CO2 uptake of modified calcium-based sorbents in a pressurized carbonation–calcination looping

Abstract This study focuses on enhancing CO 2 uptake by modifying limestone with acetate solutions under pressurized carbonation condition. The multicycle tests were carried out in an atmospheric calcination/pressurized carbonation reactor system at different temperatures and pressures. The pore structure characteristics (BET and BJH) were measured as a supplement to the reaction studies. Compared with the raw limestone, the modified sorbent showed a great improvement in CO 2 uptake at the same reaction condition. The highest CO 2 uptake was obtained at 700 °C and 0.5 MPa, by 88.5% increase over the limestone at 0.1 MPa after 10 cycles. The structure characteristics of the sorbents on N 2 absorption and SEM confirm that compared with the modified sorbent, the effective pores of limestone are greatly driven off by sintering, which hinders the easy access of CO 2 molecules to the unreacted-active sites of CaO. The morphological and structural properties of the modified sorbent did not reveal significant differences after multiple cycles. This would explain its superior performance of CO 2 uptake under pressurized carbonation. Even after 10 cycles, the modified sorbent still achieved a CO 2 uptake of 0.88.

[1]  Haruhiko Ohya,et al.  Development of porous solid reactant for thermal-energy storage and temperature upgrade using carbonation/decarbonation reaction , 2001 .

[2]  Ningsheng Cai,et al.  Synthesis, experimental studies, and analysis of a new calcium-based carbon dioxide absorbent , 2005 .

[3]  E. J. Anthony,et al.  Steam hydration of CFBC ash and the effect of hydration conditions on reactivation , 2004 .

[4]  D. D. Perlmutter,et al.  Effect of the product layer on the kinetics of the CO2‐lime reaction , 1983 .

[5]  Yu-yu Huang,et al.  Effect of Preparation Temperature on Cyclic CO2 Capture and Multiple Carbonation−Calcination Cycles for a New Ca-Based CO2 Sorbent , 2006 .

[6]  E. J. Anthony,et al.  Determination of intrinsic rate constants of the CaO–CO2 reaction , 2008 .

[7]  John R. Grace,et al.  Long-Term Calcination/Carbonation Cycling and Thermal Pretreatment for CO2 Capture by Limestone and Dolomite , 2009 .

[8]  Kevin R. Bruce,et al.  Pore-distribution changes of calcium-based sorbents reacting with sulfur dioxide , 1987 .

[9]  John R. Grace,et al.  Cyclic CO2 capture by limestone‐derived sorbent during prolonged calcination/carbonation cycling , 2008 .

[10]  Vasilije Manovic,et al.  Thermal activation of CaO-based sorbent and self-reactivation during CO2 capture looping cycles. , 2008, Environmental science & technology.

[11]  Ataullah Khan,et al.  Relationship between Structural Properties and CO2 Capture Performance of CaO-Based Sorbents Obtained from Different Organometallic Precursors , 2008 .

[12]  R. H. Borgwardt Calcination kinetics and surface area of dispersed limestone particles , 1985 .

[13]  Toshiaki Hanaoka,et al.  Hydrogen production from woody biomass by steam gasification using a CO2 sorbent , 2005 .

[14]  J. Carlos Abanades,et al.  Pore-Size and Shape Effects on the Recarbonation Performance of Calcium Oxide Submitted to Repeated Calcination/Recarbonation Cycles , 2005 .

[15]  D. W. Pershing,et al.  Calcination and sintering models for application to high-temperature, short-time sulfation of calcium-based sorbents , 1990 .

[16]  J. C. Abanades,et al.  Conversion Limits in the Reaction of CO2 with Lime , 2003 .

[17]  F. Zeman Effect of steam hydration on performance of lime sorbent for CO2 capture , 2008 .

[18]  J. Carlos Abanades,et al.  Determination of the Critical Product Layer Thickness in the Reaction of CaO with CO2 , 2005 .

[19]  P. Smirniotis,et al.  Parametric Study of Cs/CaO Sorbents with Respect to Simulated Flue Gas at High Temperatures , 2005 .

[20]  John P. Longwell,et al.  Product Layer Diffusion during the Reaction of Calcium Oxide with Carbon Dioxide , 1999 .

[21]  Juan Carlos Abanades,et al.  Enhancement of CaO for CO2 capture in an FBC environment , 2003 .

[22]  Changsui Zhao,et al.  CO2 Capture Using CaO Modified with Ethanol/Water Solution during Cyclic Calcination/Carbonation , 2008 .

[23]  R. Barker,et al.  The reversibility of the reaction CaCO3 ⇄ CaO+CO2 , 2007 .

[24]  R. Barker,et al.  The reactivity of calcium oxide towards carbon dioxide and its use for energy storage , 1974 .

[25]  Changsui Zhao,et al.  Cyclic calcination/carbonation looping of dolomite modified with acetic acid for CO2 capture , 2008 .

[26]  Hiroyuki Hatano,et al.  Repetitive carbonation-calcination reactions of Ca-based sorbents for efficient CO2 sorption at elevated temperatures and pressures , 2003 .

[27]  John R. Grace,et al.  The effect of CaO sintering on cyclic CO2 capture in energy systems , 2007 .

[28]  A. I. Lysikov,et al.  Change of CO2 Carrying Capacity of CaO in Isothermal Recarbonation−Decomposition Cycles , 2007 .

[29]  Changsui Zhao,et al.  CO2 Capture Performance of Calcium-Based Sorbents in a Pressurized Carbonation/Calcination Loop , 2010 .

[30]  J. Charland,et al.  A Study on the Reactivation of Five Fly Ashes from Commercial Circulating Fluidized Bed (CFB) Boilers , 2004 .

[31]  Vasilije Manovic,et al.  Steam reactivation of spent CaO-based sorbent for multiple CO2 capture cycles. , 2007, Environmental science & technology.

[32]  J. Carlos Abanades,et al.  CO2 Capture Capacity of CaO in Long Series of Carbonation/Calcination Cycles , 2006 .

[33]  I. Cutler,et al.  Effect of CO 2 Pressure on the Reaction with CaO , 1979 .

[34]  J. C. Abanades,et al.  Lime enhanced gasification of solid fuels: Examination of a process for simultaneous hydrogen production and CO2 capture , 2008 .

[35]  C. Müller,et al.  Synthetic Ca‐based solid sorbents suitable for capturing CO2 in a fluidized bed , 2008 .

[36]  Robin W. Hughes,et al.  Improved Long-Term Conversion of Limestone-Derived Sorbents for In Situ Capture of CO2 in a Fluidized Bed Combustor , 2004 .

[37]  Hermann Hofbauer,et al.  H2 rich product gas by steam gasification of biomass with in situ CO2 absorption in a dual fluidized bed system of 8 MW fuel input , 2009 .

[38]  Xiaoping Chen,et al.  Effect of rice husk ash addition on CO2 capture behavior of calcium-based sorbent during calcium looping cycle , 2009 .

[39]  D. P. Harrison,et al.  HIGH TEMPERATURE CAPTURE OF CARBON DIOXIDE: CHARACTERISTICS OF THE REVERSIBLE REACTION BETWEEN CaO(s) and CO2(g) , 1995 .

[40]  L. Fan,et al.  Carbonation−Calcination Cycle Using High Reactivity Calcium Oxide for Carbon Dioxide Separation from Flue Gas , 2002 .

[41]  P. Smirniotis,et al.  Calcium Oxide Doped Sorbents for CO2 Uptake in the Presence of SO2 at High Temperatures , 2009 .

[42]  P. Fennell,et al.  Regeneration of sintered limestone sorbents for the sequestration of CO2 from combustion and other systems , 2007 .

[43]  Mónica Alonso,et al.  Reactivity of highly cycled particles of CaO in a carbonation/calcination loop , 2008 .