Investigation on a novel CaO-Y2O3 sorbent for efficient CO2 mitigation

Chemical Engineering Journal

Volumn 243, Issue , 2014, Pages 297-304

  Zhang, Xueying ^a   Li, Zhenguo ^a   Peng, Yue ^a   Su, Wenkang ^a   Sun, Xiaoxu ^a   Li, Junhua ^a  

^a TSINGHUA UNIVERSITY   (China)

Author keywords

Calcium oxide; Carbonation calcination; CO2 mitigation; Sol gel combustion

Indexed keywords

CALCINATION CONDITIONS; LINEAR RELATIONSHIPS; NATURALLY OCCURRING; REALISTIC CONDITIONS; SIZE DISTRIBUTION MEASUREMENTS; SOL-GEL COMBUSTION; SOL-GEL COMBUSTION METHOD; SORPTION PERFORMANCE;

CALCINATION; LIME; SINTERING; SOL-GEL PROCESS; SOL-GELS; SORBENTS; SORPTION;

CARBON DIOXIDE;

EID: 84893424729     PISSN: 13858947     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.cej.2014.01.017     Document Type: Article

References (67)

1. 2 sorbent. Ceram. Int. 2011, 37:3291-3298.
2. Wang S.P., Yan S.L., Ma X.B., Gong J.L. Recent advances in capture of carbon dioxide using alkali-metal-based oxides. Energy Environ. Sci. 2011, 10:3805-3819.
3. Trends in global CO2 emissions: 2013 report, http://www.pbl.nl/en/publications/trends-in-global-co2-emissions-2013-report.
4. World Energy Outlook 2012, http://www.iea.org/publications/freepublications/publication/English.pdf.
5. World Energy Outlook 2009, http://www.worldenergyoutlook.org/publications/weo-2009/.
6. 2 capture capacity by modifying limestone with propionic acid. Powder Technol. 2013, 233:8-14.
7. 2 from combustion processes. Chem. Eng. Res. Des. 1999, 77:62-68.
8. 2 capture-a review of sorbent modification methods. Int. J. Environ. Res. Pub. Health 2010, 7:3129-3140.
9. 2 capture. Prog. Energy Combust. 2010, 36:260-279.
10. 2 looping cycle performance of a high-purity limestone after thermal activation/doping. Energy Fuel 2008, 5:3258-3264.
11. 2 capture looping cycles. Environ. Sci. Technol. 2008, 42:4170-4174.
12. 33 sorbent. Chem. Eng. J. 2013, 220:383-394.
13. Sun Z., Chi H., Fan L.S. Physical and chemical mechanism for increased surface area and pore volume of CaO in water hydration. Ind. Eng. Chem. Res. 2012, 51:10793-10799.
14. 2 absorption capacity of synthetic CaO-MgO absorbent for sorption-enhanced hydrogen production. Int. J. Hydrogen Energy 2012, 37:95-102.
15. 2 sorbent for multicycle operation. Chem. Eng. J. 2013, 232:280-289.
16. 2 capture using a co-precipitation technique. Int. J. Greenhouse Gas Con. 2013, 15:48-54.
17. 2 capture performance. Chem. Eng. Sci. 2012, 74:172-180.
18. 2 capture. Chinese Chem. Lett. 2011, 22:615-618.
19. 2 sorbents. Adv. Mater. 2012, 24:3059-3064.
20. 2 sorbent. Ind. Eng. Chem. Res. 2008, 47:180-184.
21. Li Z.S., Cai N.S., Huang Y.Y., Han H.J. Synthesis, experimental studies, and analysis of a new calcium-based carbon dioxide absorbent. Energy Fuel. 2005, 19:1447-1452.
22. Broda M., Kierzkowska A.M., Müller C.R. Application of the sol-gel technique to develop synthetic calcium-based sorbents with excellent carbon dioxide capture characteristics. Chemsuschem 2012, 5:411-418.
23. 2 sorbents: development of synthetic, calcium-rich dolomites. Environ. Sci. Technol. 2012, 46:559-565.
24. 2 capture. Ind. Eng. Chem. Res. 2009, 48:10604-10613.
25. Przepiórski J., Czyzewski A., Pietrzak R., Tryba B. MgO/CaO-loaded porous carbons for carbon dioxide capture. J. Therm. Anal. Calorim. 2013, 111:357-364.
26. 2 using sorbents of calcium magnesium acetate (CMA). Energy Fuel 2010, 24:3687-3697.
27. 2. Ind. Eng. Chem. Res. 2009, 48:10284-10291.
28. 2 capture during extended operating cycles. J. Phys. Chem. C 2011, 115:24804-24812.
29. 2 capture. Ind. Eng. Chem. Res. 2012, 51:10390-10398.
30. 2 capture. Energy Fuel 2009, 23:1093-1100.
31. 2 capture. Ind. Eng. Chem. Res. 2010, 49:11778-11784.
32. 33 as additives. Korean J. Chem. Eng. 2011, 28:1042-1046.
33. 3 carbon dioxide absorbent with enhanced stability for sorption-enhanced reforming applications. Ind. Eng. Chem. Res. 2011, 50:12741-12749.
34. CRC Handbook of Chemistry and Physics 93rd Edition Internet Version 2012-2013, http://www.hbcpnetbase.com/.
35. 2 sorbents: from fundamentals to the development of new, highly effective materials. Chemsuschem 2013, 6:1130-1148.
36. 2 capture-a review. Energy Fuel 2012, 26:2751-2767.
37. 2 capture. Environ. Sci. Technol. 2010, 44:841-847.
38. Lu H., Reddy E.P., Smirniotis P.G. Calcium oxide based sorbents for capture of carbon dioxide at high temperatures. Ind. Eng. Chem. Res. 2006, 45:3944-3949.
39. 2 removal at high temperature. Micropor. Mesopor. Mater. 2008, 110:119-127.
40. Florin N.H., Harris A.T. Preparation and characterization of a tailored carbon dioxide sorbent for enhanced hydrogen synthesis in biomass gasifiers. Ind. Eng. Chem. Res. 2008, 47:2191-2202.
41. Gupta H., Fan L.S. Carbonation-calcination cycle using high reactivity calcium oxide for carbon dioxide separation from flue gas. Ind. Eng. Chem. Res. 2002, 41:4035-4042.
42. 2 by a synthetic, CaO-containing sorbent. Chem. Eng. Sci. 2009, 64:2147-2157.
43. 2 capture by carbide slag from chlor-alkali plant in calcination/carbonation cycles. Int. J. Greenhouse Gas Con. 2012, 9:117-123.
44. Arias B., Abanades J.C., Grasa G.S. An analysis of the effect of carbonation conditions on CaO deactivation curves. Chem. Eng. J. 2011, 167:255-261.
45. 2 capture performance of CaO-derived sorbents. Chem. Eng. J. 2013, 217:71-81.
46. 2 capture cycles. Environ. Sci. Technol. 2007, 41:1420-1425.
47. 2 capture in energy systems. Aiche J. 2007, 53:2432-2442.
48. 2 capture cycles. Ind. Eng. Chem. Res. 2009, 48:8906-8912.
49. 2 capture behavior of limestone modified with pyroligneous acid (PA) during calcium looping cycles. Ind. Eng. Chem. Res. 2011, 50:10222-10228.
50. 2 mitigation. Fuel 2009, 88:697-704.
51. 2. Ind. Eng. Chem. Res. 2005, 44:5608-5615.
52. 4-doped CaO-based sorbent. Fuel 2010, 89:642-649.
53. Lee D.K. An apparent kinetic model for the carbonation of calcium oxide by carbon dioxide. Chem. Eng. J. 2004, 100:71-77.
54. 2 capture efficiency and carbonation/calcination kinetics of micro and nanosized particles of supercritically precipitated calcium carbonate. Chem. Eng. J. 2013, 226:357-366.
55. Mess D., Sarofim A.F., Longwell J.P. Product layer diffusion during the reaction of calcium oxide with carbon dioxide. Energy Fuel 1999, 13:999-1005.
56. 2 capture efficiency and energy requirement analysis of power plant using modified calcium-based sorbent looping cycle. Energy 2011, 36:1590-1598.
57. 2 capture of limestone modified by hydration-dehydration technology for carbonation/calcination looping. Chem. Eng. J. 2011, 173:158-163.
58. 2 capture. Environ. Sci. Technol. 2010, 44:3093-3097.
59. 2 concentration calcination conditions. Ind. Eng. Chem. Res. 2010, 49:6916-6922.
60. 2 sorbents under realistic calcination conditions. Energy Fuel 2007, 21:3560-3562.
61. 2 looping cycles. Fuel 2009, 88:1893-1900.
62. 2 capture in fluidized beds under realistic calcination conditions. J. Environ. Eng. 2009, 135:404-410.
63. 2. Energy Fuel 2012, 26:2473-2482.
64. Baker E.H. The calcium oxide-carbon dioxide system in the pressure range 1-300 atmospheres. J. Chem. Soc. 1962, 70:464.
65. 2 sorbents. Environ. Sci. Technol. 2012, 46:10849-10856.
66. 3+ ions. J. Eur. Ceram. Soc. 2012, 32:307-315.
67. 2 capture conditions of a fluidized bed limestone decomposition reactor. Fuel Process. Technol. 2010, 91:958-963.