Seawater pretreatment by continuous sand filter for seawater RO (reverse osmosis) desalination plant
Seawater pretreatment by continuous sand filter for seawater RO (reverse osmosis) desalination plant
- Book Chapter
7
- 10.1007/978-1-4615-3548-5_24
- Jan 1, 1992
Selected Applications
- Research Article
6
- 10.1016/0011-9164(89)85040-4
- Jan 1, 1989
- Desalination
Conventional pretreatment of surface seawater for reverse osmosis application, state of the art
- Research Article
17
- 10.1016/j.desal.2008.12.008
- Sep 3, 2009
- Desalination
Hybrid filtration method for pre-treatment of seawater reverse osmosis (SWRO)
- Research Article
18
- 10.1016/j.rser.2012.09.022
- Nov 1, 2012
- Renewable and Sustainable Energy Reviews
Waste energy recovery in seawater reverse osmosis desalination plants. Part 1: Review
- Research Article
118
- 10.1016/s0376-7388(03)00217-5
- Aug 5, 2003
- Journal of Membrane Science
Ion-exchange membrane electrodialytic salt production using brine discharged from a reverse osmosis seawater desalination plant
- Research Article
9
- 10.1007/s11814-014-0356-0
- Mar 17, 2015
- Korean Journal of Chemical Engineering
Our aim was to analyze, monitor, and predict the outcomes of processes in a full-scale seawater reverse osmosis (SWRO) desalination plant using multivariate statistical techniques. Multivariate analysis of variance (MANOVA) was used to investigate the performance and efficiencies of two SWRO processes, namely, pore controllable fiber filter-reverse osmosis (PCF-SWRO) and sand filtration-ultra filtration-reverse osmosis (SF-UF-SWRO). Principal component analysis (PCA) was applied to monitor the two SWRO processes. PCA monitoring revealed that the SF-UF-SWRO process could be analyzed reliably with a low number of outliers and disturbances. Partial least squares (PLS) analysis was then conducted to predict which of the seven input parameters of feed flow rate, PCF/SF-UF filtrate flow rate, temperature of feed water, turbidity feed, pH, reverse osmosis (RO)flow rate, and pressure had a significant effect on the outcome variables of permeate flow rate and concentration. Root mean squared errors (RMSEs) of the PLS models for permeate flow rates were 31.5 and 28.6 for the PCF-SWRO process and SF-UF-SWRO process, respectively, while RMSEs of permeate concentrations were 350.44 and 289.4, respectively. These results indicate that the SF-UF-SWRO process can be modeled more accurately than the PCF-SWRO process, because the RMSE values of permeate flowrate and concentration obtained using a PLS regression model of the SF-UF-SWRO process were lower than those obtained for the PCF-SWRO process.
- Research Article
13
- 10.1016/j.desal.2023.117180
- Nov 28, 2023
- Desalination
ANN based-model for estimating the boron permeability coefficient as boric acid in SWRO desalination plants using ensemble-based machine learning
- Research Article
16
- 10.1080/19443994.2014.940653
- Jul 18, 2014
- Desalination and Water Treatment
Influence of site-specific parameters on environmental impacts of desalination
- Research Article
87
- 10.1016/j.renene.2013.11.050
- Dec 8, 2013
- Renewable Energy
Environmental life cycle assessment of seawater reverse osmosis desalination plant powered by renewable energy
- Research Article
85
- 10.1016/j.desal.2008.12.023
- Sep 3, 2009
- Desalination
Artificial neural network model for optimizing operation of a seawater reverse osmosis desalination plant
- Research Article
27
- 10.1016/j.desal.2022.116094
- Sep 9, 2022
- Desalination
Fouling control in SWRO desalination during harmful algal blooms: A historical review and future developments
- Research Article
4
- 10.1080/19443994.2015.1106095
- Oct 28, 2015
- Desalination and Water Treatment
Energy consumption assessment of 4,000 m3/d SWRO desalination plants
- Research Article
40
- 10.1016/j.desal.2016.09.032
- Oct 8, 2016
- Desalination
Exergo-economic analysis of a seawater reverse osmosis desalination plant with various retrofit options
- Research Article
2
- 10.1080/19443994.2013.780791
- Sep 1, 2013
- Desalination and Water Treatment
Economic feasibility study for MF system as a pretreatment of SWRO in test bed desalination plant
- Research Article
1
- 10.3390/microorganisms10040682
- Mar 22, 2022
- Microorganisms
This pilot study investigates the formation of aggregates within a desalination plant, before and after pre-treatment, as well as their potential impact on fouling. The objective is to provide an understanding of the biofouling potential of the feed water within a seawater reverse osmosis (SWRO) desalination plant, due to the limited removal of fouling precursors. The 16S and 18S rRNA was extracted from the water samples, and the aggregates and sequenced. Pre-treatment systems, within the plant remove < 5 µm precursors and organisms; however, smaller size particles progress through the plant, allowing for the formation of aggregates. These become hot spots for microbes, due to their nutrient gradients, facilitating the formation of niche environments, supporting the proliferation of those organisms. Aggregate-associated organisms are consistent with those identified on fouled SWRO membranes. This study examines, for the first time, the factors supporting the formation of aggregates within a desalination system, as well as their microbial communities and biofouling potential.
- Research Article
62
- 10.1016/j.desal.2006.02.018
- Jan 24, 2007
- Desalination
A 13.3 MGD seawater RO desalination plant for Yanbu Industrial City
- Research Article
9
- 10.1016/j.desal.2013.03.019
- Apr 20, 2013
- Desalination
Reflection of the structural distinctions of source—different humic substances on organic fouling behaviors of SWRO membranes
- Conference Article
- 10.1109/ccdc.2014.6852628
- May 1, 2014
The rescheduling problem of seawater reverse osmosis (SWRO) desalination plant under uncertain freshwater demand is studied. A rescheduling model of this problem is built, which is a bi-objective optimization with criterions of efficiency and stability. A rolling horizon scheduling (RHS) procedure is used to solve this problem. The framework of RHS is structured. A differential evolution (DE) algorithm is used to compute the solution, and its steps are described. The simulation results of a large-scale SWRO desalination plant with fluctuations in freshwater demand show that the performance of RHS is satisfied.
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