Tire To Diesel Recycling Plant Pyrolysis And Distilation Combined
Tire To Diesel Recycling Plant Pyrolysis And Distilation Combined
1.plant parameters:
1 |
The raw materials: |
waste tyres,/plastic, oil sludge |
2 |
Daily capacity: |
10 ton/day |
3 |
The size of reactor |
2800*6000mm 16mm thickness |
4 |
Reactor material |
Q345R |
5 |
Average oil productivity: |
30%-80%, |
6 |
Average carbon productivity: |
20%-35% |
7 |
Plastic oil rate |
30%-80% |
8 |
pyrolysis time |
6-8 hours |
9 |
Discharge time |
1.5 hour |
10 |
Feeding time |
3 hourS |
11 |
Cooling time |
3 hours |
12. |
Working pressure |
Normal /slightly negative |
13 |
Power |
21 kw |
14 |
Fuel |
Coal. Wood, gas etc |
15 |
Working area |
1000 square meters |
16 |
Total weight |
35 000kgs |
17 |
Reactor rotate speed |
0.25-0.4/min |
18 |
Noise |
No less than 85DB |
19. |
Certificate |
Ce,.iso, |
20. |
Carbon slag out |
Automatic |
2.Plant Featurs:
A. one machine can be used for several material, such as tyre, rubber ,plastic, waste oil ,sludge oil, black oil ETC.
B.By using our catalyst , can increase about 13-15% oil rate than normal plant
C.More easy to use, simplifed and improved the working -art, more simple ,and more easy to use
D. Removed non-necessary parts, more efficiency and cut plant cost
E.Carbon slag more fast .shorten working time.
F. Pyrolysis and distillation togehter in one set plant, saving working area,saving fuel .
3.Major configuration:
|
Parts name |
specification |
qty |
1. |
Reactor |
2800*6000mm*16mm |
1 set |
2. |
Reactor base |
|
1 set |
3. |
cover |
|
1 set |
4. |
Oil bag |
1000*1500mm |
1 pc |
5. |
Heavy oil tank |
900*1500mm |
1 pc |
6. |
Cooling tank |
4000*6000*15000mm |
1 set |
7. |
Light oil tank |
1500*3000mm |
1 pc |
8. |
Water sealing tank |
900*1500mm |
2 pcs |
10, |
Dedust system |
12000*3000mm |
1 pc |
11 |
Waste gas recycling device |
|
1 set |
12 |
Electric control board |
Big size |
1 set |
13 |
Carbon slag machine |
|
1 set |
14 |
caalyst chamber |
1set |
|
15 |
Cooling pipe |
108*6000 |
20 pcs |
16. |
distillation tower |
1000*3000mm
|
|
4.The raw mateial
5.Final Oil
Project |
diesel |
standard |
Oxidation stability |
2.2 |
≤2.5 mg/100ml |
Sulfur content |
0.3 |
M/m≤0.2 |
10% steamed residual carbon residue |
0.33 |
M/m≤0.3 |
Ash content (10%) |
0.16 |
%m/m≤0.01 |
Waste content (10%) |
traces |
/ |
Mechanical impurities |
/ |
/ |
Density (g/ml) |
0.85 |
0.83-0.87 |
Solidifying point ( ℃) |
-10 |
0 |
Flash point (closed ) ( ℃) |
45 |
55 |
Movement viscosity |
3.5 |
(20 ℃) mm2/s 3.0-8.0 |
Combustion value(Kcal) |
9500 |
8500 |
colority |
1.2 |
≤3.5 |
cetane number |
40 |
45 |
Acidity |
/ |
MGkoh/100ml≤7 |
6. Plant pictures:
7.Other speciciation for your references
|
Pyrolysis plant |
Type |
Daily capacity |
Batch type |
5Ton 10ton 12ton 15ton |
|
Semi-continuous type |
15Ton, 20Ton |
|
Fully continuous type |
20ton 30ton 60ton |
|
Special type |
20Ton 15ton |
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