Department of Applied Science and Technology (DISAT), Politecnico di Torino, Corso Duca degli Abruzzi 24, 10129, Turin, Italy.
Department of Chemical and Geological Sciences, University of Modena and Regio Emilia, Via Giuseppe Campi 103, 4125, Modena, Italy.
J Environ Manage. 2020 Dec 1;275:111229. doi: 10.1016/j.jenvman.2020.111229. Epub 2020 Aug 27.
In this study, the adsorption capacity of the low-cost zeolite clinoptilolite was investigated for capturing carbon dioxide (CO) emitted from industrial processes at moderate temperature. The CO adsorption capacity of clinoptilolite (a commercial natural zeolite) and ion-exchanged (with Na and Ca) clinoptilolite were tested under both dynamic (using a fixed-bed reactor operating with 10% vol. CO in N) and equilibrium conditions (measuring single component adsorption isotherms). The dynamic CO adsorption capacity of bare clinoptilolite and ion-exchanged clinoptilolite were evaluated in the temperature range from 293 K to 338 K and the obtained breakthrough curves were compared with those of the commercial zeolite 13X (Z13X). Although the adsorption capacity of Z13X exceeded those of bare clinoptilolite and ion-exchanged clinoptilolite at 293 K, the clinoptilolite exhibited the highest CO uptake at a moderate temperature of 338 K (i.e. 25 % higher than Z13X). This feature appears in agreement with the lower isosteric heat of CO adsorption on clinoptilolite compared to the other samples. The surface species affecting the q and adsorption capacity were investigated through the FTIR spectroscopy using CO as probe molecule. As a whole, it has been observed that CO forms linear adducts onto K and Mg cations of the bare clinoptilolite, and carbonate-like species onto its basic sites. With the Na-exchanged clinoptilolite, Na ions led to a decrease in surface basicity and to the formation of both single (Na···OCO) and dual (Na···OCO⋯Na) cationic sites available for the formation of linear adducts. As a result of the remarkable adsorption capacity of clinoptilolite at 338 K, this material appears to be a promising adsorbent for the direct CO removal from different flue gases sources operating at such temperatures.
在这项研究中,研究了低成本沸石斜发沸石在中温下捕获工业过程中排放的二氧化碳(CO)的吸附能力。测试了天然斜发沸石(商业天然沸石)和离子交换(用 Na 和 Ca 交换)斜发沸石在动态(使用 10%vol.CO 在 N 中运行的固定床反应器)和平衡条件(测量单组分吸附等温线)下的 CO 吸附能力。在 293 K 至 338 K 的温度范围内评估了裸斜发沸石和离子交换斜发沸石的动态 CO 吸附容量,并将获得的穿透曲线与商业沸石 13X(Z13X)的穿透曲线进行了比较。尽管在 293 K 时,Z13X 的吸附容量超过了裸斜发沸石和离子交换斜发沸石,但在 338 K 的中等温度下,斜发沸石的 CO 吸收量最高(比 Z13X 高 25%)。这一特性似乎与 CO 在斜发沸石上的吸附等焓低于其他样品一致。通过使用 CO 作为探针分子的傅里叶变换红外光谱研究了影响 q 和吸附容量的表面物种。总的来说,观察到 CO 在裸斜发沸石的 K 和 Mg 阳离子上形成线性加合物,在其碱性位上形成碳酸盐样物质。对于 Na 交换的斜发沸石,Na 离子导致表面碱性降低,并形成单(Na···OCO)和双(Na···OCO···Na)阳离子位,可用于形成线性加合物。由于斜发沸石在 338 K 时具有显著的吸附能力,因此该材料似乎是一种很有前途的吸附剂,可用于直接从在这种温度下运行的不同烟道气源中去除 CO。