H2S Odor Abatement & Concrete Sewer Corrosion (MIC) Control Using Ferrous Chloride FeCl2 30% Combined with Hydrogen Peroxide H2O2 50%
Table of contents
Eliminating toxic Hydrogen Sulfide (H₂S) gas and halting Microbiologically Induced Corrosion (MIC) in industrial wastewater collection networks requires chemical intervention directly within the liquid phase before H₂S can strip into the air. By injecting Ferrous Chloride FeCl₂ 30% at upstream lift stations (15–18 g FeCl₂ 30% / m³ per 1 mg/L S²⁻) to precipitate sulfide as insoluble FeS (Ksp = 6.3 × 10⁻¹⁸), combined with polishing doses of Hydrogen Peroxide H₂O₂ 50% at the equalization basin inlet, treatment plants eliminate 95–99% of airborne H₂S (≤ 0.5 ppm in worker breathing zones), protect concrete infrastructure, and enhance primary clarification.

1. Anaerobic Sulfate Reduction, pH-Dependent H₂S Stripping & Concrete Crown Corrosion (MIC)
Wastewaters from textile dyeing (rich in Na₂SO₄ electrolyte), Kraft pulp and paper mills, tanneries, seafood processing, tapioca starch, and rubber latex contain 300 to 2,500+ mg/L of Sulfate ions (SO₄²⁻). Inside anaerobic force mains, deep collection sumps, and un-aerated equalization tanks (DO ≤ 0.2 mg/L, ORP ≤ -150 mV), Sulfate-Reducing Bacteria (SRB — Desulfovibrio) reduce SO₄²⁻ into total dissolved sulfide (S²⁻, HS⁻, H₂S):
- Anaerobic SRB Reduction:
SO₄²⁻ + 2CH₂O + 2H⁺ → H₂S (aq) + 2CO₂ + 2H₂O - Aqueous Dissociation Equilibrium (
pKa1 = 7.0at25 °C):H₂S (aq) ⇌ H⁺ + HS⁻- At
pH = 6.0:91%of dissolved sulfide exists as volatileH₂Sgas that rapidly strips into the headspace at drop manholes and pump sumps. - At
pH = 7.0:50%exists as volatileH₂Sgas and50%as non-volatileHS⁻. - At
pH = 8.5: Less than3%remains as volatileH₂Sgas (97%stays locked in solution asHS⁻).
- At
Airborne H₂S Concentration (ppm) | Human Physiological & Occupational Safety Impact (OSHA / NIOSH) | Concrete Sewer Crown Corrosion Rate (Biogenic H₂SO₄ Attack) |
|---|---|---|
0.01 – 0.3 ppm | Odor threshold (characteristic rotten-egg smell triggering community complaints). | Negligible structural damage. |
10 – 20 ppm | OSHA PEL Ceiling = 20 ppm. Eye conjunctivitis and respiratory tract irritation. | Thiobacillus bacteria colonize damp concrete crown surfaces. |
50 – 100 ppm | Olfactory Fatigue (paralysis of sense of smell) within 3–15 minutes—workers falsely believe gas has cleared! | Concrete crown surface pH drops to 1.5–2.2; mortar loss 2–4 mm/year. |
300 – 500 ppm | Immediately Dangerous to Life or Health (IDLH = 100 ppm); pulmonary edema within 30 minutes. | Cement paste converts into non-structural Gypsum mush (CaSO₄·2H₂O), exposing rebar. |
≥ 700 – 1,000 ppm | Instant unconsciousness (“Knockdown Effect”) after 1–2 breaths; fatal without SCBA. | Catastrophic collapse of manhole slabs, pump shafts, and copper electrical panels. |
2. Sulfide Precipitation by FeCl₂ 30% & Catalytic Oxidation by H₂O₂ 50%
2.1. Instantaneous Sulfide Locking with Ferrous Chloride (FeCl₂ 30%)
Dosing FeCl₂ 30% into sulfide-bearing wastewater drives an instantaneous precipitation of Ferrous Sulfide (FeS) with an ultra-low solubility product (Ksp = 6.3 × 10⁻¹⁸):
- Molecular Reaction:
FeCl₂ + H₂S → FeS (precipitate ↓) + 2HCl - Net Ionic Reaction:
Fe²⁺ + HS⁻ → FeS (precipitate ↓) + H⁺
Within 10–30 seconds of mixing, dissolved H₂S drops below 0.05 mg/L, completely eliminating H₂S vapor pressure above the water surface. When trace Ferric ions (Fe³⁺ or co-dosed Ferric Chloride FeCl₃) are present, Fe³⁺ oxidizes H₂S to elemental sulfur (S⁰) while reducing to Fe²⁺, which subsequently binds a second HS⁻ ion.
2.2. Polishing Oxidation & Iron Regeneration with Hydrogen Peroxide (H₂O₂ 50%)
- At Neutral / Slightly Acidic
pH = 6.0 – 7.8:H₂O₂ + H₂S → S⁰ (colloidal ↓) + 2H₂O(1.06 kg H₂O₂ 100% / kg H₂S). - At Alkaline
pH ≥ 8.0 – 9.0:S²⁻ + 4H₂O₂ → SO₄²⁻ (soluble) + 4H₂O(zero suspended solids generated). - Synergistic Dual
FeCl₂ + H₂O₂System: TraceFe²⁺catalyzesH₂O₂oxidation ofH₂S(5–10×faster reaction, finishing in1–3 minutes), whileH₂O₂re-oxidizesFeSto regenerate active iron ions, reducing total chemical cost and iron sludge volume by30–40%.

3. Dosing Rate Comparison & 3,000 m³/day Engineering Calculation
Table 2: Technical Comparison of H₂S Control Regimes in Industrial Wastewater
| Technical Criterion | Ferrous Chloride (FeCl₂ 30%) | Hydrogen Peroxide (H₂O₂ 50%) | Synergistic Dual System (FeCl₂ 30% + H₂O₂ 50%) |
|---|---|---|---|
| Primary Reaction Mechanism | Selective precipitation (FeS ↓) | Oxidation to S⁰ or SO₄²⁻ | Upstream sulfide locking + Downstream catalytic oxidation |
| Reaction Time Required | Instantaneous (≤ 10 – 30 sec) | 15 – 30 minutes (uncatalyzed) | Ultra-fast (≤ 1 – 3 minutes) |
Theoretical 100% Basis / 1 kg S²⁻ | 3.96 kg FeCl₂ (100%) | 1.06 kg H₂O₂ (100%) (at pH 7) | 2.2 kg FeCl₂ (100%) + 0.6 kg H₂O₂ (100%) |
Practical Commercial Dosage / 1 kg S²⁻ | 15.0 – 18.5 kg FeCl₂ 30% (11.7 – 14.4 L) | 2.6 – 3.5 kg H₂O₂ 50% (2.2 – 2.9 L) | 8.5 kg FeCl₂ 30% + 1.4 kg H₂O₂ 50% |
| Optimal Injection Point | Upstream lift station, force main inlet | Equalization tank inlet, pre-DAF channel | FeCl₂ 30% at lift station + H₂O₂ 50% at EQ tank inlet |
| Co-Benefits for WWTP | Coagulant aid for color, Phosphate (PO₄³⁻), and 25–35% COD removal | Boosts Dissolved Oxygen (DO) without increasing TDS salinity | ≥ 99% odor elimination, 35% less iron sludge, protects aerobes |
Technical Illustration (Reference Engineering Model): A packaging paper and textile wastewater plant treats
Q = 3,000 m³/day(125 m³/h) containingC(S²⁻) = 28 mg/L(84.0 kg S²⁻/day), generating85 ppmairborneH₂Sabove the equalization sump.
- Option 1 (
FeCl₂ 30%Standalone at16.0 kg / kg S²⁻):84.0 × 16.0 = 1,344 kg FeCl₂ 30%/day(43.75 L/h).- Option 2 (Combined
FeCl₂ 30%at8.5 kg/kg+H₂O₂ 50%at1.4 kg/kg):714 kg FeCl₂ 30%/day(23.2 L/h) at the upstream lift station +117.6 kg H₂O₂ 50%/day(4.10 L/h) ahead of the equalization tank—reducing dissolvedS²⁻to≤ 0.2 mg/Land airborneH₂Sto≤ 0.3 ppmwithin45 minutes.
4. Direct Manufacturer of FeCl₂ 30% & ZDHC MRSL v3.1 Certified Supply by Loc Thien Chemical
Loc Thien Investment Development Co., Ltd. (LOC THIEN INVESTMENT DEVELOPMENT COMPANY LIMITED — Tax ID: 0313650856) offers a unique dual capability in Vietnam’s environmental chemical sector:
- Strict SSOT Product Positioning:
- Direct Manufacturer: Loc Thien is the DIRECT MANUFACTURER of
FeCl₂(exclusively30%aqueous solution) and wastewater-grade Ferric Chloride (FeCl₃) in Vietnam. - Commercial Supplier: Loc Thien is a TIER-1 COMMERCIAL SUPPLIER & DISTRIBUTOR of
H₂O₂ 50%and other industrial chemicals (NaOH,HCl,H₂SO₄,PAC,NaOCl).
- Direct Manufacturer: Loc Thien is the DIRECT MANUFACTURER of
- Synchronized
ZDHC MRSL Version 3.1 Conformance Level 1Credentials:FeCl₂(Ferrous Chloride): HoldsZDHC MRSL Version 3.1 Level 1 Conformance Summary Report (CSR)No.248162921-02andAnalytical Test ReportNo.248162921-02aissued byTÜV Rheinland Vietnam(22–23/10/2024).H₂O₂(Hydrogen Peroxide): HoldsCERTIFICATE (ZDHC MRSL Conformance Level 1)No.ZDHC1 127736 0002 Rev. 00(Test Report No.2486017673-Q24VPS-CHM2869) issued byTÜV SÜD Product Service GmbH/TÜV SÜD Vietnam.
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3,000+ tons/month,5–30-tontanker fleet) & Delivery SLA: Ba Ria - Vung Tau (Phu My 1 IP), Dong Nai (Long Thanh IP), Binh Duong (Di An City), Da Nang (Hoa Khanh IP), Can Tho (Tra Noc IP), and Bac Ninh (Tien Son IP). Headquarters:452/6B Tinh Lo 10, Binh Tri Dong Ward, Binh Tan District, Ho Chi Minh City. Technical quotation within15 minutes; delivery within4 hoursin inner HCMC,24–48 hoursacross Southern & Mekong Delta industrial zones, and2–3 daysin Northern & Central Vietnam. Contact hotline 0979 891 929 for detailed delivery procedures.
Related Technical Resources & Products
- Product Pages: Ferrous Chloride FeCl₂ 30% (Direct Manufacturer) | Hydrogen Peroxide H₂O₂ 50% | Ferric Chloride FeCl₃ 38%–40%
- GHS Safety Data Sheets (MSDS): MSDS Ferrous Chloride FeCl₂ 30% | MSDS Hydrogen Peroxide H₂O₂ 50%
- Technical Inquiry & 15-Minute Quotation: Hotline
0979 891 929(tel:0979891929) — Email:[email protected].