Browsing by Author "Babaee, Saeideh."

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Carbon dioxide encapsulation in methane hydrates.
(2022) Ndlovu, Phakamile.; Naidoo, Paramespri.; Babaee, Saeideh.; Moodley, Kuveneshan.
Coal mining and petroleum refining processes face extreme pressure under climate change and global warming threats. Hence alternative sustainable and renewable energy sources must be made available for the rising energy demands. Natural gas found in permafrost and seabed areas in the form of gas hydrates possess vast amounts of low-carbon methane gas, which can replace fossil-based energy sources. The capture and storage of carbon dioxide gas in natural gas hydrate beds with the release of methane gas is a sustainable route under intense research. This study investigates the methane-carbon dioxide (CH4-CO2) replacement reaction mechanisms and the improvement of the process using different techniques, namely, additives, secondary gas, and thermal stimulation. Firstly, the gas hydrate dissociation measurements for the former gases utilized in the study were performed. This was followed by kinetic measurements with nanoparticles (aluminum oxide, copper oxide, and graphene nanoplatelets) and chemical additives (zinc oxide powder, graphite powder, and magnesium nitrate hexahydrate crystals) in the presence of sodium dodecyl sulfate (SDS) to affect kinetic or thermodynamic improvement in hydrate formation. The kinetic parameters investigated were induction time, hydrate storage capacity, water consumed in hydrate formation, fugacity of the gaseous phase, and the ratio of gas consumed to moles of water. Graphene nanoplatelets were selected for replacement reaction based on promising results obtained from the kinetic studies. The CH4-CO2 replacement process was performed in a 52 cm3 equilibrium cell using deionized water and nanoparticles. Also, a new experimental setup with a 300 cm3 reaction vessel was designed and assembled for CH4-CO2 replacement in the presence of synthetic silica sand. The results from kinetic studies showed an improvement in the hydrate formation kinetics due to the presence of nanoparticles. The CO2 hydrate formation kinetics obtained a maximum storage capacity of 51 (v/v), with 1.2 wt.% graphene nanoplatelets which also produced a maximum water conversion of 25%. When nanoparticles were added, the induction time for CO2 hydrate in deionized water was reduced from 9 minutes to less than one minute. Graphite powder with a concentration of 1.2 wt.% had the highest rate of gas uptake of 0.0024 (mol of gas/ mol of water. min). In CH4 kinetics, the induction time was reduced from 18 minutes with deionized water to less than one minute due to addition of nanoparticles. A maximum storage capacity of 28.5 (v/v), water-to-hydrate conversion of 13.09%, rate of gas uptake of 0.0089 (mol of gas/ mol of water. min), and gas consumption of 0.0238 moles were obtained with 0.1 wt.% CuO + 0.05 wt.% SDS. Also, CH4-CO2 replacement measurements showed that an 80 mol% N2/20 mol% CO2 gas mixture yielded a CH4 replacement efficiency of 17.04% at a temperature of 274.77 K and pressure of 5.34 MPa. The highest amount of CO2 sequestrated was 57.03%, and 28.77% was the highest CH4 replacement efficiency. These results were obtained using pressurized CO2 with application of thermal stimulation at a temperature of 275.90 K and pressure of 5.66 MPa. In the replacement reaction with silica sand, the maximum amount of CH4 replaced was 37.49% with the pressurized CO2 at a pressure of 7.01 MPa and temperature of 276.43 K. Applying thermal stimulation and adding secondary gas (N2) improved CO2 sequestration from 51.73% to 76.63%. These outcomes are vital in applying hydrates in gas storage and CO2 sequestration.
Hydrate phase equilibrium studies for Xe, Ar, Kr, and CF4 in the presence of TBAB aqueous solutions.
(2015) Babaee, Saeideh.; Ramjugernath, Deresh.; Mohammadi, Amir Hossein.; Naidoo, Paramespri.
Abstract available in PDF file.
Separation of noble gas mixtures of (Xe, Ar and Kr) using gas hydrate technology.
(2020) Matizakurima, Farai.; Naidoo, Paramespri.; Babaee, Saeideh.
The separation and purification of xenon from xenon + argon + krypton mixtures is an important research area owing to the increasing industrial demand for the gas. While cryogenic distillation, membrane technology and adsorption using metal-organic frameworks (MOF's) are used as separation methods, these methods are energy-intensive and sometimes financially non-viable. A comprehensive theoretical investigation of these methods is presented in this work. Hydrate-based separation technology has been reported to provide a possible solution. This study aimed to assess the performance of gas hydrate technology in separating and purifying noble gas mixtures. Hydrate technology is an interesting application, it has and is being investigated for the application in hydrocarbon gas capture and storage, carbon dioxide capture and storage, food concentration and refrigeration amongst other application. The motivation of this work was to find a cost-effective separation technology for separating and purifying xenon from the xenon + argon + krypton mixtures. Previous studies investigated the application of gas hydrate technology in separating xenon from binary noble gas mixtures, including an investigation of the effect of hydrate promoters and other factors in the capture of xenon in the hydrate phase. This study builds upon previous work focusing on the ternary mixtures of (Xe + Ar + Kr). Experimental measurements of gas hydrate phase equilibria for gas mixtures of (argon + krypton +xenon), along with compositional analysis of the hydrate and vapour phases using gaschromatography were performed. The isochoric pressure search method was used for measurements, with the use of a 52 ml stainless steel equilibrium cell. Different gas mixtures with various compositions ranging from 19 to 70 mol% xenon were investigated. To check the reliability of both the experimental equipment and procedures used in this study, dissociation data for the simple carbon dioxide + water system were measured. The newly measured data were compared with those in literature and were found to be in agreement with an acceptable uncertainty range. The instruments that were used were calibrated and the calibrations were verified. A thermodynamic model based on van der Waals and Platteeuw (vdW–P) solid solution theory was used to predict the hydrate equilibrium conditions for the Xe + Ar + Kr + water systems. An average absolute deviation (AAD%) of 1.4% between the experimental and predicted hydrate dissociation conditions was obtained. The consistency between modelled results and the novel measured experimental data demonstrated the validity of the proposed method. Concurrent to measuring thermodynamic equilibrium data, equilibrium compositional data for the systems studied were measured. The results indicate that the concentration of xenon has the highest increase in the first and second hydrate stages, reducing the concentration effect as the number of stages increases. For a mixture with 40.7 mol % argon, 33.6% krypton and 25.7% xenon, a concentration increase from 25.7% to 80.4% of xenon was achieved using two hydrate formation and dissociation stages. These findings were used to evaluate energy loads for the hydrate-based separation method. The results obtained were compared to the results obtained from an Aspen® simulation of the conventional cryogenic distillation process to determine energy loads for the conventional cryogenic distillation process. Results of the comparison revealed that the hydrate-based separation method presents a 20% energy cost advantage over cryogenic distillation.