Treatment of Highly Saline Brines by Supercritical Precipitation Followed by Supercritical Membrane Separation
- Univ. of Illinois at Urbana-Champaign, IL (United States); University of Illinois at Urbana-Champaign
- Univ. of Illinois at Urbana-Champaign, IL (United States)
A two-stage supercritical (SC) desalination system is proposed to treat highly saline brines to high-purity steam that could be used in power generation. Highly saline brines with up to similar to 20% salt content are pressurized and heated to SC conditions of 500 degrees C and 3500 psi to rapidly precipitate the dissolved salts and generate SC steam containing similar to 100 ppm salts. Two highly saline brines, collected from an oil field and a deep saline formation, and two concentrated NaCl solutions were treated in the SC desalination system. A SC membrane separation system with carbon filters is developed and used to purify the SC steam to a high purity level. Promising carbon filters or membranes prepared and tested for purifying SC steam included a porous graphite disk, a flexible graphite sheet, and a carbon nanotube-based membrane. Finally, the best performing membranes exhibited a very high water flux of similar to 200-800 kg/m2.h, with a salt rejection of >90%.
- Research Organization:
- Univ. of Illinois at Urbana-Champaign, IL (United States)
- Sponsoring Organization:
- USDOE Office of Fossil Energy (FE)
- Grant/Contract Number:
- FG02-07ER46471; FE0024015; FG02-07ER46453
- OSTI ID:
- 1607422
- Journal Information:
- Industrial and Engineering Chemistry Research, Journal Name: Industrial and Engineering Chemistry Research Journal Issue: 8 Vol. 58; ISSN 0888-5885
- Publisher:
- American Chemical Society (ACS)Copyright Statement
- Country of Publication:
- United States
- Language:
- English
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