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| id="mp-left" class="MainPageBG" style="width:55%; padding:0; vertical-align:top; color:#000;" | | | id="mp-left" class="MainPageBG" style="width:55%; padding:0; vertical-align:top; color:#000;" | | ||
| − | <h2 id="mp-tfa-h2" style="margin:0.5em; background:#cef2e0; font-family:inherit; font-size:120%; font-weight:bold; border:1px solid #a3bfb1; color:#000; padding:0.2em 0.4em;"> Featured article: | + | <h2 id="mp-tfa-h2" style="margin:0.5em; background:#cef2e0; font-family:inherit; font-size:120%; font-weight:bold; border:1px solid #a3bfb1; color:#000; padding:0.2em 0.4em;"> Featured article: Reverse Osmosis and Nanofiltration Membrane Filtration Systems for PFAS Removal</h2> |
| − | <div id="mp-tfa" style="padding:0.0em 1.0em;">[[File: | + | <div id="mp-tfa" style="padding:0.0em 1.0em;">[[File:RichardsonFig1.png|400px|left|link=Reverse Osmosis and Nanofiltration Membrane Filtration Systems for PFAS Removal]]<dailyfeaturedpage></dailyfeaturedpage> |
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*[[Passive Sampling of Munitions Constituents|Passive Sampling]] | *[[Passive Sampling of Munitions Constituents|Passive Sampling]] | ||
*[[Munitions Constituents – Photolysis |Photolysis]] | *[[Munitions Constituents – Photolysis |Photolysis]] | ||
| + | *[[Remediation of Stormwater Runoff Contaminated by Munition Constituents |Remediation of Stormwater Runoff ]] | ||
*[[Munitions Constituents – Sample Extraction and Analytical Techniques|Sample Extraction and Analytical Techniques]] | *[[Munitions Constituents – Sample Extraction and Analytical Techniques|Sample Extraction and Analytical Techniques]] | ||
*[[Munitions Constituents - Soil Sampling |Soil Sampling]] | *[[Munitions Constituents - Soil Sampling |Soil Sampling]] | ||
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*[[PFAS Soil Remediation Technologies]] | *[[PFAS Soil Remediation Technologies]] | ||
*[[PFAS Sources]] | *[[PFAS Sources]] | ||
| + | *[[PFAS Toxicology and Risk Assessment]] | ||
*[[PFAS Transport and Fate]] | *[[PFAS Transport and Fate]] | ||
*[[PFAS Treatment by Electrical Discharge Plasma]] | *[[PFAS Treatment by Electrical Discharge Plasma]] | ||
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*[[Transition of Aqueous Film Forming Foam (AFFF) Fire Suppression Infrastructure Impacted by Per and Polyfluoroalkyl Substances (PFAS)| Transition of Aqueous Film Forming Foam Fire Suppression Infrastructure Impacted by Per and Polyfluoroalkyl Substances]] | *[[Transition of Aqueous Film Forming Foam (AFFF) Fire Suppression Infrastructure Impacted by Per and Polyfluoroalkyl Substances (PFAS)| Transition of Aqueous Film Forming Foam Fire Suppression Infrastructure Impacted by Per and Polyfluoroalkyl Substances]] | ||
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<u>'''[[Regulatory Issues and Site Management]]'''</u> | <u>'''[[Regulatory Issues and Site Management]]'''</u> | ||
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*[[Sustainable Remediation]] | *[[Sustainable Remediation]] | ||
| − | + | <u>'''[[Remediation Technologies]]'''</u> | |
*[[Amendment Distribution in Low Conductivity Materials]] | *[[Amendment Distribution in Low Conductivity Materials]] | ||
*[[Bioremediation - Anaerobic|Anaerobic Bioremediation]] | *[[Bioremediation - Anaerobic|Anaerobic Bioremediation]] | ||
Latest revision as of 14:39, 4 November 2025
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| The goal of ENVIRO Wiki is to make scientific and engineering research results more accessible to environmental professionals, facilitating the permitting, design and implementation of environmental projects. Articles are written and edited by invited experts (see Contributors) to summarize current knowledge for the target audience on an array of topics, with cross-linked references to reports and technical literature. | See Table of Contents |
Featured article: Reverse Osmosis and Nanofiltration Membrane Filtration Systems for PFAS RemovalHigh-pressure membrane filtration such as nanofiltration (NF) or reverse osmosis (RO) is a filtration process that separates dissolved inorganic and organic solutes from liquid solvents, typically water. As opposed to porous and more permeable low-pressure membranes (i.e., microfiltration and ultrafiltration), NF and RO membranes are widely considered semi-permeable and therefore require higher operating pressures to force water against an osmotic gradient to produce a purified permeate stream. NF and RO systems are separation processes that yield two streams: the treated permeate and the concentrated retentate. Typical parameters used to describe operational performance of high-pressure membrane systems include solvent recovery and solute rejection. Recovery is defined as the percentage of feed water that becomes permeate. Solute rejection is defined as the percent of concentrated feed water retained by the membrane. Significant advancements in membrane material development have led to development of NF and RO membranes with varying pressure requirements and solute rejection characteristics.
(Full article...)
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