2017
DOI: 10.1016/j.seppur.2017.07.013
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A novel ultrafiltration grade nickel iron oxide doped hollow fiber mixed matrix membrane: Spinning, characterization and application in heavy metal removal

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Cited by 67 publications
(21 citation statements)
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“…The α value was also measured (α= 1.68) according to Eq. (2): Α = 2 n/4 = 2 3/4 = 1.68 (2) where n represents the number of independent variables. Water flux (L/m 2 h or LMH) and chromium removal efficiency (%) were considered as the dependent variables (responses).…”
Section: Experimental Designmentioning
confidence: 99%
See 1 more Smart Citation
“…The α value was also measured (α= 1.68) according to Eq. (2): Α = 2 n/4 = 2 3/4 = 1.68 (2) where n represents the number of independent variables. Water flux (L/m 2 h or LMH) and chromium removal efficiency (%) were considered as the dependent variables (responses).…”
Section: Experimental Designmentioning
confidence: 99%
“…In many countries, especially developing countries, significant amounts of heavy metals enter the environment through industrial activities either directly or indirectly (1,2). The most common heavy metals in industrial wastewater include arsenic, chromium, lead, cadmium, copper, nickel, and zinc, which are hazardous to human and environmental health (3)(4)(5).…”
Section: Introductionmentioning
confidence: 99%
“…Membrane-based filtration technologies like reverse osmosis (RO) and nanofiltration (NF) have some advantages like high efficiency and ease of use [13], and have been extensively applied for the removal of heavy metals. In spite of the high efficiency Zohreh Naghdali of RO and NF in heavy metal rejection, they often have to cope with membrane fouling and high hydraulic pressure [14,15].…”
Section: Introductionmentioning
confidence: 99%
“…Thus, the idea of membranes having both polymeric substrate as well as inorganic filler came in existence, which can overcome the above-mentioned limitations to a large extent. There are different studies having various fillers like Fe 3 O 4 nanoparticles (Alam et al 2013;Chan et al 2015;Ghaemi et al 2015;Bagheripour et al 2016;Mondal et al 2017), oxidized multiwalled nanotubes (Yin et al 2013;Celik et al 2011a, b), TiO 2 nanoparticles (Luo et al 2005;Rahimpour et al 2012;Esfahani et al 2015;Mbuli et al 2018;Farahani and Vatanpour 2018), functionalized MWCNT (Qiu et al 2009;Liu et al 2018;Benally et al 2018;Ho et al 2017;Lee et al 2016), silver nanoparticles (Taurozzi et al 2008;Zhang et al 2012;Sonawane et al 2017), modified silica nanoparticle (Farahani and Vatanpour 2018;Huang et al 2017;Martín et al 2016), chitosan/zinc oxide nanoparticles (Munnawar et al 2017;Ahmad et al 2017;Elizalde et al 2018), beta cyclodextrin-polyurethane (Adams et al 2014), graphene oxide (Ho et al 2017;Chai et al 2017;Karim et al 2017;Mukherjee et al 2016;Karkooti et al 2018), manganese oxide and alumina nanoparticles (Delavara et al 2017;Gohari et al 2014), zeolites (Liu et al 2014;Grabczyk et al 2017;Amiri et al 2017), attapulgite…”
Section: Introductionmentioning
confidence: 99%
“…However, membrane-based separations of these metals are becoming most efficient because of the cost-effectiveness, lesser energy consumption, thermal and mechanical stability, large surface area, and better selectivity (Delavara et al 2017). Different studies are there in which mixed-matrix membranes are employed for the removal of heavy metals (Chan et al 2015;Ghaemi et al 2015;Mondal et al 2017;Mbuli et al 2018;Delavara et al 2017;Hosseini et al 2017;Gupta et al 2015;Shah and Murthy 2013). However, there is no correlation between the membrane performance and the type of filler or the morphology.…”
Section: Introductionmentioning
confidence: 99%