# Synthesis and Characterization of Activated Carbons Prepared from Agro-Wastes by Chemical Activation

Authors: Joel Brian Njewa; Ephraim Vunain; Timothy Biswick
Journal: Journal of Chemistry
 (2022)

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## Abstract

In this present study, activated carbons were prepared from rice husks and potato peels by chemical activation with 40% phosphoric acid (H3PO4). The effects of carbonization temperature and impregnation ratio were investigated with a continuous activation period. Physicochemical characteristics such as surface morphology, surface charge, and surface functional groups were assessed. According to X-ray diffraction measurements, the results showed that the activated carbons had identical pHpzc (6.8) and that the activated carbons generated were carbonaceous. The existence of hydroxyl, carbonyl, amines, aromatic, and other functional groups, which are excellent for adsorption, was revealed by surface chemistry studies. Micrographs taken with a scanning electron microscope indicated wide opening pores with a larger mesoporous surface area and many linked pores. Rice husk activated carbon outperformed potato peel activated carbon in laboratory tests. The research has shown that the agro-wastes employed in the study are possible precursors for making locally activated carbons at a low cost, thus resolving the problem of agro-waste disposal.


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## Body

## 1. Introduction

Activated carbon AC, also commonly termed activated charcoal, has been defined differently by several authors as reported in the literature [1]. It is defined as a class of porous carbonaceous materials that can never be characterized by a structural formula or chemical analysis [2]. Further, AC can also be defined as a tasteless, solid, microcrystalline, nongraphitic form of black carbonaceous material with a very porous structure [3, 4]. Furthermore, other investigators state that AC refers to a porous material derived from a feedstock containing carbon with millions of tiny pores between the carbon atoms that have been opened due to the activation process [5]. Therefore, in summary, AC refers to a class of black carbonaceous porous materials with a large surface area prepared through the carbonization of any material rich with elemental carbon.Activated carbon is a versatile adsorbent due to its good adsorption characteristics. The adsorption characteristics of activated carbon depend on the precursor type, size of the particles, and method adopted during preparation [6, 7]. The adsorbing quality of the resulting activated carbon is also influenced by the activating reagents, activation time, impregnation ratio, carbonization temperature, and the presence of inorganic impurities, among others [1]. The preparation of AC can be accomplished in two processes: physical and chemical. Physical activation involves carbonization of the precursor followed by the activation using different gases. At first, the material is carbonized at an elevated temperature of around 500–900°C without air. Then, the activation step, also termed oxidation, occurs when the material is exposed to an oxidizing environment, carbon dioxide, oxygen, or steam, at high temperatures ranging from 800 to 1000°C. Carbonization is purposely carried out to eliminate noncarbon elements from the raw materials, while the activation stage ensures that the desired porosity of the material is attained successfully [5].Chemical activation, also known as the single-step method for the preparation of AC, occurs in the presence of activating chemical agents. Chemical activation has several advantages; first, it usually requires low activation temperature and shorter times for activation of the materials; second, it can promote pore development in the carbon structure due to the effect of the chemicals. Generally, the carbon yields obtained by chemical activation are higher than those by physical activation. However, after thermal treatment, it needs a thorough process that recovers the chemical agents. This result might limit its usage due to environmental issues [8].In general, activated carbon is prepared from materials rich in element carbon [9]. Two critical sources for activated carbon preparations are coal and agricultural wastes or biomass rich in lignocellulosic materials. The precursors used to prepare commercial activated carbons are highly costly and nonrenewable such as petroleum residues, lignite, wood, coal, and peat [1]. On the other hand, low-cost activated carbon is reported to have been successfully prepared from agricultural byproducts, for instance, Marula nutshell [10], grains, corn cobs, almond shells [11], and bamboo [10, 11].Malawi is an agro-based developing country that generates large volumes of postharvest wastes every year through intensive farming. The wastes produced create a disposal challenge, contrary to developed countries where the agro-wastes become raw materials for various purposes in industrial applications. In Malawi, the tale is different; the wastes are dumped and burned in an open field resulting in the generation of greenhouse gases like carbon dioxide gases (CO2) that cause air pollution. In some urban and rural areas, the wastes are dumped in water sources, causing water pollution, and if the wastes are disposed of on land, it releases methane (CH4) gases due to the decomposition of organic matter, causing air and land pollution altogether. The practice used in the management of agro-waste results in environmental issues, and sometimes, the wastes act as vectors for disease-causing organisms, thereby threatening the public’s health.Various published articles mentioned agro-wastes such as rice husks and potato peels as raw materials for synthesizing low-cost activated carbons [12–15, 16]. However, most of these published papers have used sweet potato peels rather than Irish potato peels as precursors for synthesis of activated carbon and there is currently no published study that reports the fixed carbon content of the raw materials used to our knowledge. Furthermore, rice husks are known to be rich sources of silicates. In this current study, before rice husks were used in the preparation of activated carbon sodium silicate, an essential ingredient with wide industrial application in the manufacturing process was extracted.In prior research, we showed that agro-wastes such as rice husks,Jatropha curcas, and cassava peels might be utilized to clarify wastewater and successfully eliminate turbidity and microbiological load from sewage wastewater collected at the Chikanda Wastewater Treatment Plant in Zomba city [17]. As a result, this effort focuses on increasing the value of diverse solid agro-wastes produced in Malawi.Therefore, in this study, agro-wastes from Irish potato peels and rice husks after successful extraction of sodium silicate from rice husks were selected and used to prepare activated carbon by chemical activation as a way of sustainable waste management. Using these agro-wastes as AC precursors has substantial economic and environmental impacts as converting undesirable agricultural waste to high-value adsorbents. Furthermore, using agro-waste residues as precursors for AC synthesis will also assist in our country’s economic growth as it will reduce the importation of activated carbon from international markets.


## 2. Materials and Methods

### 2.1. Materials and Reagents

To synthesize activated carbon, H3PO4, NaOH, KI, and NaSiO4 were obtained from UNICHEM Reagent Co., while KNO3 was obtained from LabChem, whereas HCl and HNO3 were sourced from DAEJUNG Co. and gasoline was purchased from the Total filling station. All reagents used were of analytical grade. Required solutions were made by dissolving the corresponding reagent in double-distilled water.


### 2.2. Preparation of Activated Carbons

Activated carbons were prepared through a chemical activation process according to the procedure by [18]. 100 g of rice husk fine powder was first soaked in 200 mL of 3 Mol·L−1 sodium hydroxide (NaOH) and left in an oven at a temperature of 105°C for 5 h. NaOH reacted with silica in rice husk powder producing soluble sodium silicate (Na2SiO3). After that, the raw materials treated as solid base residues were washed with deionized water several times until the supernatant pH was neutral (pH=7), oven dried at 110°C for 24 h, and used in the synthesis of activated carbon.10 g of the dried solid residues and Irish potato peel powders were impregnated with 40% orthophosphoric acid (H3PO4) ratios (1 : 1, 1 : 1.7, 1 : 2.5, and 1 : 3). The impregnated residues were left in an oven at 100°C for 12 h to reduce surplus water, and the dried samples were used for activation heated from room temperature. The samples were activated at different activation temperatures (400, 500, 600, and 700°C) with a constant activation time of 1.5 h. The samples were then cooled in desiccators and sequentially washed with 0.1 M NaOH, warm water, and finally cold water using the Buchner funnel until neutral pH was attained and then oven dried at a temperature of 105°C for 3 h. Finally, the samples were grounded, sieved with mesh 250 μm, and stored in labeled plastic bottles waiting for characterization.


### 2.3. Characterization of Activated Carbon

#### 2.3.1. Determination of Activated Carbon Yield

The weight of the precursors and activated carbons produced was measured using Mettler electronic balance. The carbon yield of each sample prepared was determined according to the procedure [19]. The carbon yield was calculated as
(1)Y=WfW0×100,where Y is the carbon yield, Wf is the final weight of activated carbon recorded at the end of carbonization, and W0 is the initial weight of the impregnated precursors.


#### 2.3.2. Determination of the Ash Content

The ash content percentage was carried out [20] by a silica crucible preheated in the furnace at 900°C for 1 h. Then, it was cooled in a desiccator and reweighed. Next, 1 g of the AC sample was placed in a crucible covered with the lid and heated at 900°C for 1 h. The crucible and its content were then cooled in the desiccator and reweighed. The weight of the incombustible residues accounts for the ash content in the activated carbon samples. The ash content percentage was calculated using the equation given below:
(2)Ashcontent%=C−DC−B×100,where B is the weight of the crucible, g, C is the weight of the crucible with the sample, g, and D is the weight of the crucible after weight loss g.


#### 2.3.3. Determination of Volatile Matter

The volatile matter in activated carbon samples was determined [20]. Thus, a silica crucible was preheated at a temperature of 900°C in a muffle furnace for 10 min. After that, samples were cooled in a desiccator. Next, 1 g of the activated carbon sample was placed in preheated silica crucible covered with the lid and placed in a muffle furnace and heated at the temperature of 900°C for 10 min. Finally, the crucible and contents were removed and cooled in a desiccator. The weight loss accounts for the volatile matter. The volatile matter was calculated as percentage using the equation as follows:
(3)Volatilematter%=100B−F−MB−GB−G100−M×100,where B is the mass of the crucible and sample before heating, g; F is the mass of the crucible with AC sample after heating, g; G is the mass of the crucible with lid; and M is the moisture content of the activated carbon samples determined above.


#### 2.3.4. Determination of the Moisture Content

The moisture content of the activated carbon samples was calculated according to [21], with some alterations in which 1 g of the activated carbon sample was weighed and placed in a porcelain cup. It was then oven heated at a temperature of 110°C for 3 h, cooled in a desiccator for 30 min, and reweighed. The weight change was measured as moisture lost and calculated as follows:
(4)MC=B−CB−D×100,where MC is the moisture content, B is the weight of the porcelain plus the activated carbon sample, C is the weight of the porcelain plus the dried activated carbon sample, and D is the mass of empty porcelain.


#### 2.3.5. Determination of the Fixed Carbon Content

The fixed carbon content in activated carbon samples was calculated as [22]. The equation which was involved in fixed carbon content calculation is given as
(5)FCC=100–%M+%A+%VM,where FCC is the fixed carbon content, %M is the percentage of moisture contained in the activated carbon sample, %A: is the percentage of ash contained in the activated carbon sample, and %VM: is the percentage of volatile matter in the activated carbon sample.


#### 2.3.6. Determination of the Iodine Number

All working solutions were prepared according to the American Society of Testing and Measurement [23]. Iodine number calculations followed the procedure described by [20].
(6)Iodinenumbermgg=B−SB×VMW×253.81,where B and S are the volumes of the thiosulfate solution required for blank and sample titrations, respectively; W is the weight of the activated carbon sample; M is the concentration (Mol) of iodine solute, 253.81 g/Mol = molar weight iodine; and V is the volume (mL) of aliquot.


#### 2.3.7. Determination of Ammonia and Gasoline Adsorption

In gas-phase applications, activated carbon samples were evaluated in gasoline and ammonia (25% NH3) adsorption. The procedure used was similar for both gasoline and ammonia adsorption. Thus, 0.5 g of AC samples was weighed using Mettler electronic balance and transferred into crucibles whose initial mass was recorded previously. Then, the samples were then taken into desiccators and sealed together with either ammonia or gasoline. The samples were left for 24 h in desiccators for adsorption to occur. After 24 h, AC samples were also reweighed and the change in mass was assumed due to the gas absorbed by the samples. Finally, the adsorption percentage was calculated using the equation reported previously by [5].
(7)Adsorption%=∆mMb×100,where ∆m is the change in mass of activated carbon after gas adsorption and Mb is the mass of activated carbon before gas adsorption.


#### 2.3.8. Adsorbent Characterization

The surface charge of the adsorbents was determined by pH titration [24–26]. The 50 mL volume of 0.01 M KNO3 was sealed in a volumetric flask containing 50 mg of the adsorbents under different pH conditions. The pH of the solutions was adjusted by drop-wise addition of 0.1 M NaOH or 0.1 M HCl solutions until the desired pH was achieved. The suspensions of activated carbons in the flasks were then agitated for 48 h. The plot between initial pH versus the change in pH was plotted, and the point of intersection was considered the point of charge. Surface chemistry was determined using FT-IR Spectroscopy (NICOLET iS 10, 2007, USA). The ratio of 1 : 10 mg thus KBr to adsorbent was adopted. The samples were analyzed, and the spectra were recorded in the range 4000 to 400 cm−1. The crystallinity analysis was carried out by Siemens X-ray diffractometer (model no: 10190376, Germany). The scan runs were performed at a diffraction angle of (2θ) with a variation ranging between 10° and 90°. The surface morphology of the adsorbents was carried out by FESEM (JEOL JSM-7100F, Japan).


## 2.1. Materials and Reagents

To synthesize activated carbon, H3PO4, NaOH, KI, and NaSiO4 were obtained from UNICHEM Reagent Co., while KNO3 was obtained from LabChem, whereas HCl and HNO3 were sourced from DAEJUNG Co. and gasoline was purchased from the Total filling station. All reagents used were of analytical grade. Required solutions were made by dissolving the corresponding reagent in double-distilled water.


## 2.2. Preparation of Activated Carbons

Activated carbons were prepared through a chemical activation process according to the procedure by [18]. 100 g of rice husk fine powder was first soaked in 200 mL of 3 Mol·L−1 sodium hydroxide (NaOH) and left in an oven at a temperature of 105°C for 5 h. NaOH reacted with silica in rice husk powder producing soluble sodium silicate (Na2SiO3). After that, the raw materials treated as solid base residues were washed with deionized water several times until the supernatant pH was neutral (pH=7), oven dried at 110°C for 24 h, and used in the synthesis of activated carbon.10 g of the dried solid residues and Irish potato peel powders were impregnated with 40% orthophosphoric acid (H3PO4) ratios (1 : 1, 1 : 1.7, 1 : 2.5, and 1 : 3). The impregnated residues were left in an oven at 100°C for 12 h to reduce surplus water, and the dried samples were used for activation heated from room temperature. The samples were activated at different activation temperatures (400, 500, 600, and 700°C) with a constant activation time of 1.5 h. The samples were then cooled in desiccators and sequentially washed with 0.1 M NaOH, warm water, and finally cold water using the Buchner funnel until neutral pH was attained and then oven dried at a temperature of 105°C for 3 h. Finally, the samples were grounded, sieved with mesh 250 μm, and stored in labeled plastic bottles waiting for characterization.


## 2.3. Characterization of Activated Carbon

### 2.3.1. Determination of Activated Carbon Yield

The weight of the precursors and activated carbons produced was measured using Mettler electronic balance. The carbon yield of each sample prepared was determined according to the procedure [19]. The carbon yield was calculated as
(1)Y=WfW0×100,where Y is the carbon yield, Wf is the final weight of activated carbon recorded at the end of carbonization, and W0 is the initial weight of the impregnated precursors.


### 2.3.2. Determination of the Ash Content

The ash content percentage was carried out [20] by a silica crucible preheated in the furnace at 900°C for 1 h. Then, it was cooled in a desiccator and reweighed. Next, 1 g of the AC sample was placed in a crucible covered with the lid and heated at 900°C for 1 h. The crucible and its content were then cooled in the desiccator and reweighed. The weight of the incombustible residues accounts for the ash content in the activated carbon samples. The ash content percentage was calculated using the equation given below:
(2)Ashcontent%=C−DC−B×100,where B is the weight of the crucible, g, C is the weight of the crucible with the sample, g, and D is the weight of the crucible after weight loss g.


### 2.3.3. Determination of Volatile Matter

The volatile matter in activated carbon samples was determined [20]. Thus, a silica crucible was preheated at a temperature of 900°C in a muffle furnace for 10 min. After that, samples were cooled in a desiccator. Next, 1 g of the activated carbon sample was placed in preheated silica crucible covered with the lid and placed in a muffle furnace and heated at the temperature of 900°C for 10 min. Finally, the crucible and contents were removed and cooled in a desiccator. The weight loss accounts for the volatile matter. The volatile matter was calculated as percentage using the equation as follows:
(3)Volatilematter%=100B−F−MB−GB−G100−M×100,where B is the mass of the crucible and sample before heating, g; F is the mass of the crucible with AC sample after heating, g; G is the mass of the crucible with lid; and M is the moisture content of the activated carbon samples determined above.


### 2.3.4. Determination of the Moisture Content

The moisture content of the activated carbon samples was calculated according to [21], with some alterations in which 1 g of the activated carbon sample was weighed and placed in a porcelain cup. It was then oven heated at a temperature of 110°C for 3 h, cooled in a desiccator for 30 min, and reweighed. The weight change was measured as moisture lost and calculated as follows:
(4)MC=B−CB−D×100,where MC is the moisture content, B is the weight of the porcelain plus the activated carbon sample, C is the weight of the porcelain plus the dried activated carbon sample, and D is the mass of empty porcelain.


### 2.3.5. Determination of the Fixed Carbon Content

The fixed carbon content in activated carbon samples was calculated as [22]. The equation which was involved in fixed carbon content calculation is given as
(5)FCC=100–%M+%A+%VM,where FCC is the fixed carbon content, %M is the percentage of moisture contained in the activated carbon sample, %A: is the percentage of ash contained in the activated carbon sample, and %VM: is the percentage of volatile matter in the activated carbon sample.


### 2.3.6. Determination of the Iodine Number

All working solutions were prepared according to the American Society of Testing and Measurement [23]. Iodine number calculations followed the procedure described by [20].
(6)Iodinenumbermgg=B−SB×VMW×253.81,where B and S are the volumes of the thiosulfate solution required for blank and sample titrations, respectively; W is the weight of the activated carbon sample; M is the concentration (Mol) of iodine solute, 253.81 g/Mol = molar weight iodine; and V is the volume (mL) of aliquot.


### 2.3.7. Determination of Ammonia and Gasoline Adsorption

In gas-phase applications, activated carbon samples were evaluated in gasoline and ammonia (25% NH3) adsorption. The procedure used was similar for both gasoline and ammonia adsorption. Thus, 0.5 g of AC samples was weighed using Mettler electronic balance and transferred into crucibles whose initial mass was recorded previously. Then, the samples were then taken into desiccators and sealed together with either ammonia or gasoline. The samples were left for 24 h in desiccators for adsorption to occur. After 24 h, AC samples were also reweighed and the change in mass was assumed due to the gas absorbed by the samples. Finally, the adsorption percentage was calculated using the equation reported previously by [5].
(7)Adsorption%=∆mMb×100,where ∆m is the change in mass of activated carbon after gas adsorption and Mb is the mass of activated carbon before gas adsorption.


### 2.3.8. Adsorbent Characterization

The surface charge of the adsorbents was determined by pH titration [24–26]. The 50 mL volume of 0.01 M KNO3 was sealed in a volumetric flask containing 50 mg of the adsorbents under different pH conditions. The pH of the solutions was adjusted by drop-wise addition of 0.1 M NaOH or 0.1 M HCl solutions until the desired pH was achieved. The suspensions of activated carbons in the flasks were then agitated for 48 h. The plot between initial pH versus the change in pH was plotted, and the point of intersection was considered the point of charge. Surface chemistry was determined using FT-IR Spectroscopy (NICOLET iS 10, 2007, USA). The ratio of 1 : 10 mg thus KBr to adsorbent was adopted. The samples were analyzed, and the spectra were recorded in the range 4000 to 400 cm−1. The crystallinity analysis was carried out by Siemens X-ray diffractometer (model no: 10190376, Germany). The scan runs were performed at a diffraction angle of (2θ) with a variation ranging between 10° and 90°. The surface morphology of the adsorbents was carried out by FESEM (JEOL JSM-7100F, Japan).


## 2.3.1. Determination of Activated Carbon Yield

The weight of the precursors and activated carbons produced was measured using Mettler electronic balance. The carbon yield of each sample prepared was determined according to the procedure [19]. The carbon yield was calculated as
(1)Y=WfW0×100,where Y is the carbon yield, Wf is the final weight of activated carbon recorded at the end of carbonization, and W0 is the initial weight of the impregnated precursors.


## 2.3.2. Determination of the Ash Content

The ash content percentage was carried out [20] by a silica crucible preheated in the furnace at 900°C for 1 h. Then, it was cooled in a desiccator and reweighed. Next, 1 g of the AC sample was placed in a crucible covered with the lid and heated at 900°C for 1 h. The crucible and its content were then cooled in the desiccator and reweighed. The weight of the incombustible residues accounts for the ash content in the activated carbon samples. The ash content percentage was calculated using the equation given below:
(2)Ashcontent%=C−DC−B×100,where B is the weight of the crucible, g, C is the weight of the crucible with the sample, g, and D is the weight of the crucible after weight loss g.


## 2.3.3. Determination of Volatile Matter

The volatile matter in activated carbon samples was determined [20]. Thus, a silica crucible was preheated at a temperature of 900°C in a muffle furnace for 10 min. After that, samples were cooled in a desiccator. Next, 1 g of the activated carbon sample was placed in preheated silica crucible covered with the lid and placed in a muffle furnace and heated at the temperature of 900°C for 10 min. Finally, the crucible and contents were removed and cooled in a desiccator. The weight loss accounts for the volatile matter. The volatile matter was calculated as percentage using the equation as follows:
(3)Volatilematter%=100B−F−MB−GB−G100−M×100,where B is the mass of the crucible and sample before heating, g; F is the mass of the crucible with AC sample after heating, g; G is the mass of the crucible with lid; and M is the moisture content of the activated carbon samples determined above.


## 2.3.4. Determination of the Moisture Content

The moisture content of the activated carbon samples was calculated according to [21], with some alterations in which 1 g of the activated carbon sample was weighed and placed in a porcelain cup. It was then oven heated at a temperature of 110°C for 3 h, cooled in a desiccator for 30 min, and reweighed. The weight change was measured as moisture lost and calculated as follows:
(4)MC=B−CB−D×100,where MC is the moisture content, B is the weight of the porcelain plus the activated carbon sample, C is the weight of the porcelain plus the dried activated carbon sample, and D is the mass of empty porcelain.


## 2.3.5. Determination of the Fixed Carbon Content

The fixed carbon content in activated carbon samples was calculated as [22]. The equation which was involved in fixed carbon content calculation is given as
(5)FCC=100–%M+%A+%VM,where FCC is the fixed carbon content, %M is the percentage of moisture contained in the activated carbon sample, %A: is the percentage of ash contained in the activated carbon sample, and %VM: is the percentage of volatile matter in the activated carbon sample.


## 2.3.6. Determination of the Iodine Number

All working solutions were prepared according to the American Society of Testing and Measurement [23]. Iodine number calculations followed the procedure described by [20].
(6)Iodinenumbermgg=B−SB×VMW×253.81,where B and S are the volumes of the thiosulfate solution required for blank and sample titrations, respectively; W is the weight of the activated carbon sample; M is the concentration (Mol) of iodine solute, 253.81 g/Mol = molar weight iodine; and V is the volume (mL) of aliquot.


## 2.3.7. Determination of Ammonia and Gasoline Adsorption

In gas-phase applications, activated carbon samples were evaluated in gasoline and ammonia (25% NH3) adsorption. The procedure used was similar for both gasoline and ammonia adsorption. Thus, 0.5 g of AC samples was weighed using Mettler electronic balance and transferred into crucibles whose initial mass was recorded previously. Then, the samples were then taken into desiccators and sealed together with either ammonia or gasoline. The samples were left for 24 h in desiccators for adsorption to occur. After 24 h, AC samples were also reweighed and the change in mass was assumed due to the gas absorbed by the samples. Finally, the adsorption percentage was calculated using the equation reported previously by [5].
(7)Adsorption%=∆mMb×100,where ∆m is the change in mass of activated carbon after gas adsorption and Mb is the mass of activated carbon before gas adsorption.


## 2.3.8. Adsorbent Characterization

The surface charge of the adsorbents was determined by pH titration [24–26]. The 50 mL volume of 0.01 M KNO3 was sealed in a volumetric flask containing 50 mg of the adsorbents under different pH conditions. The pH of the solutions was adjusted by drop-wise addition of 0.1 M NaOH or 0.1 M HCl solutions until the desired pH was achieved. The suspensions of activated carbons in the flasks were then agitated for 48 h. The plot between initial pH versus the change in pH was plotted, and the point of intersection was considered the point of charge. Surface chemistry was determined using FT-IR Spectroscopy (NICOLET iS 10, 2007, USA). The ratio of 1 : 10 mg thus KBr to adsorbent was adopted. The samples were analyzed, and the spectra were recorded in the range 4000 to 400 cm−1. The crystallinity analysis was carried out by Siemens X-ray diffractometer (model no: 10190376, Germany). The scan runs were performed at a diffraction angle of (2θ) with a variation ranging between 10° and 90°. The surface morphology of the adsorbents was carried out by FESEM (JEOL JSM-7100F, Japan).


## 3. Results and Discussions

### 3.1. Physicochemical Properties

#### 3.1.1. Carbon Yield

The carbon yield results for the prepared RH-AC and PP-AC show that as activation temperature increases from 400°C to 700°C at impregnation ratios 1 : 1 to 1 : 3; the percentage of carbon yield decreases as presented in Figure1. The results showed that increasing carbonization temperature decreases the percentage of AC yield. This result is likely associated with promoting carbon burn-off and volatilization of tar at elevated temperatures. Again, the decrease in carbon yield could be attributed to the increasing impregnation ratio, which promotes the release of volatiles from the sample resulting in the decrease in carbon yield. The lower carbon yield with a higher impregnation ratio might be due to the enhancement of carbon burn-off by excess activating agents [27, 28]. A similar pattern of results was reported in the literature by investigators who worked on deriving activated carbon from agro-wastes [29]. Higher carbon yield on prepared carbons was attained in PP-AC samples than RH-AC.Figure 1
The effect of the impregnation ratio and carbonization temperature on carbon yield.


#### 3.1.2. Moisture Content

The moisture content in prepared activated carbon was determined to ascertain its suitability in adsorption studies. The results indicate an increase in impregnation ratios from 1 : 1 to 1 : 3 and carbonization temperature from 400°C to 700°C for both RH-AC and PP-AC; the moisture content of the derived activated carbon samples reduced as shown in Table1. It was observed that as the activation temperature increased, the moisture content in activated carbon samples decreased. This result might be connected to removing volatile matter, thereby reducing carbon yield and concurrently reducing the moisture content in the prepared RH-AC and PP-AC samples. The samples with a similar impregnation ratio but different activation temperatures had minimal moisture content. The activated carbon derived from potato peels had high moisture content instead of activated carbon obtained from rice husks. The comparison of prepared activated carbons with commercial activated carbon was made, and the results displayed by RH-AC were similar to that of commercial activated charcoal (4%).Table 1
The effect of the impregnation ratio and activation temperature on moisture content.
Activation temperature (°C)Impregnation400500600700RatioRH-ACPP-ACRH-ACPP-ACRH-ACPP-ACRH-ACPP-AC1 : 13.65±0.256.80±0.24.9±0.356.2±0.404.4±0.355.9±0.254.4±0.035.4±0.31 : 1.73.45±0.155.40±0.14.5±0.155.7±0.153.7±0.375.6±0.154.2±0.154.95±0.151 : 2.53.15±0.254.88±0.324.4±0.305.0±0.204.2±0.35.2±0.24.1±0.14.35±0.251 : 32.95±0.153.16±0.344.1±0.184.4±0.243.6±0.25.1±0.24.05±0.24.3±0.2


#### 3.1.3. Ash Content

The ash content findings are presented in Figure2. The results showed that increasing impregnation ratios from 1 : 1 to 1 : 3 and carbonization temperature from 400 to 700°C for both RH-AC and PP-AC increased the ash content for both the prepared RH-AC and PP-AC samples. It was noted that increasing the activation temperature increased the ash content in activated carbon samples. The increase in ash content might be associated with a high degree of biomass burn-off at elevated temperatures. Comparing the ash content with commercial activated carbon, the ash content in all prepared activated charcoal samples exceeded the recommended range of 2–10 (%) but activated carbon prepared from rice husks had less ash content. This result implies that the activated carbons synthesized were not of high purity. However, different investigators reported similar results in the literature on activated carbons from agro-wastes [30].Figure 2
The effect of the impregnation ratio and activation temperature on the ash content.


#### 3.1.4. Volatile Matter

While the impregnation ratio increases from 1 : 1 to 1 : 3 with activation temperature from 400°C to 700°C, volatile matter decreases for RH-AC and PP-AC (Table2). The results indicated that increasing carbonization temperature caused a decrease in the volatile matter content in both RH-AC and PP-AC. The reduction in the volatile matter percentage as activation temperature increases is connected to the fact that more volatile matter is released at an elevated temperature, lowering its content in activated carbon samples. The study has recognized high-volatile matter content in activated carbon samples prepared from Irish potato peels compared with rice husks. Volatile matter in commercial activated carbon was noted at 30% compared to prepared activated carbon samples within the required range.Table 2
The volatile matter in the prepared activated carbon samples.
Activation temperature (°C)Impregnation400500600700RatioRH-ACPP-ACRH-ACPP-ACRH-ACPP-ACRH-ACPP-AC1 : 114.05±0.1716.22±0.2412.79±0.3315.02±0.0412.34±0.1314.39±0.0712.89±0.0212.38±0.151 : 1.715.33±0.1116.37±0.6213.09±0.3215.07±0.0913.34±0.3614.88±0.1113.28±0.3112.48±0.261 : 2.517.61±0.1818.12±0.3514.35±0.1416.52±0.1814.43±0.2515.51±0.1714.09±0.3214.01±0.121 : 318.01±0.1318.66±0.1915.39±0.1716.76±0.1314.58±0.3215.61±0.1514.58±0.2014.51±0.17


#### 3.1.5. Fixed Carbon Content

The carbon content in prepared activated carbon samples was calculated. At given impregnation ratios 1 : 1 to 1 : 3 and increasing carbonization temperature from 400°C to 700°C, the carbon content for the prepared activated carbon samples decreased as displayed in Table3. The fixed carbon content results depend on volatile matter, ash, and moisture content. The results indicated that an increase in carbonization temperatures promotes the release of volatile matter and increases the ash content while at the same time decreasing the moisture content. The activated carbons prepared at 400°C were within the recommended range of commercial activated carbon, whereas in commercial activated carbon, the carbon content ranges 50–95%. The activated carbon derived from rice husks had carbon content within the commercial activated charcoal.Table 3
The fixed carbon content of the prepared activated carbons.
Activation temperature (°C)Impregnation400500600700RatioRH-ACPP-ACRH-ACPP-ACRH-ACPP-ACRH-ACPP-AC1 : 157.48±0.6949.88±0.2155.88±0.3549.39±0.2954.49±0.3949.88±0.3953.27±0.3150.79±0.251 : 1.756.21±0.3248.16±0.2755.46±0.7949.28±0.1251.96±0.6347.99±0.4250.88±0.2249.78±0.351 : 2.552.07±0.1846.68±0.0152.97±0.5245.58±0.2250.99±0.2547.90±0.1344.78±0.5648.10±0.421 : 351.4±0.5144.47±0.5051.33±0.5646.45±1.3147.08±0.2047.08±0.2044.76±0.2047.68±0.46


#### 3.1.6. Iodine Number

The iodine number of the prepared activated carbons was calculated. Results shown in Figure3 indicate that as carbonization temperature changed from 400°C to 700°C with an impregnation ratio from 1 : 1 to 1 : 1.7, the value of the iodine number also increased. However, the further increase of impregnation to 1 : 3 resulted in reduction in the iodine number, as presented in Figure 3. So, as impregnation increases, the decrease in iodine number might be associated with the excess dehydration and destruction of micropores at a higher impregnation ratio. If the micropores are destroyed to form larger pores, the iodine number and adsorption capacity eventually decrease [2–16, 24–26, 31–35]. According to the findings, it can be observed that the prepared activated carbons gave a higher iodine numberof 420 mg/g than commercial activated carbon. On the other hand, the activated carbon prepared from rice husks produced a higher iodine value than activated carbon prepared from potato peels.Figure 3
The iodine number of the prepared activated carbon samples.


#### 3.1.7. Ammonia and Gasoline Adsorption

The results for ammonia and gasoline adsorption are presented in Figure4. Results showed that at impregnation ratios from 1 : 1 to 1 : 3 and as carbonization temperature increased from 400°C to 700°C, the adsorption rates of gasoline and ammonia firstly increased and, a few moments after, started to decrease. These results might be connected with heat treatment during carbonization, facilitating pore opening and widening and increasing the surface area. However, massive thermal treatment results in carbon burn-off affecting the pore size and surface area of the activated carbon, affecting adsorbing capacities [14, 16]. The lowest values in ammonia gas and gasoline adsorption efficiency were attained in activated carbon samples derived from potato peels compared to rice husk activated charcoal.Figure 4
Ammonia (a) and gasoline (b) adsorption of the prepared activated carbons.


### 3.2. Point of Zero Charges (pHpzc)

The point of zero charge(s) for the prepared activated carbons was evaluated through a 0.01 M KNO3 solution. The pH adjustment was performed by drop-wise addition of either 0.1 M NaOH or 0.1 M HCl. pHpzc is used to evaluate the pH of the adsorbents. Figure 5 shows the results of RH-AC and PP-AC having a similar point of zero charges equivalent to pHpzc=6.8. At this point, the adsorbents have a net electrical neutral charge on the surface. When the solution pH is lower than the pHpzc, the adsorbent surface becomes protonated due to excess competition of H+ ions resulting in the surface favoring the removal property of contaminants like anions. When pH is greater than the pHpzc, the adsorbent surface becomes deprotonated by OH− ions in the solution and the surface has a negative charge density and favors the adsorption of pollutants like cations [36]. The prepared activated carbon pHpzc was nearby neutral pH.Figure 5
The point of zero charge plot for RH-AC and PP-AC.


### 3.3. X-Ray Diffractions

The X-ray pattern of the prepared activated carbons is presented in Figure6. The results show the Bragg diffraction peak for both activated carbon samples at the region of 2θ=20–30°. The existence of the hump depicts the high degree of disorder characteristic of carbonaceous materials. Furthermore, the nonappearance of a sharp peak suggests that no discrete mineral peaks were noticed in the samples [37]. Similar patterns were also reported by other researchers who prepared activated carbons from agro-wastes [19, 20].Figure 6
The XRD spectra for RH-AC and PP-AC, respectively.


### 3.4. Surface Functional Group Results

The results for functional groups of the activated carbon understudy are shown in Figure7. The peaks observed at wavenumbers, 3743–3646 cm−1, are assigned to the stretching bond vibration of free hydrogen bonded to −OH groups [38]. The absorption bands at around 2336–2376 cm−1 are associated with stretching vibration of the C-O for carbon dioxide or carbon monoxide derivatives. The peak present at 2180 cm−1 corresponds to bond stretching vibrations of alkynes (C≡C). The bands visible at (1673, 1400) cm−1 relate to the stretching vibration of C=C in the benzene ring [39]. The N-oxide group observed at 1548 cm−1 was assigned to asymmetric and symmetric stretching (N=O). The peak detected at 1052 cm−1 is associated with the antisymmetric stretch of C-O-C [40]. The presence of the most functional groups indicates suitable characteristics of the activated carbons.Figure 7
The IR spectra for RH-AC and PP-AC, respectively.


### 3.5. FESEM Results

The micrographs shown in Figure8 revealed a porous surface area accompanied by several wide opening pores of different sizes and shapes. The images revealed cavities, porous structures, and large interconnected pores that allow access to inner zones of the adsorbents. The chemical activation of precursors at 500°C with 40% orthophosphoric acid (H3PO4) resulted in an extensive removal of volatile matter and promoted the opening and formation of more pores (micropores and mesopores) on the surface of the adsorbents [41]. The pre-existent pores had a crucial role in increasing the surface area of the prepared carbon. The results suggest that the prepared adsorbents could be suitable for various uses due to the surface porosity.Figure 8
FESEM micrographs (a) PP-AC and (b) RH-AC.
(a)(b)The characteristic results of the prepared activated carbons were compared with other adsorbents. Table4 provides the key features of derived activated carbon compared to other adsorbents mentioned in the literature.Table 4
A comparison of the characteristics of the activated carbons with other literature reported values.
PrecursorActivatorActivation temp (°C)Functional groupsXRDSEMpHpzcReferenceWisteria sinensis seedsKOH850C=O, C=C, O-H, C-OAmorphousMesoporous surface—[42]Biomass date seedsH2SO4, KOH600–900O-H, C=O, C-O———[43]Coffee groundsKOH800C=O, O-H, C-O—Microporous surface—[44]Tobacco cigarettesZnCl2700C=C, CH, OH—Microporous surface7.47[45]NaOH700C=C, C=N, OH—Mesoporous surface12.84[45]Tobacco stemsH3PO4750OH,C-O,C=O, C-C—Mesoporous surface9.59[46]Acacia auriculiformisH3PO4850——Microporous surface4.8[47]NaOH850——Mesoporous surface8.2[47]NaCl850——Microporous surface6.8[47]Almond shellH3PO4600COO−, C=O,C-H,—Microporous surface5.5[48]Pineapple wastesZnCl2500OH, N-O, C-N—Mesoporous surface—[49]Baobab fruit shellsH3PO4700C=C, C-O, C-HAmorphousMicroporous surface—[41]Food wastesZnCl2500–600C-O, C=C, C=O, O-HAmorphousMesoporous surface[50]LemnaminorH3PO4600N-H, C-H, O-H, C=O—Mesoporous surface—[51]Daniellia oliveriH3PO4—OH, C-H, C≡C, C=C—Microporous surface7.6[52]Leucaena leucocephalaNaOH550C=O, C≡C-H, C=C, OH—Mesoporous surface5.2[53]Rice huskNaOH650—AmorphousMesoporous surface—[54]Hazelnut husk—950—AmorphousMicroporous surface—[55]Green vegetable wastesKOH800C≡N, C=O, CH, OH—Microporous surface—[56]Soya bean strawNaOH120CH, C-O, OH—Mesoporous surface—[57]Feather fiber—600N-C=O, C-C, C-N—Mesoporous surface5.94[58]Human hair—500C=O, C=C, C-OH, C-HAmorphousMicroporous surface—[59]Mango kernelH3PO4600N-H, C=O, OH, CH—Mesoporous surface6.8[60]Rice husksH3PO4500C=O, OH, C-O, C≡CAmorphousMicroporous surface6.8This studyIrish potato peelsH3PO4500C≡C, C=O, C-O, OHAmorphousMicroporous surface6.8This study


## 3.1. Physicochemical Properties

### 3.1.1. Carbon Yield

The carbon yield results for the prepared RH-AC and PP-AC show that as activation temperature increases from 400°C to 700°C at impregnation ratios 1 : 1 to 1 : 3; the percentage of carbon yield decreases as presented in Figure1. The results showed that increasing carbonization temperature decreases the percentage of AC yield. This result is likely associated with promoting carbon burn-off and volatilization of tar at elevated temperatures. Again, the decrease in carbon yield could be attributed to the increasing impregnation ratio, which promotes the release of volatiles from the sample resulting in the decrease in carbon yield. The lower carbon yield with a higher impregnation ratio might be due to the enhancement of carbon burn-off by excess activating agents [27, 28]. A similar pattern of results was reported in the literature by investigators who worked on deriving activated carbon from agro-wastes [29]. Higher carbon yield on prepared carbons was attained in PP-AC samples than RH-AC.Figure 1
The effect of the impregnation ratio and carbonization temperature on carbon yield.


### 3.1.2. Moisture Content

The moisture content in prepared activated carbon was determined to ascertain its suitability in adsorption studies. The results indicate an increase in impregnation ratios from 1 : 1 to 1 : 3 and carbonization temperature from 400°C to 700°C for both RH-AC and PP-AC; the moisture content of the derived activated carbon samples reduced as shown in Table1. It was observed that as the activation temperature increased, the moisture content in activated carbon samples decreased. This result might be connected to removing volatile matter, thereby reducing carbon yield and concurrently reducing the moisture content in the prepared RH-AC and PP-AC samples. The samples with a similar impregnation ratio but different activation temperatures had minimal moisture content. The activated carbon derived from potato peels had high moisture content instead of activated carbon obtained from rice husks. The comparison of prepared activated carbons with commercial activated carbon was made, and the results displayed by RH-AC were similar to that of commercial activated charcoal (4%).Table 1
The effect of the impregnation ratio and activation temperature on moisture content.
Activation temperature (°C)Impregnation400500600700RatioRH-ACPP-ACRH-ACPP-ACRH-ACPP-ACRH-ACPP-AC1 : 13.65±0.256.80±0.24.9±0.356.2±0.404.4±0.355.9±0.254.4±0.035.4±0.31 : 1.73.45±0.155.40±0.14.5±0.155.7±0.153.7±0.375.6±0.154.2±0.154.95±0.151 : 2.53.15±0.254.88±0.324.4±0.305.0±0.204.2±0.35.2±0.24.1±0.14.35±0.251 : 32.95±0.153.16±0.344.1±0.184.4±0.243.6±0.25.1±0.24.05±0.24.3±0.2


### 3.1.3. Ash Content

The ash content findings are presented in Figure2. The results showed that increasing impregnation ratios from 1 : 1 to 1 : 3 and carbonization temperature from 400 to 700°C for both RH-AC and PP-AC increased the ash content for both the prepared RH-AC and PP-AC samples. It was noted that increasing the activation temperature increased the ash content in activated carbon samples. The increase in ash content might be associated with a high degree of biomass burn-off at elevated temperatures. Comparing the ash content with commercial activated carbon, the ash content in all prepared activated charcoal samples exceeded the recommended range of 2–10 (%) but activated carbon prepared from rice husks had less ash content. This result implies that the activated carbons synthesized were not of high purity. However, different investigators reported similar results in the literature on activated carbons from agro-wastes [30].Figure 2
The effect of the impregnation ratio and activation temperature on the ash content.


### 3.1.4. Volatile Matter

While the impregnation ratio increases from 1 : 1 to 1 : 3 with activation temperature from 400°C to 700°C, volatile matter decreases for RH-AC and PP-AC (Table2). The results indicated that increasing carbonization temperature caused a decrease in the volatile matter content in both RH-AC and PP-AC. The reduction in the volatile matter percentage as activation temperature increases is connected to the fact that more volatile matter is released at an elevated temperature, lowering its content in activated carbon samples. The study has recognized high-volatile matter content in activated carbon samples prepared from Irish potato peels compared with rice husks. Volatile matter in commercial activated carbon was noted at 30% compared to prepared activated carbon samples within the required range.Table 2
The volatile matter in the prepared activated carbon samples.
Activation temperature (°C)Impregnation400500600700RatioRH-ACPP-ACRH-ACPP-ACRH-ACPP-ACRH-ACPP-AC1 : 114.05±0.1716.22±0.2412.79±0.3315.02±0.0412.34±0.1314.39±0.0712.89±0.0212.38±0.151 : 1.715.33±0.1116.37±0.6213.09±0.3215.07±0.0913.34±0.3614.88±0.1113.28±0.3112.48±0.261 : 2.517.61±0.1818.12±0.3514.35±0.1416.52±0.1814.43±0.2515.51±0.1714.09±0.3214.01±0.121 : 318.01±0.1318.66±0.1915.39±0.1716.76±0.1314.58±0.3215.61±0.1514.58±0.2014.51±0.17


### 3.1.5. Fixed Carbon Content

The carbon content in prepared activated carbon samples was calculated. At given impregnation ratios 1 : 1 to 1 : 3 and increasing carbonization temperature from 400°C to 700°C, the carbon content for the prepared activated carbon samples decreased as displayed in Table3. The fixed carbon content results depend on volatile matter, ash, and moisture content. The results indicated that an increase in carbonization temperatures promotes the release of volatile matter and increases the ash content while at the same time decreasing the moisture content. The activated carbons prepared at 400°C were within the recommended range of commercial activated carbon, whereas in commercial activated carbon, the carbon content ranges 50–95%. The activated carbon derived from rice husks had carbon content within the commercial activated charcoal.Table 3
The fixed carbon content of the prepared activated carbons.
Activation temperature (°C)Impregnation400500600700RatioRH-ACPP-ACRH-ACPP-ACRH-ACPP-ACRH-ACPP-AC1 : 157.48±0.6949.88±0.2155.88±0.3549.39±0.2954.49±0.3949.88±0.3953.27±0.3150.79±0.251 : 1.756.21±0.3248.16±0.2755.46±0.7949.28±0.1251.96±0.6347.99±0.4250.88±0.2249.78±0.351 : 2.552.07±0.1846.68±0.0152.97±0.5245.58±0.2250.99±0.2547.90±0.1344.78±0.5648.10±0.421 : 351.4±0.5144.47±0.5051.33±0.5646.45±1.3147.08±0.2047.08±0.2044.76±0.2047.68±0.46


### 3.1.6. Iodine Number

The iodine number of the prepared activated carbons was calculated. Results shown in Figure3 indicate that as carbonization temperature changed from 400°C to 700°C with an impregnation ratio from 1 : 1 to 1 : 1.7, the value of the iodine number also increased. However, the further increase of impregnation to 1 : 3 resulted in reduction in the iodine number, as presented in Figure 3. So, as impregnation increases, the decrease in iodine number might be associated with the excess dehydration and destruction of micropores at a higher impregnation ratio. If the micropores are destroyed to form larger pores, the iodine number and adsorption capacity eventually decrease [2–16, 24–26, 31–35]. According to the findings, it can be observed that the prepared activated carbons gave a higher iodine numberof 420 mg/g than commercial activated carbon. On the other hand, the activated carbon prepared from rice husks produced a higher iodine value than activated carbon prepared from potato peels.Figure 3
The iodine number of the prepared activated carbon samples.


### 3.1.7. Ammonia and Gasoline Adsorption

The results for ammonia and gasoline adsorption are presented in Figure4. Results showed that at impregnation ratios from 1 : 1 to 1 : 3 and as carbonization temperature increased from 400°C to 700°C, the adsorption rates of gasoline and ammonia firstly increased and, a few moments after, started to decrease. These results might be connected with heat treatment during carbonization, facilitating pore opening and widening and increasing the surface area. However, massive thermal treatment results in carbon burn-off affecting the pore size and surface area of the activated carbon, affecting adsorbing capacities [14, 16]. The lowest values in ammonia gas and gasoline adsorption efficiency were attained in activated carbon samples derived from potato peels compared to rice husk activated charcoal.Figure 4
Ammonia (a) and gasoline (b) adsorption of the prepared activated carbons.


## 3.1.1. Carbon Yield

The carbon yield results for the prepared RH-AC and PP-AC show that as activation temperature increases from 400°C to 700°C at impregnation ratios 1 : 1 to 1 : 3; the percentage of carbon yield decreases as presented in Figure1. The results showed that increasing carbonization temperature decreases the percentage of AC yield. This result is likely associated with promoting carbon burn-off and volatilization of tar at elevated temperatures. Again, the decrease in carbon yield could be attributed to the increasing impregnation ratio, which promotes the release of volatiles from the sample resulting in the decrease in carbon yield. The lower carbon yield with a higher impregnation ratio might be due to the enhancement of carbon burn-off by excess activating agents [27, 28]. A similar pattern of results was reported in the literature by investigators who worked on deriving activated carbon from agro-wastes [29]. Higher carbon yield on prepared carbons was attained in PP-AC samples than RH-AC.Figure 1
The effect of the impregnation ratio and carbonization temperature on carbon yield.


## 3.1.2. Moisture Content

The moisture content in prepared activated carbon was determined to ascertain its suitability in adsorption studies. The results indicate an increase in impregnation ratios from 1 : 1 to 1 : 3 and carbonization temperature from 400°C to 700°C for both RH-AC and PP-AC; the moisture content of the derived activated carbon samples reduced as shown in Table1. It was observed that as the activation temperature increased, the moisture content in activated carbon samples decreased. This result might be connected to removing volatile matter, thereby reducing carbon yield and concurrently reducing the moisture content in the prepared RH-AC and PP-AC samples. The samples with a similar impregnation ratio but different activation temperatures had minimal moisture content. The activated carbon derived from potato peels had high moisture content instead of activated carbon obtained from rice husks. The comparison of prepared activated carbons with commercial activated carbon was made, and the results displayed by RH-AC were similar to that of commercial activated charcoal (4%).Table 1
The effect of the impregnation ratio and activation temperature on moisture content.
Activation temperature (°C)Impregnation400500600700RatioRH-ACPP-ACRH-ACPP-ACRH-ACPP-ACRH-ACPP-AC1 : 13.65±0.256.80±0.24.9±0.356.2±0.404.4±0.355.9±0.254.4±0.035.4±0.31 : 1.73.45±0.155.40±0.14.5±0.155.7±0.153.7±0.375.6±0.154.2±0.154.95±0.151 : 2.53.15±0.254.88±0.324.4±0.305.0±0.204.2±0.35.2±0.24.1±0.14.35±0.251 : 32.95±0.153.16±0.344.1±0.184.4±0.243.6±0.25.1±0.24.05±0.24.3±0.2


## 3.1.3. Ash Content

The ash content findings are presented in Figure2. The results showed that increasing impregnation ratios from 1 : 1 to 1 : 3 and carbonization temperature from 400 to 700°C for both RH-AC and PP-AC increased the ash content for both the prepared RH-AC and PP-AC samples. It was noted that increasing the activation temperature increased the ash content in activated carbon samples. The increase in ash content might be associated with a high degree of biomass burn-off at elevated temperatures. Comparing the ash content with commercial activated carbon, the ash content in all prepared activated charcoal samples exceeded the recommended range of 2–10 (%) but activated carbon prepared from rice husks had less ash content. This result implies that the activated carbons synthesized were not of high purity. However, different investigators reported similar results in the literature on activated carbons from agro-wastes [30].Figure 2
The effect of the impregnation ratio and activation temperature on the ash content.


## 3.1.4. Volatile Matter

While the impregnation ratio increases from 1 : 1 to 1 : 3 with activation temperature from 400°C to 700°C, volatile matter decreases for RH-AC and PP-AC (Table2). The results indicated that increasing carbonization temperature caused a decrease in the volatile matter content in both RH-AC and PP-AC. The reduction in the volatile matter percentage as activation temperature increases is connected to the fact that more volatile matter is released at an elevated temperature, lowering its content in activated carbon samples. The study has recognized high-volatile matter content in activated carbon samples prepared from Irish potato peels compared with rice husks. Volatile matter in commercial activated carbon was noted at 30% compared to prepared activated carbon samples within the required range.Table 2
The volatile matter in the prepared activated carbon samples.
Activation temperature (°C)Impregnation400500600700RatioRH-ACPP-ACRH-ACPP-ACRH-ACPP-ACRH-ACPP-AC1 : 114.05±0.1716.22±0.2412.79±0.3315.02±0.0412.34±0.1314.39±0.0712.89±0.0212.38±0.151 : 1.715.33±0.1116.37±0.6213.09±0.3215.07±0.0913.34±0.3614.88±0.1113.28±0.3112.48±0.261 : 2.517.61±0.1818.12±0.3514.35±0.1416.52±0.1814.43±0.2515.51±0.1714.09±0.3214.01±0.121 : 318.01±0.1318.66±0.1915.39±0.1716.76±0.1314.58±0.3215.61±0.1514.58±0.2014.51±0.17


## 3.1.5. Fixed Carbon Content

The carbon content in prepared activated carbon samples was calculated. At given impregnation ratios 1 : 1 to 1 : 3 and increasing carbonization temperature from 400°C to 700°C, the carbon content for the prepared activated carbon samples decreased as displayed in Table3. The fixed carbon content results depend on volatile matter, ash, and moisture content. The results indicated that an increase in carbonization temperatures promotes the release of volatile matter and increases the ash content while at the same time decreasing the moisture content. The activated carbons prepared at 400°C were within the recommended range of commercial activated carbon, whereas in commercial activated carbon, the carbon content ranges 50–95%. The activated carbon derived from rice husks had carbon content within the commercial activated charcoal.Table 3
The fixed carbon content of the prepared activated carbons.
Activation temperature (°C)Impregnation400500600700RatioRH-ACPP-ACRH-ACPP-ACRH-ACPP-ACRH-ACPP-AC1 : 157.48±0.6949.88±0.2155.88±0.3549.39±0.2954.49±0.3949.88±0.3953.27±0.3150.79±0.251 : 1.756.21±0.3248.16±0.2755.46±0.7949.28±0.1251.96±0.6347.99±0.4250.88±0.2249.78±0.351 : 2.552.07±0.1846.68±0.0152.97±0.5245.58±0.2250.99±0.2547.90±0.1344.78±0.5648.10±0.421 : 351.4±0.5144.47±0.5051.33±0.5646.45±1.3147.08±0.2047.08±0.2044.76±0.2047.68±0.46


## 3.1.6. Iodine Number

The iodine number of the prepared activated carbons was calculated. Results shown in Figure3 indicate that as carbonization temperature changed from 400°C to 700°C with an impregnation ratio from 1 : 1 to 1 : 1.7, the value of the iodine number also increased. However, the further increase of impregnation to 1 : 3 resulted in reduction in the iodine number, as presented in Figure 3. So, as impregnation increases, the decrease in iodine number might be associated with the excess dehydration and destruction of micropores at a higher impregnation ratio. If the micropores are destroyed to form larger pores, the iodine number and adsorption capacity eventually decrease [2–16, 24–26, 31–35]. According to the findings, it can be observed that the prepared activated carbons gave a higher iodine numberof 420 mg/g than commercial activated carbon. On the other hand, the activated carbon prepared from rice husks produced a higher iodine value than activated carbon prepared from potato peels.Figure 3
The iodine number of the prepared activated carbon samples.


## 3.1.7. Ammonia and Gasoline Adsorption

The results for ammonia and gasoline adsorption are presented in Figure4. Results showed that at impregnation ratios from 1 : 1 to 1 : 3 and as carbonization temperature increased from 400°C to 700°C, the adsorption rates of gasoline and ammonia firstly increased and, a few moments after, started to decrease. These results might be connected with heat treatment during carbonization, facilitating pore opening and widening and increasing the surface area. However, massive thermal treatment results in carbon burn-off affecting the pore size and surface area of the activated carbon, affecting adsorbing capacities [14, 16]. The lowest values in ammonia gas and gasoline adsorption efficiency were attained in activated carbon samples derived from potato peels compared to rice husk activated charcoal.Figure 4
Ammonia (a) and gasoline (b) adsorption of the prepared activated carbons.


## 3.2. Point of Zero Charges (pHpzc)

The point of zero charge(s) for the prepared activated carbons was evaluated through a 0.01 M KNO3 solution. The pH adjustment was performed by drop-wise addition of either 0.1 M NaOH or 0.1 M HCl. pHpzc is used to evaluate the pH of the adsorbents. Figure 5 shows the results of RH-AC and PP-AC having a similar point of zero charges equivalent to pHpzc=6.8. At this point, the adsorbents have a net electrical neutral charge on the surface. When the solution pH is lower than the pHpzc, the adsorbent surface becomes protonated due to excess competition of H+ ions resulting in the surface favoring the removal property of contaminants like anions. When pH is greater than the pHpzc, the adsorbent surface becomes deprotonated by OH− ions in the solution and the surface has a negative charge density and favors the adsorption of pollutants like cations [36]. The prepared activated carbon pHpzc was nearby neutral pH.Figure 5
The point of zero charge plot for RH-AC and PP-AC.


## 3.3. X-Ray Diffractions

The X-ray pattern of the prepared activated carbons is presented in Figure6. The results show the Bragg diffraction peak for both activated carbon samples at the region of 2θ=20–30°. The existence of the hump depicts the high degree of disorder characteristic of carbonaceous materials. Furthermore, the nonappearance of a sharp peak suggests that no discrete mineral peaks were noticed in the samples [37]. Similar patterns were also reported by other researchers who prepared activated carbons from agro-wastes [19, 20].Figure 6
The XRD spectra for RH-AC and PP-AC, respectively.


## 3.4. Surface Functional Group Results

The results for functional groups of the activated carbon understudy are shown in Figure7. The peaks observed at wavenumbers, 3743–3646 cm−1, are assigned to the stretching bond vibration of free hydrogen bonded to −OH groups [38]. The absorption bands at around 2336–2376 cm−1 are associated with stretching vibration of the C-O for carbon dioxide or carbon monoxide derivatives. The peak present at 2180 cm−1 corresponds to bond stretching vibrations of alkynes (C≡C). The bands visible at (1673, 1400) cm−1 relate to the stretching vibration of C=C in the benzene ring [39]. The N-oxide group observed at 1548 cm−1 was assigned to asymmetric and symmetric stretching (N=O). The peak detected at 1052 cm−1 is associated with the antisymmetric stretch of C-O-C [40]. The presence of the most functional groups indicates suitable characteristics of the activated carbons.Figure 7
The IR spectra for RH-AC and PP-AC, respectively.


## 3.5. FESEM Results

The micrographs shown in Figure8 revealed a porous surface area accompanied by several wide opening pores of different sizes and shapes. The images revealed cavities, porous structures, and large interconnected pores that allow access to inner zones of the adsorbents. The chemical activation of precursors at 500°C with 40% orthophosphoric acid (H3PO4) resulted in an extensive removal of volatile matter and promoted the opening and formation of more pores (micropores and mesopores) on the surface of the adsorbents [41]. The pre-existent pores had a crucial role in increasing the surface area of the prepared carbon. The results suggest that the prepared adsorbents could be suitable for various uses due to the surface porosity.Figure 8
FESEM micrographs (a) PP-AC and (b) RH-AC.
(a)(b)The characteristic results of the prepared activated carbons were compared with other adsorbents. Table4 provides the key features of derived activated carbon compared to other adsorbents mentioned in the literature.Table 4
A comparison of the characteristics of the activated carbons with other literature reported values.
PrecursorActivatorActivation temp (°C)Functional groupsXRDSEMpHpzcReferenceWisteria sinensis seedsKOH850C=O, C=C, O-H, C-OAmorphousMesoporous surface—[42]Biomass date seedsH2SO4, KOH600–900O-H, C=O, C-O———[43]Coffee groundsKOH800C=O, O-H, C-O—Microporous surface—[44]Tobacco cigarettesZnCl2700C=C, CH, OH—Microporous surface7.47[45]NaOH700C=C, C=N, OH—Mesoporous surface12.84[45]Tobacco stemsH3PO4750OH,C-O,C=O, C-C—Mesoporous surface9.59[46]Acacia auriculiformisH3PO4850——Microporous surface4.8[47]NaOH850——Mesoporous surface8.2[47]NaCl850——Microporous surface6.8[47]Almond shellH3PO4600COO−, C=O,C-H,—Microporous surface5.5[48]Pineapple wastesZnCl2500OH, N-O, C-N—Mesoporous surface—[49]Baobab fruit shellsH3PO4700C=C, C-O, C-HAmorphousMicroporous surface—[41]Food wastesZnCl2500–600C-O, C=C, C=O, O-HAmorphousMesoporous surface[50]LemnaminorH3PO4600N-H, C-H, O-H, C=O—Mesoporous surface—[51]Daniellia oliveriH3PO4—OH, C-H, C≡C, C=C—Microporous surface7.6[52]Leucaena leucocephalaNaOH550C=O, C≡C-H, C=C, OH—Mesoporous surface5.2[53]Rice huskNaOH650—AmorphousMesoporous surface—[54]Hazelnut husk—950—AmorphousMicroporous surface—[55]Green vegetable wastesKOH800C≡N, C=O, CH, OH—Microporous surface—[56]Soya bean strawNaOH120CH, C-O, OH—Mesoporous surface—[57]Feather fiber—600N-C=O, C-C, C-N—Mesoporous surface5.94[58]Human hair—500C=O, C=C, C-OH, C-HAmorphousMicroporous surface—[59]Mango kernelH3PO4600N-H, C=O, OH, CH—Mesoporous surface6.8[60]Rice husksH3PO4500C=O, OH, C-O, C≡CAmorphousMicroporous surface6.8This studyIrish potato peelsH3PO4500C≡C, C=O, C-O, OHAmorphousMicroporous surface6.8This study


## 4. Conclusion

The study has shown that the activated carbons prepared were not of high purity due to, among other factors, high ash content, moisture content, and less fixed carbon content as compared to commercial activated carbon. Nevertheless, the iodine value was much higher than that of commercial activated carbon. Furthermore, the analysis has confirmed that the prepared activated carbons were amorphous with the small crystalline domain, more porous, and with surface functional groups appearing at fingerprint regions. The study has further demonstrated that the materials understudy could be viable raw materials to prepare low-cost but high-porous activated carbon for adsorbing chemical pollutants in water and wastewater treatment. This result also offers a solution to the challenges Malawi as a developing country faces in agro-waste disposal.



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*Source: 9975444-2022-03-22.xml*