Open AccessTechnoeconomic Investigation of Amine-Grafted Zeolites and Their Kinetics for CO2 Capture
Author(s) -
Vijaya Tejavath,
Viswateja Kasarabada,
Spandana Gonuguntla,
Vijayanand Perupoga,
Satyanarayana V. Nandury,
B. Sreedhar,
Ujjwal Pal
Publication year - 2021
Publication title -
acs omega
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.779
H-Index - 40
ISSN - 2470-1343
DOI - 10.1021/acsomega.0c05397
Subject(s) - adsorption , zeolite , diethylenetriamine , amine gas treating , chemistry , ethylenediamine , thermogravimetric analysis , inorganic chemistry , materials science , chemical engineering , organic chemistry , catalysis , engineering
Solid adsorbents with precise surface structural chemistry and porosity are of immense interest to decode the structure-property relationships and maintain an energy-intensive path while achieving high activity and durability. In this work, we reported a series of amine-modified zeolites and their CO 2 capture efficiencies. The amine impregnated molecular zeolite compounds were characterized and systematically investigated for CO 2 adsorption capacity through thermogravimetric analysis for the occurrence of atmospheric pure CO 2 gas at 75 °C with diethylenetriamine (DETA), ethylenediamine (EDA), monoethanolamine (MEA), and triethanolamine (TEA)-loaded zeolite 13X, 4A, and 5A adsorbents. The kinetics of the adsorption study indicated that the adsorption capacity for CO 2 adsorption was improved with amine loading up to a certain concentration over 13X-DETA-40, showing an adsorption capacity of 1.054 mmol of CO 2 per gram of zeolite in a very short amount of time. The result was especially promising in terms of the initial adsorption capacity of zeolite, which adsorbed approximately 0.8 mmol/g zeolite within the first two minutes of experimentation. A detailed flow chart that includes a brief look into the process adopted for adsorption was included. Lagergren pseudo-first- and pseudo-second-order models of 40 wt % DETA zeolite 13X gave CO 2 adsorption capacities of 1.055 and 1.058 mmol/g and also activation energies of 86 and 76 kJ/mol, respectively. The CO 2 adsorption capacity of 13X-DETA-40 in a lab-scale reactor was found to be 1.69 mmol/g. A technoeconomic study was conducted for the solid amine zeolites to understand the investment per ton of CO 2 adsorbed. This study was used as a basis to improve cost estimates from a microscale to a lab-scale reactor. The cost of investment for 13X-DETA-40 was reduced by 84% from $49,830/ton CO 2 adsorbed in a microscale reactor to $7,690/ton of CO 2 adsorbed in a lab-scale reactor.