Name		Unit	Specification
			Ф2. 0	Ф2. 4	Ф2. 6	Ф3. 0	Ф3. 2
Chamber diameter		Mm	2000	2400	2600	3000	3200
Applicable fuel			Non-caking or weak-caking anthracite, biruminous coal, coke, coaproperty should be coincident with the requirement 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
oil content in dust		Mg/m3	≤100
Net heating value		kJ/Nlm3	≥5800
Gas temperature	Distillationstage	℃	80-120
	Gasifyingstage	℃	400-600
Gas pressure	Distillationstage	Pa	1000-1500
	Gasifyingstage	Pa	1470-1960
Biast 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		℃	50-65
Feeding coal mode			Automatic
Coal feeding system			Hydraul ic dr iving
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
Saturated temperature		Cool gas station, hot gas station