November 24, 2024
Mohsen Abbasi

Mohsen Abbasi

Academic Rank: Associate professor
Address:
Degree: Ph.D in Chemical Engineering
Phone: 07731221495
Faculty: Faculty of Petroleum, Gas and Petrochemical Engineering

Research

Title
Kinetic study of the effects of zirconia and alumina on the synthesized calcium-based sorbent for improving calcium looping CO2 capture process
Type Thesis
Keywords
جذب كربن دي اكسيد، چرخه كلسيم، اكسيد زيركونيوم، اكسيد آلومينيوم، رسوبدهي
Researchers Mohammad Hashem Sedghkerdar (Primary advisor) , Mohsen Abbasi (Primary advisor) , Ali Izadbakhsh (Advisor) , Davood Karami (Advisor)

Abstract

Emissions of greenhouse gases (especially carbon dioxide) into the atmosphere have cause many environmental problems in recent years. Therefore, finding a suitable method to reduce the amount of carbon dioxide in the atmosphere is very important. Among the existing methods, the use of adsorbents and adsorption method is one of the most effective methods. So far, many adsorbents for CO2 adsorption have been prepared and evaluated, among which calcium oxide adsorbents are of special importance due to their low cost, great activity, easy access and high porosity. However, due to the high temperature, this adsorbent is associated with a decrease in adsorption capacity and resistance during the calcium looping. In this study, in order to increase the mechanical and thermal resistance of calcium oxide adsorbent, the chemical structure of this adsorbent was modified by alumina and zirconia by precipitation method. Four CaO, CaO-10% Al2O3, CaO-10% ZrO2 and CaO-5% Al2O3-5% ZrO2 adsorbents were prepared and evaluated under different operating conditions in a fixed bed reactor during five carbonation-calcination cycles (The adsorbents of the first group are exposed to 20 ml/min of pure CO2 flow for the carbonation process and 20 ml/min of pure argon gas for the calcination process, the second group of adsorbents are exposed to 40 ml/min of pure CO2 flow for the carbonation process and 40 ml/min of pure argon for the calcination process and the adsorbents of the third group are exposed to 10 ml/min of CO2 flow and 20 ml/min of argon gas for the carbonation process and 20 ml/min of pure argon gas for the calcination process). The results showed that the two modified adsorbents CaO-10% Al2O3 and CaO-10% ZrO2 have higher stability and resistance than the unmodified adsorbent. According to the results of XRD analysis, the reason for the increase in the stability of these two adsorbents compared to the unmodified adsorbent of calcium oxide was attributed to the formation of two comp