Product Description:
Lime can be divided into two types: ordinary lime and active lime.
The former is mostly fired in earth kilns and ordinary shaft kilns,
and its activity is generally within 200ml, which is mainly used
for construction and road repair; the latter is mainly composed of
mechanical shaft kilns and rotary kilns. After calcination, the
activity can reach 300~420ml. Limes calcined in rotary kilns are of
better quality, and they are mainly used in industries such as
steel smelting, chemical industry and power plant desulfurization.
Raw Material: The particle size of limestone is required to be
10-40mm, and the part exceeding the upper limit of 40mm and the
lower limit of 10mm shall not exceed 5%.
Features:
1. The combustion equipment uses energy-saving burners to
automatically control the air distribution volume to reduce the
loss of incomplete fuel combustion.
2. Rotary kiln refractory bricks adopt light-weight insulation on
the outer layer and composite bricks with refractory and
wear-resistant inner layer to reduce heat dissipation from the
outer skin of the rotary kiln.
3. There is a vertical preheater at the end of the rotary kiln,
which makes full use of the high-temperature flue gas produced by
the combustion of the rotary kiln to preheat the materials in the
preheater, so that the materials are partially decomposed in the
preheater.
4. A vertical cooler is installed at the head of the rotary kiln to
make full use of the heat contained in the high-temperature
calcined white material of the rotary kiln to preheat the secondary
air to 600°C, which improves the thermal efficiency. Yaotou mining
5. The vertical cooler and the kiln hood are integrated in the
design and construction, which has a small footprint and good
sealing, which effectively avoids the fugitive emission of hot
exhaust gas.
6. The kiln tail is environmentally friendly and dust collection is
good. The cyclone dust collector and pulse bag filter are used for
secondary dust removal, and the emission concentration is lower
than the standard.
7. The level of automation is high. The adjustment, control and
alarm of the production system are controlled by PLC in the main
control room. There are few on-site operators and high labor
efficiency.
Technical Parameters:
| 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.
Production Process:
(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 large 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 introduced 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.
