Active lime is made from minerals with high calcium carbonate content, such as limestone, dolomite, and chalk, which are calcined at 1000-1100°C. The choice of active lime production process is determined by many factors: investment cost, lime activity requirements, fuel selection, raw material size, system capacity requirements, and environmental protection requirements. We will determine the production process according to the customer's specific conditions and requirements.
Active lime production line refers to the whole process of active lime production. Our production process adopt the rotary kiln with the vertical preheater and vertical cooler for the limestone calcination to achieve the production requirements of energy saving, environmental protection, the high activity.
We can provide technological solutions and complete production equipment for 50-1200TPD quicklime (active lime) production line. We adopt the new type, energy saving and environmental system, through which fuel consumption can be reduced 40%, output capacity increased 30%.
1. Advanced Technology: The calcination process adopts pre-heater+ rotary kiln+ vertical cooler system, it can reduce the fuel consumption 40%, and increase output capacity 30% due to reuse the waste gas in the system.
2. High Automation Level: The Production line is arranged with temperature and pressure monitoring instrumentation, operating parameters of the computer display, the production line can adopt the advanced computer control, to achieve automatic operation of the entire system.
3. Mature Experience: We have professional engineer team, mature experience, and over 100 successful project cases from home and abroad, to maximize your investment costs and meet the customized solution demand.
4. Good dust collecting treatment: The cyclone dust collector and pulse bag filter can control the dust emission is lower than China standard.
(1) Raw material storage, transportation and delivery
Limestone with a particle size of 10-50mm is transported to the factory area and stacked in the stockyard. Loaders are used for the stockyard operations. The material with qualified particle size is loaded into the receiving trough set up in the material yard by the loader, and under the receiving trough is quantitatively fed by the feeder, the stone is fed to the inclination conveyor, and then sent to the screening building, where the limestone is screened After being divided, the qualified particle size is weighed and sent to the silo on the top of the preheater by a large inclination conveyor. The powder under the sieve is sent to the storage yard by the 3# conveyor and is regularly transported out by a forklift.
(2) Limestone calcination
Limestone calcination is composed of a vertical preheater + a rotary kiln + a vertical cooler, with an output of 100~1200t/d. The material is fed into the preheater body from the silo on the top of the preheater through the discharge chute, and at the same time by the rotary kiln The incoming high-temperature flue gas preheats the material to above 1000°C to partially decompose the limestone, and then is pushed into the tail of the rotary kiln by a hydraulic push rod in turn, after being calcined at a high temperature in the rotary kiln, it is discharged into the cooler and blown in by a fan The material is cooled by the cold air, and the material is cooled to the ambient temperature +60 ℃ or less and discharged from the cooler. The air blown in by the cooler enters the rotary kiln as secondary air to participate in combustion.
(3) Finished product delivery
The finished lime is unloaded from the cooler and transported to each finished lime storage by chain conveyor, bucket elevator and belt conveyor. The discharge valve under the lime storage silo is used to load the lime in the silo into cars and tankers for transportation. Set up storage silos of different sizes according to customers' reserve requirements.
The finished product silo adopts circular silo, 2 5-50mm finished product silo, 1 finished product silo less than 5mm, the volume of each silo is about 800t;
(4) Flue gas treatment
The high-temperature flue gas generated by the combustion of the rotary kiln is exchanged with limestone in the preheater, and the temperature is reduced to below 250 ℃, and then enters the cyclone dust collector for primary dust collection to collect large particles of dust, and then It enters the bag filter and is discharged into the atmosphere by a high-temperature fan after dust removal. The dust concentration of the exhaust gas is less than 30mg/m3. A cold air control system is installed at the inlet of the dust collector to protect the dust collector.
Capacity(t/d) | 150 | 200 | 250 | 300 | 350 | 400 | 500 | 600 | 800 | 1000 | 1200 |
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Major 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 | ||||||||||
Lime overburning rate /% | ≤5 | ||||||||||
Lime activity /ml | ≥340(It depends on the composition of limestone) | ||||||||||
Ash out temperature /℃ | Ambient temperature +60 | ||||||||||
Granularity of limestone into kiln /mm | 10~20/20~40 | ||||||||||
Emission concentration /(mg/Nm3) | ≤10 | ||||||||||
Annual working days / day | ≥340 | ||||||||||
Overhaul cycle / year | 1~3 | ||||||||||
Number of operators / (people / class) | 2~3 | ||||||||||
Available Fuel | Pulverized coal, coke oven gas, blue charcoal furnace gas, converter gas, blast furnace gas, calcium carbide furnace gas, natural gas, diesel, heavy oil, liquefied petroleum gas, biomass fuel |