1999
DOI: 10.1016/s0376-7388(99)00044-7
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Unstable secondary oil/water emulsion treatment using ultrafiltration: fouling control by backflushing

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Cited by 156 publications
(81 citation statements)
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“…[94][95][96] Employing ceramic filtration membranes for oily wastewater treatment is also studied and reported by some researchers. [96][97][98][99][100][101][102][103][104][105][106][107][108][109] Because of the limitation of their pore sizes, directly employing ceramic membranes for the separation of emulsified oil/water mixtures would cause severe fouling problem and low fluxes. 99,104,108 Among the various ceramic filtration membranes, zirconia ceramic membranes exhibit better performance than others for oily wastewater treatment.…”
Section: Ceramic Filtration Membranesmentioning
confidence: 99%
“…[94][95][96] Employing ceramic filtration membranes for oily wastewater treatment is also studied and reported by some researchers. [96][97][98][99][100][101][102][103][104][105][106][107][108][109] Because of the limitation of their pore sizes, directly employing ceramic membranes for the separation of emulsified oil/water mixtures would cause severe fouling problem and low fluxes. 99,104,108 Among the various ceramic filtration membranes, zirconia ceramic membranes exhibit better performance than others for oily wastewater treatment.…”
Section: Ceramic Filtration Membranesmentioning
confidence: 99%
“…Scholars reported the existence of several studies using MSP for the treatment of oily waste, including in the form of stable emulsions, most focusing on the use of ultrafiltration (UF) and microfiltration (MF) membranes in rejection of the oil droplets. In this study the drops of oil are completely rejected and the continuous phase is permeated [9][10][11] . The phase inversion method is used to obtain polymeric membranes which are produced by precipitation from a polymer solution, allowing morphological modification from changes made in the parameters used during the membranes preparation 12 .…”
Section: Introductionmentioning
confidence: 99%
“…Typically, backpulsing is used with a relatively high frequency, ranging from every second (Levesley and Hoare 1999) to every minute (Srijaroonrat et al 1999). However, the expected frequency for backpulsing in the WTP crossflow filters ranges from every hour to every 12 hours.…”
Section: Pnnl Efforts To Model Flux Time Dependencementioning
confidence: 99%