Pore-Scale Imaging and Analysis of Oil Shale

Slides:



Advertisements
Similar presentations
Oil and Gas Deposits Fossil Fuels: Reference: Pages
Advertisements

The influence of wettability and carbon dioxide injection on hydrocarbon recovery Saif Al Sayari Martin J. Blunt.
Experimental Investigation and Mathematical Modeling of Cold-Cap Behavior in HLW Melter D. Pierce, J. Chun, P. Hrma, J. Rice, R. Pokorny, M. Schweiger.
Qatar Carbonates and Carbon Storage Research Centre 1 Dynamic Imaging of Reaction at Reservoir Conditions, Considering the Influence of Chemical Heterogeneity.
Pore-Scale Analysis of WAG Flooding V. Sander Suicmez Dr. Mohammad Piri Prof. Martin J. Blunt 5 Jan 2005 Centre for Petroleum Studies Department of Earth.
Branko Bijeljic, Ali Raeini, Peyman Mostaghimi and Martin Blunt What Determines Transport Behaviour in Different Porous Media? Dept. of Earth Science and.
Zaki Al Nahari, Branko Bijeljic, Martin Blunt
Geological and Petrophysical Analysis Of Reservoir Cores
Pore-scale modelling of carbonates 1 Hiroshi Okabe Petroleum Engineering and Rock Mechanics Research Group Department of Earth Science and Engineering.
Multipoint Statistics to Generate Geologically Realistic Networks 1 Hiroshi Okabe supervised by Prof. Martin J Blunt Petroleum Engineering and Rock Mechanics.
Tim Armitage.  Shale Gas Reservoir's  The problems with Shale Reservoirs  What is needed to Create a usable model  Possible solutions to Porosity.
Oil and Gas n Describe and explain the origin of oil and natural gas and migration from source-rock to reservoir-rock under a cap rock. Define and recognise.
Hydrocarbon migration
PTS research activities related to COST FP 1005 Simulation of micro structure mechanics in dynamic fibre networks Timo Kuntzsch, Jan Matheas, Sven Altmann.
“PRODUCTION” MIDDLE EAST TECHNICAL UNIVERSITY
Imperial College Consortium on Pore-Scale Modelling Annual Review 11 th January 2013 Martin Blunt Department of Earth Science and Engineering Imperial.
Peyman Mostaghimi, Prof. Martin Blunt, Dr. Branko Bijeljic 16 January 2009, Imperial College Consortium on Pore-Scale Modelling The level set method and.
Finite-Element-Based Characterisation of Pore- scale Geometry and its Impact on Fluid Flow Lateef Akanji Supervisors Prof. Martin Blunt Prof. Stephan Matthai.
Peyman Mostaghimi, Martin Blunt, Branko Bijeljic 11 th January 2010, Pore-scale project meeting Direct Numerical Simulation of Transport Phenomena on Pore-space.
Presenter: Ahmed Ahed Al-Ratrout Supervisors: Prof. Martin J. Blunt
Vivek Muralidharan Simulation and imaging experiments of fluid flow through a fracture surface: a new perspective.
Texas A&M UniversityFeb, 2004 Application of X-Ray CT to Investigate Effect of Rock Heterogeneity and Injection Rates During CO 2 Flood Process Deepak.
Do Now Give an example for each of the following energy conversions. 1.Electrical → Thermal 2.Chemical → Mechanical 3.Electrical → Mechanical 4.Mechanical.
3D Images of residual oil in an Ottawa sand Congjiao Xie, Saif Ai-Sayari and Martin Blunt Earth Science and Engineering, Imperial College London.
The Effect of Wettability on Relative Permeability, Capillary Pressure, Electrical Resistivity and NMR Saif AL-Sayari Prof. Martin Blunt.
Pore-Scale Analysis of WAG & Development of a New Empirical Model
Imperial College, PETROLEUM ENGINEERING AND ROCK MECHANICS GROUP 10 th January 2003 PETROLEUM ENGINEERING AND ROCK MECHANICS GROUP Pore Scale Modeling.
WEEK20 PHYSICAL SCIENCE VOCABULARY. 1) THERMAL ENERGY Total amount of energy in all of the particles contained in a sample of matter.
Statistical analysis of pore space geometry Stefano Favretto Supervisor : Prof. Martin Blunt Petroleum Engineering and Rock Mechanics Research Group Department.
New Directions and the Importance of Geology Susan Smith Nash, Ph.D. AAPG.
Sedimentology & Stratigraphy:
Annual Review 13th January 2014
Pore-Scale Analysis of Oil Shale: Planned Research
Advanced Analytical Chemistry – CHM 6157® Y. CAIFlorida International University Updated on 9/28/2006Chapter 6Electron Spectroscopy Chapter 6 Electron.
Fossil Fuels Chapter 19.
Microwave Power and Electromagnetic Energy Microwave Heating of Metal.
Prediction of wettability variation and its impact on flow using pore- to reservoir-scale simulations Matthew Jackson, Per Valvatne and Martin Blunt Centre.
Design Analysis of Furnace Of A Steam Generator P M V Subbarao Professor Mechanical Engineering Department Perfection of Primary Cause for All that Continues…..
DEVELOPMENT OF A FLUIDIZED BED COAL GASIFICATION TECHNOLOGY
1 Carbon Capture and Storage Martin Blunt Department of Earth Science and Engineering Imperial College London.
Dr. Branko Bijeljic Dr. Ann Muggeridge Prof. Martin Blunt Diffusion and Dispersion in Networks Dept. of Earth Science and Engineering, Imperial College,
4 th International Conference and Exhibition on Materials Science & Engineering Florida, Orlando, USA, September 14-16, 2015 A. K. Gujba, L. Hackel, D.
By Dr. Estee Yong Siek Ting
1 Pore-Scale Simulation of NMR Response in Porous Media Olumide Talabi Supervisor: Prof Martin Blunt Contributors: Saif AlSayari, Stefan Iglauer, Saleh.
11 Imperial College Consortium on Pore-Scale Modelling Martin Blunt Department of Earth Science and Engineering.
Modelling the damage to carbon fibre composites due to a lightning strike Please use the dd month yyyy format for the date for example 11 January 2008.
Heat and States of Matter
Guray Yildiz a*, Tom Lathouwers a, Hilal Ezgi Toraman b, Kevin M. van Geem b, Frederik Ronsse a, Ruben van Duren c, Sascha R. A. Kersten d, Wolter Prins.
The Potential of Oil Shale Stephen Mut, CEO Shell Unconventional Resources Energy ASPO’s Denver World Oil Conference Beyond Oil: Intelligent Response to.
Imperial College Consortium on Pore-Scale Modelling Annual Review 12 th January 2015 Martin Blunt Department of Earth Science and Engineering Imperial.
Copyright © 2014 All rights reserved, Government of Newfoundland and Labrador Earth Systems 3209 Unit: 5 Earth’s Resources Reference: Chapters 21; Appendix.
Research Institute of Petroleum Industry
What Determines Transport Behaviour in Different Porous Media?
Annual Review 11th January 2015
SHALE OIL EXTRACTION AND CO2 SEQUESTRATION BY A NOVEL METHOD OF HOT GAS INJECTION Michael Youtsos – Energy Group Cambridge University Engineering Department.
Direct simulation of multiphase flow on pore-space images
Fast Pyrolysis of Biomass using Concentrated Solar Radiation Emily Beagle Graduate Mentor: Daniel Mosiman Faculty Mentor: Dr. Yuan Zheng University of.
Investigation of the Performance of Different Types of Zirconium Microstructures under Extreme Irradiation Conditions E.M. Acosta, O. El-Atwani Center.
Characterization of torrefied sugarcane bagasse for gasification in a downdraft biomass gasifier system. A I Anukam, S N Mamphweli, P Reddy, E L Meyer.
Chapter 1.  In order to have hydrocarbon to accumulate we need to have sediment basin, High level of organic materials, and temperature/pressure.  Source.
In situ Measurements of Contact Angle Distribution From Multiphase Micro-CT Images Presenter: Ahmed Ahed Al-Ratrout Supervisors: Prof. Martin J. Blunt.
Modeling Light Gas and Tar Yields from Pyrolysis of Green River Oil Shale Demineralized Kerogen Using the CPD Model Ronald J. Pugmire Departments of Chemical.
Fig. 16-2, p. 357 Oil and natural gas Floating oil drilling platform Oil storage Coal Contour strip mining Oil drilling platform on legs Geothermal energy.
Ongoing and Future Work Computed Tomography (CT) Scanning of Cores CT scanning of rock cores enable non-destructive fine scale characterization of rock.
Hasan Nourdeen Martin Blunt 10 Jan 2017
Introduction Results Objectives Catalyst Synthesis Results Conclusions
PETROLEUM ENGINEERING AND ROCK MECHANICS GROUP
Source Rock BY: ABDELRAHMAN AHMED ALI ABDELRAHMAN UNDER SUPERVISOR OF:
RESEARCH IN EARTH SCIENCE & ENGINEERING
Chapter 11 Resources & Energy.
Presentation transcript:

Pore-Scale Imaging and Analysis of Oil Shale Tarik Saif Supervisors: Prof. Martin Blunt & Dr Branko Bijeljic 12 January 2015

Unconventionals: Oil Shale

What is Oil Shale? The term Oil Shale is a misnomer because it does not contain oil, and is not always made of shale. Instead, rock is actually marlstone (mixture of clay and calcium carbonate), and the main organic constituent is kerogen. It is a potential petroleum source rock that would have generated hydrocarbons if it had been subjected to geological burial at the requisite temperatures and pressures for a sufficient time.

Where is Oil Shale found? Russia Canada Estonia UK France Italy United States Israel China Morocco Jordan Egypt Zaire Brazil Australia 2.8-3.3 Trillion Barrels of Shale Oil Worldwide 4

Oil Shale Pyrolysis Several complex physical changes occur during the thermal conversion of kerogen in oil shale to produce hydrocarbons. It is (1) the formation of oil and gas resulting from kerogen decomposition, (2) the creation of pore structure in the shale, (3) the fluid flow through the pore channels and the ultimate recovery which are of interest in this research. The pore structure and the connectivity of the pore space are important characteristics which determine fluid flow. A study investigating the nature of the pores and subsequent permeability is essential.

Previous Literature X-ray micro tomography has been applied to describe thermal cracking of Chinese Fushun oil shale at different temperatures for sample sizes of 7 mm (Kang et al., 2011). A study on the characterisation of oil shale using X-ray tomography before and after pyrolysis has also been presented in recent literature (Tiwari et al., 2013, Mustafaoglu, 2010). However, the exact mechanism of kerogen decomposition at the pore-scale and the flow behaviour of the produced oil and gas are unknown. Therefore, with improved imaging techniques and advanced modelling methods this research is intended to make a valuable contribution to the oil shale industry. Before Pyrolysis After Pyrolysis (500°C, 100°C/min, 24 hours) Source: Tiwari et al. (2012)

Research Aims & Objectives The aim of this research is to describe how oil shale reacts at a given temperature where kerogen decomposes to produce oil and gas, and to understand the dynamics of the subsequent two-phase flow through the pore space created. As well as temperature (300°C, 400°C, 500°C, 600°C), heating rate (1, 10, 100°C/min), this study will investigate the effects of stress state/lithostatic load. The goal is to have a model based on experimental observation of the physico-chemical mechanisms that govern the process, which will be able to advise on how the recovery can be optimised.   Emphasis on understanding changes in pore structure and fluid distribution.

Research Aims & Objectives

Primary sample – Kimmeridge Oil Shale Kimmeridge oil shale samples collected from the cliffs in Dorset This oil shale is from the Upper Jurassic and is the primary sample for this study The Kimmeridge Clay Formation contains shales with some of the highest total organic carbon (TOC) contents 20%+ Bulk density ~ 1.7g/cm3

Kimmerdige Oil shale – mineral analysis Chemical Formula Mineral % Quartz SiO2 10.4 Pyrite   FeS2 1.3 Oligoclase Na0.8Ca0.2Al1.2Si2.8O8 14.2 Microcline KAlSi3O8 3.8 Illite KAl2[AlSi3O8](OH)2 6.2 Calcite CaCO3 22.8 Dolomite CaMg(CO3)2 23.4 Total Organic Carbon (TOC) 24.2

Micro-CT: before and after pyrolisis Pixel size of 1µm Exposure time: 10 seconds 3200 projections in 11 hours Sample size: 6mm Xradia micro-CT scanner Image size: 10003 voxels After Pyrolysis (500°C, 10°C/min, 3 hours) Before Pyrolysis

FIB – Focused Ion Beam Helios NanoLab 600 Uses Ga+ ion beam to mill a small amount of material from the surface The generated secondary electrons (or ions) are collected to form an image of the surface of the sample Sample size: 6mm

Nano-CT: dry image Photon Energy: Monochromatic beam, 11.8 keV Voxel size: 60 nm Exposure time: 15 s per projection Total tomography time: 3 to 4 hours (800 projections)

Future work: Imaging

Heating Oil Shale - Furnace Furnace has capability to reach ~ 1400°C. Heating rates of 1, 10 and 100°C/min to be tested. 10mm holes on either side of the furnace to allow penetration of X-rays for imaging. Two ceramic end caps placed on either end for a closed system. Ex-situ experiments to be performed initially. In-situ experiments to be performed at a later stage.

Future work: Modelling Modelling the kerogen decomposition to produce oil and gas and the flow of the fluids through the created pore structure using pore network modelling and also a Finite Volume method. The research questions to be answered include: Does the solid-fluid conversion occur at the rock matrix-kerogen interface, at the centre of the organic matter, or randomly? What is the percolation threshold point at which the pores become connected? What are the changes in fluid distribution as pyrolysis progresses? The network will be periodically updated by extracting it over selected times. Initially, the parameters studied will include pore size distribution, connectivity (topological), and the rate of fluid formation as a temperature dependence. 

Pore-Scale Imaging and Analysis of Oil Shale Thank You! Tarik M. A. Saif PhD Student (Petroleum Engineering) Earth Science and Engineering Department Imperial College London Email: t.saif13@imperial.ac.uk

References Aboulkas, A., & El Harfi, K. (2008). Study of the kinetics and mechanisms of thermal decomposition of Moroccan Tarfaya oil shale and its kerogen. Oil shale, 25(4), 426-443. Doan VL., (2011). Oil Shale Pyrolysis Laboratory & Technique. Oil Shale Symposium. Han X., Xiumin J., Lijun Y., Zhigang C., (2006). Change of pore structure of oil shale particles during combustion. Part 1. Evolution mechanism. Energy Fuels; 20, 2408-12. Kang Z., Yang D., Zhao Y., Hu Y., (2011). Thermal cracking and corresponding permeability of Fushun oil shale. Oil shale; 28, 273-83. Külaots, I., Goldfarb, JL., & Suuberg, EM., (2010). Characterization of Chinese, American and Estonian oil shale semicokes and their sorptive potential. Fuel, 89(11), 3300-3306. Lin CL., Miller JD., (2011). Pore scale analysis of Oil Shale/Sands pyrolysis. Prepared for the United States Department of Energy and the National Energy Technology Laboratory. Oil & Natural Gas Technology. Mustafaoglu O., (2010). Charactrization and pyrolysis of oil shale samples: An alternative energy option. LAP Lambert Academic Publishing. Nazzal, JM., (2002). Influence of heating rate on the pyrolysis of Jordan oil shale. Journal of analytical and applied pyrolysis, 62(2), 225-238. Tiwari, P., Deo, M., Lin, CL. & Miller, JD., (2012). Characterization of Core Pore Structure Before and After Pyrolysis using X-ray Micro CT. Fuel, 2013, 107, 547-554. Williams PT., Ahmad, N., (1999). Influence of process conditions on the pyrolysis of Pakistani oil shales. Fuel, 78(6), 653-662.