1.Technical parameters
| NO. |
Name |
Parameter |
| 1 |
The raw materials: |
Tyres |
| 2 |
Daily capacity: |
20 Ton/day |
| 3 |
The size of reactor |
11*2.2*2 m |
| 4 |
Reactor material |
Q345R |
| 5 |
Average oil productivity: |
30%-50%, |
| 6 |
Average carbon productivity: |
30%-35% |
| 7 |
Average steel productivity: |
10%-15% |
| 8 |
Average waste-gas productivity: |
5-8% |
| 9 |
pyrolysis time |
10-12 hours |
| 10 |
Discharge time |
1.5 hour |
| 11 |
Feeding time |
3 hour |
| 12. |
Cooling time |
3 hours |
| 13 |
Working pressure |
Normal /slightly negative |
| 14 |
Power |
21 kw |
| 15 |
Fuel |
Coal. Wood, gas etc |
| 16 |
Working area |
1000 square meters |
| 17 |
Total weight |
40 000kgs |
| 18 |
Reactor rotate speed |
0.25-0.4/min |
| 19. |
Noise |
No less than 85DB |
| 20. |
Certificate |
CE.,ISO |
2. Major parts :
reactor with base and cover
oil -gas separator
heavy oil tanl
cooling system
light oil tank
water sealing
dedust system
waste gas recycle system
control board
3.Plant features:
1.) Reactor is tube or tunnel type with full open door
2.) Feed raw material by trolley, more fast and easy, high efficiency
3.) Whole tyre can be put in trolley then push trolley inside reactor , no need to cut tire, saving working time and labor
4.) After pyrolysis , carbon salg is in cloddy shape, no carbon powder, no carbon powder fly in air
5.) carbon discharge by trolley more fast and no powder fly in air, more environmental
6.)Static pyrolysis, reacator non-rotate, produce higher quality oil with less dust
7.) Pyrolsysis reacator non-rotate, no need reducer nor motor to drive, saving power electricity
4. oil rate
| Oil yied/day |
Waste tire/ rubber |
Big tyres |
45%--50% |
| Car tyres |
40% |
| Bicycles and motorcycles tyres |
30%--35% |
| Waste plastic |
Fishing net |
45%--50% |
| Safety net , farm-oriented film |
| Conwenient bags , weave bags |
40% |
| Off cut of recycled paper mill |
20%--30% |
5. Working flow or steps:
A. Feed tyre into trolley
B, move trolley inside tube type reactor
C.closed the reactor door ,heating reactor
D. Pyrolysis finished, stop burning fire, cool down reator
E.open the door of reactor
F.pull the strolley out of reactor , now only carbon slag inside trolley.
G. take carbon slage out of reactor
H, Feeding tyre agian, begain next batch
6.oil parameter
| project |
Tire oil |
Plastic oil |
| Water content |
3%-5% |
3%-5% |
| Sulfur content |
0.3%-0.5% |
0.3% |
| Density (g/ml) |
0.86-0.94 |
0.84-0.94 |
| Cetane number |
30 |
30 |
Combustion value
(kcal) |
9500 |
9000 |
| Asphalt |
≤0.5% |
≤0.8% |
| Ash |
≤1% |
/ |
| Impurity |
1%-3% |
/ |
| Solidifying point( ºC) |
-10 |
10 |
| Flash point ( ºC) |
30-40 |
20-35 |
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