This paper reports the use of naturally available raw material as sugarcane bagasse (SB) to prepare cost-effective activated carbon. Activated carbon preparation from SB by using ZnCl2 was carried out by chemical activation method. The raw bagasse, its char and activated carbon were characterized on the basis of iodine number, carbon, hydrogen, nitrogen analysis, Fourier-transform infrared spectroscopy (FTIR), scanning electron microscopy (SEM), thermogravimetric analysis (TGA) and Brunauer–Emmett–Teller (BET) surface area to check their effectiveness. During activated carbon synthesis, the impregnation ratio of SB and ZnCl2 was maintained at 1:1–1:3 and activation temperature was in the range of 600–900 °C for 1 h. From the characterization study, the highest iodine adsorption of activated carbon was found to be 1140.69 mg/g with a 1:2 ratio at 900 °C whereas char gives an iodine number of 529.63 mg/g at the same temperature. The BET surface area of raw bagasse, its char and activated carbon (SB-Zn2-900) obtained was 4.30, 514.27 and 1386.58 m2/g, respectively, which shows charrification and chemical activation improves surface area. The optimum ratio of impregnation and activation temperature was found to be 1:2 at 900 °C. In this work, activated carbon was successfully prepared and obtained product has better characteristics than previously reported studies.

  • Utilization of agricultural waste material for production of value-added material such as activated carbon.

  • Minimizes the burden of solid waste management.

  • Prepared activated carbon can be utilized for pollutant removal.

  • Minimizes water pollution by adsorption.

  • Can replace expensive commercial activated carbon.

The role of the agricultural sector in human and economic development cannot be overemphasized. The impact of agricultural solid waste on human and animal well-being as well as on the environment is substantial, which is mainly due to ignorance during managing agricultural solid waste. A lot of lignocellulosic biomass is created every year causing environmental issues and hence, one can convert agro-waste into net worth products. This step can promote the utilization of sustainable raw materials in a proper way (Hon & Siraishi 2000; Obi et al. 2016).

Due to an incessant demand for commercial activated carbon (AC) for industrial applications, the market cost of commercial activated carbon reached $1,100–1,500/tons. Hence, the preparation of activated carbon from cheap and easily available raw materials can make it cost-effective (Hock & Zaini 2018). One such agricultural waste is sugarcane bagasse (SB) which is used to synthesize biomass waste-based activated carbon in this study.

SB is the residue left after the extraction of sugarcane juice and it contains 35% of cellulose, 25% of hemicellulose and 22% of lignin (Rezende et al. 2011). SB is treated as a potential material for energy recovery. Once it has been processed properly, it can be used as a carbon-neutral energy material (Ramajo-Escalera et al. 2006; Hofsetz & Silva 2012; Dantas et al. 2013). SB is used as a fuel in sugar plants for the generation of steam and in ethanol distillation (Nunes et al. 2020). It is used in the production of derived fuels using gasification and rapid pyrolysis (Naik et al. 2010). It is also used in the paper and pulp industry for the manufacturing of corrugated boards (Samariha & Khakifirooz 2011). Due to its wide range of uses, it is no longer considered a waste nowadays. Due to high lignocellulosic content, its usefulness in the form of char and activated carbon is capturing researchers’ attention. The microporous structure of any activated carbon is due to its high cellulose and low lignin content (Misran et al. 2018; Dwiyaniti et al. 2020).

The term ‘char’ represents the solid residue that forms after thermal degradation of carbon-rich agricultural waste in limited oxygen conditions. It consists of organic material with a composition varying from barely carbonized agricultural waste at low temperatures to a highly carbonized material at high temperatures. The physical and chemical characteristics of biochar depend on the temperature used for pyrolysis and the type of biomass used. It can be used to improve contaminated soil quality, soil productivity, removal of toxic metals and production of bio-fuel, etc. (Kumar & Bhattacharya 2018). Activation of biochar can also be found useful in removing particular contaminants from water.

There are various methods used for the removal of pollutants removal from liquid or gaseous phases like membrane filtration, precipitation and coagulation, reverse osmosis distillation, adsorption, ion-exchange, photochemical degradation, biological degradation and chemical oxidation (Rashed 2013; Raut et al. 2021). Amongst these methods, the adsorption of organic as well as inorganic impurities with activated carbon is gaining importance and has been widely used (Harry & Francisco 2006). It has been found to be an economical and effective treatment method because of no sludge formation (Ioannidou & Zabaniotou 2007).

Activated carbons are porous materials with rich porosity and larger surface area with greater adsorption capacity (Paraskeva et al. 2008; Oubagaranadin & Murthy 2012). Activated carbons possess a large internal surface area in the range of 500–2,000 m2/g (Chisutia et al. 2014). Activated carbon synthesis can be carried out by two methods: physical and chemical activation. Physical activation (Salgado et al. 2018) involves the carbonization of a precursor followed by activation. CO2 or steam gasifying agents were used as a medium of activation. Carbonization is carried out between 400 and 850 °C and activation is carried out between 600 and 900 °C. This method will help to form new functional groups which enhance the sorption properties of the char. These gasifying agents will extract carbon from the network of porous carbon given in the following reactions:
formula
(1)
formula
(2)

In chemical activation, the precursor was impregnated with a chemical agent followed by activation. The activating agents that can be used are H3PO4, ZnCl2, KOH, NaOH, Na2CO3, K2CO3 and H2SO4 (Hayashi et al. 2002; Demiral et al. 2008; Kalderis et al. 2008; Gardare et al. 2015; Ghani et al. 2017). The AC is washed with hydrochloric acid followed by deionized water and dried for further use.

This study discusses the synthesis and characterization of char and ZnCl2-made activated carbon. The effect of activation temperature and impregnation ratio on yield and iodine number was studied and discussed. The raw bagasse (precursor), char and activated carbon were characterized by iodine number, CHN analysis, Fourier-transform infrared spectroscopy (FTIR), scanning electron microscopy (SEM), thermogravimetric analysis (TGA-DTA) and Brunauer–Emmett–Teller (BET) surface area and elemental analysis energy-dispersive spectroscopy (EDS).

This study focuses on activated carbon preparation and its comparison with raw bagasse and bagasse char. Such types of comparative studies based on raw stage, char stage and activated carbon stage have not been extensively studied earlier, hence this study discusses the thermochemical conversion of bagasse into char and activated carbon.

Materials

Raw SB was collected from Manas Agro Industries (Umrer, India). Analytical (AR) grade chemicals used were dry ZnCl2 (EMPLURA), Na2S2O3 (EMPLURA), Merk Life Science, Pvt Ltd (Worli, Mumbai), resublime iodine (Q24904), KI (Loba Chemie Pvt. Ltd, Jehangir Villa, Colaba, Mumbai), HCl & starch (Fisher Scientific, Thermo Electron LLS India Pvt, Sion (East), Mumbai), purchased from Vaishnavi Scientific & Trading Company (Ayodhya Nagar, Nagpur, India). Instruments used were heating mantle (Bio Technics India, Mumbai), electric muffle furnace (Tempo Instruments, Mumbai), pH meter (Deluxe pH-101), digital balance (Citizon) and laboratory oven (BTI).

Methods

Production of SB char

Raw SB was washed and dried in an oven for 1 h at 110 °C. The dried bagasse was then cut into small pieces. The dried bagasse was kept in a muffle furnace at four different temperatures ranging from 600 to 900 °C. In the absence of an inert atmosphere, no ash was formed in obtained char. The prepared char was washed with deionized water, dried in an oven at 110 °C for 1 h and packed in an air-tight container for further use. The resulting chars were labeled as SBC600, SBC700, SBC800 and SBC900 which denote SB char at 600, 700, 800 and 900 °C. Figures 1 and 2 show raw SB and its char, respectively.
Figure 1

Sugarcane bagasse.

Figure 1

Sugarcane bagasse.

Close modal
Figure 2

Sugarcane bagasse char.

Figure 2

Sugarcane bagasse char.

Close modal

Production of sugarcane bagasse activated carbon

The sugarcane bagasse (SB) obtained from the source was washed with water for the removal of impurities and dried in sunlight for 5 days. SB was cut into small pieces and allowed to dry in a laboratory hot air oven for 1 h at 110 °C. The impregnation of bagasse with ZnCl2 was carried out on a heating mantle. For a 1:1 ratio, a known amount of SB was taken in a glass beaker. An equal amount of solid ZnCl2 in a known volume of distilled water was dissolved in another beaker. ZnCl2 solution in bagasse was added and the contents were mixed. This mixture was kept on a heating mantle at 80 °C until it turned into a paste (Ekpete et al. 2017). After 24 h, the impregnated material was kept in a muffle furnace (Tempo Instruments, Mumbai) for 1 h at 600 °C. During activation, between temperatures of 300–600 °C, gaseous products start releasing from the outlet pipe with maximum fumes. Above 600 °C, the removal of fumes stopped. The major observation after activation and cooling of the furnace was no ash formation in the prepared product. The prepared carbons were washed with 1 M HCl followed by hot deionized water until neutral pH was reached. The washed material of activated carbon was dried in an oven at 110 °C for 1 h and ground with the help of an iron rod. The ground powder was sieved through an ASTM-70 test sieve and packed in an air-tight container for further use. The activation procedure for ratios 1:2 (wt/wt) and 1:3 (wt/wt) was the same at four different temperatures from 600 to 900 °C. The resulting carbons so prepared were labeled as SB-Zn1-600, SB-Zn1-700, SB-Zn1-800, SB-Zn1-900, SB-Zn2-600, SB-Zn2-700, SB-Zn2-800, SB-Zn2-900, SB-Zn3-600, SB-Zn3-700, SB-Zn3-800, SB-Zn3-900, which denotes SB ZnCl2 followed by ratio 1:1, 1:2, 1:3 and activation temperature. The yield of activated carbon is calculated by the following equation:
formula
(3)
where W1 is the weight of activated carbon, W2 is the weight of raw material taken.

The raw SB, its char and activated carbon were characterized by iodine number which is an indication of the micro-porosity of activated carbon. It is determined as per ASTM: D4607-94 standard method. CHN analysis was carried out by using a ThermoFinnigan analyzer available at the Department of CIL, Punjab University, Chandigarh. The thermal decomposition of material was tested by TGA by using DTG-60 simultaneous DTA-TG apparatus. The functional group availability of the surface of activated carbon was recorded by FTIR by using an IR-Affinity-1 spectrometer. The amorphous or crystalline nature of activated carbon was studied by powder X-ray diffraction studies (XRD) by using Rigaku’ Miniflex diffractrometer. The surface structure of activated carbon was studied by scanning electron microscope (JEOL-6380A).

Yield of activated carbon and char

From Table 1, it is observed that activation reduces the mass of produced carbon and char. The percentage of mass loss increases with the increase in ratio and temperature. As soon as the activation temperature increases, the yield of activated carbon decreases, as shown in Table 1. The decrease in yield indicates the evolution of more volatile matter at higher temperatures (Foo & Hameed 2011). The same observation was reported by Lua & Ting (2004). Loss in weight also represents the reaction mechanism carried out between lignocellulosic material and chemical agent (Angin et al. 2013). In ZnCl2 activation, the aqueous solution is entered into the carbon skeleton to produce pores at a temperature above its melting point. The reaction between the carbon atoms and ZnCl2 is promoted in the inner layers of the carbon. The use of ZnCl2 as a chemical agent generally increases the carbon content through the formation of aromatic graphitic structures (Hock & Zaini 2018). During activation, it has been observed that around 400 °C of the removal of most volatile matter gets started like CO and CO2 due to the effect of activation. During the initial stage of thermal degradation from 400 to 600 °C, zinc chloride is completely dehydrated from water molecules taken by bagasse (Bouchemal et al. 2015). Also, it takes off H2 and O2 atoms from the carbon structure to form H2O molecules (Cartula et al. 1990). The activated carbon with the highest yield of 31.87% was obtained at 600 °C for the ratio 1:1. It has been observed from the experimental work that as the impregnation ratio increases, yield decreases. This is because at higher ratios, swelling and elasticity increase. This indicates that there may be an additional oxidation reaction occurring during impregnation with the removal of volatile matter (Hamza et al. 2015). The yield of prepared chars also decreases with increasing activation temperature. The percentage yield and loss of activated carbon and char at different temperatures are presented in Table 1.

Table 1

Percentage yield and loss of SB activated carbon (SBAC) SBAC

Sample code% Yield% Loss
SB-Zn1-600 31.87 68.13 
SB-Zn1-700 28.73 71.27 
SB-Zn1-800 26.53 73.47 
SB-Zn1-900 20.27 79.73 
SB-Zn2-600 28.53 71.47 
SB-Zn2-700 25.60 74.4 
SB-Zn2-800 22.34 77.66 
SB-Zn2-900 18.23 81.77 
SB-Zn3-600 25.12 74.88 
SB-Zn3-700 20.66 79.34 
SB-Zn3-800 18.22 81.78 
SB-Zn3-900 16.31 83.69 
SBC600 45.06 54.94 
SBC700 37.83 62.17 
SBC800 22.72 77.28 
SBC900 12.94 87.06 
Sample code% Yield% Loss
SB-Zn1-600 31.87 68.13 
SB-Zn1-700 28.73 71.27 
SB-Zn1-800 26.53 73.47 
SB-Zn1-900 20.27 79.73 
SB-Zn2-600 28.53 71.47 
SB-Zn2-700 25.60 74.4 
SB-Zn2-800 22.34 77.66 
SB-Zn2-900 18.23 81.77 
SB-Zn3-600 25.12 74.88 
SB-Zn3-700 20.66 79.34 
SB-Zn3-800 18.22 81.78 
SB-Zn3-900 16.31 83.69 
SBC600 45.06 54.94 
SBC700 37.83 62.17 
SBC800 22.72 77.28 
SBC900 12.94 87.06 

Characterization

Iodine number determination

Iodine numbers of activated carbon measure the approximate surface area and micro-pore volume. The iodine number of activated carbon and char was determined in the laboratory as per ASTM D 4607-94 standard method (Standard Test Method 2006). The milligram of I2 adsorbed on the surface of 1 g activated carbon when the iodine concentration of residual filtrate is 0.02 N. All the required solutions of I2, 10% HCl, sodium thiosulfate, potassium iodide and starch indicator were prepared in the laboratory with distilled water.

In this method, 1 g of activated carbon sample was taken in a 250 mL conical flask. Ten mL of 5% of HCl solution was added to it. The flask was then kept on a hot plate for boiling for 30 s. The flask was allowed to cool and 100 mL of 0.1 N iodine solution was added to it. The conical flask was immediately covered and shaking of contents for 30 s was carried out. The contents were filtered using filter paper immediately after the shaking period. The initial 20–30 mL of filtrate was discarded and a further 50 mL of filtrate was titrated with 0.1 N sodium thiosulfate by using starch as an indicator until the solution changes to colorless.

It can be seen from Table 2 that, in the case of SB char, the iodine number increases as the impregnation ratio increases from 1:1 to 1:3. The bagasse char gives iodine numbers of 496.17, 500.81, 504.12 and 510.75 mg/g at 600, 700, 800 and 900 °C, respectively. The maximum iodine number (510.75 mg/g) was found at 900 °C. In the case of activated carbon, the iodine number decreases first from 1:1 to 1:2 ratio from 600 to 800 °C. However, at 900 °C, as the impregnation ratio increases from 1:1 to 1:2, the iodine number increases and from 1:2 to 1:3, it decreases. The highest iodine number (1,140.69 mg/g) was obtained at 900 °C for a 1:2 ratio. Hence, the optimum impregnation ratio (bagasse: zinc chloride) was found to be 1:2. Char without activation provides a lesser iodine number than activated carbon (SB-Zn2-900). This proves that activation by using chemical reagents enhances iodine numbers and adsorption capacity.

Table 2

Iodine number of SBAC and SBC

Sample codeIodine number (mg/g)
SB-Zn1-600 970.09 
SB-Zn2-600 839.80 
SB-Zn3-600 1,062.94 
SB-Zn1-700 771.27 
SB-Zn2-700 995.37 
SB-Zn3-700 1,079.37 
SB-Zn1-800 952.91 
SB-Zn2-800 1,019.44 
SB-Zn3-800 952.91 
SB-Zn1-900 928.12 
SB-Zn2-900 1,140.69 
SB-Zn3-900 920.30 
SBC600 496.17 
SBC700 500.81 
SBC800 504.12 
SBC900 510.75 
Sample codeIodine number (mg/g)
SB-Zn1-600 970.09 
SB-Zn2-600 839.80 
SB-Zn3-600 1,062.94 
SB-Zn1-700 771.27 
SB-Zn2-700 995.37 
SB-Zn3-700 1,079.37 
SB-Zn1-800 952.91 
SB-Zn2-800 1,019.44 
SB-Zn3-800 952.91 
SB-Zn1-900 928.12 
SB-Zn2-900 1,140.69 
SB-Zn3-900 920.30 
SBC600 496.17 
SBC700 500.81 
SBC800 504.12 
SBC900 510.75 

All the prepared samples at four different temperatures with three impregnation ratios were tested for iodine number. However, the char and activated carbon with the highest iodine number are only characterized further for FTIR, XRD, SEM and BET. Hence, based on the iodine number determined, SBC900 and SB-Zn2-900 (1:2 ratio at 900 °C) were found to have the highest iodine number and therefore further characterization was carried out for FTIR, XRD, SEM and BET.

CHN analysis of raw bagasse, bagasse char and activated carbon

Elemental analysis works on the basic principle of oxidation of C, H, N and S into gases like CO2, H2O and SO2 that are then separated by the chromatographic method. In this method, an accurately weighed sample was introduced in the furnace in the presence of a constant supply of inert gases (He). Oxygen gas is injected into the inert gas stream with a sample and allowed to combust in a tin capsule. The exothermic reaction takes place with the evolution of combustion gases which raised the furnace temperature from 1,000 to 1,800 °C within a short time. The combustion gases then swept through a series of oxidation columns containing agents like chromium oxide, tungsten trioxide, cobaltic oxide, etc., which ensures complete combustion of C, H, N and S into CO2, H2O and SO2. The unreacted oxygen was then consumed by metallic copper present in the reduction column which was maintained at 700 °C and nitrogen-containing components were reduced to N2. Separation of individual gases is carried out in the chromatographic column containing porous polymer maintained at less than 100 °C. Each element was then quantified by the signal generated during its sequential passage through a thermal conductivity detector (TCD) yielding a peak in abundance at different times (Michael et al. 2017). Elemental analysis was carried out on a ThermoFinnigan analyzer available at the Department of CIL, Punjab University, Chandigarh. The CHN analysis of raw bagasse, its char and activated carbon (SB-Zn2-900) is shown in Table 3.

Table 3

CHN analysis of raw SB, SBAC and SBC

Samples% Carbon% Hydrogen% Nitrogen
Raw SB 42.049 5.538 0.106 
Sugarcane bagasse char (SBC) 48.150 2.076 0.018 
SB-Zn2-900 80.126 3.569 1.873 
Samples% Carbon% Hydrogen% Nitrogen
Raw SB 42.049 5.538 0.106 
Sugarcane bagasse char (SBC) 48.150 2.076 0.018 
SB-Zn2-900 80.126 3.569 1.873 

Thermogravimetric and differential thermal analysis of raw bagasse, bagasse char & activated carbon

The thermal decomposition of raw material was tested by TGA-DTA analysis. TGA was carried out on DTG-60 simultaneous DTA-TG apparatus (SHIMADZU CORP. 00812), available at RTMNU, Nagpur. In this analysis, samples were heated in an inert environment like nitrogen (flow rate 20 mL/min) at a controlled rate of 10 °C/min up to 900 °C. The temperature was raised at a constant rate for a known weight of sample and changes in weights were recorded as a function of temperature at different time intervals. The plot of change in weight with respect to temperature is plotted as a thermogram.

The decomposition of raw bagasse was observed in three stages. In the first stage, the removal of moisture takes place below 150 °C (Hanum et al. 2017), in the second stage, the decomposition of cellulose and lignin were observed in the range of 250–400 °C and in the third stage the curves become flat above 400 °C. This was due to the aromatization of lignin and at this stage, less weight loss occurs. Raw SB decomposition is shown in Figure 3.
Figure 3

TGA-DTA curve of raw bagasse.

Figure 3

TGA-DTA curve of raw bagasse.

Close modal
The decomposition of char with increasing temperature is shown in Figure 4. In the case of char, in the range of 100–400 °C, an almost flat curve was observed and above 400 °C considerable weight loss occurs up to 600 °C. Above 600 °C, very little weight loss was observed, as shown in Figure 4.
Figure 4

TGA-DTA curve of char.

Figure 4

TGA-DTA curve of char.

Close modal
Activated carbon shows moisture removal up to 150 °C. The major decomposition process occurs between 200 and 400 °C with a weight loss of approximately 70%wt (Wereko-Brobby & Hagen 1996). Above 600 °C, little weight loss was found as per the TGA curve shown in Figure 5. At lower temperatures, decomposition of lignocellulosic material takes place and at higher temperatures, lignin decomposes, as shown in Figure 5.
Figure 5

TGA-DTA curve of activated carbon (SB-Zn2-900).

Figure 5

TGA-DTA curve of activated carbon (SB-Zn2-900).

Close modal

Fourier-transform infrared spectroscopy of raw bagasse, char and activated carbon

The functional group availability on the surface sample was recorded by Fourier-transform infrared spectrophotometer IR-Affinity-1 (SHIMADZU CORP), available at RTMNU, Nagpur. A broad peak at 3,329.43 cm−1 corresponds to free phenolic –OH stretching which is attributed to the –OH group of alcohols, carboxyl and phenols. The peaks at 1,000–1,200 cm−1 show the existence of a phenolic and alcoholic group which is identified in raw bagasse. The FTIR spectra of raw SB is shown in Figure 6.
Figure 6

FTIR spectra of raw bagasse.

Figure 6

FTIR spectra of raw bagasse.

Close modal
FTIR spectra of char at 1,711.65 and 1,568.96 cm−1 corresponds to the –C = O group stretching of carboxylic acid. The band at 1,089.79 cm−1 indicates the presence of a primary amine. The FTIR spectra of bagasse char is shown in Figure 7.
Figure 7

FTIR spectra of char.

Figure 7

FTIR spectra of char.

Close modal

FTIR spectra of ZnCl2 activated carbon shows peaks around 3,600–3,700 cm−1 which corresponds to free phenolic –OH stretching which is attributed to the –OH group of alcohols, carboxyl and phenols. This band is not observed in char corresponding to structure decomposition and hydroxyl group removal. The bands obtained between 2,857 and 3,000 cm−1 are due to symmetric and asymmetric C–H vibrations. The band at 2,926.38 cm−1 shows methylene C–H stretching. This peak does not exist in char. The band around 1,747.58 cm−1 shows the presence of a C–O double bond group. The band at 1,555.27 cm−1 informing aromatic C = C ring. The peaks at 1,000–1,200 cm−1 show the existence of phenolic and alcoholic groups which are identified in raw bagasse, char and activated carbon. The peaks around 600–900 cm−1 denote the existence of an aromatic ring structure which is observed in raw bagasse, char and activated carbon. The transmittance at 1,000–1,300 cm−1 was observed in raw bagasse only which corresponds to C–O stretching in ethers. After activation of bagasse, C = O stretching in aldehydes, ketones and C–O stretch in ethers disappeared in the same fashion as reported by Guo & Lua (2000). At high temperature C–O and C = O groups were removed, forming polyaromatic structures (Li et al. 2008; Abdul Hamid et al. 2014).

It is proven from the FTIR spectra that raw bagasse and char show much less functional groups. The appearance of functional groups occurred by chemical activation at various temperatures. The activated carbon was found to contain aliphatic, aromatic and oxygen-containing functional groups. The FTIR spectra of activated carbon is shown in Figure 8.
Figure 8

FTIR spectra of activated carbon (SB-Zn2-900).

Figure 8

FTIR spectra of activated carbon (SB-Zn2-900).

Close modal

XRD of raw bagasse, char and activated carbon

Structural analysis was carried out by powder XRD studies. XRD study was carried out by using ‘Rigaku’ (Miniflex) diffractrometer, available at RUSA, Nagpur. XRD studies show the amorphous or crystalline nature of materials. X-ray scattering is an analytical technique which gives information about the crystallographic structure, chemical composition and physical properties of materials. These techniques are based on detecting the scattered intensity of an X-ray beam hitting a sample as a function of incident and scattered angle, polarization and wavelength or energy (Pradhan 2011).

Crystalline material shows sharp peaks while amorphous material shows a single broad diffused peak. The diffraction spectra was recorded at the rate of 0.02 °C. The angle range (2θ) was investigated between 0 and 70 °C. XRD pattern of raw bagasse is shown in Figure 9.
Figure 9

XRD pattern of raw bagasse.

Figure 9

XRD pattern of raw bagasse.

Close modal
XRD data of bagasse char show the amorphous nature of char with no sharp peaks. The XRD spectra is shown in Figure 10.
Figure 10

XRD pattern of char.

Figure 10

XRD pattern of char.

Close modal
The XRD spectra of activated carbon confirms the amorphous nature of activated carbon. The XRD spectra of activated carbon is shown in Figure 11.
Figure 11

XRD pattern of activated carbon (SB-Zn2-900).

Figure 11

XRD pattern of activated carbon (SB-Zn2-900).

Close modal

SEM of raw bagasse, char and activated carbon

The surface morphology of activated carbon was studied by scanning electron microscope. The SEM gives an indication of the nature of porosity. A SEM is a type of electron microscope that scans a sample with a high-energy electron beam. The electrons interact with the atoms of the sample thereby producing signals which tell about the surface structure of the sample, its composition and other properties such as electrical conductivity. In the SEM technique, the sample was coated with gold for good conductivity. Surface morphology was obtained by magnifying the real image 1,200 times (Pradhan 2011). The scanning electron microscope used was the JEOL-6380A model available at VNIT, Nagpur.

It can be observed from the micrographs that no pores were observed on the surface of raw bagasse. The SEM images of raw bagasse is shown in Figure 12.
Figure 12

SEM image of raw bagasse.

Figure 12

SEM image of raw bagasse.

Close modal
During char formation, volatiles are removed thereby producing pores on the char surface. The SEM image of bagasse char is shown in Figure 13.
Figure 13

SEM image of bagasse char.

Figure 13

SEM image of bagasse char.

Close modal
More cavities and a wider pore network were observed on the activated carbon surface (Hanum et al. 2017). It is concluded from SEM images that chemical activation leads to the formation of pores and widening of existing pores. This confirms the porous nature of activated carbon. The SEM image of activated carbon SB-Zn2-900 is shown in Figure 14.
Figure 14

SEM image of activated carbon (SB-Zn2-900).

Figure 14

SEM image of activated carbon (SB-Zn2-900).

Close modal

BET surface area of raw bagasse, char and activated carbon

BET surface area analysis is the multi-point measurement of specific surface area through gas adsorption analysis in which an inert gas nitrogen is continuously flown over a solid sample of activated carbon. Small gas molecules adsorb to the solid substrate and its porous structures due to weak van der Waals forces, forming a monolayer of adsorbed gas. This monomolecular layer and rate of adsorption can be used to calculate the specific surface area of a solid sample (Pradhan 2011). It was determined by QUANTACHROME (Nova-Touch) surface area analyzer available at RTMNU, Nagpur.

The raw bagasse has 0 m2/g of surface area with a pore volume 0.4771 cc/g. The linear isotherm of adsorption–desorption of nitrogen for raw bagasse is shown in Figure 15.
Figure 15

Linear isotherm of raw bagasse char.

Figure 15

Linear isotherm of raw bagasse char.

Close modal
The surface area of bagasse char at 900 °C obtained was 514.27 m2/g with a total pore volume of 0.4090 cc/g. This confirms that charrification of raw material can improve porousness and thereby surface area. The linear isotherm of adsorption-desorption of nitrogen for bagasse char is shown in Figure 16.
Figure 16

Linear isotherm of char.

Figure 16

Linear isotherm of char.

Close modal
The surface area of zinc chloride-activated SB was found to be 1,386.58 m2/g with a total pore volume of 0.9947 cc/g. The comparative table of surface areas of raw bagasse, its char and activated carbon is shown in Table 4. The linear isotherm of adsorption–desorption of nitrogen for activated carbon is shown in Figure 17.
Table 4

BET surface area, pore volume and size

SampleBET surface area (m2/g)Vtot (cm3/g)Avg. pore size (A°)
Raw SB 0.00 0.4771 – 
SB Char 514.270 0.4090 15.907 
SB-Zn2-900a 1,386.58 0.9947 15.507 
SampleBET surface area (m2/g)Vtot (cm3/g)Avg. pore size (A°)
Raw SB 0.00 0.4771 – 
SB Char 514.270 0.4090 15.907 
SB-Zn2-900a 1,386.58 0.9947 15.507 

aBold indicates that activated carbon has the highest surface area, pore volume and pore size compared with raw material and its char.

Figure 17

Linear isotherm of SB-Zn2-900.

Figure 17

Linear isotherm of SB-Zn2-900.

Close modal

Energy-dispersive spectroscopy analysis of raw bagasse, char and activated carbon

EDS is an analytical technique used for the elemental analysis or chemical characterization of a sample. It was determined with SEM by the JEOL-6380A instrument available at VNIT, Nagpur.

The EDS analysis of raw bagasse, char and activated carbon is shown in Table 5. It was revealed from the EDS studies that raw bagasse contains 56.25% C, 42.22% O, 0.79% Pt, 0.42% Si and 0.33% Al. SB after carbonization contains 81.87% C, 16.72% O, 0.44% Pt, 0.53% Si and 0.45% Ca. Activated carbon produced after chemical activation with zinc chloride contains 74.50% C, 12.27% O, 0.22% Pt, 0.04% Si, 12.17% N, 0.52% Cl and 0.20% Zn. These results revealed that after carbonization the char and activated carbon met the requirement of 65% C as per SNI No. 06-3730-1995 (Guo & Lua 2000; Adlim et al. 2021).

Table 5

Elemental analysis

Sample name% C% O% Pt% Si% Al% Ca% N% Cl%Zn
Raw bagasse 56.25 42.22 0.79 0.42 0.33 – – – – 
Bagasse char 81.87 16.72 0.44 0.53 – 0.45 – – – 
SB-Zn2-900 74.50 12.27 0.22 0.04 – – 12.17 0.52 0.20 
Sample name% C% O% Pt% Si% Al% Ca% N% Cl%Zn
Raw bagasse 56.25 42.22 0.79 0.42 0.33 – – – – 
Bagasse char 81.87 16.72 0.44 0.53 – 0.45 – – – 
SB-Zn2-900 74.50 12.27 0.22 0.04 – – 12.17 0.52 0.20 

The comparative study of raw material, activating agent used, condition of activation, CHN analysis, iodine number and BET surface area with previous research studies is shown in Table 6.

Table 6

Comparative study with the previous research

Raw materialActivating agentOptimum impregnation ratio/temperature (°C)% C% H% NIodine no. (mg/g)BET surface area (m2/g)Reference
Safflower seed press cake ZnCl2 4:1/900 76.29 2.26 2.48 128.21 801.5 Lua & Ting (2004)  
Sugarcane bagasse ZnCl2 1:1/400 – – – 868 – Joshi & Vishnu (2020)  
Sugarcane bagasse ZnCl2 5:1/500 – – – – 905 Tsai et al. (2001)  
Sugarcane bagasse ZnCl2 2:1/900    277.78 1,302.4 Nemr et al. (2021)  
Sugarcane bagasse ZnCl2 2:1/600    239.6 831 Cai et al. (2019)  
Mangrove waste H3PO4 4:1/300 94.18 2.83 – 72.3 1,011.8 Zakaria et al. (2021)  
Rice husk H3PO4 500 – – – – 420 Njewa et al. (2022)  
Marula nutshell H3PO4 500 – – – 1,075.7 – Mkungunugwa et al. (2021)  
Kenaf core fiber H3PO4 1:4/500 – – – – 299.02 Shamsuddin et al. (2016)  
Mangrove charcoal H3PO4 725 – – – 1,019.87 354.97 Budianto et al. (2019)  
Olive stone H3PO4 500 – – – – 1,218 Yakout & El-Deen (2012)  
Palm kernel shell KOH 1.5:1/800 61.10 1.40 0.00 994.83 – Andas et al. (2017)  
Bamboo stem KOH 3:1/800 79.11 1.60 0.10 – 726 Khalil et al. (2013)  
Sugarcane bagasse ZnCl2 2:1/900 80.126 3.569 1.873 1,140.69 1,386.58 This study 
Raw materialActivating agentOptimum impregnation ratio/temperature (°C)% C% H% NIodine no. (mg/g)BET surface area (m2/g)Reference
Safflower seed press cake ZnCl2 4:1/900 76.29 2.26 2.48 128.21 801.5 Lua & Ting (2004)  
Sugarcane bagasse ZnCl2 1:1/400 – – – 868 – Joshi & Vishnu (2020)  
Sugarcane bagasse ZnCl2 5:1/500 – – – – 905 Tsai et al. (2001)  
Sugarcane bagasse ZnCl2 2:1/900    277.78 1,302.4 Nemr et al. (2021)  
Sugarcane bagasse ZnCl2 2:1/600    239.6 831 Cai et al. (2019)  
Mangrove waste H3PO4 4:1/300 94.18 2.83 – 72.3 1,011.8 Zakaria et al. (2021)  
Rice husk H3PO4 500 – – – – 420 Njewa et al. (2022)  
Marula nutshell H3PO4 500 – – – 1,075.7 – Mkungunugwa et al. (2021)  
Kenaf core fiber H3PO4 1:4/500 – – – – 299.02 Shamsuddin et al. (2016)  
Mangrove charcoal H3PO4 725 – – – 1,019.87 354.97 Budianto et al. (2019)  
Olive stone H3PO4 500 – – – – 1,218 Yakout & El-Deen (2012)  
Palm kernel shell KOH 1.5:1/800 61.10 1.40 0.00 994.83 – Andas et al. (2017)  
Bamboo stem KOH 3:1/800 79.11 1.60 0.10 – 726 Khalil et al. (2013)  
Sugarcane bagasse ZnCl2 2:1/900 80.126 3.569 1.873 1,140.69 1,386.58 This study 

This study investigated the preparation of activated carbon from naturally available bio-waste material SB. In this study, the characterization results of CHN analysis, FTIR, XRD, BET surface area and SEM analysis of raw bagasse, bagasse char and zinc chloride-impregnated activated carbon were compared. From the results, it was observed that more activation temperature gives lesser yield of the product. It means product yield is inversely proportional to the activation temperature. The iodine number gives an indication about the porousness of activated carbon. Higher iodine numbers mean highly porous carbon. The iodine numbers of SB-Zn2-900 and char at 900 °C were found to be 1,140.69 and 510.75 mg/g, respectively. The CHN analysis data reveal that activation of raw material can transform into activated carbon with carbon % of 42.049, 48.150 and 80.126 for raw bagasse, its char and activated carbon. The FTIR study investigated that raw bagasse and char shows very less functional groups. The appearance of functional groups occurred by chemical activation at various temperatures. The activated carbon was found to contain aliphatic, aromatic and oxygen-containing functional groups. From SEM micrographs, it is concluded that there are very less pores in raw bagasse, some pores were seen in char and a large number of pores were observed in SB-Zn2-900. It means activation with the chemical agent can impart porousness in the carbon. The BET surface area of SB-Zn2-900, char and raw bagasse was found to be 1,386.58, 514.270 and 0 m2/g, respectively, which shows raw bagasse does not exhibit adsorption properties. On the other hand, char has less and activated carbon has a larger adsorption capacity. The optimum ratio of impregnation and activation temperature was found to be 1:2 at 900°. Elemental analysis was also carried out by EDS and showed that char contains 81.87% C whereas activated carbon contains 74.50% C. However, SB can produce good surface area carbon that can be utilized for further adsorption studies.

All the data are available in the manuscript

E.R.R. carried out the collection of biomaterials, synthesis, characterization and preparation of manuscript. M. A. B. and A. R. C. carried out the concept and guidance of research work.

All relevant data are included in the paper or its Supplementary Information.

The authors declare there is no conflict.

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