کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
593152 1453933 2014 10 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Modeling of the initial deposition of individual particles during the cross-flow membrane filtration
ترجمه فارسی عنوان
مدل سازی رسوب اولیه ذرات فردی در طی فیلتراسیون غشاء جریان متقاطع
کلمات کلیدی
مدل سازی رسوب ذرات، فوران غشاء، مسیر عبور ذرات، حرکت براونیا، تعامل قطبی مدفوع
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی شیمی کلوئیدی و سطحی
چکیده انگلیسی

This study is devoted to the modeling of the deposition of individual particles onto a clean membrane surface in cross-flow filtration systems. Comprehensive force analysis approach is applied, which accounts for the random Brownian force and the polar component of the particle–membrane interactive forces. The inclusion of the polar interactive force is important in that when a hydrophilic membrane is involved, it can easily predominate over the rest of lateral forces in the near-field. The repulsive polar particle–membrane interaction can greatly decrease the stability of the particle on the membrane surface. In the far-field that is about 0.1 μm or farther away from the membrane, the particle transport is primarily dictated by the hydrodynamic lift and drag forces and the Brownian force. In sharp contrast to semi- or non-Brownian particles, the transport trajectory of Brownian particle is hardly definitive. The filtration flux and the cross-flow velocity can influence the particle transport trajectory of all sizes. Nevertheless, the existence of critical flux or critical cross-flow velocity is more evident for non-Brownian particles. Above the critical cross-flow rate or below the critical flux, particle deposition is minimized. Under appropriate operational conditions, a force-balanced level exists in the viscous sub-layer for a particular particle size, which is independent of the initial position of the particle. The model can be expanded further for more complicated water filtration conditions.

The particle within the viscous sub-layer may be exerted by three groups of forces, which include hydrodynamic forces (drag forces and lift force, fTD, fD and fL), inherent force (the random Brownian force, fB) and interfacial forces (hydrophobic force, fHP, and electrostatic force, fEL). The particle transport trajectories can be simulated. Under otherwise identical conditions, there exists a critical flux for a non-Brownian particle, above which the particle will be transported to and attached on the membrane surface, causing particle deposition.Figure optionsDownload as PowerPoint slideHighlights
► Comprehensive force analysis was conducted on initial particle deposition on membrane.
► Semi-Brownian particles are mostly likely the membrane foulants.
► The effect of hydraulic factors on the deposition of individual particles can be simulated.
► Critical flux exists for semi-Brownian and Brownian particles during water filtration.

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Colloids and Surfaces A: Physicochemical and Engineering Aspects - Volume 440, 5 January 2014, Pages 91–100
نویسندگان
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