Heavy Oil and Bitumen Analytical. Understanding Their Capabilities

Similar documents
COQA Presentation Maxxam Analytics

Delayed Coking Process Design, Operations and Optimization. Canada Coking Conference October 22-26, 2012 Fort McMurray, Alberta

Comparative Analysis of Offshore and Onshore Nigeria Crude Oil

White Paper. Impact of Opportunity Crudes on Fouling in Preheat, distillation, and furnace systems

Initially, quality issues for investigation will not be limited and may include issues associated with:

Edwin J. Veith, Fractal Systems USA, Inc.; Michel Chornet, Fractal Systems, Inc. WHOC16-232

Heavy Oil Upgrading from mine to motor

Upgrading with a soft touch

CEEN 3144 Construction Materials. Asphalts. Francisco Aguíñiga Assistant Professor Civil Engineering Program Texas A&M University Kingsville

CCQTA Project Update for CCQTA/COQA joint meeting. San Francisco October 31, 2014

A New Approach to Simultaneously Enhancing Heavy Oil Recovery and Hindering Asphaltene Precipitation

SCOPE OF ACCREDITATION

Petroleum Refining. Environmental Guidelines for. Multilateral Investment Guarantee Agency. Industry Description and Practices. Waste Characteristics

Comparison of the Corrosivity of Dilbit and Conventional Crude

Oil Based Mud Filtrate Effect on Downhole Samples Obtained for Crude Assay Testing. Magdy Samir Principal reservoir Engineer Aberdeen

AFPM 2018 Operations & Process Technology Summit

"The Key to Residue Upgrading" Advanced EUREKA Process

LABORATORY TURNAROUND TIMES AND CHARGES

Reforming is an upgrading process in which low octane gasoline is converted to high octane gasoline.

Metals in Crude Oil ICP (ASTM D5708B) vs. HDXRF

Crude Oil Quality Group (COQG)

The Effect of Ageing on Physical and Chemical Properties of Asphalt Cement

Corrosion Management Methods of High TAN Crude. Case study: (Fula Crude Oil-Sudan)

Chapter 2 Physicochemical Properties of Crude Oils

THE INFLUENCE OF NAPHTHENIC ACID AND SULFUR COMPOUND STRUCTURE ON GLOBAL CRUDE CORROSIVITY UNDER VACUUM DISTILLATION CONDITIONS

PERP Program Unconventional Heavy Oils New Report Alert

Bitumen Upgrader Residue Conversion to Incremental Synthetic Fuels Products

September 2010 API Recommended Practice

Laboratory Turnaround Times and Prices

bakerhughes.com/opportunitycrudes Profiting from Western Canada Opportunity Crudes

Addressing the Challenges Associated with Canadian Crudes

HEAVY OIL PRODUCTION ENHANCEMENT UNCONVENTIONAL HEAVY OIL PRODUCTION OPTIMIZATION

Heavy Oil Upgrading. Technology Today Spring 2010 D1M Author illustration; equipment in background is not operating.

Section 904. ASPHALTIC MATERIALS

Approach for a Subset of Petroleum Substances Prioritized during Categorization. Environment and Climate Change Canada Health Canada

Application Temperatures. Apply asphaltic materials within the temperature ranges shown in Table

Taravosh Jam Design & Engineering Co.

Chemistry of Petrochemical Processes

Feasibility of Partial Upgrading of Athabasca Bitumen. Jim Colyar, Technology Consultant Colyar Consultants October 2010

Study of the influence of asphaltenes on modeling of viscosity of Nigerian crude mixtures

Heavy oil and bitumen from

Thrust 2: Utilization of Petroleum Refinery Technology for Biofuel Production. Prof. Chunshan Song, Penn State Douglas C.

Bitumen Upgrader Residue Conversion to Incremental Synthetic Fuels Products

Corrosion Monitoring Solutions for Hydroprocessing Units

SUEZ helps refineries to save time, reduce energy consumption, emissions and waste by efficient decontamination

Filtration Applications for the Refining & Petrochemical Industries

Overview. Challenges in Opportunity Crude Processing 16 th April 2012

Simulating the Injection of Carbon Dioxide Gas and Impact of Asphaltene Precipitation on Permeability and Porosity the One Oil Reservoirs

Ralph Navarrete and George Duggan, Baker Hughes Inc., USA,

Introduction to Production and Gas Processing Facilities Core

The Case for Exporting Partially Upgraded Bitumen Offshore. By Jim Hutton MSc. P. Eng.

ENGINEERING STANDARD FOR PROCESS DESIGN OF CRUDE OIL ELECTROSTATIC DESALTERS ORIGINAL EDITION JULY 1995

SOLUTIONS FOR HEAVY OIL

Stability of fast pyrolysis bio-oils and upgraded products

Asphalt is found in natural deposits in different parts of the world or as a product of the distillation of crude petroleum.

Powered by TCPDF (

Crude Quality and Quantity Issues Kesavalu M. Bagawandoss, Ph.D., J.D., & Louis Ory.

Chapter-1 INTRODUCTION

Study the Effect of Using Microwave Radiation and H-Donors on Improving Heavy Oil

OPTI. October 2002 SHELL GLOBAL SOLUTIONS CANADA INC.

SOLUTIONS FOR HEAVY OIL

Corrosion Session Summary

Brownfield Projects. Equinox Engineering

Excellent Insulation and Cooling of Power Transformer Oil 25#&45# Brand Transformer Oil Specification

COQA - Salt Lake City, Utah 9 June 2011

Gasification...Meeting the Challenges of Oil Sands

MEASUREMENT AND MODELING METHODOLOGY FOR HEAVY OIL VAPOR PRESSURE. O. Castellanos-Díaz, W. Y. Svrcek, H. W. Yarranton, and M. A.

Schedule of Accreditation issued by United Kingdom Accreditation Service 2 Pine Trees, Chertsey Lane, Staines-upon-Thames, TW18 3HR, UK

WWT Two-Stage Sour Water Stripping

Final DRAFT API TECHNICAL REPORT. Carbon Content, Sampling, & Calculation

HEAVY CRUDE UPGRADING: AN OPTION FOR GASIFICATION

FAQ: Modeling Heavy Oils Using Aspen HYSYS

Multiphase flow simulators for heavy oil; Innovations to be expected. Norbert Hoyer February 2009

REAL-TIME PREDICTIVE ANALYTICS AND CORROSION MONITORING WITH PREDICT -RT

(12) Patent Application Publication (10) Pub. No.: US 2008/ A1

10/2/2013. Gas CHEMICAL PLANTS AMMONIA METHANOL UTILITIES TOWN GASS SUPPLIES ENERGY INTENSIVE INDUSTRIES. Power Generation

Construction Materials

Corrosion and Materials Selection for Bitumen with Heavy Naphthenic Acid in Canadian Oil Sands

The naphtha hydrotreater

Specifications For Manufactured Materials

COQA Update. June 10, 2010 Denver

Schedule of Accreditation issued by United Kingdom Accreditation Service 2 Pine Trees, Chertsey Lane, Staines-upon-Thames, TW18 3HR, UK

Investigation of Heat Exchanger Network Flexibility of Distillation Unit for Processing Different Types of Crude Oil

SPE DISTINGUISHED LECTURER SERIES SPE FOUNDATION

North West Sturgeon Refinery Project Overview Carbon Capture Through Innovative Commercial Structuring in the Canadian Oil Sands

Geochemical Characteristics of Oil Sand Tailings and Bitumen Upgrading By-Products, Alberta, Canada

An Investigation on Remediation of Transformer Oil Contaminated Soil by Chemical Oxidation Using Hydrogen Peroxide

BITUMEN 1 (ASPHALT CEMENT)

SEGREGATION 20 CRUDE QUALITY PROGRAM EAGLE FORD, BAKKEN, MIDLAND WTI

WASTE WATER TREATMENT REFINERIES

Chemistry of Fossil Fuels and Biofuels

Salt deposition in FCC gas concentration

GT-LPG Max SM. Maximizing LPG Recovery from Fuel Gas Using a Dividing Wall Column. Engineered to Innovate

FOULING MANAGEMENT IN CRUDE OIL PREHEAT TRAINS/DHP UNITS

CERTIFICATE OF ACCREDITATION

SPE Distinguished Lecturer Program

Micro Methods Laboratory Quality Assurance Manual

A Single Analyzer Solution for Refinery Flare Emissions Monitoring (40 CFR 60 Subpart Ja) Using Mass Spectrometry

Physical Properties and Process Conditions Affecting Hydrocarbon Measurement

Corrosion Issues Associated With Thermochemical Production Of Biofuels

Transcription:

Heavy Oil and Bitumen Analytical Methods: Understanding Their Capabilities and dlimitationsi i Project Review & Update /COQG Meeting Calgary, Alberta June 24 th, 2008 Project Manager: Bryan Fuhr, ARC (fuhr@arc.ab.ca)

Background Many petroleum methods were developed dfor light crudes and are not easily applied to heavy oils and bitumens Over the last 30 years experienced users have developed special handling techniques and modification for application to bitumen A considerable data base related to heavy oil methods has been collected in terms of reviews and round robins

Project Goal To document the capabilities and limitations it ti of heavy oil and bitumen methods to allow users to make informed ddecisions i on method selection Not to provide detailed method descriptions

Targeted Methods Sample Preparation Asphaltenes TAN Density Viscosity Chlorides Distillation Sulfur BS&W

Sample Preparation One of the most overlooked challenges in analytical chemistry Cleaning method of choice depends on the analysis method and nature of the sample Bitumens and emulsions are particularly difficult

Sample Preparation Most common methods are centrifugation and filtration; however, they often are not applicable to heavy oils Solvent extraction or distillation are more useful for heavy oil and bitumen All data should include a statement on the sample preparation used

Asphaltenes Bitumens and heavy oils contain high quantities of asphaltenes Asphaltenes may precipitate during recovery operations due to pressure drop, acids, CO 2 and condensate addition, i and incompatibilityibili The asphaltene fraction is a precursor of coke formation, and dthus a measure of upgrader feedstock quality

Asphaltenes Many ASTM, UOP and IP methods are available; however, the following guidelines apply: N-pentane or n-heptane precipitants 40 ml precipitant per g sample 2h contact time in the dark Samples dispersed in toluene (1:1) prior to n-pentane addition; samples refluxed in n-heptane

Total Acid Number TAN was originally developed to indicate the quality of petroleum products and used lubricating oils TAN is used as a measure of naphthenic acid corrosion potential of crudes, but presents challenges when applied to bitumen

Total Acid Number ASTM D664 was modified by to handle heavy oils using pre-dilution with toluene UOP 565, Procedures B and C, would require extensive modifications for application to heavy oils ASTM D974, colorimetric method, is not applicable to heavy oil

Density Density (or API gravity) is a major criterion in setting crude prices Conversion tables (ASTM D1250) are frequently used for converting densities to the 15 C reference temperature Bitumens typically have densities >1000 kg/m 3 (<10 API)

Density ASTM D4052, digital density meter, is fast and reliable for bitumen ASTM D70, pycnometer, is reliable and precise for bitumen, but is time-consuming ASTM D71, displacement method, is useful for small samples, but both it and the previous method may have surface tension issues ASTM D1298, hydrometer, may be applied to bitumen, but is tedious and requires large sample

Viscosity Viscosity of crude impacts viability of production techniques Pipelining requires crude to meet viscosity criteria; dilution is required for bitumens It is generally assumed that bitumen is Newtonian, but some instances of non- Newtonian behavior have been observed

Viscosity ASTM D445, kinematic capillary viscometer, may be used for bitumen. For >10,000 cst and for samples with water which may be non-newtonian, cone-andplate is more appropriate ASTM D3205, dynamic cone-and-plate viscometer, applicable for 10 3 to 10 10 P and non-newtonian behavior; commonly used for bitumen even though it was withdrawn in 2000

Chlorides Inorganic chlorides (water soluble) affect primary distillation towers; salt levels are used to optimize desalting units Organic chlorides (hydrocarbon soluble) historically i linked to corrosion in hydrotreating units Recent evidence to suggest that organic chlorides play a role in crude unit corrosion

Chlorides ASTM D6470, salt in crude, by dissolution in xylene and aqueous extraction; testing for halides by potentiometry, is applicable to most heavy petroleum products ASTM D4929, determines organic chloride in the naphtha fraction (sodium biphenyl reduction or oxidative combustion/microcoulometry); most heavy oils contain very little naphtha

Distillation Most basic and important separation process in refineries and also in the lab Distillation curves provide an important set of data in its own right, but distillation cuts also simplify compositional analysis

Distillation Vacuum Distillations (actual cuts obtained for further analysis) ASTM D2892 and D5236 are most commonly used for bitumens (up to 538 C and 15 theoretical plates) Spinning band (up to 450 C and 50 plates) Short path (up to 700 )

Distillation Simulated Distillations by GC (no cuts) to produce curves) ASTM D7169, most applicable to bitumen, provides sample recovery to 720 C ASTM D6352, for cuts with FBP<720 C ASTM D5307, for bitumens, provides sample recovery to 538 C ASTM D2887, applicable to cuts with FBP<538 C

Distillation Things to Watch out for with Vacuum Distillations of Bitumen Water causes bumping Flooding the column must watch Cracking thermal degradation may occur bt between 250-350 C 250350 C - fogging, drop in vapor temperature

Sulfur Bitumens and heavy oils can contain up to 5% S, much higher than light to medium crudes Sulfide, mercaptan, thiophenes are common, and speciation can be important to refiners with respect to potential for catalyst contamination and corrosion Removal of S is key to meet new ultra low specs of products

Sulfur ASTM D2622 and D4294, X-ray methods, are applicable to heavy oils, but are matrix dependent; matrix matching calibration standards to samples ASTM D1552, oxidative microcoulometry (LECO method), also applicable to heavy oils Generally LECO and X-ray data are equivalent, but certified standards d are required to reduce inter-lab lb biases

BS&W Measure of solids and free water in crude or emulsions Used as estimate of fluids composition in SAGD Spec test for crudes and dilbit for pipelines In determination i of net oil volumes in sales, taxation and custody transfers

BS&W ASTM D4007, centrifuge method is applicable to heavy oils, but emulsions may be problematic; accepted method in custody transfers For more accurate results, D4006 (distillation) or Syncrude modified Dean-Stark should be used

Future Areas of Investigation Carbon, hydrogen, nitrogen and oxygen Molecular weight Carbon residue Ah Ash Nickel and vanadium Flash point Pour point