Autopsy of high-pressure membranes to compare effectiveness of MF and UF pretreatment in water reclamation.
A pilot-plant study was designed to compare the effectiveness of microfiltration (MF) and ultrafiltration (UF) as pretreatment for high-pressure membranes in reclamation of biologically treated wastewater effluent. Granular media, filtered secondary effluent from a full-scale wastewater treatment plant, was fed to MF and UF units that operated in parallel. Each of these filtrates served as the feedwater to two reverse osmosis (RO) units and one nanofiltration (NF) unit that operated in parallel. The decline in specific flux was substantially lower for high-pressure membranes receiving UF than MF pretreatment over the course of each of four pilot plant runs that lasted from 1 to 7 weeks. The removal of organic matter as measured by dissolved organic carbon (DOC) was somewhat higher by UF than MF pretreatment (about 15% by UF compared with 11% by MF). Addition of ferric chloride ahead of the UF unit, but not ahead of the MF unit, may account for this additional removal of organic matter. However, the additional DOC removal appeared insufficient to explain the differential in foulant accumulation between high-pressure membranes receiving UF and MF pretreatment. Extensive autopsy analyses of these high-pressure membranes showed from 35% to 56% less organic carbon on those receiving UF rather than MF pretreatment. A more specific indicator of a differential in organic fouling was the accumulation of polysaccharides and this showed from 27% to 38% less on UF- than on MF-pretreated membranes. Yet another possible source of foulants is inorganic material given that the inorganic and organic weight percentages were nearly equal (56% vs. 44%) on the membrane surface. One specific source was aluminum added for phosphorus removal. Less fouling of high-pressure membranes pretreated by UF than MF could be due to the following: (1) a small, but very important, colloidal fouling fraction may have passed through MF but was rejected by UF pretreatment; (2) organic fouling was not related to organics in either the MF or UF filtrates but rather to organics that are generated in situ by microbial activity on the membrane surface; and/or (3) less passage of colloidal Al-P that carried over from secondary wastewater treatment.
Kim
Jeonghwan
J
Department of Civil and Environmental Engineering, Michigan State University, East Lansing, MI 48823, USA. kimjeo21@msu.edu
DiGiano
Francis A
FA
Reardon
Roderick D
RD
D002244:Carbon / Q000032:analysis; D002712:Chlorides / Q000032:analysis; D008670:Metals / Q000032:analysis; D009757:Nylons; D010758:Phosphorus / Q000032:analysis; D011108:Polymers; D011126:Polypropylenes; D011134:Polysaccharides / Q000032:analysis; D011312:Pressure; D012825:Silicon / Q000032:analysis; D013450:Sulfones; D013455:Sulfur / Q000032:analysis; D014462:Ultrafiltration / Q000295:instrumentation / Q000379:methods; D014865:Waste Disposal, Fluid / Q000295:instrumentation* / Q000379:methods; D014873:Water Pollutants / Q000032:analysis*; D018508:Water Purification / Q000295:instrumentation* / Q000379:methods
D002712:Chlorides; D008670:Metals; D009757:Nylons; D011108:Polymers; D011126:Polypropylenes; D011134:Polysaccharides; D013450:Sulfones; D014873:Water Pollutants; C022840:polyether sulfone; D010758:Phosphorus; D013455:Sulfur; D002244:Carbon; D012825:Silicon