Table 12. Promoted Ni Based Catalysts Reported in the Literature for the Pyrolysis and In-line Steam Reforming of Biomass and Plastic Mixtures.

Catalyst	Feed	Preparation methoda	Reactor configuration	Operating conditionsb	H2 conc. (vol %)	H2 prod. (wt %)	Ref.
35.4Ni-Mg-Al 1:1:1	PP-wood sawdust	cp	fixed/fixed (2 g)	TP = 600 °C	51.0	6.3	Kumagai et al.198
				TR = 800 °C
				steam = 0.05 g min–1
21.1Ni-Mg-Ca-Al 1:1:1:2	PP-wood sawdust PP	cp	fixed/fixed (2 g)	TP = 600 °C	51.5	6.2	Kumagai et al.198
				TR = 800 °C
				steam = 0.05 g min–1
5-20Ni-Ca-C	LDPE-pine sawdust (5:5)	cp	fixed/fixed (0.5 g mixture)	TP = 700 °C	86.7	23.1	Chai et al.53
				TR = 600 °C
				steam = 5 mL h–1
10Ni-Ca-C	HDPE-pine sawdust (5:5)	cp	fixed/fixed (0.5 g mixture)	TP = 800 °C	80.4	14.0	Chai et al.166
				TR = 700 °C
				steam = 5 mL h–1
10Ni-Ca-C	PP-pine sawdust (5:5)	cp	fixed/fixed (0.5 g mixture)	TP = 800 °C	59.4	13.8	Chai et al.166
				TR = 700 °C
				steam = 5 mL h–1
10Ni-Ca-C	PS-pine sawdust (5:5)	cp	fixed/fixed (0.5 g mixture)	TP = 800 °C	38.5	13.2	Chai et al.166
				TR = 700 °C
				steam = 5 mL h–1

^acp, Co-impregnation.

^bT_P = Pyrolysis temperature; T_R = reforming temperature.