Management of Water Extracted From Carbon ...

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Calculate that 1,300 to 1,500 L of water could be extracted and managed for every metric ton ... managed per year ... Source: CETCO Oilfield Service Company ...
Management of Water Extracted From Carbon Sequestration Projects: Parallels to Produced Water Management John A. Veil, Christopher B. Harto Argonne National Laboratory and Andrea T. McNemar DOE - National Energy Technology Laboratory SPE Americas E&P Health, Safety, Security and Environmental Conference Houston, TX

March 21-23, 2011

Acknowledgments

 DOE/NETL provided funding to support the work  Coauthors

Outline of Presentation

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Why is water extracted? Water extraction issues Options for managing extracted water Economics Challenges

Why Is Water Extracted?

 CCS projects are likely to inject huge volumes of CO2 into underground formations with suitable properties  Injection of large volumes of material will create a plume and associated pressure front – In large-scale projects, the plume could extend laterally for several kilometers – This creates more opportunity for the plume to intersect conduits to aquifers and/or the surface

 The size of the plume can be reduced by extracting the water already present in the injection formation – Presume that the formations will be deep saline formations

Key Water Extraction Issues  When – Before, when injection begins, delay then begin

 Frequency – Continuous, intermittent

 Quantity  Where – Near well bore, offset – Single well, multiple wells • Plume steering

– Vertical well, horizontal well

 What to do with the water – Focus of our study

Scope of Project

 Identify formations proposed by regional partnerships as suitable deep saline formations for receiving CO2  Examine water quality in those formations  Identify and evaluate management options for extracted water – – – – –

Minimize water managed at the surface Reuse opportunities Disposal options Treatment technologies prior to reuse or disposal Opportunities for deriving secondary value

 Evaluate costs and challenges

Target Formations  Visited the websites of each regional partnership to identify key target formations – Found 99 formations or basins identified as potential future sites for carbon sequestration – The total estimated capacity of these saline formations is 1.7 to 20 trillion metric tons

 Obtained a large database of historical produced water data from NATCARB – Found geochemical water quality information for 61of the 99 locations

Deep Saline Water Quality  Examples of the geochemical data – Formation TDS varies significantly by location – Formation pH ranges from slightly acidic to slightly basic

 Management solution must be targeted to unique local brine chemistry

Variation in TDS Between Regions

9

Other Constituents (1)

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Other Constituents (2)

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How Much Water Could Be Involved? • Assume a CO2 density of 0.65 to 0.78 g/cm • Calculate that 1,300 to 1,500 L of water could be extracted and managed for every metric ton of CO2 injected • This equals a range of 8.1 to 9.5 bbl of water/metric ton of CO2 and an average of 8.8 bbl/metric ton • U.S. produced water generation volume was 21 billion bbl/year in 2007 • The U.S. emitted 5.9 billion metric tons of CO2 in 2008 • Assuming at some point in the future carbon sequestration is scaled up to be equivalent to 10% of 2008 emissions, and an equivalent volume of water is extracted to the volume of CO2 sequestered, this would require that about 5 billion barrels of water would need to be extracted and managed per year • This is about one-fourth of the water volume currently managed by the oil and gas industry.

Extracted Water Management Options • Follow 3-tier water management/pollution prevention hierarchy – Water minimization – Recycle/reuse – Treatment and disposal

• Use most environmentally friendly option where possible

Minimize Water Managed at the Surface

 Inter-formation transfer 

Need to ensure that water chemistry is compatible between formations

Reuse of Extracted Water  Use as is – Injection for recovering more oil – Injection for hydrological purposes

 Use after treatment – Industrial – Agricultural – Drinking

Injection for Recovering More Oil – California • Nearly 25,000 produced water injection wells • 1.8 billion bbl/year total injection – 900 million bbl/year water flood – 560 million bbl/year steam flood – 360 million bbl/year injection for disposal

– Texas • 38,540 wells permitted for enhanced recovery – 5.3 billion bbl/year • 11,988 wells permitted for disposal – 1.2 billion bbl/year

Injection for Hydrological Purposes  Subsidence control

Industrial Use  Cooling water makeup  Use in drilling fluids or hydraulic fracturing fluids  Dust control  Other

Agricultural Use  Irrigation  Livestock and wildlife watering  Managed wetlands Source: USDA

Source: USFWS

Source: USFWS

Options for Disposal of Extracted Water  Discharge – Probably only practical when located near the ocean

 Injection to non-hydrocarbon producing formation – Injection of salt water is likely to face less stringent requirements than injection of CO2 – Would need clarification of UIC regulations • Would not automatically qualify for Class II injection well status

 Evaporation  Offsite commercial disposal

Evaporation  Evaporation ponds  Mechanical evaporation  Freeze-thaw evaporation Source: BC Technologies Ltd.

Source: U.S. Fish and Wildlife Service Source: BC Technologies Ltd.

Offsite Commercial Disposal

http://www.ead.anl.gov/project/dsp_topicdetail.cfm?topicid=18

Treatment Technologies for TDS/Salt Removal

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Membrane processes Ion exchange Thermal distillation Others

Membrane Processes

 Filtration  Reverse osmosis

Ion Exchange

Overflow H2O

D

Loop Valves (Typical) D

Backwash

A

A Pulse Water

Feed Water

Pulse

B

B Adsorption

Displaced Water

Treated Water Spent Brine

C

C Clean Water

Rinse Acid Regen

Regeneration

Ion Exchange Service

Source: Severn Trent Services

Resin Pulsing

Thermal Distillation

Source: Altela Inc.

Source: Altela Inc.

Treatment Technologies for Organics Removal

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Physical separation Flotation Adsorption Others

Physical Separation

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Separation Hydrocyclone Filtration Centrifuge

Source: Natco Source: USEPA

Flotation

Source: Natco

Adsorption

 Organoclay  Activated carbon  Zeolite

Source: CETCO Oilfield Service Company

Opportunities for Secondary Uses

 If hot enough, can generate geothermal energy – RMOTC trial – Borealis Geopower project in Canada

 Mineral extraction – Li – others

Produced Water Management Information System Shows More Information on These Technologies

http://www.netl.doe.gov/technologies/PWMIS/

Cost Considerations  The cost of managing large volumes of extracted water can be a significant factor in the economic viability of a CCS project  The total life-cycle cost includes: – The cost of constructing treatment and disposal facilities, including equipment acquisitions – The cost of operating those facilities, including chemical additives and utilities – Transportation costs , including pumping, piping, and trucking – The cost of managing any residuals or byproducts resulting from the treatment of produced water – Permitting, monitoring, and reporting costs

 Costs for managing produced water range from $8.00/bbl  Costs for managing extracted water should be comparable or higher, due to a possible lack of infrastructure

Final Remarks  Water extraction is not required for CCS programs but may be selected to improve operations or ease permitting  When water is extracted, the volume is likely to be quite large  Management of extracted water poses significant costs and challenges  There are various options available for managing extracted water  In a water-short world, extracted water may have a role as a new water resource

 QUESTIONS?