Comparison of nanofiltration efficiency with GAC adsorption and air stripping processes for CHCl3 removal from Tehran drinking water

2009 ◽  
Vol 58 (4) ◽  
pp. 285-290 ◽  
Author(s):  
M. T. Samadi ◽  
S. Nasseri ◽  
A. R. Mesdaghinea ◽  
M. R. Alizadehfard
1998 ◽  
Vol 37 (10) ◽  
pp. 135-146 ◽  
Author(s):  
Akira Yuasa

Microfiltration (MF) and ultrafiltration (UF) pilot plants were operated to produce drinking water from surface water from 1992 to 1996. Microfiltration was combined with pre-coagulation by polyaluminium chloride and was operated in a dead-end mode using hollow fiber polypropylene and monolith type ceramic membranes. Ultrafiltration pilot was operated in both cross-flow and dead-end modes using hollow fiber cellulose acetate membrane and was combined occasionally with powdered activated carbon (PAC) and granular activated carbon (GAC) adsorption. Turbidity in the raw water varied in the range between 1 and 100 mg/L (as standard Kaolin) and was removed almost completely in all MF and UF pilot plants to less than 0.1 mg/L. MF and UF removed metals such as iron, manganese and aluminium well. The background organics in the river water measured as KMnO4 demand varied in the range between 3 and 16 mg/L. KMnO4 demand decreased to less than 2 mg/L and to less than 3 mg/L on the average by the coagulation-MF process and the sole UF process, respectively. Combination of PAC or GAC adsorption with UF resulted in an increased removal of the background organics and the trihalomethanes formation potential as well as the micropollutants such as pesticides. Filtration flux was controlled in the range between 1.5 and 2.5 m/day with the trans-membrane pressure less than 100 kPa in most cases for MF and UF. The average water recovery varied from 99 to 85%.


Desalination ◽  
2007 ◽  
Vol 210 (1-3) ◽  
pp. 215-224 ◽  
Author(s):  
K.G. Babi ◽  
K.M. Koumenides ◽  
A.D. Nikolaou ◽  
C.A. Makri ◽  
F.K. Tzoumerkas ◽  
...  

2001 ◽  
Vol 1 (4) ◽  
pp. 19-24
Author(s):  
J.-M. Laîne ◽  
K. Glucina ◽  
L. Malleret ◽  
A. Bruchet ◽  
I. Baudin ◽  
...  

The occurrence of tastes and odours (T&O) in potable water is considered one of the main problems by the drinking water companies. Thus, several treatment processes have been developed over the years to control T&O, including air stripping, activated carbon and oxidation using ozone. However, little information is available in the literature on the use of membranes for T&O removal. Therefore, the objective of this paper is to present potential of membrane processes for the removal of taste and odour-causing compounds. Several membranes were tested including ultrafiltration (UF), UF combined with powdered activated carbon (PAC), nanofiltration (NF) and low pressure reverse osmosis (LP RO) membranes. Combination of UF with PAC was found to be effective for T&O control. The use of NF or LP RO is still unclear in the objective of T&O control.


2004 ◽  
Vol 54 (5) ◽  
pp. 529-539 ◽  
Author(s):  
Balaji Ramakrishnan ◽  
George A. Sorial ◽  
Thomas F. Speth ◽  
Patrick Clark ◽  
Alan Zaffiro ◽  
...  

2005 ◽  
Vol 51 (6-7) ◽  
pp. 257-265 ◽  
Author(s):  
A. Bruchet ◽  
J.M. Laîné

The occurrence of tastes and odors (T&O) in drinking water is considered as one of the main problems by the drinking water companies. Thus, several treatment processes were developed over the years to control T&O including air stripping, activated carbon and oxidation using ozone. However, little information is available in the literature on the use of membranes for T&O removal. Therefore, the objectives of this paper are to present potential of membrane processes for removal of taste and odor causing compounds. Several membranes were tested including ultrafiltration (UF), UF combined with powdered activated carbon (PAC), nanofiltration (NF) and low pressure reverse osmosis (LP RO) membranes. The results of this study indicate that the combination of UF with PAC is effective for T&O control whereas the benefit of NF and LP RO remains unclear for T&O control.


Data in Brief ◽  
2018 ◽  
Vol 18 ◽  
pp. 1292-1297 ◽  
Author(s):  
Meghdad Pirsaheb ◽  
Jalil Mohammadi ◽  
Touba Khosravi ◽  
Hooshmnd Sharafi ◽  
Masoud Moradi

2013 ◽  
Vol 5 (3) ◽  
pp. 177-184

A pilot-plant study was carried out with the water supply to Athens water works filtered through a granular activated carbon (GAC) filter- adsorber. The objective of this study was to evaluate the performance of GAC for the removal from drinking water of the two main groups of disinfection by -products (DBPs), trihalomethanes (THMs) and haloacetic acids (HAAs), as well as of dissolved organic matter. The pilot treatment facility is located at the Water Treatment Plant of EYDAP in Galatsi, Athens, and was operated as a rapid gravity filter - adsorber. It was fed with chlorinated water, coming from the overflow of the sedimentation tanks, and operated continuously in parallel with a full-scale sand filter. At regular time intervals water samples were taken from both filters and analysed for THMs, HAAs and DOC. Other parameters were measured too. The operation of the GAC filter-adsorber continued until the GAC adsorption capacity for THMs and HAAs was almost exhausted. The results of the analyses showed that GAC was more effective in removing the dissolved organic matter than the smaller molecules of THMs and HAAs, fact which is in agreement with the relevant literature. GAC was also proved more effective in removing HAAs than removing THMs. The removal of THMs and the most part of the removal of HAAs and DOC must be attributed to adsorption by GAC, while that of a smaller part of DOC and HAAs may be attributed to biological activity in the filter bed, where chlorine had been totally removed by the catalytic action of the activated carbon surface.


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