2011
DOI: 10.2172/1030557
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Cost Effective Recovery of Low-TDS Frac Flowback Water for Re-use

Abstract: The project goal was to develop a cost-effective water recovery process to reduce the costs and environmental impact of shale gas production. This effort sought to develop both a flowback water pretreatment process and a membrane-based partial demineralization process for the treatment of the low-Total Dissolved Solids (TDS) portion of the flowback water produced during hydrofracturing operations. The TDS cutoff for consideration in this project is < 35,000 ~ 45,000 ppm, which is the typical limit for economic… Show more

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Cited by 12 publications
(8 citation statements)
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“…Maximum permissible total suspended solid concentrations in produced water ranges from 1000 mg/L [131] to 10,000 mg/L [132]. The high total dissolved solid abundance (up to 200,000 mg/L) prefers the thermal desalination process [133]. The economic operation of thermal desalination units occurs between the 20,000 and 100,000 mg/L range of the total dissolved solids [123].…”
Section: Treatment Of Produced Watermentioning
confidence: 99%
“…Maximum permissible total suspended solid concentrations in produced water ranges from 1000 mg/L [131] to 10,000 mg/L [132]. The high total dissolved solid abundance (up to 200,000 mg/L) prefers the thermal desalination process [133]. The economic operation of thermal desalination units occurs between the 20,000 and 100,000 mg/L range of the total dissolved solids [123].…”
Section: Treatment Of Produced Watermentioning
confidence: 99%
“…will be necessary to provide cost-effective, energy-efficient desalination of resource extraction wastewaters and brines. 174,175,176,177 Most methods of treatment and desalination of produced and mining wastewaters generate residual streams. Management of these residual streams is complicated by the quality, quantity, and potentially hazardous nature of concentrated brine streams.…”
Section: I3mentioning
confidence: 99%
“…Ion exchange and NF membrane softening are also viable options for hardness reduction, depending on source water quality, system size, and water quality objectives. Both TDS and hardness can be removed via RO, but starting TDS levels greater than ∼35,000 mg/L present economic challenges (110). Thermal processes, including MD, are promising for high-TDS PW, as MD is not significantly influenced by feed salinity (111).…”
Section: Current Treatmentmentioning
confidence: 99%