Table 2.

Key process assumptions regarding the RJF conversion technologies [8, 29, 30, 55, 56]

Process	Unit	HEFA [29]	FT [55]	Pyrolysis [56]		HTL [56]		ATJ [30]	DSHC [8]
Sub-process				Ex situ	In situ	Ex situ	In situ		Increased blend level	10% blend level
Inputs
Feed	MJ feed/MJ RJF	1.17	12.93	26.39	26.39	16.89	16.89	1.49a	6.28	3.25
Natural gas consumptionb	MJ/MJ RJF	0.18
Electricity consumption	MJ/MJ RJF	0.005			1.53	0.21	0.86	0.03
Hydrogen consumption	MJ/MJ RJF	0.15		5.44		1.31		0.08	0.52	0.12
Hydrogen feedstock		Natural gas		Natural gas	Process off-gases	Natural gas	Process off-gases and waste water	Natural gas	Natural gas	Natural gas
Outputs
Co-product allocation ratio
RJF	Normalized	1	1	1	1	1	1	1	1	1
Diesel	MJ/MJ RJF		3.00	2.95	2.95	2.95	2.95	0.12	0.15
Gasoline	MJ/MJ RJF		1.69	7.88	7.88	4.57	4.57
Heavy fuel oil	MJ/MJ RJF			2.17	2.17	1.65	1.65
Naphtha	MJ/MJ RJF	0.14						0.21	0.54
Propane	MJ/MJ RJF	0.10	0.49
Methane	MJ/MJ RJF		0.24
Electricity	MJ/MJ RJF		0.45	0.51					0.13	0.07

^aFeedstock is ethanol

^bExcluding natural gas used for hydrogen generation