Divyashree A
ab and
Gurumurthy Hegde
*a
aBMS R and D Centre, BMS College of Engineering, Bull Temple Road, Bangalore, 560019, India. E-mail: murthyhegde@gmail.com
bSai Vidya Institute of Technology, Bangalore, 560064, India. E-mail: ria.divyashree@gmail.com
First published on 8th October 2015
Supercapacitors are perfect energy storage devices; they can be charged almost instantly and release energy over a long time. They can be charged multiple times with minimal degradation in performance. Supercapacitor performance is determined by the composition of the electrode and advanced configurations. In this review, we compare the performance of different electrode materials which are obtained from biowaste based precursors. Our main interest in this review is to study the supercapacitor properties using carbon based spherical natured particles well known as carbon nanospheres. Carbon based electrodes, particularly bio-waste activated carbon nanospheres, have gained interest due to their excellent energy storage ability. In this paper, Activated Carbon Nanospheres derived from several bio-waste materials are reviewed on the basis of their cyclic voltammograms, specific capacitances, surface areas, electrolytes used and fabrication process.
Batteries are rechargeable storage devices that convert the stored chemical energy into electrical energy through redox reactions at anode and cathode, the conversion and storage of the energy occurs in the same compartment.7,8 This principle was first proposed by Becker in 1957.9,11 The electrochemical reaction involves the transfer of electrons from anode to cathode when the battery is connected to an external load.12,13
The cross section of a conventional battery, the electrons built in the anode due to the redox reaction causes a potential difference between anode and cathode as shown in Fig. 1. When an external load is connected to anode and cathode, a closed path is established between them and the electrons begin to flow from anode to cathode constituting to the electric current.
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Fig. 1 Cross section of a conventional rechargeable battery with anode, electrolyte and cathode connected using an external electrically powered device.10 |
When the battery has to be recharged, the direction of the flow of electrons is reversed using another power source. This helps in restoring the original state of anode and cathode for further redox reaction.14,15
The chemical reactants required for the smooth working of the battery is stored within the battery. Once the chemical reactants are completely used up, the batteries have to be either recharged or disposed. This stands as a major hurdle in the energy storage sector and hence fuel cells came into existence. Fuel cells can generate power as long as there is a fuel supply.
Fuel cell are the electrochemical device that converts chemical energy obtained from the fuel into electricity through a chemical reaction between the positively charged hydrogen ions with an oxidizing agent preferably oxygen.16 Electricity is produced as long as there is a flow of fuel into the cell.17,18 Fuel cell comprises of three adjacent layers: anode, cathode and electrolyte. Fuel is consumed due to the chemical reactions that occur at the interface of the three different segments resulting in the precipitation of water which in turn produces an electric arc.19
Basically fuel cells are the devices that combine fuel with oxygen to produce electricity, heat and water as a by-product see Fig. 2. Apart from anode, cathode and electrolyte fuel cells have an additional layer called the catalyst layer. This layer helps in speeding up the chemical reaction. The reaction between the fuel and air occurs at anode and cathode. The cathode receives oxygen from the ambient air. From Fig. 2, it can be seen that hydrogen is produced in the anode through a reforming process between the hydrocarbon fuel and water. Subsequently the hydrogen is then electrochemically consumed in carbonate electrolyte medium producing water and electrons.
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Fig. 2 The cross section of a fuel cell showing the interface between the layers along with the chemical reaction occurring at each layer.20 |
Further the electrons flow through the external load owing to the electric current. The electrons return to the cathode which is made use of in the electrochemical reaction. Oxygen along with carbon di-oxide that is recycled from the anode reacts with the electrons in the cathode producing the carbonate ions. The anode reaction is supported by these carbonates that reach the anode through the electrolyte.
Due to the advantages of the fuel cells, it was used as a source of power for a quite bit of time but fuel cell requires a considerable amount of start-up time making it inevitable to use a short-term energy source till the fuel cell starts to operate in full swing. This drawback is overcome by the supercapacitors which ramps up huge current with negligible amount of voltage drop.
Electrochemical Capacitors (EC) also called as supercapacitors or Electric Double Layer Capacitors (EDLC) stores charge either using ion absorption or redox reactions.21–23 The performance of the supercapacitor depends on the charge accumulation capability from an electrolytic solution through electrostatic attraction by polarized electrodes.24,25 EDLCs consist of an isolator in addition to anode, cathode and electrolyte to electrically separate the two electrodes. The metal–electrolyte interface can store charge up to ∼106 Farad.26 The capacitance that is produced from the electrochemical double layer is analogues to a parallel plate capacitor.21 The excess or deficiency of the charge, builds up on the surface of the electrode.27,28 In order to provide the electroneutrality, ions of the opposite charge build in the electrolyte near the electrode–electrolyte interface.28,29 The structure of an electric double layer capacitor with electrolyte separating the two electrodes is as shown in the Fig. 3.
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Fig. 3 Basic structure of electric double layer capacitor.30 |
The specific capacitances and the performance of the supercapacitors fabricated with various metal oxide obtained at different scan rates is as shown in the Fig. 4. From the Fig. 4 we observe that the performance of the electrode with Co3O4 delivers the best specific capacitance in comparison to all the precursors.
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Fig. 4 Specific capacitance obtained at different scan rates for different metal oxide thin film based supercapacitors.32 |
Supercapacitor comprises of two non-reactive porous plates which are suspended within an electrolyte with voltage applied across the porous plates.34 The potential applied on the cathode attracts the electrons from the electrolyte while the potential applied on the anode attracts the positive charge as shown in Fig. 5.34 This phenomenon effectively gives room to two layers for the chare storage.35 This helps in making supercapacitors more suitable for electrostatic storage of charges.
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Fig. 5 Schematic diagram of charge distribution in a supercapacitor.34 |
The charging and discharging of the electric double layer supercapacitor is as shown in Fig. 6. It shows the concentration of charge distribution around the electrode during charging and discharging of a supercapacitor. The characteristics of a supercapacitor as listed in Table 1 pronounces the galvanometric characteristics of a typical supercapacitor.
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Fig. 6 The structure of double layer capacitor during charging and discharging.40 |
Features | Range |
---|---|
Voltage level (V) | 50–100 V |
Current (I) | 100–300 A |
Pulse duration (Δt) | 1.0 ms to 1 s |
Capacitance © | 1–10 F |
Power density (kW L−1) | 5–180 |
Energy density (kJ L−1) | 0.5–0.6 |
ESR ® | 20–30 |
Temperature cycle | −20 °C to +60 °C |
Comparison of the energy density versus power density characteristics of batteries, supercapacitors and capacitors is as shown in Fig. 6.34
Fig. 7 depicts that energy density of a supercapacitor falls in-between that of a battery and a conventional capacitor. It clearly shows that the power storage capacity with least drop in the voltage is high in batteries followed by supercapacitors and capacitors respectively.
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Fig. 7 Energy density versus power density of capacitors, batteries and supercapacitors.34 |
From the Fig. 8, it is visible that supercapacitors occupy a significant position in specific energy and specific power. The need for energy storage in the present world is met by supercapacitors because of its high power capability and huge energy density.36 Supercapacitors operate in a wide range of temperature; they have long cycle-life and also deliver high power density.37
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Fig. 8 Ragone plot of energy storage devices.17 |
The comparison between the capacitor, battery and a supercapacitor is as listed in the Table 2. From Table 2, it is clearly visible that the supercapacitors are better than conventional batteries and a simple capacitor.
Function | Electronic capacitor | Battery | Supercapacitor |
---|---|---|---|
Charge time | μs–ms | Hours | ms–min |
Discharge time | μs–ms | 1–900 min | ms–days |
Energy density | <0.01 W h L−1 | 50–300 W h L−1 | 0.5–5 W h L−1 |
Power density | >104 W L−1 | <500 W L−1 | 103 to 3 × 103 |
Cycle life | 106 to 108 | 200–1000 | 106 to 108 |
Supercapacitors are widely preferred over conventional capacitors as they can store more energy in comparison with conventional capacitors.38 Substantially more energy can be stored in the supercapacitors because the interface between the electrolyte and electrode which facilitates the charge separation in the electrical double layer is very bleak and comparatively more amount of charge can be stored due to the high surface area formed as a result of large number of pores. Charging of the supercapacitor is rapid as it just involves in the movement of ions to and from to electrode superficially.35 Supercapacitors have a high degree of reversibility and better cycle life. The distinguishing criteria in supercapacitors are electrode material, structure and electrolyte. On the electrode materials used, supercapacitors can be classified into carbon based and metal oxide based.
The most important criteria in using the metal oxide electrode are the faradaic process.39,40 These electron-conducting reactions predominantly occur in oxides of ruthenium, iridium, iron, manganese etc. The storage and the discharge of the charge occur with the proton insertion and liberation. The electrodes made from metal oxides are known to have better reversibility and long-time stability. But the cost of production of the metal based supercapacitors is very high. Metal oxide based supercapacitors also suffers from self-discharge poor performance at low temperature and degradation in the collector current.41,42 In considering all these aspects, supercapacitors fabricated from metal oxides as precursor, the technology is at infancy. Carbon precursor is preferred as the electrode material in supercapacitors due to its low cost, easy availability, high surface area, and easy production methodologies.43 Carbon electrodes also contribute to the high stability and conductivity due to its enhanced pore volume distribution.
Materials | Specific surface area (m2 g−1) | Density (g cm−3) | Aqueous electrolyte | Organic electrolyte | ||
---|---|---|---|---|---|---|
(F g−1) | (F cm−3) | (F g−1) | (F cm−3) | |||
Carbon materials | ||||||
Commercial activated carbons (ACs) | 1000–3500 | 0.4–0.7 | <200 | <80 | <100 | <50 |
Particulate carbon from SiC/TiC | 1000–2000 | 0.5–0.7 | 170–220 | <120 | 100–120 | <70 |
Functionalised porous carbons | 300–2200 | 0.5–0.9 | 150–300 | <180 | 100–150 | <90 |
CNT | 120–500 | 0.6 | 50–100 | <60 | <60 | <30 |
Templated porous carbons (TC) | 500–3000 | 0.5–1 | 120–350 | <200 | 60–140 | <100 |
Activated carbon fibers (ACF) | 1000–3000 | 0.3–0.8 | 120–370 | <150 | 80–200 | <120 |
Carbon cloth | 2500 | 0.4 | 100–200 | 40–80 | 60–100 | 24–40 |
Carbon aerogels | 400–1000 | 0.5–0.7 | 100–125 | <80 | <80 | <80 |
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||||||
Carbon-based composite materials | ||||||
TC–RuO2 composite | 600 | 1 | 630 | 630 | ||
CNT–MnO2 composite | 234 | 1.5 | 199 | 300 | ||
AC–polyaniline composite | 1000 | 300 |
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Fig. 9 600 dpi in TIF format)[QUESTION MARK]?>Capacitive performance of electrodes made from carbon.47 |
Templated process is the most widely used technique in producing porous carbons for supercapacitor application. Templated porous carbons having microporous mesoporous and macroporous sizes with a tailored hierarchical structure as shown in the Fig. 10 acts as superior electrode materials for the supercapacitor.47,48
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Fig. 10 Schematic representation of micropore, mesopore and macropore in a carbon particle.49 |
From Fig. 11 it's clear that the microporous carbon well distributed with the narrow pore size in an ionic electrolyte is well suited for high energy density electrodes in a supercapacitor.
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Fig. 11 Normalized capacitance as a function of pore size of the carbon electrode in ionic electrolyte medium.50 |
Chiefly the electrodes made from carbon because of its low cost, easy accessibility and processability. Carbon-materials is stable both in acidic as well as basic solutions.57 It can be used in wide range of temperatures. By using various physical activation methods, it is possible to produce materials with huge surface area and controlled pores distribution that chiefly determines the electrode–electrolyte interface for electrochemical application.58
Taking into account all these physical and chemical characteristics which is listed in Table 4, the electrodes made from carbon for the storage of energy in electrochemical capacitors is hugely advantageous. The surface functionalities of the porous activated carbon nanospheres forms an important criterion in the capacitive performance as they affect the wettability of the carbon surface by the electrolyte and this exhibits pseudo capacitance.59 In this regard nano-porous carbons which are produced using template methods have well controlled pore size, large specific area and interconnected pore network.60,61
Carbon | Specific capacity (F g−1) | Specific capacity (F cm−2) | BET (m2 g−1) | Pore volume (cm3 g−1) | Pore size (Å) |
---|---|---|---|---|---|
M-10 | 55.95 | 0.041 | 1370 | 0.500 | 9.12 |
M-14 | 57.20 | 0.0047 | 1223 | 0.561 | 9.60 |
M-15A | 78.10 | 0.043 | 1800 | 0.629 | 9.17 |
M-15B | 55.80 | 0.034 | 1624 | 0.563 | 9.37 |
M-15C | 63.34 | 0.042 | 1518 | 0.600 | 9.79 |
M-20 | 100 | 0.046 | 2130 | 0.709 | 14.73 |
M-30 | 62.9 | 0.024 | 2571 | 1.230 | 14.95 |
A-10 | 35.3 | 0.031 | 1150 | 0.424 | — |
A-20 | 41.20 | 0.020 | 2012 | 0.902 | 14.23 |
SACF-20 | 48.8 | 0.027 | 1839 | 0.699 | 9.74 |
SACF-25 | 27.9 | 0.011 | 2371 | 0.977 | 11.93 |
Activated carbon nanospheres in its crude form before the post processing is as shown in the Fig. 12.
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Fig. 12 Activated carbon nanospheres.49 |
Constituent | Percentage of lignocellulose (%) |
---|---|
Paper and paper products | 37.8 |
Food waste | 14.2 |
Yards waste | 14.6 |
Wood waste | 3.0 |
Total cellulose waste | 69.6 |
Plastic | 4.6 |
Rubber and leather | 2.2 |
Textiles | 3.3 |
Glass and ceramics | 9.0 |
Metals | 8.2 |
Miscellaneous | 3.1 |
Total | 100 |
The reasonable way to address the global economic issues is to make use the bio-waste.72 The structural components of the cells, cellulose and hemicellulose of bio-waste are suitable for the energy storage devices.73
The lignocellulosic biomass is the primary fraction of the solid bio-waste comprising of 35–50% of cellulose.74,75 The raw materials obtained from bio-waste have vast option in the energy storage industry.76 Percentage of lignocellulose composition in various bio-waste materials is as listed in Table 5. The use of bio-waste materials has relatively less harmful environmental impacts; it is cost effective and also helps in the reduction on the dependency on fossil fuels.77,78
Sugarcane bagasse rinsed in hot water at 100 °C using sonicator for 8 hours is further air dried at the same temperature for 48 hours. The residue obtained after drying is mixed with ZnCl2 in the ratio 1:
1. The same mixture is then sonicated four 4–5 hours in room temperature, followed by air drying at 100 °C produces activated carbon nanospheres.85
Activated carbon nanospheres after the treatment were found to possess surface area of 2871 m2 g−1, specific capacitance of 109 F g−1 and pore volume of 0.81 cm3 g−1 in 1 M H2SO4 electrolyte. It showed retention of 77% after 10000 cycles.85
The Ragone plot as shown in the Fig. 13, confirms that the carbons derived by treating sugarcane bagasse is suitable in supercapacitor fabrication.
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Fig. 13 Ragone plot for the activated carbon nanospheres obtained from sugarcane bagasse.85 |
Ground coffee beans mixed with ammonium polyphosphate heated to 1000 °C in a microwave oven for about 30 min and then cooled for about 2 hours yields the carbon that is suitable for supercapacitor application.89
Activated carbon nanospheres obtained after synthesising ground coffee beans had the surface area of 999.67 m2 g−1, specific capacitance of 286 F g−1 in 1 M H2SO4 electrolyte and pore volume of 0.57 cm3 g−1. It is found to be stable even after 2000 cycles in both acidic and alkaline electrolytes.89
From Fig. 14, it can be seen that the shape of the cyclic voltammogram is quasi rectangular which indicates that ground coffee beans can be used for energy storage application.
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Fig. 14 Cyclic voltammograms of activated carbon nanospheres obtained from ground coffee beans in 1 M H2SO4.89 |
Activated carbon nanospheres is obtained by drying ground corncobs for 12 hours at 120 °C followed by heating to 400 °C for hours under the flow of nitrogen. The carbonized powder is then sonicated in KOH solution for two hours and then dried in vacuum for about 12 hours at 120 °C which is further heated to 800–900 °C under the thin flow of nitrogen.93
Activated carbon nanospheres obtained from the process is found to possess surface area of 3530 m2 g−1, total pore volume of 1.95 cm3 g−1, specific capacitance of 401.6 F g−1 in 1 M H2SO4 electrolyte. The retention is found to be observed after 100000 cycles.93
It is observed that quasi rectangular structure is obtained from quasi voltammogram as shown in the Fig. 15 proving that corncob is suited for supercapacitor application.
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Fig. 15 Cyclic voltammograms of activated carbon nanospheres obtained from corncob.93 |
Carbon fiber cloth immersed in 70 mL KMnO4 solution for one day at 60 °C followed by rinsing and drying of the same in deionised water at 65 °C yields activated carbon nanospheres which is suitable for the fabrication of electrodes for supercapacitor application.95
The MnO2 film coated with processed natural flax activated using KMnO4 is found to have specific capacitance of 325.8 F g−1, surface area of 645 m2 g−1, 94% retention was found in the capacitance after 1000 cycles.95
The cyclic voltammogram curves as shown in Fig. 16 shows the supercapacitance characteristics of carbon fiber.
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Fig. 16 Capacitive performance of processed natural flax using cyclic voltammogram.95 |
Ground acacia gum dissolved in water and sonicated is vacuum heated to 180 °C for 12 hours. The precipitate obtained after cooling is rinsed with water and ethanol followed by drying at 60 °C for 8 hours. The carbon obtained is mixed with KOH and heated in a tube furnace under the flow of nitrogen for about an hour. The porous carbon is then rinsed with 1 M HCl and dries at 110 °C for 12 hours.98
The obtained microporous carbon has a surface area of 1764 m2 g−1, total pore volume of 0.99 cm3 g−1 and specific capacitance of 272 F g−1 in 1 M HCl and has a capacitance retention of 59% after 1000 cycles.98
The CV curves shows a quasi-rectangular structure which can be seen in Fig. 17 owing to the typical characteristics of a supercapacitor.
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Fig. 17 Cyclic voltammograms of activated carbon nanospheres obtained from acacia gum.98 |
Ground coconut shells are rinsing them with distilled water and dried for two days at 110 °C is carbonized by heating it to a temperature of 1000 °C for two hours under nitrogen gas flow yields activated carbon nanospheres which can be used as a precursor in fabricating electrodes for supercapacitor application.102,103
The activated carbon nanospheres obtained after KOH activation and further post processing of coconut shells were found to have a surface area of 2000 m2 g−1, total pore volume of 1.21 cm3 g−1, specific capacitance of 250 F g−1 in 1 M H2SO4 electrolyte. 93% capacitance retention was observed after 2000 cycles.102,104
The cyclic voltammometric curve as shown in the Fig. 18 depicts a quasi-rectangular shape. This proves that the activated carbon nanospheres obtained from coconut shell as a precursor is well suited for supercapacitor application.
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Fig. 18 Cyclic voltammograms of activated carbon nanospheres obtained from coconut shell in 1 M H2SO4 electrolyte.104 |
Impregnated sunflower seed shells in KOH is dried for 12 hours at 100 °C is carbonized using a tube furnace under nitrogen gas flow at a temperature ranging between 600–800 °C for about an hour. The residue obtained is washed through with 0.1 M HCl followed by distilled water and dried thoroughly yields the carbons which is suitable for supercapacitor application.107
The carbon sample obtained after the processing of sunflower seed shell is found to have specific capacitance of 244 F g−1 in 0.1 M HCl electrolyte, surface area of 2585 m2 g−1 and total pore volume of 1.41 cm3 g−1 and a good cycle stability.107
From the Ragone plot as shown in the Fig. 19, it proves that the activated carbon nanospheres obtained using sunflower seed shells as a precursor is suitable for supercapacitor applications.
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Fig. 19 Ragone plot for the carbons obtained by sunflower seeds as a precursor.107 |
Cleaned, dried and ground rice husk is impregnated in 0.5 M NaOH solution for 2 hours at 343 K. It is further sonicated and soaked in ZnCl2 solution for 2 hours and dried for 48 hours at 383 K. The residue obtained is then dried to obtain the porous activated carbon nanospheres.113
The activated porous carbon obtained from rice husk has the specific capacitance of 171 F g−1 in an organic electrolyte, surface area of 1768 m2 g−1 and total pore volume 1.07 cm3 g−1. A negligible degradation in the specific capacitance was observed even after 1000 cycles of charge and discharge.113,114
The quasi-rectangular shape of the CV curve as shown in the Fig. 20 depicts the ion diffusion and hence proving their absorption quality in supercapacitor application.
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Fig. 20 CV curve of electrodes made from porous carbon obtained from rice husk at different scan rate.113 |
Dissolved carrageenan is vacuum heated for 12 hours at 200 °C. The precipitate is collected using centrifugation technique and is dried at 70 °C for 8 hours after it has been washed in ethanol solution. The carbon that is produced is activated chemically using KOH. The mixture obtained is heated using a tube furnace under nitrogen flow for two hours. Activated carbon nanospheres is obtained by cleansing the same using 2 M HCl and water which is further dried at 110 °C for 12 hours.119
Activated carbon nanospheres obtained from carrageenan after KOH activation has a surface area of 2502 m2 g−1 in 6 M KOH electrolyte, total pore volume of 1.43 cm3 g−1, specific capacitance of 230 F g−1 in aqueous electrolyte. A small bleak in capacitance retention was observed after 1000 cycles.119
The electrochemical capacitive properties of the activated carbon nanospheres obtained from carrageenan studied using a cyclic voltammometer showed that the activated carbon nanospheres exhibited quasi-rectangular shape as shown in the Fig. 21 proving its suitability in double layer capacitance application.
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Fig. 21 CV curves of activated carbon nanospheres obtained from carrageenan.119 |
Self-adhesive carbon fibers prepared by pre-carbonization of oil palm seeds at a temperature of 280 °C which is followed by milling continuously for 8 hours.126 The mixture is wetted using deionised water for an hour and is treated with KOH solution. The mixture is carbonised in nitrogen atmosphere at 800 °C to obtain activated carbon nanospheres.127
Activated carbon nanospheres obtained from the above process were found to possess a surface area of 1704 m2 g−1, total pore volume of 0.89 cm3 g−1, specific capacitance of 343 F g−1 using KOH + CO2 activation in 1 M H2SO4 electrolyte. And it has a cycle life of about 2500 cycles.127
Recently Gomma et al.125 reported a reasonably promising specific capacitance values using catalyst free carbon nanospheres obtained from bio-waste oil palm leaves.127 Template method is considered as a responsible factor for increasing specific capacitance without activating carbon.
The cyclic voltammogram of the activated carbon nanospheres from oil palm leaves is as shown in the Fig. 22. A large window area shows the apt electrode performance of the obtained activated carbon nanospheres.
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Fig. 22 CV curves of activated carbon nanospheres obtained from oil palm.125 |
Double layered hydroxides are synthesized in the presence of graphene by the process of co-precipitation of Co2+ and Ni2+ ions using NH3·H2O as a precipitator. The electrochemical performance of the resultant was found to have a specific capacitance of 2770 F g−1 and shows 93.4% retention after 500 cycles.129
Activated carbon nanospheres were synthesized by one step pyrolysis using shaddock peel as the precursor. Shaddock peel is first washed using distilled water which is then dried at a temperature of 80 °C for about 12 hours in vacuum. The resultant is then pyrolysed at 800–1400 °C in inert atmosphere for 2 hours. The product is then washed using HCl and distilled water followed by drying at a temperature of 120 °C for 12 hours.131
Activated carbon nanospheres obtained from the above process were found to possess a surface area of 1272 m2 g−1 with pore volume of 0.49 cm3 g−1 distributed over 0.6–15 nm range. It is found to have a stable cycle life.132
Cyclic voltammograms of the activated carbon nanospheres obtained from shaddock peel is as shown in the Fig. 23. It depicts the CV curves of the carbon obtained at a scan rate of 0.1 mV s−1.
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Fig. 23 CV curve of activated carbon nanospheres derived from shaddock peel.131 |
Change in texture under different pressure of processing showed that the asparagus lettuce cells at low pressure were found to be spherical and small. At moderate pressure, it was found that there was an initial texture loss in the asparagus lettuce due to loose skeleton wall. At high pressures, there was apparently less texture loss of asparagus lettuce which was the resultant of the unchanged pectin distribution. This shows that the asparagus lettuce cells synthesized at high pressure are spherical in shape and are applicable in supercapacitors.133
Several carbon nanospheres obtained from bio-waste materials showed excellent performance in the area of supercapacitors. Advantages of reducing pollution in the environment followed by the cost reduction are the key factors for the future generation supercapacitors. Different bio-waste materials showed different characteristics which is listed in Tables 6 and 7 based on their lignocellulosic content. So it is worth-while to study more in this aspect, so that one is able to get high energy supercapacitors using carbon nanospheres which are obtained from cost effective bio-waste materials.
Bio-waste carbon source | Activation method | Surface area (m2 g−1) | Specific capacitance (F g−1) | Electrolyte | Reference |
---|---|---|---|---|---|
Sugarcane bagasse | ZnCl2 | 2871 | 109 | 1 M H2SO4 | 85 |
Coffee beans | ZnCl2 | 999.67 | 286 | 1 M H2SO4 | 89 |
Corncob | KOH | 3530 | 401.6 | 1 M H2SO4 | 93 |
Natural flax | KMnO4 | 645 | 325.8 | 1 M H2SO4 | 95 |
Acacia gum | KOH | 1764 | 272 | 1 M HCl | 98 |
Coconut shell | KOH | 2000 | 250 | 1 M H2SO4 | 102 |
Sunflower seeds | KOH | 2585 | 244 | 0.1 M HCl | 107 |
Rice husk | ZnCl2 | 1768 | 171 | 0.5 M NaOH | 113 |
Carrageenan | KOH | 2502 | 230 | 6 M KOH | 119 |
Oil palm | No activation | — | 342 | 5 M KOH | 125 |
Scaphium scaphigerum | No activation | — | 2770 | — | 129 |
Shaddok peel | HCl | 1272 | — | 0.1 M HCl | 132 |
Asparagus lettuce cells | — | — | — | — | 133 |
Bio-waste carbon source | Pore volume (cm3 g−1) | Stability (cycle life) | Reference |
---|---|---|---|
Sugarcane bagasse | 0.81 | 10![]() |
85 |
Coffee beans | 0.57 | 2000 | 89 |
Corncob | 1.95 | 100![]() |
93 |
Natural flax | — | 1000 | 95 |
Acacia gum | 0.99 | 1000 | 98 |
Coconut shell | 1.21 | 2000 | 102 |
Sunflower seeds | 1.41 | — | 107 |
Rice husk | 1.07 | 1000 | 113 |
Carrageenan | 1.43 | 1000 | 119 |
Oil palm | 0.02 | 2500 | 125 |
Scaphium scaphigerum | — | 500 | 129 |
Shaddok peel | 0.49 | — | 132 |
Asparagus lettuce cells | — | — | 133 |
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