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Treatment Guide

Chlorinated Solvent Remediation Services

Comprehensive strategies for treating PCE, TCE, DCE, vinyl chloride, and other chlorinated compounds using proven oxidation, reduction, and combined technologies

Treatment Technologies

Excellent
3-12 months
Ferric Iron-Activated Persulfate

Target Compounds

PCE
TCE
DCE
Vinyl Chloride
Carbon Tetrachloride
1,1,1-TCA
Chloroform

Mechanisms

  • Persulfate radical (SO₄•⁻) oxidation: 2.60V potential
  • Ferrate (Fe(VI)) oxidation: 2.20V potential
  • Direct persulfate (S₂O₈²⁻) oxidation: 2.01V potential
  • Secondary bioremediation via sulfate/iron electron acceptors

Advantages

  • Rapid oxidation with sustained biological treatment
  • Effective in all soil types including low permeability
  • No rebound - combined oxidative and reductive mechanisms
  • Single component system with integrated activator
  • No exothermic heat generation
  • Treats both dissolved and DNAPL phase

Limitations

  • Higher cost than bioremediation alone
  • Initial turbidity possible
  • Requires site characterization for dosing optimization
Excellent
12-36 months
Enhanced Reductive Dechlorination (ERD)

Target Compounds

PCE
TCE
DCE
Vinyl Chloride
1,1,1-TCA
1,1-DCA

Mechanisms

  • Sequential reductive dechlorination: PCE → TCE → DCE → VC → Ethene
  • Dehalococcoides bacteria catalyze complete dechlorination
  • Electron donors (emulsified oil, HRC) fuel anaerobic processes
  • Hydrogenolysis and dihaloelimination pathways

Advantages

  • Complete detoxification to ethene
  • Cost-effective for large plumes
  • Long-lasting treatment zones
  • Proven for high concentration DNAPL
  • Minimal site disruption

Limitations

  • Requires anaerobic conditions
  • Slow degradation of vinyl chloride without Dehalococcoides
  • May stall at DCE without bioaugmentation
  • Methane generation possible
  • Sulfate/nitrate can inhibit process
Excellent
6-24 months
Emulsified Zero-Valent Iron (EZVI)

Target Compounds

PCE
TCE
Carbon Tetrachloride
Chloroform
1,1,1-TCA

Mechanisms

  • Direct reduction via ZVI: Fe⁰ + RCl → Fe²⁺ + R⁻ + Cl⁻
  • Beta-elimination reactions
  • Catalyzed H₂ generation supports bioremediation
  • Food-grade surfactant enables ZVI distribution in low-K zones

Advantages

  • Effective in low permeability formations
  • Treats sorbed and DNAPL phase contaminants
  • Long-term reductive capacity (years)
  • IET proprietary emulsification technology
  • Synergistic chemical/biological treatment

Limitations

  • Requires subsurface mixing/injection
  • Carbonates can passivate iron surface
  • Not suitable for high sulfate environments
  • Higher installation cost
Excellent
6-18 months
Combined ZVI-Peroxide-Persulfate

Target Compounds

PCE
TCE
DCE
VC
1,4-Dioxane
Co-contaminants

Mechanisms

  • ZVI catalyzes H₂O₂ → hydroxyl radicals (OH•): 2.80V
  • Ferrous iron activates persulfate → sulfate radicals (SO₄•⁻): 2.60V
  • Residual ZVI provides long-term reductive capacity
  • Sequential oxidation then reduction prevents rebound

Advantages

  • Treats chlorinated solvents + 1,4-dioxane simultaneously
  • Most powerful oxidation: hydroxyl + sulfate radicals
  • Long-term treatment from residual ZVI
  • Prevents contaminant rebound
  • Effective on recalcitrant compounds

Limitations

  • Complex chemistry requires expertise
  • Higher material costs
  • Careful ratio optimization needed
  • May produce temporary turbidity

Degradation Pathways

Reductive Dechlorination Pathway

PCE → TCE → cis-1,2-DCE → Vinyl Chloride → Ethene

Sequential removal of chlorine atoms under anaerobic conditions

Key Organism:

Dehalococcoides spp.

Conditions:

Anaerobic, electron donor required, pH 6-8

Oxidative Degradation

Chlorinated Solvent + SO₄•⁻ → CO₂ + Cl⁻ + SO₄²⁻

Direct mineralization via sulfate radicals

Key Mechanism:

Persulfate radical oxidation

Conditions:

Activator (Fe²⁺, Fe³⁺) required, all soil types

ZVI Reductive Pathway

PCE/TCE + Fe⁰ → Acetylene/Ethene + Fe²⁺ + Cl⁻

Surface-catalyzed reduction and dechlorination

Key Mechanism:

Electron transfer at iron surface

Conditions:

No oxygen, low to moderate pH, low sulfate

Design Considerations

Site Characterization
  • Contaminant distribution (dissolved vs. DNAPL)
  • Geochemistry (pH, redox, sulfate, nitrate, TOC)
  • Geology and hydraulic conductivity
  • Electron acceptor/donor availability
  • Presence of co-contaminants (petroleum, metals, dioxane)
Technology Selection
  • PCE/TCE dominant → Persulfate or ERD
  • High vinyl chloride → ERD with Dehalococcoides
  • Low permeability → Persulfate or EZVI
  • DNAPL source zones → High-dose persulfate or ERD
  • Mixed contaminants → Combined oxidation systems
Implementation Strategy
  • Pilot test to optimize dosing and delivery
  • Injection spacing based on geology (15-30 ft typical)
  • Direct push or permanent wells depending on monitoring needs
  • Performance monitoring: parent compounds, daughter products, geochemistry
  • Contingency planning for stall or rebound

Specialized Chlorinated Solvent Treatment Methods

Enhanced In-Situ Dechlorination

Enhanced In-Situ Dechlorination (EID)

IET delivers electron donor substrates (emulsified vegetable oil, HRC, lactate) combined with Dehalococcoides bioaugmentation cultures to drive complete sequential reductive dechlorination: PCE → TCE → DCE → vinyl chloride → ethene. IET's patented slow-release encapsulated substrates (US-9126244-B2) sustain reducing conditions for 2–5 years from a single injection event.

PCE/TCE
ERD
Bioaugmentation
Complete Dechlorination
Permeable Reactive Barriers

Permeable Reactive Barriers (PRBs)

IET designs and installs PRBs for passive long-term interception of chlorinated solvent plumes. Zero-valent iron (ZVI) or reactive media are installed in-situ to intercept groundwater flow, providing continuous abiotic dechlorination of TCE, PCE, and DCE as the plume migrates through. IET has installed PRBs at industrial, military, and dry cleaner sites nationwide.

ZVI PRB
Passive Treatment
Long-Term
Plume Interception
Combined Technologies

Combined & Sequential Approaches

The most effective chlorinated solvent remediation often layers multiple technologies. A typical IET sequence: (1) ferric iron-activated persulfate ISCO destroys the DNAPL source zone; (2) the iron-amended subsurface transitions into a bioremediation-supporting reducing environment; (3) ERD/bioaugmentation addresses the dissolved plume to closure. One mobilization, multi-year treatment.

ISCO + ERD
DNAPL + Plume
Sequential
Cost-Effective

Ready to Discuss Your Chlorinated Solvent Project?

Our technical team has successfully remediated 300+ chlorinated solvent sites. Contact us for a site-specific technology assessment.

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