Abstract

The production of demineralised water from drinking water by nanofiltration/membrane distillation system (NF/MD) has been investigated. The precipitation of CaCO 3 on the membrane surface and a rapid flux decline was observed when tap water was used directly as a feed. The problem of scaling was eliminated by the acidification of the feed to pH = 4 and stable module efficiency was observed. The performance of the MD module was significantly improved when tap water was subjected to softening in NF process. The precipitation of the silica compounds during the operation of MD process with the NF permeate was found. These compounds caused clogging of the capillary membrane inlets, resulting in a gradual decline of the module efficiency. The application of filtration net assembled at the module inlet prevented blocking of the capillary membrane inlets. The MD process can be run without a flux decline, associated with the scaling, when the pH of NF permeate was adjusted at a level of 4. A partial wettability of the membrane resulting in a flux decline by 30% was observed after 1100 h of process duration. The quality of obtained distillate was stable and practically independent of the feed concentration. The produced distillate has the electrical conductivity in the range of 1.5–2.5 μS cm −1 and contained 0.5 ppm of inorganic carbon and below 1 ppm TOC.

Full Text
Paper version not known

Talk to us

Join us for a 30 min session where you can share your feedback and ask us any queries you have

Schedule a call

Disclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.