Gasifier Introductions:
Main types and technologic specification:
name | unit | specification | ||||||||
Φ2.0 | Φ2.4 | Φ2.6 | Φ3.0 | Φ3.2 | ||||||
Chamber diameter | mm | 2000 | 2400 | 2600 | 3000 | 3200 | ||||
applicable fuel |
| Non-caking or weak-caking anthracite, biruminous coal, coke, coal property should be coincident with the requiirement of GB9143 | ||||||||
Fuel size | mm | 25—50 | ||||||||
Coal consumption | Kg/h | 800~1000 | 1200~1500 | 1300~1800 | 1800~2100 | 2200~2500 | ||||
Gas agent |
| Air, steam | ||||||||
Gas output | Nm3/h | 2500~3000 | 3600~4500 | 4000~5500 | 6000~7000 | 7000~8000 | ||||
Tar | Mg/m3 | ≤100 | ||||||||
Net heating value | kJ/Nm3 | ≥5800 | ||||||||
Gas temperature | distillation stage | °C | 80~120 | |||||||
gasifying stage | °C | 400~600 | ||||||||
Gas pressure | distillation stage | Pa | 1000~1500 | |||||||
gasifying stage | Pa | 1470~1960 | ||||||||
Blast pressure | Pa | ≤6000 | ||||||||
steam products | Kg/h | 300 | 450 | 500 | 550 | 550 | ||||
Inner steam pressure |
| 0.07 | 0.07 | 0.07 | 0.07 | 0.07 | ||||
Saturated temperature | °C | 50~65 | ||||||||
Feeding coal mode |
| Automatic | ||||||||
Coal feeding system |
| Hydraulic driving | ||||||||
Hydraulic station power | Kw | 7.5×2 | 11×2 | 11×2 | 11×2 | 11×2 | ||||
Ash tray speed | r/h | 2.97 | 1.7 | 1.5 | 1.5 | 1.5 | ||||
Equipment weight | t | 70 | 85 | 95 | 110 | 130 | ||||
Oweral dimensions | H1 | m | 5.5 | 5.5 | 5.5 | 5.5 | 5.5 | |||
H2 | m | 10 | 10 | 10 | 11.5 | 11.5 | ||||
H3 | m | 13.5 | 13.7 | 13.7 | 15.2 | 15.5 | ||||
applicable gas station |
| cool gas station, hot gas station | ||||||||