the coho - netl.doe.gov · the coho ef icient carbon capture and water reuse doe ofe award...

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The COHO Ef�icient Carbon Capture and Water Reuse DOE OFE Award DE-FE0024057 Jennifer Klare, Porifera Inc., Hayward, CA Porifera’s Forward Osmosis (PFO) Technology COHO System Design Waste Water Concentration and CO2 Capture Combined About Switchable Polarity Solvents How Does COHO Work? Acknowledgements Aaron Wilson, Ph.D. DOE NETL: Charles Miller DOE SBIR: Andrea Dunn Contact Forward osmosis is uniquely suited to concentrate high fouling waters that clog up other membranes. Key Innovations High �lux, high selectivity membrane Most ef�icient element form factor Unprecedented reductions in FO system size and cost; highest processing power and smallest footprint. The draw solution puri�ies wastewater (1) using osmotic potential to drive water across a selective membrane. (2) The draw solution is generated using carbon dioxide from �lue gas to switch the draw solute to the miscible aqueous phase. Carbon dioxde (3) is released and clean water is produced (4) by using low-grade heat, switching the drawsolute (5) back to its original immiscible phase for mechanical separation. Wilson; Stewart Structure-Function Study of Tertiary Amine Switchable Polarity Solvents, RSC Advances 2014, 4, 11039-11049. Simulated Power Plant Feeds Porifera has developed simulated power plant feeds based off an existing plant that may be ideal for piloting. Target water recoveries ~60 - 80%. Feed 1: Cooling Tower Feed TDS = 800 ppm, pH = 9.1 Ca, Na, Ba, Fe, Carbonate, Sulfate, F, Cl Feed 2: FGD Unit Feed TDS = 16,000 ppm, pH = 7 Ca, Na, Ba, Fe, Carbonate, Sulfate, F, Cl Initial studies revealed maximum achievable recoveries, above which membrane scaling occurs. We are developing anti-scalant methods for these challenging feeds. Bene�its of COHO: 1) reduce the volume of wastewater 2) expand the capabilities of water treatment 3) facilitate carbon dioxide capture from �lue gas 4) use waste heat for draw recovery to reduce the energy costs to treat water Goals of the Project: 1) Optimize the system process, including: carbon dioxide capture and water processing as well as the draw chemistry. 2) Operate and model the system for installation at a power plant. Initial Studies 1) High concentration in water miscible polar form. 2) Can be mechanically seperated when switched to non-polar form. 3) High membrane retention and chemical compatability. Jennifer Klare, Director of New Applications 3502 Breakwater Ct. Hayward, CA [email protected]

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Page 1: The COHO - netl.doe.gov · The COHO Ef icient Carbon Capture and Water Reuse DOE OFE Award DE-FE0024057 Jennifer Klare, Porifera Inc., Hayward, CA Porifera’s Forward Osmosis (PFO)

The COHO Ef�icient Carbon Capture and Water Reuse

DOE OFE Award DE-FE0024057Jennifer Klare, Porifera Inc., Hayward, CA

Porifera’s Forward Osmosis (PFO)Technology

COHO System Design

Waste Water Concentration and CO2 Capture Combined

About Switchable Polarity Solvents

How Does COHO Work?

AcknowledgementsAaron Wilson, Ph.D.

DOE NETL: Charles MillerDOE SBIR: Andrea Dunn

Contact

Forward osmosis is uniquely suited to concentrate high fouling waters that clog up other membranes.

Key Innovations• High �lux, high selectivity membrane• Most ef�icient element form factor• Unprecedented reductions in FO systemsize and cost; highest processing power and smallestfootprint.

The draw solution puri�ieswastewater (1) using osmoticpotential to drive water across a selective membrane. (2) The draw solution is generated using carbon dioxide from �lue gas to switch the draw solute to the miscible aqueous phase. Carbon dioxde (3) is released and clean water is produced (4) by using low-grade heat, switching the drawsolute (5) back to its original immiscible phasefor mechanical separation.

Wilson; Stewart Structure-Function Study of TertiaryAmine Switchable Polarity Solvents, RSC Advances 2014,4, 11039-11049.

Simulated Power Plant FeedsPorifera has developed simulatedpower plant feeds based off an existingplant that may be ideal for piloting.Target water recoveries ~60 - 80%.

Feed 1: Cooling Tower FeedTDS = 800 ppm, pH = 9.1Ca, Na, Ba, Fe, Carbonate, Sulfate, F, Cl Feed 2: FGD Unit FeedTDS = 16,000 ppm, pH = 7Ca, Na, Ba, Fe, Carbonate, Sulfate, F, Cl

Initial studies revealed maximum achievablerecoveries, above which membrane scaling occurs. We are developing anti-scalantmethods for these challenging feeds.

Bene�its of COHO:1) reduce the volume of wastewater2) expand the capabilities of water treatment3) facilitate carbon dioxide capture from �lue gas4) use waste heat for draw recovery to reduce the energy costs to treat water

Goals of the Project:1) Optimize the system process, including:carbon dioxide capture and water processingas well as the draw chemistry.2) Operate and model the system forinstallation at a power plant.

Initial Studies

1) High concentration in water miscible polar form.2) Can be mechanically seperated when switchedto non-polar form.3) High membrane retention and chemical compatability.

Jennifer Klare,Director of New Applications 3502 Breakwater Ct. Hayward, [email protected]