【Capacity】:
50~1200TPD【Main Materials】:
By calcining industrial residues, specifically sugar/beet plant waste and papermaking white mud【Main Equipment】:
lime rotary kiln, rotary dryer rotary cooler, jaw crusher, bucket elevator, etc.
As a professional lime solution provide, ZK has developed an innovative and sustainable solution for producing high-quality lime by calcining industrial residues, specifically sugar/beet plant waste and papermaking white mud. Moving beyond traditional limestone-based production, this system embodies the principles of a circular economy by converting challenging waste streams—characterized by high moisture and viscosity—into valuable industrial products (lime and CO₂). The core design philosophy fully integrates energy conservation, environmental protection, and resource reuse. A successful reference plant is already operational in the UAE, validating the technology's commercial and technical feasibility.
1. Material Preparation & Drying: Sugar residue (30-40% moisture) is fed via a specialized box feeder to a metering belt conveyor. A shaftless screw conveyor, ideal for viscous materials, then transfers it to a rotary dryer. Here, a built-in chain device breaks up clumps to prevent wall adhesion and enhance heat exchange. Crucially, the dryer utilizes hot flue gas from the kiln tail, recovering waste heat.
2. Calcination & Cooling: The dried material enters the rotary kiln, where a burner system maintains a calcination temperature of approximately 1250°C, ensuring complete conversion to lime (CaO). The hot lime discharges into a single-cylinder cooler. Ambient air cools the lime down to approximately ambient temperature +50°C, and this pre-heated air is then recycled as combustion support air back into the kiln, significantly improving thermal efficiency.
3. Finishing & By-Product Recovery: The cooled lime is ground into powder in a ball mill. The flue gas treatment system is integral to the project's environmental and circular design: kiln exhaust first passes through a cyclone dust collector, then a heat exchanger, and finally a CO₂ collection unit. The captured CO₂ is intended for reuse in sugar production. Similarly, dust from the grinding system, collected by a wet scrubber, can be hydrated into lime for reuse in the sugar plant.
| Capacity (t/d) | 150 | 200 | 250 | 300 | 350 | 400 | 500 | 600 | 800 | 1000 | 1200 |
|---|---|---|---|---|---|---|---|---|---|---|---|
| Main Equipment | Main supporting equipment models and technical and economic indicators | ||||||||||
| Vertical Preheater | YRQ04 | YRQ06 | YRQ06 | YRQ08 | YRQ08 | YRQ10 | YRQ12 | YRQ12 | YRQ14 | YRQ18 | YRQ20 |
| Rotary Kiln | φ2.5×40m | φ2.8×43m | φ3.0×48m | φ3.2×50m | φ3.3×52m | φ3.6×55m | φ3.8×58m | φ4.0×60m | φ4.3×65m | φ4.9×70m | φ5.1×72m |
| Vertical Cooler | LSF36 | LSF44 | LSF56 | LSF80 | LSF112 | ||||||
| Calcination Temperature /℃ | 1100±50 | ||||||||||
| Energy Consumption Index /(kCal/kg) | 1200±100 | ≤1150 | ≤1100 | ||||||||
| Power Consumption Index /(kW·h/t) | 40±5 | ||||||||||
| Limestone: Lime | 1.7~1.78:1 | ||||||||||
| Light and Over burnt Rate /% | ≤5 | ||||||||||
| Lime Activity /ml | ≥340(depends on the composition of limestone) | ||||||||||
| Lime Discharging Temperature /℃ | Ambient Temperature +60 | ||||||||||
| Limestone Feeding Size /mm | 10~20/20~40 | ||||||||||
| Emission Concentration /(mg/Nm3) | ≤10 | ||||||||||
| Annual Working Day / Days | ≥340 | ||||||||||
| Overhaul Cycle / Year | 1~3 | ||||||||||
| Labor / Shift | 2~3 | ||||||||||
| Applicable fuel | Coal powder, Coke oven gas, Semi-coke furnace gas, Converter gas, Blast furnace gas, Calcium carbide furnace gas, Natural gas, Diesel oil, Heavy oil, Liquefied petroleum gas, biomass fuel etc. | ||||||||||
Note: This configuration table is for reference only and varies according to project site conditions and customers requirements.