New molecular basket sorbents for CO2 capture based on mesoporous sponge-like TUD-1

被引:25
作者
Wang, Xiaoxing [1 ,2 ]
Song, Chunshan [1 ,2 ,3 ]
Gaffney, Anne M. [4 ]
Song, Ruozhi [5 ]
机构
[1] Penn State Univ, Clean Fuels & Catalysis Program, EMS Energy Inst, University Pk, PA 16802 USA
[2] Penn State Univ, Dept Energy & Mineral Engn, University Pk, PA 16802 USA
[3] Penn State Univ, Dept Chem Engn, University Pk, PA 16802 USA
[4] AMG Catalysis & Chem Consulting, W Chester, PA 19382 USA
[5] Lummus Technol, Bloomfield, NJ 07003 USA
关键词
CO2; capture; Molecular basket sorbent; Flue gas; Polyethylenimine; TUD-1; Mesoporous molecular sieve; Diffusion constant; CARBON-DIOXIDE CAPTURE; FLUE-GAS; ACTIVATED CARBON; SOLID SORBENTS; ZEOLITE; 13X; ADSORPTION; SILICA; SEPARATION; ADSORBENT; ENERGY;
D O I
10.1016/j.cattod.2014.02.022
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
In this work, a new class of mesoporous and sponge-like TUD-1 materials have been explored as the support matrix for immobilizing a functional polymer, polyethylenimine (PEI), to prepare molecular basket sorbents (MBS) for CO2 capture. The performance of TUD-1 based MBS has been evaluated in a fixed-bed flow system using a simulated flue gas. Effects of the pore properties, PEI loading amount and moisture on the sorption capacity were examined. Compared to the well-known SBA-15, the TUD-1 based nano-porous MBS showed not only a comparable gravimetric capacity (similar to 115 mg-CO2/g-sorb), but also a significantly higher volumetric capacity (as high as 68 mg-CO2/mL-sorb). Both the pore volume and pore size play a crucial role in determining the CO2 sorption capacity of the TUD-1 based MBS. Furthermore, the TUD-1 supported PEI samples exhibited faster CO2 sorption kinetics than SBA-15 based MBS, due likely to the improved CO2 diffusion constant which was estimated by Parabolic diffusion equation. The highest CO2 sorption capacity of 116 mg-CO2/g-sorb was obtained with PEI loading of 50 wt% at 75 degrees C under dry conditions, which was further enhanced to 130 mg-CO2/g-sorb in the presence of moisture (3 vol%). The PEI/TUD-1 sorbent was tested for 45 sorption-desorption cycles, showing a good regenerability and cyclic stability. Because of its high CO2 sorption performance and commercial availability of the support, the TUD-1 based MBS could be promising for cost-effective capture of CO2 from flue gas. C) 2014 Elsevier B.V. All rights reserved.
引用
收藏
页码:95 / 102
页数:8
相关论文
共 75 条
[1]  
Allam R.J., 2003, CARBON DIOXIDE RECOV
[2]  
ANGEVINE PJ, 2008, CATALYSIS ORGANIC RE, P367
[3]  
Aquino C, 2009, ORDERED POROUS SOLIDS: RECENT ADVANCES AND PROSPECTS, P3, DOI 10.1016/B978-0-444-53189-6.00001-9
[4]   Carbon Dioxide Sorbents with Propylamine Groups-Silica Functionalized with a Fractional Factorial Design Approach [J].
Aziz, Baroz ;
Zhao, Guoying ;
Hedin, Niklas .
LANGMUIR, 2011, 27 (07) :3822-3834
[5]   Effect of pore expansion and amine functionalization of mesoporous silica on CO2 adsorption over a wide range of conditions [J].
Belmabkhout, Youssef ;
Sayari, Abdelhamid .
ADSORPTION-JOURNAL OF THE INTERNATIONAL ADSORPTION SOCIETY, 2009, 15 (03) :318-328
[6]   Adsorption of CO2 on nitrogen-enriched activated carbon and zeolite 13X [J].
Bezerra, Diogo P. ;
Oliveira, Ronan S. ;
Vieira, Rodrigo S. ;
Cavalcante, Celio L., Jr. ;
Azevedo, Diana C. S. .
ADSORPTION-JOURNAL OF THE INTERNATIONAL ADSORPTION SOCIETY, 2011, 17 (01) :235-246
[7]   CO2 capture processes - Opportunities for improved energy efficiencies [J].
Chakma, A .
ENERGY CONVERSION AND MANAGEMENT, 1997, 38 :S51-S56
[8]   Amine-impregnated silica monolith with a hierarchical pore structure: enhancement of CO2 capture capacity [J].
Chen, Chao ;
Yang, Seung-Tae ;
Ahn, Wha-Seung ;
Ryoo, Ryong .
CHEMICAL COMMUNICATIONS, 2009, (24) :3627-3629
[9]   Adsorbent Materials for Carbon Dioxide Capture from Large Anthropogenic Point Sources [J].
Choi, Sunho ;
Drese, Jeffrey H. ;
Jones, Christopher W. .
CHEMSUSCHEM, 2009, 2 (09) :796-854
[10]   COMPARISON OF ACTIVATED CARBON AND ZEOLITE 13X FOR CO2 RECOVERY FROM FLUE-GAS BY PRESSURE SWING ADSORPTION [J].
CHUE, KT ;
KIM, JN ;
YOO, YJ ;
CHO, SH ;
YANG, RT .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1995, 34 (02) :591-598