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Article

Extraction of cerium(III) with N, N′-dimethyl-N, N′-dioctyl-diglycolamide in [Bmim][PF6] compared in 40% octanol/kerosene

ORCID Icon, , , , , , , , & show all
Pages 580-587 | Received 23 Oct 2018, Accepted 04 Apr 2019, Published online: 14 Apr 2019

Figures & data

Figure 1. (a): Structure of N, N′-dimethyl-N, N′-dioctyl-diglycolamide (DMDODGA = L). (b): Structure of [Bmim][PF6].

Figure 1. (a): Structure of N, N′-dimethyl-N, N′-dioctyl-diglycolamide (DMDODGA = L). (b): Structure of [Bmim][PF6].

Figure 2. Dependence of the extraction of Ce(III) on the acid concentration in aqueous solution. Black circles: L-[Bmim][PF6] system, black squares: L-40% octanol/kerosene system, black triangle: pure [Bmim][PF6] system. ([L]ILs = 0.024 M, [L]o = 0.112 M, [Ce(III)]aq = 3.4 × 10–3 M).

Figure 2. Dependence of the extraction of Ce(III) on the acid concentration in aqueous solution. Black circles: L-[Bmim][PF6] system, black squares: L-40% octanol/kerosene system, black triangle: pure [Bmim][PF6] system. ([L]ILs = 0.024 M, [L]o = 0.112 M, [Ce(III)]aq = 3.4 × 10–3 M).

Figure 3. Effect of the initial concentrations of [Bmim]Cl and NaCl on the extraction of Ce(III) by L-[Bmim][PF6] system. ([L]ILs = 0.030 M, [Ce(III)]aq = 3.4 × 10–3 M, [HNO3] = 1 M).

Figure 3. Effect of the initial concentrations of [Bmim]Cl and NaCl on the extraction of Ce(III) by L-[Bmim][PF6] system. ([L]ILs = 0.030 M, [Ce(III)]aq = 3.4 × 10–3 M, [HNO3] = 1 M).

Figure 4. Effect of the H+ and NO3 concentration on the extraction of Ce(III) by L-40% octanol/kerosene system. (black circles: [H+]ini = 2 M, black squares: [NO3]ini = 2 M, [L]o = 0.0715 M, [Ce(III)]aq = 3.4 × 10–3 M).

Figure 4. Effect of the H+ and NO3− concentration on the extraction of Ce(III) by L-40% octanol/kerosene system. (black circles: [H+]ini = 2 M, black squares: [NO3−]ini = 2 M, [L]o = 0.0715 M, [Ce(III)]aq = 3.4 × 10–3 M).

Figure 5. Slope analysis of Ce(III) extraction as a function of the concentration of L-[Bmim][PF6] system and L-40% octanol/kerosene system. ([Ce(III)]aq = 3.4 × 10–3 M, [HNO3] = 1 M).

Figure 5. Slope analysis of Ce(III) extraction as a function of the concentration of L-[Bmim][PF6] system and L-40% octanol/kerosene system. ([Ce(III)]aq = 3.4 × 10–3 M, [HNO3] = 1 M).

Figure 6. Ce(III) loading capacity of L-[Bmim][PF6] and L-40% octanol/kerosene system. (L-[Bmim][PF6] system: [L]ILs = 0.026 M, [Ce(III)]aq = 3.5 × 10–3 M, [HNO3] = 0.1 M; L-40% octanol/kerosene system: [L]o = 0.106 M, [Ce(III)]aq = 3.4 × 10–3 M, [HNO3] = 1 M).

Figure 6. Ce(III) loading capacity of L-[Bmim][PF6] and L-40% octanol/kerosene system. (L-[Bmim][PF6] system: [L]ILs = 0.026 M, [Ce(III)]aq = 3.5 × 10–3 M, [HNO3] = 0.1 M; L-40% octanol/kerosene system: [L]o = 0.106 M, [Ce(III)]aq = 3.4 × 10–3 M, [HNO3] = 1 M).

Figure 7. IR spectra of different systems. (a) L; (b) Ce(III)-L in 40% octanol/kerosene system; (c) [Bmim][PF6]; (d) L-[Bmim][PF6]; and (e) Ce(III)-L-[Bmim][PF6]. ([L]ILs = 0.024 M, [Ce(III)]aq = 3.4 × 10–3 M, [HNO3] = 1 M).

Figure 7. IR spectra of different systems. (a) L; (b) Ce(III)-L in 40% octanol/kerosene system; (c) [Bmim][PF6]; (d) L-[Bmim][PF6]; and (e) Ce(III)-L-[Bmim][PF6]. ([L]ILs = 0.024 M, [Ce(III)]aq = 3.4 × 10–3 M, [HNO3] = 1 M).

Figure 8. The proposed extraction process of L-[Bmim][PF6] system with Ce(III) at low nitric acid concentration.

Figure 8. The proposed extraction process of L-[Bmim][PF6] system with Ce(III) at low nitric acid concentration.

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