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Frontiers of Environmental Science & Engineering

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Front Envir Sci Eng    0, Vol. Issue () : 326-340    https://doi.org/10.1007/s11783-013-0510-7
REVIEW ARTICLE
Activated carbons and amine-modified materials for carbon dioxide capture –– a review
Zhenhe CHEN1, Shubo DENG1,2(), Haoran WEI1, Bin WANG1, Jun HUANG1, Gang YU1,2
1. State Key Joint Laboratory of Environment Simulation and Pollution Control, School of Environment, POPs Research Center, Tsinghua University, Beijing 100084, China; 2. Tsinghua University – Veolia Environment Joint Research Center for Advanced Technology, Tsinghua University, Beijing 100084, China
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Abstract

Rapidly increasing concentration of CO2 in the atmosphere has drawn more and more attention in recent years, and adsorption has been considered as an effective technology for CO2 capture from the anthropogenic sources. In this paper, the attractive adsorbents including activated carbons and amine-modified materials were mainly reviewed and discussed with particular attention on progress in the adsorbent preparation and CO2 adsorption capacity. Carbon materials can be prepared from different precursors including fossil fuels, biomass and resins using the carbonization-activation or only activation process, and activated carbons prepared by KOH activation with high CO2 adsorbed amount were reviewed in the preparation, adsorption capacity as well as the relationship between the pore characteristics and CO2 adsorption. For the amine-modified materials, the physical impregnation and chemical graft of polyethylenimine (PEI) on the different porous materials were introduced in terms of preparation method and adsorption performance as well as their advantages and disadvantages for CO2 adsorption. In the last section, the issues and prospect of solid adsorbents for CO2 adsorption were summarized, and it is expected that this review will be helpful for the fundamental studies and industrial applications of activated carbons and amine-modified adsorbents for CO2 capture.
Keywords adsorption capacity      CO2 capture      activated carbon      amine-impregnated adsorbents     
Corresponding Author(s): DENG Shubo,Email:dengshubo@tsinghua.edu.cn   
Issue Date: 01 June 2013
 Cite this article:   
Zhenhe CHEN,Shubo DENG,Haoran WEI, et al. Activated carbons and amine-modified materials for carbon dioxide capture –– a review[J]. Front Envir Sci Eng, 0, (): 326-340.
 URL:  
https://academic.hep.com.cn/fese/EN/10.1007/s11783-013-0510-7
https://academic.hep.com.cn/fese/EN/Y0/V/I/326
sourcescontent/(vol. %)temperature/°Cpressure/bar
CO2H2ON2O2
flue gas [2]3-146-1573-773-450-150~1
air [3,4]~0.0391-478.0820.95-20-401
Tab.1  Components and characteristics of flue gas and air
adsorbentadsorption temperature/°CCO2 pressure/barCO2 uptake/mmol·g-1CO2/N2 selectivity a)adsorbent costregenerationRef.
AC012.8-8.62-15lowEEP b)[8,9]
2511.5-4.8
MOFs250.10.1-5.953-500highEEP[10,11]
250.50.6-7.2
25≥146.8-54.5
Zeolite2510.75-4.6610-15lowEIP c)[12,13]
00.152.5-5.2
AMMs7512.0-4.95-mediumEEP[14,15]
250.1-0.150.79-14.0
254 × 10-41.05-1.77
LDH200-4000.15<1-lowEIP[16]
M2CO360-1000.1-0.152.0-3.0-lowEIP[14]
CaO650-8000.158-11-lowEIP[17]
Tab.2  Comparison of different adsorbents for CO capture
precursorspreparation methodsadsorption conditionsCO2 uptake /(mmol·g-1)Ref.
coal tar pitchcarbonization-activation(steam)30°C, 100kPa1.9[8]
coal tar pitchcarbonization25°C, 1bar~2.2[29]
petroleum pitchcarbonization-activation(KOH)0°C /25°C, 1bar8.6/4.7[30]
petroleum cokecarbonization-activation(KOH)25°C, 1bar3.5[31]
anthracitecarbonization-activation (steam)30°C, 1bar1.5[32]
carpetcarbonization-activation(KOH)25°C, 1bar1.9[33]
polypyrrolecarbonization-activation(KOH)0°C,1bar6.2[24]
polyacrylonitrilecarbonization-activation30°C, 4.1MPa11.6[34]
graphene and polypyrrolecarbonization-activation (KOH)25°C,1bar4.3[27]
eucalyptus sawdustcarbonization-activation(KOH)0°C /25°C, 1bar6.6/4.8[35]
almond shellcarbonization-activation(CO2)25°C, 1bar2.6[36]
olive stonecarbonization-activation (CO2)25°C, 1bar2.4[37]
yeastcarbonization-activation(KOH)25°C, 1bar4.8[9]
soybeancarbonization-activation(ZnCl2/CO2)30°C, 0.15bar0.93[38]
resorcinol and formaldehydecarbonization25°C, 1bar3.3[39]
resorcinol and formaldehydecarbonization25°C, 1bar3.1[25]
urea and formaldehydecarbonization-activation (K2CO3)25°C, 1bar1.8[26]
melamine and terephthalaldehydecarbonization25°C, 1bar3.2[28]
phloroglucin and formaldehydecarbonization (STM a)25°C, 800Torr1.5[40]
acetonitrilecarbonization (HTM b)25°C, 1bar4.0[41]
acetonitrilecarbonization (HTM)0°C /25°C, 1bar6.9/4.4[42]
melamine and formaldehydecarbonization (HTM)25°C, 1bar2.3[43]
carbon tetrachloride and ethylenediaminecarbonization (HTM)25°C, 1bar2.9[44]
Tab.3  CO uptake on different carbon materials prepared by different methods
porous materialsPEI molecular weightCO2 uptake/(mmol·g-1)adsorption conditionsRef.
HMS a)6004.7775°C, 1bar[53]
MHS b)4234.9175°C, 0.2bar[54]
HMS6004.9575°C, 1bar[55]
PMCM-41 c)4234.62/1.7075/25°C, 1bar[14]
MCF d)6004.570°C, 0.67bar[56]
Carbon black4233.575°C, 1bar[57]
SBA-154233.93/2.5675/25°C, 0.1bar[58]
PMMA e)4232.5025°C, 0.15bar[59]
Meso-Al2O36001.9525°C, 0.1bar[60]
Meso-Al2O36001.7425°C, 400ppm[60]
Meso-Al2O34231.1325°C, 0.15bar[61]
SBA-154232.3975°C, 0.15bar[62]
SBA-156002.9375°C, 1bar[63]
MCM-416002.5275°C, 1bar[63]
F-silica f)250001.7225°C, 0.12bar[64]
P-silica g)8003.3470°C, 1bar[65]
P-silica250002.9570°C, 1bar[65]
GF h)GF25000250004.122.0230°C, 0.24bar, humid30°C, 0.16bar, humid[66][67]
Tab.4  PEI-impregnated adsorbents for CO capture
Fig.1  Effects of PEI molecular weights and the pore characteristics of the porous materials on CO adsorption on the PEI-impregnated adsorbents
porous materialsaminespreparationmethodsCO2 uptake /(mmol·g-1)adsorption conditionsRef.
PMCM-41 a)TAP b)silane2.825°C, 1bar[80]
PMCM-41AP c)silane2.05/2.7025°C, 0.05/1bar[81]
MCM-48APsilane1.14/2.0525°C, 0.05/1bar[82]
SBA-15SBA-15SBA-15APDAP d)TAPsilanesilanesilane0.651.511.8060°C, 0.15bar, humid60°C, 0.15bar, humid60°C, 0.15bar, humid[83][83][83]
MS e)MSMSAPDAPTAPsilanesilanesilane1.251.711.7425°C, 1bar25°C, 1bar25°C, 1bar[84]
[84]
[84]
MSAPsilane1.5920°C, 0.9bar[85]
SBA-12SBA-15APAPsilanesilane1.01.525°C, 0.1bar25°C, 0.1bar[86][86]
MCM-41TAPsilane1.4125°C, 0.05bar[87]
SBA-15SBA-15SBA-15APDAPTAPsilanesilanesilane0.50.91.2160°C, 0.15bar, humid60°C, 0.15bar, humid60°C, 0.15bar, humid[88][88][88]
CNT f)DAPsilane2.5960°C, 0.5bar[89]
CNTAPsilane1.3220°C, 0.15bar[90]
NFC g)DAPsilane1.3925°C, 506ppm, humid[91]
MCM-41MCM-48TREN h)TRENcouplingcoupling1.361.5925°C, 1bar25°C, 1bar[92][92]
MSPEIcoupling0.9830°C, 1bar[93]
PPN-6 i)PPN-6PPN-6PPN-6EDA j)DTA k)TRENTETA l)couplingcouplingcouplingcoupling3.254.33.53.2522°C, 0.15bar22°C, 0.15bar22°C, 0.15bar22°C, 0.15bar[94][94][94][94]
SBA-15polyarizidinepolymerizaiton3.1125°C, 0.1bar[95]
SBA-15polyarizidinepolymerizaiton5.5525°C, 0.1bar, humid[95]
MSpolyarizidinepolymerizaiton0.4745°C, 0.1bar[96]
MCFMel m) and EDApolymerizaiton0.8920°C, 0.9bar[97]
PANF n)poly(allylamine)polymerizaiton6.2222°C, 0.15bar, humid[98]
Tab.5  CO uptake on different amine-grafted adsorbents
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