1.Technical parameters
| NO. |
Name |
Parameter |
| 1 |
The raw materials: |
waste tyres,/rubber/plastic/oil sludge |
| 2. |
output |
Fuel oil |
| 3 |
Daily capacity: |
2-3 ton /day |
| 4 |
The size of reactor (D*L) |
1800*4000mm |
| 5 |
Reactor material |
Q345R |
| 6 |
Average oil productivity: |
30%-50%, (for tire ) |
| 7 |
Average carbon productivity: |
30%-35% (for tire) |
| 8 |
Average steel productivity: |
10%-15% (for tire) |
| 9 |
Average waste-gas productivity: |
5-8% |
| 10 |
pyrolysis time |
6hours |
| 11 |
Discharge time |
1 hour |
| 12. |
Feeding time |
1 hour |
| 13 |
Cooling time |
2 hours |
| 14 |
Working pressure |
Normal /slightly negative |
| 15 |
Power |
11 kw |
| 16 |
Fuel |
Coal. Wood, gas etc |
| 17 |
Working area |
300 square meters |
| 18 |
Total weight |
26 000kgs |
| 19 |
Reactor rotate speed |
0.25-0.4/min |
| 20. |
Noise |
No more than 85 db |
|
Type |
NEW TECH Pollution free |
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
slag out device
control board
3. Work flow
loading plastic into reactor
heating reactor
after heating , solid plastic converted to oil gas
oil gas go into oil-gas separator ,heavy oil deposit and go to heavy oil tank, light oil gas go to cooling system
after cooling ,light oil gas change to liquid oil and go into light oil tank
non-liquid oil gas will to water sealing tank, then back to combustor burning to heat reactor as fuel
smoke produced by heating reactor will go to dedust system, after dedust system treatment , smoke change to white clean waster steam ,then go to sky through chimney.
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. Plant features:
| 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 ( ºC) |
-10 |
0 |
| Flash point (closed ) ( ºC) |
45 |
55 |
| Movement viscosity |
3.5 |
(20 ºC) mm2/s
3.0-8.0 |
| Combustion value(Kcal) |
9500 |
8500 |
| colority |
1.2 |
≤3.5 |
| cetane number |
40 |
45 |
| Acidity |
/ |
MGkoh/100ml≤7 |
1)Carbon slag using new tech, slag in sealing way, keep sure no carbon powder flay in air, completely pollution free. Carbon slag automatic and slag more fast than normal design
2)Improved an simplified design of plant, more easy to use, and cut down plant cost
3)All parts including small parts we use high standard material to keep our quality for long term usage.
4) Dedust system use latest design, no black smoke emit to air by chimney.
6.oil parameter
| 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 ( ºC) |
-10 |
0 |
| Flash point (closed ) ( ºC) |
45 |
55 |
| Movement viscosity |
3.5 |
(20 ºC) mm2/s
3.0-8.0 |
| Combustion value(Kcal) |
9500 |
8500 |
| colority |
1.2 |
≤3.5 |
| cetane number |
40 |
45 |
| Acidity |
/ |
MGkoh/100ml≤7 |
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