Process model for the simulation.

Process model for the simulation.

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The recent advancement in efficient and recoverable CO2 capture solvents has been stimulated by the environmental harm resulting from the accumulation of greenhouse gases. Ionic liquids (ILs) and IL-based solvents have given rise to a novel method of CO2 collection that is highly efficient, economical, and environmentally benign. However, there is...

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Context 1
... conditions were identified based on cost, energy, and uptake capacity. Figure 3 depicts the ASPEN Plus model used to simulate the physical absorption of CO2 by utilizing IL. ASPEN Plus has been used by experts in the field to study the CO2 absorption and desorption processes in several feasibility studies [69,70]. ...
Context 2
... whereas the colder side fluid from the heat exchanger is upstream of the heater placed on the left side with 1.01 kW (3665 kJ/h) of duty. The HEN design network also shows the pinch and cross pinch lines specified where the vertical dotted lines are the cross-pinch temperatures (Supplementary Datasheet Figure S3). Moreover, cross pinch duties are demonstrated in Table 8. ...

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Article
The concurrent utilization of an adsorbent and absorbent for carbon dioxide (CO2) adsorption with synergistic effects presents a promising technique for CO2 capture. Here, 1-butyl-3-methylimidazole acetate ([Bmim][Ac]), with a high affinity for CO2, and the molecular sieve SAPO-34 were selected. The impregnation method was used to composite the hybrid samples of [Bmim][Ac]/SAPO-34, and the pore structure and surface property of prepared samples were characterized. The quantity and kinetics of the sorbed CO2 for loaded samples were measured using thermogravimetric analysis. The study revealed that SAPO-34 could retain its pristine structure after [Bmim][Ac] loading. The CO2 uptake of the loaded sample was 1.879 mmol g–1 at 303 K and 1 bar, exhibiting a 20.6% rise compared to that of the pristine SAPO-34 recording 1.558 mmol g–1. The CO2 uptake kinetics of the loaded samples were also accelerated, and the apparent mass transfer resistance for CO2 sorption was significantly reduced by 11.2% compared with that of the pure [Bmim][Ac]. The differential scanning calorimetry method revealed that the loaded sample had a lower CO2 desorption heat than that of the pure [Bmim][Ac], and the CO2 desorption heat of the loaded samples was between 30.6 and 40.8 kJ mol–1. The samples exhibited good cyclic stability. This material displays great potential for CO2 capture applications, facilitating the reduction of greenhouse gas emissions.