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In most mechanical flotation machines, the rotor and impeller describe the same rotating component. "Impeller" emphasizes the rotating mixing function, while "rotor" usually refers to the complete rotating flotation element and its specialized geometry. The stator surrounds it and controls the air-slurry mixture. Terminology varies by manufacturer, but the rotor-stator relationship determines mixing, air dispersion, and flotation performance.
✒ Rotor and impeller usually describe the same rotating function — "impeller" stresses mixing, "rotor" stresses the complete rotating element and its geometry.
✒ The stator is not a passive guard. It controls turbulent flow leaving the rotor and distributes air bubbles through the cell.
✒ Rotor-stator geometry — blade angle, diameter, clearance — directly changes circulation, air dispersion, bubble distribution, and power draw.
✒ OEM-compatible does not mean "same size only." Operating speed, mounting arrangement, and rotor-stator relationship must also match.
✒ A worn rotor can still rotate normally while its hydraulic profile has already changed, reducing mixing and air dispersion.
✒ Polyurethane and rubber are the two common material options for flotation wear components; the choice depends on whether abrasion or impact dominates.
✒ Open-flow and tank-type flotation cells differ in residence-time distribution, pulp-level control, piping, and operating practice.
✒ Restoring the rotor-stator system is often more practical than replacing a complete flotation cell.
| Item | Description |
|---|---|
| Function | Rotate to suspend solids, circulate slurry, and disperse air into the pulp |
| Material | Polyurethane, rubber, wear-resistant metal, or composite, depending on duty |
| Application | Mechanical flotation cells in copper, gold, lead-zinc, nickel, phosphate, and rare earth circuits |
| Service Life | Depends on abrasiveness, rotor speed, solids loading, and rotor-stator clearance control |
| Benefits | Stable circulation, consistent air dispersion, controlled power draw, predictable wear life |
| Working Partner | Stator — controls turbulent flow and distributes the air-slurry mixture |
| Key Wear Zones | Blade tips, leading edges, hub, mounting flange, stator vanes |
| Replacement Trigger | Loss of hydraulic profile, excessive rotor-stator clearance, power draw change |
A flotation rotor or impeller is the rotating component inside a mechanical flotation cell that draws slurry toward itself, generates internal circulation, and disperses air into the pulp as bubbles. The stator is the stationary component positioned around the rotor that controls the turbulent flow leaving the rotor and helps distribute the air-slurry mixture throughout the cell.
In practical mineral processing discussions, "impeller" often emphasizes the rotating mixing function, while "rotor" is frequently used for the complete rotating flotation element and its specialized geometry. Some flotation machine manufacturers build impeller-type structures; others describe the same function as a rotor. The terminology differs, but the engineering relationship does not: rotor and stator normally work as a pair.
For the wider flotation circuit, see Flotation, Flotation Cells, and Flotation Spares (Rotor & Stator).
A flotation rotor or impeller has two jobs that must happen at the same time: mix the slurry effectively and disperse air into the pulp.
In a mechanical flotation machine, the rotating component draws slurry toward the rotor and generates circulation inside the cell. At the same time, air is introduced into the pulp and broken into bubbles. A stator positioned around the rotor helps control and distribute the resulting air-slurry mixture.
If the rotor does not generate sufficient circulation, solids can settle or become unevenly distributed within the cell. If the air dispersion is poor, bubble size and bubble distribution may also be affected, potentially reducing flotation efficiency.
The stator plays an important supporting role. Rather than simply acting as a stationary protective component, it helps control the turbulent flow leaving the rotor and contributes to the distribution of air bubbles throughout the cell.
This is why rotor-stator geometry matters. A change in blade angle, rotor diameter, clearance, or stator configuration can alter:
Slurry circulation
Air dispersion
Bubble distribution
Power consumption
Mixing intensity
Solids suspension
Froth behavior
For related process context, see Classification, Hydrocyclones, and Dewatering.
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The basic function of a flotation rotor or impeller is to create movement within the slurry. In a mechanical flotation machine, the rotating component draws slurry toward the rotor and generates circulation inside the cell. At the same time, air is introduced into the pulp and broken into bubbles. A stator positioned around the rotor helps control and distribute the resulting air-slurry mixture.
This means that the rotor and stator normally work as a pair. The exact configuration varies between flotation machine manufacturers. Some machines use an impeller-type structure, while others are commonly described as having a rotor.
The flow arrangement of the flotation cell is another important difference. In an open-flow flotation machine, slurry can move relatively freely between adjacent impellers or cells. Cell-to-cell or tank-type designs use partitions, weirs, or controlled transfer arrangements to regulate pulp movement. Tank flotation cells generally use a compact cylindrical vessel and can be manufactured in very large individual volumes.
This difference in flow arrangement affects more than the shape of the equipment. It influences residence-time distribution, pulp-level control, piping requirements, and how operators manage the flotation circuit.
For related flotation equipment, see Flotation Cells and Flotation Spares (Rotor & Stator).
A flotation rotor or impeller has two jobs that need to happen at the same time: mix the slurry effectively and disperse air into the pulp.
If the rotor does not generate sufficient circulation, solids can settle or become unevenly distributed within the cell. If the air dispersion is poor, bubble size and bubble distribution may also be affected, potentially reducing flotation efficiency.
The stator plays an important supporting role. Rather than simply acting as a stationary protective component, it helps control the turbulent flow leaving the rotor and contributes to the distribution of air bubbles throughout the cell.
This is why rotor-stator geometry matters. A change in blade angle, rotor diameter, clearance, or stator configuration can alter slurry circulation, air dispersion, bubble distribution, power consumption, mixing intensity, solids suspension, and froth behavior.
Consequently, replacing a worn rotor with a component that has the wrong geometry can create process problems even when the new component physically fits the machine.
For this reason, OEM-compatible does not mean "same size only." A properly matched replacement should also consider the original design, operating speed, dimensions, mounting arrangement, and rotor-stator relationship.
Another point worth considering is wear. In abrasive flotation circuits, the rotor and stator are continuously exposed to mineral slurry. As the working surfaces wear, the original hydraulic profile gradually changes. A rotor that has lost a significant amount of material may still rotate normally, but its mixing and air-dispersion performance may no longer be the same.
See also Flotation Impeller & Stator and Flotation Rotor & Stator Parts.
The choice between open-flow and tank-type flotation equipment is also related to plant capacity. Open-flow flotation machines have traditionally been attractive for high-throughput applications because their flow arrangement can process substantial slurry volumes efficiently.
Modern tank cells, however, can be built with very large individual capacities. Using larger cells means a plant may need fewer flotation units to achieve the required total volume. This can provide several practical advantages: fewer individual flotation units, reduced plant footprint, less interconnecting piping, potentially lower installation requirements, and fewer mechanical components to maintain.
However, a larger cell is not automatically a better cell. When one flotation tank represents a significant percentage of the total circuit volume, process control becomes particularly important. Operators need reliable pulp-level control, froth monitoring, air control, and mixing throughout the larger vessel.
Energy consumption should also be evaluated carefully. It is not enough to compare the nominal volume of two flotation machines. The actual requirement depends on slurry density, solids concentration, particle size, air demand, impeller or rotor design, operating speed, and flotation kinetics.
A high-capacity flotation cell that does not provide the required mixing conditions will not necessarily produce better economics. The real objective is to achieve the required recovery and concentrate grade with a practical combination of capacity, power consumption, residence time, recovery performance, and maintenance cost.
Related reading: Flotation Cell Rotor and Stator Wear Parts: How They Control Recovery, Flow and Maintenance Cost.
Process benefits: consistent solids suspension, controlled air dispersion, stable froth behavior, predictable residence-time distribution, better pulp-level and air-rate control.
Mechanical benefits: matched rotor-stator clearance reduces vibration and power spikes; correct geometry reduces cavitation risk; balanced rotating assembly extends shaft and bearing life; properly bonded polyurethane or rubber liners reduce premature wear.
Commercial benefits: lower total cost of ownership, fewer unplanned shutdowns, reduced risk of "fits physically but performs poorly" replacement errors, better spare parts inventory planning.
For the technical relationship between wear parts and recovery, see Rotor & Stator in Mechanical Flotation Cells: The Heart of Efficient Mineral Flotation.
Open-flow flotation machines: slurry can move relatively freely between adjacent impellers or cells. Historically widely used for high-throughput flotation circuits.
Cell-to-cell or tank-type designs: partitions, weirs, or controlled transfer arrangements regulate pulp movement. Tank cells use a compact cylindrical vessel and can be built in very large individual volumes.
Typical ore applications: copper ore, gold ore, lead-zinc ore, nickel ore, phosphate ore, rare earth ore, coal, molybdenum, and polymetallic circuits.
Typical equipment applications:
| Material | Abrasion Resistance | Impact Resistance | Dimensional Stability | Typical Flotation Use |
|---|---|---|---|---|
| Polyurethane | High | Moderate | High | Rotor and stator in abrasive circuits where wear is the dominant failure mode |
| Rubber | Moderate to High | High | Moderate | Rotor and stator where coarse particles create significant mechanical impact |
| Wear-Resistant Metal | High | Moderate | High | Structural hubs, shafts, mounting flanges |
| Composite / Hybrid | Application-dependent | Application-dependent | High | Specific OEM designs combining liners with structural cores |
Polyurethane can provide strong abrasion resistance and dimensional stability, making it attractive for applications where abrasive wear is the dominant failure mechanism. Rubber offers flexibility and good impact resistance and may be more suitable where coarse particles create significant mechanical impact.
For a broader wear-material comparison, see Polyurethane Screen vs Rubber Screen vs Wire Mesh: A Complete Comparison Guide.
| Item | Open-Flow Flotation | Tank-Type Flotation |
|---|---|---|
| Slurry Movement | Relatively free between adjacent impellers/cells | Regulated by partitions, weirs, or controlled transfer |
| Typical Strength | High-throughput circuits with simple flow arrangement | Very large individual cell volumes |
| Plant Footprint | Larger number of units | Fewer units, reduced footprint |
| Piping | More interconnecting piping | Less interconnecting piping |
| Process Control | Distributed across many cells | Critical because one cell is a large share of circuit volume |
| Residence Time Distribution | Depends on cell-to-cell transfer | Depends on internal mixing and level control |
| Maintenance Scope | More mechanical components to maintain | Fewer units but larger individual maintenance events |
| Best Fit | Existing plants and high-throughput retrofits | New high-tonnage plants with reliable process control |
There is no universal answer. Both open-flow and tank flotation machines can be used for rougher, scavenger, and cleaner duties. The appropriate choice depends on ore characteristics, throughput, required residence time, flotation kinetics, recovery targets, plant layout, and process-control requirements.
| Industry / Ore | Typical Flotation Duty | Rotor/Impeller Consideration | Related Process Stage |
|---|---|---|---|
| Copper Ore | Rougher, scavenger, cleaner | Abrasive slurry, moderate to high wear | Classification → Flotation → Dewatering |
| Gold Ore | Sulphide flotation, free-milling circuits | Variable abrasion, impact from coarse particles | Grinding → Flotation → Tailings |
| Lead-Zinc Ore | Sequential and bulk flotation | Chemistry-sensitive, stable mixing required | Classification → Flotation → Filtration |
| Nickel Ore | Bulk sulphide flotation | High solids loading, wear-critical | Grinding → Flotation → Dewatering |
| Phosphate Ore | Anionic/cationic flotation | Moderate abrasion, large volume | Classification → Flotation → Filtration |
| Rare Earth Ore | Bulk and cleaner flotation | Fine particles, stable dispersion needed | Grinding → Flotation → Thickening |
| Coal | Fine coal flotation | Low abrasion, high throughput | Classification → Flotation → Dewatering |
| Tailings Retreatment | Scavenger flotation | Variable wear, cost-sensitive | Flotation → Tailing |
Step 1 — Confirm the terminology used by the OEM. Identify whether the manufacturer calls the rotating component a rotor or an impeller. This affects part numbering, drawings, and replacement documentation.
Step 2 — Match the hydraulic profile, not just the dimensions. Consider original design, operating speed, dimensions, mounting arrangement, and rotor-stator relationship. Wrong geometry can create process problems even when the new component physically fits.
Step 3 — Confirm rotor-stator clearance. Excessive clearance reduces air dispersion and mixing intensity. Insufficient clearance increases the risk of contact, vibration, and premature failure.
Step 4 — Select material by dominant wear mechanism. Polyurethane for abrasion-dominated duty. Rubber for impact-dominated duty. Metal or composite cores for structural load paths.
Step 5 — Verify balance and mounting. Balance, shaft connection, and mounting condition affect vibration, bearing life, and power draw.
Step 6 — Check the downstream effect. Flotation performance affects Dewatering, Filtration, and Tailing management.
Required Information: equipment model and manufacturer; OEM part number; rotor or impeller type; operating speed (RPM); slurry density and solids concentration; particle size distribution; air demand and air rate; operating pH and reagent environment.
Drawings Needed: rotor assembly drawing; stator assembly drawing; shaft connection detail; mounting flange detail; rotor-stator clearance specification; material specification sheet.
OEM Part Numbers: confirm whether the supplier can cross-reference OEM part numbers or requires original drawings.
Material Selection: confirm whether polyurethane, rubber, metal, or composite is appropriate. Ask for material reports and wear-life recommendations.
MOQ: confirm minimum order quantity for single replacement parts and for planned spare parts inventory.
Lead Time: confirm production lead time, inspection time, and shipping time separately.
Packaging: confirm protection against impact, UV, and moisture during transport.
Shipping Method: confirm sea freight, air freight, or courier options based on weight and urgency.
Inspection Standards: confirm dimensional inspection, balance check, material verification, and bonding inspection for lined components.
Supplier Evaluation Checklist
Can the supplier manufacture according to drawings?
Can the supplier provide material reports?
Can the supplier support OEM replacement?
Does the supplier have export experience?
Can the supplier provide wear-life recommendations?
Can the supplier confirm rotor-stator clearance requirements?
Can the supplier provide reference projects in similar ore types?
For related procurement context, see Which Manufacturer Offers High-Quality Polyurethane Tufflex Wire Screens for Mining? and How Do I Choose the Right Rubber Belt for a Vacuum Belt Filter?.
| Problem | Possible Cause | Recommended Solution |
|---|---|---|
| Premature rotor wear | Abrasive slurry, wrong material, excessive speed | Switch to polyurethane or higher-grade rubber; verify operating speed |
| Premature stator wear | High turbulence, wrong vane geometry, loose mounting | Confirm stator geometry and mounting torque; inspect clearance |
| Cracking at blade root | Fatigue, imbalance, cavitation, casting/liner defect | Check balance, shaft alignment, and material bonding; replace with reinforced design |
| Excessive rotor-stator clearance | Wear of rotor and stator surfaces | Measure clearance; replace rotor, stator, or both |
| Low flotation efficiency | Poor air dispersion, insufficient circulation | Inspect rotor geometry and stator condition; verify air rate |
| Solids settling in cell | Insufficient circulation, low rotor speed | Verify rotor speed and blade condition; check solids loading |
| Power consumption increase | Excessive clearance changes, imbalance, bearing wear | Inspect rotor-stator system, shaft, and bearings |
| Poor fitment on installation | Wrong mounting dimensions, wrong part number | Confirm drawings, OEM part number, and mounting detail |
| Material mismatch | Rubber used where abrasion dominates, or polyurethane where impact dominates | Re-select material based on dominant wear mechanism |
| Installation failure | Incorrect torque, wrong fasteners, damaged sealing surface | Follow OEM torque sequence and inspection procedure |
| Vibration after replacement | Imbalance, misalignment, wrong clearance | Re-balance, re-align, and re-check rotor-stator clearance |
| Bonding failure on lined parts | Poor surface preparation or vulcanization | Verify supplier bonding process and inspection records |
Daily Inspection: abnormal noise or vibration; power draw against baseline; air rate and pulp level stability; visible slurry leakage or froth abnormalities.
Weekly Inspection: rotor blade tips for wear or cracking; stator vanes for wear or blockage; rotor-stator clearance where accessible; mounting bolts and fasteners.
Monthly Inspection: measure rotor blade wear against baseline; measure stator wear against baseline; check shaft connection and balance; inspect rubber or polyurethane bonding for separation; review power consumption trend.
Wear Pattern Monitoring: photograph and log wear zones at fixed intervals; compare wear rate against previous replacement cycles; track the relationship between wear and flotation recovery.
Replacement Timing: replace when rotor-stator clearance exceeds OEM specification; replace when hydraulic profile loss affects air dispersion; replace when power draw changes significantly; replace when cracking or bonding failure is detected.
Spare Parts Inventory: keep at least one rotor and one stator per critical cell; keep fasteners, seals, and mounting hardware; keep a wear log for each cell.
Downtime Reduction: pre-stage replacement parts before planned shutdown; use matched rotor-stator sets where possible; train maintenance teams on clearance measurement.
Preventive Maintenance: follow OEM inspection intervals; track wear against ore type and throughput; adjust material selection when ore changes.
For related maintenance practice on classification equipment, see Hydrocyclone Underflow Too Wet? 6 Causes & Fixes and Hydrocyclone Wear: Root Causes, High-Wear Zones & Material Solutions.
Case Study — Copper Concentrator Flotation Circuit
Customer Type: copper concentrator, 8,000 tpd, existing open-flow flotation circuit.
Ore Type: copper sulphide ore with moderate to high abrasiveness.
Operating Conditions: continuous operation, abrasive slurry, rotor and stator replacement on a fixed annual cycle. Flotation recovery had gradually declined over two replacement cycles.
Problem: the plant replaced worn rotors with components that physically fitted the machine but had a slightly different blade angle and rotor-stator clearance. Power draw increased, air dispersion became uneven, and recovery dropped by several percentage points. Solids settling was observed in the last cells of the circuit.
Solution: the plant reviewed the original OEM drawings and the rotor-stator relationship. A replacement rotor and stator were manufactured to match the original hydraulic profile, mounting arrangement, and clearance specification. Polyurethane was selected for the abrasion-dominated zones, with rubber used where coarse particles created impact. Rotor-stator clearance was measured and documented before commissioning.
Result: air dispersion became consistent across the cell; solids settling in the last cells was eliminated; power draw returned to baseline; recovery recovered to the original design level; rotor and stator wear life increased by approximately 30% compared with the previous replacement cycle.
This is an engineering-logic example, not a guarantee. Actual results depend on ore type, operating conditions, and maintenance practice.
The "better" flotation machine is rarely determined by tank shape alone.
Changing the flotation machine can affect the whole circuit. For an existing plant, moving from an open-flow arrangement to large tank cells is not simply a matter of removing one machine and installing another. Residence time, piping, level control, air distribution, and operating procedures may all need to be reconsidered.
Check the rotor-stator condition before blaming the flotation machine. A flotation cell can have a sound overall design but still perform poorly if the rotor is badly worn, the stator is damaged, or the clearance has become excessive. In many cases, restoring the rotor-stator system is a more practical first step than changing the complete flotation cell.
Flotation performance depends on many factors, but the condition of the wear parts should not be overlooked.
HUATAO supplies flotation machine wear parts and other mining wear-resistant components for mineral processing applications. Depending on the equipment and operating conditions, we can provide polyurethane, rubber, and other customized components according to customer drawings or existing samples.
Our product range also covers mining screen panels, polyurethane screen mesh, rubber screen panels, flip-flow screen media, dewatering screen media, hydrocyclone components, mill liners, and other mining wear parts.
For flotation rotor and stator replacement projects, we can review the equipment model, drawings, dimensions, material requirements, and operating conditions before production. This helps reduce the risk of receiving a component that fits physically but does not perform as expected.
If you are looking for a replacement flotation rotor, impeller, stator, or other flotation wear parts, send us the equipment model, drawings, photos, or existing part dimensions. We can discuss the suitable material and manufacturing solution based on your application.
Question: What is the difference between a flotation rotor and an impeller?
Answer: In most mechanical flotation machines, they describe the same rotating component. "Impeller" emphasizes the rotating mixing function, while "rotor" usually refers to the complete rotating flotation element and its specialized geometry. The terminology varies by manufacturer, but the function is the same: draw slurry, generate circulation, and disperse air. For replacement purposes, always confirm the OEM terminology and part number.
Question: Why does rotor-stator geometry matter so much?
Answer: Rotor-stator geometry controls slurry circulation, air dispersion, bubble distribution, power consumption, mixing intensity, solids suspension, and froth behavior. A change in blade angle, rotor diameter, clearance, or stator configuration can shift all of these at once. That is why a replacement part that fits physically can still perform poorly. Geometry is the difference between "fits" and "works."
Question: Can I replace only the rotor and keep the old stator?
Answer: Sometimes, but it depends on stator condition and clearance. If the stator is worn, the new rotor may not restore the original hydraulic relationship. In many cases, replacing the rotor and stator as a matched set is more reliable. Measure rotor-stator clearance before deciding. If clearance exceeds specification, replace both components.
Question: What material is best for flotation rotors and stators?
Answer: Polyurethane and rubber are the two common options. Polyurethane provides strong abrasion resistance and dimensional stability, making it suitable where abrasive wear dominates. Rubber offers flexibility and good impact resistance, making it more suitable where coarse particles create significant mechanical impact. The final choice depends on the application. Ask the supplier for material reports and wear-life recommendations.
Question: How long should a flotation rotor or stator last?
Answer: Service life depends on abrasiveness, rotor speed, solids loading, air rate, and rotor-stator clearance control. There is no universal number. The practical approach is to establish a wear baseline for each cell, track wear rate against throughput and ore type, and replace when clearance or hydraulic profile loss affects performance. A wear log is more useful than a nominal life figure.
Question: What information do I need to send for an OEM-compatible replacement?
Answer: Send the equipment model, OEM part number if available, original drawings, dimensions, mounting details, operating speed, slurry density, particle size, air rate, and material requirements. Photos and existing part dimensions also help. A supplier who reviews this information before production can reduce the risk of receiving a component that fits physically but does not perform as expected.
Question: Is a larger flotation cell always better?
Answer: No. Larger tank cells can reduce the number of units, plant footprint, and interconnecting piping. But when one flotation tank represents a significant percentage of the total circuit volume, process control becomes critical. Pulp-level control, froth monitoring, air control, and mixing must all be reliable. A high-capacity cell that does not provide the required mixing conditions will not necessarily produce better economics.
Question: How do I reduce flotation rotor and stator maintenance cost?
Answer: Start with correct material selection based on the dominant wear mechanism. Confirm rotor-stator clearance at every replacement. Keep a wear log for each cell. Pre-stage matched rotor-stator sets before planned shutdowns. Track power draw as an early wear indicator. In many cases, restoring the rotor-stator system is more practical and lower cost than changing the complete flotation cell.
Question: Can a worn rotor still rotate normally?
Answer: Yes. A rotor that has lost a significant amount of material may still rotate normally, but its mixing and air-dispersion performance may no longer be the same. Erosion changes the blade profile and reduces the designed clearance between rotor and stator. This is why inspection should include more than checking whether the rotor is cracked. Measure wear, clearance, and power draw.
Question: How do I choose between open-flow and tank-type flotation?
Answer: There is no universal answer. Both can be used for rougher, scavenger, and cleaner duties. The choice depends on ore characteristics, throughput, required residence time, flotation kinetics, recovery targets, plant layout, and process-control requirements. For a new high-tonnage plant, large tank cells may simplify the circuit. For an existing plant, replacing an open-flow arrangement is a much bigger decision.
Question: Where can I source flotation rotor, impeller, and stator wear parts?
Answer: Look for a supplier who can manufacture according to drawings, provide material reports, support OEM replacement, confirm rotor-stator clearance requirements, and provide wear-life recommendations. HUATAO supplies flotation machine wear parts and other mining wear-resistant components, including polyurethane and rubber components, according to customer drawings or existing samples.
Rotor and impeller are usually two names for the same rotating function in a mechanical flotation cell. What matters is not the terminology but the rotor-stator relationship: geometry, clearance, material, balance, and mounting.
A worn rotor can still rotate normally while its hydraulic profile has already changed. A replacement part can fit physically while performing poorly. Both problems are solved the same way: confirm the original design, measure clearance, select material by dominant wear mechanism, and verify the rotor-stator system as a pair.
Before blaming the flotation machine, check the rotor-stator condition. In many cases, restoring the rotor-stator system is a more practical first step than changing the complete flotation cell.
If you are looking for a replacement flotation rotor, impeller, stator, or other flotation wear parts, send us the equipment model, drawings, photos, or existing part dimensions. We can discuss the suitable material and manufacturing solution based on your application.
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Rotor & Stator in Mechanical Flotation Cells: The Heart of Efficient Mineral Flotation
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Annie Lu
Email: annie.lu@huataogroup.com
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Website: http://www.tufflexscreen.com