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Naji, M. |
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Motta, Antonella |
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Aletan, Dirar |
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Mohamed, Tarek |
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Ertürk, Emre |
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Taccardi, Nicola |
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Kononenko, Denys |
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Petrov, R. H. | Madrid |
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Alshaaer, Mazen | Brussels |
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Bih, L. |
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Casati, R. |
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Muller, Hermance |
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Kočí, Jan | Prague |
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Šuljagić, Marija |
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Kalteremidou, Kalliopi-Artemi | Brussels |
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Azam, Siraj |
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Ospanova, Alyiya |
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Blanpain, Bart |
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Ali, M. A. |
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Popa, V. |
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Rančić, M. |
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Ollier, Nadège |
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Azevedo, Nuno Monteiro |
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Landes, Michael |
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Rignanese, Gian-Marco |
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Manović, Vasilije
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article
Nitrogen-rich hyper-crosslinked polymers for low-pressure CO2 capture
Abstract
<p>A series of poly[methacrylamide-co-(ethylene glycol dimethacrylate)] (poly(MAAM-co-EGDMA)) porous polymeric particles with high CO<sub>2</sub>-philicity, referred to as HCP-MAAMs, were synthesised for CO<sub>2</sub> capture. The polymers with a MAAM-to-EGDMA molar ratio from 0.3 to 0.9 were inherently nitrogen-enriched and exhibited a high affinity towards selective CO<sub>2</sub> capture at low pressures. A techno-economic model based on a 580 MW<sub>el</sub> supercritical coal-fired power plant scenario was developed to evaluate the performance of the synthesised adsorbents. The presence and density of NH<sub>2</sub> moieties within the polymer network were determined using Fourier transform infrared (FTIR) spectroscopy and X-ray photoelectron spectroscopy (XPS). The thermogravimetric analysis (TGA) showed that the polymers were thermally stable up to 515–532 K. The maximum CO<sub>2</sub> adsorption capacity at 273 K was 1.56 mmol/g and the isosteric heat of adsorption was 28–35 kJ/mol. An increase in the density of amide groups within the polymer network resulted in a higher affinity towards CO<sub>2</sub> at low pressure. At a CO<sub>2</sub>:N<sub>2</sub> ratio of 15:85, CO<sub>2</sub>/N<sub>2</sub> selectivity at 273 K was 52 at 1 bar and reached 104 at ultra-low CO<sub>2</sub> partial pressure. The techno-economic analysis revealed that retrofitting a HCP-MAAM-based CO<sub>2</sub> capture system led to a net energy penalty of 7.7–8.0%<sub>HHV</sub> points, which was noticeably lower than that reported for MEA or chilled ammonia scrubbing capture systems. The specific heat requirement was superior to the majority of conventional solvents such as MDEA-PZ and K<sub>2</sub>CO<sub>3</sub>. Importantly, the economic performance of the HCP-MAAM retrofit scenario was found to be competitive to chemical solvent scrubbing scenarios.</p>