Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
623105 | Desalination | 2015 | 9 Pages |
Abstract
Brine management is a major bottleneck for coal seam gas (CSG) production in Australia. This study investigated the concentration of CSG reverse osmosis (RO) brine using a pilot membrane distillation (MD). The system was equipped with a novel spiral-wound air gap membrane distillation (AGMD) module. By operating the pilot MD system at low feed temperature and a small temperature gradient, a stable distillate production rate could be maintained. The resulting low permeate flux can be offset by a high packing density of the spiral-wound membrane module. Here, using a module with diameter, height, and total membrane surface area of 0.4Â m, 0.5Â m, and 7.2Â m2, respectively, the pilot MD system sustainably achieved 80% water recovery and produced 10Â L/h of distillate from CSG RO brine. Overall, 95% water recovery could be obtained from CSG produced water for beneficial uses by a combination of RO and AGMD without any observable membrane scaling. A preliminary thermal energy demand analysis suggests that if installed in New South Wales (Australia), 1Â ha of flat-plate solar thermal collector arrays could provide sufficient thermal energy to treat 472Â m3/day (2970Â bbl/day) of CSG produced water using the proposed RO/AGMD treatment train.
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Filtration and Separation
Authors
Hung C. Duong, Allan R. Chivas, Bart Nelemans, Mikel Duke, Stephen Gray, Tzahi Y. Cath, Long D. Nghiem,