From Wastes to Anode Materials for Na-Ion Batteries

PDF Publication Title:

From Wastes to Anode Materials for Na-Ion Batteries ( from-wastes-anode-materials-na-ion-batteries )

Previous Page View | Next Page View | Return to Search List

Text from PDF Page: 008

Batteries 2022, 8, 183 the fourth one, while C-FFP2 (Figure 5b) showed an initial 37% reversibility, increasing to 86% at cycle 4. As previously mentioned, the low initial reversibility was imputable to the SEI formation, while in the following cycles, the SEI reached stabilization and acted as a protective layer. In the following cycles, the broad peak in the 0.05–1 V range was associated with the reversible redox process of Na intercalation/absorption in the biochar composite (a) 30 -30 -60 -90 -30 (a) 400 300 200 100 0 The electrochemical impedance spectroscopy (EIS) was measured at open circuit 500 (b) 500 voltage (OCV) after 3 h of rest at OCV and after the cyclic voltammetric test (the electrode. 8 of 13 (b) 30 00 0.0 0.5 1.0 1.5 2.0 2.5 3.0 E vs. Na+/Na Cycle 1 Cycle 1 Cycle 2 Cycle 3 Cycle 4 0.0 0.5 1.0 1.5 2.0 2.5 3.0 E vs. Na+/Na Cycle 2 -60 Cycle 3 Cycle 4 Batteries 2022, 8, x FOR PEER REVIEW Figure 5. Cyclic voltammetric profiles of C-surgical (a) and of C-FFP2 (b) in 1 M NaClO4 in PC -90 Figure 5. Cyclic voltammetric profiles of C-surgical (a) and of C-FFP2 (b) in 1 M NaClO4 in PC recorded at a scan rate of 0.1 mV s−1 in t−h1e 0.05–3 V vs. Na+/Na ra+nge. recorded at a scan rate of 0.1 mV s in the 0.05–3 V vs. Na /Na range. corresponding Nyquist plots are shown in Figure 6). Both the fresh cells were 400 characterized by a very low intercept with the real axis (around 5 Ω), corresponding to a very low bulk resistance (Rb, mainly associated with the resistance of the electrolyte). The fresh cell 300 fresh semicircle amplitudaeftewr 3ahsreastssociated with the charge transfer resistance (Rafctet)r 3ohfreNst a+ ion after CV after CV diffusion between the electrode and the electrolyte. In contrast, the final straight line in 200 the low-fr6e0quency range was associated with a Warburg capacitance, associated with the diffusion 4o0f ions [49,50]. After 3 h, Rct increased for both samples (up to 100 Ω in the real 40 B (-Im(Z)/Ohm) Current density (mA cm-2g-1) B (-Im(Z)/Ohm) Current density (mA cm-2g-1) part for C-surgical), thus it was most likely associated with the interfacial layer growth 20 100 20 between the electrode and the electrolyte (SEI) [51]. Finally, after voltammetric cycling 00 0 20 40 60 80 100 120 140 0 20 40 60 80 100 120 140 (blue square spectra), the overall cell r0esistance decreased, most likely suggesting a 0 100 200 300 0 100 200 300 + stabilization of the SEI upon cycling, indicating a much easier diffusion of Na ions from Re(Z)/Ohm Re(Z)/Ohm the electrolyte to the electrode after a few electrically promoted cycles [50]. Figure 6. EIS spectra of C-surgical (a) and of C-FFP2 (b) in 1 M NaClO4 in PC vs. Na, recorded at Figure 6. EIS spectra of C-surgical (a) and of C-FFP2 (b) in 1 M NaClO4 in PC vs. Na, recorded at three different stages, i.e., just after assembling the cell, after 3 h of rest at OCV and after the cyclic three different stages, i.e., just after assembling the cell, after 3 h of rest at OCV and after the cyclic voltammetric analysis shown in Figure 5. voltammetric analysis shown in Figure 5. C-surgical and C-FFP2 showed similar behavior during galvanostatic cycling, as seen C-surgical and C-FFP2 showed similar behavior during galvanostatic cycling, as seen in Figure 7. Plots (a) and (d) highlight the charge/discharge profiles of C-surgical and C- in Figure 7. Plots (a) and (d) highlight the charge/discharge profiles of C-surgical and FFP2, respectively, in a Na-metal cell with the configuration Na/NaClO4/C at different C-FFP2, respectively, in a Na-metal cell with the configuration Na/NaClO4/C at different current regimes (C/20, C/10, C/5, C/2 and 1C) in the 0.05–3 V vs. Na+/Na r+ange. Typical current regimes (C/20, C/10, C/5, C/2 and 1C) in the 0.05–3 V vs. Na /Na range. Typical sloping profiles for hard carbon anodes upon reversible insertion/deinsertion of Na+ ions+ sloping profiles for hard carbon anodes upon reversible insertion/deinsertion of Na ions were observed. The specific capacity delivered by the cell exceeded 100 mAh g were observed. The specific capacity delivered by the cell exceeded 100 mAh g for surgical and 115 mAhg −1 −1 for C-FFP2 during the initial cycles at a C/20 rate. A capacity drop C-surgical and 115 mAhg for C-FFP2 during the initial cycles at a C/20 rate. A capacity occurred upon doubling the current rate to C/10, delivering 82 and 98 mAh g−1, −1 drop occurred upon doubling the current rate to C/10, delivering 82 and 98 mAh g , respectively. Further increases in the current rate caused a progressive decrease in the respectively. Further increases in the current rate caused a progressive decrease in the −1−1 −1−1 specifsicpeccaipfiaccictaypvaacliutyesv,awluheicsh,wheirceh6w4earned6840amndA8h0gmAathCg/5,4a3taCn/d55,843maAnhdg58amtACh/2g, at −1 −1 and 30C/an2,dan45dm30Aahndg45amt 1ACh. Ogveraatl1l,Ct.hOevoevrearlpl,ottheenotivaelripnoctrenatsiealwinhcirleaisnecrwehasiliengintchreaCsi-ngthe rate wCa-srartaethwearslirmatihtedr,liamccitoeudn,taicncgoufonrtitnhgefgoorotdheegleocotrdoenlieccctroondicuctoinvdituycotifvtihtyeocfotmhepocsoimteposite electroedleecst.rodes. 60 9 of 15 −1 −1 for C-

PDF Image | From Wastes to Anode Materials for Na-Ion Batteries

PDF Search Title:

From Wastes to Anode Materials for Na-Ion Batteries

Original File Name Searched:

batteries-08-00183.pdf

DIY PDF Search: Google It | Yahoo | Bing

Salgenx Redox Flow Battery Technology: Salt water flow battery technology with low cost and great energy density that can be used for power storage and thermal storage. Let us de-risk your production using our license. Our aqueous flow battery is less cost than Tesla Megapack and available faster. Redox flow battery. No membrane needed like with Vanadium, or Bromine. Salgenx flow battery

CONTACT TEL: 608-238-6001 Email: greg@salgenx.com (Standard Web Page)