Difference between revisions of "Main Page"
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**[[Vapor Intrusion - Separation Distances from Petroleum Sources]] | **[[Vapor Intrusion - Separation Distances from Petroleum Sources]] | ||
**[[Vapor Intrusion – Sewers and Utility Tunnels as Preferential Pathways|Vapor Intrusion - Sewers and Utility Tunnels as Preferential Pathways]] | **[[Vapor Intrusion – Sewers and Utility Tunnels as Preferential Pathways|Vapor Intrusion - Sewers and Utility Tunnels as Preferential Pathways]] | ||
+ | **[[Assessing Vapor Intrusion (VI) Impacts in Neighborhoods with Groundwater Contaminated by Chlorinated Volatile Organic Chemicals (CVOCs)|Vapor Intrusion - Assessing VI Impacts in Neighborhoods with Groundwater Contaminated CVOCs]] | ||
<u>'''[[Characterization, Assessment & Monitoring]]'''</u> | <u>'''[[Characterization, Assessment & Monitoring]]'''</u> | ||
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*[[PFAS Transport and Fate]] | *[[PFAS Transport and Fate]] | ||
*[[PFAS Treatment by Electrical Discharge Plasma]] | *[[PFAS Treatment by Electrical Discharge Plasma]] | ||
− | *[[Photoactivated Reductive Defluorination - PFAS Destruction|Photoactivated Reductive Defluorination]] | + | *[[Photoactivated Reductive Defluorination - PFAS Destruction|Photoactivated Reductive Defluorination]] |
<u>'''[[Regulatory Issues and Site Management]]'''</u> | <u>'''[[Regulatory Issues and Site Management]]'''</u> |
Revision as of 20:48, 22 July 2024
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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: Photoactivated Reductive Defluorination - PFAS DestructionHigh-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.
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