(455a) Development of Cellulose-Based Composite Adsorbents for CO2 Capture
AIChE Annual Meeting
2023
2023 AIChE Annual Meeting
Innovations in Process Engineering
New processes for efficient CO2 capture and utilization under mild conditions
Wednesday, November 8, 2023 - 8:00am to 8:21am
This research aims at exploring the use of cellulose-based solid adsorbents in capturing CO2 by reusing and recycling waste paper. Office paper comprises 85% cellulose which is extracted using an alkali and bleaching treatment in this study. Alkali treatment is done to remove hemicellulose while bleaching eliminates lignin. Cellulose is the most abundant biopolymer in the world which is inexpensive, non-toxic, and can be easily functionalized with CO2-philic functionalities due to the presence of abundant hydroxyl groups. To further enhance the CO2 uptake of cellulose-based materials, by creating more functional groups, higher specific surface area, and porosity; aerogels are synthesized, and the pristine cellulose is combined with graphene oxide (GO) which is a 2D material comprising hydroxyl, alkoxy, carbonyl, and carboxyl functional groups. In this study, the aerogels are prepared by dissolving cellulose in a NaOH/urea/ DI water solvent which is subsequently solvent exchanged with organic solvents and vacuum freeze-dried. The synthesized cellulose-GO aerogels were evaluated for CO2 adsorption as a function of temperature and absolute pressure. Furthermore, the cellulose-GO aerogels were functionalized with an amino silane called 3-aminopropyltriethoxysilane (APTES) to study the effect of introducing different concentrations of APTES in adsorbing CO2 at different temperatures and absolute pressure. To functionalize cellulose and GO, the wet gel is grafted with APTES dissolved in a hydroalcoholic mixture. By functionalizing the aerogel with APTES, it is observed that the aerogel can uptake a good amount of CO2 at low pressures which makes the material promising for low-concentration CO2 capture such as Direct Air Capture (DAC) applications. The study has analyzed the effect of different GO and APTES concentrations on CO2 uptake. The optimized non-functionalized cellulose-GO aerogel displaying physisorption behavior has an uptake of 0.48 mmol/g at 1 bar and 25oC. On the other hand, the improvised APTES grafted cellulose-GO aerogel which presented chemisorption characteristics has a CO2 uptake of 2.52 mmol/g at 1 bar and 25oC. Figure 1 represents the adsorption isotherm of cellulose, cellulose-GO, and cellulose-GO-APTES aerogels.
The cellulose-GO aerogel and the APTES functionalized cellulose-GO aerogels had also been studied for their kinetics, regeneration, and cyclability for up to 10 cycles by using both Pressure Swing Adsorption (PSA) and Temperature Pressure Swing Adsorption (TPSA), selectivity to nitrogen (N2), water adsorption and CO2 adsorption at humid conditions. In addition, the CO2 adsorption of the aerogels had been tested at 40oC and 60oC. As expected, the APTES functionalized cellulose-GO aerogels had higher CO2 uptake at higher temperatures while the non-functionalized cellulose-GO aerogels had lower uptake as the temperature increased. Furthermore, the functionalized samples had much faster kinetics, higher selectivity against N2, and showed good regeneration ability while performing TPSA. Due to the hydrophilic nature of both cellulose and GO it was observed that the non-functionalized sample had a higher water adsorption capacity and the CO2 uptake in humid conditions at 25oC dropped to 0.4 mmol/g at 1 bar. However, due to the APTES grafting the aerogel had some hydrophobic nature due to which it adsorbed much lesser water than the non-functionalized sample. At humid conditions, the APTES functionalized sample had a lesser CO2 adsorption capacity than the sample tested at dry conditions however, the uptake was still much higher than the cellulose-GO aerogel.
Other crucial parameters such as surface area, pore volume, pore size, and heat of adsorption have also been estimated. It is observed that the synthesized aerogels are mesoporous in nature. An important observation that was made is that the cellulose-GO aerogel had a much lower surface area than the APTES functionalized sample. This is because the cellulose-GO aerogel had a much higher average pore size and with the introduction of APTES the average pore size decreased thus, as a result of having a greater number of pores with a smaller size the surface area increased. The heat of adsorption for the aerogels was estimated using the Clausius-Clapeyron equation and the value obtained for the APTES functionalized samples was 35.95 kJ/mol while the non-functionalized sample gave a value of 14.28 kJ/mol. Both values represent how chemisorption requires higher heat of adsorption than physisorption and are within the range reported in the literature. Finally, the modeling of the CO2 isotherms at 25oC was done using Langmuir and Freundlich models. From the curve fitting it has been observed that for the cellulose-GO aerogel both the Langmuir and Freundlich models were promising. On the contrary, for the APTES functionalized samples the Langmuir model overestimated the CO2 capacity at low pressures and underestimated the values at higher pressures. But by using the Freundlich model the error associated with the adsorption capacity was much lesser and ânâ which represents the affinity between the adsorbent and the adsorbate had a value of 5.32. Since a value of n between 2 to 8 represents high affinity and heterogenicity of the sites in the adsorbent it is concluded that the functionalized adsorbent is better modeled using the Freundlich model.
In conclusion, this works focuses on the development of a cellulose-based composite adsorbent for CO2 capture by recycling paper and functionalizing it with APTES which is an area that has not been explored. The synthesized aerogel which is functionalized displays promising CO2 adsorption at different conditions and when compared with similar such cellulose-based adsorbents the values are consistently making it applicable for both low CO2 concentration sources such as DAC and industrial emissions capture.