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Summary of clay-based CO2 capture

https://doi.org/10.1016/j.ijggc.2020.103005

Clay based materials have attracted attention for CO2 capture applications due to their potential to overcome issues related to commercial availability, cost, and hydrothermal stability (Wang et al., 2013bb). Clays are cost effective materials that are available abundantly in nature having a molecular structure that comprises a combinatorial sheet of tetrahedral silicates and octahedral hydroxides. These characteristics together with appreciable chemical and mechanical stability make clays appropriate as support materials for CO2 capture (Jozefaciuk and Bowanko, 2002Karahan et al., 2006Roth et al., 2013), though acid or alkaline treatment is often necessary in order to overcome deficiencies related to textural features, which may compromise their application potential (Jozefaciuk and Matyka-Sarzynska, 2006Wang et al., 2014b). This section examines works on various clay – supported PEI sorbent systems based on montmorillonitekaolinitesepiolitesaponitepalygorskitehalloysite, and bentonite.

Formation of BPEI – impregnated clays for CO2 adsorption was reported by Wang et al. (Wang et al., 2014b). The clays were pretreated with either acid or alkali in order to increase surface area and pore volume, and thereby to enhance BPEI impregnation efficiency. The authors examined the suitability of two types of clays, i.e., kaolinite and montmorillonite (MMT). In comparison to other studied systems, MMT treated with 6 M HCl exhibited significantly enhanced surface area and porosity. At 75 °C, the observed CO2 adsorption capacities for MMT with 50 wt% PEI loading were ca. 2.55 mmol g−1 and 3.23 mmol g−1 in dry conditions and at 3% moisture, respectively, coupled also to appreciable cycling and thermal stabilities. Gomez-Pozuelo et al. (Gómez-Pozuelo et al., 2019) developed a series of PEI – impreganated clays, and CO2 capacities of 1.53, 1.52, 1.38, 1.27, and 1.04 mmol g−1 were recorded at 45 °C and 1 bar into palygorskite, saponite, MMT, sepiolite, and bentonite, respectively, after 37 wt% PEI loading.

Vilarrasa-Garcia et al. (Vilarrasa-García et al., 2017b) designed a solid CO2 sorbent based on sepiolite by following initial microwave radiation aided by HNO3 treatment and subsequent PEI impregnation. For such an adsorbent with 30 wt% of BPEI (Mn = 600), a CO2 uptake of ca. 1.70 mmol g−1 was observed at 1 atm and 65 °C. Additionally, high CO2/N2 selectivity value of ca. 440 mol CO2/mol N2 was achieved. Ouyang et al. (Ouyang et al., 2018) presented the fabrication of CO2 adsorbent through the PEI loading into HCl – treated sepiolite clay fibers. Acid treatment of sepiolite clay resulted in the generation of MgO-SiO2 nanowires. The obtained CO2 adsorption capacity at 75 °C and 1 atm was 2.48 mmol g−1 for PEI loading of 50 wt%. This system maintained ca. 98 % of its adsorption capacity after 10 successive adsorption-desorption cycles.

Cai et al. (Cai et al., 2015) reported the functionalization of halloysite nanotubes (HNTs) by PEI impregnation for CO2 capture. Adsorption studies at room temperature (25 °C) revealed a capacity of 1.25 mmol g−1 for 35 wt% PEI loading, with appreciable regenerability for over 50 cycles. In another work, Niu et al. (Niu et al., 2016) reported a nanocomposite adsorbent designed by impregnating PEI into pre-treated HNTs for CO2 capture. HNTs pre-treatment, which included calcination and subsequent HCl treatment, resulted in generation of silica mesoporous nanotubes with enhanced specific surface area and pore volume. After PEI impregnation, this material displayed an adsorption uptake of ca. 2.75 mmol g−1 at 85 °C for 50 wt% PEI. Also, cyclic analysis underlined the promising regenerability for this adsorbent. An uptake of 7.84 mmol g−1 was reported by Taheri et al. (Taheri et al., 2019) at 9 bar and 20 °C for a nanocomposite adsorbent consisting of 30 wt% PEI (Mn = 800) – modified silica mesoporous nanotubes, Notably, the drop in adsorption performance was limited to only 5 % after 15 adsorption-desorption cycles.

A PEI/bentonite composite adsorbent was prepared by Chen et al. (Chen et al., 2013a). Analysis at 75 °C and 1 bar revealed an adsorption capacity of ca. 1.07 mmol g−1 after the infusion of 30 wt% of PEI, versus ca. 0.14 mmol g−1 for the neat bentonite, with promising CO2/N2 selectivity and regenerability. In another study, Vilarrasa-Garcia et al. (Vilarrasa-García et al., 2017a) reported the preparation of porous heterostructures from bentonite and then carried out PEI functionalization for CO2 capture application, where PEI contributed to capture CO2 by chemical means through the reaction of the amine groups with CO2. Analysis at 25 °C and 1 bar unveiled an adsorption capacity of 1.47 mmol g−1 for 60 wt% of BPEI loading (Mn = 600). Table 3 provides summarized adsorption performance data for the various clay – supported PEI CO2 sorbents.

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