Flotation Reagent Preparation
Collectors, frothers, modifiers and depressants must be diluted or dissolved at a controlled concentration. A mix tank prevents uneven chemical strength and reduces undissolved material.
A properly engineered Mining Mixing Tank helps maintain solids suspension, distribute processing chemicals, improve gas-liquid contact and stabilize slurry conditions. Reliable selection requires more than choosing a tank volume. Slurry density, particle size, viscosity, impeller geometry, motor torque and operating mode must all be evaluated as one complete mixing system.
A mining mixing system combines a tank, drive unit, shaft and impeller to produce controlled circulation inside mineral slurry. Its configuration should be matched to the required process, such as suspension, reagent preparation, leaching, neutralization or gas dispersion.
The question “what is mixing tank” usually refers to both the vessel and the mechanical agitation equipment installed inside it.
A mixing tank is an industrial vessel designed to blend liquids, suspend solid particles, dissolve powders, distribute chemicals or improve contact between different phases. In mining applications, the material is often more demanding than ordinary liquid products because it may contain abrasive particles, high solids concentrations and corrosive processing chemicals.
The terms mixing tank and mix tank are often used interchangeably. A tank mixer generally refers to the complete agitation assembly, including the motor, gearbox, coupling, shaft and impeller. The tank provides the working volume, while the tank mixer creates the circulation required to achieve the process objective.
Keeps mineral particles away from the bottom and reduces compacted sediment.
Balances slurry concentration, pH and reagent distribution throughout the vessel.
Breaks incoming liquid, powder or gas into smaller regions for faster contact.
Creates repeatable conditions before flotation, leaching or solid-liquid separation.
Different mining operations require different circulation patterns, impeller loads and material protection systems.
Collectors, frothers, modifiers and depressants must be diluted or dissolved at a controlled concentration. A mix tank prevents uneven chemical strength and reduces undissolved material.
The tank mixer distributes chemicals through the slurry before flotation. Stable mixing improves contact between the mineral surface and the selected reagent.
Continuous agitation keeps ore particles exposed to the leaching solution. The equipment may require corrosion-resistant materials, gas introduction and temperature-control components.
Powders must be wetted, dispersed and maintained at a consistent concentration. Impeller design should reduce floating powder, agglomeration and bottom accumulation.
A heavy-duty mixing tank can support neutralization, conditioning and controlled flocculation before thickening, dewatering or water recovery.
Acidic or alkaline chemicals must be distributed quickly without creating local zones of extreme concentration. Material compatibility is a critical design consideration.
Industrial mixing tank specifications with stirrer systems should describe the vessel, agitation assembly and actual process conditions rather than listing tank capacity alone.
| Specification Item | Typical Configuration | Engineering Significance |
|---|---|---|
| Working volume | 0.5 to 500 m³ | Determines batch capacity, retention time and process throughput. |
| Tank diameter | 800 to 10,000 mm | Affects impeller diameter, circulation distance and structural loading. |
| Slurry solids content | 5% to 70% | Higher solids normally increase torque, wear and suspension demand. |
| Viscosity range | 1 to 100,000 mPa·s | Influences impeller type, shaft speed and gearbox selection. |
| Agitator speed | 10 to 300 rpm | Large slurry tanks often use lower speed with higher operating torque. |
| Impeller-to-tank ratio | 0.25 to 0.55 | Controls pumping capacity, shear rate and bottom circulation. |
| Drive power | 0.75 to 500 kW | Must be calculated from density, geometry, mixing duty and startup load. |
| Tank material | Carbon steel, stainless steel or lined steel | Selected according to corrosion, abrasion, temperature and service life. |
| Seal arrangement | Packing, mechanical or labyrinth design | Depends on pressure, leakage limits, dust and chemical exposure. |
| Operating mode | Batch or continuous | Changes residence time, feed position and control requirements. |
Two tanks with the same working volume may require very different agitator systems. A low-density reagent solution may use a smaller high-speed impeller, while dense mineral slurry may require a larger impeller, stronger shaft and low-speed high-torque gearbox.
“How to size a mixer for a tank” is an engineering question that must be answered from the process duty, material properties and tank geometry.
Tank geometry: working volume, diameter, liquid height and bottom shape.
Slurry properties: density, viscosity, solids percentage and flow behavior.
Particle data: average size, maximum size, settling rate and abrasiveness.
Mixing objective: blending, suspension, dissolution, dispersion or reaction.
Operating conditions: temperature, pressure, pH and continuous operating time.
Internal components: baffles, coils, pipes, draft tubes and level instruments.
In this relationship, P is mixing power, Np is the impeller power number, ρ is fluid density, N is rotational speed and D is impeller diameter. It provides a useful starting point, but a mining slurry system also requires allowances for solids loading, gearbox efficiency, wear and full-load startup conditions.
Settled solids may create a much higher startup torque than the normal operating torque. Motor and gearbox selection should therefore consider whether the mixer must restart after an unplanned shutdown with material already settled in the tank.
Selecting a larger motor without checking the shaft, gearbox, impeller and support structure may transfer excessive loads into weaker components. A complete tank mixer design should verify torque, shaft deflection, critical speed, bearing load, impeller thrust and tank-top reinforcement.
Impeller selection determines the flow direction, pumping rate, shear intensity and ability to keep particles suspended.
Produces strong vertical circulation and is commonly selected for solids suspension, bulk blending and low-to-medium viscosity slurry.
Typical duty: suspension and circulationCombines axial and radial flow. It is suitable for slurry conditioning, chemical distribution and general-purpose mineral processing.
Typical duty: combined pumping and shearGenerates higher local shear and can disperse gas or chemical feed effectively. Power demand is generally higher than an axial-flow design.
Typical duty: gas dispersion and intensive mixingOperates close to the tank wall and is more suitable for viscous liquids. It is not normally the first choice for rapidly settling coarse mineral particles.
Typical duty: high-viscosity wall circulationUsed in tall tanks where a single impeller cannot maintain uniform circulation over the complete liquid height.
Typical duty: high liquid level and large vesselsUses selected alloys, protective coatings or replaceable wear components to handle abrasive ore particles and extend maintenance intervals.
Typical duty: abrasive mineral slurryThe search question “can you mix gas in your tank” depends on the gas type, process purpose and tank design. Gas can be introduced through a bottom sparger, ring distributor or specialized hollow shaft. The impeller then divides the incoming gas into smaller bubbles and distributes them through the liquid or slurry.
Oxidation, oxygen supply, leaching, pH control and selected conditioning processes.
Gas flow rate, bubble size, impeller flooding, liquid depth and solids suspension.
Gas compatibility, ventilation, pressure relief, grounding and explosion protection.
Excessive gas flow may surround the impeller and reduce its ability to pump liquid. This condition can weaken slurry circulation even when the motor continues to operate. Gas-liquid mixing should therefore be calculated as part of the complete agitation duty.
The main difference is the intended process. A mixer is primarily designed to create physical movement, uniformity, suspension or dispersion. A reactor is designed to provide controlled conditions for a chemical or biological reaction.
| Design Area | Mixing Tank | Reactor |
|---|---|---|
| Primary purpose | Physical mixing | Controlled reaction |
| Pressure | Usually atmospheric or low | May be vacuum or pressurized |
| Temperature control | Optional | Frequently essential |
| Instrumentation | Basic operating control | Detailed reaction monitoring |
| Sealing | Based on material handling | Often more demanding |
Some leaching and neutralization tanks perform both mixing and reaction functions. These vessels may look like a conventional mix tank but require additional temperature control, corrosion protection, gas distribution, sealing and process instrumentation.
The vessel and wetted components should be selected according to both chemical corrosion and mechanical abrasion.
Suitable for many neutral slurry applications. Internal coatings or replaceable liners can be added where abrasion or moderate corrosion is expected.
Applied where corrosion resistance, cleanliness or chemical compatibility is more important than the lower initial cost of carbon steel.
Provides a protective barrier against abrasive slurry and selected chemicals. Lining quality and edge protection influence operating life.
Hardened alloys, replaceable blades and protective surface treatments can reduce impeller and shaft wear in high-solids service.
Changes in vibration, motor current, mixing pattern or solids distribution can indicate a process or mechanical problem.
Possible causes include insufficient speed, a small impeller, excessive installation height, worn blades or an unexpected increase in slurry density.
A strong vortex may be related to missing baffles, excessive speed or incorrect impeller placement. It can draw air into the slurry and reduce effective circulation.
Increased density, compacted solids, bearing resistance, impeller blockage or gearbox problems may raise the operating load.
Check impeller balance, shaft alignment, coupling condition, bearing wear, critical speed and structural support.
Worn impeller edges can change the original diameter and blade profile, reducing pumping capacity even when the operating speed remains unchanged.
Seal wear, shaft movement, pressure fluctuation or unsuitable sealing materials may allow liquid, vapor or dust to escape.
A dependable mining mixing system should be designed around process data rather than a standard tank model alone. Vessel dimensions, impeller arrangement, drive torque, shaft strength, material grade and maintenance access can be configured for the required duty.
Working volume, wall thickness, support structure, bottom shape and nozzle arrangement.
Impeller type, diameter, installation height, shaft speed and multiple-stage arrangement.
Motor power, gearbox ratio, service factor, coupling and full-load startup capability.
Steel grade, rubber lining, protective coating and replaceable wear components.
Provide the following information to support a more accurate configuration:
If you have any questions, please contact us.
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