Synthesis of CaO-Based Sorbents for CO2 Capture by a Spray-Drying Technique Wenqiang Liu,*,† Junjun Yin,‡ Changlei Qin,‡ Bo Feng,*, ‡ and Minghou Xu† † State Key Laboratory of Coal Combustion, Huazhong University of Science and Technology, Wuhan 430074, China ‡ School of Mechanical and Mining Engineering, The University of Queensland, St Lucia, Queensland 4072, Australia Sorbent Characterization, 1 table and 5 figures included 1 Sample Characterization 1) Sorbents Preparation Two more sample (CG-MG75-1 and CG-MG75-2 ) were produced to investigate the effect of spray drying operating conditions (pump settings). The preparation was the same as that for CG-MG-75 and the operating conditions are shown in Table S1. 2) Porosimetric Analysis Porosimetric analysis was performed on three uncalcined sorbents (u-CG-MG75, u-CG-MG75-1 and u-CGMG75-2). The nitrogen adsorption isotherms of samples were measured at 77 K within the relative pressure of 10–6~1 by a TriStar 3000 specific surface area and pore size analyser (Micromeritics Co., USA). Before measuring the isotherms, the sorbents were dried at 140 °C for 48 h and then degassed to 40 mbar at 250 °C for 48 h. 3) Particle Size Distribution The particle size distributions of three calcined sorbents (CG-MG-75, CG-MG75-1 and CG-MG75-2) were measured using a Master Mini particle size analyzer (Malvern Instruments Ltd). 4) Morphologies Changes with Cycles The morphology changes of the sorbent CG-MG-75 before cycles and after 44 cycles were observed with a JEOL JSM-6610 scanning electron microscope (SEM). The powders were dispersed on the surface of conductive adhesive carbon tab and platinum-coated using an EIKO IB-5 Sputter Coater for 5 min (approximately 15 nm thick) to obtain a better electronic signal. All SEM images were obtained from secondary electrons with 20 kV of accelerating voltage. 2 Table S1. Specific BET surface areas of uncalcined sorbents collected from cyclone after spraying drying under the conditions in Table 1S1. Sample Name BET Surface Area before Calcination(m2/g) u-CG-MG-75 7.7227 u-CG-MG-75-1 8.1828 u-CG-MG-75-2 6.8367 3 0.05 30 u-CG-MG-75 u-CG-MG-75 0.04 dV/dlogD (cm3/g.nm) Relative Pressure (P/Po) 25 20 15 10 5 0.02 0.01 0 0 0 0.2 30 0.4 0.6 0.8 1 1 100 1000 Pore Diameter (nm) BJH Desorption 0.05 u-CG-MG-75-1 25 u-CG-MG-75-1 dV/dlogD (cm3/g.nm) 0.04 20 15 10 5 0.03 0.02 0.01 0 0 0 0.4 0.2 Adsorption Desorption 0.6 0.8 1 1 10 Relative Pressure (P/Po) 100 1000 Pore Diameter (nm) BJH Desorption 0.05 30 u-CG-MG-75-2 u-CG-MG-75-2 25 0.04 dV/dlogD (cm3/g.nm) Relative Pressure (P/Po) 10 Relative Pressure (P/Po) Adsorption Desorption Relative Pressure (P/Po) 0.03 20 15 10 5 0.03 0.02 0.01 0 0 0 0.2 Adsorption Desorption 0.4 0.6 0.8 1 1 Relative Pressure (P/Po) 10 100 1000 Pore Diameter (nm) BJH Desorption Figure S1. Isotherm Linear Plot and BJH Pore Size Distributions for the Sorbent u-CG-MG-75, u-CGMG-75-1 and u-CG-MG-75-2. 4 Figure S2: Particle Size Distributions of Three Calcined Sorbents (CG-MG-75, CG-MG75-1 and CGMG75-2) Prepared Under Different Spray Drying Conditions. 5 CaO Conversion (3 minutes carbonation) VS Cycle No. 1 0.8 CaO Conversion 0.6 0.4 0.2 0 0 2 4 CA-MA-75 CH-CE-75 6 8 10 12 14 Number of Cycle CL-MA-75 CG-MG-75 16 18 20 22 CaO160nm-CE-75 Figure S3: 3-Minute Conversion of Multi Cycles of Carbonation and Calcination of Sorbents Produced Using the Spray Drying Technique . 6 A B Figure S4: SEM Images of Sorbent CG-MG-75 (A) Before Cycles, and (B) After 44 Cycles 7
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