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- China / 1999
50-800TPD quicklime (active lime) Production Line
- ◾ Price: Negotiable
- ◾ MOQ: Negotiable
50-800TPD quicklime (active lime) Production Line
- ◾ Price: Negotiable
- ◾ MOQ: Negotiable
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Required Quantity
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Brand name-
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Shipping / Lead TimeNegotiable / Negotiable
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Keyword
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Category
Specifications
| Size | - | Weight | - | Stock | - |
|---|---|---|---|---|---|
| Country of Origin | China | ||||
| Production method | Negotiable | ||||
Trade Terms
| Payment Terms | - | ||||
|---|---|---|---|---|---|
| Price(FOB) | Negotiable | MOQ | Negotiable | ||
| Transportation | - | ||||
| Lead time | Negotiable | Shipping time | Negotiable | ||
Company
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Country / Year Established
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Membership
- PRO
Business typeManufacturer
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Verified Certificate
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9
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9
Product Description
Main Materials:
Limestone
During all the active lime production
process, the rotary kiln production process is the most advanced one. 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
50-800TPD quicklime (active lime) production line.
OUR ADVANTAGE
1. Saving energy
Vertical preheater is equipped at the kiln
inlet. It will use the hot air from rotary kiln to preheat the raw material
which also can partially decomposed inside the preheater. This will increase
the 40% of output capacity and 30% of thermal efficiency. Vertical cooler is
equipped at the kiln outlet. It will use the high temperature from the calcined
material to heating the secondary air to 600℃. Kiln outlet adopts
integration design for vertical cooler and kiln outlet hood, and it needs less
construction land and good sealing.
2. Environmental protection
Good
dust collecting treatment at kiln inlet. The cyclone dust collector and pulse
bag filter can control the dust emission is lower than China standard. High
level of automation requires less workers, the adjusting of production system
operation, control and alarm are controlled at control room by PLC.
PRODUCTION TECHNOLOGY
10-50mm qualified limestone are fed to
receiving hopper by loader. The vibrating feeder under the hopper will feed
limestone to inclined belt and then transport to screening equipment. After
screening, the limestone will be transported to the top silo of preheater by
inclined belt conveyor. Limestone are fed from top silo to preheater through
feeding chute. At the meantime, the hot air from rotary kiln will preheating
the limestone to more than 1000℃ and also can partially decomposed. Preheated limestone are pushed
into kiln inlet by hydraulic pusher and discharged into vertical cooler after
calcination at rotary kiln. The cooling air blows by fan can cool down the
temperature of material to room temperature +60℃ and then discharged
ot of vertical cooler. After discharging from vertical cooler, active lime will
be transported to lime silo by apron conveyor, bucket elevator and belt
conveyor. Temperature of hot air from rotary kiln can be reduced to 250℃ after heat
exchange with limestone inside the preheater. Then the hot air will flow into
cylcone dust collector for primary dust collecting. After bigger size dust are
collected, the waste air will flow into bag filter for secondary dust
collecting. The emission dust concentration is less than 50mg/m3
CONFIGURATION
|
Capacity |
200t/d |
225t/d |
250t/d |
300t/d |
400t/d |
500t/d |
600t/d |
800t/d |
|
|
Preheater |
Shape |
Hexagon |
Hexagon |
Octagon |
Octagon |
Octagon |
Decagon |
Dodecagon |
Dodecagon |
|
Qty. Of Top Silo |
6 |
6 |
8 |
8 |
8 |
10 |
12 |
12 |
|
|
Qty. Of Hydraulic Pusher |
6 |
6 |
8 |
8 |
8 |
10 |
12 |
12 |
|
|
Preheating Capacity (t) |
600 |
600 |
800 |
800 |
800 |
1000 |
1600 |
1600 |
|
|
Rotary Kiln |
Size |
Φ2.8×42m |
Φ3.0×50m |
Φ3.2×50m |
Φ3.3×55m |
Φ3.6×55m |
Φ3.8×58m |
Φ4×60m |
Φ4.3×56m |
|
Slope |
3.50% |
3.50% |
3.50% |
3.50% |
3.50% |
3.50% |
3.50% |
3.50% |
|
|
Rotating Speed (r/min) |
0.3-1.8 |
0.3-1.8 |
0.3-1.8 |
0.3-1.8 |
0.3-1.8 |
0.3-1.8 |
0.3-1.8 |
0.3-1.8 |
|
|
Calcination Temperature (℃) |
1350 |
1350 |
1350 |
1350 |
1350 |
1350 |
1350 |
1350 |
|
|
Cooler |
Type |
Vertical |
Vertical |
Vertical |
Vertical |
Vertical |
Vertical |
Vertical |
Vertical |
|
Qty Of Temperature Control Area |
3 |
3 |
3 |
3 |
3 |
3 |
3 |
3 |
|
|
Qty. Of Wind Tower |
4+1 |
4+1 |
4+1 |
4+1 |
4+1 |
4+1 |
4+1 |
4+1 |
|
|
Size(m) |
3.6×3.6 |
3.6×3.6 |
3.6×3.6 |
3.6×3.6 |
4.1×4.1 |
4.1×4.1 |
4.1×4.1 |
4.7×4.7 |
|
|
Output Temperature (℃) |
≤120 |
≤120 |
≤120 |
≤120 |
≤120 |
≤120 |
≤120 |
≤120 |
|
|
Product Thermal Loss(kcal/kg) |
5500 |
5400 |
5400 |
5400 |
5400 |
5400 |
5400 |
5000 |
|
|
Available Fuel |
Coke oven gas, mixed gas, natural gas, coal powder, low
heating value coal gas |
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Contact:Ann Chen
Email:ec03 at zkcorp.com






