Synthesis and Characterization of Activated Biocarbons Produced from Avocado Seeds Using the Non-Toxic and Environmentally Friendly Activating Agent K₂CO₃ for CO₂ Capture

Abstract

Activated biocarbons were synthesized from avocado seeds using potassium carbonate as an activating agent. The study aimed to evaluate K₂CO₃ as a greener and less corrosive alternative to KOH, traditionally used for producing porous carbons. Twelve samples were obtained under varying activation conditions using both dry K₂CO₃ and its saturated solution. The material activated at 800 °C with a 1:1 precursor-to-activator ratio (C_K₂CO₃_800) showed the highest CO₂ adsorption capacity of 6.26 mmol/g at 0 °C and 1 bar. Nitrogen adsorption–desorption analysis confirmed a predominantly microporous structure, with ultramicropores (0.3–0.7 nm) primarily responsible for the high CO₂ uptake. The Sips model provided the best fit to the adsorption equilibrium data, indicating a heterogeneous surface. The isosteric heat of adsorption (22–26 kJ/mol) confirmed a physical adsorption mechanism. Furthermore, the CO₂/N₂ selectivity, evaluated using the Ideal Adsorbed Solution Theory (IAST), reached values up to 18 at low pressures, highlighting the excellent separation performance. These findings demonstrate that avocado seed-derived activated carbons prepared with K₂CO₃ are efficient, renewable, and environmentally friendly sorbents for CO₂ capture, combining high adsorption capacity with sustainability and ease of synthesis.

1. Introduction

Carbon dioxide (CO₂) released into the atmosphere as a result of anthropogenic activities, such as the combustion of fossil fuels, industrial processes, and deforestation, is widely recognized as the primary driver of global warming and climate change. The continuously increasing atmospheric concentration of CO₂ enhances the greenhouse effect by trapping outgoing infrared radiation, which leads to a progressive rise in global mean temperatures, disturbance of climatic patterns, and severe environmental consequences [1].

To mitigate these adverse effects, a wide range of strategies have been developed to limit CO₂ emissions or remove it from the atmosphere. Among them, carbon capture and sequestration (CCS) has emerged as one of the most promising approaches. This strategy involves capturing CO₂ from large point sources, such as power plants and industrial facilities, followed by its transportation and long-term storage in geological formations or its utilization in chemical, biological, or mineralization processes [2].

Adsorption is one of the most effective and widely applied techniques for gas separation due to its simplicity, high efficiency, and low energy consumption compared with other methods. Unlike absorption, membrane separation, or cryogenic distillation, adsorption processes can operate efficiently at relatively low temperatures and pressures. Moreover, they allow for the selective removal or recovery of specific gas components, such as CO₂, using solid porous materials with tailored surface properties. Hence, designing adsorbent materials that exhibit superior affinity and capacity for the target gas is essential to ensure effective adsorption performance [3].

Among various materials investigated for this purpose, activated carbons have attracted significant attention due to their well-developed porous structure, large specific surface area, chemical stability, and tunable surface functionality [4,5]. These features make them particularly suitable for CO₂ capture, as they enable high adsorption capacities under mild operating conditions and excellent regenerability over multiple cycles. Furthermore, activated carbons can be synthesized from a wide range of low-cost and renewable precursors, including agricultural and industrial wastes, which enhances their environmental and economic attractiveness [6,7].

Activated carbons can be synthesized from a wide variety of precursors using different preparation techniques. Among these methods, chemical activation is of particular importance and is the most commonly employed approach for producing materials with a well-developed pore structure [8,9]. In this process, various chemical agents are used as activating substances, including KOH [10,11,12], ZnCl₂ [13], H₃PO₄ [14], and NaOH [15]. Among these activating agents, KOH is the most widely used, as it enables the formation of materials with a high specific surface area and a well-developed hierarchical porosity [16,17].

The use of KOH as an activating agent in the production of activated carbons involves several significant drawbacks that limit its large-scale application [17,18,19]. Activation with KOH generates large amounts of wastewater containing dissolved potassium salts, mainly K₂CO₃, K₂O, and K₂SiO₃. These wastes require neutralization and disposal, which substantially increases both the operational costs and the environmental impact of the process. Another disadvantage is the strong corrosive nature of KOH, which necessitates the use of chemically resistant reactors, pipelines, valves, and specialized laboratory equipment, thereby raising investment and maintenance expenses. The recovery of KOH after activation is also difficult and economically unfeasible, since the reaction products, such as K₂CO₃, undergo partially irreversible transformations, making the activator suitable only for single use. Moreover, in cases of improper waste neutralization, potassium-containing solutions may pose an environmental hazard, leading to water and soil contamination, which requires the implementation of costly and energy-intensive purification procedures.

In comparison with KOH, the use of K₂CO₃ as an activating agent offers several significant advantages that make the activation process safer, cleaner, and more sustainable [17]. The amount of alkaline wastewater generated after activation is considerably lower, and the post-treatment solutions are easier to neutralize, since K₂CO₃ produces fewer soluble inorganic residues than KOH. Moreover, K₂CO₃ is a mild, non-corrosive, and stable compound, which greatly reduces equipment degradation and improves the overall safety of the process. Its non-toxic and environmentally benign nature minimizes ecological risks in case of accidental release, in contrast to the highly caustic behavior of KOH. Another important benefit is the ease of handling and storage, as potassium carbonate is chemically stable and non-hygroscopic, allowing for simple and safe operation on both laboratory and industrial scales. Additionally, K₂CO₃ can be obtained from recycled streams or industrial residues containing potassium salts, which aligns well with the principles of green chemistry and circular economy, making it an attractive and eco-friendly alternative to conventional activating agents [20].

It is commonly believed that KOH is a superior activating agent for the production of activated carbons due to the higher CO₂ adsorption capacity typically observed for such materials [21,22,23]. However, this is not always the case, as can be seen from the analysis of

Table 1. CO₂ capture comparison of activated carbons from different feedstocks at 0 °C and 1 bar.

Feedstock	Activator	Adsorption	Reference
avocado seeds	KOH	6.47	[24]
petroleum coke	KOH	6.08	[25]
coal tar pitch	KOH	6.00	[26]
rice husk	KOH	5.70	[27]
pollens	KOH	5.63	[28]
nitrogen-free phenolic resin	KOH	5.07	[29]
argan paste cakes	KOH	4.58	[30]
waste tea	KOH	2.32	[31]
bamboo powder	K2CO3	6.08	[32]
bamboo shoot	K2CO3	5.93	[33]
cotton waste	K2CO3	5.37	[34]
peanut shell	K2CO3	5.21	[35]
coconut shell	K2CO3	5.12	[17]
sugarcane	K2CO3	4.90	[36]

.

Therefore, we decided to investigate the activation of avocado seeds using K₂CO₃ instead of KOH, which had previously yielded high CO₂ adsorption [24]. We were the first to describe the use of avocado seeds as a precursor for activated carbon for CO₂ adsorption [24]. In that study, KOH was used as the activating agent. In the present manuscript, we demonstrate how avocado seeds can be efficiently converted into highly microporous CO₂ sorbents using K₂CO₃—a non-corrosive, non-toxic, and environmentally friendly activating agent that offers a practical alternative to KOH. Previous studies involving avocado seeds relied mainly on KOH activation which, although effective, has significant drawbacks: (i) it generates large amounts of highly corrosive wastewater, (ii) it causes severe equipment corrosion, and (iii) it does not allow recovery of the activating agent. In contrast, our work shows for the first time that K₂CO₃ can replace KOH while still providing very high CO₂ adsorption performance (up to 6.26 mmol/g at 0 °C and 1 bar).

Moreover, our study provides new insights by demonstrating that ultramicropores (0.3–0.7 nm) are formed most effectively when using a saturated K₂CO₃ solution, a 1:1 mass ratio of avocado seeds to K₂CO₃, and an activation temperature of 800 °C. These ultramicropores directly determine the highest CO₂ adsorption.

Our work advances existing research by introducing a sustainable activation method that enables the production of highly efficient CO₂ sorbents from avocado seeds, without the environmental and operational drawbacks associated with KOH.

This demonstrates that although KOH may in some cases achieve slightly higher values (as in our earlier work where 6.47 mmol/g was obtained), K₂CO₃ provides a very competitive performance considering its much lower environmental and operational cost.

2. Results and Discussion

Figure 1 presents CO₂ adsorption at 0 °C on all activated biochars prepared using K₂CO₃ applied either in aqueous or dry form. In Figure 1, the materials activated at different temperatures with dry K₂CO₃ and with its saturated aqueous solution are grouped together for comparison. Figure 1 show the materials obtained at various mass ratios of the carbon precursor to the activating agent, using K₂CO₃ in solution (Figure 1) and in dry form (Figure 1).

The highest CO₂ adsorption capacity (6.26 mmol/g) (

Table 2. Carbon dioxide adsorption at 0 °C and 100 kPa for activated biocarbons obtained from avocado seeds using K₂CO₃ as the activating agent.

Sample Name	CO2 Adsorption (mmol/g)
C_K2CO3_750	5.75
C_K2CO3_800	6.26
C_K2CO3_850	5.83
C_K2CO3dry_750	5.81
C_K2CO3dry_800	5.60
C_K2CO3dry_850	6.08
C_K2CO3_0.5_850	5.87
C_K2CO3_1.5_850	6.03
C_K2CO3_2_850	5.85
C_K2CO3dry_0.5_850	5.73
C_K2CO3dry_1.5_850	5.54
C_K2CO3dry_2_850	5.84

) was obtained for the activated carbon produced using a saturated solution of the activating agent, a mass ratio of dried seeds to K₂CO₃ of 1:1, and an activation temperature of 800 °C. Deviations from the 1:1 ratio, either increasing or decreasing the amount of activating agent, resulted in only minor variations in CO₂ adsorption and, in every case, led to a decrease in adsorption capacity, regardless of whether the activator was used in solid or solution form. Therefore further analyses focused exclusively on the activated carbons prepared with a 1:1 precursor-to-activating-agent ratio.

In [24], the activation of avocado seeds with KOH led to the formation of materials with very high specific surface areas (up to approximately 2000 m²/g), dominated by wider micropores and some mesopores, resulting from the intensive chemical etching characteristic of strongly alkaline activators. In contrast, activation with K₂CO₃ leads to a higher proportion of ultramicropores (0.3–0.7 nm), which are known to be crucial for CO₂ adsorption at low temperatures; a lower contribution of mesopores, which enhances the adsorption potential within narrow pores; and a milder, more controllable activation mechanism (without strong corrosion), allowing for more precise tailoring of the microporous structure. As a result, although the specific surface area obtained with K₂CO₃ is lower than in the KOH-activated material, the proportion of ultramicropores is higher, which compensates for differences in SBET and explains the high CO₂ uptake. A comparison of CO₂ adsorption performance (K₂CO₃ vs. KOH) at 0 °C and 100 kPa shows that KOH activation yields 6.47 mmol/g (0 °C, 1 bar), whereas K₂CO₃ yields 6.26 mmol/g. This difference is small, and considering the milder nature of K₂CO₃, the absence of corrosive wastewater, the lack of equipment corrosion, the scalability, and the overall process safety, the achieved CO₂ adsorption capacity is fully comparable while being more environmentally sustainable.

In the case of K₂CO₃, the activation mechanism at elevated temperatures (≥700 °C) can be summarized by the following reactions:

(1) K₂CO₃(s) → K₂O(s) + CO₂(g)

(2) K₂CO₃(s) + 2C(s) → 2K(g,l) + 3CO(g)

(3) K₂O(s) + C(s) → 2K(g,l) + CO(g)

(4) C(s) + CO₂(g) → 2CO(g)

In our system, these reactions lead to the in situ formation of CO and CO₂, which gasify the carbon matrix and generate both micro- and macroporous structures. At the same time, the metallic potassium formed (via reactions (2) and (3)) can intercalate between carbon layers, causing their expansion; its removal during washing leaves behind a well-developed pore network. The release of CO and CO₂ within the carbon matrix is therefore responsible for the development of both micropores and wider pores.

KOH also decomposes to K₂CO₃ during activation. However, the overall activation chemistry of KOH is more complex and significantly more aggressive, as it involves additional steps such as:

(5) 2KOH(s) → K₂O(s) + H₂O(g)

(6) K₂O(s) + CO₂(g) → K₂CO₃(s)

and reactions leading to hydrogen evolution at high temperatures, for example:

(7) 2KOH(s) + C(s) → K₂CO₃(s) + H₂(g)

(8) C(s) + H₂O(g) → CO(g) + H₂(g)

These reactions generate substantial amounts of H₂O and H₂, in addition to CO and CO₂, which results in significantly stronger chemical etching.

The CO₂ adsorption capacity of our best-performing sample (C_K₂CO₃_800), equal to 6.26 mmol/g at 0 °C and 1 bar, compares very favorably with activated carbons reported in the literature, as summarized in Table 1. For KOH-activated carbons, the majority of materials exhibit CO₂ uptakes in the range of 5.0–6.5 mmol/g: petroleum coke (6.08 mmol/g), waste tea (2.32 mmol/g). For K₂CO₃-activated carbons, reported capacities typically fall within 4.9–6.1 mmol/g: bamboo-derived carbon (6.08 mmol/g), sugarcane (4.90 mmol/g). Against this background, the capacity of our material (6.26 mmol/g) is among the highest reported for K₂CO₃-activated carbons, and is comparable to or higher than many KOH-activated carbons, despite the milder, non-corrosive nature of K₂CO₃. This clearly demonstrates that avocado-seed-derived activated carbons prepared using K₂CO₃ not only match, but also in several cases surpass the performance of conventional activated carbons, highlighting their strong potential for CO₂ capture applications.

Nitrogen adsorption–desorption isotherms at 196 °C for activated biocarbons prepared using K₂CO₃ as the activating agent, applied either as a saturated aqueous solution (C_K₂CO₃) or as a dry salt (C_K₂CO₃dry), at activation temperatures of 750, 800, and 850 °C are shown in Figure 2a. All samples exhibit type I isotherms with a pronounced nitrogen uptake at low relative pressures (p/p₀ < 0.1), characteristic of a microporous structure. A slight increase in adsorption at higher relative pressures and the absence of a noticeable hysteresis loop suggest the presence of a small amount of mesopores. The highest nitrogen adsorption was observed for the sample activated with dry K₂CO₃ at 850 °C, indicating the largest pore volume. The material obtained at the same temperature using the K₂CO₃ solution showed a lower nitrogen uptake (the second highest among the samples). The activated carbon that exhibited the highest CO₂ adsorption capacity (C_K₂CO₃_800) showed a relatively low nitrogen adsorption. The sample exhibited the second-lowest nitrogen adsorption volume at relative pressure near unity, indicating limited pore development compared with the other carbons.

The pore size distribution curves (Figure 2b), obtained from the N₂ adsorption data using the DFT model, confirm the predominance of micropores in all samples, with a main peak centered around 0.5 nm. A minor contribution of wider micropores and narrow mesopores (1–2 nm) is also visible, especially for the carbons activated at higher temperatures. The C_K₂CO₃_800 material shows the highest and most intense peak at 0.5 nm, indicating the greatest proportion of ultramicropores, which explains its excellent CO₂ adsorption performance. In contrast, the carbons activated at 850 °C, particularly those obtained using dry K₂CO₃, exhibit broader pore distributions extending toward the mesopore range, suggesting progressive pore widening with increasing activation temperature. The obtained results are consistent with the shape of the N₂ adsorption isotherms (Figure 2a), confirming that activation with dry K₂CO₃ promotes a more intensive development of the total porosity compared with activation using the aqueous solution.

The preliminary analysis of Figure 2 indicates that high total pore volume does not necessarily determine high CO₂ adsorption capacity.

Table 3. Textural properties of activated biocarbons obtained from avocado seeds using K₂CO₃ as the activating agent.

Activated Carbon	BET (m2/g)	Vtot (cm3/g)	Vmicro (cm3/g)
C_K2CO3_750	1365	0.572	0.460
C_K2CO3_800	1573	0.534	0.670
C_K2CO3_850	1951	0.925	0.658
C_K2CO3dry_750	1738	0.800	0.585
C_K2CO3dry_800	1562	0.710	0.528
C_K2CO3dry_850	2076	1.036	0.670

presents the textural properties of the activated biocarbons, namely the specific surface area, total pore volume, and micropore volume. The values of these parameters are consistent with the adsorption isotherm profiles and confirm the conclusions drawn from Figure 2. A more detailed analysis of the textural parameters, aimed at identifying possible correlations between each of them and the CO₂ adsorption capacity, revealed that their values do not directly influence CO₂ uptake (Figure S1).

The exceptionally high surface area of 2076 m²/g results from a synergistic effect of two factors: the use of dry K₂CO₃ and a high activation temperature of 850 °C. Individually, neither variable explains the result: For the dry-activated samples, the BET surface area does not increase monotonically with temperature (1738 m²/g at 750 °C, decreasing to 1562 m²/g at 800 °C, and increasing again to 2076 m²/g at 850 °C). For the solution-activated samples, the highest surface areas remain significantly lower (1365–1951 m²/g). This indicates that only the combination of dry K₂CO₃ with the highest activation temperature (850 °C) provides conditions that favor extensive CO₂—carbon gasification and the generation of both micropores and wider pores—resulting in the maximum surface area observed. Therefore, we conclude that: The dominant factor is the synergistic action of high activation temperature (850 °C) and the dry form of K₂CO₃, rather than either variable alone.

An attempt was also made to identify a correlation between the cumulative pore volume restricted to pores of a specific size range. The highest correlation coefficient was obtained for pores not larger than 1.08 nm, reaching a value of 0.63. This indicates a moderate positive correlation between the analyzed variables. Considering Figure 2b, it can be assumed that CO₂ adsorption is primarily influenced by pores in the range of 0.3–0.7 nm, although pores with sizes between 0.7 and 1 nm also have a certain contribution.

The XRD patterns (Figure 3) of all activated biocarbons obtained using K₂CO₃ as the activating agent display a broad diffraction peak centered at approximately 2θ ≈ 43°, corresponding to the (100) plane of turbostratic carbon. This indicates a certain degree of ordering of carbon atoms within the sp² structure. Only for the samples C_K₂CO₃_750, C_K₂CO₃_800, and C_K₂CO₃dry_800, a very weak peak at around 2θ ≈ 23°, corresponding to the (002) plane, can be observed. This suggests that well-ordered graphene layers are absent in the carbon structure of all materials, with only a very low degree of ordering in the mentioned samples. No crystalline potassium-containing phases were detected, confirming efficient washing and removal of inorganic residues after activation. Based on the XRD results and CO₂ adsorption data, it is evident that amorphous/turbostratic carbon is more favorable for CO₂ capture than graphitized carbon. The samples exhibiting the most disordered structures (broad (100) peak and negligible (002) reflection) developed the highest ultramicropore volume and consequently showed the highest CO₂ uptake.

In addition to the CO₂ adsorption measurements at 0 °C, experiments were also carried out at 10 °C and 30 °C to obtain a more comprehensive description of the adsorption equilibrium and its temperature dependence, enabling a more detailed analysis and mathematical modeling.

CO₂ adsorption isotherms obtained at 0, 10, and 30 °C (Figure 4) were analyzed using the Langmuir, Freundlich, Sips, Toth, and Radke–Prausnitz models [37]. The HYBRID error function (1) was employed to identify the best-fitting adsorption isotherm model.

$$HYBRID={\displaystyle \frac{100}{n-p}}{\sum }_{i=1}^n{\displaystyle \frac{{\left(q_{i,exp}-q_{i,calc}\right)}^2}{q_{i,exp}}}$$

(1)

q_e,calc—theoretical value of adsorption on the activated carbon surface calculated based on the model;

q_e,exp—experimental value of adsorption on the activated carbon surface;

n—total number of measurements;

p—number of model parameters.

Figure 4. Isotherms of CO₂ adsorption measured at 10 °C and 30 °C for activated biocarbons obtained from avocado seeds using K₂CO₃ as the activating agent.

Figure 4. Isotherms of CO₂ adsorption measured at 10 °C and 30 °C for activated biocarbons obtained from avocado seeds using K₂CO₃ as the activating agent.

Nonlinear regression was performed in Excel 365 employing the Solver add-in to identify the model that provided the best fit to the experimental data. The Sips equation is defined by (2):

$$q={\displaystyle \frac{q_m·b·p^n}{1+b·p^n}}$$

(2)

where

q—the CO₂ equilibrium adsorption at p;

p—equilibrium pressure;

q_m—the saturation capacity;

b—equilibrium constant;

n—exponential parameter indicating the heterogeneity of the sorbent.

The optimized parameters of the Sips equation together with the corresponding HYBRID values at 0, 10, and 30 °C are summarized in

Table 4. Parameters of the Sips equation at 0 °C, 10 °C, and 30 °C and the corresponding HYBRID values for CO₂ adsorption on activated biocarbons obtained from avocado seeds using K₂CO₃ as the activating agent.

	C_K2CO3_750	C_K2CO3_800	C_K2CO3_850	C_K2CO3dry_750	C_K2CO3dry_800	C_K2CO3dry_850
0 °C
qm	13.012	16.358	22.012	20.601	16.640	28.778
b	0.025	0.018	0.009	0.012	0.017	0.007
n	0.750	0.765	0.791	0.748	0.742	0.780
HYBRID	0.0072	0.0065	0.0052	0.0078	0.0046	0.0086
10 °C
qm	11.490	14.711	17.455	16.408	13.454	20.184
b	0.020	0.014	0.008	0.011	0.014	0.007
n	0.781	0.796	0.815	0.782	0.777	0.818
HYBRID	0.0052	0.0037	0.0061	0.0048	0.0063	0.0043
30 °C
qm	7.782	10.017	11.243	9.387	8.876	11.654
b	0.014	0.009	0.006	0.009	0.010	0.006
n	0.854	0.860	0.876	0.855	0.845	0.882
HYBRID	0.0018	0.0038	0.0037	0.0024	0.0041	0.0033

. The n values notably differ from unity, reflecting the heterogeneous nature of the surface of all investigated activated carbons.

For the best CO₂ adsorbent (C_K₂CO₃_800), additional CO₂ and N₂ adsorption measurements were carried out at 20 °C Figure 5. Comparison of N₂ and CO₂ adsorption at 20 °C for C_K₂CO₃_800. This enabled the construction of reliable temperature-dependent relationships for the parameters qₘ, b, and n, and for the CO₂/N₂ adsorption selectivity.

Mathematical analysis of the data presented in Figure 5 indicated that, for both CO₂ and N₂, the Sips model provided the best fit to the adsorption equilibrium. The calculated parameters are summarized in

Table 5. The parameters of the Sips equation at 20 °C and the corresponding HYBRID values for CO₂ and N₂ adsorption for C_K₂CO₃_800.

C_K2CO3_800 20 °C	CO2	N2
qm	13.693	3.203
b	0.010	0.002
n	0.817	0.993
HYBRID	0.0040	0.0002

.

The parameters in the Sips Equation (2) are temperature dependent:

$$q_m=q_{m0}·exp\left[\chi \left(1-{\displaystyle \frac{T}{T_0}}\right)\right],$$

(3)

$$b=b_{0}exp\left[{\displaystyle \frac{Q}{RT}}\left({\displaystyle \frac{T_0}{T}}-1\right)\right],$$

(4)

$$n=n_0+\alpha \left(1-{\displaystyle \frac{T_0}{T}}\right),$$

(5)

In Equations (3)–(5) q_mo, χ, Q, b₀, n₀, and α are the constants. R is ideal gas constant. T₀ is the reference temperature. In this work, the lowest temperature (273 K) was chosen as the reference temperature.

To determine the parameter q_m0, a plot of ln(q_m) versus temperature was constructed. The parameters Q and b₀ were derived from the linear dependence of b on 1/T. Similarly, n₀ and α were obtained from the n versus 1/T relationship. These correlations are illustrated in Figure 6. In all cases, linear relationships with high correlation coefficients were observed. This allowed the determination of additional parameters of the equations defining the temperature dependencies. The parameters are summarized in

Table 6. Parameters of the Sips Equations (3)–(5) describing temperature-dependent adsorption behavior.

Parameter	Values	Unit
Q	15,527	J/mol
b0	0.0099	bar−1
n0	0.763
α	0.931
qm0	16.99	mmol/g
χ	4.212

.

In addition to the high CO₂ adsorption capacity, the selectivity of CO₂ over nitrogen, the main component of flue gases, is also of great importance. The CO₂/N₂ adsorption selectivity was evaluated using the Ideal Adsorbed Solution Theory (IAST) [38].Within this theoretical framework, the selectivity of component A over component B in a binary gas mixture can be derived from the individual adsorption isotherms of both components. The selectivity equilibrium is expressed by Equation (6):

$$S_{eq}={\displaystyle \frac{q_{{CO}_2\left(p\right)}}{q_{N_2\left(p\right)}}},$$

(6)

Using the parameter values presented in Table 6, the adsorption of CO₂ ($q_{{CO}_2\left(p\right)}$) and N₂ ($q_{N_2\left(p\right)}$) was calculated for the same pressure values. Figure 7 shows the calculated values of CO₂/N₂ adsorption selectivity for an equimolar mixture at 20 °C as a function of pressure.

The equilibrium selectivity at low pressures is the highest, reaching a value of 18. It then decreases to approximately 8 at a pressure of 40, while further pressure increase results in only minor changes.

Nitrogen constitutes the dominant component of flue gases, typically representing more than 70% of the dry volume. This results from the fact that air, used as the oxidizing medium in combustion, contains about 78% nitrogen. As nitrogen remains largely inert under standard combustion conditions, it passes through the process without significant chemical transformation.

Conversely, carbon dioxide is the principal product of the complete oxidation of organic carbon in fossil fuels and biomass. Its concentration in flue gases depends on the fuel type and oxygen availability, generally ranging from 10% to 20% [39].

For the evaluation of CO₂/N₂ adsorption selectivity, gas mixtures reflecting the typical composition of flue gases were considered, namely: 10% CO₂ and 90% N₂, 15% CO₂ and 85% N₂, and 20% CO₂ and 80% N₂. For this purpose, Equation (7) was applied

$$S_{CO2\%}={\displaystyle \frac{q_{{CO}_2\left(p\right)}/q_{N_2\left(p\right)}}{p_{{CO}_2}/p_{N_2}}},$$

(7)

where CO₂% is the CO₂ content in the CO₂/N₂ gas mixture.

The calculated CO₂/N₂ adsorption selectivity for C_K₂CO₃_800 under model flue gas compositions at temperature of 20 °C are presented in

Table 7. Calculated CO₂ over N₂ adsorption selectivity for C_K₂CO₃_800 under model flue gas.

Flue Gas [CO2/N2]	Seq
10/90	14.15
15/85	12.69
20/80	11.65

.

The CO₂ adsorption selectivity values for C_K₂CO₃_800 under model flue gas compositions are high, which makes this material a promising CO₂ sorbent for various types of flue gases.

The determination of the isosteric heat of adsorption (Q_iso) is essential for understanding the energetics of the adsorption process. This parameter provides valuable insight into the strength and nature of the interaction between the adsorbate molecules and the surface of the adsorbent. High Q_iso values indicate strong adsorbate–adsorbent interactions, typically associated with microporous structures or the presence of specific active sites, while lower values reflect weaker physical adsorption. Moreover, Q_iso is crucial for evaluating the regeneration energy requirements of sorbents and for assessing their practical applicability in cyclic adsorption–desorption processes, such as CO₂ capture.

The isosteric heat of adsorption was calculated using Clausius—Clapeyron Equation (8):

$$Q_{iso}=-R{\left({\displaystyle \frac{\partial \mathrm{l}\mathrm{n}\left(p\right)}{\partial \left(\frac{1}{T}\right)}}\right)}_{\theta },$$

(8)

where

R is the universal gas constant,

T is the temperature, p is the pressure,

θ is the degree of surface coverage.

After integrating Equation (8), a linear function is obtained (9):

$${\ln \left(p\right)}_{\theta }=-{\displaystyle \frac{Q_{iso}}{R}}{\displaystyle \frac{1}{T}}+C$$

(9)

Plots of the logarithm of equilibrium pressure versus the reciprocal of temperature were constructed for several fixed surface coverages (adsorption isosteres), as shown in Figure 8.

The isosteric heat of adsorption (Figure 9) ranged from 22 kJ/mol for the low surface coverage. These values confirmed that CO₂ adsorption on the C_K₂CO₃_800 proceeds predominantly through a physical mechanism. A gradual decrease in the isosteric heat with increasing surface coverage reflects the weakening of interactions between CO₂ molecules and the carbon surface. CO₂ is bound mainly through van der Waals forces, which explains its relatively easy desorption from the adsorbent surface.

3. Materials and Methods

3.1. Materials

Analytical-grade reagents, including K₂CO₃—activating agent and hydrochloric acid (35–38%, Chempur, Łódź, Poland), were used. Activated biocarbons were synthesized using avocado seeds as the carbon precursor. The seeds were dried at 60 °C for 24 h and ground.

3.2. Synthesis of Activated Carbons

Twelve activated biocarbons were produced from avocado seed powder under various conditions, as summarized in

Table 8. Preparation conditions and sample designations of activated biocarbons obtained from avocado seeds using K₂CO₃ as the activating agent.

Sample Name	Form of Activating Agent	Carbon Source to Activating Agent Ratio	Carbonization/Activation Temperature
C_K2CO3_750	K2CO3 solution	1:1	750
C_K2CO3_800	K2CO3 solution	1:1	800
C_K2CO3_850	K2CO3 solution	1:1	850
C_K2CO3dry_750	K2CO3 dry	1:1	750
C_K2CO3dry_800	K2CO3 dry	1:1	800
C_K2CO3dry_850	K2CO3 dry	1:1	850
C_K2CO3_0.5_850	K2CO3 solution	1:0.5	850
C_K2CO3_1.5_850	K2CO3 solution	1:1.5	850
C_K2CO3_2_850	K2CO3 solution	1:2	850
C_K2CO3dry_0.5_850	K2CO3 dry	1:0.5	850
C_K2CO3dry_1.5_850	K2CO3 dry	1:1.5	850
C_K2CO3dry_2_850	K2CO3 dry	1:2	850

and illustrated schematically in Figure 10.

The dried and powdered avocado seeds were impregnated with either a saturated solution of K₂CO₃ or dry K₂CO₃. Different mass ratios of avocado seeds to the activating agent were applied (Table 8). The samples prepared using the K₂CO₃ solution were dried in a dryer at 190 °C prior to carbonization. Combined carbonization and chemical activation were carried out in a tubular furnace at various temperatures (Table 8) for 1 h under a continuous nitrogen flow. The resulting materials were subsequently washed with 1 M HCl and rinsed with distilled water until a neutral pH was reached.

3.3. Sample Characterization

The porous structure of the synthesized activated carbons was characterized by N₂ adsorption–desorption measurements at −196 °C (ASAP 2460, Micromeritics, Norcross, GA, USA), from which the specific surface area (S_BET), total pore volume (V_tot), micropore volume (V_micro), and pore size distribution were evaluated. The specific surface area (SBET) was determined using the Brunauer–Emmett–Teller (BET) model within the relative pressure range of 0.05–0.30, typically suitable for nonporous and mesoporous materials. Given that the investigated carbons were mainly microporous, the modified BET evaluation proposed by Rouquerol et al. [40] was employed. This approach ensures the physical relevance of the BET parameters by satisfying two conditions: (i) a positive BET constant (C > 0) and (ii) a monotonic increase in the V(1 − p/p₀) function with p/p₀. The total pore volume was assessed from the nitrogen adsorption capacity at relative pressures close to unity. Micropore volume and pore size distribution were subsequently derived through density functional theory (DFT) analysis of the N₂ isotherms, assuming slit-like pore geometry.

Adsorption isotherms were collected volumetrically with an ASAP 2460 analyzer (Micromeritics, Norcross, GA, USA). CO₂ adsorption was studied over the temperature range of 0–30 °C, while N₂ adsorption was evaluated at 20 °C and pressures up to 1 bar.

X-ray diffraction (XRD) patterns of the activated carbons were collected on a PANalytical Empyrean diffractometer (X’Pert–PRO, Panalytical, Almelo, The Netherlands, 2012) operated with Cu Kα radiation to assess their crystalline structure.

4. Conclusions

Activated biocarbons were successfully synthesized from avocado seeds using potassium carbonate (K₂CO₃) as an activating agent. The results demonstrated that K₂CO₃ can serve as an efficient, environmentally friendly, and non-corrosive alternative to the traditionally used KOH, while still enabling the formation of highly microporous carbon materials with excellent adsorption performance. The sample C_K₂CO₃_800, prepared using a saturated aqueous K₂CO₃ solution at an activation temperature of 800 °C and a 1:1 precursor-to-activating-agent ratio, exhibited the highest CO₂ adsorption capacity of 6.26 mmol/g at 0 °C and 1 bar.

The CO₂ adsorption capacity of 6.26 mmol/g obtained in our work is fully consistent with the expected performance of K₂CO₃-activated carbons derived from avocado seeds. Values above 6 mmol/g are generally considered high for this activation system. The material described in [19], which shows an exceptionally high uptake of 7.18 mmol/g, was produced from spent coffee grounds, a precursor with a substantially higher oxygen content and significantly greater reactivity toward K₂CO₃, which strongly promotes the development of a very large volume of ultramicropores (<0.5 nm). In contrast, avocado seeds contain more lignin and ash and therefore develop a less extreme ultramicroporous structure under identical activation conditions.

Thus, the difference in CO₂ uptake arises primarily from the distinct precursor chemistry and the associated mechanisms of textural development. The value of 6.26 mmol/g reported in this work is high for avocado seed-based carbons activated with K₂CO₃ and lies within the upper range typically observed for this activation system.

Textural analysis revealed that the outstanding CO₂ uptake of this material was associated with the predominance of ultramicropores (0.3–0.7 nm), which are particularly effective for CO₂ molecule confinement. Although samples activated at higher temperatures showed a greater total pore volume, this did not directly translate into higher CO₂ adsorption, confirming that pore size distribution—rather than surface area alone—plays a decisive role in determining sorption efficiency.

The adsorption equilibrium data were best described by the Sips model, confirming the heterogeneous nature of the surface of the investigated carbons. The CO₂/N₂ selectivity analysis based on the Ideal Adsorbed Solution Theory (IAST) indicated high separation performance, with equilibrium selectivity values up to 18 at low pressures and 11–14 under flue-gas-like compositions. The isosteric heat of adsorption, ranging from 22 to 26 kJ/mol, confirmed the predominance of physisorption, ensuring good regenerability of the sorbent.

Overall, the study confirms that avocado seed-derived activated carbons prepared with K₂CO₃ are promising candidates for CO₂ capture applications. Their combination of high adsorption capacity, good selectivity, and sustainable synthesis route based on a renewable precursor highlights the potential of this approach for the development of efficient, low-cost, and environmentally responsible sorbent materials.