O. Antonia, and M. Penev Prepared under Task No. HT12.2010 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/TP-5600-51995 Golden, Colorado 80401 March 2013 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, 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. -
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]. -
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. -
Assessment of Innovative and Automated Freight Strategies and Technologies—Phase I Final Report
Technical Report Documentation Page 1. Report No. 2. Government Accession No. 3. Recipient's Catalog No. FHWA/TX-17/0-6837-1 4. Title and Subtitle 5. Report Date ASSESSMENT OF INNOVATIVE AND AUTOMATED FREIGHT February 2017 STRATEGIES AND TECHNOLOGIES—PHASE I FINAL REPORT 6. Performing Organization Code 7. Author(s) 8. Performing Organization Report No. Curtis Morgan, Jeffery Warner, Allan Rutter, Dahye Lee, C. James Report 0-6837-1 Kruse, Dong Hun Kang, Mario Monsreal, Jolanda Prozzi, Juan Carlos Villa, Jeffrey Borowiec, Leslie Olson, David Bierling, and Edwin Varela 9. Performing Organization Name and Address 10. Work Unit No. (TRAIS) Texas A&M Transportation Institute The Texas A&M University System 11. Contract or Grant No. College Station, Texas 77843-3135 Project 0-6837 12. Sponsoring Agency Name and Address 13. Type of Report and Period Covered Texas Department of Transportation Technical Report: Research and Technology Implementation Office March 2016 125 E. 11th Street 14. Sponsoring Agency Code Austin, Texas 78701-2483 15. Supplementary Notes Project performed in cooperation with the Texas Department of Transportation and the Federal Highway Administration. Project Title: Assessment of Innovative and Automated Freight Systems and Development of Evaluation Tools URL: http://tti.tamu.edu/documents/0-6837-1.pdf 16. Abstract Many innovative freight delivery strategies and technologies have been proposed to address the future freight needs of Texas’s growing population. Changes in both buying habits and a shift toward direct home package delivery threaten to dramatically change distribution patterns and increase the number of intercity and local delivery trucks on Texas Department of Transportation (TxDOT) roadways. -
Oxidation of Ethane to Ethylene and Acetic Acid by Movnbo Catalysts Martial Roussel, Michel Bouchard, Elisabeth Bordes-Richard, Khalid Karim, Saleh Al-Sayari
Oxidation of ethane to ethylene and acetic acid by MoVNbO catalysts Martial Roussel, Michel Bouchard, Elisabeth Bordes-Richard, Khalid Karim, Saleh Al-Sayari To cite this version: Martial Roussel, Michel Bouchard, Elisabeth Bordes-Richard, Khalid Karim, Saleh Al-Sayari. Oxida- tion of ethane to ethylene and acetic acid by MoVNbO catalysts. Catalysis Today, Elsevier, 2005, 99, pp.77-87. 10.1016/j.cattod.2004.09.026. hal-00103604 HAL Id: hal-00103604 https://hal.archives-ouvertes.fr/hal-00103604 Submitted on 4 Oct 2006 HAL is a multi-disciplinary open access L’archive ouverte pluridisciplinaire HAL, est archive for the deposit and dissemination of sci- destinée au dépôt et à la diffusion de documents entific research documents, whether they are pub- scientifiques de niveau recherche, publiés ou non, lished or not. The documents may come from émanant des établissements d’enseignement et de teaching and research institutions in France or recherche français ou étrangers, des laboratoires abroad, or from public or private research centers. publics ou privés. Oxidation of ethane to ethylene and acetic acid by MoVNbO catalysts M. Roussel 1, M. Bouchard 1, E. Bordes-Richard 1*, K. Karim 2, S. Al-Sayari 2 1: Laboratoire de Catalyse de Lille, UMR CNRS 8010, USTL-ENSCL, 59655 Villeneuve d'Ascq Cedex, France 2: SABIC R&T, P.O. Box 42503, Riyadh, Saoudi Arabia ABSTRACT The influence of niobium on the physicochemical properties of the Mo-V-O system and on its catalytic properties in the oxidation of ethane to ethylene and acetic acid is examined. Solids based on MoV 0.4 Ox and MoV 0.4 Nb 0.12 Oy composition and calcined at 350 or 400°C were studied by X-ray diffraction, and by laser Raman and X-ray photoelectron spectroscopies. -
Chapter 2: Alkanes Alkanes from Carbon and Hydrogen
Chapter 2: Alkanes Alkanes from Carbon and Hydrogen •Alkanes are carbon compounds that contain only single bonds. •The simplest alkanes are hydrocarbons – compounds that contain only carbon and hydrogen. •Hydrocarbons are used mainly as fuels, solvents and lubricants: H H H H H H H H H H H H C H C C H C C C C H H C C C C C H H H C C H H H H H H CH2 H CH3 H H H H CH3 # of carbons boiling point range Use 1-4 <20 °C fuel (gasses such as methane, propane, butane) 5-6 30-60 solvents (petroleum ether) 6-7 60-90 solvents (ligroin) 6-12 85-200 fuel (gasoline) 12-15 200-300 fuel (kerosene) 15-18 300-400 fuel (heating oil) 16-24 >400 lubricating oil, asphalt Hydrocarbons Formula Prefix Suffix Name Structure H CH4 meth- -ane methane H C H H C H eth- -ane ethane 2 6 H3C CH3 C3H8 prop- -ane propane C4H10 but- -ane butane C5H12 pent- -ane pentane C6H14 hex- -ane hexane C7H16 hept- -ane heptane C8H18 oct- -ane octane C9H20 non- -ane nonane C10H22 dec- -ane decane Hydrocarbons Formula Prefix Suffix Name Structure H CH4 meth- -ane methane H C H H H H C2H6 eth- -ane ethane H C C H H H H C H prop- -ane propane 3 8 H3C C CH3 or H H H C H 4 10 but- -ane butane H3C C C CH3 or H H H C H 4 10 but- -ane butane? H3C C CH3 or CH3 HydHrydorcocaarrbobnos ns Formula Prefix Suffix Name Structure H CH4 meth- -ane methane H C H H H H C2H6 eth- -ane ethane H C C H H H H C3H8 prop- -ane propane H3C C CH3 or H H H C H 4 10 but- -ane butane H3C C C CH3 or H H H C H 4 10 but- -ane iso-butane H3C C CH3 or CH3 HydHrydoroccarbrobnsons Formula Prefix Suffix Name Structure H H -
Enabling Ethane As a Primary Gas Turbine Fuel: an Economic Benefit from the Growth of Shale Gas
GE Power GEA32198 November 2015 Enabling ethane as a primary gas turbine fuel: an economic benefit from the growth of shale gas Dr. Jeffrey Goldmeer GE Power, Gas Power Systems Schenectady, NY, USA John Bartle GE Power, Power Services Atlanta, GA, USA Scott Peever GE Power Toronto, ON, CAN © 2015 General Electric Company. All Rights Reserved. This material may not be copied or distributed in whole or in part, without prior permission of the copyright owner. GEA32198 Enabling ethane as a primary gas turbine fuel: an economic benefit from the growth of shale gas Contents Abstract ............................................................................3 Introduction ........................................................................3 Fuel Supply Dynamics ...............................................................3 Hydrocarbon Sources and Characteristics ...........................................5 Combustion System Considerations .................................................6 Evaluating Fuels .....................................................................6 GE’s Gas Turbine Combustion Systems ..............................................8 Non-Methane Hydrocarbon Capability ...............................................9 Economic Value of Alternative Fuels .................................................9 Conclusions ........................................................................10 References ........................................................................11 2 © 2015 General Electric Company. All Rights -
Chlorine and Hydrogen Chloride
This report contains the collective views of an nternational group of experts and does not xcessarily represent the decisions or the stated 1 icy of the United Nations Environment Pro- '€mme, the International Labour Organisation, or the World Health Organization. Environmental Health Criteria 21 CHLORINE AND HYDROGEN CHLORIDE 'ublished under the joint sponsorship of Ic United Nations Environment Programme. the International Labour Organisation, and the World Health Organization / \r4 ( o 4 UI o 1 o 'T F- World Health Organization kz Geneva, 1982 The International Programme on Chemical Safety (IPCS) is a joint ven- ture of the United Nations Environment Programme. the International Labour Organisation, and the World Health Organization. The main objective of the IPCS is to carry out and disseminate evaluations of the environment. Supporting activities include the development of epidemiological, experi- mental laboratory, and risk assessment methods that could produce interna- tionally comparable results, and the development of manpower in the field of toxicology. Other relevant activities carried out by the IPCS include the development of know-how for coping with chemical accidents, coordination of laboratory testing and epidemiological studies, and promotion of research on the mechanisms of the biological action of chemicals. ISBN 92 4 154081 8 World Health Organization 1982 Publications of the World Health Organization enjoy copyright protec- tion in accordance with the provisions of Protocol 2 of the Universal Copy- right Convention. For rights of reproduction or translation of WHO publica- tions, in part or in loto, application should be made to the Office of Publica- tions, World Health Organization, Geneva. Switzerland. The World Health Organization welcomes such applications. -
Organic Chemistry Name Formula Isomers Methane CH 1 Ethane C H
Organic Chemistry Organic chemistry is the chemistry of carbon. The simplest carbon molecules are compounds of just carbon and hydrogen, hydrocarbons. We name the compounds based on the length of the longest carbon chain. We then add prefixes and suffixes to describe the types of bonds and any add-ons the molecule has. When the molecule has just single bonds we use the -ane suffix. Name Formula Isomers Methane CH4 1 Ethane C2H6 1 Propane C3H8 1 Butane C4H10 2 Pentane C5H12 3 Hexane C6H14 5 Heptane C7H16 9 Octane C8H18 18 Nonane C9H20 35 Decane C10H22 75 Isomers are compounds that have the same formula but different bonding. isobutane n-butane 1 Naming Alkanes Hydrocarbons are always named based on the longest carbon chain. When an alkane is a substituent group they are named using the -yl ending instead of the -ane ending. So, -CH3 would be a methyl group. The substituent groups are named by numbering the carbons on the longest chain so that the first branching gets the lowest number possible. The substituents are listed alphabetically with out regard to the number prefixes that might be used. 3-methylhexane 1 2 3 4 5 6 6 5 4 3 2 1 Alkenes and Alkynes When a hydrocarbon has a double bond we replace the -ane ending with -ene. When the hydrocarbon has more than three carbon the position of the double bond must be specified with a number. 1-butene 2-butene Hydrocarbons with triple bonds are named basically the same, we replace the -ane ending with -yne. -
Changing LNG Market Dynamics – Implications on Supply Security in the APEC Region
Changing LNG Market Dynamics – Implications on Supply Security in the APEC Region APEC Oil and Gas Security Studies | Series 17 APEC Energy Working Group September 2020 APEC Project: EWG 01 2020S Produced by Asia Pacific Energy Research Centre (APERC) Institute of Energy Economics, Japan Inui Building, Kachidoki 11F, 1-13-1 Kachidoki Chuo-ku, Tokyo 104-0054 Japan Tel: (813) 5144-8551 Fax: (813) 5144-8555 E-mail: [email protected] (administration) Website: http://aperc.or.jp/ For Asia-Pacific Economic Cooperation Secretariat 35 Heng Mui Keng Terrace Singapore 119616 Tel: (65) 68919 600 Fax: (65) 68919 690 Email: [email protected] Website: www.apec.org © 2020 APEC Secretariat APEC#220-RE-01.9 ISBN: 978-981-14-7794-2 OGSS Series 17 Changing LNG Market Dynamics – Implications on Supply Security in the APEC Region 3 | P a g e TABLE OF CONTENTS Table of Contents .......................................................................................................................... 3 Foreword ....................................................................................................................................... 6 Acknowledgements ....................................................................................................................... 7 Project coordinators .................................................................................................................. 7 Authors ...................................................................................................................................... 7 Editors -
NATURAL GAS STORAGE: Actions Needed to Assess Inspection
United States Government Accountability Office Report to Congressional Requesters October 2019 NATURAL GAS STORAGE Actions Needed to Assess Inspection Workload and Progress toward Safety Outcomes GAO-20-167 October 2019 NATURAL GAS STORAGE Actions Needed to Assess Inspection Workload and Progress toward Safety Outcomes Highlights of GAO-20-167, a report to congressional requesters Why GAO Did This Study What GAO Found About 400 natural gas storage sites In 2018, the U.S. Department of Transportation’s Pipeline and Hazardous are important to the U.S. natural gas Materials Safety Administration (PHMSA) set a goal for its natural gas storage system, providing about 30 percent of inspection program to inspect all approximately 400 natural gas storage sites the nation's energy. During a 2015 leak within 5 years, according to agency officials. PHMSA expected that all 25 eligible at a storage site near Los Angeles, states would help inspect sites, but only 10 states agreed to partner with the about 8,000 families were temporarily agency. As a result, the agency’s inspection workload increased by almost 60 relocated due to symptoms such as percent from when it set its goal, according to PHMSA data. Because of the migraines, nausea, and respiratory increase in its inspection workload over its preliminary estimate, PHMSA does problems. The leak raised concerns not have assurance that it has enough resources to meet its inspection goal. about health and safety risks from Furthermore, PHMSA has not used a workforce analysis to inform its budget other storage sites. In 2017, GAO recommended that PHMSA take requests. -
ETHANE PROPANE MIXTURE Version 1.2 Revision Date 2017-12-18
SAFETY DATA SHEET ETHANE PROPANE MIXTURE Version 1.2 Revision Date 2017-12-18 SECTION 1: Identification of the substance/mixture and of the company/undertaking Product information Product Name : ETHANE PROPANE MIXTURE Material : 1012531, 1012527 Company : Chevron Phillips Chemical Company LP 10001 Six Pines Drive The Woodlands, TX 77380 Emergency telephone: Health: 866.442.9628 (North America) 1.832.813.4984 (International) Transport: CHEMTREC 800.424.9300 or 703.527.3887(int'l) Asia: CHEMWATCH (+612 9186 1132) China: 0532 8388 9090 EUROPE: BIG +32.14.584545 (phone) or +32.14583516 (telefax) Mexico CHEMTREC 01-800-681-9531 (24 hours) South America SOS-Cotec Inside Brazil: 0800.111.767 Outside Brazil: +55.19.3467.1600 Argentina: +(54)-1159839431 Responsible Department : Product Safety and Toxicology Group E-mail address : [email protected] Website : www.CPChem.com SECTION 2: Hazards identification Classification of the substance or mixture This product has been classified in accordance with the hazard communication standard 29 CFR 1910.1200; the SDS and labels contain all the information as required by the standard. Classification : Flammable gases, Category 1 Gases under pressure, Liquefied gas Labeling Symbol(s) : SDS Number:100000002557 1/12 SAFETY DATA SHEET ETHANE PROPANE MIXTURE Version 1.2 Revision Date 2017-12-18 Signal Word : Danger Hazard Statements : H220: Extremely flammable gas. H280: Contains gas under pressure; may explode if heated. Precautionary Statements : Prevention: P210 Keep away from heat/sparks/open flames/hot surfaces. No smoking. Response: P377 Leaking gas fire: Do not extinguish, unless leak can be stopped safely. P381 Eliminate all ignition sources if safe to do so.