Steam Reforming of Glycerol for Hydrogen Production over Ni/SiO₂ Catalyst

Table 3

Glycerol conversion and product gas distribution in the glycerol steam reforming over Ni/SiO₂ (3 × 5 mm).

S. no.	Temp (°C)	GWMRs	Glycerol conversion (%)	Product gas distribution (vol %)
				H2	CO2	CO	CH4
1	500	1 : 9	82	63	21.5	4.5	11
2	550	1 : 9	94	63.5	22.5	7.5	6.5
3	600	1 : 9	100	66	18	12.5	3.5
4	600	1 : 12	100	67.5	22.5	8.5	1.5
5	600	1 : 15	100	68.5	23.9	6.9	0.6
6	600	1 : 18	100	69.5	25	5	0.5