A5034602903- Carbon Dioxide Capture Technologies
- Membrane Separation and Gas Transport
- Phase Equilibria and Thermodynamics
- Membrane Separation Technologies
- Membrane-based Ion Separation Techniques
- Refrigeration and Air Conditioning Technologies
- Biofuel production and bioconversion
- Catalysis for Biomass Conversion
- Process Optimization and Integration
- Thermodynamic and Exergetic Analyses of Power and Cooling Systems
- Supercapacitor Materials and Fabrication
- Zeolite Catalysis and Synthesis
- Carbon dioxide utilization in catalysis
- Per- and polyfluoroalkyl substances research
- Enzyme Catalysis and Immobilization
- Microbial Metabolic Engineering and Bioproduction
- Microbial Fuel Cells and Bioremediation
- Carbohydrate Chemistry and Synthesis
- Thermodynamic properties of mixtures
- Extraction and Separation Processes
- Lignin and Wood Chemistry
- Adsorption and Cooling Systems
Walailak University
2018-2024
Nanyang Technological University
2017-2018
Qatar University
2015-2017
Chulalongkorn University
2017
Hunan University
2014-2016
University of Regina
2016
King Mongkut's University of Technology Thonburi
2009-2012
The performance of a hybrid solid acid catalyst consisting physical mixture γ‐Al 2 O 3 and H‐ZSM‐5 in terms the rate heat duty for solvent regeneration (i.e., CO stripping) ‐rich MEA solution was compared with individual , H‐ZSM‐5, H‐Y catalysts using (2–7 mol/L), initial loading 0.5 mol /mol at 378 K. It observed that any significantly decreased energy required regeneration. investigated ranked as follows: /H‐ZSM‐5 = 2/1 > if process is lean region whereas it rich region. These results...
A stopped‐flow apparatus was used to measure the kinetics of carbon dioxide (CO 2 ) absorption into aqueous solution 1‐diethylamino‐2‐propanol (1DEA2P) in terms observed pseudo‐first‐order rate constant (k o and second‐order reaction ), this work. The experiments were conducted over a 1DEA2P concentration range 120–751 mol/m 3 , temperature 298–313 K. As is tertiary amine, base‐catalyzed hydration mechanism was, then, applied correlate experimental CO constants obtained from apparatus. In...
The formation of bicarbonate ions in an amine solution during CO2 absorption results lowering the heat duty for solvent regeneration capture process because breakdown needs lowest energy input to release CO2. In this study, was conducted two mixed solvents consisting tertiary amines (1DMA2P (1 M) or MDEA M)) blended with MEA order determine both rate and capacity as compared alone. concentrations used study were (5 M), MEA–MDEA (5:1 molar ratio, 6 M total), MEA–1DMA2P total) at various...
Abstract Anaerobic digestion-based processes for converting wastewater into clean water and energy are attracting ever-growing industrial interest. However, apart from the microbial digestion step, current technologies require further progress an integrated process point of view, including post-treatment steps. effluents normally undergo extensive steps to meet stringent discharge standards, while valuable nutrients rarely recovered. Additionally, a significant portion produced methane...