Difference between revisions of "Main Page"
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[[File:WH Picture1.PNG|thumb|center|x350px|link=Dispersion and Diffusion|Molecular diffusion slowly transports solutes into clay-rich, lower permeability zones<br/><br/><br/><br/>]] | [[File:WH Picture1.PNG|thumb|center|x350px|link=Dispersion and Diffusion|Molecular diffusion slowly transports solutes into clay-rich, lower permeability zones<br/><br/><br/><br/>]] | ||
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[[File:WH Picture15.PNG|thumb|center|x350px|link=Emulsified Vegetable Oil (EVO) for Anaerobic Bioremediation|Emulsified Vegetable Oil (EVO) mixed in field during early pilot test. EVO is commonly added as a slowly fermentable substrate to stimulate the in situ anaerobic bioremediation of chlorinated solvents, explosives, perchlorate, chromate, and other contaminants<br/><br/>]] | [[File:WH Picture15.PNG|thumb|center|x350px|link=Emulsified Vegetable Oil (EVO) for Anaerobic Bioremediation|Emulsified Vegetable Oil (EVO) mixed in field during early pilot test. EVO is commonly added as a slowly fermentable substrate to stimulate the in situ anaerobic bioremediation of chlorinated solvents, explosives, perchlorate, chromate, and other contaminants<br/><br/>]] | ||
| − | [[File:WH Picture16.PNG|thumb|center|x350px|link=Vapor_Intrusion_(VI)| | + | [[File:WH Picture16.PNG|thumb|center|x350px|link=Vapor_Intrusion_(VI)|Key elements of vapor intrusion pathways<br/><br/>]] |
| − | + | [[File:WH Picture17.PNG|thumb|center|x350px|link=Sorption_of_Organic_Contaminants|Batch reactor experiments to generate points on a sorption isotherm <br/><br/>]] | |
| − | [[File:WH Picture17.PNG|thumb|center|x350px|link=Sorption_of_Organic_Contaminants| | + | [[File:WH Picture18.PNG|thumb|center|x350px|link=Metagenomics|Results for metagenomic analysis of a groundwater sample obtained from a site impacted with petroleum hydrocarbons<br/><br/>]] |
| − | + | [[File:WH Picture19.PNG|thumb|center|x350px|link=Perchlorate|Perchlorate releases and drinking water detections<br/><br/>]] | |
| + | [[File:WH Picture20.PNG|thumb|center|x350px|link=Mass_Flux_and_Mass_Discharge|Data input screen for ESTCP Mass Flux Toolkit<br/><br/>]] | ||
| + | [[File:WH Picture21.PNG|thumb|center|x350px|link=Bioremediation_-_Anaerobic_Design_Considerations|Amendment addition for biobarrier<br/><br/>]] | ||
| + | [[File:WH Picture22.PNG|thumb|center|x350px|link=Thermal_Remediation_-_Desorption|Thermal Remediation - Desorption schematic<br/><br/>]] | ||
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Revision as of 09:20, 13 May 2019
Peer Reviewed. Accessible. Written By Experts |
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| The goal of the ENVIRO.wiki is to make scientific and engineering research results more accessible to the target audience, facilitating the permitting, design and implementation of environmental projects. Articles are written and edited by invited experts (see Contributors) to summarize current knowledge for environmental professionals on an array of topics, with cross-linked references to reports and technical literature. | Table of Contents Your Environmental Information Gateway |
Featured article / Biodegradation - HydrocarbonsRemoval of Perfluoroalkyl and Polyfluoroalkyl Substances (PFAS) from impacted soils is challenging due to the modest volatility and varying properties of PFAS compounds. Thermal treatment technologies have been developed for treatment of semi-volatile compounds such as dioxins, furans, poly-aromatic hydrocarbons and poly-chlorinated biphenyls in soils at temperatures near 325°C. In controlled bench-scale testing, removal of targeted PFAS compounds to concentrations below reporting limits was demonstrated at temperatures of 400°C. Thermal treatment temperatures of at least 400°C and a holding time of 7-10 days are recommended. The energy requirement to treat typical wet soil ranges from 300 to 400 kWh per cubic yard. Extracted vapors have typically been treated using condensation and granular activated charcoal filtration, with thermal and catalytic oxidation as another option which is currently being evaluated for field scale applications.Thermal treatment of PFAS in soils is energy intensive, and the cost of that energy may be prohibitive for some clients. Also, while it often is the least costly option for complete PFAS removal when compared to excavation followed by offsite disposal or destruction, heating soil to treatment temperatures on site or in situ typically takes longer than excavation.
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