Characterization and Refinery Processing of Partially-upgraded Bitumen
|
|
- Myles Tucker
- 5 years ago
- Views:
Transcription
1 CCQTA-COQA Joint Meeting in Edmonton, 2016 Characterization and Refinery Processing of Partially-upgraded Bitumen Tomoki Kayukawa JGC Corporation 1
2 Outline Background Properties of Partially Upgraded Product Characterization Olefin Saturation by Hydrotreating Olefin Analysis Refinery Processing Compatibility Test Heat Exchanger Fouling Desalting Performance Summary 2
3 Heavy Oil Transportation Diluent Well Dilution Pipeline Dil-Bit Refinery Diluent shortage High diluent price Full Upgrader Sweet SCO Complex scheme Large oil field Partial Upgrader Sour SCO Simple scheme No diluent 3
4 Partial Upgrading of Bitumen Advantage over Dilution Diluent cost can be reduced Pipeline size can be reduced Environmentally safe (diluent easily vaporized) Advantage over Full Upgrading Lower capital cost Smaller foot print Smaller by-product 4
5 Ongoing Partial Upgrading Project Process (Licensor) Process type CCU (UOP) RFCC HTL (Ivanhoe) Thermal (Coking) I Y Q (ETX) Thermal (Coking) HI-Q (MEG) Thermal + SDA Eureka (Chiyoda) Thermal HSC (TEC) Thermal SDA (KBR) SDA SCWC (JGC) Thermal + Extraction Many partial upgrading technologies are existing Most of them are thermal cracking and/or extraction (SDA) 5
6 Properties of Partially-upgraded Bitumen SCO produced by thermal cracking and extraction (5BPD scale pilot plant, SCO yield : ~70vol%) ANALYSIS METHOD UNIT Upgraded Bitumen TARGET OLEFIN 1H-NMR wt% 3.67 <1.0 SPECIFIC GRAVITY KINETIC VISCOSITY ELEMENTAL ANALYSIS TYPE ANALYSIS SIMDIS DENSITY ASTM D4052 g/ml API - o 22.9 > 10C (Calc.) ASTM D7042 cst 32.1 < 350 Sulfur ASTM D4294 wt% 3.23 SATURATES wt % 37.2 AROMATICS ASTM D2007M wt % 37.3 POLARS wt % 9.9 ASPHALTENE ASTM D4055M wt % o C wt% o C ASTM D2887 wt% 41 MCRT TAN DIENE VALUE 540 o C+ wt% 4 ASTM D4530 wt% 0.5 ASTM D664 mg KOH/g 2.87 UOP326 g I2/100g
7 Properties of Partially-upgraded Bitumen Boiling point [degc] SCO produced by thermal cracking and extraction (5BPD scale pilot plant, SCO yield : ~70vol%) Fraction BP Yield wt% Naphtha IBP Distillate HGO degC 200degC 10wt% Fraction [wt%] 49wt% 7
8 Objectives of Study Investigate product quality of partial upgrading Characterization Olefin Saturation by Hydrotreating Olefin Analysis Address refinery issues in processing partially upgraded oil Refinery Processing Compatibility Test Heat Exchanger Fouling Desalting Performance 8
9 Characterization Olefin Saturation by Hydrotreating Olefin Analyses 9
10 Olefin Saturation by Hydrotreating Target olefin content: < 1.0wt% (1H-NMR) Less hydrogen consumption Less cracking, less desulfurization, less saturation of aromatic compounds Maximize liquid yield Test unit : bench scale hydrotreating (packed bubble column reactor, 30cc of catalyst) 10
11 Product Quality Reactor WABT 1 H-NMR Olefin Desulfurization Aromatics Saturation RUN No. LHSV Sulfur Aromatics degc 1/hr wt% wt% % wt% % Feedstock RUN 1 BASE-25 BASE x RUN 2 BASE BASE RUN 3 BASE+25 BASE x RUN 4 BASE+50 BASE x Target olefin content was achieved at all conditions Lower desulfurization and aromatic saturation were observed at lower temp. Feedstock Product 11
12 Fraction Yields Boiling point [degc] Feedstock RUN 2 Product Fraction [wt%] Distillation curve does not change FEED STOCK RUN 2 PRODUCT Fraction BP Yield wt% Yield wt% Naphtha IBP Distillate HGO
13 Olefin Conversion in Fraction Olefin [wt%] wt% Loss Naphtha Distillate HGO 0.80wt% Conversion % Naphtha 77.2 Distillate 74.2 HGO Feedstock 15-B14-Product (R02, R03, R04) Olefin in naphtha and distillate fraction was drastically reduced 13
14 Detail Analysis for Olefin in Naphtha Naphtha(IBP-200 ): GCxGC, TOF-MS Alkenes Diene/Cycloalkenes wt% Before Hydrotreating After Hydrotreating wt% Before Hydrotreating After Hydrotreating 0 C5 C6 C7 C8 C9 C10 C11 C12 C13 C14 0 C5 C6 C7 C8 C9 C10 C11 C12 C13 C14 Alkenes in naphtha were reduced significantly Diene/Cycloalkenes were reduced only close to 50% 14
15 Detail Analysis for Olefin in Distillate Distillate ( ): HPLC, GCxGC, TOF-MS Alkenes Diene/Cycloalkenes wt% Before Hydrotreating 0.4 After Hydrotreating 0.3 wt% Before Hydrotreating After Hydrotreating 0.0 C11 C12 C13 C14 C15 C16 C17 C18 C19 C20 C C11 C12 C13 C14 C15 C16 C17 C18 C19 C20 C21 Alkenes in distillate were reduced significantly Diene/Cycloalkenes slightly increased. Cycloalkenes were formed by hydrogenation of aromatics?? 15
16 Characterization of Olefin Olefin target (<1.0wt%) can be achieved at various operating conditions. Lower temperature would be preferred to reduce hydrogen consumption. Olefin is concentrated mostly in naphtha. Alkenes in naphtha and distillate were reduced significantly by hydrotreating 16
17 Refinery Processing Compatibility Test Heat Exchanger Fouling Desalting Performance 17
18 Test Method for Compatibility Test Test Method : Wiehe s oil compatibility model I N : Insolubility number S BN : Solubility blending number Blending partially-upgraded Bitumen (SCO) with WCS 18
19 Total Insolubles S BNmix SBNmix, IN WCS SCO I N S BN Blending ratio of SCO [vol%] Blended samples were compatible at any ratios. I N 19
20 Test Method for Fouling Evaluation Test unit : Alcor unit Test conditions : 400, 4 hours Criterion for fouling [Defined by Brons, (400, 3hours)] Low fouling : ΔT < 15 Medium fouling : 15 < ΔT < 30 High fouling : ΔT > 30 [Defined by Shell Canada, (400, 4hours)] Low fouling : %F < 23% 20
21 Equipment for Fouling Evaluation Schematic diagram of experimental unit Heating Section Heater Tube Movable TC (Ts) Outlet Temp (To) Spent Sample Fresh Sample PUMP Inlet Temp (Ti) TC1 (Inlet) TC2 (Outlet) TC3 (Heated Tube) TC4 (Room Temp) 21
22 Temperature Trend during Test Sample: SCO before hydrotreating ΔT = 10ºC Temperature, T (ºC) ºC 270ºC Tc1 Tc2 Tc3 Tc Elapsed Time (min) ΔT=10 is defined as low fouling 22
23 Test Method for Desalting Test Method : Mixing and Settling Test Sample : 20ml of water and 80ml of oil ph 5~8 23
24 Pictures during Settlement Sample: SCO before hydrotreating 1 minute 5 minutes Separation was carried out within 5 minutes at various ph. Water in oil were 0.18~0.25%. 24
25 <Characterization> Conclusion Olefin target can be achieved by hydrotreating. Olefin is concentrated mostly in the naphtha. <Refinery Processing> No problem was found for blending, fouling tendency or desalting performance with SCO before hydrotreating. This study will be continued for understanding about quality of cracked products 25
26 Acknowledgement This study was consulted by OMNICON Consultants Inc.. Hydrotreating, heat exchanger fouling tests and analytical works were performed by CanmetENERGY. Detail analysis of olefins was performed by NHMFL at FSU. Desalting test was performed by Nalco Champion. 26
27
28 Test Method for Storage Stability Test Method : ASTM D4625 (Accelerated Stability Test) Conditions: 43.5 for 24 weeks 28
29 Total Insolubles Total Insolubles [mg/100ml] 長期貯蔵安定性 Storage Stability (ASTM D4625) Weeks Total insoluble increased with the time. But leveled off after 12 weeks 29
Impact on Crude Quality
Partial Upgrading of Bitumen Impact on Crude Quality Presented to the joint COQA/CCQTA Meeting Denver, Colorado May 2018 Overview Interest in partial upgrading of bitumen Alberta Government incentives
More informationResults Certified by Core Labs for Conoco Canada Ltd. Executive summary. Introduction
THE REPORT BELOW WAS GENERATED WITH FEEDSTOCK AND PRODUCT SAMPLES TAKEN BY CONOCO CANADA LTD, WHO USED CORE LABORATORIES, ONE OF THE LARGEST SERVICE PROVIDERS OF CORE AND FLUID ANALYSIS IN THE PETROLEUM
More information- Supercritical Water Cracking Technology -
JOGMEC Techno Forum 2014, November 26 th -27 th 2014 Upgrading of Heavy Crude Oil - Technology - Hisato Aoyama Manager, Technology Development Center JGC CORPORATION Organization--Background The Super
More informationDiluent Evaluation for Pipelining
NCUT National Centre for Upgrading Technology a Canada Alberta alliance for bitumen and heavy oil research Diluent Evaluation for Pipelining Parviz Rahimi, Zhiming Fan, Simon Cooper, Teclemariam Alem,
More informationChanging Refinery Configuration for Heavy and Synthetic Crude Processing
Changing Refinery Configuration for Heavy and Synthetic Crude Processing Gary Brierley UOP LLC 2006 UOP LLC. All rights reserved. UOP 4525A-01 Why Should I Even Think About Running Synthetics? Oil sands
More informationUOP UNITY Hydrotreating Products
Satyam Mishra UOP UNITY Hydrotreating Products 19 February 2018 Honeywell UOP ME-TECH Seminar Dubai, UAE UOP 8080A-0 2018 UOP LLC. A Honeywell Company All rights reserved. Outline 1 Unity UNITY UOP Unity
More informationChallenges and Solutions for Shale Oil Upgrading
Challenges and Solutions for Shale Oil Upgrading Don Ackelson UOP LLC, A Honeywell Company 32 nd Oil Shale Symposium Colorado School of Mines October 15-17, 2012 2012 UOP LLC. All rights reserved. UOP
More informationCanadian Bitumen and Synthetic Crudes
Understanding the Quality of Canadian Bitumen and Synthetic Crudes Pat Swafford Spiral Software Limited Crude Oil Quality Group Meeting February 26, 2009 Introduction Canadian crude production is increasing
More informationOn-Line Process Analyzers: Potential Uses and Applications
On-Line Process Analyzers: Potential Uses and Applications INTRODUCTION The purpose of this report is to provide ideas for application of Precision Scientific process analyzers in petroleum refineries.
More informationUnity TM Hydroprocessing Catalysts
Aravindan Kandasamy UOP Limited, Guildford, UK May 15, 2017 May 17, 2017 Unity TM Hydroprocessing Catalysts A unified approach to enhance your refinery performance 2017 Honeywell Oil & Gas Technologies
More informationSolvent Deasphalting Conversion Enabler
Kevin Whitehead Solvent Deasphalting Conversion Enabler 5 th December 2017 Bottom of the Barrel Workshop NIORDC, Tehran 2017 UOP Limited Solvent Deasphalting (SDA) 1 Natural Gas Refinery Fuel Gas Hydrogen
More informationOptimizing Distillate Yields and Product Qualities. Srini Srivatsan, Director - Coking Technology
Optimizing Distillate Yields and Product Qualities Srini Srivatsan, Director - Coking Technology Email: srini.srivatsan@amecfw.com Optimizing Distillate Yields and Product Properties Overview Delayed coker
More informationSOLVENT DEASPHALTING OPTIONS How SDA can increase residue upgrading margins
SOLVENT DEASPHALTING OPTIONS How SDA can increase residue upgrading margins ME Tech Dubai, February 18 & 19, 2014 Steve Beeston - Vice President, Technology Business Environment Requirements Improve refinery
More informationBitumen has become an
Revamping crude and vacuum units to process bitumen Revamping crude and vacuum units to process dilbit can involve extensive equipment replacement as well as major changes to the crude preheating scheme
More informationMaximize Vacuum Residue Conversion and Processing Flexibility with the UOP Uniflex Process
Maximize Vacuum Residue Conversion and Processing Flexibility with the UOP Uniflex Process Hans Lefebvre UOP LLC, A Honeywell Company XVIII Foro de Avances de la Industria de la Refinación 11 and 12, July,
More informationLCO Processing Solutions. Antoine Fournier
LCO Processing Solutions Antoine Fournier 1 Outline Market trends and driving factors The light cycle oil Feedstock characteristics Hydroprocessing challenges Main option for LCO upgrading Catalyst update
More informationPetroleum Refining Fourth Year Dr.Aysar T. Jarullah
Catalytic Operations Fluidized Catalytic Cracking The fluidized catalytic cracking (FCC) unit is the heart of the refinery and is where heavy low-value petroleum stream such as vacuum gas oil (VGO) is
More informationCrude Assay, ASTM, TBP distillations, Evaluation of crude oil properties.
Crude Assay, ASTM, TBP distillations, Evaluation of crude oil properties. Crude Oil Distillation Crude oil distillation is an open art technology. The crude oil is distilled at atmospheric pressure and
More informationOIL REFINERY PROCESSES
OIL REFINERY PROCESSES 1 Types of hydrocarbons Types of hydrocarbons (parafffins, naphthenes, and aromatics). This rating is important to the refinery since the value of the crude oil decreases from classification
More informationCCQTA Update for COQA Houston Meeting
CCQTA Update for COQA Houston Meeting October 13, 2016 Randy Segato President CCQTA Sr Crude Quality Specialist Suncor CCQTA The New Direction 1. Have completed change from a volunteer board to a governance
More informationMEG/WRI s Partial Bitumen Upgrader Project Adding Value to MEG and Alberta
MEG/WRI s Partial Bitumen Upgrader Project Adding Value to MEG and Alberta February 2015 Presentation Format Who we are - MEG and WRI Introduction to Alberta oil sands Resource recovery, transportation
More informationTHE OIL & GAS SUPPLY CHAIN: FROM THE GROUND TO THE PUMP ON REFINING
THE OIL & GAS SUPPLY CHAIN: FROM THE GROUND TO THE PUMP ON REFINING J. Mike Brown, Ph.D. Senior Vice President Technology BASICS OF REFINERY OPERATIONS Supply and Demand Where Does The Crude Oil Come From?
More informationCrude Distillation Chapter 4
Crude Distillation Chapter 4 Gases Gas Sat Gas Plant Polymerization LPG Sulfur Plant Sulfur Alkyl Feed Alkylation Butanes Fuel Gas LPG Gas Separation & Stabilizer Light Naphtha Heavy Naphtha Isomerization
More informationLC-FINING Options for Heavy Oil Upgrading
Annual Meeting March 9-11, 2008 Manchester Grand Hyatt San Diego, CA LC-FINING Options for Heavy Oil Upgrading Presented By: David Wadsworth Americas Director Chevron Lummus Global Bloomfield, NJ National
More informationCo-Processing of Green Crude in Existing Petroleum Refineries. Algae Biomass Summit 1 October
Co-Processing of Green Crude in Existing Petroleum Refineries Algae Biomass Summit 1 October - 2014 1 Overview of Sapphire s process for making algae-derived fuel 1 Strain development 2 Cultivation module
More informationUnit 7. Vaccum Distillation of Crude
Unit 7. Vaccum Distillation of Crude Assistant teacher Belinskaya Nataliya Segeevna 2015 Introduction To extract more distillates from the atmospheric residue, the bottom from the atmospheric crude distillation
More informationCrude Assay Report. Crude Oil sample marked. Barrow Crude Oil. On Behalf Of. Chevron Australia Pty Ltd. Laboratory Supervisor. Crude Assay Chemist
Crude Assay Report on Crude Oil sample marked Barrow Crude Oil On Behalf Of Chevron Australia Pty Ltd. Reported by: Approved by: Michelle Fernandez Laboratory Supervisor Jhonas Fernandez Crude Assay Chemist
More informationSensitivity analysis and determination of optimum temperature of furnace for commercial visbreaking unit
ISSN : 0974-7443 Sensitivity analysis and determination of optimum temperature of furnace for commercial visbreaking unit S.Reza Seif Mohaddecy*, Sepehr Sadighi Catalytic Reaction Engineering Department,
More informationUpgrading Biomass Pyrolysis Vapors to Fungible Hydrocarbon Intermediates
Upgrading Biomass Pyrolysis Vapors to Fungible Hydrocarbon Intermediates tcbiomass 2017 K. Magrini, J. Olstad, M. Jarvis, Y. Parent, B. Peterson, S. Deutch, K. Iisa, M. Sprague, G. Powell September 20,
More informationReducing octane loss - solutions for FCC gasoline post-treatment services
Reducing octane loss - solutions for FCC gasoline post-treatment services Claus Brostrøm Nielsen clbn@topsoe.com Haldor Topsoe Agenda Why post-treatment of FCC gasoline? Molecular understanding of FCC
More informationCrude Oil Compatibility
Crude Oil Compatibility Irwin (Irv) Wiehe Soluble Solu COQG Meeting Houston, Texas October 2, 2003 Irv@SolubleSolu.com www.solublesolu.com Including Fouling Tendency in Crude Oil Purchase Decisions Irwin
More informationUpgrade Bottom of the Barrel to Improve Your Margins
Agafeev Viacheslav OOO UOP, A Honeywell Company Upgrade Bottom of the Barrel to Improve Your Margins 28-30 November 2016 CIS Downstream Summit 2016 Vienna, Austria UOP 7802-1 2016 UOP LLC. A Honeywell
More informationASTM D2007M/ASTM D2549M In-house method/astm D6560/D3279
ID Test Standard Amount Required Price for Cost Recovery Projects (Can $) 1 2 3 4 5 Sulfur compounds distribution by boiling point (GC-SCD) Sulfur compound speciation by GC-SCD Nitrogen compounds distribution
More informationRefComm Galveston May 2017 FCC naphtha posttreatment
RefComm Galveston May 2017 FCC naphtha posttreatment Henrik Rasmussen Haldor Topsoe Inc. Houston TX Agenda Why post-treatment of FCC naphtha? The new sulfur challenge Molecular understanding of FCC naphtha
More informationPORLA Heavy and Crude Oil Stability and Compatibility Analyzer as a Tool to Improve Profitability of Oil Industry
PORLA Heavy and Crude Oil Stability and Compatibility Analyzer as a Tool to Improve Profitability of Oil Industry J. Vilhunen and J. Waldvogel Finnish Measurement Systems Ltd WOULD YOU LIKE TO MAKE MILLIONS
More informationCharacterization of crude:
Crude Oil Properties Characterization of crude: Crude of petroleum is very complex except for the lowboiling components, no attempt is made by the refiner to analyze for the pure components that contained
More informationNew Residue Up-grading Complex at European Refinery Achieves Euro 5 Specifications
New Residue Up-grading Complex at European Refinery Achieves Euro 5 Specifications Presented by: Gert Meijburg Technical Manager - Criterion Co-author: John Baric - Licensing Technology Manager - Shell
More informationStrategies for Maximizing FCC Light Cycle Oil
Paste Logo Here Strategies for Maximizing FCC Light Cycle Oil Ann Benoit, Technical Service Representative Refcomm, March 4-8, 2015 LCO and Bottoms Selectivity 90 Bottoms wt% 24 LCO wt% Hi Z/M Low Z/M
More informationOPPORTUNITY CRUDES: TO PROCESS OR NOT TO PROCESS?
OPPORTUNITY CRUDES: TO PROCESS OR NOT TO PROCESS? Claire Weber Serena Yeung 1 Oct. 27, 2011 COQA Meeting Doubletree by Hilton Hotel Tulsa, Oklahoma HYDROCARBON PUBLISHING COMPANY Translating Knowledge
More informationReport. Refining Report. heat removal, lower crude preheat temperature,
Delayed coker FCC feed hydrotreater FCCU Crude unit Hydrotreater Hydrotreater P r o c e s s i n g Better fractionation hikes yields, hydrotreater run lengths Scott Golden Process Consulting Services Houston
More informationSTUDIES ON FUSHUN SHALE OIL FURFURAL REFINING
Oil Shale, 2011, Vol. 28, No. 3, pp. 372 379 ISSN 0208-189X doi: 10.3176/oil.2011.3.02 2011 Estonian Academy Publishers STUDIES ON FUSHUN SHALE OIL FURFURAL REFINING G. X. LI, D. Y. HAN *, Z. B. CAO, M.
More informationCONTENTS 1 INTRODUCTION SUMMARY 2-1 TECHNICAL ASPECTS 2-1 ECONOMIC ASPECTS 2-2
CONTENTS GLOSSARY xxiii 1 INTRODUCTION 1-1 2 SUMMARY 2-1 TECHNICAL ASPECTS 2-1 ECONOMIC ASPECTS 2-2 3 INDUSTRY STATUS 3-1 TRENDS IN TRANSPORTATION FUEL DEMAND 3-3 TRENDS IN ENVIRONMENTAL REGULATION 3-3
More informationGTC TECHNOLOGY WHITE PAPER
GTC TECHNOLOGY WHITE PAPER Refining/Petrochemical Integration FCC Gasoline to Petrochemicals Refining/Petrochemical Integration - FCC Gasoline to Petrochemicals Introduction The global trend in motor fuel
More informationCorrelating TBP to Simulated Distillations. COQA Long Beach, CA
Correlating TBP to Simulated Distillations COQA Long Beach, CA 2017-10-05 Maxxam Analytics Overview Maxxam Analytics A Bureau Veritas Group Company 69,000 1,400 3 Maxxam Analytics Part of the Bureau Veritas
More informationR&D on New, Low-Temperature, Light Naphtha Isomerization Catalyst and Process
2000M1.1.2 R&D on New, Low-Temperature, Light Naphtha Isomerization Catalyst and Process (Low-temperature isomerization catalyst technology group) Takao Kimura, Masahiko Dota, Kazuhiko Hagiwara, Nobuyasu
More informationNational Oil Corporation Libyan Petroleum Institute. Crude oil assay Sarir crude oil
National Oil Corporation Libyan Petroleum Institute Crude oil assay Sarir crude oil Work Order No. LPI- 00344/10/IL02/2008 Client: National Oil Corporation Date of Issue: Dec., 2008 Prepared by: Industrial
More informationImpact of Processing Heavy Coker Gas Oils in Hydrocracking Units AM Annual Meeting March 21-23, 2010 Sheraton and Wyndham Phoenix, AZ
Annual Meeting March 21-23, 2010 Sheraton and Wyndham Phoenix, AZ Impact of Processing Heavy Coker Gas Oils in Hydrocracking Units Presented By: Harjeet Virdi Hydrocracking Technololgy manager Chevron
More informationThe Role of the Merox Process in the Era of Ultra Low Sulfur Transportation Fuels. 5 th EMEA Catalyst Technology Conference 3 & 4 March 2004
The Role of the Merox Process in the Era of Ultra Low Sulfur Transportation Fuels 5 th EMEA Catalyst Technology Conference 3 & 4 March 2004 Dennis Sullivan UOP LLC The specifications for transportation
More informationUnit 1. Naphtha Catalytic Reforming. Assistant lecturers Belinskaya Nataliya Sergeevna Kirgina Maria Vladimirovna
Unit 1. Naphtha Catalytic Reforming Assistant lecturers Belinskaya Nataliya Sergeevna Kirgina Maria Vladimirovna Introduction Catalytic reforming of heavy naphtha and isomerization of light naphtha constitute
More informationPILOT PLANT DESIGN, INSTALLATION & OPERATION Training Duration 5 days
Training Title PILOT PLANT DESIGN, INSTALLATION & OPERATION Training Duration 5 days Training Date Pilot Plant Design, Installation & Operation 5 21 25 Sep $3,750 Dubai, UAE In any of the 5 star hotels.
More informationTechnipFMC RFCC Technology converts bunker fuels into high value products for African refiners
TechnipFMC RFCC Technology converts bunker fuels into high value products for African refiners Eusebius Gbordzoe, Harvey McQuiston and Steve Gim ARA Week March 13 2017 TechnipFMC Process Technology What
More informationREBCO (RUSSIAN EXPORT BLEND CRUDE OIL) SPECIFICATION GOST
REBCO (RUSSIAN EXPORT BLEND CRUDE OIL) SPECIFICATION GOST 51858-2002 Characteristics Units Result Test Method Density (Specific Gravity) @ 20 C g /sm 3 0.870 ASTM D5002 Sulphur Content wt.% 1.8 ASTM D4294
More informationModernizing a Vintage Cat Cracker. Don Leigh HFC Rahul Pillai KBR Steve Tragesser KBR
Modernizing a Vintage Cat Cracker Don Leigh HFC Rahul Pillai KBR Steve Tragesser KBR El Dorado Refinery Refinery located in El Dorado, Kansas is one of the largest refineries in the Plain States and Rocky
More informationUOP Unicracking TM Process Innovations in Hydrocracking Technology
Kevin Whitehead UOP Unicracking TM Process Innovations in Hydrocracking Technology 15 February 2016 Egypt Downstream Summit & Exhibition 2016 Cairo 2016 UOP LLC. A Honeywell Company All rights reserved.
More informationFCC UNIT FEEDSTOCK FLEXIBILITY IN MOL S DANUBE REFINERY
FCC UNIT FEEDSTOCK FLEXIBILITY IN MOL S DANUBE REFINERY Tamás Kasza PhD Head of Technology Development Tamás Németh Process Technology MOL 04.10.2017 Budapest - RefComm AGENDA 1 INTRUDUCING DANUBE REFINERY
More informationGrowing the World s Fuels
Growing the World s Fuels May, 2013 Converting algae derived Biocrude into high quality Diesel Neil Osterwalder, Dan Sajkowski, Ben Saydah Overview Background Algae production Bio-crude production Bio-crude
More informationConversion Processes 1. THERMAL PROCESSES 2. CATALYTIC PROCESSES
Conversion Processes 1. THERMAL PROCESSES 2. CATALYTIC PROCESSES 1 Physical and chemical processes Physical Thermal Chemical Catalytic Distillation Solvent extraction Propane deasphalting Solvent dewaxing
More informationNational Oil Corporation Libyan Petroleum Institute. Crude Oil Assay Messla Crude Oil
National Oil Corporation Libyan Petroleum Institute Crude Oil Assay Messla Crude Oil Work Order No. LPI- 00344/08/IL02/2008 Client: National Oil Corporation Date of Issue: Nov., 2008 Prepared by: Industrial
More informationFCC Gasoline Treating Using Catalytic Distillation. Texas Technology Showcase March 2003, Houston, Texas. Dr. Mitchell E. Loescher
F Gasoline Treating Using atalytic Distillation Texas Technology Showcase March 2003, Houston, Texas Dr. Mitchell E. Loescher Gasoline of the Future Lead is out Olefins reduced Aromatics reduced Benzene
More informationHow. clean is your. fuel?
How clean is your fuel? Maurice Korpelshoek and Kerry Rock, CDTECH, USA, explain how to produce and improve clean fuels with the latest technologies. Since the early 1990s, refiners worldwide have made
More informationLecture 3: Petroleum Refining Overview
Lecture 3: Petroleum Refining Overview In this lecture, we present a brief overview of the petroleum refining, a prominent process technology in process engineering. 3.1 Crude oil Crude oil is a multicomponent
More informationHydrocracking of atmospheric distillable residue of Mongolian oil
Hydrocracking of atmospheric distillable residue of Mongolian oil Ts.Tugsuu 1, Sugimoto Yoshikazu 2, B.Enkhsaruul 1, D.Monkhoobor 1 1 School of Chemistry and Chemical Engineering, NUM, PO Box-46/574, Ulaanbaatar
More informationRefinery / Petrochemical. Integration. Gildas Rolland
Refinery / Petrochemical Integration Gildas Rolland 1 Global Middle Eastern Market 2 nd ~30% 10ppm Growing market for global Refined Product Demand +1.6% AAGR 2014-2035 of worldwide refining capacity expansion
More informationRefining/Petrochemical Integration-A New Paradigm Joseph C. Gentry, Director - Global Licensing Engineered to Innovate
Refining/Petrochemical Integration-A New Paradigm Introduction The global trend in motor fuel consumption favors diesel over gasoline. There is a simultaneous increase in demand for various petrochemicals
More informationRecycle and Catalytic Strategies for Maximum FCC Light Cycle Oil Operations
Recycle and Catalytic Strategies for Maximum FCC Light Cycle Oil Operations Ruizhong Hu, Manager of Research and Technical Support Hongbo Ma, Research Engineer Larry Langan, Research Engineer Wu-Cheng
More informationUnderstanding Cloud Point and Hydrotreating Relationships
Understanding Cloud Point and Hydrotreating Relationships Brian Watkins Manager, Hydrotreating Pilot Plant & Technical Service Engineer Meredith Lansdown Technical Service Engineer Advanced Refining Technologies
More informationCommercial Demonstration Case Study of a Novel Partial Upgrading Technology using Athabasca Bitumen
GPS18-137 Commercial Demonstration Case Study of a Novel Partial Upgrading Technology using Athabasca Bitumen Edwin J. Veith, Clementina Sosa and Dave Lamontagne, Fractal Systems Inc. This paper has been
More informationConversion of Peanut Oil into Jet and Diesel Fuels. Panama City, Florida 22 July 2016 Edward N. Coppola
Conversion of Peanut Oil into Jet and Diesel Fuels Panama City, Florida 22 July 2016 Edward N. Coppola SOLVING PROBLEMS OF GLOBAL IMPORTANCE About ARA, Inc. Founded 1979, Albuquerque, New Mexico 1,086
More informationBitumen to Finished Products
Bitumen to Finished Products Presented by: Gerald W. Bruce Jacobs Canada Inc. Canadian Heavy Oil Association Technical Luncheon Calgary, Nov 9, 2005 Overview Why all the interest? Value chain Adding value
More informationStudying effects of hydrotreatment on PAC compositions in refinery streams using GC GC-FID/SCD and GC GC-ToFMS. Asger B.
Studying effects of hydrotreatment on PAC compositions in refinery streams using GC GC-FID/SCD and GC GC-ToFMS Asger B. Hansen, HTAS Presentation outline Petroleum refining Refinery streams Hydrotreatment
More informationBottom of Barrel Processing. Chapters 5 & 8
Bottom of Barrel Processing Chapters 5 & 8 Gases Gas Sat Gas Plant Polymerization LPG Sulfur Plant Sulfur Alkyl Feed Alkylation Butanes Fuel Gas LPG Gas Separation & Stabilizer Light Naphtha Heavy Naphtha
More informationCeiba Crude (31.44 API, Sul WT%)
Ceiba Crude (31.44 API, 0.398 Sul WT%) Crude Name: Ceiba Crude API Gravity API 31.44 Component Wt % Vol % Crude ID: CEIBA2015 Density @15 deg C KG/L 0.8679 C2 Minus 0.004 0.01 Country: Equatorial Guinea
More informationUPGRADER FOR HEAVY, EXTRA-HEAVY CRUDE/BITUMEN AND RESIDUAL FRACTIONS
UPGRADER FOR HEAVY, EXTRA-HEAVY CRUDE/BITUMEN AND RESIDUAL FRACTIONS TABLE OF CONTENTS Section A Refiners General Introduction face tremendous and Market Overview pressures to maintain profits, whil e
More informationSelected Answers to the 2010 NPRA Q&A Hydroprocessing Questions
Selected Answers to the 2010 NPRA Q&A Hydroprocessing Questions By Geri D'Angelo, Technical Service Engineer,, LLC Chicago, IL Question # 10 Brian Watkins What are refiners' experience with respect to
More informationRefining/Petrochemical Integration-A New Paradigm
Refining/Petrochemical Integration-A New Paradigm Introduction The global trend in motor fuel consumption favors diesel over gasoline. There is a simultaneous increase in demand for various petrochemicals
More informationAlkylation & Polymerization Chapter 11
Alkylation & Polymerization Chapter 11 Petroleum Refinery Schematic Gasses Polymerization Sulfur Plant Sulfur Gas Sat Gas Plant Alkyl Feed Butanes LPG Fuel Gas Alkylation LPG Gas Separation & Stabilizer
More informationMaximize Yields of High Quality Diesel
Maximize Yields of High Quality Diesel Greg Rosinski Technical Service Engineer Brian Watkins Manager Hydrotreating Pilot Plant, Technical Service Engineer Charles Olsen Director, Distillate R&D and Technical
More informationAlkyClean Solid Acid Alkylation
Development of a Solid Acid Catalyst Alkylation Process AlkyClean Solid Acid Alkylation October 6, 2006-1 - AlkyClean solid acid alkylation Presentation Outline Introduction Process Development Demonstration
More informationExceed Your Hydrocracker Potential Using The Latest Generation Flexible Naphtha/Middle Distillate Catalysts
Exceed Your Hydrocracker Potential Using The Latest Generation Flexible Naphtha/Middle Distillate Catalysts Criterion Catalysts & Technologies/Zeolyst International Prepared by: Ward Koester on March 2001
More informationDiesel hydroprocessing
WWW.TOPSOE.COM Diesel hydroprocessing Optimizing your diesel production 32 Optimizing your diesel production As an increasing number of countries move towards requirements for low and ultra-low sulfur
More informationHOW OIL REFINERIES WORK
HOW OIL REFINERIES WORK In order to model oil refineries for model railroads some research was conducted into how they operate and what products a refinery produces. Presented below is a basic survey on
More informationAbstract Process Economics Program Report 246 NEAR ZERO SULFUR DIESEL FUEL (November 2002)
Abstract Process Economics Program Report 246 NEAR ZERO SULFUR DIESEL FUEL (November 2002) Desulfurization of diesel fuel is growing worldwide into a process critical to petroleum refinery profitability.
More informationQuenching Our Thirst for Clean Fuels
Jim Rekoske VP & Chief Technology Officer Honeywell UOP Quenching Our Thirst for Clean Fuels 22 April 2016 Petrofed Smart Refineries New Delhi, India UOP 7200-0 2016 UOP LLC. A Honeywell Company All rights
More informationThe Advantage of Real Atmospheric Distillation using D7345 Test Method. Presented by Jonathan Cole, PAC
The Advantage of Real Atmospheric Distillation using D7345 Test Method Presented by Jonathan Cole, PAC Distillation - a Critical Measurement Crude feedstock has a complex mixture of hydrocarbons Separate
More informationRefining/Petrochemical Integration A New Paradigm. Anil Khatri, GTC Technology Coking and CatCracking Conference New Delhi - October 2013
Refining/Petrochemical Integration A New Paradigm Anil Khatri, GTC Technology Coking and CatCracking Conference New Delhi - October 2013 Presentation Themes Present integration schemes focus on propylene,
More informationSupply of Services for Detailed OEB Crude Assay Analysis
Tender Number [9900009229] Supply of Services for Detailed OEB Crude Assay Analysis SCOPE OF WORK SCOPE OF WORK 1. Introduction Orpic is the brand name for Oman Oil Refineries and Petroleum Industries
More informationConverting 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 Overview Introduction
More informationDIESEL. Custom Catalyst Systems for Higher Yields of Diesel. Brian Watkins Manager, Hydrotreating Pilot Plant and Technical Service Engineer
DIESEL Custom Catalyst Systems for Higher Yields of Diesel Brian Watkins Manager, Hydrotreating Pilot Plant and Technical Service Engineer Charles Olsen Director, Distillate R&D and Technical Service Advanced
More informationTechnology for Producing Clean Diesel Utilizing Moderate Pressure Hydrocracking With Hydroisomerization
Technology for Producing Clean Diesel Utilizing Moderate Pressure Hydrocracking With Hydroisomerization XIII Refining Technology Forum IMP-Pemex Pemex Refinacion Mexico City, Mexico November 14, 2007 J.
More informationTechnip Stone & Webster Process Technology Offering in Refining
Technip Stone & Webster Process Technology Offering in Refining High Severity Fluidized Catalytic Cracking (HS-FCC ): From concept to commercialization Alexander MALLER and Eusebius GBORDZOE Technip Stone
More informationThe Role of a New FCC Gasoline Three-Cut Splitter in Transformation of Crude Oil Hydrocarbons in CRC
8 The Role of a New FCC Gasoline Three-Cut Splitter in Transformation of Crude Oil Hydrocarbons in CRC Hugo Kittel, Ph.D., Strategy and Long Term Technical Development Manager tel. +0 7 80, e-mail hugo.kittel@crc.cz
More informationPreface... xii. 1. Refinery Distillation... 1
Preface... xii Chapter Breakdown... xiii 1. Refinery Distillation... 1 Process Variables... 2 Process Design of a Crude Distillation Tower... 5 Characterization of Unit Fractionation... 11 General Properties
More informationengineering technology for the future
GENOIL HYDROCONVERSION UPGRADER (GHU ) High Sulphur Heavy Crude and VTB / ATB Residue Upgrading engineering technology for the future TABLE OF CONTENTS engine ering te chnolog gy for th he future Section
More informationHOW OIL REFINERIES WORK
HOW OIL REFINERIES WORK In order to model oil refineries for model railroads some research was conducted into how they operate and what products a refinery produces. Presented below is a basic survey on
More informationFig:1.1[15] Fig.1.2 Distribution of world energy resources. (From World Energy Outlook 2005, International Energy Agency.)[16,17]
Introduction :Composition of petroleum,laboratory tests,refinery feedstocks and products Fig:1.1[15] Fig.1.2 Distribution of world energy resources. (From World Energy Outlook 2005, International Energy
More informationSpecifications Of Straight Run Naphtha for Exportation
Specifications Of Straight Run Naphtha for Exportation ASTM Specific Gravity @ 60/60 F 1298 160 0.690-0.730 Colour VISUAL Colourless R.V.P @ 100 F kg/cm2 max 323 69 0.07 Sulphur, Total %mass max 1266 107
More informationUOP/EMRE Alliance for High Quality Lube and Diesel Production Technology
UOP/EMRE Alliance for High Quality Lube and Diesel Production Technology ExxonMobil Research and Engineering Company Girish Chitnis, Tim Hilbert, and Tim Davis Research and Engineering International Conference
More informationUPGRADER FOR HEAVY, EXTRA-HEAVY CRUDE/BITUMEN AND RESIDUAL FRACTIONS
UPGRADER FOR HEAVY, EXTRA-HEAVY CRUDE/BITUMEN AND RESIDUAL FRACTIONS HYDROGEN ADDITION UPGRADER FOR HEAVY AND EXTRA-HEAVY CRUDE/BITUMEN GenOil has a hydroconversion process that is the most cost efficient
More informationAsphaltene Precipitation in Domestic Sweet. Ron Fisher BP, Refining and Logistics Technology June 11, 2015
Asphaltene Precipitation in Domestic Sweet Ron Fisher BP, Refining and Logistics Technology June 11, 2015 Overview Precipitated asphaltenes can cause storage tank and heat exchanger fouling, desalter upsets,
More informationCatalytic Reforming for Aromatics Production. Topsoe Catalysis Forum Munkerupgaard, Denmark August 27 28, 2015 Greg Marshall GAM Engineering LLC 1
Catalytic Reforming for Aromatics Production Topsoe Catalysis Forum Munkerupgaard, Denmark August 27 28, 2015 Greg Marshall GAM Engineering LLC GAM Engineering LLC 1 REFINERY CONFIURATION LPG NAPHTHA HYDROTREATING
More information