Yes, EDTMP•Na₅ can replace ATMP•Na₄ in many applications, but the suitability depends on specific requirements such as scale inhibition efficiency, corrosion protection, thermal stability, and environmental factors. Below is a detailed comparison and replacement analysis.
1. Key Differences Between EDTMP•Na₅ and ATMP•Na₄
Property EDTMP•Na₅ ATMP•Na₄
Chemical Structure Contains 4 phosphonate groups + N Contains 3 phosphonate groups + N
Chelating Ability Stronger (higher metal ion binding) Moderate
Scale Inhibition Better for CaSO₄, BaSO₄, SrSO₄ Better for CaCO₃
Corrosion Inhibition Stronger (forms stable metal films) Moderate (requires Zn²⁺ synergy)
Thermal Stability Stable up to 100°C Stable up to 80°C
pH Range Effective at pH 2–12 Effective at pH 2–9
Biodegradability Low (like ATMP) Low
Cost Higher (more complex synthesis) Lower
2. When Can EDTMP•Na₅ Replace ATMP•Na₄?
✅ Preferred Replacement Cases
(1) High-Sulfate Water (Oilfield, Seawater Cooling)
EDTMP•Na₅ is superior for BaSO₄/SrSO₄ inhibition, making it ideal for oilfield injection water where ATMP•Na₄ may fail.
Example: In offshore platforms, EDTMP prevents sulfate scaling in seawater-based systems.
(2) High-Temperature Systems (>80°C)
EDTMP•Na₅ remains stable up to 100°C, while ATMP•Na₄ degrades above 80°C.
Example: High-pressure boilers or geothermal applications.
(3) Stronger Corrosion Protection Needed
EDTMP•Na₅ forms more stable chelates with Fe³⁺, Cu²⁺, reducing pitting corrosion in carbon steel and copper alloys.
Example: Closed-loop cooling systems in power plants.
(4) Wider pH Range Applications
EDTMP•Na₅ works in h3ly alkaline (pH 12) or acidic (pH 2) conditions, unlike ATMP•Na₄ (best at pH 2–9).
Example: Metal pickling (acidic) or textile bleaching (alkaline).
❌ Cases Where ATMP•Na₄ is Still Preferred
(1) Cost-Sensitive Applications
ATMP•Na₄ is cheaper (~20–30% lower cost) and sufficient for low-hardness freshwater systems.
Example: Small-scale cooling towers with moderate scaling risk.
(2) Calcium Carbonate (CaCO₃) Dominant Scaling
ATMP•Na₄ is slightly better at inhibiting CaCO₃ in low-sulfate water.
Example: Municipal water treatment for drinking water systems.
(3) Where Phosphorus Discharge is Restricted
Both contain phosphorus, but ATMP•Na₄ has slightly lower P content (if regulatory limits are tight).
3. How to Switch from ATMP•Na₄ to EDTMP•Na₅?
Dosage Adjustment
EDTMP•Na₅ is typically more efficient; reduce dosage by 10–30% compared to ATMP•Na₄.
Example: If ATMP•Na₄ was dosed at 20 mg/L, EDTMP•Na₅ may work at 15 mg/L.
Compatibility Testing
Check for precipitation risks when mixed with other water treatment chemicals (e.g., Zn²⁺, polyacrylates).
Performance Monitoring
Test scale/corrosion rates after switching (e.g., using coupon tests or LSI/RSI indices).
4. Environmental & Safety Considerations
Both are non-biodegradable and contain phosphorus (regulated in some regions).
EDTMP•Na₅ has lower toxicity than ATMP•Na₄ for aquatic life (lower Zn²⁺ mobilization risk).
Final Recommendation
Replace ATMP•Na₄ with EDTMP•Na₅ if:
You deal with sulfate scales (BaSO₄, SrSO₄).
Operating high-temperature (>80°C) or wide pH range systems.
Need h3er corrosion inhibition.
Stick with ATMP•Na₄ if:
Cost is a major constraint.
Only CaCO₃ scaling is present.
Local regulations strictly limit phosphorus discharge.
For critical applications, conduct bench-scale testing before full replacement.
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