Performance of Reverse Osmosis and Nanofiltration in the Removal of Fluoride from Model Water and Metal Packaging Industrial Effluent

2014 ◽  
Vol 49 (8) ◽  
pp. 1135-1145 ◽  
Author(s):  
Imen Bejaoui ◽  
Amine Mnif ◽  
Béchir Hamrouni
2017 ◽  
Vol 2017 ◽  
pp. 1-10 ◽  
Author(s):  
Amine Mnif ◽  
Imen Bejaoui ◽  
Meral Mouelhi ◽  
Béchir Hamrouni

Nanofiltration and reverse osmosis are investigated as a possible alternative to the conventional methods of Cr(VI) removal from model water and industrial effluent. The influences of feed concentration, water recovery, pH, and the coexisting anions were studied. The results have shown that retention rates of hexavalent chromium can reach 99.7% using nanofiltration membrane (NF-HL) and vary from 85 to 99.9% using reverse osmosis membrane (RO-SG) depending upon the composition of the solution and operating conditions. This work was also extended to investigate the separation of Cr(VI) from car shock absorber factory effluent. The use of these membranes is very promising for Cr(VI) water treatment and desalting industry effluent. Spiegler-Kedem model was applied to experimental results in the aim to determine phenomenological parameters, the reflection coefficient of the membrane (σ), and the solute permeability coefficient (Ps). The convective and diffusive parts of the mass transfer were quantified with predominance of the diffusive contribution.


Desalination ◽  
1999 ◽  
Vol 126 (1-3) ◽  
pp. 219-226 ◽  
Author(s):  
Antonio Pérez Padilla ◽  
Eduardo L. Tavani

2020 ◽  
Vol 82 (11) ◽  
pp. 2259-2270
Author(s):  
Shaik Nazia ◽  
Sugali Chandra Sekhar ◽  
Veeriah Jegatheesan ◽  
Suresh K. Bhargava ◽  
Sundergopal Sridhar

Abstract The goal of the present study is to treat industrial wastewater containing sodium aluminate using a chemically inert polyurea (PU) based thin film composite (TFC) reverse osmosis (RO) membrane to promote water reclamation and zero liquid discharge (ZLD). Pretreatment was carried out to reduce the pH of the effluent from 12.5 to 7.1. The TFC RO membrane was fabricated by coating PU on Polyethersulfone (PES) substrate by interfacial polymerization (IP). The surface and cross-sectional morphologies of the membrane were characterized using scanning electron microscopy (SEM). The indigenously synthesized membrane was effective in the removal of total dissolved solids (TDS), chemical oxygen demand (COD), colour and electrical conductivity. The experiments were conducted by varying the feed composition of the wastewater. The maximum water recovery and flux were found to be 74% and 73.9 L/m2·h. RO process using PU membrane exhibited significant potential for cost effective, safe and pollution-free treatment of sodium aluminate industrial effluent.


2003 ◽  
Vol 78 (10) ◽  
pp. 1061-1067 ◽  
Author(s):  
Sundergopal Sridhar ◽  
K Krishna Prasad ◽  
G Suryanarayana Murthy ◽  
A Gangagni Rao ◽  
Asad Ali Khan

2018 ◽  
Vol 15 (30) ◽  
pp. 305-312
Author(s):  
L. KERBER ◽  
P. MARIOTTI ◽  
L. VOGNACH ◽  
J. A. TASSINARY ◽  
S. STULP

Due to population growth, there is an increase in the tendency of water resource degradation. One of the biggest polluters is the practice of dumping industrial and domestic effluents without any treatment on the watercourse. The utilization of effluents is an alternative to minimize the inadequate waste dump, thus avoiding the overload on the treatment system as well as cutting down costs and expenses. This work’s objective is to evaluate the application of reverse osmosis in a food industrial effluent, in physicochemical and toxicological terms. A reverse osmosis technical application was conducted and then the effluent was examined, before and afterward, in terms of pH, Turbidity, Colouring, Conductivity, Dissolved Oxygen, Total Organic Carbon, and Total Nitrogen as well as a toxicological evaluation (Allium cepa). According to the obtained result, it can be identified that the technique of reverse osmosis showed treatment efficiency when applied to the effluent containing coloring and soy isoflavones, with regards to the physicals and chemical evaluation. In terms of toxicological evaluation, with respect to the radicular development, the treated effluent (permeate) showed a radicular growth, once the raw effluent did not develop any root.


1992 ◽  
Vol 25 (10) ◽  
pp. 291-298 ◽  
Author(s):  
C. J. Brouckaert ◽  
C. A. Buckley

A computer model, based on the equations formulated by Sourirajan and Matsuura (1985), has been used to analyse data generated by a tubular reverse osmosis (TRO) pilot-plant treating a cooling-tower blow-down stream at Lethabo power station near Sasolburg, South Africa. These data, covering more than 3 000 hours of operation over a period of 10 months, were examined in terms of the variation of modelling parameters, as determined by regression, with time. This transformation of the data has yielded valuable insight into the effect of the plant's operating history on the condition of the membranes. Furthermore, using the model to simulate the operation of a full-scale plant has made it possible to explore some of the implications that the pilot-plant measurements hold for an eventual design. Simulation is not yet able to substitute for pilot-plant investigation, particularly in cases of complex and/or fouling streams such as are often encountered in industrial effluent treatment applications, but may be used.very effectively to enhance the quality of information gained from such studies.


Author(s):  
H. K. Plummer ◽  
E. Eichen ◽  
C. D. Melvin

Much of the work reported in the literature on cellulose acetate reverse osmosis membranes has raised new and important questions with regard to the dense or “active” layer of these membranes. Several thickness values and structures have been attributed to the dense layer. To ensure the correct interpretation of the cellulose acetate structure thirteen different preparative techniques have been used in this investigation. These thirteen methods included various combinations of water substitution, freeze drying, freeze sectioning, fracturing, embedding, and microtomy techniques with both transmission and scanning electron microscope observations.It was observed that several factors can cause a distortion of the structure during sample preparation. The most obvious problem of water removal can cause swelling, shrinking, and folds. Improper removal of embedding materials, when used, can cause a loss of electron image contrast and, or structure which could hinder interpretation.


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