Table 2. Operating and Inlet Conditions of Steam Reforming Tests and Corresponding Experimental Results of χ_Ctar and Kinetic Constants k_Ctar,1^app and K_S.

	test 1	test 2	test 3	test 4	test 5	test 6
Process Conditions
P [atm]	1	1	1	1	1	1
T [°C]	800	800	750	750	700	700
W [g]	3.9	3.9	6.5	6.5	6.5	6.5
Inlet
h [-]	7.92	7.92	7.92	7.92	7.92	7.92
c [-]	7.57	7.57	7.57	7.57	7.57	7.57
FN2,in [NL min–1]	600	600	780	780	780	780
tar concentration [g Nm–3dry]	30.0	10.0	12.8	12.8	12.8	12.8
H2S equivalent [ppmv]	100	100	40	40	40	40
FCtar,in [mol min–1]	1.35 × 10–2	4.5 × 10–3	7.5 × 10–3	7.5 × 10–3	7.5 × 10–3	7.5 × 10–3
αin [molH2O molCtar–1]	6.6	19.8	19.9	19.9	19.9	19.9
βin [molN2 molH2O–1]	3.0	3.0	2.3	2.3	2.3	2.3
WHSV [molin h–1 kgcat–1]	570.0	556.1	466.0	466.0	466.0	466.0
WHSVCtar [molCtar,in h–1 kgcat–1]	20.8	6.9	6.9	6.9	6.9	6.9
Outlet
χCtar,out [%]	29.2	30.5	38.5	38.2	21.3	21.9
Kinetic Calculations
kCtar,1app [m3 kgcat–1 min–1]	0.290	0.297	0.318	0.314	0.149	0.154
kCtar,1[m3 kgcat–1 min–1]a	2.148	2.148	1.205	1.205	0.636	0.636
KS [atm–1]	64181	62269	69708	70859	82053	78466

^aCalculated at T, by eq 7 with k_Ctar,1⁰ = 297152 m³ kg_cat^–1 min^–1 and E_a,1 = 105.6 kJ mol^–1.²⁵