Contents
How to use this guide
This is a practical decision aid for mining & minerals processing teams. Use it to align procurement, EHS, and operations on selection criteria, acceptance checks, and monitoring signals. When you have site-specific constraints (recycle ratio, pH window, temperature, evaporation/concentration steps), share them so we can propose compliant, supply-ready options.
Mining reality: scale issues rarely come from a single number. They usually come from where chemistry changes (pH shifts, CO2 stripping, heating, evaporation, mixing streams) and where solids concentrate (recycle loops, filters, heat exchangers, RO/NF membranes, spray systems).
Where it fits
- Process goal: protect uptime, maintain flow/heat transfer, reduce cleanup downtime, stabilize reagent consumption.
- Operating window: pH setpoints, temperature, residence time, and shear (pipes, pumps, cyclones, sprays).
- Interfaces: pipelines, valves, heat exchangers, spray nozzles, clarifiers/thickeners, filters, membranes.
- Constraints: recycle water quality limits, discharge limits, product quality/spec, site restricted substances list.
Common scale types in mining water
A quick way to avoid wrong chemistry: match the deposit type to the operating condition that triggers it.
| Scale type (common) | Typical trigger | Where it shows up | Program levers |
|---|---|---|---|
| Calcium carbonate | Higher pH, CO2 stripping, heating | Warm surfaces, spray systems, recycle loops | pH/alkalinity control, threshold inhibitors, dispersants, softening upstream |
| Calcium sulfate (gypsum) | High sulfate + concentration (evaporation/recycle) | Pipes, filters, RO/NF pretreatment, evaporative systems | Antiscalants tuned for sulfate, manage concentration factor, upstream precipitation where possible |
| Barium/strontium sulfate | Mixing incompatible waters (barite risk), concentration | Injection points, mixing zones, membranes | Specialized antiscalants, control mixing, remove Ba/Sr upstream if feasible |
| Silica / magnesium silicate | High silica, high pH, high Mg, heating/concentration | Heat exchangers, membranes, high-recycle circuits | Silica-focused antiscalants, pH management, avoid high-pH Mg + silica zones, solids control |
| Iron scale / mixed mineral deposits | Oxidation, pH shifts, carryover solids | Dead legs, low-flow zones, equipment with oxygen ingress | Redox/pH control, dispersants, solids management, filtration |
Quick selection map (antiscalant vs pH vs precipitation)
| Your constraint | Primary lever | Why | Watch-outs |
|---|---|---|---|
| Process requires a fixed pH window (metallurgy or reagent performance) | Antiscalant + dispersant | Lets you keep pH while reducing precipitation tendency and deposit adhesion | Choose chemistry compatible with flocculants and downstream solids handling |
| You can adjust pH without harming recovery/quality | pH control | Often the lowest-cost way to reduce carbonate/silicate precipitation risk | Local high-pH zones at injection points can still precipitate—mixing matters |
| High hardness / high alkalinity makeup and you can treat upstream | Precipitation/softening upstream | Remove scale-formers before they enter recycle-heavy circuits | Sludge handling, solids carryover, and polymer compatibility become critical |
| Sulfate scaling under high concentration factor | Sulfate-focused antiscalant + manage concentration factor | Gypsum/barite risks are strongly concentration-driven | Confirm mixing points and temperature effects; watch membrane differential pressure |
| Silica-limited circuit (membranes / hot surfaces) | Silica program (antiscalant + pH discipline) | Silica behavior is sensitive to pH, temperature, and Mg | Avoid “hidden” high-pH zones and Mg pickup; ensure solids control is stable |
Program building blocks
1) Know the “problem stream” and the “trigger step”
- Problem stream: the exact water feeding the fouling surface (not just makeup or pond water).
- Trigger step: the moment chemistry changes (pH adjust, heating, evaporation, CO2 loss, blending).
- Concentration factor: where dissolved ions concentrate (recycle loops, thickeners, RO, evaporation).
2) Choose the chemistry “family” by risk profile
| Need | Common approach | Best fit examples |
|---|---|---|
| Threshold inhibition | Antiscalant blends (polymer / phosphonate programs) | Carbonate and sulfate control in recycle-heavy circuits |
| Dispersion (keep fines/deposit precursors suspended) | Dispersants (often polymeric) | Mixed mineral deposits, iron/silt-related fouling, sticky scale precursors |
| Precipitation management | Softening / controlled precipitation upstream | Very hard makeup, high alkalinity, limited tolerance for scaling in sensitive equipment |
| pH discipline | pH optimization + mixing best practices | Carbonate & silicate risks where process allows pH movement |
Compatibility check that saves projects: make sure the scale-control chemistry is compatible with your flocculant/coagulant program (settling and clarity KPIs) and does not create downstream filter/membrane fouling.
Monitoring plan (practical)
The best program is the one you can measure and trend. In mining, trending a few signals by stream is usually more valuable than occasional full lab panels.
| What to monitor | Where | Why it matters | Typical cadence |
|---|---|---|---|
| pH + temperature | Before/after pH adjustment; near hot/evaporative units | Scale risk is extremely sensitive to these two parameters | Per shift (or continuous) |
| Hardness + alkalinity | Key recycle streams and makeup | Primary drivers for carbonate scaling and precipitation | Daily to weekly |
| Sulfate + (Ba/Sr if relevant) | Streams impacted by evaporation/recycle or blending | Gypsum/barite risk often increases with concentration factor | Weekly (more during changes) |
| Silica (and Mg) | Membrane feed/hot surfaces/recycle-heavy circuits | Silica scaling and Mg-silicate risk in high-pH or high-T systems | Weekly (more if silica-limited) |
| Differential pressure / flow / energy | Filters, exchangers, membranes, critical lines | Early warning of deposition and fouling | Continuous or daily trend |
| Solids carryover (turbidity/clarity) | Thickener overflow / clarified water | Solids accelerate deposition and consume chemicals | Per shift to daily |
Troubleshooting signals
If performance drops, these are common early indicators and what to check first:
| Signal | What it often suggests | First checks |
|---|---|---|
| Poor settling / cloudy overflow | Polymer incompatibility, solids carryover, pH drift | Coag/floc doses, pH at mixing points, antiscalant dose vs clarity trend |
| High reagent consumption | Uncontrolled precipitation, poor mixing, changing water blend | Water source changes, recycle ratio, injection location and mixing energy |
| Scaling in lines / nozzle plugging | Local supersaturation at injection points or high-T zones | pH “hot spots,” CO2 stripping zones, heat input, antiscalant feed point |
| Rising differential pressure (filters/membranes/exchangers) | Scale deposition or solids fouling | Compare DP vs turbidity; check sulfate/silica/hardness; validate dose pump and dilution water |
| Frequent cleaning / shorter runtime | Wrong chemistry family, underfeed, or process shift | Deposit analysis, confirm actual stream chemistry at foulant surface, review recent pH/recycle shifts |
Best “one test” if you can do it: deposit analysis from the fouled surface. Even a simple characterization (carbonate vs sulfate vs silica vs mixed) prevents weeks of trial-and-error.
Specification & acceptance checks
When comparing products, ask for the data you can verify on receipt:
| Category | What to request | Why it matters |
|---|---|---|
| Identity | Product name/grade, manufacturer, batch/lot traceability | Consistency and easier troubleshooting when water sources change |
| Quality (COA) | Active % / assay, appearance, density, pH, viscosity (as supplied) | Dose control depends on concentration and physical properties |
| Compatibility statement | Compatibility with common flocculants/coagulants and typical materials of construction | Avoids clarity failures and equipment compatibility surprises |
| Safety | Up-to-date SDS, handling precautions, PPE, storage segregation | Aligns with EHS review and site controls |
| Logistics | Lead time, Incoterms, shelf life, storage temperature range | Prevents degraded product performance due to storage or delays |
| Packaging | Drum/IBC/bulk, closures, liner type (if applicable), labeling compliance | Safe transfers and receiving acceptance checks |
Handling & storage
- Store in original, sealed packaging, away from incompatible materials (follow SDS guidance).
- Use secondary containment and clear labeling in the operating area.
- For transfers: verify hose/seal compatibility; use dedicated transfer equipment where practical.
- For dilution: add product to water per supplier guidance; avoid poor mixing that can create local precipitation zones.
RFQ notes (what to include)
- Water sources and blending: makeup, recycled tailings water, thickener overflow, RO permeate/concentrate, etc.
- Operating pH window(s) by unit operation and any planned pH adjustments (locations + setpoints).
- Temperature profile and any heat exchange/evaporation/concentration steps.
- Key water chemistry: hardness, alkalinity, sulfate, silica (and Mg), TDS/conductivity, suspended solids/turbidity.
- Where scaling occurs (exact equipment/line) and the runtime to failure; any deposit photos or analysis.
- Current reagents in the circuit (coag/floc, collectors, frothers, biocides, corrosion inhibitors).
- Estimated monthly volume, packaging preference, delivery country, and documentation requirements (COA/SDS).
- Any compliance constraints (restricted substances list, discharge limits, site rules).
Need a compliant alternative?
Send your constraints and target performance. We’ll propose options with SDS/COA expectations and procurement-ready specs.
Educational content only. Always follow site EHS rules and the supplier SDS for safe use.