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doi: 10.5281/zenodo.2812440 , 10.5281/zenodo.2827801 , 10.5281/zenodo.2672027 , 10.5281/zenodo.2825063 , 10.5281/zenodo.2840022 , 10.5281/zenodo.2664325 , 10.5281/zenodo.2669000 , 10.5281/zenodo.2813921 , 10.5281/zenodo.2661696 , 10.5281/zenodo.2837299 , 10.5281/zenodo.2819229 , 10.5281/zenodo.2666316 , 10.5281/zenodo.2812441 , 10.5281/zenodo.2830474 , 10.5281/zenodo.2664324 , 10.5281/zenodo.2661695 , 10.5281/zenodo.2665287 , 10.5281/zenodo.2825064 , 10.5281/zenodo.2666317 , 10.5281/zenodo.2665286 , 10.5281/zenodo.2840021 , 10.5281/zenodo.2672026 , 10.5281/zenodo.2862093 , 10.5281/zenodo.1093683 , 10.5281/zenodo.2662755 , 10.5281/zenodo.2830475 , 10.5281/zenodo.2662362 , 10.5281/zenodo.2862094 , 10.5281/zenodo.2663370 , 10.5281/zenodo.2827802 , 10.5281/zenodo.2819228 , 10.5281/zenodo.2668999 , 10.5281/zenodo.2663371 , 10.5281/zenodo.2824137 , 10.5281/zenodo.2837300 , 10.5281/zenodo.2824138 , 10.5281/zenodo.2813922 , 10.5281/zenodo.2662361 , 10.5281/zenodo.1093684 , 10.5281/zenodo.2662756
doi: 10.5281/zenodo.2812440 , 10.5281/zenodo.2827801 , 10.5281/zenodo.2672027 , 10.5281/zenodo.2825063 , 10.5281/zenodo.2840022 , 10.5281/zenodo.2664325 , 10.5281/zenodo.2669000 , 10.5281/zenodo.2813921 , 10.5281/zenodo.2661696 , 10.5281/zenodo.2837299 , 10.5281/zenodo.2819229 , 10.5281/zenodo.2666316 , 10.5281/zenodo.2812441 , 10.5281/zenodo.2830474 , 10.5281/zenodo.2664324 , 10.5281/zenodo.2661695 , 10.5281/zenodo.2665287 , 10.5281/zenodo.2825064 , 10.5281/zenodo.2666317 , 10.5281/zenodo.2665286 , 10.5281/zenodo.2840021 , 10.5281/zenodo.2672026 , 10.5281/zenodo.2862093 , 10.5281/zenodo.1093683 , 10.5281/zenodo.2662755 , 10.5281/zenodo.2830475 , 10.5281/zenodo.2662362 , 10.5281/zenodo.2862094 , 10.5281/zenodo.2663370 , 10.5281/zenodo.2827802 , 10.5281/zenodo.2819228 , 10.5281/zenodo.2668999 , 10.5281/zenodo.2663371 , 10.5281/zenodo.2824137 , 10.5281/zenodo.2837300 , 10.5281/zenodo.2824138 , 10.5281/zenodo.2813922 , 10.5281/zenodo.2662361 , 10.5281/zenodo.1093684 , 10.5281/zenodo.2662756
{"references": ["J. Losier, A. Fernandez, Using a membrane bioreactor/reverse osmosis\nsystem for indirect potable reuse, Proc. of the conf. on Membranes,\nParis, October 2000, Desalination publications, L'Aquila, Italy. Vol. 2,\n297-311.", "O. Duin, P. Wessels et al., Direct nanofiltration or ultrafiltration at\nWWTP effluent. Proc. of the conf. on Membranes, Paris, October 2000,\nDesalination publications, L'Aquila, Italy. Vol. 2, 105-112.", "M. Abdel-Javad, S. Ebrahimet. al., Advanced technologies for municipal\nwastewater purification: technical and economic assessment,\nDesalination, 124 (1999), 251-261.", "Pervov A. Scale formation prognosis and cleaning procedure schedules\nin reverse osmosis operation, Desalination (1991), 83, 77-118.", "Pervov A., Andrianov A. Application of membranes to treat wastewater\nfor its recycling and reuse: new considerations to reduce fouling and\nincrease recovery up to 99 per cent, Desalination and water treatment\n(2011) 35, 2-9.", "R.A. Riddle. Open channel ultrafiltration for reverse osmosis\npretreatment. IDA World Conference on Desalination and Water Reuse.\nAugust 25-29, 1991, Washington DC. Pretreatment and Fouling.", "R. Bian, K. Yamamoto,Y. Watahabe. The effect of shear rate on\ncontrolling the concentration polarization and membrane fouling.\nProceedings of the Conf. on Membranes in Drinking and Industrial\nWater Production, Paris, France, 3-6 October 2000, v.1, p. 421-432.", "ITT PCI Membranes - Membrane Technology- tubular membranes -\nmicro-, ultra-, nanofiltration, reverse osmosis, http: //\nwww.pcimembranes.eu/ (accessed 7 November 2010).", "H. Futselaar, H. Schoneville, W.Meer. Direct capillary nanofiltration for\nsurface water. Desalination, 157 (2003), 135-136.\n[10] N. Matveev,A. Pervov. Use of reverse osmosis to treat domestic\nwastewater for local utilities and in small industries. Tianjin ida world\ncongress 2013 on desalination and water reuse. IDAWC REF: TIAN13-\n217. 20-25 october, China, 2013.\n[11] A. Pervov, N. Matveev. Applications of Open Channel Membrane\nModules to Treat and Reuse Wastewater. Journal of Membrane and\nSeparation Technology | Volume 3 Number 1, 2014, 11-28. DOI:\nhttp://dx.doi.org/10.6000/1929-6037.2014.03.01.2"]}
Local utilities often face problems of local industrial wastes, storm water disposal due to existing strict regulations. For many local industries, the problem of wastewater treatment and discharge into surface reservoirs can’t be solved through the use of conventional biological treatment techniques. Current discharge standards require very strict removal of a number of impurities such as ammonia, nitrates, phosphate, etc. To reach this level of removal, expensive reagents and sorbents are used. The modern concept of rational water resources management requires the development of new efficient techniques that provide wastewater treatment and reuse. As RO membranes simultaneously reject all dissolved impurities such as BOD, TDS, ammonia, phosphates etc., they become very attractive for the direct treatment of wastewater without biological stage. To treat wastewater, specially designed membrane "open channel" modules are used that do not possess "dead areas" that cause fouling or require pretreatment. A solution to RO concentrate disposal problem is presented that consists of reducing of initial wastewater volume by 100 times. Concentrate is withdrawn from membrane unit as sludge moisture. The efficient use of membrane RO techniques is connected with a salt balance in water system. Thus, to provide high ecological efficiency of developed techniques, all components of water supply and wastewater discharge systems should be accounted for.
Reverse osmosis, openchannel module, stormwater treatment, wastewater reuse.
Reverse osmosis, openchannel module, stormwater treatment, wastewater reuse.
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