Pushing the limits of off-the-shelf technology...–Reverse Osmosis/Nanofiltration: 30,000-50,000...

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Pushing the limits of off-the-shelf technology: Achieving better efficiency and recovering useful byproducts from produced water Presented by Malynda Cappelle Presented at WRRI Produced Water Workshop / 24 May 2016

Transcript of Pushing the limits of off-the-shelf technology...–Reverse Osmosis/Nanofiltration: 30,000-50,000...

Page 1: Pushing the limits of off-the-shelf technology...–Reverse Osmosis/Nanofiltration: 30,000-50,000 mg/L TDS –Electrodialysis: typically < 10,000 mg/L TDS –Ion Exchange: less than

Pushing the limits of off-the-shelf technology:Achieving better efficiency and recovering useful byproducts from produced water

Presented by Malynda Cappelle

Presented at WRRI Produced Water Workshop / 24 May 2016

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Overview

• BRIEF overview on cost of disposal

• Desalination technologies

• High recovery desalination

• Resource recovery potential

• Thoughts on combining desalination and resource recovery

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• Fresh water can be expensive (especially retail or municipal water)

• If SWDs aren’t prevalent and/or if trucking is required, disposal of produced water can be substantial and significant

Cost of Fresh & Produced Water

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• Cost varies

• McCurdy 2011:

– Salt water disposal facilities: $0.25-8/bbl

– Trucking cost: $1/bbl

– Pipelines more efficient & reduces traffic

• Argonne National Laboratories (Veil, 2006)

– Injection > Evaporation > Burial

– Range of cost $0.30-10/bbl (most < $1/bbl)

– Recycling was not widely reported

Produced Water Disposal

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• PRE-TREATMENT IS KEY

• Scale-forming constituents must be removed from water for use by O&G

• Biological/organic constituents can limit desalination implementation

Treatment of Produced Water(probably repeating others)

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• Salinity (measured by TDS):

– Reverse Osmosis/Nanofiltration: 30,000-50,000 mg/L TDS

– Electrodialysis: typically < 10,000 mg/L TDS

– Ion Exchange: less than 1,000 mg/L TDS, maybe higher in some cases

• High organic and biological feedwaterconcentrations will require pre-treatment

Limits of Desalination(as currently practiced)

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• Pros:– Excellent product water quality

– Well-known process & proven designs/performance

– Newer membranes (nanofiltration, wider spacer) offer potential for desalination of difficult waters

• Cons– Salinity limit (pressure limitations)

– Solubility limits (solubility limitations)

– Fouling limits

– Waste Disposal

Pros & Cons of Membrane processes:Reverse Osmosis/Nanofiltration

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• Pros:– Good product water quality– Known process & proven designs/performance– Resource recovery possibility– Able to handle (somewhat) higher fouling water– Able to dial in specific water quality– Can produce “kill” brines– More efficient at higher temperatures & salinity– Pairs well with renewable energy

• Cons– Can be expensive (capital and operating cost)– Specialized membranes are expensive– Still require pre-treatment (similar to RO/NF)

Pros & Cons of Membrane processes:Electrodialysis

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• Pros:

– Excellent product water quality

– Known process & proven designs/performance

– Able to handle higher fouling water

• Cons

– Expensive (capital and operating cost)

– Cleaning is regularly needed

Pros & Cons of Thermal processes

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Case Study: Four Corners Desalination with Nanofiltration

Source: Cappelle, et al. (2010)

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Case Study: Four Corners Desalination with Nanofiltration (cont)

RIP, Allan SattlerSource: Cappelle, et al. (2010)

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Potential Technology: Electrodialysis Methathesis

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Potential Technology: ED with monovalent selective membranes

Na+

Cl-

SC

Na+

Cl-

Na+

Concentrate Diluate Concentrate Diluate

Supernatant

from tank

Supernatant

from tank

Rinse Rinse

+ -

REPEATING

CELL

Ca2+

SO4=

SO4=

Ca2+

Ca2+

SA SC SA SC

Na+

Ca2+

SC

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ZDD (Zero Discharge Desalination)Brackish Water application (<10,000 mg/L TDS)

Finished Water

Brackish Water Reverse

Osmosis/Nanofiltration75-85% Recovery

Solar Salt Recovery & Evaporation Ponds

>95-99% Recovery & Zero Liquid Discharge

Mg(OH)2

CaSO4

Ca-rich SO4-richLime

Electrodialysis Metathesis (EDM)

95-98% Recovery

NaCl

Mixed ClMixed Na

RO/NF Concentrate

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Potential Combination: EDM + RO/NF (>10,000 mg/L TDS)

Mixed SodiumNa + (SO4, Cl, Br, HCO3, CO3, …)

Mixed Chloride(Ca, Mg, Ba, Na, …) + Cl

NaCl

Finished Water

Pre-treated PW Water

NF Concentrate

• Mix & recover solid gypsum and liquid NaCl

• Use Mixed Cl or Mixed Na as a kill fluid?

• Recover useful minerals from either Mixed Na or Mixed Cl?

• Send to evaporation pond

• Send to thermal process

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Potential Combination:ED(R) + RO/NF (>10,000 mg/L TDS)

ED Concentrate(mostly monovalent ions)

Finished Water

Pre-treated PW Water

NF Concentrate

• Use concentrate as a kill fluid?

• Recover useful constituents from concentrate?

• Send to evaporation pond

• Send to thermal process

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• Geo-Processors SAL-PROC™

• Selective Salt Recovery from Reverse Osmosis Brine Using Inter-stage Ion Exchange (Goldman, 2011)

• GE’s AquaSel™

Other High Recovery Technologies with salt recovery potential

Sources:• SAL-PROC: Mickley, 2008 (WateReuse Foundation Report)• GE: http://www.ge.com/mining/docs/2981884_1346772848_GE_AquaSel_Non-

Thermal_Desalination_Systems_Brochure.pdf• Goldman, et al.: 56th Annual New Mexico Water Conference Proceedings

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• Produced water revenue potential:– BEST: rubidium

formate, rubidium chloride and cesium

– MODERATE: bromine, iodine, lithium hydroxide and lithium carbonate

– MAYBE: magnesium, potash, and soda ash

Resource Recovery:Thinking outside the barrel

CaCO3 MgSoda Ash

PotashSalt

Lithium compounds

Bromine

Iodine

Rubidium compounds

Cesium

Source: S. Ray (2016) – Thesis & upcoming USGS report

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• Treat to need• Academia and industry have ideas – we need to test

them with real PW• Pre-treatment, pre-treatment, pre-treatment• Some chemicals added for pipeline protection

(biocides, anti-corrosion, etc.) make water treatment more challenging

• At what point is centralized or portable water treatment more affordable?

• What business model works best for water treatment & resource recovery? (service industry?)

Final thoughts (questions?)

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Malynda Cappelle

Associate Director, Center for Inland Desalination Systems

915-747-8953

[email protected]

Thank you