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#contaminant removal

2 public questions tagged with this topic.

Phytovolatilization involves:

Phytovolatilization constitutes specialized phytoremediation pathway where selected plants absorb contaminants that are volatile in their native form or can be enzymatically transformed into volatile derivatives, translocate upward via xylem driven by transpiration pull generating negative pressure minus 1 to 2 MPa, and release through stomatal conductance into atmosphere as less toxic gaseous species. Classic illustrations include selenium taken up as selenate via sulfate transporters Sultr in Brassica juncea, metabolized through cysteine synthase to selenocysteine, methylated by selenocysteine methyltransferase to methyl selenocysteine and further converted to dimethyl selenide, dimethyl diselenide volatile compounds emitted 10 to 100 micrograms per square meter per day, elemental mercury taken up as Hg2+ and reduced by bacterial merA mercuric reductase expressed in transgenic poplar to elemental Hg0 vapor with high Henry's constant, and trichloroethylene oxidized by cytochrome P450 2E1 then transpired as chlorinated metabolites. High transpiration rate 10 to 100 liters per day per mature phreatophyte tree generates large water flux facilitating contaminant mass flow. Although atmospheric dilution reduces immediate risk near ground, regulatory acceptance controversial because pollutant transferred rather than destroyed, necessitating atmospheric dispersion modeling, risk assessment and air monitoring to avoid local hotspots. Distinguished from accumulation in roots or rhizosphere microbial degradation.

Ref: Pilon-Smits 2005 Selenium volatilization; Terry et al. Environmental Science Technology selenium; EPA phytovolatilization evaluation.

Bioslurping is effective for removal of:

Bioslurping represents hybrid technology merging vacuum-enhanced free product recovery with bioventing to address sites where light non-aqueous phase liquid LNAPL such as gasoline, diesel and jet fuel accumulates as floating layer 2 to 100 centimeter thick on top of water table, serving as persistent secondary source dissolving into groundwater. Technique deploys adjustable slurp tube inside well connected to high-vacuum blower generating 20 to 30 inches mercury, extracting groundwater, free-phase hydrocarbon and soil vapor simultaneously through same conduit via Venturi effect; liquid rises into knockout separator where LNAPL skimmed for off-site recycling or disposal while water treated via air stripping or carbon adsorption. High vacuum expands capture zone radius 10 to 30 feet enhancing mobility of floating product toward extraction well through increased hydraulic gradient. Concurrent soil gas extraction induces airflow through smear zone stimulating aerobic biodegradation of residual sorbed phase via alkB bearing microbes, polishing source zone after bulk liquid removal. Unlike heavy metal or chlorinated solvent DNAPLs denser than water, floating hydrocarbons uniquely amenable because they reside at air-water interface accessible to slurp tube. Pilot tests measuring transmissivity and product thickness determine viability versus dual-phase extraction.

Ref: EPA Bioslurping Fact Sheet 1996; Afentoulis et al. Remediation Journal 1996 bioslurp effectiveness; US Army Corps design guide.