Defect engineering on constructing surface active sites in catalysts for environment and energy applications

Yawen Cai, Baowei Hu, Xiangke Wang

Front. Chem. Sci. Eng. ›› 2024, Vol. 18 ›› Issue (7) : 74.

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Front. Chem. Sci. Eng. ›› 2024, Vol. 18 ›› Issue (7) : 74. DOI: 10.1007/s11705-024-2427-z

Defect engineering on constructing surface active sites in catalysts for environment and energy applications

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Abstract

The precise engineering of surface active sites is deemed as an efficient protocol for regulating surfaces and catalytic properties of catalysts. Defect engineering is the most feasible option to modulate the surface active sites of catalysts. Creating specific active sites on the catalyst allows precise modulation of its electronic structure and physicochemical characteristics. Here, we outlined the engineering of several types of defects, including vacancy defects, void defects, dopant-related defects, and defect-based single atomic sites. An overview of progress in fabricating structural defects on catalysts via de novo synthesis or post-synthetic modification was provided. Then, the applications of the well-designed defective catalysts in energy conversion and environmental remediation were carefully elucidated. Finally, current challenges in the precise construction of active defect sites on the catalyst and future perspectives for the development directions of precisely controlled synthesis of defective catalysts were also proposed.

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Keywords

defect engineering / vacancy / void defects / doping / single atomic sites

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Yawen Cai, Baowei Hu, Xiangke Wang. Defect engineering on constructing surface active sites in catalysts for environment and energy applications. Front. Chem. Sci. Eng., 2024, 18(7): 74 https://doi.org/10.1007/s11705-024-2427-z
Carbon dioxide (CO2), an anthropogenic greenhouse gas, contributes to global warming and climate change with its rising concentrations in the atmosphere as a result of fossil fuel combustion. CO2 capture has thus received special attention in the field of environmental science, which can be done by capturing CO2 from point sources or the air. The captured CO2 will then be either utilized or stored. The efficient adsorbent materials are necessary for the effective CO2 capture. So far, a variety of CO2 adsorbents are available, including carbon-based materials, metal oxides, covalent organic frameworks, metal-organic frameworks, silica, and polymers. A special attention is paid to carbon-based adsorbents due to their cost-effectiveness, stability, and environmental friendliness. Especially, biochar is a fascinating CO2 adsorbent because its manufacture could cut CO2 emissions by avoiding the open space combustion of agricultural and domestic wastes, i.e., the sources of biochar. Besides, this leads to the conversion of waste into valuable material (circular economy through sustainable waste management). In line with the life cycle analysis, preparing biochar from waste materials promotes environmental sustainability with a reduced environmental impact. According to the United States Environmental Protection Agency, improper food waste management emits 170 million MT of CO2-equivalent greenhouse gases each year, which is equivalent to the annual CO2 emissions of 42 coal-fired power plants [1]. Therefore, preparing biochar from carbonaceous waste and using it as CO2 adsorbent is advantageous, i.e., getting two mangoes with one stone (carbon abatement and sustainable management).
A wide range of carbon resources (e.g., biomass wastes, municipal wastes, plastic wastes, food wastes, municipal wastes) provides the platform to tune the characteristics and CO2 adsorption capacity of biochar simply by varying its carbon source. Also, many synthetic methods (hydrothermal carbonization, gasification, pyrolysis, and torrefaction) are available for preparing biochar, which can also have impacts on the properties of biochar [2]. This variety of sources and preparation methods highlights an excellent opportunity to develop a highly efficient CO2 adsorbent in the coming years.
Biochar has inherent microporosity and specific functional groups (e.g., C=O and –OH), which are required for the physisorption and chemisorption of CO2, respectively. Biochar’s macropores and mesopores facilitate CO2 diffusion and transportation but not adsorption (Fig.1). Unlike other adsorbents, biochars can be easily activated by increasing microporosity, surface area, and functional groups to enrich the active sites for enhanced CO2 adsorption. Biochars are activated either physically (using steam or CO2) or chemically (using alkali or acid). Zhang et al. [3] made biochar from wood pellets and activated it separately using steam (physical) and KOH (chemical). Chemical treatment improves microporosity in a better way; hence biochar activated by the chemical approach has a higher CO2 absorption (50.75 mg·g−1) than biochar activated by the physical method (38.30 mg·g−1) under the same conditions. Although yielding biochar with a higher adsorption capacity, the chemical treatment may release secondary contaminants [3]. Zhang et al. [4] used a unique activation approach that involved impregnating bamboo-derived biochar with lignin and then treating it with the microwave. As a result, activated biochar has a better porosity and a CO2 uptake of 134.46 mg·g−1. Luo et al. [5] also used the microwave to install micropores in biochar made from marine biomass.
Fig.1 Porosity in biochar and mechanism of CO2 adsorption over biochar.

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To achieve maximum CO2 adsorption, the synergistic interplay of physisorption and chemisorption is essential, underlining the combined presence of active sites for physisorption (microporosity) and chemisorption (functional groups) in biochar. As the functional groups located in the pore walls may block the micropores [6], it is important to have functional groups without interrupting microporosity. Chemisorption dominates at both low and high-pressure conditions whereas physisorption dominates usually at the enhanced pressure. On the contrary, the higher temperature does not favor physisorption, attributing to the desorption of physisorbed CO2 molecules due to their weak interaction with active sites. Therefore, optimizing adsorption conditions and porosity of biochar is essential to establish a better synergism between physisorption and chemisorption. Like enriching microporosity simply by physical and chemical activation methods, the functional groups, in addition to the inherent groups, can be introduced into biochar by facile methods. Especially, enriching the nitrogen-based functional groups is attractive due to their basicity that facilitates the Lewis acid-base interaction with CO2 and promotes the adsorption of CO2 (Fig.1). With proper biomass source selection (e.g., microalgae), the intrinsic nitrogen groups in biochar can be obtained without extra treatment [7]. For example, biochar made from Enteromorpha, a marine biomass, contains basic nitrogen groups (e.g., pyridinic-N, pyrrolic-N, and graphitic-N) that aid in CO2 adsorption through chemical interactions [5]. Also, nitrogen groups can be added through the co-carbonization of carbon and nitrogen compounds (e.g., urea). Special emphasis is given to amine-modified biochar adsorbents because the amine groups involve strong and selective interaction with CO2 molecules, forming carbamates [7]. Ji et al. [8] created a biochar-silica hybrid material with amine groups connected to silica rather than biochar, utilizing siloxane linkers with numerous amine groups. A linker molecule comprises three amine sites, which enables the increased CO2 adsorption.
The compatibility of biochar with both inorganic and organic materials enables the formation of a synergistic hybrid composite for optimal CO2 adsorption efficiency. Because of their basicity, alkaline earth metal oxides (e.g., magnesium) are frequently added to biochar, allowing for both physisorption and chemisorption of CO2. Pu et al. [9] added MgO into walnut shell-derived biochar to improve dynamic CO2 uptake. Fortunately, many biomass sources contain alkali earth metals in their structure. For example, tamarind bark contains calcium oxalate, which can be used to make biochar with a high calcium content for good CO2 adsorption [10]. Similarly, organic molecules (e.g., ionic liquids) capable of CO2 chemisorption are mixed into biochar, resulting in effective composite materials. Arjona-Jaime et al. [11] created a biochar-ionic liquid composite that shows 90% better efficiency and faster kinetics than the bulk ionic liquid. As stated above, physisorption dominates at high pressure.
As known, biochar materials exhibit different CO2 adsorption capacities depending upon the nature of their biomass sources. Interestingly, the same biochar could also display different CO2 capacity values according to the conditions like CO2 concentration, temperature, and competitive adsorbates. The CO2 concentration usually reveals positive impacts on the CO2 adsorption capacity of biochar, i.e., the CO2 adsorption capacity increases with the concentration of CO2. For instance, Ding and Liu [12] studied the CO2 adsorption capacity of SCK-800-1 (a biochar prepared using KOH and sargassum with 1:1 weight ratio at 800 °C) under various CO2 concentrations (3%, 8%, 12%, and 18%) without changing the feed flow rate of total flue gas. As shown in Fig.2(a), the breakthrough times decrease from 6.6 to 5.1 min while increasing CO2 concentration from 3% to 18%. This is because the higher CO2 concentration allows more CO2 molecules to pass via the reactor per unit time, enabling the faster saturation of active sites. Notably, the CO2 adsorption capacity of SCK-800-1 enhances from 0.23 to 1.08 mmol·g−1, with the increase of CO2 concentration from 3% to 18%, which is attributed to the increase of CO2 concentration gradient and the resultant CO2 mass transfer rate. The authors also studied the variation of CO2 adsorption capacity with temperature. The adsorption capacity of SCK-800-1 is maximum (1.05 mmol·g−1) at 25 °C. With the increase in temperature, the CO2 adsorption capacity gradually decreases and reduces to 0.45 mmol·g−1, at 100 °C. This is because the rise in temperature increases the surface energy and the molecular diffusion of CO2 on the biochar’s surface. As a result, the adsorption force of biochar is reduced for CO2, increasing the chance of CO2 desorption at elevated temperatures [12]. Though this seems a common trend in the literature, exceptions cannot be excluded based on the modification or activation carried out on biochar materials [5]. Like CO2 concentration and temperature, humidity can also have a significant impact on the CO2 adsorption capacity. Especially, the CO2 adsorption capacity of hydrophilic biochar (i.e., activated with oxygen-related polar functional groups) gradually loses its CO2 adsorption capacity with the increase of humidity. As illustrated in Fig.2(b), the increase in humidity levels does not have a significant impact on the CO2 adsorption capacity of wood-derived raw biochar (BC-Raw), as biochar adsorbs 1.3 and 0.85 mg·g−1 CO2 at 8.8% and 87.9% relative humidity (RH) levels, respectively. However, for the KOH-activated biochar (BC-KOH1:1) containing more polar functional groups, the impact of humidity is apparent, i.e., the CO2 adsorption capacity of BC-KOH1:1 decreases from 3.7 to 1.3 mg·g−1 when increasing RH from 8.8% to 87.9%, respectively [3]. This might be due to the strong interaction between the hydrophilic polar groups of biochar and water. Hence, preparing biochar materials with hydrophobic and non-polar properties is important to limit the competitive adsorption of water molecules and realize the practical applications of biochar.
Fig.2 (a) CO2 breakthrough curves of SCK-800-1 at various CO2 inlet concentrations [12]. Reprinted with permission from ref. [12], copyright 2020, Elsevier. (b) 15% CO2 adsorption ability of wood-derived biochar (BC) samples at different relative humidity (RH) levels [3]. Reprinted with permission from ref. [3], copyright 2022, Elsevier. (BC-Raw: wood-derived raw biochar; BC-Steam: steam activated biochar; BC-KOH1:1: KOH activated biochar; BC-KOH-lmp: biochar actirated with KOH by impregnation) (c) Multicomponent breakthrough curves of CO2, NO, and SO2 through LBB20 (a kind of biochar) at 25 °C [4]. Reprinted with permission from ref. [4], copyright 2024, Springer Nature. (d) Unique advantages of biochar materials for CO2 adsorption.

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Both flue gas and open air are a mixture of multiple gases, including CO2. Therefore, to realize the practical applications, biochar materials should achieve the selective adsorption of CO2. In the literature, the CO2 adsorption selectivity of biochar is studied in the presence of various gases like N2, NOx, SOx, etc. In general, the typical flue gas from coal-fired power plants possesses 10%–16% CO2, and small traces of NOx, and SOx. So, Zhang et al. [4] prepared a gas mixture (CO2-12 vol %, NO-0.4 vol %, and SO2-0.4 vol %) for a multicomponent competitive adsorption experiment using a biochar (LBB20). During the individual gas adsorption experiments, LBB20 adsorbs 28.50 mg·g−1 CO2, 0.24 mg·g−1 NO, and 50.10 mg·g−1 SO2 under identical conditions. While using the prepared multicomponent gaseous mixture, the adsorption capacity of LBB20 is invariably declined for CO2 (23.70 mg·g−1), NO (0.14 mg·g−1), and SO2 (45.06 mg·g−1). Owing to its small size and dynamic diameter, NO quickly passes the column. Both CO2 and SO2 slowly reach the active site and replace weakly adsorbed NO molecules, as supported by the increasing outlet concentration of NO. Unlike NO, SO2 demonstrates an adverse effect on CO2 adsorption because both SO2 and CO2 display an acidic nature and involve competitive adsorption. However, the faster movement of CO2 could allow the reduction of CO2 adsorption capacity only by 16.8% even in the presence of SO2 (Fig.2(c)) [4]. This might be assigned to the lignin impregnation of biochar at a suitable quantity which selectively enhances the mobility of CO2 inside the pore channels. Therefore, a higher selectivity for CO2 adsorption is possible by modifying raw biochar using suitable methods. The selective adsorption of CO2 from N2 is equally important for the post-combustion CO2 capture and direct air capture. At low pressures, the biochar materials achieve a higher CO2 adsorption selectivity due to the dominant role of their functional groups and non-reactive adsorption of N2. Differently, while increasing the pressure, the CO2 adsorption selectivity is gradually decreased owing to the dominant role of pore filling and eventually reaches the stable selectivity [13]. During the competitive adsorption between CO2 and CO over biochar materials, achieving a maximum CO2 adsorption selectivity is not difficult due to the easy and complete removal of weakly adsorbed CO molecules by CO2 molecules even with 50% CO concentration [14]. These reports suggest that biochar selection, biochar modification, and adsorption conditions can control the CO2 adsorption selectivity. However, attaining the maximum CO2 adsorption selectivity using biochars remains a big challenge because it demands many optimization experiments, especially, in real conditions. To help with this problem, Yuan et al. [15] attempted an active learning strategy for preparing a high-performance engineered biochar by recommending optimal synthesis parameters and feedstocks.
In summary, the following unique characteristics (Fig.2(d)) make biochar an interesting CO2 adsorbent than other adsorbents: (1) low cost, thermal stability, and environmental friendliness; (2) preparation promoting carbon abatement and sustainable management; (3) availability of various precursors; (4) availability of simple preparation methods; (5) ease of activation to enrich microporosity and functionalization; (6) physisorption and chemisorption in synergy; (7) compatibility with organic and inorganic compounds, resulting in highly efficient hybrid adsorbents. Despite these advantages, a few issues must be solved before proposing biochar as a commercial CO2 adsorbent. Biochar regeneration, or CO2 desorption, must take place at a lower temperature, even for nitrogen-rich biochar materials. There have been very few CO2 adsorption experiments with biochar under practical conditions. The real environment comprises complicated gas combinations. Therefore, acidic gases such as SOx and NOx can occupy the basic nitrogen groups of biochar, preventing CO2 adsorption. Humidity, temperature, and pressure are the variables in the environment; hence the CO2 adsorption behavior of biochar materials must be studied under fluctuating humidity, pressure, and temperature conditions, but such studies are rare. Hope these issues will be addressed by rationally designing biochar materials and studying their CO2 adsorption capacity under practical conditions.
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Competing interests

The authors declare that they have no competing interests.

Acknowledgements

We gratefully acknowledge funding support from the National Science Foundation of China (Grant No. 22306124), the Beijing Outstanding Young Scientist Program.

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