Difference between revisions of "Main Page"
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− | <slideshow sequence="random" transition="fade" refresh=" | + | <slideshow sequence="random" transition="fade" refresh="5000"> |
[[File:WH Picture1.JPG|thumb|center|x350px|link=Dispersion and Diffusion|Molecular diffusion slowly transports solutes into clay-rich, lower permeability zones]] | [[File:WH Picture1.JPG|thumb|center|x350px|link=Dispersion and Diffusion|Molecular diffusion slowly transports solutes into clay-rich, lower permeability zones]] | ||
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*[[Dispersion and Diffusion]] | *[[Dispersion and Diffusion]] | ||
*[[Metals and Metalloids - Mobility in Groundwater | Mobility of Metals and Metalloids]] | *[[Metals and Metalloids - Mobility in Groundwater | Mobility of Metals and Metalloids]] | ||
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*[[pH Buffering in Aquifers]] | *[[pH Buffering in Aquifers]] | ||
*[[Sorption of Organic Contaminants]] | *[[Sorption of Organic Contaminants]] | ||
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**[[Geophysical Methods - Case Studies | Case Studies]] | **[[Geophysical Methods - Case Studies | Case Studies]] | ||
*[[Groundwater Sampling - No-Purge/Passive]] | *[[Groundwater Sampling - No-Purge/Passive]] | ||
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*[[Long-Term Monitoring (LTM)|Long-Term Monitoring (LTM)]] | *[[Long-Term Monitoring (LTM)|Long-Term Monitoring (LTM)]] | ||
**[[Long-Term Monitoring (LTM) - Data Analysis | LTM Data Analysis]] | **[[Long-Term Monitoring (LTM) - Data Analysis | LTM Data Analysis]] | ||
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*[[In Situ Treatment of Contaminated Sediments with Activated Carbon]] | *[[In Situ Treatment of Contaminated Sediments with Activated Carbon]] | ||
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+ | <u>'''[[Light Non-Aqueous Phase Liquids (LNAPLs)]]'''</u> | ||
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+ | *[[LNAPL Conceptual Site Models]] | ||
+ | *[[LNAPL Remediation Technologies]] | ||
+ | *[[NAPL Mobility]] | ||
<u>'''[[Munitions Constituents]]'''</u> | <u>'''[[Munitions Constituents]]'''</u> | ||
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*[[Injection Techniques - Viscosity Modification]] | *[[Injection Techniques - Viscosity Modification]] | ||
*[[Landfarming]] | *[[Landfarming]] | ||
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*[[Metal and Metalloids - Remediation | Remediation of Metals and Metalloids]] | *[[Metal and Metalloids - Remediation | Remediation of Metals and Metalloids]] | ||
*[[Remediation Performance Assessment at Chlorinated Solvent Sites]] | *[[Remediation Performance Assessment at Chlorinated Solvent Sites]] | ||
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*[[N-nitrosodimethylamine (NDMA)]] | *[[N-nitrosodimethylamine (NDMA)]] | ||
*[[Perchlorate|Perchlorate]] | *[[Perchlorate|Perchlorate]] | ||
− | *[[Perfluoroalkyl and Polyfluoroalkyl Substances (PFAS) | + | *[[Perfluoroalkyl and Polyfluoroalkyl Substances (PFAS)]] |
*[[Petroleum Hydrocarbons (PHCs)]] | *[[Petroleum Hydrocarbons (PHCs)]] | ||
*[[Polycyclic Aromatic Hydrocarbons (PAHs)]] | *[[Polycyclic Aromatic Hydrocarbons (PAHs)]] |
Revision as of 16:01, 17 September 2020
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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: Sustainable RemediationHigh-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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