Contents Locations to Consumers and to Provide Diversity Key Points and Conclusions 08 and Security for the Gas Supply
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A.22G Liquefied Natural Gas Management Plan
APPENDIX A.22G: Liquid Natural Gas Management Plan Volume A.i: PREFACE VOLUME A.V: Volume A.V: Volume A.ii: Volume A.iii: Volume A.iV: ADDITIONAL Project BioPhysicAl socio-economic AdditionAl introduction VAlued VAlued YESAAyesAA & oVerView comPonents comPonents REQUIREMENTSreQuirements A.1 Introduction A.6 Terrain Features A.13 Employment and A.20 Effects of the Income Environment on Concordance Table to the the Project A.1A A.7 Water Quality A.13A Economic Impacts of the Executive Committee’s Request Casino Mine Project for Supplementary Information A.21 Accidents and A.7A Variability Water Balance Model Malfunctions Report A.14 Employability First Nations and A.2 A.7B Water Quality Predictions Report A.22 Environmental Community A.15 Economic Management Consultation A.7c Potential Effects of Climate Change on Development and the Variability Water Balance A.22A Waste and Hazardous Business Sector Materials A.2A Traditional Knowledge Management Plan Bibliography A.7d Updated Appendix B5 to Appendix 7A A.16 Community A.22B Spill Contingency A.7e 2008 Environmental Vitality Management Plan A.3 Project Location Studies Report: Final A.17 Community A.22c Sediment and Erosion A.7F The Effect of Acid Rock Drainage on Control Management A.4 Project Description Casino Creek Infrastructure and Plan Services A.7G Toxicity Testing Reports A.22d Invasive Species A.4A Tailings Management Facility Management Plan Construction Material Alternatives A.7h Appendix A2 to Casino Waste Rock A.18 Cultural and Ore Geochemical Static Test As- A.22e Road Use -
Guidance on Estimating Condensate and Crude Oil Loading Losses from Tank Trucks Section I
Guidance on Estimating Condensate and Crude Oil Loading Losses from Tank Trucks Section I. Introduction The purpose of this guidance document is to provide general guidance on estimating condensate and crude oil evaporative emissions from tank trucks during loading operations. • OAC 165:10-1-2 defines condensate as “a liquid hydrocarbon which: (A) [w]as produced as a liquid at the surface, (B) [e]xisted as a gas in the reservoir, and (C) [h]as an API gravity greater than or equal to fifty degrees, unless otherwise proven.” • OAC 165:10-1-2 defines crude oil as “any petroleum hydrocarbon, except condensate, produced from a well in liquid form by ordinary production methods.” The Air Quality Division (AQD) has received permit applications requesting the use of a reduced Volatile Organic Compounds (VOC) loading emission factor for estimating tank truck loading loss emissions. This is to account for methane and ethane entrained in the petroleum liquid that, along with VOC, are released in the vapors as the petroleum liquid is loaded. In some cases, the proposed non-VOC reduction represents a combined methane and ethane vapor concentration of greater than 30 percent by weight. Permit applications are submitted with loading loss emissions calculated using the methodology outlined in AP-42 (6/08), Section 5.2, using process simulation software, or both. Process simulation software estimates emissions based on all streams reaching equilibrium. The majority of permitted loading losses are calculated assuming negligible concentrations of methane and/or ethane. Due to the high concentrations of methane and ethane proposed in some permit applications, a review of the calculation methodology was conducted and resulted in this guidance document. -
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. -
Safe Operation of Vacuum Trucks in Petroleum Service
Safe Operation of Vacuum Trucks in Petroleum Service API RECOMMENDED PRACTICE 2219 THIRD EDITION, NOVEMBER 2005 REAFFIRMED, NOVEMBER 2012 --``,,```,`,,,`,,`````,,,,``,``-`-`,,`,,`,`,,`--- Copyright American Petroleum Institute Provided by IHS under license with API Licensee=Shell Global Solutions International B.V. Main/5924979112, User=Elliott No reproduction or networking permitted without license from IHS Not for Resale, 12/30/2013 09:55:43 MST --``,,```,`,,,`,,`````,,,,``,``-`-`,,`,,`,`,,`--- Copyright American Petroleum Institute Provided by IHS under license with API Licensee=Shell Global Solutions International B.V. Main/5924979112, User=Elliott No reproduction or networking permitted without license from IHS Not for Resale, 12/30/2013 09:55:43 MST Safe Operation of Vacuum Trucks in Petroleum Service Downstream Segment API RECOMMENDED PRACTICE 2219 THIRD EDITION, NOVEMBER 2005 REAFFIRMED, NOVEMBER 2012 --``,,```,`,,,`,,`````,,,,``,``-`-`,,`,,`,`,,`--- Copyright American Petroleum Institute Provided by IHS under license with API Licensee=Shell Global Solutions International B.V. Main/5924979112, User=Elliott No reproduction or networking permitted without license from IHS Not for Resale, 12/30/2013 09:55:43 MST SPECIAL NOTES API publications necessarily address problems of a general nature. With respect to particular circumstances, local, state, and federal laws and regulations should be reviewed. Neither API nor any of API's employees, subcontractors, consultants, committees, or other assignees make any warranty or representation, either express or implied, with respect to the accuracy, completeness, or usefulness of the information contained herein, or assume any liability or responsibility for any use, or the results of such use, of any information or process disclosed in this publication. Neither API nor any of API's employees, subcontractors, con- sultants, or other assignees represent that use of this publication would not infringe upon pri- vately owned rights. -
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. -
Liquefied Natural Gas/ Compressed Natural Gas Opportunities
Liquefied Natural Gas/ Compressed Natural Gas Opportunities Fixed Gas and Flame Detection Applications While there are many solutions that can help meet our energy needs into the future, natural gas and its benefits are available now. The significant increase in the supply of natural gas, brought about by technical advancements in producing gas from shale deposits, has revolutionized the gas industry; opening up new sources of gas production in North America. Such increased production has escalated U.S. competitiveness, promoted job growth and bolstered the economy with lower, more stable natural gas prices.¹ ¹http://www.powerincooperation.com Because every life has a purpose... LNG/CNG Opportunites Liquefied natural gas (LNG) is natural gas that has been converted Total U.S. natural gas production, consumption, to liquid form for ease of storage or transport, and its use allows for and net imports, 1990-2035 the production and marketing of natural gas deposits that were (trillion cubicfeet) History 2010 Projections previously economically unrecoverable. This technology is used for 30 natural gas supply operations and domestic storage, and in Net exports, 2035 5% consumption such as for vehicle fuel. 25 Compressed natural gas (CNG) is natural gas under pressure Consumption which remains clear, odorless, and non-corrosive. CNG is a fossil 11% Net imports, 2010 fuel substitute for gasoline (petrol), diesel, or propane/LPG and is a 20 Henry Hub spot market more environmentally clean alternative to those fuels, and it is natural gas prices (2010 dollars per million Btu) much safer in the event of a spill. Domestic production 10 Interest in LNG and CNG has been rekindled and is expected to play 15 5 an important role in the natural gas industry and energy markets 0 over the next several years. -
Quantifying the Potential of Renewable Natural Gas to Support a Reformed Energy Landscape: Estimates for New York State
energies Review Quantifying the Potential of Renewable Natural Gas to Support a Reformed Energy Landscape: Estimates for New York State Stephanie Taboada 1,2, Lori Clark 2,3, Jake Lindberg 1,2, David J. Tonjes 2,3,4 and Devinder Mahajan 1,2,* 1 Department of Materials Science and Chemical Engineering, Stony Brook University, Stony Brook, NY 11794, USA; [email protected] (S.T.); [email protected] (J.L.) 2 Institute of Gas Innovation and Technology, Advanced Energy Research and Technology, Stony Brook, NY 11794, USA; [email protected] (L.C.); [email protected] (D.J.T.) 3 Department of Technology and Society, Stony Brook University, 100 Nicolls Rd, Stony Brook, NY 11794, USA 4 Waste Data and Analysis Center, Stony Brook University, 100 Nicolls Rd, Stony Brook, NY 11794, USA * Correspondence: [email protected] Abstract: Public attention to climate change challenges our locked-in fossil fuel-dependent energy sector. Natural gas is replacing other fossil fuels in our energy mix. One way to reduce the greenhouse gas (GHG) impact of fossil natural gas is to replace it with renewable natural gas (RNG). The benefits of utilizing RNG are that it has no climate change impact when combusted and utilized in the same applications as fossil natural gas. RNG can be injected into the gas grid, used as a transportation fuel, or used for heating and electricity generation. Less common applications include utilizing RNG to produce chemicals, such as methanol, dimethyl ether, and ammonia. The GHG impact should be quantified before committing to RNG. This study quantifies the potential production of biogas (i.e., Citation: Taboada, S.; Clark, L.; the precursor to RNG) and RNG from agricultural and waste sources in New York State (NYS). -
Natural Gas Liquids
Brookings energy security initiative natural gas task Force natural gas BrieFing Document #1: Natural Gas Liquids march 2013 charles k. ebinger govinda avasarala Brookings natural g as task Force Issue Brief 1: Natural Gas Liquids 1 PREFACE n may 2011, the Brookings institution energy security initiative (ESI) assembled a task Force of independent natural-gas experts, whose expertise and insights provided inform its research on various issues regarding Ithe u.s. natural gas sector. in may 2012, Brookings released its first report, analyzing the case and prospects for exports of liquefied natural gas (lng) from the united states. the task Force now continues to meet pe- riodically to discuss important issues facing the sector. With input from the task Force, Brookings will release periodic issue briefs for policymakers. the conclusions and recommendations of this report are those of the authors and do not necessarily reflect the views of the members of the task force. members of the Brookings institution natural gas task Force JOHN BANKS, Brookings institution KELLY BENNETT, Bentek energy, LLC JASON BORDOFF, columbia university KEVIN BOOK, clearview energy Partners, LLC TOM CHOI, Deloitte CHARLES EBINGER, Brookings institution, task Force co-chair DAVID GOLDWYN, goldwyn global strategies, LLC, task Force co-chair SHAIA HOSSEINZADEH, Wl ross JAMES JENSEN, Jensen associates ROBERT JOHNSTON, eurasia group MELANIE KENDERDINE, massachusetts institute of technology energy initiative VELLO KUUSKRAA, advanced resources international MICHAEL LEVI, council on Foreign relations ROBERT MCNALLY, the rapidan group KENNETH MEDLOCK, rice university’s James a. Baker iii institute for Public Policy LOU PUGLIARESI, energy Policy research Foundation, inc. BENJAMIN SCHLESINGER, Benjamin schlesinger & associates, LLC JAMIE WEBSTER, PFc energy non-participating observers to task Force meetings included officials from the energy information adminis- tration and the congressional research service. -
A Comparative Exergoeconomic Evaluation of the Synthesis Routes for Methanol Production from Natural Gas
applied sciences Article A Comparative Exergoeconomic Evaluation of the Synthesis Routes for Methanol Production from Natural Gas Timo Blumberg 1,*, Tatiana Morosuk 2 and George Tsatsaronis 2 ID 1 Department of Energy Engineering, Zentralinstitut El Gouna, Technische Universität Berlin, 13355 Berlin, Germany 2 Institute for Energy Engineering, Technische Universität Berlin, 10587 Berlin, Germany; [email protected] (T.M.); [email protected] (G.T.) * Correspondence: [email protected]; Tel.: +49-30-314-23343 Received: 30 October 2017; Accepted: 20 November 2017; Published: 24 November 2017 Abstract: Methanol is one of the most important feedstocks for the chemical, petrochemical, and energy industries. Abundant and widely distributed resources as well as a relative low price level make natural gas the predominant feedstock for methanol production. Indirect synthesis routes via reforming of methane suppress production from bio resources and other renewable alternatives. However, the conventional technology for the conversion of natural gas to methanol is energy intensive and costly in investment and operation. Three design cases with different reforming technologies in conjunction with an isothermal methanol reactor are investigated. Case I is equipped with steam methane reforming for a capacity of 2200 metric tons per day (MTPD). For a higher production capacity, a serial combination of steam reforming and autothermal reforming is used in Case II, while Case III deals with a parallel configuration of CO2 and steam reforming. A sensitivity analysis shows that the syngas composition significantly affects the thermodynamic performance of the plant. The design cases have exergetic efficiencies of 28.2%, 55.6% and 41.0%, respectively. -
The Future of Gasification
STRATEGIC ANALYSIS The Future of Gasification By DeLome Fair coal gasification projects in the U.S. then slowed significantly, President and Chief Executive Officer, with the exception of a few that were far enough along in Synthesis Energy Systems, Inc. development to avoid being cancelled. However, during this time period and on into the early 2010s, China continued to build a large number of coal-to-chemicals projects, beginning first with ammonia, and then moving on to methanol, olefins, asification technology has experienced periods of both and a variety of other products. China’s use of coal gasification high and low growth, driven by energy and chemical technology today is by far the largest of any country. China markets and geopolitical forces, since introduced into G rapidly grew its use of coal gasification technology to feed its commercial-scale operation several decades ago. The first industrialization-driven demand for chemicals. However, as large-scale commercial application of coal gasification was China’s GDP growth has slowed, the world’s largest and most in South Africa in 1955 for the production of coal-to-liquids. consistent market for coal gasification technology has begun During the 1970s development of coal gasification was pro- to slow new builds. pelled in the U.S. by the energy crisis, which created a political climate for the country to be less reliant on foreign oil by converting domestic coal into alternative energy options. Further growth of commercial-scale coal gasification began in “Market forces in high-growth the early 1980s in the U.S., Europe, Japan, and China in the coal-to-chemicals market.