Petroleum Residue Upgrading Via Delayed Coking: a Review
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Petroleum Coke
Report No. 72 PETROLEUM COKE by SAMUEL C. SPENCER October 1971 A private report by the 0 PROCESS ECONOMICS PROGRAM STANFORD RESEARCH INSTITUTE MENLO PARK, CALIFORNIA I * CONTENTS 1 INTRODUCTION, . 1 2 SUMMARY . * . , . Economic Aspects ...................... 6 Technical Aspects ..................... 10 3 INDUSTRY STATUS . , . , , . 17 Trends . .................... 17 Applications . , . .................... 29 Fuel . .................... 31 Aluminum (anodes) .................... 32 MetallurgicalCoke .................... 36 Chemicals . .................... 37 Formed Shapes . .................... 38 Other Uses . , .................... 39 4 DEVELOPMENTOF COKING PROCESSES . , , , , . , . 41 5 CHEMISTRY ......................... 47 Composition ........................ 47 Basic Chemistry ...................... 52 6 DELAYED COKING. ...................... 59 Review of Process ..................... 59 Process Description .................... 68 Materials of COnStrUctiOn ................. 83 Process Discussion ..................... 84 Process Variations and Innovations ............. 93 Cost Estimates ....................... 95 Capital Costs ...................... 96 Production Costs ..................... 100 Needle Coke Economics ................... 112 V CONTENTS 7 FLUID COKING ........................ 119 Review of Process ..................... 119 Process Description .................... 129 Materials of Construction ................. 133 Process Discussion ..................... 140 Process Variations and Innovations ............. 144 Cost Estimates -
Screening-Level Hazard Characterization of Petroleum Coke
U.S. Environmental Protection Agency June 2011 Hazard Characterization Document SCREENING-LEVEL HAZARD CHARACTERIZATION Petroleum Coke Category SPONSORED CHEMICALS Petroleum coke, green CASRN 64741-79-3 Petroleum coke, calcined CASRN 64743-05-1 The High Production Volume (HPV) Challenge Program1was conceived as a voluntary initiative aimed at developing and making publicly available screening-level health and environmental effects information on chemicals manufactured in or imported into the United States in quantities greater than one million pounds per year. In the Challenge Program, producers and importers of HPV chemicals voluntarily sponsored chemicals; sponsorship entailed the identification and initial assessment of the adequacy of existing toxicity data/information, conducting new testing if adequate data did not exist, and making both new and existing data and information available to the public. Each complete data submission contains data on 18 internationally agreed to “SIDS” (Screening Information Data Set1,2) endpoints that are screening-level indicators of potential hazards (toxicity) for humans or the environment. The Environmental Protection Agency’s Office of Pollution Prevention and Toxics (OPPT) is evaluating the data submitted in the HPV Challenge Program on approximately 1400 sponsored chemicals by developing hazard characterizations (HCs). These HCs consist of an evaluation of the quality and completeness of the data set provided in the Challenge Program submissions. They are not intended to be definitive statements regarding the possibility of unreasonable risk of injury to health or the environment. The evaluation is performed according to established EPA guidance2,3 and is based primarily on hazard data provided by sponsors; however, in preparing the hazard characterization, EPA considered its own comments and public comments on the original submission as well as the sponsor’s responses to comments and revisions made to the submission. -
Converting Visbreakers to Delayed Cokers - an Opportunity for European Refiners
Converting Visbreakers to Delayed Cokers - An Opportunity for European Refiners European Coking.com Conference Sept. 30 - Oct. 2, 2008 Alex Broerse Lummus Technology a CB&I company © Lummus Technology Overview Introduction Delayed Coking Delayed Coking vs. Visbreaking Case Study Conclusions © Lummus Technology Converting Visbreakers to Delayed Cokers - 2 Fuel Oil Market General trend: reduction of sulfur content in fuel oil Typically 1.0-1.5 wt% S International Maritime Organization introduced SOx Emission Control Areas: . Sulfur content of fuel oil on board ships < 1.5 wt% . 1st SECA: Baltic Sea (effective 2006) . North Sea end of 2007 . More to follow Similar trend in other fuel oil application areas End of bunker fuel oil as sulfur sink? © Lummus Technology Converting Visbreakers to Delayed Cokers - 3 European Fuels Market Increased demand for ULS diesel Gradually decreasing fuel oil market Price gap between low sulfur crudes and opportunity crudes Re-evaluation of bottom-of-the-barrel strategy maximize diesel and minimize/eliminate fuel oil production What are the options? © Lummus Technology Converting Visbreakers to Delayed Cokers - 4 Bottom-of-the-Barrel Conversion Technologies Non Catalytic Catalytic Delayed coking Atm. / vac. resid hydrotreating Fluid / flexicoking Ebullated bed hydrocracking Gasification Resid FCC © Lummus Technology Converting Visbreakers to Delayed Cokers - 5 Lummus Capabilities for Bottom-of-the-Barrel Lummus Technology – Houston Delayed coking Resid FCC Chevron Lummus Global JV – Bloomfield Atmospheric/vacuum residue hydrotreating LC-FINING ebullated bed hydrocracking Lummus Technology – Bloomfield / The Hague Refinery planning studies (e.g., grassroots, revamps, processing of opportunity crudes) © Lummus TechnologyExtensive experience in heavy crude upgrade Converting Visbreakers to Delayed Cokers - 6 scenarios Overview Introduction Delayed Coking Delayed Coking vs. -
Why the Bay Area Should Say “No” to Coal and Petroleum Coke Exports
Why the Bay Area should say “No” to Coal and Petroleum Coke Exports Big coal and oil companies are looking for ways to ship their dirty commodities abroad from U.S. ports. As Northwest communities push back against proposed export terminals in Washington and Oregon, the companies have turned to their next target: the Bay Area. If coal and petroleum coke-carrying trains come to our area, coal dust from open rail cars will threaten community health by polluting our air, land and water. Thousands of people on the West Coast are leading a grassroots movement against coal exports. It’s time to let big coal and oil know that their exports aren’t welcome in California. Where is the coal coming from? To reach Bay Area ports, coal trains from mines in the Powder River Basin (PRB) or the Utah and Colorado region travel through many communities including Sacramento, Richmond, Stockton, Pittsburg, Bakersfield, Fresno, Merced and Modesto. And these trains are already on the move.1 Where is petcoke coming from, and what is it? • Petroleum coke, or petcoke, is a solid carbon byproduct that results from oil refining processes. When petcoke is burnt, it emits 5 to 10 percent more carbon dioxide 2) per (C0 unit of energy than coal. On average, one ton of petcoke yields 53.6 percent more CO2 than a ton of coal.2 Petcoke also emits toxic residues, from heavy metals to sulfur. • Petcoke is so dirty that the U.S. Environmental Protection Agency bans it from being burned in our country. Yet, the EPA still allows it to be exported abroad, pushing the pollution offshore. -
Upgrading of Coker Distillate Under Variable Hydrotreating Operating Conditions
View metadata, citation and similar papers at core.ac.uk brought to you by CORE provided by Elsevier - Publisher Connector Egyptian Journal of Petroleum (2011) 20, 25–31 Egyptian Petroleum Research Institute Egyptian Journal of Petroleum www.elsevier.com/locate/egyjp www.sciencedirect.com Upgrading of coker distillate under variable hydrotreating operating conditions H.A. Elsayed *, H.S. Ahmed, M.F. Monufy Refining Department, Egyptian Research Institute, Nasr City, Cairo, Egypt Received 28 February 2010; accepted 2 January 2011 Available online 19 October 2011 KEYWORDS Abstract Studies on hydrotreating coker distillates, produced from a delayed coker unit were done Hydrotreating; using a commercially available CoMo/c-Al2O3 catalyst, on which 0.2 wt% P2O5 was added in order Hydrotreating catalyst; to improve its characteristics. The experimental studies were conducted in a fixed-bed continuous- Coker distillate; reactor (cata-test unit) at temperatures (300–400 °C) and total hydrogen pressure (40–65 bar). These Hydrodesulfurization conditions have affected the feedstock characteristics and great reduction of sulfur, aromatics and boiling ranges. Other improvements were obtained in diesel index (DI) due to hydrogenation reac- tion of aromatics and desulfurization of its sulfur contents. ª 2011 Egyptian Petroleum Research Institute. Production and hosting by Elsevier B.V. Open access under CC BY-NC-ND license. 1. Introduction in fuels and gas oil or diesel to <0.01 wt%. The removal of sulfur containing compounds, such as thiophenes, mercaptans, In recent years, sulfur reduction from light gas oil or diesel fuel dibenzothiophene and especially its alkyl substituted deriva- using catalytic hydrodesulfurization (HDS) is a routine opera- tives is necessary in order to minimize the polluting effects of tion in petroleum refining process due to environmental regu- containing gases such as SO2 that may be released into the lations and to improve the combustion qualities of automotive atmosphere during combustion [1]. -
Residuum Processing
CHAPTER SIX Residuum Processing DELAYED COKING Delayed coking is a thermal process in which the vacuum residue from crude distillation is heated in a furnace then confined in a reaction zone or coke drum under proper operating conditions of temperature and pressure until the unvaporized portion of the furnace effluent is converted to vapor and coke. Delayed coking is an endothermic reaction, with the furnace supplying the necessary heat for the coking reactions. The reactions in the delayed coking are complex. In the initial phase, the feed is partially vaporized and cracked as it passes through the furnace. In the next step, cracking of the vapor occurs as it passes through the drum. In the final step, succes- sive cracking and polymerization of the liquid confined in the drum takes place at high temperatures, until the liquid is converted into vapor and coke. The coke produced in the delayed coker is almost pure carbon contain- ing some of the impurities of the feed, such as sulfur and metals. THE DELAYED COKING PROCESS The reduced crude or vacuum resid enters the coke fractionator bottom surge zone (see Figure 6-1). The feed is mixed with recycle condensed in the bottom section of the fractionator and pumped by heater charge pump P-04 through coke heater H-Ol, where the charge is rapidly heated to the desired temperature for coke formation in the coke drums. Steam is injected in each heater coil to maintain the required minimum velocity and residence time and suppress the formation of coke in the heater coils. BLOWDOWN CONDENSER BLOWDOWN SETTLING DRUM V-05 E-02 TO FLARE BLOWDOWN DECOKING WATER BLOWDOWN WATER SLOP OIL STORAGETANK CIRCULATION PUMP PUMP T-01 P-08 OIL COOLER P-09 SLOP OIL E-01 COKER RAW WATER BLOWDOW^ DRUM V-04 COKER GAS FRACTIONATOR N. -
Environmental, Health, and Safety Guidelines for Petroleum Refining
ENVIRONMENTAL, HEALTH, AND SAFETY GUIDELINES PETROLEUM REFINING November 17, 2016 ENVIRONMENTAL, HEALTH, AND SAFETY GUIDELINES FOR PETROLEUM REFINING INTRODUCTION 1. The Environmental, Health, and Safety (EHS) Guidelines are technical reference documents with general and industry-specific examples of Good International Industry Practice (GIIP).1 When one or more members of the World Bank Group are involved in a project, these EHS Guidelines are applied as required by their respective policies and standards. These industry sector EHS Guidelines are designed to be used together with the General EHS Guidelines document, which provides guidance to users on common EHS issues potentially applicable to all industry sectors. For complex projects, use of multiple industry sector guidelines may be necessary. A complete list of industry sector guidelines can be found at: www.ifc.org/ehsguidelines. 2. The EHS Guidelines contain the performance levels and measures that are generally considered to be achievable in new facilities by existing technology at reasonable costs. Application of the EHS Guidelines to existing facilities may involve the establishment of site-specific targets, with an appropriate timetable for achieving them. 3. The applicability of the EHS Guidelines should be tailored to the hazards and risks established for each project on the basis of the results of an environmental assessment in which site-specific variables— such as host country context, assimilative capacity of the environment, and other project factors—are taken into account. The applicability of specific technical recommendations should be based on the professional opinion of qualified and experienced persons. 4. When host country regulations differ from the levels and measures presented in the EHS Guidelines, projects are expected to achieve whichever is more stringent. -
Tutorial: Delayed Coking Fundamentals
Tutorial: Delayed Coking Fundamentals Paul J. Ellis Christopher A. Paul Great Lakes Carbon Corporation Port Arthur, TX Prepared for presentation at the AIChE 1998 Spring National Meeting New Orleans, LA March 8-12, 1998 Topical Conference on Refinery Processing Tutorial Session: Delayed Coking Paper 29a Copyright 1998 Great Lakes Carbon Corporation UNPUBLISHED March 9, 1998 1 ABSTRACT Great Lakes Carbon Corporation has worked closely with refineries producing delayed coke in all forms, fuel grade (shot or sponge), anode grade (sponge), and electrode grade (needle) since start-up of the company's first calcining operation in 1937. With on-going research in the area of delayed coking since 1942, Great Lakes Carbon (GLC) has operated delayed coking pilot units including an excellent large-scale pilot unit with a coke drum 0.3 meter (1 ft) diameter by 2.1 meters (7 ft) long and has developed physical models which explain coke formation in coke drums. Knowledge of commercial delayed coking units as well as that of the GLC Pilot Delayed Coker is used in this tutorial paper to describe the formation and uses of the three types of structures of delayed petroleum coke: needle, sponge, and shot. Troubleshooting tips are included on many aspects of the delayed coking drum cycle including: steam stripping, water quenching, coke cutting, drum warm-up, and drum switching technique. Suggestions and descriptions of delayed coking unit hardware are included. The objective of this tutorial paper is to acquaint the non-refinery technologist and further the knowledge of refinery personnel with the delayed coking operation, delayed coking unit hardware, types of coke that can be produced, coke formation models, and the uses of petroleum coke. -
Impact of Feed Properties and Operating Parameters on Delayed Coker Petcoke Quality
Impact of Feed Properties and Operating Parameters on Delayed Coker Petcoke Quality Robert (Bob) Clarke Process Manager, Refining Canada Coking Conference October 22 – 26, 2012 Fort McMurray, Alberta, Canada Categorizing Petroleum Coke Usage: Appearance: • Fuel Grade Shot Coke – Power Generation − Small spherical – Cement balls manufacturing − “Beebees” • Anode Grade Sponge Coke – Aluminum Grade − Amorphous – “Calcinable” − May contain shot beebees • Electrode Grade Needle Coke – Steel Electric Arc − Crystalline Furnace − Clusters of aligned – “Calcinable” needles Coke Formation • Thermal cracking of paraffins & Paraffinic side chains. • Polymerization & aromatic formation. • Heavy aromatics condense to a mesophase. • Mesophase converts to coke. • Asphaltenes & very high MW aromatics rapidly convert to coke skipping mesophase. • Thermal Cracking is endothermic • Condensation & coke formation is exothermic Petroleum Coke General Properties • Volatile Combustible Matter (VCM) • Hardgrove grindablity index (HGI) • Contaminants –Sulfur – Nitrogen – Metals •Ash • Granulometry (fines) Petroleum Coke General Properties: Volatile Combustible Matter (VCM) • VCM is unconverted pitch – Target 12% Max, fuel coke 9% to 10% – 14% VCM is very high; Coke will be soft • Increases green coke hydrogen content • Rules of thumb for control in fuel coke – Increase heater outlet 5-7 °F for 1% decrease in VCM – Increase heater outlet 1-2 °F for each hour reduction in coking cycle time • Best practice: Increase heater outlet 5-7 °F in final hours of coking cycle -
Delayed Coking of South African Petroleum Heavy Residues for the Production of Anode Grade Coke and Automotive Fuels
DELAYED COKING OF SOUTH AFRICAN PETROLEUM HEAVY RESIDUES FOR THE PRODUCTION OF ANODE GRADE COKE AND AUTOMOTIVE FUELS John Graham Clark A dissertation submitted to the Faculty of Engineering and the Built Environment, University of the Witwatersrand, in fulfilment of the requirements for the degree of Master of Science in Engineering Johannesburg, 2008 2 DECLARATION I declare that this dissertation is my own unaided work. It is being submitted to the Degree of Master of Science in Engineering to the University of the Witwatersrand, Johannesburg. It has not been submitted before for any degree or examination to any other University ……………………………………………… (Signature of Candidate) ………………. day of …………………… year…………… (day) (month) (year) 3 ABSTRACT A laboratory scale delayed coking process was used to produce petrol precursors, diesel precursors, methane rich gas, green and calcined coke from five previously untested South African heavy petroleum residues. The ash content of the heavy petroleum residues was found to be detrimental to the microstructure of the green coke and Coefficient of Thermal Expansion (CTE) of the calcined coke. The sulphur content of the calcined cokes produced was found to be in-line with typical global anode grade cokes. De-ashing of the feedstock would be necessary to produce anode grade fillers for the aluminium industry. The local production of anode grade coke would serve to reduce imports and supply the aluminium smelters on the east coast of South Africa. The heavy petroleum residues (also known as heavy fuel oil) are currently used as bunker fuel in the shipping industry and are responsible for substantial air pollution. Delayed coking of these residues could extend the production of petrol and diesel per barrel of imported crude oil and reduce the effect on South Africa’s balance of payments deficit and impact the environment in a beneficial manner with respect to carbon dioxide and sulphur emissions. -
Coker Distillate(S)
STUDY ON HYDROTREATING OF COKER DISTILLATE(S) Mohamed F. Menoufy', Galal M. Abdel- Aleim2,MohamedS. Ebrahim and Mohamed Abdel-Aaty 1. Petroleum Refining Division, Egyptian Petroleum Research Institute, NasrCity.Cairo, Egypt 2. Petrochemicals and Refining Engineering Dcpt, Faculty of Petroleum Engineering and Mining, Suez canal University, Suez-Egypt. 3. Suez Oil Processing Company 4. Chemist, Nasr Petroleum Company. ABSTRACT The primary method to remove sulfur , improve cetane index and reduce aromatic content of gas oil / diesel is hydroprocessing. Therefore, the significant advancements in hydrotreating of light coker gas oil (LCGO) derived from delayed coker unit at Suez Oil Processing Company have been performed in a cata-test fixed bed micro-reactor unit, using a commercial CoMo/AljOj Catalyst after sulfidation. The operating conditions were varied in order to study the impact of these processes conditions (temperature;275-400"C, hydrogen pressure;30-85 bar, and hourly space velocity; 0.5-1.5h"' ) on the yield , and quality of gas oil within hydrotreating regime, which is the important to aid the optimization of the process from the environmental regulations and national market demands point of view. The present investigation is conducted on the LCGO, which was selected as a hydrotreated feedstock due to its higher unsaturated hydrocarbon contents ( aromatics and olefins) and heteroatom (sulfur and nitrogen), in order to produce an upgraded gas oil acceptable as transportation fuel according to the TESCE, Vol. 30, No.2 <s^ >' December 2004 environmental and national regulations, and / or the world wide fuel charter December 2002. 1-INTRODUCTION In recent years, the development and use" of "environmentally friendly" fuels has had high priority throughout the world. -
Petroleum Coke Category Analysis and Hazard Characterization
Contents 1. DESCRIPTION OF PETROLEUM COKE .......................................................................... 1 1.1. Composition and Structure............................................................................................. 1 1.2. Coking Processes and Terminology .............................................................................. 2 1.3. Analytical Characterization............................................................................................. 3 2. CATEGORY DEFINITION AND JUSTIFICATION ............................................................. 4 3. TEST MATERIALS ............................................................................................................. 4 3.1. Previous Studies ............................................................................................................ 4 3.2. New Studies ................................................................................................................... 4 4. PHYSICAL-CHEMICAL PROPERTIES.............................................................................. 5 4.1. Physical-Chemical Screening Information Data Set (SIDS) .......................................... 5 4.2. Assessment Summary for Physical-Chemical Endpoints .............................................. 6 5. ENVIRONMENTAL FATE .................................................................................................. 6 5.1. Environmental Fate Endpoints......................................................................................