Tailored N-doped porous carbons via a MOF assembly process for high-performance CO 2 uptake †

Striking a balance between the nitrogen content and pore texture of N-containing metal–organic frame-work (MOF)-derived carbon is a considerable challenge for high-performance CO 2 capture. The high-temperature pyrolysis and activation facilitated well-developed pore structures but resulted in serious nitrogen loss of MOFs. In this work, we developed MOF (ZIF-8)-derived N-doped porous carbons (NPCs) by integrating ZIF-8 with pomelo peel via a co-carbonization and activation process to construct a high-performance CO 2 adsorbent. The pomelo peel can effectively prevent the nitrogen loss from the ZIF-8 backbone via pre-melting and polymerization and simultaneously offer the ideal porosity and BET surface area during the co-carbonization and activation process. By tuning the ZIF-8 loading capacity and the activation temperature, the sample NPC-800-4 prepared at 800 1 C possessed both ultrahigh surface area ( B 1967 m 2 g (cid:2) 1 ) and high N content ( B 13.15 wt%). Particularly, the CO 2 capacity of NPC-800-4 reached 5.51 mmol g (cid:2) 1 at 25 1 C and 9.01 mmol g (cid:2) 1 at 0 1 C under 1 bar due to its relatively high content of pyrrolic-N (N5 B 61.2%) and pyridinic-N (N6 B 16.5%), as well as the proper pore size distribution (0.64 nm). In addition, the TPD measurement and CO 2 adsorption energy ( Q st ) of NPC-800-4 also suggested the high desorption activation temperature and energy, indicating a strong binding capacity toward CO 2 . Moreover, NPC-800-4 exhibited almost constant CO 2 uptake in 8 consecutive adsorption–desorption cycles, indicating that the sample with great stability and recyclability would be easily adapted and recycled from industries. This co-carbonization and activation strategy to assembly MOFs with biomass would pave the way for enhancing CO 2 capture of MOF-derived carbons.


Introduction
Global warming, resulting from the excessive emission of greenhouse gases into the atmosphere, is one of the most serious environmental problems. [1][2][3] Among several greenhouse gases, CO 2 is considered to be the main contributor, which is responsible for about 60% of the greenhouse effect. 4 It is of great importance to reduce the CO 2 concentration in the atmosphere for the alleviation of global warming. For industrial applications, CO 2 capture using aqueous amines is a principal method due to the low cost. 5,6 However, absorption by amine scrubbing suffered from energy consumption, toxicity and equipment corrosion in the regeneration process. To overcome these problems, CO 2 adsorption using solid adsorbents is an attractive alternative, which can be applied under various conditions. Thus, many researchers have focused on the development of solid adsorbents with easy reversibility and low energy requirements for efficient CO 2 capture. For this purpose, porous solid adsorbents including zeolites, carbons, metal organic frameworks (MOF), oxides and covalent organic frameworks (COF) with high surface area and good stability have been extensively studied in the past decades. 7,8 Among all the porous materials, porous carbons are the most attractive candidates for the CO 2 capture due to their advantages of tunable pore structure, low density, high thermal and chemical stability, large specific surface area, low cost and tailored surface functionalization. [9][10][11] In addition, porous carbons 12,13 are not sensitive to water vapor by comparison with other CO 2 -philic materials. As one of the most fascinating materials, N-doped porous carbons (NPCs) exhibited improved wettability and basicity, leading to the enhancement of CO 2 adsorption. 14 A variety of N-doped porous carbon materials have been developed by post-treatment and templating approaches for the CO 2 capture. For instance, biomass-renewable materials such as fir bark, 15 bamboo, 16 pomelo peel 17 and coconut shell 18 have been utilized as NPC precursors to be thermal treated and activated by KOH for pore structure development. However, the preparation of biomass-derived NPCs by post-treatment is less controllable in both porosity and functionality. In contrast, the templating method 6,19,20 is effective for controlling the pore structure and surface chemistry of the NPC. By using the templating method, the obtained NPC could be adapted from the template and additional carbon source, and thus the more ordered pore structure and controllable N-doping gained from the design of the N-containing carbon precursor. [21][22][23] In this context, for improving CO 2 adsorption, it is crucial to survey a suitable carbon precursor to obtain well-developed pore structure and high N-containing NPCs.
As one of the most fascinating precursors of the NPC, the MOF has received much attention owing to its flexible preparation, high surface area, exclusive periodic structure, and abundant C-species in the ligands. [24][25][26][27] In addition, the N-containing ligand could offer the carbonized MOF skeleton functionalized with N-doping. All these unique features make the MOF work not only as a carbon precursor but also as a template to construct NPCs. 28,29 Especially for ZIF-8, a great deal of attention has been paid to develop NPCs from such a N-rich and commercialized MOF to improve CO 2 uptake. [30][31][32] By using ZIF-8 as a template, and furfuryl alcohol and NH 4 OH as additional carbon and nitrogen sources, Xu and co-workers constructed NPCs with a high surface area of 2747 m 2 g À1 and a N content of 2.7% at 900 1C, which exhibited a CO 2 uptake of 3.9 mmol g À1 under ambient condition. 33 Moreover, the direct carbonization of ZIF-8 has been studied by Guo and co-workers, in which the pore structure could be tuned by adjusting the crystal size and the carbonization temperature. 34,35 By carbonization of ZIF-8 at 700 1C, 35 the resultant NPC exhibited a CO 2 uptake of 3.8 mmol g À1 of under ambient condition. Besides the abovementioned, the activation method also adapted to tune the pore structure of ZIF-8-derived NPCs. 36,37 By activation with KOH, Xia and co-workers developed ZIF-8derived NDCs with higher textural properties (specific surface area B3700 m 2 g À1 ) but lower CO 2 adsorption (2.61-2.83 mmol g À1 ) and N content (5.3%), compared with the direct carbonized ZIF-8. 37 From the literature, we found that although ZIF-8 has been utilized with nitrogen-enriched ligands, well-defined crystal size, proper pyrolysis parameters and additional nitrogen sources, the CO 2 uptake of ZIF-8 derived NPCs are still not satisfying. It is still a big challenge to develop high-performance CO 2 adsorbents based on ZIF-8-derived NPCs.
For obtaining ideal CO 2 capacity, the two main factors (pore size and N-containing) of ZIF-8-derived NPCs should be precisely controlled. 10,38 On the one hand, because the CO 2 adsorption capacity largely depends on the microporosity ranging from 0.5 to 0.8 nm, the enhancement of effective pore diameter is very important. 38,39 On the other hand, both pyrrolic-N and pyridinic-N exhibited basicity, which could serve as an active site to adsorb CO 2 by acid-base and hydrogen-bonding interactions, respectively. 10,40,41 Thus, increasing the amount of pyrrolic-N and pyridinic-N groups could improve the CO 2 uptake of ZIF-8-derived NPCs. In other words, the CO 2 uptake quantity is correlated with the effective porosity (0.5-0.8 nm) and enough content of pyrrolic-N and pyridinic-N in ZIF-8-derived NPCs. As one of the most effective and regular strategies, the activation method is effective to facilitate the regulation of the pore size around 0.5 to 0.8 nm and tune the BET surface area. 42 However, the high temperature of activation process always caused a serious loss of pyrrolic-N and pyridinic-N in ZIF-8-derived NPCs. 43,44 Therefore, for improving CO 2 adsorption, how to strike a balance between effective nitrogen content and pore texture of ZIF-8-derived NPCs is a fundamental task.
In this work, we selected N-containing pomelo peel as a secondary carbon and nitrogen source to assemble with N-rich ZIF-8 for the preparation of ZIF-derived NPCs by co-carbonization and activation, in which the pomelo peel not only offers additional pores, carbon and nitrogen, but also prevents nitrogen loss from the ZIF-8 backbone through pre-melting and polymerization during high-temperature (800 1C) treatment. By tuning the assembly amount of ZIF-8 and the co-carbonized temperature, NPC-800-4 exhibited a well-maintained N-content of pyrrolic-N (61.2%) and pyridinic-N (16.5%), which served as effective activated sites of CO 2 adsorption. Moreover, the porosity of NPC-800-4 is precisely controlled with a size distribution of 0.64 nm and an ultrahigh BET surface area of 1967 m 2 g À1 . The CO 2 capacity of NPC-800-4 reached 5.51 mmol g À1 under ambient condition, which is higher than that of any other ZIF-8-derived NPC. To the best of our knowledge, there is still no comprehensive investigation of biomass materials effect on the prevention of N-loss in MOFs during NPC formation from high temperature so far. The co-carbonization and activation strategy of the ZIF-8 assembled pomelo peel would build the bridge between biomass materials and MOFs, which offered a potentially cost-effective method to improve the CO 2 uptake of NPCs.

Materials
The chemicals 2-methylimidazole (2-Hmim), (Zn(NO 3 ) 2 Á6H 2 O), nitric acid, methanol, and potassium hydroxide were purchased from Aladdin Company, Shanghai, China. The origin pomelo peel was obtained from pomelos of commercial plantation area in Guangxi Province, China. Deionised water was used in the experiment (resistivity Z18.2 MO). All chemical reagents and solvents were used without further purification.

Pre-treatment of pomelo peel
The pre-treatment of pomelo peel was performed according to the literatures. 17,45 First, small pieces of the sponge-like peel were removed from the yellow outer skin of pomelo and washed with water. Then, the as-washed sponge-like peel was placed in an oven at 80 1C for 24 hours to make it dry. The dried pomelo peel was ground in a mortar to get a white powder. Then, 10 g of white powder was put into 1 L of the NaOH (1 M) solution and heated to 80 1C for 3 hours to form a suspension. The suspension was filtered and freeze-dried for 12 hours to get a solid powder. The solid powder was dispersed in 1 L of nitric acid (1 M) at 80 1C for 4 hours to obtain a carboxyl-modified pomelo peel (PP-COOH yield 37%).

Co-Carbonization and activation of ZIF-8-PP
As shown in Scheme S1 (ESI †), 1.0 g of dried ZIF-8-PP-1 composite and 1.5 g of KOH were mixed well and placed in an alumina boat of a tube furnace. First, the mixture was heated to 350 1C under a flow of air to eliminate volatile substances. Then, the furnace was heated to the co-carbonization and activation temperature (600 1C, 700 1C and 800 1C) in a nitrogen atmosphere and maintained at the target temperature for 3 hours in flow nitrogen, and the heating rate was 10 1C min À1 . After cooling down, the resulting mixtures were washed several times with 1 M of HCl at room temperature until the pH reached 7 to remove inorganic species, followed by further washing with distilled water. The as-activated sample was dried in an oven at 100 1C for 24 hours to obtain N-doped porous carbons (NPC-600-1, NPC-700-1 and NPC-800-1, yield around 15%). By using the same method, ZIF-8-PP-2, ZIF-8-PP-3, ZIF-8-PP-4 and ZIF-8-PP-5 could also be co-carbonized and activated by KOH under the same condition, and thus NPC-600-2, NPC-700-2, NPC-800-2, NPC-600-3 NPC-700-3, NPC-800-3, NPC-600-4, NPC-700-4, NPC-800-4, NPC-600-5, NPC-700-5, and NPC-800-5 were obtained. Characterization X-ray diffraction (XRD) measurements were carried out using a Smart Lab diffract meter equipped with a Cu-Ka radiation source (l = 0.154 nm). Raman spectra were recorded using a Renishaw Raman microscope and collected at an excitation laser of 632.8 nm (1.96 eV). The N 2 (77 K) adsorptiondesorption experiments were carried out using a Micrometrics ASAP 2020 instrument. Scanning electron microscopic (SEM) images were obtained using a field emission SEM (JSM-7610F) at an accelerating voltage of 10 kV. Thermogravimetric analysis (TGA) curves were tested using an SDT Q600 Analyzer from 25 to 800 1C in a nitrogen atmosphere. Fourier transform infrared (FT-IR) spectroscopy measurements were performed using a PerkinElmer FT-IR/NIR spectrometer. The measurements of UV absorption of the samples were performed using a PerkinElmer spectrometer.

Characterization of ZIF-8-PP
The choice of biomass materials and MOFs for the assembly process is the key point to form carbon precursors for co-carbonization and activation, and thus obtain NPCs with high BET surface area, ideal pore structure and N content for improving CO 2 adsorption. It has been previously reported that the pomelo peel-derived NPC possessed an excellent BET surface area, nitrogen content and well-designed 3D structure. 17 Our basic idea is to assemble ZIF-8 as an N-rich carbon precursor to integrate with N-containing pomelo peel as the secondary carbon and nitrogen precursor for obtaining NPCs with derived 3D structure, ideal N-content and porosity. Because of the big block, the pomelo peel will pre-melt and polymerize outside the surface of ZIF-8, rather than get into the pore during the co-carbonization and activation process, which may protect the N-content of ZIF-8 backbones from being destroyed by high temperatures.
To demonstrate that ZIF-8 assembled with PP-COOH, as shown in Fig. 1A, we characterized PP, PP-COOH, ZIF-8 crystals and ZIF-8-PP composites by FTIR spectra. Compared to PP, PP-COOH exhibited a typical carboxyl stretching vibration located at 1741 cm À1 of the FT-IR spectrum, indicating that COOH was successfully grafted onto the surface of PP. In Fig. 1B, compared with ZIF-8, ZIF-8-PP composites exhibited similar vibration peaks on the FT-IR spectra. By comparison of PP-COOH, the COOH stretching vibration range of ZIF-8-PP composites around 1740-1750 cm À1 indicated a lower intensity due to the electrostatic attraction and coordination effect 46 between 2-methylimidazole with -COOH on the surface of PP. Thus, the FTIR spectra effectively suggested that ZIF-8 assembled with PP-COOH.
Further investigation of the assembly process was conducted with X-ray diffraction (XRD) patterns to study the structure of ZIF-8, PP-COOH, and ZIF-8-PP composites (Fig. S1, ESI †). From the XRD pattern of PP-COOH, a broad and weak diffraction was detected, suggesting that PP-COOH exhibited an amorphous structure. Compared with the XRD pattern of pure ZIF-8 powder (yellow line), the XRD pattern of ZIF-8-PP composites suggested almost the same diffraction peaks, indicating that ZIF-8 was successfully assembled on the surface of PP-COOH. Moreover, the morphologies of the carboxyl-modified pomelo peel (PP-COOH) and ZIF-8-PP composites were also investigated by SEM in Fig. 2 to demonstrate the assembly process. PP-COOH exhibited soft network structures and micrometer-scaled large pores in Fig. 2A, which is promising as an excellent supporting matrix to encapsulate ZIF-8. From Fig. 2B and C, we could find that ZIF-8-PP-1 and ZIF-8-PP-2 showed lower concentrations of ZIF-8-assembly than ZIF-8-PP-3, ZIF-8-PP-4 and ZIF-8-PP-5, suggesting large pieces of matrix wrinkles on PP-COOH. Fig. 2D-F exhibit an increasing amount of ZIF-8 assembly, in which ZIF-8 crystals are embedded and connected by thin fiber network structures of PP-COOH, indicating a successful assembly process of ZIF-8 with both low and high contents.

Surface properties of NPCs
As shown in Fig. 3, ZIF-8-PP-4 and NPC-800-4 were investigated by a SEM technique to confirm the morphological change during co-carbonization and activation at high temperatures.
We found that ZIF-8-PP-4 suggested a uniform ZIF-8 assembly of PP-COOH with a low magnification in a large range of several layers (Fig. 3B), while NPC-800-4 exhibited 3D porous structures after carbonization and activation at 600 1C, 700 1C and 800 1C. The morphology of ZIF-8 could not be detected in the SEM image of NPC-800-4, indicating that amorphous carbons are formed during co-carbonization and activation process.
As shown in Table 1, the elemental analysis results suggested that with the higher ZIF-8 assembled, the NPC exhibited more N contents, meaning that ZIF-8 played a predominant role for offering N elements of NPCs. The samples treated at high temperatures of 700 1C and 800 1C exhibited minor nitrogen loss compared with the NPC gained at 600 1C, due to the pre-melting and polymerization of PP-COOH covered onto the ZIF-8 surface, thus preventing nitrogen loss from the backbone during co-carbonization and activation process at high temperatures. Moreover, by observation of the CO 2 adsorption quantity, we could find that NPC-800-4 exhibited the higher uptake capacity than other NPCs, but its N content (13.15 wt%) was lower than that of NPC-800-5, indicating that the nitrogen content was not completely related to CO 2 adsorption capacity of NPCs. This result is in accordance with the literature reports, 10 suggesting that only the effective nitrogen species (pyrrolic-N and pyridinic-N) could improve the CO 2 uptake of NPCs.
As shown in Fig. 4, more explanations have been given by XPS measurements to demonstrate the pyrrolic-N and pyridinic-N content of NPC-800-4. Fig. S2 (ESI †) suggested the wide-scan XPS spectra of NPC-800-4, which exhibited the obvious C 1s and N 1s peaks located around 284 eV and 400 eV, respectively. By comparing with the C 1s of ZIF-8-PP-4, we could find that the peak (289 eV) of O-CQO disappeared and the peak (286 eV) of C-N became weaker on C 1s of NPC-800-4, suggesting the carbon and nitrogen loss during the co-carbonization and activation processes. To confirm the temperature influence of co-carbonization and activation, the N 1s XPS spectra of NPC-600-4, NPC-700-4 and NPC-800-4 have been deconvoluted into three peaks including pyridinic N at 398.5 eV, pyrrolic N at 400.1 eV, and quaternary N at 401.5 eV (Fig. 4). In the histogram (Fig. 4D), we find that upon co-carbonization and activation, NPC-800-4 contained 61.2% of pyrrolic-N and 16.5% of pyridinic-N, respectively. The higher quaternary N content of NPC-800-4 suggested that NPC-800-4 exhibited a higher pyridinic-N content than NPC-600-4 and NPC-700-4. This result indicated that the high temperature treatment of ZIF-8-PP-4 may facilitate higher contents of pyrrolic-N in the skeleton of NPC-800-4 and, thus, improve CO 2 capture.   Table 1, increasing the treatment temperature from 600 to 800 1C, the BET specific surface areas of NPC samples obviously increased. For example, the BET surface area of NPC-600-4 is 966 m 2 g À1 , while the BET surface areas of NPC-700-4 and NPC-800-4 are 1312 m 2 g À1 and 1967 m 2 g À1 . The BET surface area is conformed to this order: S BET NPC-800 4 S BET NPC-700 4 S BET NPC-600 , implying that with certain amounts of ZIF-8 assembled, the high temperature of carbonization and activation facilitated the enhancement of the BET surface area of NPCs. Moreover, the assembly amount of ZIF-8 in the composite could also affect the BET surface area of the resultant NPC samples. From the observation of all the NPC samples treated at different temperatures (600-800 1C), we found that when the mass ratios of ZIF-8 and PP-COOH increased from 1 : 1 to 1 : 18, the BET surface area of NPCs gradually enhanced, suggesting that ZIF-8 played an important role to devote the BET surface area during carbonization and activation. However, after increasing the mass ratio of ZIF-8 and PP-COOH to 1 : 27, the BET surface area suggested an obvious decline by comparison of other samples (S BET NPC-800-4 4 S BET NPC-800-5 , S BET NPC-700-4 4 S BET NPC-700-5 , S BET NPC-600-4 4 S BET NPC-600-5 ). This result may ascribe to the incomplete assembly of ZIF-8 on PP-COOH when the concentration of ZIF-8 became higher. Thus, the BET surface area of NPCs is correlated not only with the temperature but also with the amount of ZIF-8 in the composite precursors.    Furthermore, the pore volumes of NPCs gained from different temperatures are shown in Table 1; the total pore volume and narrow micropore (o1 nm) volume of NPC-800-4 exhibited the highest value among all the samples, suggesting that NPC-800-4 may exhibit an excellent CO 2 adsorption capacity. We also studied the pore size distribution based on the DFT equilibrium model ( Fig. 5C and D); the narrow micropore (o1 nm) diameter of NPC-800-4 is B0.64 nm and the mesopore diameter is around 2-3 nm, suggesting the best effect for CO 2 capture. The other NPC samples exhibited narrow micropore (o1 nm) of diameter around 0.5-0.6 nm, or almost no mesopores with a diameter around 2-3 nm could be detected, implying that both mesopores and narrow micropores exerted an effect on CO 2 adsorption. In other words, by tuning the treatment temperatures and the ZIF-8 assembly quantity, the NPC could be gained with an ideal pore structure and pore diameter for improving CO 2 uptake.

CO 2 uptake by NPCs
As shown in Fig. 6, the CO 2 uptake by NPCs gained from 600-800 1C has been evaluated at 25 1C and 0 1C. The detailed data of CO 2 capacity of NPC samples are shown in Table 1. We found that CO 2 adsorption at 25 1C and 0 1C is in the range of 2.57-5.51 mmol g À1 and 3.40-9.01 mmol g À1 , respectively. In general, NPC-800-4 with an ideal pore size (0.64 nm) and N content (13.15%) exhibited larger CO 2 uptake than other samples, which mainly resulted from the synergetic regulation of the ZIF-8 amount and the activation temperature of the carbon precursor and, thus, are beneficial to the adsorption of CO 2 molecules. From Fig. 6, we could find that all the samples of NPCs exhibited an enhancement of CO 2 uptake for all the samples with the increase in pressure at 25 1C and 0 1C. The shape of CO 2 adsorption isotherms also showed a synergetic regulation of pore size based on the factors of ZIF-8 content and activation temperature. In most cases, the NPC gained from higher temperatures suggested bigger pores, and thus exhibited a little lower CO 2 uptake under relatively low pressure. However, in this work, most of the NPCs treated at 800 1C showed higher uptake by comparison of other samples, implying that the precise pore structure and properties of NPC-800-4 were regulated by ZIF-8 quantity and activation temperature for improving CO 2 uptake. As shown in Fig. S4 (ESI †), we could find that carbon samples derived from the mixture of ZIF-8 and pomelo peel, pomelo peel and naked ZIF-8 exhibited 3.04, 2.75 and 2.96 mmol g À1 of CO 2 uptake at 25 1C, whose CO 2 uptake were lower than NPC-800-4, suggesting that the assembly process plays an important role to develop carbonization precursors and thus obtain ideal porosity and N-content of the NPC sample.
As shown in Fig. 7A, the TPD measurements were performed to investigate the strength of interaction between CO 2 molecules and NPC-800-4 and the regeneration temperature of NPC-800-4. The CO 2 desorption peak is around 107.2 1C, which is slightly higher than that of NPC-700-4 (Fig. S5, ESI †), indicating that the desorption energy of NPC-800-4 is higher than that of NPC-700-4. In other words, the higher activation temperature may facilitate stronger combination between the obtained NPC and CO 2 molecules, and thus benefit to improve the CO 2 capacity. Table 2 summarizes several CO 2 capture data and the N content of polymers, biomass-derived and MOF-derived NPCs, suggesting the highest CO 2 capacity of NPC-800-4 among all   To further evaluate the interaction force between CO 2 molecules and NPC-800-4, the CO 2 adsorption energy (heat of adsorption, Q st ) of NPC-800-4 was calculated based on the Clausius-Clapeyron equation using CO 2 adsorption isotherms measured at 25 1C and 0 1C. As shown in Fig. 7B, we could find that isosteric adsorption heat curves for NPC-800-4 were calculated in the range of 25.6-34.7 kJ mol À1 , which was representative for a physisorption course. At low CO 2 uptake, the initial Q st for NPC-800-4 is 32-34.7 kJ mol À1 , which is in the range of typical NPCs and is lower than the previous reported value, 37,40 suggesting the lower energy requirement for regeneration. The recyclability performance of NPC-800-4 was conducted for repeating several adsorptions-desorption cycles at 25 1C under ambient condition. Between each cycle, the NPC-800-4 was heated at 200 1C for 8 h in vacuum. As shown in Fig. S6 (ESI †), the CO 2 uptake exhibited a slight decrease after 8 cycles. Therefore, NPC-800-4 possessed reusability with relatively low energy requirement for regeneration.

Conclusions
In summary, we utilized the assembly process to integrate ZIF-8 with pomelo peel for further co-carbonization and activation to obtain NPC. By tuning the amount of ZIF-8 in the carbon precursor and the activation temperature, the NPC-800-4 exhibited the highest CO 2 uptake of 5.51 mmol g À1 at 25 1C and 9.01 mmol g À1 at 0 1C under 1 bar among all the NPC samples. The high CO 2 uptake of NPC-800-4 resulted from the precise control of the pore size diameter of B0.64 nm, and pyrrolic-N (61.2%) and pyridinic-N (16.5%) contents by using the pomelo peel as secondary carbon and nitrogen precursors, which could prevent nitrogen loss from ZIF-8 during the synthesis of NPCs. Therefore, the assembly of MOFs with biomass materials to form NPC precursors is an effective way to regulate the pore texture, nitrogen content and nitrogen type for effectively improving the CO 2 capture under ambient conditions. By using this method, we could introduce new concepts to combine biomass materials and MOFs as NPC precursors for the further development of highly efficient CO 2 adsorbents.

Conflicts of interest
There are no conflicts to declare. Materials Advances Paper