Facilely synthesized mesoporous polymer for dispersion of amino acid ionic liquid and effective capture of carbon dioxide from anthropogenic source
Graphical abstract
Introduction
The carbon cycle of the earth has been broken for centuries due to the anthropogenic emission of carbon dioxide (CO2), especially energy harvesting process [1,2]. As a result, the concentration of CO2 in the atmosphere has risen to an unprecedent level. CO2 is a kind of greenhouse gas, and its accumulation in the atmosphere may lead to many climatic and environmental problems, including global warming, sea level elevating, green land degradation, etc.. Given this situation, the capture of CO2 from anthropogenic source is proposed as a solution [3]. Currently, the most widely employed method for CO2 capture in the industry is scrubbing with aqueous alkanolamines [4]. However, aqueous alkanolamines are very volatile, making the loss of solvents and consumption of energy considerably high. Besides, aqueous alkanolamines are very corrosive, making the investment on facilities and cost for maintenance also considerably high. Therefore, it is of great significance to explore alternatives to aqueous alkanolamines for application in CO2 capture.
In recent years, ionic liquids (ILs) have attracted widespread interest as a new class of green solvents [5,6]. They are organic salts with the melting points at around or below room temperature, and have unique characteristics such as wide liquidus range and extremely low volatility. One of the most promising applications of ILs is in gas separation [7], [8], [9], [10], [11], [12], which provides an opportunity to address the volatile issue associated with traditional solvents. At the end of 20th century and beginning of 21st century, researchers determined the solubilities of CO2 in many ILs [13], [14], [15], [16], [17]. It was found that the solubilities of CO2 in ILs are much higher than those of other inert gases such as N2 and CH4, which establishes the fundament of CO2 capture with ILs. However, normal ILs enable only physical absorption of CO2, which is unsatisfying for the capture of CO2 from anthropogenic source, the content of CO2 in which is normally low [3]. Therefore, ILs enabling reversible chemical absorption of CO2 are highly required.
Another interesting characteristic of ILs is adjustable chemical structure, because the combinations of anions and cations for ILs can be changed, and various functional groups can be grafted to the frameworks of ILs [18]. Based on this characteristic, researchers developed many kinds of functionalized ILs enabling reversible chemical absorption of CO2, such as carboxylate-based ILs [19,20], amine-functionalized ILs [21], [22], [23] and aprotic heterocyclic anion-based ILs [24], [25], [26], [27]. As a subcategory of amine-functionalized ILs, amino acid ILs (AAILs) are particularly attractive because of the low cost and biocompatibility of amino acids [28,29]. However, the practical application of AAILs in CO2 capture is still greatly limited by their high viscosities. In addition, AAILs suffer from dramatical increase in viscosities after CO2 absorption. The viscous issue makes the capture of CO2 by AAILs very slow, and the transportation of AAILs in pipelines very difficult. To address this issue, researchers diluted AAILs in other low-viscous solvents for CO2 capture [30,31]. Nonetheless, the possible employment of volatile solvents diminishes the advantage of AAILs with extremely low volatility, and the corrosive issue associated with AAILs is still not addressed.
Instead, AAILs can also be dispersed in porous supports to overcome the viscous and corrosive issues of AAILs [32,33]. With such method, the capture of CO2 by AAILs can be enhanced by increasing the efficiency for contact between AAILs and CO2. Moreover, the transportation of AAILs in pipelines, and the direct contact of AAILs with metal facilities are avoided. The performance of dispersed AAILs for CO2 capture is greatly dependent on the porous structure of supports. In this regard, supports with rich mesoporosity and large pore volume are most preferred, because the rich mesoporosity is favorable for the good dispersion of AAILs, and the large pore volume is favorable for the accommodation of more AAILs. Besides, the synthesis of AAILs and porous supports should be as simple as possible from the perspective of practical application.
In this work, a mesoporous polymer−polydivinylbenzene (PDVB)−that can be facilely synthesized by a one-step solvothermal route without the use of any templates [34], was used as the support of AAILs for CO2 capture. A simple AAIL−tetraethylammonium glycinate ([N2222][Gly]) was synthesized for dispersion in PDVB by physical impregnation according to the literature [35], [36], [37], [38], [39]. The chemical structures of PDVB and [N2222][Gly] are shown in Scheme S1. The prepared [N2222][Gly]@PDVB samples were then systematically characterized and investigated for CO2 capture performance. To simulate the anthropogenic source of CO2 emission, low-content CO2 balanced in N2 was used for investigation.
Section snippets
Experimental
See the Supplementary Material.
Characterization results
In this work, four [N2222][Gly]@PDVB samples with different [N2222][Gly] loadings were prepared. The actual [N2222][Gly] loadings of [N2222][Gly]@PDVB samples were estimated by TGA, as shown in Fig. 1. It can be seen that PDVB does not show obvious weight loss until ~380 °C. However, [N2222][Gly] starts to show obvious weight loss at ~150 °C, and the weight loss almost completes at ~380 °C. Therefore, [N2222][Gly]@PDVB samples show two steps of weight loss: the first step starts at ~150 °C,
Conclusions
In summary, a mesoporous polymer—PDVB was used as the support of a simple AAIL—[N2222][Gly]) for CO2 capture. The unique mesoporosity of PDVB enables the good dispersion of large amount of [N2222][Gly]. As a result, [N2222][Gly]@PDVB samples have strong ability for the selective adsorption of dilute CO2 from N2 at elevated temperature. The CO2 capacities of [N2222][Gly]@PDVB samples are higher than those of most other solid-dispersed ILs. The utilization ratios of dispersed [N2222][Gly] for CO2
Declaration of Competing Interest
The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.
Acknowledgements
This work was supported by the National Natural Science Foundation of China (22008033) and Natural Science Foundation of Jiangxi Province (20192ACB21016).
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