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. 2022 Apr 1;15(7):2597.
doi: 10.3390/ma15072597.

Influence of Resorcinol to Sodium Carbonate Ratio on Carbon Xerogel Properties for Aluminium Ion Battery

Affiliations

Influence of Resorcinol to Sodium Carbonate Ratio on Carbon Xerogel Properties for Aluminium Ion Battery

Martin Eckert et al. Materials (Basel). .

Abstract

Carbon xerogels were synthesized using a soft-template route with resorcinol as the carbon source and sodium carbonate as the catalyst. The influence of the resorcinol to catalyst ratio in the range of 500-20,000 on pore structure, graphitic domains, and electronic conductivity of as-prepared carbon xerogels, as well as their performance in an aluminium ion battery (AIB), was investigated. After carbonization steps of the polymers up to 800 °C, all carbon samples exhibited similar specific volumes of micropores (0.7-0.8 cm³ g-1), while samples obtained from mixtures with R/C ratios lower than 2000 led to carbon xerogels with significantly higher mesopore diameters up to 6 nm. The best results, in terms of specific surface (1000 m² g-1), average pore size (6 nm) and reversible capacity in AIB cell (28 mAh g-1 @ 0.1 A g-1), were obtained with a carbon xerogel sample synthetized at a resorcinol to catalyst ratio of R/C = 500 (CXG500). Though cyclic voltammograms of carbon xerogel samples did not exhibit any sharp peaks in the applied potential window, the presence of both oxidation and a quite wide reduction peak in CXG500-2000 cyclic voltammograms indicated pseudocapacitance behaviour induced by diffusion-controlled intercalation/de-intercalation of AlCl4- ions into/from the carbon xerogel matrix. This was confirmed by shifting of the (002) peak towards lower 2θ angle values in the XRD pattern of the CXG500 electrode after the charging step in AIB, whereas the contribution of pseudocapacitance, calculated from half-cell measurements, was limited to only 6% of overall capacitance.

Keywords: Raman; X-ray diffraction; aluminium-ion battery; carbon; conductivity; intercalation; pseudo-capacitance; resorcinol; soft-template; xerogel.

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Conflict of interest statement

The authors declare no conflict of interest. The funders had no role in the design of the study; in the collection, analyses, or interpretation of data; in the writing of the manuscript, or in the decision to publish the results.

Figures

Figure A1
Figure A1
Long-term cycling of CXG500 in AIB full-cell setup.
Figure A2
Figure A2
Scan-rate variation of cyclic voltammograms for CXG500||Al (a) and natural graphite||Al (b).
Figure A3
Figure A3
Determination of b-values in CXG500||Al at the anodic (a) and cathodic (b) CV scan and for natural graphite for intercalation peaks a1–5 (c) and deintercalation peaks c1–4 (d).
Figure A3
Figure A3
Determination of b-values in CXG500||Al at the anodic (a) and cathodic (b) CV scan and for natural graphite for intercalation peaks a1–5 (c) and deintercalation peaks c1–4 (d).
Figure 1
Figure 1
As-prepared resorcinol-formaldehyde resins after drying step from high catalyst concentration (R/C = 50) on the left side to low concentration (R/C = 20,000) on the right side.
Figure 2
Figure 2
Characterisation of CXG by isotherms (a), pore size distribution with respect to Vsum (b), contribution of microporous and mesoporous pore volume and surface area (c) and repartition of relative mesopore and micropore volume (d).
Figure 3
Figure 3
XRD diffractogram of selected CXG and natural graphite (a). Stacking width LA and stacking height LC of graphene crystallites as a function of R/C ratio during CXG synthesis (b).
Figure 4
Figure 4
Raman spectra of selected CXG (a). Position of D and G-band as well as ΓD- and ΓG-band as a function of R/C value (b).
Figure 5
Figure 5
Conductivity and density values of CXG powders as a function of R/C ratio.
Figure 6
Figure 6
SEM images of CXG500 (a), CXG750 (b), CXG1000 (c), CXG1500 (d), CXG2000 (e), CXG2500 (f) and natural graphite powders (g) at 5 kV.
Figure 6
Figure 6
SEM images of CXG500 (a), CXG750 (b), CXG1000 (c), CXG1500 (d), CXG2000 (e), CXG2500 (f) and natural graphite powders (g) at 5 kV.
Figure 7
Figure 7
CVs of selected CXGs and natural graphite in 1:1.5 n(EmimCl):n(AlCl3) electrolyte (a) and influence of average pore size on max. current density taken from CVs of selected CXG at 2.25V (b). Deconvoluted current contribution of non-diffusion limited (pseudo)capacitance and diffusion-limited Faradaic currents in CXG500||Al (c) and in graphite||Al (d). “(pseudo)capacitance” designation comprises both EDLC and pseudocapacitance contribution.
Figure 7
Figure 7
CVs of selected CXGs and natural graphite in 1:1.5 n(EmimCl):n(AlCl3) electrolyte (a) and influence of average pore size on max. current density taken from CVs of selected CXG at 2.25V (b). Deconvoluted current contribution of non-diffusion limited (pseudo)capacitance and diffusion-limited Faradaic currents in CXG500||Al (c) and in graphite||Al (d). “(pseudo)capacitance” designation comprises both EDLC and pseudocapacitance contribution.
Figure 8
Figure 8
Charging/discharging experiments of CXG500 (a), CXG750 (b), CXG1000 (c), CXG1500 (d), CXG2500 (e) and natural graphite (f) in Swagelok-type straight-cells with tungsten as cathodic current collector and aluminium rod as anode in n(EMimCl):n(AlCl3) 1:1.5 electrolyte.
Figure 9
Figure 9
Charging and discharging curves of AIBs equipped with CXG500–2500 (a) and natural graphite for comparison (b).
Figure 10
Figure 10
Ex situ XRD analysis of pristine and fully charged natural graphite and CXG500 electrodes. Peaks marked with (*) indicate position of (002) peak in both pristine electrodes. The peak marked with (∆) is assumed to be associated with the (002) peak shift due to intercalated species in CXG500. Peaks indexed with (◊) are related to GIC-induced peaks in natural graphite sample.

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