Effects of Metal-Support Interactions and Interfaces on Catalytic Performance over M₂O₃- (, Al-) Supported Ni Catalysts

Table 2

Comparison of the catalytic performances with previously reported catalysts.

References	Catalyst and its specific surface area (m^2/g)	Temperature of reaction (°C)/molar ratio of water to carbon	GHSV ethanol-water vapor (mL/gcat·h)	Inactivation rate of activity (%)^a/time on stream (h)	Rate of carbon deposit (mg/gcat·h)
[29]	Ni15LaSn950 (62)	650/4.5	41000	1/80	0.78
[30]	1CeNi/SBA-15 (538)	650/4	57000	10/50	1.6
[31]	Ni-1Ce/MMT (67.2)	650/2	—	8.9/50	—
[19]	Meso-3LaNiAl (202)	600/2	57000	0/50	2.28
[32]	Ni-0.25Sn/CeO2 (7.3)	600/5	57000	5/20	—
[33]	Ni/Ce0.8Zr0.2 (85)	600/2.5	60000	10/10	27
[34]	Ni/La2O3-α-Al2O3 (33.9)	700/6	13800	0/4	2.6
[35]	Ir/CeO2 (148)	650/1.5	18000	35/300	—
[36]	Ni-Ce-La (76)	550/3	7742	10/60	1
[37]	Ni/10 mg-ATP (356.7)	700/1.5	19200	2/50	6.1
[38]	Ni/MgO (28)	650/4.2	80000	42/24	2.4
[20]	Ni-CeO2 (29.4)	600/2	55920	17.1/50	2.6
This work	Ni-La2O3 (23.3)	600/2	55920	6.1/50	3.0