How to Prepare 5% – 10% Milk of Lime Slurry [Ca(OH)2] & Design Non-Clogging Recirculation Loops for Dosing Pumps

How to Prepare 5% – 10% Milk of Lime Slurry [Ca(OH)2] & Design Non-Clogging Recirculation Loops for Dosing Pumps
Table of contents

In industrial wastewater treatment plants, Hydrated Lime Ca(OH)₂ is the most economical alkaline reagent for acid neutralization and heavy-metal/fluoride precipitation, yet it frequently causes severe maintenance downtime due to jammed dosing pump check valves and rock-hard plugged uPVC pipelines. The root cause lies in its physical chemistry: the saturation solubility of Ca(OH)₂ at 20 °C is only 1.65 g/L (0.165%), meaning that in a 5%–10% w/w Milk of Lime slurry (51.8–107.2 g/L), over 98% of the lime exists as suspended solid particles. Eliminating pipe clogging requires combining ≥ 325 mesh (≤ 45 µm) grit-free Ca(OH)₂ powder with a continuous Turbulent Ring-Main Recirculation Loop operating at 1.2 – 1.8 m/s.

Moisture-proof 25kg chemical bag rack storage at Loc Thien Chemical warehouse


1. Retrograde Solubility of Ca(OH)₂ & Specific Gravity Table for 1% – 20% Milk of Lime

Because the dissolution of Calcium Hydroxide is mildly exothermic (ΔH = -16.7 kJ/mol), Ca(OH)₂ exhibits retrograde (inverse) solubility—dissolving less as water temperature rises (1.85 g/L at 0 °C, 1.65 g/L at 20 °C, 1.41 g/L at 40 °C, and 0.94 g/L at 80 °C).

Table 1: Specific Gravity, Baume, and Makeup Recipe for 1,000 Liters (1 m³) of Milk of Lime Slurry at 20 °C

Slurry Concentration (% w/w Ca(OH)₂)Slurry Density at 20 °C (d, kg/L)Baume Degree (°Be)Mass of Ca(OH)₂ Powder per 1 m³ (kg/m³)Volume of Clean Water per 1 m³ (L/m³)Apparent Viscosity (cP)Engineering Operating Recommendation
1.0%1.0060.9 °Be10.1 kg995.9 L1.2 cPVery dilute; requires large tank volume.
3.0%1.0213.0 °Be30.6 kg990.4 L2.1 cPSuitable for small WWTPs using diaphragm pumps.
5.0% (Optimal Standard)1.0354.9 °Be51.8 kg983.2 L4.5 cPGolden ratio for automated pH dosing; highly pumpable.
8.0%1.0577.8 °Be84.6 kg972.4 L12.0 cPStandard concentration for medium-to-large WWTPs.
10.0% (Upper Slurry Limit)1.0729.7 °Be107.2 kg964.8 L28.0 cPMaximum recommended concentration for piping loops.
15.0%1.11114.5 °Be166.7 kg944.3 L95.0 cPNon-Newtonian behavior begins; prone to settling in bends.
20.0%1.15219.1 °Be230.4 kg921.6 L280.0 cPThick paste; restricted to Semi-Dry FGD atomizers.

2. Three Root Causes of Lime Dosing Pump & Pipeline Clogging

  1. Flow Velocity Below Critical Settling Velocity (v ≤ 0.9 m/s) in Dead-End Lines: Suspended Ca(OH)₂ particles (solid density 2.24 g/cm³) require turbulent flow (Re ≥ 4,000, line velocity v ≥ 1.2–1.8 m/s) to stay suspended. In dead-end pipes fed by intermittent pulsing pumps, solids settle within 3–5 minutes whenever the pump pauses, packing 90° elbows solid.
  2. Carbonation by Air Sparging (Ca(OH)₂ + CO₂ → CaCO₃↓): Using compressed air blowers to agitate lime tanks introduces atmospheric CO₂ that converts Ca(OH)₂ into hard Calcium Carbonate (CaCO₃) limestone scale on tank walls, pipes, and pH probes. Strictly use mechanical turbine agitators (1.5–2.5 kW/m³), never air sparging!
  3. Coarse Unslaked Grit & Silica (SiO₂) in Low-Grade Lime: Crude lime containing > 5%–10% sand grit (> 150 µm) immediately jams ball check-valve seats and abrades pump rotors.

3. Non-Clogging Lime Slurry System Design Matrix

Table 2: Engineering Standards for Zero-Blockage Milk of Lime Dosing Systems

System ComponentCommon Faulty Practice (Causes Chronic Plugging)Loc Thien Engineering Standard (100% Non-Clogging)
Ca(OH)₂ Powder SpecificationCrude lime (Ca(OH)₂ ≤ 75%, high sand grit).Refined Industrial Ca(OH)₂ ≥ 90%–96%, fineness ≥ 325 mesh (≤ 45 µm), insoluble grit ≤ 1.0%.
Slurry Tank AgitationCompressed air bubbling or undersized mixer without baffles.Dual-impeller 45° pitched-blade turbine (120–200 rpm, 1.5–2.5 kW/m³) + 3–4 wall baffles + 1–2 mm stainless top loading screen.
Slurry Transfer PumpSmall ball-valve diaphragm pump lifting from tank top.Progressive Cavity (Mono) Pump, Peristaltic Hose Pump, or Open-Impeller Centrifugal / AODD Pump with flooded suction.
Piping ArchitectureDead-end line with sharp 90° elbows; start/stop pump control.Continuous Ring-Main Recirculation Loop running 24/7 back to tank top at 1.2 – 1.8 m/s using long-radius bends (R ≥ 5D).
pH Dosing ModulationTurning dosing pump motor ON/OFF directly.Pneumatic Pinch Valve or Diaphragm Drop-Valve on a short vertical tee (≤ 30 cm) directly above the reaction tank.
Periodic DescalingWaiting until pipe is blocked solid.Automated 3–5 min fresh water flush before shutdown; monthly 15 min circulation with 2%–3% dilute Hydrochloric Acid HCl.

Bulk tanker and truck delivery fleet of Loc Thien Chemical


4. Supply of 325-Mesh Refined Hydrated Lime Ca(OH)₂ by Loc Thien Chemical

Loc Thien Investment Development Co., Ltd. (LOC THIEN INVESTMENT DEVELOPMENT COMPANY LIMITED — Tax ID: 0313650856) is a specialized commercial supplier and distributor of industrial chemicals across Vietnam:

  • Refined Ca(OH)₂ Specifications: Active Ca(OH)₂ ≥ 90%–96%, ultra-fine air-classified ≥ 325 mesh (98% passing 45 µm), acid-insoluble residue ≤ 0.5%–1.0%, packed in moisture-proof 25 kg PE-lined PP bags or 500–1,000 kg Jumbo bags.
  • 6 Strategic Warehouses (3,000+ tons/month, 5–30-ton fleet): 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). Legal Headquarters: 452/6B Tinh Lo 10, Binh Tri Dong Ward, Binh Tan District, Ho Chi Minh City.
  • Quotation & Delivery SLA: Technical quotation within 15 minutes; delivery within 4 hours in inner HCMC, 24–48 hours across Southern & Mekong Delta industrial zones, and 2–3 days in Northern & Central Vietnam. Contact hotline 0979 891 929 for detailed delivery procedures.
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