Yao
Tong
a,
Junyu
Yang
b,
Jiajun
Li
a,
Ziyang
Cong
a,
Li
Wei
a,
Miaomiao
Liu
a,
Shangru
Zhai
a,
Kai
Wang
*b and
Qingda
An
*a
aFaculty of Light Industry and Chemical Engineering, Dalian Polytechnic University, Dalian 116034, China. E-mail: anqingda@dlpu.edu.cn
bDalian National Laboratory for Clean Energy, Dalian Institute of Chemical Physics, Chinese Academy of Sciences, Dalian 116023, China. E-mail: wangkai@dicp.ac.cn
First published on 7th December 2022
Lignin is one of the most abundant natural polymers and is affordable, has high carbon content and abundant active functional groups. At present, lignin-derived carbon is considered an ideal, promising electrode material for supercapacitor applications and this route is showing a vigorous development trend. In this review, we summarize the progress of lignin-derived materials for supercapacitor applications. Firstly, the concept, classification strategy and basic chemistry of lignin are introduced in brief. Then, the up-to-date developments of the synthesis strategies of carbon electrodes from lignin for supercapacitors are reviewed in detail. Finally, the work is summarized and the major challenges of the lignin-based supercapacitors are discussed. This review is presented to guide the synthesis of lignin-based electrodes for supercapacitors and facilitate their widespread application.
Lignin is a heterogeneous and amorphous polymer. At present, approximately 70 million tons of lignin are produced during the extraction of cellulose for the paper industry each year. The affordability and bio-renewable properties make lignin a desirable candidate material for numerous applications.19–24 Despite the huge possibilities, lignin has not yet been converted into high-value-added products on a large scale thus far.25–28 Only a tiny percentage, approximately less than 2% of the gross product is applied as stabilizing agents,29,30 concrete additives or surfactants and dispersants.31–35 The rest is thrown away directly as waste or burned as low-quality fuel.36–38 On the other hand, due to the integrated advantages of lignin, such as high carbon content, high thermal stability, biodegradability and feasible stiffness, deriving more value-added products, such as electrode materials, from lignin for supercapacitors is a potential alternative.39–42 At present, massive efforts have already been devoted to converting lignin into carbon materials for the design of safe and reliable supercapacitors.
This review covers the recent progress in the transformation of lignin into valuable products applied in the field of supercapacitors. We shall first briefly introduce the categorization and isolation processes of lignin materials. Subsequently, the synthesis of electrode materials from lignin and their applications for supercapacitors are elaborated. Finally, the challenges and possible future directions are presented to spark new thoughts for bringing supercapacitors into practical and daily-life applications.
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Fig. 1 (a) The natural structure of cellulose, hemicellulose and lignin in the lignocellulosic biomass. Adapted with permission from ref. 53. Copyright 2015 Royal Society of Chemistry. (b) Lignin monomer units and their precursors. (c) The linkages of lignin. Adapted with permission from ref. 54. Copyright 2017 Royal Society of Chemistry. |
In terms of molecular structures, lignin is an amorphous polymer with a three-dimensional network structure consisting of phenyl-propane structural units connected by ether bonds and carbon–carbon bonds.49–52 Its phenyl-propane structural unit is usually comprised of three basic phenylpropanolic monomers, i.e., sinapyl, p-coumaryl and coniferyl alcohols, corresponding to the three types of lignin structural units, namely, guaiacyl (G), p-hydrophenyl (H), and syringyl units (S), respectively (Fig. 1b).55–58 The β-O-4′ ether linkages are the main type in lignin that account for more than 50% of the linkage structures and are certainly a critical criterion in the degradation studies.57 The 4-O-5′, β-β′, β-5′, β-1′ and 5-5′ linkages also exist in lignin but they account for smaller percentages (Fig. 1c). The proportion of structural units and connection structures in various lignins are dissimilar depending on the plant species, growth parts, growth environment, and interference from external factors. As an example, G units constitute softwood, GS units are abundant in hardwood, while the grasses are comprised of the three monolignols, HGS-units.23,59
Industrial lignin can be divided into four different types depending on whether it is subjected to the sulphuring process.36 Kraft lignin is the dominant industrially processed lignin worldwide.63,64 During the kraft process, the structure of pristine lignin is dramatically broken. As a consequence, kraft lignin contains more phenolic –OH groups and more condensed C–C structures.65 Lignosulfonate is mainly derived from the waste liquid produced during the pulping process, which usually consists of active groups including phenolic hydroxyl, aliphatic hydroxyl and carbonyl. The sulfur content of lignosulfonate is rather high (i.e. 4–8%), most of which is in the form of sulfonate.66,67 Organosolv lignin is derived from the by-products of the organosolv pulping process, which exhibit smaller molecular weights and possess a higher concentration of phenolic hydroxyl groups.36,68 Aside from these, soda lignin is mainly derived from the soda or soda–anthraquinone pulping process.54 In comparison with kraft pulping, soda lignin has no sulfur and is more like native lignin, thus soda lignin possesses more active sites for chemical modification.36,69 Enzymatic hydrolysis lignin is a new type of industrial lignin that is extracted from crop waste obtained during the production of bioethanol. It preserves the original lignin structure to a large extent and has higher hydrophilicity as compared to other lignin.70,71
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Fig. 2 Schematic diagram of (a) EDLCs and (b) pseudo-capacitors. Adapted with permission from ref. 76. Copyright 2016 Royal Society of Chemistry. |
Electrode materials | Structural properties | Synthesis | Electrolytes | Specific capacitance | Energy density | Cycle stability | Ref. |
---|---|---|---|---|---|---|---|
Lignin/PAN carbon nanofiber | S BET: 1176.0 m2 g−1 | Electrospinning and self-activation process | Lignin hydrogel electrolyte | 129.23 F g−1 at 0.5 A g−1 | 4.49 W h kg−1 at 2.63 kW kg−1 | 95% after 10![]() |
18 |
V t: 0.394 cm3 g−1 | 108.90 F g−1 at 5 A g−1 | ||||||
LFW@PANI | — | In situ self-polymerization | 1 M H2SO4 | 800 F g−1 at 10 A g−1 | 46 W h kg−1 at 68 kW kg−1 | 96% after 5000 cycles at 50 mV s−1 | 39 |
LCA/Ni cubic carbon | S BET: 892 m2 g−1 | ZnCl2 activation and template | 6 M KOH | 26.6 F cm−2 at 1 mA cm−2 | — | 98.5% after 10![]() |
42 |
V t: 0.53 cm3 g−1 | 16.4 F cm−2 at 200 mA cm−2 | ||||||
HPC | S BET: 1504 m2 g−1 | Hydrothermal carbonization and KOH activation | 6 M KOH | 324 F g−1 at 0.5 A g−1 | 17.9 W h kg−1 at 458 W kg−1 | 98.07% after 5000 cycles at 5 A g−1 | 70 |
V t: 0.757 cm3 g−1 | 249 F g−1 at 50 A g−1 | ||||||
HPC/WO3 | S BET: 1430 m2 g−1 | Carbonization and solvothermal process | 1 M H2SO4 | 432 F g−1 at 0.5 A g−1 | 34.2 W h kg−1 at 243 W kg−1 | 86.6% after 10![]() |
71 |
V t: 0.41 cm3 g−1 | 214 F g−1 at 20 A g−1 | ||||||
SC-1![]() ![]() |
S BET: 1886 m2 g−1 | KOH activation | EMIBF4 | 231 F g−1 at 1 A g−1 | — | 50% after 10![]() |
91 |
V t: 0.86 cm3 g−1 | 203 F g−1 at 10 A g−1 | ||||||
LAC4 | S BET: 3775 m2 g−1 | Carbonization and KOH activation | 6 M KOH | 286.7 F g−1 at 0.2 A g−1 | 8.87 W h kg−1 at 51.92 W kg−1 | — | 97 |
V t: 2.703 cm3 g−1 | 207.1 F g−1 at 8 A g−1 | ||||||
LHC-3K | S BET: 1660 m2 g−1 | Hydrothermal carbonization and KOH activation | 6 M KOH | 420 F g−1 at 0.1 A g−1 | 10 W h kg−1 at 50 W kg−1 | 99% after 5000 cycles at 5 A g−1 | 103 |
V t: 0.78 cm3 g−1 | 284 F g−1 at 100 A g−1 | ||||||
PCS | S BET: 1590 m2 g−1 | Spray drying; KOH activation | 3 M KOH | 345 F g−1 at 0.5 A g−1 | 9.7 W h kg−1 at 250 W kg−1 | 94.5% after 5000 cycles at 4 A g−1 | 198 |
V t: 0.89 cm3 g−1 | 245 F g−1 at 10 A g−1 | ||||||
S–PC–L-900 | S BET: 1054 m2 g−1 | Silica template | 6 M KOH | 328 F g−1 at 0.2 A g−1 | 6.9 W h kg−1 at 50 W kg−1 | 94% after 10![]() |
161 |
V t: 1.73 cm3 g−1 | 192 F g−1 at 20 A g−1 | ||||||
CO2-activated mesoporous carbon from lignin | S BET: 1148 m2 g−1 | Surfactant Pluronic F127/CO2-activated | 6 M KOH | 102.3 F g−1 at 1 mVs−1 | — | — | 107 |
V t: 1.00 cm3 g−1 | |||||||
SLC | S BET: 803 m2 g−1 | Dual template of P123 and KIT-6 | 6 M KOH | 3.0 F cm−2 at 0.1 A g−1 | 0.16 mW h cm−2 at 1.75 mW cm−2 | 96% after 1500 cycles at 2 A g−1 | 109 |
V t: 0.86 cm3 g−1 | 1.4 F cm−2 at 10 A g−1 | ||||||
CNSs | Thickness: 50–100 nm | Freeze-casting lignin aqueous dispersion | 1 M H2SO4 | 281 F g−1 at 0.5 A g−1 | 25.1 W h kg−1 at 583 W kg−1 | 91% after 5000 cycles at 1 A g−1 | 199 |
S BET: 854.7 m2 g−1 | 153 F g−1 at 20 A g−1 | ||||||
LCNFs–PRL (5![]() ![]() |
S BET: 1063 m2 g−1 | Electrospinning PAN![]() ![]() ![]() ![]() |
6 M KOH | 339.2 F g−1 at 0.1 A g−1 | 56.9 W h kg−1 at 339 W kg−1 in 1 M Na2SO4 | 90.52% after 5000 cycles at 1 A g−1 in 1 M Na2SO4 | 112 |
V t: 0.53 cm3 g−1 | 289.6 F g−1 at 5 A g−1 | ||||||
Carbon nanofiber mats | Thickness: 50–174 μm | Electrospinning process | 6 M KOH | 130 F cm−3 at 0.1 A g−1 | 3.4 W h L−1 at 10 kW L−1 | Over 90% after 10![]() |
116 |
102.7 F g−1 at 100 A g−1 | |||||||
ML-7 K CFs | S BET: 2042.86 m2 g−1 | Modification and fractionation | 6 M KOH | 442.2 F g−1 at 1 A g−1 | 37.1 W h kg−1 at 400 W kg−1 | 97.1% after 10![]() |
118 |
384 F g−1 at 10 A g−1 | |||||||
AILCFN/Ni–Co–S | S BET: 715.38 m2 g−1 | Electrospinning and thermal treatment | 6 M KOH | 1140.0 C g−1 at 10 A g−1 | 30.8 W h kg−1 at 800 W kg−1 | 84.7% after 3000 cycles at 10 mA cm−2 | 123 |
V t: 0.3240 mL g−1 | |||||||
K-ACFs | — | Electrospinning, carbonization and KOH activation | 6 M KOH | 344 F g−1 at 10 mv s−1 | 8.1 W h kg−1 at 50 mV s−1 | 96.5% after 5000 cycles | 125 |
196 F g−1 at 50 mV s−1 | |||||||
Lignin–cellulose-based CFs-5 | S BET: 837.4 m2 g−1 | Preoxidation and carbonization treatment | 6 M KOH | 346.6 F g−1 at 0.1 A g−1 | 31.5 W h kg−1 at 400 W kg−1 in 1 M Na2SO4 | — | 126 |
V t: 0.488722 cm3 g−1 | 285.3 F g−1 at 5 A g−1 | ||||||
Lignin–NiWO4 | — | Depositing | PVA/H3PO4 gel | 129.7 mF cm−2 at 0.013 A g−1 | 2 W h cm−2 at 100 W cm−2 | 84% after 2000 cycles | 139 |
6.39 mF cm−2 at 0.128 A g−1 | |||||||
ECNF/MnO2 (1![]() ![]() |
S BET: 583 m2 g−1 fiber diameters of ∼200 nm | Electrospinning | 1 M LiPF6 | 83.3 F g−1 at 250 mA g−1 | 84.3 W h kg−1 at 5.72 kW kg−1 | 99% after 10![]() |
142 |
MCNFs@SnO2 | S BET: 659 m2 g−1 | Co-electrospinning | 6 M KOH | 406 F g−1 at 0.5 A g−1 | 11.5 W h kg−1 at 451 W kg−1 | 95% after 10![]() |
144 |
128 F g−1 at 50 A g−1 | |||||||
LDC/ZnO | S BET: 372.6 m2 g−1 | Electrostatic self-assembling carbonization process | PVA/KOH gel | 193 F g−1 at 0.5 A g−1 | 6.7 W h kg−1 at 197.7 W kg−1 | 94.2% after 10![]() |
145 |
151 F g−1 at 20 A g−1 | |||||||
PC–Ni/MnO2-1 | S BET: 80.14 m2 g−1 | Carbonization process | 6 M KOH | 267.34 F g−1 at 0.1 A g−1 | 28 W h kg−1 at 360 W kg−1 | 83.6% after 5000 cycles at 1 A g−1 | 146 |
182.16 F![]() |
|||||||
KL/TAC | — | Ultrasonic-assisted deposition method | 1 M H2SO4 | 293 F g−1 at 1 A g−1 | — | 98.1% after 1000 cycles at 1 A g−1 | 200 |
HLRGO11 | S BET: 1804 m2 g−1 | Hydrothermal process | 6 M KOH | 190 F g−1 at 0.5 A g−1 | — | 86.5% after 10![]() |
133 |
133.9 F g−1 at 10 A g−1 | |||||||
Lig–GHs | S BET: 109 m2 g−1 | Hydrothermal process | 0.1 M HClO4 | 549.5 F g−1 at 1 A g−1 | — | 83.7% after 1000 cycles at 20 A g−1 | 132 |
335 F g−1 at 20 A g−1 | |||||||
C–LRGOs | S BET: 444.29 m2 g−1 | Hydrothermal reaction and carbonization | 1 M H2SO4 | 330 F g−1 at 1 A g−1 | 11.3 W h kg−1 at 254 W kg−1 | 100% after 10![]() |
134 |
V t: 0.773 cm3 g−1 | 265 F g−1at 10 A g−1 | ||||||
HPCSLS-700-1 | S BET: 903 m2 g−1 | Direct carbonization | 7 M KOH | 247 F g−1 at 0.05 A g−1 | 8.6 W h kg−1 at 14.3 W kg−1 | 92% after 10![]() |
162 |
V t: 0.53 cm3 g−1 | 104 F g−1 at 20 A g−1 | ||||||
NHPC1:1-3-800 | S BET: 1867.4 m2 g−1 | Hydrothermal crosslinking reaction and KOH activation | 6 M KOH | 440 F g−1 at 0.5 A g−1 | 18.5 W h kg−1 at 300 W kg−1 in 6 M KOH | 95.1% after 3000 cycles at 20 A g−1 in 6 M KOH | 163 |
V t: 0.997 cm3 g−1 | 1 M H2SO4 | 331 F g−1 at 1 A g−1 | |||||
N, S–HPC-1 | S BET: 1454.7 m2 g−1 | Carbonization and KOH activation | 6 M KOH | 269 F g−1 at 0.5 A g−1 | 37.4 W h kg−1 at 62 W kg−1 | 98.4% after 10![]() |
164 |
V t: 0.894 cm3 g−1 | 168 F g−1 at 50 A g−1 | ||||||
L–U | S BET: 3130 m2 g−1 | Carbonization and KOH activation | KOH–PVA | 306 F g−1 at 0.1 A g−1 | 17 W h kg−1 | 96.8% after 5000 cycles at 0.1 to 10 A g−1 | 172 |
V t: 1.67 cm3 g−1 | 251 F g−1 at 10 A g−1 | ||||||
PL-700 | S BET: 2265 m2 g−1 | KOH activation | 6 M KOH | 333 F g−1 at 20 mV s−1 | — | 100% after 1000 cycles at 1 A g−1 | 173 |
GNs–N–S co-doped ACNFs-5 | S BET: 2439 m2 g−1 | Electrospinning, carbonization and activation process | 6 M KOH | 267.32 F g−1 at 5 mV s−1 | 9.28 W h kg−1 at 493 W kg−1 | 96.7% after 5000 cycles | 175 |
V t: 1.2882 cm3 g−1 | 148.47 F g−1 at 50 mV s−1 | ||||||
ONS–HPCs–L-700 | S BET: 1269 m2 g−1 | Direct pyrolysis | 6 M KOH | 300.5 F g−1 at 0.5 A g−1 | 66.8 W h kg−1 at 1750 W kg−1 in EMIM BF4 | 91.6% after 10![]() |
180 |
V t: 0.598 cm3 g−1 | 243 F g−1 at 60 A g−1 | ||||||
CKL-1098 | S BET: 1092 m2 g−1 | Direct carbonization | 1 M H2SO4 | 114 F g−1 at 5 mV s−1 | 12.8 W h kg−1 at 1006 W kg−1 | 80% after 10![]() |
201 |
76 F g−1 at 100 mV s−1 | |||||||
Ca-800 | S BET: 1362 m2 g−1 | Carbonization | 6 M KOH | 182 F g−1 at 1 mA cm−2 | 25 W h kg−1 at 150 W kg−1 | 95% after 1000 cycles at 10 mA cm−2 | 202 |
V t: 0.83 cm3 g−1 | 122 F g−1 at 20 mA cm−2 | ||||||
CHMS-5-700–N | S BET: 991 m2 g−1 | Carbonization and post-nitric acid modification | 7 M KOH | 284 F g−1 at 0.1 A g−1 | 2.9 W h L−1 at 11.3 W L−1 | 93.4% after 10![]() |
203 |
V t: 0.75 cm3 g−1 | 124 F g−1 at 20 A g−1 | ||||||
HPCS-700 | S BET: 1255 m2 g−1 | Thermostabilization and carbonization | 7 M KOH | 276 F g−1 at 0.1 A g−1 | 34.3 W h kg−1 at 9.4 kW kg−1 in 1 M SBPBF4/PC | 99.5% after 10![]() |
204 |
V t: 0.87 cm3 g−1 | 155 F g−1 at 20 A g−1 | ||||||
HAPC-11-900 | S BET: 856 m2 g−1 | Template and chemical activation | 6 M KOH | 286 F g−1 at 0.25 A g−1 | 13 W h kg−1 at 27 kW kg−1 | 89.4% after 2000 cycles at 4 A g−1 | 205 |
V t: 0.17 cm3 g−1 | 141 F g−1 at 10 A g−1 | ||||||
PNG | S BET: 515 m2 g−1 | Co-pyrolysis | 6 M KOH | 170 F g−1 at 0.2 A g−1 | — | 92.5% after 1000 cycles at 100 mV s−1 | 206 |
138.5 F g−1 at 5 A g−1 | |||||||
HPGC-160-8 | S BET: 856.84 m2 g−1 | Cross-linking and carbonization | 6 M KOH | 331 F g−1 at 5 mV s−1 | — | 78% after 1000 cycles at 20 mV−1 | 207 |
V t: 0.425 cm3 g−1 | 202 F g−1 at 100 mV s−1 | ||||||
LHPC | SBET: 907 m2 g−1 | Template-free and KOH activation | 1 M H2SO4 | 165 F g−1 at 0.05 A g−1 | 3.75 W h kg−1 at 1070 W kg−1 | 97.45% after 5000 cycles at 1 A g−1 | 208 |
V t: 0.515 cm3 g−1 | 123.5 F g−1 at 10 A g−1 | ||||||
NiO/HMPC NSs | S BET: 851.8 m2 g−1 | Self-assembly and carbonization | 6 M KOH | 508 F g−1 at 20 mV s−1 | — | 92% after 2000 cycles at 20 mV s−1 | 209 |
V t: 0.16 cm3 g−1 | |||||||
1-HPC600-600-5 | S BET: 2753.9 m2 g−1 | Carbonization and KOH activation | 6 M KOH | 428 F g−1 at 0.04 A g−1 | 12 W h kg−1 at 9908 W kg−1 | 96% after 12![]() |
210 |
V t: 1.43 cm3 g−1 | 288 F g−1 at 10 A g−1 | ||||||
CA-L20 | S BET: 779 m2 g−1 | Carbonization and KOH activation | 6 M KOH | 142.8 F g−1 at 0.5 A g−1 | — | 96% after 2000 cycles at 10 A g−1 | 211 |
V t: 0.48 cm3 g−1 | 112.5 F g−1 at 10 A g−1 | ||||||
PANI/LGS | — | — | 1 M H2SO4 | 502.1 F g−1 at 0.1 A g−1 | — | 74.3% after 10![]() |
212 |
377.2 F g−1 at 10 A g−1 | |||||||
PANI/LG | — | In situ oxidation polymerization | 1 M HClO4 | 485.3 F g−1 at 0.5 A g−1 | — | 67.4% after 5000 cycles at 1 A g−1 | 213 |
284.4 F g−1 at 30 A g−1 | |||||||
ECNFs (70/30) | S BET: 583 m2 g−1 | Electrospinning, stabilization and carbonization | 6 M KOH | 64 F g−1 at 0.4 A g−1 | 5.67 W h kg−1 at 94.19 W kg−1 | 90% after 6000 cycles at 2 A g−1 | 214 |
V t: 0.289 cm3 g−1 | 50 F g−1 at 2 A g−1 | ||||||
NiCo2O4@CNF55 | Fiber diameters of 1830 ± 155 nm | Electrospinning, stabilization and carbonization | 2 M KOH | 1757 F g−1 at 2 mA cm−2 | 47.75 W h kg−1 at 799.53 W kg−1 | 138% after 5000 cycles at 7 mA cm−2 | 215 |
1304 F g−1 at 50 mA cm−2 | |||||||
LCNFs-2 | S BET: 1140 m2 g−1 | Electrospinning PVP![]() ![]() ![]() ![]() ![]() ![]() ![]() ![]() |
6 M KOH | 248 F g−1 at 0.2 A g−1 | — | 97% after 1000 cycles at 20 A g−1 | 216 |
V t: 0.627 cm3 g−1 | 146 F g−1 at 20A g−1 | ||||||
MnO2–CNFM4 | — | Electrospinning, carbonization | 1 M Na2SO4 | 171.6 F g−1 at 5 mV?s−1 | 6.0 W h kg−1 at 160 W kg−1 | 98.95% after 1000 cycles at 0.5 A g−1 | 217 |
88.4 F g−1 at 50 mV s−1 | |||||||
MnO2–LCF-800 mat | S BET: 273.70 m2 g−1 | Electrospinning, stabilization and carbonization | 1 M Na2SO4 | 131.28 F g−1 at 0.3 A g−1 | 14.77 W h kg−1 at 135.01 W kg−1 | — | 218 |
V t: 0.09 cm3 g−1 | |||||||
LUDC_0.5 | S BET: 764 m2 g−1 | DES-templated | 6 M KOH | 177.5 F g−1 at 0.5 A g−1 | — | 96% after 12![]() |
219 |
V t: 0.47 cm3 g−1 | 136.8 F g−1 at 10 A g−1 | ||||||
BALC-9 | S BET: 1831 m2 g−1 | Carbonization and bacterial activation | 6 M KOH | 428 F g−1 at 1 A g−1 | 66.18 W h kg−1 at 312 W kg−1 in EMIM TFSI | 96.7% after 10![]() |
104 |
V t: 1.53 cm3 g−1 | EMIM TFSI | 289 F g−1at 1 A g−1 | |||||
ARS/PGLS-1 | S BET: 1727.7 m2 g−1 | Carbonization and graphitization | 6 M KOH | 469.5 F g−1 at 0.5 A g−1 | 9.45 W h kg−1 at 100.06 W kg−1 in PVA/KOH/ARS | 99.7% after 2000 cycles at 2 A g−1 in PVA/KOH/ARS | 220 |
V t: 1.33 cm3 g−1 | 200.2 F g−1 at 10 A g−1 | ||||||
LSG-P36–Au | S BET: 338.3 m2 g−1 | One-step CO2 laser irradiation | H2SO4/PVA gel | 11.9 mF cm−2 at 0.02 mA cm−2 | — | 98.47% after 12![]() |
221 |
V t: 0.232 cm3 g−1 | |||||||
sLIG-O/S14 | S BET: 181.37 m2 g−1 | A duplicated laser scribing process | PVA/H2SO4 gel | 53.2 mF cm−2 at 0.08 mA cm−2 | 0.45 mW h cm−3 at 1.6 mW cm−2 | 81.3% after 8000 cycles at 50 mV s−1 | 222 |
V t: 0.351 cm3 g−1 | |||||||
N–BLPC | S BET: 2646 m2 g−1 | KOH activation | 6 M KOH | 337 F g−1 at 0.5 A g−1 | 9.34 W h kg−1 at 250 W kg−1 | 98% after 3000 cycles at 10 A g−1 | 223 |
V t: 1.285 cm3 g−1 | 254 F g−1 at 20 A g−1 | ||||||
LPC-3 | S BET: 2866 m2 g−1 | Microwave heating | 6 M KOH | 216 F g−1 at 0.5 A g−1 | 55.5 W h kg−1 at 1.1 kW kg−1 | 99.9% after 2000 cycles at 5 A g−1 in gel-like PVA/LiCl electrolyte | 224 |
V t: 2.02 cm3 g−1 | 188 F g−1 at 10 A g−1 | ||||||
NSC-700 | S BET: 1199 m2 g−1 | Fe3O4 template and KOH activation | 6 M KOH | 241 F g−1 at 1 A g−1 | 27.2 W h kg−1 at 10![]() |
95% after 3000 cycles at 10 A g−1 | 225 |
196 F g−1 at 20 A g−1 | |||||||
E-CNFs | S BET: 2313 m2 g−1 | Esterification, electrospinning, and carbonization processes | 6 M KOH | 320 F g−1 at 1 A g−1 | 17.92 W h kg−1 at 800 W kg−1 in 1 M Na2SO4 | 94.5% after 5000 cycles at 1 A g−1 in 1 M Na2SO4 | 226 |
200.4 F g−1 at 20 A g−1 | |||||||
LUPCF-2 | S BET: 1363 m2 g−1 | Electrospinning, pre-oxidation, carbonization, and pickling processes | 6 M KOH | 289 F g−1 at 0.1 A g−1 | — | 92% after 10![]() |
227 |
V t: 0.689 cm3 g−1 | 162 F g−1 at 20 A g−1 | ||||||
PLC-650-2 | S BET: 1069 m2 g−1 | Zinc oxalate-assisted gas-exfoliation and in situ templating | 6 M KOH | 365 F g−1 at 0.5 A g−1 | 9.75 W h kg−1 at 6157.9 W kg−1 in PVA/KOH gel electrolytes | 93.5% after 10![]() |
105 |
V t: 1.375 cm3 g−1 | 260 F g−1 at 20 A g−1 | ||||||
CNFs-6 | S BET: 1061.7 m2 g−1 | ECH modification and heat treatment | 6 M KOH | 320.3 F g−1 at 1 A g−1 | 30.2 W h kg−1 at 400 W kg−1 in 1 M Na2SO4 | — | 228 |
V t: 0.57 cm3 g−1 | |||||||
L–CNFs@Fe3O4 nanofibers | — | Electrospinning, stabilized and carbonized | 1 M Na2SO4 | 216 F g−1 at 0.1 A g−1 | 43 W h kg−1 at 242 W kg−1 | 96.7% after 1000 cycles at 1 A g−1 | 229 |
C800-SS | S BET: 28.3 m2 g−1 | Electrospinning and carbonization | PVA-1 M H2SO4 | 451.1 F g−1 at 1 A g−1 | 62.6 W h kg−1 at 1250 W kg−1 | 99.5% after 10![]() |
230 |
V t: 0.068 cm3 g−1 | |||||||
HPCS-X-3 | S BET: 3406 m2 g−1 | Simple spray drying and carbonization-activation | 6 M KOH | 236.2 F g−1 at 0.2 A g−1 | — | 91.7% after 5000 cycles at 20 A g−1 | 231 |
V t: 2.46 cm3 g−1 | 130.6 F g−1 at 20 A g−1 | ||||||
LPC-700 | S BET: 529 m2 g−1 | Carbonization-induced self-template method | 6 M KOH | 170 F g−1 at 0.5 A g−1 | — | 81% after 5000 cycles at 1 A g−1 | 232 |
89 F![]() |
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NCA-12 | S BET: 482 m2 g−1 | Co-electrospinning, freeze-casting and freeze-drying, carbonization | 6 M KOH | 282 F g−1 at 0.2 A g−1 | 32 W h kg−1 at 125 W kg−1 | 96% after 5000 cycles at 5 A g−1 | 233 |
60 F g−1 at 10 A g−1 | |||||||
LPCs | S BET: 3178.36 m2 g−1 | Hydrothermal and KOH-assisted synthesis | 6 M KOH | 201.69 F g−1 at 0.5 A g−1 | — | 90.21% after 10![]() |
234 |
171.88 g−1 at 10 A g−1 | |||||||
LCNS | S BET: 736 m2 g−1 | Self-assembly, stabilization treatment, and carbonization | 6 M KOH | 147 F g−1 0.5 A g−1 | 3.5 W h kg−1 at 62.6 W kg−1 | 85.37% after 10![]() |
235 |
86 F g−1 at 20 A g−1 | |||||||
LSC–ZnC2O4/PANI | — | Carbonization and in situ polymerization | 1 M H2SO4 | 643 F g−1 at 1.0 A g−1 | 36.3 W h kg−1 at 850.2 W kg−1 in 1 M Na2SO4 | 88.0% after 5000 cycles at 5.0 A g−1 | 236 |
390 F g−1 at 30 A g−1 |
Of special note, the activator plays a paramount role in the ultimate SSA and pore structure of the lignin-based carbon materials. Wu et al. demonstrated that the electrochemical performance of lignin-based ACs depends on the various activators (ZnCl2, KOH, K2CO3).98 Interestingly, the ZnCl2-activated ACs exhibited the smallest SSA because ZnCl2 only acts as a catalyst for dehydroxylation and dehydration in the activation process, whereas both KOH and K2CO3 serve to dehydrate and oxidize lignin. Furthermore, K2CO3 decomposes into CO2 and introduces physical activation. As such, the K2CO3-activated ACs exhibited the maximum SSA of 1585 m2 g−1 and an excellent specific capacitance of 263.5 F g−1 at 40 mA g−1 in 6 M KOH.
A high SSA is of significance for raising the performance of lignin-based ACs, but a suitable pore structure is a prerequisite to the high utilization of the SSA.99 For example, most high SSA materials are usually microporous with a narrow pore size distribution of 0.5–1.5 nm, which severely restrains the diffusion of electrolyte ions, and undermines the rate capability.100–102 To tackle these issues, hierarchical porous carbons (HPCs) combining micro-, meso- and macro-pores have been utilized as EDLCs electrode materials as they are capable of offering effective diffusion paths. In HPCs, the macropores provide a high buffer capacity for electrolyte ions, the mesoporous channels are conducive to the rapid transport of ions, and the micropores can further enhance the ion-accessible surface area for the construction of an electric double layer, resulting in excellent electrochemical performance.101 Lignins enjoy a loose structure that is conducive to the formation of porous structures during pyrolysis. In this regard, tremendous efforts have been devoted to constructing HPCs via appropriate pyrolysis and activation strategies by adopting lignin as a carbon source. Guo and co-workers configured a 3D HPC from the enzymatic hydrolysis of lignin via hydrothermal carbonization followed by a KOH activation process (Fig. 3a).103 The unique 3D porous network (Fig. 3b) exhibited a high SSA of 1660 m2 g−1 and realized a superior specific capacitance of 420 F g−1 at 0.1 A g−1, together with considerable rate performance in 6 M KOH (Fig. 3c). Moreover, it can retain 99% of the pristine capacitance upon undergoing 10000 cycles at 5 A g−1, indicative of excellent structural stability. Strikingly, the assembled symmetric supercapacitor exhibited an outstanding energy density of 46.8 W h kg−1 in ionic liquid systems (Fig. 3d). Based on this work, our group systematically studied the effects of hydrothermal carbonization conditions on the structure and properties of HPCs according to the Taguchi method.70 The optimized sample enjoyed a favorable SSA of 1504 m2 g−1 and the corresponding supercapacitors delivered a desirable specific capacitance of 324 F g−1 at 0.5 A g−1 in 6 M KOH coupled with decent rate performance and excellent cycle stability. Zhang et al. developed a green bacterial activation strategy to prepare HPCs.104 It is worth noting that bacterial activation can break the β-O-4, β-β′, and β-5 linkages in lignin, reduce the molecular weight, and promote the carbonization and graphitization of lignin. As such, an enhanced specific capacitance of 428 F g−1 at 1 A g−1 in 6 M KOH was achieved. In addition, the symmetric supercapacitor can deliver a superior energy density of 66.18 W h kg−1 at a power density of 312 W kg−1 in the ionic liquid system. It also achieved a decent cycle performance, with a capacitance retention of up to 96.7% after 10
000 cycles at 5 A g−1.
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Fig. 3 (a) Schematic of the synthesis of LHC samples. (b) SEM image of the LHC-3K. (c) Rate performance of the LHC-based electrodes. (d) Ragone profiles of LHC-based supercapacitors (LHC denoted as enzymatic hydrolysis lignin-derived 3D HPCs). Reproduced with permission from ref. 103. Copyright 2017 Royal Society of Chemistry. |
However, the synthesis and removal of the hard template are complicated, and the properties of PCs largely depend on the properties of templates. Recently, the soft template method has attracted much more attention because it is unnecessary to remove the soft templates after carbonization. The soft template and abundant oxygen-containing functional groups in lignin can self-assemble into precursors through hydrogen bond interactions, and the mesoporous materials can be synthesized by subsequently carbonizing the precursors. Saha et al.107 prepared lignin-based ordered mesoporous carbons (OMCs) by adopting Pluronic F127 as the template. The OMCs showed an SSA of 1148 m2 g−1, with a mesoporosity of 66%. The OMCs electrode activated by CO2 delivered a capacitance of 102.3 F g−1 and excellent rate performance in 6 M KOH. Moreover, Herou et al.108 adopted the dual precursor system comprising equal-weight phloroglucinol and lignin to prepare OMCs through a soft template strategy. The synthesized OMCs displayed superior electrochemical performance as compared to the material prepared by only utilizing phloroglucinol because the smaller mesopores in the former boosted the electrolyte diffusion rate.
Compared with the hard template method, the soft template method shows an underdeveloped capability of selectively regulating the pore structure of PCs and thus, the prepared PCs possess fewer micropores and smaller SSA. With the above information in mind, an efficient strategy is to couple the hard template with the soft template method to achieve carbon electrodes possessing appropriate pore structures. Li et al. configured large-scale hierarchical porous carbon monoliths (HPCMs), by effectively carbonizing the mixture of P123, lignin and mesoporous silica (hereafter denoted as SLC), as shown in Fig. 4a.109 The SLC displays a favorable microstructure and excellent conductivity. As expected, the assembled symmetric supercapacitor exhibited a superior areal capacity of 3.0 F cm−2 and a volume capacity of 97.1 F cm−3 at a current density of 1.4 mA cm−2 in 6 M KOH without utilizing binders and conductive additives (Fig. 4b). Moreover, a considerable areal energy density of 0.16 mW h cm−2 at 1.75 mW cm−2 was achieved (Fig. 4c). In another study, Song et al. constructed the mesostructured carbons by employing MgO and Pluronic F127 as templates. They revealed that both the space-occupying effect of the MgO template and the mass ratio of lignin/MgO are critical for regulating the porosity of carbons. Eventually, the obtained material achieved a high SSA of 712 m2 g−1 and the fabricated electrodes yielded a larger specific capacitance of 186.3 F g−1 at a current density of 0.1 A g−1 in 1 M H2SO4.111
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Fig. 4 (a) Schematic illustration of the SLC process. (b) Areal/volumetric capacitances of SLC. (c) Areal Ragone plots (energy density vs. power density) for the full cell. Reprinted with permission from ref. 109. Copyright 2016 Elsevier. (d) Schematic of the formation of lignin/K2CO3 composite microspheres. (e) Micropore and mesopore size distribution of HPCMs. (f) The rate performance of various HPCMs at different scan rates. Reprinted with permission from ref. 110. Copyright 2018 Wiley Online Library. |
Recent studies have demonstrated that the templates not only construct pores but also play other roles in the preparation of lignin-based carbon materials.110 As illustrated in Fig. 4d, Wang and coworkers reported an inverse phase dehydration method to effectively synthesize the HPCMs.110 In this work, K2CO3 firstly acts as a pH regulator to promote the dissolution of lignin, and subsequently serves as the mesopore template and activator to promote the formation of abundant micropores of approximately 4 nm (Fig. 4e). The supercapacitor fabricated based on the optimal sample (HPCM-0.75) delivered a remarkable capacitance of 140 F g−1 at 0.05 A g−1 and excellent rate performance where the electrolyte used was 1 M tetraethylammonium tetrafluoroborate salt solution in propylene carbonate (Fig. 4f).
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Fig. 5 (a) Schematic diagrams of the preparation of lignin-based porous submicron ACFs. (b) CV profiles of various ACFs. Adapted with permission from ref. 125. Copyright 2014 Elsevier. (c) Proposed mechanism of phosphoric acid-functionalized ACFs. Adapted with permission from ref. 126 Copyright 2020 American Chemical Society. |
The low molecular weight, high heterogeneity and large dispersion index of lignin hinder the preparation of high-quality CFs from pure lignin.118,127 Zhou and coworkers utilized the reaction between the hydroxyl groups in lignin and the isocyanate groups in isophorone diisocyanate to enhance the molecular weight and reduce the heterogeneity of lignin, thus decreasing the carbon weight loss of precursor fibers and maintaining the morphology of lignin-based CFs.118 Correspondingly, the prepared CFs exhibited an outstanding SSA of 2042.86 m2 g−1. The assembled optimized supercapacitors displayed a high specific capacitance of 428.9 F g−1 at 1 A g−1 in 6 M KOH. Also, an excellent energy density of 37.1 W h kg−1 at a power density of 400 W kg−1 was realized in 1 M Na2SO4 electrolyte. In another study, Cao and co-workers modified lignin with cellulose-acetate to obtain precursor fibers by employing a facile phosphating process (Fig. 5c).126 Thereafter, lignin-based CFs were subjected to pre-oxidizing and carbonizing processes, thereby obtaining electrodes with high SSA and excellent electrochemical performance. Accordingly, the fabricated supercapacitor exhibited a capacitance of up to 346.6 F g−1 at 0.1 A g−1 in 6 M KOH. A superior energy density of 31.5 W h kg−1 at a power density of 400 W kg−1 was achieved in 1 M Na2SO4 electrolyte as well. Notably, the energy density of the supercapacitor was astonishingly maintained at 24.3 W kg−1 when the power density increased to 4000 W kg−1.
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Fig. 6 (a) Schematic of the synthesis of the lignin–RGO composite. Adapted with permission from ref. 133. Copyright 2017 Elsevier. (b) A schematic diagram of the molecular conformation conversion of lignin and the preparation of micropores in RGO-templated pseudo-capacitors. Adapted with permission from ref. 134. Copyright 2020 Elsevier. (c) Illustration of the preparation of LS–GH flexible solid-state supercapacitors. (d) Digital photograph of the flexible device; SEM images of the interior microstructure at (e) low and (f) high magnification. Adapted with permission from ref. 135. Copyright 2017 Royal Society of Chemistry. |
Ni2+ + 3OH− ↔ NiOOH + H2O + e− | (1) |
Co2+ + 3OH− ↔ CoOOH + H2O + e− | (2) |
CoOOH + OH− ↔ CoO2 + H2O + e− | (3) |
The assembled asymmetric supercapacitor can provide a wide voltage window of 1.6 V and give a superior energy density of 105.6 W h kg−1 at 400.5 W kg−1 in 6 M KOH, in conjunction with the considerable stability of 80.74% capacitance retention after 10000 cycles. Moreover, Cao et al.144 prepared the multi-channel carbon nanofiber (MCNFs)@SnO2 nanocomposites via the co-electrospinning method, whereby poly(vinyl pyrrolidone)–SnCl2·2H2O and lignin–poly(methyl methacrylate) were used as the shell and core, respectively (Fig. 7a). Notably, the hollow structures function as fast electron transfer pathways to achieve intimate contact with electrolyte ions. Besides, SnCl2·2H2O not only serves as a pore-forming agent to enhance the SSA but also acts as a precursor for SnO2 to provide pseudocapacitance for nanocomposites. Accordingly, the optimal nanocomposite electrode displays an excellent specific capacitance of 406 F g−1 at 0.5 A g−1 in 6 M KOH. Moreover, the specific capacitance can retain 95% after 10
000 cycles, indicative of exceptionable cycle stability.
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Fig. 7 (a) Schematic procedure for the preparation of MCNFs@SnO2 nanocomposites. Adapted with permission from ref. 144. Copyright 2020 Elsevier. (b) Illustration of the fabrication mechanism of the LDC/ZnO materials. Reprinted with permission from ref. 145. Copyright 2019 American Chemical Society. (c) Proposed catalytic graphitization mechanism of Ni. Reprinted with permission from ref. 146. Copyright 2021 Elsevier. |
In the past two decades, due to the considerable specific energy density, good electrochemical activity, nontoxicity, and environmental friendliness, ZnO has become one of the promising metal oxides for supercapacitors.147–149 Fu et al. successfully constructed a lignin-derived carbon/ZnO (LDC/ZnO) composite with a 3D porous structure via electrostatic self-assembly. The composite was in situ carbonized by using ZnC2O4 particles as the catalyst and activator, leading to a large SSA and excellent conductivity (Fig. 7b).145 The fabricated symmetric supercapacitor device based on LDC/ZnO electrodes achieved a capacitance of up to 193 F g−1 at 0.5 A g−1 using the PVA/KOH gel as the electrolyte, with considerable cycle stability. Furthermore, Ji and co-workers incorporated Ni and MnO2 in lignin-based porous carbon materials (PC–Ni/MnO2),146 whereby C4H6O4Ni·4H2O and KMnO4 were utilized as a catalyst and a dopant, respectively. As illustrated in Fig. 7c, lignin is converted to highly graphitized carbon nanosheets and multilayer graphene due to the catalytic effect of Ni during the carbonization process, while KMnO4 decomposes into MnO2 loading on the carbon material. As a result, the PC–Ni/MnO2 can realize a superior gravimetric capacitance of 267.34 F g−1 at 0.1 A g−1 in 6 M KOH. Furthermore, the assembled symmetrical supercapacitor displays an energy density of 28 W h kg−1 and a power density of 360 W kg−1, with a favorable cycle stability after 5000 cycles in 6 M KOH.
PPy0(Lig–QH2) → PPy+(ClO4−)(Lig–QH2) + e− | (4) |
PPy+(ClO4−)(Lig–QH2) → PPy+(ClO4−)(Lig–Q) + 2e− + 2H+ | (5) |
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Fig. 8 (a) The electrochemical redox reaction of quinone functions in an LS biopolymer within a PPy matrix. Reprinted with permission from ref. 86. Copyright 2012 Science. (b) Schematic diagram of the PPy/AL–AC cell. (c) Illustrative schematic of the lignin structure along with the redox processes occurring between QH2/Q. Adapted with permission from ref. 159. Copyright 2015 Royal Society of Chemistry. |
Rojo et al. fabricated the full-cell supercapacitor device composed of lignin/PEDOT as the positive electrode and partially reduced graphite oxide (prGrO) as the negative electrode,156 which delivered a higher capacitance of 34.6 F g−1 at 0.1 A g−1 in 0.1 M HClO4 electrolyte in comparison with the symmetric cells of lignin/PEDOT and prGrO. The enhanced electrochemical properties of the asymmetric device can be ascribed to the synergistic effect between the homogeneous distribution of the pseudocapacitive centers and enhanced electrical conductivity triggered by the intimate combination of both materials in the same electrode. Ajjan et al. synthesized bio-composites via both oxidative chemical and electrochemical polymerization of poly(3,4-ethylenedioxythiophene) (PEDOT) by adopting lignin sulfonate as the dopant and surfactant.157 Compared to reference PEDOT electrodes, the synthesized PEDOT/lignin composite electrodes exhibited an increased specific capacitance from 80.4 F g−1 to 170.4 F g−1 in a 0.1 M HClO4/water:
acetonitrile (9
:
1) mixed solvent, which is attributed to the additional pseudocapacitance of quinone moieties in lignin. In order to further improve the capacitance of the composite electrode, they fabricated a trihybrid electrode (PEDOT/lignin/poly(aminoanthraquinone) (PAAQ)) by introducing a third component of PAAQ to provide more pseudocapacitance.158 The trihybrid electrode manifested an excellent specific capacitance of 418 F g−1 at a current density of 1 A g−1 in 0.1 M HClO4. The asymmetric supercapacitor device was assembled, wherein the PEDOT/lignin/PAAQ and PEDOT/PAAQ were employed as the positive and negative electrodes, respectively. Benefitting from the synergistic effect of the two electrodes, it demonstrated excellent electrochemical performance, allowing for a specific capacitance of 74 F g−1 in 0.1 M HClO4. Additionally, a capacitance retention rate of 80% was identified after 10
000 cycles under a voltage window of 0.7 V. Alkali lignin (AL) accounts for 98% of lignin from paper-pulping; however, it encounters its own limitations due to its underdeveloped solubility in inorganic acids. To address this issue, Leguizamon et al. employed organic acid as the deposition solvent to fabricate PPy/AL electrodes (Fig. 8b).159 The PPy/AL electrode delivers an improved capacitance of 444 F g−1 in 0.5 M H2SO4, which is 30% higher than the electrodes containing identical compositions of sodium lignosulfate and 56% higher than pure PPy electrodes. Fig. 8c shows the redox processes occurring between hydroquinone/quinone (QH2/Q).
Despite these achievements, the cycle stability of the composite electrodes based on lignin with various conductive polymers is still restrained due to the instability of the conductive polymer during the electrochemical charging/discharging process. A ternary composite electrode comprised of phosphomolybdic acid (HMA, H3PMo12O40·nH2O), lignin and PPy was fabricated by Admassie's group via one-step simultaneous electrochemical deposition.160 The incorporation of HMA enabled the specific capacitance of the PPy–lignin composite to increase from 477 to 682 F g−1 at 1 A g−1 in 0.1 M HClO4.
Co-doping with two or more kinds of heteroatoms is an efficient way to further boost the device performance through synergistic effects.175–179 Tian et al. synthesized the nitrogen and sulfur co-doped 3D multilevel hierarchical porous carbons (N, S–HPCs) by utilizing sodium lignosulfonate as the C and S sources, while the polyaniline-coated polystyrene spheres were spotlighted as the N precursor and template for macropores (Fig. 9a).164 Startlingly, this high N, S-doping content (up to 2.1 and 4.3 wt%) and lower internal series resistance boosted the specific capacitance of the N, S–HPC electrode material to 269 F g−1 (at 0.5 A g−1) from 16.9 F g−1 of solely carbonized lignin in 6 M KOH (Fig. 9b and c). As depicted in Fig. 9d, this N–S–HPC electrode also demonstrated outstanding rate performance (62% capacitance retention at 50 A g−1) and cycle stability (98.4% capacitance retention after 10000 cycles) in 6 M KOH. Moreover, Liu et al. fabricated the O–N–S co-doped HPCs with a large SSA (338–1307 m2 g−1) by directly pyrolyzing kraft lignin.180 As expected, the fabricated symmetric supercapacitor in aqueous electrolyte delivered a high energy density of 66.8 W h kg−1 at a power density of 1.75 kW kg−1 while utilizing EMIMBF4 as the electrolyte. Our group successfully synthesized O, N and S co-doped HPC via a carbonization activation route using enzymatically hydrolyzed lignin as the carbon source.181 The obtained HPC has large SSA, abundant multiscale pores and high O, N, and S doping density. The faradaic redox reactions of N–O–S-containing functional groups in KOH electrolyte are shown in the following equations:182–186
–C–N–C− + H2O + e− ↔ –C–NH–C– + OH− | (6) |
–C–S–C− + H2O + 3e− ↔ –C–SO2–C– + 3OH− | (7) |
–C![]() | (8) |
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Fig. 9 (a) Schematic preparation procedure for N, S–HPC. High-resolution N1s (b), S2p (c) XPS of N, S–HPC-1. (d) The specific capacitances of the samples at various current densities. Adapted with permission from ref. 164. Copyright 2019 Elsevier. |
Consequently, the HPC electrode delivered a superior specific capacitance of 318 F g−1 at 0.5 A g−1 and excellent rate performance (62% retention at 50 A g−1) in 6 M KOH. The assembled asymmetric supercapacitor yielded a high energy density of 16.7 W h kg−1 at a power density of 249 W kg−1 and outstanding cycle stability (99.58% retention over 10000 cycles) in 6 M KOH.
Thanks to the unique structural characteristics, lignin can interact with graphene and CNTs through π–π effects to offset this irreversible agglomeration, having exhibited a huge potential for FSCs.194,195 Peng et al. fabricated FSCs by utilizing a lignosulfonate/single-walled CNT composite as the electrode and cellulose/Li2SO4 hydrogel as the electrolyte, which delivered an outstanding specific capacitance of 292 F g−1 at 0.5 A g−1 coupled with excellent rate capability, and a high energy density of 17.1 W h kg−1 at the power density of 324 W kg−1.196 The FSCs also exhibited excellent mechanical stability, retaining 98% of the initial capacitance after 1000 bending cycles. This excellent performance can be attributed to the synergistic effect of lignosulfonate-based carbon and CNT, as well as the superior 3D porous network structure. Moreover, Jha et al. assembled FSCs composed of Al/AC/lig–MnO2 as the anode, Al/AC as the cathode, and (PVA)/H3PO4 gel as the electrolyte.197 Due to their synergistic effect, the FSCs yielded a high specific capacitance of 5.52 mF cm−2, excellent mechanical stability (97.5% retention after 2000 cycles), and a favorable energy density of 14.11 W h kg−1 at the power density of 1 kW kg−1.
In the quest for renewable and highly efficient energy storage devices, Park et al. prepared all-lignin-based FSCs based on lignin hydrogel electrolytes and electrospun lignin/PAN nanofiber electrodes.18 The lignin hydrogel electrolytes display high ionic conductivity and excellent mechanical integrity, and the lignin-based carbon/PAN composite electrode possessing interconnected porous channels exhibits exceptional charge storage capability and kinetics. The FSCs attained a high capacitance of 129.23 F g−1 and beneficial capacitance retention of 95% over 10000 cycles, as well as excellent flexibility and durability under diverse bending angles. Moreover, a maximum energy density of 4.49 W h kg−1 at the power density of 2.63 kW kg−1 was achieved. Accordingly, utilizing renewable lignin-based materials to assemble environmentally friendly and biocompatible FSCs provides a novel option for the development of sustainable energy storage systems.
(1) The physicochemical properties of lignin (e.g., molecular weight, solubility, and purity) depending on the natural sources and extraction methods will play a decisive role in the properties of the derivative carbon materials. Thus, further endeavors should be devoted to developing feasible methods to attain stable and homogeneous lignin, in favor of optimizing the properties of carbon materials for specific applications.
(2) The carbon materials converted from lignin generally possess controllable microstructures and diverse morphologies. However, the current converting strategies are complex and costly, which severely limits their large-scale applications. Of special note, the commonly utilized alkali activators are highly corrosive to the equipment and effortlessly lead to environmental pollution. Therefore, future research should focus on developing a green route for the large-scale production of lignin carbon materials.
(3) The structure–function relationship between the microstructure of lignin-based carbons and their charge storage performance/mechanisms remains ambiguous. Operando characterization techniques, such as ATR-FTIR, EQCM-D and in situ NMR, etc., are highly desirable to investigate the alteration of surface states of lignin-based PCs during the electrochemical process, which is beneficial to expound the energy storage mechanism and lay a foundation for designing and optimizing lignin-based energy storage materials.
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