Table 2. Data Sources of Extraction Equilibrium for HNO₃–H₂O–TBP, UO₂(NO₃)₂–H₂O–TBP, and UO₂(NO₃)₂–HNO₃–H₂O–TBP in Diluent Systems.

		concentration range [mol/L]
system	refs	HNO3	UO2(NO3)2	TBP (vol %)	diluent
HNO3–H2O–TBP–diluent	Burns and Hanson17	0.35–10		20–30	kerosene
	Marin et al.18	1–4		15–20	dodecane
	Davis19	0.01–8.5		10–100	Amsco 125–82
	Davis et al.20	0.1–10		100
	Balasubramonian et al.21	0.01–7		30	dodecane
	Zongcheng et al.14	0–5.6		5–100	n-heptane
UO2(NO3)2–HNO3–H2O–TBP–diluent	Puzikov et al.22	0.05–5	0.01–0.257	30	paraffins
	Hlushak et al.2	1.79–5.99	0–1	30	dodecane
	Stas et al.8	0.5–7a	0–0.5a	20	kerosene
	this work	0.01–4.14	0.05–1.8	10–40	kerosene
UO2(NO3)2–H2O–TBP–diluent	Davis et al.3		0–2.5	30	Amsco 125-82

^aValues are extracted from the graph.