Petroleum Refining: Introduction, Products, Refinery's Configurations, Hydrogen Technologies
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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. -
Sulfuric Acid from Sulfur Updates on Contact Process PEP Review 2018-12 February 2018
` Sulfuric Acid from Sulfur Updates on Contact Process PEP Review 2018-12 February 2018 Rajiv Narang Director Process Economics Program IHS Markit | PEP Review 2018-12 Sulfuric Acid from Sulfur/Updates on Contact Process PEP Review 2018-12 Sulfuric Acid from Sulfur/Updates on Contact Process Rajiv Narang, Director Abstract Sulfuric acid (H2SO4) is the world’s largest consumed chemical, with consumption of around 260 MMT (million metric tons) on a 100% acid basis and a growth rate of around 2%. Traditionally, consumption of this chemical is considered as a barometer of a nation’s GDP. The majority of sulfuric acid production (59%) is from burning of elemental sulfur, in a contact process. The sulfur is sourced mostly from oil and gas processing facilities, in which the sulfur is removed from various petroleum or natural gas products. IHS Markit’s Process Economics Program (PEP) last addressed this production technology in PEP Report 84A, Sulfuric Acid (June 1985), which covered the manufacture of sulfuric acid from sulfur in new versus old, retrofitted plants, as well as from metallurgical offgases. This review specifically updates the contact process for the production of sulfuric acid by burning of elemental sulfur. The review examines the developments in this production technology, including advances in catalyst, material of construction, and heat recovery. The process is simulated using Aspen Plus™ software. It focuses on technology basis, raw material and utility consumptions, equipment list, capital cost, along with capacity exponents, and production costs for a 2,000 STPD (short ton per day) of (100% basis) sulfuric acid product. This review provides insight into sulfuric acid plant process economics, and can be used as a tool for cost estimation for different plant capacities. -
Catalytic Transfer Hydrogenolysis Reactions for Lignin Valorization to Fuels and Chemicals
catalysts Review Catalytic Transfer Hydrogenolysis Reactions for Lignin Valorization to Fuels and Chemicals Antigoni Margellou 1 and Konstantinos S. Triantafyllidis 1,2,* 1 Department of Chemistry, Aristotle University of Thessaloniki, 54124 Thessaloniki, Greece; [email protected] 2 Chemical Process and Energy Resources Institute, Centre for Research and Technology Hellas, 57001 Thessaloniki, Greece * Correspondence: [email protected] Received: 31 October 2018; Accepted: 10 December 2018; Published: 4 January 2019 Abstract: Lignocellulosic biomass is an abundant renewable source of chemicals and fuels. Lignin, one of biomass main structural components being widely available as by-product in the pulp and paper industry and in the process of second generation bioethanol, can provide phenolic and aromatic compounds that can be utilized for the manufacture of a wide variety of polymers, fuels, and other high added value products. The effective depolymerisation of lignin into its primary building blocks remains a challenge with regard to conversion degree and monomers selectivity and stability. This review article focuses on the state of the art in the liquid phase reductive depolymerisation of lignin under relatively mild conditions via catalytic hydrogenolysis/hydrogenation reactions, discussing the effect of lignin type/origin, hydrogen donor solvents, and related transfer hydrogenation or reforming pathways, catalysts, and reaction conditions. Keywords: lignin; catalytic transfer hydrogenation; hydrogenolysis; liquid phase reductive depolymerization; hydrogen donors; phenolic and aromatic compounds 1. Introduction The projected depletion of fossil fuels and the deterioration of environment by their intensive use has fostered research and development efforts towards utilization of alternative sources of energy. Biomass from non-edible crops and agriculture/forestry wastes or by-products is considered as a promising feedstock for the replacement of petroleum, coal, and natural gas in the production of chemicals and fuels. -
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. -
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. -
Category Assessment Document For
U.S. EPA HPV Challenge Program Category Assessment Document for Acids and Caustics from Petroleum Refining Category Tar acids, cresylic, sodium salts, caustic solutions (CAS No. 68815-21-4); Neutralizing agents (petroleum), spent sodium hydroxide (CAS No. 064742- 40-1); Phenols, sodium salts, mixed with sulfur comp; gasoline alky scrubber residues (CAS No. 68988-99-8); Sludges (petroleum), acid (CAS No. 064742-24-1). Submitted by: American Petroleum Institute Petroleum HPV Testing Group American Petroleum Institute 1220 L Street NW Washington, DC 20005 Consortium Registration # 1100997 July 6, 2009 Acids and Caustics From Petroleum Refining Consortium Registration # 1100997 CATEGORY ASSESSMENT DOCUMENT Acids and Caustics from Petroleum Refining Table of Contents Tables ........................................................................................................................................... 3 Figures ......................................................................................................................................... 3 Annexes........................................................................................................................................ 3 Plain Language Summary ......................................................................................................... 4 1. Introduction ........................................................................................................................ 5 2. Category Description ........................................................................................................ -
Olefins Recovery CRYO–PLUS ™ TECHNOLOGY 02
Olefins Recovery CRYO–PLUS ™ TECHNOLOGY 02 Refining & petrochemical experience. Linde Engineering North America Inc. (LENA) has constructed more than twenty (20) CRYO-PLUS™ units since 1984. Proprietary technology. Higher recovery with less energy. Refinery configuration. Designed to be used in low-pressure hydrogen-bearing Some of the principal crude oil conversion processes are off-gas applications, the patented CRYO-PLUS™ process fluid catalytic cracking and catalytic reforming. Both recovers approximately 98% of the propylene and heavier processes convert crude products (naphtha and gas oils) components with less energy required than traditional into high-octane unleaded gasoline blending components liquid recovery processes. (reformate and FCC gasoline). Cracking and reforming processes produce large quantities of both saturated and Higher product yields. unsaturated gases. The resulting incremental recovery of the olefins such as propylene and butylene by the CRYO-PLUS™ process means Excess fuel gas in refineries. that more feedstock is available for alkylation and polym- The additional gas that is produced overloads refinery erization. The result is an overall increase in production of gas recovery processes. As a result, large quantities of high-octane, zero sulfur, gasoline. propylene and propane (C3’s), and butylenes and butanes (C4’s) are being lost to the fuel system. Many refineries Our advanced design for ethylene recovery. produce more fuel gas than they use and flaring of the ™ The CRYO-PLUS C2= technology was specifically excess gas is all too frequently the result. designed to recover ethylene and heavier hydrocarbons from low-pressure hydrogen-bearing refinery off-gas streams. Our patented design has eliminated many of the problems associated with technologies that predate the CRYO-PLUS C2=™ technology. -
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. -
Anaerobic Degradation of Methanethiol in a Process for Liquefied Petroleum Gas (LPG) Biodesulfurization
Anaerobic degradation of methanethiol in a process for Liquefied Petroleum Gas (LPG) biodesulfurization Promotoren Prof. dr. ir. A.J.H. Janssen Hoogleraar in de Biologische Gas- en waterreiniging Prof. dr. ir. A.J.M. Stams Persoonlijk hoogleraar bij het laboratorium voor Microbiologie Copromotor Prof. dr. ir. P.N.L. Lens Hoogleraar in de Milieubiotechnologie UNESCO-IHE, Delft Samenstelling promotiecommissie Prof. dr. ir. R.H. Wijffels Wageningen Universiteit, Nederland Dr. ir. G. Muyzer TU Delft, Nederland Dr. H.J.M. op den Camp Radboud Universiteit, Nijmegen, Nederland Prof. dr. ir. H. van Langenhove Universiteit Gent, België Dit onderzoek is uitgevoerd binnen de onderzoeksschool SENSE (Socio-Economic and Natural Sciences of the Environment) Anaerobic degradation of methanethiol in a process for Liquefied Petroleum Gas (LPG) biodesulfurization R.C. van Leerdam Proefschrift ter verkrijging van de graad van doctor op gezag van de rector magnificus van Wageningen Universiteit Prof. dr. M.J. Kropff in het openbaar te verdedigen op maandag 19 november 2007 des namiddags te vier uur in de Aula Van Leerdam, R.C., 2007. Anaerobic degradation of methanethiol in a process for Liquefied Petroleum Gas (LPG) biodesulfurization. PhD-thesis Wageningen University, Wageningen, The Netherlands – with references – with summaries in English and Dutch ISBN: 978-90-8504-787-2 Abstract Due to increasingly stringent environmental legislation car fuels have to be desulfurized to levels below 10 ppm in order to minimize negative effects on the environment as sulfur-containing emissions contribute to acid deposition (‘acid rain’) and to reduce the amount of particulates formed during the burning of the fuel. Moreover, low sulfur specifications are also needed to lengthen the lifetime of car exhaust catalysts. -
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 ............................................................................................................................. -
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 ......................................................................................................... -
Providing a Guide
Lydia Miller, Emerson Automation Solutions, USA, explores how guided wave radar instruments can help a refinery make accurate level measurements in a corrosive environment. he alkylation process has long been an important The first two product streams come out of the main technique for refiners to create economical fractionator and are sent on for additional refinement. The gasoline blending components capable of raising propane is part of a mixed stream coming out of the acid the octane rating. There are two main process settler, also containing unrecovered HF and unreacted Tapproaches that are distinguished from one another by isobutane. This stream is sent to a de-propanising stage, their catalyst, either sulfuric acid or hydrofluoric acid (HF). which is effectively a large trayed distillation column, Both approaches take lighter components – primarily where propane is separated from the liquid and sent on for isobutane and olefins (various low-molecular-weight purification. The liquid stream is recycled back to the alkenes) – and, using one of the acids as a catalyst, convert original reactor and mixed with fresh feedstocks. The them to alkylate, which can be added to gasoline. highest possible degree of separation is desirable because This octane booster can be used year-round as it does when the propane is sold as a product it must not have HF not cause vapour pressure problems that are common to residues, and returning propane to the reactor reduces its alternative additives. Both processes were developed efficiency. during World War II to help increase the supply of high-octane aviation fuel available to allied air forces, and The de-propanising tower both have been in use ever since.