Three classes of amine‐modified sorbents. Class 1 sorbent: polyethyleneimines (PEI) impregnated in porous materials. Class 2 sorbent: amines covalently tethered through silane linkages. Class 3 sorbent: in situ aziridine polymerization on a solid material.142

Three classes of amine‐modified sorbents. Class 1 sorbent: polyethyleneimines (PEI) impregnated in porous materials. Class 2 sorbent: amines covalently tethered through silane linkages. Class 3 sorbent: in situ aziridine polymerization on a solid material.142

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The urgency to address global climate change induced by greenhouse gas emissions is increasing. In particular, the rise in atmospheric CO2 levels is generating alarm. Technologies to remove CO2 from ambient air, or “direct air capture” (DAC), have recently demonstrated that they can contribute to “negative carbon emission.” Recent advances in surfa...

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... Based on the sorption mechanism, CO 2 can either be captured through physisorption or chemisorption. 4 Physisorption relies on physical interactions between CO 2 and a sorbent. The regeneration temperature of physisorption-based sorbents is relatively low (<100 C), 5 but the weakness of physical interactions also makes it challenging to capture CO 2 effectively from the dilute source. ...
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... Absorbents and adsorbents are key components of the DAC process system and their performance directly affects the overall cost and efficiency of the process. Thus, the technological maturity of DAC in general is still low and the application of this innovative solution is in its infancy [20]. ...
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... To address these challenges, researchers have successfully synthesized task-specific ILs by incorporating suitable moieties into conventional ILs, thereby enhancing their absorption capacity. While detailed synthesis methods of ILs have been previously summarized in reviews [37][38][39], the focus of this review article will lie in exploring the diverse applications of ILs, rather than delving extensively into the synthesis procedures. ...
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... In der Desorptionskolonne kommt es auf Grund der höheren Temperatur zu einem noch größeren Verlust an Waschmittel in die Gasphase, welches dann über den CO 2 -reichen Gasstrom aus der Regenerationsstufe ausgetragen wird. Zusätzlich entzieht der Phasenwechsel dem System Energie in Form der Verdampfungsenthalpie [20]. Trotz einer nachgelagerten Kondensation zur Waschmittelrückführung wird ein Teil des Waschmittels über die Abgase in die Umgebungsluft freigesetzt [21]. ...
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... was taken into account for the experiment. As per Stein (2022) and Shi et al. (2020) concentration of atmospheric carbon dioxide (CO 2 ) in air is in range of 410-421 ppm. Concrete specimens 500 × 100 × 100 mm 3 and 150 mm cube was tested for flexural and compressive strength as per the Indian standards [IS 516:2014]. ...
... An example of such technology is steam methane reforming used for the H 2 production [32]. However, in most cases it is, of course, necessary to take up СО 2 at low temperatures close to the ambient temperature [5,[19][20][21][22][23][24][25][26][27]. The lower is the temperature required for the regeneration of a low-temperature sorbent, the more cost-effi cient will be the process. ...
... To solve the problem of the loss of the volatile amine when using traditional aqueous amine solutions, nonvolatile amine-containing chemisorbents have been suggested. These sorbents have a polymeric structure or are organic salt melts (ionic liquids); after the reaction with CO 2 , they can be regenerated at low temperatures (about 100°С) [21,23]. However, the majority of such materials are very viscous [50,51], which can considerably reduce the rate of the CO 2 sorption due to diff usion hindrance. ...
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... For large-scale applications, water immersion or spraying is also often applied to ensure rapid humidification of the sorbents 14,15 . The humidification operation necessitates not only a large amount of water but also stringent water-quality requirements to prevent hetero-ion contamination and maintain the integrity of the functional groups (CO3 2-) 10 . These limitations substantially increase the cost of MSDAC technology and hinder its implementation. ...
... , but their performance has not yet improved enough to render MSDAC competitive compared with other DAC technologies17 . Current research on MSDAC has predominantly focused on quaternary ammonium-based AER materials loaded with CO3 2-ions10,13,16,18,19 , but the potential of which to increase CO2 sorption capacity seems nearly exhausted16 . Attempts have been therefore made to explore a wider range of MSDAC sorbents 20 . ...
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... Activated carbon is a widely used physical adsorbent with low cost and good thermal stability. Under low CO2 partial pressure, the adsorption capacity and selectivity of activated carbon are lower than those of zeolite [51] ; under high CO2 partial pressure, activated carbon has strong adsorption capacity, is suitable for pressure swing adsorption, is easy to regenerate, and the adsorption process is reversible. Sethia and Sayari [52] prepared microporous activated carbon materials with a larger nitrogen content, specific surface area, and pore volume. ...
... (2) Combination with coupling agent: Coupling agent is a chemical substance that can be combined with both porous materials and amine-containing compounds. First, the coupling agent is grafted onto the surface of the porous material, and then the amine-containing compound is combined with it [51] . Belmabkhout et al. [64] used the gravimetric method to study the adsorption of CO2, N2 and other gases by triamine-grafted porous expanded mesoporous silica (TRIPE-MCM-41). ...
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