GHG Emissions from LNG Operations, Accounting for the Diversity of Operations;
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Oil and Gas Security
GREECE Key Figures ________________________________________________________________ 2 Overview _________________________________________________________________ 3 1. Energy Outlook __________________________________________________________ 4 2. Oil _____________________________________________________________________ 5 2.1 Market Features and Key Issues __________________________________________________ 5 2.2 Oil Supply Infrastructure ________________________________________________________ 7 2.3 Decision-making Structure for Oil Emergencies ______________________________________ 9 2.4 Stocks ______________________________________________________________________ 9 3. Other Measures ________________________________________________________ 11 3.1 Demand Restraint ____________________________________________________________ 11 3.2 Fuel Switching _______________________________________________________________ 12 3.3 Others _____________________________________________________________________ 12 4. Natural Gas ____________________________________________________________ 12 4.1 Market Features and Key Issues _________________________________________________ 12 4.2 Natural gas supply infrastructure ________________________________________________ 14 4.3 Emergency Policy for Natural Gas _______________________________________________ 16 List of Figures Total Primary Energy Supply -------------------------------------------------------------------------------------------------- 4 Electricity Generation, by Fuel Source -------------------------------------------------------------------------------------- -
Sulfur Recovery
Sulfur Recovery Chapter 16 Based on presentation by Prof. Art Kidnay Plant Block Schematic Adapted from Figure 7.1, Fundamentals of Natural Gas Processing, 2nd ed. Kidnay, Parrish, & McCartney Updated: January 4, 2019 2 Copyright © 2019 John Jechura ([email protected]) Topics Introduction Properties of sulfur Sulfur recovery processes ▪ Claus Process ▪ Claus Tail Gas Cleanup Sulfur storage Safety and environmental considerations Updated: January 4, 2019 3 Copyright © 2019 John Jechura ([email protected]) Introduction & Properties of Sulfur Updated: January 4, 2019 Copyright © 2017 John Jechura ([email protected]) Sulfur Crystals http://www.irocks.com/minerals/specimen/34046 http://www.mccullagh.org/image/10d-5/sulfur.html Updated: January 4, 2019 5 Copyright © 2019 John Jechura ([email protected]) Molten Sulfur http://www.kamgroupltd.com/En/Post/7/Basic-info-on-elemental-Sulfur(HSE) Updated: January 4, 2019 6 Copyright © 2019 John Jechura ([email protected]) World Consumption of Sulfur Primary usage of sulfur to make sulfuric acid (90 – 95%) ▪ Other major uses are rubber processing, cosmetics, & pharmaceutical applications China primary market Ref: https://ihsmarkit.com/products/sulfur-chemical-economics-handbook.html Report published December 2017 Updated: January 4, 2019 7 Copyright © 2019 John Jechura ([email protected]) Sulfur Usage & Prices Natural gas & petroleum production accounts for the majority of sulfur production Primary consumption is agriculture & industry ▪ 65% for farm fertilizer: sulfur → sulfuric acid → phosphoric acid → fertilizer $50 per ton essentially disposal cost ▪ Chinese demand caused run- up in 2007-2008 Ref: http://ictulsa.com/energy/ “Cleaning up their act”, Gordon Cope, Updated December 24, 2018 Hydrocarbon Engineering, pp 24-27, March 2011 Updated: January 4, 2019 8 Copyright © 2019 John Jechura ([email protected]) U.S. -
Thesis a Modeling Tool for Household Biogas Burner
THESIS A MODELING TOOL FOR HOUSEHOLD BIOGAS BURNER FLAME PORT DESIGN Submitted by Thomas J. Decker Department of Mechanical Engineering In partial fulfillment of the requirements For the Degree of Master of Science Colorado State University Fort Collins, Colorado Summer 2017 Master’s Committee: Advisor: Thomas Bradley Jason Prapas Sybil Sharvelle Copyright by Thomas J Decker 2017 All Rights Reserved ABSTRACT A MODELING TOOL FOR HOUSEHOLD BIOGAS BURNER FLAME PORT DESIGN Anaerobic digestion is a well-known and potentially beneficial process for rural communities in emerging markets, providing the opportunity to generate usable gaseous fuel from agricultural waste. With recent developments in low-cost digestion technology, communities across the world are gaining affordable access to the benefits of anaerobic digestion derived biogas. For example, biogas can displace conventional cooking fuels such as biomass (wood, charcoal, dung) and Liquefied Petroleum Gas (LPG), effectively reducing harmful emissions and fuel cost respectively. To support the ongoing scaling effort of biogas in rural communities, this study has developed and tested a design tool aimed at optimizing flame port geometry for household biogas- fired burners. The tool consists of a multi-component simulation that incorporates three- dimensional CAD designs with simulated chemical kinetics and computational fluid dynamics. An array of circular and rectangular port designs was developed for a widely available biogas stove (called the Lotus) as part of this study. These port designs were created through guidance from previous studies found in the literature. The three highest performing designs identified by the tool were manufactured and tested experimentally to validate tool output and to compare against the original port geometry. -
Biogas Stove Design: a Short Course
Biogas Stove Design A short course Dr David Fulford Kingdom Bioenergy Ltd Originally written August 1996 Used in MSc Course on “Renewable Energy and the Environment” at the University of Reading, UK for an Advanced Biomass Module. Design Equations for a Gas Burner The force which drives the gas and air into the burner is the pressure of gas in the pipeline. The key equation that relates gas pressure to flow is Bernoulli’s theorem (assuming incompressible flow): p v2 + +z = constant ρ 2g where: p is the gas pressure (N m –2), ρ is the gas density (kg m –3), v is the gas velocity (m s –1), g is the acceleration due to gravity (9.81 m s –2) and z is head (m). For a gas, head ( z) can be ignored. Bernoulli’s theorem essentially states that for an ideal gas flow, the potential energy due to the pressure, plus the kinetic energy due to the velocity of the flow is constant In practice, with gas flowing through a pipe, Bernoulli’s theorem must be modified. An extra term must be added to allow for energy loss due to friction in the pipe: p v2 + −f ()losses = constant . ρ 2g Using compressible flow theory, flow though a nozzle of area A is: γ p γ ()γ − γ m = C ρ A 2 0 r2 (1− r 1 ) & d 0 γ − ρ 1 0 ρ where p0 and 0 are the pressure and density of the gas upstream of the = nozzle and r p1 p0 , where p1 is the pressure downstream of the nozzle. -
Still Vital for Russian Gas Supplies to Europe As Other Routes Reach Full Capacity
May 2018 Ukrainian Gas Transit: Still Vital for Russian Gas Supplies to Europe as Other Routes Reach Full Capacity OXFORD ENERGY COMMENT Jack Sharples Introduction In recent years, natural gas demand in Europe has reversed the decline witnessed between 2010 and 2014. During the same period, ‘domestic’ gas production in Europe has continued to decline (most notably in the Netherlands), leading to increased European gas import demand. This has particularly benefitted Gazprom, which has experienced significant success in growing the volumes of its exports to the European market to record levels in 2016 and 2017. This success continued into Q1 2018, with Gazprom announcing a 6.6% increase in gas exports to Europe versus Q1 2017, and a new monthly record, with the 19.6 bcm exported in March 2018 surpassing the previous record of 19.1 bcm exported to Europe in January 2017.1 In a recent OIES paper, Henderson and Sharples identified infrastructure as a limiting factor in the further growth in Russian gas exports to Europe, noting that the overall high annual level of utilisation means that “in key peak demand winter months…the system is practically full”.2 Gazprom’s reports of record monthly gas exports to Europe prompted this author to consider the extent to which the pipeline system that brings Russian gas to Europe really was ‘full’ on peak days in Q1 2018, and whether there is now a capacity constraint. The conclusions drawn from this analysis have relevance not only to Gazprom’s ongoing pipeline projects, Nord Stream 2 and Turkish Stream, but also to the question of gas transit via Ukraine after the end of 2019, when Gazprom’s existing gas transit contract with Naftogaz Ukrainy expires. -
Potential for a Basin-Centered Gas Accumulation in Travis Peak (Hosston) Formation, Gulf Coast Basin, U.S.A
Potential for a Basin-Centered Gas Accumulation in Travis Peak (Hosston) Formation, Gulf Coast Basin, U.S.A Geologic Studies of Basin-Centered Gas Systems U.S. Geological Survey Bulletin 2184-E Discrete-Type Accumulations Structural Stratigraphic Accumulation Accumulation Continuous-Type Accumulation U.S. Department of the Interior U.S. Geological Survey Potential for a Basin-Centered Gas Accumulation in Travis Peak (Hosston) Formation, Gulf Coast Basin, U.S.A. By Charles E. Bartberger, Thaddeus S. Dyman, and Steven M. Condon Geologic Studies of Basin-Centered Gas Systems Edited by Vito F. Nuccio and Thaddeus S. Dyman U.S. Geological Survey Bulletin 2184-E This work funded by the U.S. Department of Energy, National Energy Technology Laboratory, Morgantown, W. Va., under contracts DE-AT26-98FT40031 and DE-AT26-98FT40032, and by the U.S. Geological Survey Central Region Energy Resources Team U.S. Department of the Interior U.S. Geological Survey U.S. Department of the Interior Gale A. Norton, Secretary U.S. Geological Survey Charles G. Groat, Director Posted online April 2003, version 1.0 This publication is only available online at: http://geology.cr.usgs.gov/pub/bulletins/b2184-e/ Any use of trade, product, or fi rm names in this publication is for descriptive purposes only and does not imply endorsement by the U.S. Government Contents Abstract.......................................................................................................................................................... 1 Introduction .................................................................................................................................................. -
Hydrocarbon Processing®
HYDROCARBON PROCESSING® 2012 Gas Processes Handbook HOME PROCESSES INDEX COMPANY INDEX Sponsors: SRTTA HYDROCARBON PROCESSING® 2012 Gas Processes Handbook HOME PROCESSES INDEX COMPANY INDEX Sponsors: Hydrocarbon Processing’s Gas Processes 2012 handbook showcases recent advances in licensed technologies for gas processing, particularly in the area of liquefied natural gas (LNG). The LNG industry is poised to expand worldwide as new natural gas discoveries and production technologies compliment increasing demand for gas as a low-emissions fuel. With the discovery of new reserves come new challenges, such as how to treat gas produced from shale rock—a topic of particular interest for the growing shale gas industry in the US. The Gas Processes 2012 handbook addresses this technology topic and updates many others. The handbook includes new technologies for shale gas treating, synthesis gas production and treating, LNG and NGL production, hydrogen generation, and others. Additional technology topics covered include drying, gas treating, liquid treating, effluent cleanup and sulfur removal. To maintain as complete a listing as possible, the Gas Processes 2012 handbook is available on CD-ROM and at our website for paid subscribers. Additional copies may be ordered from our website. Photo: Lurgi’s synthesis gas complex in Malaysia. Photo courtesy of Air Liquide Global E&C Solutions. Please read the TERMS AND CONDITIONS carefully before using this interactive CD-ROM. Using the CD-ROM or the enclosed files indicates your acceptance of the terms and conditions. www.HydrocarbonProcessing.com HYDROCARBON PROCESSING® 2012 Gas Processes Handbook HOME PROCESSES INDEX COMPANY INDEX Sponsors: Terms and Conditions Gulf Publishing Company provides this program and licenses its use throughout the Some states do not allow the exclusion of implied warranties, so the above exclu- world. -
A Wood-Gas Stove for Developing Countries T
A WOOD-GAS STOVE FOR DEVELOPING COUNTRIES T. B. Reed and Ronal Larson The Biomass Energy Foundation, Golden, CO., USA ABSTRACT Through the millennia wood stoves for cooking have been notoriously inefficient and slow. Electricity, gas or liquid fuels are preferred for cooking - when they can be obtained. In the last few decades a number of improvements have been made in woodstoves, but still the improved wood stoves are difficult to control and manufacture and are often not accepted by the cook. Gasification of wood (or other biomass) offers the possibility of cleaner, better controlled gas cooking for developing countries. In this paper we describe a wood-gas stove based on a new, simplified wood gasifier. It offers the advantages of “cooking with gas” while using a wide variety of biomass fuels. Gas for the stove is generated using the “inverted downdraft gasifier” principle. In one mode of operation it also produces 20-25% charcoal (dry basis). The stove operates using natural convection only. It achieves clean “blue flame” combustion using an “air wick” that optimizes draft and stabilizes the flame position. The emissions from the close coupled gasifier-burner are quite low and the stove can be operated indoors. Keywords: inverted downdraft gasifier, domestic cooking stove, natural draft *Presented at the “Developments in Thermochemical Biomass Conversion” Conference, Banff, Canada, 20-24 May, 1996. 1 A WOOD-GAS STOVE FOR DEVELOPING COUNTRIES T. B. Reed and Ronal Larson The Biomass Energy Foundation, Golden, CO., USA 1. Introduction - 1.1. The Problem Since the beginning of civilization wood and biomass have been used for cooking. -
Natural Gas Acid Gas Removal and Sulfur Recovery Process Economics Program Report 216A
` IHS CHEMICAL Natural Gas Acid Gas Removal and Sulfur Recovery Process Economics Program Report 216A December 2016 ihs.com PEP Report 216A Natural Gas Acid Gas Removal and Sulfur Recovery Anshuman Agrawal Principal Analyst, Technologies Analysis Downloaded 3 January 2017 10:20 AM UTC by Anandpadman Vijayakumar, IHS ([email protected]) IHS Chemical | PEP Report 216A Natural Gas Acid Gas Removal and Sulfur Recovery PEP Report 216A Natural Gas Acid Gas Removal and Sulfur Recovery Anshuman Agrawal, Principal Analyst Abstract Natural gas is generally defined as a naturally occurring mixture of gases containing both hydrocarbon and nonhydrocarbon gases. The hydrocarbon components are methane and a small amount of higher hydrocarbons. The nonhydrocarbon components are mainly the acid gases hydrogen sulfide (H2S) and carbon dioxide (CO2) along with other sulfur species such as mercaptans (RSH), organic sulfides (RSR), and carbonyl sulfide (COS). Nitrogen (N2) and helium (He) can also be found in some natural gas fields. Natural gas must be purified before it is liquefied, sold, or transported to commercial gas pipelines due to toxicity and corrosion-forming components. H2S is highly toxic in nature. The acid gases H2S and CO2 both form weak corrosive acids in the presence of small amounts of water that can lead to first corrosion and later rupture and fire in pipelines. CO2 is usually a burden during transportation of natural gas over long distances. CO2 removal from natural gas increases the heating value of the natural gas as well as reduces its greenhouse gas content. Separation of methane from other major components contributes to significant savings in the transport of raw materials over long distances, as well as savings from technical difficulties such as corrosion and potential pipeline rupture. -
Combustion of Low-Calorific Waste Biomass Syngas
Flow Turbulence Combust (2013) 91:749–772 DOI 10.1007/s10494-013-9473-9 Combustion of Low-Calorific Waste Biomass Syngas Kamil Kwiatkowski · Marek Dudynski´ · Konrad Bajer Received: 7 March 2012 / Accepted: 31 May 2013 / Published online: 19 June 2013 © The Author(s) 2013. This article is published with open access at Springerlink.com Abstract The industrial combustion chamber designed for burning low-calorific syngas from gasification of waste biomass is presented. For two different gases derived from gasification of waste wood chips and turkey feathers the non-premixed turbulent combustion in the chamber is simulated. It follows from our computations that for stable process the initial temperature of these fuels must be at least 800 K, with comparable influx of air and fuel. The numerical simulations reveal existence of the characteristic frequency of the process which is later observed in high-speed cam- era recordings from the industrial gasification plant where the combustion chamber operates. The analysis of NO formation and emission shows a difference between wood-derived syngas combustion, where thermal path is prominent, and feathers- derived fuel. In the latter case thermal, prompt and N2O paths of nitric oxides formation are marginal and the dominant source of NO is fuel-bound nitrogen. Keywords Biomass · Waste · Gasification · Syngas · Turbulent combustion K. Kwiatkowski (B) · M. Dudynski´ · K. Bajer Faculty of Physics, University of Warsaw, Pasteura 7, 02-093 Warsaw, Poland e-mail: [email protected] K. Kwiatkowski · K. Bajer Interdisciplinary Centre for Mathematical and Computational Modelling, University of Warsaw, Pawinskiego´ 5a, 02-106 Warsaw, Poland M. Dudynski´ Modern Technologies and Filtration Sp. -
Liquefied Natural Gas: Description, Risks, Hazards, Safeguards
Liquefied Natural Gas: Description, Risks, Hazards, Safeguards Instructor: Dr. Simon Waldram Done by: Maryam Manojahri Maha Kafood Mohd Kamal CHEN455- Process Safety Engineering Nov. 17, 2009 Table of Contents Executive Summary..……………………………………………………………………………..……..i List of Tables.……………………………………………………………………….……………..….…ii List of Figures.……………………………………………………………………….………………..…ii Introduction.……………………………………………………………………………..……………….1 Value Chain…………………………………………………………………………………..………..….1 Liquefied Natural Gas Process Description and Risks Associated 1.1: Inlet Receiving and Condensate Stabilization………………………………………….….…3 1.2:Acid Gas Removal and Sulfur Recovery……………..………………………….…………….3 1.3:Dehydration and Mercaptan Remov.…………………………………………………….…….3 1.4:Mercury Removal…..…………………………………………………………………….……4 1.5:Gas Chilling and Liquefaction…..………………………………………….………………….4 1.6:Refrigeration ………………………..……………………………………………..…………..5 1.7:Fractionation and Nitrogen Rejection……………………...……………………………...…...5 1.8:Helium Extraction……..……………………………………………..…………..….…………6 1.9:Process Risks, Hazards and Safeguard………………………….…………...………………...6 Safety and Risk Assessments in LNG Main Parts 2.1: Safety in Locating LNG Plants….…………………………………………….………………8 2.1-1:Phast Simulation……………...……………………………………………………..9 2.2:Safety in Process Operation …………………………………………………………11 2.2-1:Risk Assessment in LNG Process Operation…...………………………….11 2.2-1-1:Training ………...……………………………………………….11 H2S Gas in LNG………………………………………………….12 2.2-1-2:Personal Protective Equipment (PPE)……………...…....………13 2.2-1-3:Emergency -
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.