Role of Hydrogen in Removing Sulfure Liquid Fuels
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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. -
Concept Papers for Changes to Rule 9-1 -- Refinery Fuel Gas Sulfur
Draft: 05‐14‐15 Appendix C: Concept Paper for Changes to Rule 9‐1: Refinery Fuel Gas Sulfur Limits Rules to Be Amended or Drafted Regulation of refinery fuel gas (RFG) requires amendments to Air District Regulation 9, Rule 1, Sulfur Dioxide. Goals The goal of this rulemaking is to achieve technically feasible and cost‐effective sulfur dioxide (SO2) emission reductions from RFG systems at Bay Area refineries. Background The lightest components of crude oil separated by a refinery’s atmospheric fractionator are methane and ethane, which are also the primary components of natural gas. At petroleum refineries, these products are not produced in marketable quantities, but are used as fuel in the numerous onsite steam generators and process heaters. When produced at a refinery, this product is called refinery fuel gas (RFG). Pipeline natural gas may be used as a supplemental fuel when needed to enhance the quality of RFG or when there is not enough RFG available. Unlike, pipeline natural gas, refinery fuel gas often contains significant quantities of sulfur that occur naturally in crude oil. When burned, these sulfur compounds are converted to SO2. Process and Source Description RFG can contain between a few hundred and a few thousand parts per million‐volume (ppmv) sulfur in the form of hydrogen sulfide (H2S), carbonyl sulfide (COS), and organic sulfur compounds, such as mercaptans. During combustion, the sulfur in all of these compounds will oxidize to form SO2, which is a criteria air pollutant and a precursor to particulate matter. Scrubbing with an amine or caustic solution can be effective at removing H2S and some acidic sulfur containing compounds, but is generally ineffective at removing nonacidic sulfur compounds. -
Catalyst Precursors for Hydrodesulfurization Synthesized in Supercritical Fluids Manuel Théodet
New generation of ”bulk” catalyst precursors for hydrodesulfurization synthesized in supercritical fluids Manuel Théodet To cite this version: Manuel Théodet. New generation of ”bulk” catalyst precursors for hydrodesulfurization synthesized in supercritical fluids. Material chemistry. Université Sciences et Technologies - Bordeaux I,2010. English. NNT : 2010BOR14092. tel-00559113 HAL Id: tel-00559113 https://tel.archives-ouvertes.fr/tel-00559113 Submitted on 24 Jan 2011 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. Distributed under a Creative Commons Attribution - NonCommercial - NoDerivatives| 4.0 International License N° d’ordre : 4092 THÈSE présentée à L’UNIVERSITÉ BORDEAUX I ÉCOLE DOCTORALE DES SCIENCES CHIMIQUES Par Manuel THEODET Ingénieur ENSCPB POUR OBTENIR LE GRADE DE DOCTEUR SPÉCIALITÉ : Physico-Chimie de la Matière Condensée ___________________ NOUVELLE GENERATION DE PRECURSEURS « BULK » DE CATALYSEUR D’HYDRODESULFURATION SYNTHETISES EN MILIEU FLUIDE SUPERCRITIQUE ___________________ NEW GENERATION OF « BULK » CATALYST PRECURSORS FOR HYDRODESULFURIZATION SYNTHESIZED IN SUPERCRITICAL FLUIDS ___________________ Co-superviseurs de recherche : Cristina Martínez & Cyril Aymonier Soutenue le 03 Novembre 2010 Après avis favorable de : M. E. PALOMARES, Professor, UPV, Valencia, Spain Rapporteurs M. M. TÜRK, Professor, KIT, Karlsruhe, Germany Devant la commission d’examen formée de : M. -
Liquefied Petroleum Gas (LPG)
Liquefied Petroleum Gas (LPG) Demand, Supply and Future Perspectives for Sudan Synthesis report of a workshop held in Khartoum, 12-13 December 2010 The workshop was funded by UKaid from the Department for International Development Cover image: © UNAMID / Albert Gonzalez Farran This report is available online at: www.unep.org/sudan Disclaimer The material in this report does not necessarily represent the views of any of the organisations involved in the preparation and hosting of the workshop. It must be noted that some time has passed between the workshop and the dissemination of this report, during which some important changes have taken place, not least of which is the independence of South Sudan, a fact which greatly affects the national energy context. Critically, following the independence, the rate of deforestation in the Republic of Sudan has risen from 0.7% per year to 2.2% per year, making many of the discussions within this document all the more relevant. Whilst not directly affecting the production of LPG, which is largely derived from oil supplies north of the border with South Sudan, the wider context of the economics of the energy sector, and the economy as a whole, have changed. These changes are not reflected in this document. This being said, it is strongly asserted that this document still represents a useful contribution to the energy sector, particularly given its contribution to charting the breadth of perspectives on LPG in the Republic of Sudan. Liquefied Petroleum Gas (LPG) Demand, Supply and Future Perspectives for Sudan Synthesis report of a workshop held in Khartoum, 12-13 December 2010 A joint publication by: Ministry of Environment, Forestry and Physical Development – Sudan, Ministry of Petroleum – Sudan, United Kingdom Department for International Development, United Nations Development Programme and United Nations Environment Programme Table of contents Acronyms and abbreviations . -
Claus Process
PROSIMPLUS APPLICATION EXAMPLE CLAUS PROCESS INTEREST OF THIS EXAMPLE This example corresponds to the simulation of the well-known Claus process. This process allows the recovery of elemental sulfur from acid gas containing H2S and water, and possibly hydrocarbons and carbon dioxide. The particularity of this example lies in the use of equilibrium reactors calculated by minimization of Gibbs free energy to simulate the different steps of the process. ACCESS Free Internet Restricted to ProSim clients Restricted Confidential CORRESPONDING PROSIMPLUS FILES PSPS_EX_EN-Claus-Process.pmp3 Il est rappelé au lecteur que ce cas d'utilisation est un exemple et ne doit pas être utilisé à d'autres fins. Bien que cet exemple soit basé sur un cas réel il ne doit pas être considéré comme un modèle de ce type de procédé et les données utilisées ne sont pas toujours les plus exactes disponibles. ProSim ne pourra en aucun cas être tenu pour responsable de l'application qui pourra être faite des calculs basés sur cet exemple Copyright © 2015 ProSim, Labège, France - Tous droits réservés www.prosim.net Claus Process Version: September 2012 Page: 2 / 11 TABLE OF CONTENTS 1. PROCESS MODELING ..................................................................................................... 3 1.1. Process Description ............................................................................................................................. 3 1.2. Process Flowsheet ............................................................................................................................. -
CCS: Applications and Opportunities for the Oil and Gas Industry
Brief CCS: Applications and Opportunities for the Oil and Gas Industry Guloren Turan, General Manager, Advocacy and Communications May 2020 Contents 1. Introduction ................................................................................................................................... 2 2. Applications of CCS in the oil and gas industry ............................................................................. 2 3. Conclusion ..................................................................................................................................... 4 Page | 1 1. Introduction Production and consumption of oil and gas currently account for over half of global greenhouse gas emissions associated with energy use1 and so it is imperative that the oil and gas industry reduces its emissions to meet the net-zero ambition. At the same time, the industry has also been the source and catalyst of the leading innovations in clean energy, which includes carbon capture and storage (CCS). Indeed, as oil and gas companies are evolving their business models in the context of the energy transition, CCS has started to feature more prominently in their strategies and investments. CCS is versatile technology that can support the oil and gas industry’s low-carbon transition in several ways. Firstly, CCS is a key enabler of emission reductions in the industries’ operations, whether for compliance reasons, to meet self-imposed performance targets or to benefit from CO2 markets. Secondly, spurred by investor and ESG community sentiment, the industry is looking to reduce the carbon footprint of its products when used in industry, since about 90% of emissions associated with oil and gas come from the ultimate combustion of hydrocarbons – their scope 3 emissions. Finally, CCS can be a driver of new business lines, such as clean power generation and clean hydrogen production. From the perspective of the Paris Agreement, however, the deployment of CCS globally remains off track. -
THE H-OIL PROCESS: a Worldwxide LEADER in VACUUM RESIDUE HYDROPROCESSING” \ ^
—t&CR I'd, D 3 YJj TT-097 CONEXPO ARPEL '96 . i ' 1 "THE H-OIL PROCESS: A WORLDWXiDE LEADER IN VACUUM RESIDUE HYDROPROCESSING” \ ^ J.J. Colyar1 L.I. Wisdom2 A. Koskas3 SUMMARY With the uncertainty of market trends, refiners will need to hedge their investment strategies in the future by adding processing units that provide them with flexibility to meet the changing market. The various process configurations involving the H-Oil® Process described in this paper have been tested commercially and provide the refiner with the latest state of the art technology. ABSTRACT The H-Oil® Process is a catalytic hydrocracking process, invented by HRI, Inc., a division of IFP Enterprises, Inc. which is used to convert and upgrade petroleum residua and heavy oils. Today the H-Oil Process accounts for more than 50 percent of the worldwide vacuum residue hydroprocessing market due to its unique flexibility to handle a wide variety of heavy crudes 'while producing clean transportation fuels. The process is also flexible in terms of changes in yield selectivity and product quality. The unconverted vacuum residue from the process can be utilized for fuel oil production, blended into asphalt, routed to resid catalytic cracking, directly combusted or gasified to produce hydrogen. This paper will discuss additional background information on the H-Oil Process, some of the key advances made to the process and applications for the Latin America market. The paper will also discuss the status of recent commercial plants which are in operation or which are under design or construction and which utilize these new advances. -
Facts About Alberta's Oil Sands and Its Industry
Facts about Alberta’s oil sands and its industry CONTENTS Oil Sands Discovery Centre Facts 1 Oil Sands Overview 3 Alberta’s Vast Resource The biggest known oil reserve in the world! 5 Geology Why does Alberta have oil sands? 7 Oil Sands 8 The Basics of Bitumen 10 Oil Sands Pioneers 12 Mighty Mining Machines 15 Cyrus the Bucketwheel Excavator 1303 20 Surface Mining Extraction 22 Upgrading 25 Pipelines 29 Environmental Protection 32 In situ Technology 36 Glossary 40 Oil Sands Projects in the Athabasca Oil Sands 44 Oil Sands Resources 48 OIL SANDS DISCOVERY CENTRE www.oilsandsdiscovery.com OIL SANDS DISCOVERY CENTRE FACTS Official Name Oil Sands Discovery Centre Vision Sharing the Oil Sands Experience Architects Wayne H. Wright Architects Ltd. Owner Government of Alberta Minister The Honourable Lindsay Blackett Minister of Culture and Community Spirit Location 7 hectares, at the corner of MacKenzie Boulevard and Highway 63 in Fort McMurray, Alberta Building Size Approximately 27,000 square feet, or 2,300 square metres Estimated Cost 9 million dollars Construction December 1983 – December 1984 Opening Date September 6, 1985 Updated Exhibit Gallery opened in September 2002 Facilities Dr. Karl A. Clark Exhibit Hall, administrative area, children’s activity/education centre, Robert Fitzsimmons Theatre, mini theatre, gift shop, meeting rooms, reference room, public washrooms, outdoor J. Howard Pew Industrial Equipment Garden, and Cyrus Bucketwheel Exhibit. Staffing Supervisor, Head of Marketing and Programs, Senior Interpreter, two full-time Interpreters, administrative support, receptionists/ cashiers, seasonal interpreters, and volunteers. Associated Projects Bitumount Historic Site Programs Oil Extraction demonstrations, Quest for Energy movie, Paydirt film, Historic Abasand Walking Tour (summer), special events, self-guided tours of the Exhibit Hall. -
Sulfur Recovery from Acid Gas Using the Claus Process and High Temperature Air Combustion (Hitac) Technology
American Journal of Environmental Sciences 4 (5): 502-511, 2008 ISSN 1553-345X © 2008 Science Publications Sulfur Recovery from Acid Gas Using the Claus Process and High Temperature Air Combustion (HiTAC) Technology 1Mohamed Sassi and 2Ashwani K. Gupta 1Department of Chemical and Mechanical Engineering, The Petroleum Institute, P.O. Box 2533, Abu Dhabi, UAE 2Department of Mechanical Engineering, University of Maryland, College Park, MD 20742, USA Abstract: Sulfur-bearing compounds are very detrimental to the environment and to industrial process equipment. They are often obtained or formed as a by-product of separation and thermal processing of fuels containing sulfur, such as coal, crude oil and natural gas. The two sulfur compounds, which need special attention, are: hydrogen sulfide (H2S) and sulfur dioxide (SO2). H2S is a highly corrosive gas with a foul smell. SO2 is a toxic gas responsible for acid rain formation and equipment corrosion. Various methods of reducing pollutants containing sulfur are described in this paper, with a focus on the modified Claus process, enhanced by the use of High Temperature Air Combustion (HiTAC) technology in the Claus furnace. The Claus process has been known and used in the industry for over 100 years. It involves thermal oxidation of hydrogen sulfide and its reaction with sulfur dioxide to form sulfur and water vapor. This process is equilibrium-limited and usually achieves efficiencies in the range of 94-97%, which have been regarded as acceptable in the past years. Nowadays strict air pollution regulations regarding hydrogen sulfide and sulfur dioxide emissions call for nearly 100% efficiency, which can only be achieved with process modifications. -
Thermal Stability Analysis of Hydroprocessing Unit A
THERMAL STABILITY ANALYSIS OF HYDROPROCESSING UNIT A Thesis by YONGCHUL CHO Submitted to the Office of Graduate and Professional Studies of Texas A&M University in partial fulfillment of the requirements for the degree of MASTER OF SCIENCE Chair of Committee, M. Sam Mannan Committee Members, Mahmoud M. El-Halwagi Maria A. Barrufet Head of Department, M. Nazmul Karim May 2018 Major Subject: Chemical Engineering Copyright 2018 Yongchul Cho ABSTRACT Thermal stability is one of the most critical safety issues in the hydroprocessing units. Runaway reactions in the units can lead to catastrophic consequences as the reactors are being operated at high temperature and pressure, and the reactor effluent is a highly explosive mixture which contains hydrogen and hydrocarbons. For example, a fire and explosion due to a runaway reaction in a hydrocracking unit caused one death and forty-six injuries in 1997, in California. While the temperature runaway is the topic which has been studied extensively, most of the studies worked on simple reactions and little focused on the complex reactions such as hydroprocessing reactions. Also, in the studies on the hydroprocessing reactions, a lumping kinetic model was used which is less accurate and requires experiments for each application. In this research, the thermal stability of a naphtha hydrotreater will be analyzed by using a commercial process simulator ProMax where a novel mechanistic kinetic model, Single Event Kinetics has been integrated. Also, a simplified model will be established by using the data provided by ProMax for further analysis. The continuity and energy equations and parametric sensitivity equations will be solved by Matlab based on the methodology presented by Morbidelli and Varma. -
Multi-Objective Optimization of a Rectisol Process
Jiří Jaromír Klemeš, Petar Sabev Varbanov and Peng Yen Liew (Editors) Proceedings of the 24th European Symposium on Computer Aided Process Engineering – ESCAPE 24 June 15-18, 2014, Budapest, Hungary. Copyright © 2014 Elsevier B.V. All rights reserved. Multi-objective Optimization of a Rectisol® Process Manuele Gatti a,*, Emanuele Martelli a, Franҫois Maréchal b, Stefano Consonni a a Politecnico di Milano, Dipartimento di Energia, Via Lambruschini 4, Milano, Italy b Industrial Process Energy Systems Engineering (IPESE), Ecole Polytechnique Fédérale de Lausanne, 1015, Lausanne, Switzerland [email protected] Abstract This work focuses on the design, simulation and optimization of a Rectisol®-based process tailored for the selective removal of H2S and CO2 from gasification derived synthesis gas. Such task is quite challenging due to the need of addressing simultaneously the process design, energy integration and utility design. The paper, starting from a Rectisol® configuration recently proposed by the authors, describes the models and the solution strategy used to carry out the multi-objective optimization with respect to exergy consumption, CO2 capture level and capital cost. Keywords: Rectisol, CO2 Capture, Numerical Optimization, PGS-COM, Pareto frontier 1. Introduction Coal to Liquids (CTL) as well as Integrated Gasification Combined Cycle (IGCC) plants take advantage from the conversion of a cheap, fossil fuel like coal into a clean synthetic gas, mainly composed of hydrogen, carbon monoxide, carbon dioxide and other minor species, either to produce Liquid Fuels or Electricity as output. In such plants, sulfur-containing compounds are among the most critical contaminants, and they should be separated from the raw syngas not only to cope with emissions regulations but, in the specific case of CTL, also to avoid any potential detrimental impact on the catalyst of the downstream chemical synthesis process. -
Refining Company Perspective & Approach to High Quality Binders
June 18, 2019 Refining company perspective & approach to high quality asphalts Pavel Kriz, Ph.D., P.Eng. Americas Asphalt Group & Discipline Technical Leader This communication may contain confidential information for the use of the entity to which it is addressed. If you are not the intended recipient, you are hereby notified that any use, dissemination, distribution, or copying of this communication is prohibited. If you are the intended recipient, information may not be reproduced or further distributed out of your organization without the originator's authorization in writing. 2019 © Imperial Oil Limited. All rights reserved. Imperial & ExxonMobil: Funding Members of Asphalt Institute 2 Global Asphalt Operations In NA Imperial & ExxonMobil manufacture asphalt at Joliet, Billings, Nanticoke & Strathcona Refineries • Produce over 2MTa of premium asphalt • Utilize high quality WestCan crudes • Committed to product quality & integrity Sarnia Technology Applications & Research • Canada’s first & largest petroleum research est. 1924 • 700+ patents • ~40+ PhDs out of ~100 employees • Global Centre of Excellence for Asphalt Asphalt Production • Long heritage & deep expertise in asphalt research Asphalt Technology/R&D 3 Crude Oil • “Crude oil is a naturally occurring, yellowish-black liquid found in geological formations beneath the Earth's surface” • It is a mixture of a large number of different hydrocarbons • Each oil has a unique mix of molecules, which define its properties, like color and viscosity Composition by weight Element Percent range Carbon 83 to 85% Hydrogen 10 to 14% Nitrogen 0.1 to 2% Oxygen 0.05 to 1.5% Sulphur 0.05 to 6.0% Metals < 0.1% 4 Crude Oil Origin 5 Crude Oil Reservoir Saturated porous reservoir rock Impermeable layers (e.g.