Submerged Ultrafiltration for Minimizing Energy Process of Refinery Wastewater Treatment

被引:0
|
作者
Yuliwati, Erna [1 ,2 ]
Ismail, Ahmad Fauzi [3 ]
机构
[1] Univ Bina Darma, Adv Membrane Technol Res Ctr AMTEC, Palembang 30251, Indonesia
[2] Univ Bina Darma, Fac Engn, Dept Ind Engn, Palembang 30251, Indonesia
[3] UTM, Fac Petr & Renewable Energy Engn, Skudai Johor, Malaysia
关键词
Submerged membrane ultrafiltration; refinery wastewater; economic evaluation; scale-lab model; HOLLOW-FIBER MEMBRANES; PERFORMANCE; BIOREACTOR;
D O I
10.4028/www.scientific.net/AMR.0.531
中图分类号
T [工业技术];
学科分类号
08 ;
摘要
Refinery wastewater treatment is needed especially in the oil-producing arid regions such as oil refineries due to water scarcity. One of potentially applicable process to treat refinery wastewater is a submerged membrane technology. However, the application of submerged membrane systems for industrial wastewater treatment is still in its infancy due to significant variety in wastewater composition and high operational costs. Aim of this study was to investigate ultrafiltration (UT) membrane morphology and performance for refinery produced wastewater treatment. Submerged UT bundle was equipped using polyvinylidene fluoride (PVDF) hollow fibers, which added by dispersing lithium chloride monohydrate (LiCl center dot H2O) and titanium dioxide (TiO2). The comparison of morphological and performance tests was conducted on prepared PVDF ultrafiltration membranes. Distinctive changes were observed in membrane characteristics in term of membrane wettability, tensile testing and roughness measurement. Mean pore size and surface porosity were calculated based on permeate flux. Fouling characteristics for hydrophilic PVDF hollow fibers fouled with suspended solid matter was also investigated. Mixed liquor suspended solid (MLSS) of 3 g/L and 4.5 g/L were assessed by using submerged PVDF membrane with varied air bubble flow rates. Results showed that effect of air bubbles flow rate of 2.4 ml/min increased flux, total suspended solids (TSS) and sulfide removal of 148.82 L/m(2)h, 99.82 % and 89.2%, respectively due to increase of turbulence around fibers, which exerts shear stress to minimize particles deposited on membrane surface. It was concluded that submerged ultrafiltration is an available option to minimize energy process for treating such wastewater solution.
引用
收藏
页码:531 / +
页数:3
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