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Technical Aspects of Oil Technical Aspects of Oil Shale Production and Shale Production and Processing Processing Milind D. Deo Milind D. Deo Professor, Chemical Engineering Professor, Chemical Engineering Institute for Clean and Secure Energy Institute for Clean and Secure Energy
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Page 1: Technical Aspects of Oil Shale Production and Processingrepository.icse.utah.edu/.../oil_shale_production_processing_milind... · Artificial Lift Kerogen Oil Hydrocarbon Gases Spent

Technical Aspects of Oil Technical Aspects of Oil

Shale Production and Shale Production and

ProcessingProcessing

Milind D. DeoMilind D. Deo

Professor, Chemical EngineeringProfessor, Chemical Engineering

Institute for Clean and Secure EnergyInstitute for Clean and Secure Energy

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Shale CompositionShale Composition

• Composition varies from deposit to deposit and even within deposit

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Energy ValuesEnergy Values

Crude Oil Crude Oil –– 45 MJ/kg45 MJ/kg–– Price $10/MMBTU (at $60/barrel)Price $10/MMBTU (at $60/barrel)

Coal Coal –– 2727--31 MJ/kg31 MJ/kg–– Price $1.5/MMBTUPrice $1.5/MMBTU

Natural Gas ~55 MJ/kgNatural Gas ~55 MJ/kg–– Price $6Price $6--10/MMBTU10/MMBTU

Shale oil ~ 42 MJ/kgShale oil ~ 42 MJ/kg

Shale ~ 4.3 Shale ~ 4.3 –– 8 MJ/kg8 MJ/kg

Value is added by making liquid hydrocarbonsValue is added by making liquid hydrocarbons

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EnergyEnergy

• Without any heat losses the ratio of energy out/energy in = 13• This is the absolute maximum that one can hope to achieve• Energy-in values for conventional oil/gas type operations have to be

added along with heat losses to compute more practical ratios which will be in the 3-6 range

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Production potentialProduction potential

OIL

•One ton of sandstone

•Porosity 20%

•Grain density = 2.65 g/cc

•Oil saturation 80%

•Oil quantity = 25 gallons/ton

OIL SAND

•One ton of oil sand

•Bitumen wt fraction (10%)

•Bulk density = 2.2 g/cc

•Oil quantity = 28 gallons/ton

OIL SHALE

•One ton of oil shale

•Organic content (9.5%)

•Shale density = 2.67 g/cc

•Complete conversion

•25 gallons/ton shale oil

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Shale Production PotentialShale Production PotentialAverage thickness = 550 feetAverage thickness = 550 feet

Density = 2.67 g/ccDensity = 2.67 g/cc

Average oil content = 30 gallons/tonAverage oil content = 30 gallons/ton

Barrel of Oil Equivalent/Acre = 1.3 millionBarrel of Oil Equivalent/Acre = 1.3 million

Shale

From T. Dammer

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Oil ShaleOil Shale

To produce 100,000 barrels of oil/dayTo produce 100,000 barrels of oil/day–– 140,000 tons of oil shale/day will have to be 140,000 tons of oil shale/day will have to be

processed, if surface production facilities are usedprocessed, if surface production facilities are used

–– Kennecott processes 500,000 tons of material/dayKennecott processes 500,000 tons of material/day

–– For a 1000 MW power plant, about 10,000 tons of For a 1000 MW power plant, about 10,000 tons of coal is required/daycoal is required/day

LargeLarge--scale operation scale operation –– operations at such operations at such scales existscales exist

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Processing OptionsProcessing Options

Mining Crushing Retorting

Fracturing RetortingProduct

Recovery

Refining

Liquid Fuels

By-Product

ATPGas combustion (Bureau, Petrosix)UnionToscoHydrogen AtmosphereKiviter Galoter

NaturalHydraulicExplosiveElectocarbonizationDrilling &Dewatering

CombustionHot gasesSteamGradual HeatingPyrolysis

In-Formation

Gas DriveArtificial Lift

Kerogen OilHydrocarbon Gases

Spent Shale

Thermal & Chemical TreatingHydrogenation

Mild-cat crackingHydrocracking

UtilizeDispose

Mine FillRevegetateDump

Underground Room & Pillar

Cut and FillBlock Carving

Open-Pit

Source: Strategic Significance of America’s Oil Shale resources, Vol II, 2004

Control on Operational Parameter

Ex-Situ

In-Situ

Not necessary?

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Ex-Situ Process Diagram

RetortCombustor

K + S

KU + S + CS + coke + char

CSP

CH4

S + others

CS: Combusted Shale

Direct or Indirect

KU: kerogen Unreacted

S: Feed Shale

P: Product

air

Depending on the kerogen conversion

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Direct and Indirect ProcessesDirect and Indirect Processes

From the U.S. Office of Technology Assessment Reports

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The Petrosix RetortThe Petrosix Retort

From the U.S. Office of Technology Assessment Reports

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Sample Products (based on 100% conversion)

Products Weight Percent

Naphtha 28.5 %

Distillate 15.9 %

Gas oil 1.8 %

Char 18.8 %

Coke 8.9 %

Other 26.1 %

Page 13: Technical Aspects of Oil Shale Production and Processingrepository.icse.utah.edu/.../oil_shale_production_processing_milind... · Artificial Lift Kerogen Oil Hydrocarbon Gases Spent

Surface Processing IssuesSurface Processing Issues

KnowledgeKnowledge--experience in the 70sexperience in the 70s--80s80s

–– Scattered, not integratedScattered, not integrated

Solids handlingSolids handling

–– Oil mistsOil mists

Problem of fines in the oilProblem of fines in the oil

Scale of operation Scale of operation

–– Must be large to overcome the oilMust be large to overcome the oil--price price

thresholdthreshold

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Oil Shale Oil Shale –– Insitu ProcessesInsitu Processes

Rubble inRubble in--situ extractionsitu extraction

–– Create a rubbleCreate a rubble

–– Air and steam injection at the topAir and steam injection at the top

–– Large scale experiments runLarge scale experiments run

Yields of about 7 gpt Yields of about 7 gpt –– 40% of the oil in place40% of the oil in place

Modern inModern in--situ processessitu processes

–– Electric heating Electric heating -- ShellShell

–– Other forms of heatingOther forms of heating

–– Porosity creation, inPorosity creation, in--situsitu

Hybrid processes (Redleaf Hybrid processes (Redleaf –– Ecoshale)Ecoshale)

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Shell ICP (Insitu Conversion Process)Shell ICP (Insitu Conversion Process)

From www.shell.com

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InIn--situ Issuessitu Issues

Porosity, permeability creationPorosity, permeability creation

Conversion and recoveryConversion and recovery

Question of residual oilQuestion of residual oil

Heat losses and energy efficiencyHeat losses and energy efficiency

Impact on waterImpact on water

Carbon footprintCarbon footprint

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Upgrading Shale OilUpgrading Shale Oil

ObjectivesObjectives–– Nitrogen removal Nitrogen removal

–– Molecular weight reductionMolecular weight reduction

–– HydrogenationHydrogenation

Some modifications to the existing hydroSome modifications to the existing hydro--processing technologies may be requiredprocessing technologies may be required

Similar costsSimilar costs

Page 18: Technical Aspects of Oil Shale Production and Processingrepository.icse.utah.edu/.../oil_shale_production_processing_milind... · Artificial Lift Kerogen Oil Hydrocarbon Gases Spent

ResourcesResources

WaterWater

–– No direct water input requiredNo direct water input required

–– Surface processingSurface processing

Water for mining operations Water for mining operations

Same order as a refinery or chemical process plantSame order as a refinery or chemical process plant

–– InIn--situ processingsitu processing

Water required for drilling/associated activitiesWater required for drilling/associated activities

Carbon footprintCarbon footprint

–– Process and fuel dependentProcess and fuel dependent

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Carbon Footprint Kilograms of Carbon Footprint Kilograms of

COCO22 Per BarrelPer BarrelOil Oil Sands

Mining/

Extraction

Oil Sands

In-Situ

Oil Shale

Mining/

Extraction

Oil Shale

In-Situ

Production 25 45 95 85 66 (NG)261 (Coal)

Upgrading 28 37 37 37 35

Transportation(gasoline,Diesel, jet fuel)

450 450 450 450 450

Preliminary Estimates Only

Oil sands numbers from Professor Murray Gray, University of Alberta

Page 20: Technical Aspects of Oil Shale Production and Processingrepository.icse.utah.edu/.../oil_shale_production_processing_milind... · Artificial Lift Kerogen Oil Hydrocarbon Gases Spent

Process PossibilitiesProcess Possibilities

InIn--situ situ Surface ProductionSurface Production

–– Energy selfEnergy self--sufficientsufficient

Sequester CO2

Shale Deposit

Heat Gas

LiquidHydrocarbons

Sequester CO2Re-use, recycle all water

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Ongoing Research at U of UOngoing Research at U of U

Depositional heterogeneity and inDepositional heterogeneity and in--situ modelingsitu modeling

Fundamental transformation kinetics and compositions Fundamental transformation kinetics and compositions

of oilsof oils

KerogenKerogen--asphaltene atomistic modelingasphaltene atomistic modeling

Impact on water qualityImpact on water quality

OxyOxy--fuel combustion for providing the energyfuel combustion for providing the energy

PorePore--scale analysisscale analysis

Climate change legislationClimate change legislation

Market analysisMarket analysis

Data repositoryData repository

Summary

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Fundamental kinetics and compositional understanding

P

Temperature Controller

Gas Cylinder

Back Pressure

Regulator

Vent line-1

Pressure Gauge

Heater

Check valve

Relief valve

Waste Container

PPressure GaugeSeparation unit

Cooling

Unit

Product 1

Condenser-1

Condenser-2

Gas Sampler

Product 2Product 3

Product 4

Vent line-2

Vent line-3

Flow meter

Insulation

Page 24: Technical Aspects of Oil Shale Production and Processingrepository.icse.utah.edu/.../oil_shale_production_processing_milind... · Artificial Lift Kerogen Oil Hydrocarbon Gases Spent

SummarySummaryPossible to institute environmentally Possible to institute environmentally

responsible, energyresponsible, energy--efficient processesefficient processes

Key issues need to be resolved with Key issues need to be resolved with

respect to both surface extraction and inrespect to both surface extraction and in--

situ technologiessitu technologies

A lot to be learnt from previous research A lot to be learnt from previous research ––

particularly on exparticularly on ex--situ processessitu processes

Fundamental and applied research on Fundamental and applied research on

resource characterization pyrolysis, resource characterization pyrolysis,

environmental and policy aspects environmental and policy aspects

underway at the University of Utahunderway at the University of Utah


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