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Environmental and Technological Issues Associated with Non-Conventional Oil - Recent Technological Advancements

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Environmental and Technological Issues Associated with Non-Conventional Oil - Recent Technological Advancements
Environnemental and Technological Issues Associated with

Non-Conventional Oil







Recent Technological Advancement





Claude MANDIL

Chairman and CEO

Institut Français du Petrole





IEA Conference on non-conventional oil/ Calgary November 25-26, 2002

Non-Conventional Oil

Specific properties of heavy and extra-heavy oils



Heavy oil Light oil



Gravity (°API) 10 000 cp

> 10 000 cp









IEA Conference on non-conventional oil/ Calgary November 25-26, 2002

Non-Conventional Oil

Recent Technological Advancement



Production methods

- industrial primary production

- industrial and pilot enhanced recovery

- laboratory enhanced production

Transportation methods

- traditionnal technologies

- technologies to be developed

Upgrading methods

- recent advancement

- in the futur

CO2 issues

Conclusion



IEA Conference on non-conventional oil/ Calgary November 25-26, 2002

Production Methods



High viscosity Low ability to flow through the

porous media









Primary production Enhanced recovery methods







Industrial solutions

Industrials solutions

- Foamy oils

- Cyclic Steam Stimulation (CSS)

- Wormholes

- Steam assisted gravity drainage (SAGD)

Pilot solutions

- Polymer injection

- Solvent injection (VAPEX)

Laboratory solution

- In-situ combustion (THAI process)



IEA Conference on non-conventional oil/ Calgary November 25-26, 2002

Industrial primary production methods



Foamy oil



Gas bubbles are trapped by the viscous oil Numerical modeling of

the phenomena?









Wormholes



Unconsolidated sand reservoirs

Sand production enhances oil recovery How to control

After wormhole formation?

Before production

production

Development

of a cavity



IEA Conference on non-conventional oil/ Calgary November 25-26, 2002

Industrial and pilot solutions for enhanced production

SAGD: Steam Assisted Gravity Drainage



Overbunden

How to monitor the

Steam chamber steam chamber?





Mobile oil

Underbunden



Legend : Injector

Producer





Vapex and NAGD (Naphtha Assisted Gravity Drainage)



- Steam replaced by propane or naphtha Solvents are

- No use of water, less environmental problem expensive products.





IEA Conference on non-conventional oil/ Calgary November 25-26, 2002

Laboratory solutions: in-situ combustion



- THAI process (Toe-to-Heel Air injection)

(U. of Bath, PRI) Will it work at the

field scale?









Injector Combustion front Producer



Overbunden

Mobile cold heavy oil

Air and water oil zone









Underbunden



IEA Conference on non-conventional oil/ Calgary November 25-26, 2002

Transportation Methods



High viscosity important frictions high pressure

drop









Reduction of the viscosity Reduction of frictions







Traditional solution

- Dilution To be developed

- Heating and isolation - Core Annular Flow

- Emulsion for combustion - Friction Reducing Agents

- Partial on-site upgrading

To be developed

- Emulsion for transportation





IEA Conference on non-conventional oil/ Calgary November 25-26, 2002

Transportation: Traditional technologies (1)



Dilution



- Blending the heavy oil with a light one Diluent disponibility

and/or recycling

- Easy to realize and efficient









Heating and isolation

High temperature

induces greater

- Crude is heated (50°C) and pipes isolated corrosion









IEA Conference on non-conventional oil/ Calgary November 25-26, 2002

Transportation: Traditional technologies (2)





Partial on-site upgrading



Conversion at the

- Production of transportable synthetic crude well-site?









Emulsion for combustion





- oil in water emulsion as combustible for High emissions of flue

electric power plant gas and CO2







IEA Conference on non-conventional oil/ Calgary November 25-26, 2002

Transportation: technologies to be developed



Emulsion for transportation

Oil

Breaking the

emulsion?

Water







Core annular flow

Pipe



Oil adherence while

stopping the flow

Water layer

Viscous oil







Friction Reducing Agents

Optimized proportion

- optimization of the dilution and the heating between FRA and

processes dilution



IEA Conference on non-conventional oil/ Calgary November 25-26, 2002

Comparison of transportation methods efficiency









*

*









* : V% oil/water

source: Intevep



IEA Conference on non-conventional oil/ Calgary November 25-26, 2002

Comparison of the transportation methods



Heating Dilution Upgrading Emulsion Annular flow



Required pipe Normal Larger Normal Larger Normal

diameter





Corrosion Potential None None Potential Potential





Additional Normal High High (field Normal/high Normal/high

investments (heaters) (parallel refinery) (supply (supply

diluant system) system)

system)

Environmental Electricity No specifity No specifity Water Water

problems source separation / treatment

treatment





Traditional solutions Solutions to be developed



IEA Conference on non-conventional oil/ Calgary November 25-26, 2002

Upgrading heavy oils

Products:

Atmospheric Gas

Classic conversion

distillation & LPG

hydrotreatment

Gasoline

Vacuum

distillation Kerosene

Atmospheric gasoil

residue Deep fuel-oil

Vacuum conversion

Coke

residue





Yield °API S (W%) Ni ppm V ppm

Conventional 20% 5.9 4.2 47 144

Non-conventional 40% 1.9 4.8 153 590





IEA Conference on non-conventional oil/ Calgary November 25-26, 2002

Upgrading heavy oils

- High gravity

- Few light products

- Lots of impurities

- Lots of heavy residues

- Low H content



Upgrading the residues: deep conversion process









Traditional solutions

- Visbreaking

- Delayed coking

- Solvent Deasphalting

Current R&D pathways

- Hydrotreating

- Association of processes

- Gasification





IEA Conference on non-conventional oil/ Calgary November 25-26, 2002

Upgrading heavy oils

improved catalyst process









1st generation 2nd generation

catalyst catalyst



Residue conversion, V % 45-75 45-80

Hydrodesulfurisation 55-80 75-90

Denitrogenation 23-35 30-50

Metals removal 65-90 65-90

source: IFP









IEA Conference on non-conventional oil/ Calgary November 25-26, 2002

Upgrading heavy oils

Combination of hydrotreating and solvant deasphalting





Combination of H-Oil and Solvahl IFP process





Heavy Crude Syncrude



Yield V% 100 85 - 95

Gravity °API 10.8 23

Sulfur W% 4.39 1.74

CCR W% 13.2 0.5 - 1.8

Ni+V Wppm 205 5-6

Viscosity cSt 1447 2.7 - 3.2

source: IFP/WPC









IEA Conference on non-conventional oil/ Calgary November 25-26, 2002

Upgrading heavy oils

Global interest for Gasification





Partial

oxidation

Heavy oil Synthesis gas (mainly H2 and CO)









Global interest:

- Integrated gasification combined cycle (IGCC)

- Combination with GTL

But!

- Investment still quite high, especially for oxygen production

- High CO2 emissions







IEA Conference on non-conventional oil/ Calgary November 25-26, 2002

CO2 issues

Energetic yield “From well to syncrude”

%



100

Conventional





90 Orinoco



Steam

85

injection HW

80 oil sand

75 Steam

injection VW

2.5 10 15 25

CO2 emissions

HW: horizontal wells g/MJ

VW: vertical wells

IEA Conference on non-conventional oil/ Calgary November 25-26, 2002 source: IFP

Conclusion



Lots of technical innovations for

non-conventional oil exploitation







3 main issues for R&D focus

- energetic yield to improve,

- environmental impact to reduce

- CO2 emissions to reduce









IEA Conference on non-conventional oil/ Calgary November 25-26, 2002


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