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用于同时降解青霉素 G 和分离 TiO2 的膜可视-LED 光反应器。

Membrane vis-LED photoreactor for simultaneous penicillin G degradation and TiO2 separation.

机构信息

School of Civil and Environmental Engineering, Nanyang Technological University, 50 Nanyang Avenue, Singapore 639798, Singapore.

出版信息

Water Res. 2012 Apr 15;46(6):1825-37. doi: 10.1016/j.watres.2011.12.057. Epub 2012 Jan 3.

Abstract

The hybrid membrane photoreactor (MPR) combining a photoreactor irradiated with visible-light-emitting diode (vis-LED) and a cross-flow microfiltration (MF) membrane module was investigated in both closed-loop and continuous flow-through modes for the simultaneous degradation of penicillin G (PG) and separation of visible-light responsive TiO(2) particles, namely C-sensitized-N-doped TiO(2) (T300) and C-N-S tridoped TiO(2) (T0.05-450). The turbidity of permeate water was <0.2 NTU for both T300 and T0.05-450 suspensions in the MPR system operated at different transmembrane pressures (TMPs) and cross-flow velocities (CFVs), indicating effective separation of TiO(2) particles by the MF membrane. The operations at a higher TMP or lower CFV were more prone to induce TiO(2) deposition on the membrane surface without backwashing, which resulted in the membrane fouling, the loss of TiO(2) from the photoreactor and the decrease of PG photocatalytic degradation efficiency. 75% and 84% of PG were degraded in the closed-loop MPR without backwashing operated at 10 kPa and 0.15 m s(-1) after 4 h of vis-LED irradiation using 1.0 g L(-1) of T300 and T0.05-450, respectively. With backwashing of the membrane, the PG photocatalytic degradation efficiencies in the closed-loop MPR could be significantly enhanced to achieve 93% and 95% using 1.0 g L(-1) of T300 and T0.05-450, respectively, which were almost comparable to those achieved in the batch photoreactor. Due to its shorter hydraulic residence time in the photoreactor, the PG degradation efficiency in the continuous flow-through MPR with backwashing was lower than that achieved in the closed-loop MPR.

摘要

将可见光发光二极管(vis-LED)照射的光反应器与错流微滤(MF)膜组件相结合的混合膜光反应器(MPR)在闭路和连续流通两种模式下进行了研究,用于同时降解青霉素 G(PG)和分离可见光响应 TiO2 颗粒,即 C 敏化 N 掺杂 TiO2(T300)和 C-N-S 三掺杂 TiO2(T0.05-450)。在不同跨膜压力(TMP)和错流速度(CFV)下操作的 MPR 系统中,对于 T300 和 T0.05-450 悬浮液,透过水的浊度均<0.2 NTU,表明 MF 膜可有效分离 TiO2 颗粒。在不反冲洗的情况下,较高 TMP 或较低 CFV 操作更容易导致 TiO2 在膜表面沉积,从而导致膜污染、TiO2 从光反应器中损失以及 PG 光催化降解效率下降。在没有反冲洗的闭路 MPR 中,使用 1.0 g L-1 的 T300 和 T0.05-450 ,在 vis-LED 照射 4 小时后,在 10 kPa 和 0.15 m s-1 下分别可降解 75%和 84%的 PG。通过膜反冲洗,可显著提高闭路 MPR 中的 PG 光催化降解效率,使用 1.0 g L-1 的 T300 和 T0.05-450 时,可分别达到 93%和 95%,几乎可与批式光反应器相媲美。由于在光反应器中的水力停留时间较短,反冲洗后的连续流通 MPR 中的 PG 降解效率低于闭路 MPR。

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